DRAFT
        DEVELOPMENT DOCUMENT FOR
    EFFLUENT LIMITATIONS GUIDELINES
  AND NEW SOURCE PERFORMANCE STANDARDS
   MISCELLANEOUS FOODS AND BEVERAGES
         POINT SOURCE CATEGORY
                PART IV
      EFFLUENT GUIDELINES DIVISION
OFFICE OF WATER AND HAZARDOUS MATERIALS
  U.S. ENVIRONMENTAL PROTECTION AGENCY
         WASHINGTON, D.C. 20460
               MARCH 1975

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DRAFT
                             SECTION VIII

               COST, ENERGY AND NON-WATER  QUALITY ASPECTS


This section presents an evaluation of the costs, energy requirements, and
non-water quality aspects associated with  the treatment and  control  alter-
natives developed in Section VII in terms  of the model processes  and plants
developed in Section V.

COST AND REDUCTION BENEFITS OF ALTERNATIVE TREATMENT AND CONTROL
TECHNOLOGIES

In absence of complete cost information for individual processes, the cost
figures developed herein are based on reliable actual cost figures reported
for various installations coupled with engineering  estimates.   An estimate
completely applicable to all members of an entire  industry is  obviously  im-
possible.  For instance, it must be realized that  land costs vary widely.
Construction cost, in terms of both labor  and material costs,  is  another
element that is highly variable.  The costs presented herein have been de-
veloped for the different industry subcategories,  rather than  the entire
industry, thus reducing some of the variability expected in  costs.  These
costs are, nevertheless, intended to serve as a guide only.Vprincipally for
subsequent economic impact analysis to be  conducted by the U.S. Environmental
Protection Agency.

Assumptions for Cost Analysis

The following assumptions are common for all of the cost estimates in this
section:

     1.   All costs are reported in August 1972 dollars.   All  engineering
          cost estimates were made in December 1974 costs  and  converted  to
          August 1972 dollars by the Construction  Cost Index of the
          Engineering News Record.

     2.   Annual interest rate for capital stock is taken  to be eight per-
          cent.

     3.   All investment cost is depreciated over  a period of  20 years
          except rolling stock which is depreciated over ten years.

     4.   Salvage value is taken as zero at the end of the depreciation
          period.

     5.   Depreciation is attributed by the straight line  method.
                                  841

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DRAFT


     6.   Total yearly cost = (investment cost/2)  (0.08)  + yearly  de-
          preciation cost + operating cost.

     7.   Power costs = $0.04/kw-hr.

     8.   Excavation and fill is estimated at $3.92/cu m ($3.00/cu yd)
          for December 1974.

     9.   Personnel costs for operation is $5.00/hr plus 50 percent fringe
          benefits, administration, and other overhead.

   10.    All capital construction work is performed by an outside con-
          tractor using normal profit margins.

   11.    When between 10 and 20 aeration units are purchased, a discount
          of 5.0 percent is obtained.  When more than 20 units are pur-
          chased, the discount is 7.5 percent.

   12.    The December 1974 cost of steel is $0.20/kg ($0.45/lb).

   13.    The December 1974 cost of concrete is $134/cu m ($175/cu yd).

   14.    The December 1974 cost of contracted truck hauling of dewatered
          sludge or solid waste is $0.77/cu m ($1.00/cu yd).

   15.    The December 1974 cost of contracted truck hauling of liquid
          sludge or wastewater is $5.28/1000 1 ($20.00/1000 gal).

The Feasibility and Costs of Municipal Treatment

Although the purpose of the document is to recommend effluent limitations
guidelines for point source discharges into navigable waters, discharge to
municipal treatment systems is a viable alternative for some installations
and is now the case for many existing plants.  To avoid redundancy, costs
for this alternative are not provided for every subcategory, but are ad-
dressed in the following discussion.

The combined treatment of municipal and industrial wastes often offers an
attractive alternative for industry, if municipal  treatment is available.
Many plants within the miscellaneous foods and beverages industry dis-
charge to municipal sewers and, in fact, all plants within some of the
subcategories discussed in this document,use municipal treatment.   Pre-
treatment for these industrial wastes varies from non-existent to the
equivalent of secondary treatment.

Many of those plants which do not presently utilize municipal facilities
may not have the feasible option to do so because of location restraints.
Others do not use municipal treatment by choice because of municipal
treatment cost or because they had already invested heavily in separate
treatment facilities before municipal treatment became available.

                                   842

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DRAFT
It is conceivable that some plants currently discharging to municipal
treatment will in the future decide to provide separate treatment as
municipal charges will inevitably increase.  It is even more conceiv-
able that more stringent requirements for pretreatment will be made by
municipalities in the future.

Municipal wastewater charges vary widely, as was illustrated in a sur-
vey by Maystre and Geyer (155) in 1970.  The results of the survey
indicated that about 10 percent of small cities, 15 percent of middle
size cities, and 20 percent of larger cities had industrial waste
charges.  All of the 28 cities responding to the inquiry based sur-
charges on BOD and suspended solids, or their equivalents per unit
volume, and on the excess loads of the individual plant relative to
some average value stipulated by ordinance.  Some cities also consid-
ered excess loads of grease and chlorine demand.

Based on the unit costs of treatment applied by the 28 cities, the in-
vestigators calculated the surcharge cost per month for two hypothetical
industries, both having BOD and suspended solids concentrations of 800 mg/1,
but one industry having a flow of 2830 cu m/month (100,000 cu ft/month)
and the other a flow of 28,320 cu m/month (one million cu ft/month).  The
surcharge for the smaller industry ranged from $8/month to $269/month while
the surcharge for the larger industry ranged from $78/month to $2690/month.

                 VEGETABLE OIL PROCESSING AND REFINING

Cost and Reduction Benefits of Alternative Treatment Technologies
for Subcatdgory A 1  - Oilseed Crushing, Except Olive Oi1?_by Direct
Sol vent Extracti on and Prepress Operations	
A model plant representative of subcateogry A 1  was developed in
Section V for the purpose of applying control and treatment alter-
natives.  In Section VII, eight alternatives were selected as being
applicable engineering alternatives.  These alternatives provide for
various levels of waste reductions for the model plant which processes
816 kkg (900 ton) of raw oilseed per day.

Alternative A 1-1 - This alternative assumes no treatment and no re-
duction in the waste load.  It is estimated that the effluent from a
816 kkg (900 ton) per day plant is 148 cu  m/day (0.039 MG-) per day.  The
BOD waste load is 0.061 kg/kkg (0.122 Ib/ton), the suspended solids
load is 0.038 kg/kkg (0.076 Ib/ton), and the oil and grease load is
0.069 kg/kkg (0.138 Ib/ton).  The model plant developed is assumed to
discharge its process wastewater and noncontact waters separately, and
to provide gravity separation and skimming of process waters.  Floatable
oils and sludges from the gravity separation are pumped to an in-plant
oil recovery system.

               Costs:               0
               Reduction Benefits:  None

                                  843

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DRAFT


Alternative A l-II - This alternative provides a flow equalization
basin, complete-mix activated sludge, secondary clarification, a
sludge recirculating pump, a sludge thickening tank, and a sludge
holding tank.

The resulting BOD waste load is 0.0072 kg/kkg (0.014 Ib/ton), the
suspended solids load is 0.0090 kg/kkg (0.018 Ib/ton) and the oil
and grease load is 0.0054 kg/kkg (0.011 Ib/ton).

               Costs:  Total investment cost:  $172,650
                       Total yearly cost:      $ 32,580

An itemized breakdown of costs is presented in Table 163.  It is assumed
that land costs $82,040 per hectare ($33,200 per acre).  It is further
assumed that one operator is required.

               Reduction Benefits:  BOD:  88.2 percent
                                     SS:  76.3 percent
                                    O&G:  92.2 percent

Alternative A l-III - This alternative provides in addition to
Alternative A l-II  dual  media filtration with a pump station to
generate sufficient head for filter operation.

The resulting BOD waste load is 0.0036 kg/kkg (0.0072 Ib/ton), the
suspended solids load is 0.0045 kg/kkg (0.0090 Ib/ton) and the oil
and grease load is 0.0027 kg/kkg (0.0054 Ib/ton).

               Costs:  Total investment cost:  $189,960
                       Total yearly cost:      $ 37,680

An itemized breakdown of costs is presented in Table 164.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that one operator is required.

               Reduction Benefits:  BOD:  94.1 percent
                                     SS:  88.2 percent
                                    O&G:  96.0 percent

A cost efficiency curve is presented in Figure 265.

Alternative A 1-IV - This alternative provides a flow equalization
basin, an aerated lagoon system, and a settling pond.

The resulting BOD waste load is 0.0072 kg/kkg (0.014 Ib/ton), the
suspended solids load is 0.0090 kg/kkg (0.018 Ib/ton) and the oil
and grease load is 0.0054 kg/kkg (0.011 Ib/ton).

               Costs:  Total investment cost:  $154,740
                       Total yearly cost:      $ 38,870

An itemized breakdown of costs is presented in Table 165.  It is
assumed that land costs $4100 per hectare ($1660 per acre).   It is


                                   844

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DRAFT
                            TABLE 163

              ITEMIZED COST SUMMARY FOR ALTERNATIVE A 1-11
                   (OILSEED SOLVENT EXTRACTION)
 ITEMIZED COST SIKKARY FOR I*AST£MTER  TREATMENT  CHAIN
 DESIGN EFFICIENCY... 88.2 PERCENT 600  REDUCTION
 TREATMENT
                   81..CONTROL HCLSE
                   B. ..PUMPING STATION
                   C...EQUALIZATION BASIN
                   K....ACTIVATED SLUDGE
                   G...SLLOGE THICKENER
                   Y...HOLDING TANK
 INVESTMENT  CCSTSI
                i.
                2.
                3.
                4.
            CONSTRUCTION
            LAND
            fc.NGINEER.IMG
            CONTINGENCY
                TOTAL
 YEARLY
OPERATING
        1.
        2.
        3.
  COSTS*
    LABOR
    PCwER
    CHEMICALS
4.  KAINTENANCE&SLPPLIES.
TOTAL
 TOTAL YEARLY COSTS?
                1. YEARLY OPERATING  COST
                ?.. YEARLY INVESTMENT
                   COST RECOVERY
                3. DEPRECIATION
                TOTAL
                          97510.00
                          556«0.00
                           9750.00
                           9750.00
                          172650.00
                                           12490.00
                                            4830.00
                                               0.0
                                            2500.00
                                           19820.00
                                   19820.00

                                    6910.00
                                    5850.00
                                   32580.00
                            845

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  DRAFT
                             TABLE 164

                ITEMIZED COST SUMMARY FOR ALTERNATIVE A l-III
                    (OILSEED SOLVENT EXTRACTION)
ITEMIZED COST SUMMARY FOR HASTEMTEP-  TREATMENT  CHAIN
DESIGN EFFICIENCY... 94.1 PERCENT  BOO  REDUCTION

TREATMENT MCDuLESs
                  ei..CONTROL  WCLSE
                  9...PUMPING  STATION
                  C...EQUALIZATION  BASIN
                  K...ACTIVATED  SLUDGE
                  C...SLUDGE  THICKENER
                  Y...HOLDING  TANK
                  B...PUHP1MG  STATION
                  N...DUAL  *EDIA  FRESSLRt"  FILTRA'N

INVESTMENT TCSTSt
               1,  CONSTRUCTION          111940.00
               2.  UANH                   556aO.OO
               3.  ENGINEERING            11190.00
               a.  CONTINGENCY            11190.00
               TOTAL                     189960.00

YEARLY OPERATING CCSTSt
               1.  LA80R                  I2a90.00
               2.  POER                   6990.00
               3.  CHEMICALS                  0.0
               4.  KATNTENANCERSliPPLlES    3880.00
               TCTAL                      23360.00

TOTAL YEARLY COSTS?
               1. YEARLY OPERATING  COST   23360.00
               ?. YEARLY INVESTMENT
                  COST RECOVERY            7600.00
               3. DEPRECIATION             6720.00
               TOTAL                      37680.00
                             846

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             79.0
             »3.6
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                eo.ee     ai.io     aj.ee    ««.se     at.ce    IT.so     e«.co    «c.so     »2.co    «j.se     «s,oo



                                                    EFFICIENCY



                                                    FIGLRE  265



                        INVESTMENT  AND YEARLY COSTS  FOR SUBCATEGORY  Al,  ALTERNATIVE II  t  III

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DRAFT
                             TABLE 165

               ITEMIZED COST SUMMARY FOR ALTERNATIVE A 1-IV
                   (OILSEED SOLVENT EXTRACTION)
    ITEMIZED COST SUMMARY FOR MSTEMTER  TREATMENT  CHAIN
    DESIGN EFFICIENCY,.. 68.2 PERCENT  ROD  REDUCTION
    TREATMENT MODULES}
                      8. ..PUMPING STATIC^
                                        8ASIN
    INVESTMENT COSTS!
                   1.
                   2.
                   3.
                   4.
                   5.
                      L... AERATED LAGOON
      CONSTRUCTION
      LAND
      ENGINEERING
      CONTINGENCY
      PVC LINEH
                   TOTAL

    YEARLY OPERATING COSTS:
    TCTAL YEARLY
  1.  LABOR
  2.  POWER
  3.  CHEMICALS
  V.  MAINTENANCERSLPPLIES
  5.  PVC LTNFR
  TOTAL

CCSTSl
  1. YEARLY OPERATING COST
  2. YEARLY INVESTMENT
     COST RECOVERY
  3. DEPRECIATION
  TCTAL
123110.00
  3330.00
 12310.00
 12310.00
  3680.00
                                              12490.00
                                              10600.00
                                                  0.0
                                               1920.00
                                                100.00
                                              25110.00
                                              25110.00

                                               6190.00
                                               7570,00
                                              38870.00
                             848

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DRAFT
further assumed that one operator is required.

               Reduction Benefits:  BOD:  88.2 percent
                                     SS:  76.3 percent
                                    O&G:  92.2 percent

Alternative A 1-V - This alternative provides in addition to Alter-
native A 1-IV dual media filtration with a pump station to generate
sufficient head for filter operation.

The resulting BOD waste load is 0.036 kg/kkg (0.0072 Ib/ton), the
suspended solids load is 0.0045 kg/kkg (0.0090 Ib/ton) and the oil
and grease load is 0.0027 kg/kkg (0.0054 Ib/ton).

               Costs:  Total investment cost:  $172,050
                       Total yearly cost:      $ 43,970

An itemized breakdown of costs is presented in Table 166.  It is assumed
that land costs $4100 per hectare/$1660 per acre).  It is further
assumed that one operator is required.

               Reduction Benefits:  BOD:  94.1 percent
                                     SS:  88.2 percent
                                    O&G:  96.0 percent

A cost efficiency curve is presented in Figure 266.

Alternative A 1-VI - This alternative provides a flow equalization
basin, and pressurized air flotation utilizing chemical flocculating
agents to enhance floe formation and floatability of wastes.   Oil
and grease waste skimmings are pumped to an in-plant oil  reclamation.
system.

The resulting BOD waste load is 0.018 kg/kkg (0.036 Ib/ton),  the
suspended solids load is 0.011 kg/kkg (0.022 Ib/ton), and  the  oil
and grease load is 0.021 kg/kkg (0.042 Ib/ton).

               Costs:   Total investment cost:    $149,370
                        Total yearly cost:        $ 31,200

An itemized breakdown of costs is presented in Table 167.  It is
assumed that land costs $82,040 per hectare ($33,200 per  acre).   It
is further assimed that one operator is required.

               Reduction Benefits:    BOD:   69.8 percent
                                      SS:   70.2  percent
                                     O&G:   70.3  percent

Alternative A 1-VII - This alternative provides  in addition to Alter-
native A 1-VI a complete mix activated sludge unit, secondary clarif-
ication, a sludge recirculating pump, a sludge thickening tank,  and
sludge hauling.


                                849

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DRAFT
                            TABLE  166

               ITEMIZED COST SUMMARY FOR ALTERNATIVE A 1-V
                   (OILSEED SOLVENT EXTRACTION)
  ITEMIZED COST  SUMMARY  FOR  KASTEKATER TREATMENT CHAIN
  DESIGN EFFICIENCY... 94.1  PERCENT  BOD REDUCTION
  TREATMFNT MODULES:
                     P...PULPING  STATION1
                     C...EQUALIZATION BASIN
                     L...AE«ATEO  LAGCQN
                     e...PUMPING  STATION
                     N...DUAL  MEDIA  PRESSURE FILTRA'N
  INVESTMENT CCSTS:
                  1.
                  2.
                  3.
                  4..
                  5.
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
                   PVC LINER
               TOTAL

YEARLY OPERATING COSTS:
               1.  LABOR
               2.  POWER
               3.  CHEMICALS
               4.  MAINTFNANCE&SLFPLIES
                   FVC LINE*
                  5.
TOTAL YEARLY
                  TOTAL

               COSTS:
                  1.  YEARLY  OPERATING  COST
                  2.  YEARLY  INVESTMENT
                     COST  RECOVERY
                  3.
                  TOTAL
137540.00
  3330.00
 13750.00
 13750.00
  3660.00
172050.00
 12«
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      W)
      Z
      H4
           150.5
     1*6.9
           1SI.5
           »»«.«
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            76.5
            65.0
      51.S
            38.C
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                                                    EFFICIENCY



                                                    FIGURE  266



                      INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY  Al, ALTERNATIVES IV  &  V

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  DRAFT
                             TABLE  167

                ITEMIZED COST SUMMARY  FOR ALTERNATIVE A 1-VI
                    (OILSEED SOLVENT  EXTRACTION)
ITEMIZED COST SUMMARY FOR  WASTEMTEfl  TREATMENT CHAIN
DESIGN EFFICIENCY... 70.0  P£RCE*T  «00 REDUCTION

TREATMENT MOOULESi
                  ei..CONTROL  MCLSE
                  B...°UMPING  STATION
                  C...EQI ALIZATICN BASIN
                  J...AIR  FLOTATION
INVESTMENT CCSTSl
               1.
               2.
               3.
                   CONSTRUCTION
                   LANO
                   ENGINEERING
               «.  CCNTINGENCY
               TCTAL
YEARLY OPERATING CC5TS:
               1.  LABOR
               2.  PCWER
               3.  CHEMICALS
 78110.00
 55fc40.00
  7810.CO
  7610.00
1U9370.00
 12U90.00
  2120.00
     0.0
  5930.00
 20540.00
               TCTAL

TOTAL YEARLY COSTS:
               1. YEARLY OPERATING  COST
               2, YEARLY INVESTMENT
                  COST RECOVERY            5970.
               3. DEPRECIATION             4690.
               TOTAL                      31200.00
                                          20540.00
                                                00
                                                00
                             852

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DRAFT
The resulting BOD waste load is 0.0036 kg/kkg (.0072 Ib/ton),  the
suspended solids load is 0.0045 kg/kkg (0.0090 Ib/ton) and the oil
and grease load is 0.0027 kg/kkg (0.0054 Ib/ton).

               Costs:  Total investment cost:  $209,480
                       Total yearly cost:      $ 40,690

An itemized breakdown of costs is presented in Table 168.   It  is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that one operator is required.

               Reduction Benefits:  BOD:  94.1 percent
                                     SS:  88.2 percent
                                    O&G:  96.0 percent

A cost efficiency curve is presented in Figure 267.

Alternative A 1-VIII - This alternative provides in addition to
Alternative A 1-VI (dissolved air flotation) an aerated lagoon system
including a settling pond.

The resulting BOD waste load is 0.0036 kg/kkg (0.0072 Ib/ton), the
suspended solids load is 0.0045 kg/kkg (0.0090 Ib/ton) and the oil
and grease load is 0.0027 kg/kkg (0.0054 Ib/ton).

               Costs:  Total investment cost:  $188,460
                       Total yearly cost:      $ 43,300

An itemized breakdown of costs is presented in Table 169.   It  is
assumed that land costs $4100 per hectare ($1660 per acre).  It
is further assumed that one operator is required.

               Reduction Benefits:  BOD:  94.1 percent
                                     SS:  88.2 percent
                                    O&G:  96.0 percent

A cost efficiency curve is presented in Figure 268.

Cost and Reduction Benefits of Alternative Treatment Technologies
for Subcategory A 2 - Oilseed Crushing, Except Olive Oil,  by.
Mechanical—Screw Press Operations

No model plant was developed for this subcategory in Section V as
the industry presently discharges less than 4000 liters (1000  gallon)
of process wastewater per day to municipal facilities.  In Section  VII
two alternatives were considered as being applicable engineering alter-
natives for handling these small volumes of waste.

Alternative A 2-1 - This alternative provides no additional treatment.
                                   853

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    DRAFT
                               TABLE  168

                  ITEMIZED COST SUMMARY FOR ALTERNATIVE A 1-VII
                      (OILSEED SOLVENT EXTRACTION)
ITEMIZED COST SUMMARY FOR  MSTEMTEP  TREATMENT CHAIN
DESIGN EFFICIENCY... 9U.1  PERCENT  BOD REDUCTION
TP.FATN'ENT MODULES:
                  PI..CONTROL  HCLSE
                  P... PULPING  STATION
                  C...EQUALIZATION  BASIN
                  J...AIP  FLOTATION
                  K...ACTIVATED  SLUDGE
                  R...SLUDGE  THICKENER
                  Y...MOLDING  TANK
INVESTMENT CCSTS:
                1 .
                2.
                3.
                «.
                TOTAL

YEARLY OPERATING. COSTS;
                   CONSTRICTION
                   LAND
                   ENGINEERING
               i
               2
               3
                   LA30R
                   PO^FR
                   CHEMICALS
                   KAINTF.NANCERSLPPLIES
TOTAL
               TOTAL

      YEARLY COSTS:
               i . YEARLY OPERATING  COST
               2. YEARLY INVESTMENT
                  COST RECOVERY
               3. D
               TOTAL
127360.00
 566^0.00
 12740.00
 12740.00
2094PO.OO
      i.OO
      '.00
    .0.0
  7330.00
 2U670.00
                                          2^670.00

                                           83PO.OO
                                           76410.00
                               854

-------
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            210.0
            m.i
            IS*.3
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            120.5
            IOJ.6
            »*.«
            Jl.O iv
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                                                     EFFICIENCY




                                                     FIGURE  267




                        INVESTMENT AND  YEARLY COSTS FOR SUBCATEGORY AL ALTERNATIVES VI S VII

-------
DRAFT
                           TABLE 169

              ITEMIZED COST SUMMARY FOR ALTERNATIVE A 1-VIII
                   (OILSEED SOLVENT EXTRACTION)
  ITEMIZED COST SUMMARY  FOR  WASTEIMTER TREATMENT CHAIN
  DESIGN' EFFICIENCY
  TREATMENT MODULES:
                      9.4.1  PERCENT BOD REDUCTION
                    8...PUMPING  STATION
                    C...EQUALIZATION  BASIN
                    J...AIR  FLOTATION
                    L...AF.RATFD  LAGOON
  INVESTMENT CCSTSi
                  1.
                  2.
                  3.
                  a.
                  5.
                    CONSTRUCTION
                    LAND
                    ENGINEERING
                    CONTINGENCY
                    PVC LINER
               TOTAL

YEARLY OPERATING COSTS:
               1.  LABOR
               Gt 9  * W I™ t, i»
               3.  CHEMICALS
               4.  MAINTENANiCE&SLPPLlES
               5.  PVC LINER
               TCTAL

TOTAL YEARLY COSTS!
               i. VEARLY OPERATING  COST
               2. YEARLY INVESTMENT
                  COST RECOVERY
               3. DEPRECIATION
               TCTAL
151210.00
  3330.00
 15120.CO
 15120.00
  3660.00
188460.00
                                            12490.00
                                             6780.00
                                                0.0
                                             7130.00
                                              100.00
                                            26500.00
                                            26500.00

                                             7540.00
                                             9260.00
                                            43300.00
                             856

-------
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                                                   FIGURE  268



                       INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY Al,  ALTERNATIVE  VIII

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DRAFT
               Costs:                0
               Reduction Benefits:  None

Alternative A 2-11 - This alternative consists of a storage tank and
truck hauling of the wastewater to a municipal sewage treatment facility
or suitable land disposal site.  The resulting waste volume to be trucked
averages less than 4000 liter (1000 gallon) per day.

               Costs:   Total investment cost:  $19,450
                       Total yearly costs:     $ 1,510
               Reduction Benefits:             100

.Cost and Reduction Benefits of Alternative Treatment Technologies
for Subcategfirv_jL_l.-. Hydraulic Pressing and Solvent. Fxtrartinn of
Olive Oil

A model plant representative of Subcategory A 3 was developed in Section
V for the purpose of applying control and treatment alternatives.  In
Section VII, three alternatives were selected as being applicable engineer-
ing alternatives.  These alternatives provide for various levels of waste
reductions for the model plant which utilizes 21.7 kkg (24 ton) of whole
olives and 65.3 kkg (74 ton) of cannery pits and culls per day to pro-
duce olive oil.  It is estimated that the effluent from the model plant
is 10.9 cu m (0.0029 KG) per day.  The BOD concentration is 63,000 mg/1,
the suspended solids concentration is 14,000 mg/1, and the oil and grease
concentration is 3220 mg/1.

Alternative A 3-1 - This alternative consists of a pumping station, a
holding tank and spray irrigation of the raw waste effluent.

The resulting BOD waste load is 0.0 kg/kkg (0.0 Ib/ton), the suspended
solids load is 0.0 kg/kkg (0.0 Ib/ton), and the oil and grease load is
0.0 kg/kkg (0.0 Ib/ton).

               Costs:   Total investment cost:  $40,850
                       Total yearly cost:      $ 5,460

An itemized breakdown of costs is presented in Table 170.  It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that no operators are required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent
                                    O&G:  100 percent

Alternative A 3-11 - This alternative consists of four 0.10 ha (0.25
acre) evaporation ponds, lined with PVC fabric to prevent contamination
of the fresh water aquifer.

The resulting BOD waste load is 0.0 kg/kkg (0.0 Ib/ton), the suspended
solids load is 0.0 kg/kkg (0.0 Ib/ton), and the oil and grease load is
0.0 kg/kkg (0.0 Ib/ton).

                                  858

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DRAFT
                        TABLE 170

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A3-I
      (OLIVE OIL, HYDRAULIC PRESS AND SOLVENT EXTRACTION)
ITEMIZED COST SUMMARY  FOR  I"ASTE*ATER TREATMENT CHAIN
3E8IGN EFFICIENCY...100.0  PERCENT POO REDUCTION

TREATMENT MODULESJ
                   Y...HDLDINC  TANK
                   I...SPRAY  IRRIGATION

INVESTMENT CCSTSl
                1.   CONSTRUCTION          31020.00
                2.   LAND                    3630.00
                3.   ENGINEERING            3100.00
                4.   CONTINGENCY            3100.00
                TOTAL                      40850.00

YEARLY OPERATING  CCSTSl
                1.   LABOR                      0.0
                2,   POWER                    850.00
                3.   CHEMICALS                 0.0
                4.   MINTENANCESSUPPLIES   1120.00
                TOTAL                       1970.00

TOTAL YEARLY CCSTSl
                1.  YEARLY OPERATING COST   1970.00
                2.  YEARLY INVESTMENT
                   COST RECOVERY           1630.00
                3.  DEPRECIATION            1860.OC
                TOTAL                       5460.00
                            859

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DRAFT


               Costs:  Total Investment cost:  $60,330
                       Total yearly cost:      $ 6,920

An itemized breakdown of costs is presented in Table 171.   It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that no operators are required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent
                                    O&G:  100 percent

Alternative A 3-111 - This alternative consists of land spreading the
raw waste effluent.

The resulting BOD waste load is 0.0 kg/kkg (0.0 Ib/ton), the suspended
solids load is 0.0 kg/kkg (0.0 Ib/ton), and the oil and grease load is
0.0 kg/kkg (0.0 Ib/ton).

               Costs:  Total investment cost:  $21,720
                       Total yearly cost:      $ 8,330

An itemized breakdown of costs is presented in Table 172.   It is assumed
that; land costs $4100 per hectare ($1660 per acre).  It is further
assumed that one half-time operator is required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent
                                    O&G:  100 percent

Cost and Reduction Benefits of Alternative Treatment Technologies for
Subcateciory A 4 - Mechanical'Screw Pressifig for the Recovery of Olive Oil

A model plant representative of Subcategory A 4 was developed in Section V
for the purpose of applying control  and treatment alternatives.  In Section
VII, three alternatives were selected as being applicable  engineering
alternatives.  These alternatives provide for various levels of waste
reductions for the model plant which utilizes 43.5 kkg (48 ton) of whole
olives per day to produce olive oil.  It is estimated that the effluent
from a 43.5 kkg (48 ton) per day plant is 114 cu m (0.030  MG) per day.
The BOD waste Toad is 78.2 kg/kkg (156 Ib/ton), the suspended solids
load is 149 kg/kkg (297 Ib/ton), and the oil  and grease load is 52
kg/kkg (104 Ib/ton).

Alternative A 4-1 - This alternative consists of a pumping station a
holding tank and spray irrigation of the raw waste effluent.

The resulting BOD waste load is 0.0 kq/kkg (0.0 Ib/ton), the suspended
solids load is 0.0 kg/kkg (0.0 Ib/ton), and the oil and grease load is
0.0 kg/kkg (0.0 Ib/ton).

               Costs:  Total investment cost:  $92,030
                       Total yearly cost:      $10,840
                                   860

-------
  DRAFT
                        TABLE 171

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A3-II
ITEMIZED COST SUMMARY FOR WASTEWATER TREATMENT  CHAIN  A 3-II
DESIGN EFFICIENCY...100 PERCENT BOD REDUCTION

TREATMENT MODULES:
                  EVAPORATION POND

INVESTMENT COSTS:
               1.  CONSTRUCTION              48,170.00  .
               2.  LAND                      2,920.00
               3.  ENGINEERING               4,820.00
               4.  CONTINGENCY               4.820.00
               TOTAL                         60,330.00

YEARLY OPERATING COSTS:
               1.  LABOR                        300.00
               2.  POWER                          0.00
               3.  CHEMICALS                      0.00
               4.  MAINTENANCE & SUPPLIES       340.00
               TOTAL                         1,640.00

TOTAL YEARLY COSTS:
               1.  YEARLY OPERATING COST     1,640.00
               2.  YEARLY INVESTMENT
                   COST RECOVERY             2,410.00
               3.  DEPRECIATION              2,870.00
               TOTAL                         6,920.00
                            861

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 DRAFT
                       TABLE 172

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A3-III
ITEMIZED COST SUMMARY FOR WASTEWATER TREATMENT  CHAIN  A3-III
DESIGN EFFICIENCY...100 PERCENT BOD REDUCTION

TREATMENT MODULES:
                  PUMPING STATION
                  LAND APPLICATION

INVESTMENT COSTS:
               1.  CONSTRUCTION             16,720.00
               2.  LAND                      1,660.00
               3.  ENGINEERING               1,670.00
               4.  CONTINGENCY               1,670.00
               TOTAL                        21,720.00

YEARLY OPERATING COSTS:
               1.  LABOR                     6,230.00
               2.  POWER                      100.00
               3.  CHEMICALS                     0.0
               4.  MAINTENANCE & SUPPLIES     130.00
               TOTAL                         6,460.00

TOTAL YEARLY COSTS:
               1.  YEARLY OPERATING COST     6,460.00
               2.  YEARLY INVESTMENT
                   COST RECOVERY              870.00
               3.  DEPRECIATION              1,000.00
               TOTAL                         8,330.00
                             862

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DRAFT
An  itemized breakdown of costs is presented in Table 173.  It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that no operators are required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent
                                    O&G:  100 percent

Alternative A 4-II - This alternative consists of four 0.4 ha (1.0 acre)
evaporation ponds lined with PVC fabric to prevent contamination of the
fresh water aquifer.

The resulting BOD waste load is 0.0 kg/kkg (0.0 Ib/ton), the suspended
solids load is 0.0 kg/kkg (0.0 Ib/ton), and the oil and grease load is
0.0 kg/kkg (0.0 Ib/ton).

               Costs:  Total investment cost:  $254,970
                       Total yearly cost:      $ 49,530

An itemized breakdown of costs is presented in Table 174.  It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that operators are required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent
                                    O&G:  100 percent

Alternative A 4-111 - This alternative consists of land spreading the
raw waste effluent.

The resulting BOD waste load is 0.0 kg/kkg (0.0 Ib/ton), the suspended
solids load is 0.0 kg/kkg (0.0 Ib/ton), and oil and grease load is 0.0
kg/kkg (0.0 Ib/ton).

               Costs:  Total investment cost:  $46,140
                       Total yearly cost:      $11,390

An itemized breakdown of costs is presented in Table 175.  It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that one half-time operator is required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent
                                    O&G:  100 percent

Cost and Reduction.Benefits  of Alternative Treatment Technologies
for Suhcategory--&-5 - Processing of Edib'Te Oil  by Gaustic RefTriing

A model plant representative of Subcategory A 5 was developed in Section
V for the purpose of applying control  and treatment alternatives.  In
Section VII,  eight alternatives were selected as being applicable engi-
neering alternatives.  These alternatives provide for various levels


                                      863

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DRAFT
                       TABLE 173

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A4-I
       (OLIVE OIL, MECHANICAL SCREW PRESS EXTRACTION)
FEMIZED COST SUMMARY FOR  HASTEMTER  TREATMENT CHAIN
'SIGN EFFICIENCY...100.0  PERCENT  BOD REDUCTION

1EATMFNT MODULES:
                 Y...HOLDING  TANK
                 U... SPRAY  IRRIGATION

DIVESTMENT CCSTSj
               1.  CONSTRUCTION1           66150.00
               2.  LAND                   12660.00
               3.  ENGINEERING            6610.00
               4.  CONTINGENCY            6610.00
               TOTAL                      92030.00

EARLY OPERATING CCSTSl
               i.  LABOR                      0.0
               2.  POWER                    980.00
               3.  CHEMICALS                  0.0
               4.  MAINTENANCE&SLPPLIES   2210.00
               TOTAL                       3190.00

OTAL YEARLY COSTSl
               1. YEARLY OPERATING COST   3190.00
               2. YEARLY INVESTMENT
                 COST RECOVERY            3680.00
               3. DEPRECIATION            3970.00
               TOTAL                      108^0.00
                            864

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DRAFT
                        TABLE 174

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A4-II
ITEMIZED COST SUMMARY  FOR WASTEWATER  TREATMENT CHAIN A4-II
DESIGN EFFICIENCY..,100  PERCENT

TREATMENT MODULES:
                  EVAPORATION  POND

INVESTMENT COSTS:
               1.  .CONSTRUCTION            205,CIO. :C
               2.  LAND                      3.96...V.J
               3.  ENGINEERING              20,500.00
               4.  CONTINGENCY              20,500.00
               TOTAL                       254S9?0.00

YEARLY OPERATING COSTS:
               1.  LABOR                     1,66C.OO
               2.  POWER           •              C.OO
               3.  CHEMICALS                     0. T-
               4.  MAINTENANCE &  SUPPLJ£?   25,370.00
               TOTAL                        2:,0:C OC

TOTAL YEARLY COSTS:
               1.  YEARLY OPERATING  CC~~   2/  OJ'.C;
               2.  YEARLV INVESTMENT
                   COST  RECOVERY            iu,200.00
               3.  DEPRECIATION             '. ",30C-CO
               TOTAL                        4i  -,30. CO
                           365

-------
 DRAFT
                       TABLE  175

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A4-III
ITEMIZED COST SUMMARY FOR WASTEWATER TREATMENT  CHAIN  A4-III
DESIGN EFFICIENCY...100 PERCENT

TREATMENT MODULES:
                  PUMPING STATION
                  LAND APPLICATION

INVESTMENT COSTS:
               1.  CONSTRUCTION             32,920.00
               2.  LAND                      6,640.00
               3.  ENGINEERING               3,290.00
               4.  CONTINGENCY               3,290.00
               TOTAL                        46,140.00

YEARLY OPERATING COSTS:
               1.  LABOR                     6,230.00
               2.  POWER                      830.00
               3.  CHEMICALS                     0.00
               4.  MAINTENANCE & SUPPLIES     500.00
               TOTAL                         7,560.00

TOTAL YEARLY COSTS:
               1.  YEARLY OPERATING COST     7,560.00
               2.  YEARLY INVESTMENT
                   COST RECOVERY             1,850.00
               3.  DEPRECIATION              1,980.00
               TOTAL                        11,390.00
                             866

-------
 DRAFT
of waste reductions for the edible oil model plant which refines
454 kkg (500 ton) of crude edible oil per day.
Alternative A5-1 - This alternative assumes no treatment and no
                              It is estimated that the effluent from
                                              The BOD waste load is
reduction in the waste load.
a 454 kkg per day plant is 314 cu m per day.
4.59 kg/kkg (9.18 Ib/ton), the suspended solids load is 2.49 kg/kkg
(4.98 Ib/ton), and the oil and grease load is 2.39 kg/kkg (4.78 Ib/ton).
The model plant developed for Subcategory A 5 is assumed to have separate
discharge of non-contact and process wastewaters, in-plant gravity sep-
aration, skimming, pH control, and an oil recovery system for the
skimmed oil and water wastes.

               Costs:               0
               Reduction Benefits:  None

Alternative A 5-11 - This alternative provides pressurized air floatation
utilizing chemical flocculating agents to enhance the formation and float-
ability of wastes.  Oil and grease skimmings  are pumped to an in-plant oil
recovery system.

The resulting BOD waste load is 1.37 kg/kkg (2.74 Ib/ton), the suspended
solids load is 0.75 kg/kkg (1.50 Ib/ton), and the oil and grease load
is 0.73 kg/kkg (1.46 Ib/ton).

               Costs:  Total investment cost:  $145,530
                       Total yearly cost:      $ 42,500

An itemized breakdown of costs is presented in Table 176.  It is assumed
that land costs $82,040 per hectare ($33,200  per acre).  It is further
assumed that two operators are required.
               Reduction Benefits:
                                    BOD:   70.1  percent
                                     SS:   70.0  percent
                                    O&G:   69.5  percent
Alternative A 5-111 - This alternative provides in addition to Alter-
native A 5-II a complete mix activated sludge unit including a secondary
clarifier, sludge recirculation, sludge thickening, vacuum filtration,
and a sludge holding tank.

The resulting BOD waste load is 0.069 kg/kkg (0.14 Ib/ton), the suspended
solids load is 0.069 kg/kkg (0.14 Ib/ton), and the oil and grease load
is 0.069 kg/kkg (0.14 Ib/ton).

               Costs:  Total investment cost:  $354,770
                       Total yearly cost:       $ 82,560

An itemized breakdown of costs  is presented in Table 177.   It is assumed
that land costs $82,040 per hectare ($33,200 per acre).  It is further
assumed that two operators are  required.
                                   867

-------
DRAFT
                       TABLE 176

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A5-II
                  (EDIBLE OIL REFINING)
 ITEMIZED  COST  SUMMARY FOP
 DESIGN  EFFICIENCY...  70.0
       WA8TEMTER TREATMENT CHAIN
       PERCENT BOD "EDUCTION
 TREATMENT  MODULES»
 INVESTMENT  CCSTSj
                1.
                2.
                3.
                a.
                   B...PUMPING STATION
                   31..CONTROL HOUSE
                   J...AIR FLOTATION
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                TOTAL

 YEARLY  OPERATING COSTS!
                1.   LABOR
                2.   POWER
                3.   CHEMICALS
                4.   MAINTENANCERSUPPLIES
                TOTAL

 TOTAL YEARLY  CCSTSl
                1.  YEARLY OPERATING COST
                c.  YEARLY INVESTMENT
                   COST RECOVERY
                3.  DEPRECIATION
                TOTAL
 71300.
 59970.
  7130.
                      24990
                        1490
00
00
00
  7130.00
145530.00
       00
       00
     0.0
  5920.00
 32400.00
                      32400.00

                       5820.00
                       4280.00
                      42500.00
                            868

-------
DRAFT
                      TABLE 177

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A5-III
                  (EDIBLE OIL REFINING)
ITEMIZED COST  SUMMARY  FOR  WASTEMTER TREATMENT CHAIN
DESIGN EFFICIENCY...  98.5  PERCENT BOD REDUCTION
TREATMENT  MODULES:
                   B.
                   Bi
                   J.
                   K.
                   G.
                   S.
                   Y.
    .PUMPING STATION
    .CONTROL HOUSE
    .AIR FLOTATION
    .ACTIVATED SLUDGE
    .SLUDGE THICKENER
    .VACUUM FILTRATION
    .HOLDING TANK
INVESTMENT  COSTS:
                1.
                2.
                3.
                4.
  CONSTRUCTION
  LAND
  ENGINEERING
  CONTINGENCY
                TOTAL
YEARLY OPERATING
                1.
                2.
                3.
                4.
CCSTSl
  LABOR
  POWER
  CHEMICALS
  MAINTENANCE&SLPPLIES
                TOTAL

TOTAL YEARLY CCSTSl
                1.  YEARLY  OPERATING  COST
                2.  YEARLY  INVESTMENT
                   COST  RECOVERY
                3.  DEPRECIATION
                TOTAL
2U5660.00
 59970.00
 24570.00
 24570.00
354770.00
 24990.00
 15350.00
  2610.00
 10680.00
 53630.00
                        53630.00

                        14190.00
                        14740.00
                        62560.00
                            869

-------
DRAFT


               Reduction Benefits:  BOD:  98.5 percent
                                     SS:  97,2 percent
                                    O&G:  97,1 percent

Alternative A 5-1V - This alternative provides in addition to Alter-
native A 5-III dual media pressure filtration equipped with a pump
to generate sufficient head for filter operation.

The resulting BOD waste load is 0.035 kg/kkg (0.070 Ib/ton), the
suspended solids load is 0.035 kg/kkg (0.070 Ib/ton), and the oil
and grease load is 0.014 kg/kkg (0.028 Ib/ton).

               Costs:  Total investment cost:  $386,850
                       Total yearly cost:      $ 91,380

An itemized breakdown of costs is presented in Table 178.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.5 percent
                                     SS:  99.6 percent
                                    O&G:  99.7 percent

Alternative A 5-V - This alternative provides in addition to Alter-
native A 5-IV an activated carbon adsorbtion unit before final discharge.

The resulting BOD waste load is 0.021 kg/kkg (0.042 Ib/ton), the
suspended solids load is 0.017 kg/kkg (0.034 Ib/ton), and the oil and
grease load is 0.007 kg/kkg (0.014 Ib/ton).

               Costs:  Total investment cost:  $459,900
                       Total yearly cost:      $117,120

An itemized breakdown of costs is presented in Table 179.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.5 percent
                                     SS:  99.6 percent
                                    O&G:  99.7 percent

A cost efficiency curve is presented in Figure 269.

Alternative A 5-VI - This alternative provides in addition to Alter-
native A 5-II (i.e., dissolved air flotation) an aerated lagoon with
a settling pond.

The resulting BOD waste load is 0.069 kg/kkg (0.14 Ib/ton),  the
suspended solids load is 0.069 kg/kkg (0.14 Ib/ton), and the oil
and grease load is 0.069 kg/kkg (0.14 Ib/ton).


                                   870

-------
DRAFT
                       TABLE 178

         ITEMIZED COST SUMMARY FOR  ALTERNATIVE A5-IV
                  (EDIBLE OIL REFINING)
  ITEMIZED  COST SLPMARY FOR WASTEMTER TREATMENT CHAIN
  DESIGN  EFFICIENCY... 90.2 PERCENT BOD REDUCTION
  TREATMENT MODULES!
                    B.
                    81
                    J.
                    8.
                    Y.
                    B.
                    N.
    .PULPING STATION
    .CONTROL HCU3E
    .AIR FLOTATION
    .ACTIVATED SLUDGE
    .SLIDGE THICKENER
    .VACUUM FILTRATION
    .HOLDING TANK
    .PUMPING STATION
    .DUAL XEDIA PRESSURE FILTRA'N
  INVESTMENT  COSTS?
                 1.
                 2.
                 3.
                 fl.
  CCNSTRLCTICN
  LAND
  EN-GINIEEPING
  CONTINGENCY
                 TOTAL
  YEARLY  OPERATING
                 1.
                 2.
                 3.
                 4.
CCSTSt
  LABOR
  POWER
  CHEMICALS
  MAINTENANCEHSIPPLIES
                 TOTAL

  TOTAL  YEARLY  COSTS:
                 i.  YEARLY OPERATING COST
                 2.  YEARLY INVFSTPENT
                    COST RECOVERY
                 3.  DEPRECIATION
                 TOTAL
272^100.00
 59970.00
 27240.00
 27240.00
386850.00
 24990.00
 20450.00
  2610.00
 11520.00
 59570.00
                        59570.00

                        15470.00
                        16340.00
                        91380.00
                             871

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DRAFT
                       TABLE 179

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A5-V
                  (EDIBLE OIL REFINING)
 ITEMIZED  COST  SUMMARY  FOP KASTEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY...  99.5 PERCENT BOD REDUCTION
 TREATMENT  MGDULESi
                   B.
                   Bi
                   J.
                   K.
                   G.
                   S.
                   Y.
                   B.
                   N.
                   Z.
              .PUMPING STATION
              .CONTROL HOUSE
              .AIR FLOTATION
              .ACTIVATED 8LUDGE
              .SLUDGE THICKENER
              .VACUUM FILTRATION
              .HOLDING TANK
              .PUMPING STATION
              .DUAL MEDIA PRESSURE FILTRA'N
              .ACTIVATED CAPBCN  ADSORPTION
 INVESTMENT  COSTSl
                1.
                2.
                3.
                a.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
                TOTAL
 YEARLY
OPERATING
        1.
        2.
        3.
        a.
COSTS!
  LABOR
  POWER
  CHEMICALS
  MAINTENANCEHSLPPLIES
                TOTAL

 TOTAL  YEARLY  CCSTSt
                1.  YEARLY CPERATING COST
                3.  YEARLY INVESTMENT
                   COST  PFCTVERY
                3.  DEPRECIATION
                TOTAL
                       333270.00
                        59970.00
                        33330.00
                        33330.00
                       U59900.00
24990.00
23520.00
 2610.00
27600,00
78720.00
                                   78720.00

                                   isaoo.oo
                                   20000.00
                                  117120.00
                            872

-------
CO

•^4

CO
        o:
        IL
        O
        o



        D
        U



        _1
                       7o.ro    T3.C8    76.cc     7«.c:    fi.ce     ts.oo    ss.os     cj.cc    ;*.eo    ST.OC    ico.eo
                                                              EFFICIENCY
                                                    FIGURE  269



                             INVESTMENT AND YEARLY COSTS  FnR SUBCATEGORY  As,   ALTERNATIVES 11 THRU v
o
•ya
f>
-n

-------
 DRAFT
               Costs:  Total investment cost:  $249,080
                       Total yearly cost:      $ 92,170

An  itemized breakdown of costs is presented in Table 180.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one operator is required.

               Reduction Benefits:  BOD:  98,5 percent
                                     SS:  97.2 percent
                                    O&G:  97.1 percent

Alternative A 5-VII - This alternative provides in addition to Alter-
native A 5-VI dual media pressure filtration and a pump station to
generate sufficient head for filter operation.

The resulting BOD waste load is 0.035 kg/kkg (0.070 Ib/ton), the
suspended solids load is 0.035 kg/kkg (0.070 Ib/ton), and the oil
and grease load is 0.014 kg/kkg (0.028 Ib/ton).

               Costs:  Total investment cost:  $281,160
                       Total yearly cost:      $101,010

An itemized breakdown of costs is presented in Table 181.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further ass uned that one operator is required.

               Reduction Benefits:  BOD:  99.2 percent
                                     SS:  99.2 percent
                                    O&G:  99.4 percent

Alternative A 5-VIII - This alternative provides in addition to Alter-
native A 5-VII an activated carbon adsorbtion unit before f-inal discharge.

The resulting BOD waste load is 0.021  kg/kkg (0.042 Ib/ton), the
suspended solids load is 0.017 kg/kkg (0.034 Ib/ton), and the oil
and grease load is 0.007 kg/kkg (0.014 Ib/ton).

               Costs:  Total investment cost:  $354,2":0
                       Total yearly cost:      $126,730

An itemized breakdown of costs is presented in Table 182.  It is &ssu~;^d
that land costs $4100 per hectare ($1660 per acre).  It :s further
assumed that one operator is required.

               Reduction Benefits:  BOD:  99.5 percent
                                     SS:  99.6 percent
                                    O&G:  99.7 percent

A cost efficiency curve is  presented in Figure 270.
                                   874

-------
DRAFT
                        TABLE 180

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A5-VI
                   (EDIBLE OIL REFINING)
 ITEMIZED COST SU*MA*Y FOP  *AdT£*ATER TREATMENT
 DESIGN EFFICIENCY... 98.5  PEPCFKT  HOD PfDUCTICK
 TREATMENT
                   P...PUKFING  STATION
                   L...AEKATEO  L

 INVESTMENT CCSTSf


                3.  EKGIMFEP-I-VG            ?O80,GO
                ^ •  CCNTI\G£NC'Y            £ C 0 6 C s 0 0
                5.  PVC LIKffc               4150.00
                T T T A L                     ? i *5 0 6 0 . 0 0

 YEARLY OPERATING CCSTS:

                2.  PC^ER                  ifc.-9C,00
                3.  CHEMICALS                  C00
                <«.  ^AlMTFN.ANCFgSLPPLlES  10370,00
                5.  FVC LUEF                210.00
                TCTAL
 TCTAL  YEARLY CCSTS:
                1. YEARLY CPFeATUG  CCSV  «<)*'.-*.
                t. YEARLY INVESTMENT
                   CTST RPCCvFPY            V - f.-a
                3. DfcPPFClATinr.            -£250.
                TCTAL                      - " V
                              875

-------
DRAFT
                       TABLE 181

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A5-VII
                  (EDIBLE OIL REFINING)
 ITEMIZED  COST SliHMPY FOP fcASTEMTE* TREATMENT  CHAIN
 DESIGN  EFFICIENCY... 99.2 PERCENT PCO REDUCTION
 TREATMENT  MODULES:
                   P.. .PUMPING STATION
                   J...AJR FLOTATION
                   L...AERATtD LAGCON
                   B...PUMPIMG STATION
                   N...DUAL MFOIA PRESSURE  ?ILTRA«.\
INVESTMENT CCSTS:
               1.
               2 .
               3.
               fl.
               5.
CCNSTRUCTIO
L A N 0
ENGINEERING
CONTINGENCY
FVC LINER
YEARLY OPERATING CCSTSi
               1.  LABOR
               2.  POWER
               3.  CHEMICALS
               a.  MA1NTENANCERSLPPLIES
               5.  FVC LINEH
               TCTAL

TOTAL YEARLY CCSTg!
               1. YEARLY OPERATING  COST
               2. YEARLY
                  CCST
               3. DEPRECIATION
               TCTAL
                                         227S10.00
                                            4 0 fi 0 . 0 0
                                           22750,00
                                           2275uaOO
                                           41
                                           
-------
DRAFT
                        TABLE 182

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A5-VIII
                   (EDIBLE OIL REFINING)
   ITEMIZED  CDST  SLMMRY FOP HASTEHTfR  THrAUENT CHAIN
   DESIGN  EFFICIENCY... 99.5 PERCENT  BCD REDUCTION

   TREATMENT  MOOULESt
                      E... PUMPING STATIC^
                      L...AtnATt.r> L AC-CON
                      fi...PU*P!>;P STATION
                      N...n.Al "TCIA  FRE?Su«E FT.TRA'
                      7. ..ACTIVATE..'.  -A^C.'-  60^rK' !C^

   INVESTMENT  COSTSl
                   1.   CCNSTRL'CTICN          PB33.°0.00
                   2.   LAND                    *jrorucr
                   2.   ENGINEERING            2*8ar..0f'
                   ^.   CCMINGENCY,            tffld- .00
                   5.   FVC LTNEP               -150.00
                   TCTAL                     :-;^21C.OO

   YEARLY OPERATING  CCSTS:
                   1.   LABCF                  l
-------
                     35S.O
              (f)
              cr
              8

              u.
              o
                     32?.1
                     269.2
                                                                                                           o
                                                                                                           70

                     22).a
CO
-vl

CO
              z
              W


              h-
>-
v^

>-
              <
              O
              v«*


              .J
              Ci
              <
              u
                     157.4
                     IZ..7
                                                                      9j.ce
                                                                                                         ,-~ Y"
                                                                                                             ico.oo
                                                                EFFICIENCY
                                                      FIGURE  270


                               INVESTMENT AND YEARLY  COSTS FOR  SUBCATEGORY As,  ALTERNATIVES VI  THRU VIII

-------
 DRAFT
Cost and  Reduction Benefits of Alternative Treatment Technologies for
Subcategory A 6 - Edible Oil Processing by Caustic Refining and
Acidulation     	

A model plant representative of Subcategory A 6 was developed in Section
V for the purpose of applying control and treatment alternatives.  In
Section VII, eight alternatives were selected as being applicable engi-
neering alternatives.  These alternatives provide for various levels of
waste reductions for the model plant which refines 454 kkg (500 ton) of
crude edible oil per day.

Alternative A 6-1 - This alternative assumes no treatment and no reduction
in the waste load.  It is estimated that the effluent from a 454 kkg
per day plant is 534 cu m (0.141 MG ) per day.  The BOD waste load is
8.95 kg/kkg (17.90 Ib/ton), the suspended solids load is 4.03 kg/kkg
(8.06 Ib/ton), and the oil and grease load is 3.51 kg/kkg (7.02 Ib/ton).
The model plant developed for Subcategory A 6 is assumed to have separate
discharge of non-contact and process wastewaters, in-plant gravity sep-
aration, skimming, pH control, and an oil recovery system for the skim-
med oil and water wastes.

               Costs:               0
               Reduction Beneftis:  None

Alternative A 6-11 - This alternative provides for the addition of
pressurized air flotation utilizing chemical flocculating agents to
enhance floe formation and floatability of wastes.  Oil, water, and
solid waste skimmings are pumped to an in-plant oil reclamation
system for dewatering, and recovery of inedible oils.

