105048

EPA-450/2-74-021-C
January 1976
PB 251 618
       BACKGROUND INFORMATION
   FOR STANDARDS OF PERFORMANCE:
       COAL PREPARATION PLANTS
VOLUME 3: SUPPLEMENTAL INFORMATION
          U.S. ENVIRONMENTAL PROTECTION AGENCY
             Office of Air sod Waste Management
           Office of Air Quality Planning and Standards
          Research Triangle Park, North Carolina 27711

-------
                                 EPA-450/2-71-021-C
        BACKGROUND INFORMATION
   FOR STANDARDS OF PERFORMANCE:
        COAL PREPARATION PLANTS
VOLUME 3:  SUPPLEMENTAL INFORMATION
             Emission Standards and Engineering Division
               U.S. ENVIRONMENTAL PROTECTION AGENCY
               Office of Air and Waste Management
             Office of Air Quality Planning and Standards
             Research Triangle Park, North Carolina 27711

                     January 1976

-------
This report has been reviewed by the Emission Standards and Engineering
Division, Office of Air Quality Planning and Standards, Office of Air
and Waste Management, Environmental Protection Agency, and approved
for publication.  Mention of company or product names does not constitute
endorsement by EPA.  Copies are available free of charge to Federal em-
ployees, current contractors and grantees, and non-profit organizations -
as supplies permit - from the Air Pollution Technical Information Center,
Environmental Protection Agency. Research Triangle Park, North Carolina 27711,
or may be purchased f^om the National Technical Information Service,
5285 Port Royal Road, Springfield, Virginia 22161.
                     Publication No. EFA-450/2-74-02I-C

-------
                      Table of Contents
                                                             Page
I.   Introduction	  1

II.   Mass Emission Standard for Thermal Dryers  	   3

III.   Opacity Standards	    9

IV.   Economic Impact	   13

V.   Inflationary and  Energy Impacts  	    16

VI.   Summary of Public Comments and  EPA Responses  	   19

Appendi x A		  37

Appendi x B	  56
                               111

-------
I.  Introduction
     On October 24, 1974 (39 FR 37922), the Environmental Protection
Agency proposed standards of performance for new and modified coal
preparation plants.  At that time, EPA made available for public
distribution a background document (in two volumes) entitled
"Background Information for Standards of Performance:  Coal Preparation
Plants, " EPA -450/2-74-021 a and b (October 1974).  The background
document explained the background and bases of the proposed regulations.
Copies may be obtained by writing to Emission Standards and Engineering
Division, Environmental Protection Agency, Research Triangle Park,
North Carolina 27711,  Attention:  Mr. Don R. Goodwin.   This supplement
to the background doeuwent is being issued in connection with final
promulgation of the regulations.
     Twenty-seven parties commented on the proposed standards.   A
summary of the public comments and EPA's responses to them is presented
in Section VI of this document.  In addition, this document supplements
the information presented in the background document as indicated below.
     As a result of several comments, the standard for thermal  dryers
was reevaluated by EPA.  This document contains the results of the
reevaluation including a discussion of tests conducted in response to
one of the comments (Section II), a summary of updated control  costs
(Section IV), a discussion of the inflationary impact of these control
costs (Section V), and a projection of the annual power consumption
increases reguired by the standard (Section V).
     On November 12, 1974  (39 FR 39872), after the proposal of standards
for coal preparation plants, Reference Hethod 9 (the opacity test method)
                                  1

-------
was revised in order to base determinations of compliance with
opacity standards on the average of 24 consecutive observations,
each taken at 15-second intervals (six-minute average).  Accordingly,
EPA reevaluated the opacity standards for coal preparation plants and
revised them to be consistent .vith the changes in Method 9.  This
document contains a discussion of the changes in the opacity
standards that resulted from the revaluation (Section III).

-------
II.  Mass Emission Standard for Thermal Dryers
     The mass emission standard for participate matter from thermal
dryers is based on test data and predictions using impaction theory.
The test data include data developed by EPA test programs (described  in
Volumes 1 and 2 of the background document), data submitted in one
of the public comments (discussed below),  'Ua obtained from tests of a
plant processing Sewell Seam coal (discussed below), and data developed
by a major scrubber manufacturer from extensive control equipment
                 2
acceptance tests.
     The impaction theory for venturi scrubbers is a useful tool
that predicts the impact of parameters that affect venturi scrubber
control efficiency.  For example, it is known that both the energy of
impaction of water droplets with the particles and the size of the
particles are of primary importance.  It is also known that increasing
the pressure loss through the control device increases the energy of
impaction.  With all other factors being equal, this will lower the
emissions.  At pressure drops required for control of particulate
emissions to the limits of the mass emission standard, it is also known
that very fine (<1.5 micron) particles are less efficiently collected
than larger particles.
     In order to predict the actual effect of these parameters
mentioned above upon control equipment performance, it is necessary
to consider the extreme effects that have been observed.  This has
been accomplished by bracketing in Figure 1 the coal preparation plant
                                  7 8
emission data currently available. '   These tests, some of which are
described in Volumes 1 and 2 of the background document, show the range
of emissions that can be expected depending upon the plant operating

-------
     6D
     55
     50
     45
     40
     35
     30
     20
cc
a
UJ
EC
a.
10
                            1I     !     MINIM
              O- FACILITY J. APPENDIX 8
              A   FACILITY K.APPtNOIXB
              Q-- WESTMORELAND COAL COMPANY
              ••- Ci, BACKGROUND INFORMATION DOCUMENT. VOL. II
              •-- Cz. BACKGROUND INFORMATION DOCUMENT, VOL. II
              A- 0|. BACKGROUND INFORMATION DOCUMENT, VOL. II
              V-  °2. BACKGROUND INFORMATION DOCUMENT. VOL. II
              V   03, BACKGROUND INFORMATION DOCUMENT, VOL. II
              0- - EL BACKGROUND INFORMATION DOCUMENT, VOL. II
              Q   E£. BACKGROUND INFORMATION DOCUMENT, VOL. It
      0.01         0.015     0.02   0.025  0.03      0.04    0.05   0.06  0.07
                                 EMISSIONS, grains/dsct
              Figure 1.  Paniculate matter emissions from thermal dryers.

-------
conditions  or processing parameters.  The high ranges of the
data predict  the maximum expected effect of these parameters upon currently
constructed and operated commercial size thermal dryer emission control
equipment.  The slopes of these lines show the effect of venturi scrubber
pressure  loss upon emission control performance.  The upper line shows
the maximum effect of all other known parameters upon control equipment
performance.  Based upon the control of liquid to gas (2/6) ratios that
are part  of any venturi scrubber design, the primary parameter remaining
(predicted by impaction theory) that may vary from plant-to-plant or
i.n"thin a  plant that may affect control efficiency is particle size.  The
upper line is the maximum expected effect of larger proportions of very
fine particles, in the dryer effluent particulate matter and the lower
line is representative of considerably smaller proportions.  An owner
or operator proposing to construct a new thermal dryer must consider in
advance the size of material being dried when selecting the pressure
drop needed to control emissions within the standards promulgated herein.
     One  commentator presented data and calculations which proposed
to show that  the coal processed by his company contained an unusually
large proportion of very fine particles that would preclude attainment
of the emission standards at reasonable pressure drops.   These projections
suggested that pressure drops of 50-52 inches of water gauge would
be required to control thermal dryer participate emissions processing
this type of  coal.  Since this projection is considerably greater
than the  25-35 inches projected in Volume 1 of the background information
document, EPA decided to perform emission tests at the plant which
D'-ccessed tne coal (Sewell seam) in question.  The results of the EPA

