THE  OHIO  RIVER - McALPINE  POOL

   *
               REPORT
       KENTUCKY - INDIANA
       Environmental Protection Agency
      Surveillance and Analysis Division
               Region IV


           ATHENS, GEORGIA
   I           JUNE 1973

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THE OHIO RIVER-McALPINE POOL REPORT

        KENTUCKY-INDIANA
 Environmental Protection Agency
             Region IV
Surveillance and Analysis Division
         Athens, Georgia

            June 1973

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     This report was prepared under the direction and supervision




of Dr. David W. Hill, Chief, Industrial and Special Studies Branch.




Mr. Charles A. Sweatt served as Project Engineer for the planning




and conduct of the field survey and as principal author of  this




report.  Participating EPA personnel are stationed in Athens,




Georgia, as part of the Surveillance and Analysis Division  under




the direction of Mr. John A. Little, Region IV;  and in Evansville,




Indiana, as part of Region V.
                             ii

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                       TABLE OF CONTENTS




Title                                                       Page No.




INTRODUCTION 	   1




SUMMARY AND CONCLUSIONS	3




RECOMMENDATIONS	9




STUDY AREA	11




     DESCRIPTION OF AREA	11




WATER USES AND WATER QUALITY STANDARDS	15




     WATER USES	15




     WATER QUALITY STANDARDS AND USE CLASSIFICATIONS	15




STUDY METHODS	21




     GENERAL	21




     MUNICIPAL WASTE 	  21




     INDUSTRIAL WASTE	22




     WATER QUALITY STUDIES	22




STUDY FINDINGS	25




     WASTE SOURCES	25




          Oak Park Conservancy District,  Indiana 	  25




          Charlestown,  Indiana 	  28




          Hanover, Indiana 	  30




          Madison, Indiana 	  32




          Vevay,  Indiana  	  34




          Carrollton, Kentucky 	  35




          Louisville (Hite Creek),  Kentucky	35




          Dow Corning Corporation,  Carrollton,  Kentucky.  ...  37




          M&T Chemicals,  Inc.,  Carrollton,  Kentucky	49




                                iii

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Table of Contents (cont'd)

Title                                                         Page No.

          Kawneer, Inc., Carrollton, Kentucky	   43

          Indiana Army Ammunition Plant, Charlestown, Indiana.   45

          Indiana-Kentucky Electric Corporation, Madison,
             Indiana	   46

OHIO RIVER WATER QUALITY 	   49

    - FLOW	   49

    • TEMPERATURE	   49

    . DISSOLVED OXYGEN	   50

    * BIOCHEMICAL OXYGEN DEMAND	   53

    'TOTAL ORGANIC CARBON	   54

     NITROGEN	   56

    .PHOSPHORUS	   58

    « pH AND ALKALINITY	   58

    . SPECIFIC CONDUCTANCE	   59

    . TURBIDITY	   59

    •BACTERIOLOGICAL 	   59

REFERENCES	   67

APPENDIX A - STATION LOCATIONS AND STUDY PLAN	   69

APPENDIX B - CHEMICAL AND BACTERIOLOGICAL METHODS	   83

APPENDIX C - STREAM AND WASTE QUALITY DATA	   91

APPENDIX D - REGION V REPORT ON INDIANA ARMY AMMUNITION PLANT.  121

APPENDIX E - ORGANIC COMPOUNDS IDENTIFICATION	133

APPENDIX F - PERSONNEL ROSTER	135
                               IV

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                         LIST OF TABLES

Number   Title                                                 Page

I        MUNICIPAL AND INDUSTRIAL WASTE SOURCES	   16

II       MUNICIPAL AND INDUSTRIAL WATER INTAKES	   17

III      WATER QUALITY CONDITIONS AND SPECIFIC USE CRITERIA
            APPLICABLE TO OHIO RIVER (McALPINE POOL) 	   19

IV       MUNICIPAL & INDUSTRIAL EFFLUENT DATA SUMMARY	   26

V        BOD5 LOADING (LBS/DAY) TO McALPINE POOL	   55

VI       SUMMARY OF BACTERIAL WATER QUALITY	   62

VII      SUMMARY OF BACTERIAL WASTE SOURCE DATA	   63
                                  v

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                        LIST OF FIGURES


Figure   Title                                                     Page

   1     Location Map and Sampling Stations	Fold-out in
                                                            back (137)

   2     Ohio River Navigational Structures	12

   3     Approved Ohio River Water Classification for the
         McAlpine Pool Reach	20

   4     Oak Park Conservancy District, IN, STP	27

   5     Char lest own, IN, STP	29

   6     Hanover, IN, STP	   31

   7     Madison, IN, STP	33

   8     Carrollton, KY, STP	36

   9     Kawneer and Dow Corning Discharges	39

  10     M&T Chemicals Discharge	41

  11     Indiana-Kentucky Power Corp. Ash Pond 	   48

  12     Ohio River (McAlpine Pool), DO, TOC and BOD5
         Concentrations	51

  13     Ohio River (McAlpine Pool), River X-sectional Area,
         Velocity and K2 Rate	52a

  14     Ohio River (McAlpine Pool) Average Nitrogen Concentrations 57

  15     Ohio River (McAlpine Pool) Total and Dissolved Phosphorus
         Concentrations	60

  16     Geometric Mean Total Coliform Densities 	   64

  17     Geometric Mean Fecal Coliform Densities 	   65
                               vi

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                         INTRODUCTION




     Dissolved oxygen concentrations in the lower portion of the




McAlpine Pool reach of the Ohio River in violation of Federal and




State water quality standards were observed during a survey conducted




by the Environmental Protection Agency (EPA) during August and




September 1971.  Results of that survey are published in the report




entitled Ohio River Waste Source and Water Quality, Louisville,




Kentucky to Wabash River Reach, Kentucky-Indiana.  That report rec-




ommended that EPA investigate the causes and recommend solutions to




the low dissolved oxygen levels in McAlpine Pool.




     A field study was conducted during September 18-24, 1972, with




the following objectives:




          •  Determine the cause of low dissolved oxygen concentra-




             tions observed in the lower portion of McAlpine Pool




             during the August-September 1971 EPA, Region IV, Ohio




             River Study.




          •  Characterize the industrial and municipal wastes dis-




             charged into the McAlpine Pool reach of the Ohio River.




     The 1972 study was conducted by Region IV Surveillance and




Analysis Division personnel from Athens, Georgia, with the assistance




of EPA Region V personnel from the Evansville District Office.




     The cooperation and assistance of the Kentucky Water Pollution




Control Commission, the Indiana Stream Pollution Control Board, the




Louisville-Jefferson County Metropolitan Sewer District, and the




various municipal and industrial entities involved in this study




are gratefully acknowledged.

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                    SUMMARY AND CONCLUSIONS





     Wastewater discharges into the McAlpine Pool reach (River Miles




531.5 to 600.6 — from upstream to downstream) of the Ohio River are




relatively small compared to discharges from the Cincinnati and




Louisville areas.  The combined effect of waste discharges into the




McAlpine Pool, however, tends to retard recovery of the river from




the effects of the Cincinnati area waste load.




     1.  Water quality standards submitted by Indiana and Kentucky




         have been approved by the Environmental Protection Agency.




         The McAlpine Pool reach is classified for recreation, aquatic




         life, agricultural and industrial water supplies except in




         areas where public surface water supplies are located.




         These areas are classified for public water supplies by both




         states.  At present, the Louisville Water Company operates




         the only public surface water supply in the reach.  By June




         1973, Kentucky is expected to classify all streams for all




         uses.   (The most stringent water quality criteria will apply




         to all but very limited exceptions.)




     2.  Of the ten municipal waste sources investigated during this




         survey, Madison, Indiana, is the largest.  The 1.75 mgd




         flow, containing approximately 20 percent industrial waste,




         does not receive adequate treatment in the existing over-




         loaded primary treatment facility.  Stream standards for




         coliform bacteria are violated by the discharge from the




         plant.  During the survey, the plant discharged 3,140 Ibs/day

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         of BOD5, 2,770 Ibs/day of suspended solids, 9 Ibs/day of

         total chromium, and total coliform concentrations from

         7,300,000 to 86,000,000 per 100 ml.
         The sewage treatment plants (STP) at Carrollton, Kentucky,

         and Charlestown, Indiana, are both primary plants which pro-

         vide inadequate waste treatment.  The Carrollton STP does

         not provide chlorination.  Listed below is the treatment

         status of all plants surveyed :
Source
  Type
Treatment
Kite Cr. STP
(Louisville)   Tertiary + Cl2
Oak Park
Conservancy
District STP
Primary +
Indiana Army
Ammunition     Primary + Cl2
Plant STP
Indiana Army
Ammunition
Plant STP

Ind iana Army
Ammunition
Plant STP

Charlestown,
Indiana STP

Hanover,
Indiana STP

Madison,
Indiana STP

Carrollton,
Indiana STP

Vevay,
Indiana STP
Secondary +


Septic tanks



Primary + Cl2


Secondary +


Primary +


Primary


Secondary +
            Impl emen ta t ion
Needs       Schedule Status
None             Met

                 Met
Secondary   Secondary facility
            essentially complete.
                  Secondary   Secondary facility
                              under construction.
None             None


              Funds requested
Treatment     for design and
  Plant        construction.

                 Behind
Secondary     Plans Submitted.


None             Met

                 Behind
Secondary     Plans approved.

               Plans almost
Secondary        complete.


None             Met

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3.  Five industrial waste sources were investigated.   The




    Indiana Army Ammunition Plant, was closed by a strike and




    had no discharge during the study.  Information on this




    source is provided in the form of a trip report prepared by




    Region V personnel and contained in Appendix D.  The Indiana-




    Kentucky Clifty Creek Power Plant discharges approximately




    960,000 gpm of cooling water with a 11°F temperature rise.




    This heat load, if fully mixed, amounts to a calculated 0.42°F




    temperature rise for the Ohio River flowing at a  rate of




    30,000 cfs.  Chlorine is used for algae control in the cool-




    ing system during the summer.  This results in a  0.35 ppm




    chlorine residual in the cooling water discharge  for approx-




    imately two 30-minute periods per day during the  summer.




    Waste samples were collected from the remaining three indus-




    tries, all near Carrollton, Kentucky.




                   •  Dow Corning,




                   •  M&T Chemicals,




                   •  Kawneer, Inc.




    The waste samples from M&T Chemicals contained relatively




    high concentrations of BODc (87.5 mg/1) and ammonia (33 mg/1)




    which represent a sizable oxygen demand upon the  receiving




    waters.  Wastes from Kawneer and Dow Corning had  low oxygen




    demands and probably do not contribute measurably to the low




    oxygen levels in McAlpine Pool.  Domestic wastes  from all




    industries investigated are handled adequately with the

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    possible exception of Kawneer, Inc.   Based on the one




    effluent coliform sample which exceeded 1,600 per 100 ml,




    it appears that the septic tank system now employed by the




    plant may need improvement.




4.  Normal waste discharges from industrial and municipal waste




    sources along the study reach are not sufficiently large to




    cause the previously observed low dissolved oxygen problems




    in McAlpine Pool, even though waste  treatment is inadequate




    in several cases.  Water temperatures in the river were




    decreasing during the study and were slightly below the




    summer peak;  however, dissolved oxygen levels as low as 4.0




    mg/1 were observed.  Approximately 15 percent of mid-channel




    observations were less than the required daily average of




    5.0 mg/1.  Only slight horizontal or vertical stratification




    was observed.  No real cause and effect relationship could be




    established between any individual or group of waste dis-




    charges within the study reach and observed low oxygen levels.




5.  Reaeration rates in the sluggish impoundments of the Ohio




    River and particularly in McAlpine Pool are low resulting




    in very little reaeration.  Dissolved oxygen levels at




    Markland Dam are markedly depressed  by upstream waste sources.




    They increase steadily downstream in the first 25 miles of




    the study reach but then decline downstream to McAlpine Dam.




    This trend corresponds closely with  factors affecting re-




    aeration, namely river velocities and cross-sectional

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mg/1).  DO was lower in the Ohio  (5.4 vs.  6.1 mg/1) and  BOD5




was higher in the Ohio (1.8 vs. 1.4 mg/1).

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                       RECOMMENDATIONS






1.   All municipal wastes and sanitary waste discharges from industry




     should receive adequate secondary treatment and disinfection.




     The following sources are not meeting these criteria and/or are




     not making significant progress in meeting the federal-state




     implementation schedules:




                •  Madison, Indiana STP,




                •  Carrollton,  Kentucky STP,




                •  Charlestown, Indiana STP,




                •  Indiana Army Ammunition Plant septic tank overflow,




                •  Kawneer, Inc. septic tank overflow




     Agencies from the appropriate states and the EPA should review




     each case and take appropriate action to assure compliance with




     established implementation schedules.