The resulting BOD waste load is 2.68 kg/kkg (5.36 Ib/ton), the suspended
solids load is 1.21  kg/kkg (2.42 Ib/ton), and the oil and grease load
is 1.05 kg/kkg (2.10 Ib/ton).

               Costs:  Total investment cost:  $154,540
                       Total yearly cost:      S 44,140

An itemized breakdown of costs is presented in Table 183.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  70 percent
                                     SS:  70 percent
                                    O&G:  70 percent

Alternative A 6-111  - This alternative provides for ~/e   -.  ••  of
activated sludge, secondary clarification, sludcs re•• v•_'> ~ r.  pjnr.:'
a sludge thickening  tank, vacuum filtration, ana c. litrge T/  -, ^ .  .-,.
Sludge is hauled to  a landfill  facility every four dt-0.  The  l..:;.iv  ;:ea
sludge unit also includes a control house and tw  fuT-ti^v  operators.
                                   879

-------
DRAFT
                           TABLE 183

            ITEMIZED COST SUMMARY FOR ALTERNATIVE A6-II
                      (EDIBLE OIL REFINING)
    ITEMIZED COST SlMKARV FOR MSTEMTER  TREM^F.KT CHAIN
    DESIGN EFFICIENCY... 70.0 PERCENT .BCD  PEDUCTICK
                      B...PUPPING  STATION
                      P 1. .Cl.NTPCL  HCL3E
                      J...AIR  FLOTATIO
    TREATMENT MCDULESi
    INVESTMENT CCSTSi
                   1.
                   2.
                   3.
                   TOTAL

    YEARLY OPERATING COSTS;
                   1,   LABGR
                   2.   POF.K
                   3.   CHEMICALS
LAND
                    TCTAL

    TOTAL YEARLY  CCSTS«
                    1.  YEAKLY  CPEPATIKG COST
                    2.  YEARLY
                       CCST
                    3.  D£PRECIATIC\
                    TOTAL
7679C.CO
62390.00
 7660.00
 7660.00
                       24990.00
                        2100.00
                           C.C
                        6220.00
                       33350.00
                       33350.00

                        6160.00
                        4610.00
                                880

-------
 DRAFT


 The resulting BOD waste  load  is  0.13  kg/kkg  (0.27  Ib/ton),  the
 suspended solids  load  is 0.12 kg/kkg  (0.24 Ib/ton), and  the oil and
 grease load is 0.10 kg/kkg  (0.21  Ib/ton),

                Costs:  Total  investment  cost:   $460,940
                       Total  yearly cost:       $105,880

 An itemized breakdown  of costs is  presented  in  Table  184.   It is
 assumed that land costs  $82,040  per hectare  ($33,200  per acre).   It
 is further assumed that  two operators are required.

                Reduction Beneftis:  BOD:  98.5  perce .t
                                      SS:  97.0  percent
                                    O&G:  97.0  percent

 Alternative A 6-IV - This alternative provides  for Vr.~ addition of
 dual  media pressure filtration with pump stations  to  generate sufficient
 head  for the filter operation.

 The resulting BOD waste  load  is  0.067 kg/kkg (0.13 Ib/ton). "che suspended
 solids load is 0.061 kg/kkg (0.12  Ib/ton), and  the oil and  grease load
 is 0.023 kg/kkg (0.046 Ib/ton).

                Costs:  Total  investment cost:   $497,190
                       Total  yearly cost:       $l"i6,050

 An itemized breakdown  of costs is  presented  in  Table  185.   It is
 assumed that land costs  $82,040  per hectare  ($33,200  per acre).   It
 is further assumed that  two operators are required.

                Reduction Benefits:  BOD:  99.3  percent
                                     SS:  98.5  percent
                                    O&G:  99.3  percent

 Alternative A 6-V - This alternative provides for  the addition of activated
 carbon adsorption before final discharge.

 The resulting BOD waste  load  is  0.035 kg/kkg (0.070 Ib/ton), the
 suspended solids  load  is 0.030 kg/kkg (0.060 Ib/ton), and the oil
 and grease load is 0.012 kg/kkg  (0.024 Ib/ton).

                Costs:  Total  investment cost:   $620,340
                       Total  yearly cost:       $148,780

 An itemized breakdown  of costs is  presented  in  Table  186.   It is assumed
 that  land costs $82,040  per hectare ($33,200 per acre).  It is further
 assumed that two  operators  are required.

                Reduction Benefits:  BOD:  99.6  percent
                                     SS:  99.3  percent
                                    O&G:  99.6  percent

A cost efficiency curve is presented in  Figure 271.


                                   881

-------
DRAFT
                       TABLE 184

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A6-III
                  (EDIBLE OIL REFINING)
ITEMIZED  COST  SlfcMRY FOR M3TEMTER TREATMENT CHAIN
DESIGN EFFICIENCY... 98.5 PERCENT  BCD REDUCTION

TREATMENT  MCOL'LESi
                   B...PUMPI.VS  STATION
                   Bl . .CGiN.THC-1.  *CLSE
                   J...AIR FLCTATICN
                   «... ACTIVATED  SLUDGE
                   a.. .SLUG? TUCKENE?
                   S . . . V A C L I • V. FILTRATION
                   Y... HOLD I ^  TANK

INVESTMENT  CCSTS!
                1.   CCVSTRUCTKN          3^21^0. 30
                2.   LAND                   i>23lO.OO
                3.   FN-C-lNff »1NG            ',3220.00'
                ^.   CCN'Tl!vklr'"CY            33^2C,00
                TCTA!.                      ii^:. 9^0.0 •'/

YEARLY OPERATING  CCSTS:
                1.   LAgnfc                  2^990.00
                2.   rC'-.E*                  26:^0.00
                3.   CHfe'HlCALS               3udO.CC
                a .   ^AlNTE^ifCF&SLPPLlES  13040. ': 0
                TCTA._                      675 10. CO

TCTAL YEARLY CCSTS J
                1.  VF.-iRLY CPi-S4T!".G CCST
                   c c: s T a E c c v K p v           - - . ; c n
                3.  DEPSiECIATI:-^            199--.
                TCTAL                      IC^r-r.
                             882

-------
DRAFT
                       TABLE  185

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A6-IV
                  (EDIBLE OIL  REFINING)
         COST SUMMARY FOR
DESIGN EFFICIENCY... 99.3
                             KASTEfcATER TREATMENT CHAIN
                             PERCENT BOO REDUCTION
   TREATMENT  MODULESi
                     B.
                     Bl
                     J.
                     K.
                     0.
                     S.
                     Y.
                     «.
                     N.
                     .PUMPING STATION
                     .CONTROL HCUSE
                     .AIR FLOTATION
                     .ACTIVATED SLUDGE
                     .SLLDGE THICKENER
                     .VACUUM FILTRATION
                     .HOLDING TANK
                     .PUMPING STATION
                     .DUAL MEDIA PRESSURE  PILTRA'N
   INVESTMENT  CCSTSl
                  1.
                  2.
                  3.
                  .4.
                   CONSTRUCTION
                   LANP
                   ENGINEERING
                   CONTINGENCY
                  TCTAL
   YEARLY
       OPERATING
               1.
               2.
               3.
               4.
COSTS:
  LABOR
                      CHEMICALS
                      MAINTENANCE&SUPPLIE8
                  TCTAL

   TCTAL  YEAHLY  CCSTS!
                  1.  YEARLY OPERATING COST
                  2..  YEARLY INVESTMENT
                     COST RECOVERY
                  3n  DEPRECIATION
                  TCTAL
                       362400.00
                        62310.00
                        36240.00
                        36240.00
                       497190.00
24990.00
32330.00
 3480.00
13620.00
74420.00
                                          74420.00

                                          19690.00
                                          21740,00
                                         116050.00
                             883

-------
DRAFT
                         TABLE  186

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A6-V
                    (EDIBLE OIL REFINING)
   ITEMIZED COST SUMMARY FOP
   DESIGN EFFICIENCY... 99.6
                   WASTEMTER  TREATMENT  CHAIN
                   PERCENT  BOD  REDUCTION
             MODULES:
                     B...PUMPING  STATION
                     Bl..CONTROL  HCLSE
                     J...AIB FLOTATION
                     K...ACTIVATED  SLUDGE
                     Q...SLLDGE THICKENER
                     S...VACUUM FILTRATION
                     V...HOLDING  TANK
                     8...PUMPING  STATION
                     N...DUAL  MEDIA  PRESSURE  FILTRA'N
                     Z...ACTIVATED  CARBON  ADSORPTION
   INVESTMENT COSTSj
                  1.
                  2.
                  3.
                   CONSTRUCTION
                   LAND
                   ENGINEERING
               a,  CONTINGENCY
               TCTAL
YEAPLY
OPERATING
        1.
        26
        3.
        4.
                    CCSTSl
                      LABOR
                      PCWER
                      CHEMICALS
                      MAINTENANCE&SUPPLIES
                  TCTAL

   TOTAL YEARLY COSTS?
                  1. YEARLY OPERATING COST
                  2. YEARLY INVESTMENT
                     COST RECOVERY
                  3. DEPRECIATION
                  TCTAL
                                  065030.00
                                   62310.00
                                   46500.00
                                   a6500.00
                                  630340.00
                                         24990.CO
                                         36660.00
                                          3460.00
                                         30940.00
                                         96070.00
                                  96070.00

                                  24610.00
                                  27900.00
                                  148780.00
                               884

-------
          (rt
«        3
ui        E
                                                      * **  •*•••••**••••«•*•»•••••»»•••»••••_•••»••«»« ••»•»•»»» •••»•»«••
                                                      A*     * 4 * •     . * _ .     .^.	    »___     ^*        f      »»— f
                         ro.ee    7i.ce     76.cc     7«.ec     «.ee     «s.ee    aa.co    «i.ec     ^ioo     17.00    lec.'ej
                                                                  EFFICIENCY





                                                       FIGURE  271



                                            AND YEARLY COSTS FOR  SUBCATEGORY Ae,   ALTERNATIVES II THRU V

-------
DRAFT


Alternative A 6-VI - This alternative provides in addition to Alter-
native A 6-II (i.e., dissolved air flotation) an aerated lagoon system
including a settling pond.

The resulting BOD waste load is 0.13 kg/kkg (0,27 Ib/ton), the suspended
solids load is 0.12 kg/kkg (0.24 Ib/ton), and the oil  and grease load
is 0.10 kg/kkg (0.21 Ib/ton).

               Costs:  Total investment cost:  $374,050
                       Total yearly cost:      $152,640

An itemized breakdown of costs is presented in Table 187.  It is assumed
that land costs $4100 per hectare ($1660 per acre).   It is further
assumed that two operators are required,

               Reduction Benefits:  BOD:  98.5 percent
                                     SS:  97,0 percent
                                    O&G:  97.0 percent

Alternative A 6-VII - This alternative provides in addition to Alter-
native A 6-VI dual media pressure filtration with a  pump station to
generate sufficient head for filter operation.

The resulting BOD waste load is 0.067 kg/kkg (0.13 Ib/ton), the suspended
solids load is 0.061 kg/kkg (0.12 Ib/ton), and the oil and grease load
is 0.023 kg/kkg (0.046 Ib/ton).

               Costs:  Total investment cost:  $410,300
                       Total yearly cost:      $162,800

An itemized breakdown of costs is presented in Table 188.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.2 percent
                                     SS:  98.5 percent
                                    O&G:  99.3 percent

Alternative A 6-VIII - This alternative provides in  addition to Alter-
native A 6-VII an activated carbon adsorption unit prior to final dis-
charge.

The resulting BOD waste load is 0.035 kg/kkg (0.070  Ib/ton), the
suspended solids load is 0.030 kg/kkg (0.060 Ib/ton),  and the oil
and grease load is 0.012 kg/kkg (0.024 Ib/ton).

               Costs:  Total investment cost:  $533,480
                       Total yearly cost:      $195,540

An itemized breakdown of costs is presented in Table 189.  It is
assumed that land costs $4100 per hectare ($1660 per acre)*  It is
further assumed that two operators are required.


                                   886

-------
DRAFT
                        TABLE  187

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A6-VI
                   (EDIBLE OIL REFINING)
  ITEMIZED COST SUMKAKY  FCR  MSTEMTER TREATMENT  CHAIN
  DESIGN  EFFICIENCY... 98.7  PERCENT eCD REDUCTION

  TREATMENT MODULES:
                    B...PUHPJMG STATION
                    J...AIR  FLCTATICN
                    L...AEPATEC. LAGrfN.

  INVESTMENT CCSTSt
                 1.  CCNSTPLT1 Tf>          3f PI 10.00
                 2 .  L A N D                     5'.'' 0 0 . 0 0
                               NG           30 MO. 00
                               r Y           3 *.  • ;,. n n
                 5.  PVC LIKEt*  .              fi-iiO. C i
                 TCTAL                     37a05C.--0

  YEARLY  OPERATING CCSTSt
                 1.  L A « G ft                  i 2 6 Q * r. 0 0
                 2.  vrhFjj                  915'--. •*• c
                 3.  C-E^ICALS                   -.f
                 u.  'VAINTFN'*MCERSIP?LI£.S  i...- ft ;'  * c
                 5.  PVC LINFR                  50' «o
                 TCTAu                     l-'-eS'.OO

  TCTAL  YEARLY CCSTS:
                 1. YEAKLY CPRPATIN" '^S7 ::-'r:?0
                 2. YEARLY INVF
                    CCST RECCV-»
                 3. DEPRFCIATI^N
                 TCTAL
                             887

-------
DRAFT
                       TABLE 188

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A6-VII
                  (EDIBLE OIL REFINING)
 ITEMIZED COST SUMMARY  FOB >' ASTEK ATER  TftSiTfE."
 DESIGN  EFFICIENCY... <>9.3 PERCEM  BCD ^C.CiY

 TREATMENT MODULES:
                    P . . . P i v p I ?•' G s r - - ;: r v
                    J...AIP
                    B...°U*P".vP STATIC-
                    N...'"H.'4L  ."FOIA ??Ei
 INVE8TMEM  CCSTSJ
                 3 .  t N c- T • "- •':. K r- G            : -  • •- . o o
                 «.  Ct:,STI'- L-F-^CY                 .00
                 5.  PVC  LT>F"^                 -•    v
                 TCTAL                      "1C;,   CO

 NEARLY OPERATING CCSTSr
                 1.  LABOR                   lca«i  ,co
                 2.  PT^ER                   <97<520acn
                 3.  CHEMICALS                   0.0
                 4 .  !*AINTEMisCE*£i_PPLn-     > 7 * 4 0 "
                 5.  PVC LUFK                 j«:80.
                 TCTAL                      .26130.00

 fCTAL  YEARLY COSTS!
                 l .  YE 4 PLY cr;- FA •••'!> •"-  • ':£"'
                 3.  Yti^lY I^ Vt ; ' "- • '
                    CCS7  ftFCCVci
                 3.  3E?»FwiATI~\
                 TC -''L,
                            888

-------
DRAFT
                       TABLE 189

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A6-v.II
                  (EDIBLE OIL REFINING)
  ITEMIZED COST 8UMMRY  FQR MSTEMTFP  TPtAT^Ef-T O
  )ESIGN EFFICIENCY...  99. 6 PERCENT  BCD  PEOUC7IC.\

  TREATMENT MCDULESi
                     8...PUMPIMG STATION
                     J...AIR FLPTATTCN
                     L... AERATED LAGCCA
                     9.. .PULING STATIC*
                     N...OUAI KECIA PPF.SSu*E FILTSV'
                     2 . . o A c T i v 4 T E r  r * s r. •-• -N. &••..-• r; i- P )""•- c

  INVESTMENT CfSTS*
                  1.   fCNRTRlJCTlCK       .   -r^eC.C-O
                  2.   LAND                    51 ' 0,  J:
                  3.   ENGINEERING            -• 13' ^. 0
                  4.   CCNT!\GE\-TiT' ?• -   •      •'
                 e B  V?6Ri_Y  '. > VF?f - ,"'
                     CCST  R? f V.= « f
                 3.  CE^KtCIurir;             .,
                                              -
                             389

-------
DRAFT
               Reduction Benefits:  BOD:   99.6 percent
                                     SS:   99.3 percent
                                    O&G:   99.6 percent

A cost efficiency curve is presented in Figure 272.

Cost and Reduction Benefits of Alternative Treatment Technologies for
Subcategory A 7 - Edible Oil Processing by Caustic Refining,
Acidulation, Oil Processing, and Deodorization

A model plant representative of Subcategory A 7 was  developed in
Section V for the purpose of applying control and treatment alter-
natives.  In Section VII, eight alternatives were selected as being
applicable engineering alternatives.  These alternatives provide for
various levels of waste reductions for the model plant which refines
454 kkg (500 ton) of crude edible oil per day.

Alternative A 7-1 - This alternative assumes no treatment and no
reduction in the waste load.  It is estimated that the effluent from
a 454 kkg per day plant is 1147 cu m (0.303 M6 ) per day.  The BOD
waste load is 16.09 kg/kkg (32.18 lb/ton), the suspended solids load
is 7.84 kg/kkg (15.68 Ib/ton), and the oil and grease load is 3.93
kg/kkg (7.86 lb/ton).  The model plant developed for Subcategory A 7
is assumed to have separate discharge of process and non-contact
wastewater, in-plant gravity, separation, skimming,  pH control, and
an oil recovery system for skimmed oil and water wastes.

               Costs:               0
               Reduction Benefits:  None

Alternative A 7-II - This alternative provides for the addition of pres-
surized air flotation utilizing chemical  flocculating agents to en-
hance floe formation and floatability of wastes.  Oil, water, and
solid waste skimmings are pumped to an in-plant oil  reclamation  system
for dewatering, and recovery of inedible oils.

The resulting BOD waste load is 4.85 kg/kkg  (9.70 lb/ton), the suspended
solids load is 2.35 kg/kkg (4.70 Ib/ton), and the oil and grease load -.3
1.13 kg/kkg (2.26 lb/ton).

               Costs:  Total investment cost:  $193,640
                       Total yearly cost:      $ 4S.530

An itemized breakdown of costs is presented in Table 190.  I~: li
assumed that land costs $82,040 per hectare  ($33,2CO per acre).  :t
is further assumed that two operators are required.

               Reduction Benefits:  BOD:   69.8 oercerr.;
                                     SS:   70.0 percent
                                    O&G:   71.3 percent
                                   890

-------
                                                                                                                       o
        IL
        O


        IS
381.9
                                                                                        I.
        z
        t-H


        I-
                  33'. .2
                  260.5
00
10
         a
         U
         *—*


         _l


         H-
         *-i

         f
                   ?''.£>
                                                                         ee.co    «i.ce
                                                             EFFICIENCY
                                                                               
-------
DRAFT
                       TABLE 190

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A7-II
                  (EDIBLE OIL REFINING)
 ITEMIZED COST SUMMARY FDR *A8TE!> ATEP  TREATMENT  CHAIN
 DESIGN EFFICIENCY... 70.0 PERCENT  ROD  REDUCTION
 TREATMENT MCHULESj
 INVESTMENT CCSTSl
                1.
                2.
                3.
                a.
                   Bl..CONTROL HC-LSF
                   B...PUFFING STATION-
                   J...AIR FLOTATION
                   CONSTRICTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
                TOTAL

 YEARLY OPERATING COSTS:
                1.  LABOR
                2.  PO^FR
                3.  CHEMICALS
                «.  *AIN'TFNANCE*SLPPLlES
                TOTAL
TCTAL YEARLY CCSTSJ
               1. YEARLY
               2. YEARLY
                          OPERATING  COST
                          INVESTMENT
                   CCST RECOVERY
                3. DEPRECIATION
                TOTAL
 73300.00
 10C30.00
 10030.00
1936^0.00
                                          2^*590.00
                                              0.0
                                              0. Of
                                          357*0.00
 35760.00

  7750.00
  6020.00
 U9530.00
                            892

-------
 DRAFT
Alternative A 7-III - This alternative provides in addition to Alter-
native A 7-II complete mix activated sludge, secondary clarification,
sludge recirculating pump, a sludge thickening tank, vacuum filtration,
and a sludge holding tank.  Sludge is hauled to a landfill facility
every ten days.  The activated sludge unit also includes a control
house and two full-time operators.

The resulting BOD waste load is 0.25 kg/kkg (0.50 Ib/ton), the suspended
solids load is 0.25 kg/kkg (0.50 Ib/ton), and the oil and grease load
is 0.25 kg/kkg (0.50 Ib/ton).

               Costs:  Total investment cost:  $672,560
                       Total yearly cost:      $151,370

An itemized breakdown of costs is presented in Table 191.  It "is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required

               Reduction Benefits:  BOD:  98.4 percer/c
                                     SS:  96.8 percent
                                    O&G:  93.6 percent

Alternative A 7-IV - This alternative provides ".:. ada-;t-.on ";c Altar-
native A 7-1II dual media pressure filtration with a .jmp sva'dor. to
generate sufficient head for filter operation.

The resulting BOD waste load is 0.13 kg/kkg (0.25 Ib/ton), tr.e  jsperded
solids load is 0.13 kg/kkg (0.25 Ib/ton), and the oil ar.d grea^ load is
0.051 kg/kkg (0.10 Ib/ton).

               Costs:  Total investment cost:  $718,630
                       Total yearly cost:      $164,520

An itemized breakdown of costs is presented in Table IS  .  It -.s
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.2 percert
                                     SS:  98.4 percent
                                    O&G:  98.7 percent

Alternative A 7-V - This alternative provides in ad.:,;icn tc AV:er-
native A 7-IV activated carbon adsorption before final  diichcrge.

The resulting BOD waste load is 0.076 kg/kkg (G.",5 'Vtcr.), t:.e sjscsnded
solids load is 0.063 kg/kkg (0.13 Ib/ton), and tna c'/.  and grease
is 0.025 kg/kkg (0.050 Ib/ton).

               Costs:  Total  investment cost: SI .,00-  c/70
                       Total  yearly cost:     $  2"i6,45'


                                    895

-------
DRAFT
                        TABLE  191      .

         ITEMIZED COST SUMMARY FOR ALTERtfAflVE A7-III
                   (EDIBLE OIL
 ITEMIZED COST SUMMARY  FOR  *ASTE*ATER TKEA.TMiM  CHAIN
 DESIGN EFFICIENCY... 96.4  PERCENT BOD, REDUCTION'

 TREATMENT MODULES»              •.,.     ,'  V    j '•
                   61..CONTROL HOiSE  ;
                   B...PUMPING STATION '
                   J...AI*  FLPT-ATI-C^
                   K... ACTIVATED SLUDGE
                   C...SLLDGE ThJC
                   S... VACUUM FTtTR
                   Y...HOLDING TANK

 INVESTMENT CCSTSJ
                 1.   CCNSTRLCTICN
                 2.   LAND       '        '     73300.00
                 3.   ENGINEERING           '  d99iJO.CO
                 *1.   CCNT I \GF NC Y             a9::.
                ICTAI                     i s.. i •»;. o o
                              894

-------
 DRAFT
                        TABLE 192

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A7-IV
                   (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY FCR  ^APTE'> ATER  T«t"AT!*tNT CHAl*
DESIGN EFFICIENCY... 99.2  PERCENT  «CP REC'jCTICN
TREATMENT MODULES:
                  PI..CONTROL  HCLSE
                  e...PUMPING  STATIC^
                  J...AIR  FLGTATICN
                  K...ACTIVATED  SLIOGE
                  C...SLLCGE  T
          K TANK
B... BUMPING STATION
         *FDIA
INVESTMENT CCSTcj
                1.
                2.
                3.
    CONSTRICTICN
    LAND
    ENGINEERING
a.  CCNTINGENCY
TCTAL
YEARLY OPERATING CCSTSl
               1.  LABOR
               2.  POER
               3.  CHEMICALS
               4.  MAIMTFNAN
               TCTAL
                                           FRTPA'N
                      537770.00
                        73300.00
                        53760.00
                        53780.00
                      718630.00
                        2/1990.00
                        55000.00
                         5530.00
                        179*0.00
                       103500.00
TCTAL YEARLY CCSTS:
               1. YEARLY LPERATING  COST  103500.00
               2. YEARLY I^VPgTi^pKT
                  CCST PFCrv?»Y           2S75C.OC
               3. CEPKECIATIHN            32270.00
               TCTAL
                             895

-------
DRAFT
An itemized breakdown of costs is presented in Tafc 16^193,  It is
assumed that land costs $82,040 per hectare ;($33, 200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99, 5> percent
                                     SS:  99,2 percent .
                                    O&G: : 99,4 percent

A cost efficiency curve is presented in Figure 273.

Alternative A 7-VI - This alternative provides vi,rv addition to Alter-
native A 7-1 1 an aerated lagoon and »s§ttl iiig
                                     *     '
The resulting BOD waste load is 0.25 kg/kkg (0.50 lb/ton), the suspended
solids load is 0.25 kg/kkg (0.50 lb/to*i)t and, the oil and grease load
is 0.25 kg/kkg (0.50 lb/ton).
                                      >i     ' -
               Costs:  Total investment cost:  $607,720
                       Total yearly cost:      $266, 550
                                               *,
An itemized breakdown of costs is presented in Table 194.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  -BOD: '98.4 percent
                                     SS:  96:;8 percent
                                    O&G: ,93.6 percent

Alternative A 7-VII - This alternative provides in addition to Alter-
native A 7-VI dual media pressure filtration and a pump station to
generate sufficient head for filter operation.

The resulting BOD waste load is 0.13 kg/kkg (0.25 lb/ton), the suspended
solids load is 0.13 kg/kkg (0.25 lb/ton), and the oil and grease load
is 0.051 kg/kkg (0.10 lb/ton).

               Costs:  Total investment cost:  $653,790
                       Total yearly cost:      $279,680

An itemized breakdown of costs is presented in Table 195.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.2 percent
                                     SS:  98.4 percent
                                    O&G:  98.7 percent

Alternative A 7-VIII - This alternative provides in addition to Alter-
native A 7-VII activated carbon adsorption before final discharge.

The resulting BOD waste load is 0.076 kg/kkg (0.15 lb/ton), the suspended
solids load is 0.063 kg/kkg (0.13 lb/ton), and the oil and grease load
is 0.025 kg/kkg (0.050 lb/ton).

                                   896

-------
DRAFT
                       TABLE 193

        ITEMIZED COST SUMMARY FOR  ALTERNATIVE A7-V
                  (EDIBLE OIL REFINING)
ITEMIZED COST  SUMMARY  FuP *ASTF*ATER TREATMENT  C
DESIGN EFFICIENCY...  9V. 5 PERCENT BOO

TREATMENT  MODULFSt
                   Bl.. CONTROL hCLSE
                   B...PU*PTMG STATIC*
                   J...AIR FLCMATICN
                   K. . .ACTIVATED SLUDGE
                   G...SLLCGF THICKENER
                   Y... HALTING
                   ?... PUMPING STATION
                   N...DUflL ^FCIA FRESSLRE
                   z. . . ACTIVATEP rafi^CN A :•

           CCSTSI
                1.   CCM8TRUCTICM         77fc39G.OO
                2 .   LAND                   7 3 3 0 0 . 0 C
                3.
                TCTAL                    100«97(..00

YEARLY OPERATING  CCSTS?
                1.   LABOR                  2*9GO.OS
                2.   PC^ER                  635^0. CO
                3.   CHEMICALS              S530.C.1
                4.   MAI*TF.NANC£*SLPPLI£8  /sSelG.:*
                TCTAL                     12«s7C.;5

TCTAL VEARLY CCSTSS
                1.  YEARLY  CPfeSATJ.Vf, ,-r;T -. ^ r 7C, . C 0
                2.  YfASLY  I^•VFST^E^"
                   CCST  PECTvERY          - '.  •;.-;.•
                3.  DEPfrECIATJO           .-^-0. . '
                TCTAL                     ^r-^,,-
                            897

-------
00
       8

       U.
       O


       2S
       8
                eti.e
71*.?
               52T.C
                                             es.ce     ee.cc


                                          EFFICIENCY
                                                                            «s.cs
ICO.09
                                               FIGURE  27?


                        INVESTMENT  AND YEARLY COSTS FOR SUBCATEGORY A?,  ALTERNATIVES II THRU V

-------
DRAFT
                         TABLE 194

           ITEMIZED COST SUMMARY FOR ALTERNATIVE A7-VI
                   (EDIBLE OIL REFINING)
   ITEMIZED COST SL^MARY FOR HASTF*ATE»  TREATMENT  CHAIN
   DESIGN EFFICIENCY... 9P.« PERCFI^T  BOO  REDUCTION'
   TREATMENT
                     P. 1..COMRGL KCUSF
                     B...PUMPIN'G STMICN
                     J...AIR FLOTATION'
                     L...AERATED LA6CPN

   INVESTMENT CCSTS:
                  1. •CCNSTfiuTTICN          *87230.00
                  ?.  LAND                    feTSC.CO
                  3.  E.KS1NEERIN6            ^8720. CO
                  a.  CCNTIN'GENCY            a8720.00
                  5.  FVC LIN'E«              16270.00
                  TOTAL                     607720.00

   YEARLY OPERATING CCSTS:
                  1.  LABOR                  249SO.CO
                  I.  PCnER   •     '         16^250.00
                  3.  CHEMICALS                  O.C
                  it.  PAINTEfcANCE&Sl.PPLItS   Pc^lO.OO
                  5.  PVC L1KFR                7«O.OC
                  TCTAL                     2 1 2 i <5 0 . 0 0

   TCTAL YEARLY CCSTE:
                  1. YEARLY CPERATING  CCST  2l?190.CO
                  2. YEARLY INVF5TKENT -
                     CCST RECOVERY           2^350.CO
                  3. DEPRECIATION            3C05C.CC
                              899

-------
DRAFT
                        TABLE 195

         ITEMIZED COST SUMMARY FOR  ALTERNATIVE A7-VI!
                  (EDIBLE OIL REFINING)
  ITEKIZED  COST SlMMAHY FCR MSTEnATEP  TREATMENT CHAIN
  DESIGN  EFFICIENCY.., 9P.2 PERCENT  800 REDUCTION

  TREATMENT MODULES;
                    Bl.. CONTROL sKL-S*:
                    P... PUMP ING STATIC'-
                    J...AIP PLOTATIC-N
                    L... AERATED LAGCCN-
                    B...PU
 INVESTMENT  COSTS:
                 1.  CONSTRICTION
                 ? .  L A N D                    fr 7 r. •-* « 0 C
                 3.  ENGINEERING            h25fcO«c:

                 5.  PVC L1NFR              J6r7o|c0
                 TCTAI                      653790.00

 YEARLY  OPERATING COSTS:
                 i.  LABOR
                 c.  FOEP
                 3.  CHEMICALS                  0,-
                 41.  ^AIMENAK-CE&5LPPL1?S   • • ,' * -0 4 ' ^

                 TOTAL                     £-: > 5''. . :(?

 TOTAL YEARLY  COSTS:
                 1. YEARLY CPf-RATI^G  CCST  t-c.. tcu r.
                 2. YE4RLY TNv
                    CCST PECCVEPY
                 3. Ot:PRECTATJO^
                 TOTAL
                            900

-------
DRAFT
               Costs:   Total  investment cost:   $940,130
                       Total  yearly cost:       $331,620

An itemized breakdown  of costs is presented in Table  196,   It is
assumed that land costs $4100 per hectare  ($1660 per  acre).   It
is further assumed that two operators  are  required.

               Reduction Benefits:   BOD:  99.5 percent
                                     SS:  99.2 percent
                                    O&G:  99.4 percent

A cost efficiency curve is presented in Figure 274.
Cost and Reduction Benefits of Alternative Treatment Techno Iog4^s-	
for Subcategory A 8 - Edible Oil  Proces.si'nn hy r.aMsHc Rpfjninfy
Oil Processing, and Deodorization

A model plant representative of Subcategory A 8 was developed in Section
V for the purpose of applying control  and treatment alternatives.   In
Section VII, eight alternatives were selected as being applicable  engi-
neering alternatives.  These alternatives provide for various levels
of waste reductions for the model plant which refines 454 kkg (500 ton)
of crude edible oil per day.

Alternative A 8-1 - This alternative assumes no treatment and no reduction
in the waste load.  It is estimated that the effluent from a 454 kkg
per day plant is 927 cu m (0.245 MG )  per day.  The BOD waste load is
11.73 kg/kkg (23.46 lb/ton), the suspended solids load is 6.30 kg/kkg
(12.60 lb/ton), and the oil and grease load is 2.81 kg/kkg (5.62 Ib/ton).
The model plant developed for Subcategory A 8 is assumed to have separate
discharge of process and non-contact wastewaters, in-plant gravity sep-
aration, skimming, pH control, and an oil recovery system for the  skim-
med oil and water wastes.

               Costs:               0
               Reduction Benefits:  None

Alternative A 8-II - This alternative provides pressurized air flotation
utilizing chemical flocculating agents to enhance floe formation and  float-
ability of wastes.  Oil, water, and solid waste skimmings are pumped  to
an in-plant oil reclamation  system for dewatering, and recovery of
inedible oils.

The resulting BOD waste load is 3.53 kg/kkg (7.06 lb/ton), the suspended
solids load is 1.90 kg/kkg (3,8 lb/ton), and the oil and grease load  is
0.86 kg/kkg (1,72 lb/ton).

               Costs:  Total investment cost:  $192,460
                       Total yearly cost:      $ 49,060

An itemized breakdown of costs is presented in Table 197.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.


                                    901

-------
DRAFT
                       TABLE 196

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A7-VIII
                  (EDIBLE OIL REFINING)
   ITEMIZED COST SUMMARY FOR WASTEMTER  TREATMENT  CHAIN'
   DESIGN EFFICIENCY... 99.5 -PF«»CFNT BOD  REDUCTION

   TREATMENT MODULES:
                     Bl..CONTROL
                     B...PUMPING STATION
                     J...AJP FLOTATION
                     L...AERATED LAGOON
                     8...PUMPING STATION
                     N...DUAL M.fCIA PRESSURE  FILTRA'N
                     z...ACTIVATED  cARpr>
   INVESTMENT COSTS:
                  1.
                  2.
                  3.
                  4.
                  5.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
PVC LINER
                  TOTAL

   YEARLY OPERATING COSTS?
76«240.00
  fe760.00
 76420.00
 7fea20.00
 16270.00
940130.00
1. LAROR
2. FO'EK
3. CHfcMICALS
4. M.AINTENANCE&SLPPLIES
5. PVC LINER
TOTAL
24990.00
181070.00
0.0
40540.00
'740.00
247340.00
   TOTAL  YEARLY CCSTSJ
                  1. YEARLY OPERATING COST  247.3^0.00
                  2. YEARLY INVESTMENT
                     COST RECOVERY           376io.oo
                  3. DEPRECIATION
                  TOTAL,
                      46670.00
                     331620.00
                           902

-------
us
o
oo
         fe

         |

         1
         CO
         o
         o
                    411.0 I
                    651.5
                   76?.0
                   581.0
                   SCa.O
                   Jla.S
                   225.0
                   135.5  C
                    «*,0 \T
                                                                                                         toc.ce
                                                              EFFICIENCY
                                                     FIGURE  274


                             INVESTMENT AND YEARLY COSTS  FOR SUBCATEGORY A?   ALTERNATIVES VI  THRU VIII

-------
DRAFT
                      TABLE 197

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A8-II
                  (EDIBLE OIL REFINING)
ITEMIZED  COST  SLMMAI-'Y  FDR MSTE^ATt K TREATMENT CHAIN-
DESIGN EFFICIENCY...  70.0 PERCENT RL'D REDUCTION

TREATMENT  MODULES:
                   B1..COTPCL HCLSF.
                   B...PUTINS STATION
                   J...AIP FLOTATION
                   Y...HOLDING TANK

INVESTMENT  CCSTSs
                1.   CCNSTRLC • UN         1 02070.00
                2.   LAND                   69970.00
                3.   ENGINEERING           10210.00
                4.   CONTINGENCY           10210.00
                TCTAL                     19ef60.00

YEARLY OPERATING COSTS?
                1 .   L APOR                  2**99Q . 00
                2.   PCWER                   3310.00
                3.   CHEMICALS                  0.0
                a,   KAJNTEN'AMCR&SLPPLIES   69
-------
DRAFT
                Reduction Benefits:  BOD:  69.9 percent
                                     SS:  69.8 percent
                                    O&G:  69.4 percent

 Alternative A 8-111 - This alternative provides in addition to
 Alternative A 8-1I complete mix activated sludge, secondary clarif-
 ication,  sludge recirculating pump, a sludge thickening tank, vacuum
 filtration, and a  sludge holding tank,  Sludge is hauled to a landfill
 facility  every  seven days.  The activated sludge unit also includes
 a  control  house and two full-time operators.

 The  resulting BOD  waste load is 0.20 kg/kkg (0.41 Ib/ton), the suspended
 solids  load is  0.20 kg/kkg (0.41 Ib/ton), and the oil and grease load
 is 0.10 kg/kkg  (0.20 Ib/ton).

                Costs:  Total investment cost:  $585,720
                       Total yearly cost:      $128,180

 An itemized breakdown of costs is presented in Table 198.  It is
 assumed that land  costs $82,040 per hectare ($33,200 per acre).  It
 is further assumed that two operators are required.

                Reduction Benefits:  BOD:  98.3 percent
                                     SS:  96.8 percent
                                    O&G:  96.4 percent

 Alternative A 8-IV - This alternative provides in addition to Alter-
 native  A  8-III  dual media pressure filtration with a pump station to
 generate  sufficient head for filter operation.

 The  resulting BOD  waste load is 0.10 kg/kkg (0.20 Ib/ton), the suspended
 solids  load is  0.10 kg/kkg (0.20 Ib/ton), and the oil and grease load
 is 0.041  kg/kkg (0.082 Ib/ton).

                Costs:  Total investment cost:  $628,590
                       Total yearly cost:      $140,210

 An itemized breakdown of costs is presented in Table 199.  It is
 assumed that land  costs $82,040 per hectare ($33,200 per acre).  It
 is further assumed that two operators are required.

                Reduction Benefits:  BOD:  99.1 percent
                                     SS:  98.4 percent
                                    O&G:  98.2 percent

 Alternative A 8-V  - This alternative provides in addition to Alter-
 native  A  8-IV activated carbon adsorption before final discharge.

 The  resulting BOD  waste load is 0.051 kg/kkg (0.10 Ib/ton), the suspended
 solids  load is  0.051 kg/kkg (0.10 Ib/ton), and the oil and grease load
 is 0.020  kg/kkg (0.040 Ib/ton).


                                   905

-------
DRAFT
                       TABLE  198

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A8-III
                  (EDIBLE OIL  REFINING)
  ITEMIZED  COST SIP-MARY FOR feASTEMTER TREATMENT CHAIN
  DESIGN  EFFICIENCY... 9B.1 PERCENT BCD REDUCTION
  TREATMENT  MODULES:
                    81..CONTROL HCLSE
                    B...PUKPING STATION
                    J...AIP FLOTATION
                    Y...HOLCIN6 TANK
                    K... ACTIVATED SLUDGE
                    C...SLUDGE THICKENER
                    S...VACIU* FILTRATION
                    Y. ..HOLi, INr' fA^K
      LAND
  INVESTMENT CC8TSI
                 1.
                 2.
                 3.
                 TCTAL

  YEARLY OPERATING COSTS:
                 1.  LABOR
                 2.  PCKE*
                 3.  CHEMICfLS
                     MAINTENAN'CHSLPPLIES
                 TCTAL
429790.00
 69970.00
 429*0.00
 42980.00
585720.00
                             24990.00
                             3^590.00
                              "100.00
                             15280.00
                             78960.00
  TOTAL  YEARLY
COSTS!
  l. YEARLY OPERATING CCST   78960.oo
  2. YEARLY INVESTMENT
     CCST RECOVERY           23430.00
  3. DEPRECIATION            25790.00
                 TOTAL
                            12B180.00
                            906

-------
 DRAFT
                       TABLE 199

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A8-IV
                   (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY  FOP  WASTEMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... 99.1  PERCENT  BOO REDUCTION
TREATMENT MCDULESi
                  61,.CONTROL  l-CLSF.
                  B...PUMPING  STATION
                  J...AIP  FLOTATION
                  Y...HOLDING  TANK
                  K...ACTIVATED  SLUDGE
                  Q...SLUDGE  THICKENER
                  S...VACUUM  FILTRATION
                  Y...MOLTING  TANK
                  B...PUMPING  STATION'
                  N...DUAL  MEDIA  PRESSURE  FILTRA'N
INVESTMENT CCSTSi
               1.
               2.
               3.
               4.
CONSTRUCTION
LA\n
ENGINEERING
CONTINGENCY
               TOTAL

YEARLY OPERATING COSTS?
               i.  LABOR
               2.  PCwER
               3.  CHfcMICALS
               4.  MA
               TOTAL,
^65520.00
 69970.00
 46550.00
 46550.00
628590.00
                      24990.00
                      42110.00
                       4100.00
                      15940.00
                      87140.00
TCTAU YEARLY CCSTSs
               1. YEARLY
               2. YEARLY
               3.
      OPERATING COST  87140.00

      :CC. vF*v          25140.00
      ATK-N           27930.00
                     140210.00
                             907

-------
 DRAFT
               Costs:  Total investment cost:  $856,530
                       Total yearly cost:      $183,240

An itemized breakdown of costs is presented in Table 200.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.6 percent
                                     SS:  99.2 percent
                                    O&G:  99.3 percent

A cost efficiency curve is presented in Figure 275.

Alternative A 8-VI - This alternative provides in addition to Alter-
native A 8-II (i.e., dissolved air flotation) an aerated lagoon in-
cluding a settling pond.

The resulting BOD waste load is 0.20 kg/kkg (0.41 Ib/ton), the suspended
solids load is 0.20 kg/kkg (0.41  Ib/ton), and the oil and grease load
is 0.10 kg/kkg (0.20 Ib/ton).

               Costs:  Total investment cost:  $488,440
                       Total yearly cost:      $206,100

An itemized breakdown of costs is presented in Table 201.  It is
assumed that land costs $4100 per hectare ($1660 per acre).   It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  98.3 percent
                                     SS:  96.8 percent
                                    O&G:  96.4 percent

Alternative A 8-VII - This alternative provides in addition  to Alter-
native A 8-VI dual media pressure filtration with a pump station to
generate sufficient head for filter operation.

The resulting BOD waste load is 0.10 kg/kkg (0.20 Ib/ton), the suspended
solids load is 0.10 kg/kkg (0.20  Ib/ton), and the oil and grease load
is 0.041 kg/kkg (0.082 Ib/ton).

               Costs:  Total investment cost:  $531,310
                       Total yearly cost:      $218,140

An itemized breakdown of costs is presented in Table 202.  It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that two operators are required.

               Reduction Benefits:  BOD:  99.1 percent
                                     SS:  98.4 percent
                                    O&G:  98.5 percent
                                  908

-------
DRAFT
                       TABLE 200

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A8-V
                  (EDIBLE OIL REFINING)
  ITEMIZED  COST  SUMMARY  FOR  WA8TEKATER TREATMENT CHAIN
  DESIGN  EFFICIENCY... 99.6  PERCENT BOD REDUCTION
 TREATMENT  MODULES!
                    Bl
                    B.
                    J.
                    Y.
                    K.
                    G.
                    S.
                    Y.
                    B.
                    N.
                    z.
   CONTROL HCUSE
   PUMPING STATION
   AIR FLOTATION
   HOLDING TANK
   ACTIVATED SLUDGE
   8LITGE THICKENER
   VACUUM FILTRATION
   HOLOING TANK
   PUMPING STATION
   DUAL MEDIA PRESSURE FILTRA'N
   ACTIVATED C A R B 0 N  A~D 8 OflFffC N
 INVESTMENT CCSTSl
                 1.
                 2.
                 3.
                 a,
CCNSTRvjCTION
LAND
ENGINEERING
CONTINGENCY
                 TCTAL

 YEARLV OPERATING  CCSTSt
                 i.   LABOR
                 2.   PCKER
                 3,   CHEMICALS
                 a.   MA1NTF.NANCE&SUPPL1ES
                 TC1AL
655460.00
 69970.00
 65550.00
 65550.00
856530.00
                      24990,00
                      49140.00
                       4100,00
                      31420.00
                     109650.00
 TCTAL YEARLY CCSTS:
                 1.  YEARLY  OPERATING  COST 109650.00
                 2.  YEARLY  INVESTMENT
                    COST  RECOVERY           34260.oo
                 3.  DEPRFCIATION            39J30.00
                 TOTAL                     1832*10.00
                             909

-------
          «<7,C I
li.

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in
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o
UJ
o
          124.6
          ««.S  !»
                                                                                                  /
                 )    73.to     ?».ee    T4.ee     et.ce    if.ee    M.OO    ti.oe    ««.ee     97,00    iee.ee


                                                    EFFICIENCY  •






                                            FIGURE  27b




                  INVESTMEW ^C  YEARLY COSTS FOR SUBCATEGORY As,  .ALTERNATIVES  II THRU V

-------
DRAFT
                       TABLE  201

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A8-VI
                  (EDIBLE OIL  REFINING)
ITEMIZED COST  SUMMARY  FDP  l^STEMTEP TREATMENT CHAIN
DESIGN EFFICIENCY...  98.3  PERCENT POD REDUCTION
TREATMENT  MODULFSi
INVESTMENT  COSTS)
                1.
                2.
                3.
                «.
                5.
                   PI..CONTROL  HCL8E
                   B...PUMPING  STATION
                   J...A1P  FETATION
                   L...AERATED  LAGCCN
                   CCNSTRUCTICN
                   LAND
                   ENGINEERING
                   CONTINGENCY
                   PVC LIKE*
                         391870.00
                           6000.00
                          39190.00
                          39190.00
                          12190.00
                TCTAL
YEARLY OPFPATING  COST3»
                    LABOR
                    POWER
                                          24S90.00
                                         119100.00
                                              0.0
                                          17750.00
                                            600.00
1
? .
3.
a.   MAINTENANCE8SLPPLIES
5.   PVC LIN'FR
TOTAL
TCTAL YEARLY COSTS;
               1. YEARLY OPERATING  COST  162440. 00
               2. YEARLY INV
                  COST SECCVFRY
               3. DtPPECTATJON
                TOTAL
                                          195^0.00
                                          2«120.00
                                         206100.00
                            911

-------
DRAFT
                       TABLE  202

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A8-VII
                  (EDIBLE OIL  REFINING)
  ITEMIZED  COST  SUMMARY FOR WASTEMTEk TREATMENT CHAIN
  DESIGN  EFFICIENCY...  99.1 PFRCEM BCD DEDUCTION

  TREATMENT MODULES:
                    B1..CONTPCL KCLSE
                    B... PUMPING STATION       '
                    J...AIR FLGTATTCM
                    L... AERATED LAfiCGN
                    R... PUMPING STATION
                    N...PUAL MEDIA PHESSURp FILTRA'N

             CCSTSj                      ""
                 1.   CCN'STRLCTICN         "27600.00
                 2.   LAND                    6000.00
                 3.   EN6INEFRING           a27feO.OO
                 5.   FVC  LINFR             I2l<50,0n
                 TC^AL                     531310.0ft

 YEARLY OPERATING COSTS:
                 1.   LABOR                  2a990.00
                 2«   P»EK                 126620.00
                 3.   CHEMICALS                 0.0
                 a.   PAINT-PNANCESSLPPLIES  1^^10.00
                 5.   PVC  LINER               feOO.OO
                 TC
-------
 DRAFT
Alternative A 8-VIII - This alternative provides in addition to
Alternative A 8-VIT activated carbon adsorption before final discharge.

The resulting BOD waste load is 0,051 kg/kkg (0,10 Ib/ton), the suspended
solids load is 0,051 kg/kkg (0,10 Ib/ton), and the oil and grease load
is 0.020 kg/kkg (0.040 Ib/ton),

               Costs:  Total investment cost:  $759,220
                       Total yearly cost:      $263,200

An itemized breakdown of costs is presented in Table 203.  It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that two operators are required.

               Reduction Benefits:  BOD:  99.6 percent
                                     SS:  99.2 percent
                                    O&G:  99.3 percent

A cost efficiency curve is presented in Figure 276.

Cost and Reduction Benefits of Alternative Treatment  Technologies for
Subcategbry A 9 - Edible Oil Processing  by Caustic Refining, Acidulation,
Oil Processing. Deodorization, and Shortening arid Table Oil Processing


A model plant representative of Subcategory A 9 was developed in
Section V for the purpose of applying control and treatment alter-
natives.  In Section VII, eight alternatives were selected as being
applicable engineering alternatives.   These alternatives provide for
various levels of waste reductions for the model plant which refines
454 kkg (500 ton) of crude edible oil per day.

Alternative A 9-1 - This alternative assumes no treatment and no
reduction in the waste load.  It is estimated that the effluent from
a 454 kkg per day plant is 1320 cu m (0.349 MG ) per day.  The BOD
waste load is 17.12 kkg (34.24 Ib/ton), the suspended solids load is
8.68 kg/kkg (17.36 Ib/ton), and the oil and grease load is 4.35 kg/kkg
(8.70 Ib/ton).

The model plant developed for Subcategory A 9 is assumed to have separate
discharge of process and non-contact wastewaters, in-plant gravity sep-
aration and skimming, pH control, and an oil  recovery system for re-
el aimation of waste oil and grease skimmings.

               Cost:                 0
               Reduction Benefits:  None

Alternative A 9-11 - This alternative provides the addition of pres-
surized air flotation utilizing chemical flocculating agents to enhance
floe formation and floatability of wastes.  Oil, water, and solid waste
skimmings are pumped to an in-plant oil reclamation  system for de-
watering, and recovery of inedible oils.
                                    913

-------
                  T-iC.C
VD
       W)
       U.
       O
O
O
        Q.
        <
        O
               TO. CO     73.10    7».OI     79. Of
                                                                (5.CC    f8.CC     «J.OC    ««.CO    «7,08    J8C.80
                                                             EFFICIENCY
                                                 FIGURE  £76
                         INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY As, ALTERNATIVES  II  AND VI THRU VII

-------
DRAFT
                       TABLE 203

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A8-VIII
                   (EDIBLE OIL REFINING)
   ITEMIZED COST SUMMARY FOR K'ASTEMTER TREATMENT  CHAIN
   DESIGN  EFFICIENCY... 99.6 PERCENT BCD REDUCTION
   TREATMENT HODULESi
                     Bl.. CONTROL HCLSE
                     B... PUMP ING STATION
                     J...AIR FLOTATION
                     L... AERATED LAGOON
                     P.. .PUMPING STATION
                     N'...DUAL MF.CIA PRESSURE  FUTRA'N
                     Z. ..ACTIVATED CARBON  ADSCRPT.TO
INVESTMENT CCSTSi
              .1.
               2.
               3.
               «.
               5.
                   CCNSTRLfTIO
                   LAND
                   ENGlNPERJKiG
                   CCNTINGFA'CY
                   f-VC LINER
YEARLY OPERATING COSTS!
               i.  LABOR
               2.  POER
               3.  CHfeMIC*LS
               5.  PVC LIN.E"
                                            617530.00
                                              6000.00
                                             61750.00
                                             61750.00
                                             12190.00
                                            75
-------
 DRAFT
The resulting BOD waste load is 5.15 kg/kkg (10.30 Ib/ton), the suspended
solids load is 2.62 kg/kkg (5.24 Ib/ton), and the oil and grease load
is 1.31 kg/kkg (2:62 Ib/ton).

               Costs:  Total investment cost:  $201,480
                       Total yearly cost:      $ 50,560

An itemized breakdown of costs is presented in Table 204.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  70.0 percent
                                     SS:  70.0 percent
                                    O&G:  70.0 percent

Alternative A 9-111 - This alternative provides in addition to Alter-
native A 9-11 complete mix activated sludge, secondary clarification,
sludge recirculating pump, a sludge thickening tank, vacuum filtration,
and a sludge holding tank.  Sludge is hauled to a landfill  facility
every nine days.   The activated sludge unit also includes a control
house and two full-time operators.

The resulting BOD waste load is 0.26 kg/kkg (0.52 Ib/ton),  the suspended
solids load is 0.26 kg/kkg (0.52 Ib/ton), and the oil and grease load
is 0.13 kg/kkg (0.26 Ib/ton).

               Costs:  Total investment cost:  $694,590
                       Total yearly cost:      $157,600

An itemized breakdown of costs is presented in Table 205.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  98.5 percent
                                     SS:  97.0 percent
                                    O&G:  97.0 percent

Alternative A 9-IV - This alternative provides with the addition of
Alternative A 9-III dual media pressure filtration with a pump station
to generate sufficient head for filter operation.

The resulting BOD waste load is 0.13 kg/kkg (0.26 Ib/ton),  the suspended
solids load is 0.13 kg/kkg (0.26 Ib/ton), and the oil and grease load
is 0.058 kg/kkg (0.12 Ib/ton).

               Costs:  Total investment cost:   $743,140
                       Total yearly cost:      $171,620

An itemized breakdown of costs is presented in Table 206.  It is assumed
that land costs $82,040 per hectare ($33,200 per acre).   It is further
assumed that two  operators are required.

