OSW Doc. 530-R-94-011
                             NTIS No. PB94-170248
TECHNICAL RESOURCE DOCUMENT

EXTRACTION AND BENEFICIATION OF
        ORES AND MINERALS
             VOLUME 1
            LEAD-ZINC
                June 1994
           U.S. Environmental Protection Agency
              Office of Solid Waste
              Special Waste Branch
               401 M Street, SW
              Washington, DC 20460

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                                                               Technical Resource Document:  Lead-Zinc
                                 DISCLAIMER AND ACKNOWLEDGEMENTS
                        This document was prepared by the U.S.  Environmental Protection
                        Agency (EPA). The mention of company or product names  is not to
                        be considered an endorsement by the U.S. Government or the EPA.

                        This Technical Resource Document consists of two sections.  The first
                        section is EPA's Profile of the lead-zinc industry; the remaining
                        section is a Site Visit Report from a site visit conducted by EPA.  The
                        Profile Section was distributed for review to the U.S. Department of
                        the Interior's Bureau of Mines, the Western Governors Association,
                        the Interstate Mining Compact Commission, the American Mining
                        Congress, and Public Interest Groups.  Summaries of the comments
                        and EPA's responses are presented as an appendix to the Profile
                        Section. The Site Visit Report Section  was reviewed by individual
                        company,  state, and Federal representatives who participated in the
                        site visit.  Comments and EPA responses  are included as Appendices
                        to the specific Site Visit Section. EPA  is  grateful to all individuals
,^V                     who took the time to review sections of this Technical Resource
cy                      Document.
 *sj
  '                     The use of die terms "extraction," "beneficiation," and mineral
                        processing" in the Profile section of this document is not  intended to
 !/\                     classify any waste streams for the purposes of regulatory  interpretation
 x^                     or application.  Rather, these terms are used in the context of common
 ^                     industry terminology.
                                                                 U.S. Environmental Protection Agency
                                                                 Region  5, Library (PL-12J)
                                                                 77 West Jackson Boulevard, 12th Floor
                                                                 Chicago, IL  60604-3590

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                                                 Technical Resource Document:  Lead-Zinc
                               TABLE OF CONTENTS

                                                                                 Page

DISCLAIMER AND ACKNOWLEDGEMENTS  	  i

1.0 MINING INDUSTRY PROFILE:  LEAD-ZINC 	  1-1

     1.1  INTRODUCTION	   1-1
     1.2  ECONOMIC CHARACTERIZATION OF THE INDUSTRY	  1-3
         1.2.1    Lead	     1-3
         1.2.2    Zinc 	     1-3
     1.3  ORE CHARACTERIZATION  	   1-12
     1.4  LEAD-ZINC EXTRACTION AND BENEFICIATION PRACTICES  	   1-14
         1.4.1    Extraction Methods	   1-15
         1.4.2    Beneficiation Methods	   1-15
                 1.4.2.1   Milling  	   1-16
                 1.4.2.2   Flotation  	   1-16
                 1.4.2.3   Roasting and Sintering of Concentrates  	   1-23
     1.5  EXTRACTION AND BENEFICIATION WASTES ASSOCIATED WITH LEAD-
         ZINC MINES  	   1-25
         1.5.1    Extraction and Beneficiation Wastes	   1-25
                 1.5.1.1   Overburden and Mine Development Rock	   1-25
                 1.5.1.2   Mine Water   	   1-26
                 1.5.1.3   Flotation Wastes 	   1-28
         1.5.2    Waste Management	   1-28
                 1.5.2.1   Waste Rock Piles	   1-28
                 1.5.2.2   Mine Pits and Underground Workings	   1-29
                 1.5.2.3   Tailings Impoundments  	   1-29
                 1.5.2.4   Leachate  	   1-30
     1.6  ENVIRONMENTAL EFFECTS	   1-31
         1.6.1    Ground  Water/Surface Water	  1-31
         1.6.2    Soil	  1-32
         1.6.3    Air	  1-32
         1.6.4    Damage Cases	  1-33
                 1.6.4.1   National Priorities List Sites	  1-33
                 1.6.4.2   Clean Water Act Section 304(1) Sites	  1-33
                 1.6.4.3   Other Reported Damage Cases	  1-34
     1.7  CURRENT REGULATORY AND STATUTORY FRAMEWORK	  1-38
         1.7.1    Environmental Protection Agency Regulations 	  1-38
                  .7.1.1   Resource Conservation and Recovery Act	  1-38
                  .7.1.2   Clean Water Act 	  1-39
                  .7.1.3   Clean Air Act	  1-42
         1.7.2    Department of the Interior	  1-43
                  .7.2.1   Bureau of Land Management	  1-43
                  .7.2.2   National Park Service	  1-45
                  .7.2.3   Fish and Wildlife Service	  1-46
         1.7.3    Department of Agriculture  	  1-46
                 1.7.3.1   Forest Service	  1-46
         1.7.4    State Programs	  1-47
                 1.7.4.1   Alaska	  1-47
                 1.7.4.2   Missouri 	  1-49
     1.8  REFERENCES	  1-51

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                                            Technical Resource Document: Lead-Zinc'
2.0 SITE Vrsrr REPORT: DOE RUN FLETCHER	  2-1

    2.1 INTRODUCTION	  2-1
        2.1.1    Background	  2-1
        2.1.2    General Description	  2-2
        2.1.3    Environmental Setting 	  2-4
               2.1.3.1   Climate	  2-6
               2.1.3.2   Geology	  2-6
               2.1.3.3   Hydrology 	  2-8
    2.2 FACILITY OPERATION 	  2-10
        2.2.1    Mining Operations  	  2-11
        2.2.2    Mill Operation	  2-13
               2.2.2.1   Grinding  	  2-14
               2.2.2.2   Flotation  	  2-17
               2.2.2.3   Filtration	  2-18
               2.2.2.4   Process Control	  2-19
    2.3 WASTE MANAGEMENT	  2-21
        2.3.1    Types of Waste 	  2-21
        2.3.2    Tailings	  2-21
        2.3.3    Mine Water	:	  2-25
        2.3.4    Other Wastes	  2-26
    2.4 REGULATORY REQUIREMENTS AND COMPLIANCE	  2-27
        2.4.1    State of Missouri	  2-27
               2.4.1.1   Water Permit  	  2-27
               2.4.1.2   Metallic Minerals Waste Management	  2-30
               2.4.1.3   Dam Safety	,,	  2-30
               2.4.1.4  Other State Regulations	  2-30
        2.4.2    Federal Regulations	  2-31
    2.5 REFERENCES	  2-33
APPENDIX 1-A



APPENDDC 1-B


APPENDDC 1-C

APPENDK 1-D

APPENDDC 2-A


APPENDDC 2-B



APPENDDC 2-C
                  APPENDICES

SPECIFIC FLOTATION ACnVITIES EMPLOYED FOR
POLYMETALLIC ORES AND ASSOCIATED PROCESS
FLOW SHEETS  ;	  1-56

NPL SITE SUMMARIES RELATED TO LEAD AND ZINC
EXTRACTION AND BENEFICIATION	  1-62

SUMMARY OF COMMENTS AND EPA RESPONSES	  1-75

ACRONYMS	  1-78

THE DOE RUN COMPANY'S COMMENTS ON THE
DRAFT SITE VISIT REPORT, AND EPA'S RESPONSES	  2-34
THE BUREAU OF LAND MANAGEMENT'S COMMENTS
ON THE DRAFT SITE VISIT REPORT, AND EPA'S
RESPONSES  	
2-38
THE FOREST SERVICE'S COMMENTS ON THE DRAFT
SITE VISIT REPORT, AND EPA'S RESPONSES	  2-40
                                      in

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                                                      Technical Resource Document:  Lead-Zinc
                                      LIST OF TABLES
                                                                                         Page
Table 1-1.   Characteristics of Lead and Zinc Mines	   1-4
Table 1-2.   United States Consumption of Lead, By  Product (In Metric Tons)	   1-9
Table 1-3.   Waste to Product Ratios, Crude Ore to Product Ratios, and Material
            Handled to Product Ratios For Lead and Zinc, 1987	   1-14
Table 1-4.   Commonly Used Reagents in Lead and Zinc Flotation	   1-18
Table 1-5.   Range of Constituents of Waste Water and Raw Mine Waters Loads From
            Five Selected Lead-Zinc Mines  	   1-27
Table 1-6.   Missouri Mining Waste Damage Cases  	   1-35
Table 1-7.   Balaklala Mine Typical Metal Concentrations of Discharge	   1-37
Table 1-8.   Keystone Mine Typical Metal Concentrations of Discharge	   1-37
Table 1-9.   BPT and BAT  Standards Ore Mining and Dressing Point Source Category
            (milligrams per liter)	   1-40
Table 1-10.  BPT and BAT  Standards for Lead and Zinc Mills Using Froth-Flotation
            Alone or in Conjunction with Other Beneficiation Processes (milligrams per
            liter)	'	   1-41
Table 1-11.  Federal Water  Quality Criteria and Drinking Water Standards (in
            micrograms per liter)	   1-41
Table 1-12.  Water Quality Characteristics at Spring Creek	   1-64

Table 2-1.   Flotation Reagents, Their Function, and  Usage at the Fletcher Mill	  2-16
Table 2-2.   1989 and 1990 Tailings Composites, Fletcher Mill	  2-22
Table 2-3.   Water Chemistry Data for Monitoring Wells	  2-24
Table 2-4.   Water Quality Data for NPDES Outfalls 001 and 004, Second Quarter 1991 ....  2-28
                                     LIST OF FIGURES
                                                                                        Page
Figure 1-1.   Cross-Section Of a Typical Flotation Cell  	  1-19
Figure 1-2.   Typical Flow Sheet for Polymetallic Ore Flotation	  1-21
Figure 1-3.   Cross Section of a Typical Thickener	  1-22
Figure 1-4.   St. Joe Corporation-Balmat Plant Flow Sheet	  1-58
Figure 1-5.   Flow Sheet of the Magmont Concentrator	  1-59
Figure 1-6.   Row Sheet of Four Polymetallic Flotation Operations	  1-61

Figure 2-1.   Area of South East Missouri  	  2-3
Figure 2-2.   Topographic Map of the Site Area (modified)	  2-5
Figure 2-3.   Cross-section of Geology From USGS Reports .  . . •.	  2-7
Figure 2-4.   Cross Section of Shafts and Mine 	  2-12
Figure 2-5.   Fletcher Mill Flowsheet	  2-15
Figure 2-6.  . Fletcher Mill Daily Report  	  2-20
                                             IV

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                                                             Mining Industry Profile: Lead-Zinc
                        1.0 MINING INDUSTRY PROFILE:  LEAD-ZINC

 1.1     INTRODUCTION

This Industry Profile presents the results of the Environmental Protection Agency's (EPA's) research
into the domestic lead-zinc mining industry and is one of a series of profiles of major mining sectors.
Additional profiles describe copper mining, gold  mining, iron mining, and several industrial mineral
sectors, as presented in the current literature.  EPA prepared these profiles to enhance and update its
understanding of the mining  industry and to support mining program development by the states. EPA
believes the profiles represent current environmental management practices as described in the
literature.

Each profile addresses extraction and beneficiation of ores. The scope of the Resource Conservation
and Recovery Act (RCRA) as it applies to  mining waste was amended in 1980 when Congress passed
the Bevill Amendment, Section 3001(b)(3)(A).  The BeviJI Amendment states that "solid waste  from
extraction, beneficiation,  and processing of ores and minerals" is excluded from the definition of
hazardous waste under Subtitle C  of RCRA (40 CFR 261.4(b)(7)). The exemption was conditional
upon EPA's completion of studies required by RCRA § 8002(f) and (p) on the environmental and
health consequences of the disposal and use of these wastes.  EPA segregated extraction and
beneficiation wastes from processing wastes. EPA submitted the initial results of these studies  in the
7985 Report to  Congress: Wastes from the Extraction and Beneficiation of Metallic Ores, Phosphate
Rock, Asbestos, Overburden from Uranium Mining and Oil Shale (U.S. EPA, 1985).  In July 1986,
EPA made a regulatory determination that  regulation of extraction and beneficiation wastes under
Subtitle C was not appropriate (51 £R 24496; July 3,  1986).  EPA concluded that Subtitle C controls
were unnecessary and found  that a wide variety of existing Federal and State programs already
addressed many of the risks posed by extraction and beneficiation wastes.  Instead of regulating
extraction and beneficiation wastes as hazardous wastes under Subtitle C, EPA indicated that these
wastes should be controlled under Subtitle  D of RCRA.

EPA reported their initial findings on mineral processing wastes from the studies required  by the
Bevill Amendment in the  1990 Report to Congress: Special Wastes from Mineral Processing (U.S.
EPA, 1990).  This report covered 20 specific mineral  processing wastes. In June 1991, EPA issued a
regulatory determination (56  FR 27300) stating that regulation of these 20 mineral processing wastes
as hazardous wastes under RCRA  Subtitle C is inappropriate or unfeasible.  Eighteen of the wastes,
including slag from  primary lead processing and slag from primary zinc processing are subject to
applicable state  requirements. The remaining two wastes (phosphogypsum and phosphoric acid
process waste'water) are currently being evaluated under the authority of the Toxic Substances
Control Act (TSCA) to investigate pollution prevention alternatives.  Any mineral processing wastes
not specifically  included in this list of 20 wastes no longer qualifies for the exclusion (54 ££ 36592).
                                              1-1

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                                                              Mining Industry Profile:  Lead-Zinc
Due to the timing of this decision and the limited numbers of lead-zinc industry wastes at issue, lead-
zinc processing wastes are not addressed in this profile.

In addition to preparing profiles, EPA has undertaken a variety of activities to support state mine
waste programs.  These activities include visiting a number of mine sites; compiling data from State
regulatory agencies on waste characteristics, releases, and environmental effects; preparing summaries
of mining-related sites on the National Priorities List (NPL); and examining specific waste
management practices and technologies.  EPA has also conducted studies of State mining-related
regulatory programs and their implementation.

The purpose of this profile is to provide additional information on the domestic lead-zinc mining
industry. The report describes lead-zinc extraction and beneficiation operations with specific reference
to the wastes associated with these operations.  The report is based on literature reviews and on
comments received on earlier drafts. This report complements,  but was developed  independently of,
other Agency activities, including those described above.

This report briefly characterizes the geology of lead-zinc ores  and the economics of the industry.
Following this discussion is a review of lead-zinc extraction and beneficiation methods; this section
provides the context for descriptions of wastes and materials managed by the industry, as well as a
discussion of the potential environmental effects that may result  from lead-zinc mining.  The report
concludes with a description of die current regulatory programs  that  apply to the lead-zinc mining
industry as implemented by EPA, Federal land management agencies, and selected  states.
                                               1-2

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                                                            Mining Industry Profile:  Lead-Zinc
1.2    ECONOMIC CHARACTERIZATION OF THE INDUSTRY

1.2.1  Lead

Domestic production of lead concentrates in 1989 was 420,000 metric tons.  Domestic lead
concentrate production in 1990 increased to 495,000 metric tons (U.S. DOI, Bureau of Mines,  1991;
1992). The United States is the world's largest primary lead producer with 1/5 of all production and
reserves.  About 1/2 of the  domestic lead demand is met by recycling lead from secondary sources
(scrap), rather than primary sources (mining) (U.S. DOI, Bureau of Mines, 1990).  Approximately
874,000 metric tons of lead were recovered from scrap sources. Total consumption of lead in 1989
was reported to be approximately  1.3  million metric tons. (U.S. DOI, Bureau of Mines, 1992).

Historically, lead has been mined in 12 states: Arizona, California, Colorado, Idaho, Illinois,
Missouri,  Montana,  Nevada, New Mexico, New York, Tennessee, and Utah.  In 1988, however, lead
ore was not mined in California or Utah.  According to the U.S. Bureau of Mines,  Missouri produced
over 90 percent of all domestic lead in 1988.  Table 1-1 .is a list of active lead and zinc mines in the
United States as of 1990. Information provided includes mine owners, mine operators, commodities
produced, production data, ore reserves, and ore grade. These mines account for nearly all
domestically-produced primary lead (Michaelis, 1990/1991; Gardiner, 1990).

In 1989, the lead industry employed 1,800 workers at mines and mills, 800 at primary smelters and
refineries, and 1,700 at secondary smelters and refineries.   For 1990, employment figures were
expected to increase to 2,100 workers at mines and  mills and  1,800 at secondary smelters and
refineries.  Primary  smelter and refinery employment was not expected to change in 1990 (U.S. DOI,
Bureau of Mines,  1991).

Refined lead is used in a variety ways:  for bearing  or casting metal; as sheet lead; solder; oxide; and
in storage batteries.  Major  domestic uses of lead, by product and  SIC code, are listed  in Table  1-2
(U.S. DOI, Bureau of Mines, 1990a).  In 1989, transportation was the most common end use for lead
products, accounting for 75  percent of all lead produced.  This included automotive batteries, as well
as solders, seals, and bearings. Electrical uses, electronics, ammunition, TV glass,  building
construction, communications, and protective coatings (including radiation shielding) accounted for an
additional 20 percent of production. Currently, lead is also used in ballast weights,  ceramics, crystal
glass, tubes or containers, type metal, foil, and wire (U.S.  DOI, Bureau of Mines, 1991).

1.2.2  Zinc

In 1990, U.S. zinc mining operations extracted 515,000 metric tons of recoverable zinc, valued at
$847 million; an increase of 239,000 metric tons over that produced in 1989. The amount of zinc
from scrap sources decreased slightly (from 117,000 to 109,000 metric tons) for the same period
(U.S. DOI, Bureau of Mines, 1992).
                                             1-3

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                                        Table 1-1.  Characteristics of Lead and Zinc Mines

State

AK





AK




CO






CO








Mine Name
<_-,
Greens Creek Mine
(Startup 1989)




Red Dog Mine (Startup
1989)



Asarco Leadville Unit
(Resurrection Mine, Black
Cloud Mine)




Sunnyside Mine








Location

Admiralty
Island




Kotzebue




Lake County
(Leadville)





San Juan
County
(Silverton)






Owner(s)
[Operator]

Kennecott: 53%
Hecla Mining: 28%
Exalas Resources:
12.6%
CSX Oil & Gas: 6.3%
[Greens Creek Mining]
Cominco American,
Inc.,
NANA Regional Corp.

(Cominco Alaska, Inc.]
Asarco, Inc.: 50%
Resurrection Mining
Co., Newmont: 50%

[Asarco, Inc.]


San Juan County
Mining Venture:
Washington Mining Co.
33%, Alta Bay Venture
(Echo Bay, Alta Gold)
67%
[Washington Mining
Company]

Commodities
Produced*

Gold
Silver
Zinc
Lead


Lead
Zinc
Silver


Lead
Zinc .
Gold
Silver



Gold
Silver-
Lead
Zinc
Copper



Lead-Zinc
Production 1988
(tons
concentrate/year)
(Projected)


Pb - 8,000
Zn -23,000

(Expected)

Zn - 560,000
Pb - 120,000

Pb- 7,000
Zn - 14,900





N/A







Ore Reserves
(tons)
Ore Grade (per
ton ore)
3.500,000

0.18 oz Au
3.9% Pb
9.7% Zn
24 oz Ag
85.000,000

5.0% Pb
17.1% Zn
2.4 01 Ag
84 1,000 Ions

3.37% Pb
8.41% Zn
1 .9 oz Ag
0.06 oz Au
0.19% Cu
627,000 tons

0.15 oz Au
42% Pb
6.2% Zn
0 57% Cu


' Commodities presented in order of listing iniRandol Directory.



Sources: Michaelis, 1990/1991; Gardiner, 1990


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                                         Table 1-1. Characteristics of Lead and Zinc Mines (Continued)

Statp

ID



ID





ID





MO






Mine Name
••
Fourth of July Mine



Galena Mine





Lucky Friday Mine





Magmont Mine





•
Location

Valley County
(Yellow Pine)


Shoshone
County
(Mullan)



Shoshone
County
(Mullan)



Iron County
(Bixby)





Owner(s)
[Operator]


[American Ind. Mines
& Minerals Corp.]

Callahan Mining Corp.:
50%
Asarco Inc.: 37%
Hccla Mining Co.: 13%


Hecla Mining Company:
100%

[Hecla Mining
Company]

Cominco Ltd.: 50% '.
Dresser Industries, Inc.:
50%

[Cominco American
Incorporated]

Commodities
Produced*

Silver
Lead
Gold
Tungsten
Silver
Lead
Copper
Zinc
Gold

Silver
Gold
Zinc
Lead


Lead
Zinc
Copper



Lead-Zinc
Production 1988
(tons
concentrate/year)

N/A


N/A





Pb - 12.675
Zn - 2,301




Pb- 99.000
Zn - 15.000




Ore Reserves
(tons)
Ore Grade (per
ton ore)

N/A


1.239.000

16.39 oz Ag
10.04% Pb
0.57% Cu
0.11% Zn
598.200

15.4 oz Ag
13 0% Pb
2.3% Zn
N/A Au
3.690.000

7.5% Pb
1.2% Zn
0.3% Cu

I/I
       •Commodities presented in order of listing in Randol Directory.



       Sources:  Michaelis, 1990/1991; Gardiner, 1990

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                                   Table 1-1.  Characteristics of Lead and Zinc Mines (Continued)

State

MO



MO







MO





MT






Mine Name

Sweetwater Mine



Viburnum Mines (6
mines):
Brushy Creek
Casteel
Fletcher
Viburnum 28
Viburnum 29
Buick
West Fork Mine




,
Montana Tunnels Mine






Location

Reynolds
County
(Bunker)

Iron,
Reynolds, and
Washington
Counties




Reynolds
County
(Bunker)



Jefferson
County





Owner(s)
[Operator]

Asarco, Inc.: 100%

[Asarco, Inc.]

The Doe Run Company





(Subsidiary of the Fluor
Corporation]
Asarco, Inc.: 100%

[Asarco, Inc.]



Montana Tunnels
Mining Co. (Pegasus
Gold, Inc.): 100%

[Montana Tunnels
Mining Co.]

Commodities
Produced*

Lead
Zinc


Lead
Zinc
Copper





Lead .
Zinc




Gold
Silver
Lead
Zinc


Lead-Zinc
Production 1988
(tons
concentrate/year)
Pb - 20.900
Zn- 1,600


Pb - 326,515
Zn- 46,416






Pb - 49,000
Zn- 11.900




Zn - 18.400
Pb- 8,400




Ore Reserves
(tons)
Ore Grade (per
ton ore)
24,967.000

484% Pb
0.59% Zn
73,0749,000

5.1% Pb
0.9% Zn
0.3% Cu



10.295.000

5.93% Pb
1.47% Zn
0.04% Cu
0.30 oz Ag
37.370,000

0.021 oz Au
0.36 OL Ag
0 63% Zn
0 23% Pb
'Commodities presented in order of listing in Randol Directory.



Sources: Michaelis, 1990/1991; Gardiner, 1990
                                                                                                                                      S

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                                   Table 1-1.  Characteristics of Lead and Zinc Mines (Continued)

State
*

NM






NY



OR




TN





Mine Name
••:-
Cyprus Pinoi AMoi (Zn
suut-up 1990)





Balmat Mine No. 2
Balmat Mine No. 4
Pierrepont Mine No. 4

Silver Butte Mine (Under
construction.)



Coy Mine





Location

Grant County
(Silver City)





St. Lawrence
County


Douglas
County



Jefferson
County




Owner(s)
[Operator]

Cyprus Copper Co.:
50%
St. Cloud Mining Co.
(The Goldficld Corp.):
50%
[Cyprus Pinos Altos
Corp.]
Horschead Industries

[Zinc Corporation of
America]
Formosa Exploration
Inc.: 100%

[Formosa Exploration
Inc.]
Asarco, Inc.: 100%

[Asarco.lnc.]



Commodities
Produced*

Copper
Zinc
Silver




Zinc



Gold
Silver
Copper
Zinc

Zinc




Lead-Zinc
Production 1988
(tons
concentrate/year)
(Projected)
Zn - 2.500 to 3,000






N/A



N/A



Zn - 74.800

(Includes New
Market, Young, and
Immel Mines)
Ore Reserves
(tons)
Ore Grade (per
ton ore)
800,000

4.9% Cu




3.900,000

Grades N/A

460,000

3 40% Cu
2.83% Zn

6.398,000

3.23% Zn


•Commodities presented in order of listing in Randol Directory.



Sources:  Michael is, 1990/1991; Gardiner, 1990

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                                         Table 1-1. Characteristics of Lead and Zinc Mines (Continued)
State
TN
TN
TN
TN
WA
WA
Mine Name
Elmwood-
Gordonsville Mine
Immcl Mine
New Market Mine
Young Mine (including
former Beaver Mine)
Glass Mine (start-up 1990)
Schumaker Mine (start-up
1990)
Location
Smith County
Knox County
Jefferson
County
Jefferson
County
Pend Oreille
County
Stevens County
(Colvilk)
Owner(s)
[Operator]
Jersey Miniere Zinc:
100%
(Union Zinc)
[Jersey Miniere Zinc]
Asarco, Inc.: 100%
(Asarco.lnc.)
Asarco, Inc.: 100%
[Asarco.lnc.]
Asarco, Inc.: 100%
[Asarco.lnc.]
[Raven Hill Mining]
Cordilleran Mines
[General Mine Services
Corp.]
Commodities
Produced*
Zinc
Zinc
Zinc
Zinc
Lead
Zinc
Lead-Zinc
Production 1988
(tons
concentrate/year)
N/A
Sec Coy Mine.
See Coy Mine.
Sec Coy Mine.
N/A
N/A
Ore Reserves
(tons)
Ore Grade (per
ton ore)
N/A
( 1. 600,000 tpy ore)
Sec Coy Mine.
(863.322 tpy ore)
See Coy Mine.
(732,000 tpy ore)
See Coy mine.
(1,151. 100 tpy ore)
N/A
100.000
10.0% Zn
oo
       N/A  Not available.




       •Commodities presented in order of listing in Randol Directory.



       Sources: Michaelis, 1990/1991; Gardiner, 1990

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                                        Mining Industry Profile:  Lead-Zinc
Table 1-2.  United States Consumption of Lead, By Product
           (In Metric Tons)
SIC
Code

3482

35
36
371
37
3351
36
15

36
371
37
3443

15
3443

15
3443
Product
Metal Products
Ammunition: Shot and bullets
Bearing Metals
Machinery except electrical
Electrical and electronic equipment
Motor vehicles and equipment
Other transportation equipment
Total bearing metals
Brass and bronze: Billets and ingots
Cable covering: Power and communication
Calking lead: Building construction
Casting Metals:
Electrical machinery and equipment
Motor vehicles and equipment
Other transportation equipment
Nuclear radiation shielding
Total casting metals
Pipes, casts and other extruded products:
Building construction
Storage tanks, process vessels, etc.
Total pipes, traps, other extruded products
Sheet lead:
Building construction
Storage tanks, process vessels, etc.
Total sheet lead
1988

52,708

425
C)
5,152
457
6,034
9,994
16,170
1,618

rl,333
C)
13,474
1,065
r!5,872

11,193
C)
11,193

14,009
C)
17,458
1989

62.940

W
W
1,683
W
2,586
9,610
22,605
1,831

524
W
3,395
W
16,175

8,856
962
9,818

15,900
C)
20,987
                          1-9

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                                                                          Mining Industry Profile:  Lead-Zinc
               Table  1-2.  United States Consumption of Lead, By Product (Continued)
SIC
Code

15
3443

15
341
367
36
371

3691
3691
371
27
34

285
32
28
2911


Product
Sheet lead:
Building construction
Storage tanks, process vessels, etc.
Total sheet lead
Solder:
Building construction
Metal cans and shipping containers
Electronic components and accessories
Other electrical machinery and equipment
Motor vehicles and equipment
Total solder
Storage batteries:
Storage battery grids, post, etc.
Storage battery oxides
Total storage batteries
Terne metal: Motor vehicles and equipment
Type metal: Printing and allied industries
Other metal products'1
Total metal products
Other oxides:
Paints
Glass and ceramic products
Other pigments and chemicals
Total other oxides
Gasoline additives
Miscellaneous uses
Grand total
1988

14,009
(*)
17,458

3,985
848
4,824
3,052
6,355
19,064

'514,694
'454,964
'969,658
2,324
(c)
5,290
rl, 127,383

W
W
W
62,524
O
55,263
'1,245,170
1989

15,900
C)
20,987

3,909
762
4,092
2,029
6,217
17,009

552,308
459,847
1,012,155
2,286
(c)
4,564
'1,182,566

W
W
10,074
57,984
0
42,684
1,283,234
' Reviied.      w withheld to avoid disclosing company proprietary data; included in Total other oxide*.
' Included with "Other transportation equipment* to avoid disclosing company proprietary da|a.
* Included with 'Building conatruction* to avoid disclosing company proprietary data.
' Included with 'Other metal products' to avoid diacloaing company proprietary data.
* Includes lead consumed in foil, collapsible tube*, annealing, galvanizing, plating, and fishing weights.
* Included with "Miscellaneous uses" to avoid disclosing company proprietary data.
 Note: Totals may not add because of withheld information.


Source:  U.S.  DOI, Bureau  of Mines, 1990b
                                                       1-10

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                                                             Mining Industry Profile: Lead-Zinc
Historically, recoverable zinc has been mined in 18 states:  Arizona, Colorado,  Idaho, Illinois,
Kansas, Missouri, Montana, Nevada, New Jersey,  New Mexico, New York, Oklahoma,
Pennsylvania, Tennessee, Utah, Virginia, Washington, and Wisconsin. In 1988, however, no zinc
ore was extracted in New Jersey, Pennsylvania, or Utah, and nearly 50 percent  of all domestic zinc
was produced in Tennessee. Other known state production figures include Missouri (17 percent) and
Montana (8 percent).  Table 1-1  is a list of active lead and zinc mines in the United States as of 1990.
Information provided in the table includes mine owners, operators, commodities produced, production
data, ore reserves, and ore grade (Michaelis,  1990/1991; Gardiner,  1990).

In 1989, the zinc industry employed 2,350 workers at mines and mills and 1,500 at primary smelters.
For 1990, mine and mill employment was expected to grow to 2,600 and employment at zinc smelters
was expected to  increase to 1,550 (U.S. DOI, Bureau of Mines, 1991).  Employment increases in
mines and mills may be attributed to opening new mines, such as the Red Dog Mine in Alaska.

Zinc products are used in several major industries, including construction (45 percent of 1988
consumption for galvanizing and steel  manufacturing); transportation (23 percent); machinery
manufacturing (12 percent); electrical (10 percent); and chemical and other industries (10 percent)
(U.S. DOI, Bureau of Mines,  1990b).

Zinc has a number of properties  that make it valuable to industry.  These include a low melting point,
high electrochemical activity to protect iron and steel materials from cathodic corrosion, and the
ability to alloy with copper to  make brass (U.S. DOI, Bureau of Mines, 1985b). Galvanizing and
electrogalvanizing (steel coating) were the principal uses of refined zinc in 1988, accounting for 51
percent of all zinc use.  Zinc was also used extensively in zinc-based die-cast alloys (23 percent) and
brass alloys (13 percent).  The remaining 13 percent  of zinc consumption was used for alloys, rolled
zinc, dust, and oxide (U.S. DOI, Bureau of Mines, 1990b).

Zinc oxide is well suited for use in rubber, paints,  inks, dyes, oil additives, wood preservatives,
fungicides, varnishes, and linoleums.  Zinc oxide is used in these products because of its opacity to
ultra-violet light and high refractory index, durability, and electrostatic properties (U.S. DOI, Bureau
of Mines, 1985b).
                                              1-11

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                                                             Mining Industry Profile:  Lead-Zinc
13    ORE CHARACTERIZATION

Lead and zinc most often occur in association with the sulfide mineral group.  Other metals associated
with sulfide ores include copper, iron, mercury, arsenic, cadmium, silver, and small quantities of
gold.  These metals occur in varying amounts with lead and zinc ores.  Galena (PbS) and sphalerite
(ZnS) are the principal minerals mined to recover lead and zinc, respectively.

Deposits that contain more than one of these recoverable metals are referred to as "polymetallic ores,"
and are described by the dominant economic metal being recovered, followed by lesser constituents.
For example, a mine producing mainly lead and some zinc is referred to as a "lead-zinc mine."
Similarly, a zinc-copper mine produces mainly  zinc and some copper.  The individual metal content is
dependent on the nature of the ore body. In the United States today, minable quantities of lead and
zinc ore are recovered from three types of deposits:  strata-bound deposits, replacement deposits, and
vein deposits.