2.   As an immediate measure, equipment to provide adequate disinfection




     should be provided at the  Madison and Carrollton sewage treatment




     plants.




3.   Madison should determine the sources of heavy metals to its




     sewers (possibly the electroplating plant) and require appropriate




     pretreatment.




4.   Upstream waste sources (primarily in the Cincinnati area)  must




     provide better waste treatment before a significant water  quality




     improvement will occur in the McAlpine Pool.  Nitrification of




     these wastes will probably be necessary.

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                                                                       11
                          STUDY AREA
DESCRIPTION OF AREA
     The Ohio River is formed by the junction of the Allegheny and

Monongahela Rivers at Pittsburgh, Pennsylvania.  It flows south-

westerly for 981 miles to the Mississippi River near Cairo, Illinois

(Figure 1 - fold out map at rear of report).  Although the river flows

through a rather narrow valley, it drains 203,910 square miles of the

middle eastern portion of the United States.  The river forms portions

of the boundary between Ohio and West Virginia and separates Kentucky

from Ohio, Indiana, and Illinois.

     The specific study area was the 75.3 mile reach of the Ohio

River between Markland and McAlpine Dams.  The terrain is gently

rolling and is dominated by agricultural activities.  The population

is dispersed in rural areas and small towns.  Madison, Indiana, with

a population of 13,081 is the largest city in the study area.  Indus-

trial activity along the reach is sparse.

     The Ohio River is an Important navigational route serving the

eastern central United States.  The river was first used for commer-

cial navigation prior to early 1800 when state and private interests

began development.  Navigation was extended from the mouth to

Pittsburgh with completion of a nine-foot deep channel in 1929.

Under a modernization program inititated in 1955, the original system

of 51 locks and dams are being replaced by 19 high-lift structures

(Figure 2).

     The average daily flow of the Ohio River at Louisville is

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12
                                                                               133J Ml NOI1W313

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                                                                     13
110,700 cfs for 41 years of record.   The ten-year,  seven-day low
flow of 6,140 cfs and daily average  extremes are 1,110,000 and
2,100 cfs.

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                                                                      15
             WATER USES AND WATER QUALITY STANDARDS
WATER USES
     Water uses within the McAlpine reach consist of public and
industrial water supplies, commercial fishing, sport fishing, recre-
ation  (including swimming and water.skiing), navigation, agricultural
and municipal and industrial wastewater disposal.  In contrast to
upstream and downstream reaches, the McAlpine reach receives very
little municipal or industrial waste, increasing its popularity for
recreational uses.  Municipal and industrial waste discharges are
listed in Table I.
     Water supplies for one municipality and three industries are taken
from this reach of the Ohio River (Table II).  Most water supplies in
the area are obtained from high production wells in the river valley
alluvium.  These wells, recharged from the Ohio River, typically
produce 1,000 to 2,000 gallons per minute of good quality water.

WATER QUALITY STANDARDS & USE CLASSIFICATIONS
     The Federal Water Quality Act of 1965 (Public Law 89-234) pro-
vides that States, after public hearing, and prior to June 30, 1967,
may adopt water quality standards applicable to interstate waters
within the state and an implementation and enforcement plan.  The act
requires that the standards will protect the public health and welfare,
enhance the quality of water, and serve the purposes of this act.  In
establishing such standards, the state is required to take into con-
sideration uses for public water supplies, propagation of fish and
wildlife, recreational purposes, agricultural, industrial and all

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     16
                                                    TABLE I
                                     MUNICIPAL AND INDUSTRIAL WASTE SOURCES
                                        Ohio River (HcAlpine Pool) Study
River
Mile
597.6
595.9
593.4
592.8
Municipality
Oak Park Con-
servency Dist.
- Indiana
Louisville,
Jefferson
County
Metropolitan
Sewer Dist.
Kite Cr.
Plant, KY
Indiana Army
Ammunition
Plant
Indiana Army
Ammunition
Plant
Ave.
1970 Flow
Population (MOD)
Serves 0.23
2,000
Approx. 75% 1.5
of waste
flow is from
Ford Motor
Co.'s Truck
Assembly
Plant
0.25
160 0.02(e)
Type of Treatment
Primary and
Chlorination
Tertiary and
Chlorination
Secondary and
Chlorination
Septic tanks w/no
drain field
Treatment Status and
Federal Implementation Date
Secondary facility 90% com-
plete on 6/72. Implementa-
tion date for completion -
12/73.
No needs identified.
No needs identified.
Unsatisfactory - Scheduled
to be replaced by two packaj
aeration treatment units in
                                                                                                  Receiving Stream

                                                                                                  Unnamed tributary
                                                                                                  to the Ohio River.
                                                                                                  Hite Cr., Harrods
                                                                                                  Cr., Ohio River
                                                                                                  Ohio River
                                                                                                  Ohio River
                                                                            iplaced by two package
                                                                            i treatment units in
                                                                    FY  '73.
591.5   Indiana Army
        Ammunition
        Plant

590.5   Charlestown,
        Indiana
 554.7    Kawneer.Inc.

•543.5    M&T Chemicals,
         Inc.
 541.0   Dow Corning
        Corp.
 562.6    Hanover,  Ind.
 558.8   Madison,  Ind.
5,890
 3,018


13,081
            0.08    Primary and
                    Chlorination
0.40    Primary and
        Chlorination
            0.45    In-plant controls

            4.8     Neutralization,
                    floculation and
                    sedimentation
5.02    Sedimentation,
        neutralization,
        coagulation and
        vacuum filtration

0.11    Secondary and
        Chlorination

1.75    Primary and
        Chlorination
Secondary facility now under
construction is scheduled
for completion in FY '72.

Unsatisfactory - Plans for
secondary facility submitted
to state on 9/3.6/72.
Implementation dates for
start of construction 12/72
and completion 12/73.

No needs identified

Implementation dates for
completion of stabilization
basins are 3/74.  Final plans
were completed as required by
9/72.

Implementation dates for
completion of stabilization
basins are 6/74.
                                                            Jenny Lind Run to
                                                            Ohio River
                                                                        Ohio River
                                                            Ohio River
                                                            Ohio River
                                                                                                   Ohio River
 545.8   Carrollton,
         KY
 3,218
0.28    Primary
                                                                     No needs  identified           Ohio River
Unsatisfactory - Plans for    Ohio River
secondary facility approved
by state on 4/72.
Implementation dates are
complete plans 6/71; start
construction 12/71; complete
construction 12/72

Unsatisfactory - Implementa-  Knetucky River
tion dates for secondary
facility include completion
of plans by 9/72 and com-
pletion of construction by
7/74.  No progress reported.
 538     Vevay, Ind.


 (e)-Estimate based on population served
 1,463      0.12    Secondary and
                    Chlorination
                                                                     No needs  identified
                                                                                                   Ohio River

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                                                                      17
                             TABLE II

              MUNICIPAL AND INDUSTRIAL WATER INTAKES

                   OHIO RIVER - MCALPINE POOL

                         (NOVEMBER 1972)
Municipalities

Louisville, Ky.
    Use
Public Water Supply
  Location
(River  Mile)

    600.6
Industries

Indiana-Kentucky Power Corp.,
  Clifty Creek Plant               Cooling

Colgate-Palmolive Co., Inc.        Process

Louisville Gas & Electric Co.      Cooling

Louisville Gas & Electric Co.      Cooling
                          559.5

                          603.6

                          603.6

                          604.9

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18



 other legitimate uses.  The State of Indiana and the Commonwealth




 of Kentucky have submitted and received approval on their water




 quality standards.  Standards submitted by the water pollution control




 agericies of both states are applicable to the study reach and enforce-




 able by the two states and the Federal Government.  In addition to




 the standards submitted by the states, the Ohio River Valley Water




 Sanitation Commission (ORSANCO), a compact representing eight states




 along the Ohio River, has also adopted criteria for judging the




 suitability of the Ohio River water for various uses.  The ORSANCO




 standards, however, are not federally enforceable.  Table III presents




 a brief summary of the criteria applicable to the study reach.




      Water use classifications for the Ohio River have been proposed




 by Kentucky and Indiana and approved by EPA.  A schematic representation




 of the study area classifications is shown in Figure 3.  A clause in




 the Indiana standards provides for the classification of public water




 supply to be applied at existing or future surface water supply




 points.  The reach of river near McAlpine Dam, now classified for




 aquatic life, was planned to be upgraded in the Kentucky standards  to




 recreation in July 1974.  However, a public hearing is scheduled by




 the Department of Natural Itesources and Environmental Protection for




 June 4, 1973, after which all streams are expected to be classified




 for all uses.  Exceptions will have to be justified by dischargers




 at public hearings for their discharge permits.

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                                                                                                                  19
                                                   TABLE  III

                         Water Quality Conditions and Specific Use Criteria Applicable
                                         to Ohio River  (McAlpine Pool)
Minimtn Conditions For All Haters At All Times
   FT)  Free from substances attributable to municipal, industrial,
        agricultural or other discharges that will settle to form
        putrescent or otherwise objectionable deposits.
   (2)  Free from floating debris, oil, scum and other floating
        material attributable to municipal, industrial, agricultural
        or other discharges in amounts sufficient to be unsightly
        or deleterious.
   13)  Free from materials attributable to municipal, industrial,
        agricultural or other discharges producing color, odor, or
        other conditions in such degree as to create a nuisance.
   (4)  Free from substances attributable to municipal, industrial,
        agricultural or other discharges in concentrations or
        combinations which are toxic or harmful to human, animal,
        plant or aquatic life.
Stream polity Criteria

Hater Use Classification
Public Water Supply  (Kentucky)
                       and
                     (Indiana)
Bacteria:  Monthly arithmetic mean total coliforms ±5,000/100 ml  (MPN or  MF);  or,
           £.5,000/100 ml in more than 20 percent of samples; or,  ±20,000/100 ml  in
           more than 5 percent of samples.
Threshold Odor Number:  <3 after treatment.
Dissolved Solids:  ~50 mg/l at all times,  monthly mean ±500 mg/l or  specific
           conductance & 25°C ±1,200 ^mhos/cm at all  times or monthly mean
           ±900 vmhos/cm.
Radioactive Substances:  Gross beta activity not to exceed 1,000  picocuries  per
           liter  (pCi/l),  nor shall activity from Strontium 90  exceed 10  pCi/l,
           nor shall activity from dissolved alpha emitters exceed 3  pCi/l.
Recreation  (Kentucky)
Recreation-Whole Body Contact
           (Indiana)

         -Partial Body Contact
           (Indiana)
Aquatic Life  (Kentucky)
                and
              (Indiana)
                                   Chemical constituents:
                                   Constituents

                                   Arsenic
                                   Barium
                                   Cadmium
                                   Chromium  (Hexavalent)
                        Not to exceed the following at anytime:
                        Concentration (mg/l)   Constituents    Concentration  (mg/l)
                               0.06
                               1.0
                               0.01
                               0.05
Cyanide
Fluoride
Lead
Selenium
Silver
0.025
1.0
O.OC
0.01
0.05
Bacteria:  Total coliform monthly mean ±1,000/100 ml; daily  value  ±2, 400/100 ml.
           If above values are exceeded, during May-October  the  geometric mean
           fecal coliform density ±200/100 ml in ten samples per month  or
           ±400/100 ml in 10% of monthly samples.  During  November-April  monthly
           geometric mean ±1,000/100 ml in ten monthly samples or  ±2,000/100 ml
           in 10% of monthly samples.


Bacteria:  April-October, monthly geometric mean fecal coliform  ±200/100  mi  in
           five samples per month or ±400/100 ml in 10% monthly  samples.

Bacteria:  Geometric mean fecal coliform ±1,000/100 ml or  ±2,000/100 ml in 10%
           of samples.

Dissolved Oxygen:   (Kentucky & Indiana)  Daily average >J>,0  mg/l with minimum
           ^4. 0 mg/l.
p_H_:        "B to 9  (Ky.); 6.0-8.5  (Ind.)
Temperature:  (Ky.) Max. 89°F, 5° rise in stream, 3° rise  in impoundmer*ts.
           (Ind.) Max. 89"F, S° rise.
Toxic Substances:   (Ky. & Ind. ) ±1/10 96-hour TIM.
Taste & Odor:   (Ind.)  No substance which imparts unpalatable flavor to  food
           fish, or result in noticeable offensive odors  in  the  vicinity  of
           the water.

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 20
                      FIGURE
APPROVED OHIO RIVER  WATER
CLASSIFICATION  FOR  THE
McALPINE POOL  REACH.
           FOURTEEN MILE
                CREEK
             (RM 589-3)
         MADISON  HWY,
            BRIDGE
           (RM 557. 2)
                McALPiNE DAM
                  (RM 604.4)

              BEARGRASS
                CREEK
                (RM 602-0)
MARKLAND DAM
  (RM 531.7)
                            A
                            B
                            C
                            D
                            E
                                  Key  to Stream
                                    Classif i cation
Public  voter  supply
Recreation
Aquatic life
Industrial  water  supply
Agriculture
    x Scheduled for upgrading to  recreation  clcss  ication  in July 1974
   xx All waters which  are now used ci win be  used  in the future

     for  public or industrial  wafer suoply  rr\v.;  ,n e et the  criteria
     established  for those   uses.