                                   916

-------
DRAFT
                       TABLE  204

      ITEMIZED COST SUMMARY FOR  ALTERNATIVE A9-II
                 (EDIBLE OIL REFINING)
  ITEMIZED COST SUMMARY FOR  M8TEMTER  TREATMENT CHAIN
  DESIGN EFFICIENCY... 70.0  PERCENT  BCD RtDUCTICN

  TREATMENT MODULES!
                    Bl..CON:TRnL  HCL'SE
                    3...PUMPING  STATION
                    J...AIG  FLOTATION

  INVESTMENT CCSTS:
                 1.  rCNSTRL-ClICK          104050.00
                 2.  LAND                   76630.PO
                 3.  ENGINEERING            ICUOO.OO
                 &.  CONTINGENCY            10400.00
                 TCTAL                     20H80.00

  YEARLY OPERATING CCSTS:
                 1.  LABOR

                 3.  CHEMICALS                  0.0
                 a.  r-AINTENANCERSLPPLlES    7020.00
                 TCTAL                      36260.00

  TOTAL YEARLY CCSTSl
                 1. YEARLY OPERATING COST   36260.00

                    CCS) RFCPVERV            8060.00
                 3. CtPRECIATION             62^0.00
                 TOTAL                       50560.00
                           917

-------
DRAFT
                         TABLE 205

           ITEMIZED COST SUMMARY FOR ALTERNATIVE A9.-III
                     (EDIBLE OIL REFINING)
     ITEMIZED  COST  SUMMARY FOR MSTEWATER TREATMENT CHAIN
     DESIGN  EFFICIENCY...  96.5 PERCENT SOD REDUCTION'
     TREATMENT  MODULE'S!
                       Bl
                       B,
                       J.
                       K.
                       G.
                       S.
                       Y.
                     ,CONTROL HCUSE
                     .PUMPING STATION
                     .AIR FLOTATION'
                     .ACTIVATED  SLUDGE
                     .SLUDGE THICKENER
                     .VACUUM FILTRATION
                     .HOLDING TANK
     INVESTMENT  CCSTSl
                    1.
                    2.
                    3.
                   CCNSTPLCTICN
                   LAND
                        CCMTIK1EMCY
               TCTAl

YEARLY OPERATING COSTSt
               1.  LABOR
               ?.  PCWER
               3.  CHEMICALS
               a.  MAINTENANCE18UPPLIES
               TCTAl;

TCTAL Y&ARLY CCSTSl
               i. YEARLY CPERATING  COST
               2. YEARLY INVESTMENT
                  CCST Wl-COVERY
               3. DEPRECIATION
               TrTAL
51^960,00
 76630.00
 51500.00
 51500.00
694590.00
                                              24990.00
                                              50340.00
                                               5830,00
                                              17760.00
                                              99920.00
                                              98920.00

                                              27780.00
                                              30900.00
                                             157600.00
                              918

-------
DRAFT
                        TABLE  206

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A9-IV
                  (EDIBLE OIL REFINING)
 ITEMIZED COST SUMMARY FOR  i«ASTEkATER  TREATMENT CHAIN
 DESIGN EFFICIENCY... 99.P  PFRCFM  BCD REDUCTION
 TREATMENT MODULESt
R1..CDMPCL HCLSF
P. ..PUMPING STATIC*
J...AIR FLCTATICK'
K... ACTIVATES SLUDGE
C... SLUDGE THICKENER
S... VACUUM FILTRATION
Y...HOLCI^ TANK
B... PUMPING STATION
               PRESSURE
                                            FILTRA'N
 INVESTMENT CCSTSl
                1.
 CC^3TRUCTIC^
 LAND
                3.

                TCTAL
 YEARLY OPERATING CCSTSl
                1.  LA6HR
                2.  HGIfER
                3.  CHEMICALS
                a.  VA
                TCTAL
 TGTAL YEARLY CCSTSI
                i. VEARLY OPERATING  CCST
                2. YEARLY INVESTMENT
                   CCST RECCVFRV
                3. DEPRECIATION
                TCTAL
555430.00
 766*0.00
 55540.00
 55540.00
743140.00
                       24990.00
                       59230.00
                        5830.00
                       18510.00
                      108560.00
                      108560.00

                       29730.CO
                       33330.00
                      171620.00
                               919

-------
 DRAFT
                Reduction Benefits:   BOD:   99.2 percent
                                      SS:   98.5 percent
                                     O&G:   98.6 percent

 Alternative A 9-V -  This alternative provides  with  the addition of
 Alternative A 9-IV activated  carbon  adsorption before  final  discharge.

 The resulting BOD waste  load  is  0,073 kg/kkg  (0.15  Ib/ton),  the suspended
 solids  load is 0.073 kg/kkg  (0.15  Ib/ton),  and the  oil  and grease load
 is  0.029 kg/kkg (0.058 Ib/ton),

                Costs:  Total  investment cost:   $1,075,830
                       Total  yearly  cost:       $  229,000

 An  itemized breakdown  of costs is  presented in Table 207.  It is
 assumed that land costs  $82,040  per  hectare ($33,200 per acre).  It
 is  further  assumed that  two operators  are required.

                Reduction Benefits:   BOD:  99.6 percent
                                      SS:  99.2 percent
                                     O&G:  99.3 percent

 A cost  efficiency curve  is presented in Figure 277.

 Alternative A 9-VI - This alternative  provides  in addition to Alter-
 native  A 9-II  (i.e., dissolved air flotation)  an aerated lagoon system
 including a settling pond.

 The  resulting  BOD waste  load  is  0.26 kg/kkg (0.52 Ib/ton), the suspended
 solids  load is  0.26  kg/kkg (0.52 Ib/ton), and  the oil and grease load
 is 0.13  kg/kkg  (0.26 Ib/ton).

                Costs:  Total  investment cost:   $684,150
                       Total yearly cost:      $305,590

 An itemized breakdown of costs is presented in Table 208.   It is assumed
 that land costs $4100 per hectare ($1660 per acre).   It is further
 assumed  that two  operators are required.

                Reduction Benefits:   BOD:   98.5 percent
                                     SS:   97.0 percent
                                    O&G:   97.0 percent

Alternative A 9-VII - This alternative provides with the addition  of
Alternative A 9-VI dual media pressure filtration with  a pump station
 to generate a sufficient head for filter  operation.

The resulting BOD waste load is 0.13 kg/kkg (0.26 Ib/ton),  the suspended
solids load is 0.13 kg/kkg (0.26  Ib/ton),  and  the oil and  grease load
 is  0.058 kg/kkg (0.13 Ib/ton).

                                   920

-------
DRAFT
                       TABLE 207

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A9-V
                  (EDIBLE OIL REFINING)
ITEMIZED COST SLMVARY  FOR  WASTEMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... 99.6  PERCENT  BCD REDUCTION
TREATMENT
                  Bl
                  B.
                  J.
                  K.
                  0.
                  s.
                  Y.
                  6.
                  N.
       CONTROL HCL8E
       PUM.PING STATION
       AIR FLOTATICN
       ACTIVATED SLUDGE
       SLUDGE THICKENER
       VACLUK FILTRATION
       HOLCING TANK
       PUMPING STATION
       DUAL KEDIA PRESSURE
       AC1IVAT6C CAR8O
                             PILTRA'N
INVESTMENT CCSTSI
                u
                2.
                3,
    CONSTRUCTION
    LAND
    ENGINFfcRING
«.  CONTINGENCY.
TCTAL
                           8326*0,00
                             76630.00
                             83270.00
                             83270,00
                           1075830,00
TCTAL
       DPF.RATING CCSTSi
                1.  LABOR                  2a9
-------
MD
ro
ro
           10
           Ct
           d
           o

           u.
           o

           V)
o
o
_1


^
h-l

Q.
                      97J.il
           7»«.2
                      56J.!
                      357.
                      •52.6
                                                                                                                         a
                                                                                                                         73
                            C
                          ?;.so     73.00    7».cc     79.c:    «2,o:     es.ec     ee.co    «j,cc     <«.co    «7.oo   100.00
                                                                     EFFICIENCY
                                                     FIGURE 277




                               INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A9, ALTERNATIVE II THRUUGH V

-------
DRAFT
                         TABLE 208

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A9-VI
                  (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY  FOR  MSTEMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... 98.5  PERCENT  ROD REDUCTION
TREATMENT MODULES}
INVESTMENT CCSTSI
                1.
                2.
                3.
                4.
                5.
                  Bl.,CONTROL  HCLSE
                  P...PIPPING  STATION
                  J...AIR  FLOTATION1
                  I...AERATED  LACCfN
  CCNSTRLCHCN
  L A\D
  ENGINEERING
  CONTINGENCY
  PVC LINER
               TOTAL
YEARLY
OPERATING
        1.
        2.
        3.
        4.
        5.
COSTS:
  LABOR
                   CHEMICALS
                   VAINTENANCERSLPPLIES
                   PVC LTKFP
               TOTAL
5^7730.00
  7830.00
 54770.00
 54770.CO
 19050.00
 24990,
193820,
     C,
00
00
0
                        2^730.00
                          860.00
                       244400.00
TOTAL YEARLY COSTS*
               1. YEARLY OPERATING  COST  244400.00
               2. YEARLY INVESTMENT
                  COST HECCVgfiY
               3. DEPRECIATION
               TCTAL                     305590.00
                        27370.
                        33620.
       00
       00
                             923

-------
DRAFT


               Costs:  Total investment cost:   $732,710
                       Total yearly cost:       $319,590

An itemized breakdown of costs is presented in Table 209,   It is
assumed that land costs $4100 per hectare ($1660 per acre).   It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.2 percent
                                     SS:  98.5 percent
                                    O&G:  98.6 percent

Alternative A 9-VIII - This alternative provides in addition to Alter-
native A 9-VII activated carbon adsorption before final discharge.

The resulting BOD waste load is 0.073 kg/kkg (0.15 Ib/ton),  the suspended
solids load is 0.073 kg/kkg (0.15 Ib/ton), and the oil and grease load
is 0.029 kg/kkg (0.058 Ib/ton).

               Costs:  Total investment cost:   $1,065,380
                       Total yearly cost:       $  376,990

An itemized breakdown of costs is presented in Table 210.   It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that two operators are required.

               Reduction Benefits:  BOD:  99.6 percent
                                     SS:  99.2 percent
                                    O&G:  99.3 percent

A cost efficiency curve is presented in Figure 278.

Cost and Reduction Benefits of Alternative Treatment Technologies for
Subcategory A 10,  Edible Oil Production by Caustic Refining, Oil Processing,
Deodorization, and Shortening and Table Oil  Production
A model plant representative of Subcategory A 10 was developed in
Section V for the purpose of applying control and treatment alternatives.
In Section VII, eight alternatives were selected as being applicable
engineering alternatives.  These alternatives provide for various
levels of waste reductions for the model plant which refines 454 kkg
(500 ton) of crude edible oil per day.

Alternative A 10-1 - This alternative assumes no treatment and no
reduction in the waste load.  It is estimated that the effluent from
a 454 kkg per day plant is 1101 cu m (0.291 MG)  per day.  The BOD
waste load is 12.76 kg/kkg (25.52 Ib/ton), the suspended solids load
is 7.14 kg/kkg (14.28 Ib/ton), and the oil and grease load is 3.23 kg/kkg
(6.46 Ib/ton).

The model plant developed for Subcategory A 10 is assumed to have sep-
arate discharge of process and non-contact wastewaters, in-plant gravity
                                   924

-------
 DRAFT
                        TABLE  209

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A9-VII
                  (EDIBLE OIL REFINING)
ITEMIZED COST SLM^APY  FOR  w*STF> ATE»  TREATMENT
DESIGN EFFICIENCY... 99.2  PERCENT  BCD REDUCTION
TREATMENT MODULES!
                  PI..CONTROL  >-CLSE
                  P...PUMPING  STATION:
                  J...AIR  FLOTATION
                  L...AERATED  LAC-CCN
                  B...PUMPING  STATION
                  N...DUM  MFI516  PRESSURE FILTRA'N
INVESTMENT CCSTSI
                i.
                2.
                3.
                4.
                5.
                   CTNSTRICTTCK
                   LAND
                   FK'GINFFPJNG
                   PVC
               TOTAL

YEARLY OPERATING COSTS:
               3.  LABOR

               3.  CHEMICALS
               5.  PVC LTNEW
               Tf.TAL
TOTAL YEARLY CCSTSJ
               2.  YEARLY
                   CCST
               3.  Ct
               TCTAL
5R8190.00
  7830.00
 58820,00
 58820.00
 19050.00
732710.00
                                          2^990.00
                                         202720.00
                                              0.0
                                          25470.00
                                            860.00
                                    CCS"  254040.00

                                          29310.00
                                          36240.00
                                         319590.00
                           925

-------
DRAFT
                       TABLE 210

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A9-VIH
                 (EDIBLE OIL REFINING)
 ITEMIZED  COST  SUMMARY  FOR  HA8TEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY...  99.6  PERCENT BOO REDUCTION

 TREATMENT MCDULESj
                   81..CONTROL HCISE
                   B... PUPPING STATION
                   J...AIR  FLOTATION
                   L...AERATED LAGCON
                   B...PULPING STATION
                   N...OUAL MEDIA PRESSURE FILTRA'N
                   Z...ACTIVATED CAR8C.M AOSCHPTTGN-

 INVESTMENT CCSTSl
                1.   CONSTRUCTION         865a20.00
                2.   LAND                   7830.00
                3.   ENGINEERING           865^0.00
                a.   CONTINGENCY           86540.00
                5.   PVC  LINER              1^050.00
                TCTAL                    1065380.00

 YEARLY  OPERATING  COSTS:
                1.   LABCP                  24990,00
                2.   PCWER                 2l2a50.00
                3.   CHEMICALS                  0.0
                «.   MAJNTENANCERSLPPLIES  a3l90.00
                5.   PVC  LINER                860.00
                TCTAL                     28U90.00

 TOTAL YEARLY CCSTSI
                1.  YEARLY OPERATING COST 281490,00
                2.  YEARLY  INVESTMENT
                   CCST  RECrvEPV          i»?fe20.00
                i.  DFPKECIATICN           52800.00
                TOTAL                     376990.00
                          926

-------
ro
            tfl
             _
            O

            (ft
 o
-O
            >-

            >-
            u
                          7c.cc    n.eo     7«.oe     7«.:e    ez.s:     tt.eo    te.ce    fi.co     i».eo    97.30   icc.ee
                                                                 EFFICIENCY
                                                    FIGURE 278



                             INVESTMENT AM) YEARLY COSTS FOR  SUBCATEGORY A9. ALT.  II AND VI  THRUUGM VIII

-------
DRAFT



separation and skimming, pH control,  and an oil  recovery system for
reclamation  of waste oil and grease  skimmings.

               Costs:              0
               Reduction Benefits:  None

Alternative A 10-11 - This alternative provides  for the addition of
pressurized air flotation utilizing chemical  flocculating agents to
enhance floe formation and floatablHty of wastes.   Oil, water, and
solid waste skimmings are pumped to an in-plant  oil  reel almation
system for dewaterlng, and recovery of inedible  oils.

The resulting BOD waste load is 3.82  kg/kkg (7.64 Ib/ton), the  suspended
solids load is 2.18 kg/kkg (4,36 Ib/ton), and the oil  and grease load
is 0.95 kg/kkg (1.89 Ib/ton).

               Costs:  Total investment cost:  $191,780
                       Total yearly cost:      $ 49,200

An itemized breakdown of costs is presented in Table 211.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  70.0 percent
                                     SS:  69.5 percent
                                   O&G:  70.0 percent

Alternative A 10-111 - This alternative provides in addition to Alter-
native A 10-11, complete mix activated sludge, secondary clarification,
sludge recirculating pump, a sludge thickening tank, vacuum filtration,
and a sludge holding tank.  Sludge is hauled to  a landfill facility
every six days.  The activated sludge unit also  includes a control
house and two full-time operators.
                                i  t '.A
The resulting BOD waste load is 0.19  kg/kkg (0.39 Ib/ton), the suspended
solids load is 0.22 kg/kkg (0.44 Ib/ton), and the oil  and grease load
is 0.097 kg/kkg (0.19 Ib/ton).

               Costs:  Total investment cost:  $600,850
                       Total yearly cost:      $133,730

An itemized breakdown of costs is presented in Table 212.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits: BOD:  98.5 percent
                                     SS:  96.9 percent
                                    O&G:  97.0 percent

Alternative A 10-IV - This alternative provides  in addition to Alter-
native A 10-11I dual media pressurized filtration with a pump station to
generate sufficient head for filter operation.
                                928

-------
DRAFT
                        TABLE  211

       ITEMIZED COST SUMMARY  FOR ALTERNATIVE AlO-II
                 (EDIBLE OIL REFINING)
    ITEMIZED COST SLM^ABY FOR toASTE^ATER  THEATMENT  CHAIN
    DESIGN EFFICIENCY... 7ft.0 PERCENT BOD  REDUCTION

    TREATMENT MODULES;
                      PI..CONTROL HCLSE
                      B...PUHPINB STATION
                      J...AIP FLOTATION

    INVESTMENT COSTS*
                   1,  CCNSTRljCTTO
                   2.  LAND
                   3.  ENGINEKPiNG
                   TCTAL

    YEARLY  OPERATING CCSTSl
                   2.
                   3.
                   a.  M
                   TTTAL
    TOTAL  YEARLY CCSTSf
                   1. YEARLY CPEPATUG COST
                   2. YEARLY INVESTMENT
                      CCST ^FCCVFPY
                   3. DEPRECIATION
                   TOTAL
 73300.00
  Q670.Cn
  S870.00
191780.00
  3730.00
     0.0
  6690.00
 35610.no
 35610.00

  7670,00
  5920.00
 U9200.00
                            929

-------
DRAFT
                       TABLE 212

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A10-III
                 (EDIBLE OIL REFINING)
    ITEMIZED  CCST  SUMMARY  FOR WASTEMTER TREATMENT CHAIN
    DESIGN  EFFICIENCY...  98.5 PERCENT 30D REDUCTION
    TREATMENT  MCCULESj
    INVESTMENT  CCSTSl
                   1.
                   2.
                   3.
               TCTAL

YEARLY OPERATING CCSTSI
               1.  LABOR
               2.  PCKER
                      B1..CQNTRCL HCl'SE
                      B...PUVPING STATION
                      J...AIR FLOTATION
                      K...ACTIVATED SLUDGE
                      5...SLLDGE THICKENER
                      s...VACUUM FILTRATION
                      Y... HOLDING TA^K
                   CCKSTPL'CTIGM
                   LAND
                   ENGINEERING
                   3.   CHEMICALS
                   fl.   WAIMTENANCE4SIPPLIES
   TCTAL YEARLY
               TCTAL

             CCSTS!
               1. YtARLY CPERATING
               2. YEARLY JWEST^EK
                  CCST RECCVEKY
               3. DEPRECIATION
               TCTAL
"39630.00
 73300.00
                                             43960.00
                                            600850.00
 24990.00
 38380.00
  4340.00
 15610.CO
 83320.00
                                       CCST   83320.00

                                             24030.00
                                             26380.00
                                            133730.00
                          930

-------
DRAFT


The resulting BOD vaste load is 0.097 kg/kkg (0.19 lb/ton), the suspended
solids load is 0.11 kg/kkg (0.22 lb/ton), and the oil and grease load
is 0.048 kg/kkg (0.096 Ib/ton).

               Costs:  Total investment cost:  $646,270
                       Total yearly cost:     $146,640

An itemized breakdown of costs is presented in Table 213.  It is
assumed that land costs $82S040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.2 percent
                                     SS:  98.5 percent
                                    O&G:  98.5 percent

Alternative A 1Q-V - This alternative provides in addition to Alternative
A 10-IV activated carbon adsorption before final discharge.

The resulting BOD waste load is 0.048 kg/kkg (0.096 lb/ton), the suspended
solids load is 0.056 kg/kkg (0.11 Ib/ton), and the oil and grease load
is 0.024 kg/kkg (0.048 lb/ton).

               Costs:  Total investment cost:  $919,530
                       Total yearly cost:      $199,530

An itemized breakdown of costs is presented in Table 214.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.6 percent
                                     SS:  99.2 percent
                                    O&G:  99.2 percent

A cost efficiency curve is presented in Figure 279.

Alternative A 10-VI - This alternative provides in addition to Alter-
native A 10-11 (i.e., dissolved air flotation) an aerated lagoon and
a settling pond.

The resulting BOD waste load is 0.19 kg/kkg (0.39 lb/ton), the suspended
solids load is 0.22 kg/kkg (0.44 Ib/ton), and the oil and grease load
is 0.097 kg/kkg (0.19 lb/ton).

               Costs:  Total investment cost:   $600,480
                       Total yearly cost:      $262,740

An itemized breakdown of costs is presented in Table 215.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.
                                931

-------
 DRAFT
                         TABLE 213

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A10-IV
                  (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY FOH h'ASTEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 99.2 PERCENT BOD  REDUCTION
TREATMENT MODULESi
                  81..CONTROL HCLSE
                  B... PUMPING STATION
                  J...AIS FLOTATICN
                  K...ACTIVATED SLUDGE
                  G...SLLDGE TNICKFNER
                  s...VACUUM FILTRATION
                  Y...HOLDING TANK
                  B...PUMPING STATION
                  N...DUAL MEDIA PRESSURE  FILTRA'N
INVESTMENT CCSTSl
               1.
               2.
               3.
    CCNSTRLCTICN
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
YEARLY OPERATING CCSTSl
               1.  LA60*
               £.  POEK
               3.  CHEMICALS
               H.  MAINTENANCE&SLFPLIES
               TCTAL

TCTAL YEARLY CCSTS:
               1. YEAPLY OPERATING CCST
               2. YEARLY INVESTMENT
                  CCST REC.CVFRY
               3. DEPRECIATION
               TCTAL
477470.00
 73300.00
 47750.00
 47750.00
646270.00
 24990.00
 46500.00
  4340.00
 16310.00
 92140.00
 92)40.00

 25850.00
 2P65C.OO
146640.00
                              932

-------
 DRAFT
                        TABLE  214

        ITEMIZED COST SUMMARY FOR  ALTERNATIVE A10-V
                  (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY FOR MSTF>ATER  TREATMENT CHAIN
DESIGN EFFICIENCY... 99.6 PERCENT 800  REDUCTION
TREATMENT MODULES:
                  B1..CUMTRCL  HOUSE
                  8...PULPING  STATIC**
                  J...AIR FLOTATION
                  K...ACTIVATED  SLUDGE
                  C...SLLDGE THICKENER
                  s...VACUUM FILTRATION
                  Y...HOLDING  TANK
                  B...P';MPIN6  STATION
                  N...r>uAL  MEDIA  PRESSURE  FILTRA'N
                  Z...ACTIVATED  CARBON  4
INVESTMENT CCSTfif
               1.  CONSTRUCTION
               2.  LAND

               4.  CCNTTNGSNCY
               TOTAL

YEAPLY OPERATING CCSTSl
               1.  LAPHM
               £ •  ' L, '• t •
               3.  CHEMICALS
               4.  MAI
               TOTAL

TOTAL YEARLY CCST5:
               1. YEAPLY
               2. YEAPLV  TKVFS'
                  COST HECCvFW
               3. TEPRECTATIPK
               TOTAL
                                         705190.00
                                          73300.00
                                          70520.00
                                          70520.00
                                         919530.00
                                          27U90,00
                                          5^700.00
                                           «3flO.CO
                                          33910.00
                                         120440.CO
                                         120^40.00
                                          3fc7fiO.OO
                                          42310.00
                                         199530.00
                            933

-------
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          Q:
          o
          Q

          b
          w
          §
          <
          U)
          h-

          z
o
o
         Q

         <
         U
         Q.
         <
         U
                                                                   n.cc     *e.cc    «i.oe     ««.cc    97.00    ico.oo
                                                                                                                        a
                                                                                                                        33
                                                                                                                        3=>
                                                   FIGURE 279
                          INVESTMENT AND  YEARLY COSTS FOR SUBCATEGORY Aio,  ALT. I;I  THROUGH  V

-------
DRAFT
                        TABLE  215

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A10-VI
                  (EDIBLE OIL REFINING)
ITEMIZED COST  SLMN-ARY  FOR  KASTEMTFP TREATMENT CHAIN
DESIGN EFFICIENCY...  98.5  PfcRCF.NT ROD REDUCTION

TREATMENT MCDULESi
                   61..n:\TRCl. HCLSF.
                   p...PULPING STATION
                   J...AIB  FLPTATICN
                   L...AERATED
INVESTMENT CCSTSJ
                1.
                2.   LAND                    7000.00
                3.   ENGINEERING           48120.00
                U.   COTlNGENCY           4 8 1 ? 0 . 0 ft
                5.   FVC  LINES       .      16010.00
                TCTAL                     600480.00

YEARLY OPERATING CCSTSJ
                1.   LA8C»                  24990.00
                2.   POFR                 161970.00
                3.   C*"FMirALs                 0.0
                4.   ^•AI^iTE^'A^CF8.Sl.PFLIES  21360.00
                5.   ?VC  L^FR                710.00
                •TCT*u.                     209050.00

TOTAL YEARLY CCSTSJ
                1.  YEARLY  CPERATING CCST 209050.00
                2 .  YEARLY  I N v P; S T I" F \ T
                   CCST  RECCvFHY          2^020,00
                3.  DEPRECIATION           29670.00
                TCTAL                     262740.00
                           935

-------
DRAFT


               Reduction Benefits:  BOD:  98,5 percent
                                     SS:  96.9 percent
                                    O&G:  97.0 percent

Alternative A 1Q-VII - This alternative provides in addition to Alter-
native A 10-VI dual media pressurized filtration with a pump station
to generate a sufficient head for filter operatton.

The  resulting BOD waste load is 0.097 kg/kkg (0.19 Ib/ton), the suspended
solids load is 0.11 kg/kkg (0.22 Ib/ton), and the oil and grease load
is 0.048 kg/kkg (0.096 Ib/ton).

               Costs:  Total investment cost:  $645,910
                       Total yearly cost:      $275,650

An itemized breakdown of costs is presented in Table 216.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.2 percent
                                     SS:  98.5 percent
                                    O&G:  98.5 percent

Alternative A 10-VIII - This alternative provides in addition to Alter-
native A 10-VII activated carbon adsorption before final discharge.

The  resulting BOD waste load is 0.048 kg/kkg (0.096 Ib/ton), the suspended
solids load is 0.056 kg/kkg (0.11 Ib/ton), and the oil and grease load
is 0.024 kg/kkg (0.048 Ib/ton).

               Costs:  Total investment cost:  $919,160
                       Total yearly cost:      $326,050

An itemized breakdown of costs is presented in Table 217.  It is
assumed that land costs $4100 per hectare ($1660 per acrfe).  It is
further assumed that two operators are  required.

               Reduction Benefits:  BOD:  99.6 percent
                                     SS:  99.2 percent
                                    O&G:  99.2 percent

A cost efficiency curve is presented in Figure 280.

 Cost and  Reduction  Benefits of Alternative Treatment Technologies for
 Subcategory A  11,  Edible Oil Processing By Caustic Refining. Acidulation.
 Oil  Processing, and Deodorization. and  this Production of Shortening.'
 TableOils, and Margarine

A model plant  representative of Subcategory A 11 was developed in
Section V  for  the purpose of applying control and treatment alternatives.
 In Section VII, eight alternatives were selected as being  applicable
engineering alternatives.  These  alternatives provide for  various
                                 936

-------
DRAFT
                        TABLE 216

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A10-VII
                 (EDIBLE OIL REFINING)
ITEMIZED COST 8LM*ARY F»R  M5TEKATER  TREATMENT CHAIN
DESIGN EFFICIENCY... 99.2  PERCENT  BOD REDUCTION
TREAT^FNT MODULE!*!
           CCSTSl
                1.
                2.
                3.
                a.
                5.
               TCTAL

YEARLY OPERATING COSTS*
               i.  LABOR
                  P1..CCMRC-L  HCLSE
                  B...PUMPING  STATION
                  J...AIR  FLOTATION
                  L...Afc.Ri*TED  LA6CON
                  B..,Pl'N'PTNS  STATION'
                            MEDIA  PRESSURE ?ILTRA«N
519080.00
  7000.00
 51910.00
 51910,00
 16010.00
645910.00
                                          24990.00
                                         170090.00
                                              0,0
                                          22070.00
                                            710.00
                                         217860.00
                   CCNSTRICTICK
                   LAND
                   EN6INEEPING
                   CCNTIN6ENCY
                   PVC LTNFR
               3.  CHEMICALS
               5.  PVC
               TCTAL
TCTAL YEARLY
             resist
               1.  ''PARLY CDESATIKG  COST  217860.00
               ?..  YMPIY INVESTMENT
                   CCST RFCCVERY           258«0,00
               3.  OF.Pfi?CIATIOK            31950,00
               TTTAi.   .                  275650.00
                           937

-------
DRAFT
                        TABLE 217

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A10-VIII
                 (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY FOR WASTEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 99.6 PERCENT  BOD  SEDUCTION
TREATMENT MODULES;
                  Bl
                  8.
                  J.
                  I.
                  8.
                  N
                  z.
             ..CONTROL
             .0PUMPING
             HCLSE
             STATION
   ..AIR FLOTATION
   ..AERATED LAPCCN
  ..oPUMPING STATION'
  ...DUAL MEDIA PRESSURE  FILTRA'N
      ACTIVATED  CARBLiv  ADSCRPTK-
INVESTMENT COSTSr
               1.
               2.
               3.
               a.
               5.
            CCNSTSUCTICN
            LAND
            ENGINEERING
            CONTINGENCY
            PVC LINER
               TOTAL
YEARLY
OPERATINC-
        1.
        2.
        3.
        a.
        5.
COSTS:
  LABOR
  POER
  CHt^ICALS
  KAINTENAKCEiSLPPLlES
  PVC LINEP
                       7Ufc790.00
                          7000.00
                         7^680.00
                         7^680.00
                         16010.00
       ,00
       ,00
       ,0
       ,00
                                              0
                                          39680
               TOTAL
   710.00
243670.00
TOTAL YEARLY CCST8»
               1. YEARLY OPERATING  COST  2a3670.00
               2. YEARLY INVESTMENT
                  COST RECOVERY           36770.00
               3. DEPRECIATION            45610.00
               TOTAL                     326050.00
                            938

-------
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b

V)
(0

8
          92?.C
          63*.*
          7J15.J
657.8
          S7C.8
                       73.
                                       ?«.cc
                                              e^.o:    ee.ce


                                           EFFICIENCY

-------
DRAFT
 levels of waste reductions for the model plant which refines 454 kkg
 (500 ton) of crude edible oil per day.

 Alternative A 11-I  - This alternative assumes no treatment and no
 reduction in the waste load.  It is estimated that the effluent from
 a 454 kkg per day plant is 1574 cu m  (0.416  MG)  per day.  The BOD
 waste load is 20.57 kg/kkg (41.14 Ib/ton), the suspended solids load
 is 10.98 kg/kkg (21.96 Ib/ton), and the oil and grease load is 9.95 kg/kkg
 (19.90 Ib/ton).

 The model plant developed for Subcategory All is assumed to have sep-
 arate discharge of process and non-contact wastewaters, in-plant gravity
 separation and skimming, pH control, and an oil recovery system for re-
 clamation of waste oil and grease skimmings.

               Cost:                0
               Reduction Benefits:  None

 Alternative A 11-11 - This alternative provides for the addition of
 pressurized air flotation utilizing chemical flocculating agents to
 enhance floe formation and floatability of wastes.  Oil, water, and
 solid waste skimmings are pumped to an in-plant oil reclamation system
 for dewatering, and recovery of inedible oils.

 The resulting BOD waste load is 6.14 kg/kkg (12.28 Ib/ton), the suspended
 solids load is 3.33 kg/kkg ( 6.66 Ib/ton), and the oil and grease load
 is 2.92 kg/kkg (5.84 Ib/ton).

               Costs:  Total investment cost:  $215,730
                       Total yearly cost:      $ 52,410

 An itemized breakdown of costs is presented in Table 218.  It is
 assumed that land costs $82,040 per hectare ($33,200 per acre).  It
 is further assumed that two operators are required.

               Reduction Benefits:  BOD:  70.1 percent
                                     SS:  69.7 percent
                                    O&G:  70.6 percent

 Alternative A 11-III - This alternative provides in addition to Alter-
 native A 11-11 complete mix activated sludge, secondary clarification,
 sludge recirculating pump, a sludge thickening tank, vacuum filtration,
 and a sludge holding tank.  Sludge is hauled to a landfill facility
 every eight days.   The activated sludge unit also includes a control
 house and two full-time operators.

The resulting BOD waste load is 0.31 kg/kkg (0.62 Ib/ton), the suspended
solids load is 0.35 kg/kkg (0.70 Ib/ton), and the oil  and grease load
 is 0.30 kg/kkg (0.60 Ib/ton).
                               940

-------
DRAFT
                       TABLE 218

       ITEMIZED COST SUMMARY FOR ALTERNATIVE All-II
                 (EDIBLE OIL REFINING)
 ITEMIZED  COST  StVMAKY FOR kASTEKATER TREATMENT CHAIN
 DESIGN  EFFICIENCY...  70.0 PERCENT BCD REDUCTION
TREATMENT  MODULES:
 INVESTMENT  CCSTSJ
                1.
                2.
                3.
                0.
                   El..CONTROL MCLSE
                   8...PUMPING STATION
                   J...AIR FLOTATION'
                   CONSTRICTION
                   LANP
                   CCNTINGENCY
                TCTAL

YEARLY  OPERATING  COSTS?
                1.   LABOR
                2.   POER
                3.   CI-EMI
                a.  .MAINTCNANCE&8LPPLIE8
                TCTAL

              CCSTSJ
                1.  YEARLY CPE*ATI\>G CCST
                e.  NcARLY INVESTMENT
                   COST RECCVF.ftY
                3.  DEPRECIATION
                TCTAL
TCTAL -YEARLY
1131*10.00
 79970.00
 11310.00
 11310.00
215730.00
                                          20990.00
                                           4600.00
                                              0.0
                                           7160.00
                                          36990.00
                                          36990.00

                                           8630.00
                                           6790.00
                                          52010.00
                          941

-------
DRAFT

               Costs:   Total  investment cost:   $761,790
                       Total  yearly cost:       $175,830

An Itemized breakdown  of costs is  presented in Table  219.   It  is
assumed that land costs $82,040 per hectare ($33,200  per acre).   It
is further assumed that two operators are  required.

               Reduction Benefits:  BOD:   98.5 percent
                                     SS:   97.2 percent
                                    O&G:   97.0 percent

Alternative A 11-IV  - This alternative provides in  addition to Alter-
native A ll-III dual media pressure filtration with  a pump station
to generate a sufficient head for filter operation.

The resulting BOD waste load is 0.16 kg/kkg (0.31  Ib/ton), the suspended
solids load is 0.17 kg/kkg (0.35 Ib/ton),  and the oil and grease  load
is 0.069 kg/kkg (0.14  Ib/ton).

               Costs:   Total  investment cost:   $813,980
                       Total  yearly cost:       $191,110

An itemized breakdown  of costs is presented in Table 220.   It is
assumed that land costs $82,040 per hectare ($33,200 per acre).   It
is further assumed that two operators are  required.

               Reduction Benefits:  BOD:   99.2 percent
                                     SS:   98.4 percent
                                    O&G:   99.3 percent

Alternative A 11-V -  This alternative provides in addition to Alter-
native A 11-IV activated carbon adsorption before final  discharge.

The resulting BOD waste load is 0.076 kg/kkg (0.15 Ib/ton), the suspended
solids load is 0.087  kg/kkg (0.17 Ib/ton), and the oil and grease load
is 0.035 kg/kkg (0.070 Ib/ton).

               Costs:   Total  investment cost:   $1,214,140
                       Total  yearly cost:       $  256,440

An itemized breakdown  of costs is presented in Table 221.   It is
assumed that land costs $82,040 per hectare ($33,200 per acre).   It
is further assumed that two operators are  required.

               Reduction Benefits:  BOD:   99.6 percent
                                     SS:   99.2 percent
                                    O&G:   99.6 percent

A cost efficiency curve is presented in Figure 281.


                                942

-------
DRAFT
                        TABLE  219

       ITEMIZED COST SUMMARY  FOR ALTERNATIVE All-Ill
                 (EDIBLE OIL REFINING)
  ITEMIZED COST SUHMAPY FOP ^ASTEv-.ATER  TREATMENT  CHAIN
  DESIGN EFFICIENCY... «»8.? PERCENT POD  REDUCTION
            MCCULESi
                    PI..CONTROL NOISE
                    B...PUMPI*'P STATION
                    J...AI* FLOTATION
                    K... ACTIVATED  SLUDGE
                    C...SLLDGE ThICKFNEh
                    S...VACKIK FILTRATION
                    Y... HOLDING TANK
INVESTMENT C03TSI
               1.  CCNSTBlCTICN
               2.  LAND
               3.  ENGINEERING
                 TCTAL

  YEARLY OPERATES CCSTS:
                 1.  LABOR
                 2.  PC<*E«
                 3.  CHEMICALS
                 4.  K!AI
               TOTAL

TCTAL YEARLY CCETSt
               1. YEARLY OPERATING  COST
               2. YEARLY INVESTMENT
                  COST RECrvFSY
               3. DEPRECIATION
               TOTAL
                                           5&8180.00
 56820,00
 56820.00
761790.00
 599^0,00
  6980.00
 19360.00
111270.00
                                           111270000

                                            30470.00
                                            3^090.00
                                           175830.00
                          943

-------
  DRAFT
                           TABLE  220

         ITEMIZED COST SUMMARY FOR ALTERNATIVE All-IV
                   (EDIBLE OIL REFINING)
ITEMIZED COST SLMMA*V FUR  fcASTEMTER  TREATMENT CHAIN.
DESIGN EFFICIENCY... 9
-------
DRAFT
                        TABLE 221

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A11-V
                 (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY  FOP  WASTEKATER  TREATMENT CHAIN
DESIGN EFFICIENCY... 99.6  PERCENT  BOD REDUCTION
TREATMENT MCDULESI
                   Bl
                   o
.CONTROL HOUSE
.PUMPING STATIC^
.AIR FLOTATION
.ACTIVATED SLUDGE
.SLI.DGE THICKENER
.VACUUM FILTRATION
.HOLDING TANK
.PUMPING STATION
.DUAL MEDIA PRESSURE FILTRA«N
.ACTIVATED CARBON"
INVESTMENT  CC8TSI
                1.
                2.
                3.
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
                   945150.00
                    79^70.00
                    94S10.00
                    94510,00
                  1214140.00
YEARLY OPFRATING  COSTS?
                1.   LABOR                  2^990.00
                2.   PC^F.R                  81200.00
                3.   CHEMICALS               6980.00
                4.   ^AINTENANCERSLPPLIES  37990,00
                TCTAL                     151160.00
      YEARLY  COSTS l
                1.  YEARLY  OPERATING COST 151160,00
                2.  YEARLY  INVESTMENT
                   CCST  RECOVERY          48570,00
                3.  DEPRECIATION-           56710.00
                TCTAL                     256440.00
                           945

-------
                     1 2 I'.. C
vo
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cr>
            O
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            b

            co
            8
            u
            O
»2.;o    es.ce     es.oc.   9i.ce     ««.oo    97. oo    100.00
                          ?-:.:;    TJ.CC     t«.e:
                                                                  EFFICIENCY
                                                     FIGURE 281




                           INVESTMENT AND  YEARLY COSTS FOR SUBCATEGORY All,  ALTERfNATIVES U THRUUGH V
                                                                                                                           o
                                                                                                                           73

-------
 DRAFT


Alternative A 111-VI - This alternative provides in addition to Alter-
native A 11-11 (i.e., dissolved air flotation)  an aerated lagoon
system including a settling pond.

The resulting BOD waste load is 0.31  kg/kkg (0.62 Ib/ton), the suspended
solids load is 0.35 kg/kkg (0.70 Ib/ton), and the oil  and grease load
is 0.30 kg/kkg (0.60 Ib/ton).

               Costs:  Total inbestment cost:   $768,500
                       Total yearly cost:      $353,770

An itemized breakdown of costs is  presented In  Table 222.  It is
assumed that land costs $4100 per  hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:   98.5  percent
                                     SS:   97.2  percent
                                    O&G:   97.0  percent

Alternative A 11-VII - This alternative provides in addition to Alter-
native A 11-VI dual media pressure filtration with a pump station to
generate a sufficient head for filter operation.

The resulting BOD waste load is 0.16 kg/kkg (0.31 Ib/ton), the suspended
solids load is 0.17 kg/kkg (0.35 Ib/ton),  and  the oil and grease load
is 0.069 kg/kkg (0.14 Ib/ton).

               Costs:  Total investment cost:   $820,670
                       Total yearly cost:      $369,050

An itemized breakdown of costs is  presented in  Table 223.  It is
assumed that land costs $4100 per  hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:   99.2  percent
                                     SS:   98.4  percent
                                    O&G:   99.3  percent

Alternative A 11-VIII - This alternative provides in addition to Alter-
native A 11-VII activated carbon adsorption prior to final discharge to
navigable waters.

The resulting BOD waste load is 0.076 kg/kkg (0.15 Ib/ton), the suspended
solids load is 0.087 kg/kkg (0.17  Ib/ton), and  the oil and grease load
is 0.035 kg/kkg (0.070 Ib/ton).

               Costs:  Total investment cost:   $1,220,850
                       Total yearly cost:      $  434,380
                                947

-------
  DRAFT
                          TABLE  222

         ITEMIZED COST SUMMARY FOR ALTERNATIVE All-VI
                   (EDIBLE OIL REFINING)
ITEMIZED COST SlMf*ARY FOP  HASTEMTER  TREATMENT .CHAIN
DESIGN EFFICIENCY... 98.5  PERCENT  BOD REDUCTION
TREATMENT MODULES!
                  Bl..CONTROL  HOLSE
                  P...PUKPING  STATION
                  J...AIR  FLOTATION
                  (....AERATED  LAGOON
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
                   PVC
INVESTMENT COSTSt
               1.
               2.
               3.

               s!
               TOTAL

YFARLY OPERATING CCSTSl
               1.  LABOR

               3!  CHEMICALS
               a.  i
               5.  .
               T C T A'.
61U660.00
  6660.00
 6U70.00
 61470.00
 22240.00
768500.00
                                          80990.00
                                         230770.00
                                              0.0
                                          26260.00
                                           1020.00
                                         265040.00
TCTAL YEARLY CCSTSl
               i. YFARLY OPERATING  COST  285040.oo
               2. YEARLY INVESTMENT
                  crsT RECOVERY           30740.00
               3. DEPRECIATION            37990.00
               TOTAL                     353770.00
                             948

-------
 DRAFT
                        TABLE 223

       ITEMIZED COST SUMMARY FOR ALTERNATIVE All-VII
                 (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY FOR WASTE*ATER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 99.2 PERCEM  BOD  REDUCTION
TREATMENT MODULES:
                  El..CONTROL  HCLSE
                  B...PUMPING  STATION
                  J...AIR FLOTATION
                  L.,.AERATED  LAGCCN
                  B...PULPING  STATION
                  N...DUAL  MEDIA  FRE8SLRE  FRTRA'K
INVESTMENT COSTS!
               1.
               2.
               3,
               4.
               5.
      CONSTRUCTION
      LAND
      ENGINEERING
      CONTINGENCY
      PVC LIKE"
               TOTAL.

YEARLY OPERATING CCSTS:
               i.  LABOR
               2.  PCfcER
               3.  CHEMICALS
               a.
               5.
      MAINTENANCER5LPPLIES
      FVC L
658150.00
  8660.00
 65810.00
 65810.00
 222UO.OO
820670.00
 2^990.00
240550.00
     0.0
 29060.00
  1020.00
               TOTAL
TOTAL YEARLY
CCSTS!
  1. YEARLY CPEP«TIK6 CCST 295620.00
  2. YEARLY IKVFSTfENT
     CCST RECOVERY          32830.oo
  3. OEPRFCIATIO11           40600,00
  TOTAL                    369050.00
                          949

-------
DRAFT


An itemized breakdown of costs is presented in Table 224.   It is
assumed that land costs $4100 per hectare ($1660 per acre).   It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.6 percent
                                     SS:  99.2 percent
                                    O&G:  99.6 percent

A cost efficiency curve is presented in Figure 282.

Cost and Reduction Benefits of Alternative Treatment Technologies
for Subcategory A 12, Edible Oil  Processing by Caustic Refining.,
Oil  Processing, and Deodorization, and the Production of-Shortening,
Table Oils,_and Margarine 	.   .._

A model plant  representative of Subcategory A 12 was developed in Section
V for the  purpose of applying control and treatment alternatives.  In
Section VII, eight alternatives were selected as being applicable engi-
neering alternatives.  These alternatives provide for various levels
of waste reductions  for the model plant which refines 454 kkg (500 ton)
of edible  oil  per day.

Alternative A  12-1 - This  alternative assumes no treatment and no re-
duction in the waste load.  It is estimated that the effluent from
a 454 kkg  per  day plant is  1355 cu m  (0.358 MG)  per day.  The BOD
waste load is  16.20  kg/kkg  (32.40 Ib/ton), the suspended solids
load is 9.44 kg/kkg  (18.88  Ib/ton), and  the oil and  grease load is
8.83 kg/kkg  (17.66 Ib/ton).

The model  plant  developed  for Subcategory A 12 is  assumed to have
separate discharge of  process and non-contact wastewaters, in-plant
gravity separation and skimming,  pH control,  and an  oil recovery
system  for reclamation of  waste oil and  grease skimmings.

               Costs:               0
               Reduction Benefits:  None

Alternative  A  12-11  -  This alternative  provides for the addition of
pressurized  air  flotation  utilizing chemical  flocculating agents to
enhance floe formation and floatability of wastes.   Oil, water, and
solid waste  skimmings  are  pumped  to an  in~plant oil  reclamation
system  for dewatering, and recovery of  inedible oils.

The  resulting  BOD waste  load  is  4.84  kg/kkg (9.68  Ib/ton), the suspended
solids  load  is 2.87  kg/kkg (5.74  Ib/ton),  and the  oil  and grease load
 is  2.69 kg/kkg (5.38 Ib/ton).

               Costs:  Total  investment cost:   $202,970
                       Total  yearly cost:       $ 50,800


                               950

-------
  DRAFT
                         TABLE  224

        ITEMIZED COST SUMMARY FOR ALTERNATIVE All-VIII
                   (EDIBLE OIL REFINING)
ITEMIZED COST SIMHARY FOR  I«AS7FMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... 99.6  PERCENT  BOD REDUCTION

TREATMENT MCDULESj
                  81..CONTROL  HCtSE
                  B...PUMPING  STATION
                  J...AIR  FLOTATION
                  L. ..AERATEH  LAGOON
                  P.O.PULPING  STATION
                  N...DUAL  ^EOIA  PRESSURE  F!LT»A'N
                  2... ACTIVATE!."  CASPCK /uES
INVESTMENT COSTS«
               1.  CONSTRUCTION          991630.00
               2.  LAND                    8660,00
               3.  ENGTMF.ERING            99160.00
               4.  CONTINGENCY            99160.00
               5.  PVC LINFR              22240.00
               TOTAL                    1220850,00

YEARLY OPERATING COSTS!
               1.  LABOR   '               2^990.00
               2.  PO^Ef                 252020«00
               3.  CHEMICALS                  0.0
               «.  i^AlNTF.NANCERSLPPLltS  «6910000
               5.  PVC LU-EW               1020000
               TCTAL
TCTAL YEARLY COSTS:
               1. YEARLY OPERATING  CCST
               2. YEARLY IWVEST^EN'T
                  CCST  RECOVERY           a8830.00
               3. DEPRECIATION            60610.00
               TCTAL
                            951

-------
vo
en
ro
         V)

         QL
         b
          o
          *•*



          <


          I—I

          a
                  1221.0
                  1103.
                                                        «2.t:     f5.ee    ee.cs


                                                              EFFICIENCY
«1.C8    <«.00     «T,00    100.CO
                                                FIGURE 282
                       INVESTMEW AND YEARLY COSTS FOR  SUBCATEGORY All. ALTERNATIVES II AND VI THROUGH VIII

-------
 DRAFT

An itemized breakdown of costs is presented in Table 225.   It is
assumed that land costs $82,040 per hectare ($33,200 per acre).   It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  70.1 percent
                                     SS:  69.6 percent
                                    O&G:  69.5 percent

Alternative A 12-1II - This alternative provides in addition to Alter-
native A 12-11 complete mix activated sludge, secondary clarification,
sludge recirculattng pump, a sludge thickening tank, vacuum filtration,
and a sludge holding tank.  Sludge is hauled to a landfill  facility
every five days.  The activated sludge unit also includes  a control
house and two full-time operators.

The resulting BOD waste load is 0.24 kg/kkg (0.48 Ib/ton),  the suspended
solids load is 0.29 kg/kkg (0.57 Ib/ton), and the oil and  grease load
is 0.27 kg/kkg (0.54 Ib/ton)

               Costs:  Total investment cost:  $672,950
                       Total yearly cost:      $152,640

An itemized breakdown of costs is presented in Table 226.   It is
assumed that land costs $82,040 per hectare ($33,200 per acre).

               Reduction Benefits:  BOD:  98.5 percent
                                     SS:  97.0 percent
                                    O&G:  97.0 percent

Alternative A 12-IV - This alternative provides in addition to Alter-
native A 12-111 dual  media pressure filtration with a pump  station to
generate a sufficient head for filter operation.

The resulting BOD waste load is 0.12 kg/kkg (0.24 Ib/ton),  the suspended
solids load is 0.14 kg/kkg (0.29 Ib/ton), and the oil and  grease load
is 0.060 kg/kkg (0.12 Ib/ton).

               Costs:  Total investment cost:  $722,000
                       Total yearly cost:      $166,810

An itemized breakdown of costs is presented in Table 227.   It is
assumed that land costs $82,040 per hectare ($33,200 per acre).   It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.3 percent
                                     SS:  98.5 percent
                                    O&G:  99.3 percent

Alternative A 12-V -  This alternative provides in addition  to Alter-
native A 12-IV activated carbon adsorption before final discharge to
navigable waters.
                                 953

-------
DRAFT
                        TABLE 225

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A12-II
                 (EDIBLE OIL REFINING)
 ITEMIZED COST SUMMARY FOR ktASTEMTER  TREATMENT CHAIN
 DESIGN EFFICIENCY... 70.0 PERCENT  BOO  REDUCTION
 TREATMENT *CDULES|
 INVESTMENT CCSTSl
                1.
                2.
                3.
                u.
                   Bl..CONTROL HCLSE
                   B...PUMPING STATION
                   J...AIR FLOTATION
                   CCNSTRLCTICN
                   LAND
                   ENGINEERING
                   CCNTINGEMCV
               TCTAL

YEARLY OPERATING CCSTS!
               1.  LABOR
               2.  PCKEH
               3.  CHEMICALS
               4.  MINTENAN'CE&SL'FPLIES
               TCTAL

TCTAL YEARLY CCSTSl
               1. YEARLY OPERATING  COST
               2. YEARLY INVESTMENT
                  CCST RECOVERY
               3. DEPRECIATION
               TCTAL
1052SO.OO
 76630.00
 10530.00
 10530.00
202970.00
                                                .00
                                                .00
                                               0.0
                                            7040.00
                                           36360.00
                                           36360.00

                                            8120.00
                                            6320.00
                                           50800.00
                           954

-------
DRAFT
                       TABLE  226

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A12-III
                 (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY FC*  fASTEMTER  TREAT^tNT CHAIN
DESIGN EFFICIENCY... 98.5  PERCENT  POO REDUCTION
TREATMENT MOOULESj
                  Bl..CONTROL  hCLSE
                  B...PUfPI"G  STATION
                  J...AIR  FLOTATION'
                  K...ACTIVATED  SLLDGE
                  &...SLUG*  TUCKFKER
                  S...VACUUM  FILTRATION
                  V...HOLDING  TANK
INVESTMENT CCSTSt
                1.
                2.
                3.
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
YEARLY OPERATING CCSTSt
               1.  LABOR
               e.  PCfcER
               3.  CHEMICALS
               4.  hAINTf MANrF.&SLPPLIES
               TOTAL

TOTAL YEARLY CCSTSJ
               1. YEARLY COATING  COST
               2. YEARLV INVESTMENT
                  COST HECCVERY
               3. DEPRECIATION
               TOTAL
 76630.00
 ^9690.00
 49690.00
672950.00
                           2^990
                           ^6150
       00
       00
  5490.00
 17270.00
 95900.00
 95QOO.OO
1 5 2 6 a 0 . 0 0
                           955

-------
    DRAFT
                           TABLE  227

           ITEMIZED COST SUMMARY FOR ALTERNATIVE A12-IV
                     (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY FOP WA5TEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 99.3 PERCENT BOD  REDUCTION
TREATMENT MGOULESi
                  61
                  B.
                  J.
        .CONTROL
                  C.
                  s.
                  Y
                  e
                  N
                              HCLSE
                              STATION
                     .AlH FLOTATION
                     .ACTIVATED SLUDGE
                     .8LLDGE THICKENER
                     .VACUUM FILTRATION
                   ...HOLDING TANK
                   ...PUMPING STATION
                   ...DUAL MFQIA PRESSURE
                             FILTRA'N
INVESTMENT CCSTSl
               1.
                   CONSTRUCTION
               2.  LAND
               3.  ENGINEERING
               «.  CONTINGENCY
               TOTAL

YEARLY OPERATING COSTS?
               1.  LABOR

               3.  CHEMICALS
               4.  MAINUNANCE&SLPPLIES
               TOTAL
TOTAL YEARLY
COSTS?
  i. YEARLY OPERATING COST
  2. YEARLY INVESTMENT
     COST RECOVERY
  3. DEPRECIATION
  TOTAL
                           537810.00
                             76630.00
                             53780.00
                             53780.00
                           722000.00
                                   00
                                   00
                                   00
                                          57160.
                                           5490.
                                          18020.00
                                         105660.00
                                         105660.00

                                          26660.00
                                          32270.00
                                         166610.00
                               956

-------
DRAFT


The resulting BOD waste load is 0.060 kg/kkg (0.12 Ib/ton), the suspended
soltds load is 0.072 kg/kkg (0.14 Ib/ton), and the oil  and grease load
is 0.03 kg/kkg (0.06 Ib/ton).

               Costs:  Total investment cost:   $1,063,760
                       Total yearly cost:       $  225,270

An itemized breakdown of costs is presented in Table 228.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.6 percent
                                     SS:  99.2 percent
                                    O&G:  99.6 percent

A cost efficiency curve is presented in Figure 283.

Alternative A 12-VI - This alternative provides in addition to Alter-
native A 12-11 (i.e., dissolved air flotation) an aerated lagoon
system including a settling pond.

The resulting BOD waste load is 0.24 kg/kkg (0.48 Ib/ton), the suspended
solids load is 0.29 kg/kkg (0.57 Ib/ton),  and  the oil and grease load
is 0.27 kg/kkg (0.54 Ib/ton).

               Costs:  Total investment cost:   $706,850
                       Total yearly cost:       $319,260

An itemized breakdown of costs is presented in Table 229.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  98.5 percent
                                     SS:  97.0 percent
                                    O&G:  97.0 percent

Alternative A 12-VII - This alternative provides in addition to Alter-
native A 12-VI dual media pressure filtration  and a pump station to
generate sufficient head for filter operation.