-------
tests are shown in Table  I.  The average of all five tests of particulate
emission from the thermal drying of Sewell deep mined coal was 0.047
gr/dscf, and the pressure loss through the venturi scrubber during these
tests v/as 29 inches water gauge.  As shown by Figure 1, these results
fall near the upper lino projected for facilities that have high proportions
of very fine participate.   It is recognized among many coal producing
companies and control equipment manufacturers that certain coals  or mining
techniques may produce higher projections of fine particles.
     Figure 1 encompasses all known extremes of particular size
and other vari ,bles that could significantly affect control equipment
performance.  Examination of Figure 1 shows that the mass emission
standard is achievable v;ith a pressure drop of 20 to 40 inches for a
wide spectrum of coal types and processing techniques.  The proportion
of coal containing these very fine particles that is processed by a
thermal dryer is within the control of the plant operator.  These fine
particles are separated from the remainder of the coal processed in the
coal preparation plant and  are concentrated in the froth flotation
cells.  The product coal from froth flotation-vacuum filtration circuits
is commonly referred  to as  "filter cake,"  Depending upon the amount of
moisture removal desired, to produce the final clean coal product,
common oractice within the  industry is to dry none, part, or all of the
"filter cake" material.  EPA test data indicate that emissions from
plants drying a fraction of the "filter cake" (Plant C) are near the lower
(Figure 1), while emissions from plants drying all of the "filter cake"
(Plant 05 are nearer  the higher line.  The same tyoe co^1. (Pocahontas)
was being processed at each plant.  These results (C-,, C9 and D3) are
contained in volume 2 of  the background information document.  In addition to

-------
                                Table I
Date
of Test
6-18-75
6-19-75
6-20-75
6-23-75
6-25-75
Test or
Run Number
1
2
3
4
5
gr/dscf
0.038
0.055*
0.033
0.059**
0.035
gm/dscm
0.086
0.125*
0.085
0.132**
0.079
Type
Coal
Sewel 1
Sewell
Sewel 1
Sewel 1
Sewell
Predominant
Mining Method
strip
deep
deep
deep
deep
*Filter was discovered to be broken after test was  completed.

**Probe was discovered to be broken after test was  completed;  however,
  microscopic examination of the filter showed no deposition of glass
  particles.

-------
the test results shown in volume 2 at Plant D where all "filter cake"
is typically dryed (test D-), an additional run was performed at the
plant after EPA requested that the amount of filter cake charged to the
dryer be reduced by 50 percent.  The emission test result of this run
was 0.013 gr/dscf.   At 32 inches pressure drop, this run is near the
lower line shown in Figure 1, whereas the emission results for test Do
when all filter cake was being dryed was nearer the upper line {0.024 average).
Thus, reducing proportion of "filter cake" dried by 50* may have made
the venturi scrubber's control of emissions substantially more efficient.
     The question of drying none, part or all of the filter cake
material is a matter of balancing economic considerations, product
specifications, and desired emission control.  Even if all filter cake
and emissions are nearer the upper line, Fig-jre 1 indicates that the
pressure loss needed to attain the promulgated standard of 0.031 gr/dscf
will be 40-45 inches for the most extreme circumstances.  This projection
has been confirmed by data developed by a major scrubber manufacturer
                                       4
from extensive control equipment tests.   Pressure drops of this magnitude
and greater are technically feasible.  The economic aspects of this
reevaluation are discussed in Sections IV and V.

-------
Ill,  Opacity Standards
     The proposed standards included opacity levels for emissions from
thermal dryers, pneumatic coal cleaning equipment, and coal handling and
storage equipment.  The proposed standards were based on data obtained
in accordance with the original Reference Method 9 (the opacity test
method).  The original Reference Method 9, which was promulgated in
1971, required that compliance with opacity standards be determined
on the basis of peak observations.  In response to complaints that the
errors associated with any single observation of visible emissions
were great, studies were conducted to determine the magnitude of
errors which can be made by qualified observers while reading plumes
according to the prescribed procedures.   It was shown that opacity
can be determined with a positive error less than 7.5 percent by
averaging 24 consecutive readings (six-minute average),  Reference
Method 9 was revised accordingly and published in the FEDERAL REGISTER
on November 12, 1974 (39 PR 39872).  The  new procedure requires that
opacity observations be recorded to the nearest five percent at 15-second
intervals.  A minimum of 24 observations  must be recorded, each recorded
observation representing the opacity of emissions for the 15-second interval,
to obtain a six-minute average.  The use  of sets of opacity data precludes
a single high reading from being cited as a violation.
     These revisions to Method 9, however, made it necessary to reevaluate
previously promulgated and proposed opacity standards, since they were
based uoon data obtained with the old Reference Method 9.  Thus, the
data base for the opacity standards for coal preparation plants was
recorr..ted into 6-minute averages.  The results are shown in Table II.

-------
                          Table
Type of Range of Proposed Range of
Facility Single Standards 6-Minute
Observations Averages
(«) (*) («)
Pneumatic Coal 0-10 20 0-6
Cleaning Equipment
Thermal Dryers 0-10 30 0-5
Fugitive Emissions 0-50 20 0-]9
Promulgated
Standards
(%)
10
20
20
*The appendix contains the six-ninute opacity averages from which this
 table was procuced.
The ranges of the average observed data are significantly lower and
much more constant than single observations of plume opacity.  Since
the opacity standards must be consistent with the method used to enforce
the standards, the proposed standards for thermal dryers and pneumatic
coal-cleaning equipment were revised to lower levels consistent with the
averaging technique.  Consistent with EPA's policy on use of opacity
standards in conjunction with mass or concentration standards {see 39 ^R
9308, March 8, 1974), the revised opacity standards for these affected
facilities are less stringent than the applicable mass standards.
     Upon comparison of observed thermal dryer opacities and the
thermal dryer opacity standard, a larger difference is found than
for similar comparisons with the remaining sco.'."!.-~u's.  Due to the
nature of thermal dryer emissions, observations are not usually made
at the stack exit.  Emissions from thermal dryers are typically
controlled by venturi scrubbers which oroduce a combination of
condensed water vapor and particulate matter in the stack effluent.

-------
This water vapor or steam plume is often at least 100 feet In length and
in some instances it reaches 300 feet (or more) in length.  Since EPA
procedures under Method 9 indicate that opacity cannot be read until the
steam plume has evaporated, opacity is read at the end of the steam
plume where the particulate matter is considerably dispersed.  Under
conditions of cool ambient temperature and high humidity, opacity
readings are lower at the point of observation (after dissipation of the
steam) than they would be if they could be observed at the point of
emission.  When weather conditions are conducive to shorter plumes (warm
temperatures and/or low humidity), there is less dilution and the observed
opacity of emissions is higher.  The data which support the opacity
standard for thermal dryers were obtained under conditions conducive to
the formation of relatively long steam plumes.  Under drier and warmer
conditions the observed range of 0-5% opacity for thermal dryers would
have been higher due to the ability to observe the plume nearer the
point of emission.  Thus, the standard for thermal dryers is established
at a level higher than would otherwise be the case in order to account
for this phenomenon.  Since emissions from pneumatic coal cleaning
equipment contain no condensed moisture, the level of the standard is
lower than for thermal dryers, even though the observed opacity was
about the same for both processes.
     For fugitive emission sources, the opacity standard was established
near the maximum six-minute average observed since no mass standards
apply to those facilities.  In such cases the opacity standard is the
                                11

-------
only means of requiring control of the emission sources and is established
at a level consistent with application of best control technology to
those sources.
     As illustrated by Table II, two of the promulgated opacity standards
are numerically lower than those proposed.  In relationship to the
respective data bases {peak observations versus six-.ninute averages),
however, the promulgated opacity standards represent no increase in the
stringency of the opacity standards.  For participate emissions, the
promulgated opacity standards and the new Method 9 jix-minute averaging
concept more accurately represent the level of control achievable tlian
did the proposed opacity standards and the former Method 9,
                               12