The largest and most productive lead  and zinc ore deposits are associated with expansive, relatively
flat lying sedimentary deposits.  Strata-bound deposits, as  the name implies, are restricted to well-
defined stratigraphic units, typically limestone,  dolomite, or shale. In strata-bound deposits, the
metal-bearing minerals  may be deposited either during or  long after deposition of the host limestone
or dolomite.  Deposits that form during or shortly following deposition are referred to as strata-bound
deposits of syngenetic origin; those that form long after lithification of the sediments are referred to
as strata-bound deposits of epigenetic origin.  Most geologists agree that the origin of the lead and
zinc bearing minerals in southeast Missouri are of epigenetic origin.  Strata-bound ore deposits are
typically capped by fine-grain sediments, such as shales.  The cap rock acts to contain the migrating
mineral bearing hydrothermal  fluids.  Minerals precipitate in the host rock as a result of changes in
chemistry, temperature, and pressure.

The best known strata-bound deposits in the United States are the Mississippi Valley type, such as
those found in Missouri and Tennessee, and the relatively recent discovery in the DeLong Mountains
of Alaska. Most notable of these are the lead-zinc ores of the Viburnum Trend (also referred to as
the "New Lead Belt") in southeast Missouri and the zinc-lead ores of the Red Dog deposit  in Alaska.
Ore grades for the Viburnum Trend deposits range  between 5 and 10 percent lead, up to 1  percent
zinc, with  lesser amounts of copper, silver, nickel,  cobalt, cadmium, and silver. Mineral assemblages
found at the Buick mine are typical of the Viburnum Trend and include galena, sphalerite,
chalcopyrite (CuFeSj),  pyrite (FeSj),  calcite (CaCO3),  and dolomite (CaMgCCO^.   The Red Dog
deposit is considered to be the largest or second largest zinc-lead deposit in the world.   Mineralization
occurs in black shales of late Mississippian to Permian age.  It  is a strata-bound accumulation of silica
rock, barite, and sulfides; dominant gangue minerals are quartz and barite (U.S. DOI, Geological
Survey,  1973 a and b; Weiss, 1985; Krai, 1992).
                                               1-12

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                                                             Mining Industry Profile: Lead-Zinc
Replacement and vein type deposits make up a smaller portion of mined lead and zinc ores.
Historically, however, these kinds of deposits were the primary source of ore. These deposits form
when hydrothermal solutions containing metals migrate through vein and porous  rock and eventually
precipitate as a result of changes in chemistry, temperature, and pressure. Host  rocks vary greatly
and include sedimentary carbonates as well as igneous and metamorphic rocks.  Examples of
replacement deposits mined as ores are found in Bingham, Utah, and Oilman and Leadville,
Colorado.  Examples of vein deposits are those found in the Coeur d'Alene district of Idaho.  Typical
ore grades are on the order of 10 to 30 percent lead and zinc combined, 3 to 5 percent copper, and
smaller quantities of silver and gold.  Common mineral  assemblages include galena, sphalerite,
chalcopyrite (CuFeSj), and pyrite (FeSj).  Associated with these deposits are elements such as silver,
arsenic, antimony, and cadmium.

Other sources of zinc ores are associated with metamorphic rocks.  Examples of these are the
Ducktown district of Tennessee,  the Balmat-Edwards district of New York, and the Franklin Furnace-
Sterling Hill district of New Jersey. To date, the New York and New Jersey districts have produced
seven million tons of zinc; however, New Jersey is not currently producing measurable quantities of
zinc.  Significant reserves remain in these districts.  The Franklin zinc deposit in New Jersey is
unique in that the minerals are predominantly franklinite ((Z^CFe.Mn^OJ, willemite (Zn^SiOJ, and
zincite (ZnO).  Tennessee continues to produce significant quantities of zinc.
                                             1-13

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                                                            Mining Industry Profile: Lead-Zinc
1.4    LEAD-ZINC EXTRACTION AND BENEFICIATION PRACTICES

Lead and zinc operations consists of three major operational steps:  extraction, beneficiation, and
processing.  Extraction is defined as removing ore material from a  deposit and encompasses all
activities prior to beneficiation.   Beneficiation of lead and zinc ores includes crushing, grinding,
washing, filtration, sorting, sizing,  gravity concentration, and flotation concentration (40 CFR 261.4).
Processing activities follow beneficiation and include smelting and refining of concentrates to prepare
a marketable lead or zinc product.  This profile only discusses extraction and beneficiation activities.
A discussion of wastes generated from mineral processing is found in  EPA's 1990 Report to
Congress, Special Wastes from Mineral Processing.

Material associated with lead-zinc mining may consist of the ore itself, mine development rock (in the
case of underground mines), and overburden (in the case of surface mines).  Mine development rock
is the material removed while constructing shafts, adits, and drifts, or preparing access to the ore
body (Weiss, 1985).  Overburden consists of soil and rock material that overlies the mine area.
Industry collectively refers to these materials as waste rock. A summary of the quantities of material
handled,  waste, and crude ore, and marketable product generated at lead and zinc mines in 1987 (as
reported by  the U.S. Bureau of Mines) is presented in Table 1-3.  Also  presented in this table are
associated production ratios.

        Table 1-3. Waste to Product Ratios, Crude Ore to Product  Ratios, and Material
                   Handled to Product Ratios For Lead and Zinc, 1987
Material/Ratio
Material Handled
Crude Ore
Waste
Marketable Product
Waste to
Marketable Product Ratio
Crude Ore to
Marketable Product Ratio
Material Handled to Marketable
Product Ratio
Lead
(1,000 short tons)
8,670
5,800
2,870
290
(units)
9.9:1
20.9:1
29.9:1
Zinc
(1,000 short tons)
5,230
5,180
50
169
(units)
0.3:1
30.7:1
30.9:1
 Source:  U.S. DOI, Bureau of Mines, I990a; 1990b
                                              1-14

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                                                             Mining Industry Profile:  Lead-Zinc
1.4.1   Extraction Methods

Lead and zinc are mined almost exclusively in underground operations although a few surface
operations do exist.  For example, the Red Dog Mine in Alaska, which began production in August
1990, employs open-pit mining techniques (Alaska Division of Geological and Geophysical  Surveys,
1989).  The decision to use underground or surface mining techniques is dependent on the proximity
of the ore body to the surface.  Lead-zinc underground mining techniques use shafts, drifts, and adits
to access the ore body.  The most common underground mining method to remove the ore  is room-
and-pillar.  (U.S. DOI, Bureau of Mines, 1984; 198Sa).  Room-and-pillar techniques are commonly
used to extract lead-zinc ore from large, flat-lying, tabular-shaped, strata-bound deposits. This
mining style is employed to extract the ores in southeast Missouri. In contrast,  extraction of ore from
vein-type deposits is  best suited to more selective  slope mining methods.  Stope mining involves the
driving of horizontal shafts into the ore body, one above the other.  Sloping was used in the mines
near Leadviile, Colorado. The exact mining method used  is determined by the individual
characteristics of each ore body.

In general, underground mining operations involve sinking a shaft near the ore body to be extracted
and extending horizontal passages (levels) from the main shaft at various depths to the ore.  Ore is
removed from the mine either through shaft conveyances or chutes. In some  cases, waste rock or
classified mill tailings are returned to the mine and used to backfill mined-out areas (U.S. EPA,
Office of Water, 1982).

Profitable recovery of lead-zinc ores ranges from  as low as 3 percent metal in ore for large, easily
accessed mines, to 6 percent for small, difficult-to-access underground mines, to more than  10  percent
for extremely high-cost, remote areas.  The Red Dog Mine concentrator (in the  Delong Mountains in
northwestern Alaska) is expected to mill ore averaging 5 percent lead and 17.1 percent zinc (Sastry,
1988).  Low grade lead and zinc ores can also be  mined profitably when produced as a byproduct of
copper mining, or when appreciable quantities of precious metals (such as silver) are present (Weiss,
1985).  Few lead-zinc deposits contain more than  50 million tons of ore.

1.4.2  Benefication Methods

Beneficiation of lead  and zinc ores begins with milling (crushing and grinding).  Following these
steps, the ore is further beneficiated by flotation.  Before the advent of flotation  in the early 1900s,
gravity concentration was the chief method by which lead-zinc ores -were concentrated.  As a result of
more selective reagents and advancements in grinding techniques, flotation has virtually replaced
gravity concentration. Gravity concentration techniques, however, may still be used for
preconcentrating before fine grinding and flotation (U.S. DOI, Bureau of Mines,  1984; 1985a).
                                              1-15

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                                                               Mining Industry Profile: Lead-Zinc
 1.4.2.1    Milling

 Beneficiation starts with the milling of extracted ore in preparation for further activities to recover the
 lead and zinc values.  Milling operations are designed to produce uniformly sized particles by
 crushing, grinding, and wet or dry classification. The capital investment and operation costs of
 milling equipment are high. For this reason, economics plays a large part  in determining the type of
 milling (or comminution) equipment and the degree of crushing or grinding performed to prepare the
 ore for further beneficiation. Other factors  include the value concentration of the ore and its
 mineralogy (especially the presence or absence of pyrite), hardness, and moisture content. Milling
 procedures vary widely both between mills and within individual mills, depending on these variables
 (White and Clifford, 1977).

 Milting is a  multistaged operation of crushing and grinding.  Crushing is usually a dry operation,
. using water  sprays only to  control dust.  Frequently, a primary crusher (jaw crusher) is located at the
 mine site to  reduce the ore material into particles less than ISO millimeters (mm) (6 inches) in
 diameter.  The crushed ore is then transported to a mill site for additional  crushing, grinding,
 classification, and concentration.

 Additional milling uses a cone crusher, usually followed by grinding in rod and ball mills. Grinding
 is a wet operation in which water and initial flotation reagents are added to form a slurry.
 Alternatively, the ore may  be fed into an autogenous mill (where ore acts as a grinding medium) or a
 semi-autogenous mill (where the ore is supplemented with large steel balls).

 Between each grinding unit operation, hydrocyclones are used to classify coarse and fine particles.
 Coarse particles are returned to  the mill for further size reduction.  The resulting size of the classified
 ore is usually about 65-mesh (.208 mm).  Chemical  reagents that will be used during flotation
 separation activities may be added to the ore during milling activities (U.S. DOI, Bureau of Mines,
 198Sa; 1990a).  Mill production capacities can be as high as 7,000 to 9,000 tons per day. Mills
 located, in the eastern United States grind ore that is predominantly composed of zinc, with smaller
 quantities of lead and other minerals.  Mills in the midwest, including some in Missouri,  grind ore
 that is predominantly lead with smaller amounts of zinc and other minerals. Western mills produce
 various combinations of lead and zinc (White and Clifford,  1977; Chandler, 1970).

 1.4.2.2   Flotation

 Flotation  is  a technique by which particles of one mineral or group of minerals are made to adhere
 preferentially to air bubbles in the presence of a chemical reagent (U.S. EPA, Office of Water,
 1982).  This is achieved by using chemical  reagents that preferentially react with the desired mineral.
 Flotation  is  the most commonly used method to concentrate lead-zinc minerals.  The effectiveness of
 the technique, however, is dependent on four factors related to the nature of the ore body:  the degree
                                                1-16

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                                                              Mining Industry Profile: Lead-Zinc
of oxidation of the ore, the abundance of iron sulfides, the presence of copper minerals, and the basic
or acidic nature of the gangue (Weiss, 1985).

In addition to those factors related to the mineralogy of the ore, other factors are also important to the
success of flotation activities.  These factors include uniformity of particle size, use of reagents
compatible with the mineral, and water conditions that will not interfere with the attachment of the
reagents to the mineral or air bubbles (U.S. EPA, Office of Water,  1982).

Ore may be treated with conditioners and regulators during or after milling to modify the pH of the
ore pulp for flotation (U.S.  EPA, Office of Water, 1982).  Depending on the ore characteristics, these
conditioners or regulators may  include lime, soda ash (sodium carbonate), caustic soda (sodium
hydroxide), or sulfuric acid. The conditioned ore is then slurried in a solution of fresh or salt  water
with chemical reagents of four  main groups. Reagents typical of each group are presented in Table
1-4.  Below is a description of the function of each group (U.S. EPA, Office of Water, 1982; Weiss,
1985; U.S. DOI, Bureau of Mines,  1985a):

        •  Collectors (promoters) - Cause adherence between solid particles and air bubbles  in a
          flotation ceil.

        •  Frothers - Stabilize air bubbles by reducing surface tension, thus allowing collection of
          valuable material by skimming from the top of the cell:

        •  Activators - Promote flotation in the presence of a collecting agent when added to mineral
          pulp.

        •  Depressants - React with particle surfaces in the flotation cell to keep materials from
          remaining in the froth. Instead, materials fall  to the  bottom as tails.

For example, flotation of galena in the presence of sphalerite is possible by adding  sodium cyanide
(NaCN) and  xanthate.  Sodium cyanide depresses the sphalerite but not galena (see Table 1-4).  After
the galena has been collected from the froth, sphalerite can be floated by adding copper sulfate
(CuSOJ and  xanthate (Considine, 1975).

Several factors are important when  conditioning the ore for flotation with chemical  reagents. These
include thorough  mixing and dispersal of reagents through the pulp; repeated contact between the
reagents and  all die relevant ore particles; and time for the development of contacts with the reagents
and ore particles to produce the desired reactions.  Reagents may be added in a number of forms,
including  solid, immiscible liquid, emulsion, and solution in water.' The concentration of reagents
must  be closely controlled during conditioning; adding more reagent than  is required may retard the
reaction and reduce efficiency (Fuerstenau, 1976).
                                              1-17

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                                                             Mining Industry Profile:  Lead-Zinc
                Table 1-4.  Commonly User Reagents in Lead and Zinc Flotation
     Type of Reagent
       Lead i. .cation
     Zinc Flotation
  Promoter
         Aerofloats
         Aerophine
         Minrec A
         Xanthates
       Xanthates
       Aerofloats
    Sodium Aerofloat
  Frother
         Dow Froth
  Methyl Isobutyl Carbinol
          Pine Oil
       Dow Froth
        Flotal B
Methyl Isobutyl Carbinol
        Pine Oil
  Activator
      Alkaline Sulfides
         Phosphate
     Copper Sulfate
  Depressant
Cyanide (Sodium or Calcium)
      Sodium Bisulfate
        Dichromate
     Zinc Hydrosulfate
        Zinc Sulfate
     Sulfur Dioxide
Sodium Hydrogen Sulfide
      Zinc Sulfate
    Sodium Cyanide
Source: U.S. EPA, Office of Water, 1982; Fuerstenau, 1976

Typical flotation conditioning includes the following steps (Fuerstenau, 1976):


        •  Addition of modifiers, conditioners, and regulators to disperse slime coatings of pulp
          molecules and to adjust pulp pH

        •  Resurfacing and the addition of necessary depressants and activators

        •  Final pH adjustment

        •  Addition of and coating of collectors on pulp molecules

        •  Addition of frother

        •  Addition of small air bubbles to flotation cells by an air blower or by the action of a
          submerged rotor or impeller

Figure 1-1 presents a cross section of a typical flotation cell (Envirotech, 1974). The current trend is
toward the development of larger flotation cells that are more energy efficient.  Pulp,  a suspension
containing milled ore and flotation reagents, is fed to flotation cells.  Typically, 10 to 14 cells are
arranged in a series from roughers to scavengers.  Roughers are used to make a coarse separation of
values from the gangue.  Scavengers recover smaller quantities of the remaining values from the pulp
(Fuerstenau,  1976).  Froth sent from the scavengers and roughers go to cleaner ceils where residual
wastes are removed and a concentrate is produced.
                                              1-18

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                                                        Mining Industry Profile: Lead-Zinc
                                                             Upper portion of
                                                             rotor draws air
                                                             down the standpipe
                                                             lor thorough mixing
                                                             with pulp
                                                                    Dlsperser breaks
                                                                    air into minute
                                                                    bubble*
                            0000000000
          Larger fetation unto
          mdudefatoe bottom
          to aid pump flow
                   Figure 1-1.  Cross-Section Of a Typical notation Cell

Source:  Envirotech, 1974
                                         1-19

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                                                              Mining Industry Profile: Lead-Zinc
The height of the flotation column is determined by the position of the overflow weir.  A cell may
function as a rougher, a scavenger, or a cleaner depending on its location in the circuit. In rougher
cells, the flotation column is kept tall with a thick froth created by the reaction of flotation reagents in
contact with the mineral as air is pumped  into the bottom of the cell  (Fuerstenau,  1976).

Several separate flotation  steps may be necessary to beneficiate a polymetallic ore. Most sulfide ores
contain varying amounts of minerals such as lead, zinc, copper, and  silver; thus, multiple floats are
needed to concentrate individual metal values (U.S. DOI, Bureau of Mines, 1985a; Weiss, 1985).
The tailings (residual material) from one mineral float are often used as feed for a subsequent float to
concentrate another mineral. A  typical example includes the following steps, which are also
illustrated in Figure  1-2 (Fuerstenau, 1976):

       •   Bulk flotation of lead-copper minerals and depression of zinc and iron minerals

       •   Flotation of a copper concentrate and rejection of a lead (sink) concentrate; lead is
           recovered in a subsequent series of steps

       •   Activation and flotation of the  sphalerite from iron and gangue minerals

       •   Flotation of pyrite, if recovery is desired

       •   Flotation of barite concentrate.

A discussion of the specific  flotation activities for polymetallic ores employed by several
concentration operations,  as well as a summary of the grades and recovery rates of several
concentrators, is presented in Appendix 1-A.

The froth recovered  in the cleaning cells is transferred to thickeners, where the concentrate is then
thickened by settling (see  Figure 1-3). The thickener underflow (the concentrate)  is pumped,
dewatered by passage through a filter press and then dried.  The liquid overflow from the thickener
contains waste water, flotation reagents, and dissolved and suspended mineral  products.  This solution
may be recycled or sent to a tailings pond (Fuerstenau, 1976).

Wastes from the rougher, scavenger, and  cleaning cells are collected and directed to a tailings
thickener.  Overflow from this unit (wastewater containing high solids and some wasted reagent) is
often recycled back to the flotation cells.  Thickener underflow (tailings) contain remaining gangue,
unrecovered lead-zinc material,  chemical reagents, and waste water.  This underflow is pumped as a
slurry to a tailings pond.  The solid content of the slurry varies with each operation, ranging from 30
to 60 percent.  At the tailings pond solids are seeded out of the solution and the clarified waste water
may be recycled to the mill. Coarse tailings are sometimes sold as mortar sand and agricultural lime.
Tailings are also used as fill for underground mine workings (White  and Clifford, 1977).
                                               1-20

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                                                     Mining Industry Profile: Lead-Zinc
             Float
                    Bulk Pb, Cu Flotation
                                                          Sink
Condition to
daprass Pb
        — Rotation —
 Cu
Float
                       Pb
                       sink
                                   Condition to
                                    Actlvi
                             vata
                                      Float
                                                      Condition to
                                                      activata Zn
                                                               ata
                                             l— Rotation
                                            Zn
                                           Float
Sink
              Float
                                   Condition to
                                   Actlvata Ba
                                                                          I
                                                                        Sink
      Ba
     Float
                                      Float
                                                      Sink to Tailings Pond
               Figure 1-2.  Typical Flow Sheet for Polymetailic Ore Flotation

Source: Fuerstenau, 1976
                                        1-21

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                                                           Mining Industry Profile: Lead-Zinc
                       Figure 1-3. Cross Section of a Typical Thickener




Source: Fuerstenau, 1976






                                            1-22

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                                                             Mining Industry Profile:  Lead-Zinc
\ .4.2.3    Roasting and Sintering of Concentrates

Concentrates of lead and zinc minerals that are to be processed by pyrometallurgical methods such as
smelting and refining may require sintering, depending on the processing methods used.  Sintering
involves the partial fusion of ore concentrates into an agglomerated material suitable for processing
operations.  The sinter material is typically a crushed and graded structure of porous, cellular solids
(Weiss, 1985).

Sintering operations consist of several steps, including blending, sintering, cooling, and sizing.  Raw
materials, such as ore concentrates, ore screening, fluxes, plant recycle dusts, filter cake, and coke
breeze are blended with small amounts of moisture in pug mills, balling drums, or balling pans. The
concentrate feed is then fired (sintered) and cooled.  During cooling, the sinter is crushed and is
typically less than six inches in diameter.  This product will be graded and further crushed in some
operations to produce a smaller sinter product (Weiss,  1985).

Of the five primary lead processing facilities in the United States, four sinter the concentrate prior to
processing.  They are the Doe Run facility in Boss,  Missouri; the Doe Run facility in Herculaneum,
Missouri; the ASARCO facility in East Helena, Montana; and the ASARCO  facility in Glover,
Missouri. The ASARCO facility in Omaha, Nebraska, is a refinery, not a smelter, and thus does not
have a sintering operation (U.S. EPA, Office of Solid Waste,  1990).

The sinter plant at the Doe Run smelter and refinery in Herculaneum, Missouri, first became
operational in the early  1900s and was last modernized in  1967.  Inputs to this operation include lead
concentrate (204,000 st), sand  (6,100 st), hematite (99,200 st), coke breeze (7,500 st), baghouse fume
(29,400 st), dewatered sludge and fines (22,000 st),  and slag (176,100 st). The maximum practical
operating capacity in 1988 was 1,975 st per day.  The plant was in  operation 323 days in 1988.  The
principal product was 478,660 st of finished sinter.  Residues generated included primary lead slag,
dust and primary lead process water  (U.S. EPA, Office of Solid Waste,  1990).

The sinter plant at the ASARCO smelter in East Helena, Montana,  was built  in 1923 and was last
modernized  in 1977. The inputs for this operation are ore concentrates, recycled dust, and sinter
wastewater treatment plant sludge.  The wastes generated by the sinter plant include process water
and dust (U.S. EPA, Office of Solid Waste, 1990).

The ASARCO smelter and refinery in Glover,  Missouri, operated a sinter plant that was built in 1968
and was last modernized in 1977. The inputs to the operation include ore concentrates, 1/3  of the
slag generated from the smelter, sludge from the waste water treatment plant, and  waste water that is
recycled to the sinter plant.  The primary product from the sinter operation is sinter. Wastes,
including process water and dust, are also generated in  the process (U.S. EPA, Office of Solid Waste,
1990).
                                              1-23

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                                                              Mining Industry Profile:  Lead-Zinc
The Big River zinc facility in Sauget, Illinois; the Jersey Miniere zinc facility in Clarksville,  Indiana;
and the Zinc Corporation of America facility in Bartlesville, Oklahoma, are all electrolytic zinc
operations that have roasting operations with zinc concentrate as an input, but they are not smelting
operations.  The Zinc Corporation of America  pyrometaJlurgicaJ facility in Monaca, Pennsylvania,
however, does have a sintering operation.  The inputs to this operation are roasted ore, sinter plant
baghouse dust, and zinc lean fines (U.S. EPA, Office of Solid Waste, 1990).
                                               1-24

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                                                            Mining Industry Profile:  Lead-Zinc
1.5    EXTRACTION AND BENEFICIATION WASTES ASSOCIATED WITH LEAD-ZINC
       MINES

Wastes generated by lead-zinc operations include mine water, waste rock, tailings, and refuse.  Many
of these wastes may be disposed of onsite or offsite, while others may be used or recycled during the
active life of the operation. Waste constituents may include base metals, sulfides, or other elements
found in the ore, and any additives used in beneficiation operations. The primary waste generated by
mineral extraction in underground mines is mine development rock, which is typically used in onsite
construction for road or other purposes.  Surface mines usually generate large volumes of overburden
and waste rock that are usually disposed of in waste rock dumps.

In general, most wastes from  beneficiation of lead-zinc ores are disposed of in tailings impoundments
from which water is likely to  be reclaimed during the  mine's life.  Some materials may be either used
on site or  disposed of, depending on the operating conditions of a facility at a specific time.  For
example, mine water pumped from the mine to de-water active work areas can be used in
beneficiation operations, often with excess mine water being disposed of as a waste by discharge
through a  NPDES permit. Wastes that can be either used during operation, and/or disposed of
depending on site-specific conditions, are described in this section.

In addition to wastes generated as part of extraction and beneficiation, facilities also store and use a
variety of chemicals required  by the mine and  mill operations. A list of chemicals used at lead-
zinc mines, compiled from data collected by the National Institute for Occupational  Safety and Health
(NIOSH), is provided below (National Institute for Occupational Safety and Health, 1990).

Acetylene                          Sodium Cyanide                   Methane, Chlorodifuoro-
Calcium Oxide                     Sulfur Dioxide                     Sodium Aerofloat
Hexone                            Sulfuric  Acid                       Sulfuric Acid Copper (2+)
Hydrogen Chloride                 Diesel Fuel No. 1                   Salt (1:1)
Methyl Chloroform                 Diesel Fuel No. 2                  Zinc Solution
Methyl Isobutyl Carbinol            Chromic Acid, Disodium Salt       Zinc Sulfate
Nitric Acid                        Copper Solution
Propane                            Kerosene

1.5.1   Extraction and Beneficiation Wastes

1.5.1.1     Overburden and Mine Development Rock

Waste generated as a result of lead-zinc mining include overburden  and mine development rock,
collectively referred to as waste rock. As noted previously, the materials can be used onsite or placed
in waste rock dumps.  The quantity and composition of waste rock generated at lead-zinc mines  varies
greatly between sites.  These wastes will contain minerals associated with the ore body and host rock.
                                             1-25

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                                                             Mining Industry Profile: Lead-Zinc
Typical minerals associated with sulfide ores are chaJcopyrite, pyrite, calcite, and dolomite (Weiss,
1985).

At the Doe Run facility in Viburnum, Missouri, mine development rock (called "shaft rock" by Doe
Run) is used as a construction material around the mine.  Other mine development rock from
underground operations is simply stored in underground openings (Carter, 199lb).

1.5.1.2   Mine Water

Mine water is generated when water collects in mine workings, both surface and underground, as a
result of inflow from rain or surface water and from ground-water seepage.  During the active life of
the mine, water is pumped out of the mine as necessary to keep the mine dry and allow access to the
ore body for extraction.   As mentioned above, this water may be used in beneficiation operations or
stored on-site and discharged as a waste through an NPDES permit.

The quantity and chemical composition of mine water generated at mines varies from site to site. The
chemistry of mine water is dependent on the geochemistry of the ore body and the surrounding area.
Mine water may also contain small quantities of oil and grease from extraction machinery and nitrates
(NO,) from blasting activities.  Chemical  characteristics of mine water from several lead-zinc mines
are shown in  Table 1-5 (U.S. DOI, Bureau of Mines, 1984; U.S. EPA,  Office of Solid Waste, 1985).
This table shows the chemical composition of such waters.  The range of concentrations in mine water
(mg/1) for lead was .1-1.9, zinc .12-.46, chromium .02-.36, sulfate 295-1,825, and pH 7.9-8.8.

After the mine is closed and pumping stops, the potential exists for water exposed to sulfur-bearing
minerals in an oxidizing environment, such as open pits or underground workings,  to acidify.  This
may lead to the mobilization of metals and other constituents in the remaining ore body exposed by
mining and to the contamination of surface and/or ground water.

Actions taken by mine operators to control water during the active life of the mine  include pumping
from sumps within the mine or from interceptor wells, which withdraw ground water and create a
cone of depression in the water table, thus dewatering the mine. Surface water is often controlled
using diversion and other engineering techniques to prevent water from flowing into the mine.  (U.S.
DOI, Bureau of Mines,  1984; U.S. EPA, Office of Solid Waste, 1985).

.The Magmont facility in Missouri anticipated that 3,000 gallons per minute (gpm) of water would
eventually be pumped from the mine. The facility has installed a permanent underground pumping
station, including settling sumps, to address this problem.  It is noted that the sumps settle between 20
and 30 tons of sludge from mine water per week during operations.  The settled mine pump-out water
is sent to the mill to be used as process water or channeled directly to tailings ponds, along with the
settled sludge (Schwandt, 1970).  In  the Viburnum Trend, mine water from the underground mines is
pumped at a rate between 300 and 7,000  gpm for each mine.
                                              1-26

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                                                          Mining Industry Profile:  Lead-Zinc
        Table 1-5.  Range of Constituents of Waste Water and Raw Mine Waters Loads
                   From Five Selected Lead-Zinc Mines
Parameter
Alkalinity
Hardness
ToUl suspended solids (TSS)
ToUl dissolved solids (TDS)
Chemical oxygen demand (COD)
ToUl oxygen content (TOC)
Oil and grease
MB AS surfactants
P
Ammonia
Hg
Pb
Zn
Cu
Cd
Cr
Mg
Fe
Cyanide
Sulfate
Chloride
Fluoride
PH«
Range of Raw Waste Load
Range of
Concentration in
wastewater, mg/1
low
IB*
26
310
2
670
71.4
11
0
.18
.42
.05
.0001
.1
.12
.02
.005
.02
.02
.05
.01
295
21
.13
7.9
•«>•
la*
609
1.760
108
2,834
1,535
35.
8
3.7
.150
14
.1
1.9
.46
.36
.011
.67
.08
.53
.03
1,825
395
.26
8.8
Per unM ore milled,
c/t
fewer
lafc
410
460
7
940
6
6.35
5
.236
.108
.064
.00013
.127
.089
.026
.008
.026
.026
.064
.013
130
20
.370
- •
•ppcr
la*
1,600
4,700
285
8,500
4,800
130
21
. 13
.876
26.4
.0026
6.9
17.2
.158
0.18
1.77
.290
1.16
.109
4,800
870
.944
-
Per unit
concentrated
produced, g/t
lower
h*
1,450
2,290
30
4,800
30
30
30
2.05
.54
.32
.00168
.900
.62
.18
.18
.45
.012
.091
1,260
210
230
.
-
•ppcr
!•*
10,200
32,500
2,000
50,900
50,000
580
130
60.7
2.54
185
.130
32.2
86.0
1.96
8.85
1.39
10.0
.198
509
33,700
4,070
5.45
-
•Value in standard units

Source:  U.S.- DOI, Bureau of Mines, 1984
                                           1-27

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                                                             Mining Industry Profile:  Lead-Zinc '
After closure, both surface and underground mines fill with water as ground water rises to pre-mining
levels. As with active mines,  the quantity and chemical composition of mine water varies from mine
to mine and is dependent on the geochemistry of the area.

1.5.1.3   Flotation Wastes

After the removal of values in the flotation process, the flotation system discharges tailings composed
of liquids and solids.  Between 1/4 and 1/2 of the tailings generated are made up of solids, mostly
gangue material and small quantities of unrecovered lead-zinc minerals.  The liquid component of the
flotation waste is usually water and dissolved solids, along with any remaining reagents not consumed
in the flotation process. These reagents may include cyanide, which is used as a sphalerite depressant
during galena flotation. Most operations send tailings to impoundments where solids settle out of the
suspension1.  The characteristics of tailings from the flotation process vary greatly, depending on the
ore,  reagents, and processes used. As shown in Table 1-5, lead, zinc,  chromium,  iron, and  sulfate
were all found in the waste water of the selected facilities (U.S. DOI, Bureau of Mines, 1984).

In 1980,  the St. Joe Minerals Corporation tailings pond at Viburnum received mill wastes transported
in a  slurry of about 35 percent solid material.  In July 1982, water from the pond had a dissolved
lead concentration of less than 84 micrograms per liter (ftg/1), a dissolved zinc concentration of 620
/ig/1, a dissolved arsenic concentration of 43 /ig/1, dissolved cadmium and copper concentrations of
less  than 2 jig/1, and a dissolved selenium concentration of 81 pg/1.  During 1980, the fresh  tailings
had  a lead content of 736 micrograms per gram 0*g/g),  a zinc content of 260 /xg/g, an arsenic content
of 34 iig/g, a cadmium content of less than 10 pg/g, a copper content of 449 /xg/g, and a selenium
content of 6.1 /xg/g.  Settled solids had a lead content of 358 /xg/g, a zinc content of 222 /xg/g, an
arsenic content of 35 /xg/g, and a selenium content of 1  /xg/g (U.S. EPA, Region YD, 1983).

1.5.2 Waste Management

Wastes generated as a result of extraction and beneficiation of lead and zinc minerals are managed
(treated,  stored, or disposed) in discrete units.  For the purposes of this report, these units are divided
into three groups:  waste rock piles, mine pits and underground structures,  and tailings
impoundments.

 1.5.2.1    Waste Rock Piles

Waste rock (overburden and mine development rock) removed from the mine is stored or disposed of
in unlined piles onsite. These piles may be referred to as mine rock dumps or waste rock dumps.
Constituents of concern in runoff and leachate from waste rock piles may include heavy metals.
    1EPA has prepared a separate report on tailings disposal in impoundments.