The resulting BOD waste load is 0.12 kg/kkg (0.24 Ib/ton), the suspended
solids load is 0.14 kg/kkg (0.29 Ib/ton),  and  the oil and grease load
is 0.060 kg/kkg (0.12 Ib/ton).

               Costs:  Total investment cost:   $755,880
                       Total yearly cost:       $333,450

An itemized breakdown of costs is presented in Table 230.  It is
assumed that land costs $4100 per hectare  ($1660 per acre).  It is
further assumed that two operators are required.
                               957

-------
DRAFT
                        TABLE  228

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A12-V
                 (EDIBLE OIL REFINING)
ITEMIZED COST SUMMAKY FQ°  UiASTE^ATER  TREATMENT CHAIN
DESIGN EFFICIENCY... 99.6  PERCENT  BCD REDUCTION

TREATMENT MODULES!
                  81.. CONTROL  HCLSE
                  B... PUMPING  STATION
                  J...AIR  FLOTATION
                  K... ACTIVATED  SLUDGE
                  Q...SLIDGS  TUCXENER
                  S... VACUUM  FILTRATION
                  Y... HOLD ING  TANK
                  B... PUMPING  STATION
                  N...DU4L  Mfr.jA PRESSURE  FILTRA'N
                  2. .. ACTIVATES  CA.R»C.\- i
INVESTMENT CCSTSt
               1.  CC.N8TRUCTIGK          622610.00
               2.  LAND                   76630. oo
               3.  ENGINEERING            82260.00
               4.  CCNTINGENCY            «2260.00
               TCTAL                    1063760.00
YEARLY OPERATING
               1.  LABCR                  24990.00
               2.  PC!*ER                  67130.00
               3.  CHEMICALS               5UQC.OO
               *.  MAINTENANCE&SLPPLIES   35750.00
               TCTAL                     133360.00

TCTAL YEARLY CCSTSJ
               1. YEARLY CPERATING  COST  133360.00
               2. YEARLY INVESTMENT
                  COST RECOVERY           42550.00
               3. DEPRECIATION            U9360.00
               TCTAL                     2P5270.00
                            958

-------
UD

Ol
         V)
b


1

|

z
io
o
o
         at.
                      .4
                    861.2
                    7S9.8
                    65S.S
                   557.0
                   S5H.2
                    151.a
                        70.00    71.CO     74.00    7«.IO     82.CC     85.CC    68.00     «1.50    SS.CO     97.00   iCO.CO
                                                                EFFICIENCY
                                                                                                                        o
                                                                                                                        •yo
                                                  FIGURE 283
                        INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY Ai2, ALTERNATIVES II  THROUGH V

-------
DRAFT
                        TABLE 229

       ITEMIZED COST SUMMARY  FOR ALTERNATIVE A12-VI
                 (EDIBLE OIL REFINING)
ITEMIZED COST  Sl'MMAHY'FCR  is'ASTE^ATER TREATMENT CHAIN
DESIGN EFFICIENCY...  98.5  PERCENT. BCD REDUCTION'
TREATMENT MODULESi
INVESTMENT  CCSTSI
                i.
                2.
                3.
                4.
                5.
                   01..CONTROL  hCLSF
                   B...PL^Pl!vG  STATION
                   J...AIR  FLOTATICN
                   L...AERATcD  LAGOON
'CONSTRUCTION'
 LAND
 ENGINEERING
 CONTINGENCY
 PVC  L
YEARLY OPERATING CCSTSl
                1.  LABOR
                2.
                3.
                4.
                5.  PVC LINER
                TCTAL
                                         565780.00
                                           8000.00
                                          56580.00
                                          56580.00
                                          1
-------
DARFT
                        TABLE  230

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A12-VII
                  (EDIBLE OIL REFINING)
ITEMIZED COST SUMMARY FQR  HASTEMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... 99.3  PERCENT  POO REDUCTION
TREATMENT MODULES:
                  til..CONTROL  HCLS'E
                  6...PIMPING  STATION
                  J...AIR  FLOTATION
                  L...AERATED  LAGCCN
                  B...PUMPING  STATION
                  N...OUAL  MEDIA  PRESSURE  FILTRA'N
INVESTMENT
                1.   CONSTRUCTION
                2.   LAND


                5.   PVC L.TNE*
                TOTAL

YEARLY OPERATING CCSTSj
                1.   LABOR

                3.   CHEMICALS
TOTAL YEARLY
               5.  PVC LINER
               TCTAL

             COSTS;
               1. YEARLY LPERATING  CCST
               Z. YEARLY I*VEST.VE\T
                  CCST RECCVF«Y
               3.
               TCTAL
                                         606650.00
                                           6000.00
                                          60660.00
                                          60660.00
                                          19
-------
DRAFT

               Reduction Benefits:  BOD:  99.3 percent
                                     SS:  98.5 percent
                                    O&G:  99.3 percent

Alternative A 12-VIII - This alternative provides in addition to Alter-
native A 12-VII activated carbon adsorption before final discharge to
navigable waters.

The resulting BOD waste load is 0.060 kg/kkg (0.12 Ib/ton), the suspended
solids load is 0.072 kg/kkg (0.14 Ib/ton), and the oil and grease load
is 0.030 kg/kkg (0.060 Ib/ton).

               Costs:  Total investment cost:  $1,097,630
                       Total yearly cost:      $  391,900

An itemized breakdown of costs is presented in Table 231.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.6 percent
                                     SS:  99.2 percent
                                    O&G:  99.6 percent

A cost efficiency curve is presented in Figure 284.

Cost and Reduction Benefits of Alternative Treatment Technologies	
f or' yuRa tegory~A 13. Plastlclz"ing~and' Packagih~g""oT Margarine

A model plant representative of Subcategory A 13 was developed in Section
V for the purpose of applying control and treatment alternatives.  In
Section VII, six alternatives were selected as being applicable engi-
neering alternatives.  These alternatives provide for various levels
of waste reductions for the model plant which processes 227 kkg (250 ton)
of margarine per day.

Alternative A 13-1  - This alternative assumes no treatment and no
reduction in the waste load.  It is estimated that the effluent from
a 227 kkg per day plant is 340 cu m (0.09 MG ) per day.  The BOD waste
load is 3.92 kg/kkg (7.84 Ib/ton), the suspended solids load is 2.72 kg/kkg
(5.44 Ib/ton), and the oil and grease load is 5.81 kg/kkg (11.62 Ib/ton).

The model plant developed for Subcategory A 13 is assumed to have sep-
arate discharge of process and non-contact wastewaters, in-pi ant gravity
separation and skimming, pH control, and an oil  recovery system for re-
clamation of waste oil and grease skimmings.

               Cost:                0
               Reduction Benefits:  None

Alternative A 13-11 - This alternative provides  for the addition of
pressurized air flotation utilizing chemical flocc./sating agents to
enhance floe formation and floatafaility of wastes.  Chi, water, and solid
                                 962

-------
DARFT
                       TABLE 231

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A12-VIII
                 (EDIBLE OIL REFINING)
  ITEMIZFD COST SUMMARY FOR WA3TEMTER TREATMENT CHAIN
  DESIGN EFFICIENCY... 99.6 PERCENT BCD REDUCTION
  TREATMENT MODULES?
                    91
                    8.
                    J.
                    L.
                    8.
                    N.
                    Z.
        .CONTROL HOUSE
        .PUMPING STATION
        ,AJR FLOTATION
        .AERATED LAGOON
        .PULPING STATION
        .DUAL MEDIA PRESSURE FILTRA'N
        .ACTIVATED CARBON ADSORPTION
  INVESTMENT COSTS!
                 1.
                 2..
                 3.
                 <40
                 5,
      CONSTRUCTION
      LAND
      ENGINEERING
      CONTINGENCY
      PVC LINER
                 TOTAL
 891440.00
   6000.00
  89140.00
  89i4o.oo
  19910.00
1097630.00
  DEARLY OPERATING CCSTSi
                 1.  LABOR                 24990.00
                 2.  PCKF.R                223770.00
                 3,  CHEMICALS            '      0.0
                 «.  KAINTENANCE&SLPPLIES  43870.00
                 So  PVC LINER                880.00
                 7CTAL                    293510.00
  TCTAL YEARLY
CCSTSI
  1. YEARLY OPERATING COST 293510.00
  20 YEARLY INVESTMENT
     CCST PFCOVERY          43910,00
  38 DEPRECIATION           54480.00
  TCTAL                    391900.00
                           963

-------
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   «.ee     ei.ee



EFFICIENCY
                                                                     «t.ce    ««.eo
                                                                                             jeo.oo
                                      FIGURE 284




               INVESTMEm" AND YEARLY COST FOR SUBCATEGORY Al2, ALTERNATIVES  II  AND VI THROUGH VIJI
                                              vm

-------
DRAFT


waste skimmings are pumped to an in-plant oil reclamation system
for dewatering, and recovery of inedible oils.

The resulting BOD waste load is 1.17 kg/kkg (2.34 Ib/ton), the suspended
solids load is 0.81 kg/kkg (1.62 Ib/ton), and the oil and grease load
is 1.75 kg/kkg (3.50 Ib/ton).

               Costs:  Total investment cost:  $146,540
                       Total yearly cost:      $ 42,720

An itemized breakdown of costs is presented in Table 232.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).   It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  70.1  percent
                                     SS:  70.1  percent
                                    O&G:  70.0 percent

Alternative A 13-111 - This alternative provides in addition to  Alter-
native A 13-11 complete mix activated sludge, secondary clarification,
sludge recirculating pump, a sludge thickening tank, vacuum filtration,
and a sludge holding tank.  Sludge is hauled to a landfill facility
every 20 days.  The activated sludge unit also includes a control  house
and two full-time operators.

The resulting BOD waste load is 0.060 kg/kkg (0.12 Ib/ton), the  suspended
solids load is 0.075 kg/kkg (0.15 Ib/ton), and the oil and grease  load
is 0.075 kg/kkg (0.15 Ib/ton).

               Costs:  Total investment cost:  $295,200
                       Total yearly cost:      $ 70,200

An itemized breakdown of costs is presented in Table 233.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).   It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  98.5 percent
                                     SS:  97.2 percent
                                    O&G:  98.7 percent

Alternative A 13-IV - This alternative provides in addition to Alter-
native A 13-1II dual media pressure filtration and a pump station  to
generate sufficient head for filter operation.

The resulting BOD waste load is 0.03 kg/kkg (0.06 Ib/ton), the suspended
solids load is 0.037 kg/kkg (0.074 Ib/ton), and the oil  and grease load
is 0.037 kg/kkg (0.074 Ib/ton).

               Costs:  Total investment cost:  $327,930
                       Total yearly cost:      $ 79,280
                               965

-------
DRAFT
                        TABLE 232

      ITEMIZED COST SUMMARY FOR ALTERNATIVE A13-II
                 (MARGARINE PROCESSING)
ITEMIZED COST  St«MRV  FUR *ASTEMTEP TREATMENT  CHAIN
DESIGN EFFICIENCY,..  70.0 PERCENT POD REDUCTION
TREATMENT  MODULES:
                   BI..COK-TPCL HCLSF
                   e...PUMPING STATION
                   J...AIW FLOTATION
INVF.STMEM  CCSTSl
                1.
                2.
                3.
    CONSTRUCTION
    LAND
    FK'GIN'EEPIKG
«.  CONTINGENCY
TOTAL
YEARLY OPERATING  CCSTSs
                1.   LABOR

                3*.   CHEMICALS
                4.   VA
TOTAL YEARLY
                TOTAL

              COSTS:
                1.  YFARLY OPERATING
                2.  VEAPLY IN'VF
                   CCST  PECCVERY
                3.  DEPRECIATION
                TOTAL
                                          72150.00
                                          59970.
                                           7210.
00
00
                                           7210.00
                                         U6540.00
                                               '.00
                                           1570.00
                                              0.0
                                           5970.00
                                          32530.CO
                                    CCST  32530.00

                                           58*0.00
                                           "330.00
                           966

-------
DRAFT
                        TABLE 233

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A13-III
                  (MARGARINE PROCESSING)
 ITEMIZED  CC3T  SIMMARY  POP "ASTFMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY...  98.5 PERCENT BOO REDUCTION
 TREATMENT  MCDULEfi
                    61 ..CONTROL HCLSE
                    8. ..PUVKlMG STATION
                    J...AIR PLOTATICN
                    K... ACTIVATED SLUOGe.
                    C...SLLCGE THICKENER
                    Y...HCLrUr- TANK
CCNSTRLCTICK
LAND
  INVESTMENT  CCSTSl
                 1.
                 2.
                 3.
                 TCTiL

 YEARLY  OPERATING  CCSTS:
                 1.   LA BO*
                 £.   I-C^EK
                 3.   CHEMICALS
                 4.   PAINTENAMCE&SLPPLIES
                 TCTAL

 TOTAL YEARLY  CCSTS!
                 i.  YEARLY CPEPATING CCST
                 2.  YEARLY INVESTMENT
                    CC.S1  RECCVERY
                 3.  C
                 TCTAL
196030.00
 59970.00
 19600.00
 19600.00
£95200.00
                      2«990.00
                       9690.00
                       2080.00
                       9870.00
                      46630.OC
                      4*6630.00

                      11 fl'l 0.00
                      11760.00
                      70200.00
                           967

-------
 DRAFT
An itemized breakdown of costs is presented in Table 234,  U is assumed
that land costs $82,040 per hectare ($33,200 per acre).  It is further
assumed that two operators are required.

               Reduction Benefits:  BOD:  99.2 percent
                                     SS:  98.6 percent
                                    O&G:  99.4 percent

A cost efficiency curve is presented in Figure 285.

Alternative A 13-V - This alternative provides in addition to Alter-
native A 13-11 (pressurized air flotation) an aerated lagoon system
with a settling pond.

The resulting BOD waste load is 0.060 kg/kkg (0.12 Ib/ton), the
suspended solids load is 0.075 kg/kkg (0.15 Ib/ton), and the oil and
grease load is 0.075 kg/kkg (0.15 Ib/ton).

               Costs:  Total investment cost:  $277,070
                       Total yearly cost:      $110,220

An itemized breakdown of costs is presented in Table 235.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one operator is required.

               Reduction Benefits:  BOD:  98.5 percent
                                     SS:  97.2 percent
                                    O&G:  98.7 percent

Alternative A 13-VI  - This alternative provides in addition to Alter-
native A 13-V dual media pressure filtration and a pump station to
generate sufficient head for filter operation.

The resulting BOD waste load is 0.030 kg/kkg (0.060 Ib/ton), the suspended
solids load is 0.037 kg/kkg (0.074 Ib/ton), and the oil and grease load
is 0.037 kg/kkg (0.074 Ib/ton).

               Costs:  Total investment cost:  $309,790
                       Total yearly cost:      $119,300

An itemized breakdown of costs is presented in Table 236.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one operator is required.

               Reduction Benefits:  BOD:  99.2 percent
                                     SS:  98.6 percent
                                    O&G:  99.4 percent

A cost efficiency curve is presented in Figure 286.


                               968

-------
  DRAFT
                             TABLE  234

            ITEMIZED COST SUMMARY FOR ALTERNATIVE A 13-IV
                       (MARGARINE PROCESSING)
ITEMIZED COST SUMMARY FOP UdSTFUTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 99.? PERCENT BCD  REDUCTION
(BIBJKOSY)BN
TREATMENT MODULES;
INVESTMENT c
                  PI..CGMWQL KLSE
                  B...PUMPING STATICM
                  J...AJR FLOTATION
                  K. ..ACTIVATED  SLUDGE
                  G...SLLDGE THICKENER
                  S...VACUUM FILTRATION
                  Y...HOLDING TANK
                  H...PUMPING STATION'
                  N...rUAL MFCIA PRESSURE  FILTRA'N
               1.  CCNSTRtCTl'CN          223300.00
               P.  LAND                   59970.00
               3.  ENGINEERING            22,330.00
               «.  CONTINGENCY            22330.00
               TOTAL                     327930.00
YEARLY
               J.  LAPOR                  24990.00
               2.  PCivER                  15110.00
               3.  ChEMCALS               2080.00
               a.  ^AINTENANCE&SUPPLIES   10580.00
               TC1*L                      52760.00

TCTAU YEARLY CC5TSJ
               1. YEARLY OPERATING  COST   52760.00
               2. YM.RLY INVESTMENT
                  CCST RECOVERY           13120.00
               3. DEPRECIATION            13400.00
               TCTAL                      79230.00
                             969

-------
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                121.5
                 ei.o
                 8.0
                    90.09    ?s.eo     6c.oo     «5.oc    To.ee     75.00    eo.eo    cj.ee    »o.co     «j.oo   iee.ee


                                                       EFFICIENCY


                                                       FIGURE 285



                          INVESTMENT  AND YEARLY COSTS FOR SUBCATEGORY A13,  ALTERNATIVES II THffSJ IV.
                                                                                                                            O
                                                                                                                            yo

-------
DARFT
                       TABLE  235

       ITEMIZED COST SUMMARY  FOR ALTERNATIVE AT3- V
                  (MARGARINE PROCESSING)
  ITEMIZED COST SUGARY FOR "USFEMTER  TREATMENT
  DESIGN EFFICIENCY... 98.5 PERCENT  BCD  REDUCTION'
  TREATMENT MODULES!
  INVESTMENT CCSTSt
                 1.
                 2.
                 3.
                 4.
                 5.
                    Bl..CGMRGL  HCLSE
                    B...PUMPIM';  STATION
                    J...AIB PLOTATICN
                    L...AP.BAT£r  LAGCC'V
                   CCNSTROCTI'CN
                   LAND
                   PVC  LTNPR
               TCTAL

YEARLY OPERATING COSTS:
               1.  LABC"

               3.  CHEMICALS
               4.  MAlNTF.NANfEftSLPPLlES
                   PVC  LU'EP
  TOTAL YEARLY
  5.
  TCTAL

COSTS!
  1. YEARLY OPERATING COST
  2. YEARLY INVESTMENT
     CCST RECOVERY
  3. DEPRECIATION
  TCTAL
                            P23910.CO
                              4000.00
                             22390.00
                             22390.00
                                           277070.00
                                            24990.00
                                            50100.00
                                                0.0
                                            10170.00
                                              230.00
                                            65U90.00
                                            85490.00

                                            noeo.cn
                                            1 3650.00
                                           110220.00
                           971

-------
DRAFT
                       TABLE 236

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A13-VI
                  (MARGARINE PROCESSING)
 ITEMIZED COST  SUMMARY  FOR  fcASTEMTFR TREATMENT CHAIN
 DESIGN EFFICIENCY... 99.2  PERCENT  BOO REDUCTION

 TREATMENT MODULESl
                    Bl..CONTROL  MCLSE
                    B...PULPING  STATION
                    J...A1R  FLOTATION
                    L...AERATED  LAGCON
                    B...PULPING  STATION
                    N...DUAL  *EDIA  PRESSURE FILTRA'N

 INVESTMENT CCSTSI
                 1.   CONSTRUCTION          251170.00
                 2.   LAND                    4000.00
                 3.   ENGINEERING            25120.00
                 4.   CONTINGENCY            25120.00
                 5.   PVC LINER               "380.00
                 TOTAL                     309790.00
 YEARLY OPERATING C
                1.  LABOR                  2^990.00
                2.  FCi«ER                  55520.00
                3.  CHEMICALS                  0.0
                4.  f AH'TENANCEaSLPPLIES   10880.00
                5.  PVC LINER                230.00
                TOTAL                      91620.00

 TOTAL YEARLY CCSTSt
                1. YEARLY CPEPATING  COST   91620.00
                2. YEARLY INv/ESTHENT
                   COST RECCv/ESY           12390.00
                3. DEPRECIATJCK            15290.00
                TOTAL                     119300.CO
                         972

-------
       b

       $
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8
u
                .0
             3t*.S
        o:
        5    JZ'.O
              M.c
              aO.9
           I
        0.0 I)

          ?c!c9
                                   eo.ee    43.ee     re.ee    TS.CO     te.co    it.oe     le.eo    «J.oo    too.oo

                                                     EFFICIENCY

                                                     FIGURE  286
                           INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A  13,  ALTERNATIVES II,  V,  AND VI

-------
DRAFT


Cost and Reduction Benefits of Alternative Treat-ire.nt Technologies
for Subcategory A 14, Plasticizing and Packaging Shortening and Table  Oils

A model plant representative of Subcategory A 14 was developed in  Section
V for the purpose of applying control  and treatment alternatives.   In
Section VII, seven alternatives were selected as being applicable  engi-
neering alternatives.  These alternatives provide for various levels
of waste reductions for the model plant which processes 227 kkg (250 ton)
of finished edible oil products per day.

Alternative A 14-1 - This alternative assumes no treatment and no
reduction in the waste load.  It is estimated that the effluent
from a 227 kkg per day plant is 87 cu m (0.023 MG)   per day.  The
BOD waste load is 0.56 kg/kkg (T.12 Ib/ton), the suspended solids
load is 0.42 kg/kkg (0.84 Ib/ton), and the oil and grease load is  0.21
kg/kkg (0.42 Ib/ton).

The model plant developed for Subcategory A 14 is assumed to have  sep-
arate discharge of process and non-contact wastewaters, in-plant gravity
separation and skimming, pH control, and an oil recovery system for re-
clamation of waste oil and grease skimmings.

Alternative A 14-11 - This alternative provides for the addition of
a complete mix activated sludge unit, secondary clarification, sludge
recirculating pump, a sludge thickening tank, vacuum filtration, and
a sludge holding tank.  Sludge is hauled to a landfill facility every
26 days.  The activated sludge unit also includes a control house  and
two full-time operators.

The resulting BOD waste load is 0.029 kg/kkg (0.058 Ib/ton), the suspended
solids load is 0.038 kg/kkg (0.076 Ib/ton), and the oil and grease
load is 0.021 kg/kkg (0.042 Ib/ton).

               Costs:  Total investment cost:  $201,390
                       Total yearly cost:      $ 39,350

An itemized breakdown of costs is presented in Table 237.  It is assumed
that land costs $82,040 per hectare ($33,200 per acre).  It is further
assumed that one operator is required.

               Reduction Benefits:  BOD:  94.8 percent
                                     SS:  90.9 percent
                                    O&G:  90.0 percent

Alternative A 14-111 - This alternative provides in addition to Alter-
native A 14-11 dual media filtration and a pump station to generate
sufficient head for filter operation.

The resulting BOD waste load is 0.015 kg/kkg (0.030 Ib/ton), the suspended
solids load is 0.015 kg/kkg (0.030 Ib/ton), and the oil and grease
load is 0.008 kg/kkg (0.016 Ib/ton).
                                974

-------
 DRAFT
                         TABLE 237

        ITEMIZED COST SUMMARY FOR ALTERNATIVE AT4-II
          (SHORTENING AND TABLE OIL PROCESSING)
ITEMIZED COST SUMMARY FOR MSTEMTER  TREATMENT CHAIN   B1BKQSY
DESIGN EFFICIENCY... 9tt.8 PERCENT  BOD  REDUCTION

TREATMENT MODULES*
                  81..CONTROL HCLSE
                  B...PUMPING STATION
                  K... ACTIVATED  SLUDGE
                  G...SLUDGE THICKENER
                  S...VACUUM FILTRATION
                  Y...HOLDING TANK

INVESTMENT CCSTSI
               1.  CONSTRUCTION          122710.00
               2.  LAND                   5U1UO.OO
               3.  ENGINEERING            12270.00
               4.  CONTINGENCY            12270.00
               TOTAL                     201390.00

YEARLY OPERATING COSTS:
               1.  LABOR                  12490.00
               2.  PC*ER                   6050.00
               3.  CHEMICALS               1870.00
               a.  MAINTENANCE&SUPPLIES    3520.00
               TOTAL                      23930.00

TOTAL YEARLY COSTS!
               1. YEARLY OPERATING  COST   23930.00
               2. YEARLY INVESTMENT
                  COST KgCCVEPY            fl060.00
               3. DEPRECIATION             7360.00
               TOTAL                      39350.00
                           975

-------
DRAFT


               Costs:  Total Investment cost:  $217,340
                       Total yearly cost:      $ 44,070

An  itemized breakdown of costs is presented in Table 238,  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is  further assumed that one operator is required.

               Reduction Benefits:  BOD:  97.3 percent
                                     SS:  96.4 percent
                                    O&G:  96.2 percent

Alternative A 14-IV - This alternative provides in addition to Alter-
native A 14-1II activated carbon adsorption prior to discharge to
navigable waters.

The resulting BOD waste load is 0.008 kg/kkg (0.016 Ib/ton), the suspended
solids load is 0.008 kg/kkg (0.016 Ib/ton), and the oil and grease load
is 0.004 kg/kkg (0.008 Ib/ton).

               Costs:  Total investment cost:  $259,260
                       Total yearly cost:      $ 62,190

An itemized breakdown of costs is presented in Table 239.  It is
assumed that land costs $82,040 per hectare ($33,200 per acre).  It
is further assumed that one operator is required.

               Reduction Benefits:  BOD:  98.6 percent
                                     SS:  98.1  percent
                                    O&G:  98.1  percent

A cost efficiency curve is presented in Figure 287.

Alternative A 14-V - This alternative provides in addition to Alter-
native A 14-1 an aerated lagoon system with a settling pond.

The resulting BOD waste load is 0.029 kg/kkg (0.058 Ib/ton),  the suspended
solids load is 0.038 kg/kkg (0.076 Ib/ton), and the oil and grease load
is 0.021  kg/kkg (0.042 Ib/ton).

               Costs:   Total investment cost:   $147,390
                       Total yearly cost:       $ 34,810

An itemized breakdown of costs is presented in  Table 240.   It is
assumed that land costs $4100 per hectare ($1660 per acre).   It is
further assumed that one-half time operator is  required.

               Reduction Benefits:   BOD:   94.8  percent
                                     SS:   90.9  percent
                                    O&G:   90.0  percent
                                976

-------
     DRAFT
                             TABLE  238

            ITEMIZED COST SUMMARY  FOR ALTERNATIVE A14-III
               (SHORTENING AND TABLE OIL PROCESSING)
ITEMIZED COST SUMMARY FOR  M5TFMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... 97.3  PERCENT  80D REDUCTION
                                                 (BIBKGSY)BN
TREATMENT MODULES:
                  Bl..CONTROL  HCLSE
                  8...PUMPING  STATION
                  K...ACTIVATED  SLUPGE
                  G...SLUDGE  THICKENER
                  S...VACUUM  FILTRATION
                  V...HOLD ING  TANK
                  N...OUAL  MEDIA  PRESSURE FRTRA'N
INVESTMENT CCSTSt
                1.
                2.
                3.
            CCN9TRUCTICN
            ENGINEERING
        4.  CONTINGENCY
        TCTAL
YEARLY
GPEPATING
        1.
        2.
        ?.
        a.
                 COSTS»
                   LABOR
                   CHEMICALS
                   MAINTENANCEBSLFPLIFS
               TCTAL

TCTAL YEARLY CCSTS:
               1. YEARLY OPERATING  CC8T
               2. YEARLY INVESTMENT
                  CCST RECOVERY
               3. DEPRECIATION
               TCTAL
                                         136000.Ofl
                                          54140.00
                                          13600.00
                                          136.00.00
                                         2173^0.00
                                          12490.
                                           7670.
                                           1870.
00
00
00
                                           5190.00
                                          272PO.OO
                                   27220.00

                                    8690.00
                                    8160.00
                                   4M070.00
                                977

-------
  DRAFT
                          TABLE  239

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A14-IV
            (SHORTENING AND TABLE OIL PROCESSING)
ITEMIZED COST SUMMARY FOR  WASTF*ATER  TREATMENT CHAIN
DESIGN EFFICIENCY... 96.6  PERCENT  BOD REDUCTION
TREATMENT MODULESi
                  81..CONTROL  HOUSE
                  R...PUMPING  STATION
                  K...ACTIVATED  SLUDGE
                  Q...SLL!DGfc THICKENER
                  S...VACUUM FILTRATION
                  Y...HOLOIWC-  TANK
                  N...DUAL  *FDIA  PRESSURE FILTRA'N
                  Z... ACTIVATE  CARBON  ADSORPTION'
                   CONSTHUCTTCN
                   LAND
INVESTMENT CCSTSJ
               u
               2.
               3.
               4.  CONTINGENCY
               TOTAL
                                   170900.00
                                    saiiio.oo
YEARLY OPERATING
              . 1.
               2.
               n.
                 COSTSi
                   LABOR
                   POFR
                   CHEMICALS
                   KAINTENAMCERSIPPLIES
                                          170^0.00
                                                00
                                                00
                                                00
                                    10020,
                                     1870,
               TCTAL
                                    17180.00
                                    41.560.00
TOTAL
YEARLY COSTS:
         1. YEARLY OPERATING  COST   41560.00
         2. YEARLY INVESTMENT
          .  COST MECCVERY           10370.00
         3. DEPRECIATION            10260.00
               TOTAL
                                    62190.00
                                                  (BIBKGSYBN)Z
                            978

-------
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«*.ee    «i.e«    »»,68    i7.es     «e.ee
EFFICIENCY
                                                                                                     toe.et
                                                      FIGURE  287
                     INVESTMEm" AND YEARLY COSTS FOR SUBCATEGORY A14, ALTERNATIVES II THHUUbH IV

-------
DRAFT
                        TABLE 240

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A14-V
         (SHORTENING AND TABLE OIL PROCESSING)
 TTEMTZFD COST  81'MKAKY  FOR  KASTEMTER TREATMENT CHAIN
 DESIGN EFFICIENCY...  94.8  PERCENT BOD REDUCTION
                                                        8L
 TREATMENT MODULES?
                    B...PUMPING STATION
                    L...AERATED I.AGCCN
                     CCNSTPl-rTJCM
                     I..ANP
INVESTMENT COSTS!
               1.
               2.
               3.
               4.  CONTINGENCY
               5.  PVC  LINER
               TOTAL

YEARLY OPERATING CCSTSs

               2!  POWER
               3.  CHEMICALS
               5.  PVC
               TOTAL
TOTAL YEARLY CCSTSJ
               1. YEARLY- OPERATING  COST
               2. YEARLY  INVESTMENT
                  COST RECOVERY
               3. DEPRECIATION
               TOTAL
116910.00
  3330.00
 11690.00
 11690.00
  3770.00
147390.00
                                            6250.00
                                           13680.00
                                               0.0
                                            1640.00
                                             140.00
                                           21710.00
                                           21710.00

                                            5900.00
                                            7200.00
                                           34810.00
                            980

-------
 DRAFT


 Alternative  A 14-VI  -  This  alternative  provides  in  addition to Alter-
 native  A 14-V dual media  pressure  filtration  and a  pump  station to
 generate sufficient  head  for  filter  operation.

 The resulting BOD waste  load  is  0.015 kg/kkg  (0.030 Ib/ton),  the  suspended
 solids  load  is 0.015 kg/kkg (0.030 Ib/ton), and  the oil  and grease  load
 is  0.008 kg/kkg (0.016 Ib/ton).

                Costs:  Total  investment cost:  $163,350
                       Total  yearly  cost:      $ 39,520

 An  itemized  breakdown  of  costs is  presented in Table 241.   It is  assumed
 that land costs $4100  per hectare  ($1660 per  acre).   It  is further
 assumed that one-half  time  operator  is  required.

                Reduction  Benefits:   BOD:   97.3 percent
                                     SS:   96.4 percent
                                     O&G:   96.2 percent

 Alternative A 14-VII - This alternative provides  in  addition  to Alter-
 native  A 14-VI  activated  carbon adsorption before final discharge to
 navigable waters.

 The  resulting BOD waste load  is 0.008 kg/kkg  (0.016  Ib/ton),  the suspended
 solids  load is  0.008 kg/kkg (0.016 Ib/ton), and  the  oil and grease load
 is 0.004 kg/kkg (0.008 Ib/ton).

                Costs:  Total  investment cost:   $205,260
                       Total yearly cost:      $  57,640

 An itemized breakdown of  costs is presented in Table 242.  It is
 assumed  that  land costs $4100 per hectare  ($1660  per acre).   It is
 further  assumed that a one-half time operator is  required.

                Reduction  Benefits:   BOD:  98.6 percent
                                     SS:  98.1 percent
                                    O&G:  98.1 percent

 A cost efficiency curve is presented in Figure 288.

_Cost and Reduction Benefits of Alternative Treatment
 Technologies  for Stibcateanrv A 15 - mivo nn  Rpfinina,

 A model   plant representative of subcategory A  15 was developed in
 Section  V for the purpose of applying control  and treatment alter-
 natives.  In Section VII, three alternatives were selected as  being
 applicable engineering alternatives.   These alternatives  provide for
 various  levels  of waste reductions  for the model  plant which produces
 7.6  cu m  (0.002 MG)  of refined olive oil per day.


                                981

-------
DRAFT
                       TABLE 241

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A14-VI
         (SHORTENING AND TABLE OIL PROCESSING)
ITEMIZED COST SUMMARY FOP-  M8TEMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... 97.3  PERCENT  BOD REDUCTION
                                                        (BLJ8N
TREATMENT MODULES:
                  8...PULPING  STATION
                  L..,AFPATEr  LAGOON
                  B...PUMPING  STATION
                  M...OUAL  MEDIA  PRESSURE
                                           FILTRA'N
INVESTMENT CCSTSl
               1.
               2.
               3.
               4.
               5.
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
                   PVC LINER
               TOTAL

YEARLY OPERATING COSTS!
               1.  LABOR
               C 9  f L. " t W
               3.  CHEMICALS
                   MAINTENANCE8SLPPLIES
                   PVC LINER
TOTAL
         5.
         TOTAL

YEARLY CCSTSl
         1. YEASLY
         2. YEARLY
                         OPERATING  COST
                         INVESTMENT
                  COST
               3.
               TOTAL
                       RECOVERY
130210.00
  3330.00
 13020.00
 13020.00
  3770.00
163350.00
                                           6250.00
                                          15290.00
                                              0.0
                                           3310.00
                                            i«0.00
                                          24990.00
 24990.00

  6530,00
  ecoo.oo
 39520.00
                           982

-------
 DRAFT
                        TABLE 242
          ITEMIZED COST SUMMARY FOR ALTERNATIVE A 14-VII
            (SHORTENING AND TABLE OIL PROCESSING)
ITEMIZED COST SUMMARY FOR KASTEMTER  TREATMENT  CHAIN   (BLBN)Z
DFSIGN EFFICIENCY.., 98.6 PERCENT  BOD  REDUCTION
TREATMENT MCOULESi
                  Bo
                  Lo
                  B.
                  N.
                  Z.
                     .PUMPING STATION
                     .AERATED LAGDCN
                     .PUMPING STATION
                     .DUAL MEDIA PRESSURE  FILTRA'N
                     .ACTIVATED  CARBCN,  ADSORPTION
INVESTMENT CCSTS:
               1.
               2.
               3.
               «.
               5.
                   CPNSTPUCTICK
                   LAND
                   ENGINEERING
                   CONTINGENCY
                   PVC LINER
               TOTAL
YEARLY
       OPERATING
               1.
               2.
               3.
               a.
               s.
CCSTSt
  LABOR
  PCHES
  CHEMICALS
  MAINTENANCES-SUPPLIES
  PVC LINER
               TCTAL

TCTAL YEARLY CCSTSJ
               1. YEARLY OPERATING  COST
               2. YEARLY INVESTMENT
                  COST RECOVERY
               3. DEPRECIATION
               TOTAL
                        165140.
                         3330.
                         16510.
                         16510.
00
00
00
00
                         3770.00
                       205260.00
                                           6250.00
                                          17650.00
                                              0.0
                                          15290.00
                                            HO.00
                                          39330.00
                                          39330.00

                                           8210.00
                                          10100.00
                                          57640.00
                             983

-------
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        a


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        8
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                          t!».e
                           Ift.f
                           JJT.?
                           IZC.O
                           tei.8
                           M.4
       £
       I—I
       o.
                           SI.2
INVESTMENT
                                                                              «».oe   tce.ie
                                               11.08    «}.ee    ««.ee    «t.ee    «».oo    vr.ee    «i.ec



                                                                 EFFICIENCY



                                                                FIGURE  288



                                            YEARLY COSTS FOR  SUBCATEGORY A14, ALTERNATIVE V  THROUGH VII

-------
DRAFT
 It is  estimated  that  the  effluent  from  a  7.6  cu m (0.002  MG)  per day
 plant  is  1.1  cu  m (0.0003 MG) per day   The  BOD  waste  load  is  0.85
 kg/cu  m (7.1  lb/1000  gal),  the  suspended  solids load  is 0.044 kg/cu m
 (0.37  lb/1000 gal)  and  the  oil  and  grease load  is  0.029 kg/cu m
 (0.24  Ib/gal).

 Alternative A 15-1  -  This alternative consists  of  pumping  station, a
 holding tank  and spray  irrigation of the  raw  waste effluent.   It is
 assumed that  a minimum  of 0.65  ha  (1.6  acres) of land is  required.

 The resulting BOD waste load  is  0.0 kg/cu m (0.0 lb/1000  gal), the
 suspended solids load is  0.0  kg/cu  m (0.0 lb/1000  gal) and the oil and
 grease load is 0.0  kg/cu  m  (0.0  lb/1000 gal).

               Costs:  Total  investment  cost:  $37,730
                      Total yearly  cost:      $ 5,170

 An itemized breakdown of  costs  is presented in  Table  243. It is
 assumed that  land costs $4100 per hectare ($1660 per  acre).   It  is
 further assumed  that  no operator is required.

               Reduction Benefits:   BOD:   100  percent
                                    SS:   100  percent
                                    O&G:   100  percent

 Alternative A 15-11 - This  alternative -consists of land spreading
 the raw waste effluent.   It  is assumed  that a minimum of 0.4  ha  (one
 acre)  of  land is required and that  the  effluent does  not need to be
 pumped more than 150  m  (500 ft).

 The resulting-BOD waste load  is  0.0 kg/cu m (0.0 lb/1000  gal), the
 suspended solids load is  0.0  kg/cu  m (0.0 lb/1000  gal) and the oil
 and grease load  is 0.0  kg/cu  m  (0.0 lb/1000 gal).

               Costs:  Total investment  cost:  $5,260
                      Total yearly  cost:      $ 540

 An itemized breakdown of  costs  is presented in  Table  244.  It  is
 assumed that  land costs $4100 per hectare ($1660 per  acre).   It  is
 further assumed  that  no operator is required.


              Reduction  Benefits:  BOD:  100 percent
                                    SS:  100 percent
                                  O&G:  100 percent
                                  985

-------
DRAFT
                            TABLE  243

          ITEMIZED COST SUMMARY FOR ALTERNATIVE AT 5-1
                     (OLIVE OIL REFINING)
      ITEMIZED  COST SUMMARY FOR MSTE*ATER  TREATMENT  CHAIN
      DESIGN  EFFICIENCY.,.100.0 PERCENT POD REDUCTION
      TREATMENT  MODULES!
                        Y... HOLD INC TANK
                        I'...SPRAY IRRIGATION
INVESTMENT COSTS:
               1.  CONSTRUCTION
               2.  L*M)
               3.  fN'C-
                TGTAL

YEARLY OPERATING  COSTSt

                2.   PCWFR
                3.   CHEMICALS
                a.   MAIMTENAMCE*8LPPLIES
                TOTAL

TOTAL VEARLY COSTS!
                i. YEARLY  OPERATING  COST
                2. YEARLY  INVF9TMENT
                  COST RECOVERY
                3. DEPRRC1ATICIK
                TOTAL
                                               25220.
                                                267P.
                                                2920
                                                00
                                                00
                                                00
                                                00
                                               37730.00
                                                    0.0
                                                 830.00
                                                    0.0
                                                1080.00
                                                1910.00
                                                1910.00

                                                1510.00
                                                1750.00
                                                5170.00
                            986

-------
DRAFT
                          TABLE  244
       ITEMIZED
 COST SUMMARY
   (OLIVE OIL
                              FOR  ALTERNATIVE  A  15-11
                              REFINING)
  ITEMIZED  COST  SUMMARY  FOR  WASTEWATER  TREATMENT  CHAIN
  DESIGN  EFFICIENCY...  100  PERCENT  BOD  REDUCTION
 TREATMENT  MODULES:
INVESTMENT COSTS
               1
               2
               3
               4
                     LAND  SPREADING
    CONSTRUCTION
    LAND
    ENGINEERING
    CONTINGENCY
TOTAL
 YEARLY
OPERATING
        1
        2
        3
        4
 TOTAL  YEARLY
                 COSTS:
                   LABOR
                   POWER
                   CHEMICALS
                   MAINTENANCE
                & SUPPLIES
TOTAL
             COSTS:
               1.   YEARLY OPERATING COST
               2.   YEARLY INVESTMENT
                   COST RECOVERY
               3.   DEPRECIATION
               TOTAL
                                            3000.00
                                            1660.00
                                             300.00
                                             300.00
                                            5260.00
                                               0.00
                                               0.00
                                               0.00
                                             150.00
                                             150.00
                                             150.00
                             210
                             180
                                                 00
                                                 00
                                             540.00
                          987

-------
 DRAFT


 Alternative A 15-111 - This alternative consists of hauling the waste-
 water to a municipal treatment facility.

 The resulting BOD waste load is 0.0 kg/cu m (0.0 lb/1000 gal), the
 suspended solids load is 0.0 kg/cu m (0.0 lb/1000 gal) and the oil and
 grease load is 0.0 kg/cu m (0.0 lb/1000 gal).

               Costs:  Total investment cost:  $0.
                       Total yearly cost:       $1,200

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent
                                    O&G:  100 percent

 BEVERAGES

 Cost  and  Reduction  Benefits  of  Alternative  Treatment
 Technologies  for Subcategory A  16  - New Large Breweries

A model plant representative of subcategory A 16 was developed in
Section V for the purpose of applying control and treatment alter-
natives.  In Section VII, thirteen alternatives were selected as being
applicable engineering alternatives.  These alternatives provide for
various levels of waste reductions for the model plant which produces
1500 cu m (12,800 bbl) per day.

Alternative A 16-1 - This alternative assumes no treatment and no re-
duction in the waste load.  It is estimated that the effluent from a
1500 cu m (12,800 bbl) per day plant is 8300 cu m (2.2 m) • per day.
The BOD waste load is 10.55 kg/cu m (2.722 Ib/bbl), and the suspended
solids load is 3.89 kg/cu m  (1.004 Ib/bbl).

              Costs:               0
              Reduction Benefits:  None

Alternative A 16-11 - This alternative provides screening and a grit
chamber, flow equalization, neutralization, nutrient addition, and an
aerated lagoon system.

The resulting BOD waste load 150.28 kg/cu  m (0.072 Ib/bbl) and the sus-
pended solids load is 0.39 kg/cu m (0.100  Ib/bbl).

                Costs:   Total investment cost:   $2,355,740
                        Total yearly cost:       $1,055,530

  An itemized  breakdown  of costs  is  presented in Table  245.   It is
  assumed  that land  costs  $4100  per hectare  ($1660  per  acre).   It  is
  further  assumed that  two operators are required.

                Reduction  Benefits:  BOD:  97.4  percent
                                     SS:  90.0  percent
                                988

-------
DRAFT
                        TABLE 245

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-II
                   (NEW LARGE BREWERIES)
ITEMIZED COST SUMMARY  FOR  MSTFMTER TREATMENT CHAIN
DESIGN EFFICIENCY... 97.«  PERCENT 
-------
DRAFT


Alternative A  16-1II - This alternative provides in addition to
Alternative A  16-11 dual media filtration.

The  resulting  BOD waste  load  is 0.14 kg/cu m  (0.036 Ib/bbl), and the
suspended solids load is 0.19 kg/cu m  (0.049  Ib/bbl).

               Costs:  Total investment cost:  $2,495,160
                      Total yearly cost:      $1,088,090

An itemized breakdown of costs is presented in Table 246.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  98.7 percent
                                    SS:  95.0 percent

Alternative A  16-IV - This alternative adds activated carbon to
Alternative A  16-1II.

The  resulting  BOD waste load is 0.07 kg/cu m  (0.018 Ib/bbl), and the
suspended solids load is 0.09 kg/cu m  (0.023 Ib/bbl).

               Costs:  Total investment cost:  $3,798,200
                      Total yearly cost:      $1,324,820

An itemized breakdown of costs is presented in Table 247.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  99.4 percent
                                    SS:  97.6 percent

A cost efficiency curve is presented in Figure 239.

Alternative A  16-V - This alternative provides a control house, screen-
ing  and a grit chamber, flow equalization, neutralization, nutrient
addition, a complete-mix activated sludge system, sludge thickening,
aerobic digestion, and vacuum filtration.

The  resulting  BOD waste load is 0.28 kg/cu m (0.072 Ib/bbl), and the
suspended solids load is 0.39 kg/cu m (0.100 Ib/bbl).

              Costs:   Total investment cost:  $3,730,960
                      Total yearly cost:      $1,029,500

An itemized breakdown of costs is presented in Table 248.  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that six operators are required.

              Reduction Benefits:   BOD:  97.4 percent
                                    SS:  90.0 percent
                               990

-------
DARFT
                        TABLE  246

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-III
                  (NEW LARGE BREWERIES)
ITEMIZED COST SL^ARY FOP HASTF.MTEK  TREATMENT  CHAIN
DESIGN EFFICIENCY... 98.7 PERCENT  BOH  REDUCTION
TREATMENT MODULES:
                  EI . .SCREENING   *  GRIT  CHAMBER
                  C... EQUALIZATION  BASIN
                  F...ACID NEUTRALIZATION
                  H...NITNOGEN ADDITION
                  L.
                  L.
                  K
      . AERATED
      . AERATED
      .DU4L
                              LAGOON
                              IAQCCN
                              IA  PRESSURE
INVESTMENT CCSTSt
               1.
               2.
               3.
               u.
               5.
    CCN3TRUCTTCN'
    LAND
        LINER
TOTAL
YEARLY OPERATING COSTS?
               1.  LABOR
               2.  FOEW
               3.  CHEMICALS
               U,
               5.
    MAINTENANCERSLRPLIES
    PVC l.JKFW
                                        1995820 . 00
                                          26aiO.OO
                                         !«>95eO.OO
                                         199580.00
                                          73770.00
                                        2«95160.00
                                          24990.00
                                         696880.00
                                          7M90.00
                                          63580.00
                                           5200.00
               TCTAU
TOTAL YEARLY CCSTgJ
               1. YEARLY OPEPAT^G  CCST
               2. VEAKLY IMVFSTKFM
                  CHST *FCCVE'HY           9961.0.00
               3, DEPRECIATION           123440.00
               TCTAL
                          991

-------
DARFT
                        TABLE 247

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-IV
                   (NEW LARGE BREWERIES)
   ITEMIZED  COST  SUMMARY FOR MSTEMTER TREATMEN'T CHAIN
   DESIGN  EFFICIENCY....  99. u PERCENT 8GD REDUCTION
   TREATMENT  MODULES:
                     El..SCREENING  & GRIT CHAMBER
                     C...EQUALIZATION BASIN
                     F...ACIO NEUTRALIZATION
                     H...NITROGEN AMBITION
                     L...AERATED LAGOON
                     L...AERATED LAGOON
                     N...CUAL MEDIA PRESSURE FILTRA'N
                     2... ACTIVATED CARBON ADSCRPT'IGM
   INVESTMENT  CCSTSJ
                  1.
                  2.
                  3.
                  «.
                  5.
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
                   PVC LINER
               TOTAL

YEARLY OPERATING COSTS:
               i.
               2.
               3.
3061680.00
  36410.00
 308170.00
 30S170.00
  73770.00
3798300.00
               5.
                      CHEMICALS
                      MAIMENANCE&SLPPLIES
                      PVC LINER
                  TOTAL
  24990.00
 726220.00
  74190.00
 151700.00
   5200.00
 9P4300.00
   TOTAL  YEARLY  COSTS:
                  1.  YEARLY OPERATING COST 96^300.00
                  ?..  YEARLY INVESTMENT
                     COST RECOVERY         151930.00
                  3.  DEPRECIATION          168590.00
                  TOTAL
                                        1324820.00
                          992

-------
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          2    2701.
               2\^.i.
               : !> 7 ?. 2
               ! 3 2 "5. •
                                                          EFFICIENCY



                                                FIGURE  289



                     INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 16, ALTERNATIVE  IV
                                                                                                   :oc.cc

-------
DRAFT
                        TABLE 248

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-V
                   (NEW LARGE BREWERIES)
  ITEMIZED  COST  SUMMARY  FOR "ASTEKATER TREATMENT CHAIN
  DESIGN  EFFICIENCY...  97.0 PERCENT BOD REDUCTION

  TREATMENT  MGDULESi
                   . 81..CONTROL NCLSE  .
                    EI..SCRFEMKG  & GRIT CHAMBER
                    3. . .PUMPING STATION
                    C...EQUALIZATION BASIN
                    F...ACID  NEUTRALIZATION
                    H...NITRCGF.N ADDITION
                    *...ACTIVATED SLUDGE
                    Q...SLUDGE  THICKF.NER
                    R...AEP-CSIC DIGESTCR
                    S...VACUUM  FILTRATION
                    Y.., ACTIVATED CARBON  ADSORPTION

  INVESTMENT COSTS?
                 1.   CONSTRUCTION        3028620.00
                 2.   LAND                   96620.00
                 3.   ENGINEERING          302660.00
                 a.   CONTINGENCY          302860.00
                 TCTAL                    3730960.00

  YEARLY OPERATING  CCSTS:
                 1.   LA9f!K                  7«970.00
                 2.   pC^F.^                 058410.00
                 3.   CHEMICALS             113770.00
                 a.   MAIMTENANCE&SUPPLIES  51390.00
                 TCTAL                     696540.00

  TOTAL YEARLY CCSTSJ
                 i.  YEARLY  CPEPATIKG COST 698sao.oo
                 2.  YEARUY  INVESTMENT
                   COST "FcC\/EfiY         U9240.CO
                 3. DfPPEClATICA           181720.00
                     ^                    1029500.00
                           994

-------
DRAFT

Alternative A 16-VI - This alternative provides dual media filtration
in addition to Alternative A 16-V.

The  resulting BOD waste load is 0.14 kg/cu m (0.036 Ib/bbl), and the
suspended solids load is 0.19 kg/cu m (0.049 Ib/bbl).

              Costs:  Total investment cost:  $3,870,380
                      Total yearly cost:      $1,062,060

An itemized breakdown of costs is presented in Table 249.  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).  It
is further assumed that six operators are required.

              Reduction Benefits:  BOD:  98.7 percent
                                    SS:  95.0 percent

Alternative A 16-VII - This alternative adds activated carbon to
Alternative A 16-VI.

The  resulting BOD waste load is 0.07 kg/cu m (0.018 Ib/bbl), and the
suspended solids load is 0.09 kg/cu m (0.023 Ib/bbl).

              Costs:  Total investment cost:  $5,173,420
                      Total yearly cost:      $1,298,800

An itemized breakdown of costs is presented in Table 250.  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).  It
is further assumed that six operators are required.

              Reduction Benefits:  BOD:  99.4 percent
                                    SS:  97.6 percent

A cost efficiency curve is presented in Figure 290.

Alternative A 16-VIII-This alternative replaces vacuum filtration in
A 16-V with sludge storage and spray irrigation.

The  resulting BOD waste load is 0.28 kg/cu m (0.072 Ib/bbl), and the
suspended solids load is 0.39 kg/cu m (0.100 Ib/bbl).

              Costs:  Total investment cost:  $3,652,280
                      Total yearly cost:      $  933,750

An itemized breakdown of costs is presented in Table 251.  It is
assumed that land costs $6150 per hectare ($2490 per acre).  It is
further assumed that six operators are required.

              Reduction Benefits:  BOD:  97.4 percent
                                    SS:  90.0 percent

Alternative A 16-IX - This alternative adds dual media filtration to
Alternative A 16-VIII.