-------
IV.  Economic Impact
     As explained in Section II of this report, the mass emission
standard for thermal dryers was reevaluated in view of data and calculations
submitted by one commentator.  The reevaluation indicated that the proposed
standard can be achieved at a venturi pressure drop of approximately
40 to 45 inches water gauge even under the most extreme circumstances
expected to occur.
     Because the original cost analysis of the standard was based on a
venturi scrubber operating at 25 to 35 inches venturi pressure drop,
the cost of operating at higher pressure losses was evaluated.  Also, the
cost analysis was updated to March 1975 with inflation indices.  The analysis
indicated that the added cost of controlling pollutants even at a pressure
drop of 50 inches would be less than 14 cents per ton of plant product
(see Table III).  This would be only five cents per ton in excess of the
cost resulting from the average control level required by State regulations
in the major coal producing States.  Whfle this is more than the two
cents per ton excess cited in Volume I of the background document, it
constitutes a small percentage of the total delivered cost of coal
estimated by the Bureau of Mines for 1974 ($18.95 average delivered cost
per ton).  Even the total impact of 14 cent'., per ton for controlling
particulate matter emissions can easily be passed along to the customer
since the demand for thermal drying dut to freight rate savings, the
elimination of handling problems due to freezing, and the needs of the
customer's process (coke ovens must control bulk density and power plants
must control plugging of pulverizers) will remain unaffected by these
regulations.  Thus, the economic impact of the standard upon the growth
                               13

-------
                             Table III - Control  Costs for Coal Cleaning
                              Wet Scrubbing for a 465 TPH Thermal Dryer
                                       (March 1975 Dollars)

Plant Sire, Run of Mine, TPY                   3,500,000
Uryer Capacity, TPH*                             465
Dryer Feed, TPH                                  349
Dryer Investment (965)(1.338), $               1,291,000
Operating Hours/Year                             3840

Design Pressure Drop2                             50" H20            35" H20             30" H20

Control Investment5                          $435,000               $400,000            $381,000

Annual!zed Cost

 Labor 140 Hr/Yr @ S7.506                      1,050                1,050               1,050
 Maintenance 0 3%5                            13,050               12,000              11,430
 Electrical Power
  3000 HP 0 34/KWH (0.75)                    175,240
  2000 HP 9 3c'KWH (0.75)                                         137,370
  1700,HP 0 3C/KWH (0.75)                                                              99,300
 Water                                         8,240                8,240               8,240
 Property Tax and Insurance P 2% Inv           8,700                8,000               7,620
 Capital Recovery Factor                      64,830               59,610              56,780
  10 yrs 
-------
of thermal drying operations is not expected to be large,  and  the



inflationary impact of the standard on the price of coal will  be



insignificant (one percent or less).

-------
V.  Inflationary and Energy Impacts



     In accordance with the Agency's interim guidelines concerning



inflationary impact statements, the five-year annualized costs have



been computed for coal preparation plants.  The five-year costs and



the fifth year annualized cost of implementation of the standards



have been estimated as $18 million and $11 million, respectively.  Both



of these costs are well below the screening criteria ($100 million ind



$50 million) for preparation of inflationary impact statements, indicating



a minor impact.



     The increased power consumption resulting from the standards was



assessed and is simmarized in Table IV.  Although there is a 24% increase



in power requirement by the control system, relative to the energy



consumption of the facility for producing product coal, the standards



of performance will result in a negligille increase in power consumption



for pollution control by coal preparation plant facilities.

-------
                               Table IV
                       Annual Power Consumption
            Increases Required by Standards of Performance
                       for Coal Cleaning Plants5

Expected Average        Total Increase in Demand        Incremental Increase
Annual Growth in        Due to Standard of              in Power Oemand Due
New and Modified        Performance Compared to         to Standards of
Facilities              No Afr Pollution Control,       Performance Beyond
(Capacity Per           KWH/YR                          Requirements of
Facility                                                Typical State
                                                        Implementation Plan,
                                                        KWH/YR
    9 Dryers                 53 x Id6                      32 x 106
                              17

-------
                              References

1.  Scrubber Handbook, Volume 1, Contract CPA-70-95, A.P.T.,  Inc,
    Riverside, California.

2.  Letter, D. W. Fritz, Flex-Kleen to C. B.  Sedman, EPA, May 20, 1974.

3.  Coal Preparation Plant Emission Tests, Test No.  73-CCL-2  Island
    Creek Coal Company, Scott Research Laboratories, Plumsteadville,
    Pennsylvania.

4.  Letter, 0. K. Werle, Flex-Kleen to L. G.  Jones,  EPA, July 8, 1975.

5.  Letter, J. A. Notary, Heyl 8 Patterson to L.  G.  Jones, EPA.
    April 25, 1972.

6.  1GCI, "Air Pollution Control Technology and Cos  ;s in Nine Selected
    Areas," Seotember 30, 1972.

7.  Oneida Heat Dryer Stack Test, Oneida Mining Company, Contract
    614-299-9229, Tra Det Laboratories, Inc., June 20, 1975.

8.  Letter, Carl E, Dillion, Barnes & Tucker  Company to L. G. Jones,
    EPA, November 25, 1975.
                                18

-------
VI.  Surtmary of Public Coranents and EPA Responses
     Twenty-seven comnent letters were received on the proposed
standards, six from coal companies, four from Federal agencies, four
from steel companies, four from electric utility companies, three
from State and local agencies, three from coal industry associations
and three from other interested parties.  The comments were carefully
considered and, where determined by the Administrator to be appropriate,
changes were made to the proposed regulations.
     A surunary of these comments ar«1 EPA's responses is presented in
this section.

-------
                     Key to Industry Code







                               Industry or Organization
 A            State or Local  Air Pollution Control  Agency



 B            U.  S. Environmental Protection Agency



 C            Federal Governmental  Agencies other than EPA



 D            Coal Companies



 £            Coal Company Equipment Vendors



 F            Coal Industry Associations



,G            Iteel Companies



 H            Electric Utility Companies



 I            Chemical Companies

-------
                              LIST OF COMMENTATORS
Commentator
Number
Commentator
          Affiliation
IA-1
IA-2
IA-3
Y-l
Y-2
Y-3
Y-4
Y-5
Y-6
Y-7
Y-8
Y-9
Y-10
Y-ll
Y-12
Y-13
Y-14
Y-15
Y-16
Y-17
Y-18
Y-19
Y-20
Eric Zausner
Stanley Ooremus
William C. Rountree
J. N. Shuoe
Philip C. Reeves
George Palmer
George P. Ferreri
J. C. Anderson
0. R. Thorpe
Don Willis
David H, Anderson
J. N. Shupe
Richard W. Bliss
0. R. Sheets
Joseph H. Mullan
Milliam R. Meyer
J. R. Brough
G. L. Barthauer
J. P. HcCluskey
Howard R. Palmer
J. LeRoy Balzer
Richard H. Silverman
Robert L. Duprey
Federal Energy Administration
United States Department of the Interior
General Counsel of the Department of Commerce
Westmoreland Coal Company
Roberts & Schaefer Company
Olin Chemicals
Environmental Health Administration
United States Steel Corporation
GPU Service Corporation
National Mines Corporation
Bethlehem Steel Corporation
Westmoreland Coal Company
American Mining Congress
Kerr-HcGee Coal Corporation
National Coal Association
Virginia Air Pollution Control Board
Inland Steel Comnany
Consolidation Coal Company
Commonwealth Edison
The Dayton Power and Light Company
Utah International, Inc.
Salt River Project
EPA-Oivision of Stationary Source Enforcement
                                             21

-------
                                         Public Comment Summary:  Coal Preparation Plants
Comment
Number
      Commentator
         Number
Category
Comment
Response
tss
    2
             IA-1
Y-22
              IA-2,  Y-2Z
                         C,C
                                  Conventional coal  cleaning pro-
                                  cesses used in conjunction with
                                  flue-gas desulfurization units
                                  should be included within the
                                  standards.  The standards for
                                  coal preparation plants should
                                  also be revised to Include
                                  cleaning of coal by solvent re-
                                  fining processes.
                                           The specific coal processing operations
                                           regulated by these standards are affect*!
                                           regardless of whether they are located in
                                           coal liquefaction plants, power plants,
                                           coke ovens, etc.  Such operations have been ,
                                           in use for many years and may be regarded   ;
                                           as "conventional.  They have been identified I
                                           by the Administrator as being a source of
                                           emissions that may contribute signlficant.ly,
                                           "to air pollution that causes or contributes
                                           to the endangerment of public health or
                                           welfare.  Newer operations  for producing
                                           clean fuels from coal  (e.g. coal liquefac-
                                           tion, coal gasification, etc.) have r.ot
                                           currently been so  identified by tne
                                           Administrator and  are  not affected by
                                           these standards.
           If environmental  -impacts  are  not
           considered with  regulations the}
           should be cross  referenced to
           other applicable regulations.
           The title for subpart Y should
           be revised to include the desig
           ,iation "new or modified" and
           these terms should be defined
           within the subpart to avoid
           misunderstanding.
                    The environmental  effects of the proposed
                    regulations were considered in volume 1
                    of the background  document.  Other  	•,
                   applicable regulations are a matter of public
                    record.

