EPA-450/3-83-001a
   f\fonmetallic Mineral
   Processing  Plants-
Background Information
for Proposed  Standards
    Emission Standards and Engineering Division
   U.S. ENVIRONMENTAL PROTECTION AGENCY
      Office of Air, Noise, and Radiation
    Office of Air Quality Planning and Standards
   Research Triangle Park, North Carolina 27711

             April 1983

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This report has been reviewed by the Emission Standards and Engineering Division of The Off ice of Air Quality
Planning and Standards, EPA, and approved for publication. Mention of trade names or commercial products is
not intended to constitute endorsement or recommendation for use. Copies of this report are available through
the Library Services Office (MD-35), U.S. Environmental  Protection Agency, Research Triangle Park, North
Carolina  27711; or, for a fee, from the  National Technical Information  Services, 5285 Port Royal Road,
Springfield, Virginia 22161.

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                      ENVIRONMENTAL PROTECTION  AGENCY

                          Background Information
                                 and Draft
                      Environmental Impact Statement
                            No.nmetallic  Mineral
                             Processing  Plants
                               Prepared  by:
     R.  Goodwin
 Director,  E/iission Standards and Engineering Division
 U.S. Environmental Protection Agency
 Research Triangle Park, NC  27711
'  (Date)
 1.   The proposed standards of performance would limit emissions of
     parti cul ate matter from new, modified, and reconstructed nonmetall-'c
     mineral processing plants.  Section 111 of the Clean Air Act
     (42 U.S.C. 7411), as amended, directs the Administrator to establish
     standards of performance for any category of new stationary source
     of air pollution that ". .  . causes or contributes significantly to
     air pollution which may reasonably be anticipated to endanger
     public health or welfare."

 2.   Copies of this document have been sent to the following Federal
     Departments:  Labor, Health and Human Services, Defense, Transportation
     Agriculture, Commerce, Interior, and Energy, as well as the National
     Science Foundation, the Council on Environmental Quality, State and
     Territorial Air Pollution Program Administrators, the Association
     of Local Air Pollution Control Officials, EPA Regional Administrators,
     and other interested parties.

 3.   The comment period for review of this document is 60 days.
     Mr. Gene Smith may be contacted regarding the date of the comment
     period.

4.   For additional  information contact:

     Mr. Gene Smith
     Standards Development Branch (MD-13)
     U.S.  Environmental  Protection Agency
     Research Triangle Park,  NC  27711
     telephone:   (919) 541-5624

5.   Copies  of this  document  may be obtained from:

     U.S.  EPA Library (MD-35)
     Research Triangle Park,  NC  27711

     National  Technical  Information Service
     5886  Port Royal  Road
     Springfield,  VA  22161
                               m

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r


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TABLE OF CONTENTS
                                          Page
LIST OF FIGURES .................  ...........



LIST OF TABLES ........



CHAPTER 1.  SUMMARY .................... ...!..



   1.1  PROPOSED STANDARDS  .....................  .



   1.2  ENVIRONMENTAL IMPACT  ...... .......



   1.3  ECONOMIC IMPACT .............. ... ...... ..



CHAPTER 2.  INTRODUCTION .  .  ...........



   2.1  AUTHORITY FOR THE STANDARDS ..... .......



   2.2  SELECTION OF CATEGORIES OF STATIONARY SOURCES ....... ..



   2.3  PROCEDURE FOR DEVELOPMENT OF STANDARDS OF PERFORMANCE



   2.4  CONSIDERATION OF COSTS



   2.5  CONSIDERATION OF ENVIRONMENTAL IMPACTS .  ......  .



   2.6  IMPACT ON EXISTING SOURCES ............ .



   2.7  REVISION OF STANDARDS OF PERFORMANCE .......... ...



CHAPTER 3.  THE NON-METALLIC MINERALS INDUSTRY ....



   3.1  GENERAL .............................



   3.2  NON-METALLIC MINERALS PREPARATION PROCESSES AND THEIR EMISSIONS.



   3.3  REFERENCES ....  ................ .......



CHAPTER 4.  EMISSION CONTROL TECHNIQUES .......... ...... .



   4.1  CONTROL OF PLANT PROCESS OPERATIONS ................



   4.2  FACTORS AFFECTING THE PERFORMANCE OF CONTROL METHODS  ......



   4.3  PERFORMANCE OF PARTICULATE EMISSION CONTROL TECHNIQUES .....



   4.4  REFERENCES ...... .......... ....... ....
                                            x




                                          1-1



                                          1-1



                                          1-2



                                          1-5



                                          2-1



                                          2-1



                                          2-6



                                          2-8



                                          2-11



                                          2-12



                                          2-14



                                          2-15



                                          3-1



                                          3-1



                                          3-12



                                          3-52



                                          4-1



                                          4-1



                                          4-29



                                          4-32



                                          4-59

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                          TABLE OF CONTENTS (continued)
                                                                          Page
 CHAPTER  5.   MODIFICATION AND RECONSTRUCTION	5-1



    5.1   MODIFICATION	5-1



    5.2   RECONSTRUCTION	5-2



 CHAPTER  6.   EMISSION  CONTROL SYSTEMS  	  6-1



 CHAPTER  7.   ENVIRONMENTAL IMPACT  	  7-1



    7.1   AIR  POLLUTION IMPACT	7-1



    7.2   WATER  POLLUTION  IMPACT  	  7-18



    7.3   SOLID  WASTE DISPOSAL IMPACT	7-18



    7.4   ENERGY IMPACT	'	7-19



    7.5   NOISE  IMPACT	7-23



    7.6   REFERENCES	  7-25



 CHAPTER  8.   ECONOMIC  IMPACT	.8-1



    8.0   SUMMARY	8-1



    8.1   UNITED STATED NON-METALLIC MINERALS INDUSTRY STRUCTURE 	  8-4



    8.2   COST ANALYSIS OF  ALTERNATIVE EMISSION CONTROL SYSTEMS	8-52



    8.3   OTHER COST CONSIDERATIONS	8-84



    8.4   ECONOMIC IMPACT ASSESSMENT 	  8-88



    8.5   POTENTIAL SOCIO-ECONOMIC AND INFLATIONARY IMPACTS	8-117



APPENDIX A.  EVOLUTION OF THE PROPOSED STANDARDS 	 A-l



APPENDIX B.  INDEX TO ENVIRONMENTAL IMPACT CONSIDERATIONS	,  .  . . B-l



APPENDIX C.  SUMMARY OF TEST DATA	C-l



APPENDIX D.  EMISSION MEASUREMENT AND CONTINUOUS MONITORING	D-l



   D.I  EMISSION MEASUREMENT METHODS 	 D-l



   D.2  MONITORING SYSTEMS AND DEVICES 	 D-2



   D.3  PERFORMANCE TEST METHODS	 D-2

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                        TABLE OF CONTENTS (continued)
                                                                         Page
SUPPLEMENT A.  ECONOMIC IMPACT ANALYSIS FOR PORTABLE PLANTS 	  S-l
   A.O  INTRODUCTION AND SUMMARY	S-l
   A.I  INDUSTRY CHARACTERIZATION   ...... 	  S-3
   A.2  COST ANALYSIS	S-8
   A. 3  ECONOMIC IMPACTS  .	S-30

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                               LIST OF FIGURES

                                                                         Page
Figure 3-1  FLOWSHEET OF A TYPICAL CRUSHING PLANT 	   3-13
Figure 3-2  GENERAL SCHEMATIC FOR NON-METALLIC MINERALS PROCESSING  .  .   3-17
Figure 3-3  DOUBLE-TOGGLE JAW CRUSHER 	   3-25
Figure 3-4  SINGLE-TOGGLE JAW CRUSHER 	   3-25
Figure 3-5  THE PIVOTED SPINDLE GYRATORY  	   3-28
Figure 3-6  CONE CRUSHER	3-29
Figure 3-7  DOUBLE-ROLL CRUSHER 	   3-30
Figure 3-8  SINGLE ROLL CRUSHER	3-31
Figure 3-9  HAMMERMILL	3-32
Figure 3-10 IMPACT CRUSHER  	   3-33
Figure 3-11 VIBRATING GRIZZLY 	   3-36
Figure 3-12 VIBRATING SCREEN  .... 	   3-37
Figure 3-13 CONVEYOR BELT TRANSFER POINT  	   3-40
Figure 3-14 BUCKET ELEVATOR TYPES 	   3-41
Figure 3-15 ROLLER MILL 	   3-46
Figure 3-16 BALL MILL	3-48
Figure 3-17 FLUID-ENERGY MILL	3-48
Figure 4-1  WET DUST SUPPRESSION SYSTEM	4-7
Figure 4-2  DUST SUPPRESSION APPLICATION AT CRUSHER DISCHARGE 	   4-9
Figure 4-3  HOOD CONFIGURATION USED TO CONTROL A CONE CRUSHER 	   4-14
Figure 4-4 -HOOD CONFIGURATION FOR VIBRATING SCREEN 	   4-15
Figure 4-5  HOOD CONFIGURATION FOR CONVEYOR TRANSFER, LESS THAN
            0.91 METER (3-FOOT) FALL	4-17
Figure 4-6  HOOD CONFIGURATION FOR A CHUTE TO BELT OR CONVEYOR TRANSFER,
            GREATER THAN 0.01 METERS (3-FOOT) FALL	4-18
                                    vm

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                          LIST OF FIGURES (continued)
                                                                        Page
Figure 4-7   EXHAUST CONFIGURATION AT BIN OR HOPPER .	4-19

Figure 4-8   BAG FILLING VENT SYSTEM.	"..'..'.... 4-20

Figure 4-9   TYPICAL BAGHOUSE OPERATION	 4-23

Figure 4-10  BAGHOUSE CLEANING METHODS	4-25

Figure 4-11  MECHANICAL, CENTRIFUGAL SCRUBBER 	 	 4-28

Figure 4-12  TYPICAL COMBINATION DUST CONTROL SYSTEMS 	 4-30

Figure 4-13  PARTICULATE EMISSIONS FROM NON-METALLIC MINERALS
             PROCESSING OPERATIONS	4-35

Figure 4-14  PARTICULATE EMISSIONS FROM METALLIC MINERAL PROCESSING
             OPERATIONS 	 ......... 4-43

Figure 4-15  SUMMARY OF VISIBLE EMISSION MEASUREMENTS FROM BEST
             CONTROLLED FUGITIVE PRIMARY CRUSHING SOURCES (PORTABLE-
             FACILITY T) BY MEANS OF WET SUPPRESSION (ACCORDING TO
             EPA METHOD 9)	 . 4-53

Figure 4-16  SUMMARY OF VISIBLE EMISSION MEASUREMENTS FROM BEST
             CONTROLLED FUGITIVE SECONDARY CRUSHING SOURCE (PORTABLE-
             FACILITY R) BY MEANS OF WET SUPPRESSION (ACCORDING TO
             EPA METHOD 9)	4-54

Figure 4-17  SUMMARY OF VISIBLE EMISSION MEASUREMENTS FROM BEST
             CONTROLLED FUGITIVE PRIMARY CRUSHING SOURCE (STATIONARY-
             FACILITY S) BY MEANS OF WET SUPPRESSION (ACCORDING TO
             EPA METHOD 9)	 4-55

Figure 4-18  SUMMARY OF VISIBLE EMISSION MEASUREMENT FROM BEST
             CONTROLLED FUGITIVE SECONDARY CRUSHER (SMALL, STATIONARY-
             FACILITY S) BY MEANS OF WET SUPPRESSION (ACCORDING TO
             EPA METHOD 9).  .	4-56

Figure 4-19  SUMMARY OF VISIBLE EMISSION MEASUREMENTS FROM BEST
             CONTROLLED FUGITIVE SECONDARY CRUSHING SOURCE (LARGE,
             SECONDARY-FACILITY S) BY MEANS OF WET SUPPRESSION
             (ACCORDING TO EPA METHOD 9)	4-57

Figure 7-1   PLANT LAYOUTS SHOWING THE NUMBER AND LOCATIONS OF THE
             SOURCES (STACKS)  SPECIFIED FOR EACH PLANT SIZE)	7-9

Figure 8-1   COST-EFFECTIVENESS OF ALTERNATE CONTROL SYSTEMS.  ..... 8-79

Figure 8-2   INSTALLED COSTS OF FABRIC FILTER SYSTEMS .	 8-81
                                   IX

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                    LIST OF TABLES
                                                         Page
MATRIX OF ENVIRONMENTAL AND ECONOMIC IMPACTS OF
ALTERNATIVE STANDARDS 	
1-3
Table  1-1


Table  3-1    INDUSTRY  CHARACTERISTICS	3-3

Table  3-2    MAJOR  USES OF THE  NON-METALLIC MINERALS	3-6

Table  3-3    POSSIBLE  SOURCES OF  EMISSIONS	3-16

Table  3-4    EMISSION  SOURCES AT  NON-METALLIC MINERAL  FACILITIES  .  .   3-18

Table  3-5    PARTICULATE EMISSION FACTORS FOR STONE
             CRUSHING  PROCESS	   3-19

Table  3-6    RELATIVE  CRUSHING  MECHANISMS UTILIZED BY
             VARIOUS CRUSHERS	3-23

Table  3-7    APPROXIMATE CAPACITIES OF JAW CRUSHERS	3-27

Table  3-8    APPROXIMATE CAPACITIES OF GYRATORY CRUSHERS  	   3-27

Table  3-9    PERFORMANCE DATA FOR CONE CRUSHERS	3-29

Table  4-1    PARTICULATE EMISSION SOURCES FOR THE EXTRACTION AND
             PROCESSING OF NON-METALLIC MINERALS 	   4-2

Table  4-2    BAGHOUSE  UNITS TESTED BY EPA	4-34

Table  4-3    AIR-TO-CLOTH RATIOS  FOR FABRIC FILTERS USED FOR
             EXHAUST EMISSION CONTROL	4-38

Table  4-4    BAGHOUSE  UNITS TESTED BY EPA (METALLIC MINERAL
             PROCESSING)	4-42

Table  4-5    OPACITY MEASUREMENTS  FROM BAGHOUSE EXHUAST STACKS .  . .  4-47

Table  4-6    SUMMARY OF VISIBLE EMISSIONS MEASUREMENTS FROM
             FUGITIVE SOURCES AT  NON-METALLIC MINERAL PLANTS ....  4-49

Table  4-7    SUMMARY OF VISIBLE EMISSIONS MEASUREMENTS FROM
             FUGITIVE NONCRUSHING SOURCES CONTROLLED BY WET
            SUPPRESSION (ACCORDING TO EPA METHOD 9)  	  4-52

Table  6-1   MODEL PLANTS FOR ESTIMATING ENVIRONMENTAL AND
             ECONOMIC  IMPACT 	  6-2

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                          LIST OF TABLES (continued)
                                                                     Page
Table 6-2   LIST OF PROCESS EQUIPMENT INCLUDING ENERGY
            REQUIREMENTS AND AIR VOLUME REQUIREMENTS USED IN
            DETERMINING MODEL PLANTS	6-4

Table 6-3   PLANT SIZES FOR THE VARIOUS NON-METALLIC MINERALS
            INDUSTRIES (METRIC UNITS) 	  6-6

Table 7-1   ALLOWABLE EMISSIONS UNDER GENERAL STATE PROCESS
            WEIGHT REGULATIONS. . ...	  7-2

Table 7-2   GROWTH RATES AND MINERAL PRODUCTION LEVELS FOR THE
            VARIOUS NON-METALLIC MINERALS INDUSTRIES	7-3

Table 7-3   SUMMARY OF AIR POLLUTION IMPACT	7-5

Table 7-4   STACK AND EMISSIONS DATA.	 .  7-11

Table 7-5   ESTIMATED MAXIMUM 24-HOUR AND ANNUAL GROUND-LEVEL
            PARTICULATE CONCENTRATION DUE TO EMISSIONS FROM THE
            PROCESS SOURCES IN THE MODEL NON-METALLIC MINERALS
            PLANTS HAVING BOTH CRUSHING AND GRINDING OPERATIONS . .  7-15

Table 7-6   ESTIMATED MAXIMUM 24-HOUR AND ANNUAL GROUND-LEVEL
            PARTICULATE CONCENTRATION DUE TO EMISSIONS FROM
            THE PROCESS SOURCES IN THE MODEL NON-METALLIC MINERALS
            PLANTS HAVING ONLY CRUSHING OPERATIONS	7-16

Table 7-7   ENERGY REQUIREMENTS FOR MODEL NON-METALLIC MINERALS
            PLANTS HAVING CRUSHING AND GRINDING OPERATIONS	7-21

Table 7-8   ENERGY REQUIREMENTS FOR MODEL NON-METALLIC MINERALS
            PLANTS HAVING CRUSHING OPERATIONS ONLY	  7-21

Table 7-9   ENERGY IMPACT ON INDIVIDUAL NON-METALLIC INDUSTRIES
            UNDER PROPOSED NSPS	  7-24

Table 8-1   SAND AND GRAVEL:  SALIENT STATISTICS	  8-9

Table 8-2   U.S. CRUSHED STONE INDUSTRY	8-12

Table 8-3   U.S. GYPSUM INDUSTRY.	8-16

Table 8-4   U.S. DIATOMITE INDUSTRY	8-18

Table 8-5   U.S. PERLITE INDUSTRY	8-20

Table 8-6   U.S. PUMICE INDUSTRY. .  .	8-22
                                   XI

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                          LIST OF TABLES  (continued)
                                                                     Page
Table 8-7   U.S. VERMICULITE  INDUSTRY	8-24
Table 8-8   U.S. MICA  INDUSTRY	8-26
Table 8-9   U.S. BARITE  INDUSTRY	8-29
Table 8-10  U.S FLUORSPAR INDUSTRY	8-31
Table 8-11  U.S. SALT  INDUSTRY	8-33
Table 8-12  U.S. BORON INDUSTRY	8-35
Table 8-13  U.S. SODIUM  CARBONATE INDUSTRY	8-37
Table 8-14  U.S. SODIUM  SULFATE INDUSTRY	8-38
Table 8-15  U.S. CLAY  INDUSTRY	8-41
Table 8-16  U.S. FELDSPAR INDUSTRY	8-44
Table 8-17  U.S. KYANITE INDUSTRY	  .  8-45
Table 8-18  U.S. TALC INDUSTRY.	8-48
Table 8-19  TECHNICAL PARAMETERS USED  IN DEVELOPING CONTROL
            SYSTEM COSTS.	8-54
Table 8-20  ANNUALIZED COST PARAMETERS	8-57
Table 8-21  FABRIC FILTER COSTS FOR NEW MODEL PLANT 1: 9.1 mg/Hour.  8-59
Table 8-22  FABRIC FILTER COSTS FOR NEW MODEL PLANT 1: 23 Mg/Hour  .  8-60
Table 8-23  FABRIC FILTER COSTS FOR NEW MODEL PLANT 1: 68 Mg/Hour  .  8-61
Table 8-24  FABRIC FILTER COSTS FOR NEW MODEL PLANT 1: 135 Mg/Hour.  8-62
Table 8-25  FABRIC FILTER COSTS FOR NEW MODEL PLANT 1: 270 Mg/Hour.  8-63
Table 8-26  FABRIC FILTER COSTS FOR NEW MODEL PLANT 1: 540 Mg/Hour.  8-64
Table 8-27  FARBIC FILTER COSTS FOR NEW MODEL PLANT 2: 9.1 Mg/Hour.  8-65
Table 8-28  FABRIC FILTER COSTS FOR NEW MODEL PLANT 2: 23 Mg/Hour  .  8-66
Table 8-29  FABRIC FILTER COSTS FOR NEW MODEL PLANT 2: 68 Mg/Hour  .  8-67

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                          LIST OF TABLES (continued)
Table 8-30

Table 8-31

Table 8-32

Table 8-33

Table 8-34


Table 8-35


Table 8-36


Table 8-37

Table 8-38

Table 8-39


Table 8-40

Table 8-41

Table 8-42


Table 8-43


Table 8-44
FABRIC FILTER COSTS FOR NEW MODEL PLANT 2: 135 Mg/Hour.

FABRIC FILTER COSTS FOR NEW MODEL PLANT 2: 270 Mg/Hour.

FABRIC FILTER COSTS FOR NEW MODEL PLANT 2: 540 Mg/Hour.

FABRIC FILTER COSTS FOR EXPANDED MODEL PLANTS 	

FABRIC FILTER COSTS FOR 32 Mg/Hour EXPANDED MODEL
PLANT	

MONITORING COSTS FOR NON-METALLIC MINERALS MODEL
PLANTS	

RANK ORDER OF INDUSTRIES WITH HIGHEST CONTROL COST
IMPACT	.	
PLANT INVESTMENT COSTS. . ,

EXPANSION INVESTMENT COSTS.
DISCOUNTED CASH FLOW ANALYSES CRUSHED STONE PLANT
136 Mg/Hour (150 tph) (IN THOUSANDS OF DOLLARS) . .  .
SUMMARY OF DCF RESULTS.

SUMMARY OF DCF RESULTS.
ESTIMATED NUMBER OF TYPICAL NEW PLANT REQUIRED TO
MEET PROJECT PRODUCTION	
ANNUALIZED CAPITAL AND OPERATING CONTROL COSTS
FOR NEW PLANT CONSTRUCTION  	
ANNUALIZED CONTROL COST PER TON OF INDUSTRY OUTPUT
IN 5th YEAR AND CONTROL COST AS PERCENT OF
SELLING PRICE 	
Page

8-68

8-69

8-70

8-75


8-76


8-85


8-101

8-104

8-105


8-108

8-113

8-115


8-119


8-120



8-121
                                 xi

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                                   1.   SUMMARY

1.1  REGULATORY ALTERNATIVES
     Regulatory alternatives to limit emissions of participate matter from
new, modified, and reconstructed non-metallic mineral  processing plants and
the environmental and economic impacts of these alternatives are presented
in this document.  This source was listed August 21, 1979 (44 FR 49222) in
accordance with section lll(b)(l)(A) of the Clean Air Act as contributing
signficantly to air pollution, which may reasonably be anticipated to endanger
public health or welfare.  Appendix B contains a cross-reference between
this document and the Agency's guidelines for Environmental  Impact Statements.
     Regulatory alternatives have been developed for processing of the following
minerals:
     Crushed and broken stone
        Limestone, Dolomite, Granite,
        Traprock, Sandstone, Quartz,
        Quartzite, Marl, Marble, Slate,
        Shell
     Sand and gravel
     Clay
        Kaolin, Fireclay, Bentonite,
        Fuller's Earth, Ball Clay
     Rock salt
     Gypsum
     Sodium compounds
        Chloride, Carbonate, Sulfate
     Pumice
     Gilsonite
     Boron
        Borax, Kernite, Colemanite
Barite
Fluorspar
Talc and Pyrophyl1i te
Feldspar
Diatomite
Perlite
Vermiculite
Mica
Kyanite
   Andalusite, Sillimanite,
   Topaz, Dumortierite
                                     1-1

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     The regulatory alternatives would limit emissions of particulate matter
from the following process equipment at a plant:   crushers, grinding mills
(including air separators, classifiers, and conveyors), screens,  bucket
elevators, belt conveyors, bagging operations, storage bins, and  enclosed
truck and rail car loading stations.  Unit operations not included are
drilling, blasting, loading at the mine, hauling, drying, stockpiling,
conveying (other than at transfer points), and windblown dust from stockpiles,
roads, and plant yards.
     Three regulatory alternatives were considered:   (1) to set no standards;
(2) to set standards based on baghouses; and (3)  to  set standards based on
baghouses and wet dust suppression systems.  A matrix summarizing the
environmental and economic impacts associated with the three regulatory
alternatives is included in Table 1.1.  Alternatives 2 and 3 would limit both
fugitive and stack emissions at the affected facilities.  Fugitive emissions,
which are emissions not collected by a capture system, would be limited to
10 percent opacity under alternative 2.  Under alternative 3, fugitive emissions
at all process operations except crushing would be subject to the limitation
described above.  At crushers, fugitive emissions would be limited •' z 15 percent
opacity.  Under both alternatives, stack emissions,  which are emissions
collected by a capture system, would be limited to a concentration of particulate
matter of 0.05 gram per dry standard cubic meter (g/dscm) (0.02 grain per dry
standard cubic foot (gr/dscf)) and 7 percent opacity.
1.2  ENVIRONMENTAL IMPACT
     The beneficial and adverse environmental impact associated with regulatory
alternatives 2 and 3 are presented in this section.   These impacts  are
discussed in detail in Chapter 7, Environmental Impact.

                                     1-2

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     About 550 new non-metallic mineral  processing  plants  will  be  needed
 to  process the projected increased  production  in  the  first 5  years after
 proposal.   By the  fifth  year,  regulatory alternatives  2  and 3 would reduce
 the total  amount of particulate matter emissions  to the  atmosphere by
 41,000 megagrams per year (45,000 tons per year).   This  reduction  is
 90  percent greater than  that achievable  with a  typical State  process
 weight regulation.   This will  result  in  a large positive environmental
 impact.
     The utilization of  dry  collection techniques (particulate  capture
 combined with a  dry emission control  device) for  control generates  no water
 effluent discharge.  In  cases  where wet  suppression techniques  could be used,
 most of the water  adheres  to the material being processed,  resulting in no
 significant water  discharge.   Consequently, the regulatory  alternatives
 for the non-metallic mineral industry  would have no water pollution impact.
     There  would be  an insignificant  negative solid waste disposal  impact
 resulting  from the  use of  dry  emission control  techniques.  Approximately
 1.4 megagrams  (1.6  tons) of solid waste  are collected for every 250 megagrams
 (278 tons)  of material processed.  In many cases, this material  may be
 recycled back into the process,  sold, or used for a variety of purposes.
 Where no market  exists for the collected fines, they are typically disposed
 of  in the mine or in an  isolated location in the quarry.   Where  wet dust
 suppression can  be used, no solid waste disposal problem exists  over that
 resulting from normal operation.
     The estimated incremental  energy requirements of both regulatory
 alternatives result from comparing the use of fabric filters (baghouses)
 to control  particulate matter emissions to the use of no  control system.
The estimates indicate a greater impact than would actually occur because
                                  1-4

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it is expected that less-energy consuming wet dust suppression systems would
be used in many cases.  In addition, many new plants would use baghouses
or a combination of baghouses and water sprays to meet existing State
regulations.
     The energy required to control all new non-metallic mineral  processing
plants constructed by 1985 to the levels of regulatory alternatives 2 and 3
would be about 0.21 million megawatt-hours (0.34 million kilowatt-hours)
per year.  This would be about a 15 percent increase over the amount of
energy which would otherwise be required to meet project capacity additions
without controls.  This increase would have a minor impact on national energy
demand.
     When compared to the noise emanating from crushing and grinding process
equipment, any additional noise from properly designed exhaust fans for
the control system would be insignificant.  Consequently, no significant
noise impact is anticipated due to the implementation of either regulatory
alternative 2 or 3 for non-metallic mineral plants.  There are no known
radiation impacts associated with the regulatory alternatives.
1.3  ECONOMIC IMPACT
     The economic impacts associated with regulatory alternatives 2 and 3
are presented in this section.  These impacts are discussed in detail in
Chapter 8, Economic Impact.
     The costs and economic impacts associated with regulatory alternatives 2
and 3 are considered reasonable.  The estimated impacts are based on a
comparison of fabric filter (baghouse) use to no control.  Less expensive
wet dust suppression systems may be used in some cases.  Also, many new
                                   1-5

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 plants would  use  baghouses or a combination of baghouses and water sprays
 to meet  existing  State regulations.  Thus, the actual economic impact of
 these regulatory  alternatives would probably be considerably less than the
 estimates summarized below.
     The costs associated with these regulatory alternatives would not
 prevent  construction of new non-metallic processing plants which would be
 built in the  absence of any new regulations.  However, the incremental
 costs associated  with the best system of emission reduction may preclude
 the construction  of new pumice plants and common clay plants with capacities
 of 9.1 Mg/hr  (10  tons/hr) or less; fixed sand and gravel plants and crushed
 stone plants with capacities of 22.7 Mg/hr (25 tons/hr) or less; and portable
 sand and gravel plants and crushed stone plants with capacities of 136.4 Mg/hr
 (150 tons/hr) or  less.
     The total additional capital cost for all new plants would be about
 $107 million for  the first 5 years the proposed standards would be in
 effect.  These costs would vary for each industry, ranging from about
 $93,000 for several minerals to $82.5 million for crushed stone.   The total
 annualized costs  in the fifth year would increase by about $28 million for
 crushed stone.  The average annualized control cost per ton of output in
 the fifth year would range from $0.005 for sand and gravel  to $0.137 for
 kyanite.  For all  minerals, the annualized control  cost is  less than
2 percent of the annual  revenue for that industry.
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                             2.  INTRODUCTION

2.1  BACKGROUND AND AUTHORITY FOR STANDARDS
     Before standards of performance are proposed as a Federal regulation,
air pollution control methods available to the affected industry and the
associated costs of installing and maintaining the control equipment are
examined in detail.  Various levels of control based on different technolo-
gies and degrees of efficiency are expressed as regulatory alternatives.
Each of these alternatives is studied by EPA as a prospective basis for a
standard.  The alternatives are investigated in terms of their impacts on
the economics and well-being of the industry, the impacts on the national
economy, and the impacts on the environment.  This document summarizes the
information obtained through these studies so that interested persons will
be able to see the information considered by EPA in the development of the
proposed standard.
     Standards of performance for new stationary sources are established
under section 111 of the Clean Air Act (42 U.S.C. 7411) as amended, herein-
after referred to as the Act.  Section 111 directs the Administrator to
establish standards of performance for any category of new stationary
source of air pollution which ".  .  .  causes, or contributes significantly
to air pollution which may reasonably be anticipated to endanger public
health or welfare."
     The Act requires that standards of performance for stationary sources
reflect "... the degree of emission reduction achievable which (taking
into consideration the cost of achieving such emission reduction, and any
nonair quality health and environmental  impact and energy requirements) the
Administrator determines has been adequately demonstrated for that category
of sources."  The standards apply only to stationary sources, the construc-
tion or modification of which commences  after regulations are proposed by
publication in the Federal  Register.
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     The 1977 amendments'to the Act altered or added numerous provisions
that apply to the process of establishing standards of performance.
     1.  EPA is required to review the standards of performance every 4
years and, if appropriate, revise them.
     2.  EPA is authorized to promulgate a standard based on design, equip-
ment, work practice, or operational procedures when a standard based on
emission levels is not feasible.
     3.  The term "standards of performance" is redefined, and a new term
"technological system of continuous emission reduction" is defined. The new
definitions clarify that the control system must be continuous and may
include a low- or non-polluting process or operation.
     4.  The time between the proposal and promulgation of a standard under
section 111 of the Act may be extended to 6 months.
     Standards of performance, by themselves, do not guarantee protection
of health or welfare because they are not designed to achieve any  specific
air-quality levels.  Rather, they are designed to reflect the degree of
emission limitation achievable through application of the best adequately
demonstrated technological system of continuous emission reduction, taking
into consideration the cost of achieving such emission reduction,  any
non-air-quality health and environmental impacts, and energy requirements.
     Congress  had several reasons for  including these requirements. First,
standards with a degree  of uniformity are needed to avoid situations where
some States may attract  industries  by  relaxing standards relative  to other
States.  Second, stringent standards enhance the potential for long-term
growth.  Third, stringent standards may  help achieve long-term cost savings
by avoiding  the need for more expensive  retrofitting when pollution ceilings
may  be reduced in the  future.   Fourth, certain types of standards  for
coal burning  sources can  adversely affect the coal market by driving up  the
price  of  low-sulfur coal or effectively  excluding certain coals from the
reserve base  because their untreated pollution potentials are high.  Con-
gress  does  not intend  that new  source  performance standards contribute  to
these  problems.   Fifth,  the  standard-setting process should create incen-
tives  for improved  technology.
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      Promulgation of standards of performance does  not prevent State  or
 local  agencies from adopting more stringent emission  limitations  for  the
 same sources.   States are free under section 115 of the Act  to establish
 even more stringent emission limits  than  those established under
 section 111 or those necessary to attain  or maintain  the National Ambient
 Air Quality Standards (NAAQS)  under  section 110.  Thus,  new  sources may in
 some cases  be  subject to  limitations more stringent than standards of
 performance under section 111,  and prospective owners  and operators of
 new sources should be aware  of  this  possibility in  planning  for such
 facilities.
     A  similar situation  may arise when a major emitting facility is to be
 constructed in a  geographic  area  that falls  under the  prevention of
 significant deterioration of air  quality  provisions of Part  C of the Act.
 These provisions  require, among other things,  that major emitting
 facilities  to  be  constructed in such  areas are  to be subject to best
 available control  technology.  The term Best Available Control Technology
 (BACT), as  defined  in  the Act, means
     ...  an  emission limitation  based on the maximum degree
     of reduction of each pollutant subject to regulation
     under  this Act emitted  from,  or which results from,
     any major emitting facility, which the permitting authority,
     on a case-by-case basis, taking  into account energy,
     environmental, and economic  impacts and other costs,
     determines is achievable for  such facility through
     application of production processes and available methods,
     systems, and techniques, including fuel cleaning  or treatment
     or innovative fuel combustion techniques for control of
     each such pollutant.   In no event shall application of
     "best available control  technology" result in emissions
     of any pollutants which will  exceed the emissions allowed
     by any applicable standard established pursuant to
     sections 111 or 112 of this Act. (Section 169(3))
     Although standards of performance are normally structured in  terms of
numerical  emission limits  where feasible,  alternative  approaches are some-
times necessary.  In some  cases physical  measurement of emissions  from a
new source may be impractical or exorbitantly expensive.   Section  lll(h)
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provides that the Administrator may promulgate a design or equipment stand-
ard in those cases where it is not feasible to prescribe or enforce a
standard of performance.  For example, emissions of hydrocarbons from
storage vessels for petroleum liquids are greatest during tank filling.
The nature of the emissions, high concentrations for short periods during
filling and low concentrations for longer periods during storage, and the
configuration of storage tanks make direct emission measurement impractical.
Therefore, a more practical approach to standards of performance for
storage vessels has been equipment specification.
     In- addition, section lll(i) authorizes the Administrator to grant
waivers of compliance to permit a source to use innovative continuous
emission control technology.  In order to grant the waiver, the Administra-
tor must find:  (1) a substantial likelihood that the technology will
produce greater emission reductions than the standards require or an
equivalent reduction at lower economic energy or environmental cost;
(2) the proposed system has not been adequately demonstrated; (3) the
technology will not cause or contribute to an unreasonable risk to the
public health, welfare, or safety; (4)-the governor of the State where the
source is located consents; and (5) the waiver will not prevent the
attainment or maintenance of any ambient standard.  A waiver may have
conditions attached to assure the source will not prevent attainment of any
NAAQS.  Any such condition will have the force of a performance standard.
Finally, waivers have definite end dates and may be terminated earlier if
the conditions are not met or if the system fails to perform as expected.
In such a case, the source may be given up to 3 years to meet the standards
with a mandatory progress schedule.
2.2  SELECTION OF CATEGORIES OF STATIONARY SOURCES
     Section 111 of the Act directs the Adminstrator to list categories of
stationary sources.  The Administrator "... shall include a category of
sources in such list if in his judgment it causes, or contributes signifi-
cantly to, air pollution which may reasonably be anticipated to endanger
public health or welfare."  Proposal and promulgation of standards of
performance are to follow.
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     Since passage of the Clean Air Amendments of 1970, considerable
attention has been given to the development of a system for assigning
priorities to various source categories.  The approach specifies areas of
interest by considering the broad strategy of the Agency for implementing
the Clean Air Act.  Often, these "areas" are actually pollutants emitted by
stationary sources.  Source categories that emit these pollutants are
evaluated and ranked by a process involving such factors as (1) the level
of emission control (if any) already required by State regulations,
(2) estimated levels of control that might be required from standards of
performance for the source category, (3) projections of growth and
replacement of existing facilities for the source category, and (4) the
estimated incremental amount of air pollution that could be prevented in a
preselected future year by standards of performance for the source
category.  Sources for which new source performance standards were,
promulgated or under development during 1977, or earlier, were selected on
these criteria.
     The Act amendments of August 1977 establish specific criteria to be
used in determining priorities for all major source categories not yet
listed by EPA.  These are (1) the quantity of air pollutant emissions that
each such category will  emit, or will be designed to emit; (2) the extent
to which each such pollutant may reasonably be anticipated to endanger
public health or welfare; and (3) the mobility and competitive nature of
each such category of sources and the consequent need for nationally
applicable new source standards of performance.
     The Administrator is to promulgate standards for these categories
according to the schedule referred to earlier.
     In some cases it may not be feasible immediately to develop a standard
for a source category with a high priority.  This might happen when a
program of research is needed to develop control techniques or because
techniques for sampling and measuring emissions may require refinement.  In
the developing of standards, differences in the time required to complete
the necessary investigation for different source categories must also be
considered.  For example, substantially more time may be necessary if
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numerous pollutants must be investigated from a single source category.
Further, even late in the development process the schedule for completion
of a standard may change.  For example, inablility to obtain emission data
from well-controlled sources in time to pursue the development process in a
systematic fashion may force a change in scheduling.  Nevertheless, priority
ranking is, and will continue to be, used to establish the order in which
projects are initiated and resources assigned.
     After the source category has been chosen, the types of facilities
within the source category to which the standard will apply must be deter-
mined.  A source category may have several facilities that cause air pollu-
tion, and emissions from some of these facilities may vary from insignificant
to very expensive to control.  Economic studies of the source category and
of applicable control technology may show that air pollution control is
better served by applying standards to the more severe pollution sources.
For this reason, and because there is no adequately demonstrated system for
controlling emissions from certain facilities, standards often do not apply
to all facilities at a source. For the same reasons, the standards may not
apply to all air pollutants emitted.  Thus, although a source category may
be selected to be covered by a standard of performance, not all pollutants
or facilities within that source category may be covered by the standards.
2.3  PROCEDURE FOR DEVELOPMENT OF STANDARDS OF PERFORMANCE
     Standards of performance must (1) realistically reflect best demon-
strated control practice; (2) adequately consider the cost, the non-air-
quality health and environmental impacts, and the energy requirements of
such control; (3) be applicable to existing sources that are modified or
reconstructed as well as new installations; and (4) meet these conditions
for all variations of operating conditions being considered anywhere in the
country.
     The objective of a program for developing standards is to identify the
best technological system of continuous emission reduction that has been
adequately demonstrated.  The standard-setting process involves three
principal phases of activity:  (1) information gathering, (2) analysis of
the information, and (3) development of the standard of performance.
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      During the information-gathering phase, industries are queried through
 a telephone survey, letters of inquiry, and plant visits by EPA representa-
 tives.  Information is also gathered from many other sources,  and a litera-
 ture search is conducted.  From the knowledge acquired about the industry,
 EPA selects certain plants at which emission tests are conducted to provide
 reliable data that characterize the pollutant emissions from well-controlled
 existing facilities.
      In the second phase of a project,  the information about the industry
 and the pollutants emitted is used in analytical  studies.   Hypothetical
 "model  plants" are defined to provide a common basis  for analysis.   The
 model  plant definitions, national  pollutant emission  data,  and  existing
 State  regulations  governing emissions from the source category  are  then
 used in establishing  "regulatory alternatives."   These regulatory alterna-
 tives  are  essentially different levels  of emission  control.
     EPA conducts  studies to determine  the impact of  each regulatory alter-
 native  on  the  economics  of the  industry and on the  national  economy, on the
 environment, and on energy consumption.   From  several  possibly  applicable
 alternatives,  EPA  selects the single  most plausible regulatory  alternative
 as  the  basis for a standard of  performance for the  source category  under
 study.
     In  the third  phase  of a project, the selected  regulatory alternative
 is  translated  into a  standard of performance,  which,  in  turn, is written in
 the  form of a  Federal  regulation.  The  Federal regulation, when  applied to
 newly constructed  plants,  will  limit  emissions to the  levels indicated in
 the  selected regulatory  alternative.
     As  early  as is practical in each standard-setting project,  EPA repre-
 sentatives discuss the possibilities of a  standard and the form  it might
 take with members  of  the  National Air Pollution Control Techniques Advisory
 Committee.  Industry  representatives and other interested parties also
 participate in these meetings.
     The information acquired in the project is summarized in the Background
 Information Document  (BID).  The BID, the  standard, and a preamble explain-
 ing the  standard are widely circulated to  the industry being considered for
 control, environmental groups, other government agencies, and offices
within EPA.  Through this extensive review process, the points  of view of
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expert reviewers are taken into consideration as changes are made to the
documentation.
     A "proposal package" is assembled and sent through the offices of EPA
Assistant Administrators for concurrence before the proposed standard is
officially endorsed by the EPA Administrator.  After being approved by the
EPA Administrator, the preamble and the proposed regulation are published
in the Federal Register.
     As a part of the Federal Register announcement of the proposed
regulation, the public is invited to participate in the standard-setting
process.  EPA invites written comments on the proposal and also holds a
public hearing to discuss the proposed standard with interested parties.
All public comments are summarized and incorporated into a second volume
of the BID.  All information reviewed and generated in studies in support
of the standard of performance is available to the public in a "docket" on
file in Washington, D. C.
     Comments from the public are evaluated, and the standard of performance
may be altered in response to the comments.
     The significant comments and EPA'.s position on the issues raised are
included in the "preamble" of a promulgation package," which also contains
the draft of the final regulation.  The regulation is then subjected to
another round of review and refinement until it is approved by the EPA
Administrator.  After the Administrator signs the regulation, it is published
as a "final rule" in the Federal Register.
2.4  CONSIDERATION OF COSTS
     Section 317 of the Act requires an economic impact assessment with
respect to any standard of performance established under Section 111
of the Act.  The assessment is required to contain an analysis of:
(1) the costs of compliance with the regulation, including the extent to
which the cost of compliance varies depending on the effective date of
the regulation and the development of less expensive or more efficient
methods of compliance; (2) the potential inflationary or recessionary
effects of the regulation; (3) the effects the regulation might have on
small business with respect to competition; (4) the effects of the regulation
on consumer costs; and (5) the effects of the regulation on energy use.
Section 317 also requires that the economic impact assessment be as
extensive as practicable.
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      The economic impact of a proposed standard upon an industry is usually
 addressed both in absolute terms and in terms of the control  costs that
 would be incurred as a result of compliance with typical, existing State
 control regulations.  An incremental approach is necessary because both new
 and existing plants would be required to comply with State regulations in
 the absence of a Federal standard of performance.   This approach requires a
 detailed analysis of the economic impact from the  cost differential  that
 would exist between a proposed standard of performance and the typical
 State standard.
      Air pollutant emissions may cause water pollution problems, and captured
 potential  air pollutants may pose a  solid waste disposal  problem.   The
 total  environmental  impact of an emission source must, therefore,  be analyzed
 and the costs determined whenever possible.
      A thorough study of the profitability and  price-setting mechanisms  of
 the industry is essential  to the analysis so that  an  accurate  estimate of
 potential  adverse economic impacts can be made  for proposed standards.   It
 is  also essential  to know the capital  requirements for pollution control
 systems already placed on  plants so  that  the additional capital  requirements
 necessitated by these Federal  standards can  be  placed  in  proper  perspective.
 Finally, it  is  necessary to  assess the availability of capital to  provide
 the additional  control  equipment needed to meet  the standards  of performance.
 2.5 CONSIDERATION OF ENVIRONMENTAL  IMPACTS
     Section  102(2)(C)  of  the National Environmental Policy Act  (NEPA) of
 1969 requires Federal  agencies to  prepare detailed environmental impact
 statements on proposals  for  legislation and  other major Federal  actions
 significantly affecting  the  quality of the human environment.  The objective
 of  NEPA is to build  into the decisionmaking  process of  Federal agencies a
 careful consideration  of all environmental aspects of proposed actions.
     In a number of  legal  challenges to standards of performance for various
 industries,  the United States Court of Appeals for the District of Columbia
 Circuit has held that environmental impact statements need not be prepared
 by  the Agency for proposed actions under section 111 of the Clean Air Act.
 Essentially, the Court of Appeals has determined that the best system of
emission reduction requires the Administrator to take into account counter-
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productive environmental .effects of a proposed standard, as well as economic
costs to the industry.  On this basis, therefore, the Court established a
narrow exemption from NEPA for EPA determination under section 111.
     In addition to these judicial determinations, the Energy Supply and
Environmental Coordination Act (ESECA) of 1974 (PL-93-319) specifically
exempted proposed actions under the Clean Air Act from NEPA requirements.
According to section 7(c)(l), "No action taken under the Clean Air Act
shall be deemed a major Federal action significantly affecting the quality
of the human environment within the meaning of the National Environmental
Policy Act of 1969." (15 U.S.C. 793(c)(l))
     Nevertheless, the Agency has concluded that the preparation of environ-
mental impact statements could have beneficial effects on certain regulatory
actions.  Consequently, although not legally required to do so by sec-
tion 102(2)(C) of NEPA, EPA has adopted a policy requiring that environmen-
tal impact statements be prepared for various regulatory actions, including
standards of performance developed under section 111 of the Act.  This
voluntary preparation of environmental impact statements, however, in no
way legally subjects the Agency to NEPA requirements.
     To implement this policy, a separate section in this document is
devoted solely to an analysis of the potential environmental impacts associ-
ated with the proposed standards.  Both adverse and beneficial impacts in
such areas as air and water pollution, increased solid waste disposal, and
increased energy consumption are discussed.
2.6  IMPACT ON EXISTING SOURCES
     Section 111 of the Act defines a new source as ". . . any stationary
source, the construction or modification of which is commenced ..." after
the proposed standards are published.  An existing source is redefined as a
new source if "modified" or "reconstructed" as defined in amendments to the
general provisions of Subpart A of 40 CFR Part 60, which were promulgated
in the Federal Register on December 16, 1975 (40 FR 58416).
     Promulgation of a standard of performance requires States to establish
standards of performance for existing sources in the same industry under
section 111 (d) of the Act if the standard for new sources limits emissions
of a designated pollutant (i.e., a pollutant for which air quality criteria
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have not been issued under section 108 or which has not been listed as a
hazardous pollutant under section 112).  If a State does not act, EPA must
establish such standards.  General provisions outlining procedures .for
control of existing sources under section lll(d) were promulgated on Novem-
ber 17, 1975, as Subpart B of 40 CFR Part 60 (40 FR 53340).
2.7  REVISION OF STANDARDS OF PERFORMANCE
     Congress was aware that the level of air pollution control  achievable
by any industry may improve with technological  advances.  Accordingly,
section 111 of the Act provides that the Administrator ". .  .  shall, at
least every 4 years, review and, if appropriate, revise ..." the standards.
Revisions are made to assure that the standards continue to  reflect the
best systems that become available in the future.  Such revisions will not
be retroactive, but will apply to stationary sources constructed or modified
after the proposal of the revised standards.
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                   3.  THE NON-METALLIC MINERALS INDUSTRY
3.1  GENERAL
     There are many non-metallic minerals which are individually produced
in a wide range of quantities.  For example, the annual  domestic demand  for
sand, gravel and stone is quoted in millions of tons,  whereas  the production
of industrial diamonds and gem stones is measured in carats.   Previous EPA
studies have investigated some of these non-metallic minerals,  namely, coal,
phosphate rock and asbestos.   The 18 non-metallic minerals  selected  for  in-
vestigation in this study are:
                Crushed and Broken Stone
                Sand and Gravel
                Clay
                Rock Salt
                Gypsum
                Sodium compounds
                Pumice
                Gilsonite
                Talc
                                            Boron
                                            Barite
                                            Fluorspar
                                            Feldspar
                                            Diatomite
                                            Perlite
                                            Vermiculite
                                            Mica
                                            Kyanite
These 18 categories are based upon Bureau of Mines classifications and are
the highest mined production segments of the non-metallic minerals industry
which have crushing and grinding operations, excluding coal, phosphate
rock, and asbestos.
     Total domestic production of these non-metallic minerals for 1975 was
about 1605 million megagrams (1769 million short tons).  The estimated domes-
tic production level of these minerals in 1980 has been projected to be 1829
million megagrams (2017 million short tons).  Value of the minerals ranges
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from 1.1 dollars/megagram (1.0 dollars/ton) for low grade clay, to 276 dollars/
megagram (250 dollars/ton) for high grade talc.  Geographically, the non-metallic
minerals industry is highly dispersed, with all States reporting production of
at least one of these 18 non-metallic minerals.  The industry is also extremely
diverse in terms of production capacities per facility (from 5 to several  thousand
tons per hour) and end product uses.
3.1.1  Industry Characteristics
     Table 3.1 presents  industry characteristics for each mineral under con-
sideration.   Crushed stone and sand and  gravel are by far the largest segments,
accounting for 1523 million megagrams  (1680 million tons) of the  1605 million
megagrams (1769 million  tons) produced by  the  18 industries.  There are about
5500 processing plants in the sand  and gravel  industry and about  4800 quarries
worked  in the crushed stone industry.  Each of the other industries has less
than 100 processing plants, except  for the clay industry which has about 120
plants.
     Sand and gravel plants are located  in every state.  Crushed  stone plants
are located  in every state except Delaware.  Clay plants are located in every
state except Vermont, Rhode Island, and  Alaska.  Processing plants for the
other industries are usually distributed among a few states where those
minerals deposits are located.  One of the minerals is principally mined and
processed in only one state:  boron only in California.
     Projected growth rates are also presented in Table 3.1.  The growth rates
are projected to increase at compounded  annual rates of up to 6 percent
through the  year 1985.
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TABLE 3-1  INDUSTRY CHARACTERISTICS1'3
Mineral
Crushed and
broken stone
Sand and gravel
Clay
Rock Salt
Gypsum (crude)
Sodium
compounds
Pumice
G1lson1te
Talc
Boron
Barlte
Fluorspar
1975
Production
1000 megagrams (1000 tons)
807,000 (890,000)
716,015 (789,432)
44,485 (49,047)
14,928 (13,540)
8,844 (9,751)
4,529 (4,895)
3,530 (3,892)
90 (100)
875 (965)
1,063 (1,172)
1,167 (1,287)
126 (140)
1975
Price
(Dollars/Mq)
2.63
1.97
1.10-221.00
29.78
5.05
46. 54-45. 75f
3.1-7
-
5.50-276.00
no
17.71
88-106
Annual
growth rate
(*)
4.0
1.0
3.3
2.0
2.0
2.5
3.5
2.0
4.0
5.0
2.2
3.0
Major producing states -'Number of active
in order of production operations
Pennsylvania 4800 (quarries)
Illinois
Texas
Florida
Ohio
Alaska 5500 (plants)
California
Michigan
Illinois
Texas
Ohio
Georgia 120
Texas
Ohio
North Carolina
Texas 21
New York
Louisiana
California 69 (mines)
Michigan
Iowa
Texas
California 37
Texas
Oregon. 235
California
Arizona
New Mexico
Utah 1
Vermont ' 52
Texas
California
California 6 -^.
Nevada 31
Missouri
Illinois 15
(continued)
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                                    TABLE  3.1  (continued)
Mineral
Feldspar
Oiatoraite
Peril te
Veraiculite
Mica
fyanite
1975
Production
1000 megagrams (1000 tons)
607
519
640
299
122
85
(670)
(573)
(706)
(330)
(135)
(94)**
1975
Price
(Dollars/Hg)
19.30
88.25
15.72
46.06
42.64
-
Annual
growth rate
(« '
4.0
5.5
4.0
4.0
4.0
6.0
Major producing states
in order of production
North Carolina
California
Kansas
Nevada
New Mexico
Montana
South Carolina
North Carolina
New Mexico
Virginia
Georgia
Hunter of active
operations
15
16
1.3
2
17
3






Natural  soda ash.
Sodium sulfate price.
Estimates for 1974.
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 3.1.2  End Uses
      End uses for the non-metallic minerals are many and diverse.   The  min-
 erals may be used either directly in their natural  state or processed  into
 a variety of manufactured products.  Generally, they can be classified  as
 either minerals for the construction industry;  minerals  for the chemical and
 fertilizer industries; or clay, ceramic, refractory and  miscellaneous min-
 erals.  Minerals generally used for construction are crushed and broken stone,
 sand and gravel, gypsum, gilsonite, perlite,  pumice, vermiculite, and mica.
 Minerals generally used in the chemical  and fertilizer industries are barite,
 fluorspar, boron, rock salt,  and sodium  compounds.   Clay,  feldspar,  kyanite,
 talc and diatomite can be generally classified  as clay,  ceramic, refractory,
 and miscellaneous minerals.   Table 3.2 lists  the major uses  of  each  individual
 mineral.
 3.1.3  Rock Types and Distribution
      Major rock types processed by the crushed  and  broken  stone industry in-
 clude limestone and  dolomite  (which accounted for 73.2 percent  of the total
 tonnage  in 1973 and  has  the widest and most important end  use range); granite
'(11.4 percent),  trap rock  (7.9 percent)  and sandstone, quartz and quartzite
 (2.9 percent).   Rock types including calcereous  marl, marble, shell, slate
 and  miscellaneous others accounted for only 4.6  percent.   Classifications used
 by  the industry vary considerably  and in many cases  do not reflect actual
 geological  definitions.
      Limestone  and dolomite are sedimentary rocks formed from accumulations of
 animal remains  or chemical precipitation of carbonates in  water.  In a  pure
 state, limestone  consists of  crystalline or granular calcium carbonate
 (calcite), while  dolomite consists  of calcium-magnesium carbonate (dolomite).
                                      3-5

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        TABLE 3.2  MAJOR USES OF THE NON-METALLIC MINERALS
         Mineral
                Major uses
Crushed and broken stone
Sand and gravel
Clay
Rock salt
Gypsum
Sodium compounds
Pumi ce
Gilsonite
Talc
Boron
Ban' te
Fluorspar
Feldspar
Diatomite
Perlite
Vermiculite
Mica
Kyanite
 Construction, lime manufacturing
. Construction
 Bricks, cement, refractory, paper
 Highway use, chlorine
 Wallboard, plaster, cement, agriculture
 Glass, chemicals, paper
 Road construction, concrete
 Asphalt paving
 Ceramics, paint, toilet preparations
 Glass, soaps, fertilizer
 Drilling mud, chemicals
 Hydrofluoric acid, iron and steel, glass
 Glass, ceramics
 Filtration, filters
 Insulation, filter aid, plaster aggregate
 Concrete
 Paint, joint cement, roofing
 Refractories, ceramics
                                3-6

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Both are often found together in the same rock deposit.  Depending on the pro-
portions of each, the rock may be classified as limestone, dolomitic limestone,
calcareous dolomite or dolomite.  Deposits are common and are distributed
throughout most parts of the country, although primarily located in the Central,
Middle Atlantic and South Atlantic regions which combined accounted for over
93 percent of the total production in 1973.
     Commercially, granite consists of any light-colored, coarse-grained
igneous rock.  It is composed chiefly of quartz, feldspar and, usually mica.
Deposits are located in the South Atlantic, northeastern, North Central  and
western regions of the country.   The South Atlantic region accounted for more
than 77 percent of the total  tonnage of granite produced in 1973.
     Trap rock includes any dark colored, fine-grained igneous rock composed
of the ferro-magnesian minerals  and basic feldspars with little or no quartz.
Common varieties include basalts, diabases and gabbros.   Deposits  are mostly
found in the New England, Middle Atlantic and Pacific regions, which combined
accounted for 76 percent of all  trap rock produced in 1973.
     Sandstones and quartzitic rocks are scattered throughout the  country.
Sandstones are sedimentary rocks composed predominantly of cemented quartz
grains.  The cementing material  may be calcium carbonate, iron oxide or clay.
Quartzites are metamorphosed  siliceous sandstones.   All  regions accounted for
some production of sandstone  and quartz, with the  Pacific and West South
Central and Middle Atlantic States combining for 60 percent of the total.
     Sand and gravel  are products of the weathering of rocks and thus consist
predominantly of silica.   Often, varying amounts of other minerals such  as  iron
oxides, mica, and feldspar are present.   Deposits  are common and are distributed
throughout the country.
                                     3-7

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     Clays are a group of fine-grained non-metallic minerals  which  are mostly
hydrous aluminum silicates that contain various amounts of organic  and inorganic
impurities.  Clays are classified into six groups by the Bureau  of  Mines:
kaolin, ball clay, fire clay, bentonite, fuller's earth, and  miscellaneous
(common) clay.
     Kaolin is a clay in which the predominant clay mineral  is kaolinite.   Large
quantities of high quality kaolin are found in Georgia.  Ball clay  consists
principally of kaolinite, but has a higher silica-to-alumina  ratio  than is  found
in most kaolin, as well as larger quantities of mineral impurities  and much
organic material.  Ball clays are mined in Kentucky, Tennessee,  and New Jersey.
     The terms "fire clay" and "stoneware clay" are based on  refractoriness or
on intended usage (fire clay indicating potential use for refractories, and
stoneware clay indicating uses for such items as crocks, jugs, and  jars).   Fire
clays are basically kaolinitic but include other clay minerals and  impurities.
Included under the general term fire clay are the diaspore, burley, and burley-
flint clays.  Fire clay deposits are widespread in the United States, with  the
greatest reserves being found in the Middle Atlantic region.
     Bentonites are composed essentially of minerals of the montmorillonite
group.  The swelling type has a high sodium iron concentration,  whereas the
nonswelling types are usually high in calcium.  Bentonite is  presently produced
in Wyoming and Montana.
     Fuller's earths are essentially montmorillonite or attapulgite.  A small
area in Georgia and Florida contains the known reserve of attapulgite-type
fuller's earth.
     The term "miscellaneous (common) clay" is a statistical  designation used
by the  Bureau of Mines to refer to clays and shales not included under the  other
                                     3-8

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 five  clay  types.   Miscellaneous clay may contain some kaolinite and mont-
 morillonite,  but  illite usually predominates, particularly in the shales.
 Miscellaneous  clay is widespread throughout the United States.
      Rock  salt consists of sodium chloride and is the chief source of.all
 forms of sodium.   Rock salt is mined on a large scale in Michigan, Texas,
 New York,  Louisiana, Ohio, Utah, New Mexico, and Kansas.
      Gypsum is a  hydrous calcium sulfate normally formed as a chemical pre-
 cipitate from  marine waters of high salinity.  Domestic reserves of gypsum
 are geographically distributed in 23 states.  Areas deficient in gypsum
 reserves are Minnesota, Wisconsin, the Pacific Northwest, the New England States,
 the deep South to  the east of Louisiana, and northern California.
     Sodium is a  chemically reactive metallic element used chiefly in the form
 of its many compounds.  Although too reactive to be found in the uncombined form
 in nature, the compounds of sodium are plentiful.  Sodium chloride (salt) is
 the chief source of all forms of sodium.  Increasing quantities of sodium car-
 bonate (soda ash)  and sodium sulfate (salt cake)  are produced from natural  de-
 posits of these compounds, but salt is still  the main source of both.  Natural
 sodium carbonate occurs in Wyoming and saline lake brines in California.
 Natural  sodium sulfate is produced from deposits in California, Texas, and
 Wyoming.
     Pumice is a rock of igneous origin, ranging from acidic to basic in  com-
 position, with a cellular structure formed by explosive or effusive volcanism.
The commercial designation includes the more precise petrographic descriptions
for pumice, pumicite (volcanic ash), volcanic cinders,  and scoria.   Deposits
are mostly found in the Western States.
                                    3-9

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     The mineral gilsonite is a variety of native asphalt which has many appli-
cations.  Gilsonite occurs in large boulders, several inches across.  It is
a black, lustrous mineral found in the Uintah basin in Utah and Colorado.
     The mineral talc is a soft hydrous magnesium silicate, 3 MgO-ASiCvH^O.
The talc of highest purity is derived from magnesium-rich metamorphic
carbonate rocks; less pure talc from metamorphosed ultra basic igneous rocks.
Soapstone is a term used for a massive form of rock containing the mineral.
Pyrophyllite (Al203«4Si02-H20) is a hydrous aluminum silicate similar to talc
in properties.  It is principally found in North Carolina.  Talc-group min-
erals are principally produced in New York, Texas, Vermont, California, and
Montana.
     Boron is a versatile and useful element used mainly in the form of its
many compounds, of which borax and boric acid are the best known.   Many min-
erals contain boron, but only a few are commercially valuable as sources of
boron.  The principal boron minerals are borax, kernite, and colemanite.
Half of the commercial world reserves are in southern California as bedded
deposits of borax (sodium borate) and colemanite (calcium borate), or as solu-
tions of boron minerals in Searles Lake brines.
     Barite is almost pure barium sulfate (BaSOiJ  and is the principal  com-
mercial mineral source of barium and barium compounds.   The reserves are
principally in Missouri and the southern Appalachian States, the remainder
is in Arkansas, Nevada, and California.
     Fluorine is derived from the mineral  fluorite (CaF2), commonly known as
fluorspar.  Fluorspar is principally found in deposits  located in  Kentucky
and Illinois.
                                    3-10

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     Feldspar is a general term used to designate a group of closely  related
minerals, especially abundant in igneous rocks and consisting essentially  of
aluminum silicates in combination with varying proportions of potassium, sodium,
and calcium.  The principal feldspar species are orthclase or microcline
(both K20-Al203-6Si02), albite (Na20'Al203-6Si02) and anorthite (CaO-Al203-
2Si02).  North Carolina is the foremost domestic producers followed in  order
of output by California, Connecticut, and Georgia.
     Diatomite is a material of sedimentary origin consisting mainly  of an
accumulation of skeletons or frustules formed as a protective covering  by
diatoms, single-celled microscopic plants.  The skeletons are essentially
amorphous hydrated or opaline silica but occasionally are partly composed  of
alumina.  The terms "diatomaceous earth" and "kieselguhr" are sometimes used
interchangeably and are synonymous with diatomite.  Diatomite is found  only in
the Western States with a substantial part of the total  reserve found in the
Lompoc, California area.
     Perlite is chemically a metastable amorphous aluminum silicate with minor
impurities and inclusions of various other metal oxides  and minerals.  Perlite
is mostly found in the Western States.
     Vermiculite is a micaceous mineral with a ferromagnesiurn-aluminum  silicate
composition and the property of exfoliating to a low-density material when
heated.  Presently, vermiculite is mined from deposits located in Montana  and
South Carolina.
     Mica is a group name for a number of complex hydrous potassium aluminum
silicate minerals differing in chemical composition and  physical properties but
characterized by excellent basal cleavage that facilitates splitting  into  thin,.
tough, flexible, elastic sheets.  These minerals can be  classified into four
                                    3-11

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principal types named after the most common mineral  in each group -  muscovite
(potassium mica), phlogopite (magnesium mica), biotite (iron mica),  and lepi-
dolite (lithium mica).  The major producing regions  in the United States are
the Southeast and West.
     Kyanite and the related minerals - andalusite,  sillimanite, dumortierite,
and topaz - are natural aluminum silicates which can be converted to mullite,
a stable refractory raw material.  Reserves of kyanite and the related min-
erals are mostly found in Virginia, North and South  Carolina, Idaho, and
Georgia.
3.2  NON-METALLIC MINERALS PREPARATION PROCESSES AND THEIR EMISSIONS
3.2.1  General Process Description
     Non-metallic mineral processing involves extracting from the ground;
loading, unloading, and dumping, conveying, crushing, screening, milling, and
classifying.  Some minerals processing also includes washing, drying, calcin-
ing, or  flotation operations.  The operations performed depend on the rock
type and the desired  product.
     The mining  techniques used for the extraction of non-metallic minerals
vary with the particular mineral, the nature of the deposit, and the location
of  the deposit.  Mining is carried out both underground and in open pits.
Some minerals require blasting while others can be removed by bulldozer or
dredging operations alone.
     The non-metallic minerals are normally delivered to the processing plant
by  truck, and dumped  into a hoppered feeder, usually a vibrating grizzly type,
or  on to screens, as  illustrated in Figure 3.1.  These screens separate or
scalp the larger boulders from the finer  rocks that do not require primary
crushing, thus minimizing the load to the primary crusher.  Jaw or gyratory

                                    3-12

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                                                        re

                                                        ti-
                                                        er)
                                                        c
                                                        3
                                                        u
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3-13

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crushers  are  usually used for initial  reduction, although impact crushers are
gaining favor for crushing low-abrasion rock, such as limestones, and talc, and
where  high  reduction ratios are  desired.   The crusher product, normally 7.5
to 30  centimeters (3 to  12 inches)  in  size,  and the grizzly throughs (undersize
material) are discharged onto a  belt conveyor and normally transported to either
secondary screens and crusher, or to a surge pile or silo for temporary storage.
     The  secondary screens  generally separate the process  flow into  either  two  or
three  fractions  (oversize,  undersize,  and  throughs)  prior  to  the  secondary  crusher,
The oversize  is  discharged  to the  secondary  crusher  for  further  reduction.   The
undersize,  which  require no further  reduction at  this  stage,  normal1y  by-pass the
secondary crusher.   A third fraction,  the  throughs,  is separated  when  processing
some minerals.   Throughs contain  unwanted  fines  that  are usually  removed  from the
process flow  and  stockpiled as crusher-run material.   For  secondary  crushing,
gyratory  or cone crushers are most commonly  used, although impact crushers  are
used at some  installations.
     The  product  from the secondary  crushing  stage,  usually 2.5 centimeters  (one
inch)  or  less  in  size, is  normally transported to  a  secondary  screen for  further
sizing.   Sized material  from  this  screen is  either discharged  directly to a
tertiary  crushing  stage  or  conveyed  to  a'fine-ore  bin which supplies the milling
stage.  Cone  crushers  or  hammermills are normally  used for tertiary crushing.  Rod
nil Is, ball  mills,  and hammermills   are normally  used in the milling stage.  The
product from  the tertiary crusher or the mill is  usually conveyed to a type of
classifier  such  as  a  dry  vibrating screen system,  an air separator, or a wet rake
or spiral  system  (if  wet  grinding was employed) which also dewaters the material.
The oversize  is  returned  to the tertiary crusher or mill  for further size
reduction.  At this  point,  some mineral end  products of  the desired grade are
                                    3-14

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conveyed directly to finished product bins, or are stockpiled  in open  areas  by
conveyors or trucks.  Other minerals such  as talc or  barite may require  ai>-
classification to obtain the required mesh  size, and  treatment by  flotation  to
obtain the necessary chemical purity and color.
     Most non-metallic minerals  require additional processing  depending  on the  rock
type and consumer requirements.   In certain cases, especially  in the crushed stone
and sand and gravel industry, stone washing may be required to meet  particular  end
product specifications or demands  such as  for concrete  aggregate.  Some  minerals,
especially certain  lightweight aggregates,  are washed and  dri-ed, sintered, or
treated prior to primary crushing.  Others  are dried  following secondary crushing
or milling.  Sand and gravel, crushed and  broken stone,  and most lightweight
aggregates normally are not milled and are  screened and  shipped to the consumer
after secondary or  tertiary crushing.  Table 3.3 lists  the various unit  process
operations for each industry under consideration.  Figures 3.1 and 3.2 show
simplified diagrams of the typical process  steps required  for  the  non-metallic
minerals investigated in this report.
3.2.2  Process Unit Operations and Their Emissions
     Essentially all mining and  mineral processing operations  are  potential  sources
of particulate emissions.  Emissions may be categorized  as either  fugitive
emissions or fugitive dust.  Operations included within  each category  are listed .in
Table 3.4.  Fugitive emission sources include those sources for which  emissions are
amenable to capture and subsequent control.  Fugitive dust sources are not amenable
to control using conventional control systems and generally involve  the
reentrainment of settled dust by wind or machine movement.
Information available on emissions from uncontrolled  non-metallic  minerals
processing operations is limited.  Estimates developed  by  EPA  for  uncontrolled

                                     3-15

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         COARSE
           ORE
           BIN.
            GRIZZLY
              OR
            SCREEN
                      12
                     STOCKPILE
                     OR BIN>^     //
                     13    ^       I'
                            STOCKPILE
                            OR BIN
                            14
                                                             SECONDARY
                                                             CRUSHER
                                                           SIZE
                                                          ICLASSIFIER
Figure  3.2  General  Schematic  for Non-Metallic Minerals  Processing
                                   3-17

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        Table 3.4  EMISSION SOURCES AT NON-METALLIC MINERAL FACILTIES
           Fugitive Emissions
          Drilling
          Crushing
          Screening
          Grinding
          Conveyor  Transfer  Points
          Loading
Fugitive Dust Sources
   Blasting
   Haul ing
   Haul  Roads
   Stockpiles
   Plant yard
   Conveying
crushed stone  plant  process  operations  are  presented  in Table  3.5.  Based on
these estimates,  fugitive  emission  sources  alone  (excluding drilling and fines
milling) emit  about  5.5  kilograms of dust per megagram of material processed
(11 pounds per ton).
     The following emission  sources are discussed in  detail:  crushing,screening
and conveying  operations,  grinders, fine product loading and bagging operations.
This document  will only  briefly discuss mining operations.
3.2.2.1  Factors  that Affect Emissions from Mining and Process Operations
     In general,  the factors that affect emissions from most mineral  processing
operations include:  the type of ore processed, the type of equipment and
operating practices employed, the moisture content of the ore, the amount of ore
processed, and a  variety of geographical and seasonal  factors.  These factors,
discussed in more detail below, apply to both fugitive emission and fugitive dust
sources associated with mining and processing plant operation.
     The type of ore (rock) processed is important.   Soft rocks produce a higher
percentage of fine-grained material  than do hard rocks because of their greater
                                     3-18

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                                    Table 3.5

                         Particulate Emission  Factors  for
                              Stone Crushing Process^
Process Operation
Primary crushing

Secondary crushing and screening

Tertiary crushing and screening (if used)

Recrushing and screening

Fines mill

Screening, conveying and handling
Uncontrolled Emission Factor*
kg/Mg
0.25
0.75
3.0
2.5**
3.0
1.0
Ib/ton
0.5
1.5
6.0
5.0
6.0
2.0
 * Based on feed to the primary crusher.