                                995

-------
 DRAFT
                         TABLE 249
          ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-VI
                    (NEW LARGE BREWERIES)
            MODULES!
                    Bl ..COMRCL MCI SE
                    F-1..SCRF.FNTNG  ft c-PIT CHAMPFR
                    B... PUMPING STATION
                    C...FQUALIZATICN BASIN
                    F.. .ACID  NEUTRALIZATION
                    H. ..NITRCGFN ADDITION
                    K... ACTIVATED SLUDGE
                   P...AERCSIC  DIGESTCH
                   S...VACLUM FILTRA1ICN
                   Y... HOLDING  TANK
                   N...PUAL MFCTA  PRESSURE

 INVESTMENT CCSTS:
                 '             CN         3U.800.00

                3.'   FNGTKEERN                  '°
                                        3870360.00

YEARLY OPERATING  COSTS:

                1.   LABOR                  7/jQ7rt AA
                2.   PCkPW                  7^970.00
                                         ^76510.00
               •*
                                      ES  53300.0
                                         718550.00
TCTAL YEARLY CCSTS:
               1. YEARLY CPEP-ATING  CCgl  7185^0 00
               2. YEARLY INVESTMENT         5-0.00
                  CCST RECCVPRY
                 '  L          '          106?C60.00
                         996

-------
DRAFT
                        TABLE 250

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-VII
                   (NEW LARGE BREWERIES)
  ITEMIZED COST SUMMARY FOR WASTEMTER TREATMENT  CHAIN
  DESIGN EFFICIENCY... 99.4 PERCENT BOO REDUCTION
  TREATMENT MODULES!
                       .CONTROL HCL'SE
                       .SCREENING  & GRIT CHAMBER
                       .PUMPING STATION
                       .EQUALIZATION BASIN
                       .ACID NEUTRALIZATION
                       .NITROGEN ADDITION
                       .ACTIVATED SLUDGE
                       .SLUDGE THICKENER
                       .AEROBIC DIGESTOR
                       .VACUUM FILTRATION
                       .HOLDING TANK
                       .DUAL MEDIA PRESSURE FILTRAIN
                       • ACTIVATED CARBON  ADSORPTION
  INVESTMENT CCSTSJ
                 1.
                 2.
                 3.
                 4.
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
               TOTAL

YEARLY OPERATING CCSTSl
               1.  LABOR
               2.  PC^ER
               3.  CHEMICALS
               4.  M
               TOTAL
4230660.
  96620.
 423070,
 423070,
00
00
00
00
                                         5173420.00
  74970.
 507850.
 113770.
 141430.
                                                  00
                                                  00
                                                  00
                                                  00
                                          836020.00
  TOTAL YEARLY COSTS!
                 i. YEARLY OPERATING COST 838020.po
                 2. YEARLY INVESTMENT
                    CCST RECOVERY         20*940,00
                 3, DEPRECIATION          253840.00
                 TOTAL                    1298800.00
                          997

-------
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                                             FIGURE 290


                            AND YEARLY COSTS FOR SUBCATEGORY A 16, ALTERNATIVE  VII

-------
DRAFT
                        TABLE 251

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-VIII
                   (NEW LARGE BREWERIES)
   ITEMIZED COST SlPMRV FOR kASTE^ATER TREATMENT CHAIN
   DESIGN EFFICIENCY.., °7.4 PERCENT BCD REDUCTION
             MODULES:
                       ..CONTROL HCUSE
                     El..SCREENING  I GRIT CHAMBER
                     B...PULPING STATION
                     C...EQUALIZATION BASIN
                     F...ACTD NEUTRALIZATION
                     H...NITROGEN ADDITION
                     K... ACTIVATED SLUDGE
                     G...SLLDGF THICKENER
                     P...AEROBIC CIGESTCR
                     Y... HOLD ING TANK
                     u...SPRAY  IRRIGATION
   INVESTMENT COSTS:
                  1.
      CONSTRUCTION
  2.   LAND
  3.   ENGINEERING
  4.   CONTINGENCY
  TOTAL
   YEARLY
OPERATING
        1
        2
        3
    CCSTS:
      LABOR
      POWER
      CHEMICALS
   TOTAL YEARLY
  TOTAL

CCSTSJ
  i. YF.AKLY
  2. YEARLY
     COST
  3. DEPRECIATION
  TCTAL
OPERATING
INVFSTCfNT
              3006770
                4^150
               300680,
               3C0680,
                                         00
                                        ,00
                                        ,00
                                        ,00
                                           3652280.00
                7^970.
               430350,
                                                   00
                                                   00
                                             74190.00
                                             27740.00
                                            607250.00
                                            6C7250.00

                                            146090.00
                                            IftOMO.OO
                                            933750.00
                          999

-------
DRAFT

The  resulting BOD waste load is 0.14 kg/cu m  (0.036 Ib/bbl), and the
suspended solids load is 0.19 kg/cu m  (0,049  Ib/bbl).

              Costs:  Total investment cost:  $3,791,680
                      Total yearly cost:      $  966,310

An itemized breakdown of costs is presented in Table  252.   It is
assumed that land costs $6150 per hectare ($2490 per acre).  It is
further assumed that six operators are required.

              Reduction Benefits:  BOD:  98.7 percent
                                    SS:  95.0 percent

Alternative A 16-X - This alternative adds activated carbon to
Alternative A 16-IX.

The  resulting BOD waste load is 0.07 kg/cu m  (0.018 Ib/bbl), and the
suspended solids load is 0.09 kg/cu m  (0.023  Ib/bbl).

              Costs:  Total investment cost:  $5,094,720
                      Total yearly cost:      $1,203,040

An itemized breakdown of costs is presented in Table 253.  It is assumed
that land costs $6150 per hectare ($2490 per  acre).  It is  further
assumed that six operators are required.

              Reduction Benefits:  BOD:  99.4 percent
                                    SS:  97.6 percent

A cost efficiency curve is presented in Figure 291.

Alternative A 16-XI - This alternative replaces vacuum filtration in
Alternative A 16V with sand drying.

The  resulting BOD waste load is 0.28 kg/cu m  (0.072 Ib/bbl), and the
suspended solids load is 0.39 kg/cum (0.100 Ib/bbl).

              Costs:  Total investment cost:  $6,764,510
                      Total yearly cost:      $1,527,890

An itemized breakdown of costs is presented in Table 254.  It is
assumed that land costs $20,510 per hectare ($8300 per acre).  It is
further assumed that six operators are required.

              Reduction Benefits:  BOD:  97.4 percent
                                    SS:  90.0 percent

Alternative A 16-XII - This alternative adds  dual media filtration
to Alternative A 16-XI.

The  resulting BOD waste load is 0.014 kg/cu m (0.036 Ib/bbl), and the
suspended solids load is 0.019 kg/cu m (0.049 Ib/bbl).
                                 1000

-------
DRAFT
                        TABLE  252

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-IX
                   (NEW LARGE BREWERIES)
  ITEMIZED COST SUMMARY FQR &A37EMTER TREATMENT  CHAIN
  DESIGN EFFICIENCY,.. 9H.7 PERCENT BCD REDUCTION
  TREATMENT MODULES:
                    PI..CONTROL HCLSE
                    E1..SCPFFNJKG  ft C-RJT CHAMREP
                    B...PUMPING STATION
                    C...EQUALIZATION BASIN
                    P...ACID NEUTRALIZATION
                    I-...NITROGEN APDITIC'N
                    "...ACTIVATED SLUDGF:
                    O...SLLDGE THICKENER
                    R.,.AEROBIC DIGESTPR
                    Y..,HOLDING TANK
                    t... SPRAY IRRIGATION
                    N...DUAL MEDIA PRESSURE  FILTRA'N
  INVESTMENT CCSTSz
                 1.
                 2.
                 3.
                 a.
             CCNSTRUCTICN
             LAND
             ENGINEERING
             CONTINGENCY
               TOTAL

YEARLY OPERATING COSTS:
               1.  LABOR
               2.  POKER
               3.  CHEMICALS
3t22950.00
  aaisc.oo
 312290.00
 312290.00
3791660.00
                                           7^970.00
                                 S! PPLIES
                 TCTAl
                                    7^190.00
                                    29650.00
                                   627260.00
  TCTAL
YEARLY CCSTSS
         i. YEARLY OPERATING COST 627260.oo
         2. YEARLY INVESTMENT
                    COST
                 3.
                 TOTAL
                                   151670.00
                                   1673fiO.OO
                                   966310.00
                           1001

-------
 DRAFT
                        TABLE 253

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-X
                   (NEW LARGE BREWERIES)
 ITEMIZED COST  Sl^AWY  FC"«  KAJTEMTFR
 DESIGN EFFICIENCY... '„.«  P£RCEN?TBCD
 TREATMENT .MODULES?
INVESTMENT
                   ei.. COM POL  HCUSE
                   El . .SCREENING   8 GRIT  CHAMBER
                   B...PUKPIN-G  STATION'
                   C...EQLAL I7ATICN BASIN
                   P. ..ACID  Nfl TPALIZATICN
                   H. . .NITROGEN ADDITION
                   *.. .ACTIVATED SLUDGE
                   0...3LLDGE THICKENER
                   P...AEPCHIC DIGESTCR
                   Y... HOLDING TANK
                   U... SPRAY IRRIGATION
                   N...DUAL ^EOIA  PRESSURE FILTRA'N
                   Z... ACTIVATED CA«BCN ADSCRPTJCM
COSTSl
    1.
     •
                    CCJ.8TBUCTICM
                    L  °
                                        ^208810.00

YEARLY OPERATIMG COSTS:
               IB  LABCP
    3'   CHEMICALS
    J.   M

      f  L
                                         ^79790
                                          7fll90
                                         117770
                                         7^720
                                                00
                                                00
                                               .00
                                               .00
TOTAL YEARLY CCSTS:
               1. DEARLY TPERATIKG  COST  7^6
               2. YEARLY INVESTMENT
                  CCST PFCCVERY
                  PEPRFCIAT10N
                   I  . .
                   L                   12030^0
                                               00
                          1002

-------
              5 0 0 S . 0  I
o
o
CO
       w /
       5

       8
       U.
       O

       8

       I
       O
(fl
8

>
S-H*
>-

s
       u
       a
       <
       u
              J.'io.-
3.:;-,
                                                                           «7.c:
                                                        EFFICIENCY

                                                FIGURE 291

                    INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 16, ALTERNATIVE X

-------
DRAFT
                        TABLE 254

         ITEMIZED COST SUMMARY FOR  ALTERNATIVE A16-XI
                   (NEW LARGE BREWERIES)
 ITEMIZED COST SUMMARY FOR HtSTEKATER  TREATMENT  CHAIN
 DESIGN EFFICIENCY... 97.a PERCENT  300  REDUCTION
 TREATMENT MODULESj
                   91..CONTROL HCLSF
                   El..SCREENING  8 GRIT  CHAMBER
                   R...PUMPING STATION
                   C...EQUALIZATION 8ASIN'
                   P...ACID NEUTRALIZATION
                   H...NITROGEN ADDITION
                   *...ACTIVATED SLUDGE
                   G...SLUDGE THICKENER
                   R...AEROBIC DIGESTCk
                   T...SAND DRYING BEDS
 INVESTMENT COSTS:
                i.
                2.
                3.
    CONSTRUCTION
    LAND
    ENGINEERING
4,-  CONTINGENCY
TOTAL
                           5055920.
                            217MO.
                            545590.
00
00
00
                                         545590.00
                                        6764510.00
 YEARLY OPERATING COSTS:
                1.  LABOR                 74970.00
                2.  PCWEtf                429J70.00
                3.  CHEMICALS             74190.00
                a.  MAJNTFNANCE&SIPPLIES 351630.00
                TOTAL                    929960.00
 TOTAL  YEARLY
COSTS:
  1. YEARLY OPERATING COST 929960.00
  ?. YEARLY INVESTMENT
     CCST RECOVERY
  3. DEPRECIATION
                                         270560,
                                         327350
00
00
                TOTAL
                          1527890.00
                           1004

-------
              Costs:  Total investment cost:  $6,903,930
                      Total yearly cost:      $1,560,460

An  itemized breakdown of costs is presented in Table 255.  It is
assumed that  land costs $20,510 per hectare ($8300 per acre).  It
is  further assumed that six operators are required.

              Reduction Benefits:  BOD:  98.7 percent
                                    SS:  95.0 percent

Alternative A 16-XIII - This alternative adds activated carbon to
Alternative A 16-XII.

The resulting BOD waste load is 0.07 kg/cu m  (0.018  Ib/bbl), and the
suspended solids load is 0.09 kg/cu m  (0.023  Ib/bbl).

              Costs:  Total investment cost:  $8,206,970
                      Total yearly cost:      $1,797,190

An  itemized breakdown of costs is presented in Table256.  It is
assumed that  land costs $20,510 per hectare ($8300 per acre).  It
is  further assumed that six operators are required.

              Reduction Benefits:  BOD:  99.4 percent
                                    SS:  97.6 percent

A cost efficiency curve is presented in Figure292.


 Cost and  Reduction  Benefits of Alternative  Treatment Technologies
 for Subcategory A  17 -  Old Large  Breweries

A model plant representative of subcategory A 17 was developed in
Section-V for the purpose of applying control  and treatment alternatives.
In  Section VII, thirteen alternatives were selected as being applicable
engineering alternatives.   These alternatives provide for various levels
of  waste reductions for the model  plant which produces 2600 cu m (22,000
bbl) per day.

Alternative A 17-1 - This alternative assumes  no treatment and no re-
duction in the waste load.   It is estimated that the effluent from a
2600 cu m (22,000 bbl) per day plant is 28,000 cu m  (7.5 MG) per day.  The
BOD waste load is 18.56 kg/cu m (4.78 Ib/bbl), and the suspended solids
load is 7.32 kg/cu m (1.89 Ib/bbl).

              Costs:               0
              Reduction Benefits:   None

Alternative A 17-II  - This  alternative  provides  screening  and a grit
chamber,  flow equalization,  neutralization,  nutrient addition,  and  an
aerated lagoon system.

The  resulting  BOD waste load  is  0.55  kg/cu  m (0.14 Ib/bbl),  and the sus-
pended solids  load  is 0.76  kg/cu m (0.20 Ib/bbl).


                               1005

-------
DRAFT
                       TABLE  255

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-XII
                  (NEW LARGE BREWERIES)
 ITEMIZED  COST SUMMARY FOS *ASTEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY... 98.7 PERCENT BOO REDUCTION
 TREATMENT MODULES:
                   Bl
                   El
                   8.
                   C.
                   F.
                   H.
                   K.
                   Q.
                   R
              .CONTROL HCLSE
              .SCRFFMNG  & GMIT  CHAMBER
              .PUMPING STATION
              .EOULIZATICN BASIN
              .ACID 'NEUTRALIZATION
              .NITROGEN ADDITION
              .ACTIVATED SLUDGE
              .SLUDGE THICKENER
              .AF.RCBIC DIGESTCR
           T...SAND DRYING 3EDS
           N...CUAL KEDTA PRESSURE
                                           FJLTRA'N
 INVESTMENT  CCSTSI
                i.
                c.
                3.
                   L A N P
                   El
                   C(
               TOTAL
YEARLY
OPERATING
        1
        2
        3
                  CCSTSi
                    LABOR
                    PC^ER
                    CHEMICALS
                                5572100.00
                                 217^10.00
                                 557210.00
                                 557210.00
                                6Q03930.00
                                         7^970.00
                TCTAL
                                         74190.00
                                        353540.00
                                        949970.00
 TCTAL  YEARLY
      CCSTSt
        i. YEARUV OPERATING COST 9^9970.00
        2. YEARLY INVESTMENT
           CCST 9F.CCVF.RY         276160.00
        3. DEPRECIATIOfv          334330.00
                TCTAL
                                1560460.00
                          1006

-------
DRAFT
                       TABLE  256

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A16-XIII
                  (NEW LARGE BREWERIES)
ITEMIZED  COST  SUMMARY  FOR  MSTEMTER TREATMENT CHAIN
DESIGN EFFICIENCY...  99.4  PERCENT  BOD REDUCTION
           MODULES!
                   fll
                   El
                   B.
                   C.
                   F.
                   H.
                   *.
                   Q.
                   R.
                   T.
                   N.
                   Z.
        .CONTROL HOUSE
        .SCREENING  8, GRIT CHAMBER
        .PUMPING STATION
        .EQUALIZATION BASIN
        .ACID NEUTRALIZATION
        .NITROGEN ADDITION
        .ACTIVATED SLUDGE
        ,SLlDGE THICKENER
        .AERCPIC DIGESTOR
        .SANO DRYING BEDS
        .DUAL MEDIA PRESSURE FILTRA'N
        .ACTIVATED CA«BCN  ADSORPTION
INVESTMENT  CCSTSI
                i.
                2.
                3.
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
                          6657960.00
                           217«10.00
                           665800.00
                           665800.00
                          8206970.00
YEARLY OPERATING  COSTS:
                1.   LABOR                  74970.00
                2.   POWER        .     '    478610.00
                3.   CHEMICALS              74190.00
                4.   MAINTENANCERSL'PPLIES 441660.00
                TOTAL    •                1069430.00
TOTAL  YEARLY
CCST5«
  1. YEARLY OPERATING CQSTl 069430.00
  2. YEARLY INVESTMENT
     COST RECCVERY         328280.oo
  3. DEPRECIATION          399480.00
  TOTAL                    1797190.00
                           1007

-------
o
o
00
        d
        U.

        O
        z   6 a 7:. c




        2   ,;33C
        z
        1-4


        §   „„.,
        Q




        I
            351!.
            1527.C
                  o.J:     «i.:^    «e.:?    iJ."    <>.;?     <'._:;^   «6.co    «T.CC    «e.cc




                                               FIGURE 292



                  INVESTMENT AND YEARLY COST FOR  SUBCATEGORY A 16, SUBCATEGORY XIII
                                                                                                   icc.co
                                                                                                                   5

-------
 DRAFT
              Costs:  Total investment cost:   $7,125,250
                      Total yearly cost:       $3,328,060

An itemized breakdown of costs is presented in Table 257.   It is assumed
that land costs $4100 per hectare ($1660 per acre).   It is further
assumed that two operators are required.

              Reduction Benefits:  BOD:  97.0 percent
                                    SS:  89.5 percent

Alternative A 17-1II - This alternative provides in  addition to Alter-
native A 17-11 dual  media filtration.

The resulting BOD waste load is 0.27 kg/cu m (0.07 Ib/bbl),  and the sus-
pended solids load is 0.38 kg/cu m (0.10 Ib/bbl).

              Costs:  Total investment cost:   $7,526,890
                      Total yearly cost:       $3,422,120

An itemized breakdown of costs is presented in Table 258.   It is assumed
that land costs $4100 per hectare ($1660 per acre).   It is further
assumed that two operators are required.
               Reduction Benefits:   BOD:   98.5  percent
                                     SS:   94.7  percent


 Alternative A 17-IV - This alternative adds activated  carbon to Alter-
 native A 17-111.

 The resulting BOD waste load is 0.13 kg/cu m (0.03 Ib/bbl),  and the sus-
 pended solids load is 0.19 kg/cu m (0.05 Ib/bbl).

               Costs:  Total investment cost:  $11,677,060
                       Total yearly cost:      $ 4,195,440

 An itemized breakdown of costs is presented in Table 259.  It is assumed
 that land costs $4100 per hectare ($1660 per acre).   It is further
 assumed that two operators are required.

               Reduction Benefits:  BOD:   99.3 percent
                                     SS:   97.5 percent

 A cost efficiency curve is presented in  Figure 293.

 Alternative A 17-V - This alternative provides a control  house, screen-
 ing and a grit chamber, flow equalization, neutralization, nutrient
 addition, a complete mix activated sludge system,  sludge  thickening,
 aerobic digestion, and vacuum filtration.
                                1009

-------
DRAFT
                       TABLE  257

        ITEMIZED COST SUMMARY FOR ALTERNATIVE AT 7-11
                  (OLD LARGE BREWERIES)
 ITEMIZED  COST  SUMMARY  FOR  WA3TEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY...  97.0  PERCENT 80D REDUCTION

 TREATMENT  MODULES!
                   El..SCREENING  R GPIT CHAMBER
                   P...PUMPING STATION
                   C...PENALIZATION BASIN
                   F...ACTD NEUTRALIZATION
                   H...MITROGEN ADDITION
                   L...AERATED LAGOON
                   L...AERATED LAGCCN
                   M...SETTLING PCND

 INVESTMENT CCSTSt
                1.   CONSTRUCTION        5697460.00
                2.   LANT.                   55310.00
                3.   ENGINEERING          569750.00
                4,   CONTINGENCY          569750.00
                5.   FVC  LINER            232980.00
                TOTAL                    7125250.00

 YEARLY  OPERATING  CGSTSi
                1.   LABOR                  2«990.00
                2.   POER                2259300.00
                3.   CHEMICALS            241780.00
                4.   MINTENANCE&SIPPLIES U56BO.OO
                5,   PVC  LINER             17800.00
                TOTAL                    2689550.00

 TOTAL YEARLY COSTS:
                1.  YEARLY  OPERATING COST2689550.00
                2.  YEARLY  INVESTMENT
                   CCST  RECOVERY         285010.00
                3.  DEPRECIATION          353500.00
                TOTAL                    332806C.OO
                          1010

-------
DRAFT
                       TABLE 258

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A17-III
                  (OLD LARGE BREWERIES)
ITEMIZED COST SUMMARY  FOR  wASTEMTER  TREATMENT CHAIN
DESIGN' EFFICIENCY... 98.5  PERCENT  BOD SEDUCTION
TREATMENT HODULESi
                  El
                  B.
                  C.
                  F.
                  H.
                  L.
                  L.
                  M.
               .SCREENING  g  GRIT  CHAMBER
               .PliyPJNG STATION
               .EQUALIZATION  BASIN
               .ACID NEUTRALIZATION
               .NITROGEN ADDITION
               .AERATFO LAGOON
               .AERATI-H LAGOON
               .SETTLING POND
                    MEDIA PRESSURE  FILTRA'N
INVESTMENT COSTSt
               1.
               2.
               3.
               4.
               5.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC
               TCTAL
YEARLY
OPERATING
        1.
        c •
        3.
CCSTSt
  LABOR
  PCWEP
  CHEMICALS
                      6032160.00
                        55310.00
                       603220.00
                       603220.00
                       232960.00
                      7526890.00
00
00
00
                                        2311710.
                                         2^1780.
                   MAINTENAN'CESSLPPLIES  151180.00
                   FVC LINFR              17800.00
               TOTAL                   27^7460.00
        5.
TOTAL YEARLY COSTS:
               1. VfARLY OPERATIC COST27^7a60.00
               2. YEARLY INVESTMENT
                  COST RECOVERY          301080.00
               3. DEPRECIATION           373580.00
               TOTAL                   3^22120.00
                         ion

-------
  DRAFT
                         TABLE  259

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A17-IV
                    (OLD LARGE BREWERIES)
 ITEMIZED COST SUMMARY FUR MSTEMTER TREATMENT CHAIN)
 DESIGN EFFICIENCY... 99.3 PERCENT BOD REDUCTION

 TREATMENT MODULESj
                   El..SCREENING  R GRIT CHAMBER
                   8...PUMPING STATION
                   C...EQUALIZATION BASIN
                   P...ACID NEUTRALIZATION
                   H...NITROGEN ADDITION
                   L...AERATED LAGCCN
                   L...AERATED LAGOON
                   M...SETTLING FOND
                   N...OUAL MEDIA PRESSURE FILTRA'N
                   2...ACTIVATED CARBC\ ADSORPTION

 INVESTMENT  COSTSt
                1.   CONSTRUCTION        9490650.00
                2«   LAND                   55310.00
                3.   ENGlNEtRING          $49060.00
                4.   CONTINGENCY          9a9Q60.00
                5.   PVC LINER             232980.00
                TOTAL                   11677060.00

YEARLY OPERATING COSTS?
                1.   LABOR                  2^990.00
                2«   PCh^R               2^12030.00
                3.   CHEMICALS             2^1780.00
                4.   MAIMTEMANCERSUPPLIES  450670.00
                5.   FVC LINER              17800.00
                TCTAl-                   3147270.00

TOTAL YEARLY COSTS!
                1. YEARLY OPERATING COST3147270.00
               2. YEARLY INVESTMENT
                  CCST RECOVERY         4670*0.00
               3. DEPRECIATION          581090.00
               TCTAL                   4195440,00
                           1012

-------
o
_^

oo
              IOOCP.0

fl!
               75*5.3
           O
               «i fc J. c
               i ! ? : . J I
                                                        EFFICIENCY




                                                FIGURE  293




                      INVESTMENT AND YEARLY COSTS  FOR SUBCATEGORY A  17, ALTERNATIVE IV
                                                                                                                  a

                                                                                                                  §
                                                                                                                  -n

-------
DRAFT
 The resulting BOD waste load is 0.55 kg/cu m (0.14 Ib/bbl), and the sus-
 pended solids load is 0.76 kg/cu m (0.20 Ib/bbl).

               Costs:  Total investment cost:  $11,377,110
                       Total yearly cost:      $ 3,107,230

 An itemized breakdown of costs is presented in Table 260.  it is
 assumed that land costs $41,000 per hectare ($16,600 per acre).  It
 is further assumed that six operators are required.

               Reduction Benefits:  BOD:  97.0 percent
                                     SS:  89.5 percent

  Alternative A 17-VI  - This alternative provides  dual media filtration
  in addition to Alternative A  17-V.

  The resulting BOD  waste  load  is  0.27  kg/cu  m  (0.07 Ib/bbl),  and  the
  suspended solids load is  0.38  kg/cu m (0.10 Ib/bbl).

                Costs:   Total investment cost:   $11,778,750
                        Total yearly cost:       $  3,201,290
 An itemized breakdown of costs is presented in Table 261 .   It is assumed
 that land costs $41,000 per hectare (16,600 per acre).   It is further
 assumed that six operators are required.

               Reduction Benefits:  BOD:   98.5 percent
                                     SS:   94.7 percent

 Alternative A 17-VII - This alternative  adds activated  carbon to
 Alternative A 17-VI.

 The resulting BOD waste load is 0.13 kg/cu m (0.03 Ib/bbl),  and the
 suspended solids load is 0.19 kg/cu m (0.05 Ib/bbl).

               Costs:  Total investment cost:  $15,928,940
                       Total yearly cost:      $ 3,974,630

 An itemized breakdown of costs is presented in Table 262.   It is
 assumed that land costs $41,000 per hectare ($16,600 per acre).   It
 is further assumed that six operators are required.

               Reduction Benefits:  BOD:   99.3 percent
                                     SS:   97.5 percent

 A cost efficiency curve is presented in  Figure 294.

 Alternative A 17-VIII - This alternative replaces  vacuum filtration in
 A 17-V with sludge storage and spray irrigation.

-------
DRAFT
                        TABLE 260

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A17-V
                   (OLD LARGE BREWERIES)
ITEMIZED COST SIMMARV FUR lNASTE*ATER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 97.0 PERCENT  BOO  REDUCTION
TREATMENT MODULES:
                  PI
                  F.
                  B.
                  C.
                  F.
                  H
                  R.
                  S.
                  Y.
               .CONTROL HOUSE
               .ACID NEUTRALIZATION
               .PUMPING STATION
               .EQUALIZATION BASIN
               .ACID NEUTRALIZATION
               .NITROGEN  ADDITION
               .ACTIVATED  SLUDGE
               .SLUDGE THICKENER
               .AERCBIC CIGfSTOR
               .VACUUM FILTRATION
               .HOLDING TANK
INVESTMENT CCSTSs
               1.
               2.
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
               3.
                                 9260880.00
                                  26^050.00
                                  926090.00
                                  926090.00
                                11377110.00
YEARLY
OPERATING
        1.
        2.
        3.
  COSTS}
    LABOR                 74970.00
    POWER               1518390.00
    CHEMICALS            481670.00
4.  MAIK'TENANCEIISUPPLIES  21470.00
TOTAL                   2096500.00
TOTAL YEARLY COSTS:
               1. YEARLY OPERATING COST2096500.00
               2. YEARLY INVESTMENT
                  CCST RECOVFRY          455080.00
               3. nFPRF.CIATICN          -555650.00
               TCTAL                    3107230.00
                          1015

-------
DRAFT
                       TABLE  261

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A17-VI
                  (OLD LARGE BREWERIES)
ITEMIZED COST SUMMARY FOR  MSTEMTEP  TREATMENT  CHAIN
DESIGN EFFICIENCY... 9P.5  PERCENT  POD REDUCTION
TREATMENT MODULES?
                  81 ..CONTROL  HCLSE
                  F...ACIC NEUTRALIZATION
                  B.., PUMPING  STATION
                  C... EQUALIZATION BASIN
                  F...ACIO NEUTRALIZATION
                  ^...MITRGGEN.  ADDITION
                  K... ACTIVATES  SLUDGE
                  c... SLUDGE THICKENER
                  R... AEROBIC  DIGESTOR
                  S... VACUUM FILTRATION
                  Y... HOLDING  TANK
                  N...DUAU MEDIA PRESSURE  FILTRA'N
INVESTMENT CCSTS:
               1.
               2.
               3.
               a.
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
YEARLY OPERATING COSTS:
               1.  LABOR
               
-------
DRAFT
                       TABLE 262

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A17-VII
                  (OLD LARGE BREWERIES)
ITEMIZED COST SUMMARY FOR vnASTEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 99.3 PERCENT BOD  REDUCTION
TREATMENT MODULES!
                  81
                  F
                  B
                  C
                  F
                  H
                  K
                  G
                  R
                  s
                  V
                  N
                  z
   CONTROL HCUSE
   ACTD NEUTRALIZATION
   PUMPING STATION
   EQUALIZATION BASIN
   ACID NEUTRALIZATION
   NITROGEN ADDITION
   ACTIVATED SLUDGE
   SLUDGE THICKENER
   AERCBIC CIGESTOR
   VACUUM FILTRATION
   HOLDING TANK
   DUAL MEDIA PRESSURE FILTRA'N
   ACTIVATED CARB&N 'ADSORPTION
INVESTMENT CCSTS!
               1.
               2.
               3.
               4.
CCNSTRUCTICN
LAND
ENGINEERING
CONTINGENCY
               TCTAL
13054070.00
  264050.00
 1305^10.00
 1305aiO.OO
15928940.00
YEARLY OPERATING CCSTSi
               1.  LABOR                  74970.00
               2.  PCKER                1671120.00
               3.  CHEMICALS             481670.00
               4.  KAINTENANCERSUPPLIES  326470.00
               TCTAL                    2554230.00

TCTAL YEARLY CCSTSt
               i. YEARLY OPERATING ccsT255423o.oo
               2. YEARLY INVESTMENT
                  COST RECOVERY          637160.00
               3. DEPRECIATION           783240.00
               TOTAL                    3974630.00
                           1017

-------
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            (£55.6
          «o.co
                                                  «-,cc     05. oe



                                                   EFFICIENCY
                                                                          «T.CC
                                                                                                  100.00
                                             FIGURE 294




                  INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A  17,  ALTERNATIVE  VII

-------
DRAFT
The resulting BOD waste load is 0.55 kg/cu m (0.14 Ib/bbl), and the sus-
pended solids load is 0.76 kg/cu m (0.20 Ib/bbl).

              Costs:  Total investment cost:  $11,233,200
                      Total yearly cost:      $ 2,833,190

An itemized breakdown of costs is presented in Table 263.  It is
assumed that land costs $6150 per hectare ($2490 per acre).  It is
further assumed that six operators are required.

              Reduction Benefits:  BOD:  97.0 percent
                                    SS:  89.5 percent
Alternative A 17-IX - This alternative adds dual media filtration to
Alternative A 17-VIII.

The resulting BOD waste load is 0.27 kg/cu m (0.07 Ib/bbl), and the
suspended solids load is 0.38 kg/cu m (0.10 Ib/bbl).

              Costs:  Total investment cost:  $11,634,840
                      Total yearly cost:      $ 2,927,240

 An itemized  breakdown of  costs  is  presented in  Table  264.   It  is
 assumed that land  costs $6150 per  hectare  ($2490  per  acre).  It  is
 further assumed that  six  operators  are  required.

               Reduction Benefits:   BOD:  98.5  percent
                                     SS:  94.7  percent
 Alternative  A 17-X  -  This  alternative adds activated carbon to Alter-
 native  A 17-IX.

 The  resulting BOD waste  load  is 0.13 kg/cu m  (0.03 Ib/bbl), and the
 suspended solids load is 0.19. kg/cu m (0.05 Ib/bbl).

               Costs:   Total investment cost:  $15,785,030
                       Total yearly cost:      $ 3,700,570

 An itemized  breakdown of costs is presented in Table 265.  It is
 assumed that land costs  assumed that six operators are required.

               Reduction  Benefits:  BOD: 99.3  percent
                                    SS: 97.5  percent

 A cost  efficiency curve  is presented in Figure 295.

 Alternative  A 17-XI -  This alternative replaces vacuum filtration in
 Alternative  A 17-V with  sand  drying beds.  This alternative was not
 deemed  economically viable and therefore was  not costed.
                              1019

-------
DRAFT
                       TABLE 263

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A17-VIII
                  (OLD LARGE BREWERIES)
ITEMIZED COST SUMMARY FOR HASTEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 97.0 PERCENT BOD  REDUCTION

TREATMENT MODULES:
                  PI..CONTROL HCISE
                  El..SCREENING  & GRIT  CHAMBER
                  B...PUMPING STATION
                  C...EQUALIZATION BASIN
                  F...ACID NEUTRALIZATION
                  H...NITROGFN ADDITION
                  K...ACTIVATED  SLUDGE
                  5...SLUDGE THICKENER
                  R...AEROBIC r.IGESTOR
                  Y...HOLDING TAMK
                  U...SPRAY IRRIGATION

INVESTMENT COSTS:
               1.  CONSTRUCTION        9252610.00
               2.  LAND                  130070.00
               3.  KMGINEKRING           925260.00
               it.  CONTINGENCY           925260.00
               TOTAL                   11233200.00

YEARLY OPERATING COSTS*
               1.  LABOR                 74970.00
               2.  PCHER               H30180.00
               3.  CHEMICALS             241780.00
               4.  MAINTFNANCE&SLPPLXES  81770.00
               TOTAL                   1828700.00

TOTAL YEARLY COSTS:
               1. YEARLY OPERATING COST 1828700 . 00
               2. YEARLY INVESTMENT
                  COST RECOVERY          449330.00
               3. DEPRECIATION           555160.00
               TOTAL                   2633190.00
                          1020

-------
  DRAFT
                         TABLE 264

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A17-IX
                    (OLD LARGE BREWERIES)
 ITEMIZED COST SUMMARY FOR MSTEMTER  TREATMENT  CHAIN
 DESIGN EFFICIENCY... 98.5 PERCENT  BOD  REDUCTION
 TREATMENT MCDULESt
                   Bl.. CONTROL HCUSE
                   El. .SCREENING  8 GRIT  CHAMBER
                   S... PUMPING STATION
                   C... EQUALIZATION BASIN
                   F...ACID NEUTRALIZATION
                   H... NITROGEN- ADDITION
                   *... ACTIVATED SLL-DGE
                   is... SLUDGE THICKENER
                   R...AERCPIC DIGESTOR
                   Y... HOLDING TANK
                   U... SPRAY IRRIGATION
                   N'..,DUAL MEDIA PRESSURE FILTPA'N
INVESTMENT COSTS:
                1.
                *•
                3.
                a.
            rCNSTPlifTTCN
            L^Nf5
            ENGINEERING
            CCNTINGEN-CY
                                        9587310.00
                                         130070.00
                                         956730.00
                                         95P730.00
                                       U63«8
-------
DRAFT
                        TABLE 265

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A17-X
                   (OLD LARGE BREWERIES)
 ITEMIZED COST S.UMMAKY FOP *ASTEMTER TREATMENT  CHAIN-
 DESIGN EFFICIENCY... 99.3 PERCENT BCD REDUCTION
 TREATMENT MODULES*
                       CONTROL HCUSE
                       SCREENING!  8 SPIT CHAMBER
                       PUMPING STATION
                       EQUALIZATION BASIN
                       ACID NEUTRALIZATION
                       NITROGEN ADDITION
                       ACTIVATED SLUDGE
                       SLUDGE THICKENER
                       AEROBIP DIGESTOR
                       HOLDING TANK
                       SPRAY IRRIGATION
                       DUAL MEDIA PRESSURE FILTPA'N
                       ACTIVATED CARBON ADSORPTION
 INVESTMENT COSTS!
                1.
                2.
                3.
                4.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
                      13045800,
                        130070,
                       1304580,
                       1304580,
00
00
00
00
                TOTAL
                                15785030.00
 YEARLY
OPERATING
        1.
        2.
        3.
        4.
CCSTSl
  LABOR                 7^970,00
  POKER               1582910.00
  CHEMICALS            241780.00
  MAINTENANCEftSLPPLlES 366760.00
                TOTAL
                                 2286420.00
 TOTAL  YEARLY COSTS:
                1. YEARLY OPERATING COST2286420.00
                2. YEARLY INVESTMENT
                   COST RECOVERY         631400.00
                   DEPRECIATION          782750.00
        3.
        TCTAL
                                        3700570,00
                          1022

-------
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-------
DRAFT
 The resulting BOD waste load is 0.55 kg/cu m (0.14 Ib/bbl), and the
 suspended solids load is 0.76 kg/cu m (0.20 Ib/bbl).

               Reduction Benefits:  BOD:  97.0 percent
                                     SS:  89.5 percent

 Alternative A 17-XII - This alternative adds dual media filtration
 to Alternative A 17-XI.  This alternative was not deemed economically
 viable and therefore was not costed.

 The resulting BOD waste load is 0.27 kg/cu m (0.07 Ib/bbl), and the
 suspended solids load is 0138 kg/cu m (0.10 Ib/bbl).

               Reduction Benefits:  BOD:  98.5 percent
                                     SS:  94.7 percent

 Alternative A 17-XI11 - This alternative adds activated carbon to
 Alternative A 17-XII.  This alternative was not deemed economically
 viable and therefore was not costed.

 The resulting BOD waste load is 0.13 kg/cu m (0.03 Ib/bbl), and the
 suspended solids load is 0.19 kg/cu m (0.05 Ib/bbl).


               Reduction Benefits:  BOD:  99.3 percent
                                     SS:  97.5 percent

 Cost and Reduction Benefits of Alternative Treatment Technologies
 for Subcategory A 18 - All  Other Breweries

 A model plant representative of subcategory A 18 was developed in
 Section V for the purpose of applying control and treatment alter-
 natives.  In Section VII, thirteen alternatives were selected as being
 applicable engineering alternatives.  These alternatives provide for
 various levels of waste reductions for the model plant which produces
 470 cu m (4000 bbl) per day.

 Alternative A 18-1 - This alternative assumes no treatment and no
 reduction in the waste load.  It is estimated that the effluent from
 a 470 cu m (4000 bbl) per day plant is 4500 cu m (1.2 MG) per day.
 The BOD v/aste load is 13.53 kg/cu m (3.491 Ib/bbl), and the suspended
 solids load is 6.19 kg/cu m (1.60 Ib/bbl).

               Costs:               0
               Reduction Benefits:  None

 Alternative A 18-11 - This alternative provides screening and a grit
 chamber, flow equalization, neutralization, nutrient addition, and an
 aerated lagoon system.

 The resulting BOD waste load is 0.48 kg/cu m (0.12 Ib/bbl), and the
 suspended solids load is 0.68 kg/cu m (0.18 Ib/bbl).


                             1024

-------
 DRAFT
               Costs:  Total  investment cost:  $1,344,140
                      Total  yearly cost:      $  530,240

 An  itemized  breakdown of costs  is presented in Table  266.  It is
 assumed  that land  costs $4100 per hectare  ($1660 per  acre).  It is
 further  assumed  that two operators are required.

               Reduction Benefits:  BOD:  96.4 percent
                                    SS:  89.1 percent
Alternative A  18-III - This alternative provides in addition to
Alternative A  18-11 dual media filtration.

The  resulting  BOD waste load is 0.24 kg/cu m (0.06 Ib/bbl), and the
suspended solids load is 0.34 kg/cu m (0.09 Ib/bbl).

               Costs:  Total investment cost:  $1,432,200
                      Total yearly cost:      $  551,760

An itemized breakdown of costs is presented in Table 267.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

              Reduction Benefits:   BOD:   98.2 percent
                                    SS:   94.5 percent
Alternative A 18-IV - This alternative adds activated carbon to
Alternative A 18-111.

The resulting BOD waste load is 0.12 kg/cu m (0.03 Ib/bbl), and the
suspended solids load is 0.17 kg/cu m (0.04 Ib/bbl).

              Costs:  Total investment cost:  $2,337,000
                      Total yearly cost:      $  706,630

An itemized breakdown of costs is presented in Table  268 .   It is
assumed that land costs $4100 per hectare ($1660 per  acre).  It is
further assumed that two operators are required.

              Reduction Benefits:  BOD:   99.0 percent
                                    SS:   97.3 percent

A cost efficiency curve is presented in  Figure 296.

Alternative A 18-V - This alternative provides a control house, screen-
ing  and a grit chamber, flow equalization, neutralization, nutrient
addition, a complete mix activated sludge system, sludge thickening,
aerobic digestion, and vacuum filtration.

-------
  DRAFT
                        TABLE 266

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-II
                    (OTHER BREWERIES)
ITEMIZED COST SUMMARY FOR hASTEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 96,U PERCENT  80D  REDUCTION
TREATMENT MODULES:
                  B...PULPING  STATION'
                  El..SCREENING   &  GRIT  CHAMBER
                  C...EQUALIZATION  BASIN
                  F...ACID NEUTRALIZATION
                  H...NITROGEN ADDITION
                  L...AERATED  LAQOCN
                  L...AERATED  LAGOON
INVESTMENT COSTS:
               1.
               5.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC LJNFR
               TOTAL
                      1073410.00
                         17950.00
                        107340.00
                        107J40.00
                         38100.00
YEARLY
OPERATING
        1.
CCSTS:
  LABOR
  PPMER
  CHEMICALS
  MAINTENANCE&SUPPLIE3
  PVC LINER
               TCTAL
 3^990.00
3P2080.00
 3^^00.00
 25800.00
  2890.00
410160.00
TCTAL YEARLY COSTS:
               1. YEARLY OPERATING CTST 410160.00
               2. YEARLY INVESTMENT
                  COST RECOVEKY          53770.00
               3. DEPRECIATION           66310.00
               TCTAL
                                 530240.00
                           1026

-------
DRAFT
                      TABLE 267

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-III
                   (OTHER BREWERIES)
 ITEMIZED  COST SUMMARY FtS waSTEfcATER TREATMENT CHAIN
 DESIGN  EFFICIENCY...  
-------
 DRAFT
                       TABLE  268

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-IV
                    (OTHER BREWERIES)
ITEMIZED COST SUMMARY FCR  HASTENATER  TREATMENT CHAIN
DESIGN' EFFICIENCY... 99.0  PERCENT  BOD REDUCTION
TREATMENT MCDl'LES:
                  0...PULPING  STATION
                  El..SCREENING   &  GRIT  CHAMBER
                  C...ECJIALIZATICN  BASIN
                  F...ACID  NEUTRALIZATION
                  H...NITROGEN  ADDITION
                  L...AERATED  LAGOON
                  L...AERATED  LAGCCN
                  N...DUAL  MEDIA  PRESSURE  FILTRA'N
                  2..,ACTIVATED CARBON ADSORPTION
INVESTMENT COSTS:
               1,
               c »
               3.
               
-------
        5
        8
        b
ZJ58.C  I
      I
      I
      I
      I
?!:7.i  I
      I
      I
      i
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ro
        I—  lela.B  i
        I.       !
        g  »».,:
        9        :
        <        i
        ^  107,:.i  i
            53C
                                                                                              sc:
                                                      EFFICIENCY

                                            FIGURE 296

                 INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 18, ALTERNATIVE  IV

-------
DRAFT
 The resulting BOD waste  load  is  0.48  kg/cu m  (0.12  Ib/bbl), and the
 suspended solids  load  is 0.68 kg/cu m (0.18 Ib/bbl).

               Costs:   Total investment cost:   $1,506,780
                       Total yearly cost:       $  440,710

 An itemized breakdown  of costs is presented in Table 269.   It  is
 assumed that land costs  $41,000  per hectare ($16,600 per acre).   It
 is further assumed that  six operators are required.

               Reduction  Benefits:  BOD:  96.4  percent
                                    SS:  89.1  percent
 Alternative  A 18-VI  - This  alternative provides dual media fil-
 tration  in addition  to  Alternative A  18-V.

 The  resulting BOD waste load  is 0.24  kg/cu m  (0.06 Ib/bbl), and
 the  suspended solids load is  0.34 kg/cu m  (0.09 Ib/bbl).

               Costs:  Total investment cost:  $1,594,850
                      Total yearly cost:      $  461,230

 An itemized  breakdown of costs is presented in Table 270.  it is
 assumed  that land costs $41,000 per hectare ($16,600 per acre).  It
 is further assumed that six operators are required.

               Reduction Benefits:  BOD:  98.2 percent
                                    SS:  94.5 percent
 Alternative A  18-VII - This alternative adds activated carbon to
 Alternative A  18-VI.

 The  resulting  BOD waste load is 0.12 kg/cu m (0.03 Ib/bbl), and the
 suspended  solids load is 0.17 kg/cu m  (0.04 Ib/bbl).

               Costs:  Total investment cost:  $2,499,660
                      Total yearly cost:      $  616,110

 An itemized breakdown of costs is presented in Table271.  It is
 assumed that land costs $41,000 per hectare ($16,600 per acre).
 It is  further  assumed that six operators are required.

               Reduction Benefits:  BOD:  99.0 percent
                                    SS:  97.3 percent

 A cost efficiency curve is presented in Figure  297.

 Alternative A  18-VIII - This alternative replaces vacuum filtration
 in A 18-V  with sludge storage and spray irrigation.

-------
  DRAFT
                        TABLE 269

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-V
                    (OTHER BREWERIES)
ITEMIZED COST SUMMARY FOR 'wASTE/A TKR  TREATMENT  CHAIN
DESIGN EFFICIENCY... 96. 
-------
  DRAFT
                        TABLE  270

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-VI
                     (OTHER BREWERIES)
ITEMIZED COST SUMMARY FOR HASTE*ATER TREATMENT CHAIN
DESIGN EFFICIENCY... 98.2 PERCENT SOD REDUCTION
TREATMENT MODULES!
                  Bl
                  El
                  B.
                  C.
                  F.
                  H.
                  K.
                  Q.
                  R.
                  S.
                  Y.
                  N.
              .COMROL HCL8E
              .SCREENING  * GRIT CHAMBER
              .PUMPING STATION
              .EQUALIZATION BASIN
              .ACID NEUTRALIZATICN
              .NITROGEN ADDITION
              .ACTIVATED SLUDGE
              .SLUDGE THICKENER
              .AEROBIC DIGESTCR
              .VACUUM FILTRATION
              .HOLDING TANK
              .DUAL MEDIA PRESSURE FILTRA'N
INVESTMENT CCSTSl
               1.
               2.
               3.
               a.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
               TOTAL
                        1275170.00
                          64640.00
                         127520.00
                         127520.00
                        1594850.00
YEARLY
OPERATING
        1.
        2.
        3.
  COSTS!
    LABfiR
    CHEMICALS
4.  "AJNTENANCE&3UPPLIES
TOTAL
                                         74970.00
                                        177250.00
                                         50320.00
                                         18390.00
                                        320930.00
TOTAL  YEARLY
      CCSTSl
        1. YEARLY OPERATING COST 320930.00
        2, YEARLY 'INVEST^EKT
           CCST RECOVERY          63790.00
        3. DEPRECIATION           76510.00
        TOTAL                    461230.00
                           1032

-------
 DRAFT
                       TABLE 271

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-VII
                    (OTHER BREWERIES)
ITEMIZED COST SiiMMRY FOR HASTEKATER TREATMENT  CHAIN
DESIGN EFFICIENCY... 99.0 PERCENT BOO REDUCTION

TPEATMFNT MODULES}
                  81. .CONTROL HCLSE
                  El..SCREENING  & GRIT CHAMBER
                  8...PUMPING STATION
                  C...EQUALIZATION BASIN
                  F...ACID NEUTRALIZATION
                  H...NITRC:GEN ADDITION
                  K...ACTIVATED SLUDGE
                  G...SLUrGF THICKENER
                  R0..AERrRIC DIGESTOR
                  S...VACUUM FILTRATION
                  Y...HOLDING TANK
                  N...PUAL MEDIA PRESSURE FILTRA'N
                  2...ACTIVATED CARBON ABSORPTION

INVESTMENT CTSTSl
               1.  CONSTRUCTION        2029180.00
               2.  LAND                  64640.00
               3.  ENGINEERING          202920.00
               «.  CONTINGENCY          202920.00
               TCTAL                   2499660.00

YFAPLY OPERATING COSTS:
               1.  LABOR                 74970.00
               ?..  FC'^ER                201610.00
               3.  CHEMICALS             50320.00
               4.  MMNTBNAMCE*SUPPLIES  67470.00
               TCTAL                    394370,00

TOTAL YEARLY CCSTS:
               1. YEARLY OPERATING COST 394370.00
               2. YEARLY INVESTMENT
                  COST RECOVERY          99990.00
               3. DEPRECIATION          121750.00
               TCTAL                    616110.00
                         1033

-------
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                                                 EFFICIENCY



                                            FIGURE 297



                INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A  18,  ALTERNATIVE VII

-------
 DRAFT
 The  resulting  BOD waste  load  is 0.48 kg/cu m  (0.12 Ib/bbl), and
 the  suspended  solids  load  is  0.68  kg/cu m (0.18 Ib/bbl).

               Costs:  Total investment cost:  $1,473,950
                      Total yearly cost:      $  405,140

 An itemized  breakdown of costs is  presented in Table 272.  it is assumed
 that land costs $6150 per  hectare  ($2490 per  acre).  It is further
 assumed  that six operators are required.

               Reduction  Benefits:  BOD:  96.4 percent
                                    SS:  89.1 percent
Alternative A 18-IX - This alternative adds dual media filtration
to Alternative A  18-VIII.

The resulting BOD waste load is 0.24 kg/cu m (0.06 Ib/bbl), and the
suspended solids  load is 0.34 kg/cu m (0.09 Ib/bbl).

              Costs:  Total investment cost:  $1,562,010
                      Total yearly cost:      $  425,670

An itemized breakdown of costs is presented in Table273.   It is
assumed that land costs $6150 per hectare ($2490 per acre).   It is
further assumed that six operators are required.

              Reduction Benefits:  BOD:   98.2 percent
                                    SS:   94.5 percent
Alternative A 18-X - This alternative adds activated carbon to Alter-
native A 18-IX.

The resulting BOD waste load is 0.12 kg/cu m (0.03 Ib/bbl), and the
suspended solids load is 0.17 kg/cu m (0.04 Ib/bbl).

              Costs:  Total investment cost:  $2,466,820
                      Total yearly cost:      $  580,540

An itemized breakdown of costs is presented in Table 274.  It is
assumed that land costs $6150 per hectare ($2490 per acre).  It is
further assumed that six operators are required.

              Reduction Benefits:  BOD:   99.0 percent
                                    SS:   97.3 percent

A cost efficiency curve is presented in  Figure 298.

Alternative A 18-XI - This alternative replaces vacuum filtration in
Alternative A 18-V with sand drying beds.

-------
  DRAFT
                        TABLE 272

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-VIII
                     (OTHER BREWERIES)
ITEMIZED COST SUMMARY  FOR  MSTFMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... 96.4  PERCENT  BCD REDUCTION
TREATMENT MODULES*
                      .CONTROL  HCISE
                      .SCREENING   8  GRIT  CHAMBER
                  31.
                  Fl.
                  B...PUMPING STATION
                  (•...EQUALIZATION  BASIN
                  F...ACID NEUTRALIZATION
                  H...NITRPGF.* ADDITION
                  K...ACTIVATED SLUDGE
                  Q...SLLDGE THICKENER
                  R...AERCPIC OIGESTOR
                  V...HOLD ING TANK
                  U...SPRAY IRRIGATION
INVESTMENT COSTSl
               1.
               2.
               3.
               
-------
 DRAFT
                       TABLE 273

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-IX
                    (OTHER BREWERIES)
ITEMIZFD COST SUMMARY FOR  I*ASTFMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... 9P02  PFHTFK.T  BOO  REDUCTION

TREATMENT MODULES?
                  81..CONTROL  HCH.SE
                  F-1 ..SCREENING  R GRIT  CHAMBER
                  e...PUMPING  STATION
                  C...EQUALIZATION BASIN
                  P...ACID  NEUTRALIZATION
                  H...NITROGEN AHCITICN
                  K...ACTIVATED  SLUDGE
                  •3...SLUnGE THICKENER
                  R...AEROBIC  CIGESTCR
                  Y...HOLDING  TANK
                  li... SPRAY IRRIGATION
                  N...DUAL  MEDIA PRESSURE  FILTRA'N

INVESTMENT CCSTS»
               1.  CONSTRUCTION         1283630.00
               2.  LAND                  21660.00
               3.  ENGINEERING           128360.00
               «.  CCNTINGtNfY           128360.00
               TOTAL                    1562010.00

YEARLY OPERATING COSTS*
               1.  LABCJH                 7^)970.00
               2.  PCtoER                 167120.00
               3.  CHEMICALS             3iiaOO.OO
               «.  "AINTFN4NCE&SLFPL1ES    9680.00
               TOTAL                     286170,00

TOTAL YEARLY COSTS!
               U YEARLY OPERATING COST  286170,00
               ?. YFARLY INVESTMENT
                  ctsi RECCVFPY          62i*eo.ofl
               3» DEPRECIATION1           77020.00
               TOTAL                     ^25670.00
                          1037

-------
  DRAFT
                        TABLE  274

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-X
                     (OTHER BREWERIES)
ITEMIZED COST SUMMARY FOP  KASTEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 99.0  PERCENT  BOP  REDUCTION

TREATMENT MODULES:
                  61. .CONTROL  HCUSE
                  El. .SCREENING  R  GRIT  CHAMBER
                  8. ..PUMPING  STATION
                  C... EQUALIZATION  BASIC.;
                  F...ACID NEUTRALIZATION
                  H... NITROGEN ADDITION
                  K... ACTIVATED  SLUDGE
                  C... SLUDGE THICKENER
                  R... AEROBIC  DIGESTOR
                  Y... HOLDING  TANK
                  U... SPRAY IRRIGATION
                  N...DUAL MEDIA PRESSURE  FJLTRA'N
                  Z. . .ACTIVATED  CARBON  AO
INVESTMENT COSTSl
               1.  CONSTRUCTION         2037640.00
               2.  LaND                   21660.00
               3.  ENGINEERING           203760.00
               4.  CONTINGENCY           203760.00
               TOTAL                    2466820.00

YEARLY OPERATING CCSTS>
               1.  LABOR                  74970.00
               2.  PCI^EP                 19U80.00
               3.  CHEMICALS              34400.00
               a.  "AlWTENANCeaSlPPUlES   58760.00
               TOTAL                     359610.00

TOTAL YEARLY COSTS:
               i. YEARLY OPERATING COST  3596io.oo
               2. YEARLY INVESTMENT
                  COST RECOVERY           <>867c.oo
               3. DEPRECIATION           122260. CO
               TOTAL         '            580540.00
                          1038

-------
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       IL
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       to
       CO
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       <


       u
       w

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       D.

       O
                                                                                                                    30
                                                                                                                    3>
                   t; i. i
                                                         EFFICIENCY



                                                   FIGURE 293



                        INVESTMENT AND  YEARLY COSTS FOR SUBCATEGORY A 18,  ALTERNATIVE X
                                                                                                     i c:,

-------
DRAFT
The resulting BOD waste load is 0.48 kg/cu m (0.12 Ib/bbl), and the
suspended solids load is 0.68 kg/cu m (0.18 Ib/bbl).

              Costs:  Total investment cost:  $2,694,560
                      Total yearly cost:      $  638,610

An itemized breakdown of costs is presented in Table 27S  It is
assumed that land costs $20,510 per hectare ($8300 per acre).   It
is further assumed that six operators are required.

              Reduction Benefits:  BOD:   96.4 percent
                                    SS:   89.1 percent

Alternative A 18-XII - This alternative  adds dual  media filtration
to Alternative A 18-XI.