                    The requirements in Subpart Y affact all   •
                    new coal  preparation plants, but may cr
                    may not affect facilities which undergo
                    physical  changes.   The question of what
                    constitutes a modification is being
                    addressed in proposed amendements to the
                    general provisions (Subpart A] of 40 CFR
                    Part 60.   See 39 FR 36946  (October 15» 1974-)

-------
Comment
Number
Commentator
   Number
Category
Comment
Response
            IA-2
            IA-2
ro
40
             IA-3,  Y-1Q, Y-2, Y-5,
             Y-12
                 C, F, E,
                  G
                             The economic justification for
                             standards  is unrealistic due to
                             the abnormally  large model     »
                             plants  used in  the analyses.
                            The data  in Figure 10 of the
                            Background Information document
                            show" that the West Virginia  Stats
                            standard  applicable to thermal
                            dryers is 0.10 gr/dscf rather
                            than the  0.07 gr/dscf used in th
                            economic  analyses.  Therefore,
                            the incremental costs of control
                            are inaccurate.
          Opacity is unsuitable as a
           standard and should only be
          used as a triggering device
          for performance testing.  Opacit
          standards are unreliable for
          use as an objective means of
          evaluating emissions.
                    The  largest  economic  impacts  are  incurred
                   when  control  of emissions from thirmal
                    dryers  is  required.   Since thermal  dryers
                    are  used only in the  larger,  more sophis-
                    ticated operations, smaller plants will
                    typically not be subjected to this
                    economic impact.  The economic impact on a  .
                   small plant will be attributable to thf
                    necessity for controlling fugitive
                    emissions.

                    TheO.07 gr/dscf used  in the economic
                    analyses is  not intended to directly
                    represent the standard for any single state.
                    Although the background document did
                    reference the West Virginia standard, the    i
                    0.07 ar/dscf emission level selected re-
                    presents a weighted averege of the standard;
                    for  the major coal producing states where
                    the  emission standards may be higher or
                    lower  (e.g. 0,02 gr/dscf in Pennsylvania).

                   The use of opacity standards has previously
                   been considered  in the EPA  response to the
                   remand  ordered fay the U.S.  Court of Appeals
                   for the District of Columbia Circuit in
                   Portland Cement Associationy Ruckelshaus,
                   486F.2d 375  (D.  CV Cir. 1973).Copies
                   of the  remand may be obtained by writing to
                   Emission Standards and Engineering Division,
                   Environmental  Protection Agency, Research
                   Triangle Park,  North Carolina 27711, Attn:
                   Mr- Don R. Goodwin.  On November 12, 1974,
                   EPA revised  its  reference  method for deter-
                   mining  opacity (Method 9  in Appendix A of
                   40 CFR  Part  60)  in several  respects  (39
                   FR 398  72).   Among other  things, the  re-
                   vision  made  clear  that the accuracy of the
                   method  must  be taken

-------
Comment
Number
Commentator
   Number
Category
Comment
Response
             IA-3
IS}
            Y-l
                             In  the  absence  of continuous
                             monitors, violations of  the
                             participate  standard cannot be
                             proved  without  performance tests
                             therefore the particulate stan-
                             dard  should  apply only during
                             performance  testing.
                            Scrubber manufacturers will not
                            guarantee meeting  a 0.03 gr/dscf
                            (0.07  g/dscm)  particulate stan-
                            dard for Sewell Seam and other
                                           into account for purposes of enforcement.
                                           On May  Z2,  1975 the U.S. Court of Appeals
                                           for the District of Columbia Circuit
                                           affirmed  EPA's position with respect to
                                           opacity and held that  plume opacity may be
                                           used "either as a measure of pollution or
                                           as an aid in controlling emissions1,1.
                                           Portland  Cement Association v Trairu_
                                           SI3 F.2d  $06,508-0d (D.C. Cir. 1975).

                                           Section 60.1 Ha) of the general  provisions
                                           (applicable to all subparts of 40 CFR
                                           Part 60)  provides that compliance with
                                           mass or concentration  standards  specified
                                           in Part 60 shall be determined only by   •
                                           performance tests.  In practical effect,
                                           this means that the particulate  standards
                                           for coal  preparation plants apply only
                                           during  initial and subsequent performance
                                           testing,  Section 60.11(e), however,re-
                                           quires  proper maintenance and operation
                                           of affected facilities and associated
                                           control equipment at all times,  and
                                           continuous monitoring  requirements^and
                                           opacity standards have been  included in
                                           Subpart Y as a means of  assuring proper
                                           maintenance and operation.   It should be
                                           noted  that the proper  maintenance and
                                           operation requirement  and the opacity
                                           standards are  independently  enforceable,
                                           and that  ,,the.v, apply at all times except
                                            as orovided in §60,11(c).

                                           As discussed in Section  II of this
                                           supplement  to the background document, EPA
                                           conducted emission tests at a plant pro-
                                           cessing Sewell Seam coal as a result of

-------
Comment
Number
        Commentator
           Number
Category
             Cooent
             Response
            Y-l
rv
tn
  10
 Y-l
  11
Y-l, Y-9, Y-14
 D,D,G
                                               similar  coals.   One manufacturer
                                               contacted will  not in one  case
                                               guarantee below 0.04 gr/dscf
                                               (0.09  g/dscm).
                                    Power companies do not have the
                                    capability of supplying the larg
                                    power requirements needed to
                                    achieve the 0.03 gr/dscf stan-
                                    dard in areas where the coal '
                                    fields are located.
Some companies may not be able
to procure capital investment
for new facilities badly needed
to meet current energy needs
due to the uncertainty of
achieving a 0.03 gr/scf
standard.

The marginal improvement in
emission controls of a 0.03 gr/
scf standard versus a 0.05 gr/
scf standard is not justified
due to the  increased costs,
energy consumption, and  re-
                                           this  commentator's  assertions.   In  view of
                                           the data obtained in these tests,  the
                                           scrubber manufacturer in  question  has
                                           indicate'., it will guarantee 0.07 g/dscm
                                           (0.03 gr/dscf}  for  Sewell  and other
                                           similar  coals (Reference #3).

                                           Public utility  companies  are typically
                                           ! obligated by law to provide adequate  ser-
                                           vice  in return  for a franchise to  operate
                                           a monopoly in assigned service areas.
                                           This  obligation extends to new as  well as
                                           existing customers.  There may be  some
                                           practical reasons (e.g. financing, time
                                           needed  for new  construction, etc.) why
                                           service cannot  be extended immediately
                                           upon request, but these factors must be
                                           weighed by the  owner or operator of a  coal
                                           preparation plant along with the multitude
                                           of other considerations in planning the
                                           location and design of a new facility.

                                           The  scrubber manufacturer's guarantee
                                           and  technical support should provide the
                                           assurance needed to attract capital in-
                                           vestment .
As discussed in Section IV of this supple-
ment to the background document, EPA's
analysis indicates that the economic impact
of an 0.03 gr/dscf (0.07 g/dscm) standard
would be only 5 cents per ton of coal in
excess of the average control required by

-------
Comment
Number
      Commentator
         Number
Ca I'egory
              Comment
             Response
  12
Y-l, Y-9
ro
en
 D,D
                                               suiting pollutants generated by
                                               the power company.
The technical data used to
justify the 0.03 gr/scf standard
is in error.  Pocahontas Seam
coal is not the ("ost difficult
to control.  There is no consis-
tent connection between friabil-
ity and control difficulty.
Sewcll Seam and other coals not
tested by EPA are much more
difficult to control.  The
error of this premise regarding
Pocahontas coal has been
verified by  vendors of thermal
dryers and venturi scrubber
equipment.   Pocahontas cos! was
found to be  among the easiest
coals to control.
   EPA has  no iata to show  that
the 0.03 gr/cscf  standard  is
achievable  when  coal bther than
Pocahontas  Seam  coal  is dried.
state standards, even if a 50 inch pressure
drop were necessary to meet the standard.
This is less than the cost savings attri-
butable l:o coal drying and is almost
inconsequential when compared to the sale
price of coal  (10 to 20 dollars per ton).
Although the energy requirement will
increase by about"24 percent, the net re-
duction in emissions to the atmosphere
will be about  23 percent even with
consideration  given to the increase in
emissions at a  new coal-fired power plant
 (Reference  #3).