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                                                                      21



                        STUDY METHODS
GENERAL
     The study area was limited to the reach of the Ohio River




between River Mile 600.6 (Louisville, Kentucky) and River Mile 530.6




(lower end of Markland Pool adjacent to Craigs Creek).  All waste




sources sampled on the Indiana side of the river were sampled by




personnel of the EPA, Region V, Indiana District Office, with the




assistance of personnel of EPA, Region IV, Surveillance and Analysis




Division.  These samples were analyzed at the Evansville field station




laboratory.  All other waste source and stream samples were analyzed




by Region IV personnel at the field laboratory located at the Louisville-




Jefferson County, Fort Southworth Sewage Treatment Plant or at the EPA




Laboratory in Athens, Georgia.





MUNICIPAL WASTE




     One daily effluent composite sample was collected from each of




the municipal waste treatment plants discharging into McAlpine Pool.




The Madison, Indiana STP was the only facility where influent samples




were collected.  Samples were collected and composited at hourly or




half-hour intervals with EPA automatic sampling equipment.  Additional




samples requiring special preservation techniques and bacteriological




samples were collected as grab samples.  All sources except the




Louisville Hite Creek STP were sampled prior to post chlorination.




Bacteriological samples, however,  were collected after chlorination




if chlorination was provided.   Flows were determined by in-plant




flow measuring devices or plant records.   Appendix A lists the types

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22
   of samples collected and the analyses performed.

   INDUSTRIAL WASTE
        Two daily composite samples were taken with  EPA automatic
   samplers from each industrial waste source discharging  into  the
   McAlpine Pool.   One grab sample was taken during  each 24-hour period
   for those parameters requiring special preservation.  One  or more
   bacteriological grab sample was collected from each source.  Flow
   measurements  were supplied  by the  companies based on direct  measure-
   ments or water usage.   Appendix A  lists the types of samples collected
   and analyses  performed.

   WATER QUALITY STUDIES
        Samples  were collected at 17  Ohio River and  tributary sampling
   stations located upstream and downstream from waste sources, major
   tributaries,  and at intermediate river locations.  Seventeen stations
   were sampled  at mid-channel for five consecutive  days.   Some cross-
   sectional samples were taken below waste sources  and major tributaries
   to determine  the amount of  lateral mixing.  The criteria for sampling
   depth, station identification and  utilization for each  station  are
   contained in  Appendix A.
        For quarter point samples, each individual sample  was analyzed
   for dissolved oxygen, temperature  and pH.  For selected stations,
   each quarter  point sample was also analyzed for 5-day biochemical
   oxygen demand, turbidity, acidity, alkalinity, nitrogen series
   (NH3, N02 + N02, TKN), phosphorus   (total and soluble),  and specific

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                                                                     23




conductance.  At other stations, samples were composited across the




quarter point cross-section as outlined in Appendix A.




     All stream samples analyzed for coliform bacteria were collected




immediately below the surface (approximately one foot) using a grab




technique.  When quarter point bacteriological samples were collected,




individual samples were returned to the field laboratory.  Any com-




positing was done by laboratory personnel using sterile glassware.




Salmonella samples were collected by suspending swabs in the river




at selected sites for two to three days.  When the swabs were retrieved,




they were promptly placed in nutrient broth and analyzed for Salmonella.




     Field laboratory analysis of all samples was initiated within




six to eight hours of collection.  Samples for later analysis at the




Athens, Georgia, laboratory were preserved within these time limits.




Chemical and bacteriological methods used during this study are con-




tained in Appendix B.

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                                                                      25



                        STUDY FINDINGS






WASTE SOURCES




     Four industrial and ten municipal or domestic waste discharges




into McAlpine Pool were investigated.  Other sources discharging into




the headwaters of tributary streams were not sampled since they have




very little effect upon the study objectives.  Only effluent (except




Madison STP) samples were collected and no attempt was made to assess




treatment efficiencies.  The locations of waste sources are shown in




Figure 1 with sample station descriptions in Appendix A.  A summary




of waste source data is contained in Table IV with a complete data




summary in Appendix C.  Individual waste sources are discussed in




detail.






             Oak Park Conservancy District, Indiana




     The Oak Park Conservancy District STP serves a residential




community of the Louisville metropolitan area.  The primary treatment




plant receives an estimated flow of 230,000 gallons per day from




1,063 family units, one general store, and two service stations.




After treatment in the spiral digester (modified Imhoff Tank), the




waste is chlorinated (Figure 4) and discharged to a small unnamed




tributary which flows into the Ohio River at RM 597.6.  Construction




is essentially complete on two contact stabilization units (Figure 4).




When placed in operation, the units designed to operate in parallel




should provide adequate secondary treatment for the waste.




     One 24-hour composite sample was collected from the influent




of the chlorine contact chamber.  Three samples for bacterial

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26
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                                                               27
                      Figure 4
Old Spiral Digester Primary Unit now in Operation at
the Oak Park Conservancy District STP
 One of the Two New Secondary  Units  Nearing Completion

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28
   analysis were collected  from  the plant effluent.  Suspended solids

   and  BOD5 were high at 130 mg/1  (244 Ibs/day) and 175 mg/1  (328

   Ibs/day),  respectively.  Also,  chlorination was ineffective with

   total  coliform densities of 16,000,000, 12,000,000, and 27,000,000/

   100  ml  observed  in the three  samples collected.

       At the  time of  the  1972  study, the quality of the effluent was

   unsatisfactory;  however, the  new treatment facility now under con-

   struction  should correct this situation.  Federal, state and ORSANCO

   compliance schedules require:

                    Completion of  plans by      07/72

                    Start construction by       01/73

                    Complete construction by    12/73

   The  community is proceeding well ahead of schedule.


                        Char 1 est own, Ind iana

       The city of Charlestown, with a population of 5,890,  is served

   by a primary treatment facility consisting of  sedimentation, sludge

   lagoon and chlorination  (Figure 5).  The average flow is 400,000

   mgd.   The  treated waste  is pumped through a three-mile force main

   to the  Ohio  River at Mile 590.5.

       A 24-hour composite sample was collected  at the Parshall flume

   used to measure  plant discharge.  The BOD5 concentration was 170

   mg/1 (567  Ibs/day) and suspended solids were 60 mg/1  (200  Ibs/day) .

   Bacterial  samples were not collected since the force main  is used

   for  chlorine contact and the  discharge point was not readily accessible.

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                                                           29
                      FIGURE 5
Settling Tank and Sludge Pond at Charlestown, IN,  STP

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30



                Needs for Improvements and upgrading the treatment system have




           been Identified.  Federal, state, and ORSANCO compliance schedules




           require completion of plans by 07/72 and the start of construction




           by 12/72 with completion by 12/73.  Final plans were submitted to the




           state on 9/16/72.






                                   Hanover, Indiana




                The city of Hanover, Indiana, and Hanover College are served by




           a new contact stabilization treatment facility designed for 500,000




           gpd (Figure 6), but operating considerably under capacity at approx-




           imately 100,000 gpd.  The treated waste is chlorinated and discharged




           via force main to the Ohio River near Mile 562.6.




                One 24-hour composite sample was collected from the sedimentation




           tank just prior to the overflow weir.  Two bacteriological samples




           were collected from a manhole in the discharge line after chlorination




           BOD5 concentrations were 93 mg/1 (85 Ibs/day), and suspended solids




           were 215 mg/1 (192 Ibs/day).  These values are five to ten times




           higher than would normally be expected from a plant of this type.




           It must be assumed that the system was upset and that this sample was




           not representative of the normal plant effluent.  Total coliform con-




           centrations of <100 and <1,000 per 100 ml were determined on two




           effluent samples with measured chlorine residuals of 1.0 and 0.85 ppm.




                Although treatment during the survey was inadequate, no addi-




           tional treatment needs have been specified.  The system is in com-




           pliance with the implementation schedule.

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                                                 31
          FIGURE 6
Secondary STP at Hanover, IN

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32
                                    Mad iso n.  Ind iana

                 Madison, Indiana, has a population of 13,081 and is served by


            a primary sewage treatment plant  which discharges into the Ohio River

            at Mile 558.8 (Figure 7).   Besides domestic waste, the 1,750,000 gpd


            discharged from the facility contains waste from several small indus-


            tries including a meat packing plant, an electroplating plant, a

            shoe liner plant, a musical organ plant, and other minor industrial

            discharges.   The industrial waste accounts for approximately 20 per-

            cent of the  total flow.


                 Two 20-hour composite samples were collected from the chlorine

            contact chamber discharge.  The chlorine residual at this point was


            zero when bacterial samples were  collected on two different occasions.


            Total coliform concentrations in  the effluent were 86,000,000 and

            7,300,000 per 100 ml.  The plant  operator stated that the chlorinator


            did not have sufficient capacity  to maintain a chlorine residual in


            the plant effluent.  The present  dosage and existing chlorinator

            capacity is  131 Ibs/day.  BOD5 concentrations averaged 215 mg/1 (3,140

            Ibs/day), suspended solids averaged 190 mg/1 (2,770 Ibs/day), total


            chromium averaged 615 ug/1 (9 Ibs/day), total copper averaged 125

          .  ug/1 (1.8 Ibs/day), and mercury levels of 2.9 yg/1 (0.04 Ib/day) were

            observed in  the plant influent.

                 The plant effluent constitutes the largest single waste load to


            the study reach of the Ohio River.  It accounts for approximately 43


            percent of the combined BOD5 load from waste sources surveyed.  Metals


            discharged from this plant are excessive and high coliform levels in

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                                                                     33
                      FIGURE 7
 Settling Tanks at Madison, IN, Primary STP.  Indiana-
 Kentucky Power Corp. Clifty Creek Plant in Background
Digester and Chlorine Contact Tank at the Madison STP,
The Underground Discharge is in Approximate Center of
the Picture

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34
     the river below this plant discharge violate water quality
     standards.
         The city of Madison has been directed to upgrade the treatment
     facility to provide secondary treatment.  The federal and state com-
     pliance schedule requires completion of plans by 06/71, start con-
     struction by 12/71 and complete construction by 12/72.  ORSANCO
     requires a construction completion date of 12/73.  Final plans were
     accepted by the state on 04/72.  Madison is ranked 88th on the 1973
     priority list for federal grants.  At the present time, the city has
     indicated that no contract will be awarded until grant funds are
     received.  ORSANCO is pursuing enforcemement action.

                             V evay, Ind iana
         The town of Vevay, Indiana, with a population of 1,463, is served
     by an extended aeration system similar to the Hanover system shown in
     Figure 6.  After treatment, the 120,000 gpd average flow is chlori-
     nated and discharged to the Ohio River near Mile 538.  The only known
     industry connection is a small shoe factory.
         An 18-hour composite sample was collected at the overflow weir
     from the settling unit.  The effluent 6005 was less than 5 mg/1 (5
     Ibs/day).  Samples collected after chlorination had a total coliform
     bacteria concentration of less than 1,000 per 100 ml.
         No additional treatment needs have been identified and the.
     system is in compliance with federal and state requirements.

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                                                                       35
                     Carrollton, Kentucky



     Carrollton, with, a population of 3,218, is served by a primary



sewage treatment system consisting of sedimentation and sludge di-



gestion (Figure 8).  Waste flows average 275,000 gpd and contain



very little industrial waste.  The unchlorinated effluent is dis-



charged to the Kentucky River at Mile 0.7.



     A 24-hour composite sample was collected from the settling tank



at the overflow weir.  The effluent 6005 concentration was 205 mg/1



(468 Ibs/day) and the suspended solids concentration was 66 mg/1



(151 Ibs/day) and the total coliform density in the effluent was



55,000,000 per 100 ml.



     The federal and state compliance schedule requires that plans



for a secondary treatment facility be initiated by 2/71 and completed



by 9/72.  The schedule requires construction to start by 6/73 and be



completed by 7/74.



     As of April 1973, engineering plans were reported to be 90-95%



complete.  A few more soil tests were needed to determine if pilings



were needed for the foundation.  Completion of these plans was



anticipated with an additional 30 to 60 days.