** Assume 20 percent undergoes recrushing.  Thus, the emission factor becomes
   0.5 kg/mg (1.0 Ib/ton).
                                    3-19

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friability and lower resistance to fracture.5  Thus,  it  is  concluded that  the
processing of soft rocks results in a greater  potential  for uncontrolled emissions
than the processing of hard rock.  Major rock  types arranged in  order  of increasing
hardness are:  talc, clay, gypsum, barite, limestone  and dolomite,  perlite,
feldspar, and quartz.  Thus, talc could be expected to  exhibit the  highest
uncontrolled emissions and quartz the. least.
     The type of equipment and operating practices employed also affect  uncon-
trolled emissions.  In general, emissions from process  equipment such  as crushers,
screens, grinders, and conveyors depend on the size distribution of the  material
and the velocity that is mechanically imparted to the material.   For crushers,  the
particular type of crushing mechanism employed (compression or impact) affects
emissions.  The effect of equipment type on  uncontrolled emissions  from  all  sources
will be more fully discussed in subsequent sections of  this report(see Sections
3.2.2.3.1 to 3.2.2.3.5).
     The inherent moisture content or wetness  of the  rock processed can  have a
substantial effect on uncontrolled emissions.  This is  especially evident  during
mining, initial material handling and initial  plant process operation  such as
primary crushing.  Surface wetness causes fine particles to agglomorate  or adhere
to the faces of larger stones with a resultant dust suppression  effect.  However,
as new fine particles are created by crushing  and attrition, and as the  moisture
content is reduced by evaporation, this suppressive effect  diminishes  and  may even
disappear.  Depending on the geographic and  climatic  conditions, the moisture
content of the mined rock ranges from nearly zero to  several percent.
     With regard to geographical and seasonal  factors,  the primary  variables
affecting uncontrolled particulate emissions are wind parameters and moisture
content of the material.  Wind parameters will vary with geographical  location
                                       3-20 '

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 and  season  and  it  can  certainly be expected that the level of emissions from
 sources which are  not  enclosed (principally fugitive dust sources) will be
 greater during  periods of high winds than periods of low winds.  The moisture
 content of  the  material will also vary with geographical location and season.  It
 can,  therefore, be expected that the level of uncontrolled emissions from both
 fugitive emission  sources and fugitive dust sources will be greater in arid
 regions of  the.  country than in temperate ones and greater during the summer
 months due  to a higher evaporation rate.
 3.2.2.2  Mining Operations
      Sources of particulate emissions from mining operations include drilling,
 blasting, secondary breakage and the loading and hauling of the mineral to the
 processing  plant.  Not all non-metallic mineral deposits require drilling and
 blasting to fragment portions of the deposits into pieces of material of con-
 venient size for further processing.  Some mineral deposits can be removed
without blasting by the use of power equipment such as front-end loaders, drag
lines, and  dredges.
     Particulate emissions from drilling operations are primarily caused by the
removal  of cuttings and dust from the bottom of the hole by air flushing.
Compressed air is released down the hollow drill  center, forcing cuttings and
dust up and out the annular space formed between the hole wall  and drill.
     Blasting is used to displace solid rock from its quarry deposit and to frag-
ment it into sizes which require  a minimum of secondary breakage and which can
be readily handled by loading and hauling equipment.   The frequency of blasting
            ^.
ranges from several shots  per day to one per week depending on  the plant capacity
and the  size of individual  shots.   The  effectiveness  of a shot  depends on the
characteristics  of the explosive  and the rock.   Emissions from  blasting are
                                     3-21

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 evident from visual observations and are largely unavoidable.   The emissions
 generated are affected by the blasting practices employed and  are reduced during
 wet, low wind conditions.
      If secondary breakage is required, drop-ball  cranes are usually employed.
 Normally, a pear-shaped or spherical  drop-ball, weighing several  tons,  is
 suspended by a crane and dropped on the oversize rock as many  times as  needed  to
 break it.  Emissions are slight.
      The excavation and loading of broken rock is  normally performed by shovels
 and front-end loaders.   Whether the broken rock is dumped into a  haulage vehicle
 for transport or directly into the primary crusher, considerable  fugitive dust
 emissions may result.   The most significant factor affecting these emissions is
 the wetness of the rock.
      At most quarries,  large  capacity "off-the-road"  haulage vehicles are used to
 transport broken  rock from the quarry to  the primary  crusher over  unpaved haul
 roads.   This  vehicle traffic  on  unpaved roads  is responsible for a  large por-
 tion  of  the fugitive dust  generated by quarrying operations.  Factors affecting
 fugitive  dust emissions from  hauling  operations include the composition  of the
 road  surface, the wetness  of  the road, and the volume and speed of the vehicle
 traffic.
 3.2.2.3   Processing Plant  Facilities  and Their Emissions
     Principal processing  plant facilities include crushers, grinders, screens,
and material handling and transfer equipment.   As indicated by  Table 3.4, all
these units are potential sources of particulate emissions.  Emissions are
generally emitted from process equipment at feed and discharge  points and from
material  handling equipment at transfer points.
                                    3-22

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3.2.2.3.1  Crushing Operations
     Crushing is the process by which coarse material is reduced by mechanical
energy and attrition to a desired size for mechanical separation (screening).
The mechanical stress applied to rock fragments during crushing may be accom-
plished by either compression or impact.  These two methods of crushing differ
in the duration of time needed to apply the breaking force.  In impacting,
the breaking force is applied very rapidly, while in compression, the rock
particle is slowly squeezed and forced to fracture.  All types of crushers are
both compression and impaction to varying degrees.  Table 3.6 ranks crushers
according to the predominant crushing mechanism used (from top to bottom,
compression to impaction).  In all cases, there is some reduction by the rubbing
of stone on stone or on metal surfaces (attrition).
              TABLE 3.6.  RELATIVE CRUSHING MECHANISM UTILIZED
                          BY VARIOUS CRUSHERS6
                   Compression
                   Impaction
Double roll crusher
Jaw crusher
Gyratory crusher
Single roll crusher
Rod mill (low speed)
Ball mill
Rod mill (high speed)
Hammermill  (low speed)
Impact breaker
Hammermill  (high speed)
     The size of the product from compression type crushers is controlled by
the space between the crushing surfaces compressing the rock particle.  This
type of crusher produces a relatively closely graded product with a small
                                     3-23

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 proportion  of fines.   Crushers  that  reduce  by  impact, on the other hand, pro-
 duce  a  wide range of  sizes  and  a  high proportion of fines.
      Since  the  size reduction achievable by one machine is limited, reduction in
 stages  is frequently  required.  As noted previously, the various stages include
 primary, secondary, and perhaps tertiary crushing.  Basically, the crushers used
 in  the  non-metallic minerals industry are:  jaw, gyratory, roll and impact
 crushers.
 Jaw Crushers
      Jaw crushers consist of a  vertical fixed  jaw and a moving inclined jaw which
 is  operated by  a  single toggle  or a  pair of toggles.  Rock is crushed by
 compression as  a  result of  the  opening and closing action of the moveable j.aw
 against the fixed jaw.  Their principal application in the industry is for
 primary crushing.
      The most commonly used jaw crusher is the Balke or double-toggle type.
 As  illustrated  in  Figure 3.3, an  eccentric shaft drives a Pitman arm that
 raises  and  lowers  a pair of toggle plates to open and close the moving jaw
 which is suspended from a fixed shaft.  In a single-toggle jaw crusher, the
 moving  jaw  is itself suspended from an eccentric shaft and the lower part of
 the jaw supported  by a rolling toggle plate (Figure 3.4).   Rotation of the
 eccentric shaft produces a circular motion at the upper end of the jaw and
 an elliptical motion at the lower end.  Other types,  such as  the Dodge and
 overhead eccentric are used on a limited scale.
     The size of a jaw crusher is defined by its feed  opening dimensions  and
may range from about 15 x 30 centimeters to 213 x 168  centimeters  (6 x.12
 inches  to 84 x 66  inches).   The size reduction obtainable  may range from
 3:1  to  10:1  depending on the nature of the rock.   Capacities  are quite variable

                                    3-24

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                        MOVEABLE JAW
FIXED JAW
                                                   ECCENTRIC
                                                          PITMAN ARM
                    y
                 DISCHARGE
             Figure  3.3   Double-toggle Jaw  Crusher
               MOVEABLE JAW

                  FEED
           FIXED
            JAW
                    DISCHARGE
                                  TOGGLE
            Figure 3.4  Single-toggle Jaw Crusher
                                  3-25

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 depending on the unit and its discharge setting.   Table 3.7 presents  approximate
 capacities for a number of jaw crusher sizes at both minimum and maximum  dis-
 charge settings.
 Gyratory Crushers
      Simply, a gyratory crusher may be considered to be a  jaw crusher with
 circular jaws between which the material  flows  and is  crushed.   As  indicated in
 Table 3.8, however,  a gyratory crusher has  a much greater  capacity  than a jaw
 crusher with an equivalent feed opening.
      There are basically three types  of gyratory  crushers,  the pivoted spindle,
 fixed spindle and cone.   The fixed  and pivoted  spindle  gyratories are used for
 primary and secondary crushing, and cone  crushers for  secondary  and tertiary
 crushing.   The larger gyratories  are  sized  according to feed  opening  and the
 smaller units by cone diameters.
      The pivoted spindle gyratory (Figure 3.5)  has the  crushing  head mounted on
 a shaft that is  suspended  from  above  and free to  pivot.  The bottom of the shaft
 is seated  in  an  eccentric  sleeve which  revolves,  thus causing the crusher head
 to gyrate  in  a  circular  path within a  stationary  concave circular chamber.   The
 crushing action  is similar  to that of  a jaw crusher in that the crusher element
 reciprocates  to  and from a  fixed crushing plate.  Because some part of the
 crusher head  is working at  all times,  the discharge from the gyratory  is  con-
 tinuous rather than intermittent as  in a jaw crusher.  The  crusher setting  is
 determined by the wide-side opening  at the discharge end and is adjusted  by
 raising or lowering the crusher head.
     Unlike the pivoted spindle gyratory, the fixed spindle gyratory has  its
crushing head mounted on an eccentric sleeve fitted over a  fixed  shaft.  This
produces a uniform crushing stroke from the  top  to the bottom of  the crushing
chamber.
                                    3-26

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               Table 3.7  APPROXIMATE CAPACITIES OF JAW CRUSHER$(7)
                             (Discharge opening - closed)

Size
[cm.(in.)3

91 x
107 x
122 x
152 x
213 x

61
152
107
122
168

(36
(42
(48
(60
(84

x 24)
x 60)
x 42)
x 48)
x 66)
Smal 1 est
discharge
opening
[cm.(i
>6
10.2
12.7
12.7
20.3
in.)]
(3)
(4)
(5)
(5)
(8)
Capacity* Largest
[Mg/hr (tons/hr)3 discharge
opening

68
118
159
218
363

(75)
(130)
(175)
(240)
(400)
[cm.(i
15.2
20.3
20.3
22.9
30.5
in.)]
(6)
(8)
(8)
(9)
(12)
Capacity
[Mg/hr (tons/hr)]

145
181
250
408
544

(160)
(200)
(275)
(450)
(600)
*Based on rock weighing 1600 kg/m3 (100 Ib/cu ft.)


            Table 3.8  APPROXIMATE CAPACITIES OF GYRATORY CRUSHERS (8)
                              (Discharge opening - open)

Size
[cm. (in.)]


76 (30)
91 (36)
107 (42)
122 (48)
137 (54)
152 (60)
183 (72)
Smal 1 est
discharge
opening
[cm. (in.)]
10.2 (4)
11.4 (4.5)
12.7 (5)
14.0 (5.5)
16.5 (6.5)
17.8 (7)
22.9 (9)
Capacity*
[Mg/hr. (tons/hr)]


181 (200)
336 (370)
381 (420)
680 (750)
816 (900)
1088 (1,200)
1814 (2,000)
Largest
discharge
opening
[cm. (in.)]
16.5 (6.5)
17.8 (7)
19.1 (7.5)
22.9 (9)
24.1 (9.5)
25.4 (10)
30.5 (12)
Capacity
[Mg/hr. (tons/hr)]


408 (450) '
544 (600)
635 (700)
1088 (1,200)
1451 (1,600)
•1814 (2,000)
2721 (3,000)
*Based on rock weighing 1600 kg/m3 (100 Ib/cu ft.)
                                         3-27

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                    FEED
              FIXED
             THROAT'
    CRUSHING SURFACE
             ECCENTRIC
                                                        DRIVE
                   DISCHARGE
                  Figure 3.5  The Pivoted Spindle Gyratory
     For fine crushing, the gyratory is equipped with flatter heads and con-
verted to a cone crusher (Figure 3.6).  Commonly, in the lower section a
parallel zone exists.  This results in a larger discharge to feed area ratio
which makes it extremely suitable for fine crushing at high capacity.  Also,
unlike regular gyratories, the cone crusher sizes at the closed side setting
and not the open side (wide-side) setting.  This assures that the material
discharge will have been crushed at least once at the closed side setting.
Cone crushers yield a cubical  product and a hi.gh percentage of fines due to
interparticle crushing (attrition).  They are the most commonly used crusher
in the industry for secondary and tertiary reduction.   Table 3.9 presents
performance data for typical  cone crushers.
                                   3-28

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                                FEED
                    CRUSHING
                    SURFACES
                          DISCHARGE
                                                             DRIVE
                                                      ECCENTRIC
                           Figure 3.6  Cone Crusher
               TABLE 3.9  PERFORMANCE DATA FOR CONE CRUSHERS9
Size of
crusher
(m (ft)}
                              Capacity (Mg/hr (tons/hr))
                              discharge setting (cm (in))
                      (3/8)  1.3 (1/2)  1.9
                                           2.5 (1)   3.8 (1.5)
0.
0.
1.
1.
2.
6
9
2
7
1
(2) 18 (20)
(3) 32 (35)
(4) 54 (60)
(5.5)
(7)
23 (25) 23
36 (40) 64
73 (80) 109
181
229
(25)
(70)
(120)
(200)
(330)


136
250
408
_
-
150
275 308
450 544
_
-
-
(340)
(600)
Roll Crushers
     These machines are utilized primarily at intermediate or final reduction
stages and are often'used at portable plants.  There are essentially two types,
the single-roll and the double-roll.   As illustrated in Figure 3.7, the double-
roll crusher consists of two heavy parallel  rolls which are turned toward each
                                   3-29

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other at the same speed.  Roll speeds range from 50 to 300 rpm,  Usually, one
roll is fixed and the other set by springs.  Typically, roll diameters range
from 61 to 198 centimeters (24 to 78 inches) and have narrow face widths,
about half the roll diameter.  Rock particles are caught between the rolls and
crushed almost totally by compression.  Reduction ratios are limited and range
from 3 or 4 to 1.  These units produce few fines and no oversize.  They are
used especially for reducing hard stone to a final product ranging from 1/4
inch to 20 mesh.
                               FEED
                                  DISCHARGE
ADJUSTABLE
  ROLLS
                       Figure 3.7  Double-roll Crusher
     The working elements of a single-roll crusher include a toothed or
knobbed roll and a curved crushing plate which may be corrugated or smooth.
The crushing plate is generally hinged at the top and its setting is held by
a spring at the bottom.  A to.othed-roll crusher is depicted in Figure 3.8.
The feed  caught between the roll and crushing plate is broken by a combination
of compression, impact and shear.  These units may accept feed sizes up to
                                    3-30

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51 centimeters (20 inches) and have capacities up to 454 megagrams per hour
(500 tons/hr).  In contrast with the double-roll, the single-roll crusher is
principally used for reducing soft materials such as limestones.
              ROLL
                               FEED
                      TOOTH
CRUSHING
  PLATE
                            DISCHARGE
                       Figure 3.8  Single roll  Crusher
Impact Crushers
     Impact crushers, including hamrnermills and impactors, use the force of
fast rotating massive impellers or hammers to strike and shatter free falling
rock particles.  These units have extremely high reduction ratios and produce
a cubical product spread over a wide range of particle sizes with a large pro-
portion of fines, thus making their application in industry segments such as
cement manufacturing and agstone production extremely cost effective by reducing
the need for subsequent grinding machines.
     A hammermill consists of a high speed horizontal rotor with several rotor
discs to which sets of swing hammers are attached (Figure 3.9).  As rock
particles are fed into the crushing chamber, they are impacted and shattered  by
                                   3-31

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 the  hammers which attain tangential speeds as high as 76 meters  (250 feet) per
 second.  The shattered rock then  collides with a steel  breaker plate and is
 fragmented even further.  A cylindrical grating or screen positioned at the
 discharge opening restrains oversize material.until it is reduced to a size
 small enough to pass between the  grate bars.  Rotor speeds range from 250 to
 1800 rpm and capacities to over 907 megagrams per hour (1,000 tons/hr).  Prod-
 uct  size is controlled by the rotor speed, the spacing between the grate bars,
 and  by hammer length.
                            FEED
              BREAKER
               PLATE
                               \
/-l^
f^A-
*  V V^y T*
                                                  SWING
                                                  HAMMERS
                             /
                        DISCHARGE
                                                  GRATE BARS
                          Figure 3.9  Hammermill
     An impact breaker  (Figure 3.10) is similar  to a hammermill  except that  it
has no grate or screen  to act as a restraining member.  Feed is  broken by
impact alone.   Adjustable breaker bars are  used  instead of plates to reflect
material  back into the  path of the impellers.  Primary-reduction units are
                                  3-32

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 available which can reduce quarry run material  at over 907 megagrams  per hour
 (1,000 tons/hr) capacity to about 2.5 centimeters (1  inch).   These units are
 not appropriate for hard abrasive materials,  but are  ideal  for soft rocks like
 limestone.
                 BREAKER
                  PLATE
  BREAKER
     BARS
      FEED
                              /
                         HAMMER
ROTOR
                                  DISCHARGE
                         Figure 3.10  Impact Crusher
Sources of Emissions
     The generation of particulate emissions is inherent in the crushing pro-
cess.  Emissions are most apparent at crusher feed and discharge points.  Emis-
sions are influenced predominantly by the type of rock processed, the moisture
content of the rock, and the type of crusher used.
     The most important element influencing emissions from crushing equipment,
as previously mentioned, is the type of rock and the moisture content of the
mineral being crushed.   The crushing mechanism employed has a substantial
affect on the size reduction that a machine 'can achieve; the particle size
                                   3-33

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distribution of the product, especially the proportion of fines produced; and
the amount of mechanically induced energy which is imparted to fines.
     Crushing units utilizing impact rather than compression produce a larger
proportion of fines as noted above.  In addition to generating more fines,
impact crushers also impact higher velocity to them as a result of the fan-like
action produced by the fast rotating hammers.   Because of this and the high
proportion of fines produced, impact crushers  generate larger quantities  of
uncontrolled particulate emissions per ton of material processed than any other
crusher type.
     The level  of uncontrolled emissions from jaw, gyratory, cone and roll
crushers closely parallels the reduction stage to which they are applied. As
indicated in Table 3-5, emissions increase progressively from primary to
secondary to tertiary crushing.  Factors other than the type of crushing
mechanism (compression, impact) also affect emissions.  In all likelihood,
primary jaw crushers produce greater emissions than comparable gyratory because
of the bellows effect of the jaw and because gyratory crushers are usually
choke fed to minimize the open spaces from which dust may be emitted.  For
subsequent reduction stages, cone crushers produce more fines as a result of
attrition and consequently generate more dust:
3.2.2.3.2  Screening Operations
     Screening is the process by which a mixture of stones is separated accord-
ing to size.  In screening, material is dropped into a mesh surface with  open-
ings of desired size and separated into two fractions, undersize which passes
through the screen opening and oversize which is retained on the screen surface,
When material is passed over and through multiple screening surfaces, it  is
                                    3-34

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 separated  into  fractions  of  known particle size distribution.  Screening sur-
 faces may  be  constructed  of  metal bars, perforated or slotted metal plates, or
 woven wire cloth.
     The capacity of a screen is primarily determined by the open area of the
 screening  surface and the physical characteristics of the feed.  It is usually
 expressed  in  tons of material per hour per square foot of screen area.  Although
 screening  may be performed wet or dry, dry screening is the more common.
     Screening equipment  commonly used in the non-metallic minerals industry
 includes grizzlies, shaking  screens, vibrating screens, and revolving screens.
 Gri zzli es
     Grizzlies consist of a  set of uniformly spaced bars, rods or rails.  The
 bars may be horizontal or inclined and are usually wider in cross section at
 the top than the bottom.  This prevents the clogging or wedging of stone
 particles  between bars.  The spacing between the bars ranges from 5 to 20
 centimeters (2 to 8 inches).  Bars are usually constructed of manganese steel
 or other highly abrasion-resistant material.
     Grizzlies are primarily used to remove fines prior to primary crushing,
 thus reducing the load on the primary crusher.  Grizzlies may be stationary
 cantilevered (fixed at one end with the discharge end free to vibrate) or
mechanically vibrated.  Vibrating grizzlies are simple bar grizzlies mounted
on eccentrics (Figure 3-11).  The entire assembly is moved forward and backward
at about 100 strokes a minute, resulting in better flow through and across the
grizzly surface.
Shaking Screens
     The shaking screen consists of a rectangular frame with perforated plate or
wire cloth screening surfaces, usually suspended by rods or cables and inclined
                                    3-35

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at an angle of 14 degrees.  The screens are mechanically shaken parallel  to the
plane of material flow at speeds ranging from 60 to 800 strokes per minute and
at amplitudes ranging from 2 to 23 centimeters (3/4 to 9 inches).10  Generally,
they are used for screening coarse material, 1.3 centimeters (1/2-inch) or
larger.
                       Figure 3.11  Vibrating Grizzly
Vibrating Screens
     Where large capacity and high efficiency are desired, the vibrating screen
has practically replaced all other screen types.  It is by far the most commonly
used screen type in the non-metallic minerals industry.  A vibrating screen
(Figure 3.12) essentially consists of an inclined flat or slightly convex
screening surface which is rapidly vibrated in a plane normal  or nearly normal
to the screen surface.  The screening motion is of small  amplitude but high  .
frequency, normally in excess of 3,000 cycles per minute.   The vibrations may
                                    3-36

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 be generated  either  mechanically  by means of an eccentric shaft, unbalanced fly
 wheel,  cam and  tapp.et  assembly, or electrically by means of an electromagnet.
                        Figure 3.12  Vibrating Screen
     Mechanically-vibrated units are operated at about 1,200 to 1,800 rpm and
at amplitudes of about 0.3 to 1.3 centimeters (1/8 to 1/2 inch).   Electrically
vibrated screens are available in standard sizes from 30 to 180 centimeters
(12 inches to 6 feet) wide and 0.76 to 6.1 meters (2-1/2 to 20 feet) long.
A complete screening unit may have one, two or three decks.
Revolving Screens
     This screen type consists of an inclined cylindrical frame around which
is wrapped a screening surface of wire cloth or perforated plate.   Feed material
is delivered at the upper end and, as the screen is rotated, undersized material
passes through the screen openings while the oversized is discharged at the
lower end.  Revolving screens are available up to 1.2 meters (4 feet)  in dfam-
eter and usually run at 15 to 20 rpm.11
                                     3-37

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Source of Emissions
     Dust is emitted from screening operations as a result of the agitation of
dry material.  The level of uncontrolled emissions depends on the quantity of
fine particles contained in the material, the moisture content of the material
and the type of screening equipment.  Generally, the screening of fines produces
higher emissions than the screening of coarse materials.  Also, screens agi-
tated at large amplitudes and high frequency emit more dust than those operated
at small amplitudes and low frequencies.
3.2.2.3.3  Conveying Operation
     Materials handling devices are used to convey materials from one point to
another.  The most common include feeders, belt conveyors, bucket elevators,
screw conveyors, and pneumatic systems.
Feeders
     Feeders are relatively short, heavy-duty conveyance devices used to re-
ceive material and deliver it to process units, especially crushers, at a uni-
fonr. regulated rate.  The various types used are the apron, belt,  reciprocating
plate, vibrating, and wobbler feeders.
     Apron feeders are composed of overlapping metal  pans or aprons  which are
hinged or linked by chains to form an endless conveyor supported by  rollers
and spaced between a head and tail assembly.  These feeders are constructed to
withstand high impact and abrasion and are available in various widths (18 to
27 inches) and lengths.
     Belt feeders are essentially short, heavy duty belt conveyors equipped
with closely spaced support rollers.   Adjustable gates are used to regulate
feed rates.   Belt feeders are available in 46 to 122 centimeter (18  to 48 inch)
                                    3-38

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widths  and 0.9 to 3.7 meter  (3 to  12 foot) lengths and are operated at speeds
of  12.2  to 30.5 meters  (40 to 100  feet) per minute.
      Reciprocating  plate  feeders consist of a heavy-duty horizontal plate which
is  driven in  a reciprocating motion causing material to move forward at a uni-
form  rate.  The feed rate is controlled by adjusting the frequency and length
of  the  stroke.
      Vibrating feeders  operate at  a relatively high frequency and low amplitude.
Their feed rate is  controlled by the slope of the  feeder bed and the amplitude
of  the  vibrations.  These feeders  are available  in. a variety of sizes, capa-
cities  and drives.  When  combined  with a grizzly,  both scalping and feeding
functions are performed.
      Wobbler  feeders also perform  the dual task  of scalping and feeding.  These
units consist of a  series of closely spaced elliptical bars which are
mechanically  rotated, causing oversize material  to tumble forward to the dis-
charge  and undersize material to pass through the  spaces.  The feed rate is
controlled by the bar spacing and  the speed of rotation.
Belt  Conveyors
      Belt  conveyors are the  most widely  used means of  transporting, elevating
and handling  materials  in the non-metallic minerals  industry.  .As  illustrated
 in  Figure  3.13, belt conveyors  consist of an endless belt which is carried oh
.a series of  idlers  usually  arranged  so that the  belt forms  a  trough.  The belt
 is  stretched between a  drive or head pulley  and  a  tail  pulley.  Although  belts
may be  constructed  of other material,  reinforced rubber  is  the most commonly
 used.  Belt  widths  may  range from  36 to  152  centimeters  (14 to 60  inches) with
 76  to 91 centimeter (30 to  36  inch)  belts  the  most common.   Normal operating
 speeds  may range  from 60 to 120 meters  per minute  (200 to 400 feet/minute).

                                     3-39

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 Depending  on  the  belt  speed,  belt  width  and  rock  density,  load  capacities may
 be  in  excess  of 1360 megagrams  (1,500  tons)  per hour.
                         HEAD
                         PULLEY
                                                               TAIL
                                                               PULLEY
                  Figure 3.13  Conveyor Belt Transfer Point
 E_ievpjtprs_
     Bucket elevators are utilized where substantial elevation is required
 within a limited space.  They consist of a head and foot assembly which sup-
 ports and drives an endless single or double strand chain or belt to which
 buckets are attached.  Figure 3.14 depicts the three types most commonly used:
 the high-speed centrifugal-discharge, the slow speed positive or perfect-
 discharge, and the continuous-bucket elevator.
     The centrifugal-discharge elevator has a single strand of chain or belt
 to which the spaced buckets are attached.  As the buckets round the tail pulley,
which is housed within a suitable curved boot, the buckets scoop up their load
and elevate it to the point of discharge.  The buckets are so spaced so .that
at discharge,  the material  is  thrown out by the centrifugal  action of the
bucket rounding the  head pt/ley.   The positive-discharge type also utilizes
spaced buckets but differs  from the centrifugal  type in  that it has  a
                                     3-40

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                  D
                         (b)
                         (c)
                                   LEGEND

                         (a)  centrifugal discharge
                         ^b)  positive discharge
                         (c)  continuous discharge
Figure  3.14.  Bucket Elevator Types

-------
 double-strand chain and a different discharge mechanism.   An  additional  sprocket,
 set below the head pulley,  effectively bends  the  strands  back under  the  pulley
 causing the  bucket to be totally  inverted resulting  in  a  positive  discharge.
      The continuous-bucket  elevator utilizes  closely spaced buckets  attached
 to  single or double strand  belt or  chain.   Material  is  loaded directly into
 the buckets  during ascent and  is  discharged gently as a result of  using  the
 back of the  precluding bucket  as  a  discharge  chute.
 Screw Conveyors
      Screw conveyors  are comprised  of  a steel  shaft  with  a spiral  or helical
 fin which, when  rotated, pushes material  along a  trough.  Since these con-
 veyors  are usually used with wet  classification,  no  significant emission prob-  '
 lem is  experienced.
 Pneumatic Conveyors
      Pneumatic conveyors  are comprised of  tubes or ducts  through which material
 is  conveyed.  Pneumatic  conveyors are  divided  into two classes termed by  their
 operating  principles:   pressure systems and vacuum (suction)  systems.
      Pressure systems  are further classified  into low pressure and high pressure
 types,  and vacuum  systems into low-, nedium-, and high-vacuum types.   Pressure
 and vacuum systems occasionally are used in combination for special requirements.
      Pressure systems  operate at pressure obtainable from a fan (low-pressure
 systems) or a compressed air system (high-pressure systems).   Normally, the
 airstream functions in a 20 to 31  centimeter ;3 inch  to 12 inch)  diameter pipe-
 line.   Into this line, material is fed fron: a  nopper or other  device  at con-
 trolled rates.  The airstream immediately suspends this  material  and  conveys
 it  to a cyclone-type or filter-type  collector  for deposit.  Conveying air es-
capes via the cyclone vent or througr. the  filter.
                                     3-42

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     Vacuum systems offer the advantage of clean, efficient pickup from rail-
cars, trucks or bins for unloading or in-plant conveying operations.  Cyclone
receivers or combination receiver-filters are used at the terminal of the sys-
tem to separate the material being conveyed from the air.  Below the receiver,
either a rotary feeder or gatelock (trap door feeder) is employed as a dis-
charge air lock.  Positive displacement blowers are used as exhausters to
provide the necessary conveying air at the operating vacuum.  Generally, the
vacuum system is most applicable where the feed-in point must be flexible,
such as unloading railroad cars, barges, ships, or.reclaiming material from
open warehouse storage, or where it is desirable to pick up material from a
multiplicity of stations.
Source of Emissions
     Particulates may be emitted from any of the material handling and transfer
operations.  As with screening, the level of uncontrolled emissions depends on.
the material being handled, the size of the material handled, the degree of
agitation of the material and the moisture content of the material.  Perhaps
the largest emissions occur at conveyor belt transfer points.  Depending
on the conveyor belt speed and the free fall distance between transfer points,
substantial emissions may be generated
3.2.2.3.4  Grinding Operation
     Grinding is a further step in the reduction of material to particle sizes
smaller than those attainable by crushers.  Because the material to be treated
has already been reduced to small sizes, and the force to be applied to each
particle is comparatively small, the machines used in grinding are of a dif-
ferent type, and may operate on a different principle, from those used in more
coarse crushing.
                                     3-43

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      As with  crushers,  the most  important element influencing emissions from
 grinding mills  is  the reduction  mechanism employed, compression or impact.
 Grinding mills  generally  utilize impact rather than compression.  Reduction
 by  impact will  produce  a  larger  proportion of fines.  Particulate emissions
 are generated from grinding mills at the grinder's inlet and outlet.  Gravity
 type grinding mills  accept feed  .from a conveyor and discharge product into a
 screen or classifier or onto a conveyor.  These transfer points are the source
 of  particulate  emissions.  The outlet has the highest emissions potential
 because of  the  finer material.   Air-swept mills include an air conveying sys-
 tem and an  air  separator, a classifier, or both.  The air separator and
 and classifier  are generally cyclone collectors.  In some systems, the air
 just conveys the material to a separator for deposit into a storage bin with
 the  conveying air  escaping via the cyclone vent.  In other grinding systems,
 the air.is  continuously recirculated.  Maintaining this circulating air sys-
 tem under suction  keeps the mill  dust!ess in operation, and any surplus air
 drawn tnto  the  system due to the suction created by the fan is released through
 a vent.  In both cases the vent  gases will  contain a certain amount of par-
 ticulate matter.
     The levels of uncontrolled emissions from grinding mills (fine mills)  are
 indicated in Table 3-5.
     Many types of grinding mills are manufactured for use  by various  industries,
The principal  types of mills used are:   (1)  hammer,  (2)  roller,  (3)  rod,
 (4) pebble and ball, and (5)  fluid energy.   Each  of  these  types  of mills  is
discussed separately below.
                                    3-44

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 Hammermins
      A  hammermin  consists  of  a  high  speed  horizontal rotor with several rotor
 discs to  which  sets  of swing hammers  are attached.  As rock particles are fed
 into  the  grinding  chamber,  they  are impacted and shattered by the- hammers which
 attain  peripheral  speeds greater than 4,572 meters per minute (250 feet per
 second).  The shattered rock then collides with a steel breaker plate and is
 fragmented even further.  A cylindrical grating or screen positioned at the
 discharge opening  restrains oversize material until it is reduced to a size
 small enough to pass between the  grate bars.  Product size is controlled by
 the rotor speed, the spacing between the grate bars, and by hammer length.
 These mills are used for nonabrasive materials and can accomplish a size re-
 duction of up to 12:1.
 Roller Mill
     The  roller mill,  also known  as a Raymond Roller Mill, with its integral
 whizzer separator can  produce ground material ranging from 20 mesh to 325 mesh
 or finer.  The material is ground by rollers that travel  along the inside of
 a horizontal  stationary ring.   The rollers swing outward by centrifugal  force,
 and trap the material between  them and the ring.  The material is swept out of
 the mill by a stream of air to a whizzer separator, located directly on top of
 the mill, where the oversize is separated and dropped back for further grinding
while the desired,fines pass up through the whizzer blades into the duct lead-
 ing to the air separator (cyclone).   A typical  roller mill is shown in
 Figure 3.15.
Rod Mill
     The rod  mill  is generally considered as a  granular grinding unit, prin-
cipally  for handling a maximum feed  size of 2 to 4 centimeters (1  to  2 inches),
                                    3-45

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       A  Product outlet
                           Revolving
                           whizzers
                            - Wnizzer
                              drive
                        Grinding ring
                        -Grinding roller
                                -Feeder
Figure 3.15. Roller Mill
        3-46

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and grinding to a maximum of 65 mesh.  It is normally used in a closed circuit
with a sizing device, such as classifiers or screens, and for wet or dry grind-
ing.  It will grind with the minimum of the finer sizes, such as 100 or 200
mesh, and will handle relatively high moisture material without packing.
     The mill in its general form consists of a horizontal, slow-speed, rotating,
cylindrical drum.  The grinding media consists of a charge of steel  rods,
slightly shorter than the mill's inside length and from 5 to 13 centimeters
(2 inches to 5 inches) in diameter.  The rods roll freely inside the drum during
its rotation to give the grinding action desired.
Pebble and Ball Mills
     The simplest form of a ball mill is cylindrical, horizontal, slow-speed
rotating drum containing a mass of balls as grinding media.  When other types
of grinding media such as a flint or various ceramic pebbles are used, it is
known as a pebble mill.  The ball mill uses steel, flint, porcelain, or cast
iron balls.  A typical ball mill is shown in Figure 3.16.
     The diameter of balls or pebbles as the initial charge in a mill is
determined by the size of the feed material and the desired fineness of the
product.  Usually the larger diameter ranges are used for preliminary grinding
and the smaller for final grinding.  Ball mills reduce the size of the feed
mostly by impact.  These grinders normally have a speed of 10 to 40  revolutions
per minute.  If the shell rotates too fast, centrifugal force keeps  the balls
against the shell and minimal grinding occurs.
Fluid Energy Mills
     When the desired material size is in the range of 1 to 20 microns, an
ultrafine grinder such as the fluid energy mill is required.  A typical fluid
energy mill is shown in Figure 3.17.  In this type of mill, the particles are

                                    3-47

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FEED
                                             1=1
                              REVOLVING
                                SHELL
                                                 DRIVE GEAR
                     Figure 3.16.  Ball Mill
             REDUCTION
              CHAKBLR
                                         SIZED
                            ./V—\ -SA ,  PART ICL E S
                                                      FEED
                                           AIR OR sTr.-v--. r;.n
                             NOZZLES
               Figure  3.17.  Fluid-energy 'Mill
                                 3-48

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suspended and conveyed by a high velocity gas stream in a circular or elliptical
path.  Size reduction" is caused by impaction and rubbing against mill walls,
and by interparticle attrition.  Classification of the particles takes place
at the upper bend of the loop shown in Figure 3.17.  Internal classification
occurs because the smaller particles are carried through the outlet by the gas
stream while the larger particles are thrown against the outer wall by centrif-
ugal force.  Product size can be varied by changing the gas velocity through
the grinder.
     Fluid energy mills can normally reduce up to 0.91  megagrams/hr (1 t/hr)
of solids from 0.149 mm (100 mesh)  to particles averaging 1.2 to 10 microns
in diameter.  Typical gas requirements are 0.45 and 1.8 kg (1 to 4 pounds) of
steam or 2.7 to 4.1  kg (6 to 9 pounds) of air admitted at about 6.8 atm
(100 psig) per 0.45 kg (1 pound) of product.  The grinding chambers are about
2.5 to 20 cm (1 to 8 inches) in diameter and the equipment is 1.2 to 2.4 meters
(4 to 8 feet) high.
Separating and Classifying
     Mechanical air separators of the centrifugal type cover a distinct field
and find wide acceptance for the classification of dry materials in a relatively
fine state of subdivision.  In commercial practice the separator may be said
to begin where the impact of vibrating screens leave off,12 extending from
about 40 to 60 mesh down.
     Briefly stated, the selective action of the centrifugal separator is the
result of an ascending air current generated within the machine by means of a
fan, such current tending to lift the finer particles against the combined
effect of centrifugal force and gravity.  In operation the feed opening allows
the material to drop on the lower or distributing plate where it is spread and
                                    3-49

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thrown off by centrifugal force, the larger and heavier particles  being  pro-
jected against an inner casing, while the smaller and lighter particles  are
picked up by the ascending air current created by the fan.   These  fines  are
carried over into an outer cone and deposited.  Concurrently, the  rejected
coarse material drops into the inner cone, passes out through a spout and is
recycled back to the grinding mill.
     The air, after dropping the major portion of its burden, is either  re-
circulated back to the grinding mill or vented.  In the case of the recir-
culated air, a small amount of extraneous air is entrained in the feed and
frequently builds up pressure in the separator, in which case the excess air
may be vented off.  Both vent gases are a source of particulate matter.
3.2.2.3.5  Bagging and Bulk Loading Operations   .
     In the non-metallic minerals industry the valve type paper bag, either
sewn or pasted together, is widely used for shipping fine materials.  The valve
bag is "factory closed," that is, the top and bottom are closed either by sewing
or by pasting, and a single small opening is left on one corner.  Materials  are
discharged into the bag  through the valve.  The valve closes automatically due
to the internal pressure of the contents of the bag as soon as it is filled.
     The valve type bag  is filled by means of a packing machine designed
specifically for this purpose.  The material enters the bag through a nozzle
inserted in the valve opening, and the valve closes automatically when the
filling is completed.
     Bagging operations  are a source of particulate emissions.  Dust is emitted
during the final stages  of filling when dust laden air is forced out of the bag.
The  fugitive emissions due to bagging operation are generally localized in the
area of the bagging machine.

                                     3-50

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     Fine product materials that are not bagged for shipment are either bulk
loaded in tank trucks or enclosed railroad cars.  The usual method of loading
is gravity feeding through plastic or fabric sleeves.  Bulk loading of fine
material is a source of particulate because, as in the bagging operation, dust
laden air is forced out of the truck or railroad car during the loading
operation.
3.2.3  Emissions Under Existing Regulations
     Existing State regulations applicable to the non-metallic minerals industry
take many forms, depending on whether emissions are process or fugitive in
nature.  Regulations limiting particulate emissions from process sources are
based on general process weight, concentration and/or visible emission regulations.
For a 45 megagrams per hour (50 t/hr) plant, typical  process weight regulations
would limit allowable emissions from each process step (i.e., crushing, grinding,
drying) to 25.6 kg/hr (56.4 lb/hr).13  This is  about  95 percent reduction in un-
controlled emissions.  For a typical  454 megagrams per hour (500 t/hr)  crushing
plant, most stringent and least stringent process weight regulations would limit
allowable emissions to 18.2 and 120 kg/hr (40.0 and 264.0 Ib/hr), respectively.
The most stringent regulations, such as Pennsylvania's, limit emission from a
collection device to  0.09 g/dscm (0.04 gr.dscf) and  in some cases to as low as
0.046 g/dscm (0.02 gr/dscf).1"
     Fugitive dust regulations are for the most part  subjective and vague.
Most suggest that reasonable precautions be taken for control, but provide no
means of determining compliance.   Some states prohibit fugitive dust or emis-
sions from any source from crossing property boundaries either by disallowing
any visible emissions or limiting them with an ambient concentration standard.
                                     3-51

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                                 REFERENCES


1.   Minerals Yearbook (1972), Volume I, Bureau of Mines.

2    Development Document for Interim Final Effluent Limitations  Guidelines
     and New Source Performance Standards for the Mineral  Mining  and Pro-
     cessing Industry, U.S. Environmental Protection Agency, October 1975.

3.   Commodity Data Summaries Annual, 1977, U.S. Bureau of Mines.

4.   Compilation of Air Pollution Emission Factors, Second Edition, U.S.
     Environmental Protection Agency, Publication No. AP-42, April  1973,
     p. 8.20-T.

5    Characterization of Particulate Emissions from the Stone-Processing
     Industry, Research Triangle Institute, EPA Contract No. 68-02-0607,
     May 1975, p. 57.

6.   Pit and Quarry Handbook  and Purchasing Guide.  63rd Edition, Pit and
     Quarry Publications,  Incorporated,  Chicago, 1970, p. B-17.

7.   Reference 6.

8.   Reference 6.

9    Perry, Robert H. (editor), Chemical Engineers Handbook,  5th Edition,
      McGraw-Hill, New York, 1973,  p. 8-21.

10.    Reference 9, p.  956.

11.    Reference  6, p.  B-144..

12.    Reference  6, p.  B-73.

13    Analysis  of Final  State Implementation Plans-Rules  and Regulations,
      prepared by the MITRE Corporation for the U.S.  Environmental  Protection
      Agency, Contract No.  68-02-0248, July 1972.

14.    Title 25.   Rules and Regulations, Pennsylvania Department of  Environ-
      mental Resources,  pages 123.2-123.3.
                                     3-52

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                 4.   EMISSION CONTROL TECHNIQUES

     The diversity of the particulate emission sources  involved in mining
and processing non-metallic minerals requires use of a  variety of
control methods and techniques.  Dust suppression techniques,  designed to
prevent particulate matter from becoming airborne, are  applicable to both
fugitive process and fugitive dust sources.  Where particulate emissions can
be contained and captured, particulate collection systems are used.  Emission
sources and applicable control options are listed in Table 4.1.
     This chapter discusses the control technology applicable  to  the  follow-
ing  process operations at  non-metallic minerals  plants:  crushers,  grinders,
screens, conveyor transfer points,  storage bins,  and fine products  loading
and  bagging.
4.1  CONTROL OF PLANT PROCESS OPERATIONS
     A representative non-metallic mineral processing plant, consisting of
crushers; grinders; screens; conveyor transfer points; and storage, loading
and  bagging facilities,  contains a multiplicity  of dust-producing  points.
Therefore, effective emission  control can  present a number of  problems.  Methods
utilized to reduce  emissions  include wet dust suppression, dry collection,
and  a  combination of the two.  Wet  dust suppression consists  of  introducing
moisture into  the material flow, causing fine particulate matter to be
confined and  remain with the material flow rather than becoming  airborne.
Dry  collection involves  hooding  and  enclosing dust-producing  points and
exhausting emissions to  a collection device.   Combination systems utilize
                                   4-1

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          Table 4.1.  PARTICIPATE EMISSION SOURCES FOR
       THE EXTRACTION AND PROCESSING OF NON-METALLIC MINERALS
Operation or Source
      Control Options
Drilling




Blasting

Loading (at mine)

Hauling
Crushing



Screening

Conveying (transfer points)

Stockpiling
Grinding

Storage Bins
Conveying (other than
  transfer points)

Windblown dust from
  stockpiles
Windblown dust from roads
  and plant yard
a)

b)
a)
b)

c)
d)
e)

a)
b)
a)
b)
c)

d)
a)
b)

a)
b)
c)
d)

a)
b)
c)

2)
f)
Liquid injection (water or
water plus a wetting agent)
Capturing and venting emissions to
a control device

Adopt good blasting practices

Water wetting

Water wetting of haulage roads
Treatment of haulage roads with
surface agents
Soil stabilization
Paving
Traffic control

Wet dust suppression systems
Capturing and venting
emissions to a control device

Same as crushing

Same as crushing

Stone ladders
Stacker conveyors
Water sprays at conveyor
discharge
Pugmill

Same as crushing

Capturing and Venting
to a control device

Covering
Wet dust suppression

Water wetting
Surface active agents
Covering (i.e., silos, bins)
Windbreaks

Water wetting
Oiling
Surface active agents
Soil stabilization
Paving
Sweeping
                            4-2

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                        Table 4.1  (Continued)
   Operation or Source
Control Options
   Loading (product into RR      a)
     cars, trucks, ships)        b)
   Bagging                       a)
   Magnetic Separation           a)
Wetting
Capturing and venting
to control device

Capturing and venting
to control device

Capturing and Venting
to control device
Does not include processes involving combustion
                                   4-3

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both methods at different .stages throughout the processing plant.  In
addition to these control techniques, the use of enclosed structures to
house process equipment may also be effective in preventing emissions to
the atmosphere.
4.1.1  Wet Dust Suppression
     In a wet dust suppression system, dust emissions are controlled by
applying moisture in the form of water or water plus a wetting agent sprayed
at critical dust producing points in the process flow.  This causes dust
particles to adhere to larger mineral pieces or to form agglomerates too
heavy to become or remain airborne.  Thus, the objective of wet dust
suppression is not to fog an emission source with a fine mist to capture and
remove particulates emitted, but rather to prevent their emission by keeping
the material moist at all process stages.
     The wet dust suppression method has been used on a wide variety of stone
including limestone, traprock, granite, shale, dolomite, and sand and gravel.
It can be generally considered to have a universal application to stone
handled through a normal crushing and screening operation.  In some
cases, however, watersprays cannot be used since the moisture may interfere
with further processing such as crushing, screening or grinding where
blinding problems may occur.  In addition, the capacity of the dryers
used in some of the processing steps limits the amount of water that can be
sprayed onto the raw materials.  Once the materials have passed through the
drying operations, water cannot be added and other means of dust control must
be utilized.
     When plain or untreated water is used, because of its unusually high
surface tension (72.75 dynes/cm  at 20°C), the addition of 5 to 8 percent
                                  4-4

-------
 moisture (by weight),  or greater,  may be required  to  adequately  suppress
 dust.    In  many installations  this may not be  acceptable  because excess
 moisture may cause screening  surfaces to blind,  thus  reducing  both  their
 capacity and effectiveness, or result in the coating  of mineral  surfaces
 yielding a  marginal  or non-specification product.   To counteract these
 deficiencies, small  quantitites  of specially formulated wetting  agents or
 surfactants are blended with  the water to reduce its  surface tension  and
 consequently improve its wetting efficiency so that dust  particles  may
 be suppressed with a minimum of  added moisture.  Although these  agents
 may vary in composition, their molecules are characteristically  composed
 of two  groups,  a  hydrophobic group (usually a  long  chain  hydrocarbon) and
 a  hydrophilic group  (usually a sulfate,  sulfonate,  hydroxide or  ethylene
 oxide).   When introduced into  water,  these agents effect  an appreciable
 reduction in  its  surface tension (to  as  low as 27 dynes/cm2).2   The
 dilution  of such  an  agent in minute quantities in water (1 part  wetting
 agent to  1,000  parts water) is reported  to  make  dust  control practical
 throughout  an entire crushing  plant.   In  a  crushed  stone  plant,  this may
 amount to as  little  as  1/2 to  1  percent  total moisture per ton of stone
          3
 processed.
     In adding moisture  to the process material, several  application
 points are  normally  required.   Since  the  time  required for the proper
 distribution  of the  added moisture on  the mineral is  critical to
achieving effective  dust control,  treatment normally  begins as soon as
 possible after the material  to be  processed is introduced into the  plant.
As such, the initial application point is commonly made at the primary
                                   4-5

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crusher truck dumo.  In addition to introducing moisture prior to

processing, this application contributes to reducing intermittent

dust emissions generated during dumping operations.  Spray bars located

either on the periphery of the dump hopper or above it are used.

Applications are also made at the discharge of the primary crusher and at

all secondary and tertiary crushers where new dry surfaces and dust

are generated by the fracturing of stone.  In addition, treatment may

also be required at feeders located under surge or reclaim piles if this

tenporary storage results in sufficient evaporation.  Further wetting

of the material at screens, conveyor transfer points, conveyor and

screen  discharges to bins, and conveyor discharges to storage piles may

or may not be necessary because, if properly conditioned at application

points, the wetted material exhibits a carryover dust control effect

that may suopress the dust through a number of material handling

operations.  The amount of moisture required at each application point

is dependent on a number of factors including the wetting agent used,

its dilution ratio in water, the type and size of process equipment

ard the characteristics of the material processed (type, size distribution,

feed rate and moisture content).

     A typical wet dust suppression system, such as the Chem-Jet System3

manufactured by the Johnson-March Corporation and illustrated in

Figure 4.1, contains a number of basic components and features including:

(1) a dust control agent (compound M-R); (2) proportioning equipment;
   The use of trade names or commercial products does not
   constitute endorsement or recommendation for use by the
   Environmental Protection Agency.
                                  4-6

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                                          O)
                                          +J
                                          in
                                          >>
                                          to
                                          10

                                          CO

                                          O)

                                          s-

                                          Q.

                                          Q.

                                          3

                                          CO
                                          CO
                                          rs
                                          •a
                                           O)
4-7

-------
(3) a distribution system; and (4) control actuators.,  A proportioner and
pump are necessary to proportion the wetting agent and water at the
desired ratio and to provide moisture in sufficient quantity and at
adequate pressure to meet the demands of the overall system.
     Distribution is accomplished by spray headers fitted with pressure
spray nozzles.  One or more-headers are used to apply the dust suppressant
mixture at each treatment point at the rate and spray configuration
required to effect dust control. A variety of nozzle types may be used
including hollow-cone, solid cone or fan nozzles, depending on the spray
pattern desired.  To prevent nozzle plugging, screen filters are used.
Figure 4.2 shows a typical arrangement for the control of dust emissions at
a crusher discharge.
     Spray actuation and control is important to prevent waste and
undesirable muddy conditions, especially when the material flow is
intermittent.  Spray headers at each application point are normally
equipped with an dn-off controller which is interlocked with a sensing
mechanism so that sprays will be operative only when there is material
actually flowing.  In addition, systems are sometimes designed to operate
under all weather conditions.  To provide protection from freezing,
exposed pipes are usually traced with heating wire and insulated.  When
the system is not in use, it should be drained to insure that no water
remains in the lines.  During periods of prolonged cold weather when
temperatures remain below 0°C, wetted raw materials will freeze into
large blocks and adhere to cold surfaces such as hopper walls.  Additional
labor may be required to prevent such build-ups.
                                  4-8

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                                      SUPPRESSANT.
                                          v     i
                                                -  FILTLR
                                                  CO'ftRuL
Figure 4.2.   Dust suppression application
           at crusher discharge.
             4-9

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     At a rock crushing plant with a well designed wet dust suppression
system, the Johnson-March Corporation claims that better than 90 percent
control efficiency is attainable for the emissions including all process
                                                             5
operations from the primary crusher to stockpile and reclaim.   Since
these emissions are unconstrained and not amenable to testing, no actual
particulate emission measurements have been made to verify or dispute
this contention.
4.1.2  Dry Collection Systems
     Particulate emissions generated at  plant process operations (crushers,
screens, grinders, conveyor transfer points, fine product  loading
operations and bagging operations) may be controlled by capturing and
exhausting potential emissions to a collection device.  Depending on the
physical layout of the plant, emission sources may be either manifolded
to a single centrally located collector  or  ducted to a number of
individual control units.  Collection systems consist of an exhaust
system utilizing hoods and enclosures to capture and confine emissions,
ducting  and fans to convey the captured  emissions to a collection device,
and the  collection device for particulate removal prior to exhausting
the air  stream to the atmosphere.
4.1.2.1  Exhaust Systems and Ducting
     If  a collection system is to effectively prevent particulate emissions
from being discharged to the atmosphere  at  the locations where emissions
are generated, local exhaust systems including hooding and ducting must
be properly designed and balanced.   (Balancing refers to adjusting the
static pressure balance, which exists at the junction of two branches, to
obtain the desired volume in each branch.)  Process equipment should be
                                  4-10

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enclosed as completely as practicable, allowing for access for operation,
routine maintenance and inspection requirements.  For crushing facilities,
recommended hood capture velocities range from 61 to 150 meters (200 to
500 feet) per minute.6'7  In general, a minimum indraft velocity of 61
meters (200 feet) per minute should be maintained through all open hood
areas.  Proper design of hoods and enclosures will minimize exhaust volumes
required and, consequently, power consumption.  In addition, proper
hooding will minimize the effects of  cross drafts  (wind) and the effects
of induced air (i.e., air placed  in motion as a result of machine movement
or falling material).  A well designed enclosure can be defined as a
housing which minimizes open areas between the  operation and the hood
and contains all  dust dispersion  action.
      Good  duct design dictates  that  adequate  conveying velocities be
maintained so that the  transported dust  particles  will not  settle in  the
ducts along the  way to  the  collection device.   Based on  information for
crushed stone,  conveying velocities  recommended for mineral particles
                                                            8 9
range from 1,100 to 1,400 meters/min. (3,500 to 4,500 fpm). '
      Adequate  design and construction specifications are available  and
 have  been utilized to produce efficient, long-lasting systems.  Various
 guidelines establishing minimum ventilation rates required for the control
 of crushing plant operations, and upon which the ventilation rates .most
 commonly utilized in the industry are based, are briefly discussed below.
                                   4-11

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4.1.2.1.1  Crushers and Grinders
     Hooding and air volume  requirements for the control of crusher and
grinder emissions are quite  variable depending upon the size and shape
of the emission source, the  hood's position relative to the points of
emission, and the velocity,  nature, and quantity of the released particles,
The only established criterion  is that a minimum indraft velocity of 61
meters per minute (200 fpm)  be  maintained through all open hood areas.  To
achieve this, capture velocities in excess of 150 meters per minute (500
fpm) may be necessary to overcome induced air motion, resulting from the
material feed and discharge  velocities and the mechanically induced
velocity (fan action) of a particular equipment type.    To achieve
effective emission control,  ventilation should be applied at both the
upper portion, or feed end,  of  the equipment and at the discharge point.
An exception to this would be at primary jaw or gyratory crushers because
of the necessity to have ready  access to get at and dislodge large rocks
which may get stuck in the crusher feed opening.  Where access to a device
is required for maintenance, removable hood sections may be utilized.
     In general, the upper portion of the crusher or grinder should
be enclosed as completely as possible, and exhausted according to the
criteria established for transfer points (see Section 4.1.2.1.3).
The discharge to the transfer belt should also be enclosed as  completely
as possible.   The exhaust rate varies considerably depending on crusher
                                  4-12

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type.  For impact crushers or grinders,  exhaust volumes  may range from

            O                           1 1

110 to 230 m /min.  (4,000 to 8,000 cfm).     For compression type crushers,

                       o

an exhaust rate of 46 m /min per meter (500 cfm per foot)  of discharge


                             12
opening should be sufficient.    The width  of the discharge opening  will



approximate the width of the receiving conveyor.   For either impact



crushers or compression type crushers, pick-up should be applied down-



stream of the crusher for a distance of at  least 3.5 times the width of


                       13
the receiving conveyor.    A typical hood configuration  used to control



particulate emissions from a cone crusher is depicted in Figure 4.3



     Grinding or milling circuits which employ air conveying systems



operate at slightly negative pressure to prevent the escape of air



containing the ground rock.  Because the system is not airtight, some



air is drawn into the system and must be vented.   This vent stream can



be controlled by discharging it through a control device.



4.1.2.1.2  Screens



     A number of exhaust points are usually required to achieve



effective control at screening operations.   A full coverage hood, as



depicted in Figure 4.4, is generally used to control emissions generated



at actual screening surfaces.  Required exhaust volumes vary with the



surface area of the screen and the amount of open area around the



periphery of the enclosure.  A well-designed enclosure should have a



space of no more than  5 to 10 centimeters  (2 to 4 inches) around the



periphery of the screen.  A minimum exhaust rate of  15 m  /min.  per square



meter (50 cfm per square foot) of screen area  is commonly used with no


                             14
increase for multiple  decks.    Additional  ventilation air may  be
                                  4-13

-------
                                  G)
                                  JZ
                                  tn
                                  o

                                  OJ
                                   o
                                   CO
                                    O
                                    u
                                    O
                                     0)
                                    fr,
4-14

-------
                  TO CONTROL
                    DEVICE
FEED
                                    COMPLETE
                                    ENCLOSURE

                                        SCREEN
                       THROUGHS



     Figure  4.4   Hood configuration for

              vibrating  screen.
                    4-15

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required at the discharge chute to belt or bin transfer points.  If
ventilation is needed, these points are treated as regular transfer
points and exhausted accordingly.  (See Section 4.1.2.1.3).
4.1.2.1.3  Conveyor Transfer Points
     At belt to belt conveyor transfer points, hoods should be
designed to enclose both the head pulley of the upper belt and the tail
pulley of the lower belt as completely as possible.  With careful
design, the open area should be reduced to about 0.15 square meters per
meter (0.5 square feet per foot) of belt width.    Factors affecting the
air volume to be exhausted include the conveyor belt speed and the
free-fall distance to which the material is subjected.  Recommended
exhaust rates are 33 m  per min. per meter (350 cfm per foot) of belt
width for belt speeds less than 61 meters/min. (200 fpm) and 150
meters 3/min (500 cfm) for belt speeds exceeding 61 meters/min (200
fpm).16  For a belt to belt transfer with less than a 0.91 meter
(three foot) fall, the enclosure illustrated  in Figure 4.5 is commonly
used.
      For belt to belt transfers with a free-fall distance greater than
0.91  meters  (three feet) and for chute-to-belt transfers, an arrangement
similar  to that depicted in Figure 4.6  is commonly used.  The exhaust
connection should be made as far downstream as possible to maximize dust
fallout  and  thus minimize needless dust entrainment.  For very dusty
                                4-16

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       24 mm
                                                       2" CLEARANCE  FOR LOAD
                                                           ON BELT
                                            DETAIL OF BELT Off MUG
      CONVEYOR TRANSFER LESS THAN
      3 FALL. FOR OREATER FALL
      PROVIDE ADDITIONAL EXHAUST AT
      LOWER BELT SEE DETAIL AT RIGHT.
           Figure 4.5  Hood  configuration for conveyor transfer,
                       less  than  0.91  meter (3-foot)  fall.


material,  additional exhaust air may  be required at  the  tail  pulley of

the receiving belt.   Recommended air  volumes are 20  m3/min (700 cfm)

for belts  0.91  meters (three feet)  wide and less, and 28 m3/min (1,000

cfm) for belts  wider than 0.91 meters (three feet).17

      Belt or chute-to-bin  transfer points differ from the usual transfer

 operation in that there is no open area downstream  of the transfer point.

 Thus, emissions are emitted only at  the loading point.   As illustrated
                                     4-17

-------
       FROM CHUTE
        OR BELT
ADDITIONAL
EXHAUST
TO CONTROL
  DEVICE
        RUBBER
        SKIRT
                      CONVEYOR BELT
    Figure  4.6   Hood configuration  for a  chute to belt
                or conveyor transfer,  greater than 0.91
                meters  (3-foot)  fall.
                    4-18

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      in Figure 4.7, the exhaust connection  is normally located at some
      point remote from the loading  point and exhausted at a minimum rate
             «                                                            18
      of 61 m /min per square meter  (200 cfm -?^r square foot) of open area.
TO CONTROL
: LOADING DAEVICE

^ POINT T

BELT ( *

\ / /
\
BIN
OR
HOPPER

Figure  4»7.   Exhaust configuration at  bin  or hopper.

      4.1.2.1.4  Product Loading and Bagging
           Particulate emissions from truck and railcar  loading of coarse
      material can be minimized by reducing the open height  that the material
      must fall from the silo or bin to the shipping vehicle.  Shrouds, telescoping
      feed tubes, and windbreaks can further reduce the  fugitive emissions
      from this intermittent source.  Particulate emissions  from loading of fine
      material into either trucks or railroad car can be controlled by an exhaust
      system  vented to a fabric filter system.  The system is  similar to the
                                      4-19

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system described above for controlling bin  or  hopper  transfer points
(see Figure 4.7).  The material  is  fed through  one of the vehicle's
openings and the exhaust connection is normally at another opening.  The
system should be designed with a minimum  amount of open area around the
periphery of the feed chute and  the exhaust duct.
     Bagging operations are controlled by local  exhaust systems and
vented to a fabric filter system for  product recovery.  Hood face
velocities on the order of 150 meters  (500  feet) per minute should be
used.   An automatic bag filling  operation and vent system is shown in
Figure 4.8.

     500  f::-  rr.a-
                                                Hood  attached to  bin
 Principal dust source

Scale support
               Figure 4-8.   Bag  filling vent system.19
                                 4-20

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4.1.2.2  Collection Devices
     The most efficient dust collection device used in the non-metallic
mineral industry is the fabric filter or baghouse.  For most crushing
plant applications, mechanical shaker type collectors which require
periodic shutdown for cleaning (after four or five hours of operation)
are used.  These units are normally equipped with cotton sateen bags and
operated at an air-to-cloth ratio of 2 or 3 to 1.  A cleaning cycle
usually requires no more than two to three minutes of bag shaking and is
normally actuated automatically when the exhaust fan is turned off.
     For applications where it may be impractical to turn off the
collector, fabric filters with continuous cleaning are employed.  Although
compartmented mechanical .shaker types may be used, jet pulse units are
predominately used by the industry.  These units usually use wool or
synthetic felted bags for a filtering media and may be operated at a
filtering ratio of as high as 6 or 10 to 1.  Regardless of the baghouse
type used, jet pulse or shaker, greater than 99 percent efficiency can
be attained even on submicron par/tide sizes.20  Two baghouses tested
by EPA for both inlet and outlet emission levels had collection
efficiencies of 99.8 percent.21'22
     Other collection devices used in the industry include cyclones and low
energy scrubbers.  Although these collectors may demonstrate efficiencies
of 95 to 99 percent  for coarse particles (40 microns and larger),
their efficiencies are poor, less than 85 percent, for medium and fine
                                   oq
particles (20 microns and smaller).    Although high energy  scrubbers
and electrostatic precipitators could conceivably achieve results
similar to that of a fabric filters these methods are not commonly used
to control dust emissions in the industry.
                                 4-21

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     Control options for the portable plant segments of the crushed stone, and
sand and gravel industries will be discussed in Supplement A.
4.1.2,2.1   Fabric  Filters
     Fabric filters are high efficiency collection devices used quite exten-
sively throughout  the  non-metallic minerals processing industry.  The greatest
variations in the  design of baghouses arise from the methods of cleaning the
fabric filter and  the choice of fabric and size of unit.
     The actual extraction of dust is accomplished as shown in Figure 4-9.
The airstream enters the baghouse and is pulled up into fabric sleeves that
are clustered throughout the apparatus.  External  draw on the apparatus  forces
the air to be pulled to the outside of these fabric sleeves which is a "clean
area."  The dust remains trapped in the weave of the sleeve forming a cake
while the cleansed air is exhausted to the atmosphere.  The dust is eventually
removed from the bag by one of several bag cleaning methods and is either re-
turned to the process or disposed of.
     The reverse operation can just as easily be utilized; that is, dirty air
travels from the outside to the inside of the bag  exiting through the top of
the bag, thus leaving the dirt accumulation on  the outside of the sleeves.
     This accumulation of dust forms a filter cake on the bags which must be
removed if there is to be sufficient flow through  the system.   Care must be
taken that the dust is removed and disposed of  in  such a  manner that it  does
not become reentrained and also that a residual  filter cake remains to act as
a filtering mechanism in its own right.
     Major methods of cleaning are shaking (rapping)  and  reversing airflow
by air jets or pulses.  Shaking consists of manually  or automatically shaking
the bag hangers or rapping the side of the baghouse to shake  the dust free
into a receiving hopper below.
                                     4-22

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 HANGERS
CLEAN*
 A!f?
 DIRTY>r
  AIR •••'"
CLEAN
SIDE
 AIR


 BAG
                              COLLECTED
                                 ST
  Figure 4.9   Typical baghouse operation.
                     4-23

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     A less simple method is to use reverse airflow down the tubes  at such  a
rate that there is no net movement of air through the bag.   This  causes  the
bag to collapse which results in the filter cake breaking-up and  falling off
the bag.
     A final method is reverse air pulsing where a perforated ring  travels  up
and down each bag or sleeve.  Air jets in the ring force the bag  to collapse,
then reopen,breaking the filter cake apart.  These two methods are  shown in
Figure 4-10.
     The frequency of cleaning can be continuous in which a section of bag-
house is removed from operation and cleaned before going on to another section,
Alternatively, intermittent cleaning consisting of timed cycles of  cleaning
and operation is used.  Sensors can be installed that start the cleaning
cycle when some specified pressure drop across the system occurs  because of
the buildup of the filter cake.
     Materials available for bag construction are numerous.  They are cotton,
Teflon, glass, Orion, Nylon, Dacron, wool, Dyne!, and others.   Temperature  and
other operating parameters must be taken into account in the selection of
fabric material, though most industry processes are at ambient conditions.
The most popular materials in terms of wear and performance are the synthetic
fabrics or cotton sateen.
     Several other parameters are considered in the design  of baghouses  such
as frequency of cleaning, cloth resistances to corrosion and ore  moisture.
     The last major parameter considered is the air-to-cloth ratio  or filter
ratio defined as the ratio of gas filtered in cubic feet per minute to the
area of the filtering media in square feet or —™" which reduces to feet
(or meters) per minute.  Too high a ratio results in  possible blinding or
                                     4-24

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     TUBE
     COLLECTING
     DUST
CLEAN'
SIDE
     XI

REVERSE
AIR  OM
ONLY
WALLS  COLLAPSE TOGETHER
PREVENT DUST FROM  FALLJMS
PflESSUBE JET
AND REVERSE
AIR  ON
                   SLUG OF Am  onm
                   ALLOWS WJST TO WLL FREELY
Figure 4.10  Baghouse  cleaning methods
                    4-25

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clogging of the bags and a resultant decrease in collection efficiency and
Increase in bag material wear.
£.1.2.2.2  Wet Capture Devices
     The principle  of  collection  in  wet  capture  devices  involves  contacting
dust particles with liquid droplets  in some way  and  then  having the wetted
and unwetted  particles  impinge  upon  a collecting surface  where they can  be
flushed away  with water.  The method of  contacting the dust has many  varia-
tions depending on  the  equipment  manufacturer.   The  major types of wet col-
lectors are cyclone, mechanical,  mechanical-centrifugal,  and Venturi  scrubbers.
     "hese devices  are  more efficient than inertia!  separators.   Wet  capture
de.ices can also handle high temperature gases or mist-containing gases.
Cost; and efficiencies  also vary  with equipment  selection  and operating  cond-
•t'ons.  Efficiencies are higher  at  lower particle size ranges than with dry
•1.1.2.2.2.1  Cyclone Scrubbers
     a? with dry cyclones, wet cyclones impart a centrifugal force to the
ir-cc-'ing gas stream causing it to increase in velocity.  The principal
difference nere is that atomized liquids are introduced to contact and carry
awa.v f.jst particles.  The dust impinges upon the collector walls with clean
ai-r regaining in the central area of the device.  Efficiencies in this type
of sCuiD^ent average in the vicinity of 98.2 percent.
-.'.2.2.2.2  Mechanical Scrubbers
     These devices have a water spray created by a rotating disc or drum
^r.taciing the dust particles.  Extreme turbulence is created which insures
                                    4-26

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this required contact.  Efficiencies are about the same as cyclone wet scrub-
bers.
     Mechanical centrifugal capture devices with water sprays are similar to
their dry counterparts with the exception that a water spray is located at
the gas inlet so that the particulate matter is moistened before it reaches
the blades.  The water droplets containing particulate are impinged on the
blades while the clean air is exhausted as is depicted in Figure 4-11.  In
this case, the spray not only keeps the blades wet so that dust will  impinge
upon them, but it also serves as a medium to carry away particles.
     Some types of scrubbers use high pressure-sprays, consuming more energy
and water, but have higher efficiencies than other wet capture devices.  •
     Venturi scrubbers rely on an impaction mechanism and extreme turbulence
for dust collection.  Gas velocities in the throat of the Venturi tube are
4,572 to 6,096 meters (15,000 to 20,000 feet) per minute.  It is at this point
that low pressure water sprays are placed.  The extreme turbulence causes
excellent contact of water and particulate.  The wetted particles travel
through the Venturi tube to a cyclone spray collector.  Efficiencies are very
high, averaging 99.9 percent.25  These high efficiencies are also evidenced
in the low particle size ranges collected ( <1 ym).  This design is, indeed,
best suited to applications involving removal of 0.5 to 5 micron sizes.
     The construction is similar to a Venturi meter with 25° converging and
7° diverging sections.  This results in a 4:1 area reduction between.the
inlet and throat.
4.1.3   Combination Systems
     Wet dust suppression and dry collection techniques are often used in
combination to control particulate emissions from crushing plant facilities.
                                     4-27

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                  VANES
 CLEAN
EXHAUST
                                                     WATER SPRAY
             Figure  4.11   Mechanical,  centrifugal  scrubber.
                                  4-28

-------
As  illustrated  in  Figure  4.12, wet dust  suppression techniques are generally
used  to  prevent emissions at the primary crushing stage and at subsequent
screens,  transfer  points  and crusher  inlets.  Dry collection  is generally
used  to  control emissions at the discharge of the secondary and tertiary
crushers  where  new dry  surfaces and fine particulates are formed.  In addition
to  controlling  emissions, dry collection results in the removal of a large
portion  of the  fine particulates generated with the resultant effect of
making subsequent  dust  suppression applications more effective with a minimum
of  added  moisture.  Depending on the  product specifications, dry collection
may also  be necessary, at  the finishing screens.
      Dust control  for the portable crushing plant segments of the crushed
stone, and sand and gravel industries are discussed in Supplement A.
4.2  FACTORS AFFECTING  THE PERFORMANCE OF CONTROL METHODS.
4.2.1  Dust Suppression
     The  effectiveness  of wet suppression is dependent on the amount of
moisture  added  to  the process flow.  There are a number of factors  which
may affect the  performance of a wet dust suppression system.   These include
the wetting agent  used, the method' of application, characteristics of the
material, and the  type  and size of the process equipment serviced.  The
number, type and configuration of spray  nozzles at an application point,
as  well as the  speed at which a material stream moves past an appli-
cation point, may  affect both the efficiency and uniformity of wetting.
In  addition, meteorological factors, such as wind, ambient temperature
and humidity, which affect the evaporation rate of added moisture, may
                                      4-29

-------
                BAG
                CO-LECTOR
ID
                                                                        \
                                                       ••<, CF-"J>£R
 Figure 4.12  Typical  combination dust  control  systems.
                         4-30

-------
 also adversely affect the  overall  performance  of a  dust  suppression
 system.   Where the  material  processed  contains a high  percentage  of
 fines,  such as the  product from a  hammermill,  dust  suppression  may be
 totally inadequate  because of the  enormous  surface  areas  to  be  treated.
      Dust suppression may offer a viable control alternative to dry collec-
 tion at process facilities if sufficient moisture is added to the material.
 Generally, wet dust suppression is only possible with crushing  operations
 (crushers, conveyor transfer points, and screens) because a coarser material
 is  handled and plugging  problems will  not likely occur.   In  addition,
 wet suppression may not  be possible  in freezing weather  or arid regions'.
 Also, some industries (e.g.,  talc, rock salt)  prefer not  to  handle material
 with high moisture  (even in  crushing operations).
4.2.2  Dry Collection
     For dry collection  systems, factors affecting both capture efficiency
and  collection efficiency  are important.  Wind blowing through hood
openings can significantly reduce the effectiveness of a local exhaust
system.   This  can be  appreciated when one considers that an indraft
velocity of 61 meters/min  (200 fpm)  is equivalent to less than 3.7 km/hr
(2.3 mph).  Consequently, the process equipment should be completely
enclosed or the hood openings minimized.
     Installations located in areas of high precipitation have chosen to
house process equipment in  buildings  or structures to increase their
operating hours.  An added effect of this is to reduce the impact that high
                                     4-31

-------
winds may have on a local exhaust system which is not properly enclosed.
Except for crushed and broken stone plants and sand and gravel plants, much
of the processing in the industries investigated in this study occurs in
buildings which enclose the equipment.
     An exhaust system must be properly maintained and balanced if it is
to remain effective.  Good practice dictates that systems be periodically
inspected and capture and conveying velocities checked against design
specifications to assure that the system  is indeed functioning properly.
The  primary  causes for systems becoming unbalanced are the presence of
leaks  resulting from wear due to abrasion or corrosion, and the settling
of dust in poorly designed duct runs which effectively reduces the cross
sectional area of the duct and increases  pressure drop.
4.2.3  Combined Suppression and Collection Systems
     The  factors affecting the performance of  combination systems are the
 same as those  encountered where dust  suppression or  dry collection systems
 are  used  alone.
 4.3  PERFORMANCE OF  PARTICULATE EMISSION  CONTROL TECHNIQUES
 4.3.1   Dry  Collection Techniques
 4.3.1.1   Particulate Emission  Data  From Non-Metallic Mineral  Plants
      Particulate emission measurements were  conducted by  EPA  on  16 baghouse
 collectors  used to control  emissions  generated at  crushing, screening,  and
 conveying (transfer points)  operations at five crushed stone  installations,
 one kaolin  plant,  one fuller's earth  installation  and on  one  baghouse collector
 used to control  emissions  generated at grinding, classifying, and  fine
                                  4-32

-------
 product  loading operations at a feldspar installation.  Table 4.2 briefly
 summarizes the process operations controlled by each baghouse tested, along
 with specifications for each baghouse.  The results of these measurements are
 summarized in Figure 4.13.  Complete test data summaries, for both mass
 particular  measurements  and visible emission observations, and a description
 of each  process facility  tested are contained in Appendix C.
     Of  the  eight  plants  tested,  three  processed limestone rock (A, B, and C),
 two processed traprock  (D and E), one processed feldspar (G), one processed
.kaolin  (L),  and one processed fuller's  earth (M).  Four of the five crushed
 stone plants were  commercial crushed stone operations producing a variety of
 end products including dense-graded road base stone, asphalt aggregates,
 concrete aggregates and non-specific construction aggregates.  In addition,
 plant B  produced about 60 ton/hr of agstone.  Facilities Al through A4 consist
 of process operations producing raw material for the manufacture of port!and
 cement.   Facilities Al and Bl are both  impact crushers used for the primary
 crushing of  run-of-quarry limestone rock.  Facility A3 is somewhat unique in
 that it  consists of a single conveyor transfer point at the tail of an over-
 land conveyor.  As indicated in Table 4.2, the remaining facilities tested
 consisted of multiple secondary and tertiary crushing and screening operations,
 adjunct  conveyor transfer points, and grinding operations.  These include one
 primary  jaw  crusher, three secondary cone crushers, two hammer mills, eight
 tertiary cone crushers, nineteen screens, thirteen product bins, and over
 seventeen conveyor transfer points, one pebble mill, two roller mills, one
 fluid energy mill, one impact mill, one bucket elevator, and a fine product
 loading  system.
                                     4-33

-------





































































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     A minimum of three test runs, using EPA Method 5 or 17, were conducted
at each process operation tested.  (For this industry, both EPA Method 5
and 17 are acceptable particulate sampling methods, see Appendix D.)  Sampling
was performed only during periods of normal operation and was stopped and
restarted to allow for intermittent process shutdowns and upsets (feed to
the process).  Where the process weight rate was undeterminable at a specific
process operation, as in most instances, the process weight through the
primary crushing stage was monitored to assure that the plant was operating
at or near normal capacity.  Moisture determinations on the material processed
were also performed at each  plant tested (except for plants A, G, L and M)
to permit an assessment of whether control was effected primarily by the dust
collection system or by excessive moisture inherent  in the  material processed.
The  tests were  considered valid  if the  material moisture was less than  two
percent.
     .The baghouses tested included jet pulse, reverse air, and mechanical
  shaker type units.  The shaker  type and reverse air type fabric filters
  used cotton sateen bags and were operated at about 2:1 to  3:1 air-to-
  cloth ratios.  The jet pulse units tested were fitted with wool or
  synthetic fiber felted bags.  Air-to-cloth ratios ranged from about
  5:1 to 7.5:1.
      A study26 performed by the Industrial Gas Cleaning Institute
  (IGCI) under  contract to  EPA reported  air-to-cloth  ratios  necessary to
  achieve  0.05  g/dscm  (0.02  gr/dscf) for the various  industry segments
                                      4-36

-------
 based upon  the experience  of their  member  companies.   Table  4.3  presents
 this  information.   These ratios  are based  upon  the  following premises:
      1.   Air from a dry crushing or grinding  operation at  or near  ambient
          temperature.
      2.   An inlet particulate content of 10 grains  per standard  cubic  foot
          for a volume  of air equivalent to that required  for a  face  velocity
          of 200 ft/min at crusher openings.
     3.  A particle size average  of 20 microns and a range  from  0.5
         to 100 microns.
     4.  No insulation or heating required.
The I6CI report states that the segments considered the most  troublesome
are those with the lowest air-to-cloth ratio.   The lower ratios  employed
for some segments are premised upon such particulate properties  as  a  high
abrasiveness or a tendency to "blind" the filtering medium.  The study
further states that no differentiation in the air-to-cloth  ratio is required
for the source of emission be it crushing or grinding operation.  An
exception would be a micromill source emitting an average particle size
smaller than that cited  (i.e. 20 microns).  For such a source, a lower
air_to-cloth ratio would be  needed  than that  indicated in Table 4.3.
      The  industry segment with the  lowest  air-to-cloth ratio  listed  in
Table 4.3 is feldspar.   EPA  conducted tests for particulate  emissions at
a  feldspar  plant  on  a  baghouse controlling  emissions from  a  pebble mill
system.   The results of these tests indicate  particulate emissions below
0.023 g/dscm  (0.01  gr/dscf).  The baghouse had  a  design air-to-cloth
ratio of  3.03.
                                      4-37

-------
                Table 4.3.  AIR-TO-CLOTH RATIOS FOR FABRIC
                 FILTERS USED FOR EXHAUST EMISSION CONTROL
Industrial segment
Air-to-cloth?ratioc
     acfm/ftr
Sand and gravel
Clay
Gypsum
Lightweight aggregate
  Perlite
  Vermiculite
          7.
          6.
          6.
          7.5
Pumice
Feldspar
Borate
Talc and Soapstone
          4.5
          4.
          5.
          5.
Barite
Di atomi te
Rock Salt
          5.
          6.
          4.5
Fluorspar
Mica
Kyanite
Sodium Compounds

Gilsonite
Crushed and broken stone
          6.
          6.
          4.5
          6.