As discussed in Volume 1 of the background
document, Pocahontas coal has historically
been considered to present the most diffi-
cult situation with respect to emission
controls.  Recent test data developed by
EPA by tests at the commentator's facility
have demonstrated that Sewell coal  is
equally, but no more, difficult to  control
than Pocahontas,  (See Section  II of this
supplement  to  the background document).
By  no means  is Pocahontas  coal  considered
among  the easiest to control.   No data
have been developed  to date  that would
indicate that  there  are more  difficult
control  problems  than  are posed by
Pocahontas  or  Sew°ll  coals.
  As discussed in Sections II  and  IV  of this
supplement  to  the background document,  EPA's
test data  (including that obtained  at the
commentator's  plant) indicate  that,  thp  0.03
gr/dscf standard is  achievable at reasona- I
ble cost with  Sewell  Seam or Pocahontas    |
coaIs.                                      ;

-------
Comment
Number
      Commentator
         Number
Category
Comment
Response
            Y-1
  14
Y-1
             Y-1,  Y-9
                           0,  D
                                  No sieve analysis results of the
                                  feed to thermal dryers tested
                                  by EPA are available.  Conse-
                                  quently, there are no data to
                                  show the achievability of an
                                  0.03 gr/scf limit for coal feeds
                                  with high fines content.
          We have installed and operated
          a venturi scrubber of the type
          identified by EPA's tests as
          examples of best control tech-
          nology at a location where
          Sewell Seam coal is mined and
          thermally dried.  Test results
          have averaged 0.04 gr/scf, above
          the 0.03 gr/scf limit proposed
          by EPA.

          Without relief from the 0.03
          gr/scf limit proposed, coal
          companies will not be able to
          recover the finar sizes of coal
          due to the  inability to thermal!
          dry.  Discarding this coal (as
                    The EPA test measurements were conducted
                    in a manner that would detect significant
                    differences in emissions due to high fines
                    content in the dryer feed.  Tests at dryers
                    D, and at the commentator's facility
                    were conducted with maximum input of fines
                    to the dryer.  Tests at dryer C were con-
                    ducted with only partial input of fines.
                    The emission standard is principally based
                    upon the former tests and other recently
                    developed data (see Section II of this
                    supplement to the background document)
                    rather than the lower results obtained at
                    dryer C.  The standard therefore reflects
                    any effect upon control equipment
                    efficiency due to high fines content in the
                    dryer feed.                                I

                    For the 29 inch scrubber pressure drop
                    used at this facility, these results
                    (0.04 gr/dscf) are consistent with EPA
                    data which show that the standard will be
                    achieved by operating the scrubber in the
                    40 to 45 inch water gage pressure drop
                    range.  See Section II of this supplement
                    to the background document.
                     EPA's  tests  included  facilities  where all
                     fines  produced are dried.   EPA projects
                     that facilities drying certain difficult
                     to control  coals can  achieve the 0.031 gr/
                     dscf limit by using venturi scrubber con-

-------
Comment
Number
         Commentator
            Number
 Category
              Comment
             Response
  16
00 17
Y-l, Y-10, Y-12, Y-15
Y-2
D.F.F.D
                                               much as 15 tons per hour in a
                                               typical plant) is an unjustified
                                               waste of national resources.
No data are available to evalu-
ate the degree of control
achievable with western coals.
Extension of the termal dryer
standard to these coals is with-
out foundation.

The use of diluent gases to
achieve the emission standards
should not be permitted.
Revision of §60,12 is needed to
be consistent witn the exclu-
sion of this requirement pro-
vided in the subpart.  The
purpose of this exclusion needs
explanation.
trol  equipment  that  is operated  at a
pressure  loss of  40-45 inches water gage,
(See  Section  II of this  supplement to the
background document).  Lower pressure
losses will give  satisfactory results with
many  other type coals.   In either case,
thermal drying  and recovery of fines will
not be precluded.

Because the drying characteristics and the
emission  control  levels  achievable with
subbitunrinous and lignite coals  typically
found in  the west are not currently known,
the thermal  dryer standard has been revised
to apply  only to  drying  of bituminous *uels

Section 60.254  (c) as proposed was based on
the need  for  thermal dryers to add diluent
gases for temperature control.   The
possibility that  addition of  diluent gases
will  be used  to evade the standard is un-
likely  in view  of the high operating and
capital cost  that would  be  incurred in
doing so.  However,  this paragraph has
been  deleted  from the regulations  because
it  is redundant.  Section 60.12  prohibits
use of  dilution air  only when its  purpose
is  to defeat  emission standards.  Dilution
air  for legitimate process  needs is not
prohibited.

-------
Comment
Number
      Commentator
         Number
Category
Cor.ii-cnt
                                                                                            Response
             Y-2, Y-l
  19
Y-3
20


21
             Y-22


             Y-4
  22
Y-4
                        E,D
                        C


                        A
          Coal preparation plants are not
          a significant water pollution
          hazard.  New plants use closed
          circuit systems.
          Plants with capacities of 1000
          tons/day or smaller should be
          exempted from the regulations.
          Proposed standards appear to be
          attainable.

          More explanation is needed with
          regard to procedures acceptable
          for satisfying the requirements
          of §60.254(d) when baghouses are
          used.

          The revisions to Method 9 were
          not proposed, therefore, pro-
          viding no opportunity for input
          from State agencies.
                    New coal preparation plants are expected
                    to use closed fluid systems and thereby
                    present no significant water hazard.
                    This is true, however, only if plant is
                    well designed to handle waste water and
                    overflows.

                    The intent of the proposed standards was
                    to control coal preparation of significance
                    with respect to emissions.  Therefore,
                    EPA has exempted coal preparation plants
                    processing 200 tons/day or less coal from
                    compliance with these standards.

                    The standards have been fully evaluated
                    by EPA and are attainable.                 ;

                    Baghouses must have a ducting arrangement
                    in order that Reference Method 5 may be
                    applied.
                    Certain revisions to Method 9 were pro-
                    posed on September 11, 1974 (39 FR 32852).
                    After consideration of comments, these
                    revisions were promulgated on Novsin'-er 12,
                    1974 (39 FR 39872), together wit'i certain
                    other revisions determined to be appro-
                    priate on the basis of EPA's response to
                    the remand in Portland Cement Association
                    y: Ruckelsnaus^ 486F.2d  375 (D.C. Cir.
                    1973)"  Conuients were invited on the

-------
Comment
Number
       Commentator
          Number
Category
             Comment
             Response
  23
Y-5, Y-1'0,  Y-5a
  24
OJ
o
  25
Y-5, Y-10
Y-5, Y-7, Y-8, Y-5a,
     Y-23
            Y-5, Y-10
   27
Y-6
G. F,
 G
G, F
G, D,
G, G,
F
                         G, F
The definition for "surface
moisture" is inconsistent with
tfiat recognized by the industry
or ASTM.  The definition should
be revised in terms of an air
drying procedure for determina-
tions.

Product moisture content does
not relate to dryer emissions
in any consistent manner.

Product Moisture content is
usually sampled after recombin-
ing with other product from the
preparation plant.  Sampling of
product directly from the dry<=r
is not a usual practice.

Exhaust temperature of the
flue  gases is the best source
of information regarding the
performance of the dryer.
           An allowance for water vapor
           is necessary in the procedures
latter revisions on April 22, 1975
(40 FR 17778), and after consideration of
the comments received EPA concluded that
no further revision of Method 9 was
appropriate (40 FR 41834, September 9,
1975).