                                               1-28

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                                                              Mining Industry Profile: Lead-Zinc
These piles also could generate acid drainage if sulfide minerals, oxygen, and moisture are present in
sufficient concentrations without adequate neutralization potential or other controls.

1.5.2.2    Mine Pits  and Underground Workings

In addition to wastes  generated during active operations, when the mines close or stop operation, pits
and underground workings may be allowed to fill with water, since there is no longer a need for
dewatering.  This accumulating water, which may become mine drainage, can acidify through
aeration and  contact with sulfide minerals and become contaminated with heavy metals.

At pits where quartz minerals are associated with lead-zinc deposits, silica dust exposure may be a
problem both during mine operations and following closure.  Asbestos, which may be present in pits
where limestone and dolomite ores are mined, may also be a concern (U.S. Department of Health  and
Human Services, 1982).

1.5.2.3    Tailings Impoundments

Tailings are the discarded material resulting from the concentration of ore through various
beneficiation operations. This material has minimal value at present but is produced in extremely
large quantities.  Tailings are characterized by fine particle sizes and varying mineralogical and
chemical compositions. Tailings typically take the form of a slurry; the waste slurries from milling,
gravity concentration, and flotation contain approximately 65 percent water and 35 percent solids
(Carter,  199 la).

The disposal of tailings requires a permanent site with adequate capacity for the life of the mine. The
method of tailings disposal is largely controlled by the water content of the tailings.  Literature
consulted for this report suggests that only impoundments are used in the lead and zinc industries.
However, historic beneficiation methods  using vibrating tables to concentrate values produced
"middlings" or "chat," that was disposed of in tailings piles.  This technique is not used in modern
lead-zinc mill operations.

Tailings  impoundments are created as disposal sites for wet and thickened tailings that leave the mill
in the form of slurries.  After settling in the impoundment, the aqueous component is typically
decanted and pumped back to the mill. Two general classes of structures may be used to construct a
tailings impoundment: water-retention dams and raised embankments.  Water retention dams involve
the construction of a dam with a low permeability core while raised, embankments are constructed of
waste rock and tailings, with permeability usually controlled by tailings gradation.  Both the water
retention and raised embankment methods rely on natural topography to assist in the impoundment  of
tailings and tailings water.  The height of a raised embankment may be increased to expand storage.
The choice of impounding structure is influenced by the characteristics of the mill tailings, as well  as
the site.  Evaporation and seepage  may occur with both types of impoundments.
                                              1-29

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                                                           Mining Industry Profile:  Lead-Zinc
The size of tailings impoundments varies among operations. For example, the impoundment at the
Magmont facility in Missouri consists of an 85-foot high by 1,000-foot long compacted earth-filled
dam and an 80-acre pond (Schwandt,  1970). The Doe Run Company Fletcher Project, also in
Missouri, is currently planning to expand its tailings pond capacity from its current 140 acres to 239
acres.  At capacity, the pond contents will be 4 percent liquid and 96 percent solids. The planned
expansion will accommodate the wastes generated from the remaining ore reserves of approximately
20 million tons (Doe Run Company, 1990).

1.5.2.4   Leachate

Leachate or runoff generated by exposing mine waste to precipitation may escape into the
environment.   Such leachate is not mine waste, but may be subject to regulation under the Clean
Water Act (CWA)  or the Comprehensive Environmental Response, Compensation, and Liability Act
(CERCLA).
                                             1-30

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                                                              Mining Industry Profile:  Lead-Zinc
1.6     ENVIRONMENTAL EFFECTS

Nearly any portion of waste management units at active mines may be a potential source of
environmental contamination.  Waste rock piles and tailings impoundments are of particular concern
since these are the areas in which toxic contaminants most commonly are found.  Contaminants
associated with these areas may include heavy metals, reagents, and acid rock drainage that may
degrade ground water, surface water, soil, and air quality during mine operation and after mine
closure.  A discussion of the potential environmental effects associated with lead-zinc mining is
presented in the following sections.  Specific examples from industry are included in this section, as
appropriate.  Actual release incidents occurring at lead-zinc mine sites are described in the Damage
Case Section of this report.

This section does not purport to be a comprehensive examination of environmental damages that can
occur or that actually occur at mining operations.  Rather, it is a brief overview of some of the
potential problems that can occur under certain conditions.  The extent and magnitude of
contamination depends on highly variable site-specific factors that require a flexible approach to
mitigation.  EPA  is aware that many of the potential problems can be, and generally are, substantially
mitigated or avoided by proper engineering practices,  environmental controls, and regulatory
requirements.

1.6.1   Ground Water/Surface Water

Sources of ground and surface water contamination include runoff, leachate, and seepage from tailings
impoundments, mine pits and workings (after mine closure), as well as waste rock piles.

For lead and zinc recovered from sulfur-bearing ores, acid generation due to oxidation of sulfides in
the ore body, host rock, and waste material may be of special concern.  Acidified water increases the
potential for leaching heavy metals from these sources and facilitates their transport.  Factors that
influence the acid generation potential include the sulfide content,  the buffering capacity of the ore
and/or tailings, exposure of mineral surfaces in an oxidizing environment, moisture, and the
hydrogeology of the area. Some bacteria, such as Thiobacillus ferroxidans. are catalysts for oxidation
of sulfur-bearing minerals leading to acid generation.  These bacteria pose a particular problem in
waste rock piles and tailings impoundments.

As water acidifies, the potential for leaching and mobilization of metals and other contaminants
increases. The suite of elements and minerals that may be associated with lead-zinc deposits includes
mercury, tellurium, cobalt, thallium, pyrite, and pyrrhotite.  Lowering of pH  affects the solubility of
these constituents making them available for transport in both surface and ground water. Whether
these contaminants will migrate depends on the geochemistry in the vicinity.  It should be noted that
the ore host rock in most U.S. lead mines is a dolomitic limestone.  However, not all reactions are
                                              1-31

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                                                            Mining Industry Profile: Lead-Zinc
dependent on low pH.  For example, high concentrations of arsenic have been found to be mobile at a
PH of 10 (U.S. EPA, Office of Solid Waste, 1990).

EPA and PEDCO conducted a cooperative study in 1983 concerning the St. Joe Minerals
Corporation's Viburnum Mine tailings pond. Results showed that, on average, calcium, sodium,
magnesium, TDS, sulfate, nitrate, potassium, and chloride were higher downstream of the pond than
upstream. It was not clear, however, that this was due to tailings disposal activities (U.S. EPA,
Region VII, 1983).

Surface and underground mines must be dewatered to allow extraction of ore.  This can be
accomplished in one of two ways:  pumping from ground  water weils to lower the water table or
pumping directly from the mine workings.   After a mine is abandoned, pumping is usually stopped,
allowing the pit or workings to fill with water.  Over time, this may lead to uncontrolled  releases of
mine water.  The mine water may be acidic and contain metals, as well as dissolved and suspended
solids.

1.6.2   Soil

Environmental impacts to soils as a result of mining  activities are most commonly associated with
erosion and  contamination. Erosion may be caused by land disturbances and removal of vegetation
related to mining activities.  Under these conditions, precipitation events such as snowmelt may lead
to erosion of soils.

Contamination of soils  may occur from discharge, runoff, leachate, and seepage from tailings
impoundments, pits and underground workings, as well as waste rock piles.  In addition,  deposition
of wind-blown particulates from dry tailings impoundments may also be a source of soil
contamination.  Other sources of soils contamination include spills of fuel, flotation reagents, cleaning
solutions, as well as other chemicals used or stored at the site.

Soils, if they become contaminated, contain substances found in the waste materials,  including those
materials discussed in the Ground Water/Surface Water Section above. Contaminated soils may
further act as a source of contamination to ground water, surface water, and in some instances as a
source of air pollution due to re-entrainment and/or subsequent deposition of particulates.  In some
instances, direct human contact has occurred when tailings have been used in sandboxes, as soil
amendments, and as construction fill material, although these are generally historic practices.

1.63  Air

The primary source of air contamination at mine sites is fugitive dust from the dry surfaces of tailings
impoundments, as well as waste rock piles, if they are exposed to the environment (Cornell, 1991).
Often, tailings impoundments are not completely covered by water, thus dry tailings are commonly
                                              1-32

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                                                             Mining Industry Profile:  Lead-Zinc
available for wind-blown transport (as discussed above).  Deposition of wind-blown tailings provides
exposure routes for contamination of ground water, surface water, and soil. Potential contaminants
include those discussed in the Ground Water/Surface  Water Section.

1.6.4  Damage Cases

Damages resulting from waste management from mining lead and zinc metals and associated minerals
have been documented.  Superfund, the Clean Water  Act, and other EPA investigations have verified
contamination to ground water, surface water, air, and soil media.  Examples include the following:

       •  Lead, zinc, and other contaminants in ground water proximal to mine sites have
          contaminated drinking water resources.

       •  Acid mine drainage and associated contaminants flowing to surface water have given rise
          to pollution of the water resources and sediments.

       •  Wind-blown tailings have posed health risks to humans through their inhalation of gas and
          dust containing pollutants.

       •  Deposition of sulfur compounds and other contaminants, such as dust from wind-blown
          tailings, in soils have provided human exposure pathways.

       •  Misuse and mismanagement of wastes, including construction of housing directly on wastes
          and use of tailings in gardens, have provided human exposure pathways.

1.6.4.1   National Priorities List Sites

EPA reviewed sites on the NPL and found that lead-zinc extraction and beneficiation was conducted
at the following sites: Iron Mountain in Redding, California; California Gulch  in Leadville, Eagle
Mountain in GUman, and Smuggler Mountain in Pitkin County, all in Colorado; Bunker Hill in
Kellogg, Idaho; Cherokee County,  Kansas;  Oronogo-Duenweg Mining Belt in Missouri; Tar Creek,
on the border  between Oklahoma and Kansas; all parts of the Tri-State Mining District in Kansas,
Oklahoma, and Missouri; and Sharon Steel/Midvale Tailings in Midvale, Utah.  Many of these sites
represent an accumulation of wastes over an extended period of operations. For example, Oronogo-
Duenweg operated for more  than 100 years. Mining  of the Bunker Hill site ceased in 1991, also over
100 years after mining began.  Appendix 1-B provides a general site description and a summary of
the environmental effects associated with these sites.

1.6.4.2   Clean Water Act Section 304(1) Sites

Section 304(1) of the Water Quality Act of 1987 requires States to identify water bodies not  meeting
applicable water quality criteria, to identify point source dischargers to these water bodies, and to
develop and require implementation of Individual Control  Strategies (ICSs) for those point source
dischargers that contribute significantly to exceedance of the water quality criteria.  The 304(1)
program has identified two lead-zinc sites as sources of contamination to surface waters.
                                             1-33

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                                                            Mining Industry Profile:  Lead-Zinc
The Black Cloud Mine and  Mill, a Res-ASARCO Joint Venture, is an active lead-zinc operation near
Leadville, Colorado.  All mine and mill waste waters are directed to a tailings pond.  In addition, all
runoff from process areas drains to the tailings pond, which discharges to Iowa Gulch (a tributary of
the Arkansas  River).  The discharge from the tailings pond has been shown to be toxic to  aquatic life.
The facility has consistently exceeded the discharge limitations for TSS, cyanide, zinc, and
manganese.

The Rico Mine Development Corporation operates a treatment system for mine drainage from the
inactive Rico  Mine, which produced lead, zinc, and silver. The discharge from the mine has been
identified as contributing to toxicity in Silver Creek (a tributary of the Delores River). The toxicity
in the discharge results from high concentrations of metals that exceed applicable water quality-based
standards.

1.6.4.3    Other Reported Damage Cases

EPA Study of Missouri Damages

In 1984, EPA summarized damage from the disposal of mining wastes. For the State of Missouri, 14
sites related to lead-zinc mining were identified. Of these sites, six were  active mines and eight were
inactive. The results  of this study are summarized in Table 1-6 (SCS Engineers, 1984) (note that
individual mine site names were withheld by the source).  Typical problems include surface water
quality degradation and pollution due to catastrophic and intermittent releases from tailings or settling
ponds.  Typical pollutants included lead, zinc, cadmium, copper, organics, and sediment.

Red Dog Mine, Alaska

The partnership of Cominco Alaska, Inc., and the Kotzebue-based NANA Regional Corporation owns
Red Dog Mine, which is one of the largest lead-zinc operations in the world. Cominco began
development  of Red Dog Creek in 1982 and Red Dog Mine began major  construction in 1989. The
Red Dog ore deposit in the DeLong Mountains contains large amounts of zinc and lead, as well as
aluminum, copper, iron, cadmium, silver, and nickel.  Leaching of metals from the ore-rich DeLong
Mountains into Red Dog Creek has been documented for years, but it has increased dramatically since
Red Dog Mine reached full production in the summer of 1990. Red Dog Creek contains  no fish,
partly because of high metal concentrations.  It does, however, empty into the Ikalukrok Creek,
which in turn empties into the Wulik River.  This area is one of the richest fisheries in northwestern
Alaska.  Ikalukrok Creek is a wintering  ground for Dolly Varden (Arctic char), and Wulik River is a
major habitat for Dolly Varden and spawning salmon.  The Wulik River also flows to the small
Inupiat Eskimo community of Kivalina, about 60 miles downstream from the mine.  Villagers there
catch fish and draw drinking water from the river.
                                              1-34

-------
                                             Table 1-6.  Missouri Mining Waste Damage Cases
Background
MM*
Stem*
Pb. Zn
Pb.Zn
Pb. Zn.
Cu
Pb.Zn.
Cu
Pb. Za.
Cu
Pb. Za.
Cu
Pb.Zn.
Cu
Pb.Zn.
Cu. Aq
Pb.Zn.
Cu. Aq
Pb.Zn,
Cu. Aq
Pb.Zn.
Cu. Aq
Pb.Zn.
C».A,
Pb.Zn.
Cu,A,


Fe
F^tthy
StataM
Active
Inactive
Inactive
Act
Inactive
Inactive
Active
Active
Active
Inactive
Inactive
Inactive
Inactive
Active


Wnat,
S«WC«
Mme
Mme
Mine
Mine;
mill
Mae
Mme
Mine
Mine;
mill
Mine;
mill
Mine;
mill
Mme
Mine
Mine
Mine
Mine*
Mine
w«*»
tn*
TaaVmma
infer
NS
Tub
Tub
Tub
Tub
Tub; mill
reagent
WMlet
Tub; mill
reagent
waMe.
Tub; mine
water
Tub, mme
water
Tub
Tub
Tub
Tub;
Tub
NS
Ml*.
g^j-iiiiji-i
fT*W*
Panda;
NS
Pod
Panda
Pile; pond
Pik
Pond
Pomb
Pond
Pond*
Pile; bra
Pile; pond
Pile
Pood.;
lagoona
Pond.
NS
Problems
Data.


3/1/71
J/29/77
3/25/7*
1977







8/1/75


Tyr»
Dbcbufe
Sedmt
Tub; WMer
Tub
Sedmt.
Tub;
wMhoul
Runoff;
dbchw|e
OiKfaufe;
•eepuie
Runoff
Bfk««r«
SeepMC
Sedmt
Tub
Tub. wMer
runoff
Runoff
Sedmt.
MUM*
r«rw
IntermiMent

CUMtrophk
CMMmahic
Intermmmi
Canvlropluc
Ink-imiHfml
Intemudent
InlennMenl
InlermiMcnl
!»!-„. i^-,1
Sewonal
ScMoml
CMMtrophk
Inlennident

f aiM<
Dbcnuie
(Deliberme)

Dnfuhm
DHnbreKD;
Heavy IUM
Runt
Heavy run;
wind eroMon
Heavy mio.
MilllrlmL pond
mm end pne
Heavy mim
Heavy mini
Snwllbket
formed on pile
Heavy ram*
Eraion; heavy
rain*
Dam failure
Eroaioo;
inaufficienl
pond capacity

Polhiunn)
SedmLmetab.
organic.
Sedmt
Sedmt. Cd, Cu.
Pb.Zn
Sedmt Pb.Zn
Sedmt. Pb. Zn.
Cd. Cu
Sedmt. Pb. Zn.
Cd, Cu. Be
Pb. Zn. Cu.
Cd. M|. aedmt
Sedmt. mdab.
organic.
An. Hn. Cu.
Pb, Cd, Sedmt
Sedmt metab
Sedmt Pb.Zn.
Cu. Cd
Sedmt, Pb. Zn.
Cu. Cd
Sedmt. Pb, Zn.
Cd.Cu
Sedmt
Sedmt
Duuge
Baccntor
SW;benthoa
SW;bcnmoa
SW;*oil
Sw
SW. fiah
SW
SW
SW;benmoa
SW;benmoa
SW
SW
SW
SW
Sw. fiah
SW. bemho.
SW, benmo.
Effect
WQdegrad.
WQ degnd.
WAde«nd ;
turbida> iml m
nver
WQdegrad.
WAdegrad
WA degnd; tevere
pik eraaion
WAdegrad.
WAdegrad.
WQ degnd.
Potential WQ
degnH<*iion
WQdegrad.
WQdegrad.
WQ degnd.
Severe WQ degnd
WQpoll.
WQ degrad
Macnitude
Iml creek red.
bcnduc com.
6 m. degrad n
creek, red benduc
coma
Killed crop.; red
mod value
Heavy melab
accua. m lake
Uptake PL by
plant., rah
Uptake PL by
plants, fiah
Potomal buacc.
Red. benducOrg
Lmuled
Effect on bcnduc
coma not known
Uptake PL by
plant, fwk
Unknown
Uptake PL by fmk.
plant.
Fimkill. damage to
10 5 ml creek red.
bcnduc com..
Red benlhic oil
Mitigation
Action
Y
N
Y
Y
N
N
N
Y
Y
N
N
Y
N
Y
N
N
Tj-p.
Miami rr
•yaton, 2nd
acung pond

Dam repaired
Stab dam



Recycling to
conlrol exceaa
datcharge
Slab or dam.
water reticle


New pond
(I°7I)

Slab & main


OJ
en
       Source: SCS Engineers,  1984. NS = Not Specified; SW = Surface Water; WQ = Water Quality.

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                                                            Mining Industry Profile: Lead-Zinc
In the early 1980s, before mining began, the Alaska Department of Environmental Conservation
(DEC) records showed natural concentrations of zinc in Red Dog Creek between 7 and 52 parts per
million (ppm), with one reading of 273 ppm.  Summer 1990 samples from the creek showed
consistent zinc measurements above 100 ppm, with an early July measurement of 970  ppm.
Since the fall  of 1989, Alaska Department of Fish and Game (ADF&G) biologists have identified
discoloration  in the form of a milky orange plume of precipitate beginning at Red Dog Mine and
flowing downstream for about 20 miles.  The source of the water is seepage from the  saturated zone
associated with the ore body exposed by mining.  (Although this is  not associated with a waste
management activity, there is evidence that water related problems can arise from other parts of the
mine operation.) This seep water  contains high concentrations of zinc and iron.  Cominco has agreed
to take appropriate actions to reduce the introduction of heavy metals into Red Dog  Creek.   (Alaska
Department of Environmental Conservation, Northern Regional Office vs. Cominco America, Inc.,
Compliance Order by Consent).

Balaklaia, Keystone,  and Shasta King Mines; Shasta County, California

The Balaklaia, Keystone, and Shasta King Mines are inactive mines that lie within the Shasta/Trinity
National  Forest, approximately four miles west of Shasta Dam.  All three mines are owned by Silver
King Mines,  Inc., of Salt Lake City, Utah. Copper, zinc,  silver, and gold are mined at these sites.

Acid mine drainage flowing from all three underground mines eventually discharges into Shasta Lake
by way of West Squaw Creek.  Heavy metals and acidic conditions in this flow have resulted in
deterioration  of aquatic life downstream of the mines in West Squaw Creek, and periodically cause
fishkills at the West Squaw CreekyShasta Lake confluence.

Monitoring data at the Balaklaia and Keystone Mines show highly variable flow rates and metals
concentrations (see Tables 1-7 and 1-8).  Discharges from  the Balaklaia Mine currently contribute
about 30 to 90 percent of the heavy metals in West Squaw Creek.  However, some  of this pollution is
the result of water coming from the Keystone Mine.  About 20 to 500 gpm are discharged from the
Keystone mine and joins the discharge from the Balaklaia Windy Camp mine.

Prior to sealing, the discharge from the Weil portal at the Balaklaia Mine had a pH  of 2 and metal
concentrations of 170 mg/1 of copper and 180 mg/1 of zinc. Discharges from the Shasta King Mine
are thought to account for a maximum of 6.4 percent of the total heavy metals in West Squaw Creek,
although it is impossible to sample the discharge during periods of high runoff (Advanced
Environmental Consultants, Inc.,  1983).
                                             1-36

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                                                          Mining Industry Profile: Lead-Zinc
             Table 1-7.  Balaklala Mine Typical Metal Concentrations of Discharge
Constituent
pH
Copper
Zinc
Cadmium
Iron
Concentration
2.6 to 2.9
10 to 15 mg/1
6 to 30 mg/1
0.1 mg/1
50 to 240 mg/1
Source:  Advanced Environmental Consultants, Inc., 1983




             Table 1-8.  Keystone Mine Typical Metal Concentrations of Discharge
Constituent
PH
Copper
Zinc
Cadmium
Iron
Concentration
2.9 to 3.8
2 to 13 mg/1
3 to 21 mg/1
0.02 to 0.12 mg/1
9 to 140 mg/1
Source:  Advanced Environmental Consultants, Inc., 1983.
                                           1-37

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                                                            Mining Industry Profile:  Lead-Zinc
1.7    CURRENT REGULATORY AND STATUTORY FRAMEWORK

Lead and zinc mining activities must meet the requirements of both Federal and State regulations.
Environmental statutes administered by EPA or the states, such as the Clean Water Act (CWA) and
the Clean Air Act (CAA), apply to mining sites regardless of the status of the land on which they are
located. The extent to which other Federal regulations apply depends on whether a mining operation
is located on federally-owned land. Federal regulations exist for  operations on lands managed by the
U.S. Bureau of Land Management (BLM), the U.S. Forest Service (FS), the U.S. Fish and Wildlife
Service (FWS), the National Park Service (NFS), and other land  management  agencies. In addition,
the U.S. Army Corps of Engineers has promulgated rules for construction and mining activities that
have the potential to affect wetlands and navigable waters.  Finally, operations must comply with a
variety of state requirements, some of which may be more stringent than Federal requirements.

Federal water quality regulations establish specific effluent guidelines for point source discharges to
surface waters from lead-zinc mining operations.  In contrast, air quality standards do not specifically
address lead-zinc emissions from mining operations, but do address paniculate matter from metallic
mineral processing plants and various emissions from lead and zinc smelters.   Federal land
management agencies have general mining regulations that are not specific to individual (nonfuel)
mineral types. Similarly, State regulations do not usually target specific minerals, but regulate
nonfuel mining in general.

This section summarizes the existing Federal regulations that may apply to lead-zinc mining
operations. It also provides an overview of the operational permitting (including reclamation and
waste management) and water quality, air quality, and wetlands protection regulations in two major
lead-zinc producing states - Alaska and Missouri. These states were chosen since the vast  majority of
lead mining takes place in Missouri, while one of the newest zinc mines in the U.S. operates in
Alaska.

1.7.1  Environmental Protection Agency Regulations

1.7.1.1    Resource Conservation and Recovery Act

The EPA implements the Resource Conservation and Recovery Act (RCRA) to protect human health
and the environment from problems associated with solid and hazardous wastes.  Mining wastes are
included in the Act's definition of solid waste and in  1978, when  EPA proposed regulations for the
Subtitle C hazardous waste program, special management standards were proposed for mining wastes.
However, in  1980, RCRA was amended to include what is known as the Bevill Amendment (RCRA
§3001(b)(3)(A)).  The Bevill Amendment provides a conditional exclusion from RCRA Subtitle C
hazardous waste requirements for wastes from the extraction, beneficiation, and processing of ores
and minerals.
                                             1-38

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                                                             Mining Industry Profile:  Lead-Zinc
The exemption was conditioned upon EPA's preparation of a report to Congress on the wastes and a
subsequent regulatory determination as to whether regulation under Subtitle C was warranted.  EPA
met its statutory obligation with regard to extraction and beneficiation wastes with the 1985 Report to
Congress:  Wastes from the Extraction and Beneficiation of Metallic Ores,  Phosphate Rock, Asbestos,
Overburden from  Uranium Mining and Oil Shale.  In the subsequent regulatory determination (51 FR
244%; July 3, 1986), EPA indicated that extraction  and beneficiation wastes  (including lead and zinc
mining and milling wastes) should not be regulated as hazardous but should be controlled under
Subtitle D.

EPA subsequently studied processing (i.e., smelting and refining) wastes and in  1990 submitted its
Report to Congress on Special Wastes from Mineral Processing. Slag from the primary processing of
lead and of zinc were the only lead-zinc  processing wastes retained within the Bevill exemption and
addressed in the  1990 Report to Congress.  In the subsequent regulatory determination (56 ££
27300),  EPA determined that regulation of these wastes under Subtitle C was not warranted.  All
other  lead-zinc processing wastes  may be subject to Subtitle C if they are listed by EPA as hazardous
wastes or if they exhibit one or more characteristics  of a hazardous waste.

In response to a court order, EPA, in September 1988 (53 FR 35412), listed two lead-zinc wastes as
hazardous wastes:  surface impoundments solids contained in and dredged from surface impoundments
at primary lead smelting facilities  (K065) and sludge from treatment of process waste water and/or
acid plant biowdown from primary zinc production (K066). In July 1990, however, a Federal  Court
of Appeals remanded these listings (AMC v. EPA, 31 ERC 1935).

As discussed above, wastes from the extraction and beneficiation of ores and  minerals are generally
excluded from RCRA Subtitle C requirements by the Bevill Amendment. EPA interprets this
exclusion to encompass only those wastes uniquely associated with extraction and beneficiation
activities; die exclusion does not apply to wastes that may be generated at a facility but are not
uniquely related to mineral extraction or beneficiation.  For example,  waste solvents that meet the
listing requirement as a hazardous waste under 40  CFR §§261.31 and are generated at an extraction
or beneficiation facility by cleaning metal parts (i.e., activities not uniquely related to extraction and
beneficiation) are considered hazardous wastes and regulated as such.  These wastes must be managed
as any other hazardous waste, subject to  the Federal  requirements in 40 CFR  §§260 - 271 (or State
requirements if the State is authorized to implement the RCRA Subtitle C program), including those
for manifesting and disposal in a permitted facility.

1.7.1.2    Clean Water Act

Under Section 402 of the CWA (33 USC §1342), all point-source discharges to waters of the United
States from industrial and municipal sources must be permitted under the National Pollutant Discharge
Elimination System (NPDES).  A  point source is defined as any discrete conveyance, natural or
                                             1-39

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                                                             Mining Industry Profile: Lead-Zinc
manmade, including pipes, ditches, and channels. NPDES permits are issued by EPA or delegated
States.

Effluent limits imposed on an NPDES permittee are either technology-based or water quality-based.
National technology-based effluent guideline limitations have been established for discharges from
active lead-zinc mines under the Ore Mining and Dressing Point-Source Category (40 CFR  Part 440
(Subpart J)).  These regulations address point-source discharges from all types of lead-zinc extraction
processes  including open-pit, underground, and froth-flotation.  Discharges from regulated operations
must meet Best Available Technology/Best Practicable Technology (BAT/BPT) standards for
cadmium, copper, lead, mercury, zinc, suspended solids, and pH.  The specific effluent standards for
these pollutants are summarized  in Table 1-9 (for mines) and Table 1-10 (for mills).  Permit writers
can establish  additional limitations at a specific facility based on Best Professional Judgment (BPJ).
For pollutants not addressed by these guidelines, effluent limits are based solely on BPJ.

          Table 1-9.  BPT and BAT Standards Ore Mining and Dressing Point Source
                      Category (milligrams  per liter)
POLLUTANT
Cadmium
Copper
Lead
Mercury
Zinc
Total
Suspended
Solids
pH
BPT Maximum
for 1 0*7
N/A
0.30
0.6
0.002
1.5
30
6.0 to 9.0
BPT Average of Dafly Values
for 30 Consecutive Days
N/A
0.15
0.3
0.001
0.75
20
6.0 to 9.0
BAT Maximum
for 1 Day
0.10
0.30
0.6
0.002
1.5
N/A
N/A
BAT Average of Daily
Values for 30
Consecutive Days
0.05
0.15
0.3
0.001
0.75
N/A
N/A
Source:  40 CFR Part 440 Subpart J

The permit writer also must ensure that the NPDES permit will protect water quality.  Table 1-11
identifies the Federal surface water quality criteria for lead and zinc established by EPA's Office of
Water (from EPA's 1988 "Quality Criteria for Water").  Individual States are required to adopt water
quality criteria at least as stringent as the Federal levels.  The application of these criteria is based on
the designated use of a specific receiving water (e.g., drinking water supply, aquatic life, and/or
recreational use).  Also, each State has been required to develop instream  water quality standards to
protect the designated uses of receiving waters.
                                               1-40

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                                                            Mining Industry Profile:  Lead-Zinc
   Table 1-10.  BPT and BAT Standards for Lead and Zinc Mills Using Froth-Rotation Alone
               or in Conjunction with Other Benefication Processes (milligrams per liter)
POLLUTANT
Cadmium
Copper
Lead
Mercury
Zinc
Totil
Suspended
Solid*
PH
BPT Maxkanni
for 1 Day
0.10
030
0.6
0.002
1.0
30
6.0 to 9.0
BPT Average of Daily Values
for 30 Consecutive Days
0.05
0.15
0.3
0.001
0.5
20
6.0 to 9.0
BAT Maxim urn
for 1 Day
0.10
0.30
0.6
0.002
1.0
N/A
N/A
BAT Average of Daily
Values for 30
Consecutive Days
0.05
0.15
0.3
0.001
0.5
N/A
N/A
Source: 40 CFR Part 440 Subpart J

          Table 1-11. Federal Water Quality Criteria and Drinking Water Standards
                      On micrograms per liter)

Lead
Zinc
Fresh
water
Acute
82
120
Fresh
water
Chronic*
3.2
110
Marine
Acute*
140
96
Marine
Chronic*
5.6
86
Drinking Water Standard
50 (Action Level)
5000 (MCL)
"Standards are relative to water hardness.  Standards shown are for hardness 100.

Source: U.S. EPA, Office of Water,  1986

NPDES permit writers must determine whether technology-based effluent limitations are adequate to
ensure that applicable water quality standards are met.  Where technology-based limits are not
sufficiently stringent, water quality-based effluent limitations must be developed.  As a result, an
NPDES permit may include technology-based effluent limitations for some pollutants and water
quality-based effluent limitations for other pollutants.

Contaminated storm water runoff from some mining operations has been documented as causing water
quality degradation. In the past, storm water discharges received limited emphasis under the NPDES
program.  However, EPA recently promulgated National regulations (55 £R 47990; November 16,
1990) that specifically address point-source discharges of storm water from industrial facilities,
                                            1-41

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                                                             Mining Industry Profile:  Lead-Zinc
including active and inactive/abandoned mine sites. These regulations require NPDES permits for all
discharges of contaminated storm water from mine sites.  Storm water requirements will be applied to
mine sites either individually (i.e., through individual NPDES permits) or in larger groups (i.e.,
through general NPDES permits applicable to similar operations, possibly in particular areas).

Some discharges from mine sites do not meet the traditional definition of a "point source discharge."
For example, runoff from overburden and mine development rock piles, tailings piles, and other mine
areas often is not controlled through a discrete conveyance.  As a result,  these kinds of discharges
have frequently been considered nonpoint source discharges.  Under Section 319 of the CWA, States
are required to prepare nonpoint source assessment reports and to develop programs to address
nonpoint sources on a watershed-by-watershed  basis.  Each State must report to EPA annually on
program implementation and resulting water quality improvements.

1.7.1.3   Clean Air Act

Under the CAA (42 USC  § 4209, Section 109), EPA established national primary and secondary
ambient air quality standards for six "criteria" pollutants.  These are known as the National Ambient
Air Quality Standards (NAAQS). The NAAQS set maximum concentration limits for lead, nitrogen
oxides, sulfur dioxide, carbon monoxide,  suspended paniculate matter of less than 10 microns in
diameter, and ozone.  To attain the air quality goals set by the CAA, States and local authorities are
given the responsibility for bringing their regions into compliance with NAAQS. In addition, States
may promulgate more stringent ambient air quality standards.  The current NAAQS for lead is 1.5
micrograms per cubic meter (/xg/m3) maximum arithmetic mean average over a calendar quarter (40
CFR §50.12). EPA is currently considering lowering this standard.