          N.R.
          7.
  Ratio is based on operating surface required to obtain a particulate
  concentration of 0.02 grain per standard cubic foot in the outlet
  stream from the filter.  In all cases, the filter is a pulse-jet
  type operating at 6 in. W.G. differential pressure.  The filtering
  medium is felted polypropylene or polyester.


  No recommendation for this segment.
                                  4-38

-------
     In addition, the I6CI report listed test results (using EPA sampling  .
Method 5) for two fluid energy mills processing clay (fuller's earth).  In
both cases, the particulate emissions were controlled by a fabric filter
and were below 0.023 g/dscm (0.01 gr/dscf).  The average particle size of
the inlet stream was reportedly below 10 microns in both cases.  EPA con-
ducted  tests for particulate emissions from a roller mill and a fluid energy
mill, both used to grind fuller's earth clay.  In both cases particulate
emissions were controlled by baghouses.  Emissions from the baghouse control-
ling the roller mill were less than 0.005 g/dscm (0.002 gr/dscf) and  those
from the fluid energy mill baghouse were less than 0.015 g/dscm (0.006 gr/dscf).
     Tests were also conducted at two talc plants and a gypsum plant on
baghouses controlling particulate emissions from various process sources.
Emissions from these baghouses were greater than 0.05 g/dscm (0.02 gr/dscf).
The higher emission levels are suspected to have been caused by the presence
of torn bags since there were excessive visible emissions either continuously
or frequently.  Tests conducted at a kaolin plant on an impact mill and a
roller mill resulted in measured emission rates of 0.037 and 0.016 g/dscm
(0.016 and 0.007 gr/dscf) respectively, for the two process operations.
     As previously indicated, test results are presented on only three of
the 18 industries being covered.  These are crushed stone (limestone  and tra-
pock), feldspar, and clay (fuller's earth, kaolin).  The .crushed stone data
are on crushing operations and associated process equipment.  The data for
feldspar, kaolin, and fuller's earth clay are for grinding systems.   All
the facilities tested are controlled by fabric filter collectors.  Since
the performance of fabric filter collectors is relatively unaffected  by the
size distribution of particulate, the emission levels from properly designed
baghouses should be nearly the same over the wide variety of non-metallic
                                      4-39

-------
  minerals being covered.27,28   Furthermore,  the  IGCI  report  stated  that
  there is no difference in performance  of a  baghouse  whether it  is  installed
  on a crushing or grinding operation for a particular industry.   The
  differences in design (air-to-cloth-ratio)  of a baghouse  for the various
  industries are premised upon  such particulate properties  as high abrasive-
  ness or a tendency to "blind  the filtering  medium."   The  IGCI report also
,  states that the worst situation would  be a  source emitting  an average
  particle size smaller than 20 microns.  The clay grinding mills (fluid  energy
  mill, see Section 3.2.2.3.4)  tested are the type of  grinders generally  used
  when an ultrafine product is  required.  Therefore, the data presented on
  the clay grinding mills, which have an average  particle size of 6  microns
  or less, would represent the  levels achievable  under worst  conditions.
       As discussed earlier, the average emission concentration for  the
  different process facilities  using properly operated baghouses  at  the various
  non-metallic industries shown in Figure 4-13 was 0.011 g/dscm (0.005 gr/dscf),
  The average outlet concentration at any of these facilities never  reached
  0.046 g/dscm (0.02 gr/dscf).  - In conclusion, it is felt that the data
  presented here are representative of the levels that can be achieved by
  a properly designed baghouse in each of the 18 industries.
                                                                 29
  4.3.1.2  Particulate Emission Data From Metallic Mineral  Plants
       In order to broaden the range of conditions considered for the
  performance of the control equipment,  test data for metallic mineral
  processing facilities are also included in the data base discussed in this
  chapter.  Data from the metallic mineral industries  may be  appropriately
  transferred to the non-metallic mineral industries for several  reasons.
  Much of the process equipment of interest in this document  is similar in
                                    4-40

-------
the metallic and non-metallic processing industries.  Because the ores
from which metallic-elements are extracted are primarly non-metallic in
character, the emissions from metallic mineral processing operations are
primarily non-metallic mineral constituents.  Furthermore, the similarity
of emissions from metallic and non-metallic processes in key parameters
such as particle size distribution and mass loading provide additional
evidence of similarity between the two industries.  These measurements
were routinely made during the testing of both metallic and non-metallic
processing facilities and form the basis for extrapolating control
efficiency from one industry, whether metallic or non-metallic, to another.
     Particulate emissions were measured by EPA for 8 baghouses used to
control emissions from crushing, screening, drying, and conveying operations
at 5 metallic mineral processing sites.  Table 4-4 presents a summary of
baghouse types and filter ratios (air-to-cloth) of the baghouses tested by
EPA for which information was available.  Figure 4-14 presents emission  •
levels after baghouse control.
     Plant V processes copper ore mined from low grade deposits (0.5 percent
copper) into concentrate.  This plant used a baghouse (VI) to control
emissions from a railcar loading operation that handled copper ore concen-
trate.  Use of baghouses under these conditions is fairly common because
the valuable product captured by the baghouse can be returned directly to
the operation.  A weighted average of the truck loadout hood and the
conveyor exhaust gave a calculated combined inlet concentration of
0.71 g/dscm (0.31 gr/dscf).  The baghouse outlet concentration averaged
0.03 g/dscm (0.013 gr/dscf) as shown in Figure 4-14.  Twenty percent of
the inlet particles at both truck loadout hood and conveyor belt exhaust
were smaller than 4 microns.
                                   4-41

-------














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             VI    Wl     W2  W3  XI    X2.    Yl      Zl

                                FACILITY

Figure 4-14.  Particulate emissions from baghouses at metallic mineral
              processing operations.
                            4-43

-------
     Plant W processes iron ore mined from an open pit operation.   Baghouse Wl
controlled emissions from a secondary and tertiary crushing operation and
associated screens.  The outlet concentration averaged 0.008 g/dscm
(0.003 gr/dscf) and ranged from 0.007 to 0.009 g/dscm (0.003 to
0.004 gr/dscf).  No inlet measurements or particle size distributions were
taken.
     Baghouse W2 at Plant W controlled emissions from the system that
conveyed ore from the fine crushers to the concentrator.  The inlet concen-
tration averaged 3.0 g/dscm (1.31 gr/dscf) and the outlet averaged
0.009 g/dscm (0.004 gr/dscf).  No particle size data were taken at this
facility.
     Baghouse W3 controlled emissions from an ore car dump.  The outlet
concentration averaged 0.007 g/dscm (0.003 gr/dscf).  No inlet measurements
or particle size distribtutions were taken.
     Plant X processes copper ore from an open pit mine.  Baghouse XI
controls emissions from a primary crusher complex including two grizzly
screens, the primary crusher hood, and ore bins.  The combined inlet duct
concentration averaged 5.43 g/dscm (2.37 gr/dscf) and the outlet averaged
0.013 g/dscm (0.006 gr/dscf).  Particle sizes of the combined inlet flow
were relatively large.  Ninety-five percent  of the inlet particles were
greater than 8 microns whereas 25 percent of the outlet particles were
greater than 8 microns.  The particle size distributions taken at the
grizzly screen duct and the primary crusher  hood duct were similar to the
combined inlet duct.
                                   4-44

-------
     Baghouse X2 controlled emissions from two truck dump stations from
which ore was fed to the primary crusher.  The combined inlet concentrations
averaged 0.304 g/dscm (0.133 gr/dscf) while the outlet averaged 0.041  g/dscm
(0.018 gr/dscf).  Fifty percent of the inlet particles were less than
4 microns while 20 percent of the outlet particle size distribution was
below that level.
     Plant Y processed imported bauxite into alumina.  One pulse jet
baghouse controlling emissions from an ore bin complex was tested.  The
control equipment configuration prevented sampling of the inlet duct.
The outlet from these ore bins averaged 0.007 g/dscm (0.003 gr/dscf) and
ranged from 0.007 to 0.009 g/dscm (0.003 to 0.004 gr/dscf).
     Plant Z processed gold ore from an underground mining operation.   The
baghouse at the milling operation controlled emissions from the primary,
secondary, and tertiary curshers, an ore storage inlet, and associated
conveyor transfer operations.  This baghouse had a design air-to-cloth
ratio of 9.1:1 and operated with a pulse jet cleaning system.
     During the testing of this baghouse, ore from 1500-1800 meters
(5000-6000 feet) underground was being processed.  This ore was characterized
by high levels of unbound water (4 to 5 percent) and warm temperatures
(25 to 30°C (80° to 90°F)) due to the depths from which it was extracted.
Because milling took place at the surface where the winter temperature
was 0 to 7°C  (30 to 45°F) condensation of moisture in the inlet ducts of
the baghouse was very evident.  The high moisture emissions combined with
the relatively high air-to-cloth ratio caused blinding of the fabric
filters rendering the pulse jet cleaning system ineffective.  As  a
consequence,  the pressure drop at the baghouse rose beyond design levels.
                                    4-45

-------
To circumvent this problem, the filter bags were cleaned by manually air-
lancing them before each test.  The pressure drop at the baghouse was
monitored closely during the tests.
     The duct configuration of the baghouse prevented measurement of the
combined inlet concentration.  The weighted average of the crusher inlet,
the conveyor transfer inlet, and the ore storage reclaim inlet resulted in
a concentration of 0.39 g/dscm (0.17 gr/dscf).  The outlet concentration
averaged 0.015 g/dscm (0.007 gr/dscf).  The particle size distribution at
all three inlet ducts were similar.  Thirty to forty percent of the
particles were less than 10 microns in diameter.
4.3.1.3  Visible Emissions Data
     Visible emission observations were also made during the emission tests
described above.  The opacity of the exhaust from each of the baghouses
was observed in accordance with EPA Method 9 procedures (Appendix A,
40 CFR Part 60).  Method 9 measures emissions in terms of percent opacity
ranging from 0 percent, representing no interference with transmission
of light, to 100 percent, representing complete interference with light
transmission.  Readings are taken at 15 second intervals and averaged
over 6-minute periods.
     As shown in Table 4-5, 21 of 24 baghouses showed zero emissions during
all observation periods.  The highest 6-minute average recorded at Plant B
was 1 percent opacity.  The highest 6-minute average for Baghouse 1 at
Plant X was 1 percent opacity and for Baghouse 2, the highest reading
was 6 percent opacity.  Plant L, a kaolin plant, exhibited continuous
visible emissions of less than 5 percent opacity.  This was considered to
                                   4-46

-------
TABLE 4-5.   OPACITY  MEASUREMENTS  FROM BA6HOUSE  EXHAUST  STACKS




Baghouse
Al
A2
A3
A4
Bl
B2
Cl
C2

Dl

D2
El
E2

61


LI
L2
HI
M2
VI

Ml


W2
W3
XI


X2
Yl
Zl



Processes controlled
Primary crusher
Primary crusher screen
Primary crusher transfer point
Secondary crusher and screen
Primary crusher
Secondary crusher complex
Primary crusher and hammer mill
Screens and conveyor transfer
points
Secondary and tertiary crushers
and screens
Screens and transfer points
Tertiary crushers and screens
Screens and conveyor transfer
points
Pebble mill, bucket elevator,
transfer points, and product
loadout
Impact mill
Roller mill
Roller mill
Fluid energy mill
Product loading including truck
dump hopper, and railcar loading
Secondary and tertiary crushing
operations and associated
screens
Conveyor transfer points
Ore care dump
Primary crusher complex including
grizzly screens, primary
crusher hood, and ore bins
Truck dump hopper
Ore storage bin
Primary, secondary, and tertiary


Mean
opacity
(percent)
0
0
0
0
0
0
0

0

0
0
0

0


0
0
0
0
0

0


0
0
0


0
. 1
0

Highest
6 minute
average
opacity
(percent)
0
0
0
0
1
1
0

0

0
0
0

0


0
0
0
0
0

0


0
0
0


1
6 .
0

Lowest
6 minute
average
opacity
(percent)
0
0
0
0
0
0
0

0

0
0
0

0


0
0
0
0
0

0


0
0 .
0


0
0
0

            crushers, ore storage, and
            conveyor transfer points
                             4-47

-------
be steam, since only the first of three tests (which was conducted in  the
morning) had visible emissions.  As the temperature of the ambient air
rose, the visible emissions dissipated.
     Observations for visible emissions were also made at hoods and enclosures
to record the opacity of emissions escaping capture.  The results of these
measurements are summarized in Table 4.6.  Complete data summaries are
contained in Appendix C.  In most instances, essentially no visible emissions
were observed at adequately hooded or enclosed process facilities.
     Of the 13 crushers for which visible emission measurements are
reported, 10 were cone crushers handling either limestone, traprock,
feldspar, or talc.  The other three crushers were an impact crusher handling
limestone and jaw crushers handling feldspar and talc.  Visible emissions
observed from crushers were less than 10 percent opacity.
     Visible emissions were observed at six grinding mills.  All  the mills
exhibited visible emissions of less than five percent.  Visible emissions
tests were conducted at the truck loading and rail car bulk loading operations
of a kaolin plant.  Visible emissions were less than 5 percent during  both
loading operations.  The primary source of emissions was the topping
of each compartment and the subsequent repositioning of the feed hose  in the
next compartment.
     Opacity measurements are also reported for eight screens, seven conveyor
transfer points, one bucket elevator, one product bin, and two baggers.
Visible emissions were less than 10 percent opacity from these process
facilities.
                                 4-48

-------






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4.3.2  Wet Dust Suppression Techniques
     Due to the unconfined nature of emissions from facilities controlled
by wet suppression technique, the quantitative measurement of mass particulate
emissions is not possible.  Thus, no mass emission data are available which
permit a quantitative comparison of the control capabilities of wet dust
suppression versus dry collection techniques.  Visible emission observations
were conducted at six crushed stone, and sand and gravel- facilities
(facilities F, P, Q, R, S, T) using wet dust suppression techniques to
control particulate emissions generated at plant process facilities.
Emissions generated by 13 crushers, 14 screens, 7 transfer points,
1 impact mill and 1 storage bin were visually measured by EPA Methods 9.
Facilities R and T are portable crushing facilities.  Facilities P,
Q, R, and T process crushed limestone, while facility F processes crushed
traprock, and facility S produces crushed granite..
     The results of the tests for non-crushing sources (e.g., screens,
transfer points, and storage bins) are summarized in Table 4.7.  These
results indicate that visible emissions were  10 percent opacity or  less.
The  results of the tests  for crushing sources  from  the best controlled
stationary  (facility S) and portable  (facilities R  and T) plants are summarized
in Figures  4.15 to 4.19.  The data are reported in  6-minute averaging of
Method  9 data.  For each  testing set  (approximately 1 hour),  the results of
the  two observers simultaneously measuring visible  emissions, are indicated
by a solid  and a dashed line.   In  spite of the fact that  facility R is
designated  a  well controlled portable crushing plant, the secondary
 crusher exceeded  15  percent opacity  several  times,  according  to  one of
 the  observers.  This  is attributed to the fact that during  the  test,  there
                                    4-51

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was no spray bar located near the crusher outlet.  It is felt that had the
spray bar for the crusher been relocated closer to the crusher then its
present position some 5 feet from the crusher, emissions would have dropped
below 15 percent opacity for all observer readings.
     The positioning and number of spray bars in some of the tested plants
may not have been adequate for effective emission control.  Plant S, which
was judged as the best-controlled plant based on the design and operation of its
wet suppression system was at the time of the testing a newly constructed
plant with the wet  suppression system designed into the plant.  Existing
plants may encounter difficulties in retrofitting the spray bars in the proper
locations due to space limitation or other  factors.  Therefore, the results
from Plant S may not be  representative of the effectiveness of wet suppression
systems  retrofitted to existing  plants.
     During the periods  of observation at facility  F  (see  Appendix C), no
visible  emissions were observed  at  two crushers.  The two  crushers were
observed simultaneously  for  a  period of  65  minutes.
     Visible  emission  observations  were  also conducted  at  a feldspar
crushing installation  which  had  a wet  dust  suppression  system to control
 particulate  emissions  generated  (see  facility G, Appendix  C) by crushers,
 screens, and conveyor  transfer points.   During  the  observations the
 suppression  system was used  only intermittently, presumably because  the  ore
 had sufficient surface moisture from  rains  the  previous day.  During  the
 periods of observation,  essentially no visible  emission were observed Surface
 moisture contents of the ore were 1.6 to 1.8 percent at the  primary  crusher
 discharge; 1.4 to 1.5 percent at the secondary crusher feed;  and  1.0 percent
 at the secondary crusher discharge conveyor.
                                     4-58

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REFERENCES FOR CHAPTER 4
 1.  "Rock Products Reference File -  Dust Suppression," Rock Products,
     May 1972, p.  156.
 2.  Meant, G.E.,  "Characterization of Particulate  Emissions from the
     Stone-Processing Industry,"  prepared by  Research Triangle  Institute for
     the United States  Environmental  Protection Agency, Contact No. 68-02-0607-10
     May 1975, p.  64.                                                     ;
 3.  Johnson-March Corporation, Product Literature  on Chem-Jet  Dust
     Suppression System,  1071.
 4.  Courtesy of Johnson-March Corporation.
 5.  Reference 4.
 6.  Hankin, M., "Is Dust the Stone Industry's Next Major  Problem," Rock
     Products, April 1967, p. 84.
 7.  "Air Pollution Control at Crushed Stone  Operations,"  National Crushed
     Stone Association, February  1976, page V-4.
 8.  Reference 6, p. 114.
 9.  Reference 7, page V-5.
10.  Anderson, D.M., "Dust Control Design by  the  Air  Induction  Technique,"
     Industrial Medicine and Surgery, February 1964,  p. 3.
11.  Telephone connversation between  Mr. Alfred Vervaert,  EPA,  and
     Mr. Joe McCorkel, Aggregates Equipment  Incorporated,  January 28,  1975.
12.  Reference 11.
13.  Reference 11.
14.  American Conference of Governmental Industrial Hygienists,  "Industrial
     Ventilation, A Manual of Recommended Practice,"  llth  Edition, 1970,
     p. 5-33.
15.  Reference 6, p. 2
16.  Reference 14, p. 5-32.
17.  Reference 14, p. 5-33.
18.  Reference 14, p. 5-31.
19.  Reference 14, p. 5-28.
                                    4-59

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20.  "Control Techniques for Particulate Air Pollutants," U.S. Environmental
     Protection Agency, Publication No. AP-51, January 1969, pp. 46-47.

21.  "Source Testing Report - Kentucky Stone Company, Russellville, Kentucky,"
     prepared by Engineering - Science, Incorporated, EPA Report No. 75-STN-3.

22.  "Emission Study at a Feldspar Crushing and Grinding Facility," prepared
     by Clayton Environmental Consultants, Incorporated, EPA Report
     Number 76-NMM-l.

23.  Reference 20.

24.  "Air Pollution Engineering Manual," Second Edition, U.S. Environmental
     Protection Agency, Publication AP-40.  p. 128, May 1973.

25.  Reference 25, p. 104.

26.  Emission Characteristics of the Non-metallic Minerals Industry,
     Industrial Gas Cleaning Institute, EPA Contract No. 68-02-1473,
     Task No. 25, July 1977.

27.  Reference 20.

28.  Billings, C.E., and J,  Wilder, Handbook of Fabric Filter Technology
     In:   Fabric Filter System Study (Volume I).   GCA Corporation,
     GCA/Technology Division.  Bedford, Massachusetts, Contract
     No.  CPA 22-69-38.  December 1970.

29.  "Metallic Mineral Processing Plants - Background Information for
     Proposed Standards, Volume 2" U.S. Environmental Protection Agency,
     EPA 450/3-81-009b, August 1982.
                                   4-60

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                      5.  MODIFICATIONS AND RECONSTRUCTIONS

5.1  MODIFICATION
     The facilities at non-metallic mineral processing plants that would be
subject to the proposed standards are each crusher, grinding mill, screening
operation, bucket elevator, belt conveyor, bagging operation, storage bin,
enclosed truck loading station, and enclosed rail car loading station.  For  a
change to be termed a modification, it must result in an increase in emissions
from any one of these process operations.
     Under the modification provisions, actions that would not be considered
modifications, regardless of emission increase, include the following:
     A.   Routine maintenance, repair, and replacement, such as replacement or
          refurbishing of components subject to high abrasion and impact
          (crushing surfaces,  screening surfaces,  conveyor belts,  etc.).
     B.   An  increase in  the production rate,  if the increase can  be
          accomplished without a capital expenditure exceeding the product  of
          the existing facility's Internal  Revenue Service annual  asset
          guideline repair allowance of 6.5 percent per year and  the facility's
          basis.
     C.   An  increase in  the hours  of operation.
                                     5-1

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     D.   -Use of an alternative raw material,  if the existing facility was
          designed to accomodate such material.   Because process  equipment
          (crushers, screens, conveyors, etc.) is designed to accommodate
          a variety of rock types, any change  in raw material feed would not
          likely be considered a modification.
     E.    The addition or use of any air pollution control system except
          when a system is removed or replaced with a system considered to
          be less effective.
     F.   'The relocation or change in ownership of an existing facility.
     The expected impact of the modification provision on existing
non-metallic mineral processing facilities should be very slight.  No
condition is currently foreseen that would allow an existing non-metallic
mineral  processing facility to be modified under this definition.
     When expansions at existing plants take place, usually a completely
new crushing/grinding line is added (with the possible exception  of the
primary crusher).  Such an increase in production would not be considered
a modification but rather a series of new sources.  Primary crushing
operations at non-metallic mineral plants usually operate below 100 percent
capacity and are capable of handling increased throughput without additional
equipment.  Under  (B) above, an increase in production at the primary crusher
would not be considered a modification.
5.2  RECONSTRUCTION
     The reconstruction provision is applicable only where replacement of
components of an existing facility exceeds 50 percent of the fixed capital
cost that would be required to construct a similar new facility and air
pollution control  techniques are shown to be technologically and economically
                                     5-2

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feasible.  For the non-metallic mineral industries, replacement or refurbishing
of equipment parts subject to h'igh abrasion and impact such as crushing surfaces,
screening surfaces, and conveyor belts are performed on a regular basis and
could be considered routine maintenance.  The cumulative cost of these repairs
to any one piece of equipment over a period of time could exceed 50 percent of
the fixed, capital cost of entirely new equipment.
                                     5-3

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                         6.   EMISSION CONTROL SYSTEMS

      The alternative control  systems that are considered  the  best  combination
 of the control  techniques  previously discussed are  presented  in  this  chapter.
 The analysis  of environmental  effects  in  Chapter 7  and  of economic impacts  in
 Chapter 8 will  examine the  impacts  associated with  the  alternative emission
 control  systems.
      As  discussed  in Chapter  4,  both dry  collection  and wet .suppression systems
 are considered  as  viable control alternatives.   Unfortunately, the emissions
 from a wet suppression system are not  amenable  to measurement and  therefore
 cannot be quantified.   In addition,  wet suppression  systems cannot be used
 in  all  cases  throughout the industry and  therefore cannot  be considered a can-
 didate for best technology.  Thus, major  emphasis of developing the environ-
mental and economic  impacts for the  non-metallic mineral industry will be placed
on  dry collection systems and wet suppression systems will be discussed only
briefly.   Since the dry collection systems are more costly and require more
energy (for fans), the impacts on the industry will  be  overstated  as compared
to an analysis based on industry use of both dry and wet collection systems.
     The model plants which will be  analyzed for estimating cost impact and
environmental  impact are shown in Table 6.1.  Two basic models of non-metallic
mineral plants were developed.  The  first model plant consists of crushing
operations only, and includes:  primary, secondary,  and ler~iar-T' c>-_,s  ,-•
three or four  screening operations,  five to 10 transfer points,  and the storage
bin loading operation.  The second model plant includes both a crushing

                                     6-1

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                     Table 6.1 Model Plants for  Estimating  Environmental
                                      and Economic  Impact
Plant
Size
[Mg/hr (TPH)]
9.1 (10)
9.1 (10)
22.7(25)
22.7(25)
68.0(75)
68.0(75)
Model
Plant
1
2
1
2
2
2
Gas Volume Plant
to-Baghouses Size
[nTVs (cfm)] [Mg/hr (TPH)]
4.8 (10,200)
4.8 (10,200)
1.9 (4,000)
5.4 (11,500)
5.4 (11,500)
2.2 (4,700)
8.4 (17,800)
8.4 (17,800)
3.2 ( 6,700)






136 (150)
136 (150)
272 (300)
272 (300)
544 (600)
- 544 (600)
Model
Plant
1
2
1
2
1
2
Gas Volume
to,Baghouses
[m3/s (cfm)]
11.8 (25,000)
11.8 (25,000)
5.3 (11,300)
18.9 (40,000)
3.8 ( 8,000)
18.9 (40,000)
3.8 ( 8,000)
10.4 (22,600)
4.2 ( 9,000)
15.1 (32,000)
14.6 (31,000)
4.2 ( 9,000)
15.1 (32,000)
14.6 (31,000)
21.2 (45,200)
Notes:  'Model 1 - crusher  (prima-y, secondary,  arr  -••.-'.•-/,
                   screens  (3 cr -;, transfer  pc-ir.U  . i  to  ".O/,
                   and storage bir.  loading  operation.

        "Model 2 - crusher  (primary, secondary,  and  tertiary),
                   C'-fr'der, screens  (3  or 4).  transf-.r point1;
                   (5 LU  10), storage bin loading  operation,
                   and bagging machine.

        "In all cases, baghouses are used as the control  device(s)
                                         6-2

-------
 operation and a grinding operation—the latter consisting  of  a  grinding mill,
 classifier or screen,  two additional transfer  points  and a bagging machine.
 Both model plants  use  baghouses  as  the  control  device(s).
      The model  plants  for analysis  consist  of  9,  23,  68, 136, 272, and 544
 megagrams per hour (Mg/hr)  (10,  25,  75,  150, 300  and  600 tons per hour)
 stationary plants.   The  portable crushing plant segments of the crushed stone,
 and  sand and  gravel  industries are  discussed in Supplement A.
      The process equipment  and associated energy  requirements and air volumes
 used in  defining the model  plants are contained in Table 6.2.  The parameters
 listed are used as  the basis  for the energy usage calculations presented in
 Section  7 and the  cost and  economic  impact analysis in Section 8.  Parameters
 for  the  272 and 544  Mg/hr (300 and 600 ton/hr)  model  plants were derived from
 flow diagrams  presented  in  the industrial literature.  Energy requirements and
 gas  volumes for the  smaller model plants were calculated from equipment spec-
 ifications and  flow  correlations.
      The two  model plants and six plant sizes are not applicable to each non-
 metallic mineral industry.  The  model plant used  for  each  industry, the*: b
'typical  range of plant sizes found in the industry, the typical plant size"
 and  the  plant sizes which will be used in determining the  economic and environ-
 mental impacts  for each  industry are listed in  Table 6.3.  All the industries
 employ crushing and grinding operations (Model   Plant 2) except crushed and
 broken stone, sand and gravel, perlite, vermiculite and rock salt.  Generally,
 the  size  of non-metallic minerals plants is less  than 136 Mg/hr (150 TPH)
 except for plants in the  crushed stone, and sand  and gravel  industries.
                                     6-3

-------








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6-5

-------
              TABLE 6.3.  'PLANT SIZES FOR THE VARIOUS NON-METALLIC
                            MINERALS  INDUSTRIES (METRIC UNITS)
Industry 	
Crushed f> Broken Stone
Sand & Gravel
CUy
Rock Gait
Gypsum
Sodium Compounds
Pumice
Gllsonlte
Talc
Boron
BaHte
Fluorspar
Feldspar
Dlatomlte
Pprllte
Verm1cul1te
H1ca
Kyanlte
Plant
Model
Used
1
1
2
1
2
2
2
2
2
2
2
2
2
2
1
1
2
2
Range Typical Size*
Mg/hr Mg/hr
-
14-2177
4-136
-753
-
-204
5-30
-
5-18
31-385
9-45
-23
5-23
8-60
15-54
68-272
-
-
272
272
23
68
23
23
9
9
9
272
9
9
9
23
.23
68
9
9
Model Plant Sizes**
Pertinent to the Industry Mg/hr
23,68,136,272
23,68,136,272
9,23,68,136
23,68,136,272
9,23,68
23,68,136,272
9,23,68
9,23.68
9,23
23,68,136,272
9,23.68
9.23
9,23
9,23,68
9,23,68
68,75,150,272
9,23
9,23,68
,544
,544

,544





,544








*  These values will be  used to estimate the air Impact on mass emissions for each industry.
** Thesf values will be  used to estimate the economic impact on each industry.
Note:  In all  cases, baghouses are used as  the control device(s).
                                        6-6

-------
                TABLE 6.3.   PLANT  SIZES  FOR THE VARIOUS  NON-METALLIC
                              MINERALS INDUSTRIES (ENGLISH  UNITS)
Industry
Crushed 4 Broken Stone
Sand & Gravel
Clay
Rock Salt
Gypsum
Sodium Compounds
Pum1 ce
GUsonlte
Talc
Boron
BarUe
Fluorspar
Feldspar
D1atom1te
Perllte
Verm1cu11te
M1ca
Kyanlte
Plant
model
used
1
1
2
1
2
2
2
2
2
2
2
2
2
2
1
1
2
2
Range
(TPH)

15-2400
4-150
-830
-
-225
5-33
-
6-20
34-425
10-50
-25
5-25
9-66
16-60
75-300
-
-
Typical Size*
ITPH)
300
300
?5
75
25
25
10
10
10
300
10
10
10
25
25
75
10
10
Model Plant Sizes**
Pertinent to the Industry .-P-
25,7-1., 150,300,600
1-5, ?E. 150,300 600
-10,25,757150
25,75,150,300,600
10,25,75
25,75,150,300
10,25,75
10,25,75
10,25
25,75,150,300,600
10,25,75
10,25
10,25
10,25,75
10,25,75
75,150,300
10,25
10,25,75
*  These values win be  used to estimate the air Impact on mass emissions for each Industry.
** These values will be  used to estimate the economic Impact  on each Industry.
Note:   In all  cases, baghouses are used as  the control device(s).
                                        6-7

-------

-------
                           7.  ENVIRONMENTAL IMPACT








       An assessment of the incremental impact to the environment associated


  with the application of the emission reduction systems described in Chapter 4


  is presented below.   Beneficial  and adverse impacts on air,  water,  solid


  waste,  energy and noise which may be directly or indirectly  attributed


  to the  operation  of  these emission control  systems  are assessed.


  7.1   AIR POLLUTION IMPACT



       To  determine the  true  impact of standards  of performance on air


  pollution, one must  determine the reduction in  air  pollution they effect


  beyond that which  would otherwise be achieved by state  and local regulations.


  As noted  in Section  3.2.3, present regulations which limit the emission of


  particulate from non-metallic minerals processing facilities take many


 forms and vary greatly in stringency and enforcement.   For the purpose



 of this  analysis,  it is assumed that all  non-metallic minerals plants
                                                            \

 are subject to a  general  process  weight regulation designed to limit


 particulate emissions from any source.  Table  7.1  summarizes  the high,


 low,  and  typical emission  rates allowed under  these  State process weight


 regulations.   An assessment  of the national  air  pollution impact and the


 results of dispersion analyses  conducted  for 12  model  plants  are presented


 below.



 7-1.1  National Air Pollution  Impact



     The  production of  the various  non-metallic minerals is projected  to


 increase  at compounded  annual growth  rates of up to  six  percent  through the


year 1985.  Table 7.2 presents for each non-metallic mineral, the growth
                                   7-1

-------
              Table 7.1  Allowable Emissions Under General

                     State Process Weight Regulations
Process Weight Rate
 ^3
Allowable Emissions, ] kg/hr (Ib/hr)
                      Low        Typical
1 U K
0.
2.
4.
9.
18.
27.
54.
g/ m
5
3
5
1
1
2
4
90.7
453.6
y mils/ 111 . ;
(0.5)
(2.5)
(5.0)
(10.0)
(20.0)
(30.0)
(60.0)
(100.0)
(500.0)
1.
3.
6.
13.
27.
30.
31.
43.
3
5
9
7
1
5
1
2
119.9
^" 	
(2.8)
(7.7)
(15.2)
(30.0)
(59.7)
(67.2)
(68.2)
(95.2)
(264.0)
0.
2.
2.
4.
5.
7.
15.
13.
18.
7
9
7
0
7
1
1
4
2
(1.6)
(6.3)
(6.0)
(8.7)
(12.5)
(15.6)
(33.3)
(29.5)
(40.0)
1.
3.
5.
8.
13.
18.
21.
23.
31.
2
4
5
7
9
2
0
2
3
(2.6)
(7.6)
(12.0)
(19.2)
(30.5)
(40.0)
(46.3)
(51.2)
(69.0)
                                     7-2

-------
TABLE 7.2  GROWTH RATES AND MINERAL PRODUCTION LEVELS FOR THE
           VARIOUS NON-METALLIC MINERALS INDUSTRIES
Mineral
Crushed and broken
stone
Sand and gravel
Clay
Rock salt
Gypsum
Sodium compounds
Pumice
Gilsonite
Talc
Boron
Barite
Fluorspar
Feldspar
Diatomite
Perlite
Verm'culite
Mica
Kyanite
Total
Estimated
production
10;
megagrar.s
981,839 (1
752,538
52,834
16,482
9,764
5,124
4,193
99
1,065
1,357
1,301
146
739
678
779
364
148
114
1,829,564 (2,
1980
level
1 ,000
tons
,082,292)
(829,531)
(58,240)
(18,168)
(10,763)
(5,648)
(4,622)
(109)
(1,174)
(1,496)
(1,434)
(161)
(815)
(747)
(859)
(401)
(163)
(126)
016,749)
Annual2
projected
growth
rate (•'.-)
4.0
1.0
3.5
2.0
2.0
2.5
3.5
2.0
4.0
5.0
2.2
3.0
4.0 '
5.5
4.0
4.0
4.0
6.0

Estimated
production
103
megagrams
1,194,557 (1
790,925
62,750
18,186
10,783
5,800
. 4,980
111 "
1,296
1,731
1,451
171
900
888
948
443
181
153
2,096,255 (2,
1985
level ,
1,000
tons
,316,774)
(871,847)
(69,171)
(20,046)
(11,886)
(6,394)
(5,490)
'(122)
(1,428)
(1,909)
(1,600)
1 (188)
(992)
(979)
(1,045)
(488)
(200)
(168)
310,726)
                            7-3

-------
rate, the estimated 1980 production level  based on the 1975  reported  produc-
tion level, and the 1985 estimated production level.   Based  on the latest
reported (1975) production levels, annual  production  for all  18 non-metallic
minerals was 1605 x 10s megagrams (1769 x 106 tons) in 1975  and will  increase
to 1829 x 106 megagrams (2016 x 106 tons) in 1980, and 2096  x 10& megagrams
(2311 x 106 tons) in 1985.  If one assumes that all existing plants are now
operating at 80 percent of capacity, then new plants and expansions to existing
plants will be required to produce an additional 333 x 106 megagrams (368  x   .
10*  tons)  in production capacity  projected for the 5-year period from 1980
through  1985.  An  assessment of  the air pollution  impact associated with these
capacity  additions  for each industry segment  is presented in Table 7.3.
Process  steps  included in  this evaluation are crushing, grinding,  sizing,  and
handling.   Handling includes conveying,  bagging,  storage bin  loading and fine
product loading.   Combustion sources  (e.g.,  dryer or  kilns)  are  not  included
 in the analysis.   The largest  tonnage  reduction  is in the crushed and  broken
 stone industry followed by the clay industry and  the  sand and gravel  industry.
 Reductions in the other industry segments are much smaller.
      The following procedure was used to arrive at the numbers listed  in
 Table 7.3.  The values for allowable 1985 emissions under existing State
 standards were developed by applying a typical process weight regulation
 (see Table 7.1) to a  typical plant size (see Table 6.3) for each industry.
 Using the additional  ore processing capacity installed between 1980 and
 1985 the 1985 emissions due to the new facilities were then calculated.   (A
 plant having both  crushing and grinding operations is assumed to be covered by
                                     7-4

-------
TABLE 7.3  SUMMARY OF AIR  POLLUTION  IMPACT
           [megagrarn/year  (ton/year)]


.1.— .


Allowable 1985 emissions under
Industry segment
Crushed and broken
stone
Sand and -gravel
ay
Rock salt
Gypsum
Sodium compounds
Pumi ce
Gilsonite
Talc
Boron
Barite
Fluorspar
Feldspar
Diatomite
Perlite
Vermiculite
Mica
Kyanite
Total
Existing Standards of
state regulations ,n°-°5 9/dscm
(0.02 gr/dscf)
21,272
3,838
13,978
545
1,440
945
1,512
23
444
74
288
48
309
301
119
25
63
• 76
45,337
(23,448)
(4,231)
(15,409)
(601)
(1,587)
(1,042)
(1,666)
(25)
(489)
(82)
(317)
(53)
(341)
(332)
(131)
(28)
(69)
(84)
(49,976)
2,923
527
549
35
53
32
93
23
28
74
18
9
9
11
(7)
3
9
9
4,412
(3,222)
(581)
(605)
(39)
(58)
(35)
(102)
(25)
(31)
(82)
(20)
(10)
(10)
(12)
(8)
(3)
(10)
(10)
(4,863)


Reduction -imnart


Megagram/ (ton/
year • year)
' — ' • • .. .!•..
18,385
3,311
13,430
510
1,387
974
1,419
0
415
0
269
39
300
290
112
23
52
67
40,926
(20,266)
(3,650)
(14,804)
(562)
(1,529)
(1 ,007)
(1,564)
(0)
(458)
(0)
(297)
(43)
(331)
(320)
(124)
(25)
(59)
(74)
(45,113)
                   7-5

-------
a process, weight regulation which is twice that presented in Table 7.1).
The additional ore processing capacity was determined for each industry
by multiplying the additional industry capacity (1985 capacity minus 1980
capacity) by the ore to product ratio for each industry.  For industries
such as crushed stone, sand and gravel, clay and talc, the ore to product
ratio is 1.0.  Most industry values range between 1.0 and 2.0 with a few
[boron (5.8), vermiculite (4.0), fluorspar (3.0), mica (4.2)] ranging
above 3.  The values for allowable 1985 emissions under a potential
NSPS were calculated using the same procedure except that a gas volume
was assigned for the specified plant size and the value 0.05 g/dscn
(0.02 gr/dscf) was used to calculate the emission level in terms of a
process weight rate.  The reduction impact is the difference between
the allowable 1985 emissions due to the State regulations and the potential
NSPS for new  capacity additions.
     Assuming that all states enforced standards equivalent to the typical
process weight regulations,  capacity additions over  the 5-year period
1980-1985 would  result in the emission of an additional 45,337 megagrams
 (49,976  tons) of particulate in  the year 1985.   If standards of performance
are  promulgated  at the level of  0.05 g/dscm  (0.02 gr/dscf), then  only  an
 additional  4,412 megagrams  (4,863  tons) of  particulate  emissions  would
result.  Consequently, the  national  impact  in air pollution reduction
effected by standards of  performance  if promulgated  at  the  level  of  0.05  g/dscm
 (0.02  gr/dscf) would  be on  the  order  of 40,926 megagrams  (45,113  tons)  of
 particulate in  the year 1985.   It  should  be  noted that  because of the  lack
                                    7-6

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 of uniformity of existing state regulations and the discretionary manner
 in which these regulations are enforced,  the level  of control  at existing
 plants is very likely below that established by the assumptions  that all
 existing plants are subject to the typical  process  weight regulation and
 that these regulations are universally enforced.   In addition, the air
 pollution impact assessed above does not  account for that portion of
 existing equipment which would be replaced  with new equipment, therefore
 becoming subject to standards  of performance due to obsolescence.   As a
 result,  the true impact would  probably exceed that  presented above.
 7.1.2 Dispersion Analysis
      Dispersion calculations were performed  on  six  model  plants  with  typical
 production  capacities  of 9, 23,  68,  136,  272, and 544 megagrams  per  hour
 (10,  25,  75,  150,  300,  and  600 TPH).   For each model, calculations were performed
 for  two  levels  of  emission  control which  included that achievable  using best
 control  technology and  that required to meet  typical State regulations.   A
 dry  collection  system  is  assumed  to  be used  to meet both  levels  of control
 because:   (a) emissions when wet  suppression  is used are  discharged  in an
 unconstrained manner (not discharged through  a stack); and (b) because emission
 rates achievable by wet suppression were  not determined in this  study and are
 not otherwise available.  Results of the  analysis,  including characteristics
of the models used and assumptions made,  are presented below.
7.1.2.1  Model Plant Characteristics - The model plants selected are identical
to those used in the following chapter in assessing the economic impact.   As
in Chapter 8, the 9,23,68 and 136 Mg/hr (10, 25, 75, and 150 TPH) plants  are
assumed to use two fabric filters for control and the 272 and 544 Mg/hr
                                 7-7

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 (300 and 600 TPH) plants are assumed to use three and four fabric filters,
 respectively.  (One less fabric filter is used in each model plant if a
 grinding operation is not employed).  It is also assumed that proper
 hooding and indraft velocities are used so that all  emissions from the
 process equipment are captured.  Figure 7.1 shows the physical configuration
 of the discharge points for each model.  For the 9,  23, 68, and 136
 Mg/hr (10,  25,  75, and 150 TPH) plants, the No.  1 stack is from a fabric
 filter controlling emissions from the crushing operation and its associated
 screening and handling operations,  and the No. 2 stack is from a second
 fabric filter controlling the grinding operation and its associated
 screening and handling operations.   The 272 Mg/hr (300 TPH)  plant is
 controlled  by three fabric  filters;  one for the  primary crusher, the
 second for  the  remaining  crushing operations;  (i.e.,  secondary and
 tertiary crushing and screening and  associated material  handling operations),
 and  the third for the grinding system.   The 544  Mg/hr (600 TPH)  plant  is
 controlled  by four fabric filters; one for the primary crusher,  the
 second for  the  secondary  crusher and screens,  the third  for  the  tertiary
 crushers  and  finishing screens,  and  the fourth for the grinding  system.
     The  dispersion  calculations were  performed  assuming  two  levels of  emission
                   3
 control:  0.05  g/m  (0.02 gr/dscf) and  the  process weight  regulation for Ohio
which  was chosen  as  typical  of  State  regulations.  The emission  source
characteristics for  the model  plants are presented in  Table 7.4.  A control
efficiency of about  95 percent would be required  to meet the  typical process
weight regulation  and  better than 99 percent to reflect that  achievable
using best control.
                                    7-8

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                             SOURCE  LOCATIONS
               t
               N
                    (a)  10, 25 and 75 TPH PLANTS
              t
              N
                                           o

                                           2
                   Cb) 150  TPH  PLANTS
                                           5O
100 METERS
Figure  7.1    Plant ^outs showing the number and locations of the sources (stacks)

             specified for each plant size.  The filled circles show the locations

             of the individual stacks.  The  (©> symbols show the origins of the

             receptor grids used in the model calculations.
                                  7-9

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                SOURCE LOCATIONS
    t
    N
          o
          I
         (c)  300 TPH PLANTS
     t
     N
                              •
                              2
         (d)  600 TPH  PLANTS
                             5O
IOO METERS
Figure 7.1 (continued)
                      7-10

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        Table 7.4
STACK AND EMISSIONS DATA
    (Metric Units)
Plant
Size
Casea (Mq/hr)
1 9
2 9
3 23
4 23

5 68

6 68
7 136

8 136

9 272


10 272


11 544



12 544


— 	 	 . 	 _
Stack
Number
1
2
1
2
1
2
1

1

1
2
1

1

1


1
2
3
1
2
3
4
1
2
3
4
Stack
Diameter
(m)
0.58
0.33
0.58
0.33
0.61
0.37
0.61
0.37
0.76
0.43
0.76
0.43
0.79
0.55
0.79
0.55
0.58
1.07
0.76
0.58
1.07
0.76
0.61
0.91
0.91
1.10
0.61
0.91
0.91
1.10
Stack
•Height
(m)
9.1
12.2
9.1
12.2
9.1
12.2
9.1
12.2
9.1
12.2
9.1
12.2
9.1
12.2
9.1
12.2
6.1
9.1
12.2
6.1
9.1
12.2
6.1
9.1
9.1
12.2
6.1
9.1
9.1
12.2
Stack
Exit
Velocity
(m/sec)
18.0
23.0
18.0
23.0
18.0 -
23.0 '
18.0
23.0
18.0 '
23.0
18.0
23.0
23.0
23.0
23.0
23.0
15.0
23.0
23.0
15.0
23.0
23.0
15.0
23.0
23.0
23.0
15.0
23.0
23.0
23.0
Stack
Exit
Temperature
\ *^ )
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
Particulat
Emission
Rate
I n / c o r* \
i.g/sec)
0.24
0.09
2.42
2.42
0.27
0.11
4.46
4.46
0.41
0.15
6.10
6.10
0.58
0.26
6.74
6.74
0.18
0.92
0.52
1.52
6.06
6.10
0.21-
0.74
0.71
1.04
i.n
3.84
3.96
6.72
Odd numbered cases are based on an emission level of 0.05
                              on allowabie
                              (0 02
    7-11

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                                       Table  7.4

                               STACK AND  EMISSIONS  DATA
                                    (English  Units)
Case3
1

2

3

4

5 '

6

7

8

9


10


11



12



Plant
Size
(tph)
10

. 10

25

25

75

75

150

150

300


300


600



600



• Stack
Number
1
2
1
2
1
2
1
2
1
2
1
2
1
2
1
2
1
2
3
- 1
2
3
1
2
3
4
1
2
3
4
Stack
Diameter
(ft)
1.9
1.0
1.9
1.0
2.0
1.2 .
2.0
1.2
2.5
1.4
2.5
1.4
2.6
1.8
2.6
1.8
1.9
3.5
2.5
1.9
3.5
2.5
2.0
3.0
3.0
3.6
2.0
3.0
3.0
3.6
Stack
Height
(ft)
30
40
30
40
30
40
30
40
30
40
30
40
30
40
30
40
20
30
40
20
30
40
20
30
30
40
20
30
30
40
Stack
Exit
Velocity
(ft/min)
356
455
356
455
356
455
356
455
356
455
356
455
455
455
455
455
300
455
455
300
455
455
300
455
455
455
300
455
455
455
Stack
Exit
Temperature
(°F)
ambient
ambient
ambient
ambient-
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
ambient
Parti cul ate
Emission
Rite
(Ib/hr)
1.9
0.7
19.2
19.2
2.1
0.9
35.4
35.4
3.3
1.2
48.4
48.4
4.6
2.1
53.5
53.5
1.4
7.3
4.1
12.1
48.1
48.4
1.7
5.9
5.6
8.3
8.8
30.5
31.4
53.3
Odd numbered cases are based on an emission level of 0.05 g/m  (0.02 gr/dscf).
Even numbered cases are based on allowable emissions if typical State process
weight regulations are used.
                                      7-12

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     7.1.2.2  The Dispersion Model and Meteorological Considerations - The
dispersion model used to analyze the air pollution impact of the plants
described above is the modified Single-Source (CRSTER) Model developed by
the Meteorology and Assessment Division, EPA.  The dispersion analysis was
                                                 3
performed by H. E. Cramer Company, Incorporated.
     A preliminary analysis showed that maximum short-term ground-level
concentrations produced by emissions from stacks of the type listed in
Table 7.4 are most likely to occur during periods of light-to-moderate wind
speeds and persistent wind directions in combination with neutral stability.
These meteorological conditions are quite common in the Pittsburgh,
Pennsylvania area.  Also, non-metallic minerals processing plants are located
in the vicinity of Pittsburgh.  Consequently, it was decided that the surface
and upper-air meteorological data for the Greater Pittsburgh Airport were
representative and should be used to develop the meteorological inputs
required for the dispersion-model calculations.  Because the plants are
assumed to be located outside the Pittsburgh urban area, a rural location was
assumed in the model calculations.  The prevailing wind directions in the
Pittsburgh area during periods of neutral D stability are from the west.
In order to maximize the superposition of plumes from individual sources
under worst-case meteorological conditions, all plant configurations were
given an east-west orientation (see Figure 7.1).
     The results of the preliminary analysis also showed that the maximum
short-term ground-level concentrations produced by emissions from the
sources listed in Table 7.4 can be expected to occur at downwind distances
                                      7-13

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 ranging from less than 300 meters (330 yards) to about 900 meters (985 yards).
 The property boundaries of the six plants are assumed to be a minimum distance
 of 300 meters from any stack.  For the purposes of this study, only ground-
 level particulate concentrations that occur at and beyond the plant property
 boundaries were used in assessing the air quality impact of plant emissions.
      From a consideration of the results of the preliminary analysis and
 the fact that only off-property ground-level particulate concentrations
 are of concern, two receptor grids were constructed for calculations.  The
•^©symbols in Figure 7.1 show the origins of these receptor grids.  The
 receptor grid used in the model calculations for the 9, 23, 68, and 136 Mg/hr
 (10, 25, 75, and 150 TPH) plants comprised seven concentric receptor rings with
 radii of 0.335, 0.4, 0.5, 0.6, 0.8, 1.0 and 1.5 kilometers (366, 437, 547, 656,
 875, 1094, and 1640 yards).  The receptor grid used in the model calcu-
 lations for the 272 and 544 Mg/hr (300 and 600 TPH) plants comprised six
 concentric receptor rings with radii of 0.38, 0.5, 0.6, 0.8, 1.0 and 1.5 kilo-
 meters  (415, 657, 656, 875, 1094 and 1640 yards).  All receptor grid points were
 assumed to be at the same elevation as plant grade.  Thus the only terrain
 effects included in the model calculations are those implicitly contained in
 the meteorological data from the Greater Pittsburgh Airport.
 7.1.2.3  Results and Discussion of Dispersion Calculations - Maximum 24-hour
 average and annual-average concentrations are presented in Tables 7.5 & 7.6.
 All 24-hour and annual maximums were located at either 0.3 or 0.4 kilometer
 (328 or 437 yard) from the plant.  Generally, for each case, less than 10
                                   7-14

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                                          Table 7.5

                ESTIMATED MAXIMUM 24-HOUR AND ANNUAL GROUND-LEVEL PARTICULATE
                       CONCENTRATION DUE TO EMISSIONS FROM THE PROCESS
                      SOURCES IN THE MODEL NON-METALLIC MINERALS PLANTS
                        HAVING BOTH CRUSHING AND GRINDING OPERATIONS
      Plant Size
[Mg/hr (tons/hour)]
Case*
    24-Hour Average             Annual Average
Distance to      Maximum    Distance to      Maximum
  Maximum     Concentration   Maximum     Concentration
    (Km)        (pg/rn13)         (Km)        (yg/m3)
9 (10)

23 (25)

68 (75)

136 (150)

272 (300)

544 (600)

1
2
3
4
5
6
7
8
9
10
11
12
0.3
0.3
0.3
0.3
0.3
0.3
0.4
0.3
0.4
0.4
0.4
0.4
14
200
15
354
20
430
24
383
40
279
64
363
0.2
0.3
0.3
0.3
0.3
0.3
0.3
.0.3
0.4
0.4
0.4
0.4
' 2
16
2
28
2
34
2
31
4
27
5
28
  Odd number cases are based on an emission  level  of  0.05  g/m3  (0  02  qr/dscf)
  Even number cases are based on allowable emissions  under typical  State  process
  weight regulations (as shown in Table  7.1)
                                        7-15

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                                          Table 7.6

                ESTIMATED MAXIMUM 24-HOUR AND ANNUAL GROUND-LEVEL PARTICULATE
                       CONCENTRATION DUE TO EMISSIONS FROM THE PROCESS
                      SOURCES IN THE MODEL NON-METALLIC MINERALS PLANTS
                               HAVING ONLY CRUSHING OPERATIONS
      Plant Size
[Mg/hr (tons/hour)]
Case0
    24-Hour Average             Annual Average
Distance to      Maximum    Distance to      Maximum
  Maximum     Concentration   Maximum     Concentration!
    (Km)        (ug/nT)         (Km)        (yg/mJ)    '
9 (10)

23 (25)

68 (75)

136 (150)

272 (300)

544 (600)

1
2
3
4
5
6
7
8
9
10
11 •
12
0.3
0.3
0.3
0.3
0.3
0.3
0.4
0.3
0.4
0.4
0.4
0.4
10
107
11
191
15
223
16
187
29
208
48
259
0.2
0.3
0.3
0.3
0.3
0.3
0.3
0.3
0.4
0.4
0.4
0.4
1
8
1
14
1
17 .
1
15
3
16
4
20
   Odd number cases are based on an emission level  of 0.05 g/m  (0.02 gr/dscf).
   Even number cases are based on allowable emissions under typical  State process
   weight regulations (as shown in Table 7.1)
                                         7-16

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 percent of the days  per year had 24-hour  average  concentrations exceeding
 70 percent of the maximum concentration  shown  in the  Table.
        The national  primary ambient  air quality standards  for  particulate
 matter,  as published in the Federal  Register, Volume 36, No. 84, April 30,
 1971,  are:
        a.   75 micrograms per cubic meter—annual  geometric mean;
        b.   260-micrograms  per cubic meter—maximum 24-hour concentration not
            to be  exceeded  more  than once  a year.
 Assuming a  pristine  atmosphere,  the data  presented in  Table 7.5 indicate that
 for all cases,  excluding emissions from sources other  than the stack, a
 plant meeting an  emission  limitation of 0.05 g/m3  (0.02 gr/dscf) would meet
 the ambient air quality  standards.  In comparison, any plant with a pro-
 duction rate  above 9 Mg/hr  (10 TPH) which just meets the typical process
weight regulation, even  though it may require a 95 percent reduction from
uncontrolled  levels would exceed the ambient air quality standards for
the 24-hour average.
       The dispersion results presented are only for plant process facilities
under consideration.   Process operations common to most plants  which are not
covered by the proposed standard include drilling, blasting, loading at the
mine, hauling, stockpiling, conveying (other than  transfer points), and
windblown dust from stockpiles,  roads, and plant yards.  These  operations
                                   7-17

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are not included because they are not amenable to control  using the emission
control techniques upon which the proposed standards are based.  They are,
however, significant sources of particulate matter emissions.  Methods for
controlling emissions from these operations are discussed in the document
entitled "Air Pollutant Control  Techniques for the Crushed and Broken
Stone Industry" available from the EPA Library (MD-35), Research Triangle
Park, North Carolina 27711, telephone number (919) 541-2777.
7.2  WATER POLLUTION IMPACT  .
       The almost exclusive utilization of dry collection techniques (particu-
late capture combined with a dry emission control device) for control generates
no water effluent discharge.  In cases where wet  dust suppression techniques
could be used, the water  adheres  to  the  material  processed  until  it  evaporates.
Wet suppression systems, therefore, would not result in a water discharged
Consequently, emission standards for the non-metallic minerals industry will
have no water pollution impact.
7.3  SOLID WASTE DISPOSAL IMPACT
       Disposition of quarry, plant and dust collector waste materials depends
somewhat upon State and local government and corporate policies.  When
fabric filter systems are used, about 1.4 megagrams (1.6 tons) of solid waste
                                                           *
are collected for every 250 megagrams (278 tons)  processed.   In many
cases  this material can be recycled back into the process, sold, or used
for a  variety of purposes.
       Where no market exists for the collected fines, they are typically
disposed of in the mine or in an isolated location in the quarry.  A 544 Mg/hr
(600 TPH)  crushing plant using dry collection for control would generate about
*Estimate based on the difference between controlled and uncontrolled
 emission factors.
                                    7-18

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27.6 megagrams (30 tons) of waste over an eight hour period,   ihis is  about
0.5 percent of the plant throughput.  Generally, the collected fines are
discharged to a single haul truck at the end of the day and transported
to the quarry for disposal.  This dumping and transporting can be a
source of fugitive dust if these operations are not protected from the
wind or controlled by wet suppression.  No subsequent air pollution
problems should develop provided the waste pile is protected from wind
erosion.
     Consequently, it is EPA's judgment that the application of dry
controls in the non-metallic minerals industry will not have a sig-
nificant solid waste disposal impact.  Where wet dust suppression can be
used, no solid waste disposal problem exists over  that resulting  from
normal operation.
7.4  ENERGY  IMPACT
     The implementation of standards  of  performance for the  non-metallic
minerals industry will  necessarily  result  in an  increase  in  energy
usage.  Generally,  the  energy  impact  of  alternative control  systems and
standards  is  assessed by  determining  the additional energy consumption
 (type and  amount) above that which  would be  necessitated  by  existing
State regulations.   For the non-metallic minerals  industry,  however,
because  of the non-uniformity  of current State regulations and  the
 degree  of  interpretation  necessary  for enforcement,  such  an  approach
would  likely substantially understate the  true impact on  the industry.
 An alternative approach is to  assess the energy impact against  an
                                 7-19

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 estimate  of the  current  status  (type  and  extent)  of  existing  control
 across  the  industry.   Because of  the  size of  this  industry, however, any
 such  estimates for  the non-metallic minerals  industry would be  subject
 to considerable  uncertainty.  Consequently, the energy impact analysis  _
 presented below, like  the economic impact analysis presented  in Chapter 8,
 is gauged against an assumed baseline existing control of "no control."
 In this way, the resultant energy impact  will have a liberal  bias which,
 if determined to be reasonable, will  assure that the true impact is not
 adverse.
       The  energy requirements both with  and without air pollution controls
 for six typical plant  sizes are shown in  Tables 7.7 and 7.8.  The model
 plants selected are identical to those used for the cost and dispersion
 analyses.  The energy  requirements reported are for plants with both
 crushing and grinding  operations (Table 7.7) and for plants having
 crushing operations only (Table 7.8).
       A 9 Mg/hr (10 TPH) plant with both crushing and grinding operations
 and with no controls would require motors with horsepower rating totaling
 about 214 Kw (287 hp)  to operate.   Complete fabric filter control  would
 require an additional  30 Kw (40 hp),  or an increase in plant power
 consumption of about 14 percent.   For the 23 to 544 Mg/hr (25  to 600
TPH) plants, the application of a dry collection system would  increase
 power consumption by about  5  to  10 percent.
                                   7-20

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             Table 7.7  ENERGY REQUIREMENTS FOR MODEL NON-METALLIC
            MINERALS PLANTS HAVING CRUSHING AND GRINDING OPERATIONS
                           [KILOWATTS (HORSEPOWER)]
Plant Size
Fabric Filter
Percent Energy Increase
[Mg/hr (TPH)]
9 (10)
23 (25)
68 (75)
136 (150)
272 (300)
544 (600)
Uncontrolled
214 (287)
353 (473)
908 (1218)
1584 (2124)
3016 (4045)
5810 (7792)
Controlled
244 (327)
387 (519)
966 (1296)
1666 (2234)
3170 (4252)
6098 (8177)
(*)
13.9
9.7
6.4
5.2
5.1
4.9
Table 7.8 ENERGY REQUIREMENTS FOR MODEL NON-METALLIC
MINERALS PLANTS HAVING CRUSHING OPERATIONS ONLY
[KILOWATTS (HORSEPOWER)]
Plant Size
[Mg/hr (TPH)]
9 (10)
23 (25)
68 (75)
136 (150)
272 (300)
544 (600)
Uncontrolled
102 (137)
129 (173)
312 (418)
391 (524)
630 (845)
1038 (1392)
Fabric Filter
Controlled
123 (165)
153 (205)
356 (478)
450 (604)
737 (989)
1232 (1652)
Percent Energy Increase
(X)
20.4
18.5
14.4
15.4
17.0
18.7
                                     7-21

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     For the 9 to 544 Mg/hr (10 to 600 ton/hr) plants with only
crushing operations, the application of a dry collection system would
increase power consumption between 14 and 20 percent.  It is interesting  _
to note that a 544 Mg/hr (600 ton/hr) crushing plant using a combina-
tion of both wet and dry controls sufficient to meet most existing State regu-
lations would likely require an additional 75 kW (100 hp) or about a 7
percent increase in power consumption.  Complete fabric filter control
for this same plant would require a 7 percent increase in power
consumption when compared to a plant achieving the typical State
regulations.
       The  estimated additional  energy requirement to meet the added
demand for  non-metallic minerals  projected for the year 1985 would be
about 0.805 million megawatt-hours in the absence of any air pollution
controls.   In contrast, if fabric  filter controls were installed on all
capacity additions  (including  those obtained  from new plants and expansions
to  existing plants), the estimated additional energy demand would
increase to about 0.928 million  megawatt-hours.  Consequently, the net
increase in energy  consumption for the year  1985 which would result from
the installation of emission control would be about 0.123 million megawatt-
hours or 15 percent over that  which would otherwise be required to meet
the projected capacity additions  without  controls.  When compared to
forecasts for national demand  of electrical  energy alone  in 1985  (4.1
billion megawatt-hours), this  resultant  increase in energy consumption
                                    7-22

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is equivalent to approximately 3 x 10~3 percent of that projected to be consumed
nationally.6
     In addition, the energy impact on each of the 18 affected non-metallic
industries has been calculated in Table 7.9.  The impacts of energy usage of
controlled versus uncontrolled new facilities was calculated to be 0.123
million megawatts for the year 1985.  The resultant increase in particulate
emissions generated by power plants in the production of the additional
0.123 million megawatts of required power for the control equipment was
calculated to be 51 Mg/year (56 ton/year) in 1985 using the allowable
emission rate standard of 0.03 lb/106 Btu input.  It is concluded, therefore,
that this increase of particulate emissions from power plants would be more
than offset by the potential savings in particulate emissions generated by the
non-metallic industry under an NSPS (41,000 Mg/year or 45,000 ton/year
particulate).
7.5  NOISE IMPACT
      When compared to the noise emanating from crushing and grinding process
equipment, any additional noise from properly designed exhaust fans for the
control system will be insignificant.  Consequently, no significant noise
impact is anticipated due to the implementation of standards of performance
for non-metallic minerals plants.
                                     7-23

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 REFERENCES  FOR CHAPTER 7


 1.


 2.   Commodity Data Summaries Annual, 1977, U. S. Bureau of Mines.


 3'   r21X?rSl°2 " M£delMAna^S1'S °f the Air Qual1t^ ImPact of Paniculate
     Emissions From Non-Metallic Minerals Processing Plants," prepared
     by H. E. Cramer Company, Incorporated, for the U.  S.  Environmental
     Protection Agency, December 1976.

4.   "Draft Development Document for Effluent Limitations  Guidelines  and
     Standards of Performance - Mineral  Mining and Processing Industry -
     ?±!!lL#;ne!2l^ornth* Construction Industry),  prepared by  Versar,
     "Source Testing Report -  Essex  Bituminous  Concrete  Corporation,
     Dracut, Massachusetts," prepared  by  Roy  F.  Weston,  Incorporated,  EPA
     Report No.  75 STN-2,  December 27,  1974.

     Dupree, Walter G.,  and West, James A., "United  States Enerqv
     through the Year 2000," U.  S. Department of the Interior,
     December,  1972,  p.  19.
                                  7-25

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                              8.  ECONOMIC IMPACT
 8.0  SUMMARY
      The effect of NSPS control costs on the 18 non-metallic minerals industries
 was evaluated by first screening each industry for potentially significant
 impacts.  A potentially significantly impacted industry was considered to be
 any industry which had a plant whose per unit production cost could be increased
 by 2% or more because of NSPS control costs.   This screening analysis consisted
 of measuring the effect of annualized control  cost for the smallest size model
 plant in each industry (therefore  the highest  per unit control  cost and  worst
 case situation)  on the average  selling price of the mineral.   On  the basis  of
 this screening six minerals  were selected for  further  evaluation:
      •    Pumice
      •    Sand and gravel
      •    Crushed  stone
      •    Common clay
      •    Gypsum
      •     Perlite
     These six minerals were evaluated by developing a discounted cash flow
 (DCF) analysis for each model new plant size in each industry and also for
expansion plant  sizes in the common clay and gypsum industries.  DCF is an
investment decision analysis which shows the economic feasibility of a
planned capital  investment project over the life of the project.
     The DCF analysis was conducted by using primarily "worst case" assump-
tions.  Assumptions used include:
                                     8-1

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     •    the total  of NSPS control  costs were incremental
          costs; i.e., that there are no SIP control  costs
          that a plant would have to incur in the absence
          of NSPS control.                                                  ~~
     •    the production volume is constant through the life
          of the project except for the crushed stone
          plant where it is assumed that they operate at
          50% of capacity for the first year.
     •    NSPS control cost pass through is limited by
          competition of existing plants in the same'
          industry which do not have to meet the NSPS
          standard.
     •    the new plant operates as a separate business
          entity and cannot expect to finance the control
          from another business activity or parent firm.
     For new plants Table 8.40 shows that the 9 and 23 Mg/hr (10 and 25 tph)
plants in sand and gravel, and crushed stone, and the 9 Mg/hr (10 tph) plants
in common clay and pumice are likely to be significantly impacted by the NSPS.
The DCF model was not able to determine a clear positive or negative invest-
ment decision for the 9 Mg/hr (10 tph) gypsum, 23 Mg/hr (25 tph) clay and
68 Mg/hr (75 tph) pumice, sand and gravel and crushed stone plant sizes.
However, in view of the conservative assumptions used, they were judged to
be economically feasible.  All of the other plant sizes in  the six industries
are likely to be economically feasible after the promulgation of NSPS.
     Table 8.41 shows that the DCF analysis produced an economically feasible
result for all expansion siz.e plants except for the 4.5 Mg/hr (5 tph) common
                                      8-2

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  clay  plant where  the  investment decision result was unclear.  However, in
  view  of the conservative assumptions used, it was judged to be economically
  feasible.
       For the 12 industries for which a DCF was not performed new plant
  construction would be feasible for all plant sizes because the greatest
  potential NSPS control cost absorption is equal  to or less than 2% of the
  product price.   Furthermore, for the other minerals where the potential control
 cost absorption was greater than 2% the DCF analysis produced an  economically
 feasible result.*
      New regulations  shall  be considered  a  major  action  if "additional  annual-
 ized cost of  compliance,  including  capital  charges  (interest and  depreciation),
 will total  $100 million  (i)  within  any  one  of the  first  5 years of  implementa-
 tion,  or  (ii) if applicable,  within any calendar year  up to  the date  by which
 the  law requires attainment  of  the  relevant pollution  standard,"  or "the  total
 additional cost of production of any major  industry  product  or service  will
 exceed 5% of the selling price of the product."  Total industry annualized
 control costs in the fifth year after promulgation of NSPS and control  costs
 as a percent of selling price are lower than the guidelines set for these
measures of $100 million and 5%, respectively.  Consequently, the proposed
 standards for the non-metallic minerals processing industry would  be
considered a routine action and not a major one.
*
 The portable crushing plant segments of the crushed stone, and sand and
 gravel  industries are discussed in Supplement A.
                                      8-3

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8.1  UNITED STATES NON-METALLIC MINERALS INDUSTRY STRUCTURE
8.1.0.1  Introduction
     The non-metallic minerals are numerous and range from such bulk     _
commodities as sand and gravel and stone, the annual domestic demand
for which is quoted in billions of short tons, down to industrial diamonds
and gem stones, which are measured in carats.  The last three decades of
this century will be a period of rapid growth for the non-metallic mineral
industries.  The requirements for new buildings, road construction, rehabili-
tation of blighted cities, food production, chemical manufacture, ceramics,
metal working, and the host of other established uses of non-metals can be
expected to increase in volume.  Of equal long-term significance are the
opportunities to supplement and replace metals as they become scarce and
expensive.  Development of performance specifications will expand the use
of composites of metals,  non-metals, and non-mineral materials  in new and
improved end products.  Research leading to significant improvements in the
properties of the abundantly  available non-metals also will  enhance their
utility.
     The domestic non-metallic mineral industries, with a  few exceptions,
should  be  able to provide adequate  supplies from domestic  sources at reasonable
costs  to the year 2000.   For  the exceptions,  supplies can  be obtained from
foreign sources  or  alternatives  such as  substitutes.  However,  the maintenance
of a high  degree of domestic  self-sufficiency will  require solution of many
technical  and  economic problems.   For  some  commodities, such as kyanite,
synthesis  from domestic raw materials  offers  a  feasible solution to supply
problems.   Increased recovery of by-products, improvement  of technology
                                 8-4

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 enabling use of  lower grade reserves, and improvements  in production and
 transportation facilities and costs are other means of  enhancing the domestic
 supply position.
      Serving, as non-metal!ics do, extremely heterogeneous markets, there
 is less tendency toward vertical and horizontal integration than in some of
 the metallic and fuel categories.  However,  there are advantages .of scale and
 organization to be gained in some of the larger industries so there has been
 some consolidation among producers serving the construction and fertilizer
 fields.   Continuation of this  trend may be expected where efficiency benefits
 can be achieved.
--Warren  E.  Morrison and Robert  E.  Johnson,  Jr.,  from Mineral  Facts and
   Problems:   1970 Edition.                             	—	

      The  industry structures which  follow  for  the  18 non-metallic minerals
 being considered  here have  been  prepared to  provide background information  to
 assist in the development of atmospheric emission  limits under Federal  New
 Source Performance Standards (NSPS)  for  industry processes.
      In order to. maintain as high a degree of  consistency as possible for
                                                                      &
 non-metallic minerals considered here across the years 1972-1976, statistical
and analytical data  presented is derived or cited from U.S. Bureau  of Mines
documents in most every  instance and supplemented with significant  data from
other sources when necessary.
     Each of the  individual  industry structures is based  on the general
outline that follows:
                                     8-5

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    INDUSTRY STRUCTURE

    1.  General

        Mineral(s) description coverage of the analysis

    2.  Plants-define

        t  number and employment
        •  size
        •  geographic distribution

     3.  Companies

        •  number
        •  concentration

     4.  Industry  Statistics

           Production
           Consumption
           Prices
            Imports
            Exports
            Stocks
            Employees

All items  of information noted in the outline are not available for some

individual industries.