Since determining surface moisture, using
air drying or other techniques, is
cumbersome and does not seem justified
with regard to the monitoring benefit in
addition to application of the opacity
standard, this provision has been deleted
from the regulations.

See response to comment 23.
                                                                                See response  to  comment 23.
Flue gas exhaust  temperature  is  a  good
indication  of  normal  operating conditions
The temperature usually  does  not fluctuat
except  during  start-up,  shutdown,  and
malfunction conditions.

EPA believes a cross  reference is  un-
necessary  since the general  provisions

-------
Comment
Number
       Commentator
          Number
Category
             Comment
             Response
  28
Y-7
            Y-8, Y-23
  30
 Y-8
  31
 Y-8,  Y-16,  Y-19,  Y-23
                         G, F
6, H,
H, F
                                               for determining opacity of
                                               emissions.  Section 60.11(b)
                                               should be referenced by
                                               Section 60.252.
                                                                    specified  in  Subpart A apply  to  all other
                                                                    subparts of Part 60.
          Monitoring of a source's oper-   Monitoring is needed to assure proper
          actions is not needed since they(maintenance and operation of the facility
                                           and associated control equipment after
                                           the initial performance tests.  Without
                                           some means of monitoring, degradation in
                                           emission control performance between
                                           performance tests could easi y qo unde-
                                           tected.
                                               Q V* W ( W* I t* I ^ > I V »* t I*. !«•»•*- W w • r • w
                                               are required  to comply with
                                               applicable standards.
           Sampling of  coal  from  open
           storage piles will  not produce
           accurate moisture analyses.
           The  moisture of coal at the
           surface of the  pile will  be
           different  than  the  coal  moisture
           at the interior of  the pile.

           We interpret Method 9  to
           apply only to  stack emissions.
           Application  of  opacity to
           fugitive emissions  is  subjec-
           tive and impractical.
Fugitive emissions from coal
open storage piles are dependem
                                Control of open  storage  piles  is  not
                                required  by  these  regulations.  See
                                response  to  comment  31.
Method 9 applies to fugitive emissions as
well as stack emissions.  The applica-
bility of Method 9 to fugitive emissions
is discussed further in the "Reevaluation
of Standards of Performance for Asphalt
Concrete Plants", published on April 22,
1975 (40 FR 17778).  See also responses
to comnents 6 and 47.

Section 60.251 (h.) has been revised to make
clear that open storage piles are not

-------
Comment
Number
       Commentator
          Number
Category
              Comment
             Response
  32
Y-11, Y-18
CO
  33
  34
  35
Y-ll
Y-11
Y-12, Y-14, Y-15
  0,0
  F, G,
  D
upon so many variables; the
effects of which are not re-
flected in the 20 percent opaci-
ty limitation proposed.  Other
than water sorays, control
methods are not available to
prevent dusting on windy days.
Opacity standards should not be
applied to controlling emissions
from open storage piles.  We
suggest equipment standards to
require sprays and enclosures
for fugitive emission control.

These standards should be
confined to operations within
a coal preparation plant and
not extended to similar facili-
ties at other  locations.
 Hi-Vol  samplers  and  meteorolo-
gical stations should be used
in  lieu of monitoring require-
ments.

Daily sampling of dryer product
is  too frequent.

Applying opacity standards to
sources where emissions contain
large volumes of water is
unrealistic  and unenforceable.
                                                                               considered  "coal  storage  systems" for
                                                                               purposes  of these  regulations and are
                                                                               therefore not subject  to  the fugitive
                                                                               emission  standard.   It may be necefary
                                                                               to control  fugitive  emissions'from ^pen
                                                                               storage piles to  meet  State standards,
                                                                               however.
The intent of the coal preparation plant
regulations is not only to control emissions
from coal preparation plants but also to
control any coal processing and conveying
equipment, coal storage system, or roal
transfer and loading system which dis-
charges particulate emissions into the
atmosphere, regardless of its location.

•Hi-Vol samplers and meteorological stations
measure ambient air quality and, therefore,
are inadequate for the monitoring of control
practices at particular sources.

This requirement has been deleted from
these  regulations.

Through observations  it has been determined
that steam plumes can be distinguished from
particle emissions.   Special attention is
given  to steam plumes, attached and         ;

-------
Comment
Number
       Commentator
          Number
Category
              Comment
             Response
           Y-12, Y-15
  37
Y-12, Y-14, Y-15
 OJ
  38
Y-13
  39
Y-14, Y-18
                          F, D
F, G,
 0
G, D
           Opacity standards should not be
           applied to  coal handling equip-
           ment  because  such emissions are
           beyond the  control  capabilities
           of  the owner  or operator.
Section 60.253 regarding
monitoring requirements is poor-
ly conceived.  Other variables
not considered are important.
           The 0.03  gr/dscf standard  is
           achievable.   The 30 percent
           opacity limit for dryers seems
           too high  and inconsistent  with
           the proposed particulate
           standard.
The regulations should provide
exemptions for periods of
startups, shutdowns, and
malfunctions.
detached, in Method 9 as revised on
November 12, 1974 (39 FR 39872), to Insure
valid results for opacity readings.

As discussed in Volume 1 of the background
document, many types of particulate
emission control are available to the
owner or operator, thus no problem should
be encountered in complying with opacity
standards.

In addition to continuous monitoring of
pressure loss across the scrubber and
dryer gas stream temperature at the exit,
section 60.253 has been revised to include
the continuous monitoring of water flow
into the scrubber.

As discussed in Section III of this
supplement  to the background document, the
opacity standard for thermal dryers has
been revised to take into account recent
amendments  to Method 9.  EPA believes the
revised standard (20%)  is appropriate in
terms of the observed data base and the
purpose of  the standard.


Sections 60.8(e) and 60.11(c) of the general
provisions  applicable to all subparts of
40 CFR Part 60, as amended on October 15,
1973 (38 FR 28564), in effect provide

-------
Number
Commentator
   Number
Category
Comment
Response
40

^
f*

41


Y-14




Y-16, Y-17, Y-18


G




H, H
D
-
The t
flow
fcrmc
rt 1 1 1 Y*l
qui rt
strai
gas <
be 31
flow
incl
for
meth
The
lati
Powe
sere
Jryi
dryi
to t
ther
prop
                                              The  requirement that cyclonic
                                              flow be eliminated during per-
                                              formance  testing should be  re-
                                              quired unless  it can be demon-
                                              strated that the particles  in th<
                                              gas  stream  are large enough  to
                                              be stratified  due to cyclonic
                                              flow.   Provisions should be
                                               included  within  the  regulations
                                               for  approval of  alternate test
                                               The applicability of the regu-
                                               lation needs clarification.
                                               Power plants have coal  handling.
                                               screening, crushing and thermal
                                               Drying operations.  The thermal
                                               drying operation has no emission
                                               to the atmosphere and should
                                               therefore be excluded from the
                                               proposed standards.
                                                            exemptions whe»*e  emissions unavoidably
                                                            exceed applicable standards during  periods
                                                            of  start-up,  shutdown,  or malfunction.
                                                            It  should be  noted,  however,  that  §60.11(d^
                                                            requires proper maintenance and  operation
                                                            of  affected facilities  and associated con-
                                                            trol equipment during such periods.

                                                            Although only small  particles are  not
                                                            removed by a  venturi scrubber, EPA tests
                                                            have shown that the  particles in typical
                                                            stack effluent gases a  3 relatively large;
                                                            probably due  to agglomeration in the
                                                            saturated effluent environment.  If other
                                                            types of control  equipment are used that
                                                            do  not produce these unfavorable test
                                                            conditions, application for approval of
                                                            alternative methods can be made.  See
                                                            40  CFR 60.8  (b),  as revised  on March 8,
                                                            1974  (39 FR 9314).

                                                            When  the standard was  proposed it  was
                                                             thought  that  no  thermal dryers existed
                                                             other than "mine-mouth".  Through  several
                                                             comments it is now known that thermal
                                                             dryers do  exist  other than at mines and
                                                            •  that many are closed systems.  Although
                                                             the standards do apply to all facilities
                                                             regardless of location, they are not
                                                             applicable to systems that are entirely
                                                             closed so that there is r,o direct emission
                                                             to the atmosphere.