The resulting BOD waste load is 0.24 kg/cu m (0.06 Ib/bbl), and the
suspended solids load is 0.34 kg/cu m (0.09 Ib/bbl).

              Costs:  Total investment cost:  $2,782,630
                      Total yearly cost:      $  659,140

An itemized breakdown  of costs is presented  in Table 276.  It is
assumed that land  costs $20,510  per hectare  ($8300  per acre).   It
is further assumed  that six operators are required.

              Reduction Benefits:  BOD:  98.2 percent
                                    SS:  94.5 percent

Alternative A 18-XIII  - This alternative adds activated carbon to
Alternative A 18-XII.

The resulting BOD waste load is  0.12 kg/cu m (0.03  Ib/bbl), and
the suspended solids  load  is 0.17 kg/cu m (0.04 Ib/bbl).

              Costs:   Total investment  cost:  $3,687,440
                       Total yearly cost:      $  814,010

An itemized breakdown  of costs is presented  in Table 277.   It is
assumed that land  costs $20,510  per hectare  ($8300  per acre).   It
is further assumed  that six operators are required.

              Reduction Benefits:  BOD:  99.0 percent
                                    SS:  97.3 percent

A cost efficiency  curve is presented in Figure 299 .

Cost  and  Reduction  Benefits of Alternative  Treatment Technologies
for Subcateqorv  A  19  - Malt     ~~~

A model plant representative of  subcategory  A 18 was developed in
Section V for the  purpose  of applying control and treatment alter-
                          1040

-------
   DRAFT
                       TABLE 275

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-XI
                    (OTHER BREWERIES)
ITEMIZED COST SUMMARY FQfir  fcASTEh ATEP-  TREATMENT  CHAIN
DESIGN EFFICIENCY... 96.a  PERCENT  800 REDUCTION
TREATMENT MODULES!
INVESTMENT CCSTSl
               1.
               2.
               3.
               a.
                  PI..CONTROL  HCUSE
                  E1..SCRE6MMG   & GRIT  CHAMBER
                  P...PUMPING  STATION
                  C...EQUALIZATION BASIN
                  F...A.C.TD  NEUTRALIZATION
                  H...NITROGEN  ADDITION
                  K...ACTIVATED  SLUDGE
                  G...SLUDGE THICKENER
                  P...AERCBIC  DIGESTQR
                  T...SAKD  DRYING  BEDS
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
                      31*3100.00
                        icooao.oo
                        P16210.00
                        216210.00
               TOTAL
YEARLY
       OPERATING
               1.
               2.
               3.
               a.
TCTAL YEARLY
CCSTSl
  LABOR
                   CHEMICALS
                   KAINTEMN-CE&SUPPLIES
               TCTAL

             COSTS:
               1. YEARLY OPERATING  COST
               2. YEARLY INVESTMENT
                  CCST RECOVERY
               3. DEPRECIATION
               TCTAu
                                          7^970.00
                                         .54780.00
                       136950.00
                       "01100.00
                                         107760.00
                                         129730.00
                         1041

-------
   DRAFT
                       TABLE 276

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-XII
                    (OTHER BREWERIES)
ITEMIZED COST SUMMARY  FOR  rtASTEMTFR  TREATMENT CHAIN
DESIGN EFFICIENCY... 98.?  PERCENT  BOO REDUCTION
TREATMENT MODULES*
                   81
                   El
                   8.
                   C.
                   F.
                   H.
                   K.
                   Q.
                   R.
                   T.
                   N.
               .CONTROL  HCUSE
               .SCREENING   & GRIT  CHAMBER
               .PUMPING  STATION
               .EQUALIZATION BASIN
               .ACTD  NEUTRALIZATION
               .NITROGEN ADDITION
               .ACTIVATED  SLUDGE
               .SLUDGE. THICKENER
               .AEROBIC  CIGESTCR
               .SAND  DRYING REOS
               .DUAL  MEDIA  PRESSURE  FILTRA'N
INVESTMENT CCSTSi
               1.
               2.
               3.
               a.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
2235490.00
 100040.00
 223550.
 223550.
00
00
               TOTAL
YEARLY
OPERATING
        1,
        2.
        3.
                   LAPC*
                   PCkF>'
                   CHEMICALS
TOTAL YEARLY
        TOTAL

      COSTSt
        i. YEARLY OPERATING COST
        2. YEARLY INVESTMENT
           COST FFCfVFPY
        3. DEPRECIATION
        TOTAL
                                 2782630.00
  7«970.00
 166170.00
  34400.00
 136160.00
 413700.00
                                         413700.00

                                         111310.00
                                         134130.00
                                         6591*10. 00
                          1042

-------
  DRAFT
                       TABLE 277

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A18-XIII
                   (OTHER BREWERIES)
ITEMIZED COST SUMMARY FOP
DESIGN EFFICIENCY.., 99.0
           PERCENT
                                     TREATMENT  CHAIN
                                  800 REDUCTION
TREATMENT MOPULESr
                  PI
                  El
                  P
                  C
                  F
                  H
                  K
                  G.
                  K
                  T
                  N
                  Z.
                     .COMROL HCUSE
                     .SCREENING  & GRIT CHAMBER  '
                     .PUMPING STATION
                     .EQUALIZATION BASIN
                     .ACID WEUTRALIZATICN
                     .NITRPGFN ADDITION
                     .ACTIVATED SLUDGE
                     .SLUDGE THICKENER
                     .AEROBIC CIGE8TOR
                     .SAND DRYING BEDS
                     .DUAL MEDIA PRESSURE  FILTRA'N
                     .ACTIVATED CAPB'ON AB3GRPTICM
INVESTMENT CCSTSS
               1.
               2,
               3,
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
                                       2989500.00
                                         100040,00
                                         298950.00
                                         298950.00
                                       3667JUI0.60
YEARLY OPERATING COSTS!
               1.  LABOR
               ?.  POWER
               3.  CHEMICALS
               H.  MAlNTFMMCtaSlPPLIES
               TOTAL
                                          74970.00
                                         190530.00
                                          34400.00
                                         187240.00
                                         407160.00
TOTAL YFARLY
             COSTSi
               1. YEARLY CPERATING COST  467l«0.00
               2. YEARLY INVESTMENT
                  COST RECOVERY          147500.00
               3. DEPRECIATION           179370.00
               TCTAL                     814010.00
                        1043

-------
O
-P»
-p.
       §
       s
       I
       u
            JleS.C I

            9-3.3 !
            6J«.3 I
                                                   EFFICIENCY
                                                                         «?.ec     st.oo
                                                                                                153.CJ
                                             FIGURE  299



                  INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 18, ALTERNATIVE XIII

-------
   DRAFT
 natives.  In Section VII, seven alternatives were selected as being
 applicable engineering alternatives.  These alternatives provide
 for various levels of waste reductions for the model plant which
 produces 350 kkg (16,000 bu) per day.

 Alternative A 19-1 - This alternative assumes no treatment and no re-
 duction in the waste load.  It is estimated that the effluent from
 a 350 kkg (16,000 bu) per day plant is 2590 cu m (0.685 MG) per day.
 The BOD waste load is 4.55 kg/kkg (0.218 Ib/bu), and the suspended
 solids load is 0.77 kg/kkg (0.037 Ib/bu).

 Suspended solids in the waste, consisting mostly of grain and sprouts,
 are assumed to be removed by screening prior to discharge.

               Costs:               0
               Reduction Benefits:  None

 Alternative A 19-11 - This alternative provides a control house, flow
 equalization, nutrient addition, and an aerated lagoon system.

 The resulting BOD waste load is 0.22 kg/kkg (0.011 Ib/bu), and the
 suspended solids load is 0.13 kg/kkg (0.0062 Ib/bu).

              Costs:  Total investment cost:  $1,200,150
                      Total yearly cost:      $  572,660

An itemized breakdown of costs is presented in Table 278.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

Suspended solids in the waste, consisting mostly of grain and sprouts,
is assumed to be removed by screening prior to discharge.

              Reduction Benefits:  BOD:  95.2 percent
                                    SS:  83.1 percent

Alternative A 19-111 - This alternative provides in addition to
Alternative A 19-11 dual media filtration.

The resulting BOD waste load is 0.11  kg/kkg (0.0053 Ib/bu), and
the suspended solids load is 0.06 kg/kkg (0.0029 Ib/bu).

              Costs:  Total investment cost:  $1,245,740
                      Total yearly cost:      $  583,300

An itemized breakdown of costs is presented in Table 279.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that two operators are required.

Suspended solids in the waste, consisting mostly of grain and sprouts,
is assumed to be removed by screening prior to discharge.


                            1045

-------
   DRAFT
                       TABLE  278

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A19-II
                         (MALT)
 ITEMIZED  COST  SUMMARY FOR MSTEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY,..  95.1 PERCENT BOD REDUCTION
 TREATMENT  MODUlESi
                   PI..CONTROL  HCLSE
                   B...PUMPING  STATION
                   C...EQUALIZATION BASIN
                   H...NITROGEN ADDITION
                   L.., AERATED  LAGOON
INVESTMENT CCSTSt
                1.
                2.
                3.
                a.
                5.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC LINf-R
                        959690.00
                         12740.00
                        95970.
                        95970.
       00
       00
               TOTAL
                        35780.00
                       1200150.00
YEARLY
OPERATING
        1.
        2.
        3.
        4.
        5.
COSTS!
  LABOR
  POWER
  CHEMICALS
  MAINTENAMCERSL'PPLIES
  PVC LINFR
                                          24990,
                                         401540,
                                           3030,
                                          3^080,
       00
       00
       00
       00
               TOTAL
  16«0,00
^65280.00
TOTAL YEARLY CCSTS:
               1. YEARLY OPERATING COST 465280.00
               2. YEARLY INVESTMENT
                  COST RECOVFPY          mio.oo
               3. DEPRECIATION           59370.00
               TGTAL                    572660.00
                         1046

-------
  DRAFT
                      TABLE 279

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A19-III
                       (MALT)
ITEMIZED COST SUMMARY FOR WASTEHTER TREATMENT CHAIN
DESIGN EFFICIENCY... 97.5 PERCENT BOD REDUCTION
TREATMENT MODULES!
                  Bi..CONTROL HCLSE
                  8...PUMPING STATION
                  C...EQUALIZATION BASIN
                  H...NITROGEN ADDITION
                  • L... AERATED LAGOON
                  6...PUMPING STATION
                  N...DUAL MEDIA PRESSURE  FILTRA'N
INVESTMENT COSTS!
               1.
               2.
               3.
               4.
               5.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC LINER
                       997&80.00
                        12740.00
                        99770.
                        99770.
       00
       00
               TOTAL
                        35780.00
                      1245740.00
YEARLY
OPERATING
        1.
        2.
        3.
        4.
        5.
CCSTSj
  LABOR
  POWER
  CHEMICALS
  MINTENANCE&SUPPLIES
  PVC LINER
               TOTAL
 249CQ.OO
407450.00
  3030.00
 34710.00
  1640.00
471820.00
TOTAL YEARLY CCSTSt
                i. YEARLY OPERATING  COST  471820,00
                2. YEARLY INVESTMENT
                  COST  RECOVERY           49630.00
                3. DEPRECIATION            61650.00
                TOTAL                     583300.00
                        1047

-------
   DRAFT
              Reduction Benefits:  BOD:  97.6 percent
                                    SS:  92.2 percent

A cost efficiency curve is presented in Figure 300.

Alternative A 19-IV - This alternative provides a control  house, flow
equalization, nutrient addition, a complete mix activated  sludge
system, sludge thickening, aerobic digestion, and spray irrigation.

The resulting BOD waste load is 0.22 kg/kkg (0.011 Ib/bu), and the
suspended solids load is 0.13 kg/kkg (0.0062 Ib/bu).

              Costs:  Total investment cost:  $709,240
                      Total yearly cost:       $176,410

An itemized breakdown of costs is presented in Table280.   it is
assumed that land costs $41,000 per hectare ($16,600  per acre).  It
is further assumed that three operators are required.

Suspended solids in the waste, consisting mostly of grain  and sprouts,
is assumed to be removed by screening prior to discharge.

              Reduction Benefits:  BOD:  95.2 percent
                                    SS:  83.1  percent

Alternative A 19-V - This alternative adds dual media filtration to
Alternative A 19-IV.

The resulting BOD waste load is 0.11 kg/kkg (0.0053 Ib/bu), and the
suspended solids load is 0.06 kg/kkg (0.0029 Ib/bu).

              Costs:  Total investment cost:  $761,830
                      Total yearly cost:       $187,330

An itemized breakdown of costs is presented in Table  281.   It is
assumed that land costs $41,000 per hectare ($16,600  per acre).  It
is further assumed that three operators are required.

Suspended solids in the waste, consisting mostly of grain  and sprouts,
is assumed to be removed by screening prior to discharge.

              Reduction Benefits:  BOD:  97.6 percent
                                    SS:  92.2 percent

A cost efficiency curve is presented in Figure 301 .

Alternative A 19-VI - This alternative replaces spray irrigation of
sludge in Alternative A 19-IV with sand bed drying.

The resulting BOD waste load is 0.22 kg/kkg (0.011 Ib/bu), and the
suspended solids load is 0.13 kg/kkg (0.0062 Ib/bu).
                             1048

-------
8
            1176.5
       b
       CO
       tn
       8
       LJ    *i\.t


       O
                                                                                                                       O
                                                                                                                       TO
                                                                                                                       f*
                  -:.;:     «i.:c     «?.•:?    <;j.:c     «i.::    <«.::     «».;;     <7.cc     
-------
    DRAFT
                        TABLE 280

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A19-IV
                         (MALT)
ITEMIZED COST SUMMARY FOR «ASTFiUTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 95.1. PERCENT  BCD  REDUCTION
TREATMENT MODULES!
                  ei
                  R.
                  C.
             ..CONTROL
             ..PUMPING
               HOUSE
               STATION
      .EQUALIZATION BASIN
   H...NITROGEN ADDITION
   K... ACTIVATED SLUDGE
   G...SLUDGE THICKENER
   R...AEROBIC DIGESTOR
   Y...HOLDING TANK
   U...SPRAY IRRIGATION
INVESTMENT COSTS?
               1.
               2.
               3.
               a.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY,
                         562570,
                          34150,
                          56260,
               TOTAL
YEARLY
OPERATING
        1.
        2.
        3.
  COSTS!
    LABOR
    CHEMICALS
4.  MAJNTENANCERSLPPLIES
TOTAL
TOTAL YEARLY
               TOTAL
00
00
00
                          56260,00
                         709240.00
                                          37480.
                                          62790.
                                           3030.
                                          10990.
00
00
00
00
                                         1H290.00
      COSTS*
        1. YEARLY OPERATING COST  114290.00
        2. YEARLY INVESTMENT
           COST RECOVERY           28370.00
        3. DEPRECIATION            33750.00
                                  176410.00
                       1050

-------
    DRAFT
                         TABLE 281

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A19-V
                          (MALT)
ITEMIZED COST SLMMARY FOR WASTEMTER TREATMENT  CHAIN
DESIGN EFFICIENCY... 97.5 PERCENT 800 REDUCTION
TREATMENT
                  BI
                  e.
                  c.
                  H9
                  K.
                  Y.
                  U.
                  s.
                  N.
                     .CONTROL  HCLSE
                     .PUMPING  STATION
                     .EQUALIZATION BA8IN
                     .NITROGEN ADDITION
                     .ACTIVATED SLUDGE
                     .SLUDGE THICKENER
                     .AERCPIC  DIGESTOR
                     .HOLDING  TANK
                     .SPRAY IRRIGATION
                     .PUMPING  STATION
                     .DUAL. MEDIA PRESSURE PILTRA'N
INVESTMENT
           CC8TSI
                1.
                2.
                3.
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TCTAL
YEARLY OPERATING COSTSt
                1.  LABOR
                2.  POfcFR
                3.  CHEMICALS
                a,  MAINTENANCE&SUPPLIE3
                TCTAL
                                        600560.00
                                         41150.00
                                         60060.00
                                         60060.00
                                        761830.00
                                         37060.00
                                         66700.00
                                           3030.00
                                         11620.00
                                         120630.00
TCTAL YEARLY CCSTS8
                1.  YEARLY  OPERATING  COST  120830.00
                2.  YEARLY  INVESTMENT
                   COST  RECOVERY           30«70.00
                3.  DEPRECIATION            36030.00
                TCTAL                     187330.00
                           1051

-------
o
en
ro
>-


>-
      i e s. C
                 OlC.tt
                 JSl.S
           o


           _l
                      .        .        .       .       .        .        .       .        .

                                                        EFFICIENCY



                                                 FIGURE 301



                      INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 19, ALTERNATIVE V
                                                                                             ««.C6    10C.CS

-------
   DRAFT
              Costs:  Total  investment cost:  $971,480
                      Total  yearly cost:      $229,830

An  itemized breakdown of costs  is presented in Table 282.  It is
assumed  that  land  costs $41,000 per hectare ($16,600 per acre).  It
is  further assumed that three operators are required.

Suspended solids in the waste,  consisting mostly of grain and sprouts,
is  assumed to be removed by  screening prior to discharge.

              Reduction Benefits:  BOD:  95.2 percent
                                    SS:  83.1 percent

Alternative A 19-VII - This  alternative adds dual media filtration to
Alternative A 19-VI.

The resulting BOD  waste load is 0.11 kg/kkg (0.0053 Ib/bu), and the
suspended solids load is 0.06 kg/kkg (0.0029 Ib/bu).

              Costs:  Total  investment cost:  $1,017,070
                      Total  yearly cost:       $ 240,470

An  itemized breakdown of costs  is presented in Table 283.  It is
assumed  that  land  costs $41,000 per hectare ($16,600 per acre).  It
is  further assumed that three operators are required.

Suspended solids in the waste,  consisting mostly of grain and sprouts,
is  assumed to be removed by  screening prior to discharge.

              Reduction Benefits:  BOD:  97.6 percent
                                    SS:  92.2 percent

A cost efficiency curve is presented in Figure 302.

Cost and Reduction  Benefits  of  Alternative Treatment Technologies
for Subcategorv A  20 - Wineries Without Stills

A model plant representative of subcategory A 20 was developed in
Section V for the purpose of applying control  and treatment alter-
natives.   In Section VII, ten alternatives were selected as being
applicable engineering alternatives.   These alternatives provide
for various levels  of waste reductions  for the model  plant which
processes 180 kkg (200 tons) of grapes  per day during crushing,
and produces 41  cu  m (10,800 gal)  per day during processing.   Since
the treatment system was sized on  crushing season design values, those
are the costs which will  be presented.
The following process operations are assumed for the model  plant:
(1)  stems are considered a solid waste to be spread on vineyard
property,(2) pressed pomace may be used for distilling material,
                             1053

-------
DRAFT
                      TABLE  282

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A19-VI
                       (MALT)
ITEMIZED COST SUMMARY FOR MSTEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 95.1 PERCENT BOD  REDUCTION
TREATMENT MODULES}
                  Bl
                  B.
                  C.
                  H.
                  K.
                  Q.
                  R.
                  Y.
                  T.
  .CONTROL HCLSE
  .PUMPING STATION
  .EQUALIZATION BASIN
  .NITROGEN ADDITION
  .ACTIVATED SLUDGE
  .SLUDGE THICKENER
  .AEROBIC DIGESTCR
  .HOLDING TANK
  .SAND DRYING BEDS
INVESTMENT CCSTSl
               1.
               2.
               3.
               4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
               TOTAL

YEARLY OPERATING COSTSJ
               1.  LABOH
               2.  POER
               3.  CHEMICALS
               4.  MAINTENANCE&SUPPLIES
               TOTAL

TOTAL YEARLY COSTS!
               1. YEARLY OPERATING COST
               2. YEARLY INVESTMENT
                  COST RECOVERY
               3. DEPRECIATION
               TOTAL
775270.00
 41150.00
 77530.00
 77530.00
971480.00
                      37480.00
                      61920.00
                       3030.00
                      42020.00
                     144450.00
                     144450.00

                      36860.00
                      46520.00
                     229830.00
                         1054

-------
 DRAFT
                       TABLE 283

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A19-VII
                        (MALT)
ITEMIZED COST SUMMARY FOR WASTEWATER TREATMENT CHAIN
DESIGN EFFICIENCY... 97.5 PERCENT BOD REDUCTION
TREATMENT MODULESi
                  Bl
                  B.
                  C.
                  H.
                  K.
                  Q.
                  R.
                  Y.
                  T.
                  B.
                  N.
  .CONTROL HOUSE
  .PUMPING STATION
  .EQUALIZATION BASIN
  .NITROGEN ADDITION
  .ACTIVATED SLUDGE
  .SLUDGE THICKENER
  .AEROBIC DIGESTOR
  .HOLDING TANK
  .SAND DRYING BEDS
  .PUMPING STATION
  .DUAL MEDIA PRESSURE FILTRA'N
INVESTMENT COSTSl
               1.
               2.
               3.
               4.
CONSTRUCTION
ENGINEERING
CONTINGENCY
               TOTAL

YEARLY OPERATING COSTS*
 613360.00
  41150,00
  61330.00
  81330.00
1017070.00
               1.  LABOR                  37460.00
               2.  POWER                  67830.00
               3.  CHEMICALS               3030.00
               4.  MAINTENANCE&SUPPLIES   42650.00
               TOTAL                     150990.00

TOTAL YEARLY COSTSl
               1. YEARLY OPERATING  COST  150990.00
               2. YEARLY INVESTMENT
                  COST  RECOVERY           40680.00
               3. DEPRECIATION            48800.00
               TOTAL                     240470,00
                         1055

-------
o
en
              1 5 1 S . C
            u.
            o
               7f2.il
            W)

            8
               313.6
               6«>5.7
            i
            1-  307.'
                                            «5.ec
                                                                     «6.ce
                                                        EFFICIENCY




                                                 FIGURE 302




                     INVESTMENT  AND YEARLY COSTS FOR SUBCATEGORY A  19,  ALTERNATIVE VII
                                                                                                      10C.CC

-------
 DRAFT
may be spread on"vineyard property, or'may be recbverecTas a by-product
(3) diatomaceous earth (spent filter aid) is considered to be a solid
waste to be spread on vineyard property, (4) no distillation is done
on the premises, and (5) wastewater is screened prior to discharge.
Alternative A 20-1 - This alternative assumes no treatment and no re-
duction in the waste load.  It is estimated that the effluent from a
180 kkg (200.0 ton) per day plant is 276 cu m (0.073 MG) per day.
The BOD waste load is. 3.57 kg/kkg (7.14 Ib/ton), and the suspended
solids load is 1.16 kg/kkg (2.32 Ib/ton).
              Costs:               0
              Reduction Benefits:  None

Alternative A 20-11 - This alternative provides a control house, flow
equalization, nutrient addition, neutralization, a complete mix
activated sludge system, sludge thickening, aerobic digestion, dual
media filtration, and spray irrigation of sludge.

The resulting BOD waste load is 0.77 kg/kkg (1.54 Ib/ton), and the
suspended solids load is 0.115 kg/kkg (0.230 Ib/ton).

              Costs:  Total investment cost:  $414,130
                      Total yearly cost:       $116,400

An itemized breakdown of costs is presented in Table 284 .  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.
              Reduction Benefits:  BOD:  97.8 percent
                                    SS:  90.1 percent

Alternative A 20-III - This alternative adds dual media filtration to
Alternative A 20-11.

The resulting BOD waste load is 0.38 kg/kkg (0.76 Ib/ton), and the
suspended solids load is 0.0540 kg/kkg (0.108 Ib/ton).

              Costs:  Total investment cost:  $434,350
                      Total yearly cost:      $122,300

An itemized breakdown of costs is presented in Table  285.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.
              Reduction Benefits  BOD:  98.9 percent
                                   SS:  95.3 percent
                            1057

-------
 DRAFT
                       TABLE 284

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A 20-11
                (WINERIES WITHOUT STILLS)
ITEMIZED COST SUMMARY Fl'R  M.STEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY,.. 97.fi  PERCENT  BOD REDUCTION
TREATMENT MODULES:
INVESTMENT COSTS*
                1.
                i»
                3.
                  B3
                  B.
                  C.
                  H.
                  I.
                  F.
                  G.
                  K.
                  0.
                  H.
                  Y.
                  U.
                  N'
   CONTROL HCLSE
   PUMP.IK'S S If A TICK
   EQUALIZATION BASIN
   NITROGEN ACDITIC*
   PHCSPHCRLS ADDITION
   ACID NFtTRiLIZATTO
   CALSTIC NEUTRALIZATION
   ACTIVATED SLUDGE
   SLUDGE THICKENER
   AfcROBIC DIGESTOR
   HOLDING TANK
   SPRAV IRRIGATION
   DUAt Kf-DIA PRESSURE
LAND
ENGINEERING
CCNTIKRFNCY.
                TOTAL
331230.00
 16660.00
 33120.00
 33120.00
MM30.00
YEARLY OPERATING CUSTS:
                1.   LABOR                  37480.00
                2.   POWEB                  2?510.00
                3.   CHEMICALS               7530.00
                a.   MAlNTENANCEaStPPLIES   ^auo.OO
                TOTAL                      79960.00

TOTAL YEARLV CC9TS:
                i.  YEARLY  OPERATING COST  79960.00
                2.  YEARLY  INVESTMENT
                   COST  RECOVERY           16570.00
                3.  DEPRECTATIOK            19870.00
                TOTAL                     116«OC.OO
                         1058

-------
DRAFT
                      TABLE 285

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A 20-111
               (WINERIES WITHOUT STILLS)
 ITEMIZED  COST  SUMMARY FDR foASTEMTFP TREATMENT CHAIN
 DESIGN  EFFICIENCY,.,  98.Q PERCENT BOD REDUCTION
TREATMENT  MODULES!
                   ei
                   8
                   c
                   H
                   I
                   F
                   G
                   K
                   Q
                   R
                   Y
                   I,
                   M
                   \
                    ..CGMfiOL  HCI..SF
                    ..PL^'KP-G  STATION
                    ..EQl ALIZATIO BASIN
                    ..NITRC'GFN  ADDITION
                    ..PHOSPHORUS  ADD!
                    ..ACID NEUTRALIZATION
                    ..CAUSTIC  NEUTRALIZATION
                    ..ACTIVATED  SLUDGE
                    ..SLUDGE THICKENER
                    ..AEROBIC  DIGESTOR
                    ..HOLDING  TANK
                    ..SPF.AY  IRRIGATION
                    ..HUH KFDIA  PRESSLRF.  FILTRA'N
                    ..DUAL I^CIA  PRESSURE  FXLTRAU-
 INVESTMENT  CCSTSi
                1.
                   CCNSTRICTICN
               ?..  LAND
               3.  ENGINEERING
               4.  CONTINGENCY
               TCTAL

YEARLY OPERATING CCSTS:
               1.  LABOR
               2.  FOFP

               H.  MAINTEN'AMCF.&SLPPLIES
               TOTAL

TCTAL YEARLY CCSTSi
               1. YEARLY CPFPATIK6  CCST
               2. YEARLY INVESTMENT
                  CCST r.ECCVEPY
               3.
               TCTAL
     ,00
    )0.00
34810,00
                                          ?6830.00
                                           7530.00
                                          10210.00
                                          84050.00
                                          64050.00

                                          17370.00
                                          20880.00
                                         122300.00
                        1059

-------
  DRAFT
 Alternative A 20-IV - This alternative provides in addition "to Alter-
 native A 20-1II activated carbon.

 The resulting BOD waste load is 0.23 kg/kkg (0.46 Ib/ton),  and the
 suspended solids load is 0.031  kg/kkg (0.062 Ib/ton).

               Costs:   Total  investment cost:  $502,200
                       Total  yearly cost:       $146,770

 An itemized breakdown of costs  is  presented in Table 286.  It  is
 assumed that land costs $41,000 per hectare ($16,600 per acre).  It
 is further assumed that three operators are required.
               Reduction  Benefits   BOD:  99.4  percent
                                    SS:  97.3  percent

 A cost efficiency  curve  is  presented  in Figure 303.

 Alternative  A  20-V - This alternative replaces spray irrigation of sludge
 in Alternative A 20-11 with  sand drying beds.

 The resulting  BOD  waste  load  is 0.77  kg/kkg (1.54 Ib/ton), and the
 suspended  solids load is 0.115 kg/kkg (0.230  Ib/ton).

               Costs:  Total  investment cost:  $492,450
                      Total yearly  cost:      $134,160

 An itemized  breakdown of costs is presented in Table 287.  It is
 assumed that land  costs $41,000perhectare ($16,600 per acre).  It is
 further assumed that three operators are required.
             " Reduction Benefits  BOD:   97.8 percent
                                   SS:   90.1 percent

Alternative A 20-VI - This alternative provides in addition to Alter-
native A 20-V dual media filtration.

The resulting BOD waste load is 0.38  kg/kkg (0.76 Ib/ton),  and the
suspended solids load is 0.054 kg/kkg (0.108 Ib/ton).

              Costs:   Total  investment cost:  $512,680
                      Total  yearly cost:      $140,070

An itemized breakdown of costs is presented in Table 288.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.
              Reduction Benefits  BOD:  98.9 percent
                                   SS:  95.3 percent
                            1060

-------
DRAFT
                      TABLE 286

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A 20-IV
               (WINERIES WITHOUT STILLS)
  ITEMIZED  COST  SUMMARY' P«JB ^ASTEMTEP TREATMENT CHAIN
  DESIGN  EFFICIENCY...  99.3 PERCENT BOO REDUCTION
  TREATMENT  MODULES:
Pi . .eriMROL HOUSE
B...PULPING STATION
C. ,,EQUALIZATION BASIN
H,.,NITWCGEN ADDITION
I. ,. PHOSPHORUS ADDITION
F...ACID NEUTRALIZATION
G...CAUSTIC NEUTRALIZATION
K.
CO
R...AEP08IC OIGESTC*
V...HOLDING TANK
U...SPRAY IRRIGATION
N...DU«L MF.DIA PRESSURE
                      ..ACTIVATED SLUDGE
                     ...9LLDGE THICKENER
                    N...DU4U  MEDIA  PRESSURE
                       FILTPA'N
                       FILTRA'N
 INVESTMENT CCSTS!
                 1.
                 2.
                 3.
                 a.
                    2...ACTIVATED  CARBCN  ADSCRPTION
CONSTRUCTION
LAND
ENGINEERING
CCNTINQP.NCY
                 TOTAL

 YEARLY OPERATING CCSTSi
                 i.  LABOR
                 2.  FO^F^
                 3,  CHEMICALS
                 4.  MAINTENANCF&SLPPLIES
                 TOTAL
                            .00
                       16660.00
                       ^0^60.00
                       40460.00
                      502300.00
                      37460.00
                      31770.00
                       753C.OO
                      25620.00
                     102400.00
 TOTAL YEARUY COSTS!
                1. YEARLY OPERATING  COST  102400.00
                2. YEARLY INVESTMENT
                   COST RECOVERY           20090.00
                3. DEPRECIATION            24280.00
                TOTAL                     146770.00
                        1061

-------
                501.0
"•^



§

U.
O

(f)

i
                «...
                36*.
                                                                                                                              a
                                                                                                                              po
                                                                                                                              3=«
O

no
          -
                232.1
                Ile.C

                             ll.Cf    «i.CC     «3. CC     
-------
DRAFT
                      TABLE 287

             ITEMIZED COST SUMMARY FOR ALTERNATIVE A 20-V
                      (WINERIES WITHOUT STILLS)
          COST SL^CASY  FPP  •«A.<3TF'*ATtrP TREATMENT
 DESIGN EFFICIENCY. .. «7.P  FF.RCFNT  8CR REDUCTION

 TREATMENT MODULES:
                    eU.r.C^TPOL  WCL8F
                    P...PULPING  STATION'
                    C...cC"..ALI7»TKN PA5U
                    I", . .NilTKCGFN  APDITION'
                    I.. .PHCS^HHRLS  ADDITION
                    F...ACTD  NFLTRAI.IZATION
                    C-...rALSTK  NELTRALIZATICN
                    "...ACTIVATED  SLUDGE
                    0,..?LLCGe  THICKENER
                    P...AF.PCflir  OICFS1CR
                    T...RASD  DRYING  BEDS
                    N...nUAL.  MFCIA  PRESSURE FILTRA'I

 INVESTMENT CCSTS!
                1.   CCN'ST^UCTICN          393720.00
                •( t   LANn                   19990.00
                3.   eMPTKEEPIMG            39370.00
                a.   CCMTINGENCV            35370.00
 YEAPLY CPEPATINfG COSTS?
                1.  LABOR                  37^480.00
                2.  PO'FP                  2«6*0.00
                3.  CHEMICAL'S               7530.00
                «.  HAINTf-NANCFlSLPPLlES  21170.00
                TCTAL
 TOTAL  YEARLY CCSTSJ
                1. YEARLY CPEHATJNG  CCST  906^0.00
                2 . Y F. 4 P L v T N V F S T M F N T
                   CGST PFCOVFRY           19700.00
                3. C'r0RFCT ATITN            23620.00
                TCT^L                     13«160.00
                        1063

-------
DRAFT
                       TABLE 288   '

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A 20-VI
                (WINERIES WITHOUT STILLS)
       Z F P COST 81 ^ K A P Y  r > c  wASTFMTEH TBEA7VFM  CM IN
  PESIGN FFFICTENCY...  ^F.9  PPRCEM BOH KECl-C

  TREATMENT MCDlLESt
                     r . . . F <"J I U I 7 A T I r N M 5 I *
                     H. ,.N'TT«rjGEN ACOTITO'^
                     I. ..PHfSPHnpi, .{. ACCITICN
                     ^...M.TC NFLTP4LTZATIT.K
                     G...CALST1C NEIT&AL1ZATICN
                     K,..ACTTVATEC SLLOC-E
                     T...8AND D»YINP FEDS
                              KEDIA PRESSURE
                                  A FPESSLhE
  INVESTMENT CTSTSl
                  1.   CTNSTRlJCTTCN          'J10570.00
                  2.   LAND                   19990.00
                  3.
                                             41060.00
                  TCTAL                      5
  YEARLY OPERATING
                  1.   LABCM                  37a?O.OP
                  2.   FG»»IFR                  27980.00
                  3.   C H E * I'C * I f               7530.00
                  4.   f-ATNJTEVANCE8SLPpLTES   21940.00
                  TCTAL                       94930.00

  TCTAL VEA»Ly  CCSTc.
                  1,  YEARLY CFFPATIKC- CCS^   °i'930.0f>
                  c.  V&ARIY INV(-'ST^FNT
                     CCST  RECCVFKV           '0510.OH
                  3,  PFPRFCTATIPK-            24630.00
                  TTTM                      U007G.OO
                         1064

-------
  DRAFT
 Alternative A 20-VII - This alternative adds activated carbon to
 Alternative A 20-VI.

 The resulting BOD waste load is 0.23 kg/kkg (0.46 Ib/ton), and the
 suspended solids load is 0.031 kg/kkg (0.062 Ib/ton).

               Costs:  Total investment cost:  $580,520
                       Total yearly cost:      $164,530

 An itemized breakdown of costs is presented in Table 289.   It is
 assumed that land, costs $41,000 per hectare ($16,600 per acre).   It
 is further assumed that three operators are required.
               Reduction Benefits  BOD:  99.4 percent
                                    SS:  97.3 percent

 A cost efficiency curve is presented in Figure 304.

 Alternative A 20^VlTl  -  This  alternative provides  flow equalization,
 nutrient addition,  neutralization,  an  aerated  lagoon  system,  and  dual
 media filtration.

 The  resulting BOD waste  load  is 0.77  kg/kkg  (1.54  Ib/ton),  and  the
 suspended solids load  is 0.115 kg/kkg  (0.230 Ib/ton).

               Costs:   Total  investment cost:  $413,090
                       Total yearly cost:       $172,300

 An itemized breakdown  of costs is presented  in Table290.   It  is
 assumed that land  costs  $4100 per hectare  ($1660 per  acre).   It is
 further assumed that one operator is  required.
              Reduction Benefits  BOD:  97.8 percent
                                   SS:  90.1 percent

Alternative A 20-IX - This alternative provides in addition to Alter-
native A 20-VIII dual media filtration.

The resulting BOD waste load is 0.38 kg/kkg (0.76 Ib/ton), and the
suspended solids load is 0.054 kg/kkg (0.108 Ib/ton).

              Costs:  Total investment cost:  $433,290
                      Total yearly cost:      $178,210

An itemized breakdown of costs is presented in Table 291,  It is
assumed that land costs $4100 per hectare ($1660 per acre).   It is
further assumed that one operator is required.
              Reduction Benefits  BOD:  98.9 percent
                                   SS:  95.3 percent
                             1065

-------
DRAFT
                      TABLE 289

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A 20-VII
                  (WINERIES WITHOUT STILLS)
 ITEMIZED COST SLMMARY FOR WASTEMTER TREATMENT CHAIN
 DESIGN EFFICIENCY... 90.3 PERCENT BCD REDUCTION
 TREATMENT MODULES!
 INVESTMENT CCSTSl
                1.
                2.
                3.
                a.
                   Bi. .CONTROL HOUSE
                   8...PULPING STATTCN
                   C...FQLALIZATICN BASIN
                   H...NITROGEN ADDITION
                   I...PHOSPHORUS ADDITION
                   F...ACID NEUTRALIZATION
                   G...CAUSTIC NEUTRALIZATION
                   K...ACTIVATED SLUDGE
                   G...5LUOGE THICKENER
                   R...AERCBTC CIGESTOR
                   T...SAND DRYING BEDS
                   N...DUAL MFrjA PRESSURE FILTRA'N
                   N...DU*L MEDIA PRESSURE FILTRA'N
                   Z...ACTIVATED CARBON ADSORPTION.
            CCN3TRLCTICN1
            LAND
            ENGINEERING
            CONTINGENCY
                TOTAL
467110.00
 19990.00
 «6710.00
 46710.00
S80520.OP
 YEARLY
OPERATING
        1.
 TOTAL  YEARLY
    COSTS?
      LAPOP
  2.  POWER
  3.  CHEMICALS
  4.  MAINTFNANCERSUPPLIES
  TOTAL

CCSTSl
  1. YEARLY OPERATING COST
  2. YEARLY INVESTMENT
     COST RECOVERY
  3. DEPRECIATION
  TOTAL
                                          37460.
                                          30930.
       00
       00
                                           7530.00
                                          37340.00
                                         113280.00
                                         113280.00
                                                .00
                                          28030.00
                                         364530.00
                        1066

-------
fc

I
<
D
t-t'


CO
o
u
     «>^.J
                                                                                                           O

                                                                                                           73
u
     13-.0

                                                                          It.r.S
                                                                                    .CO    1CS.CS
                                         FIGURE  304


             INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A  20,  ALTERNATIVE VII

-------
DRAFT
                        TABLE 290

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A 20-VIII
                   (WINERIES WITHOUT STILLS)
  ITEMIZED COST SUMMARY FDR MSTFMTFR  TREATMENT  CHAIN.*
  DESIGN EFFICIENCY. .. 97.P PERCFNT 80P "EDUCTION
  TREATMENT
                    R... PUMPING STATION
                    C...PQLALI7ATICN BASIN
                    H...NITROGEN ADDITION
                    I...PHCSPHORLS ADDITION
                    F...ACTO NEUTRALIZATION
                    G...CAUSTIC NEITRALIZATICN •
                    L ...AERATED LAGCGN
                    N...OUAL HFDIA PRESSURE FILT«A.'N
INVESTMENT
             CCSTSI
                 i.
                 2.
                 3.
                   CCNSTRUCTTCK
               5.  PVC
               TOTAL
                         LINER
333^80,
  "330,
 33350,
 33350,
YEARLY OPERATING I
               1.
               2 •
               3.
               «.
               5.
                     LAROR
                     CHEMICALS
                     KAINTF.MNCERSIPPLTES
                     PVC  LINER
                 TCTAL
                3.
                TCTAL
                                                00
                                                00
                                                00
                                                00
  8580.00
       00
       00
       00
       on
       oo
                                          12490.
                                         102900.
                                          7530.
                                          12230
                                            190
                                         135340.00
 TOTAL YEARLY CCSTSI
                 i.  YEARLY  OPERATING  COST 1353^0.00
                 2.  YEARLY  INVESTMENT
                         OECCVERY         .  16520.00
                                        172300.00
                          1068

-------
DRAFT
                         TABLE 291

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A 20-IX
                    (WINERIES WITHOUT STILLS)
       ZFD COST  SUMMARY  FOR  MSTF.MTEP TREATMENT CHAIN
  DESIGN EFFICIENCY...  98. li  PFRCPN'T 300 REDUCTION
  TREATMENT MODULE?:
                     B. ,.Pl.'^F-ING STATION
                     C...EULAL17ATICN 8ASIK-
                     H...NITHPGEK APCITION
                     I...PHCSPHDRLS ADDITION
                     F...ACIO  NFUTRALI2ATICN
                     G...CALSTIC WELTRALIZATICN
L... AERATED
^...^UAL NJF
N...nUAL
             LAPOCN
             IA FRFSSbPE
             IA PRESSURE
                                             FJLTPA«N
                                             FILTRA'M
             CCSTS:
                  i.
                  2.
                  3.
                  a.
                  5.
  COSTP'JCTIO1
  LAM])
  EKGJMEER1NG
  CC•^iTI^:GF^'^Y
  PVC LTNKR
                       350320.00
                        4330.00
                       35030.00
                       35030
                        85PO
                                         00
                                         00
                 TCTAL
  YEARLY
OPERATING
        1.
        2.
        3.

        s!
CCSTS:
  LAE-OR
                     CHEMICALS
                     KATJTEMANCE&SLPPLIES
                     PVC  UTNFR
                 TCTAL
                        433290.00
                        124
-------
   DRAFT


   Alternative A 20-X - This alternative provides in addition to Alter-
   native A 20-IX activated carbon.

The resulting BOD waste 'load is 0.23 kg/kkg (0.46 Ib/ton), and the
suspended solids load is 0.031 kg/kkg (0.062 Ib/ton).

               Costs:  Total investment cost:  $501,160
                       Total yearly cost:      $202,670

An itemized breakdown of costs is presented in Table 292.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one operator is required.
               Reduction Benefits:  BOD:  99.4 percent
                                     SS:  97.3 percent

A cost efficiency curve is presented in Figure 305.

Cost and Reduction Benefits of Alternative Treatment Technologies for
Subcategory A 21 - Wineries with Stills

A model plant representative of Subcategory A 21  was developed in Section
V for the purpose of applying control  and treatment alternatives.  In
Section VII, two alternatives were selected as being applicable engi-
neering alternatives.  These alternatives provide for various levels
of waste reductions for the model  plant which processes 700 kkg (760 ton)
of grapes per day.

Alternative A 21-1 - This alternative  assumes no  treatment and no reduction
in the waste load.  It is estimated that the effluent from a 700 kkg
(760 ton) per day plant is 1700 cu m (0.442 MG)  per day.   The BOD waste
load is 13.9 kg/kkg (27.7 Ib/ton), and the suspended solids load is
13.6 kg/kkg (27.3 Ib/ton).

               Costs:               0
               Reduction Benefits:  None

Alternative A 21-11 - This alternative consists of a holding tank, pumping
station, pipeline, and land spreading.

The resulting BOD waste load is zero,  and the suspended solids load is
zero.

               Costs:  Total  investment cost:  $381,640
                       Total  yearly cost:      $  52,310
                              1070

-------
DRAFT
                        TABLE 292

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A 20-X
                    (WINERIES WITHOUT STILLS)
  ITEMIZFD COST  SUMMARY  FOR  MSTEMTFR TREATMENT CHAIN
  DESIGN EFFICIENCY...  9Q.3  PERCENT BOD REDUCTION
  TREATMENT  MODULES!
                     G
                     L
                     2.
                     .PUMPING STATION
                     .EQUALIZATION BASIN
                     .NITROGEN- ADDITION
                     .PHOSPHORUS ADDITION
                     .ACID NEUTRALIZATION
                     .CAUSTIC NEUTRALIZATION
                     .AERATED LAGCON
                     .nuAL MEDIA PRESSURE  FILTRA'N
                     .DUAL MEDIA PRESSURE  FILTRA'N
                     .ACTIVATED TARPON ADSORPTION
  INVESTMENT  CCSTSt
                  1.
                  2.
                  3.
                  4.
                  s.
                   CONSTRUCTION
                   LAND
                   CCNTINGFNCY
                   PVC LINER
                  TCTAL
YEARLY
       OPERATING
               1.
               2.
               3.
               Um
               5.
                    CCSTS»
                      LAROR
                      CHEMICAi.S
                      K4IMTEIMANCF&SUPPLIES
                      PVC  LINER
TOTAL YEARLY
                  TCTAL

                CCSTSt
                  1.  YEARLY  OPERATING COST
                  2.  YEARLY  INVESTMENT
                     COST  RECOVERY
                  3.  DEPPECIATICN
                  TOTAL
                                          40690.00
                                           8580.00
                                         501160.00
                                          12490.00
                                         109170.00
                                           7530.00
                                          28400.00
                                            190.00
                                         157780.00
                                         157780.00

                                          20050.00
                                          24840.00
                                         202670.00
                          1071

-------
               5
               o
                    -fr".. '
                                                                                               i
o
«>J
ro
               V)
               8
                    Z'5-.O •
                         I
                         I
                         I
                         I
                        oe.ro    «i.cs
                                                                                                  ««.es    ico.oc
                                                        FIGURE 305

                             INVESTMENT AND YEARLY COSTS  FOR SUBCATEGORY A 20, ALTERNATIVE X

-------
   DRAFT
An itemized breakdown of costs is presented in Table 293.   It is assumed
that land costs $4100 per hectare ($1660 per acre).   It is further
assumed that two operators are required.

               Reduction Benefits:  BOD:  100 percent
                                    . SS:  100 percent

Cost and Reduction Benefits of Alternative Treatment Technologies
for Subcategory A 22   - Grain Distillers Operating Sttllage
Recovery Systems

Two model plants representative of Subcategory A 22 were developed in
Section V for the purpose of applying control and treatment alter-
natives.  In Section VII, nine alternatives were selected as being
applicable engineering alternatives.  These alternatives provide for
various levels of waste reductions for model plant A 22-A which pro-
duces 380 kkg (15,000 bu) per day.

Alternative A 22-A-I - This alternative assumes no treatment and no
reduction in the waste load.  It is estimated that the effluent from
a 380 kkg (15,000 bu) per day plant is 2500 cu m (0.650 MG) per day.
The BOD waste load is 6.02 kg/kkg (0.336 Ib/bu), and the suspended
solids load is 4.21 kg/kkg (0.236 Ib/bu).

The model plant assumes screening of the effluent prior to discharge.

               Costs:               0
               Reduction Benefits:  None

Alternative A 22-A-II - This alternative provides flow equalization,
nutrient addition, and an aerated lagoon system.

The resulting BOD waste load is 0.26 kg/kkg (0.015 Ib/bu), and the
suspended solids load is 0.32 kg/kkg (0.018 Ib/bu).

               Costs:  Total investment cost:  $1,231,320
                       Total yearly cost:      $  602,940

An itemized breakdown of costs is presented in Table 294.   It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one operator is required.

The model plant assumes screening of the effluent prior to discharge.

               Reduction Benefits:  BOD:  95.7 percent
                                     SS:  92.3 percent

Alternative A 22-A-III - This alternative provides in addition to
Alternative A 22-A-II dual media filtration.

-------
DRAFT
                        TABLE 293

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A 21-11
                  (WINERIES WITH STILLS)
   ITEMIZED COST SUMMARY  FC*  WASTEMTER TREATMENT CHAI\
   DESIGN EFFICIENCY...100.0  PERCENT PRO REDUCTION
   TREATMENT MODULES?
   INVESTMENT CCSTS:
                   1.
                   2.
                   3.
                   4.
                      V...HOLOI(vG TANK
                      B...PUPPING STATION
                      *...PIPELINE
  CONSTRUCTION!
  LAMP
  ENGINEERING
  CGNTI\'RFNlCY
                  TCTAL
   YEARLY
OPERATING
        1.
        2.
        3.
        4.
COSTSt
  LABOR
                      CHEMICALS
                      MAJNTFKANCERSUPPLIES
                  TCTAL
275QOO.OO
 51fe
-------
DRAFT
                       TABLE 294

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-A-II
    (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY SYSTEMS)
    ITEMIZED COST SUMMARY FOF WASTEi*ATER  TREATMENT CHAIN
    DESIGN EFFICIENCY... 95.7 PERCENT  BOD REDUCTION
    TREATMENT MODULES:
                      e...PUMPING  STATION
                      C...F&IALIZATICN  BASTN
                      H...NITRCGEN  ADDITION*
                      I...PHCSPHORUS  ADDITION
                      L...AERATED  LAGCON
    INVESTMENT CCSTSj
                   1.
                   2.
                   3.
                   «.
                   5.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
PVC LINER
                   TCTAL

    YEARLY GPEPATING CCSTSl
 983780.00
  12990.00
  9fl380.00
  98380.00
  37790.00
1231320.00
                   1.
                   2.
                   3.
LABOR                  12^90.00
PCWER                 ^33320.00
CNF.MICA.LS               6950.00
MAINTENANCE8SUPPLIES   38^20.00
PVC LINER               1590.00
                   TCTAL
                      49277G.OO
    TOTAL YEARLY COSTS!
                   1. YEARLY OPERATING  COST  «92770.00
                   2. YEARLY INVESTMENT
                      CCST RECOVERY           a925C.OO
                   3. DEPRECIATION            60920.00
                   TCTAL                     602940.00
                          1075

-------
   DRAFT


The resulting BOD waste load is Q.13 kg/kkg (0.0073 Ib/bu), and the
suspended solids load is 0.016 kg/kkg (0.0090 Ib/bu).

               Costs:  Total investment cost:   $1,276,250
                       Total yearly cost:      $  613,420

An itemized breakdown of costs is presented in Table 295.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one operator is required.

The model plant assumes screening of the effluent prior to discharge.

               Reduction Benefits:  BOD:  97.8 percent
                                     SS:  96.9 percent

A cost efficiency curve is presented in Figure 306.

Alternative A 22-A-IV - This alternative provides a control house, flow
equalization, a complete mix activated sludge system, sludge thickening,
aerobic digestion, and sand drying beds.

The resulting BOD waste load is 0.26 kg/kkg (0.015 Ib/bu), and the
suspended solids load is 0.32 kg/kkg (0.018 Ib/bu).

               Costs:  Total investment cost:   $1,230,170
                       Total yearly cost:      $  289,080

An itemized breakdown of costs is presented in Table 296.  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).  It
is further assumed that three operators are required.

The model plant assumes screening of the effluent prior to discharge.

               Reduction Benefits:  BOD:  95.7 percent
                                     SS:  92.3 percent

Alternative A 22-A-V - This alternative provides in addition to Alter-
native A 22-A-IV dual media filtration.

The resulting BOD waste load is 0.13 kg/kkg (0.0073 Ib/bu), and the
suspended solids load is 0.16 kg/kkg (0.0090 Ib/bu).

               Costs:  Total investment cost:   $1,275,110
                       Total yearly cost:      $  299,560

An itemized breakdown of costs is presented in Table 297.  It is assumed
that land costs $41,000 per hectare ($16,600 per acre).  It is further
assumed that three operators are required.

The model plant assumes screening of the effluent prior to discharge.
                                1076

-------
DRAFT
                       TABLE  295

         ITEMIZED COST SUMMARY FOR ALTERNATIVE .A 22-A-III
     (GRAIN DISTILLERS OPERATING  STILLAGE RECOVERY SYSTEMS)
   ITEMIZFD COST SUMMARY FOR MSTEMTER  TREATMENT  CHAIN
   DESIGN  EFFICIENCY... 97.8 PERCENT BOD  REDUCTION
   TREATMENT MQDULESi
                     B.
                     C.
                     H.
                     I.
                     L.
                     B.
                     N.
                      .PUMPING  STATION
                      .EQUALIZATION  BASIN
                      .NITROGEN  ADDITION
                      .PHOSPHORUS  ADDITION
                      .AERATED  LAGOON
                      .PUMPING  STATION
                      .DUAL  MEDIA  PRESSURE FILTRA'N
   INVESTMENT CCSTSl
                  1.
                  2.
                  3.
                  4.
                  5.
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
                   PVC LINEH
               TCTAL

YEARLY OPERATING COSTS:
               1.  LABOR
               2
               3
1021230.00
  12990.00
 102120.00
 102120.00
  37790.00
1276250.00
                      CHEMICALS
                      MAINTEN'ANCESSUPPL'IES
                      PVC LINER
                  TCTAL
  12490.00
 439140.00
   6950.00
  39040.00
   1590.00
 499210.00
   TOTAL YEARLY CCSTSl
                  1. YEARLY OPERATING  COST  499210.00
                  2. YEARLY INVESTMENT
                     CCST RECOVERY           51050.00
                  3. DEPRECIATION            63160.00
                  TOTAL                     613420.00
                         1077

-------
o
                       i e: 7. c
8
^•s
>~



4
                       * T 2 .0
                   U
                                                                                          «e.co
                                                        FIGURE  306



                               INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 22-A-III

-------
DRAFT
                         TABLE 296

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-A-IV
     (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY SYSTEMS)
   ITEMIZED CDST SLMMARY  FOR  MSTEHATER TREATMENT CHAIN
   DESIGN EFFICIENCY... 95.7  PEPCENT nCD REIH'C

   TREATMENT MGOLLESi
                     81..CONTROL  *CLSE
                     B...PUMPING  STATION
                     C...£QL'ALIZATirN BASIN
                     (-...NITROGEN  ADDITION
                     I...PHCSPHCRUS  ADDITION
                     K...ACTIVATED  SLUDGE
                     Q...SLLCGE  THICKENER
                     P...AEROBIC  UIPESTOR
                     T...SAND  .DRYING 8EDS
INVESTMENT COSTS:
                1.
                2.   LAND
                3 •   E NGif
                4.   CONTINGENCY
                TCTAL

YEARLY OPERATING COSTS?
                1.
                  3.  CHEMICALS
                  4.  MA
                  TCTAL
   TOTAL  YEARLY CCSTSJ
                  1. YEARLY TPE»ATING
                  a. YEARLY INVESTMENT
                     CCST RECOVERY
                  3. OFPRFCIiTION
                  TCTAL
                                            985360.00
                                             47730.00
                                             9B540.00
                                           1230170.00
                                             37^80.00
                                           6950.00
                                          57870.00
                                         180750.00
                                         160750.00
                                          59120.00
                                         239080.0"
                         1079

-------
DRAFT
                       TABLE  297

        ITEMIZED COST SUMMARY FOR ALTERNATIVE  A 22-A-V
    (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY SYSTEMS)
   ITEMIZED  COST SUMMARY FOR fcASTEMTER TREATMENT  CHAIN
   DESIGN  EFFICIENCY... 97.P PERCENT BCD REDUCTION
   TREATMENT  MODULES.!
INVESTMENT COSTS:
                1.  CONSTRUCTION
                2.  LAND


                4.  CONTINGENCY
                TOTAL


YEARLY OPERATING COSTS!