     The 18 non-metallic minerals being considered here have been grouped

into -three classifications by end-use.  In order of group production volume,

they are as follows:

     8.1.1 - Non-Metallic Minerals for Construction and Industrial Uses

             8.1.1.1  Sand and Gravel
             8.1.1.2  Crushed Stone
             8.1.1-3  Gypsum
             8.1.1.4  Diatomite
             8.1.1.5  Perlite
             8.1.1.6  Pumice
             8.1.1.7  Vermiculite
             8.1.1.8  Mica
             8.1.1.9  Gilsonite
                                        8-6

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      8.1.2 - Non-Metallic Minerals for the Chemical and Fertilizer Industries
              8J.2.1  Barite
              8.1.2.2  Fluorspar
              8.1.2.3  Salt
              8.1.2.4  Boron
              8.1.2.5  Sodium Compounds
      8.1.3 - Non-Metallic Minerals for Clay. Ceramic and Refractory Industries
              8.1.3.1   Clays
              8.1.3.2   Feldspar
              8.1.3.3   Kyanite
              8.1.3.4   Talc
      Each section includes a summary table illustrating  salient industry
 statistics estimates  for 1976 obtained  from the  U.S.  Bureau  of Mines  Commodity
 Data  Summaries  Annual  for 1977.   In  some  cases 1975  and  1976 data  is  not yet
 available and more complete data  from former years has been  used.

 8.1.1  NON-METALLIC MINERALS  FOR  CONSTRUCTION AND INDUSTRIAL USES
 8.1.1.1   Sand and  gravel
     Sand  and gravel has  been, and will continue to be,  the  principal con-
 struction  material in  the  United  States.   It exceeds  the use of  crushed  stone
 in construction by about  222 million  Mg or  245 million short tons  (1974).
 Sand and  gravel has the  lowest average unit value of  all mineral commodities,
 and it is  one of the fastest growing  mineral producing industries  in  the
 United States.
8.1.1.1.2  U.S. Plants
     In 1976, there were an estimated 7,000 sand and  gravel  operations.
The individual sand and gravel operations range in size  from those producing
over 3.6 million Mg (4 million tons)  annually to those reporting production
                                      8-7

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 less  than 4335 Mg (5,000 tons).   In 1974,  23 percent of total  production  was
 from  89  operations producing .9  million Mg (1  million tons)  or more,  but  58
 percent  was~ produced by 6,604 operations in the range from 45,350 to  453,500  Mg
 (50,000  to 500,000 tons) per year.
      The sand  and gravel industry is  highly mechanized and employs an esti-
 mated 50,000 men.   About 90  percent are production workers and the balance
 are clerical,  maintenance, and other  staff personnel.
      Output of sand and gravel has  grown at a  faster rate  than employment
 for the  past two  decades, reflecting  an increase  in  productivity.   Average
 output has almost doubled from 4.08 Mg  (4.5 tons) per man-hour in  1949 to
 nearly 8.2 Mg  (9  tons)  per man-hour in  1973.   This increase  in productivity
 has to date been  adequate to  compensate for the increasing hourly  cost of
 labor and  higher  costs  for equipment, land  acquisition, rehabilitation and
 other factors  related to production.
      Because of its  low unit  value  it is necessary to  produce  sand and gravel
 near  the point of  use;  therefore, geographically the sand  and  gravel  industry
 is concentrated in  the  large, rapidly expanding urban  areas and, on a transi-
 tory  basis, in areas where highways, dams,  and other large-scale public and
 private works  are  under  construction.  The  largest operations  tend to be
 concentrated in States with the largest total production, yet  production of
 sand  and gravel is so widespread many firms and plants are involved.
      In 1974,  of 89 sand and gravel operations with an annual production of
 .9 million Mg  (one million tons)  or more, 18 were located in  California.
8.1.1.1.3  U.S. Companies
     Sand and gravel operations were owned by 4,700 companies in 1976.
Producers may be large or small,  public  or private,  turning out one product
                                     8-8

-------
  or  a range  of products,  sell bank-run material or  subject  their material

  to  processing.   The average company produces 220 Mg/hr (250  TPH).

  8.1.1.1.4   U.S.  Production. Consumption and Prices

        Production  of common varieties of sand and gravel  is  tied  very closely

  to activity in the consuming industries, principally  construction of all

  general  types.   Production  of special  qualities of sand is associated

  chiefly  with the  needs of the glass  industry  and  foundries.  Sand  and

  gravel production,  consumption  and other industry statistics are  presented
  in Table 8-1.
Table 8-1 5flNO m GRAVEL: ML1ENT STATISTICS
                  Salient Statistics—United States

                  Production

                  Imports


                  Exports


                  Apparent consumption

                  Price VMg (dollars per ton)

                  Stocks, year end

                  Employment: Mine e/
                    1973     1974
 1972

 829,292  892,152    820,514
(914,324). (983,629)  (904,646)
  690     725      357
 (761)    (800)    (394)

  1,651    1,581     2.046
 (1,821)   (1,744)   (21256)
 828,330  891,295    818,825
(913,264)  (982.685)  (902,784)
  1.52     1.52     1 73
 (1.38)   (1.38)    (1.57)

      Not available
 43,000 '  49,000    39,000
                                   1975

                                  716,015
                                  (789,432)
                                    339
                                   (374)

                                    2,919
                                   (3,219)
                                  713,434
                                  (786,587)
                                    1.97
                                   (1.79)


                                   36,000
 1976e/

 698,390
(770,000)
  226
 (250)


  3,265
 (3,600)
 695,331
(766,650)

  2.18
 (1.98)
                                                                     34.000
                 Source:  Conrodity Data SuMaries Annual, 1977, U.S. Bureau of Mines)
      The highway and general building construction  industries  are the  greatest

 consumers of sand and gravel.  As  such, construction  activity  virtually  deter-

 mines the demand  and supply of sand  and gravel  for any  given period.   During

 1976, approximately 97 percent of  the total U.S.  sand and gravel  output  was

 used in  the construction industries.

      Construction will  continue to dominate the end-use  picture for sand and

 gravel.    Industrial  sand and  gravel,  although important,  will constitute only

 a  small  percentage  of the total  volume  of domestic sand  and gravel  requirements.

      Labor,  energy  (electricity,  fuel oil, and gasoline),  and water are the

major requirements  for  the production of  marketable sand  and gravel  products.

Actual  operating costs  for production are variable.   Production costs  vary  wideb
                                    8-9

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depending upon geographic  location and composition of deposits.  The portable
plant segment of the sand  and gravel  industry  is discussed  in Supplement A.
8.1.1.2  Crushed Stone
8.1.1.2.1  General
    Crushed stone is a term used to describe a rock which has been reduced
in size after mining to meet various consumer requirements.  The rock
may meet any one of many minerological definitions, including limestone,
granite, trap rock, and others.  The stone  industry is the largest non-
fuel, non-metallic mineral industry in the  United States from the stand-
point of total value of production and is second only to sand and gravel
in volume produced.
8.1.1.2.2  U.S. Plants
    There are currently 5,400 crushed stone quarries in the United States
as reported by the Bureau of Mines.  Of these, approximately 2,300 are
considered by the Bureau of the Census (SIC's 1422, 1423, and 1429)
to be commercial operations primarily concerned with the production of
crushed stone.  The remaining 3,100 consist of quarries operated by
federal, state, and local governments, quarries that are part of integrated
(cement, lime, etc.) operations, quarries operated on a temporary basis by
establishments not concerned primarily with the production of stone (e.g.,
highway contractors, SIC 1611), and small quarries operated without paid
employees but proprietor-operated.  Some of these latter categories enter
and re-enter the market.  The 5,400 quarries are served by approximately
4,000 plants.
    Included in the Bureau of Mines data, but not in the Census  data,  are
portable crushing plants.  These plants,  which number  1,700,  constitute a
good portion of those plants  referred to  above which are attached to  either
                                    8-10

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 the federal government or highway contractors, and which may enter or re-enter
 the market on an irregular basis.  They also service small quarries in rural
 areas for a short period each year, sufficient to crush and stockpile a
 community's immediate neqds.  The portable plant segment of the crushed
 stone industry is discussed in Supplement A.
 8.1.1.2.3  U.S.  Companies
      The crushed stone industry is comprised  of a large number of small,  -
 locally owned firms  which account for a minor proportion of national  pro-
 duction, and  a small number of larger firms which are regionally or nationally
 diversified,  and account  for a large  percentage of the national  production.
      Patterns  of firm ownership are similar to those  in other  sectors  of
 the  construction-oriented basic materials  industries.   At  one  extreme
 there  are the  small  local operations,  often operated  as proprietorships,
 where  the plant  manager and  the owner  are  one and the  same person.  At the
 other  extreme  are the  plants owned by  major firms for  whom the  crushed
 stone  business is but  one part  of  a number of fields of enterprise.
 Plant  managers for these  firms  rarely  have an equity  interest  in  the firm
 for which they work, being regular employees  whose tenure  at a particular
 quarry may be temporary in nature.
     In  1976 crushed stone was  produced by 2,000  companies  at 5,400
 quarries  in 49 states  for dense  graded roadbase stone,  concrete aggregate,
 roadstone, cement, bituminous aggregate, and  other uses.   Leading states
were Illinois, Pennsylvania, Texas, Missouri,  and Ohio, which accounted
for 30% of the total  production.  Output decreased 1% to 806 million Mg (888
million tons)  valued  at $2.02 billion.  Of the total, 74% was limestone,
10% was granite,  and  9% was traprock.
                                    8-11

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8.1.1.2.4   U.S. Production.  Consumption, Prices
      Salient  industry statistics are  presented  in Table  8-2,
                     ~3blea —•? J.S. CRUSHED ST01E INDUSTRY iin thousand
                       !8-2
                           Mg and thousand short tons in parentheses 1
                Production

                Inoorts for consunption

                Exports
                Apparent consur»)tion

                Average price:
                 Crjshed stone
                Stocks, year-end
 335    962   946
i920)  (1.060)  C1.043!
  4
 14)
4
14)
       3
       (3)
4
(4)
 836    962    946
 1922!  (1,061)  (1,043)
          313
          ?9C3>
          319
          (903)
307
(890)
  4
 >4)
  3
          =07
          (390)
$1.83   SI.37   S2.19  S2.S7   S2.61
(51.72;  (si.icj  ;s2.:o)  ;s:.35)  (S2.39)-
      Not  Available
64,000  64,000   64,000  55.000  54,000
 End Uses
                E,Tployff*nt; Quarry
                 I mill e/
                 Source:" Conned ity Data Sururles Annual, 1977, --S. S.resj of
      The  end uses  for crushed stone ,are many and varied but  construction
 and construction-related  applications account for at  least 80%  of total
 shipments.   Crushed stone is either  used directly in  its natural  state or
 is shipped  for further processing  into miscellaneous  manufactured products.
      In  its natural state,  stone  is  an important ingredient  for highway
 and street  construction where it  can  form  the base of the road, be included
 in the concrete  or bituminous pavement as  an aggregate or be used as  an
 anti-skid material for surface treatment.   As an aggregate in other types
 of concrete, stone is sold  to ready-mix and precast  concrete manufacturers
 as a basic ingredient for structural  concrete.
 Future Growth
      The long-term historic rate  of  growth (1963-1972) for crushed stone
 has been at an annual rate  of 3.3%.   This  rate of growth will probably
 modify  somewhat  over the  remainder of the  decade, partly because the  rate
                                        8-12

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of construction expenditures will reduce from 2.1% over the same period
to no more than 2.0% from 1972 to 1980, but also because the industry
has reached a stage of mature stability with respect to product substi-
tutions.  The rate of construction growth will be slower due to a combi-
nation of inflationary, energy and recessionary factors impacting business
and individuals, as well as the fact that base year 1972 was a strong one
for construction activity.  We thus anticipate that crushed stone consump-
tion will grow at about 3% per year compounded to 1980 from 1974 on a tonnage
basis.  Limestone and granite will both increase their current proportion of
total crushed stone consumption and grow at slightly faster rates than the
average.  Little or no growth is anticipated in the consumption of traprock
or sandstone, while miscellaneous stone types will continue to decrease in
total tonnage.
Possibilities of Substitution
     Limited substitution of alternative products can and does occur depending
on the geographic location of an operation.  Sand and gravel, blast furnace  .
slag, and lightweight aggregates can be used interchangeably with crushed
stone and many specifications accept or even encourage substitutions.  An
important criterion considered in making such a decision are the relative
distances of available materials sources from the user.  Thus, sand and
gravel pits may prove to be favored as concrete aggregates if the geology
and extraction location shows them to be more economic than stone quarries.
Blast furnace slag, readily available where steel mills are located, can
often be an economic source of aggregate and can also offer distinct
performance advantages when used as an antiskid highway surfacing material.
Lightweight aggregates, such as expanded shale or clay, perlite, or vermicu-
lite can result in considerable reductions in concrete density, and thus
                                 8-13

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 building load,  when substituted for crushed stone,  but the economic
 availability of these aggregates is limited.
 Marketing and Distribution
      Distribution  of crushed  stone is  direct from the quarry to the end
 user with no intermediary involved.  Inventories  are held  almost entirely
 at  the  quarry location,  as  double handling  would  be prohibitively expensive,
 and customers maintain only sufficient inventory  to insure uniform produc-
 tion rates over a  predetermined length of time.   Crushed stone  production
 and shipments is a very  seasonal  business in many northern regions.
 Producers there will  typically  operate their plants  for nine  months  a year
 and stockpile sufficient  stone  to cover a greatly reduced  rate  of shipments
 in  the  winter months.
 Price Elasticity and  Pricing  Dynamics
     On  an  industry basis,  the  demand  for crushed stone is  price  inelastic.
 As  the  product  is  a necessary component of  a number  of building materials
 (concrete,  asphalt) and products  (roads, airport  runways,  etc.),  its demand
 is  based  primarily on the demands  for  these  products  irrespective of its
 price.  The fact that there generally  does not exist  significant  competition
 from substitute products, and the  price of stone  as  a percentage of the
 total price of the materials  and products of which it is a component is
 low  (15% of the FOB price of  asphalt—less than 1% of the price of a high-
way for which the asphalt is being supplied, for example),  variations in
the price of crushed stone will  not affect basic demand.
     On a plant-by-plant  basis,  however, price competition  is severe.  The
crushed stone business is highly capital-intensive,  and producers need  to
                                   8-14

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  maintain production volume to provide for the amortization of their
  capital investments.  Thus, while the industry may be tending to an oligopoly
  in the local areas where business is transacted, the oligopoly is extremely
  competitive in a business sense with regards to price.
  8.1.1.3  Gypsum
  8.1.1.3.1  General
      Anhydrite  and  selenite usually  occur  together,  but calcined  gypsum  is a
 manufactured product never found  in  nature.   Calcined  gypsum  is produced by
 heating  selenite  at about  350°F for  over an  hour.  When water is  added to
 calcined  gypsum,  plaster of pan's  is  formed,  which quickly  sets and  hardens
 to  selenite  again.   All of these  products, including the articles molded from
 the plaster,  are  called gypsum.
 8.1.1.3.2 U.S.  Plants
      In 1973, there  were 76  plants calcining  gypsum in  the  U.S. with individual
yearly production falling  between 9,070 - 453,500 Mg (10,000  - 500,000 tons) per
year.
      In the  United  States,  production of crude  gypsum  is centered around
 three general areas, the Great Lakes  area, Texas-Oklahoma,  and California.
 Leading States were Michigan, California, Texas,  Iowa,  and  Oklahoma.  These
 five  States  accounted for  60 percent  of the  total output.
                                     8-15

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  8.1.1.3-3  U.S.  Companies


        The domestic gypsum industry is  a  large, well-integrated  industry,  in_


  which a few large companies  are prominent.  These  companies mine and sell


  crude gypsum  for use in cement or agriculture.  They mine and  import crude


  gypsum, calcine  it, and market gypsum products.  Leading mining companies  were


  U.S.  Gypsum Co.  (13 mines),  National  Gypsum Company (8 mines),  Georgia-Pacific


  Corporation (7 mines), the Flintkote  Company (3 mines), and H.  M. Holloway, Inc.


  (1  mine).  These five companies accounted for 73 percent of the total output


  of  crude gypsum.  Thirty-four smaller companies operated 37 mines.


  8.1.1.3.4  U.S.  Production,  Consumption, Prices


        Salient  industry statistics are  presented in  Table 8-3.




               Table 8-3 'J.S. GYPSUM INDUSTRY  (thousand Mg and thousand short tons 1n parentheses)




Production:  Crude


           Calcined

Imports:  Crude, including anhydrite


Exports:  Crude, crushed  or calcined


Consumption: Crude, apparent


Value-  Average crude (f.o.b.
      .•nine) S/Ng (per ton)

      Average calcine (f.o.b.
      plant) S/Mg (per  ton)

Stocks: Producer, crude, yearend e/


Enployntent: Mine and calcining plant
1972
11,181
(12,328)
10,888
(12,005)
ihydrite 7,000
(7,718)
:alcined 46
(51)
: 18,135
(19,995)
$4.33
($3.93)
b. $18.00
($16.32)
rend e/ 3,909
(4,310)
ng plant 4,200
1973
12,297
(13,b58)
11,420
(12,592)
6,948
(7,661)
57
(63)
19,188
(21,156)
$4.61
($4.18)
$17.98
($16.31)
3,628
(4,000)
4,500
1974
10,883
(11,999)
9,970
(10,993)
6,733
(7,424)
119
(132)
17,496
(19,291)
$4.86
($4.41)
$20.63
($18.71)
2,721
(3,000)
4,800
1975
8,844
(9,751)
8,327
(9,181)
4,941
(5,448)
68
(75)
13,717
(15,124)
$5.05
($4.58)
$22.40
($20.31)
1,814
(2,000)
5,000
1976 e/
10,430
(11,500)
9,432
(10,400)
6,049
(6,670)
68
(75)
16,384
(18,095)
$5.29
($4.80)
$23.47
($21.28)
1,360
(1,500)
5,100
      Connodity Data Summaries Annual, 1977, U.S. Bureau of Mines.
                                        8-16

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      End Uses - Crude gypsum  is marketed for use in cement, agriculture,
or fillers.  In portland cement, gypsum is universally used to retard
the setting of the concrete.   In agriculture, gypsum is used to neutralize
alkaline soils and to provide  sulfur.
      Calcined gypsum is marketed as plaster or prefabricated products.   r
Building plaster is generally  reground, and retarder and binders are added.
Retarder is usually a glue-type material made from meatpacking-plant
by-products.
      The U.S. is the leading world producer and consumer of gypsum with 18
percent of production and 28'percent of consumption.  The United States is a
net importer of gypsum.
      Gypsum is a low-cost, high tonnage commodity that must compete with many
other building materials.  Large mines and integrated plants have helped
producers remain competitive.
8.1.1.4  Diatomite
8.1.1.4.1  General
     Diatomite in its natural state is a soft rock!ike material consisting
mainly of an accumulation of siliceous frustules (shells) or skeletons of
diatoms that are microscopic single-celled plants of freshwater and saltwater
origin.  Chemically, diatomite is essentially amorphous hydrated or opaline
silica with varying amounts of contaminants such as silica sand, clay minerals,
metal salts, and organic matter.
8.1.1.4.2  U.S. Companies/Plants
     The United States is the world's largest producer and consumer of
diatomite.  In 1976, 9 companies actively mined and prepared diatomite from
16 operations in 5 states—California, Kansas, Nevada, Oregon, and Washington.
                                       8-17

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 The major firms have other mineral  and manufacturing interests such as the
 production of asbestos products,  roofing,  floor tile, acoustic insulation,
 refractories, lead and zinc, plastics, thermal  insulation, chemicals, and
 industrial fillers.                                                       ~"
      Employment in the diatomite  mining and  processing sectors of the industry
 is estimated to be about 900 employees.
 8.1.1.4.3  U.S. Production, Consumption, and Prices
      Salient industry statistics  for the diatomite industry are presented in
 Table 8-4:
                        79516 8"4' Jfd- ?"™!LE ™°US™ d" thousand
Mg and
Production: Mine
Imports, general
Exports

Apparent consumption
Price S/Mg (average per short
ton)
Stocks, yearend e/
Employment: Mine and plant e/
1972
522
(576)
(I/)*

134
(148)
390
(430)
$71.90
(65.19)
34
(38)
800
1973.
552
(609)
(I/)

161
(178)
392
(433)
$65.36
($59.26)
32
(36)
850
• r — •
1974
602
(664)
(4)
3
168
(186)
437
(482)
$84.16
($76.31)
32
(36)
• 875
N.I i *,i i^ijcj y
1975
519
(573)
(4)
3
133
(147)
390
(430)
$88.25
($80.01)
32
(36)
900
_1976 e/
563
(621)
(5)
4
140
(155)
427
(471)
$97.83
($88.70)
32
(36)
900
       Source:  Commodity Data Summaries Annual, 1977, U.S. Bureau of Mines.

     The United States  is  the  largest producer and exporter of diatomite.
Exports have risen very gradually from 116,096 Mg (128,000 short tons) in
1964 to 168,702 Mg (186,000 tons)  in  1974.
                                     8-18

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      The principal  diatomite-producing countries are also the major exporters
 of diatomite products.   Diatomite is used in nearly every country primarily
 for filtration purposes.
      Domestic use for diatomite as a filter medium comprised  53 percent  of
 the 433,546 Mg (478,000 tons)  consumed in 1974.
      The quantity of processed diatomite  used as a filler or  extender  in the
 preparation of various  industrial  chemicals and  paints  in the United States
 in 1974  was 99,770  Mg (110,000 tons),  23  percent of total  consumption.
      Transportation has always been  an important cost factor  in the price
 of diatomite to the ultimate consumer  because the product is  a high-bulk
 commodity,  and thus has a high freight rate per  ton.  The cost of moving
 diatomite  (bulk shipments) from western producing points  to midwestern and
 east  coast  markets,  for example,  has ranged  from $27 to $38/Mg ($25 to $35
 per ton).   However,  because of essential  industry applications for  diatomite,
 transportation  costs  have not  seriously affected  supply and demand  in the past.
 8.1.1.5  Perlite
 8.1.1.5.1   General
     Perlite, a glassy volcanic rock, has the unusual characteristic of
expanding to about 20 times its original volume when heated to an appropriate
temperature within its softening range.  The resultant expanded product finds
a variety of industrial and constructional applications owing to the material's
low density with attendant properties of low thermal conductivity and high
sound absorption.
                                      3-19

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8.1.1.5.2  U.S. Companies/Plants
     Domestic production of crude  perlite (quantity sold and  used) in 1976
was a  recofa 598,620 Mg (660,000 tons) from IVoperations  in  6 Western States.
Deposits in New Mexico supplied 88 percent of  the total crude perlite mined
in 1974.  Expanded  perlite was produced at 76  plants in 30 States.  The
principal States  in descending order of expanded perlite output in 1974 were
Illinois, Mississippi, Kentucky,  Pennsylvania, Colorado, Florida, New Jersey,

Texas, California,  and Indiana.
      Employment  in  perlite mining  and milling  was estimated to be 121 employees
in  1976.   In  addition, there were many  hundred more employees in  the expanding,
product development, basic research,  and  marketing activities of  the industry.
8.1.1.5.3   U.S.  Production.  Consumption,  and Prices
      Salient industry  statistics for  the  domestic perlite  industry are

presented  in Table  8-5.
               Table 8-S.  U.S. PERLITE  INDUSTRY (in thousand Mg and
                         thousand short tons in parentheses)
       Salient Statistics—United States:
       Production:  Mine

       Imports
       Exports
       Consumption, reported

       Price (sold to expanders): $/Mg
         (Per ton), f.o.b. mine
       Stocks, year-end
       Employment:  Mine and mill
 1972
1973
1974
1975    1976 e/
  588     688     613     640     598
 (649)    (759)    (676)   (706)   (660)
     None  of  Record
      Not  Available
  494     493     503     464     491
 (545)    (544)    (555)   (512)   (542)
 $12.50   $12.83   $14.21   $15.72  $17.35
($11.34) ($11.64) ($12.89) ($14.26) ($15.73)
      Not  Available
  100     100     no     no     121
       Source- Cconodity Data Summaries Annual, 1977, U.S. Bureau of Mines.
       Industrial  uses for perlite (expanded)  are many and varied.  The more

  important applications  include the following:   abrasives,  acoustical plaster
  and tile, charcoal barbecue  base, cleanser base, concrete  construction aggregates,
                                         8-20

-------
filter aid, fertilizer extender, foundry ladle covering and sand additive,
inert carrier, insulation board filler, loosefill insulation, molding filler
medium, packaging medium, paint texturizer, pipe insulator, plaster aggregate
and texturizer, propagating cuttings for plants, refractory products, soil
conditioner, tile mortar aggregate and lightweight insulating concrete for
roof-decks, and wall board core filler.
     Exfoliated vermiculite is the most directly competitive material with
perlite aggregates in plaster and other insulation applications in the construc-
tion field.  Lightweight aggregates such as pumice, expanded clay, shale, and
slag, volcanic cinders, or foamed concrete are used where"considerations of
lower cost or greater structural strength more than balance the advantage of
low density achieved by using perlite.
8.1.1.6  Pumice
8.1.1.6.1  General
     Although domestic use prior to World War II was largely as an abrasive,
the importance of pumiceous materials as low-cost construction aggregate
increased rapidly and has since dominated the U.S. pumice consumption pattern.
8.1.1.6.2  U.S. Plants
     Domestic production of pumiceous materials in 1976 was 4.03 million tons
from 235 operations in 12 States (including Hawaii) and American Samoa.  The
principal producing States are Arizona, California, and Oregon, and their
combined output accounted for 68 percent of the national total of pumiceous
materials in 1974.  Other States with significant output were Hawaii, Nevada,
and New Mexico.                                                 ~
                                    8-21

-------
     Although employment in the pumiceous  materials  industry  varies
considerably from year to year, owing primarily to closing and  opening
of volcanic cinder  pits when  local contracts for  road construction material
terminate and start up, it was estimated that about  600 workers were in
mining and processing in 1976.
8.1.1.6.3  U.S.  Companies
      In 1976 there  were 77  pumice producing companies.  Producers range  from
private individuals to companies to  governmental  agencies  at  local, State and
Federal levels.   There is also a wide  range from  small, intermittent,  to large
tonnage operations.  Most of the producers have mining and processing  of
pumiceous materials as their sole or major interest; however, some, such as
railroad companies and road construction contractors, produce the material only
as  a subsidiary part of their  principal business.
8.1.1.6.4  U.S. Production, Consumption and Price
      Industry statistics  for  the  domestic supplier industry is presented in
Table  8-6.
            Table 8-6. U.S. PUMICE INDUSTRY (in thousand Mg and
                      thousand short tons in parentheses)
      Production:  Mine
      Imports for consumption
      Exports
      Apparent consumption
      Price: $/Mg (per ton),
       f.o.b. mine or mill (avg.)
      Stocks, year-end
      Employment: Mine and mill
  1972
 3,458
(3,813)
  543
  (599)
  (I/)*
 4,002
(4,413)
 $1.88
($1.71)
     N
 525
   1973
  3,570
 (3.937)
    281
   (310)
     2
    (3)
  3,849
 (4,244)
  $2.49
 ($2.26)
o t   A v
  545
   1974
  3,570
 (3,937)
   265
   (293)
     2
    (3)
  3,833
 (4,227)
  $2.55
 ($2.32)
a i 1  a b
  560
   1975
  3,530
 (3,892)
   131
   (145)
   U/)
  3,660
 (4,036)
  $3.17
 ($2.88)
1  e
                                                        580
  1976 e/
 3,655
(4,030)
   73
   (81)
   U/)
 3,727
(4,110)
 $3.32
($3.01)
                                  600
     * less than 1000 Mg.
     Source:  Conmodity Data Summaries Annual, 1977, U.S. Bureau of Mines.
                                      8-22

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     The largest domestic use of pumiceous materials is in the construction
industry, which accounted for 92.5 percent or 3 million Mg (3.9 million tons)
of demand in 1974.  Construction uses principally include road surfacing,
maintenance, and ice control, concrete admixtures and aggregate, and railroad
ballast.  Demand for other uses totaled 263,030 Mg (290,000 tons) in 1974;
the quantity of pumice used only for various abrasive purposes was estimated
to be 22,675 Mg (25,000 tons).
     Transportation is an important cost factor in the economics of the domestic
pumice industry.  Abrasive grades ($34.00/Mg - $31.00/ton) can be shipped  even
from foreign sources and be competitive; but pumice of low market value ($1.13/Mg
$40/ton) such as that used for construction purposes, is usually limited to a
few hundred miles by rail or truck transportation.  Pumice for construction uses
becomes less competitive with alternate choice materials in rough proportion to
the distance that pumice resources are available from the place of consumption.
8.1.1.7  Vermiculite
8.1.1.7.1  General
     Vermiculite, a mica-like mineral with the unique property of exfoliating
to a low-density, bulky material when heated, is widely used in the construction
industry.  Vermiculite concrete is used for roof decks and floor fill where
lightweight, thermal insulation, and acoustical properties are of particular
importance.
8.1.1.7.2  U.S. Companies/Plants
 	  In 1975, the only domestic producers of crude Vermiculite were the
Construction Products Division, W. R. Grace & Company, which operates a large
mine near Libby, Montana, and a group of smaller mines near Enoree, South
Carolina, and Patterson Vermiculite Company, Enoree, South Carolina.
                                     8-23

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     Exfoliated vermiculite  was produced at  53 plants in 31 States in 1974.
Five States,supplied 46  percent of the total:   California,  Florida, New
Jersey,  South Carolina,  and  Texas.  W. R.  Grace & Company,  the leading   —
producer of crude vermiculite, operated 28 exfoliating plants.   Patterson
Vermiculite Company used all its production  of crude vermiculite at its
Enoree,  South Carolina exfoliating plant.  Twenty-two other firms operated
25 exfoliating plants.   W.  R. Grace & Company had a financial  interest in
several  of these firms,  but most of them were independent  processors.  Total
                                           i
production of crude and  exfoliated vermiculite in 1974 was 309,287 and
249,425 Mg (341,000 and  275,000 short tons), respectively.
     Most exfoliating  plants are small,  and  over half produce less than
4535 Mg (5,000 tons) each of expanded vermiculite annually.  About 250 workers
were employed at vermiculite mines and mills in 1973.  Several hundred
additional employees operated vermiculite  exfoliating plants.
8.1.1.7.3  U.S. Production, Consumption,  and Prices
      Industry statistics for vermiculite are presented in  the following  table.
                Table o_7  U.S. VERMICULITE INDUSTRY (in thousand Mg and
                        " thousand short tons in parentheses)
        Salient Statistics—United States:
                                       1972
        1973
                                                      1974
                        1975
                                                                      1976
Production: Mine
Imports: Crude
Exports :
Consumption: Exfoliated
305
(337)
23
(26)
NA
224
(247)
331
(365)
27
(30)
NA
265
(293)
309
(341)
38
(42)
NA
249
(275)
299
(330)
29
(33)
38
(42)
213
(235)
272
(300)
27
(30)
40
(45)
204
(225)
        Prices: Average S/Mg (per ton),
         f.o.b. mine
        Producer stocks, year end
        Employment: Mine and mill
 $26.48   $28.60   $32.73   $46.06    $46.32
($24.01)  (S25.93) ($29.68)  ($41.76)  ($42.00)
        Not   Available
 •225 "   250      250      250     250
        Source:  Conroodity Data Sundries Annual, 1977, U.S. Bureau of Mines'.
                                        8-24

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     Railroad freight rates are high, and shipping costs for crude vermiculite
sometimes exceed the mine value.  The rail-freight rate for shipping vermiculite
from Montana to the Atlantic and Gulf coasts is comparable with the transportation
cost from South Africa.  This makes it economic for some South African crude
to enter the country.  Some of this vermiculite is transshipped by rail or
barge to inland points.
8.1.1.8  Mica
8.1.1.8.1  General
     Mica is a group name, for a number of complex, hydrous potassium silicate
minerals with differing chemical composition and physical properties.  Crystals
of mica have characteristic excellent basal  cleavage and split easily into
tough, flexible sheets.  Principal minerals of this group are muscovite
(potassium mica), phlogopite (magnesium mica), biotite (magnesium iron mica)
and lepidolite (lithium mica).  Muscovite and phlogopite are the most important
commercial micas.
8.1.1.8.2  U.S. Companies/Plants
     In 1974, block and film mica was produced by 13 companies in 7 States.
New Jersey with four consuming plants, New York with three, North Carolina
with two, and Pennsylvania with one produced 75 percent of the domestically
fabricated block and film.  Other States with block and film fabricators are
Massachusetts, Ohio, and Virginia.
     Splittings were fabricated into various built-up mica products by 11 com-
p_anies with 12 plants in eight States.  Plants in New Hampshire, New York,
and Ohio consumed 80 percent of the splittings.  Other States with plants
consuming mica splittings were Michigan, Massachusetts, North Carolina and
Virginia.

                                   8-25

-------
      North  Carolina was  the largest scrap and  flake  producing State with  56

percent of  ±otal  production in  1974.   The remaining  output of scrap and  flake

mica  came from Alabama,  Arizona, Connecticut,  Georgia, New Mexico, South

Carolina, and South Dakota.

      Ground mica  was produced  by 16 companies  with  18 plants in  the following

10  States:   Alabama, Arizona,  Georgia, Illinois, New Hampshire,  New Mexico,

North Carolina,  Pennsylvania,  South Carolina,  and Texas.

 8.1.1.8.3   U.S.  Production, Consumption and  Prices

      Salient statistics  for the U.S.  mica industry  are presented in the

following table.
             Table 8-8   u-s- HICA INDUSTRY 
-------
      In  1974,  ground  mica  for  use  in  gypsum wall board  cement required
 37,187 Mg  (41,000  short  tons),  followed  by paint with  30,838 Mg  (34,000
 short tons), roofing  materials  with 9,070 Mg  (10,000 short tons), and the
 rubber industry with  6,349 Mg  (7,000  short tons).
      Many  substitutes are  available for  ground mica when it is used as a
 filler.  Ground synthetic  fluorophlogopite has been successfully used to
 replace  natural ground mica for uses  that require the  thermal properties of
 the mica.
 8.1.1.9  Gilsonite
8.1.1.9-1  General
      According to Mr. E. G. Williams, an Asphalt Institute Engineer stationed
 in Louisville, Kentucky, at present there is no  production of natural rock
asphalt  in the United States.   Production ceased about 1965 due to the
exorbitant cost of the natural   product compared to asphalt produced by
petroleum cracking processes.   There are no known plane to resume production
of natural  rock asphalt.
     The American  Gilsonite Company in Utah is the only domestic producer
of metamorphosized asphalt called gilsonite.   Production is less than 90,700
Mg (100,000 tons)  per year used primarily for specialty products.  Less than
9,070 Mg (10,000 tons) per year is consumed east of the Mississippi  River.
                         E.G. Williams
                         Asphalt Institute Engineer
                         4050 Westport Road
                         Louisville, Kentucky  40207
                         (502)  895-6966
                                     8-27

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8.1.2  NON-METALLIC MINERALS FOR THE CHEMICAL AND FERTILIZER INDUSTRIES
8.1.2.1  Barite
8.1.2.1.1  General
     Barite (BaSOj is the only source of barium and barium compounds.  The *erm
"primary barite," as used in this report, refers to the first marketable product
and includes crude barite, flotation concentrate, and other beneficiated material
such as washer, jig, or magnetic separation concentrate.  Most primary barite
requires fine grinding before it is used for drilling muds.  This grinding may
or may not be done at the mine site.
8.1.2.1.2  U.S. Plants/Companies
     Domestic production of  barium  in  1976 was  from 31 mines in 9 States.
Nevada supplied 69 percent of the tonnage.  Missouri produced 16 percent.
Alaska, Arkansas, California, Georgia,  Idaho,  Illinois, and Tennessee were
other producing States.
                                  «•
     Companies which  specialize  in  the  drilling mud business also have foreign
mines and  import  part of their barite  supplies.  They have grinding plants
strategically located throughout  the world to  serve drilling mud markets.
They provide  a  variety  of  drilling  mud minerals,  chemicals,  and services
to  the oil  and  gas  industry.
     Ground and crushed  barite was  produced in  1974 mainly in Louisiana and
Texas from domestic  and  imported  material and  in Arkansas, Missouri, and
Nevada from domestic barite.   Processing mills  were also  located in
California, Georgia,  Illinois, Tennessee, and  Utah.
     Domestic mining, milling, and  grinding of barite to  a marketable product
required  about  1200  employees  in  1976.  Most barite plants process from
9-45 Mg  (10-50  tons)  per hour.
                                     8-28

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 8.1.2.1.3   U.S.  Production,  Consumption and  Prices

       Salient statistics for  the  U.S. barite  industry are  presented  in the

 following  table.
                          Table 8~9 U.S. BARITE INDUSTRY (1n thousand Hg and
                                 thousand short tons in parentheses)
                                           197?    1973   1974   1975
                     Production: Mine J/
                     Imports for consumption
                     (crude barite)


                     Exports {ground and crushed)


                     Reported consumption
                      (ground and crushed)
                     Price: $/Mg (per ton)
                          f.o.b. mine (avg.)

                     Producer -stocks, yearend
                     Employment: Mine and mill e/  1,025

                     Source:  Commodity Data Summaries Annual,
  821
 (906)

  565
 (624)


  47
  (52)
 1,339
(1,477)

 SIS.12
($16.43)
 1,101   1,103   1,167
(1,104)  (1,106) (1,287)
 649
 (716)


  61
 (68)
661
(729)


 55
(61)
 575
(634)


 51
 (57)
 1,443  1,507   1,638
(1.592)  (1,662)  (1,807)

 $16.67  $16.77  $17.71
($15.12) ($15.21) ($16.06)
 1976 e/

 1,024
(1,129)

 680
 (750)


  42
 (47)
           1,659
           (1,830)

           $23.21
           ($21.05)
      bt  Available

       1,100   1,200  1.200  1,200


      1977, U.S. Bureau of Mines.
      The United States  is a net barite importer.   Imports of barium in  1974

 amounted to  40% of the  total  supply.   Barium imports  have remained  near this

 percentage for the twenty-year  trend.

      The major use for  barium is in  the form of  barite as a  weighting material

 in wefl-drilling muds,  accounting for  87 percent  of the 1974 U.S. consumption.

      Barite  is also a raw material of  chemical manufacturing.   The  major

 barium  chemicals are the  carbonate,  chloride, oxide,  hydroxide, nitrate,

 peroxide,  and  sulfate.  The barium compounds represent 6 percent of total

 barium  consumption.

      A  number  of materials  have  been substituted  for  barite  as  a weighting

medium  in  drilling  muds in  the  past but never with  a  real  competitive edge.
                                           8-29

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8.1.2.2  Fluorspar (Fluorine)
8.1.2.2.1  General
     Fluorine_, derived from the mineral fluorite, commonly known as fluorspar, is
one of the most versatile and useful of the elements.  Steadily increasing
quantities are required in steel production, where the mineral fluorite is useful
as a slag thinner; in aluminum production, where cryolite, another fluorine
mineral, is necessary to dissolve alumina for the electrolytic cells; and in
ceramics, where fluorite is a flux and opacifier.  Strong as the fluorine
demand has been in the foregoing uses, it has been even stronger for an
important group of fluorocarbon chemicals which are formulated into refrigerants,
plastics, solvents, aerosols, lubricants, coolants, surfactants, rocket fuels,
medicinals, aluminum fluoride, and many other industrial products.
ai.2.2.2  U.S. Plants/Companies
     At  the start of 1973, there were  23 mines and 7 froth flotation plants
in operation; during the year 8 mines  and 4 flotation plants closed down.
Cumulatively over 126,980 Mg (140,000  tons) of flotation milling capacity was
lost;  but during the past 2 years the  output from these plants has only averaged
about  81,630 Mg (90,000 tons) annually, mainly because the mines could not supply
the mills.  In 1975, 10 companies operated 15 mines in the United States.
     Although  some domestic  fluorspar  is  sold with little or  no processing
after  mining,  most crude  ore requires  beneficiation or yields a finished  product.
     Manpower  required by the U.S.  fluorspar industry, is not  large.  An
estimated  350  men are employed  in mines  and 250  in mills.
3.1.2.2.3  U.S. Production,  Consumption,  and Prices
     Salient statistics for  the U.S. fluorspar industry are presented  in
the  following  table.   (Data  in  1000 Mg;  1000 short tons in parentheses.)

                                     8-30

-------
                           Table 8-10. «-S FLUORSPAR INDUSTRY (1n thousand Mg ana thousand
                                        short tons 1n parentheses)
                                         1972
                                                        1974
                                                                1975
Production: Finished (all grades)!''
Fluorspar equivalent from phosphate rock
Imports for consumption:
  Acid-spar
  Het-spar
Exports:  Ceramic and add grades
Sales of Gov't stockpile excesses
Apparent consumption
Reported consumption: Acid-spar
              Het-spar
Price:-' Acid-spar, $/Hg (per ton)
      Het-spar. $/Hg (per ton)
Year-end stocks:  Mine
           Consumer
Employment: M1ne^
!_. .         Source:  Conraodlty C
  Shipments
227
(251)
58
(65)
644
(711)
427
(471)
2
(3)
1349
(1488)
663
(731)
563
(621)
$93
($85)
$75
($68)
1 1
! J
ns)
342
(376)
600
270
225
(225)
76
(84)
6<0
(706)
458
(506)
1
(2)
1362
(1509)
614
(677)
612
(675)
$93
(£85)
$71
($65)
3
297
(328)
600
280
182
(1S2)
67
(97)
764
447
(493)
5
(6)
1296
(1429)
762
(841)
620
(684)
$99
($99)
$77
($70)
12
(14)
390
(431)
350
100
126
(140)
72
(SO)
633
(699)
318
(351)
(I)
1179
(1300)
619
(683)
509
(562)
$106
($97)
$88
($80)
9
(11)
290
(320)
300
193 .
163
(180)
72
(80)
535
• (590)
281
(310)
(1)
1060
(1169)
498
(550)
589
(650)
$116
($106)
$95
($87)
10
(12)
• 263
(290)
300
200
                                      Sj™ries
                                               l- '977-
      Consumption  of fluorine is  chiefly in  the chemical, steel, and  aluminum
 industries.   An estimated  622,202  Mg (686,000 tons)  was consumed by  U.S.
 industries  in 1974.   Mnay  marginal  U.S. mines have been forced  to close
 owing to  low-cost  imports  of fluorspar, contributing  to greater dependence
 on  foreign  supply.   A gradual  upward -trend  in the price of foreign fluorine
 imports may  result from increasing world demand and  stimulate development
 of  more reserves.  Both domestic and foreign  producers  have instituted
 programs for increasing output  by reopening and refurbishing existing mines
 and exploring for new deposits.
      U.S.  dependence  on foreign  supplies for  most of  its  fluorine demand
has  existed  since 1952 and is increasing.   Lower foreign  production cost
rather  than  inadequate domestic  deposits of fluorine minerals is  the chief
reason  for the  U.S. increasing dependence  on  foreign sources of supply.
                                        8-31

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8.1.2.3  Salt (NaCI)
8.1.2.3.1  General
     Salt is-an essential nutrient in the human diet and a major basic raw
material for production of various chemicals and products.  In 1974, about
one-third of the world's salt was produced in Europe; another third in North
America; and one-fifth in Asia.  Vast salt reserves throughout the U.S. are
concentrated in 16 states and estimated at 61 trillion tons.
8.1.2.3.2  U.S. Plants
     In the United States there are 97 plants processing salt from 106 mines
(1974).  Most of these plants are concentrated in eight states which accounted
for 96% of the total production of 1973.  Louisiana and Texas are the major
producer/processor states with 29.1 and 24.4 percent respectively of total 1974
U.S. production.  U.S. employment in salt processing operations for 1976 was
estimated to be 5,040.
8.1.2.3.3  Companies
     There are 52 salt processing companies in the United States.  In 1974,
twelve companies each produced more than 1 million tons of salt accounting for
88% of total U.S. production.  Eighteen companies individually producing
between 90,700 - 907,000 Mg (100,000 and 1 million tons) added 11% to the
total with the remaining 1% produced by 22 companies with a yearly output of
less than 90,700 Mg (100,000 tons) each.
     Most large salt companies are vertically integrated starting with salt
produced as brine, for example, being consumed on the site for making chlorine
and caustic soda or soda ash.
                                    8-32

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8.1.2.3.4   U.S.  Production,  Consumption and Process

      Salient statistics  for  the .U.S. salt  industry  are presented  in the

following table.
                  Table 8-11.   U.S. SALT INDUSTRY (1n thousand Hg and
                                  thousand short tons In parentheses)
                     Sold or used by producers 2/


                     Imports for consumption


                     Exports

                     Apparent consumption


                     Prices: Rock salt, medium
                          course in 100 Ib.
                          bags, quoted dollars
                          $/Mg (per ton)
                          Average sales price
                          f.o.b. mine, dry
                          (including bulk I
                          pressed but exclud-
                          ing brine), $/Mg
                          (per ton)

                    Stocks, yearend

                    Eiployaent: Mine and Plant
                                            1972
 40,834
(45,022)

  3,140
 (3,463)

   788
  (869)

 43,187
(47.616)


 $21.39
($19.40)
 $11.71
($10.62)
   J973    JlZi    1975    1976

  39,826   42,208  37,214   38,127
  (43,910) (46,536)  (41,030)  (42,037)

   2,908   3,045   2,916    3.741
  (3,207)  (3,358)  (3,215)  (4,125)

    552     472   1,208     946
   (609)   (521)  (1,332)  (1,044)

  42,182   44,781   38,922   40 922
  (46,508) (49,373)  (42.913)  (45,118)


  $21.39   $21.39   $29.78   $29.78
 I($19.40) ($19.40)  (27.00)   (27.00)
  $12.97  $14.12   $15.91   $18.29
 ($11.76)  ($12.81)  ($14.43) ($16.59)
  NA

 5,070
                    Source:  Conrodity Data Sunrnaries Annual,
   «A     4.700    2,400   2.400

  4.950    5.280    4,920   5.040

1977, U.S. Bureau of Mines.
      Percentage  breakdowns for 1976 production  end-uses  roughly are:   caustic

soda and chlorine -  60%;  synthetic  soda ash  - 11%; miscellaneous  chemicals  -

3%;  highway  deicing  - 18%; salt for human consumption -  3%; and all  other uses  - 18%.

      Because of  its  relatively low  production cost and high bulk  density, the

cost of shipping salt is  usually a  large part of its  cost as  used.   Such

commodities  are  poorly suited  to international  trade.   The 6.8% U.S. 1974 salt

-import  was mainly from bordering Canada and  Mexico.

8.1.2.4  Boron

8.1.2.4.1  General
   — Boron  is a  versatile and useful element used mainly  in  the  form  of its

many compounds,  of which  borax and boric acid  are most well  known.   The
                                             8-33

-------
largest single use of boron is in glassmaking where boron compounds add
strength to the glass, especially above the temperatures of which ordinary
glass softensr
     While boron is not an extremely rare element, few commercially attractive
deposits of boron minerals are known.  It is estimated that about half of the
commercially attractive world boron resources, estimated at about 72 million
tons of boron, are in southern California.
8.1.2.4.2  U.S. Plants/Companies
     Three companies produced borax in the United States during 1975, all
operating in southern California.  U.S. Borax & Chemical Corp., by far the most
important producer, mined borax (or tincal) and kernite at a large open pit
mine at Boron.  U.S. Borax also owns and operates refineries and products plants
at Boron in Kern County, at Wilmington in Los Angeles County, California, and at
Burlington, Iowa.
     Overall, nearly 2,000 persons are employed within the U.S. boron extraction
industry.  There is no secondary recovery and .reuse of boron compounds, since
almost all of this goes into dissipative uses.
8.1.2.4.3  U.S. Production, Consumption and Prices
     Salient statistics for the U.S. boron industry are presented in
Table 8.12.
     Two-fifths or more of the boron compounds consumed were used in the manu-
facture of various kinds of glasses within the United States.  Boron materials
account for 5 to 10 percent of many special glasses by weight and 50 to-75
percent by value.  About 15 percent of all boron  consumed went into insulating
                                     8-34

-------
 fiberglass, 10  percent into textile fiberglass,  and 15 to 20  percent into all
 other glasses.   The energy shortage has created  a  further demand  for insulating
 fiberglass.
             Table  8.12  u.s. BORON INDUSTRY (in thousand Mg and
                          thousand short tons in parentheses)
                                      1972
1973
                                                      1974
1975
                        1976
1,016
(1,121)
18
(20)
172
(190)
NA
$82
($75)
N
1,800
Annual,
/i ,m
(1,225)
16
(18)
190
(210)
NA
$88
($80)
o t A v
1,800
1977, U.S.
1,074
(1,185)
19
(21)
230
(254)
103
(114)
$88
($80)
a 1 1 a b
1,800
Bureau of
1,063
(1,172)
25
(28)
223
(246)
88
(98)
$110
($100)
1 e
1,800
Mines.
1,088
(1,200)
27
(30)
235
(260)
95
(105)
$115
($105)

1,900

          Production  (boron minerals and
           compounds)
          Imports (boron minerals and
          compounds
          Exports (boric acid and
          refined borates)
          Apparent consumption
           (contained boron)
          Price: $/Mg (per ton)(granu-
               lated pentahydrate
               borax 1n bulk, f.o.b.
               mine)
          Stocks, yearend
          Employment J/
      Between year-end  1973 and November 1974, the  price of anhydrous  borax
(bulk)  rose from 121/Mg ($110 per short ton) to $223/Mg ($203) for  U.S.  Borax,
and the price of boric acid increased  from $147 to 219/Mg ($134 to  $199).  These
increases  reflect steep rises in energy cost, inflation, and strong demand.
The sharper rise in costs of anhydrous products, compared with costs  of products
with  water, can be explained by the more intense use  of energy in fusion than in
distillation and chemical processing.
8.1.2.5 Sodium Compounds
8.1.2.5.1   General
  —The compounds of  sodium are of primary importance to the whole chemical
manufacturing industry.   Although not  always present  in the finished  product,
                                       8-35

-------
sodium plays some part in the preparation of nearly every product requiring
chemical processing.
     Soda ashj's the term used in the industry for sodium carbonate.
     Solvay soda or ammonia soda are terms used interchangeably for sodium —
carbonate produced from salt by the Solvay process.
     Salt cake is the term used for sodium sulfate.  Glauber salt is a common
hydrated form of sodium sulfate.
8.1.2.5.2  U.S. Plants
     In 1975 there were nine soda ash plants, 4 synthetic and 5 natural, in the
United States, located in New York, Michigan, Ohio, Texas, Wyoming and California.
Sodium sulfate was produced at 28 plants in 15 states.
     There were only four Solvay plants left in the United States in 1975
after the permanent closing of two major producers in Louisiana.  High cost
of fuel and other raw materials, combined with strict antipollution laws, have
made it difficult for Solvay soda ash to compete with natural soda ash.
     Most of the world's supply of natural  soda ash comes from a small  area in
southwest Wyoming called the Freen River Basin.  A secondary source of natural
U.S. soda ash is in Searles Lake, California.
     Natural sodium sulfate is extracted from brines of California, Texas,  and
Utah.  About three-fourths of the by-product sodium sulfate plants are located
east of the Mississippi River.
     About 2,800 people are employed in the natural soda ash industry and
an additional 130 in producing natural sodium sulfate.
                                     8-36

-------
 8.1.2.5.3  U.S. Companies
      There were eight soda ash companies  in  1975;  4 synthetic and 4 natural;
 and three natural  sodium sulfate companies.   By-product sodium sulfate was
 produced  by 18 companies in 15 states.
      U.S.  soda ash companies are:  Kerr-McGee Chem.  Corp., Stauffer Chemical
 Corp., Allied  Chemical  Corp., and FMC Corp.
      U.S.  sodium sulfate companies are:  Stauffer  Chemical Co.,  Kerr-McGee
 Chem. Corp., U.S.  Borax & Chem.  Corp., Ozark-Mahoning  Co., and Great Salt
 Lake  Minerals  and  Chem.  Corp.
8.1.2.5.4   U.S.  Production. Consumption and Prices
      Salient statistics  for the  U.S.  sodium carbonate  industry are presented in
the following  table.
                                       1972
                                              1973
                                                      1974
                                                                     1976 e/
rroauction: Natural
Manufactured
Imports for consumption

Exports (mostly refined)
Apparent consumption (Nat
synthetic)
carl ots, 'works 'quc
$/Mg (ton)
Average sales price
(natural source) f
mine or plant $/Mg
Producer stocks at yearend,
natural
2,918
(3,218)
(solvay) 3,904
(4,305)

435
(480)
and 6,388
(7,043)
'ted fffs'itfrt
,
$24.56

(ton)
83
(92)
3,375
(3,722)
3,458
(3,813)
14
(16)
385
(425)
6,463
(7,126)
$39.15
35.50)
*?7
»Jf' ,
(525.36)
95
(105)
3,681
(4,059)
3,180
(3,507)
31
(35)
511
(564) '
6,382
(7,037)
. $59-$70
($54-$64)

$37.35
($33.87)
71
(79)
3,925
(4,328)
2,541
(2,802)
2
(3)
500
(552)
5,968
(6,581)
1 $62-$70
($57-$64)

$46.54
($42.20)
165
(182)
4,699
(5,181)
2,193
(2,418)

527
(582)
6,365
(7,018)
$62-$78
($57-$71)

$55.37
($50.20)
72
(80)
^,^,ent.  mne and plant      1,070    1>330    2,651    2,765
Source:  Comity Data Susies Annual, 1977. ^ Bureau „
                                                                   27905
                                     8-37

-------
     Salient statistics for  the U.S. sodium sulfate industry  are presented in

the following table.
           Table 8.14
U.S. SODIUM SULFATE INDUSTRY  (in thousand Mg and
thousand short tons in parentheses)
                                     1972
                    1973
       1974
       1975
       1976
Production: Natural
By-product
Imports for consumption
Exports
Apparent consumption (natural
and by-product)
Price: Quoted (salt cake -
100 % Na?S04, in
carlots bulk at works,
$/Mg (per ton)
635
(701)
567
(626)
271
(299)
26
(29)
1,449
(1,598)
$30
($28)
609
(672)
694
(766)
' 290
(320)
40
(45)
1,553
(1,713)
$30
($28)
620
(684)
602
(664)
340
(375)
46
(51)
1,516
(1,672)
$34
($31)
604
(667)
507
(560)
258
(285)
69
(77)
1,301
(1,435)
$66
($60)
594
(656)
548
(605)
314
(347)
44
.(49)
1,414
(1,559)
$71
($65)
                 Average sales price
                 (natural source),  f.o.b.
                 mine or plant, $/Mg     $17.93
                 (per ton)

           Producer stocks at year-
             end, natural
                    $19.03   $26.46   $45.75    ($54.85
            ($16.26)  ($17.26)  ($23.99)  ($41.48)  ($49.73)
              80
             (89)
 80
(89)
 29
(32)
 30
(34)

130
 34
(38)

135
           Employment: Wells & Plant       105      132      126
           Source: Conmodtty Data Sundries Annual, 1977. U.S. Sjreau of Mines.
      The manufacture of glass  absorbs from  39 to 49  percent of  the soda ash

 production  and about 7 percent of the sodium sulfate output.  The pulp and

 paper  industry consumes about  70 percent  of the sodium sulfate  output and about

 9 percent of the  soda ash  supply.  The  production  of detergents also requires

 both compounds:   about 20  percent of the  sodium sulfate supply  and 4 to 6 percent

 of the soda ash production.   In addition, 23 to 25 percent of the soda ash  supply

 is used in  producing other chemicals, and about 3  percent is used in water  treat-

 ment.   Miscellaneous uses  absorb the remaining soda  ash output  and.3 percent of

 the sodium sulfate production.
                                      8-38

-------
      Reserves of natural  sodium sulfate in  the  United  States  are  limited,
 and present requirements  are met by imported  material.   If  there  is  no
 interruption in  flow of sodium sulfate  from Canada,  however,  there is little
 likelihood  of a  real  shortage of salt cake.
 8.1.3  NON-METALLIC  MINERALS FOR CERAMIC, REFRACTORY AND MISCELLANEOUS  INDUSTRIES
 8.1.3.1   Clays
 8.1.3.1.1.   General
      Clays  are a group  of important fine-grained  non-metallic minerals  which
 are mostly  hydrous aluminum  silicates containing  various amounts  of  organic
 and inorganic impurities.
 8.1.3.1.2   U.S.  Plants/Companies
      Most clays  are mined  by open pit methods,  but in a  few instances underground
 methods are used.  About  2 percent  of the U.S.  total clay output  is  from
 underground mines.
      Kaolin  has many  industrial applications, and many grades are specifically
 designed for  use in paper, paints,  rubber, plastics  and  ceramics.
     Most of  the large kaolin producers have principal  operations in Georgia.
 In  1975 three  large diversified firms accounted for  about 36% of the total
 domestic output, and four refractories manufacturers mined 10 percent of the
 U.S. total  for their own use.  A total of 35 smaller companies accounted for
 the balance.  Altogether 52 firms operated 120 mines in  14 States.
     Ball  clay is used primarily in production of whiteware because of  its
extremely refractory nature.   The ball clay industry is  small, with 11  pro-
ducers operating 52 mines in  8 States in 1975.  Two of these were large
diversified firms with widespread foreign and domestic mineral interests.
                                  8-39

-------
     Fire clay producers were mostly refractories manufacturers that used the
clays in firebrick and other refractories.  A large part of the fire clay was
mined and used by producers of structural clay products.
     In 1975 tftere were 7 firms producing bentonite from 498 mines in 13
States.  Four were large diversified firms with international mineral operations;
two of the firms had interests in other types of clay in the United States.
     Seven of the 17 fuller's earth producers and 11 of the mines were located
in the attapulgite fuller's earth areas of Florida and Georgia.  Production,
mostly small scale, was reported from seven other States in 1975.  Most
producers were small independent firms, but four were large diversified cor-
porations with international mineral interests.
     Firms producing miscellaneous clay in 1975 were manufacturers of structural
clay products, clay pipe, lightweight aggregates, and cement.  Essentially all were
integrated to the extent of owning and operating the deposits of clay used in
making their products.  A few of the miscellaneous clay producers were diver-
sified firms having interest in metals and other non-clay products.  Some of the
miscellaneous clay producers had numerous plants.  This is necessary if they
are to be major firms, because the economic shipping radius for the individual
plants is usually about 200 miles.
     Most clay industry plants produce 3-136 Mg (4-150 tons) per hour of product.
     Employment in the clay  industries totaled  16,000 in 1975.  Approxi-
mately one-fourth of the workers were involved  in mining and exploration,
and the  balance were engaged in processing the  clays for various end uses.
Although employment was widespread, certain areas had disproportionately
large percentages of the clay workers.  An estimated 80 percent of the
                                     8-40

-------
kaolin employment was  in Georgia,  and  over 90  percent of the fuller's  earth

workers were  in Florida and Georgia.   Ohio, Missouri, and  Pennsylvania

accounted  for  over 50  percent of the fire clay employment.

8.1.3.1.3   U.S.  Production,  Consumption,  and Price

      Salient statistics for  the U.S. clay industry  are presented  in the

following  table.   (Data in  1000 Mg;  1,000 short tons  in  parentheses.)
             Table  8.15    u.s. CLAY  INDUSTRY (in thousand Mg and
                            thousand short tons in parentheses)
         Mine production:

          Kaolin


          Ball  clay

          Fire  clay ]_/


          Bentonite


          Fuller's earth


          Common clay

            Total


        Imports for consumption


        Exports
        Apparent consumption

        Price:
                                         1972
                                                 1973
                                                          1974
                                          1975
                                                                           1976
4,823
(5,318)
612
(675)
3,247
(3,581)
2,509
(2,767)
896
(988)
41,837
(46,127)
53,926
(59,456)
60
(67)
5,435
(5,933)
695
(767)
3,689
4,068)
2,787
(3,073)
1,032
(1,138)
44,725
(49,312)
58,366
(64,351)
48
(53)
5,798
(6,393)
741
(817)
3,755
(4,141)
3,002
(3,310)
1,111
(1,225)
40,733
(44,910)
55,141
(60,796)
39
(43)
4,837
(5,334)
640
(706)
2,959
(3,263)
2,928
3,229)
1,078
(1,189)
32,040
(35,326)
44,485
(49,047)
34
(38)
5,188
(5,720)
782
(863)
3,111
(3,431)
3,417
(3,768)
1,181
(1,303)
34,401
(37,929)
48,083
(53,014)
36
(40)
              ,1'675X    1,901     2,223     2,099    2,240
              (1,847)   (2,097)   (2,451)   (2,315)   (2,470)

             ,f*.'«2x  ,56'512    52,957    42,420    43,879
             (57,676)  (62,307)  (58,388)  (46,770)  (50,584)
        Stocks, yearend
        Employment:  Mine e/
                   Mill e/
$1.10 to $221/Mg ($1.00 to $200 per short ton), depending on type
and quality.

                    Not   Available
             •  4,000
              14,000
 4,000
14,000
 3,800
13,500
 3,500
13,000
      Source:  Commodity Data Summaries Annual, 1977, U.S.  Bureau of Mines.
 3,300
12,500
                                         8-41

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      Production  of miscellaneous  clays  is  tied  primarily to the construction
 industry,  while  output of the  higher  quality  clays  is  not dependent  on demand
 by a single major industry segment.   Miscellaneous  clay production  is wide-
 spread, with all States contributing  to the national  total  in most  years.
 Fire clay output is  also widespread,  with over half of the  States reporting
 production.  About half the fire clay output is used for construction  products.
 Output of the other clays is more restricted geographically because of the
 lack of resources in many States.
      The major  world uses for clays are in manufacture of heavy clay con-
 struction  products, cement, and  lightweight aggregates.  The more advanced
 industrial  areas, particularly the United  States, Western Europe, Canada,
 and Japan,  require substantial quantities  of the higher quality clays for use
 in such  products as paper,  high-grade  ceramics,  iron  ore pellets, absorbents,
 and drilling fluids.
       Although there-are other materials such as  talc, silica,  and  calcium
  carbonate that can  be substituted for  high-quality clays  in  many end  uses,
•  the comparatively low cost of clays  usually gives  them a  decided competitive
  advantage.  Alternative materials, therefore, pose no great threats to  the
  specialty  clay  industries; on the contrary, the competition is more likely
  to result  in increased clay use at the expense of the alternate materials.
        For  common, or miscellaneous clay, many alternate construction products
  and raw materials compete  very  effectively with brick, tile, and lightweight
  aggregates.  A few of the  major ones  are  wall panels made of concrete, stone,
  glass, metals, and plastics;  lightweight  aggregates  made of pumice, expanded
   vermiculite, and sintered  fly ash;  floor  and  wall tile made of plastics,
   vinyl asbestos, cork, and  concrete; and  sewer pipe made of  concrete, asbestos,
   and plastics.
                                   8-42

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8.1.3.2  Feldspar
8.1.3.2.1  General
     Feldspar, usually of the potash or soda type or in mixtures of the two,
finds its principal end uses in the manufacture of glass and ceramics; in
both of which applications it acts as a flux.  In glassmaking, feldspar
also provides a source of alumina, the presence of which enhances the
workability of the product, inhibits any tendency toward its devitrification,
and increases its chemical stability.
8.1.3.2.2  U.S. Companies/Plants
     Crude feldspar is produced in the United States as a primary product
by large diversified firms, by major firms that are primarily feldspar
producers, and by a large number of individuals or groups that mine small
quantities for sale to firms that operate feldspar-grinding plants.
     Most of the feldspar used in glass making is ground no finer than 20
mesh while that used in ceramics and filler applications is usually pul-
verized to at least minus 200 mesh.
     Nine domestic companies, operating fifteen plants in nine States, ground
feldspar for market in 1974.  Listed in descending order of output tonnages,
North Carolina had six grinding mills, while Connecticut, Georgia, and South
Carolina had one each.
8.1.3.2.3  U.S. Production. Consumption and Prices
     Salient statistics for the U.S. feldspar industry are presented in the
following table.
                                 8-43

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         Table  8  16  u-s-  FELDSPAR INDUSTRY (in thousand Mg and
                      thousand short tons in parentheses)
        Production


        Imports for consumption

        Exports


        Apparent consumption
                          1972

                          676
                          (746)
                            4
                           (5)

                          617
                          (681)
  1973

   718
  (792)
    9
  (10)

   697
1  (769)
1974

 692
(763)
  16
 (18)

 696
(768)
1975

 607
(670)
  9
 (10)

 598
(660)
1976

 637
(725)
  6
  (7)

 634
(700)
        Price, average, Mg (per ton)    $15.61    $17.86   $16.47   $19.30   $19.85
                                 ($14.16)  ($16.20)  ($14.94)  ($17.50)  ($18.00)
        Stocks, producer, yearend

        Employment:  Mine and prepara-
                  tion plant
                          225
                          (249)
   237
  (262)
 216
(239)
                          450      450      450


Source: Coroodity Data Suonariej Annual, 1977. U.S. Sureiu of Mines.
 216
(239)
                   450
 233
(257)
                                                           450
      Feldspar is a relatively unimportant  item in U.S.  foreign  trade, although

in  some areas,  particularly in  the northeastern States, a significant proportion

of  the feldspathic-materials demand is satisfied by an  alternative mineral

product, nepheline syenite, imported from  Canada.

      Feldspar is a relatively low-priced,  bulk commodity that usually can

be  produced  from some  source near  the consumer more advantageously than it

can be shipped  from a  distance.

8.1.3.3  Kyanite

8.1.3.3.1  General

      Kyanite, andalusite,  and sillimanite  are a closely related  trio of

aluminum silicate minerals that break down upon heating to form  a  mixture

of  mullite,  SAl^O-.ZSiO,,  and vitreous silica, SiCL.  The properties of
                 L. 3      C.                             L.

mullite serve to advantage as a component  in  refractory shapes and furnace

linings for  a wide range of industrial applications.
                                    8-44

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8.1.3.3.2   U.S. Companies/Plants
      All but a small  part  of the domestic  kyanite  output  in  recent years has
consisted  of the contributions of  only two firms.   Kyanite Mining Corp.
operates two mines  in Virginia, the  Willis Mountain  mine  at  Dillwyn  in
Buckingham County and the  Baker Mountain mine in adjacent Prince Edward
County.  Commercial ores, Inc., a subsidiary of Combustion Engineering, Inc.,
worked the Henry Knob mine in York County,  South Carolina, from 1948  through
1969, and  C-E Minerals, Inc., another division of  Combustion Engineering, Inc.
has  operated the Graves Mountain mine in Lincoln County, Georgia, since 1963.
8.1.3.3.3   U.S. Production,  Consumption, and Prices
      Salient statistics for  the U.S.  kyanite industry are presented  in the
following  table.
      Table 8.17    u.s. KYANITE INDUSTRY (in thousand Mg and
                     thousand short tons in parentheses)
                                 1972
         1973
                                                  1974
                          1975
     Production: Mine
               Synthetic mullite
     Imports for consumption
     Exports e/
     Apparent consumption
       Company confidential data
 42.1     52.8     37.6     21.9
                 (41.5)
(46.4)   (58.2)
 0.1      0.2
                  0.2
(24.1)
 0.1
 27.2     40.1     40.1
(30.0)   (45.0)  '  (45.0)
                          40.1
                         (45.0)
      Not  Available
                                                                   1976
 27.2
(30.0)
 0.1
 40.1
(45.0)
     Price:  Domestic concentrate, 35- to 325- mesh, in bags, f.o.b. Georgia $69-$130/Mg
            ($63 to $118 per short ton); imported kyanite, no current quotation;
            synthetic mullite, $177-$496/Hg ($160 to $450 per short ton), depending
            upon type and grade.
     Stocks (producer)
     Employment:  Kyanite mine
                and plant           165      175
     Source: Corrodity Data Sundries Annual, 1977. U.S. Sure.u of Mines.
      Not Available
                  175      175
                                  175
                                     8-45

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      In  accordance with  the  policy  of  the  firms  involved,  no  statistics on
 U.S.  production  of kyanite have  been released  since  1948-49 when  the then-
 current  figure was in  the neighborhood of  12,244 Mg  (13,500 tons) per year.
 Published  estimates  from various  sources since then  have placed the U.S. out-
 put at about 40,814  Mg (45,000 tons) in 1963 and 85,258 Mg (94,000 tons) in
 1973.  Both figures, although useful as indicators of magnitudes, are believed
 to be moderately in  error on the  conservative  side.
      Statistical  consumption data is not available.  Refractory uses have been
 dominant since the early 1920's.  Many non-refractory uses for the kyanite-
 group minerals and synthesized aluminum silicates have been developed, and
 other-possible uses appear to have  potential for future large-scale applications.
      In  the iron  and steel industries, mullite has found important use in
 critical areas of blast  furnace stoves and stacks, reheat furnaces, steel
 degassing  chambers and soaking pits, and many  types of auxiliary pouring and
 handling equipment.  .
8.1.3.4  Talc
8.1.3.4.1  General
     The mineral  talc  is a soft,  hydrous magnesium silicate.   Commercial
 talcs range from  something approaching pure mineral  composition to mineral
 products that have properties in  common with pure talc but which may contain
very little of the actual minerals.
8.1.3.4.2  Company/Plant Statistics
     Talc or soapstone was produced domestically in  1974 from 46 mines  in
Alabama, Arkansas, California,  Georgia, Maryland, Montana,  Nevada, New  York,
North Carolina, Oregon, Texas,  Vermont, Virginia, and Washington.
                                8-46

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  Pyrophyllite was produced from five mines  in  North  Carolina  and  one  mine  in
  Pennsylvania.
       There were 30 producers  of talc minerals  in  the  U.S.  in  1974.   The
  plant size range is from  5-18 mg (6 to  20  tons) per hour.
       The  largest producers of talc  minerals in the United  States  (all
  either exclusively engaged in  that  enterprise or  else horizontally inte-
  grated subsidiaries  of diversified  organizations) jointly  provided 75
1  percent of the  total 1974 domestic  output, and the remainder consisted of
  the combined contributions of about 25 smaller firms.
      The principal domestic producers of crude talc, soapstone, and
  pyrophyllite approached vertical integration to some degree in that they
 operated grinding mills,  processing their output either in plants adjacent
 to the mines or in separate installations more conveniently located with
 respect to major markets.   Part of the  mineral  from  California and Montana
was  milled in Oregon, and  a substantial  quantity of  Montana talc  was  processed
in Belgium.
     Employment  in talc, soapstone,  and  pyrophyllite mines  and  preparation
plants  in  1974 was estimated to  be  equivalent  to the services  of  about  950
full-time  workers.
8.1.3.4.3   U.S.  Production. Consumption,  and Prices
     Salient  statistics for the  U.S. talc industry are presented  in
Table 8-18.
     The largest  use  of talc-group minerals is for the manufacture of ceramics.
In this application,  addition of  talc or pyrophyllite to the usttal clay-silica-
feldspar body mixtures facilitates the firing of the ware and improves the
quality.  Second in rank for end use is paint production.  Third in order
                                8-47

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           Table  8.18   U.S. TALC INDUSTRY (in thousand Mg and
                         thousand short tons in parentheses)
        Production: Mine


        Sold by producers


        Imports for consumption


        Exports


        Apparent consumption ]_/
 1972

 1,004
(1,107)

  983
0,084)

   26
  (29)

  155
 (171)

  854
 (942)
                                    1973

                                   1,131
                                   (1.247)

                                   1,073
                                   (1,184)

                                      20
                                     (23)
                                     163
                                    (180)

                                     931
                                   (1,027)
  1974

 1,150
(1,268)

  965
(1,064)

   27
  (30)

  165
  (183)

  826
  (911)
                                                             1975
        1976
 875    1,028
(965)   (1,134)

 844      907
(931)   (1,000)
 20
 (23)

 143
(158)

 721
(796)
 20
 (23)
 175
(194)

 751
(829)
        Price: $5.50-$276.00/Mg ($5 to $250 per ton) (crude or ground) depending upon
              grade and preparation
Stocks, producer, yearend


Employment:  Mine and mill
                                     950
           950
                                                      950
                                                              231
                                                             (255)

                                                              950
                                   208
                                   (230)

                                   950
         Source:  Commodity Data Summaries Annual, 1977, U.S. Bureau of Mines.



among  outlets  for domestic talc  minerals  is use for coating  and/or loading of

high-quality papers.   In this application,  high-purity talc  helps in  obtaining

a product with the desired weight and opacity, good ink retention, and superior

surface texture.