             Louisville. Kentucky - Kite Creek Plant



     The Kite Creek sewage treatment plant is operated by the



Louisville and Jefferson County Metropolitan Sewer District.  The



plant serves the Ford Motor Company Truck Assembly Plant as well as



the residential area in the plant vicinity.  Approximately 80 per-



cent of the average daily waste flow of 1.5 mgd comes from the Ford

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36
                                    FIGURE 8
                   Settling Tank at Carrollton, KY, Primary STP
               Digester and Control Building at Carrollton STP

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                                                                       37
Plant.  The remaining 20 percent is from the surrounding residential
areas.  Weekend flows, when the plant is not in operation, are ap-
proximately 0.3 mgd.  The tertiary treatment facility consists of
an activated sludge secondary system followed by mixed bed filters
and chloriiiation.
     The 24-hour composite sample had a BOD5 concentration of 12.6
mg/1 (159 Ibs/day) and a suspended solids concentration of 6 mg/1
(75 Ibs/day).  Regular analysis performed by the Louisville-
Jefferson County Metropolitan Sewer District indicates that effluent
BODs's are normally in the 2-5 mg/1 range.  Metal concentrations in
the composite sample (listed below) were low.

             Element                Concentration (yg/1)
          •  Chromium (total)              <100
          •  Tin                         <1,500
          •  Copper                          40
          •  Zinc                           180
          •  Lead                          <100
          •  Cadmium                         25

          Dow Corning Corporation, Carrollton,  Kentucky
     Dow Corning Corporation produces a variety of silicone products
for industrial and domestic  use.   Silicones are used in mold-release
agents, rubber products,  laminates, encapsulating resins, anti-
foaming agents, and water-resistant uses.( 2)
     The 5.75  mgd average flow from five processing units is collected
in equalization ponds,  settled,  neutralized, coagulated, and discharged

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38
            through an underground sewer system to the Ohio River (Figure 9).

            Domestic waste from approximately 100 employees is treated in a

            package treatment plant and combined with the process waste before

            discharge to the river.  The effluent is continuously monitored for

            pH, temperature, and flow.  Vacuum filters are used for  sludge thick-

            ening and the sludge is deposited in a land disposal area.

                 The combined wastewater discharge from the plant was sampled

            for two consecutive 24-hour periods using automatic compositing

            samplers.  The average daily waste flows during this period were

            determined from company flow measuring equipment to be 4,000 gpm.

            The waste was an almost neutral (pH 7.4), ambient temperature (22.5°C)

            discharge with low nutrient concentrations.  Five-day BOD concentra-

            tions averaged 3.7 mg/1 (178 Ibs/day), total nitrogen concentrations

            averaged 2.7 mg/1 as N and phosphorus concentrations did not exceed

            0.01 mg/1.  Residue samples indicated that the waste is well settled

            with an average total residue concentration of 1,924 mg/1 and a non-

            filterable residue concentration of 5 mg/1.  Metal concentrations

            were low:

                         Element                  Concentration (ug/1)

                      •  Chromium  (total)               <100

                      •  Tin                          <1,500

                      •  Copper                           48

                      •  Zinc                             12

                      •  Lead                           <100

                      •  Cadmium                         <25

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                      FIGURE  9
                                                            39
Broken Discharge Flume from Kawneer, Inc., of Carrollton,
KY, at the Ohio River Edge
The Discharge from Dow Corning of Carrollton,  KY,  Flowing
into the Ohio River

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40



    Bacteriological analysis indicated very low concentrations of total




    and fecal coliform bacteria with, all results less than. 4 per 100 ml.




         Two organic compounds were detected in the effluent.  One,




    decamethylcyclopentasiloxane, was positively identified at a concen-




    tration of 0.023 mg/1.  Another actomethylcyclopentasiloxane apparently




    was present, hut no standard was available for verification.  The low




    COD and TOG values found in the waste correspond to the small number




    of organic compounds found and low concentrations of each.






              M & T Chemicals, Inc., Carrollton, Kentucky




         M & T Chemicals, Inc., a subsidiary of American Can Company, is




    the world's leading manufacturer of tin chemicals.  The facility at




    Carrollton produces a variety of industrial organo-tin chemicals.




    These chemicals have a wide range of use including additives of PVC




    and vinyl products, algicides and fungicides.  Products produced for




    use in PVC bottles, and films and sheets used in food containers are




    sanctioned by the U. S. Food and Drug Administration.—'




         The 4.8 mgd of process wastes are collected and neutralized in




    sumps, flocculants are added and the waste is settled through a




    series of ponds, with the treated effluent discharged to the Ohio




    River at Mile 543.5 through an underground sewer  (Figure 10).




         Two samples, a 24-hour composite the first day and a grab the




    following day, were collected from the. plant  effluent.  The average




    daily flow of 2,260 gpm had the following concentrations:
     I/  M & T Chemicals,  Inc.  information  pamphlet.

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                     FIGURE 10
                                                           41
Waste Discharge from M&T Chemicals, Inc. Entering the Ohio
River.  The Unstable Shoreline has Eroded
                 »l
     A Closer View of the Eroded Sand and Gravel Shoreline

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42
              •   pH - 7.6


              •   Temperature  - 20°C


              •   BODs - 87.5  mg/1


              •   TKN - 36 rag/1


              •   NH3 - 33 mg/1


              •   N02 + N03  -  1.1 mg/1


              •   Phosphorus - 0.68 mg/1


              •   Total Residue - 1,904 mg/1


              •   COD - 156  mg/1


              •   TOC - 34 mg/1



         This  waste source  contributed an average of  2,370 Ibs/day of BOD5


    or  approximately 32 percent of  the total measured waste load from all


    sources.   The ammonia load in  the waste  of  900 Ibs/day also  represents


    a large oxygen demand.  The relatively low  concentration of  nonfilter-


    able solids  (20 mg/1) indicate  that  the  waste is  well settled.  Metal


    concentrations in the effluent  are low with the exception of tin,


    which averaged 3,175 yg/1.


                 Element                    Concentration (yg/1)


              •   Chromium  (total)                  <100


              •   Tin                             3,175


              •   Copper                             40


              •   Zinc                               20


              •   Lead                             <100


              •   Cadmium                           <25

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                                                                       43
Tin, in low concentrations, improves aquatic growth and is not

toxic to humans in drinking water. CL)  Therefore, tin in this dis-

charge should have no serious adverse effect upon water quality..

The total and fecal coliform concentrations were 1,263 and 4 per

100 ml, respectively.

     Organic analysis revealed that the following compounds were

being discharged to the Ohio River:

                                           mg/1      Ibs/day

          •  tri-n-butyl-phosphine oxide   <0.1        —

          •  tri-butyl-phosphine oxide     <0.2

          •  M-xylene                       0.15       6.0

          •  0-xylene                       0.09       3.6

          o  0-cresol                       0.13       5.2

Xylene is reported to be toxic and causes taste and odor in water at

a concentration of 0.3 to 1.0 mg/1.  Since xylene is insoluble in

water, the concentration found in the effluent indicates that M & T

Chemicals is losing considerable amounts of the chemical.


           Kawneer Company, Inc., Carrollton, Kentucky

     The Kawneer Company, Inc., is engaged in anodizing, rolling,

forming and finishing aluminum trim.  The trim material is used

primarily in the electric appliance industry and consists of face

plates and other thin metal parts requiring special decorative

finishes.

     An average of 400,000 gpd of waste including treated domestic

waste (septic tanks) from 200 shift workers, is discharged from the

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44
         plant via an underground  sewer  to the  Ohio  River  near  Mile 554.7
         (Figure 9).   Plant operations are designed  for  maximum reuse of
         water.  The  spent phosphoric/nitric acid  solution from the anodizing
         tanks is stored and resold  to  the supplier  for  use in  fertilizer.
         After dipping in the acid tanks,  the metal  passes to rinse tanks
         which utilize recycled cooling  water.   Wastewater discharged from
         the process  is monitored  for pH.
              Composite samples were collected  from  the  plant discharge on two
         consecutive  days.   Chemical samples were  collected before the domestic
         waste enters the waste stream.   Bacteriological samples were collected
         on the combined waste where the waste  enters the  Ohio  River.  Average
         daily waste  flows based on  water usage averaged 278 gpm.  The indus-
         trial waste  contained :

                   •   BOD5 - 3.8 mg/1
                   •   NH3 - 0.08 mg/1
                   •   Total N - 8.1  mg/1
                   •   Total Phosphorus  - 6.7 mg/1
                   •   COD - 4.2 mg/1
                   •   Total Residue  - 561  mg/1
                   •   Nonfilterable  Residue - 26 mg/1
                   •   Total Coliform - >1,600/100 ml
                   •   Fecal Coliform - >800/100 ml

              The waste contribution from this company is small.  The BOD^
         load of 13 Ibs/day amounts  to 0.2 percent of the total waste load
         measured from all study area sources.   However, total coliform

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                                                                       45



concentrations exceeding 1,600 per 100 ml were higher than




anticipated and  indicate that some improvement may be needed in




the domestic waste treatment.  Metal concentrations were low in




the effluent and are listed below:





             Element                     Concentrations  (yg/1)




          •  Chromium  (total)                  <100




          •  Tin                             <1,500




          •  Copper                              68




          •  Zinc                                22




          •  Lead                              <100




          •  Cadmium                            <25






                 Indiana Army Ammunition Plant




     The Indiana Army Ammunition Plant (IAAP), located near Charlestown,




Indiana, is operated under Government contract by Imperial Chemical




Industries of America, Inc. (ICI).  Under the direction of the U. S.




Army, cannon and mortar propellants are loaded and single base pro-




pellants are manufactured.  The facility has previously operated




with an employment of approximately 19 ,000 but is now down to near




4,500.  A major portion of the 1,390 buildings are standing idle.




During the recent survey, the workers were out on strike and the




operation was shut down, making it impossible to collect waste samples.




A brief visit was made to the plant during normal operations in




August 1972 in preparation for the survey; however, no waste samples




were collected.

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46
         The main potential source of industrial  wastes  is  the

    Propellant Manufacturing plant.  When this plant  is  operating, acid

    wastes from the manufacture of nitric and sulfuric acids  are dis-

    charged to the Jenny Lind Flume in addition to  organic  wastes from

    the nitrocellulose line.  These organic  wastes  include  nitrocellulose,

    ether, alcohol, hutylthalate,  diphenyl,  and a few others.

         Three sources of domestic waste discharge  from  the site total

    approximately 350,000 gpd.  Approximately 250,000 gpd of  this waste

    is treated in a secondary treatment facility, chlorinated,  and dis-

    charged to the Ohio River at Mile 593.4.  Eighty  thousand gpd are

    provided primary treatment, chlorinated, and  discharged to  a large

    reservoir which overflows via  a small stream  into the Ohio  River at

    Mile 591.5.  Secondary treatment facilities are now  under contract.

    The remaining estimated 16,000 gpd is overflow  from  septic  tanks

    serving 49 military housing units (160 persons).  Overflow  from these

    units is discharged directly to the Ohio River  near  Mile  592.8.

    Design funds and construction  funds were requested  in FY  71 and

    FY 72, respectively, for two new package aeration treatment plants.

         A trip report prepared hy the EPA,  Region  V, Federal Facilities

    Office, resulting from a plant visit on September 30, 1971, is con-

    tained in Appendix D.  The report outlines in detail waste  treatment

    facilities and practices, proposed improvements and  makes recommen-

    dations for additional improvements.


            Indiana-Kentucky Electric Corporation,  Madison, Indiana

         The Clifty Creek power plant, located about  one mile west  of

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                                                                       47
Madison, Indiana, on the north bank of the Ohio River, produces

approximately 31 million KKH of electricity per day.

     No wastewater samples were collected during the recent survey;

however, a visit to the plant was made.  The main discharge is

960,000 gallons per minute of once-through, cooling water that exper-

iences a 11°F temperature rise through the system.,  Periodically

(twice per day in summer) , the cooling water system is chlorinated

for a 30-minute duration for algae control, producing 0.35 ppm chlorine

in the effluent during these periods. The company also has a fly ash

pond with an average inflow of 6,800 gpm (Figure 11).  Water in the

lower end of this pond is very clear and appears to be extremely well

settled.  Two bottom ash ponds have inflows of 2,190 gpm and 1,100

gpm.  The domestic waste from the 325 employees is treated in an

extended aeration plant and chlorinated before discharge to the

r iver.

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48
                               FIGURE 11
          Fly Ash Pond at the Indiana-Kentucky Power Corp.  Cllfty
          Creek Plant
          Another View of the Fly Ash Pond Showing the Sediment
          Deposit to the far Background of the Picture

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                                                                      49
                   OHIO RIVER WATER QUALITY
     This section contains a discussion of physical, chemical, and


microbiological data collected on the Ohio River and tributaries


during the five-day study in September 1972.  A complete tabulation


of the data is contained in Appendix C.



FLOW


     The Ohio River average daily flow at McAlpine Dam for 41 years


of record is 110,700 cfs.  Flows during the five-day survey from


September 19-23 were 27,200; 28,100; 19,200; 33,200; and 44,600 cfs-/


respectively.  These flows, which averaged 30,460 cfs, are well


below the average daily discharge for the year but about normal for


expected September flows.