EPA also has promulgated air quality regulations that specifically address smelting operations. Since
this report does not evaluate mineral processing, no further discussion of those rules are found in this
report.

New Source Performance Standards, authorized under CAA §111, also have been promulgated for
metallic mineral processing plants (40 CFR  §60(LL)).  A  processing plant is defined as "any
combination of equipment that produces metallic mineral concentrates from ore; metallic mineral
processing commences with die mining of the ore."  However, all underground processing facilities
are exempt from NSPSs.  Also, NSPS paniculate emission concentration  standards apply only to stack
emissions.  NSPSs require operations to contain stack-emitted paniculate matter in excess of 0.005
grams per dscm.  In addition, stack emissions must not exhibit greater than 7 percent opacity, unless
the stack emissions are discharged from an affected facility using a wet scrubbing emission control
device.  However, on or after 60 days following the achievement of the  maximum production rate
(but no later than 180 days after initial startup), operations must limit all process fugitive emissions
(meaning fugitive dust created  during a processing operation though not released through a stack) to
10 percent opacity.

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                                                             Mining Industry Profile:  Lead-Zinc
 Prevention of Significant Deterioration (PSD) provisions of the CAA are intended to ensure that
 NAAQS are not exceeded.  Under this program, new sources are subject to extensive study
 requirements if they will emit (after controls are applied) specified quantities of certain pollutants.
 Few mining sites are subject to PSD requirements since they typically are not predicted to emit
 sufficient quantities.

 State ambient  air standards promulgated to meet or exceed Federal NAAQS are generally maintained
 through permit programs that limit the release of airborne pollutants from industrial and land
 disturbing activities. Fugitive dust emissions from mining activities may be regulated through these
 permit programs (usually by requiring dust suppression management activities).

 Currently, only the six criteria pollutants are regulated by NAAQS. Several other pollutants are
 regulated under  National Emission Standards For Hazardous Air Pollutants (NESHAPs).  NESHAPs
 address health concerns that are considered too localized to be included under the scope of NAAQS.
 While zinc and zinc oxide are listed under 40 CFR §61.01(b) as pollutants under consideration for
 possible health effects, they have not been listed as hazardous pollutants under the NESHAP program.

 Under the 1990  Amendments to the CAA, Congress required EPA to establish technology-based
 standards for a variety of hazardous air pollutants, including lead compounds.  In November 1993,
 EPA published a list of source categories, and a schedule for setting standards for the selected
 sources.  Furthermore, if a source emits more than 10 tons per year of a single hazardous air
 pollutant or more than 25 tons per year of a combination of hazardous air pollutants, the source is
 considered a "major source."  Major sources are required to  use the maximum available control
 technology (i.e., BAT) to control the release of the pollutants (CAA Section 112).

 1.7.2   Department of the Interior

 1.7.2.1    Bureau of Land  Management

 Lead and  zinc operations on Federal lands are carried out under two basic systems:  leasing, pursuant
to statutes that grant general authority applicable to specific classes of land, and mining claims under
the 1872 Mining Law.

The authority to manage mineral activities on Federal lands in general is vested in the Secretary of the
Interior, who has delegated this authority to BLM (Section  301  of the Federal Land Policy and
Management Act [FLPMA] of 1976, 43 §USC  1731).  The BLM's-general leasing statutes,  the
Mineral Leasing Act and the Mineral Leasing Act for Acquired Lands do not authorize the leasing of
hardrock minerals (such as lead and zinc). "Hardrock minerals," defined in the BLM regulations in
43 CFR 3500iO-5(n) (1989), are those that are subject to location under the 1872  Mining Law.
                                             1-43

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                                                             .Mining Industry Profile:  Lead-Zinc
Leasing of hardrock minerals, including lead and zinc, by the BLM  is conducted pursuant to the BLM
regulations at 43 CFR Part 3500. These regulations provide for the issuance of prospecting permits
and for three types of leases:  preference right leases, competitive leases, and  noncompetitive leases.
A prospecting permit entitles  the holder to prospect on and explore Federal lands to determine the
existence or workability of a hardrock deposit.  If the permittee discovers a valuable mineral deposit,
he or she  is entitled to a preference right lease. Lands where the existence or workability of a
valuable mineral deposit is already known, are subject only to competitive leasing, except if the
deposit extends from an adjoining lease, either Federal or private, in which case the lands may be
leased noncompetitively.

The BLM will also issue permits and leases for hardrock minerals on those public domain lands
where the surface is administered by an agency outside of the U.S. Department of the Interior;
however,  the DOI will first consult with the surface managing agency (e.g., the FS).  For acquired
lands, and for public domain  lands where required by law, permits or leases will be issued only with
the written consent of the appropriate official  of the surface managing agency.  The permits or leases
will be subject to such conditions as that official may prescribe.

As of 1989, all existing Federal lead-zinc mineral leases were located in Missouri. Federal lead-zinc
leasing in Missouri is generally conducted on lands managed by the FS pursuant to the authority of
Section 402 of Reorganization Plan No. 3 of  1946, 60 Stat. 1099; 5 U.S.C. Appendix (1988).
However, this Act transferred certain functions of the Secretary of Agriculture over specific classes of
national forest lands to the BLM.  Under this authority,  the BLM may issue hardrock and other
permits and leases on certain National Forest System lands, but only when the FS, acting for the
Secretary of Agriculture, advises that the leases or permits will not interfere with the purposes  for
which the lands were acquired.  Leases and permits are  also fully subject to stipulations imposed by
the FS to protect the lands.

The FS does not currently have regulations covering issuance of leases, or for operations conducted
under such leases. Instead, the FS approves permits and leases, and imposes stipulations on a  case-
by-case basis subject to general management standards in the FS Internal Manual.

Any lead-zinc leases issued under other statutes authorizing the issuance of hardrock leases on  Federal
lands would also be subject to the BLM hardrock leasing regulations in 43 CFR  §§3500, 3560.
These other hardrock leasing authorities, applicable to certain other FS areas and certain areas under
the jurisdiction of the National Park Service (NPS), are listed in 43 CFR §§3500.0-3.

The BLM is also generally responsible for management of operations on mining claims located
pursuant to the  1872  Mining Law.  However, in  1876, an amendment to the Mining law was passed
that made the law not applicable in the state of Missouri (30 USC §49).  Mining claims for lead and
                                               1-44

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                                                             Mining Industry Profile:  Lead-Zinc
zinc, therefore, cannot be located in Missouri.  However, lead and zinc are both subject to location
under the Mining Law in most other public domain States.

Under the 1872 Mining Law, a person has a statutory right to go on the open (unappropriated and
unreserved) public lands of the United States for the purpose of prospecting for, exploring,
developing, and extracting minerals.   The discovery of a valuable mineral and proper location of a
claim creates broad possessory rights. In general, the BLM has authority under FLPMA to regulate
mining claims to prevent "unnecessary and undue degradation" of the Federal lands and  resources
involved.

The BLM's general surface management regulations governing mining claim operations, which
include lead and zinc operations, are found in 43 CFR  §3809.  These regulations cover general
operating and reclamation standards, bonding requirements, environmental review requirements, and
remedies for  noncompliance.  The regulations establish three general use categories for mining
operations, each subject to different levels of oversight b-y the BLM.  These categories are casual use
operations (i.e., those that normally result in only negligible disturbance of Federal lands and
resources and that require no prior notice to  or  approval from the BLM);  notice-level operations (i.e.,
those that involve disturbance of five acres or less, for  which the operator must notify the BLM prior
to commencing surface disturbing activities); and plan-level operations (i.e., disturbances of greater
than five acres, and operations in some specified areas, for which the operator must obtain BLM
approval of a plan of operation prior to commencing activity).

All mining operations of whatever level are subject to monitoring by the BLM to ensure that no
unnecessary or undue degradation is occurring,  and all  operators are responsible for reclaiming the
area of their  claim. Activities conducted under  either a notice  or an approved plan of operation are
subject to regulatory standards governing access, waste disposal, and reclamation.

The current BLM policy concerning bonding requirements for operations under the Mining Law is
established by an internal BLM Instruction Memorandum issued on August 4, 1990. This Instruction
Memorandum sets standards for reclamation  bonds for all plan-level operations, including acceptance
of State bonds in lieu of a BLM bond  if the State bond  is within 75 percent of BLM's estimated
reclamation costs or BLM's bond requirements.  A bond will not ordinarily be required for notice-
level operations or for casual use.  The BLM will, however, require any operator with a history of
noncompliance to post a 100 percent reclamation bond, regardless of existing State bonds,

1.7.2.2    National Park Service

Limited authority exists for leasing of hardrock  minerals on certain areas under the jurisdiction of the
NFS. Hardrock leasing, where allowed, is regulated under the BLM's general hardrock leasing
regulations in 43 CFR §§3500, 3560,  discussed above,  as well as under special provisions in 43 CFR
                                              1-45

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                                                             Mining Industry Profile:  Lead-Zinc
§§3582, 3583.  The consent of either the NPS Director or the Secretary of Agriculture, depending on
the area, is required prior to lease issuance.

The Mining in the Parks Act of September 28, 1976, prohibits the location of new mining claims in
National Parks and Monuments.  The NPS has the authority under this Act to regulate and control
operations on existing claims,  and on claims already patented, to ensure that any valid existing rights
under them are exercised in a  manner consistent with the purposes for which the particular NPS area
was created.  The NPS regulations in 36 CFR §9(A) govern surface and water protection, access
permits, claim recordation, assessment  work, and  reclamation. Operators must receive approval of a
plan of operation from the appropriate Regional Director prior to commencing activity. All
operations, once approved, must be covered by either a reclamation  bond or a security deposit.

1.7.2.3   Fish and Wildlife Service

The FWS manages a variety of lands, including those within the National Wildlife Refuge System.
Leasing of Federal minerals on FWS lands is allowed only where compatible with the major purposes
for which a specified area was established, and is  then fully subject to the imposition of restrictive
lease terms pursuant to the BLM's leasing regulations.

The prospecting, locating, or filing of mining claims on  FWS  lands  is generally prohibited.  Where
mineral rights have been vested in private parties prior to the acquisition of the lands by the United
States, the FWS regulations (in 50 CFR §29) require that, to the greatest extent possible, all
exploration, development, and production operations be conducted in such a manner as to prevent
environmental and other damage to the lands, waters, facilities, and  vegetation of the area.
Operations must comply with applicable environmental laws, and all wastes and contaminating
substances must be kept to the smallest practicable area.  Upon cessation of operations, the area must
be restored as nearly as possible to its original condition. The FWS regulations do not impose
specific technical operational or reclamation standards, and do not specify bonding requirements.

1.73   Department of Agriculture

1.7.3.1   Forest Service

As described above, limited authority exists  for leasing hardrock minerals,  including lead and  zinc, on
certain specified lands managed by the  Forest Service (FS). Hardrock leases on FS lands can
generally be issued by BLM only with  FS consent and are also subject to imposition of protective
stipulations by the FS.  Since the FS does not currently have regulations governing operations under
hardrock leases issued by the BLM on  FS lands, consent to lease and applicable stipulations are
determined on a case-by-case basis. The leases are otherwise governed by applicable BLM
regulations found in 43 CFR §3500, 3560.
                                              1-46

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                                                              Mining Industry Profile:  Lead-Zinc
The FS does, however, have regulations governing operations under mining claims on FS lands.  The
FS  regulations (36 CFR §228), rather than the BLM's Mining Law regulations, govern activities
under mining claims on FS lands.  These FS regulations generaJly mandate diat operations under
mining claims be conducted to minimize adverse environmental impacts in national forests.

The FS regulations are similar to the BLM regulations and provide for FS consultation with
appropriate agencies of the Department of the Interior in reviewing technical aspects of proposed
plans of operation.  The FS regulations require that persons proposing to initiate any operations that
might cause disturbance to surface resources must  first file a notice of intent to operate with  the
District Ranger having jurisdiction over the area to be affected.  Upon a finding by the District
Ranger that the operations will likely cause significant disturbance of surface resources, the operator
must submit a proposed plan of operation.  Neither a notice of intent to operate nor a proposed plan
of operation is required for the following activities: locations or markings of mining claims; mineral
prospecting or sampling that will not cause significant surface disturbance; operations that do not
involve the use of mechanized equipment or the cutting of trees; or uses that will be confined to
existing roads.

Proposed plans of operation must include a thorough description of the proposed site, the nature of
the proposed operations, and measures for  meeting environmental protection requirements. The FS
will conduct an environmental analysis of the proposed plan of operation, and if necessary, will
prepare a National Environmental Policy Act (NEPA) environmental impact statement (EIS).

The regulations require that all operations be conducted to minimize, where feasible, adverse
environmental impacts on  national forest resources, and to comply with applicable environmental
laws. The regulations specify standards for reclamation and provide that the District Ranger may
require a reclamation bond.

1.7.4   State Programs

1.7.4.1    Alaska

Alaska's environmental programs are managed by the Alaska Department of Environmental
Conservation (DEC). Although the State of Alaska has only one lead-zinc mine, the Red Dog  Mine
located 52 miles from the  northwestern coast of Alaska, this mine is one of the world's largest lead-
zinc mines.  Because of the sensitive environment, and because it is a massive sulfide deposit, the
mine has the potential for  nosing significant environmental impacts.if not carefully managed.  The
concentrate produced by this operation will be exported for processing to Canada, Europe, and the
Far East (Alaska Division of Geological and Geophysical Surveys, 1989).  Regulations to minimize
the environmental impacts of the Red Dog mine are a mix  of State, Federal, and local authorities.
The permitting of the mine involved three distinct parts: the mine itself, which is located on private
                                              1-47

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                                                            Mining Industry Profile:  Lead-Zinc
land; the access corridors, which are located on Federal land; and the loading facility and port, which
are located on private and State land.

The mine and associated facilities (mills, housing, etc.) are located on lands owned by the NAN A
Corporation,  a regional native corporation under the Alaska Native Claims Settlement Act.  The
operator of the mine, Cominco, Ltd., has an agreement with the NAN A Corporation that includes,
among other things, requirements for reclamation of the site and the protection of wildlife and
subsistence resources along the road corridor and the port site.  These requirements between a private
land owner and the mine operator are not discussed here; rather, this discussion is limited to the State
and Federal authorities in place at the mine.  Of note is the fact that the mine was not required to
develop a closure plan or to post reclamation bonds.

Waste Water Discharge

The Alaska DEC has authority to regulate discharges.  Because the State of Alaska does not have a
delegated NPDES program, the DEC has the following options to regulate discharges:

        •  Issue a Waste Water Discharge Permit under State authority

        •  Certify or deny  certification to the NPDES permit

        •  Take no action

At the Red Dog Mine, DEC issued certification of EPA's NPDES permit and, at a later date, issued a
separate permit for nonpoint-source discharges (Wightman, 1991).

The mine also has a  "Wetlands Permit" issued by the U.S. Army Corps of Engineers in consultation
with the FWS.  Many of the typical land management agency concerns (reclamation, slope stability,
etc.) are considered in the wetlands permit.

Fisheries Protection

The Alaska Department of Fish and Game (ADF&G) has the authority to protect fisheries when
development threatens to restrict fish access through a  water body, or when andronomous fish
(salmon or steelhead trout) or their habitats are threatened in any manner.  The ADF&G issued many
"Title 16" permits to maintain water flow, water quality, and habitat in fish-bearing streams
throughout the project area.

Other State Permits

In addition to the permits already discussed, Alaska has other permit requirements, including a Dam
Safety Permit and a right-of-way permit, both issued by the Alaska Department of Natural Resources.
The Dam Safety Permit requires certification that the tailing dam is structurally sound and can
                                              1-48

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                                                              Mining Industry Profile:  Lead-Zinc
withstand storm water events.  The right-of-way permit provides for design standards to minimize
adverse effects, primarily to prevent nonpoint-source pollution.

1.7 4.2    Missouri

In October, 1990, the Missouri Department of Natural Resources (DNR) proposed rules governing
the mining of metallic minerals in response to the State's Metallic Minerals Waste Management Act
(MMWMA), passed on July 6, 1989 (Missouri Department of Natural Resources,  1991).  The rules
implementing the MMWMA  are published in the State's Code of Regulations and took effect on April
29, 1991.  According to the rules, metallic mineral mining activities, including lead-zinc operations,
will be regulated through Metallic Minerals Waste Management (MMWM) permits during their active
lives and through closure and post-closure.  To obtain  a permit, operations must comply not only with
the new requirements under the MMWMA, but also with all other applicable environmental quality
programs and permits.  Compliance with other program requirements may be considered a condition
of me  MMWM permit.

Permit Applications

The State regulations require MMWM permit applicants to submit detailed information on site
characteristics, including maps  of the site and surrounding properties, with potential waste
management areas specifically designated.  Geological  features that could relate to surface and ground
water quality or dam stability must also be included on maps.  Applications must include information
on all known water wells and uses in the area, and a geological cross section of the area showing well
depths, the presence of ground  water, and other  information.

Closure and inspection-maintenance plans are required  with permit applications. Closure plans must
address the design, construction, and maintenance of waste control structures, tailing dams, waste
stockpiles, and supporting facilities. Mine operators must also obtain State dam safety permits
through the State's Division of Geology and Land Survey if tailings dams  (or other dams)  reach 35
feet or more in height.  Tailings piles must be sloped and graded, and repairs must be made to sloped
faces that experience erosion.  The methods for long-term control of surface water runoff and the
protection of ground water must be included in closure plans.

Site reclamation is ensured through financial assurance measures that prospective operators must
provide as part of the permit application process. Financial assurance must be provided in amounts
up to $1,000 per acre of the waste management area, but not less than $20,000 per permit. Mine
operators have the option of either presenting formal proof of assets held to guarantee reclamation of
the site or setting aside funds in a company-held bond.  Operators are required to update this financial
assurance within 90 days of the close of each succeeding fiscal year.

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                                                             Mining Industry Profile: Lead-Zinc
Under the MMWMA, permit fees ($10,000 at initial application and $2,500 annually thereafter) and
funds from forfeiture of bonds are placed in a "Metallic Minerals Waste Management Fund."  This
fund is used to administer and enforce the MMWMA program and to manage the remediation of
"metallic minerals waste management areas."

Water Quality

The State is authorized to  implement NPDES  program requirements as described in 40 CFR §123(A).
All surface waters in the State are classified according to one or more of seven designated uses. State
water quality standards have been established  to protect each of these designated uses. Lead-zinc
tailings have been specifically identified by the State as one of the five important sources of water
quality degradation.

In addition to  requiring operations to obtain NPDES permits, MMWM permits require mine
operations to implement ground water protection practices.  Operators must submit a ground water
monitoring plan as well as an analysts of background ground water quality, specifications for
monitoring wells, and the  implementation of a ground water sampling program.  Monitoring will
continue throughout the active life of the site, closure, and an inspection-maintenance period.  A
ground water monitoring point must also be established. Water contaminants at this point cannot
exceed standards  established under Missouri law to  meet Federal requirements  for drinking water.

Air Quality

State  air emission requirements and ambient air quality standards are the same as Federal
requirements.  The State has also adopted all  of EPA's NSPS and hazardous air pollutant  standards
given in 40 CFR  §60-61,  including  all the mining industry standards. Mining operations emitting
regulated pollutants must obtain major and minor source permits that specify emission limits.   In
addition to requiring air quality permits as a precondition to obtaining a MMWM permit,  MMWM
permits will specifically require the use of fugitive dust control techniques such as water spraying,
chemical binders, anchored mulches, vegetation, and physical containment.

Wetlands Protection

The State has  no  wetlands protection regulations. Operations impacting wetlands are governed by
Federal regulations.

Abandoned Mine Reclamation

The States's Mine Reclamation and Restoration Rules found at Title 10 of the Missouri Code of State
Regulations established a program for the reclamation of noncoal mine sites that were abandoned
before August 3,  1977.  To qualify for reclamation, these sites must be determined to present a threat
to public health, safety, and welfare. These sites are reclaimed by the DNR using State funds.
                                              1-50

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                                                           Mining Industry Profile: Lead-Zinc
 1.8     REFERENCES

 Advanced Environmental Consultants, Inc.  1983 (June).  Control of Acid and Heavy Metal Discharge
     from Balaklala. Keystone, and Shasta King Mine Sites, West Shasta Mining District, Shasta
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 Alaska Division of Geological and Geophysical Surveys.  1989.  Special Report No. 44:  Alaska's
     Mineral Industry,  1989 (by T.K. Bundtzen, R.C. Swainbank, J.R. Deagen, and J.L.  Moore).

 BeaJI, J.V.  1948 (September).  "Recent Developments in Heavy-Density Separation."  Mining and
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 Beelman, J. 1991. Personal Communication between J. Bee!man, Alaska Department of
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 Bechtel  Corporation. 1977.  "The Black Angel  Mine." In Lead-Zinc Update.  D.O. Rausch, P.M.
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 Camp, Dresser & McKee, Inc.  1989 (July).  Final Feasibility Study Report for the Mill Site Operable
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 Carter, J.   1991a  (February).  Personal Communication between J. Carter, Doe Run Company,
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 Carter, J.   1991b  (March 11). Personal Communication between J. Carter, Doe Run Company,
     Viburnum, MO, and J. Rissing, Science Applications International Corporation.  McLean,  VA.

 CH2M Hill.  1985 (August). Mammoth Mine Water Quality Management Planning Study. Prepared
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 Chandler,  J.W. 1970.  "Exploration, Evaluation, and Development of Lead and Zinc Ore Bodies."
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     Concentrating of Lead and Zinc. D.O. Rausch, P.M. Stephens, Jr. and B.C. Mariacher
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     Inc.

Christiansen, C.R., and J.J. Scott. 1970.  "Mining Systems in the  New Lead Belt of Southeast
     Missouri."  In AIME World Symposium on  Mining and Metallurgy of Lead and Zinc,  Volume I:
     Mining and Concentrating of Lead and Zinc.  New York:  American Institute of Mining,
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Colorado Department of Health, Office of Health Protection.  1986 (April).  Record of Decision for
     the Eagle Mine Superfund Site.  (INVALID ROD - Used for background information only).
     Denver, CO.

Colorado Department of Law. 1985 (December  2). Remedial Investigation - Eagle Mine.
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                                                           Mining Industry Profile:  Lead-Zinc
Considine. D.M. (editor).  1975.  Chemical and Process Technology.  New York: McGraw-Hill
     Book Company.

Cornell, B.  1991  (January 24).  Personal Communication between B. Cornell, Bureau of Mines
     Rolla Research Center, and J. Rissing, Science Applications International Corporation.
     McLean,  VA.

Doe Run Company.  1990 (February).  Fletcher Project: Application for Metallic Minerals Waste
     Management Area Permit.

Doyle, E.N.  1970. "The Sink-Float Process in Lead-Zinc Concentration."  In A/ME World
     Symposium on Mining and Metallurgy of Lead and Zinc, Volume 1: Mining and Concentrating
     of Lead and Zinc.  New York:  American Institute of Mining, Metallurgical, and Petroleum
     Engineers, Inc.

Dunaway, S.M., Jr.  1977.  "Mining Practice at ASARCO's East Tennessee Zinc Mines." In Lead-
     Zinc Update.  D.O. Rausch, P.M. Stephens, Jr. and B.C. Mariacher (editor).  New York:
     American Institute of Mining, Metallurgical, and Petroleum Engineers, Inc.

Ecology and Environment, Field Investigation Team, U.S. Environmental Protection Agency,  Region
     VIII.  1983a (March 14).  Potential Hazardous Waste Site Identification and Preliminary
     Assessment, Sharon Steel Corporation. Denver, CO.

Ecology and Environment, Field Investigation Team, U.S. Environmental Protection Agency,  Region
     VIII.  1983b (March 15).  Report on the Preliminary Assessment/Site Inspection of Sharon Steel
     Corporation.  Denver,  CO.

Envirotech.  1974. Cutting Flotation Costs with Wemco 1 + 1 notation Cells.  Bulletin No. F5-B55.
     Envirotech Corporation.  CAL Central Press.

Fred C. Hart Associates, Inc. 1985 (July).  Focused Feasibility Study for Groundwater Remediation,
     Smuggler Site, Aspen, Colorado. Denver, CO.

Fred C. Hart Associates, Inc.  1986 (March).  Remedial Investigation/Feasibility Study Smuggler
     Mountain Site. Denver, CO.

Fuerstenau, M. C., (editor).  1976.  Flotation,  Volume 2.  New York: Society of Mining Engineers.

Gardiner, C.D., (editor).  1990. American Mines Handbook.  Toronto, Ontario, Canada:  The
     Northern Miner Press Inc.

Gauci, S. 1970.  "A Comparison of Ore Dressing Practices at Broken Hill, Australia."  In A1ME
     World Symposium on Mining and Metallurgy of Lead and Zinc, Volume I:  Mining  and
     Concentrating of Lead and Zinc. New York:  American Institute of Mining, Metallurgical, and
     Petroleum Engineers, Inc.

Hustrulid, W.A., (editor). 1982.  Underground Mining Methods Handbook.  New York:  Society of
     Mining Engineers.
                                            1-52

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                                                           Mining Industry Profile:  Lead-Zinc
Idaho Bureau of Mines and Geology.  1963.  The Coeur d'Alene Mining District in 1963; Pamphlet
     No.  133.  Boise. ID.

Krai, Steve.  1992 (January).  "Red Dog: Cominco's arctic experience pays off again."  In Mining
     Engineering. 44(1): 43.]

Michaelis, H.,  (editor).   1990/1991.  Randol Mining Directory.  Golden, CO:  Randol International
     Ltd.

Mine Safety  and Health Administration.  1988.  Closed Metal/Nonmetal Mine Employment and
     Address Data Tape.  Unpublished.  Washington, DC.

Missouri Department of Natural Resources.  1991 (April 29).  Rules of the Department of Natural
     Resources, Title 10, Division 45 (published in response to the Metallic Minerals Waste
     Management Act).  Jefferson City,  MO: Secretary of State's Office, Administrative Rules
     Division.

National Institute for Occupational Safety and Health. 1990 (August 27).  National Occupational
     Health  Survey of Mining: Lead-Zinc Report.  Unpublished.  Morgantown, WV.

Oklahoma Water Resources Board.  1981. Summary of Data Collected by Governor's Tar Creek Task
     Force Regarding Groundwater Discharge From Abandoned Lead and Zinc Mines of Ottawa
     County, Oklahoma, December 1979 to March 1981.  Oklahoma City,  OK.

Ott Water Engineers. 1982 (October). Alternatives for Control of Toxic Metal Discharges from
     Representative  Surface Areas at Iron Mountain Mine, near Redding, California. Prepared for
     the California Regional Water Quality Control Board, Central  Valley Region.

Sastry, K. V. S., (editor).  1988.  "Column Flotation "88".  In Proceedings of an International
     Symposium on  Column Flotation. New York:   Society of Mining Engineers.

Schwandt, A.J.W.   1970.  "The Magmont Operation." In AIME  World Symposium on Mining and
     Metallurgy of Lead and Zinc, Volume 1: Mining and Concentrating of Lead  and Zinc.  New
     York:  American Institute of Mining, Metallurgical, and Petroleum Engineers, Inc.

SCS Engineers.  1984 (January).  Summary of Damage Sites from the Disposal of Mining Wastes.
     Prepared  for the U.S. Environmental Protection Agency under EPA Contract No.  68-02-3179.
     Reston, VA.

Sharp, F.H.  1976.  "Lead-Zinc-Copper Separation and Current Practice at the Magmont Mill."  In
     Flotation. New York: Society of Mining Engineers.

U.S. Department of Health and Human Services. 1982 (April).  Technological Feasibility of Control
     of Asbestos at Mines and Mills, Task 1  Progress Report, Exposure Profiles.  Washington, DC.

U.S. Department of Health and Human Services. 1990 (June). Preliminary Health Assessment for
     Oronogo-Duemveg Mining Belt, Jasper County, Missouri; CERCUS No. MDD980686281:
     Washington, DC.
                                            1-53

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                                                           Mining Industry Profile:  Lead-Zinc
U.S. Department of the Interior, Bureau of Land Management.  1990.  Public Land Statistics 1989.
     1990-773-003/12.008 Region VIII.  Washington, DC:  GPO.

U.S. Department of the Interior, Bureau of Mines.  1939 (December).  Report of Investigations 3469,
     Progress Reports - Metallurgical Division:  Ore Dressing Studies, by F.D. DeVaney and S.M.
     Shelton. Washington, DC.

U.S. Department of the Interior, Bureau of Mines.  1984 (November).  Waste Disposal Activities and
     Practices in the  United States: Copper, Lead, Zinc, Gold, and Silver.  Division of Minerals
     Availability Open File Report, by  L.V. Coppa. Washington, DC.

U.S. Department of the Interior, Bureau of Mines.  1985a.  "Lead" (by W.D. Woodbury). In
     Mineral Facts and Problems,  1985.  Washington, DC.

U.S. Department of the Interior, Bureau of Mines.  1985b.  "Zinc"  (by J.H. Jolly).   In Mineral
     Facts and Problems, 1985. Washington, DC.

U.S. Department of the Interior, Bureau of Mines.  1989.  Mineral Issues 1989:  Competitiveness and
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U.S. Department of the Interior, Bureau of Mines.  1990a.  "Lead" (by W.D. Woodbury). In
     Minerals Yearbook, Volume 1: Metals and Minerals, 1988.  Washington, DC.

U.S. Department of the Interior, Bureau of Mines.  1990b.  "Zinc"  (by J.H. Jolly).  In  Minerals
     Yearbook,  Volume 1:  Metals  and  Minerals, 1988.  Washington, DC.

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     Prinz).  In United States Mineral Resources.  Geological Survey Professional Paper No.  820.
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U.S. Department of the Interior, Geological Survey. 1973b.  "Zinc" (by F.S. Simmons and W.G.
     Prinz).  In United States Mineral Resources.  Geological Survey Professional Paper No.  820.
     Reston, VA.

U.S. Department of the Interior, Geological Survey. 1977 (August). Water Resources Investigations
     77-75:  Effects of Abandoned Lead and Zinc Mines and Tailings PUes on Water Quality in the
     Joplin Area, Missouri.  Washington, DC.
                                            1-54

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                                                          Mining Industry Profile: Lead-Zinc
U.S. Department of the Interior, Geological Survey.  1988. Assessment of Water Quality of Non-
     Coal Mining Areas of Missouri (by B.J. Smith).  Water Resources  Investigation Report No. 87-
     4286.  Washington, DC.

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     Congress:  Wastes From the Extraction and Beneficiation of Metallic Ores, Phosphate Rock,
     Asbestos, Overburden from Uranium Mining and Oil Shale.  EPA/530/SW-85-033.  Washington,
     DC.

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     Special Wastes from Mineral Processing; Summary and Findings Methods and Analyses
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     Doc. No. 440/5-86-001.

U.S. Environmental Protection Agency, Office of Water, Effluent Guidelines Division.  1982 (May).
     Development Document for Effluent Limitations Guidelines and Standards for the Ore Mining
     and Dressing Point Source Category.  Washington, DC.

Weiss, N.L., (editor).   1985. SME Mineral Processing Handbook, Volume 2.  New York: Society
     of Mining Engineers.

White, T.G., and K.L.  Clifford.  1977.  "Milling Lead-Zinc Ores-U.S.A." In Lead-Zinc Update.
     D.O. Rausch, P.M. Stephens, Jr. and  B.C. Mariacher, (editor). New York:  American Institute
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Wightman, P. 1991.  Personal Communication between P. Wightman, permit reviewer with the
     Governor's Office, Fairbanks, AK, and J. Gallagher, Science Applications International
     Corporation.  McLean, VA.
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                                         .Mining Industry Profile: Lead-Zinc
                          APPENDIX 1-A

SPECIFIC FLOTATION ACTIVITIES EMPLOYED FOR POLYMETALLIC ORES
              AND ASSOCIATED PROCESS FLOW SHEETS
                              1-56

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                                                              Mining Industry Profile:  Lead-Zinc
St. Joe-Balmat; Balmat, New York (Figure 1-4)

The St. Joe-Balmat concentrator has introduced a talc pretloat circuit system before flotation.  In this
process, a light alcohol frother is used to float the talc from the ore.  Four 8.4 m3 roughers and two
stages of cleaning  are used to reduce the calcium and magnesium content of the ore by 50 percent.
Some zinc, however, may be lost in this process as well.

The facility uses eight 8.4 m3 flotation cells for roughing and scavenging (White and Clifford, 1977).
Four stages of lead concentrate cleaning are also used.  Sodium ethylene xanthate is used as a lead
collector,  and cyanide is used as a sphalerite depressant. The facility generates a concentrate that is
57 percent grade and is recovered at a rate of 62 percent.