      Specific  end-use  percentages of total  consumption are:   Ceramics - 17%,

paint - 12%, toilet/cosmetic  -  3%, insecticides -  4%, paper  - 7%, refractories  -

3%  roofing  - 4% rubber - 2%,  and all other minor uses - 46%.

      The bulk  of the  talc, soapstone, and pyrophyllite of  commerce is made up

of  relatively  low-unit-value  material unable to bear the charges of  long-

distance transportation, but  exceptional  grades such as high-purity  talc of

pharmaceutical, cosmetic, or  even papermaking quality are  significant items
                                     8-48

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of international trade.  The quantities of talc, soapstone, and pyrophyllite
imported and exported by the United States, however, are relatively too small
to exert a decisive influence on the overall  pattern of the industry,  even
though the total values involved are substantial.
                                   8-49

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8.1.4  Bibliography
     The industry structure presented here has been compiled from information
obtained from the United States Bureau of Mines in Washington, D.C.   The	
Bureau of Mines is considered to be the definitive source for U.S.  mineral
industry data.  The text is comprised of quoted, paraphrased and edited
material from preprints of the 1975 edition of Mineral Facts and Problems.
Individual physical scientists in the Division of Non-Metallic Minerals at
the Bureau whose reports make up the lion's share of this document are:
     1.   Sand and gravel:  Walter Pajalich, mining engineer, Division of
          Non-Metallic Minerals (DNM)
     2.   Gypsum:  Avery H. Reed, Supervisory Physical Scientist, DNM
     3.   Pumice, Perlite, Arthur C. Meisinger, Industry Economist, DNM
     4.   Vermiculite:  Richard H. Singleton, Physical Scientist, DNM
     5.   Mica:  Stanley K. Haines, Physical Scientist, DNM
     6.   Barite:  Frank B. Fulkerson,  Industry Economist, DNM
     7.   Fluorspar:  Hiram B. Wood, Ecologist, DNM
     8.   Salt:  Charles L. Klingman, Physical Scientist, DNM
     9.   Boron:   K.P.  Wang,  Supervisory  Physical  Scientist,  DNM
     10.   Clays:   Sarkis 6. Ampian, Physical Scientist, DNM
     11.   Talc,  Feldspar:  J.  Robert Wells,  Physical  Scientist,  DNM
     12.   Kyanite:   Michael J.  Potter,  Physical Scientist,  DNM
 Space  limitations  do not  permit listing individual authors'  bibliographies
 here.   The  1975  Mineral Facts and Problems  preprints  contain these listings
 and are available  from the Bureau of Mines.
                                 8-50

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Data presented from these reports have been supplemented with the 1955, 1960,
1965, 1970, 1971, 1972, and 1973 Minerals Yearbooks (Vol. I):  1974 & 1975
Minerals Yearbook Preprints; 1976 and 1977 Commodity Data Summaries; 1970
edition of Mineral Facts and Problems; 1975 Mineral Facts and Problems
Preprints; Mineral Industry Annual Advance Summaries; and personal communi-
cations with most of the individual  authors as well as data clerks and
statisticians at the Bureau of Mines.  Certain statistical items are quoted
from "Engineering/Mining Journal", "Pit and Quarry", "Rock Products",
"Chemical  Market Reporter" and are referenced in the text.  It is neither the
intent nor desire of the editor of this document to claim authorship for all
or any part of the text of the individual  industry structures included herein.
                                8-51

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8.2  COST ANALYSIS OF ALTERNATIVE EMISSION CONTROL SYSTEMS
8.2.1  Introduction
     For costing purposes, two model non-metallic plants have been
developed, representative of typical new stationary plants in each of
the 18 industries studied in this document.  In addition, costs have
been developed for a model portable plant, typifying a crushed stone
or sand and gravel installation.  These costs are found in Supplement A.
     The first model plant consists of crushing operations only, and
includes: primary and  secondary  crushers,  screens (3), transfer points
(4) and the loading  operation.   The second model plant includes both a
crushing operation and a grinding operation, the latter consisting of a
grinder, another screen, two  additional transfer points, and  a bagging
machine.
      Costs are  presented in this section  for controlling particulate
emissions  from  these model new plants  to  achieve the  alternative emis-
sion  level considered in this document.
      Particulate control costs have also  been developed for expansions
at existing  non-metallic minerals plants.   The  model  plant selected here
 consists  only of a grinding  operation, since crushing operations are
 usually built with excess capacity, thus  obviating  the need for additional
 equipment.   (Refer to Section 8.2.3 for more detailed information.)
      (Costs  have also been developed for monitoring particulate
 emissions at the model plants.  However,  since  the  anticipated  new
 source performance standard (NSPS)  is not expected  to require such
 monitoring, these costs are treated separately in  Section  8.3.)
                                     8-52

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      All  control  costs  have  been  based  on  technical  parameters  associated
with  the  control  system used,  such  as the  plant  capacity.   These  param-
                                                      .»
eters are listed  in  Table  8.19.
      These model  plant  costs cannot be  assumed to reflect costs of any
given installation.  Estimating control costs for an actual installation
requires  performing  detailed engineering studies.  Nonetheless, for
purposes  of this  analysis, model  plant  costs are considered to be
sufficiently accurate.
      The model plant costs have been based primarily on data available
from  an EPA contractor  (Industrial Gas  Cleaning Institute), who had in
turn  obtained control system costs from vendors of air pollution control
          2
equipment.   These costs have been supplemented by a compendium of costs
for selected air pollution control systems.   The monitoring costs have
                                        o
been obtained from an equipment vendor.
     Two cost parameters have been developed: installed capital and total
annualized.  The installed capital costs for each emission control system
include the purchased costs of the major and auxiliary equipment, costs
for site preparation and equipment installation, and design engineering costs,
No attempt has been made to include costs for research and development,
possible lost production during equipment installation, or losses during
startup.  All  capital costs in this section reflect fourth quarter 1976
prices for equipment, installation materials, and installation labor.
                                    8-53

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             Table  8.19    TECHNICAL PARAMETERS USED  IN DEVELOPING
                          CONTROL SYSTEM COSTS3
           Parameter
          Value
1.  Temperature
2.  Volumetric flowrate
3.  Moisture content
3.  Particulate loadings:
    Inlet
    Outlet
4.  Plant capacities

5.  Operating factors:
    Crushing operations
    Grinding operations
21°C (70°F)
(See Tables 8.22 to 8.33, 8.38, & 8.39)
2 percent (by volume)
12.8 g/Nm3  (5.6 grains/scf)
0.050 g/Nm3 (0.02 grains/scf)
9,1, 23, 68, 135,180, 270, and 540 Mg/hr
(10, 25, 75, 150, 200, 300, and 600 tons/hr)
2,000 hours/year
8,400 hours/year
Reference  i.
       capacities represent the sizes typical  of generalized  model  plants.
 However, for a particular industry, only some of these sizes are applicable
                                   8-54

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      The  total  annualized  costs  consist,of  direct  operating  costs  and
 annualized  capital  charges.   Direct  operating  costs  include  fixed  and
 variable  annual  costs,  such  as:
      t  Labor  and materials needed  to operate control  equipment;
      •  Maintenance  labor and materials;
      •  Utilities, such  as  electric power;
      e  Replacement  parts;
      •  Dust disposal  (where  applicable).
      The  dust disposal  costs apply only to  dry collection systems
 (i.e.,  fabric filters)  used  to control crushing operations when no
 grinding  operations are employed.  A unit cost of  $4.40/Mg ($4/ton)  is
 used  to cover the costs of trucking  the collected  particulate to a
 disposal  point on-site  (e.g., the  mine).4
      In those plants that have both  crushing and grinding operations,
                   
-------
taxes, and insurance have been fixed at an additional 4 percent of the
installed capital cost per year.  The annual cost factors in this
                         t
section are li_sted in Table 8.20.
     Finally, the total annualized cost is obtained simply by adding the
direct operating cost to the annualized capital charges.
8.2.2  New Facilities
     As discussed in section 8.2.1, two new model plants have been
developed for costing purposes:   a stationary  installation with  crushing
operations only  (Model  Plant  1)  and another stationary  with  both crushing
and grinding  operations  (Model  Plant  2).   The  model  plant  developed for
costing the  portable plant segments  of the crushed  stone,  and sand and
 gravel  industries  is discussed in Supplement  A.  For both  models, the
 alternative emission level to be achieved is  0.050  g/dscm (0.02 grains/
 dscf).   The control option to be used to achieve this emission level is
 fabric filtration.   At an uncontrolled emission rate of 12.8 g/dscm
 (5.6 grains/dscf)  (see Table 8.19), this control option is 99.6 percent
 efficient in removing particulate at the model plants.
      The size and  number of fabric filter systems required to achieve the
 emission limit vary according to the mineral  plant  capacity.  For example,
 only two moderately-sized baghouses are required to control  the crushing
 and grinding operations at the 9.1 Mg/hour (10 tons/hour)  model plant,
 while four much larger fabric filters are needed at the 540 Mg/hour (600
 tons/hour) model.
      Each of these  fabric filter systems consists of a pulse-jet baghouse
 with polypropylene  bags,  fan and fan motor, dust hopper, screw  conveyor,
 ductwork, and stack.
                                      8-56

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                 Table  8-20.  ANNUALIZED  COST PARAMETERS9
            Parameter
              Value
1.  Operati ng Labor

2.  Maintenance Labor



3.  Maintenance Materials
4.  Utilities:

    Electric Power

•5.  Replacement Parts:

    Polypropylene Bags

6.  Dust disposal

7.  Depreciation and Interest
            i
8.  Taxes, Insurance, and Adminis-
    trative Cnarges
$10/man-hour

50 percent of operating labor (fabric
  filters)
40 man-hours/year   (opacity monitors)

2 percent of maintenance labor (fabric
  filters)
1 percent of total installed cost
  (opacity monitors)
$0.03/kw-hr



$7.00/m2 ($0.657ft2)

$4.40/Mg ($4.OO/ton)

11.75 percent of total installed cost
  (fabric filters)
16.28 percent of total installed cost
  (opacity monitors)

4.0 percent of total installed cost
 References 2, 3, 4, and EPA estimates.
                                   8-57

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     Tables 8-21 through 8-26 list installed capital, direct operating,
annualized capital, and total annualized costs for each of the fabric
filter systems.installed in the new Model Plants 1.  The six plant sizes
for which costs have been developed cover the range in capacities applicable—
to the various mineral industries.
     In Tables 8-21 through 8-24, the first column lists the technical or
cost parameter in question.  The data pertaining to the fabric filter
are listed in the second column.  However, in each of Tables 8-25 and
8-26, more than one fabric filter are needed to control the crushing
operation.  The data for these fabric filters appear in columns 2, 3, etc.,
while the right-hand column lists the totals for the model plant.
     Similarly, Tables 8-27 through 8-32 contain cost data for Model Plant 2.
The costs are itemized according to the  fabric  filters controlling the
crusher  and grinder operations, respectively.   Again, the right-hand
column lists data  for the  total model plant.  Note that the installed
capital  costs and  annualized  capital charges  for the crusher  baghouse(s)
are  the  same as in the  corresponding tables  for Model Plant 1.   However,
because  no dust disposal costs  are  included  with Model Plant  2,  the direct
operating costs—and  the total  annualized  costs—are lower.
      T.n  these  tables,  the  total  annualized cost has  been  expressed  in two
ways:   thousand dollars/year and  dollars/megagram  of product.   The  latter
 expression is  the  quotient of the total  annualized cost  and the annual
 production rate, based,  in turn,  on the operating  factor.   As Table
 8-19 indicates, crushing operations (i.e., Model  Plant  1)  are assigned
 an operating  factor of 2,000 hours/year, while  with  grinding  operations,
                                     8-58

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 8,400 hours/year has been  used.' For Model Plant 2, where both crushing
 and  grinding operations are employed, 8,400 hours/year is used as the
 operating factor, solely for the purpose of computing the unit annualized
 costs.                                        '         "'','•
     Each cost-effectiveness ratio appearing in the tables is simply the
 quotient of the total annualized cost and the amount of particulate
 collected annually by the  fabric filter system.  To compute the parti-
 culate collected, the 2,000 and 8,400 hours/year operating factors are
 applied, respectively, to  the individual crushing and grinding operations.
 However, for combined crushing and grinding operations, the following
 expression has been used to calculate cost-effectiveness:
      Cost-effectiveness =
      ($/Mg particulate
       removed)
      Where:   TACr, TACr
                 L     b
        TAC
                                          TACr
                                             b
7.65 x 10
         -7
(2000QC + 8400QG)
total annualized costs for crushing and
grinding baghouses, respectively (M$/year)
total volumetric flowrates for crushing-
and grinding baghouses, respectively (m /min)
     The numerator is the sum of the annualized costs for the crushing
and grinding operations, while the denominator represents the total
amount of particulate removed by the fabric filters controlling these
operations.  (Cost-effectiveness is further discussed in Section 8.2.4.)
     As the tables indicate, the installed costs in the crushing (only)
model  plant range from $60,000 to $336,000, as the plant capacity goes
from 9.1 Mg/hour to 540 Mg/hour.  However, given the sixty-fold increase
                                   .8-71

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in the plant capacity, the installed costs increase relatively little.
This is so because the fabric filter installed costs are a function of
the volumetric flowrate, not the plant capacity.  Moreover, the volumetric
flowrate, while dependent on the capacity, does not increase proportionately
with the plant size.
     Based on a 2000 hour operating year, the total annualized cost increases
from $14,000 to $87,000 per year, corresponding to $0.78 to $0.08/Mg
product, as the plant capacity goes from 9.1 to 540 Mg/hour.  Ordinarily,
one would also expect a more substantial increase in the total annualized
cost over such a  large range in  plant  capacities.  However, as Tables
8-21 through 8-26 show, the annualized capital  charges  comprise the bulk
of the total annualized costs.   And since  the  annualized capital  charges
are directly proportional  to the installed costs,  the  total annualized
cost very  nearly follows  the change in the capital  cost.
      There  are several  reasons  why the direct  operating costs  are so  low.
 First, because the gas  streams  controlled  are  non-corrosive and low-
 temperature,  the fabric filter maintenance is  relatively  small, amounting
 to less than one percent of the installed  cost annually.   Then, because
 there is a relatively small  pressure drop  through the  baghouse system,
 the power cost is relatively low.  Costs for replacement  parts (i.e.,
 bags) are proportional to the gas flowrate, but at the same time  amount
 to a  small fraction of the direct operating costs.
      A similar pattern  appears  with the costs  for Model Plant 2,  which
 contains both  crushing and grinding operations.  The costs  here are  about
 the same order of magnitude as  are those for Model  Plant  1.   The  main
 difference is  the additional  baghouse required to control  the grinder

                                     8-72

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  and  its  auxiliaries.   Here  the  installed  costs  range  from  $93,000  to
  $507,000, while  the annualized  costs  go from  $21,000  to  $131,000 per
  year ($0.28  to $0.03/Mg product, respectively).
       The costs described above  are for achieving the  alternative emission
  level.   It is also necessary to compare these costs to the costs required
  to meet a typical state emission regulation (SIP) in  the model plants.
  In this analysis, however, it is assumed that the SIP can be met without
  controls.  The SIP or baseline costs are, therefore, zero.   Thus, the costs
  shown in Tables 8-21  to 8-32 are solely attributable to the alternative
 emission limit.
 8-2-3  Modified/Reconstructed Faci1ities
      As Chapter 5 points  out, there  appears to be no condition which
 would deem an existing  plant modified.  Concerning reconstruction,
 if replacement of components  subject to high abrasion  and impact,
 such  as crushing  and screening surfaces and conveyor belts,
 are exempted  and  considered  routine for this category  of  sources,
there also appears to be no action which could be construed as recon-
s'truction.
      Nonetheless,  expansions of  existing plants do occur.  When they do,
only  a portion of  the plant would be covered under the alternative
emission limit.  These expansions would more than likely involve the
grinding operation, since crushing operations are usually capable of
handling increased throughput without additional equipment.   However, to
expand the plant grinding capacity, a new complete grinding line would
be added.

                                    8-73

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     In this document, sizes for three stationary model plants have been
developed to cover these expansions: 4.5, 9.1, and 32 Mg/hour (5,10,
and 35 tons/hour).  The first two sizes apply to all industries employing
grinders (i.e"., Model Plant 2).  The third size applies only to the boron
                                                                      *
industry.
     The option costed for controlling these expanded model plants  is
fabric filtration.  The gas flowrates used in the costing are listed  in
Tables 8-33 and 8-34.  The other technical parameters  appear  in Table 8-19.
     Because these fabric filters would  be installed at existing, as
opposed to  new plants, the installed capital costs  are somewhat higher,
reflecting  the higher installation  costs required.  The difference
between the existing  and new  plant  ins-tallation  costs, or retrofit  penalty,
 is  quite variable, depending  on individual plant configuration, on-site
 utility  capacity, and other seemingly random variables.  Nonetheless,
 after polling  its members,  the Industrial  Gas  Cleaning Institute  has
 developed an  approximate multiplier,  or retrofit factor, to be  used in
 estimating the existing plant installation costs.5   This retrofit factor
 is 2.0.   Using this factor, the control system existing plant installation
 cost would be twice that of the new plant installation cost.
      Table 8-33  lists the costs of fabric filter systems installed in
 the expanded 4.5 and 9.1 Mg/hour model  plants.  The 32 Mg/hour capacity
 model plant costs are listed in Table 8-34.
      The installed costs in Table  8-33 are $43,000 and $48,000 for the
 4.5 and 9.1 Mg/hour  plants, respectively.  The  installed cost difference
 is relatively small:  10 percent.  However, this is because the gas  flow-
 rates upon which the costs are based differ-by  only 23 percent, even

                                      8-74

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     Table  8-33.  FABRIC FILTER COSTS FOR EXPANDED MODEL PLANTS3'5
Parameter
Gas flowrate, m3/min (ACFM)
Installed capital cost, M$c
Direct operating cost, MS/yr
Annual ized capital charges, M$y
Total annualized cost, MS'yr
$/Mg product6
4.5 Mg/Hour
92.0 (3,250)
43
3.4
'yr 6.8
10.2
0.27
.9.1 Mg/Hour
113 (4,000)
48
3.8
7.5
11.3
0.15
 References 1, 2, 3, and 5.
 Expanded plants consist of grinding operations only.
cThe letter "M" denotes thousands; "MM" denotes millions, etc.
 Since SIP control cost is zero, total and incremental annualized costs are equal
Quotients are based on an 8,400 hours/year operating factor.
                                 8-75

-------
Parameter
              Table 8-34.  FABRIC FILTER COSTS FOR 32 Ma/Hour
                           EXPANDED MODEL PLANT3'D
                                                 Value
Gas flowrate, m3/min (ACFM)

Installed capital cost, MSC

Direct operating cost, M$/yr.

Annualized  capital  charges, M$/yr.
Total  annualized cost
         . M$/year
     $/Mg product6
 184  (6,500)

  65

 5.0

10.2
15.2
 0.057
 References 1, 2, 3, and 5.
 bThis capacity applies to the boron industry only
 GThe letter "M" denotes thousands; "MM" denotes millions,  etc.
 dSince SIP control cost is zero, total and incremental annualized costs are equal
 Quotients are based on an 8,400 hours/year operating factor.
                                     8-76

-------
 though one plant size is twice the other.  The total  annualized costs
 differ much less: $10,200/year for the 4.5 Mg/hour size,  and $11,300/year
 for the 9.1 Mg/hour case.  (Because these baghouses control  grinders,
 neither of these costs includes a cost for dust disposal.)
      Since grinding operations need not be controlled to  achieve  a  state
 regulation, the SIP costs are zero.  The annualized costs shown in  Table
 8-33 are, therefore, both total and incremental.   These incremental  costs
 are $0.27 and $0.15/Mg product, in turn, for the  4.5  and  9.1  Mg/hour
 capacity plants.   Both numbers have been based on an  8400 hours/year
 operating factor.  The 44 percent decrease in cost indicates  a  positive
 economy of scale  with plant capacity.
      Finally, the fabric filter costs for the 32  Mg/hour  expanded model
 plant are listed  in Table 8-34.  Sized for a gas  flow rate  of 184 m3/min,
 the installed cost is $65,000.  The corresponding incremental  annualized
 cost is $15,200 per year, or $0.06/Mg product, based  on the  same  8400
 hours/year operating factor.
 8.2.4  Cost-Effectiveness of the Alternative Emission Limit
      For each of  the control  options costed to achieve the alternative
 emission limit,, it  is informative to compare the  total annualized cost
 with the amount of  particulate removed.   A convenient yardstick for
.expressing this comparison is the cost-effectiveness  ratio, which is
 the quotient  of the annualized cost and  the quantity  of particulate
 removed annually.  Expressed  in dollars  per megagram  of particulate,
 these ratios  appear in Tables 8-21  through 8-32,  for  the  stationary new
                                     8-77

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model plant sizes costed herein.  (Because an NSPS impacts most heavily
on new, rather than existing plants, the cost-effectiveness analysis will
be limited to' them.)
     It is clear from these tables that the ratios vary according to the
plant capacity, design, and the model plant configuration  (i.e., Model,
Plant 1 or 2).  For Model Plant 1 (crushing only), the cost-effectiveness
ranges from $32.1 to $27.8/Mg, as the capacity goes from 9.1 to 540 Mg/
hour.  The corresponding ratios for Model Plant 2  (crushing and grinding)
are  $18.2 and $11.6/Mg particulate removed.
     The  ratios are plotted in  Figure 8-1 against  the model plant
capacity.  Note, first of all, that with Model Plant 2, the cost-
effectiveness decreases  from  $18.2 to $14.1/Mg (23 percent) between
the  9.1 and 135 Mg/hour  plant capacities.  At larger sizes, however,
this rate of  decrease  is much less pronounced.   In fact,  the cost-
effectiveness  ratio decreases only  18 percent between  135 and  540 Mg/hour.
Nonetheless,  the  fact  that  the  ratio decreases consistently with plant
size indicates  that the  control  costs for Model  Plant  2 benefit from  a
positive  economy of scale.
      The  curve for Model Plant  1  does not exhibit this  consistency,
 however.   Note that the  cost-effectiveness  decreases  gradually from a
maximum of $32.1/Mg to a minimum of $26.5/Mg.  This minimum  occurs  at a
 plant capacity of about 340 Mg/hour.   But for  larger  plant sizes,  the
 curve swings  upward,  reaching a value  of $27.8/Mg at  the  540 Mg/hour
 capacity.  This behavior indicates  a negative  economy of  scale with
 respect to plant size.
                                      8-78

-------
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     The following explanation can be offered for this anomaly.  First
of all, the fabric filter costs represented by Figure 8-1 are functions
of the gas volumetric flowrate, not the plant capacity.  Secondly, the
cost-effectiveness ratio is also a function of the volumetric flowrate,
as well as the annual operating hours.  Now, when a model plant consists
of more than one fabric filter system, the mean cost-effectiveness ratio
for the model plant is strongly affected by the volumetric flowrates
of the individual fabric filter systems.  (The equation in Section 8.2.2
bears this out.)  For instance, if one fabric filter flowrate is much
smaller or larger than the others, the mean cost-effectiveness will be
weighted toward that flowrate.
     Such a situation is illustrated  by the data in Tables 8-25 and 8-26,
for the 270 and 540 Mg/hour model plants, respectively.  In Table 8-25,
data for two fabric filters are presented, one of which is sized for five
times  the flowrate as the other.  Accordingly, the mean cost-effectiveness
($26.7/Mg) is heavily weighted toward the larger fabric filter.  But with
the 540 Mg/hour model plant (Table 8-26), there are three fabric filters,
sized  at 255, 877, and 906 m3/min.  Since two of these fabric filters are
approximately equal  in size,  the mean cost-effectiveness for the model plant
($27.8/Mg) is weighted toward them.   Note, moreover, that this ratio is
higher than  that  for the 270  Mg/hour  plant.  This, in turn, accounts for
the dip in the  curve in Figure 8-1.
 8.2.5  Control  Cost Comparison
     Before the accuracy and representativeness of model  plant control
 costs can be ascertained,  they must be compared with costs  obtained from
                                     8-80

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other data sources.  In doing this, one can either compare the installed
capital costs, the annual 1 zed costs, or both.  However, since the capital
costs  influence the annualized costs  (via  the annualized  capital charges),
and  because there  is much more variability among the several  terms in the
annualized cost (utilities,  for  instance), it is preferable  to limit the
comparison to  the  installed  costs.
      Even for  a control  system sized  for a specific emission point, the
installed cost may vary  considerably  from  site-to-site.   Such things as
the  cost  of  installation labor  (electricians, pipefitters,  etc.),  the
requirement  for special  installation  materials  (e.g.,  extra insulation  for
systems installed  in  colder  climates),  and the  presence  or  absence of
excess utility capacity  considerably  influence  the total  installed cost.
      Keeping this  in  mind,  however, capital  cost comparisons can be made,
 among a range of  control system sizes.   This .comparison  may be made
 graphically; that is, installed "costs adjusted  to the same  reference  date
 (December 1976,  in this case) can be plotted against some technical  parameter
          •*»
 relevant to the control  system.  In this  section, installed costs are
 compared among various sizes of fabric filter systems, using gas volumetric
 flowrate as the comparison parameter.
      The  model plant  costs  are  compared with cost  data obtained  from
 industry  sources6'7 and  with costs developed in-house  from  a compendium
 of air pollution  control costs  (the GARD Manual).3  These costs  have  been
 plotted against volumetric flowrate on full  logarithmic  paper (Figure  8-2).
 For all flowrates in the domain of 42 to  1,400  actual  m3/min, the costs.
 developed from the GARD Manual  are higher than  the model plant costs.   The
 discrepancy ranges from 17 to 32 percent,  the higher difference  corresponding
                                      3-82

-------
 to  42 mVmin.  The cost curve for reference 6 intersects the model  plant
 curve at  115 m3/min.  (This is approximately the size of the grinding
 operation baghouse in the 9.1 Mg/hour model plant.)   Below this  flowrate
 the reference 6 costs are lower; above it, they are  higher, but  by  no more
 than 53 percent.  The last fabric filter cost curve  (reference 7) lies
 consistently below the model plant curve for all  flowrates  between  28 and
 1,050 mVmin.  However,  the differences between the  costs-7  to  18  percent-are
 not significant.
     All in all, the model  plant fabric filter  costs  compare  reasonably well
with the data supplied by references  3, 6,  and  7.
                                   8-83

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8.3  OTHER COST CONSIDERATIONS
     As discussed in Section 8.2, it is unlikely that non-metallic minerals
plants covered under the anticipated NSPS would be required to monitor the
opacity of their particulate emissions.  Nonetheless, for the benefit of
those plants considering an opacity monitoring program, costs are presented
for these devices in this section.
     Continuous monitoring of opacity usually involves the use of a trans-
mi ssometer installed in a fabric filter stack.  This instrument relates
the transmittance of a light beam across the stack to the opacity of
the exhaust  .  These devices are fully automatic and usually require only
periodic maintenance.  (However, manual stack testing may be required for
calibration  of the  instrument.)
     Table 8-35  lists costs for a typical opacity monitoring system
obtained from an instrument vendor.8  The system shown consists of a
visible emission monitor, controls, data readout-converter, strip chart
recorder,  and other auxiliaries.  Of  the $20,000 installed cost, half
is  the equipment purchase cost,  the other $10,000 is for installation.
 It  has been  assumed that no  scaffolding would have to be erected on the
stack being  monitored.   However,  if scaffolding  is required, the installation
 cost could increase appreciably.  The scaffolding cost would,  as expected,
 vary from site  to site.   For instance,  the  cost  of scaffolding a 50-foot
 "stub" stack (the kind normally used  with nonmetallic minerals plant
 fabric filters)  would be $20,000 to  $30,000.
                                 8-84

-------
 Table 8-35.  MONITORING COSTS FOR NON-METALLIC MINERALS  MODEL  PLANTS3 'b
Parameter
Operating factor, hours/year
Installed capital cost, M$
Direct operating cost, M$/year
Annuali zed capital charges, M$/year
Total annual i zed cost, $/year
Value
2000
20
0.7
4.1
4.8
8400
20
1.0
4.1
5.1
aReference8.

 These costs are for opacity monitoring  of one  stack.  No scaffolding
 costs are included.

cThe letter "M" denotes thousands;  "m"  denotes millions, etc.
                                 8-85

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     The direct operating costs have been computed at the 2000 and 8400
hours/year operating factors.  Here, the only cost sensitive to a change
in the operating factor is the electric power cost.  At the lower operating
factor (corresponding to the crushing model  plant) the power cost.is $100/year
against $420/year at 8400 hours/year of operation.  The rest of the direct
operating cost is for maintenance of the monitoring system, which amounts to
3 percent of the installed cost.
     The annualized capital changes have been computed assuming a ten-year
life and a ten percent annual interest rate, plus four percent of the
installed cost for taxes, insurance, and administrative charges.  Depending
on the operating factor, the total annualized cost is either $4,800 or
$5,100 per year.
     For the smaller model plants, these amounts are appreciable—one-third
of the fabric filter total annualized costs at the 9.1 Mg/hour Model Plant 1.
However, with the larger plants,  more than one baghouse would need to be
monitored.  Thus, their monitoring costs could be  two or more times the
costs in Table 8-35.   In other words, there is little or no economy of
scale in the costs  for monitoring multiple stacks.  This is so because
each stack  requires separate opacity instrumentation, scaffolding, and other
equipment.  The only savings would  result from some parts of the  installation
cost, such  as engineering.   But  these latter costs, when taken together,
generally comprise  only  a  small  fraction of the  installed cost.
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                   References for Sections  8.2  and  8.3
1.    Written communications between William M.  Vatavuk  (Economic Analysis
     Branch, Strategies and Air Standards  Division)  and  James A. Eddinger,
     (Industrial  Studies Branch, Emission  Standards  and  Engineering Division)
     Dates:  August 18,  1976; June 15,  June 30,  July  8,  1977; and February 9,
     March 17, and April 20, 1978.

2.    Nonmetallie Minerals industries Control  Equipment  Costs.   Prepared by:
     Industrial Gas Cleaning Institute (Stamford,  Connecticut).  Prepared
     for: U.S. Environmental Protection Agency, Strategies  and  Air Standards
     Division, Economic Analysis Branch (Research  Triangle  Park, North
     Carolina).  Contract No. 68-02-1473,  Task  No. 19.   February 1977.
3.
4.
5.
6.
7.
8.
Kinkley, M.L. and R.B. Neveril.   Capital
Selected Air Pollution Control  Systems.
(Niles,
                                         and Operating Costs  of
             Illinois).
     Strategies and Air
     Triangle Park, North Carolina).
                    	   Prepared by:  GARD,  Inc.
                    Prepared for:  U.S.  Environmental  Protection Agency
                   Standards Division,  Economic Analysis  Branch  (Research
                                 Contract No.  68-02-2072.   May 1976.
McGlamery, G.G.,
Desulfurization
                 et al.  Detailed Cost Estimates for Advanced Effluent
	Processes.  Prepared by: Tennessee Valley Authority,
Muscle Shoals, Alabama, under Interagency Agreement EPA IAG-134(D)
Part A.  Prepared for: Office of Research and Development, U.S.
Environmental Protection Agency, Washington, D.C.   January 1975.

Written communication between William M. Vatavuk (U.S.  Environmental
Protection Agency, Strategies and Air Standards Division, Economic
Analysis Branch, Research Triangle Park, North Carolina) and Sidney
Orem (Industrial Gas Cleaning Institute, Stamford, Connecticut).
Date: June 15, 1977.

Written communications between F.J. Rogers (Gypsum Association,  Evanston,
Illinois) and William M. Vatavuk (U.S. Environmental Protection  Agency,
Strategies and Air Standards Division, Economic Analysis Branch,  Research
Triangle Park, North Carolina).  Dates: April 29,  May 11, and July  27, 1977

Written communication between William M. Vatavuk (U.S.  Environmental
Protection Agency, Strategies and Air Standards Division, Economic
Analysis Branch, Research Triangle Park, North Carolina) and Curtis
Hamilton (Englehard Minerals and Chemicals, Attapulgas, Georgia).
Date: January 18, 1978.

Written communication between William M. Vatavuk (U.S.  Environmental
Protection Agency, Strategies and Air Standards Division, Research
Triangle Park, North Carolina) and Ronald Zweben (Lear Siegler,  Inc.,
Raleigh, North Carolina).  Date: April 26, 1978.
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8.4  ECONOMIC IMPACT ASSESSMENT
8.4.1  Introduction
     The non-metallic mineral industries crush, size, and in some cases
grind material extracted from the ground.  The resultant output is generally
used as an intermediate product in such activities as highway or building
construction.
     Although the  18 non-metallic mineral  industries considered in this
economic impact  assessment  have similar production and marketing character-
istics, there are  distinct  differences among  them.  Although these minerals
must be extracted  from the  ground,  the particular method used for extrac-
tion depends on  the hardness of  the mineral  and  the  geological  deposit in
which  it  is  found.  For example,  stone must generally  be extracted by  blasting
with dynamite, while sand  can be  extracted with  only  power  shovels.  The
harder minerals  are first  broken  with drop balls and  transported by  truck
 to the crushing  plant immediately following extraction.
      As described in Section 3.2, most minerals  then go through a  number
 of crushing steps in order to produce the requisite size material  for  the
 purposes of the customer.   This stage includes primary and  secondary crushing
 and, in some cases, tertiary crushing.   In each crushing stage the material
 is further  reduced to a smaller size classification.  These crushing stages
 are important in  producing material meeting the quality specifications of
 the application.   For some minerals; e.g., clay, dryers are interposed between
 the various crushing  stages to extract the moisture found in the material.
 Other minerals  such as stone and pumice do not require dryers, while still
 other materials,  such as sand, can  be extracted  and processed in a wet form.
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     For many minerals the final crushing stage produces an output which
 can be sold for various purposes; e.g., stone, and sand and gravel used
 as a highway or concrete aggregate.  Other materials must be further
 reduced in size in a grinding mill before they are acceptable in product
 applications; e.g., clay which is to be expanded and gypsum used as a
 retarder in cement production.
     In short, non-metallic minerals are basically processed in the same
 manner, but there are production distinctions which the following economic
 impact analysis will address.
     As Section 8.1 shows, non-metallic minerals have wide price differ-
 entials.  Even within a particular mineral, there are signifcant variations
 in price depending on product application.  The prices of non-metallic miner-
 als range from $2/ton for sand gravel to $250/ton for high grade talc.
 Most non-metallic minerals have regional markets.  In general, the lower
 the value of the mineral, the shorter is the distance that the material
 travels to a customer.  For example, stone, and sand and gravel, lower price
 minerals, generally are not transported over 30 miles from the plant.
 At this distance the f.o.b. plant price of the material is approximately
 doubled by transportation costs.  Therefore, transportation costs limit
 the geographic area of competition for many non-metallic minerals and
 competition between and among minerals is localized.
     Ownership characteristics differ between the non-metallic minerals
 industries.  Stone quarrying and crushing is done primarily by privately
held companies which may have other business ventures requiring stone;
e.g.,  highway construction or concrete,manufacturing.  Gypsum, on the other
hand,  is generally produced by diversified, publicly held companies in the

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building and construction materials industry who have integrated backwards to
the mine.  Publicly held companies, diversified into many other activities,
though, are in general the largest producers in the industries.
     In the analysis which follows, each new non-metallic mineral plant
will be assessed as if it stands alone; i.e., the plant is not associated'
with any other business activity nor is it associated with any larger
parent company.  This assumption has the effect of  insulating the control
cost impact to the  plant  in  question which must then support the control
cost without  any assistance  from other business activities or firms.
     The  impact which will be  assessed is the effect of the incremental
cost of  NSPS  control  on  both:
     •     "Grassroots" new plants
     •     Expansions  of  existing  plants.
The effect to be determined  is the feasibility  of these  two  investments,
 and therefore, the potential for new and expanded plant  construction.with
 the superimposed NSPS costs  on each investment.
      Incremental  NSPS control  costs are costs over and above those
 control costs required to meet state implementation plan (SIP) standards.
 Since each state has particulate emission control standards, any new plant
 or reconstructed/modified plant would have to meet SIP standards in the
 absence of the NSPS.  Incremental costs are the difference between the costs
 associated with NSPS control  and SIP control.  In this analysis SIP costs
 are assumed  to be  non-existent, and therefore incremental costs are the
 total of  NSPS costs.  Though  SIP costs are not zero in the real world, this
 assumption is used in order to provide a conservative analysis for evalua-
 ting economic impacts.
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     This section  is organized  in three parts.  Section 8.4.2 will develop
 the methodological procedure utilized to estimate the economic impact.  Section
 8.4.3 will present the findings of this analysis and Section 8.5 will show
 the total industry costs of the promulgation of NSPS.
 8.4.2  Methodology
     This section will describe the methodology used to measure the eco-
 nomic impact on. the non-metallic mineral industries.
     The economic  impact is evaluated by developing model plants based on
 historical characteristics in the non-metallic mineral industries.  As will
 be seen, these  characteristics  include production capabilities, asset
 size and other  financial characteristics.  The models do not represent any
 particular plant as any individual plant will differ in one or more of
 these characteristics.  The models are meant to provide an indication of
 the degree of impact on all plants in a particular industry by incorporating
 in the model  the major characteristics prevailing in each segment of the
non-metallic mineral  industry.
     Two control cost models have been constructed for the 18 non-metallic
mineral  industries, as seen in Section 6.
     •    Model  1  - those industries which generally only crush the
          mineral
     •    Model  2 - those industries which generally both crush and
          grind the mineral
 In addition,  the portable crushing plant model segments of the crushed stone,
and sand and  gravel industries  are discussed in Supplement A.
     Each industry has been further disaggregated by typical model plant
sizes to account.for size variations within each industry.  Typical plant

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sizes for each mineral are shown in Section 6.  Although industry repre-
sentatives and equipment suppliers do not expect 9 Mg/hr (10 tons/hr), 23
Mg/hr (25 tons/hr) and 68 Mg/hr (75 tons/hr) plants in the crushed stone,
and sand and gravel industries to be constructed in the future, they were,
nevertheless, analyzed because they have historically represented the^
majority of plants in the industries.
     Only minerals represented by model 2 are assumed to be in need of
expansion investment  in the near future.  Expansion will consist of
4.5 Mg/hr (approximately 5 tph) and 9.1 Mg/hr (10 tph) grinding mills.
     Expansion of  existing plants represented by model 1 is not considered
because  it is expected that they will  need  to invest  in capital expansion
to meet  increased  demand only on a sporadic basis.  Reconstruction/modifica-
tion of  existing  plants is also not  considered; first, because routine
replacement of worn out equipment will  not  subject them to the NSPS;  and
second,because such replacement is expected to occur  at a very slow pace
since  the production  life  of most processing  equipment is on the order of
20  to  30 years.
     The first step  in  the analysis  consisted of  screening each of the
18  minerals  by ranking  the potential  product  price effects of  the incremen-
tal  control  cost.  Those minerals with the  potentially highest product
price  impact were then  considered  for further evaluation.
      The next step in the  analysis  established  the scenario under which
 the plant would  operate.   This  scenario consisted of  four elements:
      •    the total  of NSPS  control  costs  were  incremental
           costs;  i.e.,  that  there  are no SIP  control  costs
           that a plant would have to incur in the absence of
           NSPS control.
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     •    the production volume, is constant throughout the
          life of the project except for the crushed stone
          plant where it is assumed that they operate at
          50% of capacity for the first year.
     •    NSPS control cost pass through is limited by competition of
          existing plants in the same industry which do not have to meet
          the NSPS.
     •    the new plant operates as a separate business entity and cannot
          expect to finance the control from another business activity or
          parent firm.
     Because of technical constraints in establishing a new quarrying
operation in the crushed stone industry, which constraints are not as
severe in.the other industries, the crushed stone crushing plant is assumed
to operate at 50% of capacity during the first year.
     The plant is assumed not to be dependent on any other business
venture.  Therefore for new plants the NSPS control cost is not allocated
or spread over any operation except production of the affected facility
which is the new plant.  Financing of the equipment can(only be made from
the expected revenues of the new plant and from no other business venture.
For expanded plants a portion of the annualized control cost was assumed to
be absorbed by the existing plant which is being expanded.
     Substitutability between many of the non-metallic minerals in many
product applications prevails in the market.  Because of the variations in
control cost per ton between the minerals, the potential  price increase of
any mineral should be expected to equal the cost pass through portion of
the nearest available mineral substitute with the lowest control cost per

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ton.  If a new plant of one mineral was being constructed in the same
geographical competitive area as a new plant of another mineral and both
were perfect substitutes for each other, then the cost pass through would
likely be the control cost of the less affected mineral.  A more conserva-
tive analysis is where a new plant of a mineral is constructed in the
same geographically competitive area as existing plants of the same mineral.
The existing plants would not experience any NSPS standard and therefore,
cost, and the new plant would have to compete with this existing plant.
The new plant would not be a major supplier of the mineral in the area and
would not be able to control the price.  Therefore, this new plant would
have to completely absorb the control cost.  But as demand grew for the
mineral, additional new plants would be required and/or, in the case of gypsum
and clay, older plants would have  to expand to meet the increased demand.
This condition would bring an increasingly larger segment of the mineral
supply market under NSPS control.  Therefore,  it is likely that new plants
will be able to pass through the control cost  gradually over the years.  This
is  reflected in our  assumption  that  25  percent of the  control  cost is  passed
through every 4 years  (alternatively every 4 years 25  percent  less of
the cost  is absorbed).  This is  the  premise which is used  in the succeeding
discounted  cash flow (DCF)  analysis.
     Each  plant size of each of the  potentially  significantly  affected
minerals was  then  analyzed  by  using  a  discounted cash  flow  analysis  (DCF).
DCF is  an  investment decision  technique which  provides information on
 tne economic feasibility of a  potential capital  investment.   It measures
 the discounted  cash  inflows  over the life  of  the  investment  and compares
      to the discounted cash outflows.   If  the  sum of the  discounted  cash

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inflows is equal to or greater than the sum of the discounted cash outflows,
the investment is feasible from the firm's point of view.  If the sum of
the discounted cash inflows is less than the sum of the discounted cash
outflows, the investment is not feasible from the firm's point of view.
In order to take into consideration the time value of money, all cash
flows must be discounted to the present by use of an appropriate discount
factor.  This is necessary to bring all cash flows to a comparable present
day basis for comparison.
     Four data elements are required to complete the analysis:
     •    Expected life of the investment
     •    Cash flows to be discounted
     •    Weighted average cost of capital
                                                   /
     9    Total plant investment.
     The expected life of the investment was taken to be 20 years although
the expected life of the major pieces of equipment can range from 20 to 30
years.  The cash flows are discounted and summed over a 20 year period.
     Any potential capital investment will generate cash flows in the
form of new earnings, and depreciation.  These flows are discounted by the
weighted average cost of capital discount factors, summed, and compared to
capital outlays to determine the economic feasibility of the potential in-
vestment.  In the analysis to be presented in the following section the
incremental NSPS control costs are superimposed on this model to determine
their effect on cash flow and the decision to invest in a new "grassroots"
or expanded plant for each size plant in each of the affected non-metallic
mineral industries identified for further analysis.
                                    8-95

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     The cash flows which are considered are:
     1.   Net earnings before interest and after tax.
     2.   Depreciation of the plant including control equipment.
     3.   Depletion.
     4.   Working capital recovery.
     5.   Plant and control equipment investment.
     For each year cash inflows 1 through 4 are added (working capital
recovery occurs only at the end of the life of the investment, the 20th
year).  This resultant annual sum is discounted and the annual discounted
sums are totalled over the 20 year period.  This new sum is compared to
the discounted sum of the total investment including NSPS control invest-
ment.  If the sum of the discounted cash inflows 1 through 4 is larger than
the discounted sum of cash outflow 5, the investment is economically
feasible even after the requirement of NSPS controls.
     That an investment is found to be economically feasible does not
necessarily mean that the investment will be made by any individual firm.
Other  forces or market concerns important to the company such as the desire
to diversify into other industries, or desire to expand through acquisitions
may preclude the new plant investment from being made.
     The discount factors which are used to discount these flows are
determined by solving I/O + i)n where i is the weighted average cost of
capital and n is the year from the beginning of the project.  In this case
n is from 1 to 20.  For each year of the 20 year investment span a different
discount factor is generated.  Each year's discounted cash flow shows the
present value of that cash flow.  The cost of capital is the weighted
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average financing expense of an investment that is financed partly through
debt and partly through equity.
     Total plant investment was determined by the equipment needed for
quarrying, crushing, and, if appropriate, drying and grinding the mineral,
and added to the required NSPS control equipment capital  cost developed in
Section 8.2 and working capital requirements.
8.4.2.1  Critical  Elements
     The following list provides the major critical  elements of the
analysis for the significantly impacted industries:
     •    Control  cost absorption is 25 percent less every 4 years.
     •    Maintenance expenditures over the life of  the equipment
          equal  salvage value of the equipment.
     •    The profit rate for new plants is the same as existing
          plants.
     •    All  stationary plant equipment has a 20 year life with  "
          the exception of rolling stock which has a 7 year life.
     •    8,400  hours of operation per year is assumed for plants
          with grinding capacity.
     •    Cost of  debt capital  is  3 percent above the prime rate of
          7  percent  in 1976.
     •    The  total  investment is  financed  30 percent by debt  and
          70  percent by equity capital.
     •    Weighted average cost of capital  is 11.8 percent.
     •   The  debt financing  maturity  is  10 years  for stationary
          plants and control  investment and 7 years  for rolling
          stock.
     •    Rolling stock is 77.7 percent of  quarry  investment.
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     Maintenance expenditures are a cash outflow over the life of the
equipment while the salvage value of the equipment is a cash inflow at
the time of sale.  No estimates of maintenance expenditures were found
during this analysis.  Salvage value of equipment generally runs from 25
to 30 percent of the original cost.  Since maintenance expenditures ate
a negative cash flow and salvage value a positive cash flow and since
salvage value at the time of sale should be related to the amount of
maintenance put into the equipment it is assumed that they are equal
and counterbalance each other.
     The profit rate on the  new  plant is assumed to be equal  to an
existing plant although profit rates between  a  new and existing plant
will differ due to unique tax  consequences and  differences in technolo-
gical efficiencies.  It is felt  that these two  effects counterbalance
each other sufficiently for  the  purpose  of this analysis.
     The  plant  has a useful  life of 20 years.   Equipment life varies  among
the pieces of equipment used in  the non-metallic mineral  industry,  but,  on
average,  the  plant has a  20  year life.   In the  analysis  some  account has
been given to this aspect by separating  "rolling  stock"  (mineral  transport
 vehicles)  from stationary stock  equipment  and^ ascribing  a 7 year life to
 the rolling  stock.
      In those industries  with grinding capacity,  8,400 hours  of operation
 is used to generate  sales volume and  revenue based on information supplied
 by industry.
      Industry representatives have stated that generally an investment
 can be financed at 2 to  3% above the  prime rate.   A 3% above  prime rate
 was utilized to reflect a conservative analysis.

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     A weighted average cost of capital for the mining industry as a whole
of 11.8% and debt/equity financing of 30/70% is given by Dr. Gerald
Pogue (Section 8.4.2.2).  To the extent that particular non-metallic mineral
industries within the mining category experience a cost of capital of more
or less than 11.8%, the discounted cash flows will be different.
8.4.2.2  Data Sources
     The following list provides the data sources for various aspects
of the analysis:
     •    Average Selling Price -  Bureau of Mines
     •    Profit  Rates          -  Robert Morris Associates
                                -  Industry Representatives
                                -  Annual  Reports
                                -  Robert Morris Associates
                                -  Barber-Green  Co.
                                -  Kennedy  Von Saun  Co.
                                -  C. E.  Raymond - Combustion  Engineering
                                  Inc.
         Cost of Debt Capital   -  Federal  Reserve Bank
                                -  Industry Representatives
         Cost of Capital,       -  "Estimation of the Cost of  Capital  for
         Debt to Equity Ratio    Major U.S. Industries with  Application
                                 to Pollution  Control Investments",  Dr.
                                 Gerald A. Pogue, 1975.
         NSPS Control Costs,   - Chapter  8.2
         Sizes and Operating
         Hours
*
•
Working Capital
Plant Investment
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     •    Depreciation Schedules - Equipment Suppliers
     •    Investment Tax Credit, - Internal Revenue Code
          Depletion Allowance
     •    Expected Life of       - "Background Information
          Equipment                for the Non-Metallic Minerals
                                   Industry," Vol. I, PEDCO Environ-
                                   mental Specialists.
8.4.3  Screening Analysis
     The first step in the analysis was to assess the effect on the 18
non-metallic mineral industries of NSPS control costs based on the ratio of
control cost per ton to price per ton.  This ratio represents annualized cost
per ton as percent of average price.  Table 8-36  presents the results of
this analysis.
     Table 8-36 shows 23 entries because clay has been disaggregated into
6 distinct categories.  For both those industries that fall under the Model
1 classification (crushing only) and Model 2 classification (crushing and
grinding) the impact is shown by dividing  the annualized operating and
capital costs for  control of the smallest  size plant  specified in Table
6.3 by the annual  revenue of the mineral.
      Because control costs per  ton of mineral output  are larger for the
smallest  plant  compared to the  largest plant, this procedure inflates the
impact.   Since  large plants dominate the production  in most industries,
average industry  impact based on  this ratio would be  substantially lower.
Average industry  impact is shown  in  section 8.5.  Table  8-36 is not meant  to
show  industry  impact  but  to  be  used  as  "worst case"  screening method to
ascertain industries  requiring  further  study.

                                     8-100   '

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                               Table 8-36


                        RANK ORDER OF INDUSTRIES

Industry
Pumice
Sand and Gravel
Crushed Stone
Common Clay
Gypsum
Per lite
Fire Clay
Bentonite
Ball Clay -
Salt
Barite
Feldspar
Fuller's Earth
Mica
Kaolin
Talc
Kyanite
Vermiculite
Fluorspar
Di atomi te
Sodium Compounds
Boron
Gilsonite
WITH HIGHEST CONTROL COST IMPACT
Rank
1
2
3
4
5
6
7
9
10
11
12
13
14
14
14
17
18
18
18
18
22
23
25

Control Cost/Ton
Price/Ton u)
28.0%
15.8
13.4 Candidates
11.7 for further
5.0 evaluation.
4.1
2.0
1.4
1.3
1.2
1.1
1.1
.6
.6
.6
.4
.3
.3
•3
.3
.2
.1
-(2)
(1) Based on smallest model size in industry.

(2) No price available - only 1  company producing approximately
    100,000 tpy.
                                   8-101

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Any industry where the per ton control cost was larger than 2% of the average
price was considered to be potentially significantly impacted and worthy of
further evaluation.  Two percent was taken to be the cut-off point because
this rate, even in the worst case situations, is considerably lower than
the 5% industry average rate which is the EPA guideline for assessing major
economic impact.  The minerals considered to be potentially significantly
impacted are pumice, sand and gravel, crushed stone, common clay, gypsum,
and perlite.
     Perlite, gypsum and pumice have  three stationary model plant sizes:
9, 23 and 68 Mg/hr  (10, 25 and 75 tph).  Common clay has four; 9, 23, 68
and 136 Mg/hr (10,  25, 75 and 150 tph).  Both sand  and gravel, and crushed
stone have  six  stationary model plant sizes, 9, 23, 68, 136,  272 and 544
Mg/hr (10,  25,  75,  150, 300 and 600 tph).  The portable plant segments of the
crushed stone,  and  sand and gravel industries are discussed in Supplement A.
      Each of the six  remaining  potentially significantly affected miner-
 als  were  then compared on  the basis  of  relative prices, and  the  effect  of
 control  costs on relative  prices  of the minerals,  taking into account the
 product substitutability  among  them.  This analysis showed that  the  "worst
 case" situation was a new  plant of any  mineral  competing with an existing
 plant of the same mineral.   For each mineral,  a baseline relative price was
 computed.   This relative  price was the  ratio of the price  of each mineral
 to the price of each of the other minerals prior  to NSPS control costs.
 This baseline relative price ratio was  then compared to the "worst case"
 situation after the imposition of control  costs,  assuming  all control  costs
 were passed through.   The "worst case"  situation  was the  smallest size
 plant of any mineral  compared to the largest size plant of the remaining
                                     8-102

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 minerals since control costs per ton of output are larger for smaller
 plants.   A decline in this ratio, price of other minerals after control
 divided  by the price of this mineral after control, indicates that other
 minerals are becoming less expensive relative to this mineral and that
 demand should significantly shift away from this mineral  if the cross-
 elasticity of demand is high.1   Cross-elasticity of demand is dependent  on
 the minerals having acceptable  substitutability potential.  The substitutability
 potential  was evaluated by comparing the mineral  of interest to the two
 minerals having  the largest changes  in relative prices.   In each case sub-
 stitutability potential  was rated only low to moderate because  of the
 product  quality  differences between  the minerals  and  the  geographical
 separation  of deposits  of  different  minerals.   For  this reason  the more
 conservative scenario,  a new plant of  any mineral competing with -an existing
 plant  of the same mineral,  was  employed in the  analysis.
 8.4.4  Plant Investment
       Grassroots Plants
     Investment costs were  gathered  for quarrying, crushing,  and where
 appropriate, drying and  grinding  equipment from equipment  suppliers.
Tables 8-37  and 8-38 show the total  investment costs  for each size  plant
 studied  in each industry.   For all plant sizes smaller than  136  Mg/hr  (150
 tph), quarrying and crushing plant costs were derived by use  of  the engineer-
 ing 0.6 power capacity rule.  For the quarrying operation,  rolling  stock was
1
 Cross-elasticity of demand is the percentage change in the quantity of
 one product divided by the percentage change in price of another
 product.
                                    8-103

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                                              1
                              Table 8-37
                        PLANT INVESTMENT COSTS
                      (in thousands of dollars)
Size
Mg/hr (tph)
Industry
Pumice
9
(10)
$269.9 $
23
(25)
410.4 $
68
(75)
740.3
136
(150)
N.A.
272
(300)
N.A.
544
(600)
N.A.
Sand
       Gravel  236.9     374.4     693.2  $1,034.6  $2,036.1  $3,986.7
Crushed Stone  251.1     399.6     742.9   1,139.0   2,188.6   4,291.4
Common Clay    817.4   1,282.3   2,160.4   3,118.1     N.A.
Gypsum
Perlite
               664.9    1,058.3    1,850.2      N.A.
                555.3      822.2    1,654.1      N.A.
                                                       N.A.
                                                        N.A.
                                                                 N.A.
N.A.
N.A.
Includes NSPS control capital costs and working capital.
N>A'Not Applicable because plants of this size are not likely to  be
    constructed in the absence of a NSPS.
                                 8-104

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 Industry
                               ,   Table 8-38

                           EXPANSION INVESTMENT CQSTSl



                            (in thousands of dollars)
                                             Size
                                         Mg/hr (tph)
  4.5
  (5)
  9
(10)
 Common  Clay


 Gypsum
$288.1


 292.9
 $421.1


  430.7
Includes NSPS control costs and working capital,
                                  8-105

-------
separated from stationary stock by factoring total quarry investment cost
by 0.777.1  All plant investment costs were deflated to fourth quarter,
1976 prices in order to make investment consistent with the derivation of
sales revenue which is based on fourth quarter, 1976 average selling
                                                                      tt
prices.  The investment deflator was calculated from the Chemical Engineer-
ing equipment  cost  index.
     Once  total  plant  investment was calculated and separated  into  sta-
tionary  plant  equipment  and  rolling stock,  NSPS control  cost  investment
and working capital were added to  stationary  stock  investment.   The debt
portion  of the stationary stock investment was derived by  using  a 0.3  factor
specified by the Dr.  Gerald  Pogue  study;  i.e., 30%  of  investment financed
by the bank and 70% from the investor's  own funds,  equity.  Bank financing
 for stationary stock  debt was taken by 10%, 10 years,  giving a capital
 recovery factor (CRF) of 0.16275.   These industries are usually able to
 receive financing at 2 to 3% above the prime rate.   In T976 the prime
 rate was approximately 7%.  The debt portion of rolling stock investment
 was also established by  using  a 0.3 factor.  The rolling  stock was assumed
 to be financed  at  10% over  the useful life of the stock,  7 years.   The CRF
 is 0.20541.   Subsequent  purchase  of new  rolling  stock to  replace original
 rolling stock was  assumed to  occur at the  same price.   For both stationary
 and rolling  stock, the  annual  principal  and  interest  payment  were  calculated,
  1
Derived from "The Crushed Stone Industry:   Industry Characterization
and Alternative Emission Control Systems", Arthur D. Little, Inc.
where rolling stock equals 77.7% of total  quarry plant costs.
                                   8-106

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       Expansion Plants
     Investment costs for expansions consisted of 4.5 Mg/hr (5 tph) and 9 Kg/hr
(10 tph) grinding mill costs for the clay and gypsum industries only.  These
investment costs are shown in Table 8-38.  Debt financing was 30% of total
investment at 10% over 10 years.
8.4.5  Discounted Cash Flow Analysis
     Table 8-39 which shows an analysis for construction of a new 136 Mg/hr
(150 tph) crushed stone plant is an example of the data sheets which were
developed for each of the plant sizes for each of the six potentially
significantly impacted industries.   The steps in the DCF analysis will  be
described below using this example and referring to row entries in Table 8-39.
     •    Row 1, revenue, was generated by multiplying hours of operation
          by tons per hour of output and by the average P.O.B. plant sell-
          ing price of the output.   This revenue estimate was assumed con-
          stant for each year of the life of the investment.  For stationary
          crushed stone plants,  the plant was taken to operate at 50?- of
          capacity the first year as related by industry representatives.
          Control  equipment was  assumed to be operating; at 100 percent,
          and therefore control  operating costs are 100 percent.
     •    Row 3, interest including control, was determined by calcula-
          ting the principal  and interest repayment schedule for  the
          plant investment without control investment.
     •    Row 4, earnings before interest and tax, was derived by multi-
          plying revenue by the  before tax. profit rate of row 2 and
          adding back the interest of row 3.
                                    8-107

-------
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           • •«>. -*m  r>. n  «•
                                             .J>
                                            _;.
                                                       s
                                                       •  •
                                8-108

-------
          Row 5 shows the NSPS annualized control costs for each year.
          Since depreciation for control equipment was taken to be
          straight line over 10 years, the years from 1987 onward show
          only annual operating costs.
          Row 6, control cost absorbed, reflects the scenario mentioned
          in Section 8.4.2, methodology.  For the first 4-years all
          control cost is assumed to be absorbed because the plant is
          competing with existing established plants which have no NSPS
          costs.  Therefore, the new plant must absorb the entire cost.
          In the years 1981 to 1985 the plants must absorb 75% of the
          cost and can pass through 25% because other new plants are
          being established.  New plants must, then, meet NSPS costs.
          For each succeeding 4 year period, the plant absorbs 25%
          less of the original  cost.   Since in the year 1987 total
          operating costs are less than control cost absorbed in 1986, all
          operating costs are assumed to be passed through in the years
          from 1987 to 1996.                       ...
          Row 7, control interest, was derived by calculating the prin-
          cipal  and interest repayment schedule for the NSPS control,
          investment.
1
 The increased revenue from cost pass through is not shown since we
 are only interested in the effect of cost absorption on net earnings,
                                    8-109'

-------
Row 8, net earnings before interest and after control, shows
                                        •^
the effect of NSPS absorbed control costs on the earnings
potential of the plant.  Absorbed control costs are subtracted
from Row 4 and control interest of Row 7 is added back.  Adding
                                                               s
back of interest is required in the model because the discount
factors taken into consideration the repayment of the loan.
Row 9, federal tax liability, is derived by multiplying net
earnings after control by the appropriate marginal tax rates.
Row 10, investment tax credit, considers the effect of the 10%
investment tax credit on the tax liability of the plant.
(The investment tax credit can be  carried forward 7 years or
until 10% of the investment is credited, whichever comes first.
The tax credit cannot be greater than tax liability and for tax
liabilities over $25,000 the credit is calculated as  $25,000
plus 50% of the liability over $25,000.  For example,  in year
1977 tax liability is $800, therefore, the credit is  $800 since
the credit cannot be  greater than  tax liability.  In  year 1978
the same reasoning applies.  If tax liability had been $30,000,
then  the credit would have been $25,000  +  (0.5)  $5,000 or $27,500.
Row 11,  federal tax  liability  after credit,  is  tax liability
minus the  investment  tax  credit.
Row 12,  minimum tax,  shows the 15% minimum tax  on tax prefer-
ence  items.   In this  analysis  the  only  tax preference item  is
the depletion  allowance.
Row 13,  state  tax,  is assumed  to be 5%  of  net earnings.  The
5% rate  is  the most  common rate of the  majority of states.
Row 14,  net earnings  before  interest  after  credit, control  and
 tax,  shows  the effect of NSPS  control  costs  and the  investment
 tax credit on  after  tax earnings.   It is derived by  subtracting
                            8-110

-------
  federal  tax  liability  after  credit, the minimum tax and state
  tax,  from  Row  8.  As can be  seen, this figure varies over the
  years  as control cost  absorbed is lowered and as the original
  tax credit is  exhausted and  credit for new rolling stock is
  taken  and  exhausted and as interest payments are reduced.  Net
  earnings before interest after credit, control and tax is the
  first  category of our  cash flow.  All succeeding categories
  also affect  cash flow.
  Row 15 is  added to Row 14 and represents depreciation of
  stationary stock, depreciated straight line over 10 years.
  Row 16, depreciation of rolling stock, is added to the above.
  This depreciation, which is taken over 7 years, comes into
  play in later years as new rolling stock is purchased in
 years 1984 and 1991.
  Row 17, depreciation  of control  equipment, is taken over 10
 years  and added to the other depreciable equipment.
 Row 18, depletion,  is  added to the cash  flow since all  of
 these  industries  are  in the mining classification  and deple-
 tion allowance increases cash flow.
  (Depletion  can be  taken in  one of two  ways:   cost  depletion or
 percentage  depletion.   Cost depletion  is  dependent on the cost
 basis  of the  land,  amount of mineral mined and  estimated amount
 of mineral  reserves.   Percentage  depletion is based  on  a
 specified percentage of sales revenue, the percentage differs
 by industry,  to a  maximum of 50%  of  taxable  income before
 depletion is  counted.   Cost depletion  cannot  be  calculated  here
 because it  is site  specific;  i.e., dependent  on  the  cost of the
'property and  reserves  on the  property.  In any  case,  most
 companies generally use percentage depletion.   In  the example
 depletion is  shown as  $2,000  in  1977.  The percentage depletion
 allowance for stone is  5%.   For 1977 this  amounts  to  $17,600,
 but the plant can  only  use  $2,000 because  of  the 50%  taxable
 income limit.)                             .
                            8-113

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    •    Row 19, working capital  recovery, shows that at the end of the
         project working capital  is  recovered.  Working capital is taken
         to be 4%  of  revenue.
    •    Row 20, cash inflow,  shows  for  each year  the expected  total of
         the above cash flow categories,  and is the  amount which must be
         discounted to the present by the discount factors shown in row
         21.  Row  22  is the result;  i.e., Row  20 multiplied by  Row 21.
    •    Row 23, cash outflow, shows the investment  expenditures necessary
         to establish the  operation.  Investment of  $1.1 million is made
         initially and subsequent rolling stock  investment is made in
         years  1984 and  1991.  These cash outflows are  discounted by  the
         appropriate  discount factors of Row 21.   Row 24  is  the result.
    The weighted average  cost of capital of 11.8%  generates  the discount
factor for  each  year of the 20 year period.  These  factors  show  the present
value  of a  dollar of future cash flow for each  future year.   After the
annual  cash flows are discounted, they are summed to derive  the  present
value of the cash inflows  over the life of the project.  This  cash inflow
is then compared to the cash outflow, which is the  present value of the
total  investment.   In this example the present value of net cash inflows
is greater than the present value of cash outflows, so that an investment
in a 136 Mg/hr (150 tph) crushed stone plant with NSPS controls  attached  is
profitable at a weighted average cost of capital  of 11.8%.
8.4.6  Findings
     Table 8-40 presents the results of this analysis for each size  plant
of the potentially  significantly affected industries.  For the 9 and  23
Mg/hr (10 and 25 tph)  sand  and gravel, and crushed stone plants  the  DCF
                                      8-112

-------
                                   Table  8-40

                             SUMMARY OF DCF RESULTS

                                Grassroots Plants
                               Investment Decision
     Industry

     Pumice
      Size  -  Mg/hr  (tons per hour)
  9    23     68~136    272"    5PT
(10)   (25)    (75)   (150)   (300)   (600)
 NF
N.A.   N.A.   N.A.
     Sand  & Gravel    NF1   NF1     A1   F
     Crushed Stone   NF1   NF1     A1   F
     Common Clay     NF     A      F    F     N.A.   N.A.
     Gypsum
               F    N.A   N.A.   N.A.
     Perlite
                    N.A.  N.A.   N.A.
1.   Equipment suppliers  and industry representatives  do  not expect
    plants of this  size  to be constructed  even  in  the absence of
    NSPS.

Key:     F - economically feasible to construct
        NF - not economically feasible to  construct
         A - ambiguous
      N.A. - Not Applicable because plants of this size  are not
             likely to be constructed in the absence  of  NSPS.
                                     8-113

-------
analysis indicates that the investment is not economically feasible.   The
same result holds for the 9 Mg/hr (10 tph) common clay plant.
     For the 68 Mg/hr (75 tph) sand and gravel, and crushed stone plants, the
23 Mg/hr (25 tph) common clay plant and the 9 Mg/hr (10 tph) gypsum plant, the
DCF analysis showed negative discounted cash flows ranging from less than 2%
of total investment for common clay to approximately 16% for gypsum.  An
internal rate of return (IRR) was calculated for each of these four model
plants.  The internal rate of return is that rate which makes the discounted
cash outflow.  The IRR varied from approximately 8.5% for gypsum to slightly
less than 10% for common clay.  Since the net discounted cash flows were only
slightly negative; i.e., the IRR was fairly close to 11.8% cost of capital,
small changes in the parameters of the worst case analysis would produce
positive net discounted cash flows.  For  this reason the 68 Mg/hr (75 tph)
sand and gravel, and crushed stone plants,  the  23 Mg/hr (25 tph) common  clay
plant and the 9  Mg/hr  (10  tph) gypsum plant are determined  to be economically
feasible to construct,  if  the conservative  assumptions used throughout this
report  are  relaxed.
     Table  8-41  shows  the  results of the  DCF analysis on expansions of 4.5
and 9 Mg/hr (5  and  10  tph)  grinding  capacity in the  common  clay  and gypsum
industries.  In the  analysis  the expansion  was  assumed to take place  in  the
smallest size existing plant; i.e.,  9 Mg/hr (10 tph),  in order to provide a
 "worst  case"  situation,  the  control  costs  were assumed to  be spread  over both
 new and existing output based on  the ratio  of  new to existing output.  As is
 shown  in Table  8-41,  all expansion  size  plants  except the 4.5 Mg/hr (5 tph)
 common  clay plant were determined  to be  economically feasible to construct.
                                    8-114

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                               Table 8-41
                         SUMMARY OF DCF RESULTS

                               Expansions
                           Investment  Decison



INDUSTRY
Common Clay
Gypsum
Size
Mg/hr (tph)
4.5 ' 	
(5)
A
F


9
(10)
F
F
Key:  F - economically feasible to construct

      A - ambiguous
                                   8-115

-------
     It should be kept in mind that because an investment is found to be
economically feasible from a DCF analysis it does not necessarily mean
that the investment will, in fact, be made by a company.
     NSPS control costs will not significantly affect those non-
metallic mineral industries for which a DCF analysis was not performed.
As seen in Table 8-36 the greatest potential NSPS control cost absorp-
tion is less than or equal to 2% of product price, since these non-metallic
minerals all have a higher product price than those non-metallic minerals
for which a DCF analysis was performed.  The process economics are similar
for both industries for which a DCF analysis was performed and for which a
DCF analysis was not performed.  Since the DCF analysis was favorable for
industries whose potential control cost absorption was equal to or greater
than 4% of product price, the DCF analysis will be favorable for industries
where  this ratio was equal to or less than 2%.  For this reason a DCF
analysis performed on each of those 17 non-metallic minerals excluded from
further consideration in  Table 8-36 would show an economically feasible
investment decision  for  all  size new plants.
   .  Crushing  and grinding  facilities are also a portion of production
operations whose final output is not a specific type of  non-metallic
mineral,  such  as at  lime  and power plants;  i.e, crushing and grinding are
intermediate  processes  in these  industries.
     These  intermediate  processing facilities  are usually  constructed
by firms  in  the above mentioned  industries  because  the  need for  the
non-metallic  mineral  is  large enough  to  support  such a  facility.  Such
                                    8-116

-------
 intermediate facilities can produce the requisite size mineral at a
 lower cost to the firm than can be attained from buying the mineral from an
 independent producer.  Consequently, some cost increase could be sustained by
 intermediate processing facilities and still  permit them to be competitive
 with firms that purchase the requisite size material  from independent
 producers.  Furthermore, the intermediate processor is able to spread
 the incremental  cost over a final  product whose selling price is larger
 than that of the non-metallic mineral  input,  and,  thus can more readily
 pass on  these costs.   Finally, because of their affiliation with larger
 companies, these facilities would  tend to ha.ve a lower cost of capital.
 Therefore, the investment decision resulting  from  the  DCF analysis  for
 various  plant sizes  in the non-metallic mineral  industries per se would
 likely hold  for  intermediate processing facilities  (that  are part, of
 other facilities).
 8.5  POTENTIAL SOCIO-ECONOMIC  AND  INFLATIONARY IMPACTS
 8.5.1  Industry  Cost  Totals
     Table 8-42  presents  the upper limit  to the  number of typical new
 plants which  will be  constructed in  each  industry in each  of 5 years
 based on  projected industry  growth and  the typical plant size  in each
 industry.  The projections of  new  plants  required is based on growth  from
 1975 production statistics and assumes  that 1975 production  equals capacity.
To the extent that actual production was  lower than capacity production,
the number of estimated typical size plants required each year will be
lower.  Therefore required total industry annualized control costs will  be
lower.
                                     8-117

-------
     Table 8-43 indicates the cumulative annualized industry capital  and
operating costs in 1976 dollars to meet the NSPS standard.  The totals are
derived by multiplying the estimated number of typical plants to be con-
structed in each year by the annualized control costs for these size plants.
As can be seen, the crushed stone industry would have the largest annualized
costs by the fifth year, $19.2 million.
     Table 8-44 shows the average annualized cost per ton of output in the
fifth year after control.  These figures are based on the estimated cumu-
lative annualized costs  in the fifth year, Table 8-43, divided by the estimated
total industry production in the fifth year.   Kyanite shows the largest
industry cost per ton of $0.137 per ton.  Table 8-44 also shows that control
cost per ton as a percent of price per  ton is  highest for pumice, 1.7%.
     New regulations  shall be  considered a major action  if  "additional
annualized cost of  compliance,  including capital charges (interest and
depreciation), will  total $100 million  (i) within  any one of  the  first
 5 years  of implementation,  or (ii)  if applicable,  within any  calendar   .
year up  to the date by which the  law  requires  attainment of the relevant
 pollution standard,"  or "total  additional  cost of  production  of any major
 industry product or service will  exceed 5  percent  of the selling price  of
 the product."   Total  industry annualized control cost in the fifth year
 after promulgation of NSPS  and control  cost as a percent of selling  price
 are lower than the guidelines set for these measures of $100 million
 for annualized capital and operating expense and 5 percent, respectively.
                                       8-118

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 TABLE 8-42  ESTIMATED NUMBER OF TYPICAL NEW PLANTS REQUIRED TO
             MEET PROJECTED PRODUCTION*
Industry
Pumice
Sand and Gravel
Crushed Stone
Common Clay
Gyps in
Perl i te
Rock Salt
Sodium Compounds
Talc
Ban te
Boron
Fluorspar
Feldspar
Di atomi te
Vermiculite
Mica
Kyanite
Gilsonite
Typical
size
(Mg/hr)
9
272
272
23
23
23
68
23
9
9
272
9
9
23
68
9
9
9
Growth
rate
(%)
3.5
1.0
4.0
3.5
2.0
4.0
2.0
2.5
4.0
2.2
5.0
3.0
4.0
5.5
4.0
4.0
6.0
-
1980
2
14
72
10
1
-
2
-
-
-
-
-
- "
-
-
-
-
-
1981
2
14
75
10
1
1
2
1
1
-
-
-
'
-
-
-
-
. -
1982
2
14
78
10
1
1
3
1
1
1
-
-
1
1
-
-
-
-
1983
2
14
81
11
1
-
3
1
-
-
-
-
-
-
-
-"
-
-
1984
2
15
85
11
1
1
3
_
1
_
.'
1
'
-
1
1
1
-
n
Whenever the  projected  production  for  a  given year was not
enough  to justify  the building  of  a  new  typical size plant, no
new plants were  assumed to  be built.
                            8-119

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TABLE 8-43  ANNUALIZED CAPITAL AND OPERATING CONTROL
            COSTS FOR NEW PLANT CONSTRUCTION
Industry
Pumice
Sand and gravel
Crushed stone
Common clay
Gypsum
Perlite
Rock salt
Sodium compounds
Talc
Barite
Boron
Fluorspar
Feldspar
Di atomi te
Vermi cul i te
Mica
Kyanite
Gilsonite
Total
Annual i zed cost
(in thousands of dollars)
1980 1981
42.4 84.8
777 1 ,554
3,996 8,158.5
234 468
23.4 46.8
16
46.8 93.6
23,4
21.2
-
-
-
-
-
-
-
-
-

1982
127.2
2,331
12,487.5
702
70.2
32
163.8
46.8
424
21.2
-
-
21.2
23.4
-
-
-
-

1983
169.6
3,108
16,983
959.4
93.6
32
234
70.2
42.4
21.2
-
-
21.2
23.4
-
-
-
-

1984
212.0
3,940.5
21,700.5
1,216.8
117
48
304.2
70.2
63.6
21.2
-
21.2
21.2
23.4
23.4
21.2
21.2
-
27,825.6
                          8-120

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TABLE 8-44  ANNUALIZED CONTROL COST PER TON OF INDUSTRY
            OUTPUT IN 5TH YEAR AND CONTROL COST AS PER-
            CENT OF SELLING PRICE

Industry
Pumice
Sand and gravel
Crushed stone
Common clay
Gypsum
Perl He
Rock salt
Sodium compounds
Talc
Barite
Boron
Fluorspar
Feldspar
Diatomite
Vernriculite
Mica
Kyanite
Gilsonite
ton£?t£St An™alized cost/ton
v r§\ * price/ton
0.043
0.005
0.018
0.019
0.01
0.051
0.017
0.012
• 0.049
0.014
-
0.123
0.023
0.026
0.052
0.116
0.137
-
1.7 %
0.2
0.8
0.9
0.2
0.3
0.1
0.03
0.1
0.1
-
0.1
0.1
0.03
0.1
0.3
0.2
-

   Based on 1976 average F.O.B.  mine selling price
   and 1978 production figures.
                         8-121

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                   APPENDIX A



EVOLUTION OF THE BACKGROUND INFORMATION DOCUMENT
                      A-l

-------
      TABLE  A-l.    EVOLUTION  OF  THE  BACKGROUND INFORMATION  DOCUMENT
  Date
            Company, consultant or agency
                                                  Location
                                                                            Nature of action
04/30/73  Arizona  Portland Cement
          Ideal  Ceneot
          Albuquerque Gravel Products

09/13/73  Harry  T.  Campbell and Sons
          Texas  Plants

10/13/73  Nello  L.  Teer Company
01/16/74


02/13/74



05/28/74

   to
05/31/74
05/14/74

   to
05/15/74

06/03/74
          Paul L1me Plant, Inc.
          Arizona Portland Cement Co.