TEMPERATURE


     Ohio River water temperatures ranged from 24°C to 27 C with a


noticeable and consistent cooling of water temperatures occurring


during the study.   No significant temperature variations were ob-


served below any waste discharges or in the lateral or vertical


cross-sections of the river.  No measurable temperature change was


observed from above (Station 561.0)  to below (Station 566.3) the


Indiana-Kentucky Clifty Creek Power  Plant.  The power company dis-


charges approximately 960,000 gpm of cooling water with an 11°F


temperature rise which would amount  to a calculated 0,42°F river
I/  Flow data supplied by the U. S. Army Corps of Engineers,

    Louisville, Kentucky.

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50
   temperature increase based on a river flow of 30,000 cfs and fully
   mixed.  No variation was observed during the survey since the dial
   thermometers used were sensitive only to +_ 0,5°C.  Temperatures in
   the Kentucky River ranged Between 24°C and 26°C.

   DISSOLVED OXYGEN
        Dissolved oxygen (DO) concentrations in the study reach of the
   Ohio River ranged from 4.0 mg/1 to 6.6 mg/1.  The lowest observed
   DO was 4.0 mg/1 recorded on September 19 at RM 547.9, downstream
   from the confluence of the Kentucky River, the three industrial
   waste sources in Carrollton, Kentucky, and the Carrollton sewage
   treatment plant effluent.  Dissolved oxygen concentrations in the
   Kentucky River (Station K-1.4) upstream from the Carrollton STP
   effluent averaged 6.3 mg/1.  Of the 176 DO observations taken from
   mid-channel in the Ohio River, 27 observations or 15.3 percent were
   below 5.0 mg/1.  Of the 66 mid-channel observations at the five-foot
   depth, eight observations or 12.1 percent were less than 5.0 mg/1.
        Minimum dissolved oxygen concentrations permitted by the
   Indiana and Kentucky water quality standards for "aquatic life" are
   4 mg/1 with a daily average of not less than 5 mg/1.  No instantaneous
   DO concentrations less than 4.0 mg/1 were observed in the study
   reach.  Although daily averages were not determined (daily grab
   samples were taken at each station), a probability of violation is
   suggested at most of the nine stations where individual grab samples
   of less than 5.0 mg/1 were observed  (minimum DO values plotted on
   Figure 12).

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          Slight vertical and horizontal  stratification was  observed

     within the study reach.   Vertically, oxygen concentrations at  the

     five-foot depth, generally averaged 0.1  to  0.2 mg/1 higher than con-

     centrations one foot from the bottom; however,  at Station 600..6, the

     DO observations at the five-foot and one-foot above  the bottom levels

     averaged exactly the same.  Horizontal  stratification was present

     from Markland Dam down to the Carrollton area,  where DO concentra-

     tions were higher on the Kentucky side.  These  higher values prob-

     ably resulted because releases from  the tainter gates and locks at

     Markland Dam receive different amounts  of  reaeration than water

     passing through the generators.  Variations in  concentrations  up  to

     1.1 mg/1 were observed at Station 533.8  between the  quarter points.

     Data collected at Station 530.0 did  not show this variation; how-

     ever, the water containing higher dissolved oxygen probably passed

     between the quarter point and the Kentucky shore.

          Oxygen levels entering the McAlpine Pool from Markland Dam were

     depressed, averaging 5.0 mg/1.  The  level  increased  downstream for

     the next 25 miles due to atmospheric reaeration.  After reaching  an

     average concentration of 5.9 mg/1,  the  DO  levels fall off  steadily

     downstream to McAlpine Dam.  Oxygen  levels in the Kentucky River

     above the Carrollton waste discharge averaged  6.1 mg/1, which  is

     0.7 mg/1 higher than the Ohio River  Immediately above the  confluence.

     Due to the high dilution ratio, no Increase in DO was observed below

     the confluence.  Figure 13 presents a graphical plot of changing

     river cross-sectional area, calculated  velocities and reaeration

-------
                                                                                   52a
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                                      FIGURE 13

                        OHIO RIVER  (McALPINE  POOL) STUDY

                    RIVER X-SECTIONAL AREA, VOLOCITY 8 K2 RATE

                                   NOVEMBER 1972
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coefficients.  Cross-sections were furnished by the U. S. Army Corps




of Engineers.  Velocities were calculated as average velocities




through the cross-sectional area (i.e., V=Q/A) and reaeration rates




were calculated using the Churchill Method.(3)  The cross-sectional




area of McAlpine Pool increases from approximately 20,000 ft  below




Markland Dam to 60,000 ft2 near McAlpine Dam.  The velocity and re-




aeration rate vary inversely with area as shown in Figure 14.  The




high reaeration rate in the upper 20 miles of the study reach cor-




responds very closely to the break in the DO profile.  Thus, in the




upper reach of McAlpine Pool, the atmospheric reaeration rate exceeds




the oxygen uptake and, as the velocity decreases with increasing




cross-sectional area downstream, a decrease of reaeration rate takes




place.  Average time of travel through the reservoir was calculated




using the cross sectional areas and river flow rates of 30,000 cfs




and 13,000 cfs.  The resulting times were 5.98 days at a flow rate




of 30,000 cfs and 13.80 days at a rate of 13,000 cfs.






BIOCHEMICAL OXYGEN DEMAND




     A plot of average BOD5 values  show  a gradual decrease in con-




centration  as the river flows through the study reach (Figure 12).




The high BOD^ near Markland Dam (2.2 mg/1 average) and the general




decline in concentration through the study reach to an average of




1.2 mg/1 at the Louisville water intake indicates that the stream is




recovering from upstream (Cincinnati area) waste loads.,  Observed




values ranged from 3.7 mg/1 recorded on September 22 at Station




0-547.9 to a low of 0.9 mg/1 at Station 0-574.0 on September 23.

-------
54




   The  3.7 mg/1 concentration could reasonably be omitted since  it




   is nearly double  the quarter point readings taken at the same time




   as well as all other observations in  the study reach.,  If  this value




   is omitted, the average BOD5 plot will appear as the. dotted line  in




   Figure 13 and the maximum value observed at this station is 2.2 mg/1.




   BOD5 levels at Station K-1.4 (Kentucky River) averaged 1.5 mg/1.




   This compares to  1.8 mg/1 in the Ohio River immediately above the




   confluence.




        Table V contains a listing of the major dischargers to McAlpine




   Pool, their BOD5  loadings and relative contribution as a percentage




   of the total waste  load.  Discharges  from  the Madison, Indiana STP




   and  the M & T Chemicals Plant in Carrollton, Kentucky, account for




   over 75 percent of  the measured BOD5  discharged into the river.




        It is practically impossible to  measure the singular  effects of




   any  one of the relatively small BOD5  loads on the river.   BOD5 waste




   load discharged into the study reach  are insignificant in  comparison




   with discharges to  other reaches of the Ohio River such as the




   Cincinnati and Louisville areas.  The combined waste load  of  7,350




   pounds per day (population equivalent = 43,200) cannot have a very




   substantial effect  upon the Ohio River at  the flow rates encountered




   during the study.   These loads, although small, do retard  recovery of




   the  river which,  in this reach, is recovering from the Cincinnati




   area waste load.





   TOTAL ORGANIC CARBON



        All TOC concentrations for Ohio  River stations  fell within  the

-------
                                                                       55

                            TABLE V
            BOD5 LOADING (LBS/DAY) TO McALPINE POOL
               OHIO RIVER (McALPINE POOL) STUDY

                         SEPTEMBER 1972
                                                              Percent
Discharger                                   Lbs/Day          of Total

Madison, IN, STP                             3,140              42.7

M&T Chemicals, Carrollton, KY                2,370              32.2

Charleston, IN, STP                            567               7.7

Carrollton, KY, STP                            468               6.4

Oak Park Conservancy District, IN, STP         328               4.5

Dow Corning, Carrollton, KY                    178               2.4

Louisville Kite Creek STP                      159               2.2

Hanover, IN, STP                                78               1.1

Indiana Army Ammunition Plant                   35*              0.5

Kawneer, Inc., Carrollton, KY                   13               0.2

Vevay, IN, STP                                   5               0.1

                                             7,341             100.0
* Estimate based on information contained in Appendix D

-------
56




   2.8 to 6.3 mg/1 range.   Figure 12 presents a profile of  average




   observed concentrations..  As would be expected,  the  TOG  profile and




   BOD5 profile are similar.   In both cases,  there  is a slight  increase




   in concentration downstream from the  confluence  of the Kentucky River.




   The two largest sources of TOG discharge in this immediate area are




   M & T Chemicals (1,065  Ibs/day)  and the  Carrollton sewage treatment




   plant (243 Ibs/day).  The  average TOC concentration  of the Kentucky




   River upstream from the Carrollton STP discharge averaged 4.4  mg/1




   or essentially the  same as the Ohio River  concentrations.






   NITROGEN




        Total nitrogen concentrations averaged about 2.0 mg/1 for Ohio




   River stations.   Nitrification was actively underway as  evidenced




   by the reduced ammonia  level from 0.2 mg/1 at the head of the  reach




   to 0.05 mg/1 near the lower end with  a corresponding increase  in the




   nitrite-nitrate concentration (Figure 14).  The  nitrogen contribution




   from individual waste sources and tributary streams  within the study




   reach  had no measurable effect on nitrogen concentrations in  the




   river.  The Kentucky River station (K-1.4) had an average total




   nitrogen concentration  of  0.84 mg/l-N.




        A comparison of Figures 12 and 14 shows that the change in




   ammonia concentrations  is  very similar to  the change in  BOD5 concen-




   trations and inversely  proportional to the nitrite-nitrate concentra-




   tions.  Thus, ammonia  is oxidized to  nitrate (nitrification) within




   the reach with a corresponding uptake of oxygen. In fact, it appears




   that most of the oxygen demand is due to oxidation of ammonia.

-------
                                                                                  57
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          It has been shown that approximately 4.6 mg of oxygen are




     required to oxidize 1 mg of ammonia to the nitrate form.(6)  A 0.16




     mg/1 reduction of ammonia was observed through the study reach, which




     accounts for a theoretical oxygen, uptake of 0.16 X 4.,6 = 0.74 mg/1.




     Therefore,  considering the reservoir as a steady state with a five-day




     flow through time, calculations show that approximately 0.74 mg/1 of




     the measured 0.9 mg/1 of BOD5 can be attributed to nitrification.







     PHOSPHORUS




          Phosphorus concentrations were essentially constant throughout




     the study reach (Figure 15).   The maximum Ohio River total phosphorus




     concentration was 0.13 mg/1 and the minimum value was 0.08 mg/1.




     Approximately 93 percent of the phosphorus was dissolved.  The average




     concentration in the Kentucky River was 0.09 mg/1.







     pH AND ALKALINITY




          All pH values were in the 7.0 to 7.5 range, which is well within




     the limits established by the state standards.  The Indiana standards




     specify 6.0 to 9.0 for the aquatic life classification.  Average




     alkalinities for the Ohio River stations ranged from 52 to 60 mg/1




     with no significant trend.  Alkalinity values for the station near




     the mouth of the Kentucky River were slightly higher at 94 mg/1.  The




     pH values were also higher at 7.5.  This is probably due to extensive




     exposed limestone formations in the Kentucky River Valley,

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                                                                       59

 SPECIFIC CONDUCTANCE


      Specific conductance averaged between 401 and 431 ymhos/cm for


 all Ohio River stations..  Values decreased slightly through the reach,


 being highest near Markland Dam.


     Both the Indiana and Kentucky water quality standards require


 that dissolved solids not exceed 500 mg/1 as a monthly average value


 nor exceed 750 mg/1 at any time for Ohio River public water supply


 use classifications.  In lieu of actual dissolved solids measurements,


 both states permit the use of specific conductance data—  where 800


 and 1,200 ymhos/cm are equivalent to dissolved solids concentrations


 of 500 mg/1 and 750 mg/1, respectively.  Dissolved solids (specific


 conductance) limitations for public water supply use were not ex-


 ceeded during the study.




 TURBIDITY


     Turbidities ranged from 3 to 15 Jackson Turbidity Units (JTU)


with average values at Ohio River stations ranging between 4 and 10.


As would be expected, there was a gradual reduction in turbidity


 through the McAlpine Pool.




 BACTERIOLOGICAL


     The background station in the study reach was located upstream


 from Markland Dam at River Mile (RM) 530.0 (Figure 1).  The bacterial

                                                            2 /
 quality of the river at this point was characterized by mean—  total
JL/  Values referenced to 25°C.


2/  All means are geometric means.