Tailings from the lead circuit are conditioned with copper solution (to activate sphalerite), sodium
ethyl xanthate, a collector, frother, and lime to float zinc minerals.  Three stages of zinc concentrate
cleaning are also used.  Zinc concentrate is generated at the facility at a grade of 58.7 percent and is
recovered at a rate of 92.8 percent.

Magmont  Mill; Bixby, Missouri (Figure  1-5)

At the Magmont facility, lead and copper minerals are first floated together in bulk concentrate in a
series of six roughers and five scavengers (Sharp, 1976).   An 11 cell cleaner circuit is subsequently
employed. The cleaned bulk concentrate is then sent to a copper separation circuit where it is treated
with sulfur dioxide and starch to depress the lead minerals. The copper minerals are floated and
cleaned three  times to generate a final copper concentrate.  The underflow from the float is the final
lead concentrate.

The tailings from the copper-lead roughers, and sometimes the tailings from the copper-lead
scavengers, are treated with  copper sulfate and floated to generate a zinc concentrate. The
concentrate then undergoes four stages of cleaning to produce the final  zinc concentrate.

Kerramerican-Blue Hill; Blue Hill, Maine

The Kerramerican-Blue Hill  zinc concentrator first uses thirty 1.12 m3 flotation ceils for copper
roughing and  scavenging (White and Clifford, 1977).  Reagents, such as Z-200, Z-242, and Z-3501
(collectors) and sodium sulfite (zinc depressant) are used to produce copper concentrate.

The tails from the copper flotation process feed the zinc flotation system.  A total of 32 cells are used
in the zinc circuit; 16 1.4 m3 cells are used for roughing and 16 1.1 m3 are used for zinc scavenging.
This is followed by two stages of zinc concentrate cleaning.  The facility generates a zinc concentrate
that is 53 percent  grade and  is recovered at a rate of 93 percent.
                                               1-57

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oo
"8

 2
 a

 I

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                                     Mining Industry Profile: Lead-Zinc
                                  ZlM
Figure 1-5.  Flow Sheet of the Magmont Concentrator
                       1-59

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                                                             Mining Industry Profile:  Lead-Zinc
Doe Run Company  Brushy Creek Concentrator; Viburnum, Missouri

The St. Joe-Brushy Creek facility uses eight 8.4 mj flotation cells for lead roughing and eight 1.7 m
machines for concentrate cleaning and recleaning (White and Clifford, 1977). Sodium isopropyl
xanthate is used as a lead collector and zinc sulfate as a zinc depressant.  The facility generates a lead
concentrate that is over 74 percent grade and is recovered at a  rate of 97 percent.  Copper is also
produced as a byproduct of lead-copper  flotation.

Tailings from the lead circuit are conditioned with a copper reagent, Z-200, and a frother in
preparation for zinc flotation.  Six 8.4 m3 flotation cells are used for zinc roughing and nine  1.7 m
machines are used for three stages of zinc cleaning.

ASARCO  Young Mill; Mascot, Tennessee

The ASARCO Young Mill uses  reagents such as sodium aerofloat, aerofloat 211, and copper sulfate
in nine 8.4 m3 flotation cells for zinc scavenging (White and Clifford,  1977). Two stages of zinc
concentrate cleaning are also used.  The facility generates a zinc concentrate that is 59.6 percent
grade and is recovered at a rate of 91 percent.
                                              1-60

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                                                                Mining Industry Profile:  Lead-Zinc
 FEED
               LEAD
ZINC
             .FINAtlEAO  •*
              CONCENTRATE
   FINAL M»C
   CONCENTRATE
Figure 1 - Pilot Column Flotation Tuts at Polaris
                                                                                    •TAILS
e

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^2-_
In MO L
1

IS' 1
PILOT FIN
COLUHN ^
— TAIL 1
r— -R.C
                                                                                       CONCENTRATE
                                                                                LEACH
                            Figure 3 - Pilot Column Flotation CaM at °lne Po.nt
                              FINAl
                               CONCEKTRATE
Figure 5 • PHot Coajnw Rotation Tt
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                                          Mining Industry Profile:  Lead-Zinc
                         APPENDIX 1-B




                     NPL SITE SUMMARIES




 RELATED TO LEAD AND ZINC EXTRACTION AND BENEFICIATION




           (from "Mining Sites on the National Priorities List,




NPL Site Summary Reports Volumes I-V, Environmental Protection Agency,




                         June 21, 1991.)
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                                                            Mining Industry Profile:  Lead-Zinc
IRON MOUNTAIN,  SHASTA COUNTY, CALIFORNIA

Operating History

The Iron Mountain Mine site is a 4,400-acre underground and open-pit mine complex in the
southeastern portion of the Klamath Mountains in the West Shasta Copper-Zinc Mining District, nine
miles northwest of Redding, California.  The mine is owned by Iron Mountain Mines, Inc., but
Stauffer Chemical Company, the previous mine owner, owns the surrounding land.

Iron  Mountain Mine was used for the mining and beneficiation of copper, silver, gold, zinc, and
pyrite from 1865 to  1963.  Deposits of silver and copper were mined prior to  1900.  Processing of
copper and silver was  conducted between 1896 and  1907 at the Keswick smelter.  The smelter may
have been located near Spring Creek and the Sacramento River.  No odier smelting operations
occurred at the mine site.

Starting in 1900, pyrite ore from the so-called "old mine" was sold for offsite  beneficiation.  The
Number 8 mine and the Hornet mine were developed in 1907.  Pyrite ore from the  "old mine" and
Hornet mine was sold  for production of sulfuric acid.  Residues from this process were returned to
the Keswick smelter for recovery of copper, silver,  and  gold.

Between 1914 and 1919, a copper flotation mill operated at the town of Minnesota,  approximately
two miles east of the above mines.  Copper and pyrite ore tailings were disposed in this area.  The
mill was moved to an  area adjacent to  the Number 8 mine and operated between 1928 and 1933.  A
tailings dam was built in Slickrock Creek, but was destroyed in a 1933 flood.

Open pit mining of gold and silver required tailings disposal in a gulch adjacent to Slickrock Creek.
Approximately 2.6 million tons of ore  were processed in this area between 1929 and 1942.

The Richmond and Mattie ore bodies were developed for their copper and zinc deposits.  The
Richmond ore body was mined between  1942 and 1956; the  Mattie ore body was developed in 1942.
A copper-zinc flotation plant operated  in this area between 1943 and 1947.  The Brick Flat ore body
was mined for pyrite between 1955 and 1962 using open pit  methods.

All mining at the site was discontinued in 1963.  However,  several activities are still in operation.
Two cementation plants, the Boulder Creek Cementation plant constructed in 1940 and the Slickrock
Cementation plant constructed in 1977, and recovery of copper from acid mine drainage (AMD).
Other metals, including cadmium and zinc, are not recovered.  The Spring Creek Debris Dam,
constructed in 1963  to  control the discharge of contaminated runoff into the Sacramento River, is
operated by the State.

Environmental Damages and Risks

Mine disturbance has enhanced the natural action of bacteria that accelerates the formation of acid
mine drainage containing toxic metals. The drainage occurs when precipitation infiltrates the highly
fractured igneous and  metamorphic rock on the top of the mountain.  The Richmond and Hornet
portals are the major sources of acid and heavy metals.  Discharge from the Richmond portal has
registered pH values as low as 0.6.

Discharges from the Richmond portal drain into Boulder Creek, a perennial stream.  Others drainages
from the mine and intermittent drainages from uncovered tailings and waste piles flow into Slickrock
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                                                            Mining Industry Profile:  Lead-Zinc
Creek.  There is also acid mine seepage along a 300- to 400-yard debris slide, which diverted the
original Slickrock Creek drainage.  Both Boulder and Slickrock Creeks are tributaries to Spring Creek
(see Table 1-12), which drains into Keswick Reservoir, just upstream of the Keswick dam.

                  Table 1-12.  Water Quality Characteristics at Spring Creek
Constituent
ph
Cadmium
Copper
Iron
Zinc
Flow rate
Concentration
3.0
0.05 to 0.3 mg/l
3 to 15 mg/l
50 to 350 mg/1
10 to 80 mg/l
5 to 1,000 ftVs
An estimated average of 1,466 pounds of zinc, 423 pounds of copper, 4,800 pounds of iron, and 10
pounds of cadmium are discharged each day into the Keswick Reservoir from the Iron Mountain
Mine.

The creeks are nearly devoid of aquatic life.  Heavy metal precipitates have been found in sediments
in Keswick Reservoir.  A 1980 survey on the density and distribution of aquatic invertebrates in
Keswick Reservoir showed that invertebrate numbers were significantly reduced downstream from the
Spring Creek arm of the reservoir. Fish in the Sacramento River at Keswick have concentrations of
copper and cadmium in liver tissues exceeding levels found to be detrimental to fish reproduction.
Loss of salmonoids in the Sacramento River from copper and zinc toxicity was  first noted in 1944.
At the time, pyrite was being sold for sulfuric acid manufacture and copper was produced
sporadically.

Fishkills, which are the result of inadequate dilution of Spring Creek water, have occurred
periodically since then. The problem has been magnified by the completion of  Shasta Dam, which
reduced upstream dilution flows in the Sacramento River.

CALIFORNIA GULCH, LEADVILLE, COLORADO

Operating History

The Phase I Remedial  Investigation (RI) study area, which includes the City of  Leadville (population
3,800), encompasses an 11.5-square mile watershed that drains along California Gulch to the
Arkansas River west of Leadville. The development of Leadville dates back to the 1850s with the
mining development of the rich mineralized zones containing principally gold, silver, lead, zinc, and
copper.  Mining, processing, and/or smelting operations in the area have been active for more than
125 years and varied in degree with economic demand and technological improvements.  Early
activities consisted  of placer mining for gold in California Gulch.  Later, underground mines were
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                                                             Mining Industry Profile:  Lead-Zinc
developed to the southeast of Leadviile where the ores were extracted and then processed into metallic
concentrates. These concentrates were either shipped elsewhere or further processed at the numerous
smelters that were in the Leadviile area.  Many areas received mining-related wastes including mine
waste rock,  tailings, and slag piles.

As the mines were deepened and mining areas expanded, drainage became an economic factor in the
operational costs, particularly during periods of depressed metal prices or labor unrest.  Tunnels were
developed to drain the ore bodies and to facilitate mining.  The Yak Tunnel, which started in  1895 as
an extension of the Silver Cord Tunnel, eventually reached a length of 3.5 miles and was the first  of
two major efforts to improve drainage.

The Yak Tunnel was extended several times and has several laterals and drifts that extend into the
various mine workings.   The last extension was in 1923.  EPA estimates that 60,000 feet of tunnels
and major laterals and 55 to 74 million cubic feet of void space are associated with the runnel  mining
activities. Although mining activity has ceased in the immediate area of California Gulch, other
mining areas are active and continue to drain into the Yak Tunnel.

The current condition of the Yak Tunnel is unknown.  However, the last inspection, conducted by the
American Smelting and  Refining Company (ASARCO) in 1983, disclosed that the tunnel roof was
generally weak and had  caved in at many places.

Environmental Damages and Risks

The RI Report, completed in May  1987, presents a human risk assessment for the site and concluded
that exposure to contaminants at the site presented a threat to human health.  The risk assessment
identifies cadmium, copper, lead, and zinc as die contaminants of concern at die site. California
Gulch  and the City of Leadviile are in Lake County, a relatively small (380-square mile) rural area
with a current estimated population of approximately 6,600.  Lake County, and the surrounding area,
depends on agricultural, tourist,  and mining industries. Its past employment and economic base
stemmed primarily from mining and mine-related industries, which have diminished significantly since
1977.  Mine lay-offs have dramatically reduced employment in Lake County.

The RI Report stated that there is little specific information on wildlife within the site study area. The
wildlife found within the study area should be similar to that found in the general Leadviile area.
However, die disturbed  landscape and level of past and present human activity in both Leadviile and
the California Gulch area may tend to minimize die number and diversity of wildlife within die site.

Ground water monitoring indicated that the upper 25 to 50 feet of California Gulch alluvial ground
water are contaminated with cadmium, zinc, and other metals and  pollutants such as sulfates, which
are associated with the Yak Tunnel discharge. The concentrations of various metals in ground water
are in  excess of both primary and secondary drinking water standards.

Surface water contamination is the primary concern for the Yak Tunnel operable unit.  During the
Phase  I RI studies, EPA identified 33 existing wells that were drilled into the California Gulch
alluvium. Many of these wells have been  abandoned because of poor water quality.  In 1986, EPA
connected the one remaining household that used die aquifer as a drinking water source to the public
water system. However, at this time, no steps have been taken to prevent people from using their
existing wells or from drilling wells into the contaminated alluvium.
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                                                             .Mining Industry Profile:  Lead-Zinc
EAGLE MINE, MINTURN/REDCLIFF, COLORADO

Operating History

Mining activities in  the Eagle Mine area began in the 1870s.  Several individual mines were located
in the area where the Eagle Mine facility now exists. Mining of oxidized gold-silver ore in the
Oilman area (area between the towns of Minturn and Red Cliff) was begun in 1884 and ceased in
1894.  By  1905, mining of the zinc deposits had begun, and a roasting and magnetic  separation plant
(roaster plant) had been set up in Belden to refine the ore mined from what is the present-day Eagle
Mine.  In 1912, the New Jersey  Zinc Company began consolidating the various mines into one
facility (Eagle Mine).   New Jersey Zinc operated the roaster plant at Belden as part of the Eagle Mine
facility from  1915 to 1919 when the plant was dismantled.  Wastes  from the roaster plant were
dumped along the side  of a mountain and allowed to migrate  into the Eagle River.

A separate mill, consisting of an underground froth-flotation unit designed to treat zinc ore, was
constructed in 1929. Waste material from this mill was transported in slurry form through a buried
concrete pipeline to a location near the Rex  Flats wetlands area.   At this point, the pipeline  became an
elevated wooden stave  pipeline that carried the waste (tailings) to the old tailings pond.  Because of
the lack of a  market, the zinc mill was closed in 1931.  By 1941, mining of zinc ore  was re-
established, and after 1946, onsite milling of the ore was initiated.

Copper-silver ore was mined  from 1932 through 1940.  In fact, copper-silver ore was the only ore
mined  during those  years. However, this ore was not processed at  what is now the Eagle Mine site.
Mining of copper-silver ore was continued until October 1984, but with an inactive period between
1981 and 1983.

In the  1960s, New Jersey Zinc merged with Gulf and Western Company. Gulf and Western operated
Eagle Mine through a subsidiary, New Jersey Zinc Company (Delaware Corporation), from 1966  to
1981.  By the end of 1977, milling operations at the site had ceased and the mill facility was
converted to  an acid mine water treatment facility.  However, from September 1983 until June 1984,
some mining did occur. Mr.  Glen Miller and Battle Mountain Corporation (new owners) extracted
copper and silver ore. In June 1984, the facility was abandoned by  Miller,  and electricity to the mine
was shut off, thereby shutting off the pumps.  The mine began to flood at that time and has continued
to flood.

Environmental Damages and Risks

The results of the RI of the Eagle Mine site show damage to plant and animal life in  and around the
site and contamination of drinking water (private wells) by metals.  The RI also indicates that there
has been a decrease in recreational use and fishing in the Eagle River as a result of metals
contamination.

Three private drinking water  wells were contaminated with heavy metals. Two wells (#1 and #3)  are
no longer in  use, and the other (well #2) is in use only  for household cleaning purposes  and not for
drinking water.

Other  uses of Eagle River water are for municipal supply (for the Town of Minturn and many others
in the area),  stock watering, and irrigation downstream from the confluence with Gore Creek.  The
major consumer of  water is the Consolidated Upper Eagle Valley Sanitation District.  The river water
is also drawn from  several alluvial wells bordering the river.  The Town of Minturn, located north of
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                                                             Mining Industry Profile:  Lead-Zinc
the Eagle Mine, diverts surface water for municipal use.  In addition, Minturn has two municipal
wells located in Maloit Park. However, these wells were tested in April and May 1985, and no
hazardous metals were found in the samples taken.  As of 1985, when the RI  was written, there were
also several other municipal water systems  planned that would divert water from the Eagle River.

Aquatic organisms were found to be affected by the of metals in the river. Bioaccumulation of zinc,
copper, lead, and cadmium was evident in macroinvertebrates taken from the  Eagle River and its
tributaries.  Of the four metals, zinc was  found to have the most influence on the aquatic
environment.  Surface water concentrations of zinc exceeded chronic toxicity (0.047 mg/1) and acute
toxicity (0.18 to 0.57 mg/1) criteria in the Eagle Mine area.  Many times, zinc levels were found to
be two to three times the toxicity criteria  concentrations.  Cadmium and copper  concentrations often
exceeded acute toxicity criteria (cadmium - 0.0018 to 0.0086 mg/1; copper - 0.0092 to 0.0340 mg/1)
and lead exceeded the chronic toxicity criteria (0.00130 to 0.0077 mg/1).  The macroinvertebrate
community was seriously affected from the old tailings pond/Rex Flats reach to  Cross Creek.  Below
the mine facility, an important component of the Eagle River benthic community, mayflies, was
reduced in number at all sampling periods.

Fish population studies were conducted in the summer of 1985.  The fish community is dominated by
a brown trout population that was found to  be reduced  in number in streams receiving discharges
from the Eagle Mine and from the old tailings pond/Rex Flats (as compared to upper Cross Creek
and upper Eagle River numbers).  Trout populations were also reduced below Rock Creek.  Although
the trout biomass below Cross Creek indicated partial  recovery, it generally remained below the
biomass found in upper Cross Creek and  the upper Eagle River.

The Eagle River is no longer able to support a quality fishery because of the environmental
degradation from heavy metals.  The macroinvertebrate food base has been severely reduced from the
Eagle Mine facility to Cross Creek and recovers slowly between Cross Creek and Gore Creek.
Although the trout population has acclimated to some degree to the metals concentrations in the Eagle
River,  they have not been able to survive in the reaches where contamination  is  worse. Even  in the
river areas where the trout do exist, the reproduction and growth potential of the trout is reduced by
lack of food and chronic toxicity by heavy metals.

The loss of several miles of trout habitat affects the local economies, especially those dependent on
recreation and tourism.  The Division of Wildlife has expended funds in attempting to restock the
river and has expended additional funds leasing public access to the Eagle River.

There are several conditions at the Eagle  Mine site that adversely affect the soil, and therefore the
plant and animal life at the site.  The soils at the site contain heavy metals and are highly acidic.
Mobility of the metals is affected by acidity, electrical conductivity, and the presence of sulfates. Soil
acidity, or pH, is one of the most important parameters in controlling the availability of metals to
plants.  As the pH decreases, the metals solubility increases, increasing the potential for the metals to
become more available to plants. Because the metals are mobile, they have collected through
transport by runoff in the  Maloit Park wetland, the banks of the Eagle River,  and Rex Flats.  At these
locations,  the metals have been available to plants in phytotoxic levels.  Many areas are bare of
vegetation and, therefore,  erosional forces have taken over and increased the rate of sediment
transport.

The vegetation at the Eagle Mine site has been visibly affected by metals contamination. For
example, plants have been discolored, stunted in growth or deformed, or have not germinated  in
certain areas.  Other observed effects were lower plant density and less diversity.
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                                                             Mining Industry Profile: Lead-Zinc
Investigations of the small mammal species at the Eagle Mine site showed lead and cadmium
concentrations higher than the concentrations found in species outside the mine site.  In addition, the
numbers of different species, such as deer mice, were lower in the contaminated areas than in
unconiaminated areas.  Evidence gathered indicates mobilization of lead and cadmium from the
source(s) (tailings pond) to vegetation, and then to small and large mammals. Studies indicate that
deer and elk have come into direct contact with contaminated vegetation. Human health hazards exist
in the possibility of human consumption of cattle that have grazed on contaminated pastures, and
human consumption of deer and/or elk obtained from sport hunting.

SMUGGLER MOUNTAIN, PITKIN COUNTY, COLORADO

Operating History

Mining, milling, and smelting of silver, lead, and zinc were conducted  at the site.  In the late 1800s
and early 1900s, mining companies ran extensive mining operations onsite. Although several small
operations started and stopped after 1930, records indicate that the bulk of the mining wastes at  the
site were placed on the steep slope of the western side of Smuggler Mountain near the Smuggler shaft
from 1880 to 1915.  In the mid-1960s a reprocessing facility was run at the site, causing the
dispersion of the wastes from the  relatively distinct piles at the mine site to other locations in the
vicinity.  Reprocessing also spawned a number of settling ponds around the site. The wastes were
dispersed further by subsequent residential development.  It is believed that the mined metals (silver,
lead, and zinc) were reprocessed.

Mine wastes, such as waste rock, tailings, and slag, comprise much of  the site.  It is estimated that
approximately 2.4 million cubic yards of these waste materials were generated at the site.  The wastes
have been spread  over a wide area and at depths varying from one to two feet to 40 feet.  They  occur
covered, uncovered, or mixed with native soil, and contain high levels of minerals containing lead
and cadmium, among other constituents.

Environmental Damages and Risks

The site was  first considered to pose risks in 1981, when research into  crop uptake of trace metals
indicated a potential problem with the uptake of lead and cadmium by vegetables grown on regraded
mine and mill tailings.

Presently, the potential for human exposure exists through direct contact of soils and inhalation of
contaminant-laden dusts.  The risk of ingesting drinking water contaminated by site soils also exists,
although because of site conditions (i.e., soil and pollutant characteristics), the potential for exposure
is significantly reduced.

Lead and cadmium are the two metals of most concern at the site because of their elevated
concentrations at the site and acute toxicities. Lead exposure is of specific concern to children ages
one to five who have the greatest  risk of exposure through soil ingestion and have a greater
susceptibility to blood lead poisoning.  It should be noted that toxic effects of lead ingestion in
children from lead-based paints (i.e., elevated blood levels) have been documented, but exposure to
lead in tailings and soil such as that at the Smuggler site has not been documented.

Cadmium can also be acutely toxic and cadmium compounds are generally more bioavailable than
lead compounds.  A ground water sample of 13 ng/\ of cadmium exceeded the ambient water quality
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                                                           Mining Industry Profile:  Lead-Zinc
standard of 10 jig/I in one well on one occasion. The well was checked again and found to be less
than 10 ngl\.  Therefore, it is unclear whether cadmium contamination exists onsite.

BUNKER HILL MINING AND METALLURGICAL COMPLEX, SMELTERVILLE, IDAHO

Operating History

Lead and zinc mining began on the Bunker Hill site with the location of the Bunker Hill and Sullivan
claims  in 1885 by Noah Kellogg.  The first mill was constructed in 1886 in Milo Gulch in the
southeastern portion of the site.  The Bunker Hill and Sullivan Mining and Concentrating Company
was incorporated in 1887 (the name was changed to the Bunker Hill Company in 1956).  A larger
mill was constructed  near the site of Kellogg Tunnel in 1891.  Before the Kellogg tunnel was
completed in  1902, ore was transferred from the mines in Milo Gulch to the mill site by aerial
tramway.  The first mill located at the present mill site was constructed in 1912. Milling or
concentration was originally accomplished by gravity separation.  Flotation was  added in 1913, and
by  1938, all gravity separation was discontinued.  The mill was modified to expand production in
1941 and 1947 (the types of modifications were not specified).

Originally, tailings from the mill were discharged to the South Fork of the Coeur d'Alene River and
its tributaries. In 1928, the first impoundment at the Central Impoundment Area began operation.
The decant from this area flowed directly into the river until  1974, when the Central Treatment Plant
was installed.

The Bunker Hill Company purchased Hecla Mining Company's interest in the Zinc Plant and
consolidated both plants under one ownership in 1955.  In 1968, the Bunker Hill Company was
purchased by Gulf Resources and Chemical Company (Gulf).  Gulf operated the plant until its closure
in December 1981.  In 1982 the complex was sold to Bunker Limited Partnership, its present owners.
In 1983, the Bunker Hill Mill and an associated mine offsite were reopened. However, in 1986, the
mill and mine were shut down because of continuing depressed silver prices.  At this time, active
operations at the complex include the mine pumps, a  waste water treatment plant, and a zinc
concentrate dryer (under lease to another mining company). The mine and mill were reopened in
1988 when metal prices improved.

Environmental Damage and Risks

The Bunker Hill site contamination was brought to public attention in 1974 when symptoms of lead
poisoning in children were reported to local public health officials.  More than 98 percent of 172
children living within one mile of the smelter had  blood lead levels exceeding 40 /tg/dl at the time of
the study. CDC's safe limit is 25 /tg/dl and the World Health Organization (WHO) has determined
that the no-detected effect level for blood lead is about 10 /*g/dl.

A follow-up study, conducted by CDC and the State of Idaho, surveyed 364 children in 1983.  Blood
lead levels in the children from Smelterville ranged from 6 /ig/dl to 35 Mg/dl, with a mean of 21
/ig/dl.  These levels dropped from an average of 68 jig/dl in  1974 to 31 ng/dl in 1980. In a second
study area (Kellogg, Wardner, and Page residences), mean blood lead levels dropped from 49 /ig/dl
in 1974 to 26 jtg/dl in 1980 and to 17 jig/dl in  1983. Strong correlations were  found with residential
area soil lead levels, household dust lead levels, and (to a lesser extent) childhood mouthing behavior
and other factors.
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                                                             Mining Industry Profile:  Lead-Zinc
In 1983, when the Remedial Investigation/Feasibility Study  (Rl/FS) was started, and as a result of
the blood lead studies, EPA decided to focus on the removal of contaminated soils from public areas
in the populated portions of the site to reduce the lead poisoning in  young children.

In 1985, a follow-up survey to the 1983  study was  initiated. This was completed for CDC and
involved 348 children.  Of the 348, 10 children were identified as having blood lead levels exceeding
the CDC's limit of 25 Mg/dl, which represents a significant reduction from the previous studies.
However, within this study, the highest blood-lead  level in the area since 1979 was measured at 59
      in a four-year-old  child.
Most recently, in August 1989, the yearly Blood Lead Screening Program in the area identified eight
children with elevated blood lead levels.  Lead is of concern because it can cause nerve and kidney
damage and young children are especially susceptible.

The exposure pathways directly reaching humans are from household dusts, soils, and garden
vegetables.  In 1974, the residential mean lead levels were 1 1,920 ppm for household dust, 7,224 for
soils, and 231 ppm for garden lettuce (for residences within one mile of the smelter complex).  In
1983, household dust lead levels averaged 3,994 ppm, soils averaged 3,504 ppm, and lettuce
contained 48 ppm. Cadmium levels in  1974 were 63 ppm in soils and 28 ppm in lettuce (household
dust not analyzed).  In  1983, the levels were 54 ppm in soils, 5 ppm in lettuce, and 67 ppm in
household dusts.  For zinc, the 1974 levels were 2,340 ppm for soils (lettuce and dust were not
analyzed) and the 1983 levels were 126 ppm for soils, 2,840 ppm for household dusts, and 73 ppm
for lettuce.  The population potentially at risk of exposure is relatively well known based on the
blood,  soil, household, and vegetative lead contents surveys.

In October 1989, an inspection of the smelter complex conducted by the Agency for Toxic Substances
and Disease Registry resulted in a Public Health Advisory. The advisory concluded that the smelter
complex was a "significant risk to public health."

Environmental and ecological damage has occurred in  addition to health threats. The hillsides around
the smelter complex are denuded of vegetation because of the smelter emissions and mining activity,
as well as logging, and forest fires.  The Bunker Hill Company, as part of a revegetation effort
beginning in the early 1970s, identified about 14,400 (of 18,000) acres that had been damaged by
smelter emissions or mining.

Furthermore, there is no year-long resident population of fish inhabiting the river in or below the
project area to the confluence of the South Fork and the mainstem of the Coeur d'Alene River.
According to the Site Characterization Report, this is due to the heavy metal concentrations in the
South Fork of the Coeur d'Alene River.

CHEROKEE COUNTY, CHEROKEE, KANSAS

Operating History

The first significant lead  and zinc mine in Kansas was  in the City of Galena, where ore was
discovered in 1876. Sphalerite (zinc sulfide) and galena (lead sulfide) were the minerals that
contained the lead and zinc ore.  Pyrite and marcasite (both iron disulfide) were commonly found in
association with  the lead  and zinc minerals.  The district was also an important source of cadmium,
which  was produced as a byproduct of lead-zinc smelting.  A smelter was  built along Short Creek in
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                                                            Mining Industry Profile:  Lead-Zinc
the 1890s.  The area near the original smelter was used for various smelting facilities until 1961.
when the remaining facility was converted to produce sulruric acid.

Lead and zinc ore in the Galena district is typically found in veins 80 to 100 feet below the surface,
which permitted many small,  shallow-depth  mining operations to flourish.  Exploration and mine
development were accomplished by excavating vertical shafts using a modified room-and-pillar
method to follow the ore vein. The use of vertical shafts as a means of mineral exploration and the
subdivision of leases into small sublease mining plots result in a high density of mine shafts in the
subsite.  Several mines have collapsed, forming subsidence craters of varying  sizes and shapes.  Many
circular subsidences are less than 75 feet in  diameter, while others measure several hundred feet along
the longest dimension.  A ground level difference of 20 to 40 feet is common  in the subsidences
within the subsite, although some are filled  with water and may be deeper.

Environmental Damages and Risks

Approximately 510 households outside of the City of Galena depend on private wells in the shallow
ground water aquifer for their drinking water. These wells obtain water from the same geologic
formation that had previously been mined.  Sampling indicated that there is a potential that these wells
may become contaminated with heavy metals.

Remedial  Investigation and Operable Unit Feasibility Studies (OUFS) conducted by EPA show that
mine wastes (and soils contaminated with mine wastes) also present a human health risk as a result of
their incidental ingestion.  Levels of exposure for  lead, zinc, and cadmium, in particular, present a
health risk.

ORONOGO-DUENWEG, JASPER COUNTY, MISSOURI

Operating History

Mining began in the area around 1850 and continued until the late 1960s.  Between  1850 and 1950,
the site generated over $1 billion in revenues.  Mining activities at the  site involved retrieving crude
ores from the mines to the surface, where the ores were milled into lead and zinc concentrates.  Ore-
bearing rock was crushed and ground into a fine gravel to liberate the desired  materials.  Waste
products from the processing were removed and placed in large tailings piles.  Barren rock containing
no ore was also discarded in  piles.

Environmental Damage and Risks

A Risk Assessment (RA) has not yet been performed for the site. However, public health
implications of the site have been discussed in the U.S. Department of Health  and Human Services'
Preliminary Health Assessment for the site  (PHA).

The most important human exposure pathways for the site are believed to be ingestion of
contaminated ground water and surface water, inhalation of airborne contaminated dust particles,
ingestion of contaminated soil by children in residential areas, and ingestion of contaminated aquatic
organisms and of foodstuffs grown in contaminated soil.  Dermal or mucous membrane contact is
possible but unlikely.

Preliminary risk calculations indicate that excessive exposure to zinc, cadmium, and lead may be
occurring for residents in the Oronogo-Duenweg Mining area.  In addition, the State of Kansas has
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                                                             Mining Industry Profile: Lead-Zinc
conducted several health surveys indicating a high incidence of tuberculosis and lung cancer among
area residents.  Missouri has also started to examine lead levels in the blood of local individuals.

Surface water at the site, specifically Center Creek, is used for fishing. In addition, surface waters
potentially affected by the  site, including water contained in abandoned pits, may be used for crop
irrigation, livestock watering, commercial purposes, and recreational purposes.  Consequently, public
health risks include the risk of exposure through the food chain.

Individuals in the small towns of the Oronogo-Duenweg area (Webb City, Oronogo, Duenweg, and
Carterville) obtain their drinking water primarily from municipal wells screened in the deeper aquifer.
Individuals living outside these towns, an estimated 1,500 people, obtain water from private wells
tapping the shallow aquifer.  Ground water samples collected in November 1988 contained
concentrations of lead and  cadmium that exceed EPA's  proposed MCLs.  A municipal water supply
well located near the site was abandoned some time after 1972. The data for this well indicate that
contamination of the deep  aquifer with mine water may  have occurred.

TAR CREEK, OTTAWA COUNTY, OKLAHOMA

Operating History

Lead-zinc ores were first discovered at the site in 1901 j. and the first mining output began in 1904.  In
1914, the main body of ore was discovered, and mining activities increased substantially. Early
mining was conducted by small operators on 40-acre tracts,  but consolidation began in the 1930s.
The mines were subject to flooding  from inflows of ground water.  The floods were controlled by the
use of large capacity pumps during mining operations.  Large-scale mining activities ceased in the
mid-1960s, and the pumps were removed from the mines. By 1979, the majority of the underground
mines were completely flooded.  Acid mine water began to discharge via abandoned or partially
plugged mine shaft openings and boreholes.