          Ideal Cement Co.
          Albuquerque Gravel Products,  Inc.
          H.G. Fenton Material Co.
RHHto, Ariz.       Presurvey two sources.
Tljeras, N.  Hex.     Inspect haul  road fugitive dust control
Albuquerque, N. Hex. technique.

Texas, Md.           Measure visible emissions from the
                    asphalt batch plant.

Raleigh, N.C.        Inspect stone processing and quarrying
                    operations.

Douglas, Ariz.       Presurvey two quarries and stone pro-
RW1to, Ariz.       cesslng plants for partlculate testing.

Tljeras, N.  Mex.     Inspect crushed stone plants
Albuquerque, N. Hex.
San Diego,  Calif.
          Essex Bituminous Concrete Corp.     Dracut, Mass.
          Essex Bituminous Concrete Corp.
          Blue Rock  Industries
          Lynn Sand  and Stone Co.
          Massachusetts Broken Stone Co.

          Kentucky Stone Co.
          Caldwell Stone Co.

          Arizona Portland Cement Company
Peabody,  Mass.
Westbrook,  Maine
Swampscott, Mass.
Weston, Mass.

Russellvnie, Ky.
Danville, Ky.

RllHto, Ariz.
                    Presurveys of five crushed stone plants
                    for testing
06/02/74  Arizona Portland Cement Company    RIllUo, Ariz.
08/06/74  General Crushed Stone Co.
  to      Pennsy Supply Inc.
08/08/74  J.  M. Brenner Stone Co.

09/16/74  Essex Bituminous Concrete Co.


10/28/74  Kentucky Stone Co.
Quakertown,  Pa.
Harrlsburg,  Pa.
Lancaster, Pa.

Dracut, Mass.


Russellvllle, Kv.
11/19/74  J.  M.  Brenner Co.                 Lancaster


12/27/74  Essex  Bituminous Concrete Co.
                     Presurveys of two crushed stone plants
                     for testing.
                    Conduct emission  tests for oartlculate
                    emission

                    Test report for partlculate emission
                    testing.

                    Presurveys  for partlculate emission tests.
                                                                Trie report of emission tests  on stone
                                                                crashing operations.

                                                                ~'-ts  conducted for process  and fugitive
                                                                       test of two baghouse operations
                                                                     -isned stone plant.

                                                                iourcs  testing report of stone  crushing
                                                                •>ierat1on.
                                          (continued)
                                                A-2

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                                     TABLE  A-T  (continued)
   Date      Company, consultant or agency
       Location
                                                                              Nature  of  action
 12/20/74  Ferrante and Sons


 06/30/75  Kentucky Stone Co.



 07/08/75  Arizona Portland Cement


 11/13/75  Massachusetts  Broken Stone Co.


 04/13/76  Blue Ridge  Stone Corp.


 05/06/76  Potash  Company of America


 05/27/76  Dravco  Corp.



 05/12/76  GREFCo,  Inc.



 05/11/76  U.S. Borax



 05/27/76  Dravco Corp.


 06/10/76  FUntkote Co.
06/24/76  Englehard Minerals and
          Chemicals Co.
06/23/76  Georgia Kaolin Co,



07/08/76  Standard Slag Co.


07/09/76  Ozark-Mahonlng Co.



07/07/76  International Salt Co.



07/06/76  Eastern Magnesia Talc Co.



08/26/76  Massachusetts Broken Stone
09/27/76  International  Minerals  and
          Chemicals Corp.
 Bernardsville,  N.O.


 Russellville, Ky.



.Rillito,  Ariz.


 Western, Mass.


 MartinsvUle, Va.


 Carlsbad, N. Mex.


 Newtown,  Ohio



 Socorro, N. Hex.



 Boron, Calif.



 Newtown, Ohio


 Las Vegas, Nev.


 Attapulgus, Ga.



 Dry Branch, Ga.



 Harren, Ohio


 Roslclare, 111.



 Retsof, N.Y.



 Johnson, Vt.



Weston, Mass.


Spruce Pine, N.C.
  Emission  test report of stone
  crushing  operation.

  Source  tests on primary, secondary
  crushers, three deck screens, and
  crusher feed hopper.

  Trip report of visible emissions obser-
- vations at stone crushing facility.

  Report  on observation of visible emis-
  sion at stone processing operation.

  Plant visit to study process operation
  at crushed stone plant.

  Plant visit to study processing of
  potash ore.

  Plant visit to study processing of
  sand and; gravel  and the resultant
  particulate emissions.

  Plant visit to study processing of
  perlite ore and the resultant par-
  ticulate emissions.

  Plant visit to study processing of
  borate ore and resultant particulate
  emissions.

  Plant visit made by PEDCo Environmental
  Specialists, Inc.

  Plant visit made by PEDCo and EPA to
  study gypsum processing operations.

  Plant visit to observe fuller's earth
  processing and resultant particulate
  emissions.

  Plant visit to observe kaolin proces-
  sing operations and resultant partlcu-
  late emissions.

  Plant visit to observe slag processing
  and resultant particulate emissions:

  Plant visit to observe fluorspar pro-
  cessing and resultant particulate
 emissions.

 Plant visit to observe rock  salt pro-
 cessing and resultant particulate
 emissions.

 Plant visit to observe talc  pro-
 cessing and resultant particulate
 emissions;

 Visible emissions tests  conducted at
 stone processing operations.

 Source  sampling at  feldspar  milling
 operation  for  particulates.
                                            (continued)
                                                A-3

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                                     TABLE  A-l  (continued)
Date Company, consultant or agency Location
10/25/76 FUntkote Co.
10/21/76 Eastern Magnesia Talc Co.
Blue Diamond, Nev.
Johnson, Vt.
Nature of action
Stationary source testing of gypsum
milling operation.
Stationary source testing at several
11/10/76



05/09/77


05/10/77


06/20/77


06/20/77


07/11/78
          Pfelzer Inc.


          Johns-ManvWe Corp.


          Pfelzer, Inc.


          Pfelzer, Inc.
          National Air Pollution -
          Control Techniques and
          Advisory Comnlttee
          (NAPCTAC)
          National Asphalt Pavement
          Association
08/16/78


08/29/78  Kaolin Industry
09/14/78  National Slag  Association


10/03/78  National Limestone Institute
 12/05/78


 12/06/78


 12/20/78





 01/09/79


 01/10/79
          Georgia Kaolin Company


          Thlele Kaolin Company


          Edward C. Levy Co.
Victorvllle, Calif.


Lompoc, Calif.


V1ctorv1lle, Calif.


Victorvllle, Calif.


Raleigh, N.C.




Durham, N.C.


Durham, N.C.



Durham, N.C.



Washington, D.C.



Dry Branch, Ga.


SandersvHle, Ga.


Detroit, HI.
           Colorado Sand and Gravel           Durham, N.C.
           Association

           North  State Pyrophylllte Company   Greensboro, N.C.
 01/22/79   Gypsum Association
 02/21/79
    to
 02/23/79
          Colorado Sand and Gravel
          Association
                                             Durham, N.C.
Denver, Col.
plant.

Source sample analysis for physical
characteristics of particulate samples
from several plants.

Presurvey talc grinding operations for
possible source testing.

Presurvey diatomite processing oper-
ations for possible source testing.

Source test on pebble mill at talc pro-
cessing plant.

Source emission test report performed
by Pacific Environmental  Services, Inc.

Meeting with non-metallic industry
spokesmen to discuss proposed NSPS.
Meeting with National Asphalt Pavement
Association to discuss proposed NSPS.

Meeting between EPA and the Kaolin
Industry to discuss the proposed NSPS
as 1t pertains to the Kaolin Industry.

Meeting between EPA and the associa-
tion to discuss the proposed NSPS as
1t pertains to the slag Industry.

Meeting between Institute and EPA to
discuss proposed NSPS as it pertains to
the limestone industry.

Source test report on Raymond Impact
Mill and Roller Mill.

Fugitive emission testing at product
loading facility at kaolin plant.

Plant visit by GCA/Technology Division
to observe slag processing and
resultant participate emission.
Source testing performed by Clayton
Associates same date.

Meeting with EPA to discuss proposed
NSPS.

Meeting with GCA/Technology Division
to discuss problems plant would havt
with proposed NSPS.

Meeting between the Association and
EPA to discuss the proposed NSPS as
It pertains to the gypsum industry.

GCA/Technology Division visited sev-
eral sand and gravel processing plants
and met with the Association to
discuss the proposed NSPS as well as
to observe process and emission
control techniques used at the sand and
gravel plants.
                                                (continued)
                                                  A-4

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                                       TABLE  A-l  (continued)
   Date    Company, consultant, or agency
                                                 Location
                                                                              Nature of action
 03/06/79  Refractories Institute
 04/03/79  P-Stone, Incorporated
 04/19/79  Iowa Manufacturing Co.
 08/15/79  Johnson-March Company
 08/24/79  Tillcon-Tomasso,  Inc.
    to     Castle Concrete Co.
 08/31/79  Schmidt-Tiago  Construction Co.
           Cooley Gravel  Co.
           Brannan Sand and  Gravel Co.
           Mobile Pre-Mix Co.
           Gifford-Hill 8 Co.
           Lone  Start  Industries

 09/06/79  Vulcan Materials  Co.
    to     Vulcan Materials  Co.
 09/17/79  Martin-Marietta Co.
           Martin-Marietta Co.
           Nello  L. Teer  Co.
           Luck Quarries
           Vulcan Materials Co.
           Flintkote Stone Products Co.
           Martin-Marietta Co.
           Vulcan Materials Co.

 10/02/79  Vulcan Materials Co.
    to     Castle  Concrete Co.
 10/30/79  Brannan Sand & Gravel Co.
           Vulcan Materials Co.
           FTintkote Stone Products Co.

 10/15/79  Southern California Rock
          Products Association
11/20/79  Georgia Kaolin, Industry
01/15/80  National  Crushed Stone
          Association,  National  Sand  &
          Grave.!  Association
10/27/82  National  Crushed Stone
          Association,  National  Sand  &
          Gravel  Association
                                           Durham, N.C.
                                          Opal, Pa.
 Durham, N.C.
 Philadelphia, Pa.
 N.  Branford,  Conn.
 Colorado Springs, Colo.
 Eagle, Colo.
 Morrison, Colo.
 Denver, Colo.
 Golden, Colo.
 Chico, Tex.
 Bridgeport, Tex.

 Helena, Ala.
 Newman, Ga.
 Augusta, Ga.
 Columbia, S.C.
 Rocky  Mount, N.C.
 Manakin, Va.
 Stafford,  Va.
 Frederick, Md.
 Jamestown, N.C.
 Stoneville, N.C.

 Helena,  Ala.
 Colorado Springs, Colo.
 Denver,  Colo.
 Stafford,  Va.
 Frederick, Md.

 Durham,  N.C.
                                          Durham,  N.C.
Durham, N.C.
Washington, D.C.
 Meeting between  Institute and EPA to
 discuss the proposed NSPS as it pertains
 to the Refractories Industry.

 Plant visit by GCA/Technology Division to
 investigate portable plant using ba'ghouse
 to control  dust  emitted by process.

 Meeting between  company and EPA to
 discuss the proposed NSPS as it pertains
 to the crushed stone industry.

 Meeting with GCA/Technology Division to
 gather information on wet dust suppression
 control  systems.
 Presurvey  ten  stone crushing and sand
 and  gravel plants by GCA/Technology
 Division for visible emission testing.
 (Plants controlled by wet suppression.)
 Presurvey ten stone crushing and sand
 and gravel plants by GCA/Technology
 Division for visible emission testing.
 (Plants controlled by wet suppression.)
Visible emission testing at several
crushers, screens, transfer points, etc.
controlled by wet suppression at five
crushed stone and sand and gravel
plants.

Meeting between association and EPA to
discuss ambient monitoring data performed
by the association.

Meeting between industry representatives
and EPA to discuss the proposed NSPS as  it
pertains to the Kaolin Industry.

Meeting between associations and  EPA to
discuss recent visible emission tests
performed by EPA and ambient monitoring
data performed by the association.

Meeting between associations and  EPA to
discuss the designation of affected
facilities.
                                                      A-5

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                                APPENDIX B
               INDEX TO ENVIRONMENTAL IMPACT CONSIDERATIONS

     This'appendix consists of a reference system, cross-indexed with the
October 21, 1974 FEDERAL REGISTER (39 FR 37419) containing the Agency guide-
lines concerning the preparation of Environmental Impact Statements.  This
index can be used to identify sections of the document which contain data
and information germane to any portion of the FEDERAL REGISTER guidelines.
                                     B-l

-------
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                                  APPENDIX  C
                             SUMMARY  OF  TEST  DATA

      A test  program was  undertaken by EPA  to evaluate  the best  particulate
 control  techniques  available for  controlling particulate emissions from
 non-metallic mineral  plant  process operations  including crushers, screens
 and material handling operations, especially conveyor  transfer  points.  In
 addition, a  control technique for grinding operations  was also  evaluated.
 This  appendix describes  the  process  operations tested  (their operating con-
 ditions, characteristics of  exhaust  gas streams and, where applicable, de-
 viations from prescribed test procedures) and summarizes the results of the
 particulate  emission  tests and visible emission observations.
      Sixteen baghouse collectors controlling process operations at five
 crushed stone installations  (three limestone and two traprock), one kaolin,
 and one fuller's earth plant were tested using EPA Reference Method 5 except
 as noted in the facility descriptions for determination of particulate matter
 from  stationary sources.  Baghouse collectors utilized to control particulate
 emissions from grinding operations at a feldspar, gypsum, and two talc plants
were  also tested, but EPA Reference Method 17 was used for determination of
 particulate matter.  Results of the front-half catches (probe and filter)
 from  the particulate emission measurements conducted are shown  in Figure C-T
and the complete results are summarized in the Tables herein.
     Visible emission observations were made at the exhaust of each of the
above control devices in accordance with procedures recommended in EPA
                                     C-l

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Reference Method 9 for visual determination of the opacity of emissions from
stationary sources.
     At the hoods and collection points for the process facilities, the visible
emission opacity observations were made in accordance with procedures recommen-
ded in EPA Reference Methods 9 and 22 and the data are presented in terms of
percent of time equal to or greater than a given opacity or in percent of total
time of visible emissions as in Table  102.  Visible  emission observations were
also made at four crushed stone, two sand and gravel plants and a feldspar
crushing plant where particulate emissions are controlled by dust suppression
techniques.  The results of these tests are given in Table 102 (Method 22 data)
and Figures 2 through 6  (Method 9 data).
DESCRIPTION OF FACILITIES
     AT.  Primary crushing stage incorporating a pan feeder, vibrating grizzly,
impact breaker, T-bar belt feeder and a primary belt conveyor.  The impactor
is rated at 1,000 TPH and used to reduce run-of-quarry limestone (cement rock)
to 2 1/2-inch minus.  Particulate emissions generated at various points are
confined, captured and vented to a jet pulse type baghouse for collection.
Tests were conducted only during periods when the process was operating
normally.  Particulate measurements were performed using EPA Method 5.  Visible
emission observations were made at the baghouse exhaust and at capture points
in accordance with EPA Method 9.
     A2.  Primary  scalping screen used for scalping  the primary crusher
product of facility Al.  The plus 2  1/2-inch oversize is chuted to a belt
conveyor and returned to the primary  for recrushing.  The screen throughs
are  also discharged  to a conveyor and  transported to a storage facility.
 Particulate  emissions generated  from the top of the  screen, which is
 totally enclosed,  and from  both  chute-to-belt  transfer points are aspirated
 to a jet  pulse  baghouse  for  collection.  Tests, using EPA Method 5, were
                                     C-2

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 conducted simultaneously with  those  at  facility  AT.   Sampling  during  all
 three  tests  runs  reported herein  was overisokinetic.   Visible  emission
 observations were made  at the  baghouse  exhaust using  EPA Method 9.
     A3.   Conveyor transfer  point at the  tail of an overland conveyor,  also
 located at installation Al.  The  30-inch  belt conveyor has a 900 TPH
 capacity  at  a belt speed of  700 FPM.  The transfer point is enclosed  and
 emissions  vented  to a small  baghouse unit for collection.  Three particulate
 samples were collected  using EPA  Method 5.  Visible emission observations
 were made  at the  baghouse  outlet  and at the transfer  point using EPA
 Method 9.
     A4.   The secondary crushing  and screening stage  at installation  Al.
 consisting of a vibrating  screen  and a cone crusher.   Minus 2  1/2-inch
 material  is  fed to  the  screen at  about 165 TPH where  it is separated  in two
 fractions, plus 3/4-inch and 3/4-inch minus.  The oversize fraction is
 discharged to the  cone  crusher and reduced to 3/4-inch.  The crusher  product
 and screen throughs are then conveyed to  a milling circuit.  Dust control
 is effected  by capturing and venting emissions from the screen and crusher
 to a jet pulse baghouse  for collection.    Both particulate measurements and
 visible emission observations were made at the collector outlet using EPA
Methods 5  and 9, respectively.
     Bl.   Primary impact crusher  used for the initial  reduction of run-of-
quarry limestone rock to three inches.  The normal production  rate through
 this primary crushing stage is 350 TPH.    Particulate  emissions are collected
from the impact crusher  at its discharge  hopper and from the discharge hopper
to primary conveyor belt transfer point and then controlled by a fabric filter
                               C-3

-------
collector.  The fabric filter is mechanically shaken twice daily for
cleaning.  EPA Method 5 was used for participate measurements and EPA
Method 9 was used for visible emission readings at the collector exhaust and at
the impact crusher.
     B2.  Secondary and tertiary crushing and screening facilities at the
same installation as Bl.  These consist of a scalping screen, a 4-foot
cone crusher, two 3-foot cone crushers, a hammermill used to produce
agstone and two final sizing screens.  The plant has a 300 TPH design
capacity, crushing to 1 1/2-inch minus, including  60 TPH of agstone.  Dust
control throughout this plant is affected by enclosing or hooding dust
producing points and venting captured emissions to a fabric filter for
collection.  The collector  is mechanically shaken twice daily for cleaning.
Pickup points  include the top of the  scalping  screen, both the feed and
discharge of all three  cone crushers, the discharge of the hammermill, the
top of  both finishing screens,  five product  bins  and  six  conveyor transfer
points.   Three particulate  measurements were made in  accordance  with  EPA
Method  5.   In  addition,  visible emission observations were made  at  the
baghouse exhaust and  at the process facilities controlled using  EPA
Method  9.
      B3.  The  same facility as  B2,  except  that particulate emission
measurements were  made  using an in-stack  filter.  Testing was  conducted
 simultaneously with .that described in B2.
      Cl.   Limestone crushing plant consisting  of a  primary jaw crusher,
 scalping screen and hammermill.  The rated  capacity of the plant is  125
 TPH.  End products produced range from 1  1/2-inch minus  dense-graded road
 base stone to  minus 1/8-inch screenings.   Particulate emissions  are
 controlled by a mechanical   shaker type baghouse.   Collection  points include
 the primary crusher discharge,  the scalping screen  throughs  to stacking
                                C-4

-------
conveyor  transfer point,  and both  the hammerrr-m feed and discharge.
Tests were conducted  using  EPA Methods 5 and 9.
     C2.  Two  3-deck  vibrating screens used for final sizing at the same
installation as Cl.   Both screens  are totally enclosed and participate
emissions collected from  the top of both screens, at the feed to both
screens,  and at both  the  head and  tail of a shuttle conveyor between the
screens are vented to a mechanical shaker type baghouse.  Again, tests were
conducted in accordance with EPA Methods 5 and 9.
     Dl.  Secondary and tertiary crushing and screening facilities used
for processing traprock at "250 TPH.  The process facilities include a"
scalping  screen, a 4-foot secondary cone crusher, two sizing screens and two
4-foot tertiary cone crushers.  All process facilities are enclosed and
particulate emissions are vented to one of two baghouses for collection.
The baghouses are exhausted through a common stack.  Particulate measurements
were conducted using EPA Method 5.   Visible emission observations using
EPA Method 9 were also made at the collector exnaust and at the process
facilities controlled.
     D2.  Finishing screen at the same installation as facility Dl.  The
screen is totally enclosed and emissions collected from the top of the
screen enclosure, all  screen discharge points, and several conveyor transfer
points are vented to a fabric filter.   Tests conducted were  Identical
to those at Dl  and were performed simultaneously.
     El.  Tertiary crushing and screening facilities at a 375 TPH traprock
installation.   Process facilities include two sizing screens, four 4 1/4-foot
                               C-5

-------
cone crushers and several conveyor transfer points.  Both screens are
enclosed and emissions are collected by the enclosures and at the throughs
discharge-.  The tertiary cone crushers are hooded and vented at both feed
and discharge points.  Captured emissions are collected by a jet pulse type
baghouse.  Tests using EPA Method 5 were conducted during periods of normal
operation.  Although desirable, the pressure drop across the baghouse could
not be monitored because the pressure gauge was  inoperative.  Visible emission
observations were also made of the baghouse exhaust  using EPA Method 9.
     E2.  Five  screens used for final sizing and eight storage bins at the
same installation as El.  All screens and bins  are totally enclosed and
emissions vented to a jet pulse type  baghouse  for  collection.  Tests
conducted were  identical  to and performed simultaneously with  those at
facility El.
     Fl.  Tertiary  crushing and screening facilities used  to  reduce run-of-
quarry trap rock.   Partlculate  emissions  are  controlled by  spraying
water  at critical  dust  producing  points  in  the process  flow.   Two  to  three
percent moisture is added to  the  material  to  suppress dust.   Visible  emission
observations were  made  in accordance with EPA Method 9  procedures.
      61.  Grinding system incorporating a belt feeder,  ball  mill,  bucket
 elevator, separator and a belt conveyor.   The ball  mill  1s  used  to reduce
 feldspar to minus  200 mesh.   Partlculate emissions generated at  various
 points are confined, captured and vented to a reverse air type baghouse
 for collection.  Partlculate measurements were performed using EPA Method 17.
 Visible emission observations were made at the baghouse exhaust  and all
 capture points in accordance with EPA Method 9.
                                     C-6

-------
     62.  Crushing facilities  (primary and secondary) used to reduce feldspar
to minus 1.5 inches.  Dust control is affected by  the suppression  techniques.
Surface moisture contents were 1.6 to 1.8 percent  at the primary crusher
discharge, 1.4 to 1.5 percent at the secondary crusher feed, and 1.0 percent
at the secondary crusher discharge conveyor.  Visible emission observations
were made at all process facilities in accordance with EPA Method 9
procedures.
     HI.  Raymond roller mill used to grind gypsum.  The ground product from
the mill is air-conveyed to a cyclone collector for product recovery.  The
air is returned to the mill.  Excess air is vented to a baghouse.  Visible
emission observations were made to determine leaks from the system in
accordance with EPA Method 9 procedures.
     H2.  Same facility as HI.  Particulate measurements and visible emission
observations were made at the baghouse exhaust in accordance with EPA
Methods 5 and 9.
     I.  Bagging operation used to package ground mica.  Particulate
emissions are controlled by a baghouse.  Visible emission observations
were made at the capture point in accordance with EPA Method 9 procedures.
     Jl.  Crushing (primary and secondary), grinding "(pebble mill and vertical
mill) and bagging operations at a talc processing plant.  Particulate emis-
sons are controlled by a baghouse.  Visible emission observations were
made at the capture points in accordance with EPA Method 9 procedures.
     J2.  Same facility as Jl.  Particulate measurements and visible emission
observations were made at the baghouse exhaust 1n accordance with EPA
Methods 5 and 9.
                                   C-7

-------
     K.   Pebble mill  used to grind talc.  Captured emissions are vented to a
pulse type baghouse for collection.  Particulate measurements and visible
emission observations were made at the baghouse exhaust in accordance with
EPA Methods 5 and 9.
    LI.   Raymond Impact Mill used to grind kaolin.  Captured emissions are
exhausted to a baghouse for collection.  EPA Methods 5 and 9 were used for
particulate measurement and visible emission observation at the baghouse stack,
respectively.
    L2.   Roller Mill  used at same plant as LI.   Further grinding of kaolin
is accomplished.  Collection of captured emissions  takes place in a baghouse
which  was tested for  the  same parameters as LI,  again  by EPA Methods 5  and 9.
     Ml.    Roller mill  used to grind  fuller's  earth clay.  Captured
emissions are  exhausted to a baghouse for  collection.   Particulate measure-
ments  and visible  emission observations  were made at  the  baghouse exhaust
 in accordance  with  EPA Methods  17 and 9.
      M2.    Fluid energy mill  used to  grind fuller's earth  clay  at same
 plant as  Ml.   Captured emissions  are  exhausted to a baghouse for collection.
 EPA Methods 17 and 9 were used for particulate measurement and  visible
 emission  observation at the  baghouse  stack, respectively.
      N.   Kaolin rail car loading operation.   Three complete rail  car
 loadings  were evaluated for fugitive emissions in accordance with EPA
 Method 22 test procedures.   A baghouse  (collection system) is used  to
 collect dust that is captured in the loading area.
       P.    Facility P produces crushed stone used primarily for  road construc-
  tion  purposes.  The  processing operation  is located  in the bottom of  an open
  quarry.  The  quarried materials  are  carried by  tr-jck to  the  upper rim of  the
                                      C-8

-------
 pit where they are dumped into hoppers which feed the processing  equipment.
 The finished product is transported back out of the quarry by belt conveyor.
           Visible emission measurements were conducted at the primary  (jaw),
 secondary (impact),  and tertiary (cone) crushers, two process screens,  and one
 conveyor transfer point by means of EPA Reference Methods 9 and 22.  All  pro-
 cess  sources  of emissions are directly or indirectly controlled by means  of a
 wet suppression system.
      Q.    This  facility produces two grades  of  rock for  road-base  and decora-
 tive  stone,  respectively.   The ore  is  obtained  from an open mining operation
 at  the top of a mountain,  and  the process  equipment is permanently installed
 in  a  descending arrangement from the mine  site  to  the bottom  of the mountain.
 The processed rock is accumulated in bins  at the  lower level  for subsequent
 truck loading.
           Visible emission measurements  using the  same techniques as Facility
 P were conducted at the  primary  (jaw), and secondary  (cone) crushers, three
 process screens, and one conveyor transfer point all controlled by means of a
wet suppression system.
     R.   A fully portable crushing  plant processes bank-run material for road
construction and as concrete component.  Ore is removed from a gravel bank and
trucked to the bank top for dumping  into the initial screens before the primary
crushers.  Wet suppression techniques are used to control fugitive dust emana-
ting from the processing of the material.
          EPA Reference Methods 9 and 22 were used to measure visible emissions
  f
from primary (jaw), and secondary (cone) crushers, three process  screens, and
two conveyor transfer points.
     S.    The facility produces two grades of crushed limestone.   The plant  is
                                     C-9

-------
relatively new with all process equipment located at ground level.   One jaw
crusher, two cone crushers, two process screens and two conveyor transfer
points are all directly or indirectly controlled by means of wet suppression
systems.
          EPA Reference Methods 9 and 22 were employed to measure visible
emissions emanating from the above named process sources.
     T.   A large semi-portable rock crushing facility processing large-size
grades of crushed limestone was tested for visible emissions by means of EPA
Reference Methods 9 and 22.
          The sources  tested were the primary and secondary  (cone) crushers,
one process screen, one conveyor transfer  point, and one storage bin.  All
sources  tested are  controlled  by the same  techniques as  Facilities P,  Q, R,
and S.
                                     C-10

-------
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Figure C-l.
Particulate emissions fron non-metallic minerals
processing operations.
                         C-ll

-------

                                        Table 1
                                       FACILITY   Al
                                  Summary of Results
R>;n .'lumber
Dace
Test Tiir.e-minutes
Production rate - TPH
Stack  Effluent
     Flow rate - ACFM
     Flow rate - OSCFM
     Temperature -  °F
     Water vapor -  Vol.%
 Visible Emissions  at
 Collector Discharge -
 Percent Opacity
 Particulate Emissions
   Probe  and Filter Catch
       gr/DSCF
       gr/ACF
       Ib/hr
       Ib/ton
    Total  Catch
       gr/DSCF
       gr/ACF
       Ib/hr
       Ib/ton
    (1) Based on throughput through primary crusher.
    (2) Back-half sample for run number 1 was lost.
                                           C-12
                                                                               Average
6/10/74
400
995
26430
22351
81.0
2.5

0.00471
0.00398
0.90
0.00091
w
-
-
_
6/11/74
320
1027
26653
22140
88.0
3.0
See Tables
0.00504
0.00419
0.96
0.00102
0.00597
0.00495
1.13
0.00121
6/12/74
240'
1010
27142
22502
88.0
3.3
2 and 3
0.00727
0.00602
1.40
0.00139
0.00839
0.00695
1.62
0.00160
-'
320
1011
i
26472
22331
85.7
'2.9

0.00567
0.00473
1.07
o.oom
0.00718
0.00595
1.38
0.00140

-------
                                          TABLE 2
                                        FACILITY AT
                                                          .0)
                               Summary of Visible Emissions
Date:  6/4/74 - 6/5/74
Type of Plant:  Crushed Stone - Primary Crusher
Type of Discharge:  Stack                  Distance from Observer to  Discharge  Point:   75 ft.
Location of Discharge:  Baghouse           Height of Observation  Point:   Ground-level
Height of Point of Discharge:  14ft.       Direction of Observer  from Discharge Point:  N.E.
Description of Background:   Grey building
Description of Sky:  Clear
Wind Direction:  East
Color of Plume:  None
                                        Wind Velocity:   0-5 mi/hr.
                                        Detached Plume:   No
Duration of Observation:   6/4/74 -  78 minutes
                          6/5/74 - 210 minutes
SUMMARY OF AVERAGE OPACITY^
Set Number
1 through 6
7 through 9
10 through 13
14 through 48
Time
Start
8:50
11:23
12:12
8:11
End
9:26
11:41
12:36
11:41
Opacity
Sum
0
0
0
0
Average
0
0
0
0
(1)
      Readings  were 0 percent opacity  during  all  periods of observation.
Two observers made simultaneous readings.
                                           C-13

-------
                                       TABLE 3
                                       FACILITY  Al
                               SUMMARY  OF VISIBLE EMISSIONS
                (1)
Date:  7/8/75 - 7/9/75
Tvoe of Plant:  Crushed stone (cement rock)
Tyoe of Discharge:   Fugitive
Location of Discharge:  Primary impact crusher discharge
Height of Point of Discharge:   6 feet
Description of Background:   Grey waH
Description of Sky:  N.A.  (indoors)
Wind Direction:   N.A.
Color of Plume:   Wnite
Distance from Observer  to Discharge Point: .15 feet
Height of Observation Point:  Ground  level
Direction of Observer from Discharge  Point:  SE
Wind Velocity. No wind  (indoors)
                  /
Detached Plume:  No
Duration of Observation: 7/8/75 - 2 hours
Summary of Data:
Ooacity, Total Time Equal to or
Percent Greater Than Given Onacity
Min. Sec.
5 3 30
10 0 30
15 0 15
20 0 15
25 0 0
30 -
35 -
40 -
45 -
50 -
Sketch Showing How Opacity Varied With Time:
c 20

-------
                                   TABLE 4
                                 FACILITY A2
                            Summary of Results
Run Number
   1
                                                                     Average
Date
6/10/74
6/11/74    6/12/74
Test Time - Minutes
Production Rate - TPH^
Stack Effluent
Flow rate - ACFM
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol . %
Visible Emissions. at
Collector Discharge -
% Opacity
Particulate Emissions '^)
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch ' '
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
400 320
965 1023

15797 15771
13368 13246
90.0 90.0
1.4 2.1
SEE TABLE 5
0.00176 0.00188
0.00149 0.00158
0.20 .0.21
0.00021 0.00024
0.00235
0.00197
0.27
0.00030
240
1056

15866
13196
94.0
2.5

0.00222
0.00184
0.25
0.00024
0.00314
0.00261
0.36
0.00034
320
1015

15811
13270
91.3
2.0

0.00195
, ,0.00164
0.22
0.00023
0.00275
0.00224
0.32
0.00032
  (1)  Throughput through primary crusher.
  (2)  All  three test runs were over-isokinetic.
  (3)  Back-half sample for run number 1  was  lost.
                                    C-15

-------
                                         TABLE 5
                                        FACILITY A2
                               Summary  of Visible  Emissions
Date:  6/10/74 - 6/11/74
Type of Plant:  Crushed Stone - Primary Screen
                (1)
Type of Discharge:  Stack
Location of Discharge:  Baghouse
Height of Point of Discharge:  10 ft.
Description of Background:  Sky
           i
Description of Sky:  Clear
Wind Direction:  Southwest
Color of Plume:  None
Distance from Observer to Discharge  Point:   60  ft.
Height of Observation Point:   Ground-level
Direction of Observer from Discharge Point:   East
Wind Velocity:  0-2 mi/hr.
Detached Plume:  No
 Duration of Observation:  6/10/74 - 192 minutes
                          6/11/74 -  36 minutes
                                SUMMARY OF AVERAGE OPACITY
                                                         (1)
Time
Set Number
1 through 11
12 through 32
33 through 38
Start
10:35
12:30
9:40
End
11:41
2:36
10:16
Ojiacitv
Sum
0
0
0
Average
0
0
0
             Readings were 0 percent opacity during  all  oeriods  of  observation.
 '  'Two  observers made  simultaneous  readings.
                                           C-16

-------
 Run Number

 Date
                                    TABLE 6
                                  FACILITY  A3
                             Sumnary of Results
   1
6/10/74     6/11/74    6/12/74
(1)  Back-half sarnie  for run  number  1 was  lost.
                                   Average
Test Time - Minutes
Process Weight Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol . %
Visible Emissions at
Collector Discharge -
Fugitive (% Opacity)
Parti culate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch ^ '
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
360 288
910 915

2303 2313
1900 1902
98.0 101.0
2.4 2.4
SEE TABLES

0.00095 0.00162
0.00078 0.00134
0.02 0.03
0.00002 0.00003
0.00190
0.00156
0.03
0.00003
288
873

2422
2003
97.0
2.3
7

0.00207
0.00171
0.04
0.00004
0.00259
0.00214
0.04
0.00005
312
899

2346
1935
98.7
2.4


0.00155
0.00128
0.03
0.00003
0.00224
0.00185
0.035
0.00004.
                               C-17

-------
                                                         ,(1)
                                          TABLE 7
                                        FACILITY  A3
                               Summary of Visible Emissions'1
Date:  6/11/74
Type of Plant:  Crushed Stone - Conveyor Transfer Point
Type of Discharge:  Stack                  Distance from Observer to Discharge  Point:   60  ft.
Location of Discharge:  Baghouse           Height of Observation Point:   Ground-level
Height of Point of Discharge:  8 ft.       m>PCt.inn nf Observer from Discharge Point:  North
Description of Background:  Grey apparatus
Description of Sky:  Clear
Wind Direction:   Westerly                  Wind Velocity:  0 - 10 mi/hr.
Color  of Plune:   None                      Detached Plume:  No
Duration of Observation:  240  minutes
                               SUMMARY OF AVERAGE OPACITY
                                          Time
                                                         (1)
            Set Number
                                    Start
End
                                                            Sum
                                                                 Onaci ty
Average
            1 through 30           10:40        1:40         0             0
            31 through 40           1:45        2:45         0             0
            Readings were 0 percent opacity during all  periods of observation.
'  'Two observers  made simultaneous  readings.
                                              C-18

-------
                                   TABLE 8
                                 FACILITY A4
                            Summary of Results
Run Number

Date
6/6/74     6/7/74
6/8/74
                                   Average
Test Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol . %
Visible Emissions at
Collector Discharge -
% Opacity
Parti cul ate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
320
170

10579
9277
81.0
2.3

0.00036
0.00031
0.03
0.00017
0.00047
0.00041
0.04
0.00022
320
162

9971
8711
77.0
2.2
SEE
0.00075
0.00065
0.06
0.00034
0.00104
0.00095
0.08
0.00050
320
152

11045
9656
80.0
2.1
TABLES 9 & 10
0.00074
0.00065
0.06
0.00041

-
'
•V
320
163

10532
9214
79.3
2.2

0.00062
0.00054
0.05
0.00031
0.00678
0.00068
0.06
0.00034
                                      C-19

-------
                                          TABLE  9
                                        FACILITY  A4
                               Summary  of Visible Emissions
                        (1)
Date:  6/6/74
Type of Plant:  Crushed Stone - Secondary Crushing and Screening
Type of Discharge:  Stack
Location of Discharge:  Baghouse
Height of Point of Discharge:  15 ft.
Description of Background:  Sky
Description of Sky:  Clear
l-find Direction:  Variable
Color of Plume:  None
Duration of Observation:  240 minutes
         Distance from Observer to Discharge Point:  100 ft.
         Height of Observation Point:  Ground-level
                  nf Observer from Discharge Point:  North
         Wind Velocity:   0  to  10 nii/hr.
         Detached  Plume:  No


                       (1)
          Set Number
                               SUMMARY OF AVERAGE OPACITY
                                         Time                 Opacity
Start
End
Sum
Average
           1  through 30            10:40        1:40        0            0
           31  through 40            1:45        2:45        0            0
           Readings were 0 percent opacity during all periods of observation.
        observers  made simultaneous readings.
                                             C-20

-------
                                        TABLE  10
                                        FACIUTY A4
                                SUMMARY'OF VISIBLE EMISSIONS
                o:
 Date:   7/9/75 - 7/10/75
 Tyoe of Plant:   Crushed stone (cement  rock)
 Tyoe of Discharge:   Fugitive
 Location of  Discharge:   Conveyor (transfer point)
 Heirit  of Point  of  Discharge:   8 feet
 Description  of Background:   Sky
 Description  of Skv:    Partly cloudy
 Wind  Direction:   South
 Color of  Plume:   White
Distance from Observer to  Discharge Point: 50 feet
Heinht of Observation  Point:   6 feet
Direction of Observer  from Discharge Point: SE
Wind Velocity:  3 - 5  mph
Detached Plume:   No
 Duration  of Observation:   7/9/75  -  106 minutes
                           7/10/75 -  60 minutes
 Summary of Data:
Ooacity,
Percent

5
10
15
20
25
30
35
40
45
50
Total Tine Equal to
Greater Than Given
Min.
3
0
0
0
_
-
-
-
-
-
or
Onacity^
Sec.
0
45
30
0
_
-
-
-
-
-
                                                      Onacitv,
                                                      Percent
                                                        55
                                                        60
                                                        65
                                                        70
                                                        75
                                                        80
                                                        Q5
                                                        00
                                                        15
                                                       100
                     Total Tine Equal to or
                     Greater Than Given Opacity.
                        Min.             Sec.
Sketch Showing How Opacity Varied '-Jith Time:
        S  15
        >•  io
                                                                     I
                  7/9/75
                                          TIME, hours
                          0                1
                              7/10/75
        (1) Two observers made simultaneous readings, the greater of their readings
           is reported.
                                           C-21

-------
Run Number
Date
                                  TABLE  11
                                 FACILITY  Bl
                            Sunmary  of  Results
                                10/29/74    10/30/74    10/30/74
Average
Test Time - Minutes
Production Rate - TPH^1^
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFH
Temperature - °F
Water vapor - Vol. X
Visible Emissions at
Collector Discharge -
X Opacity
Particulate Emissions
Probe and filter catch
gr/DSC.F
gr/ACF"
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
(1) Throughput through primary

180
324

5154
4998
70
1.80


0.009
0.012
0.402
0.0012
0.009
0.011
0.496
0.0015
crusher.

120 120
359 375

6121 6078
5896 5753
76 83
1.87 2.06
See Table 12

0.001 0.010
0.004 0.011
0.072 0.500
0.0002 0.0013
0.001 0.010
0.003 0.011
0.180 0.553
0.0005 0.0015

C-22
140
353

5784
5549
76.3
1.91


0.007
0.009
0.325
0.0007
0.007
0.008
0.408
0.0012



-------
                                           TABLE ;;
                                         FACILITY  B1
Suimary o

                                              ible Emissi
                                                   1 ^
                                                           .0)
Date:  10/29/74 - 10/30/74
Type of Plant:  Crushed Stone - Primary Crusher
Type of Discharge:  Stack
Location of Discharge:  Baghouse
Height of Point of Discharge:  25 ft.
Description of Background:  Grey quarry wall
Description of Sky:   Clear to cloudy
Mind Direction:  Northwesterly
Color of Plume:  White
               Distance from Ovserver  to  Discharge Point:  15 ft.
               Height of Observation Point:  Ground level
               Direction of Observer from Discharge Point:  West
               Wind  Velocity:  Not available
                                               Detached Plume:  No
Duration of Observation:   10/29/74 - 180 minutes
                          10/30/74 - 234 minutes
           SUMMARY OF AVERAGE OPACITY
                             SUMMARY  OF  AVERAGE OPACITY
Time
Set Number
10/29/74
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Zl
22
23
24
25
26
27
28
29
30
•10/30/74 ,
31
6
-------
       TABLE 13
     FACILITY B2
Summary of Results
Run Number
Date
Test Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol. J
Visible Emissions at
Collector Discharge -
% Opacity
Particulate emissions
Probe and filter eaten
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton

1 2 3
10/31/74 10/31/74 11/11/74
108 108 108
270 270 270

19684 18921 16487
18296 17638 15681
92.0 96.6 79.0
1.95 1.92 2.01
SEE TABLES 14-23
0.003 0.005 0.003
0.003 0.005 0.003
0.427 0.753 0.457
0.0016 0.0028 0.0017
0.006 0.006 0.007
0.005 0.006 0.007
0.916 0.978 0.955
0.0034 0.0036 0.0035
C-24
Average
-
108
270

18197
17205
87.0
1.96

0.0037
0.0037
0.546
0.0020
0.0063
0.0060
0.946
0.0035


-------
                                           TABLE 14
                                         FACILITY B2
                                Summary  of-Visible Emissions
                                         (Observer 1}
 Date:  10/31/74 -  11/1/74
 Type of Plant:   Crushed  Stone  -  Secondary  and Tertiary Crushing and Screening
 Type of Discharge:   Stack                  Distance from Observer to Discharge Point:  30 ft.
.Location of Discharge:   Baghouse          Height of Observation Point:  5 ft.
 Height of Point of  Discharge:  8 ft.       Direction of Observer from Discharge Point:   East
 Description of  Background:  Sky
 Description of  Sky:  Clear to  partly cloudy
 Wind Direction:  Southeasterly             Wind Velocity:  Not available
 Color of Plume:  White                     Detached Plume:  No
 Duration of Observation:  10/31/74 -
                          240 minutes
                          11/1/74 -
                          106 minutes

                               SUMMARY OF AVERAGE OPACITY
Date
10/31/74





















11/1/74

Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21 through
40
41 through
56
1
Start
9:27
9:33
9:39
9:45
9:51
9:57
10:03
10:09
10:15
10:21
10:27
10:33
10:39
10:45
10:51
10:57
11:03
11:09
11:15
11:21

1:09

8:11
Fime
End
9:33
9:39
9:45
9:51
9:57
10:03
10:09
10:15
10:21
10:27
10:33
10:39
10:45
10:51
10:57
11:03
11:09
11:15
11:21
11:27

3:09 '

9:47

Sum
5
10
5
0
5
5
10
5
20
0
0
0
5
5
10
0
5
0
0
10

0

0
Ooaci ty
Average
0.2
0.4
0.2
0
0.2
0.2
0.4
0.2
0.8
0
0
0
0.2
0.2
0.4
0
0.2
0
0
0.4

0

0
           Readings  ranged from 0 to  5 percent opacity.
                                            C-25

-------
                                         Table 15

                                       FACILITY B2

                               SUMMARY OF VISIBLE EMISSIONS
Date: 6/30/75

Tyoe of Plant:  Crushed stone (limestone)

Tyoe of Discharge:  Fugitive

Location of Discharge: Secondary  Cone  Crusher.(#1)

Hsiflht of Point of Discharge:  25 ft.       Distance  from Observer to Discharge Point:45 ft.

Oescriotion of Background: Sky &  Equipment  Height of Observation Point:2  ft.

Ooscrintion of Skv:  Clear                 Direction of Observer from Discharge Point:North

Wind Direction: East                       Wind  Velocity:  5-10 mph

Color of  Plume:  White       .              Detached  Plume:  No

Duration  of  Observation:  231 minutes
Summary  of  Data:
Ooacity,
Percent

5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
23
0






g

or
Opacity
Sec.
0
45








                                                       Ocacitv,
                                                       Percent
                                                         55
                                                         60
                                                         65
                                                         70
                                                         75
                                                         80
                                                         85
                                                         90
                                                         95
                                                        100
Total Time Equal  to or
Greater Than Given OnacU'
                                                                    Min.
                    Se-
                                           C-26

-------
                                          Tab]*  ig

                                         FACILITY B2

                                SUMMARY  OF VISIBLE EMISSIONS
 Date:  6/30/75

 Tyoe of Plant: Crushed  stone  (limestone)

 Type of Discharge: Fugitive

 Location of Discharge:  Secondary Cone Crusher

 Height  of Point of Discharged ft.        Distance from Observer to Discharge Point:45 ft.

 Descriotion of Background: Sky & Equipment  Height of Observation  Point:  2 ft.

 Description of Sky: Clear                   Direction of Observer  from Discharge Point:North

 Wind  Direction: East                        H1r)d Velocitv: 5-10 mph

 Color of Plume: White                       Detached Plume: No

 Duration of Observation:  231  minutes
Summary of Data
Ooacity,
Percent
5
10
15
• 20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
0
0
or
Opacity
Sec.
15
0
                                                      Onacitv,
                                                      Percent
                                                        60
                                                        65
                                                        70

                                                        80
                                                        85
                                                        90

                                                       100
Total Time Equal to or
Greater Than Given Onacitv
                    Sec.
                                          C-27

-------
                                         Table 17

                                       FACILITY B2

                               SUMMARY OF VISIBLE EMISSIONS
Date:  6/30/75

Fyoe of Plant: Crushed stone  (limestone)

Type of Discharge: Fugitive

Location of Discharge: Secondary Cone  Crusher

Height of Point of Discharge: 25 ft.        Distance from Observer to Discharge .Point: 45 ft.

Oescriotion of Background: Sky & Equipment  Height of Observation Point:. 2 ft.

Description of Sky: Clear                  Direction of Observer from Discharge Point:North

Wind Direction: East                       Wind Velocitv: 5-10 mph

Color of Plume: White                      Detached Plume: No

Duration of Observation:  231 minutes
Summary of Data:

     Ooacity,
     Percent
         5
        10
        15
        20
        25
        30
        35
        40
        45
        50
Total Time Equal to or
Greater Than Given Opacity
                    Sec.
                                         0
     0
Ooaci tv,
Percent
  55
  60
  65
  70
  75
  80
  85
  90
  %
 100
Total Time Equal  to or
Greater Than Given Onacitv
   Min.             Sec.
                                              C-28

-------
                                           Tab!??  ]8

                                         FACILITY  B2

                                SUMMARY  OF VISIBLE EMISSIONS



 Date:  6/30/75 - 7/1/75

 Tvoe of  Plant: Crushed stone (limestone)

 Type of  Discharge: Fugitive

 Location of Discharge:Surge Bin

 Height of Point of Discharge:               Distance  from ^^ to'01scharge

 Description of Background:Sky  & Equipment   Height of Observation  Point:  15 ft.

 •Description of Sky: Clear                    nirortfnr,  nf  nu
                                            Direction  of  Observer  from Discharge Point-SE

 «1nd Direction': south                       Wind Velocity:  5 mph

 :olor of Plume: Wh1te           '            Detached plume: NQ

 )uration  of Observation: 6/30/74 - 234 minutes
                         7/1/75  -  53 minutes
iummary of Data:


                                                      Opacity,   Total Time Equal  to or
                                                      Percent   Greater  Than  Given Opacity
                                                                   ffin._             Sec.  '

                                                       55
                                                       60
                                                       65
                                                       70
                                                       75
                                                       80
                                                       85
                                                       90
                                                       95
                                                      100
Ooacity,
Percent

5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Nin.
2
1
-






or
Opacity
Sec.
0
15
30






                                        C-29

-------
                                         Table 19

                                       FACILITY B2

                               SUMMARY OF VISIBLE EMISSIONS
Date: 6/30/75 - 7/1/75

Tyoe of Plant: Crushed stone (limestone)

Tyoe of Discharge: Fugitive

Location of Discharge:  Scalping screen

Hsinht of Point of Discharge:50 ft.      •   Distance  from Observer to Discharge Point:150 fl

Descrintion of Background: Sky & Equipment   Height  of Observation Point:15  ft.

Inscription of Sky: Clear                   Direction of Observer from Discharge Point: SE

Wind  Direction: South                       Wind Velocity: 5 MPH

Color of  Plume: White                       Detached  Plume:  no

Duration  of  Observation: 6/30/75 - 234  minutes
                          7/1/75  -  53  minutes
Summary  of Data:
Ooacity,
Percent

5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Mi n .
44
9
3
0
-





or
Opacity
Sec.
45
45
0
30
-





                                                       Ooacitv,   Total Time Equal to or
                                                       Percent    Greater Than Given Onacitv
                                                                    Min.             Sec.

                                                         55
                                                         W
                                                         65
                                                         70
                                                         75
                                                         80
                                                         85
                                                         90
                                                         %
                                                        100
                                              C-30

-------
                                                20

                                        FACILITY B2

                               SUMMARY  OF VISIBLE EMISSIONS
fate: 6/30/75 - 7/1/75

 voe of Plant: Crushed stone  (limestone)

Type of Discharge:  Fugitive

-ocation of Discharge: Hammermi11

leight  of Point of Discharge:              Distance from Observer to Discharge  Point:150 ft

lescriotion of Background: Sky & Equipment  Height of Observation Point:  15 ft.

Inscription of Sky: Clear                   niv-pr-HAn «* ™,        *    „.   '
                                           mrection of Observer from Discharge Point: SE

find Direction: South                       W1nd Velocitv: 5 mph

olor of Plume: White                       Detached Plume: No

uration  of Observation:  6/30/75 -  234 minutes
                         7/1/75   -   53 minutes

ummary of  Data:
    Ooacity,
    Percent
       5
      10
      15
     '20
      25
      30
      35
      40
      45
      50
Total Time Equal to or
Greater Than Given Opacity
   Mln.Sec.
    0
0
               Ooacitv,
               Percent
 55
 60
 65
 70
 75
 80
 85
 90
 «J5
100
          Total Time Equal to or
          Greater Than Given Onacitv
             ^'n.             Sec.
                                          C-31

-------
                                         Tab!ft 21

                                       FACILITY B2

                               SUMMARY OF VISIBLE EMISSIONS
Date: 7/1/75

Tyoe of Plant: Crushed stone (limestone)

Type of Discharge: Fugitive

Location of Discharge: (3-Deck)  Finishing  Screen (left)
Height of Point of Discharge: 40

Oescriotion of Background:  Hazy Sky

Description of Sky: Clear

Wind Direction: Southeast

Color of Plume: White

Duration of Observation:  107 minutes
                         Distance from Observer to  Discharge Point:75  ft.

                         Height of Observation  Point: Ground level

                         Direction of Observer  from Discharge  PointrWest

                         Wind Velocitv: 5-15 mph

                         Detached Plume: No
Summary  of Data:

      Ooacity,
      Percent
         5
        10
        15
        20
        25
        30
        35
        40
        45
        50
Total Time Equal to or
Greater Than Given Opacity
   Mln.Sec.

     4               30
Ooacitv,
Percent
  55
  60
  65
  70
  75
  80
  85
  90
  05
 100
Total Time Equal to or
Greater Than Given Onacitv
   •Mln.             Sec
                                             C-32

-------
                                        Tab!" 22

                                      FACILITY 82

                              SUMMARY OF VISIBLE EMISSIONS
te:  7/1/75

oe of Plant: Crushed stone (limestone)

pe of Discharge: Fugitive

cation of Discharge: (3-Deck)  Finishing screen  (right)
ight of Point of Discharge:  40  ft.

scriotion of Background:  Hazy sky

scrintion of Sky:  Clear

nd Direction:  Southeast

lor of Plume:  White

ration of Observation: 107 minutes
                          Distance from Observer to Discharge  Point:  75  ft.

                          Height of Observation  Point: Ground level

                          Direction of Observer  from Discharge Point:  West

                          Wind Velocity: 5-15 mph

                          Detached Plume: No
nmary of Data;

   Ooacity,
   Percent
     5
     10
     15
     20
     25
     30
     35
     40
     45
     50
Total Time Equal to or
Greater Than Given Opacity
   -Hi-n.             Sec.

     0                15
Opacity,
Percent
  55
  60
  65
  70
  75
  80
  85
  90
  05
 100
Total Time Equal to or
Greater Than Given Opacity
   11 n.             Self:
                                         C-33

-------
                                         Table 23
                                       FACILITY B2
                               SUMMARY OF VISIBLE EMISSIONS
Date: 6/30/75
Tyoe of Plant: Crushed stone (limestone)
Tyoe of Discharge: Fugitive
Location of Discharge:  Two (*3-Deck) finishing screens
Height of Point of Discharge:  50  ft.
Oescriotion of Background:  Hazy sky
Oescrintion of Sky: Clear
Wind Direction:  Southeast
Color of Plume:  White
Duration of Observation: 120   minutes
Summary of Data:
Distance from Observer to Discharge  Point:  75 ft.
Height of Observation Point-.Ground level
Direction of Observer from Discharge Point:West
Wind Velocity: 10-15 mph
Detached Plume: No
Ooacity,
Percent

5
T)
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
86
28
5
0
0
-




or
Opacity^
Sec.
15
15
30
15
0
_


'

                                                      Opacity,
                                                      Percent
                                                        55
                                                        60
                                                        65
                                                        70
                                                        75
                                                        80
                                                        85
                                                        90
                                                        100
                      Total  Time  Equal  to or
                      Greater  Than  Given Ooacitv
                                                                    Min.
                                         Sec.
                                             C-34

-------
                                       TABLE  24
                                     FACILITY  B3
                                  Summary  of Results
Run Number
pate

Test Time - Minutes
Production Rate - TPH
Stack Effluent
    Flow rate - ACFM
    Flow rate - DSCFM
    Temperature - °F
    Water Vapor - Vol. %

Visible Emissions at
Collector Discharge -
* Opacity
Particulate Emissions
    Probe and filter catch
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton
    Total catch^
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton

    * 'No analysis of bark-half on in-stack filter tests.
1
10/31/74
270
18674
17335
92
2.13
0.002
0.002
0.355
0.0013
2
11/1/74
270
18405
17186
90
1.73
0.004
0.004
0.614
0.0023
3
11/1/74
270
16238
15466
79
1.87
0.003
0.003
0.411
0.0015
Averac
-
270
17772
16662
87
1.91
0.003
0.003
0.460
0.0017
                                       C-35

-------
Run Number
Date
       TABLE 25
     FACILITY Cl
Summary of Results

        123         Average

      11/19/74    11/21/74   11/22/74
Test Time - Minutes
Production Rate - TPH*1*
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol. I
Visible Emissions at
Collector Discharge -
X Opacity
Parti cul ate Emissions
Probe and filter catch
gr/DSQF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
120

7340
7250
66.0
1.0


0.003
0.003
0.18
0.001

0.007
0,007
0.43
0.003
Z4U

7560
7720
38.0
0.4
See table

0.0007
0.0007
0.05
0.0004

0.001
0.001
0.09
0.0008
£
-------
                                           TABLE  25

                                          FACILITY  Cl

                                 Summary  of Visible  Emissions^



 Date:   11/21/74



 Type of Plant:   Crushed  Stone  -  Primary  and Secondary  Crushing and Screening
 Type of Discharge:   Stack


 Location of Discharge:   Baghouse


 Height of Point of  discharge:   40  ft.


 Description of Background:   Dark Woods


 Description of Sky:  Overcast


 Wind Direction:  Easterly


 Color of Plume:  White


 Duration  of Observation:  240 minutes
Distance from Observer to discharge Point:  100 ft.


Height of Observation Point:  50 ft.


Direction of Observer from Discharge Point:  N.W.
Wind Velocity:  10 to 30 mi/hr.


Detached Plume:   No
                                    SUMMARY OF AVERAGE OPACITY

                                              Time
             Set Number
                                                                        Opacity
                                       Start
                                                       End
                                                                     jum
             1 throug.1 40              12:10            4:]0            0


             Readings were 0 percent opacity during the observation period.
Sketch Showing How Opacity Varied With Time:
        O)
        o
        
-------
Run Number
Date
Test Time - Minutes
       TABLE   27
     FACILITY C2
Sunroary of Results

        123          Average
      11/19/74   11/21/74    11/22/74
                     0)
Production Rate - TPH
Stack Effluent
   Flow rate - ACFH
   Flow rate - DSCFM
   Temperature - °F
   Water vapor - Vol. %
Visible Emissions at
Collector Discharge -
X Opacity
Particulate Emissions
   Probe and filter catch
      gr/DSCF
      gr/ACF
      Ib/hr
      1b/ton
   Total catch
      gr/DSCF
      gr/ACF
      Ib/hr
      Ib/ton
(1) Throughput through primary  crusher.
120
132
6220
6260
62.0
0.4

0.006
0.006
0.31
0.002
0.008
0.009
0.46
0.003
240
119
6870
6880
50.0
0.3
See Table
0.00003
0.00003
0.002
0.00002
0.0006
0.0007
0.04
0.0003
240
127
6540
6700
51.0
0.1
28
0.0004
0.004
0.02
0.0002
0.0009
0.001
0.05
0.0004
200
126
6543
6613
54.3
0.27

0.00214
0.00214
o.m
0.00074
0.0032
0.0057
0.18
0.0012
                                        C-38

-------
                                           TABLE
                                         FACILITY  C2
                                 Sussary  cf Visible  Emissions
 Date:   11/21/74
 Type of Plant:  Crushed Stone  - Finishing Screens
Type of Discharge:  Stack
Location of Discharge:  Baghouse
Height of Point of Discharge:  40 ft.
Description of Background:  Dark woods
Description of Sky:  Overcast

     o
     O)
     Q.
    O
    re
    Q.
    o
                                          Time, hours
                                              C-39

-------
Run Number

Date
Test Time - Minutes
Production Rate -
Stack Effluent
   Flow rate - ACFH
   Flow rate - DSCFM
   Temperature - °F
   Hater vapor - Vol. %
Visible Emissions at
Collector Discharge -
% Opacity
Particulate Emissions
    Probe and  filter catch
       gr/DSCF
       gr/ACF
       Ib/hr
       Ib/ton
    Total  catch
       gr/DSCF
       gr/ACF
       Ib/hr
       Ib/ton
(1) Throughput through primary crusher.
       TABLE  29
     FACILITY 01
Summary of Results

        1          2          3
      9/17/74    9/18/74     9/19/74
Average
240
225
31830
31370
66.0
1.2

0.0095
0.0094
2.55
0.0113
0.0100
0.0096
2.69
G.0120
240
230
31810
30650
71.0
1.7
SEE TABLES
0.0081
0.0078
2.13
0.0093
0.0085
0.0082
2.23
0.0097
240
220
31950
31230
68.0
1.6
30-36
0.0080
0.0078
2.13
0.0097
0.0086
0.0084
2.30
0.0105
240
225
31863
31083
68.3
1.5

0.0085
0.0083
2.27
0.0101
0.0090
0.0088
2.41
0.107
                                     C-40

-------
                                           TABLE 30
                                         FACILITY  Ul
                                Summary of Visible  Emissions^'
 Oate:   9/17/74
 Type of Plant:  Crushed Stone -  Secondary  and Tertiary Crushing 8 Screening
 Type of Discharge:   Stack
 Location of Discharge:   Baghouse
 Height of Point  of  Discharge:   55  ft.
 Description of Background:  Trees
 Description of Sky:  partiy Cloudy
 Wind Direction:  Northerly
 Color of Plume:  None
 Duration  of Observation:  240 minutes
          Distance from Observer to Discharge Point:  300 ft.
          Height of Observation Point:  40 ft.
          Direction of Observer from Discharge Point:  S.E.
          Mind Velocity:  5-10 mi/hr.
          Detached Plume:  No
            Set Number
SUMMARY OF AVERAGE OPACITY
       Time
             En3
Start
(2)
     Opacity	
Sum           Average
            1 through 40             9:10       1:00           0               0
            Readings were 0 percent opacity during the period of observation.
Sketch Showing How Opacity Varied With Time:
     c
     w
     &
     O
     •a
     a.
     O
                                              3_
                                             Time,  hours
                                               C-41

-------
                                         Tab!-? 31

                                       FACILITY  Dl

                               SUMMARY OF VISIBLE EMISSIONS
Date:  7/8/75

Tyoe of Plant: Crushed stone (traprock)

Tyoe of Discharge: Fugitive

Location of Discharge:  Terti'ary  gyrasphere cone crusher (S)
Heiflht of Point of Discharge:

Description of Background:  Machinery

Description of Sky: Overcast

Mind Direction:  Southwest

Color of'Plume:  white

Duration of Observation:  170 minutes
                         Distance from Observer to Discharge  Point:  30  ft.

                         Height of Observation Point:  ground level

                         Direction of Observer from Discharge Point:  West

                         Wind Velocftv:  0-10  mph

                         Detached Plume: No
Summary of Data:

     Ooacity,
     Percent
        5
        10
        15
        20
        25
        30
        35
        40
        45
        50
Total Time Equal to or
Greater Than Given Opacity
   Hin.Sec.
                      0
Ooacitv,
Percent
  55
  60
  65
  71
  75
  80
  85
  90
  95
 100
Total Time Equal  to or
Greater Than Given Onacitv
                                                                    Min.
                               Sec.
                                            C-42

-------
                                         Tablo 32

                                       FACILITY Dl

                               SUMMARY  OF VISIBLE EMISSIONS
ate:  7/8/75

/oe of Plant: Crushed stone (traprock)

ype of Discharge: Fugitive

>cation of Discharge:  Terti'ary gyrashere  cone crusher (N)
2ight of Point of Discharge:

sscriotion of Background: Machinery

sscrintion of Sky: Overcast

ind Direction:  Southwest

3lor of Plume:  White

uration of Observation:  IJQ minutes
                          Distance  from  Observer  to Discharge Point:  sg  ft

                          Height of Observation Point:  ground  level

                          Direction of Observer from Discharge Point: West

                          Wind  Velocity: 0-10 mph

                          Detached  Plume:
 mmary of Data:

    Ooacit.y,
    Percent
       5
      10
      15
      20
      25
      30
      35
      40
      45
      50
Total Time Equal to or
Greater Than Given Opacity
   Min.Sec.
     0
Opacity,
Percent
                                      55
                                      60
                                      65
                                      70
                                      75
                                      80
                                      85
                                      90
                                      95
                                     100
Total Time Equal to or
Greater Than Given Opacity
   Min"!      '•
                                           C-43

-------
                                         Table 33

                                       FACILITY Dl

                               SUMMARY OF VISIBLE EMISSIONS
Date: 7/8/75

Tyoe of Plant: Crushed stone  (traprock)

Tyoe of Discharge: Fugitive

Location of Discharge:  secondary  standard cone crusher

Heiglt of Point of Discharge:

Oescriotion of Background: Machinery

Description of Sky: Overcast

Wind Direction: southwest

Color of Plume: White

Duration of Observation:  170 minutes
                         Distance from Observer to Discharge  Point:  30  ft.

                         Height of Observation Point:Ground level

                         Direction of Observer from Discharge Point:West

                         Wind Velocity: 0-10 mph

                         Detached Plume: No
Summary of Data:

     Ooacity,
     Percent
         5
        10
        15
        20
        25
        30
        35
        40
        45
        50
Total Time Equal to or
Greater Than Given Opacity
   Hin.Sec.
                      0
Opacity,
Percent
  55
  60
  65
  70
  75
  80
  85
  90
  95
 100
Total Time Equal  to or
Greater Than Given Onacitv
                                                                    Min.
                               Sec.
                                             C-44

-------
                                         Tabl'?  34

                                       FACILITY  Dl

                               SUMMARY OF VISIBLE EMISSIONS
 Date:   7/9/75

 Tvoe of Plant:  Crushed stone (traprock)

 Type of Discharge: Fugitive

 Location  of  Discharge:  Scalping screen

 Height  of Point of Discharge:

 Oescriotion  of Background:  Equipment

 Description  of Sky:  Overcast

Wind Direction:  Southwest

Color of  Plume:  white

Duration  of  Observation:  210 minutes
Summary of Data:
              \

    Ooacity,
    Percent
                          Distance  from  Observer  to  Discharge Point:  30 ft.

                          Height  of Observation Point:  15 ft.

                          Direction of Observer from Discharge Point: North

                          Wind  Velocitv:  0-10 mph

                          Detached  Plume: No
       5
      10
      15
      20
      25
      30
      35
      40
      45
      50
Total Time Equal to or
Greater Than Given Opacity
   Mi n.              Sec.
    0
0
              Ooacitv,
              Percent
 55
 60
 65
 70
 75
 80
 85
 90
 05
100
          Total Time Equal to or
          Greater Than Given Opacity
             Mi n.              Sec!'
                                           C-45

-------
                                         Tablft 35

                                       FACILITY Dl

                               SUMMARY OF VISIBLE EMISSIONS
Date: 7/9/75

Tyoe of Plant: Crushed stone (traprock)

Tyoe of Discharge: Fugitive

Location of Discharge: Secondary (2-Deck)  sizing  screens
Height of  Point  of Discharge:

Descriotion  of Background:  Equipment

Description  of Sky: Overcast

Mind Direction:  Southwest

 Color of Plume:  White

 Duration of Observation:  210 minutes
                        Distance from Observer to Discharge Point: 30 ft.|

                        Height of Observation Point:  15  ft.