                1.
                2.
                3.
                     81.. CONTROL HOUSE
                     e...PUMPING STATION
                     C...EQUALIZATION BASIN
                     H...NITROGEN ADDITION
                     I...PHOSPHORUS ADDITION
                     K...ACTIVATED SLUDGE
                     o...SLUDGE THICKENEW
                     R,..AEFC«1C DIGESTCR
                     T...SANO DRYING BEDS
                     R...PUMPING STATION
                     N...OUAL MEDIA PRESSURE FILTRA'N
                                          102^620.00
                                            47730.
                                           102280.
                                   00
                                   00
                  TCTAU
                                           102280.00
                                          1275110.00
                             37^80.00
                             8^270.00
                              6950.00
                             58490.00
                            167190.00
  TOTAL
COSTS:
  i. YEARLY OPERATING CCST  ie7i9o.oo
  2. YEARLY INVFSTKENT
     CCST PcCf-VEPv           51000.00
  3. DtPKECIATICK            61370.00
                  TOTAL
                            P99560.00
                         1080

-------
   DRAFT
               Reduction Benefits:   BOD:   97.8 percent
                                     SS:   96.9 percent

A cost efficiency curve is presented in Figure 307.

Alternative A 22-A-VI - This alternative  replaces sand drying beds  in
Alternative A 22-A-IV wtth vacuum filtration.

The resulting BOD waste load is 0.26 kg/kkg (0.015 Ib/bu),  and the
suspended solids load is 0.32 kg/kkg (0.018 Ib/bu).

               Costs:  Total investment cost:   $839,260
                       Total yearly cost:       $221,570

An itemized breakdown of costs is presented in Table 298.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.

The model plant assumes screening of the  effluent prior to  discharge.

               Reduction Benefits:   BOD:   95.7 percent
                                     SS:   92.3 percent

Alternative A 22-A-VII  - This alternative provides in addition to  Alter-
native A 22-A-VI dual media filtration.

The resulting BOD waste load is 0.13 kg/kkg (0.0073 Ib/bu), and the
suspended solids load is 0.16 kg/kkg (0.0090 Ib/bu).

               Costs:  Total investment cost:   $884,220
                       Total yearly cost:       $232,060

An itemized breakdown of costs is presented in Table 299.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.

The model plant assumes screening of the  effluent prior to  discharge.

               Reduction Benefits:   BOD:   97.8 percent
                                     SS:   96.9 percent

A cost efficiency curve is presented in Figure 308.

Alternative A 22-A-VIII - This alternative replaces the sand drying
beds in Alternative A 22-A-IV with spray irrigation.

The resulting BOD waste load is 0.26 kg/kkg (0.015 Ib/bu),  and the
suspended solids load is 0.32 kg/kkg (0.018 Ib/bu).

               Costs:  Total investment cost:   $838,600
                       Total yearly cost:       $212,850
                                1081

-------
c
OC
IM
                0)
                a
                b
                I
a
o
               4
                    7*2.5 '
                         i
                         i
                    eSJ.S i
                         I
               3         ;
               •-1    3*7.7 i
               rf         i
               O         '

                         I
                    8««.C i
                                                  «J.CC
                                                                                    «7.CO    S6.CO
                                                                                                            ICO.50
                                                       FIGURE  307


                             INVESTMENT AND YEARLY COSTS FOR  SUBCATEGORY A 22-A-V

-------
DRAFT
                        TABLE 298

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-A-VI
    (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY SYSTEMS)
  ITEMIZED COST  SUMMARY  FCR  WASTEMTER TREATMENT CHAIN
  DESIGN EFFICIENCY...  95.7 'PERCENT BOO REDUCTION
  TREATMENT MQDULESf
                     81
                     B,
                     C.
                     H.
                     I.
                     K.
                     8.
                     R.
                     S.
                     Y.
                      .CONTROL  HCLSE
                      .PUMPING  STATION
                      .EQUALIZATION  BASIN
                      .NITROGEN ArOITION
                      .PHGSPHCK.ljS  ADDITION
                      .ACTIVATED SLUDGE
                      .SLLDGE  THICKENER
                      .AEROBIC  CIGESTOP
                      .VACUUM  FILTRATION
                      .HOLDING  TANK
  INVESTMENT CCSTSl
                  1.
                  2.
                  3.
                  a.
                   CCN3TBUCTICN
                   LAND
                   EKGTMFfRING
                   CONTINGENCY
               TOTAL

YEARLY OPERATING COSTS!
               1.
            ,   2.
               3.  CHEMICALS
               a.  MAINTFNAN'CE&SLPPLIES
               TOTAL
660510.00
 46650.00
 66050.00
 66050.00
839260.00
                                            37«80.00
                                            83060.00
                                            12700.00
                                            15130.00
                                           148370.00
  TOTAL YEARLY COSTS:
                  i.  YEARLY  CPERATJKG COST j«837o.oo
                  2.  YEAFLY  I^VEST^ENT
                     COPT  RECOVERY           33570.00
                  3.  DEPPECTATION            39630.00
               TOTAL
                                           221570.00
                           1083

-------
DRAFT
                       TABLE  299

        ITEMIZED COST SUMMARY FOR ALTERNATIVE  A 22-A-VII
    (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY SYSTEMS)
  ITEMIZED COST SUMMARY  FOR  ("ASTEMTFR TREATMENT CHAIN
  DESIGN EFFICIENCY... Q7.8  PERCENT  PCD REDUCTION
  TREATMENT MCDULESj
                    Bl
                    B.
                    C.
                    H.
                    I.
                    K
                    s
                    Y(
                    P
 ..CONTROL HCLSE
 ..PUMPING STATION'
 ..EQUALIZATION BASIN
 ..NITROGEN ADDITION
 . .PHOSPHORUS ADDITION
 ..ACTIVATED SLUDGc
 ..SLIDGE THICKENER
 ..AEROBIC DIGESTOfi
 ..VACUUM FILTRATION
 ..HOLD TNG TANK
 ..PUMPING STATION
 ..DUAL *EDIA PRESSURE
                                             FILTRA'N
  INVESTMENT CCSTSt
                  1.
                  2.
                  5.
ENGINEERING
CCNTIKGENCY
                 TOTAL

  YEARLY OPERATING CCSTS;
                 2.  POWER
                 3.  CHEMICALS
                 fi.  V^INTE
                 TOTAL
697970.00
 46650.00
 69800.00
 69800.00
684220.00
                      37460.00
                      68860.00
                      12700.00
                      15750.00
                     15^810.00
  TOTAL YEARLY COSTS:
                 1. VEARLY CPSPATUG  CCST  i54gio.oo
                 2. YEAPLV INVESTMENT
                    COST KECGVESY           ?5370.00
                 3. DEPKFCIATIOK            iJiePO.OO
                 TrTAL                     232060.00
                         1084

-------
      ; ,C
    75?.2
u
                                                                «r.se    «e.co    ««.oo
                                     FIGURE 308



            INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 22-A-VII

-------
  DRAFT
An itemized breakdown of costs is presented in Table 300.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.

The model  plant assumes screening of the effluent prior to discharge.

               Reduciton Benefits:  BOD:  95.7 percent
                                     SS:  92.3 percent

Alternative A 22-A-IX  - This alternative provides in addition to Alter-
native A 22-A-VIII dual media filtration.

The resulting BOD waste load is 0.13 kg/kkg (0.0073 Ib/bu), and the
suspended solids load is 0.16 kg/kkg (0.0090 Ib/bu).

               Costs:  Total investment cost:   $863,810
                       Total yearly cost:      $219,710

An itemized breakdown of costs is presented in Table 301.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.

The model  plant assuems screening of the effluent prior to discharge.

               Reduction Benefits:  BOD:  97.8 percent
                                     SS:  96.9 percent

A cost efficiency curve is presented in Figure 309.

Model  plant B produces 90 kkg (3500 bu) per day.
Alternative A 22-B-I - This alternative assumes no treatment and no re-
duction in the waste load.  It is estimated that the effluent from a
90 kkg (3500 bu) per day plant is 570 cu m (0.15 MG) per day.   The
BOD waste load is 5.99 kg/kkg (0.335 Ib/bu), and the suspended solids
load is 4.23 kg/kkg (0.237 Ib/bu).
                                            I
The model plant assumes screening of the effluent prior to discharge.

               Costs:                0
               Reduction Benefits:  None
                               1086

-------
DRAFT
                        TABLE 300

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-A-VIII
    (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY SYSTEMS)
   ITEKIZFD COST 8LVMARY FC'R *.ASTEMTER  TREATMENT  CHAIN
   DESIGN EFFICIENCY... 95.7 PERCENT BOD  REDUCTION
   TREATMENT MODULES}
                     Bi..CONTROL HOUSE
                     P....PUMPING STATION
                     C...EQUALIZATION SASIN
                     H...NITRnGEN ADDITION
                     I...PHOSPHORUS  ADDITION
                     K...ACTIVATED SLUDGE
                     (T... SLUDGE THICKENER
                     R...AERCPIC C1GESTCR
                     Y...HOLDING TAM<
                     U...SPPAV  IRRIGATION
   INVESTMENT CCSTS:
                  1.
                  2.
                  3.
                  a.
                   CONSTRUCTION
                   LAND
                   ENC]NFE«ING
                   CCMIKGEMCV
667600
 60760,
00
00
00
               TOTAL

YEARLY OPERATING CCSTSi
               1.  LABOR
               3,  CHEMICALS

               TOTAL
 66760.00
838600.00
                                             37U80.00
                                             79330.00
                                              6950.00
                                             15^90.00
                                            139250.00
   TOTAL YEARLY
             COSTS:
               i. YEARLY  OPERATING  COST is^so.oo
               2. VE.ARLY  INVESTMENT
                  COST  RECOVERY           33540.oo
               3. DEPRECIATION            4G060.00
                  TOTAL
                                         21P650.00
                        1087

-------
JRAFT
                        TABLE 301

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-A-IX
    (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY SYSTEMS)
   ITEMIZED COST SUMMARY  FOR
   DESIGN EFFICIENCY... 97.*
        KA3TEMTEP TREATMENT  CHAIN
        PERCENT BOD REDUCTION
   TREATMENT MODULESt
81
                         .CONTROL  HCISE
                     P.. .PULPING  STATION
                     C...EC1LALIZATICN BASIN
                     H... NITROGEN ADDITION
                     I...PHCSPHDRUS  ADDITION
                     K,., ACTIVATED  SLUDGE
                     G... SLUDGE  THICKENER
                     «... AEROBIC  DI6ESTOP
                     v... HOLDING  TANK
                     U... SPRAY  IRRIGATION
                     B... PUMPING  STATION
                     N...PUAI M.FDIA  PRESSURE FILTRA'N
   INVESTMENT CCSTSl
                  1.
                  2.
                  3.
    CONSTRUCTION
    LAND
    ENGINEERING
«.  CONTINGENCY
TCTAL
   YEARLY OPERATING COSTS!
                  1.  LABOR
                  2.  PCWFR
                  3.  CHEMICALS
                  4.  MAINTENANCE&SIPPLIES
                  TCTAL

   TOTAL YEARLY COSTS*
                  1. YEARLY OPERATING  COST
                  2. YEARLY INVESTMENT
                     COST RECOVERY
                  3. DEPRECIATION
                  TCTAL
                      668610.00
                       37480.00
                       68660.00
                       68860.00
                      863810.00
                       37480,
                       835
-------
8
53*.C
LU
     3 '. i . C
                         02.::
                                                                                        tsc.ce
                                       FIGURE 309




              INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A  22-A-IX

-------
   DRAFT
Alternative A 22-B-II  - This alternative provides flow equalization,
nutrient addition, and an aerated lagoon system.

The resulting BOD waste load is 0.25 kg/kkg (0.014 Ib/bu),  and the
suspended solids load is 0.32 kg/kkg (0.018 Ib/bu).

               Costs:  Total investment cost:   $348,170
                       Total yearly cost:      $132,190

An itemized breakdown of costs is presented in Table 302.   It ts
assumed that land costs $4100 per hectare ($1660  per acre).   It is
further assumed that one operator is required.

The model plant assumes screening of the effluent prior to  discharge.

               Reduction Benefits:  BOD:  95.8 percent
                                     SS:  92.5 percent

Alternative A 22-B-III - This alternative provides in addition to Alter-
native A 22-B-II dual media filtration.

The resulting BOD waste load is 0.13 kg/kkg (0.0073 Ib/bu),  and the
suspended solids load is 0.16 kg/kkg (0.0090 Ib/bu).

               Costs:  Total investment cost:   $373,380
                       Total yearly cost:      $139,050

An itemized breakdown of costs is presented in Table 303.   It is
assumed that land costs $4100 per hectare ($1660  per acre).   It is
further assumed that one operator is required.

The model plant assumes screening of the effluent prior to  discharge.

               Reduction Benefits:  BOD:  97.9 percent
                                     SS:  96.3 percent

A cost efficiency curve is presented in Figure 310.

Alternative A 22-B-IV - This alternative provides a control  house, flow
equalization, a complete mix activated sludge  system, sludge thickening,
aerobic digestion, and sand drying beds.

The resulting BOD waste load is 0.25 kg/kkg (0.014 Ib/bu),  and the
suspended solids load is 0.32 kg/kkg (0.018 Ib/bu).

               Costs:  Total investment cost:   $332,290
                       Total yearly cost:      $  97,130

An itemized breakdown of costs is presented in Table 304.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.
                                 1090

-------
DRAFT
                       TABLE 302

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-B-II
       (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY)
 ITEMIZED  COST SUMMARY FOR fcASTEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY.., 95.fi PERCENT BOO REDUCTION
 TREATMENT  MQDULESi
                      .PULPING STATION
                      .F.QIALIZATICN BASIN
                      .NITROGEN ADDITION
                      .PHOSPHORUS ADDITION
                      .AERATED LAGOON
 INVESTMENT  CCSTSt
                1.
                2.
                3.
                4.
                5.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC LINER
                TOTAL
 YEARLY
OPERATING
        1.
        2.
        3.
        4.
        5.
TOTAL  YEARLY
COSTSt
  LABOR
  POWER
  CHEMICALS
  MAINTENANCEiSLFPLlES
  PVC LTNER
        TOTAL

      CCSTSJ
        1. YEARLY
        2. YEARLY
           COST
        3. DEPRECIATION
        TOTAL
                          OPERATING COST
                          INVESTMENT
                        279500.00
                          4830.00
                         27950.
                         27950.
00
00
                          7940.00
                       348170.00
                                           6250.00
                                          82700.00
                                           1860.00
                                           9900
                                            380
00
00
                                         101090.00
                        101090.00

                         13930.00
                         17170.00
                        132190.00
                          1091

-------
DRAFT
                       TABLE  303

       ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-B-III
        (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY)
 ITEMIZED  COST  SUMMARY FQP
 DESIGN  EFFICIENCY...  97. 9
                   MSTEMTEP  TREATMENT CHAIN
                   PERCENT  BOD  REDUCTION
TREATMENT  MODULES!
                   8...PULPING STATION
                   C...EQLALIZATirN PASIN
                   H...NITROGEN. ADDITION
                   I...PHCSPHPRIS ADDITION
                   t...Afe-pATED LAGOON
                   S... PULPING STATION
                   M
              .DUAL MEDIA  PRESSURE  FILTRA'N
 INVESTMENT  COSTS}
                1.
                2.
                3.
                a.
                b.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            FVC LINER
                TOTAL
YEARLY
OPERATING
        1.
        2.
        3.
        4.
        5.
TOTAL  YEARLY
COSTS;
  LABOR
  PO'ER
  CHEMICALS
  MAINTENANTERSLPPLIES
  PVC LINER
        TOTAL

      COSTS•
        1. YEARLY OPERATING  COST
        2. YEARLY INVESTMENT
           COST RECOVERY
        3. DEPRECIATION
        TOTAL
                        300510.00
                          4830.00
                         30050.00
                         3 0 0 5 0 . C 0
                          7940.00
                        373380.00
                                           6250.
                                          86960.
                                           I860,
                                          10230,
00
00
00
00
                                            380.00
                                         105680.00
                                         105680.00
                                                .00
                                          18430,00
                                         139050.00
                          1092

-------
O
to
CO
                  (/)

                  5
                      30!.i
                      ?77.2
§   2SJ-"
                  >-   2?*.$
                  Q   ?
                  O


                  I
                  t-4
                  n

                  U
                                                        FIGURE 310


                               INVESTTtNT AND YEARLY COSTS FOR SUBCATEGORY A 22-B-III
                                                                                                            jce.:s

-------
DKAH
                       TABLE  304

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-B-IV
        (GRAIN DISTILLERS OPERATING  STILLAGE RECOVERY)
  ITEMIZED COST SUMMARY FQP WASTEMTEff TREATMENT  CHAIN
  DESIGN EFFICIENCY... 95.8 PERCENT POD REDUCTION
  TREATMENT MCOULESj
                    B1,,CQMRCL HCLSE
                    B...PUMPING STATION
                    C...EQUALIZATION BASIN
                    H...NITROGEN ADDITION
                    I...FHOSPHORLS ADDITION
                    K...ACTIVATED SLUDGE
                    C...SLLOGF THICKENER
                    P...AEPCRir. CIGESTCR
                    T...SAND DRYING
  INVESTMENT  CCSTSi
                 1.
                 2.
                 3.
                 4.
CCNSTRICTTCK
CCNTIN6FNCY
                 TOTAL

  YEARLY  OPERATING COSTS:
                 1.  LABOR
                 2.  PCWF.H
                 3.  CHEMICALS
                 «.  MAINTF>'4NCERSLPPLIES
                 TCTAL

  TOTAL  YEARLY  fCSTSl
                 1. YEAPLY CPERATIKG CCST
                 2. YEARLY INVESTMENT
                    CCST RPCCVERY
                 3. DEPRECIATION
                 TCTAL
263720.00
 15830.00
 26370.00
 26370.00
332290.00
                      37a80.
                      19760.
                        I860.
       00
       00
       00
                       8920.00
                      68020.00


                      66020.00

                      13290.00
                      15820.00
                      97130.00
                            1094

-------
  URAFT


The model plant assumes screening of the effluent prior to discharge.

               Reduction Benefits:  BOD:  95.8 percent
                                     SS:  92.5 percent

Alternative A 22-B-V - This alternative provides dual  media filtration
in addition to the treatment chain in Alternative A 22-B-IV.

The resulting BOD waste load is 0.13 kg/kkg (0.0073 Ib/bu), and the
suspended solids load is 0.16 kg/kkg (0.0090 Ib/bu).

               Costs:  Total investment cost:   $357,500
                       Total yearly cost:      $103,990

An itemized breakdown of costs is presented in Table 305.   It is assumed
that land costs $41,000 per hectare ($16,600 per acre).  It is further
assumed that three operators are required.

The model plant assumes screening of the effluent prior to discharge.

               Reduction Benefits:  BOD:  97.9 percent
                                     SS:  96.3 percent

A cost efficiency curve is presented in Figure 311.

Alternative A 22-8-VI - This alternative replaces sand dryinq beds in
Alternative A 22-B-IV with vacuum filtration.

The resulting BOD waste load is 0.25 kg/kkg (0.014 Ib/bu), and the
suspended solids load is 0.32 kg/kkg (0.018 Ib/bu).

               Costs:  Total investment cost:   $387,710
                       Total yearly cost:      $106,650

An itemized breakdown of costs is presented in Table 306.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).  It
is further assumed that three operators are required.

The model plant assumes screening of the effluent prior to discharge.

               Reduction Benefits:  BOD:  95.8 percent
                                    -SS:  92.5 percent

Alternative A 22-B-VII - This alternative adds dual media  filtration to
Alternative A 22-B-VI.

The resulting BOD waste load is 0.13 kg/kkg (0.0073 Ib/bu), and the
suspended solids load is 0.16 kg/kkg (0.0090 Ib/bu).

               Costs:  Total investment cost:   $412,920
                       Total yearly cost:      $113,510
                                1095

-------
 DRAFT
                       TABLE  305

        ITEMIZED COST SUMMARY FOR ALTERNATIVE  A 22-B-V
        (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY)
ITEMIZED COST SUMMARY FOP WA8TEMTER  TREATMENT  CHAIN
DESIGN EFFICIENCY.., 97.9 PERCENT BOD  REDUCTION
TREATMENT MODULES?
                  P1..CGMTROL MCLSE
                  H... PUMPING STATION
                  C...EOLALIZATICN BASIN
                  H...NITROGFN ADDITION
                  I. . .PHOSPHORUS  ADDITION
                  K...ACTIVATED SLUDGE
                  G...SLUDGE THICKENER
                  P...AERLSIC DIGESTCR
                  T...SAND DRYING 8EHS
                  B...PUMPING STATION
                  N...DUAL MEDIA  PRESSURE  FRTRA'N
INVESTMENT CCSTS:
               1.
               2.
               3.
               4.
            CCNSTPUCTION
            LAND
            ENGINEERING
            CONTINGENCY
               TOTAL
YEARLY
OPERATING
        1.
        2.
        3.
        4.
COSTS?
  LABOR
  PCWER
  CHEMICALS
  MAINTENANCE&SUPPLIES
               TCTAL

TOTAL YEARLY COSTS!
               1, YEARLY OPERATING COST
               2. YEARLY INVESTMENT
                  COST RECOVERY
               3. DEPRECIATION
               TCTAL
                       28«730(
                         15830,
                         28470,
                         28470,
      00
      00
      00
      00
                                  357500.00
                                          37400.
                                          24020.
      00
      00
 1860.00
 9250.00
72610.00
                                   72610.00

                                   14300.00
                                   17080.00
                                  103990.00
                          1096

-------
 W
     371. «
°-  i31 I
    S! ? 3 , !
        .
     °7.C
    «i.oc     r.2.:c     «j.:t     «;.::     
-------
DRAFT
                       TABLE  306

        ITEMIZED COST SUMMARY FOR ALTERNATIVE .A 22-B-VI
        (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY)
 ITEMIZED  COST  SUMMARY FOP WASTEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY...  95.8 PERCENT BCD REDUCTION
 TREATMENT  MODULES*
                   31
                   B.
              .CONTROL HCLSE
              .PUMPING STATION
           C...EQUALIZATION BASIN
           H,..NITROGEN  ADDITION
           I...PHOSPHORUS  ADDITION
           K...ACTIVATED SLUDGE
           Q...SLLnRE THICKENER
           «...AEROBIC CIGESTOR
           8...VACUUM FILTRATION
           Y...HOLDING TANK
 INVESTMENT  CCSTSl
                1.
                2.
                3.
                a.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
                TOTAL
 YEARLY
OPERATING
        1.
        2.
        3.
  CCSTSt
    LABOR
    PfkER
    CHEMICALS
4.  MAJNTFNANCE&SLPPLlfcS
TOTAL
 TOTAL  YEARLY  COSTS!
                1.  YEARLY OPERATING COST
                2.  YEARLY INVESTMENT
                   COST RECOVERY
                3.  DEPRECIATION
                TOTAL
                          296720.00
                           31650.
                           ?9fc70.
00
00
                           29670.00
                          387710.00
                                          37480.00
                                          22000.00
                                           4350.00
                                           9S10.00
                                          73340.00
                                   733^0.00

                                   15510.00
                                   17800.00
                                  106650.00
                          1098

-------
   DRAFT
An itemized breakdown of costs is presented in Table 307.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.

The model plant assumes screening of the effluent prior to .discharge.

               Reduction Benefits:  BOD:  97.9 percent
                                     SS:  96.3 percent

A cost efficiency curve is presented in Figure 312.

Alternative A 22-B-VIII - This alternative replaces  the sand drying
beds in Alternative A 22-B-IV with spray irrigation.

The resulting BOD waste load is 0.25 kg/kkg (0.014 Ib/bu), and the
suspended solids load is 0.32 kg/kkg (0.018 Ib/bu).

               Costs:  Total investment cost:   $388,320
                       Total yearly cost:      $102,870

An itemized breakdown of costs is presented in Table 308.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.

The model plant assumes screening of the effluent prior to discharge.

               Reduction Benefits:  BOD:  95.8 percent
                                     SS:  92.5 percent

Alternative A 22-B-IX - This alternative adds  dual media filtration to
Alternative A 22-B-VIII.

The resulting BOD waste load is 0.13 kg/kkg (0.0073 Ib/bu),  and the
suspended solids load is 0.16 kg/kkg (0.0090 Ib/bu).

               Costs:  Total investment cost:   $404,360
                       Total yearly cost:      $107,620

An itemized breakdown of costs is presented in Table 309.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.

The model plant assumes screening of the effluent prior to discharge.

               Reduction Benefits:  BOD:  97.9 percent
                                     SS:  96.3 percent

A cost efficiency curve is presented in Figure 313.
                                1099

-------
DRAFT
                       TABLE 307


        ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-B-VIJ
        (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY)
 ITEMIZED COST SUGARY FCJR WASTEMTER TREATMENT  CHAIN
 DESIGN  EFFICIENCY... 97.0 PERCENT BOD REDUCTICN
 TREATMENT MCDULESt
                   Bl..CONTROL HCLSE
                   fi...PUMPING STATION
                   C...EQUALIZATION BASIN
                   H...NITROGEN ADDITION
                   I...PHOSPhORLS ADDITION
                   K...ACTIVATED SLUDGE
                   G...SLUDGE THICKENER
                     ..AERCPir DIGESTCR
                     ..VACUUM FILTRATION
s.
Y...HOLDING TANK
B...PUMPING STATION
N...ntjAi MEDIA PRESSURE FRTRA'N
 INVESTMENT CCSTS:
                1.
                2.
                3.
                4.
 CONSTRUCTION
 LAND

 ENGINEERIN6
 CONTINGENCY
                TOTAL


 YEARLY  OPERATING COSTS*
                1.  LA30R
                2.  PC*E*
                3.  CHEMICALS
                U.  VAI
                TOTAL
317730.00
 31650.00
 31770.00
 31770.00
412920.00
                       37aeo.oo
                       26260.00
                        4350.00
                        9840.00
                       77930.00
 TCTAL  YEARLY COSTS:
                1. YEARLY OPERATING COST  77930.00
                2. YEARLY INVESTMENT
                   COST RECOVERY          16520.00
                3. DEPRECIATION           19060.00
                TOTAL                     113510.00
                          1100

-------
    «IJ.O  I
    JPJ.J
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QJ
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u
    1'p.l
    SC6.C
                                                                                   99.00   ISO.00
                                      FIGURE  312



             INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 22-B-VI-VII

-------
DRAFT
                       TABLE 308

        ITEMIZED COST SUMMARY FOR  ALTERNATIVE A 22-B-VIII
        (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY)
ITEMIZED  COST  SUMMARY  FOR K
-------
DRAFT
                       TABLE 309

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A 22-B-IX
        (GRAIN DISTILLERS OPERATING STILLAGE RECOVERY)
   ITEMIZED  COST SUMMARY FOR WASTEMTER TREATMENT  CHAIN
   DESIGN  EFFICIENCY... 
-------
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     2SJ.8  I
!*•?.»
                                                                  7. cc
                                                                                        105. co
                                      FIGURE  313



               INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 22-B-VII-IX

-------
   DRAFT
Cost and Reduction Benefits of Alternative Treatment Technologies for
Subcategory A 23 - Grain Distillers Not Operating SttlIs

A model plant representative of Subcategory A 23 was developed in
Section V for the purpose of applying control and treatment alter-
natives.  In Section VII, five alternatives were selected as being
applicable engineering alternatives.  These alternatives provide
for various levels of waste reductions for the model plant which
produces 50 kkg (2000 bu) per day.

Alternative A 23-1 - This alternative assumes no treatment and no re-
duction in the waste load.  It is estimated that the effluent from
a 50 kkg (2000 bu) per day plant is 91 cu m (0.024 MG)  per day.   The
BOD waste load is 0.38 kg/kkg (0.021 Ib/bu), and the suspended solids
load is 0.29 kg/kkg (0.016 Ib/bu).
                                                                    •
               Costs:               0
               Reduction Benefits:  None

Alternative A 23-11 - This alternative provides a pumping station
and aerated lagoon system.

The resulting BOD waste load is 0.06 kg/kkg (0.0034 Ib/bu), and the
suspended solids load is 0.07 kg/kkg (0.0039 Ib/bu).

               Costs:  Total investment cost:  $133,720
                       Total yearly cost:      $ 28,200

An itemized breakdown of costs is presented in Table 310.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one half-time operator is required.

               Reduction Benefits:  BOD:  85.7 percent
                                     SS:  75.0 percent

Alternative A 23-1II - This alternative provides in addition to Alter-
native A 23-11 dual media filtration.

The resulting BOD waste load is 0.03 kg/kkg (0.0017 Ib/bu), and the
suspended solids load is 0.04 kg/kkg (0.0022 Ib/bu).

               Costs:  Total investment cost:  $149,750
                       Total yearly cost:      $ 32,940

An itemized breakdown of costs is presented in Table 311.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one half-time operator is required.

               Reduction Benefits:  BOD:  92.9 percent
                                     SS:  87.5 percent

A cost efficiency curve is presented in Figure 314.

-------
DRAFT
                         TABLE  310

            ITEMIZED COST SUMMARY  FOR ALTERNATIVE A 23-11
             (GRAIN DISTILLERS NOT OPERATING STILLS)
   ITEMIZED COST SUMMARY  FOR  WASTEMTER TREATMENT CHAIN
   DESIGN EFFICIENCY... 65.7  PERCENT  BCD REDUCTION
   TREATMENT MCDULESi
                      B.,.PUMPING  STATION
                      K...NITROGEN  ADDITION
                      I...PHOSPHORUS  ADDITION
                      L...AERATED  LAGOON
   INVESTMENT COSTS;
                   1.
                   2.
                   3.
                   5.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC LINER
                   TCTAL
   YEARLY
OPERATING
        1.
        2.
        3.
CCSTSl
  LABOK
                       CHEMICALS
                       MAINTENANCES SUPPLIES
                       PVC  LINER
                   TOTAL

   TCTAL YEARLY CCSTSl
                   1.  YEARLY  OPERATING COST
                   2.  YEARLY  INVESTMENT
                      CIST  HF.CTVERY
                   3.  DEPRECIATION
                   TOTAL
                        105670.00
                          "5330.00
                         10570.00
                         10570.00
                          3560.00
                        133720.00
 6250.00
 5170.00
   60.00
 4790.00
   60.00
16330,00
                                   16330.00

                                    5350.00
                                    6520.00
                                   28200.00
                          1106

-------
DRAFT
                         TABLE 311

            ITEMIZED COST SUMMARY FOR ALTERNATIVE A 23-111
              (GRAIN DISTILLERS NOT OPERATING STILLS)
ITEMIZED COST SUMMARY  FOR
DESIGN EFFICIENCY... 92. 
-------
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                   tfo.o
               (f)   117.1
               °   »«.»

               fe
               (n

               i   ni.«
                   let.
               2
               1-1


               I-
               ^
               ~   54.•
                    n.«
10.eo    M.IO     »a.»o
                                                                          «T.»O
«0.iO    fl.TO    41.00
                                                           FIGURE  314



                              INVESTMEr^T AND YEARLY COSTS FOR SUBCATEGORY A 23-1II

-------
   DRAFT
Alternative A 23-IV  - This alternative provides in addition to Alterna-
tive A 23-11 spray irrigation.

The resulting BOD waste load is zero, and the suspended solids load
is zero.

               Costs:  Total investment cost:  $224,040
                       Total yearly cost:      $ 70,590

An itemized breakdown of costs is presented in Table 312.  It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that one half-time operator is required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent

A cost efficiency curve is presented in Figure 315.

Cost and Reduction Benefits of Alternative Treatment Technologies for
Subcategory A 24 - Molasses Distillers

A model plant representative of Subcategory A 24 was developed in
Section V for the purpose of applying control and treatment alternatives.
In Section VII, nine alternatives were selected as being applicable
engineering alternatives.  These alternatives provide for various
levels of waste reductions for the model plant which produces 30,000
pg per day.

Alternative A 24-1 - This alternative assumes no treatment and no re-
duction in the waste load.  It is estimated that the effluent from a
30,000 pg per day plant is 818 cu m (0.216 MG) per day.  The BOD
waste load is 969 kg/1000 pg (2140 lb/1000 pg), and the suspended
solids load is 183 kg/1000 pg (403 lb/1000 pg).

               Costs:              0
               Reduction Benefits: None

Alternative A 24-11 - This alternative consists of concentrating high
strength molasses slops (stillage) by multi-effect evaporation, and then
treating evaporator condensate and all other wastes with a treatment
chain consisting of a control  house, a pumping station, flow equalization,
nutrient addition, a complete mix activated sludge system, sludge thick-
ening, aerobic digestion, vacuum filtration, sludge storage and truck
hauling.   Evaporation is predicted to have an investment cost of $2,193,310
and a yearly cost of $609,620.   Evaporation is assumed to remove 97 per-
cent of the BOD and 99 percent of the suspended solids from high strength
wastes.  Two day storage of distilling slops and seven day storage of
molasses by-product is provided, and all  necessary pumping equipment is
included.
                                 1109

-------
DRAFT
                          TABLE 312

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A 23-IV
             (GRAIN DISTILLERS NOT OPERATING STILLS)
   ITEMIZED COST SUGARY  FOP  WASTEMTER TREATMENT CHAIN
   DESIGN EFFICIENCY..,100.0  PE«CFM  BOD REDUCTION
   TREATMENT MODULES!
                      R...PUKPTNG  STATION
                      h. ..NITNGC-EN AOCITICN
                      I...PHCSPHr.RL!S ADDITION
                      L... AERATED  L AGCCN
                      Y. , .HOLT* I Mf;  TANK
                      L...SPRAY  IRRIGATION
   INVESTMENT COSTSJ
                   1.
                   2.
                   3.
                   a.
                   s.
                    CTMSTRLTTICK
                    LAND
                    E^GIMPFPING
                    CCNTINGENCY
                    PVC LTNFf'
               TOTAL

YEARLY OPERATING CCSTS:
               1.  LABOR
               2.  Pr.iNEP
               3.  CHEMICALS
               5.  PVC  LINER
               TCTH

TOTAL YEARLY COSTS?
               1.  YEARLY  OPERATING  COST
               2,  YEARLY  INVESTMENT
                   CCST  HECCVFPY
               3.  OEPRECIAUCN
               1CTAI
17^270.00
 11330.00
 17430.00
 1 7 a 3 0 . 0 0
  3580.00
224040.00
                                             37480.00
                                              6130.00
                                                60.00
                                              7260.00
                                                60.00
                                             509<5G.OO
                                             50990.00

                                              8960.CO
                                             10640.00
                                             70590.00
                          1110

-------
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                                        FIGURE 315



                           AND YEARLY COSTS FOR SUBCATEGORY A 23-IV

-------
   URAFT


The resulting BOD waste load is 1.16 kg/1000 pg (2.56 lb/1000 pg),  and
the suspended solids load is 0.69 kg/1000 pg (1.52 lb/1000 pg).

               Costs:  Total investment cost:  $2,644,060
                       Total yearly cost:      $  698,640

An itemized breakdown of costs is presented in Table 313.  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that six operators are required.

It is recognized that, although not included in the above costs, add-
itional boiler and cooling capacity may be required for evaporation.
Cost recovery from saleable by-products is not reflected in the  costs.

               Reduction Benefits:   BOD:  99.9 percent
                                     SS:  99.6 percent

Alternative A 24-1II - This alternative consists of adding dual  media
filtration to the treatment chain in Alternative A 24-11.

The resulting BOD waste load is 0.58 kg/1000 pg (1.28 lb/1000 pg),  and
the suspended solids load is 0.35 kg/1000 pg (0.77 lb/1000 pg).

               Costs:  Total investment cost:  $2,671,130
                       Total yearly cost:      $  705,710

An itemized breakdown of costs is presented in Table 314.  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that six operators are required.

               Reduction Benefits:   BOD:  99.9 percent
                                     SS:  99.8 percent

A cost efficiency curve is presented in Figure 316.

Alternative A 24-IV - This alternative replaces vacuum filtration in
Alternative A 24-11 with spray irrigation of sludge.

The resulting BOD waste load is 1.16 kg/1000 pg (2.56 lb/1000 pg),  and
the suspended solids load is 0.69 kg/1000 pg (1.52 lb/1000 pg).

               Costs:  Total investment cost:  $2,638,610
                       Total yearly cost:      $  692,540

An itemized breakdown of costs is presented in Table 315.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It  is
further assumed that six operators  are required.

               Reduction Benefits:   BOD:  99.9 percent
                                     SS:  99.6 percent
                                1112

-------
DRAFT
                       TABLE  313

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A24-II
                 (MOLASSES DISTILLERS)
   ITEMIZED COST SUMMARY FOP &ASTEMTEH TREATMENT CHAIN
   DESIGN  EFFICIENCY... 9".8 PERCENT PCD REDUCTION
   TREATMENT MODULES?
                     91.. CONTROL, HftSE
                     P. . .PUMF-.ING STATION
                     FI..MULTIPLE EFFECT
                     Y... HOLD ING TANK
                     P...PUMPING STATION
                     Y...HOLD ING TANK
                     e...PUMPING STATIC
                     8...PULPING STATION
                     C...EQUAI IZATICN BASIN
                     H. . .NITROGEN ADDITION
                     I. . .PHTSPHOrtLS ADDITION
                     K...ACTIVATED SLLDGt
                     c...SLUDGE THICKENEF
                     R....AERCPIC RIGESTCR
                     s...VACUUM FILTRATION
                              TJG TAM<
                                       EVAPORATOR
   INVESTMENT  COSTS:
                  1.
    CONSTRUCTION
2.   LAND
3.   ENGINEERING
a.   CONTINGENCY
TOTAL
                                        2181 160.00
                                          26660.00
                                         218120.00
                                         218120.00
                                        26U4060.00
YEARLY
         OPERATING  COSTS:
                  1.   LA30S                  7^970.00
                  2.   rCwER                 339170.00
                  3,   CHEMICALS               7350.00
                  u.   MAINTFNANCE&SLPPLIES  «052o.oo
                  TOTAL                     /462010.00

  TOTAL YEARLY CCSTSt
                  1.  YEARLY  OPERATING  COST a62010.00
                  2.  YEASL>  INVESTMENT
                     COST RECOVERY          105760.00
                  3.  DEPRECIATION           130870.00
                  TOTAL                     6986^0.00
                          1113

-------
DRAFT
                       TABLE  314

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A24-III
                 (MOLASSES DISTILLERS)
   ITEMIZED  COST SUGARY FOR WASTEMTER TREATMENT CHAIN
   DESIGN  EFFICIENCY...  99.9 PERCENT BOD REDUCTION
   TREATMENT  MODULESt
                     Bl..CONTROL HCIJSE
                     6...PULPING STATION
                     Fl..MULTIPLE EFFECT EVAPORATOR
                     Y...HOLDING TANK
                     6...PUMPING STATION
                     Y...HOLDING TANK
                     B...PUMPING STATIC^
                     e...PijyP!NG STATION
                     C...EQUALIZATION BASIN
                     H...NITROGEN ADDITION
                     I...PHOSPHORUS ADDITION
                     K...ACTIVATED SLUDGE
                     Q...SLUDGE THICKENER
                     R...AERCBIC D1GESTCR
                     S...VACUUM FILTRATION
                     Y...HOLDING TANK
                     N...DUAL  MEDIA PRESSURE FILTPA'N
   INVESTMENT  COST?!
                  1 .
                  2.
                  3.
                  4.
CONSTRUCTION
LAND

ENGINEERING
CONTINGENCY
2203730.00
  26660.00
 220370.00
 220370.00
2671130.00
                  TOTAL


  YEARLY OPERATING  COSTS:
                  1.   LABOR                  7«970.00
                  2.   POER                 343450.00
                  3.   CHEMICALS               7350.00
                  4.   MAINTENANCERSLPPLIES   40870.00
                  TOTAL                     "66640.'00

  TOTAL YEARLY COSTS*
                  i. YEARLY OPERATING  COST  466640.oo
                  2. YEARLY INVESTMFNT
                    COST RECOVERY          106850.00
                  3. DEPRECIATION           132220.00
                      i.                     705710.00

-------
                               I
                         20SJ.1 I
                               I
                               I
                               I
                                                                                                                                 Tl
cn
                              <»c.cc    «t.co
                                                       «J.c:
                                                                            :     «o,oc    «7.oo
                                                                       *f !C!E'-C»
                                                            FIGURE 316

                                    INVESTMENT AND  YEARLY COSTS FOR  SUBCATEGORY A 24-11 1
99.00    100.00

-------
JRAFT
                        TABLE  315

          ITEMIZED COST SUMMARY FOR ALTERNATIVE A24-IV
                  (MOLASSES DISTILLERS)
   ITEMIZED COST SUMMARY FOR niASTEMTER  TREATMENT  CHAIN
   DESIGN EFFICIENCY... 99.3 PERCENT BOD REDUCTION
   TREATMENT MCOUlESi
           81..CONTROL HCLSE
           e...PUFFING STATION
           Fl..MULTIPLE EFFECT
           Y...HOLDING TANK
           B...PUMPING STATION
           Y...HOLDING TANK
           B...PUMPING STATION
           B...PUMPING STATION
           C...EQUALIZATION BASIN
           h...NITROGEN ADDITION
           I...PHOSPHORUS ADDITION
           K...ACTIVATED SLUDGE
           0...8LL-DGE THICKENER
           R...AEROBIC CIGESTOR
           Y...HOLDING TANK
           U...SPRAY IRRIGATION
                                         EVAPORATOR
   INVESTMENT COSTS?
                  1.
                  2.
                  3.
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
                                 2183560.00
                                   18330.00
                                 216360.00
                                 216360.00
                                 2636610.00
   YEARLY
OPERATING
        1.
        2.
        3.
        a.
  COSTS;
    LABOR
    POER
    CHEMICALS
    MAINTENANCE&SLPPLIES
                  TOTAL
 74970.00
337450.00
  4390.00
 39180.00
455990.00
   TOTAL  YEARLY CCST£l
                  1. YEARLY OPERATING COST 455990.00
                  2. YEARLY INVESTMENT
                     COST RF.CCVERY         105540.00
                  3. DEPRECIATION          131010,00
                  TOTAL
                                 692540.00
                         1116

-------
   DRAFT


Alternative A 24-V - This alternative provides in addition to Alternative
A 24-IV dual media filtration.

The resulting BOD waste load is 0.58 kb/1000 pg (1.28 lb/1000 pg),  and the
suspended solids load is 0.35 kg/1000 pg (0.77 lb/1000 pg).

               Costs:  Total investment cost:   $2,665,690
                       Total yearly cost:       $  699,620

An itemized breakdown of costs is presented in Table 316.  It is
assumed that land costs $4100 per hectare ($1660 per acre).   It
is further assumed that six operators are required.

               Reduction Benefits:  BOD:  99.9 percent
                                     SS:  99.8 percent

A cost efficiency curve is presented in Figure 317.

Alternative A 24-VI - This alternative replaces vacuum filtration in
Alternative A 24-11 with sand drying beds.

The resulting BOD waste load is 1.16 kg/1000 pg (2.56 lb/1000 pg),  and
the suspended solids load is 0.69 kg/1000 pg (1.52 lb/1000 pg).

               Costs:  Total investment cost:   $2,759,100
                       Total yearly cost:       $  718,490

An itemized breakdown of costs is presented in Table 317.  It is
assumed that land costs $20,510 per hectare ($8300 per acre).  It
is further assumed that six operators are required.

               Reduction Benefits:  BOD:  99.9 percent
                                     SS:  99.6 percent

Alternative A 24-VII - This alternative adds dual media filtration  to
Alternative A 24-VI.

The resulting BOD waste load is 0.58 kg/1000 pg (1.28 lb/1000 pg),  and
the suspended solids load is 0.35 kg/1000 pg (0.77 lb/1000 pg).

               Costs:  Total investment cost:   $2,786,170
                       Total yearly cost:       $  725,560

An itemized breakdown of costs is presented in Table 318.  It is
assumed that land costs $20,510 per hectare ($8300 per acre).  It
is further assumed that six operators are required.

               Reduction Benefits:  BOD:  99.9 percent
                                     SS:  99.8 percent

A cost efficiency curve is presented in Figure 318.
                                 1117

-------
DKAfr
                       TABLE  316

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A24-V
                  (MOLASSES DISTILLERS)
   ITEMIZED COST SUMMARY FOP WASTEMTER TREATMENT  CHAIN
   DESIGN'EFFICIENCY... 09.9 PERCENT eoo REDUCTION
   TREATMFNT MODULES!
Bl
e.
FI
Y.
B.
Y.
B.
B.
C.
H.
I.
K.
G.
R.
Y.
U.
N.
                         .CONTROL HCUSE
                         .PUMPING STATION
                         .MULTIPLE EFFECT
                         .MOLDING TANK
                         .PUMPING
                         .HOLDING
                         .PUMPING
                   EVAPCRATCR
           STATION
           TANK
           STATION
   PUMPING STATION
   EQUALIZATION BASIN
   NITROGEN ADDITION
   PHOSPHORUS ADDITION
   ACTIVATED SLUDGE
   SLl'CGE THICKENER
   AEROBIC DIGESTOR
   HOLDING TANK
   SPRAY IRRIGATION
   DUAL MEDIA PRESSURE FILTRA'N
   INVESTMENT COSTS:
                  i •
                  ?.
                  3.
                  4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                  TOTAL

   YEARLY OPERATING COSTS!
                  1.  LABOR
                  2.  PO'FR
                  3.  CHEMICALS
                  a.  MAINTEfUNCES-SUPPLlES
                  TOTAL

   TOTAL YEARLY COSTS:
                  i. YEARLY OPERATING COST
                  2. YEARLY INVESTMENT
                     COST RECOVERY
                  3. DEPRECIATION
                  TOTAL
                     2206140.00
                        18330,00
                      820610.00
                      220610.0.0
                     2665690.00
                      74970.00
                     341730.00
                       4390.00
                      39530.00
                     460620.00
                     460620.00

                     106630.00
                     132370.00
                     699620.00

-------
1L
O
       .9
8
    1431.8
O   1020.4
    e s i. 7
    •e«.s  >
                                                                           f£.CO
                                                Ifflfll^tl


                                      FIGURE 317


              INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY  A 24-V

-------
DRAFT
                       TABLE  317

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A24-VI
                  (MOLASSES DISTILLERS)
   ITEMIZED COST  SUMMARY  FOR  WA8TEMTER TREATMENT CHAIN
   DESIGN EFFICIENCY,.. 99.8  PERCENT  BOD REDUCTION
   TREATMENT MODULES*
           81.. CONTROL HCUSE
           B... PUSHING STATION
           FI.. MULTIPLE EFFECT  EVAPORATOR
           Y... HOLDING TANK
           B... PULPING
           Y...HGLRING
           B... PUMPING
           6. ..PUMPING
           C... EQUALIZATION BASIN
           H... NITROGEN ADDITION
           i...pHcs°H9Rus  ADDITION
           *... ACTIVATED SLUDGE
           O...SLI.-OGE THICKENER
           P...Afci»CPIC OIGE8TCF
           T...SAND DRYING REDS
                                  STATION
                                  TANK
                                  STATION
                                  STATION
   INVESTMENT CCSTSl
                   1.
                   2.
    CONSTRUCTION
    LAND
3.  ENGINEERING
4.  CONTINGENCY
TOTAL
                                 2260360.00
                                   22660.00
                                  22fiO«0.00
                                  228040.00
                                 2759100.00
   YEARLY
OPERATING
        1.
        2.
        3.
        4.
  COSTS:
    LABCR
                      CHEMICALS
                      MAIN7ENANCE8SLPPLIES
 74970,
336600,
  4390
00
00
00
                  TCTAL
                          55350.00
                         471310.00
   TOTAL YEARLY COSTS:
                  1. YEARLY OPERATING  COST  471310.00
                  2. YEARLY INVESTMENT
                     COST HFCCVERY          110360.00
                  3. DEPRECIATION           136820.00
                  TOTAL                     718490.00
                         1120

-------
DRAFT
                        TABLE  318

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A24-VII
                  (MOLASSES DISTILLERS)
   ITEMIZED COST SUMMARY FOR toASTEMTER  TREATMENT  CHAIN
   DESIGN EFFICIENCY... 99.9 PERCENT BOO  REDUCTION
   TREATMENT MODULES!
                        .CONTROL HOUSE
                        .PUMPING STATION
                        .MULTIPLE EFFECT
                        .HOLDING TANK
                        .PUMPING
                        .HOLDING
                        .PUMPING
                   EVAPCRATCR
           STATION
           TANK
           STATION
  .PUVPJNG STATION
  .EQUALIZATION BASIN
  .NITROGEN ADDITION
  .PHOSPHORUS ADDITION
  .ACTIVATED SLUDGE
  .SLUDGE THICKENER
  .AEROBIC DIGESTOR
  .SAND DRYING BEDS
  .DUAL MEDIA PRESSURE FILTRA'N
   INVESTMENT CCSTSl
                  1.
                  2.
                  3.
                  4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                  TOTAL

   YEARLY OPERATING CQSTSt
                  1.  LABOR
                  2.  POWER
                  3.  CHEMICALS
                  4.  MAINTFMANCE&SIPPLIFS
                  TOTAL
2302930.00
  22660.00
 230290.00
 230290.00
2786170.00
                            00
                            00
  74970.
 340880.
   4390.00
  55690.00
 475930.00
   TOTAL  YEARLY CCST£;
                  1.  YEARLY OPERATING COST 47^930.00
                  2.  YEARLY INVESTMENT
                     COST RECOVERY         111450.00
                  3.  TEPRECIATinN          136180.00
                  TOTAL                     725560,00
                         1121

-------
ro
ro
                   8
                   b
                   co
co
8
                            i
                            !
                       > i s. e i
                            i
                            i
                            i
                      Hi'I.2 I
                            I
                            I
                            i
                      '.««•£,« I
                  U  \:**,o
                       tf«.0
                                            <2.co
                                                        FIGURE  318

                                   INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 24-VII

-------
   DRAFT
Alternative A 24-VIII - This alternative replaces the activated sludge
and sludge handling modules in Alternative A 24-11 with an aerated
lagoon system.

The resulting BOD waste load is 1.16 kg/1000 pg (2.56 lb/1000 pg), and
the suspended solids load is 0.69 kg/1000 pg (1.52 lb/1000 pg).

               Costs:  Total investment cost:  $2,665,800
                       Total yearly cost:         800,510

An itemized breakdown of costs is presented in Table 319.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that six operators are required.

               Reduction Benefits:  BOD:  99.9 percent
                                     SS:  99.6 percent
                               i
Alternative A 24-IX - This alternative provides in addition to
Alternative A 24-VIII dual media filtration.

The resulting BOD waste load is 0.58 kg/1000 pg (1.28 lb/1000 pg), and
the suspended solids load is 0.35 kg/1000 pg (0.77 lb/1000 pg).

               Costs:  Total investment cost:  $2,692,880
                       Total yearly cost:      $  807,580

An itemized breakdown of costs is presented in Table 320.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It
is further assumed that six operators are required.

               Reduction Benefits:  BOD:  99.9 percent
                                     SS:  99.8 percent

A cost efficiency curve is presented in Figure 319.

Cost and Reduction Benefits of Alternative Treatment Technologies for
Subcategory A 25 - Bottling and Blending of Beverage Alcohol

Two model plants representative of Subcategory A 25 were developed
in Section V for the purpose of applying control and treatment alternatives.
In Section VII, three alternatives were selected as being applicable
engineering alternatives for each model plant.  These alternatives
provide for various levels of waste reductions for the model  plants.

Model plant A produces a flow of 4 cu m/day (0.001 MGD).

Alternative A 25-A-I - This alternative assumes no treatment and no
reduction in the waste load.