Environmental Damages  and Risks

At locations both above and below the acid mine water  discharge points, chronic water quality criteria
for several heavy metals is exceeded.  Heavy metal loadings increase downstream, while the pH
decreases, resulting in severe stress  to the aquatic community of Tar Creek. Studies found no fish
and only a few benthic macroinvertebrates surviving in Tar Creek.  The greatest threat to human
health comes from dermal  exposure to mine water from direct contact. Tar Creek is used for
recreational purposes, including swimming.

The Roubidoux aquifer is still a safe drinking water supply.  It serves a population of 21,000 in five
principal communities, including Miami, Richer, Cardin, Quapaw, Commerce, and a few rural
districts.  Historical drinking water-quality data for community wells indicate no degradation to date,
except  in the city wells serving Quapaw, where two wells were abandoned because of mine water
contamination.  The contamination was attributed to either casing  failure or migration of mine water
from nearby abandoned wells.

The Neosho River, the Spring River, and Grand Lake, which receive water from Tar Creek, can be
safely used as a raw water source for public water supplies,  and fish samples indicate that the fish are
safe for human consumption.  Most  of the heavy metals present in the acid  mine water precipitate out
of the water and into the Tar Creek  and Neosho River stream sediments.  This occurs primarily at the
Tar Creek and Neosho River confluence, because the Neosho River has a flow capacity approximately
                                             1-72

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                                                            Mining Industry Profile:  Lead-Zinc
500 times greater than Tar Creek and a much greater buffering capacity.  The Neosho River has
received little impact from acid mine drainage into Tar Creek other than aesthetic alteration at the Tar
Creek confluence.  Air impacts were not evaluated.

SHARON STEEL/MIDVALE TAILINGS, MIDVALE, UTAH

Operating History

U.S. Smelting conducted milling and smelting operations at the site. The milling portion of the
facility operated from 1910 to 1971.  In 1971, UV Industries bought U.S.  Smelting.  The smelter,
located to the north of 7800 South Street, is on the Mid vale Slag Superfund site, and was closed in
1958.  Sharon Steel acquired the mill and tailings site in 1979.  The original operations involved
receiving lead,  copper, and zinc ores; extracting suifide concentrates of these metals in the milling
operation; and smelting these concentrates to extract the metals in purer form.  The facility also
operated  as a custom mill, receiving ores and concentrating and extracting metals.  The wastes from
the milling operations were disposed of in unconsolidated tailings piles.  The mill site includes several
mill buildings and approximately 12 to  14 million cubic yards of tailings in uncovered piles.

In June 1982, wind-blown tailings were sampled and found to contain arsenic, cadmium,  chromium,
copper, lead, and zinc.  A 6-foot chain link fence was erected by Sharon Steel along the northern
boundary of the property to prevent direct contact with  the tailings piles. The fence, however, did
not prevent the tailings from blowing through and over  the fence and down the embankment of a
highway  right-of-way.  On September 17, 1982, the Utah State Bureau of Air Quality issued a request
for a compliance plan to control the fugitive dust emanating from Sharon Steel.   Sharon Steel
Corporation responded to this request in October of that year with  a proposal to use water flooding to
suppress the dust.  The State withdrew an initial approval of the plan and ordered that Sharon Steel
design an alternative plan.  Ultimately, a dust mitigation program using a chemical polymer dust
suppressant was implemented in May and June 1988.

Also in 1988, a slope stabilization and river bank restoration  plan was implemented.  Where the berm
bordering the site had been washed out by high river flows, it was reconstructed to serve as a buffer
zone between the tailings and the river.  Rehabilitation involved removing all tailings from the berm
where it  had been washed out. These tailings were placed on existing piles away from the river and
embankments were sloped at a ratio of approximately 3:1 in a horizontal to vertical configuration.  In
addition, stream bank areas requiring repair were filled with gravel material, compacted,  and covered
with a graded rip rap.  Debris and sediments that were directing river flow into the tailings side of the
river were also removed and the river channel was  "cleaned" so that river flow  would be redirected
away from the  bank bordering the tailings.

Environmental Damages and Risks

An environmental health problem was first suspected in June 1982 when the Utah State Department of
Health was notified that citizens were gathering wind-blown tailings for sandboxes and gardens. Sand
and wind-blown tailings were sampled by the State.  Arsenic, cadmium, chromium, copper, lead,  and
zinc were found.

The City of Midvale, less than one mile away, has  a population of 12,085 and within two miles of the
site there are 43,911 people.  The Jordan River is classified for recreational use, excluding
swimming, cold water game fishing, and agriculture.
                                              1-73

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                                                             Mining Industry Profile:  Lead-Zinc
Contaminants of concern in the mill tailings are aluminum, antimony, arsenic, cadmium, chromium.
copper, lead, manganese, silver, thallium, and zinc.  Arsenic, cadmium, and lead are likely to be of
greatest potential concern to human health as discovered in the endangerment assessment performed as
part of the RI.

The exposure pathways evaluated under current and potential future use conditions are:

     •  Direct ingestion of site tailings or contaminated surface soils

     •  Ingestion of contaminated ground water

     •  Inhalation of tailings contaminated dust

     •  Ingestion of home-grown produce by nearby residents

For all the exposure  pathways evaluated under current use in the baseline risk assessment, arsenic is
carcinogenic, and arsenic and cadmium are carcinogenic through inhalation.  The excess upper-bound
lifetime cancer risks  for all exposure pathways combined is SxlO"4, primarily from exposure to arsenic
from ingestion of tailings in sandboxes and ingestion of indoor dust. However, "public information
efforts by the State of Utah and the Environmental Protection Agency have generally eliminated the
route of exposure involving tailings ingestion from sandboxes."  Noncarcinogenic effects can also
result from exposure to arsenic  and cadmium through the pathways evaluated.

The overall excess upperbound cancer risk for exposure pathways under future use conditions is
1 x 10° (chance in 1,000), resulting primarily from arsenic through indoor dust ingestion and tailings
ingestion. Noncarcinogenic adverse effects could also occur because of exposure to arsenic  and
cadmium. Of greatest concern is the ingestion of lead from the tailings study area that can cause
noncarcinogenic adverse effects.

Potential threats to environmental receptors include vegetation, aquatic life, and wildlife. The
geometric mean contamination level of lead in  residential soils was found to be 722 milligrams per
kilogram (mg/kg) (ppm).  Aquatic life can be exposed to contaminants both in surface water and
sediments. Of greatest concern are the high levels of metals in the sediments, which may act as a
reservoir that can supply metals to the water column or be directly consumed by benthic organisms.
Wildlife in the wetlands may be exposed to site-related contaminants through direct contact with
surface waters or sediments or through the food chain.  Among the metals present at the study area,
lead has been shown to bioconcentrate in insects, small mammals, and songbirds, which may then be
consumed by larger animals.  While the potential of adverse effects due to lead exposure exists, it is
presently unknown whether wildlife is being adversely affected by the metals found in the study area.
                                              1-74

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                                Mining Industry Profile: Lead-Zinc
               APPENDIX 1-C




SUMMARY OF COMMENTS AND EPA RESPONSES
                    1-75

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                                                            Mining Industry Profile: Lead-Zinc
                  Comments on the Draft Industry Profile and EPA Responses

A copy of the draft Mining Industry Profile: Lead-Zinc was provided to the following for their
review and comment:  the U.S. Department of the Interior, the Bureau of Mines, the Western
Governors' Association, the Interstate Mining Compact Commission, and the American Mining
Congress (AMC), and Public Interest Groups.  The comments included  technical and editorial
changes, as well as comments on the scope of the profile and its relationship to the authorities
provided under  RCRA Subtitle D.

Because several general concerns were raised by a number of commenters, EPA has grouped the
comments into two categories.  The first category includes seven general concerns that were raised by
all commenters.  These concerns  are addressed in the first section below. The second category
consists of technical comments on the profile that were raised by only one reviewer as opposed to the
group as a whole.  These are addressed in the second section below. All other comments, including
minor technical and marginal notes, have been incorporated into the revised profile.  EPA believes
these comments have improved the  document's accuracy and clarity and would like to thank all the
agencies, companies, and individuals for their time and effort.

General Issues Pertaining to AH Profiles

1.    Comment:  Several commenters objected to the use of hypothetical phrases like "may cause" or
     "may occur."  Their use was characterized as misleading and inappropriate in describing
     environmental impacts in an industry profile of this type.

     Response:  We believe the descriptions of conditions and impacts that may occur regarding
     potential effects is appropriate in many cases since the intent of the relevant sections of the
     profiles is to describe potential impacts that may occur as a result of extracting and beneficiating
     ores  and minerals.  As noted in the responses to related comments (see below),  EPA has
     extensively revised the sections of the profiles addressing environmental effects.  Such sections
     are now more focused and direct and describe, in general terms, a number of specific types of
     impacts that can occur under particular conditions or  in particular environments.

2.    Comment:  A related issue raised by commenters was that EPA did not balance the profiles by
     describing environmental protection practices currently followed by the mining industry.
     Instead, the commenters were critical that EPA  selected the worst  sites to describe and these
     sites represent only a small  number of mines and even a few clandestine operations.

     Response:  We believe the profiles represent current environmental management practices as
     described in the current literature.

3.    Comment:  Commenters on the profiles were concerned that the sites described  in the discussion
     of environmental effects were under some other regulatory authority (e.g., CERCLA).

     Response:  As noted above, the relevant sections of the profile have been revised extensively.
     However, we believe, with  proper qualification, sites under other regulatory authorities,
     including CERCLA, are relevant to any examination of actual or potential environmental effects.
                                             1-76

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                                                            Mining Industry Profile:  Lead-Zinc
4.    Comment:  Commenters were concerned the profiles addressed materials other than those
     considered "wastes" under RCRA.

     Response: The profile has been edited so that only RCRA defined wastes are discussed.

5.    Comment:  Many commenters recommended a discussion of the mitigating effects of site-
     specific factors on potential environmental effects.

     Response: As noted above, EPA has revised the relevant sections of the profiles, including the
     addition of language that emphasizes the site-specific nature of potential  environmental effects.

6.    Comment:  Many commenters recommended that the effectiveness of State regulatory actions in
     preventing adverse environmental effects be integrated into any discussion of potential effects.

     Response: The profiles have been amended to reflect the fact that State  requirements can
     substantially reduce or eliminate many adverse environmental effects.

7.    Comment:  A  number of comments were received on  the table in  each draft profile that cited
     NIOSH data on the  quantities of certain chemicals found on mine  property and that included
     worker exposure limits. Commenters questioned the data's accuracy and relevance.

     Response: The table has been replaced with a simple list of chemicals typically found on sites.

Technical Issues Specific to the Lead-Zinc Profile

8.    Comment:  Discussion of processing activities such as smelters and stack emissions should be
     deleted.

     Response: EPA has revised the profile to address only extraction and beneficiation. It should
     be noted that a description of sintering, as it applies to lead and zinc concentrates, remains in the
     text since it is  a step in beneficiation.

9.    Comment:  Add information on the Van Stone Mine to Table 1 (Bureau  of Mines).

     Response: According to sources used for this table, the Van Stone Mine is located in Canada
     and therefore was not included.

10.  Comment:  In Appendix B, concerning the discussion of Clear Creek on the National Priorities
     List, verify that there is a health risk for inhalation of these materials (Hecla Mining Company).

     Response: The Record of Decision clearly stated that a low  risk to health may exist at the  site.
                                              1-77

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                  Mining Industry Profile: Lead-Zinc
APPENDIX 1-D




 ACRONYMS
     1-78

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                                                         Mining Industry Profile:  Lead-Zinc
                                       ACRONYMS

ADF&G       Alaska Department of Fish and Game
AMD          Acid Mine Drainage
ANFO         Ammonium Nitrate Fertilizer and Fuel Oil
ASARCO      American Smelting and  Refining Company
ATSDR        Agency for Toxic Substances and Disease Registry
AWQC        Ambient Water Quality  Criteria
BAT           Best Available Technology
BLM           U.S.  Bureau of Land Management
BPJ            Best Professional Judgment
BPT           Best Practicable Technology
BRA           Baseline Risk Assessment
CAA           Clean Air Act
CDC           Centers for Disease Control
CFR           Code of Federal Regulations
CWA          Clean Water Act
DEC           Department of Environmental Conservation
dscm           Dry Standard Cubic Meter
DNR           Department of Natural Resources
EA            Endangerment Assessment
EP            Extraction Procedure
EPA           U.S.  Environmental Protection Agency
FLPMA        Federal Land Policy and Management Act
FS            U.S.  Forest Service
FWS           U.S.  Fish and Wildlife Service
gpm           gallons per minute
HSWA         Hazardous and Solid Waste Amendments
ICS            Individual Control Strategy
ISP            Imperial Smelting Process
LDH           Load-Dump-Haul
MCL           Maximum Contaminant  Level
mm            millimeters
MMWM       Metallic Minerals Waste Management
MMWMA      Metallic Minerals Waste Management Act
MSHA         Mine Safety and Health  Administration
NAAQS        National Ambient Air Quality Standards
NEPA          National Environmental  Policy Act
NESHAP       National Emission Standards for Hazardous Air Pollutants
NIOSH         National Institute for Occupational Safety and Health
NPL           National Priorities List
NPDES        National Pollutant Discharge Elimination System
NPS           National Park Service
NSPS          New Source Performance Standards
OUFS          Operable Unit Feasibility Studies
PEL           Permissible Exposure Limit
PHA           Preliminary Health Assessment
ppm           parts per million
PRP           Potentially Responsible Parties
                                          1-79

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                                                          Mining Industry Profile: Lead-Zinc
                                 ACRONYMS (Continued)

PSD           Prevention of Significant Deterioration
RA            Risk Assessment
RCRA         Resource Conservation and Recovery Act
RI             Remedial Investigation
RI/FS          Remedial Investigation/Feasibility Study
ROD           Record of Decision
SDWA         Safe Drinking Water Act
SIC            Standard Industrial Category
SIP            State Implementation Plan
st             Short Tons
SWDA         Solid Waste Disposal Act
TSCA         Toxic Substances Control Act
TDS           Total Dissolved Solids
TSS           Total Suspended Solids
ug/g           micrograms per gram
ug/L           micrograms per liter
ug/m3          micrograms per cubic meter
U.S.           United States
USDA         U.S. Department of Agriculture
WHO          World Health Organization
                                            1-80

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                               Site Visit Report: Doe Run Fletcher
             MINE SITE VISIT:
DOE RUN FLETCHER MINE AND MILL
             U.S. Environmental Protection Agency
                  Office of Solid Waste
                   401 M Street SW
                 Washington, DC 20460

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                                                            Sue Visit Report:  Doe Run Fletcher
                      2.0 SITE VISIT REPORT:  DOE RUN FLETCHER

2.1    INTRODUCTION

2.1.1   Background

The U.S. Environmental Protection Agency (EPA) is assisting states to improve their mining
programs.  As part of this ongoing effort, EPA is gathering data related to waste generation and
management practices by  conducting visits to mine sites.  As one of several site visits, EPA visited
the Doe Run Fletcher Mine and Mill on September 24 and 25, 1991.

Sites to be visited were selected by EPA to represent both an  array of mining industry sectors and
different regional geographies.  All site visits have been conducted pursuant to RCRA Sections 3001
and 3007 information collection authorities.  When sites have  been on Federal land, EPA has  invited
representatives of the land management agencies (Bureau  of Land Management and the Forest
Service). State agency representatives and EPA regional  personnel have also been invited to
participate in each site visit.

For each site, EPA has collected information using a three-step approach:  (1) contacting the facility
by telephone to obtain initial information, (2) contacting state  regulatory agencies by telephone to get
further information, and (3) conducting the actual site visit. Information collected  prior to the visit
was then reviewed during the site visit.

In preparing this report, EPA collected information from  a variety of sources,  including The Doe Run
Company and the State of Missouri Department of Natural Resources (DNR) Water Quality Division.
Additional information was collected during telephone conversations, the site visit, and from other
published sources.  The following individuals participated in the site visit to the Doe Run Fletcher
Mine and Mill facility on September 24 and 25,  1991:

Doe Run
John Carter, Environmental Manager                                             314-244-8152
Terry Perkins, Mills and Metallurgy Manager                                     314-244-8612
John Fitzsimmons, VP Mining  Doe Run,
        General Manager of SEMO Operations                                    314-244-8110
Bill Tierney, Mines Manager                                                     314-244-8150
Denis Murphy, Environmental  Quality Control Specialist         '                  314-244-8104
Bill Mount, Assistant General Manager                                           314-244-8112
Quentin Schmidt, Quality Control Manager                                        314-244-8105
Dan Vornberg, Environmental  Manager                                           314-933-3143
Walter Nowotny, General Counsel                                                314-991 -7150
                                             2-1

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                                                           Site Visit Report: Doe Run  Fletcher
Missouri Department of Natural R^ources
Jim Burris, Division of Environmental Quality                                     314-785-0832

Bureau of Land Management
Bibi Booth, Hazardous  Materials Coordinator                                      703-461-1334
Jetf Carroll, Wildlife Management Biologist, Rolla Office                           314-364-0203

Forest Service
Lynn McClure, Forester                                                         314-729-5532
Richard Sibley, Appraiser                                                        314-364-4621

EPA
Steve Hoffman, Chief,  Mine Waste Section,
       Office of Sol id  Waste                                                     703-308-8421
Ron Ritter, Region VII                                                          913-551-7005
Carl Blomgren, Region VII                                                      913-551-7680

Science Applications International Corporation
Ingrid Rosencrantz, Environmental Scientist                                       703-734-2508
Joseph Rissing, Geologist                                                        703-734-4366

Participants in the site visit were provided an opportunity to comment on a draft of this report.
Comments were submitted  by The Doe Run Company, the Bureau of Land Management (BLM), and
the Forest Service. Doe Run Company comments and EPA's responses are presented in Appendix A.
BLM and Forest Service comments  and EPA responses are presented in Appendices B and C,
respectively.

2.1.2  General Description

The Fletcher facility is  located approximately 80 miles south-southwest of St. Louis, and 25 miles
south of Viburnum,  Missouri, in Reynolds County (Figure 2-1).  The Doe Run Company also
operates 5 additional mines and 3 mills on the Viburnum Trend, part of the New Lead Belt.  The
Fletcher operation was  built and operated by the St. Joe Minerals Corporation between 1965 and
1981. The Fluor Corporation purchased St. Joe in 1981.  Doe Run was formed in 1986 when St. Joe
and Homestake Mining Company combined their lead-zinc-copper assets in Missouri in a general
partnership.  In 1990, Fluor purchased all of Homestake's interests, making Doe Run  a wholly owned
subsidiary corporation of the Fluor Corporation.

The Fletcher mine and  mill extract and beneficiate a dolomitic lead-zinc-copper ore typical of those
deposits found on the Viburnum Trend.  The Fletcher surface facilities  are approximately 1180 feet
above sea level.  The mine workings are located between 1000 and 1120 feet below ground.  Access
to the mine is by two 12.5  foot diameter shafts located about 100 feet apart.  Construction of the
shafts was completed in 1965.
                                             2-2

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                                Sue Visit Report:  Doe Run Fletcher
Figure 2-1.  Area of South East Missouri
                  2-3

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                                                            SUe Visit Report: Doe Run Fletcher
Shaft Number 30 is the deepest, extending  1344 feet below the surface; it is used to lift ore to the
surface and Supply air to the mine.  Shaft Numoer 31 provides access for men and materials to the
mine. The mine is an open stope room and pillar design; rooms are 32 feet square, pillars are 28 feet
square.  Mine production capacity is 6000 wet tons per day, 5 days per week. Current projections
are that mining operations will end in 2005 and that 44 million tons of ore will have been removed.
The mill began operation early in 1967 producing lead, zinc, and copper concentrates using standard
floatation methods.  Mill capacity is 5000 tons per day, 6 days per week. Lead concentrates are
transported to smelters in Herculaneum, Missouri, zinc concentrates are sent to Sauget, Illinois and
Bartlesville, Oklahoma.  Most copper concentrates are trucked to Bussen Quarry in Missouri where
they are stored before being shipped overseas.

Surface facilities occupy approximately 320 acres owned by The Doe Run Company.  The Company
holds approximately 2000 acres of surface rights in the area and a large area of leased  mineral rights
on public land (Figure 2-2).  As part of their application required by Missouri's new Metallic
Minerals Waste Management Act, which became law on August 28, 1989, the Company submitted a
map indicating property rights as of February 1990.  Doe Run holds surface and/or mineral rights for
contiguous portions of Sections 13,  14, 23, 24,  and 25, Tier 32 North, Range 2 West, and Sections
18, 19, 29, 30, and 31, Tier 32 North, Range 1 West (Doe Run, Feb, 1990). As part of the Fletcher
Development Contract between the Doe Run  Company and the United States of America, an
additional  3,845.65 acres of public land in the Mark Twain National Forest  are leased to Doe Run by
the Bureau of Land Management (BLM) through 2 separate leases.  Lands held by other persons total
339 acres.  Doe Run estimates that 60 percent of Fletcher production comes from National Forest
Land. As of 1981 a total of 6,319.65 acres of leased and owned surface and/or mineral rights were
held by the Doe Run Fletcher Division (USGS, Vol. II, 1981). In 1986, the Fletcher Division held
9,102 acres of mineral rights, owned or leased, in addition to  the area occupied by the surface
facilities.  Doe Run also holds a prospecting permit (ES-035967) for 2376.66 acres in Reynolds
County. This permit was originally issued  to Homestake Lead Company of Missouri in November
1986 for a two year period; it  was to be reissued in November 1991 for another 4 years (BLM letter,
1991).

2.13  Environmental Setting

The Fletcher facility is located on the Ozark Plateau in Southeastern Missouri and is surrounded by
the Salem-Potosi Ranger District of Mark Twain National Forest.  This area is in the USGS seismic
zone m.  The immediate site is bordered on all sides by dense oak-hickory and oak-pine forests, and
maples and sycamores are prevalent.  There are no private residences in the immediate vicinity of the
mill or tailings impoundment, however, a few private residences are located along the Bee Fork,
downstream from the  tailings dam.  These residents use shallow wells or surface water sources such
as springs for drinking water.  The primary economic activity in the area, other than mining,  is
logging (Allgood, 1979).
                                              2-4

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                                      Site Visit Report: Dot Run Fletcher
                                            ^-jSX^lUi/  ?-Y V
1 ' *•  ;; . v>   ?  / .-viv
'/ i,-\-i iS'   .' -x ' •/
                                ^^^•jM-T«pd
                                Xi ^-^7. *V -rC ? '< ' & ••\\f~V^
                                S^^V^J .-i-Mi
r>.  -.r-*
  A  i ,',iLN--^.y / ,n

          Figure 2-2. Topographic Map of the Site Area (modified)
                            2-5

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                                                            Site Visit Report:  Doe Run Fletcher
The landscape is a highly weathered surface, dating to circa 500 million years before present.  Slope
angles in the region vary from 7 to 40 percent.  The Missouri General Soil Map classifies soils in the
region as alfisols and ultisols.  Local soils are characterized as having clay horizons with chert, and
low base saturation.  Soil thickness in the region varies from 4 to 50 feet thick.  Karst features are
present and  affect the surface hydrology.

According to information presented during the site visit, there are no threatened or endangered
animals or plants  in the immediate area, however, it was noted during the visit that some birds of
prey winter  over in the vicinity. Grasshopper Hollow is located south of the Fletcher tailings dam
across Bee Fork.  The  Nature Conservancy believes that the area is a critical wetland.  Doe Run owns
the surface and mineral rights for the lower reaches of the Hollow and the mineral rights for most of
the upper reaches.  The Company has given the Nature Conservancy a lease to manage the surface for
conservancy purposes.   Comments received from EPA Region VII indicate that the Hollow is within
or near the range of the Grey Bat (Myodis Soditos), which is an endangered species.

2.1.3.1   Climate

Southeast Missouri is dominated by  both dry continental air masses from the western plains and
humid tropical air from the Gulf of Mexico.  The average annual temperature and  precipitation in
Reynolds County is 60° F and 44 inches, respectively. The average annual  runoff is 16 inches.
Roughly 40 percent of the precipitation falls from May through August in the form of thunderstorms.
At times these storms generate  more than 10 inches of rainfall in a 24 hour period. Up to 12 inches
of snowfall  can be expected annually (Mineral and Water Resources of Missouri, 1967).

2.1.3.2   Geology

Deposits of base metal ores occur in Cambrian age sedimentary rocks surrounding a dome of
Precambrian rocks that form the St. Francois Mountains.  The sedimentary rocks are thought to have
formed reefs around the Precambrian dome.  Mineralization occurs throughout the sedimentary
deposits and includes lead, zinc, copper,  nickel, cobalt, and silver metals. In a typical section, the
Lamotte Sandstone lies unconfonnably above the Precambrian rocks, pinching out against the dome
(Figure 2-3).  The Bonneterre Formation is conformable widi the Lamotte Sandstone, and is the
lowest carbonate rock  formation in the region.  Originally deposited as a limestone, it was most likely
dolomitized during or  soon after lithification. It is theorized that base metals were deposited by
migrating hydrothermal solutions in the Bonneterre Formation.  The Bonneterre hosts the richest lead
ore in the sequence (Mineral and Water Resources  of Missouri, 1967; USGS, Vol. II,  1984).

The Davis Formation  overlies the Bonneterre and consists of interbedded shales, carbonates,
siltstones, sandstones,  and conglomerates.  These sediments are less permeable than the underlying
formations  and may have acted as a cap on the reservoir.  Other Cambrian formations,  in ascending
order through the section, include the Derby-Doerun, Potosi, Eminence, and Gasconade dolomites.
                                               2-6

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            SOUTH
FLETCHER MINE
NO  3O SHAFT
                                                                                                 NORTH

                                                                                         DAVIS  SHALE
                                                                                                      S ZONE
                                                                                   LOWER  fiONNETERRE
                                                                                               ——	
                                                                                   LAMOTTC  SANDSTONE
                                    I
                          I  ttJOMETER
                                                                      FLETCHER
                                                                      NO.  30 SHAFT
                                                                                                         EAST
                             900 METERS
                                 Figure 2-3.  Cross-section of Geology From USGS Reports
(Source: USGS, Vol. II 1981)
                                                                                                                        <%

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                                                             Site  Visit Report:  Doe Run Fletcher
The average thickness of these units above the Bonneterre formation is 800 feet (Hydro-Search, 1990;
USGS, Vol. II, 1984).

At the Fletcher mine the Bonneterre Formation is approximately 150 feet thick.  Different facies
observed in the mine include offshore deposits, aJgaJ stromatolites, back reef carbonates, reef
complexes, off-reef sands, and shelf carbonates. These are characteristic of a barrier reef system
associated with the St. Francois Mountains.  Both the mines in the Old Lead Belt, located northeast of
the St. Francois Mountains, and those in the New Lead Belt, or Viburnum trend, are centered on
these reef deposits (USGS, Vol. II, 1984).

The  Fletcher mine is located in the southern portion of the Viburnum trend.  The trend extends 30
miles north to south and is located on the western flank of the St. Francois Mountains which lie 40
miles to the east.  The richest mineral bearing zone of the Bonneterre  Formation in the Fletcher mine
is composed of porous, thick-bedded oolitic dolomite.  Mineralization  at Fletcher extends 5 miles
north to south. The northern end contains the richest ore, mineralization is up to 1000 feet wide and
averages 20 feet thick.  To the south, the ore body narrows to 200 feet and the grade diminishes
(USGS, Vol. II, 1984; MMWMA, 1990).

The  average concentration of values in the Fletcher mine ore is: galena (5.5%), sphalerite (1.0%),
and chalcopyrite (0.3%).  Gangue minerals are calcite, dolomite, pyrite, and marcasite.  Galena
occurs as open-space  filling in banded disseminations and as thin seams along bedding planes.
Sphalerite also occurs as banded disseminations, usually in association with high-grade galena
mineralization.  In the typical hand specimen, fine grain sphalerite is difficult to  distinguish from the
brown color of the dolomites. Chalcopyrite occurs as thin bands at the base of galena mineralization,
but may form as crystals in open-space  fillings.

2.1.3.3    Hydrology

Surface and subsurface hydrology in the region are controlled by karst formations in the carbonate
system.  Information  concerning the regional groundwater is limited and therefore not well
understood.  Two primary aquifers are  identified in the profile below  the Fletcher facility.  The upper
aquifer is located in the Derby-Doerun, Potosi, Eminence, and  Gasconade dolomites, extending to
800 feet below the surface.  Flow in this aquifer is probably controlled by local topography.  Wells in
this  unit may yield between 50 and 600 gallons per minute (gpm).   The lower aquifer is in the
Bonneterre-Lamotte Formations, found  at depths greater  than 1000 feet below the surface.  Flow  in
this  aquifer is controlled by regional gradients of the Ozark Plateau. This aquifer may yield between
 10 and 100 gpm.  These aquifers are separated by the shales of the Davis Formation,  which forms an
aquitard (Hydro-Search, 1990).
                                               2-8

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                                                            Site Visit Report:  Doe Run Fletcher
Water chemistry of the upper aquifer (Potosi Formation) taken from the northern end of the
Viburnum trend indicate a caJcium-magnesium-bicarbonate type water having a total dissolved solids
(TDS) concentration of 250 mg/1.  Base metal concentrations are low, with only zinc showing a
concentration of 0.1 mg/1.

Surface water in the vicinity of the Fletcher mine drains south to the Bee Fork.  This part of the
Black River drainage basin drains  most of the Viburnum trend.  Bee Fork is typical of upland  Ozark
streams, with a TDS of 62 mg/1, less than  1 mg/1 suspended solids, and hardness of 43 CaCO3
equivalents. The mill facility and  tailings impoundment are located in the West Fork Hollow. Its
upper reaches drain into the Fletcher tailing impoundment.  The mine water pond is located in the
unnamed Hollow west of West Fork hollow. Streams in these watersheds flow intermittently and are
described as wet weather creeks.  A  report by Hydro-Search stated that streams in West Fork Hollow
and the mine water pond watersheds are "water losers," since most of the surface water is lost to
bedrock in  the karst terrain (Hydro-Search, 1990).
                                             2-9

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                                                             Site Visit Report:  Doe Run  Fletcher
2.2     FACILITY OPERATION

During the first half of the 1980's, depressed metal prices and labor disputes hampered operations
throughout the New Lead Belt. When the Doe Run Company was formed in 1986, the Fletcher mine
and mill were closed.  Doe Run re-opened the Fletcher facility in 1987 with a 3 year plan to update
the mill facility and improve process control.  Work included an updating of the mill building
structure,  new tailings and mill water return pipelines were installed, and the crusher was overhauled.
Recovery  rates are 97 percent for lead and 80 percent for zinc.

The Fletcher mine/mill surface complex covers approximately 20 acres excluding the tailings pond.
Support facilities are located inside a fenced yard.  The 2 primary structures are the service and
concentrator buildings.  The service building houses the offices,  boiler room, hoist room, control
room, eating room, locker facilities,  and the surface supply house. The concentrator building is 3
stories high and  houses the mill equipment from the secondary crusher through final concentrates
including the ball and rod mills and flotation  cells.  Individual rooms include the console room,
sample analysis room, and offices. The reagent storage room is on the second floor of the
concentrator building, above the main floor, and contains a 6,200 gallon tank of mixed alcohol
(frothing agent), a 6,155 gallon tank of ammoniated cupric chloride (CuNH*Cl, activator for
sphalerite), and two 4,100 gallon tanks of zinc sulfate (depressant for sphalerite).  Dry reagents are
also stored in bags and closed drums depending on the amount used; these include starch (depressant
for copper flotation),  caustic soda (used with starch), xanthate (primary collector for galena and
sphalerite), sodium cyanide (depressant for iron sulfides), sodium dichromate (lead depressant in
copper and zinc circuits), and sodium dioctyl sulfosuccinate (filter aid).

Separate from these buildings are tanks containing: No.  1 and 2  fuel oil (5 tanks, total 40,500 gal.),
sulfur dioxide (10,000 gal., for pH regulation in copper flotation), liquid petroleum gas (2x30,000
gal.), hydraulic oil (3 tanks, total 12,500 gal.), and unleaded  gasoline (2000 gal.).  Most of these
tanks have containment walls around them.  According to the March 1991 Emissions Inventory
Questionnaire (EIQ) all tanks are fitted with fixed roofs.  Lubricating oil is stored on the surface in
drums under a roof.  Detonator caps and explosives are stored underground.  A 2 million gallon
asphalt lined mill water reservoir is located 100 feet above and 450 feet west of the service building.