                        Direction of  Observer from Discharge Point: North

                        Wind Velocity:  0-10 mph

                         Detached Plume: No
 Summary of Data:

      Ooacity,
      Percent
         5
        10
        15
        20
        25
        30
        35
        40
        45
         50
Total Time Equal to or
Greater Than Given Opacity
   MTnT             Sec.
     0
                                         0
Opacity,
Percent
  55
  60
  65
  70
  75
  80
  85
  90
  95
  100
Total Time Equal  to or
Greater Than Given Onacitv
   Min.             Sec.
                                              C-46

-------
                                          Tablr? 36

                                        FACILITY Dl

                                SUMMARY  OF VISIBLE EMISSIONS
)ate: 7/9/75

Fyoe of Plant: Crushed stone (traprock)

Fyoe of Discharge: Fugitive

.ocati-on of Discharge: Secondary  (3-Deck) sizing screens
leig'-it of Point of Discharge:

tescriotion of Background: Equipment

)escrintion of Sky: Overcast


-------
Run Number

Date
Test Time - Minutes
Production Rate -
Stack Effluent
    Flow  rate - ACFM
    Flow  rate - DSCFH
    Temperature - °F
    Water vapor - Vol.  %
 Visible Emissions  at
 Collector Discharge -
 X Opacity
 Particulate Emissions
    Probe and filter catch
       gr/DSCF
       gr/ACF_.
       Ib/hr
       Ib/ton
    Total  catch
       gr/DSCF
       gr/ACF
        Ib/hr
        Ib/ton
       TABLE  37
     FACILITY D2
Sunmary of Results

        1          2          3

       9/17/74    9/18/74    9/19/74
                                                                    Average
240
225
26790
26200
69.0
1.3

0.0027
0.0027
0.61
0.0027
0.0041
0.0040
0.91
0.0040
240
230
26260
25230
74.0
1.6
See Table
0.0038
0.0036
0 82
0.0036
0.0045
0.0043
0.98
0.0043
240
220
24830
24170
72.0
1.3
38
0.0023
0.0022
0.47
0.0021
0.0031
0.0030
0.64
0.0029
240
225
25960
25200
71.7
1.4

0.0029
0.0028
0.63
0.0028
0.0039
0.0038
0.84
0.0037
  (1)  Throughput through primary crusher.
                                         C-48

-------
                                            TABLE  38
                                           FACILITY  02
                                 Summary of Visible  Emissions^1)
 i,ate:   9/18/74
 Type of Plant:   Crushed  Stone  -  Finishing Screens
 Type of Discharge:   Stack
 Location of Discharge:   Baghouse
 Height of Point  of  Discharge:   55  ft.
 Inscription of Background:  Trees
 Description of Sky:  Clear
 Wind Direction:  Northerly
 Color of Plume:  None
 Duration  of Observation:  240 minutes
Distance from Observer to Discharge Point:   300  ft.
Height of Observation Point:   40 ft.
Direction of Observer from Discharge  Point:  North
Wind Velocity:   5 to 10 mi/hr.
Detached Plume:   No
            Set Number
                                   SUMMARY OF AVERAGE OPACITY
                                          Time
                                                             (2)
                                   Start
                     Opacity
                 Sum         Average
            1 through 40           8:30          12:30           0
            Readings were 0 percent opacity during period of observation.
Sketch Showing How Opacity Varied with Time:
       3
       o
       ID
                                             Time, hours
                                             C-49

-------
Run Number
Date
Test Time - Minutes
       TABLE 39
     FACILITY El
Sumnary of Results
        1          2          3
      11/18/74     11/18/74   11/19/74
                     0)
Production Rate - TPH
Stack Effluent
    Flow rate - ACFH
    Flow rate - DSCFH
    Temperature - °F
    Water  vapor - Vol. %

 Visible Emissions  at
 Collector Discharge -
 % Opacity
 Particulate Emissions
    Probe and filter catch
       gr/DSCF
       gr/ACF
       Ib/hr
       Ib/ton
    Total catch
       gr/DSCF
       gr/ACF
       Ib/hr
       Ib/ton
  (1) Throughput through primary crusher.
                                                                    Average
120
384
15272
16297
33.1
0.5

0.0134
0.0143
1.87
0.0049
0.0170
0.0181
2.37
0.0067
120
342
13997
14796
40,4
0.0
SEE TABLE
0.0116
0.0122
1.47
0.0043
0.0137
0.0145
1,74
0.0051
120
460
14975
15642
41.0
0.5
40
0.0147
0.0154
1.97
0.0043
0.0164
0.0171
, 2.20 .
0.0048
120
395
14748
15578
38.2
0.3

0.0132
0.0140
1.77
0.0045
0.0157
0.0166
2.10
0.0055
                                  C-50

-------
                                          TABLE  40
                                        FACILITY El
                                   »v»\/  ^
                                   Mt J  w
                                        1  * t «• I I
late:   11/W74  -  11/19/74
'ype of Plant:   Crushed Stone  -  Tertiary  Crushing  and  Screening
ype  of  Discharge:   Stack
.ocation of Discharge:   Baghouse
lelght of Point  of  Discharge:   1/2  ft.
)escription of Background:  Grey  Wall
Ascription of Sky:   Overcast
lind  Direction:   Westerly
tolor of Plume:   None
.Distance from Observer to Discharge Point:  60 ft.-
Height of Observation Point:  Ground level
Direction of Observer from Discharge Point:  South
Wind Velocity:  2 - 10 mi/hr.
Detached Plume:  No
)uration  of  Observation:   11/18/74 •? 120 minutes
                          11/19/74 -  60 minutes
                                   SUMMARY  OF AVERAGE OPACITY
                                            Time
                         Opaci ty
Set Number
11/18/74
1 through 10
11 through 20
11/19/74
21 through 30
Start

9:00
10:15

10:07
End

10:00
11:15

11:07
Sum

0
0

0
Average

0
0

0
             Readings  were 0 percent opacity during all  periods of observation.
Jketch  Showing How Opacity Varied With Time:
                                            C-51

-------
       TABLE 41
     FACILITY E2
Sunmary of Results
Run Number
Date
Test Time - Minutes-
Production Rate - TPH*1J
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFH
Temperature - °F
Water vapor - Vol. X
Visible Emissions at
Collector Discharge -
% Opacity
Parti cul ate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
lb/ ton
(1) Throughput through primary

1
11/18/74
120
384

22169
23001
44.5
1.1

0.0132
0.0137
2.60
0.0068
0.0205
0.0213
4.05
0.0105
crusher.
C-52
2
11/18/74
120
342

19772
19930
59.2
1.1
SEE TABLE
0.0096
0.0097
1.65
0.0048
0.1378
0.0139
2.35
0.0069


3
11/19/74
120
460

21426
21779
55.0
0.6
42
0.0153
0.0155
2.85
0.0062
0.0170
0.0173
3.18
0.0069


Average
-
120
395

21122
21570
52.9
0.9

0.0127
0.0130
2.37
0.0059
0.0171
0.0175
3.19
0.0081



-------
                                          TABLE 42
                                        FACILITY E2
                               Summary of Visible'Emissions
Sate;  11/16/74 - 11/19/74
Type of Plant:   Crushed Stone - Finishing Screens  and Bins
             (1)
Type of Discharge:   Stack
.ocation of Discharge:   Baghouse
leignt of Point of  Discharge:   1/2  ft.
Ascription of Background:   Hillside
tescription of Sky:   Clear
Jind Direction:  Westerly
;olor of Plume:  Hone
Distance from Observer to Discharge Point:  120 ft
Height of Observation Point:  Ground level
Direction of Observer from Discharge Point:  South
Wind Velocity:  2-10 mi/hr.
Detached Plume:  No
Juration  of Observation:  11/18/74 - 120 minutes
                         11/19/74 -  60 minutes
                                  SUMMARY OF AVERAGE OPACITY^
Set Number
IV 18/74
1 through 10
11 through 20
11/19/74
21 through 30

Start

12:50
1:50

9:05
Ti me
End

1:50
2:00

10:05
Opacity
Sum 	

0
0

0

Averaqe
"X*-
0
0

0
            Readings were 0 percent opacity during all  periods  of observation.
ketch Showing How Opacity Varied With Time:
                                            C-53

-------
                                         Table 43

                                       FACILITY  F

                               SUMMARY OF VISIBLE EMISSIONS
Date: 8/26/76

Tyoe of Plant: Crushed stone (traprock)

Type of Discharge: Fugitive

Location of Discharge:  TWO tertiary  crushers  (#4 and #5)

HMoht of Point of Discharge:  #4-20  ft.     Distance  from Observer to Discharge Point: 100 ft.
   J'                           #5-10  ft.
Descriotion of Background:  Gray equipment   Height of Observation Point:  ground  level
                             Structures
Description of Sky:  Partly cloudy          Direction of Observer from Discharge Point: West
Wind  Direction: Variable

Color of Plume: No visible plume

Duration of Observation^ minutes
                         Wind Velocity: 0-5 mph

                         Peta^hed Plume:
Summary  of Data:

     Ooacity,
     Percent
         5
        10
        15
        20
        25
        30
        35
        40
        45
        50
Total Time Equal to or
Greater Than Given Opacity
   Min.Sec.
     0
0
               Opacity,
               Percent
 55
 50
 65
 70
 75
 80
 85
 90
 05
100
         Total Time Equal to or
         Greater Than Given Onacitv
                                                                    Min.
                                             Sec.
                                          C-54

-------
                                          Tabls 44

                                        FACILITY p

                                SUMMARY OF VISIBLE EMISSIONS
Date:  8/26/76

Tvoe of Plant: Crushed stone (traprock)

Type of Discharge: Fugitive

Location of Discharge:  Four processing screens
Height of Point of Discharge:  50  ft.

Descriotion of Background:gray walls

Description of Sky: Partly cloudy

Wind Direction: Variable

Color of Plume: NO  visible  plume

Duration of Observation:  180 minutes
                          Distance from Observer  to  Discharge Point:  100 ft

                          Height of Observation Point:  ground  level

                          Direction of  Observer from Discharge Point: NE

                          Wind  Velocity: 0-5 mph

                          Detached Plume:
 ummary  of Data:

    Ooacity,
    Percent
       5
      10
      15
      20
      25
      30
      35
      40
      45
      50
Total Time Equal to or
Greater Than Given Opacity
   Hin.Sec.
     0
Ooacity,
Percent
                                      55
                                      60
                                      65
                                      70
                                      75
                                      80
                                      85
                                      90
                                      05
                                     100
Total Time Equal to or
Greater Than Given Opacity
                    Sec.
                                         C-55

-------
                                         Tabln  45

                                       FACILITY F

                               SUMMARY OF VISIBLE EMISSIONS
late: 8/27/76

fvoe of Plant: Crushed  stone  (traprock)
                                                                            v

fyoe of Discharge: Fugitive

Location of Discharge:  Conveyor  transfer points

       of Point of Discharge:  75 ft.       Distance from Observer to Discharge Point: 150 ft.
Oescriotion of Background: Gray equipment   Height of Observation Point: 50  ft.
                             structures
Description of Sky:  Overcast

•lind Direction: Variable, S-SE

Color of Plume: No visible plume

Duration of Observation:179 minutes
                         Direction of Observer from Discharge Point:  SE

                         Wind Velocity:  0-10 mph

                         Detached Plume:
Summary of  Data:

     Ooacity,
     Percent
         5
        10
        15
        20
        25
        30
        35
        40
        45
        50
Total Time Equal to or
Greater Than Given Opacity
   Min.Sec.
     0
0
               Ooacitv,
               Percent
 55
 60
 65
 70
 75
 80
 85
 90
 %
100
         Total Time Equal to or
         Greater Than Given Onacitv
                                                                     Min.
                                              Sec
                                           C-56

-------
                                                46
                                         FACILITY  Gl

                                SUMMARY  OF VISIBLE  EMISSIONS
 Date:  9/27/75

 Tyoe of Plant: Feldspar

 Type of Discharge:  Fugitive

 Location of Discharge:  Priraary

 Height of Point of Discharge:  10-30 ft.    Distance from Observer to Discharge Point: 100 ft

 Descriotion of Background: Quarry wall &   . Height of Observation Point:  Ground level
                       equipment structures                                     level
 Descrintion of Sky:  Part]y cloudy          Direction of Observer from nischar.-  D,-n>f-S
Wind  Direction: Northeast

Color of  Plume:

Duration  of Observation:  60 minutes
                          Wind  Velocity: 0-10 mph

                          Detached  Plume: NO
Summary of Data:

     Ooacity,
     Percent
        5
       n
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   Hin.
    0
45
                nnacitv,
                Percent
                                      55
                                      60
                                      65
                                      70
                                      75
                                      80
                                      85
                                      90
                                      05
                                     100
Total Tine Equal to or
fire a ter Than Givgn_0 -> a c i t •
   Min.             S/?c~~~
                                          C-57

-------
                                         Tab!--  47

                                        FACILITY  Gl

                               SUMMARY  OF VISIBLE E'JISSIQ'IS
Date:  9/27/76

Tvoe of Plant:  Feldspar

Tyoe of Discharge:  Fugitive

Loc.it ion of  Discharge: Conveyor transfer point (#1)
Ihiq'it of  Point  of Discharge: 10 ft.

Oascriotion  of Background: Quarry wall

Hoscrintion  of Sky: Overcast

'•lind  Direction:  Northeast

Color of Plune:  No plume

Ourvition of Observation:   80 minutes
                         Distance from Observer to Discharge Point:50 ft.

                         Height of Observation Point: ground  level

                         Direction of Observer from Discharge Point: SE

                         Wind Velocitv: 0-5 mph

                         Detached Plun?: No
      ry  of Data:

      Ooacity,
         5
        10
        15
        20
        25
        30
        35
        40
        45
        50
Total Time Equal to or
Greater Than Given Qnacjty_
   Min.             Sec.
    0
                                       0
Onacitv,
Percent
  55
  60
  65
  70
  75
  80
  85
  90
  05
 100
Total Time Equal  to or
Greater Than Given Onacitv
                                                                     Mi n.
                               Sec.
                                            C-58

-------
                                           Table 48

                                         FACILITY 61

                                 SUMMARY  OF VISIBLE  EMISSIONS


 Date:  9/27/76

 Tyoe of Plant: Feldspar

 Type of Discharge: Fugitive

 Location of Discharge: conveyor transfer point  (#2)

 Height of Point of Discharge: 40 ft.        Distance fro. Observer to Discharge Point-  50 f1

 Descriotion of Background: Quarry wall      Height of Observation  Point:  ground level  '

 Description of s
-------
                                         Table 49

                                       FACILITY Gl

                               SUMMARY OF VISIBLE EMISSIONS
Date:  9/27/76

Tyoe of Plant:  Feldspar

Tyoe of Discharge-.Fugitive

Location of Discharge: Secondary crusher

Height of Point of  Discharge: 10-20 ft.     Distance from Observer to Discharge Point: 75 ft|

Description of  Background: Equipment       Height of Observation Point: 75 ft
                           structure
Description of  Sky: Partly cloudy -cloudy  Direction of Observer from Discharge Point:$SE
Mind Direction: Northwest

Color of  Plume: No visible plume

Duration  of Observation: 1 hour
                         Wind Velocity:  0-7 mph

                         Detached Plums: N/A
 Summary  of Data:

      Ooacity,
      Percent
         5
        10
        15
        20
        25
        30
        35
        40
        45
        50
Total Time Equal to or
Greater Than Given Opacity
   Min.             Sec.
    0
Opacity,
Percent
  55
  60
  65
  70
  75
  80
  85
  90
  95
 100
Total Time Equal  to or
Greater Than Given Onacitv
                                                                    Mi n.
                               Sec.
                                            C-60

-------
                                          TaV!.'>  50

                                        FACILITY Gl

                                Sin,"ARY OF VISIRLE  r.'HSS ITI
 Date:  9/27/76                          '

 Tyoe of  Plant:  Feldspar

 Tyoe of  Discharge:  Fugitive

 Location  of  Discharge:  Conveyor transfer Point (#4)

 Heiqht of Point  of  Discharge: 10 ft.        Distance  from  Observer  to  Discharge  Point: 84 ft.

 Description  of Background: CTiff or wall    Height  of Observation Point: 75 ft.

 Oescrintion  of Sky: cloudy

 Wind Direction:  North-

 Color of  Plume:  No visible plume

 Duration  of  Observation:  84 minutes
                          Direction of Observer  from Discharge Point: SE

                          Wind Velocity: 0-7 mph

                          Detached Plume: N/A
Summary of Data:

     Ooacity,
     Percent
        5
       10
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   f-1in.             Sec.
    0
0
                Onacitv,
                Percent
                                      55
                                      60
                                      65
                                      70
                                      75
                                      80
                                      85
                                      90
                                      05
                                     100
Total Time Equal to or
Greater Than Given Onacitv
   Mln.              Sec.
                                           C-61

-------
Run Number
Date
Test Time-minutes
Production rate - TPH
Stack Effluent
     Flow rate - ACFM
     Flow rate - DSCFM
     Temperature - °F
     Water vapor - Vol.%
Visible Emissions at
Collector Discharge -
Percent Opacity
Particulate Emissions
  Probe and Filter Catch
     gr/DSCF
     gr/ACF
     Ib/hr
     Ib/ton
  Total Catch
     gr/DSCF
     gr/ACF
     Ib/hr
     Ib/ton
Table 51
FACILITY G2
Summary of Results
1
9/28/76
120
5070
4210
105



2
9/28/76
120
4830
3940
115



3
9/29/76
120 „
4470
3720
103



Average

120
4790
3960
108
See Tables  52  -  61
0.005
0.004
0.17
0.005
0.004
0.17
0.005
0.004
0.18
0.005
0.004
0.18
0.004
0.004
0.14
0.004
0.004
0.14
O.OUJ
0.004
, 0.16
0.005
0.004
0.16
                                       C-62

-------
                               Summary of Visible .Emissi
 Date: 9/28/76

 Ty|je of Plane:      Feldspar

 Type of Discharge: Outlet Stack

 Location of  Discharge: No.2 Mill  Baghouse

 Height  of Point of  Discharge:100'

 Description  of Background: trees  on  hillside

 Description  of Sky: Overcast

Wind Direction: NW

u)lor of Plume: No visible  plume

Duration of Observation:  2-1/4 hours

              SUMMARY OF AVERAGE OPACITY
Distance from Observer to Discharq- Point-
     Approx.  40'
Height of Observation Point:
     Approx.  100'
Direction of Observer from Discharge,>oint: E
Wind Velocity: 0-10 mi/hr

Detached Plume: N/A
               SUMMARY OF AVERAGE OPACITY

Set Number
1
2
3
4
5
6
7
8
9
10
11
12
IA
3
14
15
16
I-^
7
18
1 f\
19
20
Time

Start End
09:48 09
09:54 10
10:00 10
10:06 10
10:12 10
10:18 10
10:24 10
10:30 10
10:36 10
10:42 10
10:48 10
10:54 M
11:00 11
11:06 11
11:12 11
:54
:00
:Q6
:18
:24
:30
:36
:42
:48
:54
:00
:06
:12
:18
11:18 11:24
11:24 11:30
11:30 11:36
11:36 11:42
Dpa
Sum
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
11:42 11:48 N
Sketch Showing How Opacity
QJ
O)
a.
~;
city
Average
N
N
N
N
N
N
N
N
N
N
N
N -
N
N
N
N
N
N
N
N
lime
Set Number Start End Sum
21 11:48 11:54 N
22 11:54 12:00 N
23 12:00 12:06 N
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Opacity
Average
N
N.-.
N
















Varied With Time:
C-63





-------
                                         TABLE 53
                                       FACILITY G2
                              Summary of Visible Emissions
                                                   «• •
Date: 9/29/76
Type of Plant:     Feldspar
Type of Discharge: Outlet Stack
Location of Discharge: No.2  Mill  Baghouse
Height of Point of Discharge: T00'
Description of Background: hillside with trees
Description of Sky: Cloudy
Wind Direction:  NE                          Wind  Velocity: 0-5 mi/hr
Color of Plume: No visible plume             Detached  Plume: N/A
Duration of Observation: 2 hrs.
              SUMMARY  OF AVERAGE OPACITY
                           Distance from Observer to Discharge Point:
                               approx.  50'
                           Height of Observation Point:
                               same level as discharge   -
                           Direction of Observer from Discharge Point:
                                          SUMMARY OF AVERAGE OPACITY
                                                                 Time
Time
Opacity
Opacity
Set Number   Start    End
          Sum
    Average   Set Number    Start    End    Sum    Average
1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
08:35
08:41
08:47
08:53
08:59
09:05
09:11
09:17
09:23
09:29
09:35
09:41
09:47
09:53
09:59
10:05
10:11
10:17
10:23
10:29
08:40
08:46
08:52
08:58
09:04
09:10
09:16
09:22
09:28
09:34
09:40
09:46
09:52
09:58
10:04
10:10
10:16
10:22
10:28
10:34
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
.N
21 10:35 10:37 N N .
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
 Sketch Snowing How Opacity Varied With Time:
        c
        CD
        u
        OJ
        a.

-------
                                          TAB Li: 54

                                        FACILITY 62
                               Summary of Visible Emissions
 Date:   9/28/76
 Type  of Plant:      Feldspar

 Type  of Discharge: Outlet Stack

 Location of Discharge: No.2 Mill  Baghouse

 Height  of Point  of  Discharge:  100'

 Description  of Background:  grassy hillside

 Description  of Sky:  partly cloudy

Wind Direction: NW

Color of Plume: No visible plume

Duration of Observation: approx.  2-1/4 hrs.

              SUMMARY OF AVERAGE OPACITY
Distance from Observer to Discharge Point:
      Approx.  40'  SE
Height of Observation Point: Approx. 100'

Direction of Observer from Discharge Point: SE
Wind Velocity: 0-15 mi/hr

Detached Plume: N/A
                                                            SUMMARY OF AVERAGE, OPACITY

                                                                               pacity

                                                                                  Average
                                                                                     N
                                                                                     N

Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Opacity
Start End
14:48 14
14:54 15
15:00 15
15:06 15
15:12 15
15:18 15
:54
:00
:06
: 12
:18
:24
15:24 15:30
15:30 15:36
15:36 15:42
15:42 15:48
15:48 15:54
15:54 16:00
16:00 16:06
16:06 16:
16:12 16:
16:18 16:
16:24 16:
16:30 16:
16:36 16:
12
18
24
30
36
42
16:42 L6:43
Sketch Showing How Opacity
•*->
0)
0
i-
OJ
Q.
^
Sum
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
Varied
Average
N
N
N
N
N
N
N
N
N
• • N
N
N
N
N
-. N
N
N
N
N
N
With Time:
Time
bet Number Start End Sun
2J 16:48 16:54 N
22 16:54 17:00 N
90.
25

27
28
29
•an
•31
op
0-3
oo
34
35
OC
OD
37
38
39
40

C-65

-------
                                          Tab!" 55

                                        FACILITY 62

                                SUMMARY  OF VISIBLE EMISSIONS
Date:  9/28/76

Tyoe of  Plant:  Feldspar

Tyos of  Discharge:  Fugitive

Location of Discharge:  Ball mill (feed end)

Heiqht of Point of  Discharge: 20 ft.

Descriotion of Background: Building &
                            Equipment
Description of Sky: N/A

Wind Direction:  N/A

Color of Plume: No visible plume

Duration of Observation:  1 hour
                         Distance from Observer to Discharge Point: 35 ft.

                         Height of Observation Point:

                         Direction of Observer from Discharge Point: N/A

                         Wind Velocity: N/A

                         Detached Plume: N/A
Summary of Data:

     Ooacity,
     Percent
        5
       10
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   Mi n.             Sec.
                    0
Ooacitv,
Percent
  55
  60
  65
  70
  75
  80
  85
  90
  05
 100
Total Time Equal  to or
Greater Than Given  Ooacitv
   Min.Sec.
                                          C-66

-------
                                           Tab!s  56

                                         FACILITY G2

                                SUMMARY  OF VISIBLE  E'lISSIO'-IS
 Date:  9/28/76

 Tyoe of Plant: Feldspar

 Type of Discharge: Fugitive

 Location of Discharge: Ball  mill  (discharge end)
 Height of Point of Discharge: 20 ft.

 Oescriotion of Background: Building and

 Oescriotion of Sky:  N/A    equi'Pment

 Wind  Direction:  N/A

 Color of  Plume: NO visible plume

 Duration  of Observation:  i  hour
Distance from Observer to Discharge Point: «
                                           Ob
Height of Observation Point:

Direction of Observer from Discharge Point:N/A

Wind Velocity: N/A

Detached Plume: N/A
                                                                        -.
                                                                        T L
Summary of Data:

     Ooacity,
     Percent
        5
       10
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   Hin.Sec.
          •Ooacitv,
          Percent
                                      55
                                      60
                                      65
                                      70
                                      75
                                      80
                                      85
                                      90
                                      
-------
                                         Table  57

                                       FACILITY  G2

                               SUMMARY OF VISIBLE EMISSIONS
Date:  9/28/76

Tyoe of Plant: Feldspar

Tyoe of Discharge: Fugitive

Location of Discharge: Indoor transfer point  (#1)
Height of Point of Discharge:
                         Distance from Observer to Discharge Point:
Description of Background: Building wall    Height of Observation Point:
Description of Sky: N/A

'•find Direction: N/A

Color of Plume: No visible plume

luration of Observation: i hour
                         Direction of Observer from Discharge Point:

                         Wind Velocity: N/A

                         Detached Plume:N/A
>ummary of Data:

     Ooacity,
     Percent
        5
       10
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   Min.Sec.
    0
0
               Onacitv,
               Percent
                                      55
                                      60
                                      65
                                      70
                                      75
                                      80
                                      85
                                      90
                                      05
                                     100
Total Time Equal to or
Greater Than Given Onacitv
   Mi n.             Sec.
                                          C-68

-------
                                           Tnbl"  58

                                         FACILITY  G2

                                SUMMARY  OF VISIBLE EMISSIONS
 Date:  9/28/76

 Tvoe of Plant: Feldspar

 Type of Discharge: Fugitive

 Location of Discharge: Indoor  transfer point (#2)

 Height  of Point of Discharge:
                          Distance fror. Observer to  Discharge  Point:
 Descriotion  of Background: Building wall    Height of Observation  Point:
 Description  of Sky: N/A

 Wind  Direction:  N/A

 Color of  Plume:  No visible plume

 Duration  of  Observation: 1 hour
                          Direction  of  Observer  from Discharge Point:.N/A

                          Wind  Velocity: N/A

                          Detached Plune: N/A
Summary of Data:

     Ooacit.y,
     Percent
        5
       10
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
Onacitv,
Percent
                                    55
                                    60
                                    65
                                    70
                                    75
                                    80
                                    85
                                    90
                                    H5
                                  100
Total Time Equal to or
Greater Than Given Onacitv
        "         '
                                          C-69

-------
                                        FACILITY  G2

                               SUMMARY  OF VISIBLE  EMISSIONS
Date:  9/28/76

Tyoe of Plant:  Feldspar

Tyoe of Discharge: Fugitive

Location of Discharge: Indoor Bucket Elevator

H2iqlit of Point of Discharge:              Distance from Observer to Discharge Point:

Description of Background: Building walls   Height of Observation Point:

Description of Skv: N/A                    Direction of Observer from Discharge Point: N/A

Wind Direction: N/A                        Wind Velocity: N/A

Color of Plume: NO visible plume           Detached Plume: N/A

Duration of Observation: l hour
Summary of Data:

     Ooacity,
     Percent
        5
       T)
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   Min.Sec.
    0
0
               Onacitv,
               Percent
                                      55
                                      60
                                      65
                                      70
                                      75
                                      80
                                      85
                                      90
                                      05
                                     100
Total Time Equal  to or
Greater Than Given  Onacit
                                                                   Min.
                                                                  Sec.
                                          C-70

-------
                                           Tab!ft  go

                                         FACILITY G2

                                 SUMMARY  OF VISIBLE  EMISSIONS
 Date:  9/28/76

 Tvoe of Plant: Feldspar

 Type of Discharge: Fugitive

 Location of Discharge: Truck loading

 Height of Point of Discharge:  15  ft.

 Description of Background: Building wall

 Description of Sky:  N/A

 Wind  Direction: N/A

 Color  of Plume:   N/A

 Duration  of Observation:  13 minutes
Summary of Data:

     Ooacity,
     Percent
                          Distance from Observer to  Discharge  Point: 30 ft

                          Height of Observation  Point: ground level

                          Direction of Observer  from Discharge Point-  c
                                                           "*     .   * .. £.
                          Wind  Velocity: N/A

                          Detached Plume: N/A
        5
       10
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   Min.'             Sec.

    0               n
-Opacity,
Percent
                                      55
                                      60
                                      65
                                      70
                                      75
                                      80
                                      85
                                      90
                                      05
                                     100
Total Time Equal  to or
Greater Than Given  bnac'itv
   Min.             Sec.—
                                         071

-------
                                         Tab!ft  61

                                       FACILITY  62

                               SUMMARY OF VISIBLE EMISSIONS
Date:  9/28/76

Tyoe of Plant: Feldspar

Type of Discharge: Fugitive

Location of Discharge: Railroad car loading

Height of Point of Discharge: 15 ft.

Descriotion of Background: Building wall

Description of Sky: Cloudy

Mind Direction: N/A

Color of Plume: N/A

Duration of Observation: 32 minutes
                         Distance from Observer to Discharge Point: 25 ft.

                         Height of Observation Point: ground level

                         Direction of Observer from Discharge Point: E

                         Wind Velocity: N/A

                         Detached Plume: N/A
Summary of Data:

     Ooacity,
     Percent
        5
       10
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   Min;Sec.
    5
    0
15
 0
               Opacity,
               Percent
 55
 60
 65
 70
 75
 80
 85
 90
 05
100
          Total  Time Equal  to or
          Greater Than Given  Onacitv
                                                                    Min.
                                              Sec.
                                          C-72

-------
                                          Tabls  62
                                        FACILITY  HI
                                SUMMARY  OF VISIBLE  EMISSIONS

Date:  10/27 -  28/76
Tyoe of Plant:  Gypsum
Type of Discharge: Fugitive (leaks)
Location of  Discharge: Hammermill
Height of Point of Discharge: Leaks      Distance from Observer  to  Discharge Point:  25  ft.
Descriotion  of  Background:inside plant   Height of Observation Point: ground level
Description  of  Sky:  N/A                 Direction of Observer from Discharge Point: $W
Wind Direction: N/A                      Wind Velocity: N/A
Color of Plume:  White                    Detached Plume:  N/A
Duration of  Observation:   298 minutes

Summary of Data:
Ooacity,
Percent

5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
1
0
0
-






or
Opacity
Sec.
45
15
0







Opacity, Total Time Equal to or
Percent Greater Than Given Onacitv
Min. Sec.
55
60
65
70
75
80
85
90
05
100
                                         C-73

-------
Data
Test Time-minutes
Production rate - TPH
Stack Effluent
     Flov/ rate - ACFM
     Flow rate - DSCFM
     Temperature - °F
     '.•later vapor - Vol.*
 Visible Emissions at
 Collector Discharge -
 Percent Opacity
 Particulate Emissions
   Proba  and Filter Catch
      gr/DSCF
      gr/ACF
       Ib/hr
       Ib/ton
    Total  Catch
       gr/DSCF
       gr/ACF
       Ib/hr
       l.b/ton
                                        Table 63
                                       FACILITY  H2
                                  Summary of :'.csi;!':s
                                              1
10/27/76   10/27/76   10/28/76
88         88         88
4,548
3,542
145.4
4.6

0.071
0.055
2.16
0.073
0.057
2.53
4,364
3,486
147.0
1.8
See Table 64
0.063
0.050
1.87
0.064
0.051
2.40
4,306
3,423
145.3
2.6

0.066
0.053
1.94
0.068
0.054
2.65
                                                                               Average
88
                                       0.067
                                       0.053
                                       1.99
                                       0.068
                                       0.054
                                       2.53
                                          C-74

-------
                                         TAB If: 64
                                       FACILITY H2
                              Summary of Visible Emissions
Date: 10/27/76
Type of Plant: Gypsum board manufacturer
Type of Discharge:  Stack
Location of Discharge:  Above plant  roof
Distance from Observer to Discharge Point:  25 ft.
Height of Observation Point: roof level .
Height of Point of Discharge: 6'  above  roof   Direction of Observer from Discharge Pointr
                                                 225° (S.W.)
Description of Background: Sky
Description of Sky: Clear
Wind Direction: 0° (N)
Color of Plume: White
Duration of Observation:  87 Min
              SUMMARY OF AVERAGE OPACITY
Wind Velocity: ~  10 mph
Detached Plume: No
               SUMMARY OF AVERAGE OPACITY


Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Sketch









1
Start
1312
1357
1403
1409
1415
1421
1427
1433
1439
1445
1451
1457
1503
1509
1515










Showing
-M
C
0)
J_
o>
o.
£
•f—
o
jOQ
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00





How
ime
End
1316:
1402:
1408:
1414:
1420:
1426:
1432:
1438:
1444:
1450:
1456:
1502:
1508:
1514:
1519:





Opacity

45
45
45
45
45
45
45
45
45
45
45
45
45
45
05





Opacity
Sum
125
155
135
150
140
125
135
130
125
115
95
70
80
85
60





Varied
Average
6
6
5
6
5
5
5
5
5
4
3
2
3
3
3





With
.25
.46
.62
.25
.83
.21
.62
.42
.21
.79
.96
.92
.33
.54
.53





Time:
Time Opacity
Set Number Start End Sum Average
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40

C-75

-------
                                         TABLE 64 (con't)
                                       FACILITY  H2
                              Summary of Visible Emissions
Date: 10/27/76
Type of Plant: Gypsum board manufacturer
Type of Discharge: Stack
Location of Discharge: Above  plant roof
Distance from Observer to Discharge Point:25 ft.
Height of Observation Point: roof level
Height of Point of Discharge: 6'  above roof   Direction of Observer from Discharge Point:
                                                225   (S.W.J
Description of Background: Sky
Description of Sky: Clear
Wind Direction: 45° (N.E.)
Color of Plume: White
Duration of Observation:  92 min.
              SUMMARY  OF  AVERAGE OPACITY
Wind Velocity: - io-15 mph
Detached Plume:  NO
               SUMMARY OF AVERAGE OPACITY
Time
Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Start
0830 :QO
0836:00
0842:00
0848:00
0957:00
1003:00
1009:00
1015:00
1021:00
1027:00
1033:00
1039:00
1045:00
1051:00
1057:00
1103:00
1109:00



End
0835:45
0841:45
0847:45
0849:00
1002:45
1008:45
1014:45
1020:45
1026:45
1032:45
1038:45
1044:45
1050:45
1056:45
1102:45
1108:45
1110:45



Opacity
Sum
45
65
70
5
125
60
80
85
.75
70
85
95
90
90
70
55
25



Average
1.87
2.71
2.92
1.00
5.21
2.50
3.33
3.54
3.12
2.92
3.54
3.96
3.75
3.75
2.92
2.29
3.12



Time Opacity
Set Number Start End Sum Average
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
 Sketch Showing How Opacity Varied With Time:
        c
        CJ
        u
        i_
        o
        o.
                                              C-7fi

-------
                                         TABLF 64 (con't)
                                       FACILITY  H2
                              Summary of Visible Emissions
Date: 10/28/76
type of Plant:  Gypsum board manufacturer
Type of Discharge:  Stack                   Distance  from Observer to Discharge Point: 25 ft-
.ocation of Discharge:  Above plant roof     Height of Observation Point:  roof level
teight of Point of  Discharged1  above roof  Direction of Observer from Discharqp Point-
                                             225° (S.W.)                           '  "
description of Background:  Sky
Ascription  of Sky:  Clear
Jind  Direction: 180° (S)
)o1or of Plume: White
Jurat ion of  Observation:  87 min
Wind Velocity: ~ 10 mph
Detached Plume: No


let Number
1
2
3
4
5,
6
7
8
9
10 .
11
12
13
14
15
16 ,
17
18
19
20
bUIW
1
Start
0830:00
0930:00
0936:00
0942:00
0948:00
0945:00
1000:00
1006:00
1012:00
1018:00
1024:00
1030:00
1036:00
1042:00
1048:00




„
\KY OF AV
Tine
End
0835:45
0935:45
0941 :45
0947:45
0953:45
0959:45
1005:45
1011:45
1017:45
1023:45
1029:45
1035:45
1041:45
1047:45
1050:45





ERAGE
OPACITY

Opacity
Sum
40
95
85
65
70
60
90
40
30
25
40
60
25
70
10





Average
1.67
3.96
3.54
2.71
2.92
2.50
3.75
2.50
1.25
1.04
1.67
2.50
1.04
2.92 '
0.83





Set Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
SUMMARY OF AVERAGE OPACITY
Time Opacity
Start End Sum Average




~















ketch Showing How Opacity Varied With Time:
      OJ
      u
      
-------
                                         Tab!* 65

                                       FACILITY I

                               SUMMARY OF VISIBLE EMISSIONS
Oate:  9/30/76

Tyoe of Plant:  Mica "

Tyoe of Discharge: Fugitive

Location of Discharge:  Bagging Operation

Heiflht of Point of Discharge: 3 ft.

Oescriotion of  Background: Indoors

Doscrintion of  Sky: N/A

Wind  Direction: N/A

Color of  Plume: N/A.

Duration  of Observation: 1 hour
 Summary of Data:

      Ooacity,
      Percent
                         Distance  from  Observer to Discharge Point: 7 ft.

                         Height of Observation Point:  ground level

                         Direction of Observer from  Discharge Point:  N/A

                         Wind Velocity: N/A

                         Detached Plume: N/A
         5
        10
        15
        20
        25
        30
        35
        40
        45
        50
Total Time Equal to or
Greater Than Given Opacity
   RTruSec.
                       0
                     0
Opacity,
Percent
  55
  60
  65
  70
  75
  80
  85
  90
  05
 100
Total Time Equal  to or
Greater Than Given Onacitv
   Mi n.             Sec.
                                            C-78

-------
                                         Tab!ft 66

                                       FACILITY Jl

                               SUMMARY OF VISIBLE EMISSIONS
Date:  10/20 - 21/76

Tyoe of Plant: Talc

Type of Discharge: Fugitive (leaks)

Location of Discharge: Vertical  mill

Height of Point of Discharge:  In room

Descriotion of Background: ceiling

Description of Sky: N/A

Wind Direction: N/A

Color of Plume: White

Duration of Observation:  90 minutes
Summary of Data:

   „  Ooacity,
     Percent
                         Distance from Observer to Discharge Point: 10 ft.

                         Height of Observation Point:  Floor

                         Direction of Observer from Discharge Point:W

                         Wind Velocity:  ^/A

                         Detached Plume: N/A                            ';
        5
       10
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   Min.Sec.
Onacitv,
Percent
                                      55
                                      60
                                      65
                                      70
                                      75
                                      80
                                      85
                                      90
                                      H5
                                     100
Total Time Equal  to or
Greater Than Given Onacitv
                                                                    Min.
                               Sec.
                                          C-79

-------
                                         Table 67

                                       FACILITY Jl

                               SUMMARY OF VISIBLE EMISSIONS
Date:  10/20/76

Tvoe of Plant: Talc

Type of Discharge:  Fugitive

Location  of  Discharge: Primary crusher

Height of Point  of Discharge: In room

Oescriotion  of Background:  wall

Description  of Sky:  N/A

Mind  Direction:  N/A

Color of Plume:   White

Duration of Observation:  go minutes


Summary  of Data:
Distance from Observer to Discharge Point:  5 ft

Height of Observation Point:  Floor

Direction of Observer from Discharge Point:w

Wind Velocity: N/A

Detached Plume: N/A
Ooacity,
Percent

5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
20
8
1
0






or
Opacity^
Sec.
15
0
15







                                                       Opacity,
                                                       Percent
                                                         55
                                                         <50
                                                         65
                                                         70
                                                         75
                                                         80
                                                         85
                                                         90
                                                         05
                                                        100
                      Total Time Equal to or
                      Greater Than Given Onacltv
                                                                     Min.
                                          Sec.
                                            C-80

-------
                                          Tablr? 68
                                        FACILITY Jl
                                SUMMARY OF VISIBLE EMISSIONS
 Date:  10/20 - 21/76
 Tyoe of  Plant:  Talc
 Type of  Discharge:  Fugitive
 Location of Discharge:  Secondary crusher
 Height of Point  of  Discharge:  jn room
 Descriotion of Background: wall
 Description of Sky: N/A
Wind Direction:  N/A
 Color of Plume:  White
 Duration  of Observation: 150 minutes
Summary of  Data:
Distance from Observer to Discharge Point:  5 ft.
Height of Observation Point: floor
Direction of Observer from Discharge Point:s
Wind Velocity:  N/A
Detached Plume: N/A
Ooacity,
Percent

5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Mi n .
3
0
0
~






or
Opacity
Sec.
45
15
0
~






•Opacity, Total Time Equal to or
Percent Greater Than Given Onacitv
Mln. Sec .
55
+j j
60
65
70
75
80
85
90
05
TOO
                                          C-81

-------
                                        Tab!* 69
                                      FACILITY Jl
                              SUMMARY OF VISIBLE EMISSIONS
Oate:  10/19 - 21/76
Tyoe of Plant: Talc
Tyoe of Discharge: Fugitive
Location of Discharge: Bagger
Height of Point of Discharge: In room
Oescriotion of Background:  wall
Description of Sky: N/A
Wind-Direction: N/A
Color of Plume:    White
Duration of Observation:  150 minutes

Summary of Data:
Distance from Observer to  Discharge Point:  10 ft.|
Height of Observation  Point: floor
Direction of Observer  from Discharge. Point: W
Wind Velocity: N/A
Detached Plume: N/A
Opacity,
Percent

5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Hin.
12
5
3
2
2
2
1
1
1
1
or
Opacity
Sec.
45
15
0
15
0
0
30
30
15
15
Opacity,
Percent

55
60
-65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given
Min.
0
0
0
0
0
_




Opacity
Sec.
45
45
15
15
0
—




                                         C-82

-------
                                          Tabls  70

                                        FACILITY Jl

                                SUMMARY OF VISIBLE EMISSIONS
 Date:  10/19/76

 Tyoe of  Plant: Ta-|c

 Type of  Discharge:  Fugitive

 Location of  Discharge:  pebble Mill No. 2

 Height of Point  of  Discharge: in room

 Description  of Background: Wall

 Description  of Sky: N/A

 Wind Direction:  N/A

 Color of Plume:  white

 Duration of  Observation:  90 minutes
Summary of Data:

     Opacity,
     Percent
                          Distance from Observer to Discharge Point: lo ft.

                          Height of Observation Point: floor

                          Direction of Observer from Discharge Point:w

                          Wind Velocity: N//\

                          Detached Plume: N/A
        5
       n
       15
       20
       25
       30
       35
       40
       45
       50
Total Time Equal to or
Greater Than Given Opacity
   Mi n.             Sec.
    5
    0
    0
 0
45
 0
                •Opacity,
                 Percent
 55
 SO
 65
 70
 75
 80
 85
 90
 95
100
          Total Time Equal  to or
          Greater Than Given Opacity
                              sec.
                                          C-83

-------
Run Jtober
Date
Test Tirce-fflinutes
Production rate - TPH
Stack Effluent
     Flow rate - ACFM
     Flow rate - OSCFH
     Temperature - °F
     Hater vapor - Vol.%
Visible Emissions  at
Collector Discharge -
Percent Opacity
 Particulate  Emissions
   Probe and  Filter Catch
      gr/DSCF
      gr/ACF
      Ib/hr
      Ib/ton
   Total Catch
      gr/DSCF
      gr/ACF
      Ib/hr
      Ib/ton
Table 71
FACILITY J2
iry of Results
1 2
10/20/76 10/20/76
120 120
21 ,100 21 ,300
20,200 20,200
80 83
0.3 . 0.3
See Table 72
0.047 0.068
0.045 0.065
8.17 11.8
0.065 0.071
0.062 0.067
11.2 12.2


3
10/21/76
120
21 ,300
19,500
82
1.0

0.067
0.061
11.2
0.068
0.062
11.3
                                                                             - Average
 120
 21,200
 20,000
     82
   '0.5
 0.061
 0.057
10.4
 0.068
 0.064
11.6
                                        C-84

-------
                                          TABLF: 72
                                        FACILITY  J2
                               Summary  of Visible  Emissions
Date: 10/21/76

Type of Plant: Talc

Type of Discharge:  Stack

Location of Discharge:  Baghouse  Outlet

Height of Point of Discharge:30'

Description of Background:  Hills and trees

Description of Sky:  Overcast  - rain

Wind Direction:  60°  NE

Color of Plume: White

Duration of Observation: Approx. 2 hrs.

              SUMMARY OF AVERAGE OPACITY
Distance from Observer to Discharge Point:
      approx.  100'
Height of Observation Point:
      approx.  36'
Direction of Observer from Discharge Point:
      160° SE
Wind-Velocity: 8_12 mi/hr - Gust up to 20

Detached Plume: N/A




               SUMMARY OF AVERAGE OPACITY

Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20 *
T
Start
08:00
08:06
08:12
08:18
08:24
08:30
08:36
08:42
08:48
08:54
09:00
09:06
09:12
09:18
09:24
09:30
09:36
09:42
09:48
09:-54
ime
End
08:06
08:12
08:18
08:24
08:30
08:36
08:42
08:48
08:54
09:00
09:06
09:12
09:18
09:24
09:30
09:36
09:42
09:48
09:54
10:00
Opacity
Sum
10
0
0
5
0
5
5
0
0
0
5
10
15
5
5
5
5
0
5
5
Average
0.4
0
0
0.2
0
0.2
0.2
0
0
0
0.2
0.4
0.6
0.2
0.2
0.2
0.2
0
0.2
0.2
Time Opacity
Set Number Start End Sum
21 10:00 10:05 0
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Average
0



















Sketch Showing How Opacity Varied With Time:
       GJ
       O
       
-------
                                         TABLE 72 (con't)
                                       FACILITY  J2
                              Summary of Visible Emissions
Date:   10/20/76
Type of Plant: Talc
Type of Discharge: Stack
Location of Discharge: Baghouse  Outlet
Height of Point of Discharge: 30'
Description of Background: Hills and  trees
Description of Sky: Overcast - Rain
Wind Direction:  290° NW
Color of Plume:  White
Duration of Observation:  2:05 min.
       .:       SUMMARY OF  AVERAGE OPACITY
Distance from Observer to Discharge Point:  100'
Height, of Observation Point:approx. 36'
Direction of Observer from Discharge Point:
         160°  SE
Wind Velocity: 4-7 mi/hr
Detached Plume: N/A
               SUMMARY OF AVERAGE OPACITY
                                 Opacity
                   Time
Opacity
ime
Set Number    Start   End.    Sum    Average    Set Number    Start     End    Sum    Average
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20 •
12:54
13:00
13:06
13:12
13:18
13:24
13:30
13:36
13:42
13:48
13:54
14:00
14:06
14:12
14:18
14:24
14:30
14:36
14:42
14:48
13:00
13:06
13:12
13:18
13:24
13:30
13:36
13:42
13:48
13:54
14:00
14:06
14:12
14:18
14:24
14:30
14:36
14:42
14:48
14:54
0
0
0
5
5
10
5
5
15
15
5
0
5
0
5
0
5
5
0 '
0
0
0
0
0.2
0.2
0.4
0.2
0.2
0.6
0.6
0.2
0
0.2
0
0.2
0
0.2
0.2
0
0
21 14:54 14:59 0 0
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
 Sketch Showing How Opacity Varied With Time:
        O)
        o
        O)
                                             C-86

-------
                                          TABLC 72 (con't)
                                        FACILITY J2
                               Summary  of  Visible  Emissions
Date:  10/20/76

Type of Plant: Talc

Type of Discharge: Stack

Location of Discharge: Baghouse Outlet

Height of Point of Discharge:  30'

Description of Background: Hills and trees

Description of Sky:  Overcast

Wind Direction: 290° NW

Color of Plume: White

Duration of Observation: 2:22 min.

              SUMMARY OF AVERAGE OPACITY
                                      Distance from Observer to Discharge Point:
                                             approx. 100'
                                      Height of Observation Point:
                                             approx. 36'
                                      Direction of Observer from Discharge Point:
                                             160  SE
                                      Wind Velocity: 4-7 mi/hr

                                      Detached Plume: N/A
                                                     SUMMARY OF AVERAGE OPACITY
Time
Set Number
1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
Start
08:35
08:41
08:47
08:53
08:49
09:05
09:11
09:17
09:23
09:29
09:35
09:41
09:47
. 09:53
09:59
10:05
10:11
10:17
10:23
10J29
End
08:41
08:47
08:53
08:59
09:05
09:11
09:17
09:23
09:29
09:35
09:41
09:47
09:53
09:59
10:05
10:11
10:17
10:23
10:29
10:35
Opacity
Sum
0
5
5
5
5
5
10
5
5
5
0
10
0
0
5
5
10
5
0
10
Average
0
0.2
0.2
0.2
0.2
0.2
0.4
0.2
.0.2
0.2
0
0.4
0
0
0.2
0.2
0.4
0.2
0
0.4
Set Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Time Opacity
Start End Sum Average
10:35 10:41 5 0.2
10:41 10:47 5 0.2 .
10:47 10:53 10 0.4
10:53 10:58 5 0.25
















Sketch Showing  How  Opacity  Varied With  Time:
c
o

a.
 •*
>,
                                             C-87

-------
 Test  Tiria-firinutes

 Production rate -  TPH

 Stack Effluent

      Fle'i rate - ACFM

      Flow rate - G5CFM

      Temperature - °F

      Hater vapor T Vol.%

 Visible Emissions at
.;Col lector Discharge  -
 Percent Opacity
 %     * t    V
 Particiilate -Enilsslons
Table 73
FACILITY K
jry of Insults
1 2
6/21/77 6/21/77
120 120
4,567 4,113
3,637 3,196
135.3 152.3
1.69 1.36
See Table 74
0.024 0.027
0.020 0.022
0.75 0.75



3
6/22/77
120
4,579
3,646
136.8
1.63

0.041
0.034
1.29
                                                                                Average
                                                                                 120
4,420

3,493

141.5

  1.56
Prohs and Filter Catch
' gr/DSCF • ' •
gr/ACF*
Ib/hr
Tb/ton
Total Catch
gr/DSCF
gr/ACF
Ib/hr '
Ib/ton

0.024 0.027 0.041 0.031
0.020 0.022 0.034 0.025
0.75 0.75 1.29 0.93
- - -





                                         C-88

-------
                                          TABLE  74
                                        FACILITY K
                               Summary of Visible Emissions
 Date:   6/20 - 6/21/71
 Type of Plant: Talc
 Type of Discharge:  Stack
 Location of Discharge: Pebble mill
 Height  of Point  of  Discharge: 40 ft.
 Description of Background: Equipment  and  Mountain
 Description of Sky: Clear
                           Distance from Observer to Discharge Point: 125 ft,
                           Height of Observation Point:25  ft.
                           Direction of Observer from Discharge Puint: W
Wind Direction: North
Color of Plume:  White
Duration of Observation:
                           Wind Velocity:  5  mph
                           Detached Plume: N/A
              SUMMARY OF AVERAGE OPACITY
                               Opacity
Time
SUMMARY OF AVERAGE OPACITY
                  Opacity
                                               lime
Set Number   Start   End    Sum    Average   Set Number     Start
                                                  End
               Sum    Average
1
2
3
4
5
6
7
8
9
10
n
12
1 O
13
1 C
15
16
17
18
19
20
1314
1320 '
1326
1332
1338
1344
1350
1356
1402
1408
1417
1423
1429
1435
1441
1447
1453
1459
1505
1511
1320
1326
1332
1338
1344
1350
1356
1402
1408
1414
1423
1429
1435
1441
1447
1453
1459
1505
1511
1517
80
10
5
10
10
0
5
0
5
5
5
5
5
10
5
0
0
5
0
10
3.33
0.42
0.21
0.42
0.42
0.0
0.21
0.0
0.21
0.21
0.21
0.21
0.21
0.42
0.21
0.0
0.0
0.21
0.0
0.42
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
802
808
814
820
826
832
838
844
850
856
903
909
915
921
927
933
939
945
951
957
808
814
820
826
832
838
844
850
856
902
909
915
921
927
933
939
945
951
957
1003
10
5
5
30
0
0
40
75
50
65
35
20
55
25
55
55
30
55
70
40
0.42
0.21
0.21
1.25
0.0
0.0
1.67
3.13
2.;08
2.32
1.46
0.83
2.29
1.04
2.29
2.29
1.24
2.29
2.92
1.67
Sketch Showing How Opacity Varied With Time:
       O)
       u
       Ol
       O-
                                           C-89

-------
                                         TABLE 74 (con't)
                                       FACILITY K
                              Summary of Visible Emissions
Date: 6/20 - 6/21/71
Type of Plant: Talc
Type of Discharge: Stack
Location of Discharge: Pebble Mill
Height of Point of Discharge:  40 ft.
Description of Background: Equipment and Mountain
Description of Sky: Clear
Wind Direction: North                        Wind Velocity: 5 mph
Color of Plume: White                        Detached  Plume: N/A
Duration of Observation:
Distance from Observer to Discharge Point:125 ft]
Height of Observation Point: 25 ft.
                               ^
Direction of Observer from Discharge Point:  W
SUMMARY OF AVERAGE
Time
Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Start
1004
1208
1214
1220
1226
1232
1238
1244
1250
1256
1302
1313
1319
1325
1331
1337
1343
1349
1355
HOI
End
1009
1214
1220
1226
1232
1238
1244
1250
1256
1302
1308
1319
1325
1331
1337
1343
1349
1355
1401
1407
OPACITY
Opacity
Sum
30
105
no
85
90
125
85
105
95
25
65
95
105
40
30
60
55
35
5
75
Average
1.25
4.38
4.58
3.54
3.75
5.21
3.54
4.38
3.96
1.32
2.95
3.96
4.38
1.67
1.30
2.61
2.29
1.94
0.36
3.13
SUMMARY OF AVERAGE OPACITY
Time Opacity
Set Number Start End Sum
21 1407 1413 125
22
23
24
25
26
27
28
29
30 .
31
32
33
34
35
36
37
38
39
40
Average
5.21



















 Sketch Sftowing How Opacity Varied With Time:
       o
       o
       o.
                                            C-90

-------
 Run  Number
 Date
 Test Time  - Minutes
 Production Rate - TPH
 Stack Effluent
   Flow rate - ACFM
   Flow rate- DSCFM
   Temperature - °F
   Water vapor - Vol . %

Visible Emissions at
Collector Discharge -
% Opacity
Parti cul ate Emissions
   Probe and Filter catch
        gr/DSCF
        9r/ACF
        Ib/hr
        Ib/ton
                                 TABLE  75
                                FACILITY LI
                           Summary of Results
                                      1*
                                    12/6/78
                                       60


                                    17180
                                    14040
                                      136
                                        7.4
                                   4.53
                                   545
   Total catch
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton
* Test conducted concurrently with Run 2, Table 76.
(1) No analysis of back-half on in-stack filter tests,
                                 C-91

-------
Run Number
Date
Test. Time - Minutes
Production Rate - TPH
Stack Effluent
   Flow rate - ACFM
   Flow rate- DSCFM
   Temperature - °F
   Water vapor - Vol . %

Visible Emissions at
Collector Discharge  -
%  Opacity
Parti oil ate Emissions
   Probe and Filter  catch
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton
   Total
                               TABLE 76
                              FACILITY LI
                         Summary of Results
                                    1
                                  12/6/78
                                    96
  2*           3       Average
12/6/78      12/6/68
  96           96    "     96
17690
14790
131.
7.0
see
Table
77
17960
14650
141.
7.8

-

18060
15080
141.
5.4

-

17903
14840
138
6.7

-

0.020
0.017
2.49
0.012
0.010
1.54
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton
*Test conducted concurrently with Run 1,  Table 75.
(1) No analysis of back-half on in-stack  filter tests,
                                                          0.016       0.016
                                                          0.013       0.013
                                                          2.01        2.01
                                 C-92

-------
                                  TABLE 77
                                 FACILITY LI
                      Summary of Visible Emissions
Date:  12/6/78
Type of Plant:  Clay Processing
Type of Discharge:  Stack             Distance from Observer to Discharge Point:  7 ft.
Location of Discharge:  Baghouse      Height of Observation Point:  80 ft.
Height of Point of Discharge:  80 ft. Direction of Observer  from Discharge Point:  South
Description of Background: Green Pine Forest
Description of Sky:  Blue
Wind Direction:    Northwest           Wind Velocity:   5 mi/hr.
Color of Plume:   White                Detached Plume:   No
Duration of Observation:   90 minutes
SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Start
1400
1406
1412
1418
1424
1430
1436
1442
1448
1454
1500
1506
1512
1518
1524
Time
End
1406
1412
1418
1424
1430
1436
1442
1448
1454
1500
1506
1512
1518
1524
1530
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Opacity
Average
0
0
o
0
0
0
0
0
n
\j
0
n
w
o
\J
o
o
0
                                      C-93

-------
Run Number
Date
Test Time - Minutes
Production Rate - TPH
Stack Effluent
   Flow rate - ACFM
   Flow rate- DSCFM
   Temperature - °F
   Water vapor - Vol . %

Visible Emissions at
Collector Discharge  -
% Opacity
Parti cul ate Emissions
   Probe and Filter  catch
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton
  Total
                              TABLE 78
                              FACILITY 12
                         Summary  of Results
                                   1
                                  12/6/78
                                   56


                              •    8550
                                  6960
                                   134
                                     7.9
                                  see
                                 Table
                                  82
                                  1.76
                                  1.43
                                105.
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton
(1)  No analysis  of back-half on  in-stack filter tests.
                              C-94

-------
 Run Number
 Date
 Test Time -  Minutes
 Production; Rate  - TPH
 Stack Effluent
    Flow  rate - ACFM
    Flow  rate- DSCFM
    Temperature - °F
    Water  vapor - Vol. %
Visible Emissions at
Collector Discharge -
% Opacity
Particulate Emissions
    Probe and Filter catch
        gr/DSCF
        gr/ACF
        Ib/hr
        lb/ton
      TABLE 79
     FACILITY L2
Summary of Results
           1           2
         12/5/78    12/5/78
          120        120
   Total catch
              (1)
0.010
0.008
0.73
0.005
0.004
0.38
        gr/DSCF
        gr/ACF
        ?b/hr
        Ib/ton
(1)  No analysis of back-half on in-stack filter tests.
  3       Average
12/6/78     -    ,
 120         120
9780
8120
129
8.4
see
Table
80
9830
8150
123
9.4
see
Table
81
10340
8560
136
6.7
see
Table
82
9983
8277
129
8.2

—

                                0.007       0.007
                                0.006       0.006
                                0.48        0.53
                                   C-95

-------
                                       TABLE 80
                                      FACILITY 12
                            Summary  of Visible Emissions

Date:  12/5/78
                                                                             ff
Type of Plant:  Clay
Type of Discharge:  Stack             Distance from Observer to  Discharge  Point:   25 ft.
Location of Discharge:  Baghouse      Height of  Observation Point:   100  ft.
Height of Point of Discharge: 100 Ft. Direction  of Observers from Discharge  Point:  Southeast
Description of Background:  Clear Blue
Description of Sky:  Clear Blue
Wind Direction:   East                Wind Velocity:  5-10 mi/hr.
Color of Plume:  White                Detached Plume:  Yes
Duration of Observation:  approx. 120 minutes

                        SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8

9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
0953:00
0959:15
1005:45
1011:45
1018:15
1024:15
1030:15
1037:00
1044:00
1048:00
1054:15
1100:15
1106:15
1112:15
1118:30
1124:30
1131:00
1137:00
1143:15
1149:30
1156:30
Opacity Set Time Opacity
End
0959:15
1005:45
1011:45
1018:15
1024:15
1030:45
1037:00
1039:00
1048:00
1054:15
1100:15
1106:15
1112:15
1118:30
1124:30
1131:00
1137:00
1143:15
1149:30
1156:30
1202:30
Sum Average Number Start End bum Average
120
120
120
120
120
120
100

80
120
120
120
120
120
120
120
120
120
120
115
no
5 21 1202:30 1203:00 10 5
5
5
5
5
5
4.2

3.3
5
5
5
5
5
5
5
5
5
5
4.8
4.6
                                      C-96

-------
                                  TABLE 81
                                FACILITY 12
                      Summary of Visible Emissions
Date:  12/78
Type of Plant:  Clay
Type of Discharge:  Stack
Location of Discharge:   Baghouse
Distance from Observer to Discharge Point:   25  ft.
Height of Observation Point:   100 ft.
Height of Point of Discharge:   100 ft.Direction of Observer  from Discharge  Point:  South
                                                                                   east
Description of Background:   Clear Blue
Description of Sky:   Clear Blue                                                         :
Wind Direction:  East                 Wind Velocity:   5-10 mi/hr.
Color of Plume:  White                Detached Plume:   Yes
Duration of Observation:   128  minutes
                        SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
1357
1403
1409
1415
1421
1427
1433
1439
1445
1451
1457
1503
1509
1515 '
1521
1527
1533
1539
1545
1551
Opacity Set Time Opacity
End
1403
1409
1415
1421
14?7
1433
1439
1445
1451
1457
1503
1509
1515
1521
1527
1533
1539
1545
1551
1557
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average Number Start End Sum Average'
0 21 1557 1603 0 0
0 22 1603 1605 '. • 0 0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
                                       C-97

-------
                                  TABLE 82
                                FACILITY L2
                      Summary of Visible Emissions
Date:  12/5/78
Type of Plant:  Clay
Type of Discharge:  Stack
Location of Discharge:  Baghouse
Distance from Observer to Discharge Point:   25  ft.
Height of Observation Point:   100  ft.
Height of Point of Discharge:  100 ft.Direction of Observer  from Discharge  Point:  South)
                                                                                   east
Description of Background:  Clear Blue
Description of Sky:  Clear Blue
Wind Direction:  East                 Wind Velocity:   5-10 mi/hr.
Color of Plume:  White                Detached Plume:   Yes
Duration of Observation:  approx. 120 minutes
                        SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
18
20
Time
Start
1050
1056
1102
1108
1114
1120
1126
1132
1138
1144
1152
1158
1204
1210
1216
1222
1228
1234
1240
1246

End
1056
1102
1108
1114
1120
1126
1132
1138
1144
1150
1158
1204
1210
1216
1222
1228
1234
1240
1246
1251
Opacity
Set Time
Sum Average Number Start End
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0 •
0
0
0
0
0
0
0
0
0
0
0
0
0
Opacity
Sum Average




















                                    C-98

-------
Run Number
Date
Test Time - Minutes
Production Rate - TPH
Stack Effluent
   Flow rate - ACFM
   Flow rate- DSCFM
   Temperature - °F
   Water vapor - Vol. %

Visible Emissions at
Collector Discharge -
% Opacity
Particulate Emissions
   Probe and Filter catch
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton
   Total
                                TABLE 83
                               FACILITY Ml
                          Summary of Results
                                     1           2
                                   6/14/78     6/15/78
                                    120        120
0.001
0.001
0.01
0.001
0.001
0.02
        gr/DSCF
       .gr/ACF
        Ib/hr
        Ib/ton
(1)  No analysis of back-half on in-stack filter tests,
  3       Average
6/15/78
 120         120
1840
1620
124
2.8
see
Table
84
1490
1300
121
4.1
see
Table
85
1560
1360
124
4.2
see
Table
86
1630
1427
123
3.7
-
                                                           0.007       0.003
                                                           0.006       0.003
                                                           0.09        0.04
                                   C-99

-------
                                  TABLE 84
                                FACILITY Ml
                      Summary of Visible Emissions
Date:  6/14/78
Type of Plant:  Clay
Type of Discharge: Stack
Location of Discharge:  Baghouse
Height of Point of Discharge:
Description of Background:  Sky
Description of Sky:  Partly cloudy
Wind Direction:   NNE
Color of Plume:
Duration of Observation:  151 minutes
Distance from Observer to Discharge Point:   90 ft.
Height of Observation Point:   35 ft.
Direction of Observer  from Discharge Point:   East
Wind Velocity:  10 mi/hr.
Detached Plume:
                        SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
1538
1544
1550
1556
1602
1608
1614
1620
1626
1632
1638
1644
1650
1656
1702
1708
1714
1720
1726
1732

End
1544
1550
1556
1602
1608
1614
1620
1626
1632
1638
1644
1650
1656
1702
1708
1714
1720
1726
1732
1738

Opacity
Sum Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set
Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Time
Start
1738
1744
1750
1756
1802
1808















End
1744
1750
1756
1802
1808
1809















Opacity I
Sum Average 1
0
0
0
0
0
0














o
o
o
o
o
0














                                       C-100

-------
                                 • TABLE 85
                                FACILITY Ml
                      Summary of Visible Emissions
Date:  6/15/78
Type of Plant:  Clay
Type of Discharge:  Stack
Location of Discharge:  Baghouse
Height of Point of Discharge:
Description of Background:  Sky
Description of Sky:  cloudy
Wind Direction:  NNE
Color of Plume:
Duration of Observation:   134 minutes
Distance from Observer to Discharge Point:   90 ft.
Height of Observation Point:  35 ft.
Direction of Observer  from Discharge Point:   East
Wind Velocity:  10 mi/hr.
Detached Plume:
                        SUMMARY OF AVERAGE OPACITY
Set
Numbc
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
jr Start
913
919
925
931
937
943
949
955
TOO!
1007
1013
1019
1025
1031 -
1037
1043
1049
1055
1101
1107
End
919
925
931
937
943
949
955
1001
1007
1013
1019
1025
1031
1037
1043
1049
1055
1101
1107
1113
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0 '
Set Time Opacity
Number Start
21 1113
22 1119
23 1125
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
End Sum Average
1119 0 0
1125 0 0
1127 0 0

















                                       C-101

-------
                                    TABLE 86
                                 FACILITY HI
                      Summary of Visible Emissions
Date:  6/15/78
Type of Plant:  Clay
Type of Discharge:  Stack
Location of Discharge:  Baghouse
Height of Point of Discharge:
Description of Background:  Sky
Description of Sky:  cloudy
Wind Direction:  NNE
Color of Plume:
Duration of Observation:  183 minutes
Distance from Observer to Discharge Point:   90  ft.
Height of Observation Point:   35 ft.
Direction of Observers from Discharge Point:  East
Wind Velocity:  10 mi/hr.
Detached Plume:
                        SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
1332
1338
1344
1350
1356
1402
1442
1448
1454
1500
1506
1512
1518
1524
1530
1536
1542
1548
1554
1600
Opacity
End
1338
1344
1350
1356
1402
1408
1448
1454
1500
1506
1512
1518
1524
1530
1536
1542
1548
1554
1660
1606
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Q
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set Time
Number Start End
' 21 1605 1608 '
1625 1629
22 1629 1634
24
25
26
27
28
29
30
31 .
32
33
34
35
36
37
38
39
40
Opacity
Sum Average

0 0
0 0

















                                       C-102

-------
                                TABLE 87
                               FACILITY M2
                          Summary of Results
Run Number
Date
Test Time - Minutes
Production Rate - TPH
Stack Effluent
   Flow rate - ACFM
   Flow rate- DSCFM
   Temperature - °F
   Water vapor - Vol. %

Visible Emissions at
Collector Discharge -
% Opacity
Parti culate Emi ss ions
   Probe and Filter catch
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton
   Total catch
              (1)
1
6/14/78
120
2580
2100
183
1.1
see
Table
88
0.002
0.002
0.03
2
6/15/78
120
2460
2090
151
1.7
see
Table
89
0.002
0.002
0.04
3
6/15/78
120
2450
2100
150
1.6
see
Table
90
0.001
0.001
0.02
Average
-
120
2497
2097
161
1.5
*•
0.002
0.002
0.03
        gr/DSCF
        gr/ACF
        Ib/hr
        Ib/ton

(1) No analysis of back-half on in-stack filter tests,
                                   C-103

-------
                                  TABLE  88
                                FACILITY M2
                      Summary of Visible Emissions
Date:  6/14/78
Type of Plant:  Clay
Type of Discharge:  Stack
Location of Discharge:  Bag'house
Height of Point of Discharge:
Description of Background:  Sky
Description of Sky:  Partly cloudy
Wind Direction:  NNE
Color of Plume:
Duration of Observation:  30 minutes
Distance from Observer to Discharge Point:  90 ft.
Height of Observation Point:  85 ft.
Direction of Observer  from Discharge Point:  East
Wind Velocity:  10 mi/hr.
Detached Plume:
SUMMARY OF AVERAGE OPACITY |
Set Time
Number Start End
1 1528 1534
2 1534 1540
3 1540 1546
4 1546 1552
5 1552 1558
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Opacity
Sum Average
0 0
0 0
0 0
0 0
0 0















Set Time
Number Start End
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Opacity
Sum "Average!
"I



















                                       C-104

-------
                                  TABLE 89
                                FACILITY M2
                      Summary of Visible Emissions
Date:  6/15/78
Type of Plant:  Clay
Type of Discharge:  Stack
Location of Discharge:  Baghouse
Height of Point of Discharge:
Description of Background:  Sky
Description of Sky:  cloudy
Wind Direction:  NNE
Color of Plume:
Duration of Observation:   128 minutes
Distance from Observer to Discharge Point:  90 "ft.
Height of Observation Point:  85 ft.
Direction of Observer  from Discharge Point:  East
Wind Velocity:  10 mi/hr.
Detached Plume:
                        SUMMARY OF AVERAGE OPACITY
Set
Numbi
,
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
?r Start
850
856
902
908
914
920
926
932
938
944
950
956
1002
1008 „
1014
1020
1026
1032
1038
1044
End
856
902
908
914
920
926
932
938
944
950
956
1002
1008
1014
1020
1026
1032
1038
1044
1050
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set Time Ooacitv
Number Start
21 1050
22 1056
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
End Sum Average
1056 0 0
1058 - 0 0


















                                   C-105

-------
                                 TABLE  90
                                FACILITY M2
                      Summary of Visible Emissions
Date:  6/15/78
Type of Plant:  Clay
Type of Discharge:  Stack
Location of Discharge:  Baghouse
Height of Point of Discharge:
Description of Background:  Sky
Description of .Sky:   Partly cloudy
Wind Direction: :  NNE
Color  of Plume:
Duration of Observation:   139 minutes
Distance from Observer to Discharge Point:   90 ft.
Height of Observation Point:   85 ft.
Direction of Observers from Discharge Point: East
Wind Velocity:  10 mi/nr.
Detached  Plume:
                         SUMMARY OF AVERAGE  OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
1359
1405
1411
1417
1423
1429
1435
1441
1447
1453
1459
1505
1511
1517
1523
1529
1535
1541
1547
1553

End
1405
1411
1417
1423
1429
1435
1441
1447
1453
1459
1505
1511
1517
1523
1529
1535
1541
1547
1553
1559
Opacity

Sum Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set Time Opacity
Number Start End Sum Average
21 1559 1605 0 0
22 1605 1611 0 0
23 ' 1611 1617 0 0
24 1617 1618 0 0
25
26
27
28
29
30
31
32 '
33
34
35
36
37
38
39
40
                                         C-106

-------
                       TABLE 91

                      FACILITY N
Summary of Results of Fugitive. Emission Tests performed
        on three separate rail car loadings
Accumulated Accumulated
Observation observation emission % Emission
area period time (AET/AOP x 100)
(mi n: sec) (mi n: sec)












1.
A.
B.
C.

A
B
C

A
B
C

A
B
C
Designation

144:32
144:32
144:32

99:45
99:45
99:45

154:20
154:20
154:20
Test #1
22:42 •
17:30
0:00
Test #2
18:50
2:06
0.00
Test #3
63:42
0:20
9:21

15.7
12.1
0

18.9
2.1
0

41.3
0.2
6.1
	 — 	 _ 	
of observation positions
Loading hose
West end of
East end of
shed
shed




                        C-107

-------
                         TABLE 92

          SUMMARY OF METHOD 22 RESULTS - FACILITY P
       Time
      peri od
Observed time
  (minutes)
   Percent of time
with visible emissions

       Observer
Test point 5, Final screens, 10/3/79

     1035-1055         20

     1105-1125         20

     1130-1150         20


Test point 7, Transfer point, 10/3/79

     1324-1424     .    60
                                  0

                                  0
                             C-108

-------
              TABLE 93
    METHOD 9 - 6-MINUTE AVERAGES*
            FACILITY P

Run
TP-1
Primary
Crusher
Observer
3 4
1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
9
7
14
14
13
11
12b
7C
-
9
11
10
13
8
10
10
8



13
11
15
17
11
11
11
10
13
10
15
18
10
8
10
11
5



TP-4 TP-6
Impact Cone
Crusher Crusher
Observer Observer
34 34
15 10 4
11 7 5
11 7 9
n 10 n
n 10 9
10 8 10
10 13 9
n 13 7
13 10 10
n 9 8
8
13
7
8
8
1
0
0
0
1
n
18
22
25
23
17
16
15
15
16
15
21
13
13
15
4
2
1
1
4

 Values reported in percent opacity.
34-minute  average
"5-minute  average

               C-109

-------
                                  TABLE 94

                 SUMMARY OF METHOD 22 RESULTS - FACILITY  Q

Time Obse
period - (m
Test point 2, Initial screens
1010-10409
0820-0856
Test point 3, Transfer point,
0851-0921a
0931-1001a
wi
iv*\/^H "f"im*s
> I V Cvl U I MIC
linutes)

, 10/10/79 - 10/11/79
30 '
30
10/10/79
30
30
Percent of time
th visible emissions
Observer "
1

34
4

27
64
2

65
7

31
67
Test point 5, Secondary screens, 10/8/79
0848-0918
0940-1010
1015-1045
1057-1127
Test point 7, Final screens,
1250-1320
1330-1400
1407-1437
1451-1521
30
30
30
30
10/8/79
30
30
30
30
0
0
0
<1

0
0
0
0
0
0
0
0

0
0
0
0

a"Red Rock" material.   Not  processed  under representative conditions.   Data
 omitted.
                                   c-no

-------
            TABLE 95
   METHOD 9 - 6-MINUTE AVERAGES9
           FACILITY Q
Run
1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
21
TP-1 TP-6
Primary crusher Cone crusher
Observer
3
11
11
6
12
12
3
2
1
2
1
1
1
2
3
3
3
2
2
1
1

4
11
14
8
18
17
5
9
4
8
6
6
7
8
12
TO
6
6
5
2
3

Observer
3
15
18
18
17
10
. 15
19
20
23
24
28
26
28b
25
28
29
27C
27
29
26
25C
4
12
17
19
19
12'
18
19
21
23
23
24
26
28b
23
28
26
26^
29
34
38
39C
 Values  reported  in percent opacity.
 4-minute average.
c5-minute average.
              c-m

-------
                               TABLE  96
               SUMMARY  OF  METHOD  22 RESULTS  -  FACILITY  R

Time Observi
period (min
Test point 1, Initial screens
0720-0750
0800-0830
0840-0910
0920-0941 )
0722-0732 |
Test point 3, Transfer point,
0731-0801
Percent of time
with visible emissions
cU U 11116
utes)

10/12/79, 10/15/79
30
30
30
30
10/16/79
30
Observer
-*
1

2
1
2
2

6
2

1
<1
T
4

12
Test point 4, Secondary screens, 10/16/79
0907-0937
0945-1015
1035-1105
1310-1340
Test point 6, Final screens,
1020-1050
1055-1125
1130-1200
1303-1333
Test point 7A, Transfer point
1610-1640
1646-1716
Test point 7B, Transfer point
1415-1445
1455-1525
30
30
30
30
10/15/79
30
30
30
30
, 10/15/79
30
30
, 10/16/79
30
30
5
1
42a
5

0
0
0
0

0
0

0
4
15
1
4a
10

0
0
0
0

6
0

0
4

Data omitted - wind interference.
                                C-112

-------
            TABLE  97

 METHOD 9 - 6-MINUTE AVERAGES3
          FACILITY R

Run •
1
2
3
4
5
6
7
8
9
10
11
12 .
13
14
15
16
17
18
19
20
TP-2 TP-5
Primary crusher Cone crusher
Observer
3
14
16
16
16
12
9
13
9
13
12
17
9
14
13
15
8
6
7
10
9
4
13
14
14
9
13
15
14
14
15
13
16
13
11
12
13
9
6
9
11
12
Observer
3
8
9
9
12
13
11
13
12
13
12
12
10
9
7
8
12
13
11
11
12
4
12
14
17
15
15
15
16
14
16
14
17
17
17
10
15
10
11
11
11
11

Data reported in percent opacity.
             C-113

-------
                TABLE 98
SUMMARY OF METHOD 22 RESULTS - FACILITY S

Time Obs
period (
Test point 2, Initial Screens
1516-1546
1558-1628
1100-1130
1302-1332 v
Percent of time
with visible emissions
ci VcU U Mile
minutes)

, 10/24/79
30
30
30
30
Observer
1

0
0
0
0
2

0
0
0
0
Test point 4, Secondary screens, 10/22/79, 10/23/79
1108-1138
1143-1158
0745-0805
0810-1840
0845-0915
Test point 6, Transfer point,
1257-1327
1335-1350
1338-1353
1355-1425
1433-1503
Test point 7, Transfer point,
0750-0820
0826-0856
0915-0945
0955-1025
30
15
15
30
30
10/23/79, 10/24/79
30
15
15
30
30
10/25/79
30
30
30
30
1-
1
1
1
1

0
0
0
0
0

0
0
0
0
10
13
5
6
7

0
1
0
0
0

0
0
0
0

                 C-114

-------
                   TABLE  99

         METHOD  9  - 6-MINUTE  AVERAGES*1
                  FACILITY S

TP-3
TP-1

Run
Primary


crusher


Observer

1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
3
2
1
1
1
1
1
1
<1
0
1
1
0
0
0
2
1
3
3
2
0
4
1
2
1
0
1
3
2
1
2
1
1
0
0
1
2
0
2
3
1
1
4-1/2
in.
Cone crusher




Observer
3
3
4
4
2
4
6
6
3
2
5
4
5
3
5
5
4
3
3
3
1
4
3
4
5
3
3
4
4
2
2
3
3
5
2
4
3
2
0
2
1
2
TP-5
5-1/2
in.
Cone crusher




Observer
3
0
0
3
5
4
10
11
14
11
13
n
n
12
8
10
12
9
6
7
5~
4
0
2
5
5
4
9
9
10
10
10
n
10
15
9
12
12
TO,
9
11
9

Data reported in percent opacity.
                    C-115

-------
                 TABLE 100



SUMMARY OF METHOD 22 RESULTS - FACILITY T

Time
period
Test point 2, Transfer
1353-1427
1428-1458
1533-1603
1125-1155
Test point 3, Initial
1300-1330
1336-1406
1412-1542
1450-1520
Test point 5, Storage
0755-0825
1023-1053
0908-0938
0947-1017
Observed time
(minutes)
point, 10/26/79, 10/29/79
30
30
30
30
screens, 10/29/79, 10/30/79
30
30
30
30
bin, 10/29/79, 10/30/79
30
30
30
30
Percent of time
with visible emissions
Observer
1 2

0 1
4 2
3 1
2 0

0 0
0 0
0 0
0 0

0 0
0 0
0 0
0 0

                 C-116

-------
            TABLE 101

 METHOD 9 - 6-MINUTE AVERAGES9
          FACILITY T

TP-1 TP-4
Primary crusher Cone crusher
Run,
T
2
3._
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Observer
3
4
6
9
3
5
10
4
9
8
7
8
8
8
13
10
13
10
9
10
6
4
8
7
8
3
5
8
3
5
7
7
8
8
6
8
6
8
5
4
6
5
Observer
3
18
21
22
23
19
17
20
15
15
15
16
6
10
17
19
18
15
16
18
13
4
15
14
14
15
13
n
13
8
8
9
6
7
11
16
16
15
15
13
16
14

*Data reported  in  percent  opacity.
                C-117

-------
     Table 102 and Figures 2 through 6 represent visible emission data  given  in
this Appendix, on a basis of percent of total time of recorded visible emissions
(e.g., in a Method 22 format) and on a basis of how opacity varied with time
(e.g., in a Method 9 format).  These observations were executed for fugitive
emissions.  The use of Method 22, as it applies to the proposed standard for
non-metallic mineral processing plants would be applicable to all fugitive non-
crushing sources of dust.  This test would also be employed to check the effec-
tiveness of a capture system, if used, at any process facility.  Method 9
would be used for measurement of all crusher-related sources of dust.   A des-
cription of each of the process facilities listed in Table. 102 is given at the
beginning of this Appendix.
     Data-for 64 observation periods of visible emissions readings covering
54 process facilities at 14 non-metallic processing plants is given in Table
102.  All facilities observed were fugitive emission discharges from uncontrol-
led, hooded or wet suppression controlled facilities.
                                    C-118

-------





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-------
                                   APPENDIX D
                 EMISSION MEASUREMENT AND CONTINUOUS MONITORING
D.I  EMISSION MEASUREMENT METHODS
     For participate matter and visible emissions measurements from stacks,
EPA relies primarily upon Methods 5 and 9, which have been established as
reference methods.  The emission data from the non-metallic industry may
be obtained using these reference methods as prescribed in the Federal
Register.  In addition, as the particulate concentrations are expected to
be independent of temperature for this industry, Method 17 (in-stack
filtration) is an acceptable particulate sampling method.
     The one serious problem encountered during the testing of stacks in
the non-metallic minerals industry was the low concentration levels of
particulate.  Some emissions tests resulted in particulate catches of less
than 10 mg corresponding to 0.0005 gr/dscf.  An EPA laboratory study showed
that because of positive biases from the "clean-up" blank, results from
tests where low concentration levels are encountered are biased toward the
high side.  This bias was no more than a factor of two for particulate
catches down to 8 mg.
     Data from an EPA report, "Additional Studies on Obtaining Replicate
Particulate Samples From Stationary Sources," by William J. Mitchell,
indicate that particulate catches of about 50 mg are adequate to insure an
error of no more  than 10 percent.   Lower levels were not studied.  Based on
theoretical calculations, particulate  weights as small as  12 mg were
 estimated to be sufficient to insure an error no greater than 10 percent.
                                     D-l

-------
D.2  MONITORING SYSTEMS AND DEVICES
     The effluent streams from the non-metallic industry sources are at
essentially ambient conditions.  The visible emissions monitoring
instruments found adequate for power plants would be applicable for this
industry.  These systems are covered by EPA performance standards contained
in Appendix B of 40 CFR Part 60.
     Equipment and installation costs are estimated to be $18,000 to
$20,000 and annual operating costs, including data recording and reduction,
are  estimated at $8,000 to $9,000.
D.3  PERFORMANCE TEST  METHODS
     Either Method 5 or 17 for particulate matter is recommended as the
performance test method.  Due to  low concentrations sometimes  encountered,
a minimum  sample volume must be established  to  insure adequate amounts of
particulate matter are collected  to minimize recovery errors.   This
particulate  catch amount  is  preferably  50 mg,  but should  be at least  25  mg.
 It is  also recommended that  sampling  trains  with  higher  sampling  rates,  which
 are allowed  by Method  5  and  are  commercially available,  be  used to  reduce
•sampling time and  costs.
      Sampling costs  for a test consisting of three  particulate runs,
 the number normally specified by performance test regulations, is estimated
 to be about $5,000 to $7,000.   This estimate is based on sampling site
 modifications and testing being conducted by contractors.  If in-plant
 personnel  are used to conduct the test, the costs will  be somewhat less.
      Since the outlet gas streams from control devices used in this
 industry are generally well  contained, no special  sampling probelms are
 anticipated.
                                      D-2

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                              SUPPLEMENT A
              ECONOMIC IMPACT ANALYSIS FOR PORTABLE PLANTS.