-------
 Comment
 Number
  42
        Commentator
           Number
Category
Comment
Response
 Y-16
  43
 Y-17
to
   44
Y-17
   45
Y-18
   46
Y-18
          State standards for control of
          fugitive emissions from open
          storage piles contain provisions
          that exempt the source during
          periods of adverse weather con-
          ditions.  Similar provisions are
          needed for these regulations.

          The monitoring requirements
          appear to be excessively costly
          in view of their minimal faene -
          fit.
          Continuous monitors are too
          expensive and are not adaptable
          to monitoring of fugitive
          emissions from coal handling
          equipment.

          Reference Method 9 should be
          cited  as the  procedure for
          determining opacity of emis-
          sions.
           An exemption of three  minutes
           TP)  hour should be added to
                   See response to comment 31
                   Under section 60,253 continuous monitoring
                   svstems are required only on thermal dryers.
                   EPA believes the monitoring requirements
                   are necessary in view of the potential for
                   large amounts of particulate emissions
                   should the dryer and the air pollution
                   coiitrol equipment not be properly operated.
                   As discussed in the preamble to the final
                   regulations, the cost of the monitoring
                   instruments is minor when compared to the
                   total costs of thermal dryers.

                   Continuous monitoring of fugitive emissions
                   from coal handling equipment is not
                   required.
                   Section  60.11{b)  of the  general  provisions
                   applicable  to  all  subparts  of 40 CFR
                   Part  60  specifies Method 9  as the procedure
                   for determining  opacity  of  visible
                   emissions.

                   In view  of  the revision  of  visible emission
                   observation procedures on November 12,  1974

-------
Comment
Number
       Commentator
          Number
Category
Comment
Response
  47
  48
  49
 Y-18
Y-21
Y-21
                                               opacity standards.
          The opacity standards should not
          apply when the opacity is  due to
          other sources.
          Baghouse controls used on small
          6 ton/hour thermal dryers can
          achieve compliance with a 0.02
          gr/dscf standard.
          Under some conditions, emissions
          as low as 0.005 gr/dscf are
          achievable using venturi
          scrubber controls.
                   (see 39  FR 39872), and the provisions  for
                   start-ups, shutdowns and malfunctions
                   promulgated on October 15, 1973 (see
                   38 FR 28B64), an exemption of three
                   minutes  per hour for opacity standards is
                   unnecessary.

                   According to Method 9 the observer's line
                   of sight should not include more than  one
                   plume (or source) at a time.  This applies
                   not only to sources fr->n» other processes
                   besides  coal preparation, but to sources
                   from other parts of the coal preparation
                   process.

                   Emission controls used on small pilot
                   scale and sand dryers have not been
                   demonstrated to be applicable to commer-
                   cial size coal dryers.  Although 0.02
                   gr/dscf is achievable at 35-40 inches water
                   gage pressure drop for several coals, it is
                   not universally achievable for all coals,
                   especially Pocahontas and Sewell types.

                   Considering  all technical and economic
                   factors,  0.03 gr/dscf is achievable at
                   reasonable costs with commercially sized
                   drying equipment.  Although lower emission
                   levels can always be achieved by exagger-
                   ated application of control techniques, the
                   extreme conditions needed are not practical
                   for commercial operations.

-------
Appendix A
          37

-------
Visible Emissions:  Six minute opacity averages
Plant:  Coal Dumping and Ship loading Operations
Plant Address:  Lambert's Point (Norfolk)» Virginia
Date;  March 26, 1975
Time:  8:30 a.m. - 11:30 a.m.:  Dumping Operations
       1:00 p.m. -  4:30 p.m.:  Ship Loading Operations
                                   %
Observers:  John Brown and John Davis
Type of Discharge:  Fugitive Emissions
Type of Control:  Water Sprays
Background;  Bl le Sky
Dumping Operations;
        J. Davis - north dumper
        J. Brovw - south dumper
                                38

-------
                                                                  Coal Dumping
                                                                  March 26, 1975
    Period                     Brown               Davis
(six irinuU averages)     (percent opacity)     (percent opacity)       Conments
                                                   0.2
                                                   0.0
                                                       *
                                                   4.2
                                                   2.5
                                                   1.7
1 -
2
3
4
5
6
7
8
9,
10
11
12
13
14
15
16
17
18
19
20
21
22
23
0
0
0
2.3
6.7
5.4
1.0
1.9
0.6
1.7
2.1
1.0
2.9
0.8
0.6
1.5
0.0
0.8
4.6
0.2
1.5
2.5
0.6
                                                   3.1
                                                                  process problems,
                                                              north dumper shut dr.

-------
                                                                   Coal  Dumping

                                                                   March 26, 1975
       Period                   Brown                Davis
(six minute averages)     (percent^ opacity)     (percent opacity)          Comnents
24
25
26
27
28
29
30
0.4
2.1
0.4
2.5
1.9
1.0
1.9

-------
                                                                     Ship Loading
                                                                     March 26, 1975
        Period                Brovm                 Davis
(six minute averages)     (percent opacity)    (fercent opacity)
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.2
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
uo
0.0
0.0
0.0
0.0
0.4
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
ao
ao
2.7
                                         41

-------
                                                                    Ship Loading
                                                                    March 26. 1975
        Period                 Brown                 Davis
(six minute averages)      (percent  opacity)      (percent opacity)
        24                      -                      -

        25                     0.0                  0,0


        26                     3'5

        27                     1'9

        28                     °'6

        29                     0.0

        30                     °-°
                                         42

-------
St^cU  -nth V-iln'.c^d lid
Hi";'.:   Cr-?l  !Jr--\->'.<.v-l-.on (air t, jle-3)

Co.TpaiV.'t  Florence IMning Company

Plert  ,-:-d-c-s>:   Se.:r»-a,  Pennsylvania

Date:   Jciurry  31, 1975

Ti-s:   10:-'.1  a.P. 1"  Il:f5 a.rr,.


Pb;-£-;;•::  Jclnt Y/,:.T- cr.ri <}. C.  I'.cCcrd

j,.,,., ^f -!.-.,•_  r _.  c:•«--.£«  -.,•>••=•.  •  "

Yyce or Co.urol:  C^cic..;

Stack  Difr.ster:  3,9  feet

L'£r''rrc,r'.*d;   ; cCcrJ -  C"*"^y sil---- ".-Si I '-"it;! *-0 f'Src.:
               Yfit^s  — black 5€?.2.c iv,; vntii n,J p.-rc
                                  ant clcud cov:
                                      cloud cov;
                43

-------
1
2
3
4
r
7
a
0
1 «J
1
2
3
4
r
5
6
7
3
9
i:-

0.0
o.o
0.0
0.0
0.0
0.0
0.0
o.c
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
o.c

B.S
5.0 1 ntinuitj
shutdo.;,;,
relay s.-itch
check
4.0
5.2
6.0
2.2
0.8
0.2
0.2
0.6
0.0
0.3
1.0
0.0
0.0
0.3
0.0
0.0
0.0
0.3 3 r;i!iyV
c'l'_ ,,f

-------
Visible Emissions:  Six Minute Opacity Average
Type of Plant:  Coal Preparation
Plant Address:  Vansant, Virginia
Date:  2/5/74 and 2/7/74
Observers:  Sedman and Meyer
Type of Discharge:  Stack and 3aghoc?se
Type of Control:  Scrubber Dryer, Baghouse, Rotoclone
Background:
   Dryer Scrubber
     9:37  -  sky, blue  with 0  percent  cloud cover
     11:00  -  sky, blue  with 60 percent cloud cover
     11:10  -  sky, blue  with 20 percent cloud cover
     11:30  -  sky, blue  with 30 percent cloud cover
     12:09  -  sky, blue  with 0  percent  cloud cover
      1:10  -  sky, blue  with 40 percent cloud cover
      1:35  -  sky, blue  vvith 60 percent cloud cover
      2:54  -  sky, blue  with 0  percent  cloud cover
   Coal Transfer Baghouse
     12:10  -  hillside,  brown with 40 percent cloud cover
     12:48  -  hillside,  brown with 0  percent cloud cover
      1:10  -  nillside,  bro,;n v:itii 4C ^ririt coud cover
                                     45