Automation is an important factor  in process  control at the Fletcher mill. Automatic grinding control
and level-sensing devices installed on the flotation cells control the flow through the mill.  A Courier
30 Cm-stream X-Ray  Analyzer and Proscon Process Control and Management System was installed in
1989.  The X-Ray Analyzer is used to assay  6 process streams including: feed to the flotation cells,
final lead, zinc,  and copper concentrates, and tails. Data generated are in percent concentration of
lead, zinc, copper, and iron.   The Process Control and Management System has helped to stabilize
Doe Run's mill  process and improved recoveries (Jones, 1991).  Additional information on this
system is  presented in Section 2.2, Mill Operation under Process Control.
                                              2-10

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                                                             Sue Visit Report: Doe Run Fletcher
As part of their pollution prevention effort following the re-opening of the Fletcher facility in 1987,
Doe Run is participating in EPA's 33/50 Program.  This is a voluntary pollution prevention program
to reduce  releases and off-site transfers of 17 toxic chemicals by 33 percent by the end of 1992, and
by 50 percent by the end of 1995. Changes in metallurgy and automation produced a 6 percent
increase in concentrate quality at the mill, thereby reducing smelter slag volume and  containment
content.

2.2.1   Mining Operations

The  mine  is centered around the shafts,  extending more than  1 miie north of the shaft and 1.5 miles
south (Figure 2-2).  Vertically,  the mine uses 2 main levels (Figure 2-4). The upper level is the main
mining level  and location of the underground offices, storage areas, and maintenance shops. The
mine employs 65 people underground.  Blasting material (ammonium nitrate and fuel oil (ANFO) and
dynamite), diesel fuel (5,000 gallon tank), hydraulic oil (55 gallon drums), and lubricants are stored
underground. All the underground equipment is diesel powered.  The shop consists of 3 bays for
performing all vehicle and equipment maintenance.  Mine wall surface areas near the shops and office
areas are painted with Bondex and latex  every 3 to 5 years to reflect more light.  Fletcher receives
explosives from deliveries by the distributor on rounds to Doe Run operations. The lower level
covers a smaller area and is the location for the sumps used to remove mine water and the
underground ventilation system.

Mine water is pumped from the mine at  a rate of 3,000 to 3,750 gpm. Water collects in 3 large
sumps, one each located at the north, central, and south ends of the mine. The largest sump is 200
feet wide, 300 feet long and 30 feet deep. According to Doe Run personnel,  an oil skimmer is used
at each sump to remove any waste oil from the surface of the sumps; at the time of the visit, all 3
sumps  were working. Seven large turbine pumps  remove water from the mine through a pipe in shaft
number 30.   Small amounts of mine water are used for drilling and dust control for the jaw crusher
and are supplied throughout the mine in  a 2 inch pipe.

Ventilation is supplied by six 5  foot diameter air shafts.  Two are located at the north end, two near
the main shafts and two at the south end of the mine. The shafts supply air to the upper and lower
mine levels.  Air is pulled into the mine using Joy Axivane fans.  Mine air is exhausted out shaft
number 30.  Air flows through the mine at a rate of 240,000 cubic feet per minute (USGS, Vol. II,
1981).

The Fletcher mine uses an open stope room and pillar design to extract the ore. Current ore
production capacity is 6000 wet tons per day, or about 1.44 million tons per year.  The mine operates
5 days per week, using 2 shifts  each day for production (blasting and hauling) and maintenance and 3
shifts to hoist the ore to the surface. An even pillar pattern is maintained and each pillar is 28 feet
square and 32 feet apart. The height of  the mine opening is determined by the ore thickness.
                                             2-11

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                                                          Sue Visit Report:  Doe Run Fletcher
           SECTION  THTOUGH S***FT CENTEPHNES
                        Figure 2-4.  Cross Section of Shafts and Mine



(Source: USGS, Vol. D 1981)
                                           2-12

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                                                             Sue Visit Report: Doe Run Fletcher
Ore is removed by drilling and blasting.  Truck mounted hydraulic drills are used to drill holes for
placing explosives.  The Fletcher mine uses both ANFO and dynamite.  The choice of which
explosive to use is determined by whether the holes are wet or dry; when holes are wet, dynamite is
used.  Fletcher uses approximately 80 %  ANFO; 20 % dynamite.  A charging tractor is used to place
the explosives. Typically, with each mining pass (blasting),  18-20 vertical feet of material is
removed across a 32 foot wall to a depth  of 11 feet.  An average round breaks 600 tons of rock.  In
the first pass the upper ore zone is removed; if ore grade material remains in the roof after the first
pass, the ore removed can be used as a platform for additional drilling and blasting of the roof.
Subsequent downward passes remove the bottom until the lower limit of the ore body is reached.  The
typical ore thickness at Fletcher  can be as much as 110 feet,  with an extraction ratio of 78 to 80
percent.  At the end of mining activity, it is possible that some of the high-grade pillars may be
removed.

Each drilling and charging shift ends by blasting the ore.  The next shift loads and hauls the blasted
ore, while a drilling crew  prepares to blast in another  location.  Loose ore is loaded using Caterpillar
988B and 988C front end loaders equipped with 10 ton capacity buckets.  The loaders fill I or two
Caterpillar 63ID SO ton capacity haul trucks.  These trucks haul the ore from the stope to one of two
5000 ton ore pockets located near shaft 30 for dumping. Depending on the distance to the ore
pocket, the average time to remove, or muck, the blasted ore is 2 to 3 hours.  Haul roads in the mine
are maintained by a grader.  Road surfaces are made of mine development rock crushed to  less  than 2
inches.

Primary crushing is done underground at  Fletcher.   The 5000 ton ore pockets feed down a chute to  an
Allis-Chalmers 32 by 42 inch jaw crusher.  Output from the  crusher is less than 6 inches in diameter.
The crushed ore is fed  into a measuring hopper; the hopper empties into one of two 8.5 ton ore skips,
which carry the ore to the surface.  The skips make a total of 30 trips per hour.  At Fletcher, the ore
hoisting operation is automatic.   Each ore skip empties from  the bottom into the 1,000 ton ore bin
located on the west side of the mill building along side the headframe of shaft number 30.

2.2.2   Mill Operation

The mill operates 6 days a week, 3 shifts each  day,  beneficiating up to 5,000 tons of ore  per day.
The surface operation employees 15 people.  The staff includes a mill superintendent, metallurgist,
technician and a sample man; each shift has a foreman, operator, and 2 helpers.
The ore from the mine contains an average of 5.5 percent galena, 1 percent sphalerite, 0.3 percent
chalcopyrite, and 3 percent moisture.  Doe Run estimates that current water usage in the mill
averages 2000 gpm (2.9 million gallons per day (GDP)). Mill water is supplied by  the 2  million
gallon reservoir located 400 feet west of the mill complex.  The reservoir is supplied by water
recycled from the tailings impoundment.  Mine water is added as necessary as makeup, however, the
bulk of the mine water is discharged to the mine water pond.  Based on ratios established in the
                                             2-13

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                                                              Site VLsif Report:  Doe Run Fletcher
USGS Mining and Reclamation Plan, clarified tailings water is currently pumped to the mill water
reservoir at a rate of 1,350 gpm (1.9 million GPD).

The Fletcher mill process is described as a highly automated 3 step process consisting of crushing and
grinding, flotation, and filtering of the final concentrates (Figure 2-5). Crushed ore from the  1,000
ton storage bin is delivered by conveyor belt to a screen that separates feed into greater than and less
than 0.75 inches (2 cm) fractions. The oversize material is fed into the secondary crusher
(Hydrocone type; no water added) and crushed to less than 1 inch (2.65 cm).  Dust generated by the
crusher collects in a sump and is returned to the mill  circuit.   Undersize material from the screen and
the secondary crusher drop to a common belt feeding the rod mill  feed box.  Through-put to the rod
mill ranges between 200 to 250 tons per hour.  Sumps are located below the lead, zinc,  and copper
flotation circuits and collect any spills or water generated by the mill.  Each sump returns solution
back to its corresponding flotation circuit.

2.2.2.1   Grinding

Crushed ore, water, and the first reagents (zinc sulfate [1], depressant; xanthate [2], collector; and
sodium cyanide [6], depressant) are  mixed before entering the rod mill.  Numbers in brackets
correspond to locations on the flow sheet  (Figure 2-5) where reagents are added; Table 2-1 describes
the function of the reagent and the nominal quantity used.  The rod mill is an Allis-Chalmers,  12 feet
in diameter  and 15 feet long.  Output from the rod mill enters a sump where additional water is
added. A pump transfers the ore slurry to 2 cyclone classifiers.  A particle size monitor controls the
feed to the flotation circuit (cyclone overflow); the cyclones pass 55 percent -200 mesh.  Underflow
material from the cyclones can be routed in one of two  ways,  either directly to the ball mill feed or
the "Skim Air" unit.  Typically, cyclone underflow material is routed to a ball mill (Allis Chalmers,
14 feet in diameter and 16 feet long). Output from the  ball mill enters the sump shared with the rod
mill and is returned to the cyclones.  Particle residence time in the grinding circuit ranges from 10 to
15 minutes, requiring  an average of 2.5 passes before passing to the flotation cells.  The slurry
contains about 45 percent solids and exits the grinding circuit at approximately 235 tons per hour.

The Skim Air or flash flotation machine is designed to beneficiate high-grade galena minerals from
the cyclone underflow before additional grinding, while the particles are still quite large. In normal
grinding circuits minerals with high specific gravity would be returned to the ball mill.  The system is
used  infrequently at Fletcher.  When operating, it makes a particle size cut that is more than 65
percent -200 mesh, primarily separating large galena particles and some copper (both referred  to as
values) from the finer mineral values and gangue.  The froth, or heads, containing coarse values is
sent directly to the lead-copper conditioner cells, further along in the flow sheet (Figure 2-5).
Tailings from the skim air system are returned to the ball mill feed.
                                               2-14

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                                                         Sue  Visit Report: Doe Run Fletcher
                                                    flHJUCTD 1M1




                             Figure 2-5. Fletcher Mill Flowsheet




(Source: The Doe Run Company)
                                           2-15

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                                 Table 2-1. Flotation Reagents, Their Function, and Usage at the Fletcher Mill

FLOWSHEET
LOCATION
1
2
3
5
6
7
9
10
11
12
16
CHEMICAL
Zinc Sulfate
Sodium Isoprophyl Xanthate
Isoprophyl Ethyl Thionocarbamate
Mixed Alcohol
Sodium Cyanide
Anunoniated Cupric Chloride
Sulphur Dioxide
Starch
Caustic Soda
Sodium Dichromate
Sodium Dioctyl Sulfosuccinate
FUNCTION
Depressant for sphalerite
Primary collector for galena and sphalerite
Collector for sphalerite and chalcopyrite
Frothing agent
Mineral depressant
Activator for sphalerite
pH regulation for copper flotation
Lead depressant
Mixed with starch
Lead depressant in copper flotation circuit
and zinc circuit
Filter aid to improve concentrate dewatering
USAGE
LBS/TON1
1.600
0.70
0.010
0.050
0.002
0.210
0.600
0.090
0.030
0.057
0.140
TONS/YEAR2
960
857
6
30
1
126
360
54
18
34
8
K>
       (Source: The Doe Run Company)
              'Based on nominal usage per short ton.




              2Annual Consumption:  nominal usage * average mining rate of 1.2 million short tons per year.

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                                                              Sue Visit Report: Doe Run Fletcher
2.2.2.2    Flotation

Flotation consists of 3 steps - roughers, cleaners, and re-cleaners - each producing a higher grade of
concentrate than the preceding step.  Each step in the flotation process produces a froth, and tailings.
Reagents are used throughout the process to separate metal values from gangue and one metal from
another. Ore slurry from the cyclones enters a feedbox, a frothing agent (5] is added and the solution
flows to the lead-copper roughers.  These make the first cut by separating lead and copper from zinc
and gangue minerals.  The roughers are composed of six 500 cubic foot Denver flotation cells, with a
junction box  between the 3rd and 4th cell.  Rougher cells use agitators powered by electric motors to
keep the slurry suspended and inject air  to provide bubbles for collection of lead and copper values.
The froth  flows over the lip of the  cells  into launder where a water spray is used to collapse the lead
and copper-laden bubbles and form a slurry.

This slurry is pumped to the lead-copper cleaning circuit.  Tailings from the lead-copper roughers exit
the cells and  are pumped to the  zinc conditioner, located at the head of the zinc circuit.  The
lead-copper cleaners and re-cleaners are in series with each other.  Froth containing lead and copper
concentrates  from the roughers enters the cleaner circuit. The cleaner and re-cleaner circuits consist
of 5 cells  each.  Both types of cleaners use agitation only;  air is provided by the vigorous agitation
motion. Froth from the cleaner is  pumped to the re-cleaner; tailings are pumped back to the
distributor that feeds the lead-zinc roughers and passed through the system again (Figure 2-5).  The
tailings contain fugitive lead and copper minerals as well as zinc and gangue minerals.  In the
re-cleaner a higher grade lead-copper concentrate froth is collected in the launder and pumped to the
lead-copper absorber-conditioner; tailings pass to the cleaner cells. The conditioner consists of 3 cells
and functions to mix to the following reagents, a pH adjuster [9], depressant [10],  and starch [11].
The conditioned concentrate is passed to the copper rougher.  The pH of the conditioned pulp is 4.8.
This is also the point in the flotation circuit where  concentrate from the Skim Air system would enter
the flotation circuit.

The copper rougher consists of 6 cells; agitators are used with air injection to produce a froth of
copper concentrate and a tailing of lead concentrate.  Lead concentrate is pumped to the lead
thickener.  The copper concentrate is pumped to the copper cleaner.  Froth from the  copper  cleaner is
passed to  the re-cleaners. Tailings are pumped back to the copper rougher and passed through this
sub-system again.

Between the copper cleaner and re-cleaner,  a lead depressant [12] is added that further refines the
copper froth produced by the re-cleaners.  Copper  concentrates from the re-cleaners are collected and
pumped to the copper thickener. Tailings from the re-cleaners are returned to the copper rougher.

The Fletcher zinc  circuit was in the process of being updated during the site visit.  New rougher cells
were being installed and are now on line.  A new  system of column cells is to replace existing cleaner
                                               2-17

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                                                              Site Visit Report:  Doe Run Fletcher
cells. These cells are projected to improve zinc recovery by 2 percent, up to a total recovery of 80
percent.  They will not use mechanical agitators to suspend the feed.  This discussion will focus on
the zinc circuit as it existed during the site visit.

The zinc feed pump box  pumps tailings from the lead-copper rougher cells composed of dolomite,
zinc, and water as well as tailings from the zinc cleaners along with additional frothing agent (5]  and
an activator for sphalerite [7] to 5 zinc rougher cells. A lead depressant [12] is occasionally added to
the float from these cells before they are pumped to  the zinc cleaners  and re-cleaners.  The  depressant
minimizes the amount of lead passing with the zinc concentrates in  the cleaners.  Tailings from the
rougher cells exit the mill to the tailings impoundment.  The zinc flotation circuit uses a cleaner and
re-cleaner similar to the lead-copper system; however, in the current system a re-re-cleaner  is used to
produce a higher quality  concentrate. The zinc float concentrate is  pumped directly to the zinc
thickener.  Tailings from the cleaner cells are returned to the conditioner tank and travel back through
the system.

Each of the concentrates  are pumped to a Eimco thickener that functions as a solid/liquid separator.
The copper  tank is 30 feet in diameter and 14 feet deep. The zinc tank Is 40 feet in diameter and 14
feet deep. The lead tank is SO  feet  in diameter and 14 feet deep.  Rakes in the bottom of the tank
move the concentrates toward a center point in the tank. Underflow from the thickeners is pumped to
the filtration circuit at 70 to 75 percent solids.  Water is recovered from the top of the tank  and
returned to the tailings impoundment.

The tailings exit the flotation circuit from the zinc rougher cells by  gravity.  Composite samples of
the tailings for each shift during 1989 and 1990 were analyzed using atomic adsorption and wet
chemistry; from these samples a yearly composite is  maintained.  Typically, the tails contain 52
percent dolomite, 0.11 percent  lead, 0.02 percent zinc, 0.02 percent copper, and 40 percent water by
volume.  Other constituents include iron and sulfur minerals passing the flotation process. Tailing
solution pH  is 7.8 as it exits the mill.

2.2.2.3    Filtration

Two disk filter systems are in use at Fletcher.  A 4 disk model receives concentrates from either the
zinc or copper thickeners.  When changing back and forth between  zinc and copper the disk filter unit
is cleaned prior to use.  Due to the  low copper  content in the ore, copper concentrates are filtered
approximately once each week.  An 8 disk unit is used continuously to filter lead  concentrates.
Concentrates enter the filtration units containing 75 percent solids and exit containing 92 percent.
The disk filters operate on a vacuum - the disks pull water through the filter allowing concentrates to
accumulate on the surface. As a portion of the disk  emerges from the tank, a burst of air inside each
disk knocks the material off and into a hopper and onto a conveyor  belt positioned below each of the
                                              2-18

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                                                             Site Visit Report:  Doe Run Fletcher
disk filters.  The belt empties into an 8 ton concentrate box stationed on one of 2 turntables.  Each
turntable is equipped with 8 concentrate boxes.

Concentrates are shipped from the Fletcher mill by truck under contract with Doe Run.  Drivers are
trained in the use of the overhead crane used to lift and empty bins into an open-top truck, a cover is
placed on the truck before leaving the mill.  The loading process is completed inside the mill
building.  Lead concentrates are transported to the Doe Run Herculaneum smelter in Herculaneum,
Missouri; zinc is sent to Sauget, Illinois and Bartlesville, Oklahoma. Copper concentrates are trucked
to Bussen Quarry where they are stored before being shipped overseas.

2.2.2.4   Process Control

Automation at Fletcher is most visible in the control room.  In the past the mill processes  were
controlled with a long bank of switches and indicator lights.  These are now being replaced with a
Proscon Process Control and Management System, a Courier 30 On-Streara  X-Ray Analyzer, and an
Expert Display System. The Proscon control system monitors 12 direct control loops for reagent and
tonnage addition and 4 separate control loops monitor grinding.  In addition, 16 analog and 16
discrete inputs monitor other points in the process. The facility plans to add air control, pulp lever,
and discrete motor control to the Proscon system (Jones et. al., 1991).

The Courier 30 X-Ray Analyzer samples the ore fed to the flotation cells, lead slurry, lead tailings,
zinc slurry,  copper slurry, and final tailings every  10 minutes.  Pumps transfer sample slurry from
each point in the process to the analyzer.  Between samples water flushes the sample port clean.
Solutions from each of the 5 sample streams are analyzed by X-ray fluorescence.  A spectrometer and
proportional counter determine relative concentrations of lead, zinc, copper,  and iron. Data generated
are in percent concentration of each in the respective sample streams.

An Expert Display System presents every aspect of the mill process flow,  integrating information
from the Courier 30 and other variables monitored by the Proscon equipment. Presets, or master
controls, determine reagent use and other variables.  Based on information collected throughout the
process the Proscon system or the operator (manually)  can make adjustments to reagent flow rates and
other variables to maximize recovery.  Along with the  concentration information obtained from the
X-Ray unit, the Expert Display shows the rate of reagent consumption in cubic centimeters per
minute.  This information is aggregated into a daily report for the mill.  An  example of the computer
printout for  the Fletcher mill from September 23,  1991 is presented in Figure 2-6.

The report shows recoveries of lead and zinc from the ore feed to be 97.22 percent; and 76.29
percent, respectively. Because of the low copper content in the feed assays,  the copper circuit was
not running on this day.  Usage of reagents in this daily report are all greater than those presented in
Table 2-1 since they represent wet reagent usage.
                                              2-19

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                                                                  Site  Visit Report:  Doe Run  Fletcher
                                                                                         DAY  ENHIM
        SOD HIL1
                    :uET»:
                 11.40   MRS
                 2643   TfiNS
                 232.1   TPM
                                       r (H-tJATiMG T:*E:      47.5
                                       i cumt ciacui OH:   36.o
                            ASSAYS
 PEED
 PB COWC
 :* CtWC
 -:u COM
 TAIL
 6.07
31.07
 3.39
 4.14
 0.31
   BACK CALCULATED
 BULK C3NC   81.32
 ZINC FEED    0.66
 UN
 0.46
 0.72
34.79
 0.23
 0.15
           0.62
           0.46
  ZCU
  o.oa
  0.46
  1.14
 :9.67
  0.05
           0.45
           0.06
                                          ZFI
                                          1.52
                                          1.51
                                          3.66
                                         :7.62
                                          1.33
            1.39
            1.53
                                       DJY TONS
                                       PHODCiCED
                                         :5&&.i
                                         170.2
                                          14.5
                                           0.0
                                         2383.8
                                         2363.6
     IPB

    97.52
     0.37
     0.00
     2.46
                                                       7.3  TPM
                                                     102.7  TPH
 11M

 9.S7
76.29
 0.00
13.7}
        37. tl
         8.U3
                                                                              ZFE

                                                                              6.51
                                                                              1.42
                                                                              0.01
                                                                             91.79
XANTIMTB      313
ZNS04        1131
NACN           38
FIOTHCT-P8     60
  PI REAGENTS
cc/min   Ib/ton
           1.33
         343.60
         0.0083
          0.061
                                                 2N tUGEMTS
                                               ee/ain   Ib/ton
                                    3M4           12      3.24
                                    CUS04         101     36.13
                                                          6.43
                                    101
                                    4«4
                       FKRHUHZN     37
                                                         0.040
                                                             CU
                                                           ec/«n    ib/ton
                                               STARCH        4103       2.51
                                               DICXIWATC     368       0.56
                                               pH/502
                                                    5.67
                           MINIMM ASSAYS
                                                         HAXINUN ASSAYS
     FEED
     PI CONC
     ZN CONC
     CU CONC
     TAIl
 ZP8
 3.44
73.37
 1.67
 3.49
 0.10

94.42
               ZZM
               0.11
               0.34
              48.86
               0.20
               0.09

              26.40
               ZCU
               0.04
               0.09
               0.47
              29.43
               0.01

               o.oo
                xrs
                0.43
                0.96
                0.51
               27.47
                0.82

                 o.o
                                                           82.77
                                                            7.03
                                                            4.13
                                                            1.90

                                                           97.90
                                                          ZZM
                                                          0.31
                                                          1.74
                                                         37.89
                                                          0.23
                                                          3.70

                                                         84.30
                    ZCU
                    0.14
                    1.03
                    4.38
                   30.18
                    0.14

                   16.01
               IFC
               1.93
               6.44
               7.42
              27.96
               1.74

              264.2  TPH
  COUIIEI 30
  NOW F*croi
  H20 DIA6NOS
    PS
  0.9*77
    17.3
  ZN
0.9C32
  10.9
  CU
0.9927
   3.8
                                       rs
                                     0.9900
                                        7.3
                                   SO
                                 0.93H
                                   68.7
  PI      ZN
1.0371   1.0944
 231.3     73.3
  CU
1.03N
  27.2
                                                                     FE      SO
                                                                   1.0413  1.0338
                                                                     30.2  1380.7
                               Figure 2-6.  Fletcher Mill Daily Report

(Source:  The Doe Run Company)
                                                  2-20

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                                                             Sue Visit Report: Doe Run  Fletcher
2.3     WASTE MANAGEMENT

2 J.I   Types of Waste

Large volumes of wastes generated by the Doe Run Fletcher facility include tailings, and waste rock.
Tailings from the mill consist of gangue, reagents and water and are transported as a slurry by
pipeline for disposal in the tailings impoundment.  Approximately 4,500 tons of tailings are generated
per day containing 2.9 million gallons of mill water.  The composite analysis of final tailings
presented in Table 2-2 show small quantities of lead, zinc, and copper and increasing amounts of
manganese, iron, and oxides of magnesium and calcium.

Waste rock, also known as mine development rock, is crushed underground  using a portable crusher.
The crushed rock is used in the mine for road surfacing material. The quantity of waste rock
generated is not known.

Mine water is pumped from the mine at approximately 3,200 gpm and piped to the mine water pond.
It is subsequently discharged into local surface water.  Sampling data generated for the Fletcher
NPDES permit show suspended solids, pH, lead, zinc, copper, and  cadmium to be below limits set in
the permit for the period January 1990 through April 1991. Smaller volumes of other wastes
generated onsite include sanitary sewage, laboratory wastes generated during mill solution testing,
waste oil and other lubricants, used tires and refuse.

2.3.2   Tailings

Tailings from the mill are generated at the rate of approximately 4,500 tpd or 1.4 million tons per
year. They are disposed of in the tailings impoundment.  The Fletcher tailings impoundment lies in
the lower reaches of West Fork Hollow (Figure 2-2).  It covers an area  of 270 acres and has a
drainage area of 902 acres above the main dam.  The Dam is permitted  by the Missouri Department
of Natural Resources (DNR) Dam and Reservoir  Safety Council, permit number MO-30160.

The dam is composed of earthen materials, rock,  and coarse tailings.  A report prepared by the USGS
shows that the dam has an earthen core 30 to 35 feet high composed of native clay soils (USGS, Vol.
II, 1981). A coarse rock Miter blanket on the downstream face of this core drains water into  the
seepage collection pond.  The dam is 2500 feet long.  Its height has been increased to accommodate
the increasing volume of storage needed.  The height is increased using  coarse tailings; fine tailings
are added to the inside face as a seal.  A cyclone  is used to sort the  tailings before depositing them.
The downstream face is maintained at approximately a 3:1 slope.  Missouri adopted construction
guidelines, including earthquake requirements, in 1981. Since the dam was built before Missouri
adopted construction guidelines, the dam has not been evaluated with earthquake loading. The
elevation of the dam was 1,105 feet  above mean  sea level (MSL) as of February 1990.  At that time
plans called for increasing the height of the dam 40 feet to accommodate the remaining tailings
                                             2-21

-------
                                         Table 2-2. 1989 and 1990 Tailings Composites, Fletcher Mill

                                                   (All values in percent unless noted.)
1989 COMPOSITES

Lead Concentrate
Copper Concentrate
Zinc Concentrate
Final Tails
Pb
77.11
3.32
1.91
0.23
Zn
1.08
0.23
57.32
0.22
Cu
0.50
31.25
0.59
0.11
Fe
1.13
28.20
2.40
1.70
Co
0.055
0.59
0.127
0.012
Ni
0.073
0.75
0.133
0.013
Ag
oz/ton
1.07
0.84
13.05
0.109
CaO
1.69
0.27
2.04
27.8
MgO
0.96
0.17
1.40
19.6
Cd
0019
0004
089
0004
Mn
0015
0004
0016
0292
S
14 1
34 1
31 1
0 10
1990 COMPOSITES

Lead Concentrate
Copper
Concentrate
Zinc Concentrate
Final Tails
Pb
78.47
3.34
2.37
0.18
Zn
0.98
0.25
58.35
0.15
Cu
0.41
30.70
0.32
0.10
Fe
0.92
27.65
2.15
1.59
Co
0.052
0.77
0.070
0.009
Ni
0.075
1.02
0.076
0.013
Ag
oz/ton
1.02
0.92
11.57
0.100
CaO
1.55
0.33
1.61
24.0
MgO
086
0.20
0.89
19.6
Cd
0.017
0.004
0.86
0001
Mn
0012
0.003
0012
0.298
S
0065
0037
0012
0008
As
0 044
0 19
001
N/A
to

to
to
       Source:  The Doe Run Company

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                                                             Sue Visit Report:  Doe Run Fletcher
through 2005.  The spillway elevation was 1,093 feet MSL and is regulated under the Fletcher
NPDES permit as outfall 002.  No discharges from this outfall are reported in the information
available for this report.

Since the start of operations in 1965 the configuration of the impoundment has changed to
accommodate additional tailings.  Also the height of the dam has  been raised several times.
Originally, the  mine water pond was located  above the tailings impoundment near the mill.  The mine
water pond was moved to its current location in 1976 (See Figure 2-2).  Either one or two tailings
dams were located below the previous mine water pond;  however, this could not be confirmed since
records for the site were not available.  The current tailings impoundment covers any earlier dams.

As part of the Fletcher Project Application for  Metallic Minerals  Waste Management Area Permit
prepared by SRK,  groundwater monitoring in the area  around the tailings impoundment was
conducted by Hydro-Search, Inc.  Their report is based on information collected from 4 monitoring
wells installed in 1987 and sampled in 1988.  Well locations are identified in Figure 2-2.  Monitoring
well F-l is upgradient of the facility, located in the Potosi ground-water. Wells F-2 and F-3 are
downgradient, located below the tailings dam; well F-4 is near the spillway. The available data for
these wells is presented in Table 2-3.  Data for 1988 show that total dissolved solids, lead,
manganese,  and sulfate concentrations at F-2 and F-3 and iron in  F-3 exceed the EPA primary
drinking water standards. Data from well F-2, in the shallow ground water, show concentrations of
heavy metals including cobalt,  copper, nickel, lead, and zinc to be higher than those for the
upgradient well F-l in bedrock. Chromium was also found in Well F-3. Hydro-Search reported  that
results of the initial samples from  wells indicated downgradient water in both the bedrock and
alluvium were impacted by  the tailings impoundment.  The report recommended that wells F-2 and F-
3 should be sampled bi-annualiy for TDS, major ions, cadmium, and the metals listed above
(Hydro-Search, 1990).

As part of the permit with DNR, quarterly inspections of the dam are required.  The quarterly reports
for the first two quarters of 1991 prepared by E. George Tapp and William G. Huffman indicate that
the top of the dam  had several  erosion gullies.  The reports indicate that the erosion problem was  first
observed in  August 1989. By the second quarter of 1990, all of the contour terraces on the face of
the dam were cut or breached by erosion gullies.

In the August 30, 1991 Report it is noted that Druy Construction was recontouring the downstream
face  of the dam. The phreatic  levels within the dam are routinely monitored, as is the seepage into
the seepage return pond.

In April 1990, concurrent with their tailings dam permit renewal,  Doe Run submitted a request to the
DNR Dam and  Reservoir Safety Program for approval  of a phased expansion of the tailings dam.
SRK prepared the engineering report; a copy  was not available for this report.  The permit was issued
                                             2-23

-------
                                                   Table 2-3.  Water Chemistry Data for Monitoring Wells
K)

*r~t*r

I*
ccMoucnvm
total OUeolvod lot Ml (1M)
fluorine (M)
OilorlM (Cl)
tut late (10.)
•1 trite <»£)
•Itroci (HOC)
Oroide (Or)
Oodlta (Be)
9oct*iiui (K)
Celclui (Co)
Mofnotlui (No)
•MOM II
•IcortoiMte
•lUor («•)
Codriui (Cd)
Cooslt (Co)
fhnai'™ (Cr)
Copper (Cu)
Iron (Ft)
Hongcntie (Nn)
•Icket (It)
Leod {«*)
•ntloany (•»
2lnc (In)
Mrcury (Ho)
•runic (Ai)
•olonlui (»*) .
Choalcol Oiyecn Oteand (COD)
total SuwonMd Sol Mi (TSS)
(FIILO MU)
toapcreture (*C)
Conductivity
Altai Inlty
M
"Tewi**1
Crouid-Ueter

7.1
U7
217
•.12
1.0
U.I
-•
.-
••
1.71
O.M
40.2
24.1
200
• -
4. Ml
4. Ml
4.021
4.001
I.M1
4.021
4.M1
4.021
4.021
•*
0.1M
•-
••
• •



17.7
..
•-
**
rettnll.l*
Vourc«i
M«t.
rorai

7.1
IMO
1)14
4.1
n
1101
..
-.
..
u
1.4
110
00
744
--
4. Ml
O.MS
0.021
0.021
0.004
•.021
O.M
0.14
4.UI
• -
0.9











net.
k«c.
uo
4.9
4000
15J4
4.)
101
1412
..
..
..
71
M
441
240
2099
•0.001
0.001
0.44
•.Oil
0.011
•.025
1.2
1.)
4.021
--
40












r
4/07
OA1A
7.1
2710
2292
0.9
99
sa
4
<1.
1.1
S4.0
7.0
240
10
1410
220
4.00}
4. Mi
O.M
4.M7
•••1
4.021
1.2«
0.14
•.03
•0.021
0.12
4.0002
<0.001
4.005
..
•-

19
2111
in
4.0
In
-2
i/M

4.9
WOO
2140
4.1
4M
IB!

..
..
12
4.4
110
170
tt74
..
4.001
4.M1
0.049
4.001
0.014
0.025
0.007
0.10
0.014
..
0.12
..
-.
..
1
14

..
..
--
•-
nrtdlmt IM
1
4/07

7.1
MOO
2420
I.I
107
197
24

1.*
77.0
4.0
2/0
200
1497
270
4.001
4.M!
0.02
4.M7
0.01
4.02!
0.19

4io2I
4.021
0.01
4. 0002
4.001
4.001

--

20

211
7.1
t«r will DM
-3
I/U

7.1
moo
2090
4.1
101
toll

..
..
a
7.7
4M
210
1*97

4.001
4.001
0.021
0.012
0.020
0.011
0.11
0.042
• .Oil
..
1.017

..
..
^
10


...
..
• •

f
4/17

1.7

40
•0.1
2
4

,)
4.1
1.0
0.1
10
4
M
10
4.M!
4.001
4. Ml
4.007
4.001
4.021
D.M
4.021
4.021
4.021
4.001
4.0002
4.005
•O.MS

••

M
4
27
1.1

•4
i/M

4.1
n
42
4.1
2.4

. .