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                                                                    61



and fecal collform densities of 980 and 82/100 ml, respectively




(Table VI)




     Downstream from Station 530..0, the. first significant source of




bacterial contamination enters the river from the Carrollton, Kentucky




sewage treatment plant (Municipal Station CK — Table VII), discharging




an average of 0.28 mgd to the Kentucky River near the mouth.  The mean




effluent total and fecal coliform densities were 81,000,000 and




18,000,000/100 ml, respectively.  The effect of the Carrollton STP




discharge on the river was seen in quarter point samples at RM 547.9,




which showed slightly higher mean total and fecal coliform densities




of 3,500 and 200/100 ml (Table VI, Figures 16 and 17).  Total and




fecal coliform densities in the Kentucky River upstream from the




Carrollton effluent were 52/100 ml and 14/100 ml, respectively.




     Downstream from Carrollton, the next major waste source dis-




charging to the river is the Madison, Indiana STP, which discharged




an average of 1.75 mgd of wastes with mean total and fecal coliform




densities of 25,000,000 and 340,000/100 ml, respectively (Table VII).




The impact of this waste discharge was seen at RM 561.0 (Figures 16




and 17).




     At RM 597.6, the Oak Park STP discharged to the river via a small




tributary stream an average of 0.23 mgd of waste with mean total and




fecal coliform densities of 17,000,000 and 850,000/100 ml.  As shown




in Figures 16 and 17, there was little effect on the bacterial quality




of the river resulting from this discharge.

-------
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66
        The bacterial  quality  of  the river at  the most downstream sampling
   site in the  study reach- at  KM  600.6 was characterized by mean  total
   and  fecal coliform  densities of  490 and 47/100 ml, respectively-.   The
   densities at this station, were lower  than those  observed during a  1971
   EPA  investigation when the  mean  total and fecal  coliform densities
   were 4,500 and  140/100 ml,  respectively.,
        Salmonella swabs  were  retrieved  from River  Mile 530.0,  540.4,
   547.9,  and 561.0, but  no Salmonella were isolated  from  these samples.
        Applying the Kentucky  water quality standards to the  bacterial
   water quality observed during  the September 1972 investigation, the
   following violations were noted:
             •   The total coliform  portion of  the Kentucky standard was
                violated  between  RM 545.0 and  582.7.
             •   The fecal coliform  portion of  the Kentucky standard was
                violated  between  RM 561.0 and  566.3.
        The Indiana water quality standard for recreational waters was
   violated between RM 561.0 and  566.3.   These violations  result  from the
   high coliform discharges from  the Carrollton,  Kentucky, and  Madison,
   Indiana, sewage treatment plants.

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                                                                      67

                         REFERENCES
1.  J. E. McKee and H. W. Wolf, Water Quality Criteria. Second Edition
    (Revised 1963), California State Water Resources Control Board,
    Publication No.. 3-A, Sacramento Q.971).

2.  R. Norris Shreve, Chemical Process Industries, Third Edition,
    Mc-Graw-Hill Book Company, 1967.

3.  Tennessee Valley Authority, "The Prediction of Stream Reaeration
    Rates," Chattanooga, Tennessee, July 1962.

4.  U. S. Department of Health, Education, and Welfare, Public Health
    Service, "Ohio River - Cincinnati Pool," Part I - 1957 Survey.

5.  U. S. Department of Health, Education, and Welfare, Public Health
    Service, "Ohio River - Cincinnati Pool," Part II - 1960 Survey.

6.  U. S. Department of Health, Education, and Welfare, Public Health
    Service, "Oxygen Relationships in Streams,"  Robert A. Taft
    Sanitary Engineering Center, Cincinnati, 26, Ohio, March 1958.

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       APPENDIX A

 STATION LOCATIONS AND
       STUDY PLAN

OHIO RIVER-McALPINE POOL
                                               69

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70
                   OHIO RIVER  (McALPINE POOL) STUDY
                          STATION LOCATIONS
   Industrial

   DC      The  effluent  from Dow Corning Corporation of Carrollton, Kentucky.
          Samples were  collected  from a manhole in the effluent discharge
          pipe between  the Company parking  lot and Hwy. 42.  The discharge
          flows  into  the Ohio River near R.M. 541.0.

   M&T     The  effluent  from M&T Chemicals,  Inc. of Carrollton, Kentucky.
          Samples were  collected  from the waste discharge pipe on the bank
          of the Ohio River.  The waste flows into the river near R.M. 543.5.

   KG      The  effluent  from Kawneer Co., Inc. of Carrollton, Kentucky.  Samples
          were collected from the waste sump inside the plant.  The waste flows
          into the  river near R.M. 554.7.
   Municipal

   CK      The  effluent  from  the Carrollton, Kentucky, primary sewage treatment
          plant.  The waste  flows into the Kentucky River at mile 0.7.

   LK      The  effluent  from  the Louisville Jefferson County Sewer District's
          Kite Creek tertiary  sewage treatment plant.  This waste flows into
          Hite Creek tributary to Herrods Creek  tributary to the Ohio River
          near mile 595.9.

   OP*    Effluent from the  Oak Park Conservency District's primary sewage
          treatment plant.   The waste flows into a small stream which flows
          into the Ohio River  near mile 597.6.

   CH*    Effluent from Charlestown, Indiana, primary sewage treatment plant.
          The  waste is  piped to the Ohio River near R.M. 590.5.

   HA*    Effluent from the  Hanover, Indiana, secondary sewage treatment
          plant.  The waste  is piped to the Ohio River near R.M. 562.6.

   MA*    Effluent from the  Madison, Indiana, primary sewage treatment plant.
          The  effluent  is piped to the Ohio River at R.M. 558.8.

   VE*    Effluent from the  Vevay secondary sewage treatment plant.  The
          waste flows into the Ohio River near R.M. 538.
   Stream

   0-530.0  Ohio River 1.5 miles  upstream of Markland  Lock and Dam.

   0-532.3  Ohio River 0.8 mile downstream of Markland Lock and  Dam.

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                                                                       71

0-533.8  Ohio River 1.0 mile downstream of Markland Lock and Dam and
         adjacent to Lindenburn day mark.

0-540-4  Ohio River 0.6 mile upstream of Dow Corning waste outfall and
         adjacent to Minnet run light.

0-542.0  Ohio River upstream of M&T Chemicals and downstream of Dow
         Corning waste outfalls.

0-545.0  Ohio River 1.5 miles downstream of M&T Chemicals outfall.

0-547.9  Ohio River 2.2 miles below confluence with the Kentucky River
         adjacent to Notch Lick light.

0-555.6  Ohio River 2.2 miles upstream of Madison, Indiana, STP effluent
         and 0.9 mile downstream of Kawneer Company outfall.  Adjacent
         to the Richwood light.

0-561.0  Ohio River 3 miles downstream of the Madison, Indiana, STP
         effluent and adjacent to the Clifty Creek light.

0-566.3  Ohio River downstream of Hanover STP and Clifty Creek Power
         Company effluents and adjacent to Spring Creek light.

0-574.0  Ohio River adjacent to Bethlehem Reach light.

0-582.7  Ohio River adjacent to Oldham C.ounty's water district municipal
         intake.

0-587.7  Ohio River 1.7 miles upstream of Fourteen Mile Creek.

0-595.0  Ohio River below outfalls from the Indiana Army Ammunition
         Plant and above the confluence of Harrods Creek.

0-600.6  Ohio River adjacent to the Louisville, Kentucky, municipal
         water intake.

K-1.4    Kentucky River upstream of the Carrollton, Kentucky, STP
         effluent and 1.4 miles above the confluence of the Ohio River.

H-1.6    Harrods Creek at U.S. Hwy. # 42 bridge 1.6 miles above the mouth.
*  Samples analyzed by EPA, Evansville, Indiana, office.

Note:  Ohio River mileage and station location descriptions are based on
       the Ohio River Navigation Charts produced by the U.S. Army Crops
       of Engineers.

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72
                              STUDY PLAN
                      OHIO RIVER-MCALPINE POOL
   OBJECTIVES

        •  To determine  the  cause  of  low  dissolved  oxygen concentrations

           observed  in the lower portion  of McAlpine Pool during the

           August-September  1971 EPA,  Region IV, Ohio River Study.

        •  To characterize the  industrial and municipal waste discharges

           into the  study reach of the Ohio River.


   SCOPE

        The study area will  be  limited to the reach of Ohio River between

   Louisville, Kentucky  (RM  600),  and Markland  Pool adjacent to Craigs

   Creek at RM 530.


   AUTHORITY

        Authority for the study is granted in  the Federal Water Pollution

   Control Act as amended.   The work will be performed under the direction

   and supervision of the Environmental Protection  Agency, Surveillance

   and Analysis Division, Athens,  Georgia.


   TIME SCHEDULE

        •  Field study - September 18-25, 1972

        •  Complete lab  analysis  - October 31,  1972

        •  Finished report  - November 30, 1972


   GENERAL FIELD ACTIVITIES

        The principal effort in this study will be  directed  toward  the

   collection of stream quality data.  The relatively few sources  of

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                                                                       73




municipal and industrial waste discharged into the study reach will




be sampled to determine possible effects upon Ohio River water quality.




     The Louisville-Jefferson County Metropolitan District will




provide laboratory space for the study at the Fort Southworth sewage




treatment plant.  Samples will be collected, packed in ice, and delivered




to the Fort Southworth lab for a portion of the required analysis.   The




samples will be forwarded to the Environmental Protection Agency lab




in Athens, Georgia, for completion of the analysis.







WATER QUALITY STUDIES




     Samples will be collected for five consecutive days at the 17




stream sampling stations listed in Table 1.  Field analysis will consist




of:




     •  DO (Field titration)




     •  pH (Field meter)




     •  Temperature




Other chemical analyses:




     •  BOD 5




     •  Turbidity




     •  Acidity and Alkalinity




     •  Nitrogen series (NH3, N02-N03, TKN)




     •  Phosphorus - Total and Soluble




     •  Specific Conductance




Bacteriological analyses:




     •  Total and Fecal Coliform




     •  Salmonella Isolation

-------
            74
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-------
76
     Samples will be collected at the following depths:


          •  Field Analysis (DO, pH, Temperature)


             1)  Stream depth <10 feet mid depth.


             2)  Stream depth 10 to 15 feet - 5 feet from surface


                                            - 1 foot from bottom


             3)  Stream depth >15 feet - 5 feet from surface


                                       - mid depth


                                       - 1 foot from bottom


          •  Chemical Analysis - mid depth in stream <10 feet deep and at


             5 feet in stream = 10 feet deep.


          •  Bacteriological - immediately below surface (approximately 1


             foot) .



     MUNICIPAL WASTE


          Samples will be collected at the nine waste treatment facilities


     listed in Table 2.  Composite samples will be collected proportional


     to flow where possible.  Grab samples will be collected from the


     septic tank overflow.  The following analyses will be made:


          •  Flow  (field measurement or plant equipment)


          •  pH (field meter)
           •  TOC


           •  Total Solids


           •  Nitrogen  Series  (TKN, NH3, N02-N03)


           •  Total Phosphorus

-------






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-------
78
       •  Total Suspended Solids




       •  Volatile Suspended Solids




       Samples will be collected prior to chlorination with the excep-




   tion of bacteriological samples which will be collected after the




   chlorine contact chamber where possible.







   INDUSTRIAL WASTES




       Two 24-hour composite samples will be collected on the industrial




   waste discharges listed in Table 3.  Flow rates will be determined




   by:




       •  Company flow measuring equipment




       •  Flow measurement by EPA personnel




       •  Company water records




       •  Company estimate




       One grab sample for coliform analysis will be collected at each




   effluent.  Standard analyses will be:




       •  Temperature (beginning and end of composite)




       •  pH (beginning and end of composite)




       •  Alkalinity and Acidity




       •  BOD5




       •  COD




       •  TOC




       •  Nitrogen Series (TKN, N02-N03,




       •  Total Phosphorus




       •  Total Solids




       •  Suspended Solids

-------










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80
   These  additional  analyses may be  required on industrial samples:




   • Metals  --  chromium,  tin,  copper,  zinc, lead




   • Organics




   • Oil and grease




   • Phenols




   • Cyanide




   • Detergent

-------
                                                                  81
                           APPENDIX A

                PERSONNEL ROSTER AND TIME SCHEDULE
                 OHIO RIVER (MCALPINE POOL) STUDY
                  Study Director  - David W. Hill

Personnel

     Project Engineer	Charles Sweatt

     Microbiologist	Herbert Barden

     Chemist	Tom Bennett

     Chemist Aide	Tom Sack

     Aide	Wayne Bent ley

     Field Personnel	Rod Davis
                                    Hugh Vick
                                    Ray Wilkerson
                                    Eddie Shollenberger

-------
82
                      TENTATIVE TIME SCHEDULE

                                                           No. Samples
                       Daily Activity                     chem    Bacti

          •  Drive from Athens to Louisville

 9/19      •  Make boat run upstream                        25      17
          •  Set up automatic samplers at:
             1)  Ammunition Plant Primary
             2)  Ammunition Plant Secondary
             3)  Ammunition Plant Laundry Waste
                 Ammunition Plant Septic Tank (Grab)       _1       1
                                                           26      18

 9/20      •  Make boat run downstream                      25      17
          •  Collect composite samples                      3       3
          •  Set up automatic samplers at:
             1)  Oak Park Primary
             2)  Charlestown Primary
             3)  Hanover Secondary                         --      —
                                                           28      20

 9/21      •  Make boat run downstream                      25      17
          •  Collect composite samples                      3       3
          •  Set up automatic samplers at:
             1)  Dow Corning Corporation
             2)  M&T Chemicals, Inc.                       --
             3)  Kawneer Company, Inc.                     --      --
                                                           28      20

 9/22      •  Make boat run upstream                        25      17
          •  Collect composite samples                      3       3
                                                           28      20

 9/23      •  Make boat run upstream                        25      17
          •  Collect composite samples                      3       3
          •  Set up automatic samplers at:
             1)  Madison Primary
             2)  Carrollton Primary
             3)  Louisville Tertiary                       --      --
                                                           28      20

 9/24      •  Collect composite samples                      3       3
          •  Collect any missed or  lost  samples;           <6      <6
             collect samples on Bear Grass and Goose
             Creeks if time permits                        	     	
                                                           <9      <9

-------
                                                      83
            APPENDIX B




CHEMICAL AND BACTERIOLOGICAL METHODS

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                                                                       87





BACTERIOLOGICAL METHODS




     Total Coliform Enumeration;  The membrane filter procedure out-




lined in Standard Methods (1) was used.  The method employs M-Endo




Broth with an incubation at 35 + 0.5°C for 22-24 hours.