 A.O  Introduction and Summary

      After the preparation of Section 8,  Economic  Impact, of the  background
 information document9 comments were received from  the  crushed stone and
 sand and gravel  industries concerning the impact analysis conducted for
 portable plants.   Specifically, they commented  that the  costs of  controlling
 portable processing  plants with baghouses are substantially  higher than
 those for fixed  processing plants.   The reasons given  for the higher costs
 are the  regular movement  of the plants  and the  changes made  in the operating
 configuration  of  the plants.   Since these issues were  not addressed in the
 original  analysis, this analysis was prepared.
      Because portable plants  are used primarily in  the crushed stone and
 sand and  gravel industries,  the impacts on these plants were  evaluated by
 developing  a Discounted Cash  Flow (DCF) analysis for each model new plant
 size in these  industries.   DCF  is an investment decision analysis which
 shows  the economic feasibility  of a  planned  capital investment project over
 the  life of the project.
     The DCF analysis was conducted  by  using  conservative assumptions.
Assumptions used include:
     •    the total of NSPS control  costs were  incremental costs; i.e.,
          that there are no SIP control costs that the plant would have to
          incur in the absence of NSPS control.
     9    the plants operate at 1250  hours per year through the life of the
          project.
     0    NSPS control cost pass through  is limited by competition of
          existing plants  in the same industry which do not have to meet
          the NSPS.
     •    the new plant operates as  a separate business entity and cannot
        - expect to finance the control  from another business activity or
          parent firm.
                                 S-l

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     For new plants, the DCF analysis indicated that the 68 and 135 Mg/hr
(75 and 150 ton/hr) portable plants in both industries are likely to be
precluced by an NSPS.  The DCF model was unable to determine a clear positive
or negative investment decision for the 270 Mq/hr (300 ton/hr) portable
plants in both industries.  However, in view of the conservative assumptions
used, they were judged to be economically feasible.  All of the ottier plant
sizes in the two industries are likely to be economically feasible after the
promulgation of the NSPS.
                                 S-2

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A.I  INDUSTRY CHARACTERIZATION

A.1.1  General Profile
     Portable mineral processing plants (portable plants) are used primarily
by sand and gravel processors and crushed stone processors.  The United
States Geological Survey estimates that there were 3,285 portable plants in
the sand and gravel industry-and 1,232 portable plants in the crushed stone
industry in 1978.   Portable plants account for 53 percent of total existing
plants in the sand and gravel industry and 42 percent of total existing
plants in the crushed stone industry.
     Based on industry data, portable plants account for 40 to 50 percent of
total annual mine output for the sand and gravel industry2'3 and 30 to 40
percent of total annual mine output for the crushed stone industry.4'5  .In
1978, this amounted to 340-425 million megagrams (375-469 million tons) of
sand and gravel and 260-347 million megagrams (287-382 million tons) of
crushed stone.
     The clay, gypsum, and pumice industries also use portable plants.  How-
ever, these plants are used for specialized small output crushing operations
which amount to an insignificant portion of total mine output for these
industries.6'7'8
     The major manufacturers of portable plant equipment are Iowa Manufac-
turing, Telsmith Division of Barber-Green, Portec, Universal Engineering,
and Allis-Chalmers.  These companies manufacture a variety of interchangeable
portable crushers, screens, conveyor belt units, and combination systems
which can be combined into an integrated portable plant that meets the
requirements of the individual mineral processor.
     The output capacity of manufactured portable plant equipment ranges
from 45 megagrams per hour (50 tons per hour) to 998 megagrams per hour
(1,100 tons per hour).  A large majority of new and,existing portable plants
are in the 227 megagrams per hour (250 tons per'hour) to 635 megagram per
hour (700 tons per hour) output capacity range.
                                    S-3

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     Portable plants are owned and operated by a variety of mineral processing
firms.  These firms range from the small, independent mineral processor with
one portable plant to large construction materials companies (e.g. Moline
Consumers Company, Flintkote) which may own and operate 12 or more portable
plants.
     Construction companies .also purchase portable plant equipment for large
and/or remote site construction projects.  The portable plant equipment is
used to supply material for a specific construction project and is usually
sold or scrapped after completion of the project. '  '
     The contract processor owns portable plant equipment and contracts min-
eral processing services to a community or another firm.  These services may
be contracted for during periods of high product demand when a mineral
processor's output capacity is limited or when a community or firm requires
a supply of construction material.  A contract processor may cover a geogra-
phical area which encompasses several states.  '

A.1.2  Geographic Distribution
     Portable plants are used throughout the nation.  However, over 70
percent of existing portable plants are located west of the Mississippi
       14
River.    The popularity of portable plants in the western and mid-western
states is due mostly'to the demand for crushed stone and sand and gravel in
sparsely populated areas.  Such areas can not be economically served
by fixed plants due to high transportation cost for crushed stone and sand
and gravel.
     The crushed stone and sand and gravel industries can be divided into
three  basic national regions based on portable pi ant/fixed plant usage
(see Figure 1).  These regions are:
     Region I    - In this region, which encompasses the states in the
                   Northeast and Southeast and most of California, over
                   80 percent of mine output for the sand and gravel and
                   crushed stone industries is from fixed plants.  The
                   region has a relatively high population density and well
                   established product markets for construction materials.
                   Portable plants are used at large construction projects
                   (i.e. dams, highways) and to supplement mine output at
                   fixed operations, particularly during periods of high
                                      S-4

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S-  5

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                  product demand.
    Region II   - In this region, which encompasses most of the Midwest
                  section of the country, portable plants account for 20
                  to 40 percent of mine output  for the  crushed stone indus-
                  try and 30 to 50 percent of mine output for the sand and
                  gravel industry.  The region  has many large metropolitan
                  areas with well established product markets for construction
                  materials.   However, some  of  the areas are sparsely popu-
                  lated and portable  plants  are used to meet the fluctuating
                  product demand in these areas.  Product transportation  costs
                  for sand and gravel  and crushed stone, which  range from
                  $0.08 to $0.15 per  megagram kilometer ($0.12  to $0.22 per
                  ton mile) nationally, make the establishment  of a fixed
                  plant economically  unattractive  in parts  of this  region and
                  most of  Region  III.
     Region III  - In  this  region, which encompasses  the Western  states  and
                  northern California, portable plants  account  for  over 50
                  percent  of  mine  output  for the sand  and gravel and crushed
                   stone  industries.   In New  Mexico,  Utah, Wyoming,  Colorado,
                   and Nebraska,  over 80 percent of mine output  for  both indus-
                   tries  is  from portable  plants.  The  region  is  sparsely  popu-
                   lated  and  product demand  for  construction materials  is  usually
                   not high  enough  to warrant the establishment  of  a fixed plant.
The portable plant/stationary  plant usage  distribution,  as  described above, is
                                          14
not expected to change in  the  near future.

A.1.3  Industry Trends
     The projected growth  rate-for the sand and gravel  industry  through  1985
is 1.0 percent per year,  while the growth  in crushed stone over the  same period
is 4.0 percent per year.15  These growth projections are for the entire  industry;
separate projections for  the  portable plant  segments  of  each industry are
unavailable.
     Based on mineral processing equipment sales, more portable plant
equipment  is sold per year than fixed plant equipment.   However, the total
                                   S-6

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output capacity of the portable plant equipment is less than the total
output capacity of the fixed plant equipment.10'14  This equipment sales
trend, which is expected to continue for the near future, indicates that the
average new portable plant would have a lower output capacity than the
average new fixed plant.

A.1.4  Methods of Operation
     The mobility of portable crushed stone plants allows portable plant
operators to move their plants according to either of two major methods:
among various quarry sites, or both among, as well as within, quarries.
With regard to the former, the operator may choose to move a single plant
to a number of quarries over the year; however, once set at a site, several
haul trucks are used to transport blasted rock to the primary crusher.
However, other operators may elect to move not only to different quarries
but also within an individual quarry as well.  Movement within quarries
allows the plant to follow blasting activities as they take place at various
locations around larger quarries.  In effect, the movement of portable
plants within individual quarries reduces the need for haul trucks to trans-
port newly blasted rock to the primary crusher.  While the decision to move
about or remain stationary within a quarry may depend upon the physical
condition of the quarry and/or the individual preferences of operators, the
economic analysis has recognized both methods of operation.
                                 S-7

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A.2 COST ANALYSIS
A.2.1  Model Portable Plants
     Model portable plants have been developed which describe the types
of equipment and size ranges for portable plants in the sand and gravel
and crushed stone processing industries.  The equipment selected for
these model portable plants are:
  I.  Portable sand and gravel plant
     1.   Primary crusher
     2.   Secondary crusher and associated screen
     3.   Final  screen
     4.   Conveyor belts
 II.  Portable crushed stone plant
     1.   Primary crusher
     2.   Secondary crusher and associated screen
     3.   Tertiary crusher and associated screen
     4.   Final  screen
     5.  'Conveyor belts
     Five output capacities were chosen for both  the  sand  and  gravel  and
 crushed stone model  portable  plants.   The five  output capacities  used are
 68, 135, 270, 540,  and  817 megagrams  per  hour (75,  150,  300, 600,  and
 900 tons per hour).   Specific sizes of portable crushing and screening
 equipment have been combined  to meet the  output capacities of  the model
 portable plants.  Tables 1  through 5 list the equipment requirements  for
 the model portable plants along with energy usage and air  volume requirements.
 The equipment size ranges listed in Tables  1 through 5 represent minimum
 and maximum product outputs for each piece  of processing equipment.
      Processing equipment for a portable plant can be arranged in a
 variety of operating configurations at the mine site.  Two basic operating
 configurations are used for the model portable plants.  One configuration
  is a straight line setup in which the portable plant equipment lies  in a
 basic straight line.  The second configuration is an "L" shaped setup.
  In this  configuration the final screen is situated at a right angle from
 the secondary screen at the portable sand and gravel plant, and the
  tertiary  crusher/screen unit and final screen are situated at a right
  angle from the secondary screen at the portable crushed stone plant.
                                     S-8

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                                    TABLE 1


                  MODEL PORTABLE PLANT EQUIPMENT REQUIREMENTS


                             68 megagrams per  hour

                              (75 tons per hour)
 1.   Primary crusher




 2.   Secondary crusher




 3.   Secondary screen




 4.   Tertiary  crusher




 5.   Tertiary  screen




 6.   Final screen





 Given in megagrams per hour with tons per hour in parenthesis

 Given in kilowatts with horsepower in parenthesis
c
 Given in cubic meters per minute with actual cubic feet per minute in
 parenthesis


References:   Portable processing equipment brochures from Iowa Manufacturing

             Company, Tel smith Division of Barber-Green, and All is Chalmers.

a
Size"
54
(60
68
(75
45
(50
109
(120
45
(50
45
(50
- 227
- 250)
- 104
- 115)
- 181
- 200)
- 136
- 150)
- 181
--200)
- 181
- 200)
Energy
Usageb
56.0
(75)
74.6
(100)
14.9
(20)
m.9
(150)
14.9
(20)
14.9
(20)
Air
Vol ume
43
(1500)
43
(1500)
127
(4500)
43
(1500)
99
(3500)
127
(4500)
                                   S-9

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                                   TABLE 2

                 MODEL PORTABLE PLANT EQUIPMENT REQUIREMENTS

                           135 megagrams per hour
                             (150 tons per hour)
1.  Primary crusher


2.  Secondary crusher


3.  Secondary screen


4.  Tertiary crusher
    j*      .

5.  Tertiary screen


6.  Final screen



aGiven in megagrams per hour with tons per hour in parenthesis

 Given in kilowatts with horsepower in parenthesis
°Given in cubic meters per minute with actual  cubic feet per minute in
 parenthesis

References:  Portable processing equipment brochures from Iowa Manufacturing
             Company, Telsmith Division of Barber-Green, and Allis Chalmers.
Size9
91
(100
181
(200
45
(50
136
(150
45
(50
45
(50
- 363
- 400)
- 272
- 300)
- 181
- 200)
- 227
- 250)
- 181
- 200)
- 181
- 200)
Energy
Usage"
74.6
(100)
93.3
(125)
14.9
(20)
167.9
(225)
14.9
(20)
14.9
(20)
Air
' Volume
99
(3500)
99
(3500)
142
(5000)
57
(2000)
113
(4000)
142
(5000)
                                     S-10

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                                   TABLE  3

                  MODEL  PORTABLE  PLANT  EQUIPMENT  REQUIREMENTS

                            270 megagrams  per  hour
                              (300  tons per  hour)
Sizea
136
(150
227
(250
181
(200
272
(300
181
(200
1ST
(200
- 363
- 400)
- 454
- 500)
- 363
- 400)
-363
- 400)
- 363
- 400)
- 363
- 400)
Energy
Usageb
93.3
(125)
111.9
(150)
22.4
(30)
186.5
(250)
22.4
. (30)
14.9
(20)
Air
Vol umec
113
(4000)
113
(4000)
198
(7000)
142
(5000)
198
(7000)
198
(7000)
     Primary  crusher


     Secondary crusher


     Secondary screen


     Tertiary crusher


     Tertiary screen


     Final screen
 Given in megagrams per hour with tons per hour in parenthesis

 Given in kilowatts with horsepower in parenthesis
cGiven in cubic meters per minute with actual cubic feet per minute in
 parenthesis

References:   Portable processing equipment brochures from Iowa Manufacturing
             Company, Tel smith Division of Barber-Green, and All is Chalmers.
                                    S-ll

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                                   TABLE  4
                 MODEL PORTABLE PLANT EQUIPMENT REQUIREMENTS
                           540 megagrams  per hour
                             (600 tons per hour)

Size
408 -
(450 -
408 -
(450 -
363 -
(400 -
408 -
(450 -
363 -
(400 -
363 -
(400 -

a
635
700)
635
700)
680
750)
635
700)
680
750)
680
750)
Energy
Usage"
186.5
(250)
223.8
(300)
29.8
(40)
261.1
(350)
29.8
(40)
29.8
(40)
Air
- Vol ume
142
(5000)
142
(5000)
227
(8000)
170
(6000)
227
(8000)
227
(8000)
1.  Primary crusher
2.  Secondary crusher
3.  Secondary screen
4.  Tertiary crusher
5.  Tertiary screen
6.  Final screen
aGiven in megagrams per hour with tons per hour in parenthesis
bGiven in kilowatts with horsepower in parenthesis
cGiven in cubic meters per minute with actual cubic feet per minute in
 parenthesis
References:  Portable processing equipment brochures from Iowa Manufacturing
             Company, Telsmith Division of Barber-Green, and All is Chalmers.
                                      S-12

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                                    TABLE 5

                  MODEL PORTABLE PLANT EQUIPMENT REQUIREMENTS
 1.   Primary crusher


 2.   Secondary crusher


 3.   Secondary screen


 4.   Tertiary  crusher


 5.   Tertiary  screen


 6.   Final screen
                            817 mega grams per hour
                              (900 tons per hour)
   Size8

 726 - 907
(800 - 1000)

 635 - 907
(700 - 1000)

 816 - 998
(900 - 1100)

 816 - 998
(900 - 1100)

 816 - 998
(900 - 1100)

 816 - 998
(900 - 1100)
Energy
Usage"

298.4
(400)

298.4
(400)

 37.3
 (50)

298.4
(400)

 37.3
 (50)

 37.3
 (50)
   Air
 Volume

    170
  (6000)

    170
  (6000)

    283
(10,000)

    170
  (6000)

    283
(10,000)

    283
(10,000)
a
 Given in megagrams per hour with tons per hour in parenthesis

 Given in kilowatts with horsepower in parenthesis

 Given in cubic meters per minute with actual cubic feet per minute in
 parenthesis

References:  Portable processing equipment brochures from Iowa Manufacturing
             Company, Tel smith Division of Barber-Green, and All is Chalmers.
                                    $-13

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     The average output capacity for new and existing portable sand and
gravel plants in the eastern U.S. is between 227 and 270 megagrams per hour
(250 and 300 tons per hour).  The installed capital cost for these plants
would be between approximately $0.45 minion and $1 million. '  '   '   '
The average output capacity for new and existing portable sand and gravel
plants in the western U.S. is between 540 and 635 megagrams per hour (600
and 700 tons per hour).  The installed capital cost for these plants would
be at least $1 million.9'10'15'17'18
     The average output capacity for new and existing portable crushed
stone plants is between 227 and 270 megagrams per hour (250 and 300 tons
per hour).  The installed capital cost for these plants is between $0.6
million and $1.3 million.9'10'16'17'18
     The,cost per ton of material processed by a portable plant is higher
than the cost per ton of material processed by a similar output capacity
fixed plant.  This higher cost is primarily due to higher maintenance
costs and a lower annual operating  schedule for portable plants.   Portable
plants are designed  for mobile transport and  lack  some of the structural
strength of fixed plants.  Thus, portable plants have shorter operating
lives than fixed plants and require more (nan-hours to maintain.  On the
average, portable plants operate fewer hours  per year (1250 to 1600
hours)16'17'18'19 than fixed plants  (2000 hours).   This difference is due
primarily to  the downtime associated with the movement of portable plants.
Due to this,  total annual costs  for  a portable plant must be recovered on
a  lower  total product output compared to similar output capacity  fixed
plants.

A.2.2  Movement
     There are  two basic  types of portable  plant movements.  One  type
involves  transporting  the entire portable plant from one quarry to another.
On the average, this type of move occurs four times per year.  '
i n in
   '    The second type of portable  plant move is an  in-quarry operation  in
which  the  primary crusher is moved  near the mined  material  along  the
highwall.   In this mode,  the mineral  processor establishes  a core  operating
configuration in the quarry and  transports  the product from the primary
                                    S-14

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 crusher to  the core operating  configuration  by  a  conveyor  belt.  This
 eliminates  the need for haul trucks  for  the  transporting of mined material
 from  the highwall  to the portable  plant.   In-quarry moves  of  the primary
 crusher may occur  up to 24  times per year.   This  type of move is characteris-
 tic of  the  small,  independent  processor.   The larger firms in the sand and
 gravel  and  crushed  stone industries  usually  employ haul trucks to transport
 mined material  from the highwall to  the  portable  plant, instead of moving
 the primary crusher to  the mined material.21'22   Table 6 lists average
 movement parameters  and associated costs for a typical portable plant.
 These parameters and  costs were obtained from mineral processors who use
 portable plants.  Also  listed  in this table are estimated movement para-
 meters  and  associated costs for the  baghouse systems considered in this
 analysis.   The  baghouse movement costs are based on rental  charges for
 equipment necessary for an offsite move.  A mineral processor may decide
 to purchase 'a crane for moving the baghouse systems and/or haul trucks to
minimize the amount of  in-quarry moves necessary.  The cost of a crane is
$80,000 and the cost of a 20 megagram (22 ton) capacity haul  truck is
$50,000.

A.2.3  Control Options
     Two control options are used for the model  portable plants.   The
options are:
          Option I  - In this option, one baghouse would be  used to control
          the entire portable plant for the 68,  135,  and 270  megagrams per
          hour (75, 150, and 300 tons per hour)  model  plants.   For the 540
          and 817 megagrams  per hour (600 and 900 tons  per  hour)  model
          plants, the primary crusher would be ducted to one  baghouse and
          all other pieces of equipment would be ducted to  a  second
          baghouse.
          Option II  - In this option, the following pieces  of equipment or
      _   groupings  of equipment would have their own baghouse for all
          output sizes of model plants:
                                 S-15

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          1.    Primary crusher
          2.    Secondary crusher and associated screen
          3.    Tertiary crusher and associated screen
          4.    Final  screen
For both options, emissions from conveyor belt transfer points  are  hooded
and ducted to the baghouse systems.
     Costs are presented for the two baghouse control options used  for
controlling particulate emissions from the five output capacities of the
two model portable plants.  The control costs have been based on technical
parameters associated with the control system used.  These parameters are
listed in Table 7.
     These costs cannot be assumed to reflect control costs for any given
installation.  Estimating control costs for an actual installation  requires
performing detailed engineering studies.  Nonetheless for purposes  of this
analysis, control costs are considered to be sufficiently accurate.
     The control costs have been obtained from a variety of sources.  These
sources include vendors of air pollution control equipment, industrial
contractors, metal work contractors, and published reports on air pollution
control system costs.23'24'25'26'27'28
     Two cost parameters have been developed: installed capital and total
annualized cost.  The installed capital costs for each emission control
system include the purchased cost of the major and auxiliary equipment,
costs for site preparation and equipment installation, and design engineering
costs.  The capital costs in this section reflect third quarter 1979
prices for equipment, installation materials, and installation labor and
are based on pulse-jet baghouses with a pressure differential of 1.5 kPa
(6 in. W.G.) and an air to cloth ratio of seven to one.  The filter bags
for the baghouses are polypropylene.
     The total annualized costs consist of direct operating costs and
annualized capital charges.  Direct operating costs  include fixed and
variable -annual costs, such as:
     •    Labor and materials required for operation of the control equipment
     t    Maintenance labor and materials
                                     S-17

-------
                                    TABLE 7
                         TECHNICAL PARAMETERS  USED  IN
                       DEVELOPING CONTROL SYSTEM COSTS
      Parameter
1.  Temperature
2.  Volumetric flowrate
3.  Moisture content
4.  Particulate loadings:
    A.  Inlet
    B.  Outlet
5.  Plant capacities
6.  Operating schedule
                 Value
Ambient
See tables 1 through 5, 9, and 10.
2 percent (by volume)
12.8 g/Nm3 (5.6 grains/scf)
0.050 g/Nm3 (0.02 grains/scf)
68, 135, 270, 540, and 817 megagrams per hour
(75, 150, 300, 600, and 900 tons per hour)
1,250 hours per year
                                     S-18

-------
     9    Dust disposal
     »    Replacement parts
Dust disposal costs apply to the baghouse control  systems  A unit cost of
$4.40 per megagram ($4.00 per ton) of particulate collected is used to
cover the costs of trucking the collected particulate to an on-site
disposal point.
     The snnualized capital charges account for depreciation, interest,
administrative Overhead, property taxes, and insurance.  The depreciation
and interest havsr been computed by use of a capital  recovery factor.  The
capital recovery-factor depends on the depreciable life of the control
system and the interest rate.  For the portable plant analysis, a seven
year depreciable life for the control system and a 10 percent interest
rate are used.  This gives a capital recovery factor of 20.54 percent.
Administrative overhead, taxes, and insurance have been fixed at an
additional four percent of the installed capital cost per year.  Table 8
lists the annualized capital cost factors used.                  .

A.2.4.  New Portable Plants
     Two model portable plants have been developed for costing purposes.
One is a portable sand and gravel plant and the other is a portable
crushed stone  plant.  The control option used to achieve the emission
level of 0.05  grams "per dry  standard cubic meter (0.02 grains per dry
standard cubic foot) is a baghouse system.  For an uncontrolled emission
rate of 12.8 grams per dry standard cubic meter (5.6 grains per dry
standard cubic foot) this control option is 99.6 percent efficient in
removing particulate at the  model portable plants.  The size and number
of baghouses required to achieve  the emission limit vary according to the
output capacity of the portable plant.  The air flowrates for the baghouse
systems are  listed in Tables 9 and 10.
     Tables  11 through 15  list installed capital, direct operating,
annualfzed capital, and total annualized costs  for each of the baghouse
systems installed  in the two model portable plants.  The five  portable
plant  output capacities for  which costs  have been developed  represent the
output capacities  applicable to portable plants in the  sand  and gravel
                                  S-19

-------
                                  TABLE 8
                         ANNUALIZED CAPITAL COSTS
1.  Operating labor
2.  Annual maintenance
3.  Utilities:
    Electric power
4.  Replacement parts:
    Polypropylene bags
5.  Capital recovery factor
6.  Taxes, insurance, and
    administration charges
7.  Estimated life of baghouse
    control system
$12.00/hour
5 percent of the total installed cap-
ital cost for each control system
$0.04/kWh

$8.00/m2 ($0.75/ft2)
14.60 percent of total cost for
each control system
4 percent of total installed capital
cost for each control system
7 years
     *Three quarters of total filter bag area is replaced every year
                                    S-20

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and crushed stone industries.  The cost-effectiveness ratios appearing in
Tables 11 through 15 are simply the total  annualized costs divided by the
estimated amount of particulate collected  per year.
                                   S-29

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A.3  ECONOMIC IMPACTS
A.3.1  Introduction and Summary
     In order to further  analyze the  potential  economic  impacts  of  NSPS
controls upon the  portable  plant segments  of  the  crushed stone  and  sand
and gravel  industries, a  Discounted Cash Flow (DCF)  model  was developed.
This model  has  been used  to estimate  the financial  status  or profitability
of portable plant  operations,  both before  and after the  aodition of NSPS
controls.
     The model  has recognized  several  major variations in the methods  of
operation  chosen  by various firms  within the  industry.  For this reason
separate analyses  have been completed under different assumptions regarding:

      •  •  Portable plant  capacity
      •   [Average hours  of operation per year
      •    Level of portable plant  mobility, i.e., mobility among quarries
           alone,  or both  mobility  among and within various quarry sites.

      In the discussion which follows, those plants which typically move
 within the quarry (in order to minimize the distance  between the primary
 crusher and newly blasted  rock) are said to "follow the highwall", while
 those which remain stationary within each  quarry are  denoted as "no highwall".
 Sand and gravel plants were not examined under the "follow the highwall"
 option since this mode of  operation is not used by such plants.
      The results  of the DCF analysis are summarized in  Table 16.   For
 those cases where the potential new investment is Tabled F  (feasible), the
 economic feasibility of  the investment will be unaffected by NSPS controls.
 Where NF  (not  feasible)  is  noted, the  investment may  not be made if the plant
 is to operate  under the  parameters specified.  Where  A  (ambiguous) is noted,
 the DCF analysis  has yielded '"borderline" potential impacts for reasons
 discussed  below.  All assumptions made and steps taken  in arriving at these
 conclusions are detailed in the sections which follow.
 A.3.2  Methodology
       The  findings noted  above  have been derived  through the application of
  a Discounted Cash Flow (DCF) model, constructed to  reflect  the  financial
  situation  of a given  portable  crushed  stone  or sand and gravel  plant which

                                 S-30

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 may  be  purchased  and  operated  in the future.   The basic  distinctions  between
fixed and portable operations have been considered in the development of
 this model.   These distinctions  include variations in equipment life,  annual
 hours of operation,  investment requirements,  markets served,  and the  costs
 associated with the  NSPS  controls.

                                        TABLE  16
                        SUMMARY .OF DCF RESULTS FOR PORTABLE  PLANTS
                                       Crushed Stone
Sand and Gravel
Plant
Capacity
Mg/hr tph
68
135
270
540
75
150
300
600
Operating
Hours
(hours/year)
1250
1600
1250
1600
1250
1600
1250
1600
Uncon-
trolled
NF
NF
NF
A
A
F
F
F
With NSPS
No
Highwall
NF
NF
NF
NF
NF
A
F
F
Controls
Follow
Highwall
NF
NF
NF
NF
NF
NF
F
F
Uncon-
trolled
NF
NF
NF
A
A
F
F .
F
With NSPS Controls
No-
High wall
NF
NF
NF
NF
NF
A
F
F
 Key:   F - economically feasible
      NF - not economically feasible
       A - ambiguous (investment not necessarily precluded)

      All plants for which the DCF analysis has been applied have been assumed
 to function within a scenario defined by the following conditions:

      s    The plant will operate as a separate business entity or "profit
           center",
                                      S-31

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     •    The  pass  through  of  control  costs to the consumers of the products
         of new portable plants'is, to some extent,  limited by competition
         of existing portable plants  which will  not  be affected by the NSPS
         to the same degree,
     •     Individual  plants may choose to operate either 1250 hours/year or
         "1600 hours/year,
     •     Individual  plants may choose to remain stationary within each
          quarry (i.e., not follow the highwall) or move about within the
          quarry (i.e., follow the highwall),
     •'    The  planning horizon for potential investors in portable plants
          is 10 years.
     The assumption that the new portable plant will  operate as a separate
business entity implies that the plant will not at any time be dependent
upon, or supported by revenues generated by other business  activities of the
investing firm.  It is implied therefore, that debt incurred through the
initial investment, and all other expenses associated with  the plant's
operation will be paid only through those revenues generated by the new plant
itself. This assumption may reflect a  conservative point-of-view for vertically
integrated  or multi-plant firms;  however, the  assumption  is plausible  for
horizontally integrated firms  having a  single  processing  plant.
     The condition that  the pass through of  control costs to the consumers
of portable plant  products, will be limited  by competition  from existing
portable plants  (which will not be affected  by NSPS),  reflects  the  reality
that portable  plants  typically compete with  other portable  plants,  since
the  ability of  a  plant to  locate near  the  site of an  impending  job,  is  the
key  to  lowering  customer transport costs and thus securing  orders  for  crushed
stone  and sand  and gravel.  For stationary  plants it  has  been  projected that,
due  to  the  replacement of  old plants  by new (NSPS) plants,  25  percent  of  the
cost of pollution  control  will be  passed through  every four years  (see
Section 8.4.2).  Recognizing that the  competition  among portable plants is
potentially greater,  and thus the  cost pass through  ability lower,  it  has
been assumed  that  portable plant  operators will  require twice  as much  time
 (i.e.,  eight years)  to pass through 25 percent of pollution control  costs.
 In  the DCF  analysis  this level is  reached  by way  of  pass  through  increments
 of  6.25 percent every two  years.   This assumption is  conservative  in that  for
 those  sections of the country where  competition is less intense,  product
 prices may  be increased  sooner to  reflect  additional  costs.

                                 S-32

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     The DCF analysis detailed in Section A.3.3 has been constructed in such
a way that the operational peculiarities of individual portable plant opera-
tors are considered.  For example, it has been noted that the preferences of
individual operators vary, especially with regard to the hours of operation
per year and the movement of plants within individual quarries. -Therefore,
in an attempt to differentiate impacts for each of these modes of operation,
each model plant has been individually examined assuming 1250 and 1600
operating hours per year, as well as preference for moving within individual
quarries (i.e., following the highwall) or remaining stationary within each
quarry (i.e., no highwall).  It should be noted that the preference for
within quarry mobility will entail higher pollution control costs due to the
need to dismantle and set up control equipment more often.
     The investment planning horizon of 10 years has been selected based upon
the 10 year normal useful life of portable plants.  The 10 year life has been
supported by representatives of the industry.30
     The cash flows considered by the DCF model are:

     •    Earnings after tax,
     •    Depreciation of plant and rolling stock,
     •    Depreciation of pollution control equipment,
     •    Working capital recovery,
     e    The salvage value of plant and rolling stock, and
     •    Payback of debt.

     Earnings after tax have been determined after consideration of all oper-
ating costs, depreciation expenses, interest expenses, overhead, and pollution
control costs.  In the determination of earnings after tax the availability
of depletion allowances and investment tax credits, have been recognized.
Regarding depreciation, plant and rolling stock have been depreciated  (straight-
line) over their respective useful lives.  Pollution control equipment has
been depreciated over five years to a zero salvage value.  It has also been
assumed that working capital requirements are funded out of equity and that
all plant and rolling stock is sold at salvage value after 10 years. Each of
these items is discussed in greater detail in the following section.
                                   S-33

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     A.3.2.1  Critical Elements.  In the estimation of the potential impacts
of NSPS controls, numerous data elements have been assembled and evaluated to
allow their incorporation into the DCF model.  In the descriptions listed
below each of the critical elements is identified and discussed in terms of
its use in the model.  Sources of data pertinent to each critical element are
listed in Section A.3.2.2.
     With regard to operating hours per year, individual firms contactedSO
indicated a variety of preferences, however most tended toward two  levels,
1250 and 1600 hours per year.  Although the actual hours per year is heavily
dependent upon the weather, these two figures have been identified  as target
levels.  The number of operating hours per year is perhaps the most critical
data element since it is  the prime determinant of net revenues generated by
each plant, in this high fixed cost, low profit margin industry.   In the DCF
model all production  is assumed to be sold and thus there  is no net change  in
the inventories  of the model plant.
     Concerning  product prices, distinctions between crushed stone  and sand
and gravel have  been  made.  The values employed in the DCF model  are $3.25/ton
for crushed stone and $2.86/ton for sand and gravel.  The price of  crushed stone
was noted by two industry representatives and the price of sand and gravel
was derived from the  crushed stone price, based upon Bureau of Mines31*32
data indicating  that  for  recent years the price of sand and gravel  has
approached 88 percent of  that for  crushed stone.
     Based upon  the  $3.25/ton price of crushed stone, operating costs  (exclu-
ding depletion,  depreciation, interest and overhead) have  been  identified
based  on discussion  with  industry  representatives, as $2.10/ton.  Operating
costs  for sand and  gravel plants  have been estimated by applying  the ratio  of
operating cost/price  for  crushed  stone  ($2.10/$3.25), to the price  of  sand
and gravel, to estimate sand and  gravel operating costs of $1.85/ton.
     The validity of the  $2.10  and $1.85/ton operating  cost levels  for
  i
crushed stone and sand  and  gravel  portable plants, respectively,  has been
supported through the determination of the pre-control  Internal Rates  of
Return  (IRR) for those  plants faced by these costs.  Such  rates  have been
calculated  and are  summarized  in  Table 17.
                                 S-34

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                                    TABLE  17
              INTERNAL  RATES  OF  RETURN FOR PORTABLE  CRUSHED  STONE
                        AND SAND AND GRAVEL PLANTS
                         (Pre-Pollution Control)
Plant Capacity
(Mg./hr) (tph)
68
135
270
540
75
150
300
600
Operating Hours
(hours/year)
1250
1600
1250
1600
1250
1600
1250
1600
Crushed
Stone
io.°o%
10.1%
14.0%
14.2%
18.2%
20.9%
25.6%
Sand and
Gravel
<9.9%
9.9%
10.2%
14.3%
14.5%
18.4%
21.4%
     The  IRR percentages  in Tabie  17 appear to be  reasonable. In  light of
current returns on other  forms of  long-term investment.  Had  the pre-control
rates been higher than those actually calculated,  the understatement of
operating costs could be  a suspected cause.  On the other hand,  if the
pre-control rates were estimated to be lower than  those of Table 17, the
overstatement of operating costs/ton might have been suspected.
     Depreciation of plant equipment has been taken as straight-line over
its 10 year life.  Depreciation of rolling stock has been taken  as straight-
line over a seven year life in order to take full  advantage  of the investment
tax credit.  Depreciation of pollution control equipment has  been taken as
straight-line over five years to a zero salvage value.  Investment tax credit
is also available, and is taken on pollution control equipment using a 5-year
rapid amortization writeoff.
     Debt terms for plant, rolling stock, and pollution control  equipment
have been assumed to be five years at a 15 percent interest  rate.  Industry
contacts have noted that the availability of debt  financing  at terms better
than those noted, would be uncommon.  It should be noted that the results of
the DCF model  are not sensitive to variation of the interest  rate.
     The financing of portable equipment in terms  of debt/equity has been
observed to range from 0 percent to 100 percent, dependent upon  the prefer-
ences and abilities of individual firms.  For purpose of the  DCF model a
                                 S-35

-------
ratio of 50/50 is employed.  The use of this ratio has been judged realistic
by industry representatives.  It should be noted that the results of the
DCF model are not sensitive to variation in the debt/equity ratio over the
0 to 100 percent range.
     With regard to overhead expenses of portable  plant  operations,  industry
sources  have  indicated that for  a 270 Mg/hr  (300 tph) portable  plant'such
costs would be  about  $.25/ton for each  ton of  crushed stone  produced.   For
the  540  Mg/hr (600 tph)  plants  this  figure has been  reduced  to  $.22/ton  due,
for  the  most  part, to economies  of  scale.  These  figures have been  employed
for  both crushed stone and sand and  gravel plants.
      Pollution control  costs  for purposes  of the  DCF analysis,  have been
grouped  into  four  basic classes:

      t     Excess moving costs,
      •     Annual Cost of operation  and  maintenance,
      t     Depreciation, and
      •     Interest on borrowed capital  used to purchase and  install pollution
           control  equipment.
 The inclusion of excess moving  costs account  for  those  added costs  incurred
 due to  the need to dismantle, move  and set up the pollution  control system
 each time the portable'plant is moved, regardless of whether the move is
 within  the quarry or to another quarry.  The  costs  associated  with  these
 activities are summarized in Table  6,  while their inclusion  into the DCF
 model is described in  Section  A.3.3.   Regarding the number  of  moves made by
 the typical  portable plant,  industry sources  have indicated  that the typical
 portable  plant moves to a different quarry,  on average, four times  each
 year.30  For those plants which prefer to follow  the highwall, an  average
 of  24 such within-quarry  moves might be made. Sand and gravel plants,  on
 the other hand, do not often move  within  the  gravel pit,  since very little
  blasting  is  done.
      The  annual  cost category represents  the  annual total  of pollution  control
  costs  incurred by each mo-del  plant. .The  costs summarized under this heading
  include annual maintenance and operating  costs,  utilities,  filter replacement,
  dust disposal costs, property taxes,  insurance,  and administrative expenses.
       Depreciation of pollution control equipment is taken over a 5 year useful
  life,  with a zero salvage value.   For those  plants  which choose to follow the
                                     S-36

-------
 highwall, the  cost  of  a  small  crane  (needed to facilitate  dismantling  and
 reconnecting of  pollutions-control equipment) has been  added to the  plant
 costs, and  is  thus  depreciated  over  ten years.   (Plant  investment costs are
 summarized  in  Section  A.3.2.3.)
      Interest  on the pollution  control equipment for each  plant  has been
 determined  by  calculating the  annual  interest-principal  repayment schedule
 according to the debt  terms described above.
      Depletion expenses  have been determined for each model plant,  under the
 assumption  that  the quarry site  is leased rather than  owned by the  portable
 plant operator.  Under these circumstances the operator  is entitled to a
 depletion allowance according to a depletion base defined  as:

               Depletion base = price/ton - royalty/ton.

 Industry representatives have noted  that royalties paid  by portable plant
 operators are  typically  5 percent of the sale price per  ton.  In the DCF
 model the annual depletion allowance  is calculated as:

        Depletion = depletion base x annual output x % depletion.

 The Internal Revenue Code allows percentage depletion for  both crushed stone
 and sand and gravel minerals of five percent.  Two limitations to the  use of
 percent depletion are:

     •    The maximum  depletion claimed in any year cannot exceed one-half of
          that year's  earnings before tax, and
     •    Depletion is subject to minimum tax as a tax preference item.

     These  limitations have been included, where appropriate, in the year-by-
year calculations of the DCF model.  The assumption that the owner must pay
 royalties represents a conservative  point of view, since this slightly
 reduces the available  depletion base.
     Regarding the  Federal tax  rate, the marginal tax  rate can "vary up to a
 maximum of 46 percent  of earnings before tax and after depletion.   In  the DCF
 model it is assumed that taxable income of the firm, resulting from other
 activities, is sufficiently greater  than $100,000 annually, and  thus the tax
 rate employed  is 46 percent.  State  taxes are assumed to be 5 percent  of
 earnings before tax since this  is the most common state  tax rate.
                                   S-37

-------
     Working capital or capital required to finance accounts receivable and
inventories have been considered in the DCF models.  Industry contacts30
have noted that both accounts receivable and inventories each require -
capital financing on the level of 15 percent of sales, giving total working
capital requirements of 30 percent of sales.  In the DCF models it has been
assumed that working capital  is financed from equity and that all working
capital is recovered after the tenth year.
     Salvage values of plant  and rolling stock  have been considered  in the
DCF model  as cash inflows resulting from their  sale in the  tenth year.  The
salvage values  have been determined through  industry contacts as well  as
inspection of  the used equipment markets as  defined by  industry trade  jour-
nals. 33   The'salvage value  factors  used in the  DCF model  are 36 percent  for
plant  and equipment and  16  percent  for  rolling  stock.
     The  model  assumes that  firms  will  take  maximum advantage  of  the invest-
ment tax  credit.   It  is  recognized that the  credit cannot  exceed  10  percent
of the investment  and  may  not be  carried forward more  than  seven years.
     A.3.2.2   Sources  of Data.   Sources of data used  in  the DCF analysis  are
noted  in  Table 18.
     A.3.2.3.   Plant  Investment.   Estimates of the costs of new  portable
crushed stone and sand and gravel  plants were assembled after discussion  with
 both the manufacturers of portable plants34 and firms  who use portable
 equipment in their quarrying activities.   On the basis of these  discussions
 the investment levels noted  in Table 19 were developed and used in the DCF
 model.   In those instances where a small crane is purchased, in order to
 maintain within-quarry mobility, the cost of such a crane  is assumed to be
 $80,000.
        Plant and equipment investment  for the 270 Mg/hr (300 tph) sand and
 gravel plant was determined  by noting  the difference in equipment require-
 ments  (and thus costs) between the 270 Mg/hr (300 tph) crushed stone model
 plant  and the  sand and gravel model plant of the  same capacity. Plant and
 equipment investments for the 68, 135  and 540 Mg/hr (75, 150 and 600 tph)
 plants were estimated through the  .6 power  capacity rule.
                                     S-38

-------
    TABLE 18
SOURCES OF DATA
                Source
























Data Element
Operating Hours/Year
Product Prices
Operating Costs
Depreciation
Debt Terms
Debt/Equity
Overhead
Pollution Control Costs
Moves/Year
Depletion
Tax Rates
Investment Tax Credit
Working Capital
Salvage Values
Plant Investment













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      S-39

-------
                               TABLE 19
             REQUIRED INVESTMENT FOR NEW PORTABLE CRUSHED STONE
                        AND SAND AND GRAVEL PLANTS
                              ($l,000's 1979)
Plant Capacity

Mg/hr)   (tph)
     Crushed Stone
PI ant .and  Rolling
Equipment  Stock
Total
Invest-
ment
                                                     Sand and Gravel
Plant and
Equipment
Rolling  Total
Stock    Invest-
          ment
68
135
270
540
75
150
300
600
305
462
700
1061
217
330
500
758
522
792
1200
1819
213
323
490
743
218
330
500
758
431
653
990
1501
      A.3.3   Discounted Cash Flow (DCF)  Analysis.   Table .20 presents an
 example of  the data sheets which were developed for each model  plant under
 the previously discussed scenarios regarding operating hours and plant
 movements.   The example presented in Table 20 is that for the 270 Mg/hr
 (300 tph) crushed stone plant which operates at 1,600 hours per year and
 prefers to maintain its mobility within the quarry (i.e., follow the highwall),
 In this case the total investment required  (excluding pollution control)  is
 $1,748,000 represented by:
 Plant
 Small  Crane
 Rolling  Stock
 Working  Capital
 Total  Investment
                      Cost
                   $700,000
                     80,000
                     500,000
                     468,000
                  $1,748,000
                   Source of Funds
                50% debt, 50% equity
                         -do-
                         -do-
                    100% equity
                                    S-40

-------
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-------
Since the plant, crane and rolling stock are financed 50/50 debt/equity,
and working capital from equity alone, the total investment from equity
is 51,108,000.
     The steps summarized below detail how the  discounted cash flows for the
ten year life of this plant were determined.  The derivation  of  individual
values are explained in Section A.3.2.1.

     •    Row 1, Revenue, was  determined by multiplying  operating  hours  per
          year  (1,600) by the  capacity  per  hour (300  tph) and the  price  per
          ton for  crushed stone  ($3.25).
     •    Row 2, Operating  Costs:   Plant and  Rolling  Stock,  has  been esti-
          mated  by multiplying operating hours  per  year  (1,600)  by the
         '. capacity per  hour (300  tph) and  the operating  costs per ton
           ($2.10). In  addition $8,000/  year was included as  the  operating
           costs  for the  small  crane.
      t    Row 3, Depreciation:  Plant,  was derived  by subtracting from the
           total  investment  in plant ($700,000 + $80,000),  the estimated
           salvage value at  36 percent ($281,000) and calculating the annual
           depreciation charge for each of the 10 years.
      •    Row 4, Depreciation:  Rolling Stock,  was  determined by subtracting
           from the investment ($500,000)  its salvage value of 16 percent
           (580,000) and calculating the annual  depreciation  charge for each
           of seven years.  For years 8, 9 and  10, the model   assumes the fully
           depreciated rolling stock  requires increased maintenance and so
           operating costs have been  increased  by $60,000 (i.e. the value  of
           annual  depreciation) for those years  (Row  2).
      •    Row 5,  Interest:  Plant  and Rolling  Stock  for each year has been
           determined by calculating  the annual  interest-principal repayment
           schedule  based on the terms of  a five year loan of $640,000 at  15
           percent.
       t    Row  6,  Overhead, has been  determined by  multiplying the operating
           hours  per year (1,600) by  the capacity per hour (300  tph)  and the
           estimated overhead  costs per ton  ($.25).
       .    Row  8,  Excess  Moving  Costs:  Pollution Control have been  estimated
            based upon  the data summarized  in  Table  6  regarding the  cost  of
                                    S-42

-------
 moving the control  system.   Based upon an estimated 24 mcves/yesr
 within the quarry,  4 moves/year among quarries, labor costs for
 control  system dismantling  and set up of $1,440/move and average
 transportation costs of $5,120 for moves to different quarries, the
 annual excess moving costs  have been determined to be $61,000-.
 Row 9, Annual Cost:   Pollution Control was obtained by summing  the
 following annual  direct cost components (Table 13); annual  0 &M costs
 utilities,  filter replacement, dust disposal,  and taxes,  insurance
 and administration.                 ,       ~
 Row 10,  Depreciation:   Pollution  Control,  was  determined  by assuming
 the total  installed  capital  costs  ($203,6£0) of Table 13  will be
 depreciated to zero  salvage  value  over five years.
 Row 11,  Interest:  Pollution Control,  was. determined through the
 interest-principal repayment schedule  for  a loan of ($203,600)  for
 five years  at 15  percent.
 Row 13,  Pass-through,  was determined based on  the assumptions
 regarding the gradual  pass-through  of  pollution control costs to
 the consumers of  crushed stone and  sand and gravel  (see Section
 A.3.2).   More specifically,  the DCF model  assumes that the  follow-
 ing percentages ,.of the  total  costs  of  pollution control will  be
 passed to consumers  in  the form of  higher  prices:
 -   Years  1  and 2           =     0  percent
 -   Years  3  and 4           =6.25  percent
 -   Years  5  and 6           = 12.50  percent
 -   Years  7  and 8           = 18.75  percent
 -   Years  9  and 10          = 25.00  percent
 While  in  reality the pass through of control costs  will increase
 the yearly  revenues, the arithmetic  of  Table 20 is  based  upon
 the deduction  of the pass through amounts  from  total  costs.
 Row 16, Depletion, has  been  estimated for  each  year by multiplying
 the depletion  base ($3.08),   the calculation of  which  is described
 in  Section A.3.2.1, by  the capacity  per hour, operating hours per
year, and the  five percent depletion allowance.   Following this
 procedure has yielded a maximum annual  depletion  of $73,000.
 However, Federal tax laws prohibit  the  claiming  of  depletion allow-
                        S-43

-------
ances  in  excess  of one-half  of  earnings  before  tax.   In  the  case
presented in Table 20 the  plant cannot  claim full  depletion
until  the fifth  year  of  operation.
Row-18,  Federal  Tax Liability,  has  been calculated on the basis of
 a marginal tax rate  of  46  percent.
 Row 19,  Investment  Tax  Credit,  has  been calculated or, the assump-
 tion that the firm  will  attempt to  apply the full  credit available,
.which in this case  is $148,000 (i.e., 10 percent of the total
 investment of $1,483,600 including pollution control).  Current tax
 laws dictate that credit may be taken on the first $25,000 of
 earnings  before tax and after  depletion, plus  a percentage of
 earnings  above  this amount.  Presently  the  tax  laws  allow credit
 for 60 percent  of earnings  above the $25,000 level in 1979,  and  70
 and 80 percent  for 1980 and 1981,  respectively.   For 1982 and  all
 following years the  percentage is  90 percent.
 Row  21,  Adjustment:  Minimum Tax.   Since the previously discussed
  depletion allowance  is  a  "tax  preference  item" the tax  law  calls
  for the payment of  a minimum tax if the amount of the firm's
  Federal  tax (row 20)  is less than  the  depletion claimed (row 16).
  For those years which  this is  so,  an adjustment of the year's
  depletion must be  made in order to define a "minimum tax base" (• ow
  22).  This adjustment is taken as  the years Federal  tax (row 20)
  unless that tax is less than  $10,000 in which case the adjustment
  is $10,000 according to the Internal Revenue Code.
  Row  22,  Minimum Tax Base,  was determined by subtracting the adjust-
  ment (row 21)  from the year's depletion (row  16).
  Row  23,  Minimum Tax, was determined by applying  the  minimum tax
   rate of 15 percent, to each year's minimum tax base (row 22).
   Row 24,  Total  Federal  Tax, was  derived through the  addition of  each
  year's  minimum tax  (row  23) and Federal tax (row 20).
   Row 25, State  Tax,  was determined through  the application  of  the
   most common  state  tax rate (5 percent) to  each year's  earnings
   before income  tax  (row 15).
   Row 26, Total  Tax,  shows the  amount of Federal  and  state taxes
   payable for a particular year.
                              S-44

-------
           Row  27, Earnings After Tax, forms the first  item  in the cash flow
           calculations  (Rows 27 through 37).
           Rows 28, 29,  and 30, entail the "adding back" of  various deprecia-
           tion amounts  into the annual cash flows of the portable plant.
           Row 32, Working Capital Recovery, was added to the final year's
           cash flow to  reflect the recovery of equity capital previously
           sunk in accounts receivable and inventories.
           Row 33, Salvage Value, was added to the tenth year's cash flow to
           reflect cash gene -ated from the sale of the ten year old portable
           plant.   The calculation of this salvage value was noted previously
           in Section A.3.2.1.
           Row 34, Principal  Repayment:  Plant  and Rolling Stock,  was deducted
           from each  of the first five year's cash flows since one-half of the
           investment in  pi ant  and rolling stock has  been financed through
           debt  over  five years  at 15 percent.
           Row 35, Principal  Repayment:  Pollution  Control,  was  also  deducted
           from  the cash  flows  of years one through five since the investment
           in pollution control  equipment  has been  financed  completely, through
           debt  over  five years  at  15  percent.
           Row 38,  Discount Factor.   In order to account for the fact  that
           cash  flows  to  be received  during the near  future  are  "more  valuable"
           to  the  firm  than those  to  be generated  in  the later years,  all  cash
           flows have  been discounted  to their  present  value.  The discount
           factors  have been determined on the  basis  of  a cost of  equity of  15
           percent.  The  cost of equity has been used since  the DCF'analysis
           detailed above  has accounted for the repayment of  all loans  (i.e.,
           debt) used to  support the portable plant's operation.
           Row 39, Discounted Cash Flow.  When  the  cash  flows  of each year are
           discounted to  their present  value  and summarized  a  value of  $828,000
           is derived.  It is this value which  is compared to  the  original
           investment from equity  ($1,108,000)  to allow the further calcula-
          tion of the  Internal  Rate of Return  (IRR)  as described  below.
A.3.4  Conclusions
     A.3.4.1  Internal Rates of Return*  IP an effort to gain greater insight
into the specific economic impacts upon those plants examined, the Internal
                                 S-45

-------
Rate of Return (IRR) for each plant was determined.  Such a rate is defined,
in each instance, as that rate of return which equates the present value of
future cash flows with the value of the initial required investment from
equity.  Therefore, according to this definition, the feasibility of  indivi-
dual investments  is judged by whether or not the  IRR is greater than  the
cost of equity  (and thus economically attractive) or less than the cost of
equity  (and thus  not  attractive).   Based on  discussions with  industry repre-
sentatives, the  cost  of  equity was  assigned  a  value of  15 percent per year.
     A.3.4.2   Feasibility Definitions.  Once each IRR was identified  it
became  necessary to  establish  boundaries or  "cut-off" points  so that  eco-
nomically  feasible  and non-feasible investments might  be more clearly dis-
tinguished.   While  in the  strictest sense, such  a cut-off  point  should be
the cost  of equity,  a middle range of "ambiguous" results  has been  selected.
The need  for such a range  is based upon the reality that the economic envi-
 ronment of all portable plants is not,  and will  not be identical.   Recognizing
 this reality, the values for a number of parameters chosen  in the above DCF
 analysis  have reflected conditions which would be faced by a small  number of
 plants in the extreme.  Recognition of the use of such conservative  assumptions
 is crucial in the interpretation of the DCF results (Table 16) since, in
 reality,  many plants will  not face conditions of such an unfavorable nature.
      Specific examples of the use of conservative assumptions made in this
 analysis  include:

      •    Operating  hours per year - it is  quite possible that the plants  in
           question  can  or will operate for  a  number of years during  the 10-year
            span  at  rates higher than  1,250 hours  per year,
      •     Prices -  control  costs may be passed to the  consumer at a  rate much
            higher than that  assumed,  especially  in those areas of less strict
            competition,
       •    Debt terms -  some firms,  especially those with well established
            credit lines, may be  able to obtain bank financing at  less than  15
            percent,  or over periods longer than  5 years.

  For these reasons  a range of ambiguity of 12  to 15 percent  IRR has  been
  selected, and for the purpose of Table 16,  NSPS controls  for those  plants
                                   S-46

-------
whose post-control IRR is greater than 15 percent are identified as "econo-
mically feasible", while those below 12 percent are said to be "not economi-
cally feasible".  For a specific plant whose internal rate of return, as
calculated by the method employed here, .falls within the 12 to 15 percent
range (termed "ambiguous"), an investment decision will have to be made
after careful revaluation of prevailing process, market and economic condi-
tions.

     A.3.4.3  Adaptation of Portable Plants to NSPS Control.  In general, the
implications of the results of the DCF analysis summarized by Table 16 are
that the profitability of those new plants who desire to operate at relatively
low hours per year and/or maintain within quarry mobility will be adversely
affected.  With specific regard to crushed stone, it appears that the new 270
Mg/hr (300tph) portable plants may be forced to operate at a greater number
of hours each year and limit the number of within quarry moves made.
However, it should be noted that for those new plants which can operate at
levels above 1,250 hours per year and also pass a greater portion of
control  costs to consumers of crushed stone, profitability will be main-
tained.   Since sand and gravel plants ordinarily do not move within gravel
pits, the new 270 Mg/hr (300 tph) portable plants which will maintain
profitability will be those which either operate at a higher level of hours
each year, or can increase the price of their products enough to cover the
increased costs of pollution control.
                                  S-47

-------
                            REFERENCES

1.  Letter and attachments from Brown,  Howard, _Iowa Manufacturing Company,
    to Viconovic, George, GCA/Technology Division.  June 18, 1979.  Data
    on portable and stationary plants in the crushed  stone and sand and
    gravel industries.

2.  Telecon.  Hart, Michael, Colorado Sand and Gravel Association with
              Viconovic, George, GCA/Technology Division.  June  13, 1979.
              Portable plants in the sand and gravel  industry.

3.  Telecon.  Davidson, Edward, National Sand and Gravel  Association  with
              Viconovic, George, GCA/Technology Division.  June  13, 1979.
              Portable plants in the sand and gravel  industry.

4  Telecon.  Hoover, Earl, United States Bureau of Mines with Viconovic,
4.  Telecon.  noo^, GCA/f echnol Qgy Division.  june 8, 1979.   Portable

              plants in  the crushed stone industry.

 5.  Telecon.  Renninger,  Frederick, National Crushed Stone Association
              with Viconovic, George,  GCA/Technology Division.  June 13,
              1979. Portable  plants in  the  crushed stone industry.

 6.   Telecon.   Pressler,  J., United States Bureau of Mines with Viconovic,
               George,  GCA/Technology Division.  June 8, 1979.  Portable
               plants in the gypsum  industry.
 7.  Telecon.  Messinger, Arthur, United States  Bureau of      o
               Viconovic, George, GCA/Technology Division.   June 8, 1979.
               Portable plants in the pumice industry.

 8   Telecon.  Ampian, S., United States Bureau  of Mines with  Viconovic,
 8.  Telecon.  gjjjj; GC^Technol0gy D1v1s1on.   June 11,  1979.  Portable

               plants in the clays industry.

 9.  Telecon.  Brown, Howard, Iowa Manufacturing Company with  Viconovic,
               George, GCA/Technology Division.   June 11,  1979.  Portable
               plant industry data.

 10.  Telecon.  Brown, Howard, Iowa Manufacturing Company with  Viconovic,
               George, GCA/Technology Division.   June 15,  1979.   Industry
               data.

 11.  Telecon.  Hart, Michael , Colorado  Sand .and Gravel Association with
               Viconovic,  George, GCA/Technology Division.  June 18,  1979.
                Industry  data.
                                  S-48

-------
 15,
22,
23,
24,
      Telecon.  Olson-, DeTv Gifford-Hill  Company with  Viconovic,  George,
                GCA/Technology Division.   June  28,  1979.   Industry data.

                Cole, Richard, Flintkote  Company with  Harnett, William,
                Gu,A/ Technology Division.   November 8,  1979.  Portable
                plant operating and  movement  data.
 12,
 13.   Telecon,
 14.   Telecon.
                Brown,  Howard,  Iowa Manufacturing Company with Viconovic
                George,  GCA/Technology Division.  June 21, 1979.  Portable
                and  stationary  plant sales data.

      U.S.  Bureau  of Mines Mineral Commodity Summaries 1979.  Washington
      B.C.,  U.S. Department of  the Interior, 1979.  190 p.
 16.   Telecon,
 17.   Telecon,
               Cole, Richard, Flintkote Company with Viconovic, George,
               GCA/Technology Division.  June 13, 1979 and June 14,
               1979.  Portable plant cost and movement data.

               Olson, Del, Giffor-Hill company with Viconovic. George,
               GCA/Technology Division, June 15, -1979.  Portable plant
               cost and movement data.
 19.  Telecon,
20.  Telecon,
 18.  Telecon.  Hart, Michael, Colorado Sand and Gravel Association with
               Viconovic, George, GCA/Technology Division.  June 17,
               1979.  Portable plant movement data.

               Lahu, Peter, Speer Construction with Viconovic, George,
               GCA/Technology Division.  July 17, 1979.   Portable plant
               operating and movement data.

               Ellis, Oscar, Moline Consumers Company with Viconovic,
               George, GCA/Technology Division.   July 18,  1979.   Portable
               plant operating and movement data.

21.  Telecon.  Hart, Michael, Colorado Sand and  Gravel Association, with
               Viconovic,'George, GCA/Technology Division.   July 19,
               1979.  Portable plant operating and movement data.

     Telecon.  Ellis, Oscar, Moline Consumers Company with Harnett,
               William,  GCA/Technology Division.   November 8,  1979.
               Portable  plant operating and movement data.

     Letter and attachments from Schroeder, Philip N., M.C.  Schroeder
     Company to Viconovic,  George, GCA/Technology Division.  July 27, 1979
     Baghouse cost data.

     Letter and attachments from Meyer, Robert J.,  Joy Industrial
     Equipment Company-Western Precipitation Division to Viconovic,  George,
     GCA/Technology Division.   July 27, 1979.  Baghouse cost data'.
                                   S-49

-------
25.  Telecon.  Schroeder, Philip N., M.C._Schroeder Company with Viconovlc,
               George, GCA/Technclogy Division.  August 6, 1979.  UuctworK
               cost data.

26.  Telecon.  Hamlin, Robert, Hamlin Sheet Metal Company with  Vlconovlc,
               George, GCA/Technology Division.  August 8, 1979.  Ductwork
               cost data.

27.  PEDCo.    Environmental  Inc.  Cost Analysis  Manual for Standards
     Support Document.   Cincinnati,  PEDCo.  Environmental  Inc., April  1979.

     82  p.

28.  Perry,  Robert  H.  and Cecil  H.  Chilton.   Chemical  Engineers'  Handbook.
     New York, McGraw-Hill  Book  Company,  1973.

29.  Memo from Brown,  Howard, Iowa Manufacturing Company,  to  Goodwin,
     Don  EPA/OAQPS.   March 1,1979.  Data on portable plants and
      stationary  Plants in the crushed stone and sand and gravel industries.

 30.   Included among industry contacts are;

          ':     Douglas E. Anderson, B.L. Anderson, Inc., Jedar Rapids, Iowa
                Larry Hinton, Azrelli Construction, Inc., Kankakee, Illinois
                Flovd Lillig, Iowa Manufacturing Company, Cedar Rapids, Iowa
                William J. Paxson, Chief Engineer, Iowa Manufacturing Co.,

                AlbertRRichardson! Gordon Quarries, Inc., Forrest City, Missouri-
                Howard L. Slife, V.P., Cedar Rapids Aggregate Equipment Sales,
                Iowa Manufacturing Co., Cedar Rapids,  Iowa
      •         Robert Treager,  Farmers Stone and Treager Quarries, Inc.,
                lafi,  Missouri

  31   U.S. Bureau of Mines  Mineral Commodity  Profiles  Stone.  MCP-17.   U.S.
      Department  of the  Interior,  Washington, D.C. July 19/8.   p.10

  32.  Lr.S. Bureau of Mines.  Mineral  Commoidity  Profiles.   Sand  and Gravel.
      MCP-23.  U.S. Department  of  the Interior.   Washington,  u.t.
       September  1978.  p.12

  33.   Highway and Heavy  Construction.   September 1979. p.  150-158.

  24.   Iowa Manufacturing Company.   Cedar Rapids. Iowa
ig-
                                    S-50

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                                   TECHNICAL REPORT DATA
                            (nease read Instructions on the reverse before completing)
  EPA-450/3-83-QQla
                                                            3. RECIPIENT'S ACCESSION MO.
 I. TITLE AND SUBTITLE
  Nonmetallic Mineral Processing  Plants _
  Background Information for  Proposed Standards
             5. REPORT DATE

              April 1983
-ftp.
n%
             6. PERFORMING ORGANIZATION CODE
      )OR(S)
                                                            8. PERFORMING ORGANIZATION REPORT N'O.
                 IZATION NAME AND ADDRESS
 Office  of Air Quality Planning  and  Standards
 U.S.  Environmental Protection Agency
 Research  Triangle Park, North Carolina-  27711
                                                            10. PROGRAM ELEMENT NO.
             11. CONTRACT/GRANT NO.

               68-02-3057
 12. SPONSORING AGENCY NAME AND ADDRESS
 DAA  for  Air  Quality Planning and  Standards
 Office of  Air, Noise, and Radiation
 U.S.  Environmental  Protection Agency
 Research Triangle Park, North Carolina   27711
             13. TYPE OF REPORT AND PERIOD COVERE-1
             14. SPONSORING AGENCY CODE
               EPA/200/04
      Standards  of performance for  the  control  of emissions from  nonmetallic mineral
 processing  plants are being proposed under the authority of  Section 111  of the Clean
 Air Act.  These standards would apply  to  new,  modified, or reconstructed facilities
 at any nonmetallic mineral processing  plant including crushers,  grinding mills,
 screens, bucket elevators, conveyor belt  transfer points, bagging  operations, storage
 bins, and enclosed truck and railcar loading stations.  This document contains
 background  information and environmental  and economic impact assessments, as proposed
 under 40 CFR  Part 60, Subpart 000.
 7.
                                KEY WORDS AND DOCUMENT ANALYSIS
                  DESCRIPTORS
                                              b.lDENTIFIERS/OPEN ENDED TERMS
                                                                         c. cos AT I ! ield/Group
 Air pollution
 Pollution control
 Standards of performance
 Nonmetallic mineral  processing plants
 Particulate emissions
Air Pollution  Control
                  13B
 8. DISTRIBUTION STATEMENT
 Unlimited
                                              19. SECURITY CLASS (This Report/
                                               Unclassified
                          21. NO. OF PAGES
                               469
                                              20. SECURITY CLASS (Thispage!
                                               Unclassified
                                                                         22. PRICE
EPA Form 2220-1 (Rev. 4-77)
                      PREVIOUS EDITION IS OBSOLETE

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