1.0
1.1
12
1
42

4.001
4^001
O.M7
4. Ml
0.012
4.021
0.11
4. an
4.021

0.11

..

s
96

..
w f
..
..

•1^

/
4
11
<0.

v
,
,
4
c
,
,
,
,J
,J
4 001
•O.Htt
4 Ml
4 M7
4. Ml
4 on

4. on
4.021
4 on
4 Ml
4.0002
• 0.001
•o.oos

-•


..

..
1.

2.
S.
Ml ratuM •*• flvM In •IUI(r«M p*r liter (••/!), «u«pt
*n*lyM* by •«• Oui Ctaytoy, C«ntr«l l«k, Hlburaa. NliMurl
0*t« !• fr«* II. JM Hlrwral* C«r»., J«ru*ry, 1904, CwpMit*
                                                                             tnltt). »nt conduct I ylly
i o n°o
                                                                                                                                                                 s;-
                                                                                                                                                                 50
        (Source:  Hydro-Search, Inc., 1990)

-------
                                                            Sue  Visit Report:  Doe Run Fletcher
June  12, 1990, contingent on the Company submitting (1) a plan to repair existing erosion on the face
of the dam and preventing future erosion, and (2) specifications for the saddle dike.  Doe Run
submitted the plans and specifications in November of 1990.  In January of 1991 the DNR Dam
Safety Program notified the Company that their concerns were satisfied, thus completing the permit
renewal process.

The first phase of construction will increase the height of the dam 15 feet to  1,120 feet MSL.  The
spillway will be raised from 1,093 feet  MSL to 1,100 feet MSL.  During the site visit of September
24-25, dam re-facing was complete and construction to raise the height of the spillway had begun.
The cyclone used to sort coarse and fine tailings was being prepared for installation. The second
phase is tentatively  planned for 1996, and will raise the height of the dam an additional 20 to 25 feet.

Seepage from the bottom of the tailings dam  is collected in a pond at the base of the dam where it is
pumped back to the impoundment.  The seepage collection pond is approximately 0.5 acres;  its
drainage area from  the face of the dam  is approximately 15 acres. As reported in the quarterly dam
inspections, pumpback from the seepage collection pond to the tailings impoundment ranged  from  an
average low of 103,000 GPD during the period February through March 1991, to an average high of
238,000 GPD during the period May through June of 1990. Doe Run personnel reported that the
variation is due to seasonal changes. Pumpback for the period June through July of 1991 however,
was 83,000 GPD.  Surface discharge from the pond is regulated"under the NPDES permit as outfall
003.

At closure four surface water bodies will remain in the tailings impoundment, one each located in the
hollows to the east of the main West Fork Hollow drainage (Figure 2-2). Surface water from the
upper reaches of the drainage area will drain to the pond closest to the mill site and flow through each
of the succeeding ponds and then over the spillway. Rip rap will be used to control erosion where
slopes exceed 3:1.   Dry portions of the  tailings will  be vegetated.  Seepage from the dam will be
pumped back to the impoundment until flow stops or its quality improves to allow discharge  into Bee
Fork (SRK, 1990).

2 J 3   Mine Water

Water from the mine is pumped to the mine water pond at an average rate of 4.63 million gallons per
day (MGD).  The mine water dam was built in  1976 and is permitted through the DNR Dam Safety
Program, permit number MO-31141. Its purpose it to clarify  incoming mine water before
discharging it to Bee Fork.  According to the Application for the Metallic Minerals Waste
Management Act, the mine water pond was designed to be converted from a water retention structure
to a tailings impoundment.  Revised  estimates for tailings storage needs indicate this will not be-
necessary.  At closure no water will  flow from the mine, however, the shafts will most likely fill with
                                             2-25

-------
                                                             Site Visit Report: Doe Run  Fletcher
water to within 150 feet of the surface based on water levels in the upgradient monitoring well (well
F-l, Hydro-Search 1990).  Shafts will be sealed at the top of the Davis Formation and the surface.

The pond receives surface water drainage from the 570 acres above the dam.  The dam  is constructed
of compacted earth fill taken from adjacent land.  The surface area of the pond is 22.5 acres, with a
storage capacity of 340 acre feet. The surface of the dam is 1,040 feet MSL, spillway elevation is
1,030 feet, and the normal  outfall elevation is 1,024 feet. Surface discharge from the pond is to Bee
Fork and is regulated under the NPDES permit as outfall 001.  Discharge rates reported in the
quarterly monitoring reports range from 2 to 5 MGD. As discussed above,  sampling data for the
period January  1990 through April 1991 generated for die Fletcher NPDES permit show suspended
solids, pH, lead, zinc, copper, and cadmium to be below limits set in die permit.  At closure pumping
will stop and water input to the pond will be limited to direct infall precipitation and surface water
runoff.  A new equilibrium level is expected to be reached  in 2 to  3 years; at dial time die shore line
will be landscaped and seeded.  Discharge from the pond will continue to flow into Bee  Fork.

23.4   Other Wastes

Sanitary sewage is disposed of in 3 septic tanks located along the north side  of die mill building.
Two of the tanks are capable of supporting up to 200 people, a third is described as a 500 gallon
tank. Laboratory analyses are generally conducted at the Viburnum offices.   Wastes generated at the
Viburnum laboratory during ore  assays and mill solution testing consist of dilute acids and are
disposed of in the municipal sewer system. Used standard truck tires are sold to recyclers; tires from
large machinery are not easily disposed of and are accumulating in a storage area on the west side of
the tailings impoundment (numbers not provided). Refuse is transported  and disposed of in the
Viburnum City landfill (amounts not provided).

The number and volume of wastes regulated as hazardous at the Fletcher facility are small.  Solvents,
waste oil and other lubricants are picked up monthly under contract with  the Safety-Kleen
Corporation.  For die six quarters ending July 1991 an average of  1,765 gallons per quarter of wastes
described as petroleum naphtha (UN 1255; EPA D001) are shipped off site.  In one case, sulfuric
acid wastes generated when a tank was cleaned were picked up by  contract hauler; however, details
such as amounts, were not included in the lab analysis report.  Other RCRA wastes such as old
reagents, have been disposed of by CECOS International (again, amounts are not available).

An inspection of transformers and capacitors conducted in June 1990 identified 6 units containing
PCBs underground.  At this time only one unit containing PCBs remains  underground; one unit
remains in the shop and 4 in the mill building.
                                             2-26

-------
                                                             Site Visit Report:  Doe Run Fletcher
2.4     REGULATORY REQUIREMENTS AND COMPLIANCE.

2.4.1   State of Missouri

The State of Missouri Department of Natural Resources implements three regulatory programs that
affect the Doe Run Fletcher operation.  The Division of Environmental Quality has authority to
implement the National Pollutant Discharge Elimination System (NPDES) program and the Metallic
Minerals Waste Management Act that became law on August 28,  1989.  The Division of Geology and
Land Survey, Dam and Reservoir Safety Program is responsible for permitting and inspecting all
dams greater than  35 feet in height.

2.4.1.1    Water Permit

The current NPDES permit for the Fletcher facility (MO-0001856) was issued by the Division of
Environmental Quality June 30, 1989, and is effective for five years.  The letter transferring the
permit states that the NPDES permit is Fletcher's "new State operating permit, replacing all previous
operating permits." Doe Run and the State agree that the current  permit meets the new Storm Water
requirements under NPDES.

The permit regulates surface water discharge at three outfalls from waste disposal facilities and a
water quality compliance point in Bee Fork.  Outfall 001 is the discharge from the mine water pond.
Outfall 002 is for discharge from the seepage collection pond located below the tailings dam; outfall
003  is the tailings  impoundment spillway.  The tailings impoundment is designed to contain the  10-
year 24-hour storm event.  As determined by the United States Hydrologic map, this equates to 5.8
inches of precipitation. Rainfall exceeding this amount will flow over the spillway (NPDES outfall
002). The Water Quality Compliance Point (004) is located where the road below the tailings dam
crosses Bee Fork (Figure 2-2). The Division of Environmental Quality conducts inspections of the
outfalls and receiving stream annually.

The tailings impoundment is a zero discharge facility as specified by the permit; therefore, discharge
from outfalls 002 and 003 is permitted only when precipitation exceeds the 10 year, 24 hour amount
or as specified in the Ore Mining and Dressing Effluent Limitation Guidelines (40 CFR Part 440,
Subpart J). Any discharge must meet effluent standards specified  in the permit. However, if the
Company is in compliance with the special conditions in the permit and a discharge from outfall 002
or 003 occurs, the Company need only monitor the discharge.  Monitoring required under the special
conditions includes water quality analysis at outfalls 001,  002, 003, and 004 each month; data is
collected and reported to the Division of Environmental Quality quarterly.  Monthly monitoring data
for the 5 quarters ending in  April 1991 show all  samples to be in compliance with standards
established in the permit.  Data reported for outfalls 001 and 004 during the second quarter of 1991
are presented in Table 2-4.  No discharges from outfalls 002 and 003 were reported in the period.
Rainfall is monitored daily and Whole Effluent Toxicity is monitored once per year.  All whole
                                             2-27

-------
                                                    SUe Visit Report:  Doe Run Fletcher
Table 2-4.  Water Quality Data for NPDES Outfalls 001 and 004, Second Quarter 1991
           (Source:  Quarterly Monitoring Report)
Surface Discharge from Mine Water Pond, Outfall 001
PARAMETER
Flow MGD
Temperature Degrees F
Suspended Solids mg/1

pfi units
Oil and Grease mg/1
Lead (Total) mg/1
Zinc (Total) mg/1
Copper (Total) mg/1
Cadmium (Total) mg/1
Mercury (Total) mg/1
(once/year monitoring)
Final
Limits
no
limits
no
limits
20.0
6.0-
9.0
15.0
.30
.73
.15
.05
.001
Results of Analysis
2.52
61
<1
7.8

-------
                                                           Site Visit Report:  Doe Run Fletcher
 Effluent Toxicity data submitted by the University of Missouri at Rolla satisfy the criteria established
 in the permit.

 In June 1987 Doe Run requested  DNR to modify their NPDES permit, allowing treatment and
 discharge of excess runoff as allowed under the Special Conditions in the NPDES permit and the Ore
 Mining and Dressing Effluent Limitation Guideline (Doe Run, 1987a).  Similar requests were made
 by the St. Joe Minerals Corporation in 1985 and 1986.  They proposed to modified their piping
 system to pump water from the tailings impoundment to the mine water pond for treatment and
 disposal.  According to the DNR this change would require Doe Run to submit a new NPDES permit
 application; however,  no correspondence to this effect was obtained.

 In a letter dated November 3, 1987 Doe Run notified the DNR that the Fletcher facility began
 production on November 2, 1987.  The letter also stated that pumping from the tailings impoundment
 to the mine water pond began on  June 6 and ended November 2, 1987 with a total of 400,000,000
 gallons pumped (Doe Run,  1987b).  This volume is approximately 60 percent of the total discharge
 from the mine water pond  through outfall 001 for the five month period.  Monitoring data for the
 NPDES permit show no significant change in quality during this time.

 Doe Run stated that water discharged through the NPDES point met BAT Effluent Limits for mine
 and mill water at all times, and that in the future pumping would not exceed an amount equal to the
 annual precipitation minus  annual evaporation.  The Company stated that water being discharged
 through the NPDES compliance point would be monitored on a weekly basis to meet BAT limits.  No
 additional communication between Doe Run and the DNR concerning this matter is available until a
 letter was sent by Doe Run on August 31, 1990.  In this letter, Doe Run makes a similar request to
 DNR to pump tailings water to the mine water  pond for treatment and disposal.  No additional
 correspondence was available for  this report. Doe Run applied for a renewal of their NPDES permit
 in January 1988.  DNR issued an NPDES permit in June of 1989. In neither the application nor the
 permit was there mention of the request to divert water from the tailings impoundment to the mine
 water pond; however,  the special  conditions of the permit did cite the Ore Mining and Dressing
 Effluent Limitation Guideline.

 In May of 1987 and again in 1990 Doe Rum reported to the DNR that water was discharged  from the
 seepage collection pond (outfall 002) directly into Bee Fork. In  both cases this was due to heavy
 rains exceeding the capacity of the pumps and/or pump failure.  The Company reported that daily
 inspections discovered  the problem and they were studying ways to- install an alarm system to give
 advance warning of problems.

During an inspection by DNR personnel in May of  1991 a black stain was observed on the stream
bottom of Bee Fork where mine water effluent mixes with the stream.  In the inspection report DNR
asked Doe Run to report on the situation in 60 days. The Company responded by contracting with
                                            2-29

-------
                                                            Sue Visit Report:  Doe Run Fletcher
the University of Missouri at Rolla to study the problem and prepare a report by December 1991.
The results of their findings indicate that the black material is manganese, probably MnO:.  Other
constituents may include iron, cobalt, cadmium, lead, and zinc (Doe Run 1992). Based on data
presented in the quarterly monitoring reports, discharge from the mine water pond through outfall 001
contributes up to 80 percent of the flow in Bee Fork during extreme low flow conditions.

2.4.1.2    Metallic Minerals Waste Management

The new Metallic Minerals Waste Management Act regulates disposal of waste from metallic mineral
mining, beneficiation, and processing. Facilities must apply for a permit from the DNR Division of
Environmental Quality.  The application is to include a closure plan and an inspection-maintenance
plan which will ensure the containment of metallic mineral wastes.  Each of the plans must be
coordinated with other environmental permits regulating water quality, air quality, solid waste
disposal, and dam safety.  Since this is a new rule, the Division of Environmental Quality Regional
Office in Poplar Bluff is still in the process of implementation.

Doe Run submitted their Fletcher Project Application For Metallic Minerals Waste Management Area
Permit in February of 1990. The application was  prepared by SRK with support from Hydro-Search,
Inc.  concerning groundwater monitoring information required for the closure plan (SRK,  1990).  A
discussion  of the groundwater monitoring reported in the Hydro-Search report is presented in the
tailings discussion.  Doe Run completed the application requirements including financial  assurance
documents. The application was re-written by  Melaren/Hart and resubmitted to DNR.  The State
issued permit  MM-009 to the Fletcher facility on January 13,1992.  All permit requirements,
including financial assurance, have been met.  A bill pending in the Missouri legislature,  co-
sponsored  by  DNR and the mining industry, may raise the annual fee to $7,500.

2.4.1.3    Dam Safety

The DNR  Division of Mines and Geology,  Dam and Reservoir Safety Program has issued permits for
the Fletcher tailings dam (MO-30160) and mine water dam (MO-31141). An annual inspection of
these structures is required to verify the dams safety. As noted in the tailings impoundment
discussion, inspection reports for 1989 and 1990 identified gully erosion on the face of the dam.  This
was repaired as part of the dam expansion project begun during the summer of 1991.  No problems
were identified with  the mine water dam.

2.4.1.4    Other State Regulations

Construction permits were not required for facilities built before 1980, However, the State does
require facilities to submit an Emissions Inventory Questionnaire (EIQ) annually. In conjunction with
the EIQ, a State inspector conducts an annual inspection.   The inspection conducted in January 1990
examined seven point sources and their control equipment.  Sources having no opacity at the time of
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                                                             Sue Visit Report:  Doe Run Fletcher
inspection include: the ore lift/vent shaft, rod mill, concentrator building, and boiler #2.  Sources
having opacities less than 10 percent include the secondary crusher, boiler #1, and the haul  roads.
Control equipment includes wet scrubbers on the crusher and rod  mill, and a surfactant spray on haul
roads. The other point sources are not fitted with control equipment.

Missouri regulates storage of waste tires under RSMo 260.200 to  260.345 (1990).  This regulation
applies to facilities that store more than 500 whole, cut, chipped or shredded waste tires for more
than 30 days.  Doe Run does not store tires in this quantity,  however, they did point out that disposal
of the large tires is difficult.  The State of Missouri issued Hazardous  Waste Generator Identification
No. 010% to the Fletcher operation for waste oil only.

A violation  was issued to Doe Run in August 1989 following an inspection of the drinking water
system.  The problem was thought to  be related to mechanical difficulties and a high coliform bacteria
count in  samples taken from the facilities.  As required, the Company issued a public notice and
agreed to upgrade the drinking water system. The system was upgraded by the  installation of a
chlorination unit.

2.4.2  Federal Regulations

The surface facility at Fletcher is located  on land owned by the Doe Run Company; however, much
of the underground workings are  on public lands managed by the Forest Service. The BLM has
jurisdiction over mineral rights, the Forest Service manages the surface in  Mark Twain National
Forest.  The BLM and, at that time, The St. Joe Minerals Company entered into the Fletcher
development contract on June  12, 1970 for the purpose of mining  lead, zinc, and copper in the Mark
Twain National Forest.  The main purpose of the contract was to delineate boundaries and establish
ownership of lands in the area of the Fletcher project.

The Doe Run Fletcher Mine has two leases with the BLM totaling 5,980 acres.  The Solid Mineral
Leases BLM-A-047477 and BLM-A-049307 expire May 31,  1993. According to the BLM they will
be renewed  if the operation remains in production.  A Prospecting Permit (ES-035967) was to expire
on October 31, 1991; the BLM noted  that this permit would be extended for an additional four years.
Bonds for all of Doe Run's operations in  Missouri are under  one "Statewide" bond totaling
$1,405,000. The bond covers potential unpaid royalties, lease rental ($1/acre/year), and surface
reclamation  (mainly from exploratory  drilling and vent shafts)(BLM 1991).  BLM and the Forest
Service confer on issues concerning the lease; the Forest Service must review and approve lease
terms. A general operating plan provides guidelines for activities on Forest Service land; a plan  of
operations is prepared for activities such as drilling a  vent shaft. For surface activities on these lands,
a letter of authority from the Forest Service is required.  Activities in non-lease areas require a
special use permit.
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                                                           SUe Visit Report: Doe Run Fletcher
The Environmental Protection Agency prepared a Preliminary Assessment of the Fletcher Facility in
August 1984 because EPA had reason to believe the mining wastes may be hazardous (EPA,  1984).
The recommendation made was to conduct sampling on a low priority basis due to the presence of
heavy metals and hazardous materials in the mine effluent.  Sampling locations include sites
downstream of the tailings pond  in the West Fork Hollow and Bee Fork past the Fletcher property
line.  Background samples were  suggested upstream in Bee Fork.
                                             2-32

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                                                          SUf Visit Report: Doe Run Fletcher
2.5    REFERENCES

Allgood, Ferris P. and Ival D. Persinger. 1979. The Missouri General Soil Map and Soil Association
     Description, USDA Soil Conservation Service and Missouri Agricultural Experiment Station.

BLM, September 30, 1991.  Letter from Jeffrey Carroll, BLM, to Steve Hoffman, EPA  on lease and
     bond information for the Fletcher Mine.

Doe Run, January 1992.  Black Rocks in the Black River or How do You Suppose the Black River
     Got Its Name?  Prepared for Doe Run by Dr. Nord Gale and Dr. Barbara R. Patterson,
     University of Missouri-Rolla.

Doe Run, February 1990. Fletcher Project Application for Metallic Minerals Waste Management
     Area Permit. Prepared by Steffen, Robertson and Kirsten, Lakewood Colorado.

Doe Run, 1987a. Letter from John Carter, Doe Run, to Jim Burris, DNR, on June 10, 1987
     informing the State that changes to the piping system to connect the tailings water to the mine
     water pond were underway.

Doe Run, 1987b. Letter from John Carter, Doe Run, to Jim Burris, DNR, on November 3, 1987
     providing information on the volume of water pumped from the tailings impoundment in the last
     6 months (400,000,000 gallons).

Hydro-Search, Inc.,  1990.  Hydrology and Monitoring Sections of Closure Plan Fletcher Tailings
     Pond Reynolds County, Missouri, February  13, 1990.  Prepared for Steffen, Robertson and
     Kirsten, Lakewood  Colorado by Hydro-Search, Inc., Brookfield, Wisconsin.

Jones, James A. ej. a]., December 1991. Process Control at Doe Run's Fletcher Concentrator.
     Mining Engineering, Vol. 43, Number 12, pages 1407-1411.

Mineral and Water Resources of Missouri, 1967.  Report of the United States Geological Survey and
     the Missouri Division of Geological Survey and Water Resources.  Document No.  19 of the 1st
     Session of the 90th  Congress.

USGS Mining And Reclamation Plan, Volume II, Public Information, April 1981.  Prepared for the
     St. Joe Minerals Corporation Fletcher Division by Impact Environmental Consultants, Ltd.,
     1409 Larimer Square, Denver Colorado 80202.
                                            2-33

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                               Site Visit Report: Doe Run Fletcher
               APPENDIX 2-A

THE DOE RUN COMPANY'S COMMENTS ON THE
        DRAFT SITE VISIT REPORT,
           AND EPA'S RESPONSES
                   2-34

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                                                           Site Visit Report:  Doe Run Fletcher
EPA has revised the site visit report to incorporate ail of the comments submitted by The Doe Run
Company.   In some cases, EPA made minor changes to wording as suggested by Doe Run in order to
attribute the changes to the Company or enhance clarity.  The Doe Run Company submitted
comments  in the form of a mark-up of the draft text.  Their comments are summarized below.
Comment  1:   Page 1, paragraph 2; The Doe Run Company clarified the text concerning Company
              ownership.

Comment 2:   Page 4, paragraph I; zinc concentrates are shipped to Sauget, Illinois and Bartlesville,
              Oklahoma. Copper  concentrates are shipped over seas.

Comment 3:   Page 6, paragraph 2; The Doe Run Company has issued a lease to the Nature
              Conservancy to manage the surface in this area.

Comment 4:   Page 10, paragraph  I; Recovery rates for zinc are 80 percent.

Comment 5:   Page 10, paragraph  3; Individual buildings for storage of blasting caps and explosives
              have been removed.   Blasting caps and explosives are now stored underground; there
              is an oil storage building on the surface.  There is no equipment storage area on the
              west side of the tailings dam.

Comment 6:   Page 10, paragraph  4; Automatic grinding control and level-sensing devices.    Also,
              6 processes, not 5, are analyzed.

Comment 7:   Page 11, paragraph  1; Due to changes in metallurgy and automation,  a 6 percent
              increase in concentrate quality was achieved at the mill, thereby reducing smelter slag
              volume and contaminant content during smelting.

Comment 8:   Page 11, paragraph  3; According to Doe Run personnel, an oil skimmer is used at
              each sump to remove any waste oil from the surface of the sump; at the time of the
              visit all 3  sumps were working.

Comment 9:   Page 11, paragraph  4; Air is pulled into the mine using Joy Axivane fans.

Comment  10:  Page 13, paragraph  1; Fletcher uses approximately SQ %  ANFO; 2Q % dynamite.

Comment  11:  Page 13, paragraph  2; Loose ore is loaded using Caterpillar 988B and 988C front end
              loaders equipped with 10 ton capacity buckets.  The loaders fill 1 or two Caterpillar
              63ID 5Q ton capacity haul trucks.

Comment  12:  Page 14, top of page; delete the following text: "Similarly, mine water is added at the
              rate of . . .[to end of paragraph]."

Comment  13:  Page 14, paragraph  1; Each sump returns solutions  back to its' corresponding flotation
              circuit.

Comment  14:  Page 14, paragraph  2; Recommend the following changes  to this paragraph:  Crushed
              ore, water, and the  first reagents (zinc sulfate [1], depressant; xanthate [2], collector;
              and sodium cyanide [6], depressant) are  mixed before entering the rod mill.  Numbers
                                            2-35

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                                                              Site Visit Report:  Doe Run Fletcher
               in brackets correspond to locations on flow sheet (Figure 5) where reagents are added;
               Table 1 describes the function of the reagent and quantity used.  The rod mill is an
               Allis-ChaJmers, 12 feet in diameter and 15 feet long.  Output from the rod mill enters
               a sump  where additional water is added.  A  pump transfers the ore slurry to 2 cyclone
               classifiers. A particle size monitor controls the feed to the flotation circuit (cyclone
               overflow): the cyclones pass 55 percent -200 mesh.  Underflow material from the
               cyclones can  be routed in one of two ways, either directly to the ball mill feed or the
               "Skim Air" unit. Typically, cyclone underflow material is routed to the ball mill
               (Allis-Chalmers, 14 feet in diameter and  16  feet long}. Output from the ball mill
               enters the sump shared with the rod mill  and is returned to the cyclones.  Particle
               residence time in the grinding circuit ranges from 10 to 15 minutes, requiring an
               average of 2.5 passes before passing to the flotation cells.  The slurry contains about
               45 percent solids and exits the grinding circuit at approximately 235 tons per hour.

Comment 15:  Page 17, paragraph 1; Recommend the following changes to this paragraph: Flotation
               consists of 3  steps, roughers, cleaners, and re-cleaners, each producing a higher grade
               of concentrate than the preceding step. Each step in the flotation process produces a
               froth, and tailings.  Reagents are  used throughout the process to separate metal values
               from gangue  and one metal from  another. Ore slurry from the cyclones enters a feed-
               bjQx, a frothing agent [5] is added and the solution flows to the lead-copper roughers.
               These make the first cut by separating lead,  copper from zinc and gangue minerals.
               The roughers are composed of six 500 cubic foot Denver flotation cells, with  a
               junction box  between the 3rd and 4th cell.  Rougher cells use agitators powered by
               electric  motors to keep the slurry suspended  and inject air to provide bubbles for
               collection of  metal values.  The froth flows over the lip of the cells into a launder
               where a water spray is used to collapse ths metal-laden bubbles and forms a slurry.

Comment 16:  Page 18, paragraph 2 and 3; Recommend the following changes to these paragraphs:
               The Fletcher  zinc circuit was in the process of being updated during the site visit.
               New rougher cells were being installed and are now on line.  A new system of
               column  cells  is to replace existing cleaner cells bv Mav 1992.  These cells are
               projected to improve zinc recovery by 2 percent.  They will not use mechanical
               agitators to suspend the  feed.  This discussion will focus on the zinc circuit as it
               existed during the site visit.

               The zinc feed pump box pumps tailings from the lead-copper rougher cells composed
               of dolomite, zinc, and water as well as tailings from the zinc cleaners along with
               additional frothing agent [5] and an activator for sphalerite [7] to five zinc rougher
               fiSUa.  A lead depressant [12] is occasionally added to the float from these cells before
               they are pumped to the zinc cleaners and  re-cleaners.

Comment 17:  Page 20, paragraph 1; Recommend the following changes to this paragraph: The
               report shows  recoveries  of lead and zinc from the ore feed to be 97.22 percent; and
               76.29 percent, respectively. Because of the low copper content in the feed assays, the
               copper circuit was  not running on this day.  Usage of reagents in this daily report are
               all greater than those presented in Table 1 and no explanation for this is available at
               this time.

Comment 18:  Page 22, paragraph 2; Currently,  waste rock is crushed underground using a portable
               crusher.
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                                                            Sue Visit Report:  Doe Run Fletcher
Comment 19:   Page 24, paragraph 5;  Recommend the following changes to this paragraph:  In the
               August 30,  1991  report it is noted that Druy Construction was in the process of
               recontouring the downstream face of the dam.  The phreatic levels within the dam are
               routinely monitored, as is the seepage  into the seepage return pond.

Comment 20:   Page 26, paragraph 4;  The range of seepage from the bottom of the tailings dam
               (average low of 103,000 GPD during the period February through March 1991, to an
               average high of 238,000 GPD during the period May through June of 1990)  was due
               to seasonal changes.

Comment 21:   Page 27, paragraph 4;  Recommend the following changes to this paragraph:  An
               inspection of transformers and capacitors conducted in June 1990 identified 6
               containing PCBs underground.  At this time only one unit containing PCBs remains
               underground; one unit  remains in the shop and  four in the mill building.

Comment 22:   Page 29, end of the top paragraph; Recommend the following changes to this
               paragraph:  Rainfall is  monitored daily and Whole Effluent Toxicity is monitored once
               per year.  All Whole Effluent Toxicity data submitted by the University of Missouri  at
               Rolla satisfy the criteria established in  the permit.

Comment 23:   Page 31, paragraph 1;  It should be noted that discharge from the mine water pond
               amounting to 80 percent of the volume in Bee Fork occurs only under extreme low
               flow conditions.

Comment 24:   Page 31, paragraph 3;  Add the following text to the end of this paragraph: The
               application was re-written by Mclaren/Hart and resubmitted to DNR. The State
               issued permit MM-009 to the Fletcher  facility on January  13,1992.  All permit
               requirements, including financial assurance, has been met. A bill pending in the
               Missouri legislature, co-sponsored by DNR and the mining industry, will raise the
               annual fee to $7,500.

Comment 25:   Page 32, paragraph 3;  Add the following text to the end of this paragraph: The
               system was upgraded by the installation of a chlorination unit.

Comment 26:   Page 33, paragraph 1;  The  following discussion concerning the Draft EIS is not
               relevant to the Fletcher facility and should be deleted: In  1987, the United States
               Departments of Agriculture and Interior (Forest Service and BLM) prepared a Draft
               Environmental Impact Statement for Hardrock Mineral Leasing in the Mark Twain
               National Forest, Missouri.  The Final EIS was not available for this report.  The
               analysis presented indicates that alternatives other than no  action could have adverse
               effects on water resources through a risk of tailings impoundment failure or chronic
               leakage and visual impacts to the landscape caused by structures.  The preferred
               alternative was a modified forest plan that avoided sensitive areas and minimized
               visual impacts while providing access to larger areas for exploration and development.
                                             2-37

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                                    Stie Visit Report: Doe Run Fletcher
                    APPENDIX 2-B

THE BUREAU OF LAND MANAGEMENT'S COMMENTS ON THE
              DRAFT SITE VISIT REPORT,
                 AND EPA'S RESPONSES
                        2-38

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                                                            Site Visit Report:  Doe Run Fletcher
Comment 1:    A review for consistency and technical wording is needed among figures referred to in
               the report.  Examples include the reported volume of ore and tailings produced.

Response:      The document has been edited for consistency and technical wording.


Comment 2:    Where the report indicates that information is "not available", some clarification is
               needed.

Response:      Wherever possible, information gaps in the earlier drafts of the report have been
               clarified.

Comment 3:    Overall, we would like to see some conclusion or judgment incorporated into the
               report, if appropriate.  Some context in which to evaluate the Fletcher facility would
               be helpful.

Response:      EPA is gathering information to characterize mining waste and waste management
               practices.  These site visits were designed to collect only factual information without
               making any qualitative assessments of environmental risks.
                                             2-39

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                                                             SUe Visit Report:  Doe Run  Fletcher
Comment 1:    Page 22. paragraph  1; The technical discussion of reagent volume in the slurry is
               unclear.

Response:      This statement has been deleted since it was not pertinent to the waste discussion.
Comment 2:    Page 24,  top of page; The text indicates that the dam does not meet Missouri's
               earthquake requirements since it was built before construction guidelines were adopted
               in  1981.  This should be clarified in the text.

Response:      The text has been revised as follows:  Missouri adopted construction guidelines,
               including earthquake requirements,  in 1981.  Since the dam was built before Missouri
               adopted construction guidelines, the dam has  not been evaluated with earthquake
               loading.
Comment 3:    Page 24, paragraph 2; With the understanding that the report is not intended to draw
               any conclusions, there is concern about the implications of dissolved solids, sulfate
               concentrations, and some heavy metals in the monitoring wells. Some concentrations
               exceed EPA primary drinking water standards.

Response:      EPA is gathering information to characterize mining waste and waste management
               practices.  These site visits were designed to collect only factual information without
               making any qualitative assessments of environmental risks.
                                                                                      6
                                                                                      I
                                                            U.S. Environmental Protection Agency
                                                            Region 5, Library (PL-12J)
                                                            77 West Jackson Boulevard, 12th Floor
                                                            Chicago, 1L  60604-3590
                                             2-41

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                              Site Visit Report: Doe Run Fletcher
              APPENDIX 2-C

THE FOREST SERVICE'S COMMENTS ON THE
        DRAFT SITE VISIT REPORT,
          AND EPA'S RESPONSES
                  2-40

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