     Fecal Coliform Enumeration;  The membrane filter procedure out-




lined in Standard Methods (1) was used.  The method employs M-FC




Broth with an incubation temperature of 44.5 +_ 0.2°C for 24 hours.




     Salmonella Isolation and Identification:  Swabs used for isola-




tion purposes were placed into wide-mouthed jars containing approxi-




mately 200 ml of 1-1/2 strength Tetrathionate Broth with brilliant




green added (1:100,000 w/v).   The inoculated enrichment was incubated




for 24-48 hours at 41.5°C according to the procedure of Spino (2).




Some of the primary enrichments were subcultured again to Tetrathionate




Broth with brilliant green for 18-24 hours at 41.5°C.




     After either primary or subculture enrichment, an inoculum from




each enrichment was streaked onto Hekton Enteric Agar and Xylose-




Lysine-Desoxycholate Agar (XLD) and incubated for 18-24 hours at




35 +_ 0.5°C.  Suspect Salmonella colonies were picked from the




respected plates and subjected to the identification scheme outlined




in Table I.




     The methods and media outlined in Table I are described by




Ewing (3) with the exception of the cytochrome oxidase procedure.




Oxidase was determined using Patho-Tec-CO—  reagent impregnated




paper strips.
JL/ Does not imply  endorsement of this product

-------
                                                     TABLE B-4
                              IDENTIFICATION  SCHEME FOR  SALMONELLA SUSPECTS
                                        Suspect colony


                                   Lysme Iron Agor (LIA)
                        i                                           I
          Alkaline slant and alkaline or                    Acid slant and butt;  Alkaline
          neutral butt with or  without  H2S                 slant and acid butt-DISCARD


                 Urease Production
    I                                        1
Positive                                   Negative
DISCARD                                     I
                                    Cytochrome Oxidase
                   Positive                                     Negative
                   DISCARD                                       I
                                                    Lactose,Sodium Maionate, Indole
                                    Positive                                               Negative
                                    DISCARD                                                 I
                                                                           Lysme decarboxylOM, Citrate, Motility, HZS
                                                                Positive                                           Negative
                                                                    |                                              DISCARD
                                                             Poly Q" Antisera
                                             Positive                                 Negative
                                                I                                    DISCARD
                                  Complete  Serological  Identification

                                                 I
                              Confirmation of identification by National
                                     Center For Disease Control

-------
                                                                       89


                           REFERENCES
1.   American Public Health Association,  Standard Methods for the
    Examination of Water and Wastewater,  13th Edition,  1971.

2.   Spino, D. V., "Elevated-temperature  Technique for the Isolation
    of Salmonella from Streams," Appl. Microbiol.,  14,  No.  4,  1966.

3.   Ewing, W. H., "Enterobacteriaceae,  Biochemical  Methods  for Group
    Differentiation," Public Health Service Publication No.  734,
    Revised 1962.

-------
                                                    91
          APPENDIX C




STREAM AND WASTE QUALITY DATA

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                                                  121
          APPENDIX D

     REGION V REPORT ON
INDIANA ARMY AMMUNITION PLANT

-------
122
                  REPORT ON WASTE DISPOSAL FACILITIES
                      AT FEDERAL INSTALLATIONS
                       DEPARTMENT OF THE ARMY
                    INDIANA ARMY AMMUNITION PLANT
                    DATE OF REPORT:  January 6, 1972

                 ENVIRONMENTAL PROTECTION AGENCY
                            REGION V

                    1 NORTH WACKER DRIVE
                    CHICAGO, ILLINOIS 60606

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                                                                123
     A visit was made to the Indiana Army Ammunition Plant,
Charlestown, Indiana, on September 30, 1971, by Messrs. Harry
Maroney, and Irving Bernstein, of the U. S. Environmental Protection
Agency, Region V, Chicago, Illinois, to inspect previously recom-
mended improvements contained in "Report on Waste Disposal Practices
at Indiana Army Ammunition Plant", dated May 1, 1969, conducted by
the Federal Water Pollution Control Administration, Ohio Basin Region,
and to observe current operations.  The following persons were in
attendance:

1.  Indiana Army Ammunition Plant:

      Lt. Col. W. F. Crews              Commanding Officer
      Mr. Maurice Mennen                Executive Assistant

      Mr. W. W. Struck                  Operations Review
      Mr. T. R. Owen                    Industrial Specialist

2,  Olin Inc.

      Mr. B. C. Baldridge               Resident Manager
      Mr, W, Rice                       Director, Engineering
      Mr. E. L. Allen                   Engineer
      Mr. H. D. Foster                  Engineer
I.  General Description;

      The Indiana Army Ammunition Plant is located in Clark County,
Indiana, approximately 1/4 mile south of Charlestown.  The instal-
lation consists of 1,390 buildings located on approximately 10,600
acres, the terrain being flat to slightly rolling, and situated on
bluffs above the Ohio River.  The major portion of the drainage
flows to three minor tributaries of the Ohio River, namely, Jenny
Lind Run, Battle Creek, and Lentzier Creek.

      The present population numbers approximately 4,500 employees.
The manufacturing plant has been reduced to five hundred (500)
employees, and the present employment at the loading plant is 4,000.
The population figure includes approximately 60 persons living in
housing areas on the plant site.

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124

                                    -2-

   Subject:  Report on Waste Disposal Facilities at Indiana
             Army Ammunition Plant
        The primary mission of IAAP is the manufacture of single base
   propellants and the loading of cannon and mortar propellants.
   Formerly, Indiana Army Ammunition Plant was operated as two separate
   plants, designated as Indiana Ordnance Works (the propellaht manu-
   facturing plant), and Hoosier Ordnance Plant (the loading plant).

        A.  Responsible Agency:

        The installation is Government Owned(Army) Contractor Operated,
   (Olin Corporation), and is directly under control of the U. S.
   Army Ammunition Procurement and Supply Agency, Joliet, Illinois.

        B.  Dates of Visit:

        September 30, October 1, 1971

        C.  Background Data:

        1.  Receiving Waters:  Industrial wastes are discharged to
   Jenny Lind Run, then to the Ohio River.  Sanitary wastes are dis-
   charged to the Jenny Lind Flume, and then Jenny Lind Run? or to
   the Ohio River directly.  Storm, waters drain to Jenny Lind Run,
   tributary to the Ohio River, or to Lentzier Creek,

        2,  Waste discharge flows:  Present, 333,OQOGPD Sanitary
   wastes  (253,000 HOP and 80,000 IOW),  The average flow of the
   industrial waste is approximately 1,287,000 GPD, which includes
   an unknown quantity of springwater infiltration.  The major
   portion of the industrial waste is generated in the HOP production,
   since IOW activities have been curtailed.

   II.  Waste Treatment Facilities and Practices;

        A.  Separate storm, sanitary and industrial waste sewer
   systems are installed.

        1.  Storm Sewer:  Storm water drainage in the IOW area is in
   most part from roof surfaces, either directly, or via gutters, and
   downspouts, parking areas, surface roads, unimproved land, etc.,
   by natural runoff to two parallel 48" diameter storm sewers, then
   to the  Jenny Lind Run, tributary to the Ohio River,  Storm water
   drainage in the HOP area is by natural runoff, and a series of
   ditches to Lentzier Creek.

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                                                               125
                             -3-

Subject:  Report on Waste Disposal Facilities at Indiana
          Army Ammunition Plant
     2.  Sanitary Wastes:  All sewage generated at IAAP is treated
at the IOW and HOP sewage treatment plants and numerous septic tank
facilities, as follows:

         a.  IOW sewage treatment plant.   This primary treatment
plant serves the entire propellant manufacturing area and is
currently operating at a reduced level,  since the production of
single base propellant has ceased.  The  plant has been designed
for a population equivalent of 10,000, and the sanitary waste is
generated in the administrative and shop areas.

Performance of all equipment is satisfactory and no appreciable
odor prevailed.  The plant consists of the following equipment:
Bar screen, two primary settling tanks with mechanical scrapers,
two anaerobic digesters (one heated with fixed cover, and the
other open), and four sludge drying beds.  The plant effluent
flow is monitored by utilizing a flow recorder and V-notch weir,
and  is discharged to Jenny Lind Lagoon  without benefit of chlorine
contact chamber or plant effluent chlorination.  However, the
sewage in the primary tank is dosed with hypochlorite.  Jenny Lind
Lagoon is elevated and diked, and the spillover is aerated in
flowing to a lower level lagoon.  The two lagoons are known as
Jenny Lind Run, tributary to the Ohio River»  The plant effluent
discharged was observed to be clear, colorless,odorless, and
exhibited no signs of floating oil, grease or scum.

     A typical plant effluent analysis is listed below:

                            November 1971

                            Monthly Average

BOD                             7.7 PPM

pH                              8.0

Dissolved Oxygen               11.0 PPM*

                    *Stream Analysis

     The BOD concentration of 7.7 PPM is at a minimum of 25% of
that to be expected from a primary treatment plant.  The low
concentration could be due to infiltration and dilution of the
waste waters from the vehicle wash rack.  The BOD discharged from

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126
                                  -4-

   Subject:  Report on Waste Disposal Facilities  at  Indiana
             Army Ammunition Plant
   the plant is not degrading the waters of the lagoon,  since  the
   dissolved oxygen in the stream approaches saturation.

             b.  HOP Sewage Treatment Plant.  This secondary sewage
   treatment plant provides services for the loading  area.   The plant
   was designed for a population equivalent of 9,000,  and an average
   flow of 1.25 MGD, and consists of a "Bio-Activation Process",
   combining a trickling filter and activated sludge  treatment.
   Components include lift station, comminutor, bar screen,  Parshall
   flume, two primary tanks, dosing chamber, high rate rotary  trick-
   ling filter (no mercury seal), aeration tank, intermediate  and
   final settling tanks, aerobic digester, six (6) sludge drying beds,
   three plant effluent pumps, and an eight-inch force main  to the
   Ohio River.  There are two streams of raw sewage influent to the
   sewage treatment plant.  The one originating in the bag manufacturing
   area flows by gravity, and the other is pumped to  the sewage treat-
   ment plant.  The lift station and final settling tanks have by-
   passing facilities to the Lenzier Creeks.  There is no chlorine
   contact chamber.  Chlorination is provided in the  effluent  lift
   station wet well and a pipe three miles long is utilized  to
   obtain the required detention time.  The plant effluent discharged
   was observed to be clear, colorless, odorless, and exhibited no
   signs of floating oil, grease or scum.  There is no recording in-
   strumentation,  Flow is calibrated from the height on V-notch weir.