-------
Loadout Rotoclone Stack
  12:10 - hillside with 40 percent to 60 percent  cloud cover
  12:43 - hillside with 0 percent cloud cover
   1:14 - hillside with 40 percent to 60 percent  cloud cover
Rotary Breaker Baghouse
  side of building, gray metal with 100 percent cloud cover
                              46

-------
                                              Dryer Scrubber
                                              Stack Diameter - 7 ft,
                                              2/5/74


    Period                  Sed,!.an                Meyer
(6 min. average)       (percent opacity)      (percent opacity)     Comments
I
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
2.5
0.8
0.0
2.1
4,6
5.4
3.8
0.4
1,3
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
2.5
1.2
0.8
1,2
3,3
3.5
2.9
0,5
1.3
0.4
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
                                47

-------
                                             Dryer Scrubber
                                             Stack Diameter - 7 ft.
                                             2/5/74
    Period                  Sedman                 Meyer
(6 min. average)       (percent opacity)      (percent opacity)      Comments
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
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
2.1
0.4
10.0
-
20.9
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
C.O
0.0
0.0
0.0
0.0
0.0
0.0
2.5 production ci
0.4
10.0 shutdov.n - 4
break - 2 ho
21.9 start--,:; - ~

-------
                Coal  Transfer Baghouse
                Stack Diameter -2.5 ft.
                2/5/74
(6 rr.in. average)
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
(percent opacity)
0.0
3.6
0.0
0.0
4.6
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
, mytrj
(percent o
0.0
0.0
0.0
0.0
4.4
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

49

-------
                                               Load Out Rotoclone Stack
                                               Stack Diameter -  2.5 ft.
                                               2/5/74
    Period                  Sedman                Meyer
(6 min.  average)       (percent opacity)     (percent opacity)      Comments
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
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
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

-------
(6 min. average)
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
(percent opacity)
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
Rotary Breaker Baghouse
Duct Diameter - 1.8 ft.
2/7/74
     Meyer
(percent opacity)     Comments

       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

-------
Visible Emissions:  Six Minute Opacity Average
Type of Plant:  Coal Preparation
Company flame:   Island Creek
Plant Address:  Jewell Valley, Virginia
Date:  2/6/74
Observers:  Sedman and Meyer
Type of Discharge:  Stack
Type of Control:  Scrubber Dryer, Baghouse, Rotoclone Stack
Background:   Scrubber  Dryer  -  Sky,  gray with  100  percent cloud cover
              Coal Transfer Baghouse -  Hillside, brown with 100"percent
                                       cloud cover
              Coal Transfer Rotoclone Stack -  Sky, uray v/i th  100  percent
                                              cloud cover
                                  52

-------
    Period
. average)
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
(percent opacity)
35.00
35.00
35.00
0.2
8.3
0.0
0.0
0.0
4.6
0.0
0.0
0.0
17,1
6.4
27.7
0.0
0.0
0.0
8.4
1 IC^UI
(percent opacity)
35.00 -
35.00
35.00 — '
0.4
6.9
0.4
0.0
1.7
4.6
0,0
0,0
0.0
15.8
6.4
27.0
0.0
0.0
0.0
9.2
                                                         Scrubber Dryer
                                                         Stack Diameter - 7 ft.
                                                         2/6/74
                                                                     Comments
                                                               - start-up - 18 min.
                                                                 upset - 6 min.
                                                                 upset - 3 min.

                                                                 shutdown - 2 min,*

                                                                 start-up - 8 min.
                                                                 shutdown -  4 min.
* 15 minute break between shutdown and start-up
                                         53

-------
                                                    Coal Transfer Baghouse
                                                    Stack Diameter
                                                    2/6/74
   F-oriod
Meyer
. average)
1
2
3
4
5
6
7
8
9
10
11
12
13
(percent opacity)
0.0
0.0
0,0
0.0
0.0
20.0
19.4
11.5
0.0
1Z.3
0.0
0.0
1.3
{percent 01
0.0
0.0
0.0
0,0
0.0
19.8
20.8
12.1
0.0
12.3
0.0
0.0
1.9
                                                                 start-up  -  6 min.*
                                                                 shutdown  -  2  min.
* 20 minute shutdown and break before start-up
                                       54

-------
                                                  Coal  Transfer Rotodone  Stack
                                                  Stack Diameter -  2.5  ft.
                                                  2/6/74
   Period
•"eyer
. average)
1
2
3
4
5
6
7
8
9
10
11
12
13
14
(percent cp^ci ty)
0.0
0.0
0.0
0.0
0.0
18.1
37.9
4.8
0.0
13.3
0.0
0.0
12.5

(percent of
0.0
0.0
0.0
0.0
0.0
15.8
19.H
8.5
0.0
15.2
0.0
0.0
18.3

                                                                 start-up - 6 min.*
                                                                 shutdown - 2 min.
* 15 minute siiUtcL.
                                          55

-------
Appendix 8
     56

-------
                            Facilities
     J.  Fl u i d-bedthermaldryer.  The plant operation is approximately
200 tons per hour of cleaned coal.  All of the filter cake is fed to
the dryer.  A venturi-type scrubber is used to control participate
emission (AP of 43 inches w.g.).  The coal processed is lower kittanning.
     K.  Fluld-bed thermal dryer.  The dryer was designed to process 340
tons per hour of 1/4-inch x 0 cleaned bituminous coal (wet has"•''-} and
to discharge it at a rate of 312 tons per hour dried to a surface
moisture of 4 percent (wet basis).  The plant operation averages 400
tons per hour.  All of the filter cake was fed to the dryer.  The dryer
is controlled by a multiclone bank followed by a flooded disk venturi
scrubber (&P of 32 inches w.g.).
                                 57

-------
                                   TECHNICAL REPORT DATA
                            (fleait read Iiainiclions on the reverie before completing)
l. REPORT NO.
  EPA-450/2-74-021-C
                                                           3_ RECIPIENT'S ACCESS1OWNO.
•». TITLE AND SUBTITLE
  Background Information  for Standards of Performance:
  Coal  Preparation Plants
  Volume 3:   Supplemental  Information
             6. PERFORMING ORGANIZATION CODE
7. AUTHOH(S)
             s. PERFORMING ORGANIZATION REPORT NO.
9. PERFORMING ORGANIZATION NAME AND ADDRESS
   U.S.  Environmental Protection Agency
   Office of Air and Waste  Management
   Office of Air Quality Planning and Standards
   Research Triangle Park,  North Carolina 27711
                                                           10. PROGRAM ELEMENT NO.
             11. CONTRACT/GRANT NO.
12. SPONSORING AGENCY NAME AND ADDRESS
                                                            13. TYPE OF REPORT AND PERIOD COVERED
                                                              Final
                                                           14. SPONSORING AGENCY CODE
IS. SUPPLEMENTARY NOTES
16. ABSTRACT
        This report is issued in connection with  final  promulgation of  regulations for
   standards of performance  fcr new and modified  coal  preparation plants.   This
   document supplements  information presented  in  too earlier background documents
   (EPA-450/2-74-021 a and b).   This report contains a  revaluation of  the  standard
   for thermal dryers, a  summary of undated control costs, a discussion of  the in-
   flationary effects of  these  control costs,  ajid a projection of the annual  power
   consumption increases  required by the standards.  It also contains a discussion
   of  changes in the opacity standards for coal preparation plants.
17.
                                KEY WORDS AND DOCUMENT ANALYSIS
                  DESCRIPTORS
  Standards of performance
  Coal  preparation plants
 ; Control  costs
b.IDENTlFIERS/OPE.J ENDED TEHMS  c. COSATI I;ldd/C>i lup
                                                               PRICES SUUECT TO CHANGE
18 DISTRIBUTION STATEMENT
  Unlimited
19 SECURITY CLASS (Tills Kcporli
  Unclassified
                                                                              Of PAfiiS
                                              2O_ SECURITY CLASS I'tlu'lpage>

                                                Unclassified
                           77, PRICE
                             f- 
-------