        A typical plant effluent analysis is listed below for
   November 1971:

                                 Monthly Average

        BOD                      2.2 PPM

        pH                       7.4

        Dissolved Oxygen        12.0

   The BOD concentration is too low for the degree of  treatment provided,
   which could signify that infiltration is affecting  the results.

             c.  Septic Tanks:  Domestic wastes from  the military
   housing River Ridge Area (49 houses - 160 persons)  are discharged
   to three septic tanks.  These tanks do not have terminal  drain-
   fields, and the effluent is discharged directly to the Ohio
   River, without disinfection or other treatment. Approximately
   100 additional septic tanks exist at Indiana Army  Ammunition Plant,

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                                                               127
                              -5-

Subject:  Report on Waste Disposal Facilities at Indiana Army
          Ammunition Plant
the major portion of which have been replaced by sanitary sewer
connection to the treatment plant.

          d.  Cafeteria:  Currently, the cafeteria cooking facil-
ities are not being utilized.  Food is delivered by a Louisville
caterer, and only dishes are washed.  Solid wastes are disposed
of in a container and removed and disposed of by the caterer with
his facilities.  The building is fitted with grease traps.

          e.  Automobile Service Station:  All crankcase oil from
the servicing operation is recovered and disposed of by sale.
Motor oil is reprocessed.

          f.  Vehicle Maintenance Area:  The locomotive repair
shop, Building 718, has floor drains in the service pits which
lead to the sanitary sewer.  The building is equipped with traps
to intercept grease and oil.  There are two wash racks in
Building 2552, the effluent from which (emulsified oil and grease)
is also discharged to the sanitary sewer.  Traps have been
installed to intercept any oil before discharge to the sewer.

          g.  Laundry wastes from Building 1021 are discharged to
a baffled settling tank, which overflows into the sanitary sewer
system.  The waste contains detergent and some lint.

     3.  Industrial Wastes:

        a. Bag Loading:    The bag loading plant (HOP) is currently
active.  The operations consist of the fabrication of a cloth bag,
and the loading of mortar and cannon propellant into these bags.
The latter are manufactured from purchased cloth and made to
various bag sizes by sewing machine operators at the plant.  Also,
paper tubes are manufactured for the packaging of the propellant
bags, before inserting them into a box for shipment to an ammuni-
tion loading plant.  Also, titanium dioxide is purchased and
blended with a wax compound.  This material is utilized for gun
tube protection.  No appreciable amounts of industrial waste are
generated from the above operations.

          b.  Propellant Manufacturing: (IOW).  The plant is
currently in an inactive status, but when operative, includes
the manufacture of smokeless cannon and mortar propellants and

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128
                                  -6-
   Subject:   Report  on Waste  Disposal  Facilities  at  Indiana Army
             Ammunition Plant
   support acids  (nitric and sulfuric), which  are  as  follows:

        1.  Nitrocellulose is produced by  the  interaction  of wood
   pulp and/or cotton linters and  nitric acid.   In this  process
   sulfuric acid  is used as a dehydrating  agent.

        2.  In the next  step, ether  and alcohol are used as a  drying
   agent to remove water from the  nitrocellulose.   The dry, lumpy
   material formed is extruded through a die,  forming strands  approxi-
   mately 4 feet  long, which are then cut  to grain size  about  3/4
   inch long.

        3.  Nitric acid  is manufactured by the oxidation of ammonia
   gas (AOP process), and sulfuric acid by the burning of  sulfur to
   sulphur dioxide, and  subsequent oxidation to sulfur trioxide  in
   the presence of a vanadium pentoxide catalyst.   The sulfuric
   trioxide is collected in water  to form  sulfuric acid.

   The wastes  from the propellant  lines, and sulfuric and  nitric
   acid plants are discharged to the industrial waste sewer system,
   which leads to the Jenny Lind Flume.  The acid  wastes include
   sulfuric and nitric acids.  Other wastes which  enter  Jenny  Lind
   Flume include  nitrocellulose and other  organic  materials from
   the propellant lines  (ether and alcohol, butylthalate,  diphenyl,
   etc.).  Lime is added to both lines for neutralization  (controlled
   manually),  based on pH readings taken near  the  junction of  Jenny
   Lind Run and the Ohio River.

             c.  Cooling towers are used in the loading  plant  to
   condition air.  A closed loop system is used with  a minimum of
   blowdown.  Copper piping is used in the system, and consequently
   no corrosion inhibitors or fungicides are required.

             d.  Indiana Army Ammonition Plant has two powerhouses
   (in an inactive status) which contain boilers,  air compressors
   electrical generators and other supporting  equipment.  Each power-
   house is operated in  conjunction with a cooling tower and  reservoir,
   The water reaching the boiler room receives treatment with ferric
   sulfate, and the coagulated solids are  removed  in  a precipitator.
   The effluent is then  discharged to an anthrafelt filter,  and then
   a clear well.   The boiler make  up water (clear  well  effluent)
   then receives additional treatment in a zeolite softener,
   Backwash from the zeolite softener (calcium and

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                                                               129

                            -7-

Subject:  Report on Waste Disposal Facilities at Indiana Army
          Ammunition Plant
magnesium chloride) , and anthrafelt filter, precipitator sludge
(ferric hydroxide), coal ash, and boiler blow down are discharged
to a suinp which overflows to the lagoon.  There are numerous other
package steam and hot water boiler plants scattered over Indiana
Army Ammunition Plant.  The make up water for these boiler plants
is treated with a chelating agent, and receives subsequent condition-
ing in a zeolite softener.  The boiler blowdown, and softener
regeneration x^stes are discharged to an impervious clay bottom,
land locked settling basin.

III.  Storage of Hazardous Material

     There are two 18,000 gallon fuel oil storage tanks which do
not have sufficient diked capacity to contain the full content of
each tank in the event of a major spill.  The fuel oil storage tank
farm is also diked.  Numerous other oil storage tanks are either
diked or installed underground.  The acid tanks (sulfuric, nitric
and mixed acid)are not diked, but any spillage would be discharged
into the process sewer lines, receive subsequent neutralization,
and sulfate precipitation treatment, before discharge to the
receiving streoin.  Ether, alcohol, and ammonia tanks are not diked.

There are numerous above ground storage magazines for storage of
loaded propellant bags at ambient temperature.  Any spillage in
these magazines would be on a dry basis.  In the event of a spill,
the powder could be swept up and taken to the disposal ground.

IV.  Improvements Proposed by Indiana Army Ammunition Plant:

     The following improvements will be, or have been, made
consistent with the recommendations contained in the May 1, 1969
FWPCA Report, and the U. S. Army Environmental Hygiene Agency,
Edgewood Arsenal, Maryland, Sanitary Engineering Survey,
Indiana Army Ammunition Plant, Charlestown, Indiana:

     1.  Improved ventilation in chlorine cylinder storage room
Building 403-2.

     2.  Provided Bureau of Mines - approved respiratory
protective masks in the chlorine cylinder storage room, Build-
ing 403-2, cooling tower chlorinatio,  room and Building 6001
(HOP well water chlorination facilities).

     3.  Installation of Standard Methods, (OTA) procedure to
determine free avaJ" able chlorine residual in progress.

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130
                                 -8-

    Subject:  Report on Waste Disposal Facilities at Indiana Army
              Ammunition Plant
         4.  Completed 65% of a survey to establish the points where
    storm waters could enter the sanitary sewer system and other
    sources of infiltration.

         5.  Provided multiplication factors for calculating flow
    from the continuous recorder at HOP Sewage Treatment Plant.
    The factors have been placed on the instrument.

         6.  Conducted a study as to the best approach to provide the
    degree of treatment required (secondary) in the River Ridge septic
    tank area.  The conclusion reached is that the only method to cope
    with the problem is the construction of two new package aeration
    treatment plants.  Accordingly, FY'72 funds have been requested
    to construct these facilities.   Completion is expected in FY '73.

         7.  FY '71 funds ($5,000)  were requested for the design of
    the package type aeration treatment facilities to replace septic
    tanks.  FY '72 (MCA) funds ($89,000) have been requested to
    construct these facilities.

         8.  Provided chlorination facilities for the HOP Sewage Treatment
    Plant.

         9.  The dried sludge disposal area has been relocated from
    a position where it could be a source of water pollution,
    especially during heavy and prolonged rainfall.

         10. FY '72 - '74 Funds have been requested for integrating
    and totalizing flow recorders for both sewage treatment plants.
    Included also is the purchase and installation of an automatic
    (Technicon) sampler.  The monitor will be located between the
    lower settling pond and the Ohio River.

         11.  FY '74 funds will be requested to reroute the HOP
    Sewage Treatment Plant lift station and final settling tank by
    pass lines, and sludge bed effluent piping to a new lift station.
    The latter will pump any sanitary wastes from these sources to
    the head of the sewage treatment plant.  The pumps will be driven
    by a liquified petroleum internal combustion engine, and. serve
    in a stand by capacity for use during a power failure.

         12.  The updating of the IOW sewage treatment plant from
    primary to secondary treatment is scheduled for completion during
    FY '72.  Included in the new facilities are a trickling filter,
    final settling tanks and chlorination facilities.

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                                                                131
                               -9-

 Subject:  Report on Waste Disposal Facilities at Indiana Army
           Ammunition Plant
      13.  Grease traps have been installed in Buildings 401-2,
 718, and 2552.

      14.  The settling tank baffles at the laundry, Building 1021,
have been repaired.

      15.  Upon resumption of manufacturing operation, an industrial
 waste monitoring program will be provided.

      16.  Funds have been requested to enlarge the dike capacity
 for the 18,000 gallon fuel oil storage tanks to hold at least
 the contents of each tank.

      17.  Replaced septic tank at Building 2558 with line to
 sewage treatment plant.

 V.   Recommendations:
      1.  The existing practice of neutralizing industrial wastes
 with lime be augmented with facilities for removing the nitrate ion.
 Under present conditions industrial wastes are neutralized with
 lime before discharge to the Ohio River.  Most of the sulfate is
 removed by precipitation, but the nitrate ion is discharged to
 the river unaffected by treatment.  This project should be initi-
 ated if and when the production of cannon and mortar propellant
 is resumed.

      2.  Consideration be given to diking of the ether, alcohol
 and ammonia tank at the IOW plant, upon resumption of operation.

      3.  The raw and treated sanitary and industrial waste be
 monitored on a regular basis.

      4.  A testing program be established which should include
 5 day BOD, suspended and settleable solids, pH and chlorine
 residual.  For the HOP sewage treatment plant, in addition to
 the above tests, sludge index and colorimetric dissolved oxygen
 should be run.  BOD of the raw wastes and final effluent be
 determined at least once a week, preferably twice a week,
 (3 hour composites) taken at 11:00 A.M., 12:00 Noon, and IrOOP.M.,
 suspended solids of raw waste and final effluent at least once
 a week at the same hours, settleable solids once or twice a week
 at representative flows.

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132

                              -10-

    Subject:  Report on Waste Disposal Facilities at Indiana Army
              Ammunition Plant
    Chlorine residual of the effluent daily,  Monday through Friday,
    twice daily when stream conditions require, sludge index and
    colorimetric dissolved oxygen test weekly.

         Daily monitoring be conducted on the combined effluent at
    the junction of Jenny Lind Run and the Ohio River for flow,
    BOD, COD, pH, suspended solids, dissolved solids, and nitrates.

         5.  The discharge of septic tank effluent to the Ohio River
    be curtailed as expeditiously as possible.

         6.  The overflow line from the boiler plant water treatment
    sump be diverted from the lagoon to the sanitary sewer.  It is
    conceivable that during heavy rainfall there could be a discharge
    to the lagoon.

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                                                   133
           APPENDIX E




ORGANIC COMPOUNDS IDENTIFICATION

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                                           135
   APPENDIX F




PERSONNEL ROSTER

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136
                           APPENDIX F

                        Personnel  Roster
                 Ohio  River (McAlpine Pool)  Study
     David W.  Hill -  Study Director


     Charles  Sweatt - Project  Engineer (Field)
                                           \

     Tom Bennett  - Project Chemist  (Lab)


     Herbert  Barden - Project  Microbiologist (Lab)


     Tom Sack - Physical  Science  Technician  (Lab)


     W.  R.  Davis  - Chemist  (Field)


     Hugh Vick -  Chemist  (Field)


     Ray Wilkerson -   Hydraulics  Engineering Technician (Field)

     Eddie Shollenberger  - Engineering Technician  (Field)


     E.  Chaudoir  - Hydrologist (Evansville)


     S.  Paulson - Engineering  Technician  (Evansville)

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                                                                                               137
                                                                                           FIGURE  I
    INO.   f~
\
                       \
    ALA   I     GA.
                               Indiana - Kentucky
                              Clactric Corporation
                           Cl.lly Cr«k Powar Plant
      LOCATION MAP
             Indiana
     Indiana Army      ,
     Ammunition Plant	/*•
                                                       5404
                                                          V
                                                               Corning Wait* \

                                                         M8T Chamicalf Wont \
                                                                                     •Iftftuetf Hirtr
McAlplna L*
     LOUISVILLE
                                                               US. ENVIRONMENTAL PROTECTION AGENCY
                                                                            REGION
                                                                         LOCATION  MAP
                                                                    AND SAMPLING  STATIONS
                                                               SURVEILLANCE AND ANALYSIS DIVISION
                                                               ATHENS                      GEORGIA
                                          *  U.S. GOVERNMENT PRINTING OFFICE : 1973 748—252/3203 Region 4

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