               Costs:               0
               Reduction Benefits:  None

-------
DRAFT
                       TABLE 319

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A24-VIII
                 (MOLASSES DISTILLERS)
   ITEMIZED COST SUMMARY FOP MSTEKATER  TREATMENT  CHAIN
   DESIGN EFFICIENCY... 99.fi PERCENT  BCD  REDUCTION
   TREATMENT MODULES}
Pi ..CONTROL HCLSE
P, . .PUFFING STATION
FI..MULTIPLE EFFECT
V...HOI.CINC TANK
e...PUMP.TNG
v.. .HOLDING
                                          EVAPORATOR
                         PUMPING
            STATION
            TANK
            STATION
            STATION
C...FQLALIZATICN: BASIN
H...MTRC6FN ADDITION
T...PHrSPHORLS ADDITION
L...AERATES LAPCOM
   INVESTMENT COSTS:
                  1.
                  2.
                  3.
                  a.
                  5.
 CONSTRUCTION
 LAND
 ENGINEERING
 CONTINGENCY
 PVC LINER
                  TCTAL

   YEARLY OPERATING CCSTSi
                  1.  LABOR

                  3!  CHEMICALS
                  5.  PVC LINER
                  TCTAL
                     2206570.00
                        5630.00
                      220660.00
                      2206*0.00
                        12080.00
                     2665800.00
                       74970.00
                      "37430.00
                             .00
                             .00
                         450.00
                      5608*0.00
   TCTAL YEARLY COSTS:
                  i. YEARLY OPERATING COST  56oeso.oo
                  2. YEARLY INVESTMENT
                     COST RECOVERY          106630.00
                  3. DEPRECIATION           133000.00
                  TOTAL
                      800510.00
                         1124

-------
DRAFT
                       TABLE  320

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A24-IX
                 (MOLASSES DISTILLERS)
   ITEMIZED COST SENARY FOP MSTEMTER TREATMENT CHAIN
   DESIGN EFFICIENCY... 99.9 PERCENT BCD REDUCTION
   TREATMENT MODULES*
                                         EVAPOPATCR
   81., CONTROL MOUSE
   8,.. PULPING STATION
   PI..MULTIPLE EFFECT
   Y...HOLDING TANK
   B...PUMPING STATION
   Y...HOLDING TANK
   B...PUMPING STATION
   P...PUMPING STATION
   C...EQUALIZATION BASIN
   H...NITROGEN ADDITION
   I...PHCSPWORLS ADDITION
   L...AERATED LAGOON
   N...DU*L MFRIA PRESSURE FRTRA'N
INVESTMENT COSTS:
               1.
               2.
               3.
               4.
               5.
               TOTAL

YEARLY OPERATING COSTS:
               1.  LABOP
               £f t  * L * t • *
               3.  CHEMICALS
                      CCNSTKUCTICN
                      LAND
                      ENGINEERING
                      CONTINGENCY
                      FVC L
5.  PVC
TCTAL
                          LINER
                        2229150.00
                           5P30.00
                         222910.00
                         2P2910.00
                           12080.00
                        2692B80.00
 74970.00
441700.00
  4390.00
 44000.00
   450.00
565510.00
   TCTAL  YEARLY CCSTSJ
                  i.  VEARLY OPERATING COST 5655io.oo
                  2,  YEARLY INVESTMENT
                     COST rtECCVERY
                  3.  DEPRECIATION
                  TCTAL                    807580,00
                         107720.
                         134350.
                                                00
                                                00
                          1125

-------
ro
                          Z-tfU.t
                      8
                          2fle7.S
                          t.

                      8
                      w
                      CL.
                      <
                      u
                               «C.Cfl    *1.CO
                                                            FIGURE 319


                                    INVESTMEISTT AND YEARLY COSTS FOR SUBCATEGORY A  24-IX
                                                                                                                  ioo.cc

-------
   DRAFT
Alternative A 25-A-II - This alternative provides daily truck hauling
of all plant process wastes to municipal treatment facilities or
approved land disposal sites.  A holding tank is provided.

The resulting BOD waste load is zero, and the suspended solids load is
zero.

               Costs:  Total investment cost:  $12,860
                       Total yearly cost:      $16,470

An itemized breakdown of costs is presented in Table 321.  It is assumed
that land costs $4100 per hectare ($1660 per acre).  It is further
assumed that no operators are required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent

Alternative A 25-A-III - This alternative provides for spray irrigation
of the final effluent.  A holding tank, pump, and pipelines are provided.

The resulting BOD waste load is zero, and the suspended solids load is
zero.

               Costs:  Total investment cost:  $38,270
                       Total yearly cost:      $ 5,210

An itemized breakdown of costs is presented in Table 322.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It
is further assumed that no operators are required.

               Reduction Benefits: BOD:  100 percent
                                    SS:  100 percent

Model plant B has a flow of 40 cu m (0.01 MG) per day.

Alternative A 25-B-I - This alternative assumes no treatment and no
reduction in the waste load.

               Costs:               0
               Reduction Benefits:  None

Alternative A 25-B-II - This alternative provides daily truck hauling
for all plant process wastes to municipal treatment facilities or
approved land disposal sites.  A holding tank is provided.

The resulting BOD waste load is zero, and the suspended solids load is
zero.

               Costs:  Total investment cost: $ 14,670
                       Total yearly cost:     $153,470
                                 1127

-------
DRAFT
                       TABLE 321

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A 25-A-II
         (BOTTLING AND BLENDING OF BEVERAGE ALCOHOL)
  ITEMIZED  COST  SUMMARY  FOR WA8TEMTER TREATMENT CHAIN
  DESIGN  EFFICIENCY...100.0 PERCENT BOO REDUCTION
  TREATMENT  MCDULE8»
                     Y...HOLDING TANK
                     V...  TRICK HAILING
  INVESTMENT  COSTS!
                  1.
                  2.
                  3.
    CONSTRUCTION
    L*ND
    ENGINEERING
4.  CONTINGENCY
TOTAL
  YEARLY
OPERATING
        1.
        2.
        3.
        a.
  TOTAL YEARLY
  CGSTS:
    LABOR
    POWER
    CHEMICALS
    MAINTFNANCE&SUPPLIES
        TCTAL

      CCSTSJ
        1. YEARLY OPERATING  COST
        2. YEARLY INVESTMENT
           COST RECOVERY
        3. DEPRECIATION
        TCTAL
                                    6490.00
                                    2670.00
                                     650.00
                                     650.00
                                   12660,00
                                                0.0
                                                0.0
                                                0.0
                                            isaso.oo
                                            isaso.oo
                                            15450.00

                                              510.00
                                              510.00
                                            16470.00
                          1128

-------
                    TABLE  322

     ITEMIZED COST SUMMARY FOR ALTERNATIVE A 25-A-IH
      (BOTTLING AND BLENDING OF BEVERAGE ALCOHOL)
ITEMIZED  COST  SWAflY FOP
DESIGN EFFICIENCY. ..100.0
                           MSTEMTFtf TREATMENT CHAIN
                           PERCENT  qQD REDUCTION
TREATMENT MODULES}
                   V... HOLDING
                   U... SPRAY
                               TANK
CCNSTPUCTICKi
INVESTMENT CCSTS:
                1.
                2.
                3.   ENGINEERING
                «.   CCN1INGENCY
                TCTAL

YEARLY CPbRATII^G CCSTSs
                1.   LABOR
                2.   PCfcFR
                3.   CHEMICALS
                u.   M*INTENANCERSUPPLIES
                TCTAL

TCTAL YEARLY CCSTSt
                1. YEARLY  CPERJTIKG  CCST
                2. YEARLY  INVESTMENT
                  CCST RECCVEfrY
                3. DEPRECIATION'
                                          2<»3SO,00
                                           3000.00
                                           2940,00
                                          38270.00
                                              0.0
                                            ftao.00
                                              0.0
                                           ioeo.oo
                                           1920.00
                                           1920.00

                                           1530.00
                                           1760.00
                                           5210.00
                       1129

-------
 ,,RAFT
Vi itemized breakdown of costs is presented in Table 323.   It is
assumed that land costs $4100 per hectare ($1660 per acre).   It is
further assumed that no operators are required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent

Alternative A 25-B-III - This alternative provides truck hauling on
a monthly basis for redistillation residue, bad product, and deminer-
alizer regeneration.  It is assumed these wastes are collected in
holding tanks.  All other process wastes are spray irrigated.  A
holding tank, pump, and pipeline are provided.

The resulting BOD waste load is zero, and the suspended solids load
is zero.

               Costs:  Total investment cost:  $48,860
                       Total yearly cost:      $ 6,360

An itemized breakdown of costs is presented in Table 324.   It is
assumed that land costs $4100 per hectare ($1660 per acre).   It
is further assumed that no operators are required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent

Cost and Reduction Benefits of Alternative Treatment Technologies for
Subcategory A 26 - Soft Drink Canners

A model plant representative of Subcategory A 26 was developed in
Section V for the purpose of applying control and treatment alter-
natives.  In Section VII, seven alternatives were selected as being
applicable engineering alternatives.  These alternatives provide
for various levels of waste reductions for the model plant which
produces 309 cu m (81,500 gal) per day.

Alternative A 26-1  - This alternative assumes no treatment and no re-
duction in the waste load.  It is estimated that the effluent from a
309 cu m (81,500 gal) per day plant is 229 cu m (0.0605 MG)  per day.
The BOD waste load is 1.02 kg/cu m (0.505 lb/1000 gal), and the
suspended solids load is 0.123 kg/cu m (1.03 lb/1000 gal).

               Costs:               0
               Reduction Benefits:  None

Alternative A 26-11 - This alternative provides a control  house, flow
equalization, nutrient addition, a complete mix activated  sludge
system, sludge thickening, and spray irrigation of sludge.

The resulting BOD waste load is 0.052 kg/cu m (0.43 lb/1000 gal), and
the suspended solids load is 0.030 kg/cu m (0.25 lb/1000 gal).
                                1130

-------
DRAFT
                        TABLE  323

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A 25-B-II
          (BOTTLING AND BLENDING OF BEVERAGE ALCOHOL)
     ITEMIZED  COST  SUMMARY FOR MSTEMTER TREATMENT  CHAIN
     DESIGN  EFFICIENCY...100.0 PERCENT BOD REDUCTION

     TREATMENT  MODULES*
                       Y...HOLDING TANK
                       V... TRUCK HAILING

     INVESTMENT CCSTS:
                    1,   CONSTRICTION            9940.00
                    2.   LAND                    2750.00
                    3.   ENGIKiEEPING              990.00
                    4.   CONTINGENCY              990.00
                    TOTAL                      14670.00

     YEARLY  OPERATING COSTS:
                    1.   LABOR                      0.0
                    2.   POWER                      0.0
                    3.   CHEMICALS                  0.0
                    fl.   MAINTENANCFRSLPPLIES  152280.00
                    TOTAL                     152280.00

     TOTAL  YEARLY  COSTS*
                    1.  YEARLY OPERATING COST  152280.00
                    2.  YEARLY INVESTMENT
                       COST RECOVERY             590.00
                    3.  DFPRECIATION              600.00
                    TOTAL                     153470.00
                          1131

-------
DRAFT
                        TABLE  324

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A 25-B-III
          (BOTTLING AND BLENDING OF BEVERAGE ALCOHOL)
   ITfMlZED  COST  SlfVAPY FO? fcASTE'*ATER  TREAT*£KT CHAl*
   DESIGN  EFFICIENCY...100.0 PERCENT  BOO REDUCTION

   TREATMFNT MOuULESj
                      Y...HOLDING  TA*;K
                      U...SPHAY  IRRIGATION

   INVESTMENT COSTS*
                   I.  CCN3T^UCTIO^           37110.00
                   2.  L4ND                    U330.00
                   3.  ENGIMEEHIMR             37io.oo
                   y.  CTNTINC-ffNTY             3710.00
                   TCT4L                      48860.00

   YEARLY  OPERATING CCfTS:
                   1.  LA 60ft                      0.0
                   2.  PC I* EH                    880.00
                   3.  CHEMICALS                  0.0
                   0.  f'AI.-JTFK;AMCr:*iSL.PPL.II£S   1300,00
                   TCTil.                       21PO.OO

   TOTAL  YEARLY CCSTS:
                   1. YtARLY CPERAT1NG  COST   2180.00
                   2. YFiKLY INVESTMENT
                      COST HECTVFRY            1950.00
                   3. DEPSECIATION             2230.00
                   TCTAL                       6360.00
                          1132

-------
  DRAFT


               Costs:  Total investment cost:  $238,880
                       Total yearly cost:      $ 49,390

An itemized breakdown of costs is presented in Table 325.  It is
assumed  that land costs $41,000 per hectare ($16,600 per acre).  It
is further assumed that one operator is required.

               Reduction Benefits:  BOD:  94.9 percent
                                     SS:  76.0 percent

Alternative A 26-III - This alternative provides in addition to Alter-
native A 26-11 dual media filtration.

The  resulting BOD waste load is 0.026 kg/cu m (0.22 lb/1000 gal), and
the  suspended solids load is 0.015 kg/cu m (0.13 lb/1000 gal).

               Costs:  Total investment cost:  $258,070
                       Total yearly cost:      $ 55,010

An itemized breakdown of costs is presented in Table 326.  It is
assumed  that land costs $41,000 per hectare ($16,600 per acre).  It
is further assumed that one operator is required.

               Reduction Benefits:  BOD:  97.5 percent
                                     SS:  88.1 percent

A cost efficiency curve is presented in Figure 320.

Alternative A 26-IV  - This alternative provides a control house, flow
equalization, nutrient addition, a complete mix activated sludge system,
and  sludge thickening.

The  resulting BOD waste load is 0.052 kg/cu m (0.43 lb/1000 gal), and
the  suspended solids load is 0.030 kg/cu m (0.25 lb/1000 gal).

               Costs:  Total investment cost:  $210,270
                       Total yearly cost:      $ 47,070

An itemized breakdown of costs is presented in Table 327.  It is
assumed  that land costs $41,000 per hectare ($16,600 per acre).  It
is further assumed ,that one operator is required.

               Redaction Benefits:  BOD:  94.9 percent
                                     SS:  76.0 percent

Alternative A 26-V - This alternative provides,™ addition  to  alter-
native A 26-IV dual  media  filtration.
The resulting BOD waste load is 0.026 kg/cu m (0.22 lb/1000 gal), and
the suspended solids load is 0.015 kg/cu m (0.13 lb/1000 gal).
                                1133

-------
DRAFT
                          TABLE 325

         ITEMIZED COST SUMMARY FOR ALTERNATIVE
                   (SOFT DRINK CANNERS)
                    A 26-11
   ITEMIZED COST  SUMMARY  FOR  WA3TCMTER TREATMENT CHAIN
   DESIGN EFFICIENCY... 95,0  PERCENT BOD REDUCTION
   TREATMENT MODULES?
                      Bl..CONTROL  HCL'SE
                      §...PUMPING  STATION
                      C...EQUALIZATION BASIN
                      H...NITROGEN ADDITION
                      K...ACTIVATED SLUDGE
                      C...SLUDGE  THICKENER
                      Y...HULDING  TANK
                      U...SPRAY  IRRIGATION
   INVESTMENT CCSTSl
                   1.
                   2.
                   3.
                   4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                   TOTAL

   YEARLV OPERATING CCSTSl
                   1.   LAPPR
                   2.   PCIA-ER
                   3.   CHEMICALS
                   4.   MAINTENANCE&SUPPLIES
                   TOTAL
165180.00
 16660.00
 16520.00
 16520.00
238880.00
                       12490.00
                       9940.00
                        890.00
                       5400.00
                       26720.00
   TOTAL YEARLY CCSTSl
                  1. YEARLY CPERATIKG  CCST   28720.00
                  2. YEARLY INVEST^EK;T
                     COST RECOVERY            9560.00
                  3. DEPRECIATION            11110.00
                  TOTAL                      49390.00
                          1134

-------
DRAFT
                          TABLE  326

       ITEMIZED COST SUMMARY FOR ALTERNATIVE
                    (SOFT DRINK CANNERS)
                A 26-111
    ITEMIZED COST  SUMMARY  FOR
    DESIGN EFFICIENCY... 97.5
       toASTEMTER TREATMENT CHAIN
       PERCENT BOP REDUCTION
    TREATMENT MODULES*
                       Bl..CONTROL  HCUSE
                       B...PULPING  STATION
                       C...EQUALIZATION  BASIN
                       H...NITROCFN  ADDITION
                       K...ACTIVATED  SLUDGE
                       Q...SLUDGE  THICKENER
                       Y...HOLDING  TANK
                       U...SPRAY  IRRIGATION
                       B..,PUMPING  STATION
                       N...DUAL MEDIA  PRESSURE  FILTPA'N
    INVESTMENT COSTS!
                   1.
                   2.
                   3.
                   4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                   TOTAL

    YEARLY OPERATING CCSTSi
                   1.  LABOR
                   2.  POfcER
                   3.  CHEMICALS
                   4.  MAINTENANCEISUPPLIES
                   TOTAL

    TOTAL YEARLY COSTS:
                   i. VEARLY OPERATING  COST
                   2. YEARLY INVESTMENT
                      COST RECOVERY
                   3. DEPRECIATION
                   TOTAL
201170.00
 16660.00
 20120.00
 20120.00
258070.00
                      12490.00
                      12850.00
                        890.00
                       6390.00
                      32620.00
                      32620.nO

                      10320.00
                      12C70.00
                      55010.00
                           1135

-------
co
en
                 o:
                 <
                  IL

                  O
                      217.C
                      l«*.C
                  
-------
JRAFT
                          TABLE 327

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A 26-IV
                   (SOFT DRINK CANNERS)
   ITEMIZED COST SUMMARY FDR MASTffcAYER  TREATMENT  CHAIN
   DESIGN EFFICIENCY... 95.0 PERCENT BOD  REDUCTION
   TREATMENT MGOULESt
                     Bl..CONTROL HCU8E
                     8...PUMPING STATION
                     C..,EQUALIZATION BASIN
                     H...NITHOGEN ADDITION
                     K...ACTIVATED SLUDGE
                     C...8LIOGE THICKENER
                     Y...HOLDING TANK
   INVESTMENT CCST85
                  1.
                  2.
                  3.
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
   YEARLY
OPERATING
        1.
  COSTS*
    LABOR
2,  POWER
3.  CHEMICALS
4.  MAINTEMNCE4SIPPLIES
TOTAL
   TOTAL  YEARLY CGSTSl
                  1. YEARLY OPEPATING COST
                  2. YEARLY INVESTMENT
                     CPST RECt-VERY
                  3. DEPRECIATION
                  TOTAL
                                  153010.00
                                   26660.00
                                   15300.00
                                   15300.00
                                  210270.00
                                             12U90.
                                             9100.
                                              890.
                                             7000.
                                             29480,
00
00
00
00
00
                                   29«80eOO

                                    8410.00
                                    9180.00
                                   47070.00
                          1137

-------
  JRAFT


               Costs:  Total  Investment cost:   $227,790
                       Total  yearly cost:       $ 52,630

An itemized breakdown of costs is presented in Table 328.* It is
assumed that land cost $41,000 per hectare ($16,600 per acre).   It
is further assumed that one operator is required.

               Reduction Benefits:  BOD:   97.5 percent
                                     SS:   88.1 percent

A cost efficiency curve is presented in Figure 321.

Alternative A 26-VI - This alternative provides flow equalization,
nutrient addition, and an aerated lagoon  system.

The resulting BOD waste load is 0.052 kg/cu m (0.43 lb/1000 gal), and
the suspended solids load is 0.030 kg/cu  m (0.25 lb/1000 gal).

               Costs:  Total  investment cost:   $204,690
                       Total  yearly cost:       $ 66,240

An itemized breakdown of costs is presented in Table 329.   It is
assumed that land costs $4100 per hectare (1660 per acre).   It is
further assumed that one operator is required.

               Reduction Benefits:  BOD:   94.9 percent
                                     SS:   76.0 percent
Alternative A 26-VII - This alternative provides in addition to Alter-
native A 26-VI dual media filtration.

The resulting BOD waste load is 0.026  kg/cu m (0.22 lb/1000 gal), and
the suspended solids load is 0.015 kg/cu m (0.13 lb/1000 gal).

               Costs:  Total investment cost:  $223,890
                       Total yearly cost:      $ 71,860

An itemized breakdown of costs is presented in Table 330.   It is
assumed that land costs $4100 per hectare ($1660 per acre).   It is
further assumed that one operator is required.

               Reduction Benefits:  BOD:  97.5 percent
                                     SS:  88.1 percent

A cost efficiency curve is presented in Figure 322.

Cost and Reduction Benefits of Alternative Treatment Technologies
for Subcategory A 27 - Soft Drink Bottling or Combined
Bottling/Canning Plants

A model plant representative of Subcategory A 27 was developed  in
Section V for the purpose of applying  control and treatment alter-
                                1138

-------
DRAFT
                         TABLE  328

         ITEMIZED COST SUMMARY FOR ALTERNATIVE  A 26-V
                    (SOFT DRINK CANNERS)
    ITEMIZED  COST  SUMMARY  FDR
    DESIGN  EFFICIENCY...  97.5
WASTEMTER TREATMENT CHAIN
PERCENT BOO REDUCTION
    TREATMENT  MODULESt
                      81..CONTROL HCUSE
                      8...PUMPING STATION
                      C...EQUALIZATION BASIN
                      H...NITROGEN ADDITION
                      K...ACTIVATED SLUDGE
                      Q...8LLDGF  THICKENER
                      Y..,HOLDING TANK

                      N...DUAL MEDIA PRESSURE FILTRA'N
    INVESTMENT  COSTSt
                   1.
                   2.
                   3.
    CONSTRUCTION-
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
   YEARLY OPERATING  CCSTSi
                   1.   LABOW
                   2.   POi«ER
                   3.   CHEMICALS
                   4.   KA1MTENANCERSLPPLIES
                   TOTAL

   TOTAL YEARLY CCSTSt
                   1.  YF.ARLY  OPERATING  COST
                   2.  YEARLY  INVESTMENT
                      COST  RECOVERY
                   3.  DEPRECIATION
                   TOTAL
              169000.00
               24990.00
               16900.00
               16900.00
              227790.00
               12490.00
               12010.00
                 890.00
                7990.00
               33380.00
               33380.00

                9110.00
               10UO.OO
               52630.00
                          1139

-------
CO
LL
O
LU
<
X**
u
    r?-.0 I
     !
-------
^RAFT
                          TABLE  329

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A26-VI
                   (SOFT DRINK CANNERS)
    ITEMIZED  COST SUMMARY FOR WA8TEKATER TREATMENT CHAIN
    DESIGN  EFFICIENCY..,  94,3 PERCENT BOD REDUCTION
    TREATMENT  MODULES*
                      B...PUMPING STATION
                      C...EQUALIZATION BASIN
                      H...NITROGEN ADDITION
                      L...AERATED LAGOON
    INVESTMENT  CCSTSl
                   1.
                   2.
                   3.
                   4.
                   5.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
PVC LINER
                   TOTAL

    YEARLY  OPERATING CCSTSl
                   1.  LABOR
                   2.  PO*FR
                   3.  CHEMICALS
                   4.  MAINTENANCE&SUPPLIES
                   5.  PVC LINFR
                   TOTAL

    TOTAL YEARLY  COSTS!
                   1. YEARLY OPERATING COST
                   2. YEARLY INVESTMENT
                      COST RECOVERY
                   3. DEPRECIATION
                   TOTAL
164360.00
  3580,00
 16440.00
 16440.00
  3870.00
204690.00
                       6250.00
                      35460.00
                        890.00
                       5210.00
                        160.00
                      47990.00
                      47990.00

                       8190.00
                      10060.00
                      66240.00

-------
L'RAFT
                          TABLE  330

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A26-VII
              (SOFT DRINK CANNERS)
    ITEMIZED COST SUMMARY FOR WASTEMTER TREATMENT CHAIN
    DESIGN EFFICIENCY... 97.5 PERCENT BCD REDUCTION
    TREATMENT MODULES:
                      B...PUMPING STATION
                      C...EQUALIZATION BASIN
                      H...NITROGEN ADDITION
                      L...AERATED LAGOCN
                      8...PULPING STATION
                      N...DUAL MEDIA PRESSURE FILTRA'N
    INVESTMENT CCSTSi
                   1.
                   2,
                   3.
                   4.
                   5.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC LINER
                   TOTAL
    YEARLY
OPERATING
        1.
        2.
        3.
        4.
        5.
COSTS:
  LABOR
  POWER
  CHEMICALS
  MAINTENANCE&SLPPLIES
  PVC LINER
                   TOTAL

    TOTAL  YEARLY  COSTS!
                   1.  YEARLY OPERATING COST
                   2.  YEARLY INVESTMENT
                      COST RECOVERY
                   3.  DEPRECIATION
                   TOTAL
                        180360.00
                         3580.00
                         18040.00
                         18040.00
                               00
 3870
                                  223890.00
                                              6250,
                                             38390,
                                               890,
                                              6190,
      00
      00
      00
      00
  160.00
51880.00
                                   51680.00

                                    8960.00
                                   11020.00
                                   71860.00
                           1142

-------
                  c/v
                  Q.
                  O


                  8
                  8
                      iC?.J I
                      !««.«.
57e.o
                       •'.«
                                                                                                                               I
co
                   ID
                     113. J
                   O
                    .
                   O
                        , * •'
                      f=!.c I
                                                         FIGURE 32X


                              INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A  26,  ALT. VII

-------
  ORAFT

ru fives.  In Section VII, seven alternatives were selected as being
applicable engineering alternatives.  These alternatives provide for
various levels of waste reductions for the model  plant which produces
136 cu m (35,900 gal) per day.

Alternative A 27-1 - This alternative assumed no treatment and no re-
duction in the waste load.  It is estimated that the effluent from
a 136 cu m (35,900 gal) per day plant is 477 cu m (0.126 MG) per day.
The BOD waste load is 2.30 kg/cu m (19.2 lb/1000 gal), and the
suspended solids load is 0.38 kg/cu m (3.2 lb/1000 gal).

               Costs:               0
               Reduction Benefits:  None

Alternative A 27-11 - This alternative provides a control house,
flow equalization, neutralization, nutrient addition, a complete mix
activated sludge system, sludge thickening, and spray irrigation of
sludge.

The resulting BOD waste load is 0.24 kg/cu m (2.00 lb/1000 gal), and
the suspended solids load is 0.14 kg/cu m (1.17 lb/1000 gal).

               Costs:   Total  investment cost:   $289,990
                       Total  yearly cost:       $  65,980

 An itemized breakdown of costs is presented in Table 3:jl.   It is
 assumed that land costs $20,510 per hectare ($8300  per acre).   It is
 further assumed that one operator is required.

               Reduction Benefits:  BOD:   89.4 percent
                                     SS:   63.0 percent

 Alternative A 27-111 - This  alternative provides in addition to
 Alternative A 27-11 dual  media filtration.

 The resulting BOD waste load is 0.123 kg/cu m (1.03 lb/1000 gal), and
 the suspended solids load is 0.07 kg/cu m (0.584 lb/1000 gal).

               Costs:   Total  investment cost:   $313,900
                       Total  yearly cost:       $  72,700

 An itemized breakdown of costs is presented in Table 332.   It is
 assumed that land costs $41,000 per hectare ($16,600 per acre).   It
 is further assumed that one  operator is required.

               Reduction Benefits:  BOD:   94.7 percent
                                     SS:   81.5 percent

 A cost efficiency curve is  presented in Figure 3J3.

 Alternative A 27-IV - This  alternative provides  a control  house, flow
 equalization, neutralization, nutrient addition, a  complete-mix activated
 sludge system,  and sludge thickening.
                                1144

-------
DRAFT
                       TABLE  331

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A27-II
              (SOFT DRINK PLANTS EXCEPT A26)
 ITEMIZED COST SUMMARY FOR I»ASTEWAT€R TREATMENT  CHAIN
 DESIGN EFFICIENCY... 89,4 PERCENT 800 REDUCTION
 TREATMENT MODULES!
                   EM ..CONTROL HOUSE
                   B...PULPING STATION
                   C...EQUALIZATION BASIN
                   F...ACID NEUTRALIZATION
                   H...NITROGEN ADDITION
                   «... ACTIVATED SLUDGE
                   Q...SLLDGE THICKENER
                   Y...HOLDINr, TANK
                   u...SPRAY IRRIGATION
INVESTMENT COSTSi
               1.  CONSTRUCTION
               2.  LAND

               til  CONTINGENCY
               TCTAl
                 COSTSi
                   LA80P
                   PCXER
                   CHEMICALS
 YEARLY OPERATING
                1
                2
                3
                a.  P
                TCTAL
 TOTAL YEARLY COSTS!
                1. YEARLY CREATING COST
                2. YEARLY INVESTMENT
                   CCST MFCCVFKY
                3. DEPRECIATION
                TCTAL
                                          225690,00
                                           19160,00
                                           22570,00
                                           22570.00
                                          289990.00
18740.00
11580.00
 "520.00
 6000,00
"0840.00
                                          40840.00

                                          11600.00
                                          135^0.00
                          1145

-------
DRAFT
                       TABLE 332

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A27-III
              (SOFT DRINK PLANTS EXCEPT A26)
 ITEMIZED  COST  SUMMARY FOR M8TEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY...  94.7 PtRCENT BCD "EDUCTION
 TREATMENT  MCDULESj
                   Bl..CONTROL MCtSE
                   B...PUMPING STA
                   C...EQUALIZATION BASIN
                   P...ACID NEUTRALIZATION
                   H...NITROGEN ADDITION:
                   K...ACTIVATED SLUDGE
                   6...SLUDGE THICKENER
                   V... HOLD ING TANK
                   U...SPRAY IRRIGATION
                   B...PUMPING STATION
                   N'...DUAL MEDIA PRESSURE FILTRA'N
 INVESTMENT  CCSTS:
                1.
                2.
                3.
                4.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
                TCTAL
YEARLY
OPERATING
        1.
        2.
        3.
                  CCSTSl
                    LABOR
                    CHEMICALS
                TOTAL
                               RSLPPLIES
 TOTAL  YEARLY  COSTS!
                1.  YEARLY OPERATING COST
                2.  YEARLY INVESTMENT
                   COST RECOVERY
                3.  DEPRECIATION
                TOTAL
                                         2a5620.00
                                          19160.00
                                          24560.00
                                          24560.00
                                         313900.00
                                          15830.00
                                           4520.00
                                           6310.00
                                          45400.00
                                   45400.00

                                   12560.00
                                   14740.00
                                   7270.0.00
                          1146

-------
     3t».o

-------
  DRAFT
 The resulting BOD waste load is 0.24 kg/cu m (2.00 lb/1000 gal), and the
 suspended solids load is 0.14 kg/cu m (1.17 lb/1000 gal).

               Costs:  Total investment cost:  $264,650
                       Total yearly cost:      $ 61,140

 An itemized breakdown of costs is presented in Table 333.  It  is>-
 assumed that land costs $41,000 per hectare ($16,600 per acre).  It
 is further assumed that one operator is required.

               Reduction Benefits:  BOD: 89.4 percent
                                     SS: 63.0 percent

 Alternative A 26-V - This alternative.'orovides in addition to Alternative
 A 2fi-IV dual media filtration.

 The resulting BOD waste load is 0.123 kg/cu m (1.03 lb/1000 gal), and
 the suspended soljds load is 0.07 kg/cu m (0.584 lb/1000 gal).


              Costs:  Total investment cost:  $288,560
                      Total yearly cost:      $ 67,840

An itemized breakdown of costs is presented in Table 334.  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that one operator is required.

              Reduction Benefits:  BOD:  94.7 percent
                                    SS:  81.5 percent

A cost efficiency curve is presented in Figure 324.

Alternative^ 27-VI - This alternative provides flow equalization,
neutralization, nutrient addition, and an aerated lagoon system.

The resulting BOD waste load is 0.24 kg/cu m (2.00 lb/1000 gal), and
the suspended solids load is 0.14 kg/cu m (1.17 lb/1000 gal).
                 •
              Costs:  Total investment cost:  $243,870
                      Total yearly cost:      $ 78,820

An itemized breakdown of costs is presented in Table 335.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one operator is required.

              Reduction Benefits:  BOD:  89.4 percent
                                    SS:  63.0 percent

Alternative A 27-VII - This alternative provides in addition to Alter-
native A 27-VI dual media filtration.

The resulting BOD waste load is 0.123  kg/cu m (1.03 lb/1000 gal), and
the suspended solids load is 0.07 kg/cu m (0.584 lb/1000 gal).


                                1148

-------
DRAFT
                       TABLE  333

        ITEMIZED COST SUMMARY FOR ALTERNATIVES A27-IV
              (SOFT DRINK PLANTS EXCEPT A26)
 ITEMIZED COST SUMMARY FDR WA3TEMTEH  TREATMENT  CHAIN
 DESIGN EFFICIENCY... 89.4 PERCENT  BOO  REDUCTION
 TREATMENT MODULES*
                   81
                   P.
                   C.
                   F.
                   H.
                   K.
                   C.
                   V.
              .CONTROL HCLSE
              .PUMPING STATION
              .EOUAL1ZATICN BASIN
              .ACID NEUTRALIZATION
              .NITROGEN' ADDITION
              .ACTIVATED SLUDGE
              .SLUDGE THICKENER
              .HOLDING TANK
 INVESTMENT CCST5J
                1.
                2.
                3.
                4.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
                TOTAL
 YEARLY
OPERATING
        1.
        2.
        3.
        4.
COSTS:
  LABOR
  POWER
  CHEMICALS
  MAINTEN4NCE8SLPPLIES
                TOTAL

 TOTAL YEARLY CCSTSl
                1. YEARLY OPERATING  COST
                2. YEARLY INVESTMENT
                   COST RECOVERY
                3. DEPRECTATIDM
                TOTAL
                        194160.00
                        31650
                         19U20
      00
      00
      00
                                  264650.00
18740.00
10740.00
 4520.00
 4900.00
38900.00
                                   38900.00

                                   10590.00
                                   11650.00
                                   61140.00
                          1149

-------
DRAFT
                       TABLE 334

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A27-V
              (SOFT DRINK PLANTS EXCEPT A26)
 ITEMIZED COST  SUMMARY  FOR  MSTEMTER TREATMENT CHAIN
 DESIGN EFFICIENCY... 94,7  PERCENT  80D REDUCTION
 TREATMENT MODULESi
                    81.. CONTROL  HCl'SE
                    8...PULPING  STATION
                    C...EQUALIZATION BASIN
                    F...ACID  NEUTRALIZATION
                    H...NITROGEN ADDITION
                    K...ACTIVATED SLUDGE
                    Q... SLUDGE  THICKENER
                    Y...HOUDTNG  TANK
                    8...PUMPING  STATION
                    N...DUAL  MEDIA PRESSURE FILTRA'N
 INVESTMENT COSTS*
                 1.
                 2.
                 3.
                 4.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
                 TOTAL
 YEARLY
OPERATING
        1.
        2.
        3.
        a.
COSTS:
  LABOR
  PCWER
  CHEMICALS
  MAINTENANCE&SLPPLIES
                 TOTAL

 TOTAL YEARLY COSTS:
                 1.  YEARLY  OPERATING  COST
                 2.  YEARLY  INVESTMENT
                    COST  RECOVERY
                 3.  DEPRECIATION
                 TOTAL
                       21«090.00
                        31650.00
                        21410.00
                        21410.00
                       288560.00
19740.00
1*1990.00
 4520.00
 5200,00
43450.00
                                   43450.00

                                   11540.00
                                   12850.00
                                   67840.00
                          1150

-------
    2P9.0
8

u.
o
   l18-6
   i«7.e
o
a

6
        oc.c:    «i.ic     fi.if     ««.^c    «t.::     ir.«;    ««.9t     «o.«
                                                EFFICIENCY




                                  FIGURE 324




        INVESTMENT MID  YEARLY COSTS  FOR SUBCATEGORY A 27, ALT. V
                                                                                   93.50

-------
DRAFT
                       TABLE 335

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A27-VI
              (SOFT DRINK PLANTS EXCEPT A26)
ITEMIZED COST SLMMAPY FOR  WASTEMTER  TREATMENT CHAIN
DESIGN EFFICIENCY... B9.
-------
  DRAFT
              Costs:  Total investment cost:   $267,780
                      Total yearly cost:      $ 85,530

An itemized breakdown of costs is presented in Table 336.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one operator is required.

              Reduction Benefits:  BOD:  94.7 percent
                                    SS:  81.5 percent

A cost efficiency curve is presented in Figure 325.

Cost and Reduction Benefits of Alternative Treatment
Technologies for. Subcategory A 28 - Beverage Bases

A model plant representative of subcategory A 28 was developed in
Section V for the purpose of applying control and treatment alter-
natives,  In Section VII, thirteen alternatives were selected as being
applicable engineering alternatives.  These alternatives provide for
various levels of waste reductions for the model plant which produces
379 cu m (0.10 M|) of beverage bases per day,
It is estimated that the effluent from a 379 cu m (0.10 M§) per day
plant is 379 cu m (0.10 MG) per day.  The BOD waste load is 0.24
kg/cu m (2.00 lb/1000 gal), and the suspended solids load is 0.05
kg/cu m (0.42 lb/1000 gal).

Alternative A 28-1 - This alternative consists of a pumping station, a
flow equalization tank, and an aerated lagoon.

The resulting BOD waste load is 0.010 kg/cu m (0.084 lb/1000 gal), and
the suspended solids load is 0.003 kg/cu m (0.025 lb/1000 gal).

              Costs:  Total investment cost:   $290,570
                      Total yearly cost:      $114,720

An itemized breakdown of costs is presented in Table 337.   It  is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one operator is required.

              Reduction Benefits:  BOD:  95.8 percent
                                    SS:  40.0 percent

Alternative A 28-11 - This alternative consists of a pumping station,
a flow equalization tank, a complete-mix activated sludge basin, a
sludge thickner, an aerobic digestor, and a sludge holding tank
followed by land application of the digestor sludge.

The resulting BOD waste load is 0.018 kg/cu m (0.084 lb/1000 gal), and
the suspended solids load is 0.003 kg/fcu m  (0.025  lb/1000 gal).
                               1153

-------
DRAFT
                       TABLE 336

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A27-VII
              (SOFT DRINK PLANTS EXCEPT A26)
 ITEMIZED COST  SUMMARY  FOR  WASTEMTER TREATMENT CHAIN
 DESIGN EFFICIENCY...  94.7  PERCENT BOD REDUCTION
 TREATMENT  MODULES?
                    B...PUMPING  STATION
                    C...EQUALIZATION BASIN
                    F...ACID  NEUTRALIZATION
                    H...NITROGEN ADDITION
                    L...AERATED  LAGGON
                    B...PUMPING  STATION
  INVESTMENT  COSTS*
                 1.
                 2.
                 3.
                 4.
                 5.
           N...DUAL
            CONSTRUCTION
            LAND
            ENGINFEPIMG
            CONTINGENCY
            PVC L
                 TOTAL
                                   PRESSURE FILTRA>N
                       215810.00
                          4160.00
                         21580.00
                         21580.00
                          4650.00
                       267780.00
 YEARLY
OPERATING
        1.
        2.
        3.
        4.
        5,
COSTSl
  LABOR
                     CHEMICALS
                     MAINTENANCE&SLPPLIES
                     PVC  LINER
                 TOTAL

 TOTAL YEARLY  CCSTSl
                 1.  YEARLY  CPERATIKG COST
                 2,  YEARLY  INVESTMENT
                    COST  RECOVERY
                 3.  DEPRECIATION
                 TOTAL
124QQ.
38460.
 4520,
 5850,
00
00
00
00
                          320.00
                        61640.00
                                   61640.00

                                   10710.00
                                   13180.00
                                   85530.00
                          1154

-------
                      Ztt.O
cn
en
                  I
                  H   253.C
                      211.C
                  in




                  5

                  z
                      173.C
                  O
                  O
                       „.,
                                          53. c:
                                                               EFFICIENCY



                                                       FIGURE  325
                                                                                                                            73
                                                                                                                            f-
                                                                                                    «i.5e    «5.eo
                               INVESTMENT WD  YEARLY COSTS FOR SUBCATEGORY A 27, ALT.  VII

-------
DRAFT
                       TABLE  337

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-I
                  (BEVERAGE BASE SYRUP)
 ITEMIZED  COST  SUMMARY  FOR  WA3TEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY,..,95.8  PERCENT BCD REDUCTION
TREATMENT  MODULESi
                   8...PUMPING STATION
                   C...EQUALIZATION BASIN
                   L...AERATED LAGOON
INVESTMENT COSTS*
                i.
                2.
                3.
                4.
                5.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC LINER
                TOTAL
YEARLY
OPERATING
        1.
        2.
        3.
        4.
        5.
COSTSl
  LABOR
  POWER
  CHEMICALS
  MAINTENANCE&SUPPLIES
  PVC LINER
               TOTAL

TOTAL YEARLY COSTS!
               1, YEARLY OPERATING  COST
               2. YEARLY INVESTMENT
                  COST RECOVERY
               3, DEPRECIATION
               TOTAL
                        233430.00
                          4160.00
                         23340.00
                         23340.00
                          6300.00
                        290570.00
12490.00
70050.00
    0.0
 5970.00
  270.00
88780.00
                                  88780.00

                                  11620.00
                                  14320.00
                                  114720.00
                          1156

-------
  DRAFT
              Costs:  Total investment cost:  $720,590
                      Total yearly cost:      $123,020

An itemized breakdown of costs is presented in Table  338.   It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that three operators are required.

              Reduction Benefits:  BOD:  95.8 percent
                                    SS:  40.0 percent

Alternative A 28-111 - This alternative replaces the land spreading of
digester sludge in alternative A 29-11 with vacuum filtration.

The resulting BOD waste load is 0.010 kg/cu m (0.084 lb/1000 gal), and
the suspended solids load is 0.003 kg/cu m (0.025 lb/1000 gal).

              Costs:  Total investment cost:  $359,350
                      Total yearly cost:      $ 99,690

An itemized breakdown of costs is presented in Table 339.  It is
that land costs $41,000 per hectare ($16,600 per acre).  It is further
assumed that three operators are required.

              Reduction Benefits:  BOD:  95.8 percent
                                    SS:  40.0 percent

Alternative A 28-IV - This alternative replaces the land spreading
of digester sludge in Alternative A 29-11 with sand drying beds.

The resulting BOD waste load is 0.010 kg/cu m (0.084 lb/1000 gal), and
the suspended solids load is 0.003 kg/cu m (0.025 lb/1000 gal).

              Costs:  Total investment cost:  $545,980
                      Total yearly cost:      $138,320

An itemized breakdown of costs is presented in Table 340. It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that three operators are required.

              Reduction Benefits:  BOD:  95.8 percent
                                    SS:  40.0 percent

Alternative A 28-V - This alternative provides dual media filtration
in addition to the treatment modules of Alternative A 28-1

The resulting BOD waste load is 0.005 kg/cu m (0.042 lb/1000 gal),
and the suspended solids load is 0.001 kg/cu m (0.0083 lb/1000 gal).

              Costs:  Total investment cost:  $324,190
                      Total yearly cost:      $124,150
                             1157

-------
DRAFT
                       TABLE  338

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-II
                  (BEVERAGE BASE SYRUP)
 ITEMIZED COST SUMMARY FOR HASTEMTER TREATMENT  CHAIN
 DESIGN EFFICIENCY... 95.8 PERCENT 800 REDUCTION
 TREATMENT MODULE3|
                   81
                   B.
                   C.
                   K.
                   0.
                   R.
                   Y.
  .CONTROL HCLSE
  .PUMPING STATION
  .EQUALIZATION BASIN
  .ACTIVATED SLUDGE
  .SLUDGE THICKENER
  .AEROBIC DIGESTOR
  .HOLDING TANK
 INVESTMENT COSTSl
                1.
                2.
                3.
                4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                TOTAL

 YEARLY  OPERATING COSTSl
                1.  LABOR
                2.  POWER
                3.  CHEMICALS
                4.  MAINTENANCE&8UPPLIES
                TOTAL

 TOTAL  YEARLY COST8»
                1. YtARLY OPERATING COST
                2. YEARLY INVESTMENT
                   COST RFCCVFRY
                3. DEPRECIATION
                TOTAL
306170.00
353180.00
 30620.00
 30620.00
720590.00
                      37480
                      27600
                          0
                      10750
       00
       00
       .0
       00
                      75830.00
                      75630.00

                      28P20.00
                      18370.00
                     123020.0ft
                         1158

-------
DRAFT
                        TABLE 339

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-III
                   (BEVERAGE BASE SYRUP)
 ITEMIZED  COST SUMMARY FOR NASTEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY... 95.8 PERCENT BOD REDUCTION'
 TREATMENT  MODULESt
                   PI
                   e.
                   c.
                   K.
                   G.
                   S.
                   Y.
              .CONTROL HCLSE
              .PUMPING STATION
              .EQUALIZATION BASIN
              .ACTIVATED SLUDGE
              .SLUDGE THICKENER
              .VACUUM FILTRATION
              .HOLDING TANK
 INVESTMENT  COSTS!
                1.
                2.
                3.
                4.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
                TOTAL
 YEARLY
OPERATING
        1.
        2.
        3.
        4.
CCSTSl
  LABOR
  POWER
  CHEMICALS
  MAINTFNANCE&SUPPLIES
                TOTAL

 TOTAL  YEARLY  COSTS!
                1.  YEARLY OPERATING COST
                2.  YEARLY INVESTMENT
                   crsT RECOVERY
                3.  DEPRECIATION
                TOTAL
                       277250.00
                        26660.00
                        27720.00
                        27720.00
                       359350.00
37480.00
21760.00
 3060.00
 6390.00
68690.00
                                   68690.00
                                   14370.00
                                   16630.00
                                   99690.00
                          1159

-------
DRAFT
                       TABLE  340

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-IV
                  (BEVERAGE BASE SYRUP)
 ITEMIZED COST SUMMARY FOR  M8TEMTER  TREATMENT  CHAIN
 DE8IGM EFFICIENCY... 95.8  PERCENT  800 REDUCTION
 TREATMENT MCDULES|
                   Bl
                   0.
                   C.
                   K.
                   0.
                   R.
                   T.
                   V.
  .CONTROL HCLSF
  .PUMPING STATION
  .EQUALIZATION BASIN
  .ACTIVATED SLUDGE
  .SLLDGE THICKENER
  .AEROBIC riGESTCP
  .SAND DRYING BEDS
  .HOLDING TANK
 INVESTMENT COSTS:
                1.
                2.
                3.
                4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                TOTAL

 YEARLY OPERATING COSTS*
                1.  LABOR
                2.  POWER
                3.  CHEMICALS
                4.  MAINTFNANCE&SIPPLIE8
                TOTAL

 TOTAL YEARLY COSTS!
                1. YEARLY OPERATING  COST
                2. YEARLY INVESTMENT
                   COST RECOVERY
                3. DEPRECIATION
                TOTAL
451370.00
  4330.00
 U5140.00
 45140.00
545980.00
                      37480.00
                      27600.00
                          0.0
                      24320.00
                      89400.00
                      89400.00

                      21840.00
                      27080.00
                     138320.00
                         1160

-------
 DRAFT
An itemized breakdown of costs is presented in Table 341.  It is
assumed that land costs $4100 per hectare ($1600 per acre).  It is
further assumed that one operator is required.

              Reduction Benefits:  BOD:  97.9 percent
                                    SS:  80.0 percent

Alternative A 28-VI - This alternative provides dual media filtration
in addition to the treatment modules of Alternative A 28-11.

The resulting BOD waste load is 0.005 kg/cu m (0.042 lb/1000 gal), and
the suspended solids load is 0.001 kg/cu m (0.0083 lb/1000 gal).

              Costs:  Total investment cost:   $754,210
                      Total yearly cost:      $132,450

An itemized breakdown of costs is presented in Table 342.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that three operators are required.

              Reduction Benefits:  BOD:  97.9 percent
                                    SS:  80.0 percent

Alternative A 28-VII - This alternative provides dual media filtration
in addition to the treatment modules of Alternative A 28-11I.

The resulting BOD waste load is 0.005 kg/cu m (0.042 lb/1000 gal), and
the suspended solids load is 0.001 kg/cu m (0.0083 lb/1000 gal).

              Costs:  Total investment cost:   $393,000
                      Total yearly cost:      $109,130

An itemized breakdown of costs is presented in Table 343.  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that three operators are required.

              Reduction Benefits:  BOD:  97.9 percent
                                    SS:  80.0 percent

Alternative A 28-VIII - This alternative provides dual  media filtration
in addition to the treatment modules of Alternative A 28-IV.

The resulting BOD waste load is 0.005 kg/cu m (0.042 lb/1000 gal), and
the suspended solids load is 0.001 kg/cu m (0.0083 lb/1000 gal).

              Costs:  Total investment cost:   $579,610
                      Total yearly cost:      $147,750

An itemized breakdown of costs is presented in Table 344.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that three operators are required.
                              1161

-------
DRAFT
                        TABLE 341

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-V
                   (BEVERAGE BASE SYRUP)
ITEMIZED COST SUMMARY FOR KASTEWATER TREATMENT  CHAIN
DESIGN EFFICIENCY... 97.0 PERCENT BOO REDUCTION

TREATMENT MODULES*
                  8...PULPING STATION
                  C...EQUALIZATION BASIN
                  L...AERATED LA60CN
                  P...PUMPING STATION
                  N...DUAL MEDIA PRESSURE  FILTRA'N

INVESTMENT CCSTSJ
               1.  CCNSTRUCTICN         261450.00
               2.  LAND                    4160.00
              '3.  ENGINEERING           26140.00
               4.  CONTINGENCY           26140.00
               5.  PVC LINER               6300.00
               TOTAL                    324190.00

YEARLY OPERATING COSTS!
               1.  LABOR                 12490.00
               2.  POWER                 75920.00
               3.  CHEMICALS                  0.0
               4.  MAINTENANCE&SIPPLIES    6500.00
               5.  PVC LINER                270.00
               TOTAL                     95180.00

TCTAL YEARLY CCSTSl
               1. YEARLY OPERATING COST  95180.00
               2. YEARLY INVESTMENT
                  COST RECOVERY          12970.00
               3. DEPRECIATION           16000.00
               TCTAL                    124150.00
                          1162

-------
DRAFT
                       TABLE 342

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-VI
                   (BEVERAGE BASE SYRUP)
 ITEMIZED  COST SUMMARY FOP WASTEMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY... 97.9 PERCENT BOO REDUCTION
 TREATMENT  MODULES:
                     ..CONTROL HCL'SF
                   i...PUMPING STATION
           Bl
           8. .._._.-
           C!!]EQLALIZATICN  BASIN
           K... ACTIVATED  SLUDGE
           Q...SLLDGE THICKENER
           R...AERCBIC CIGESTOR
           Y...HOLDING TANiK
           8...PUMPING STATION
           N...DUAL MEDIA  PRESSURE  FRTRA'N
 INVESTMENT COSTS!
                1.
                2.
                3,
                4.
            CCKSTRUCTIO
            LAND
            ENGINEERING
            CCNTINGENCV
                TOTAL
                       334190.00
                       353180.
                        33420.
      00
      00
                        33420.00
                       754210.00
 YEARLY
OPERATING
        1.
        2.
        3.
        4.
CCSTS:
  LABCJR
  PO^ER
  CHEMICALS
  MAINTFMAMCESSL'PPLIES
                TCTAL

 TOTAL  YEARLY  CCSTSl
                1.  YEARLY CPERATIN'G COST
                2.  YFARLY INVESTMENT
                   COST RECOVERY
                3.  DEPRECIATION
                TCTAL
37480.00
33470.00
    0.0
11280.00
82230.00
                                   82230.00

                                   30170.00
                                   20050.00
                                  132450.00

-------
DRAFT
                       TABLE  343

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-VII
                  (BEVERAGE BASE SYRUP)
  ITEMIZED  COST  SUMMARY  FDR M3TEMTER TREATMENT CHAIN
  DESIGN  EFFICIENCY...  97.3 PERCENT BOD REDUCTION
  TREATMENT  MODULESs
                    65
                    8.
                    C.
                    K.
                    C.
                    S.
                    Y.
                    8.
                    K.
  .CONTROL
  .PUMPING
HCLSE
STATION
  .EQUALIZATION BASIN
  .ACTIVATED SLUDGE
  .SLUDGE THICKENER
  .VACUUM FILTRATION
  .HOLDING TAN'K
  .PUMPING STATION
  .DUAL MEDIA PRESSURE
            FILTRA'N
  INVESTMENT  COSTS!
                 1.
                 2.
                 3.
                 4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                 TOTAL

  YEARLY  OPERATING  COSTS:
                 1.   LABOR
                 2.   FOWFR
                 3.   CHEMICALS
                 4.   MAINTENANCE&SUPPLIES
                 TOTAL

  TOTAL YEARLY  CCSTSl
                 1.  YEARLY OPERATING COST
                 2.  YEARLY INVESTMENT
                    COST  RECOVERY
                 3.  DEPRECIATION
                 TOTAL
          305280.00
           26660.00
           30530.00
           30530.00
          393000.00
                      37U80.00
                      27620,00
                       3060.00
                       6930,00
                      75090.00
                      75090.00

                      15720.00
                      18320.00
                     109130.00
                         1164

-------
DRAFT
                       TABLE  344

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-VIII
                  (BEVERAGE BASE SYRUP)
 ITEMIZED  COST  SUMMARY FOR WASTEDATER TREATMENT CHAIN
 DESIGN  EFFICIENCY... 97.9 PERCENT BOD REDUCTION
 TREATMENT  MODULES:
                   81..CONTROL HOUSE
                   B...PUMPING STATION
                   C...EQLALIZATKN BASIN
                   «... ACTIVATED SLUDGE
                     ..SLUDGE THICKENER
                     ..AERCBIC DIGESTOR
                   T...SAND DRYING BEDS
                   Y...HOLDING TANK
                   B...PUMPING STATION
                   N...DUAL MEDIA PRESSURE FILTRA'N
 INVESTMENT  CCSTSl
                1.
                2.
                3.
                a.
CONSTRUCTION
LAND
FNGINEERING
CONTINGENCY
                TCTAL

 YEARLV  OPERATING  CCSTS:
                i.   LABPR
                2.   PCwPS
                3.   CHEMICALS
                U,   MAINTEN'ANCERSLPPLIES
                TCTAL

 TCTAL YEARLY  CCSTSs
                1.  YEARLY OPERATING COST
                2.  YEARLY INVESTMENT
                   COST RECCvr&Y
                3.  CEPREf.TATlCM
                TOTAL
^79^00.00
 U7<540.00
579610.00
                      37U80.00
                      33«70.00
                           0.0
                      24860.00
                      95610.00
                      95810.00

                      23180.00
                      28760.00
                      U7750.00
                        1165

-------
  DRAFT


               Reduction Benefits:  BOD:  97.9 percent
                                     SS:  80.0 percent

Alternative A 28-IX - This alternative provides carbon adsorption
in addition to the treatment modules of Alternative A 28-V.

The resulting BOD waste load is 0.0025 kg/cu m (0.021 lb/1000 gal),
and the suspended solids load is 0.005 kg/cu m (0.0042 lb/1000 gal),

               Costs:  Total investment cost:  $406,070
                       Total yearly cost:      $152,030

An itemized breakdown of costs is presented in Table 345.  It is
assumed that land costs $4100 per hectare ($1660 per acre).  It
is further assumed that one operator is required.

               Reduction Benefits:  BOD:  98.9 percent
                                     SS:  90.0 percent

A cost efficiency curve is presented in Figure 326.
 Alternative A  28-X  - This  alternative  provides carbon adsorption  in
 addition  to the  treatment  modules of Alternative A 28-VI.

 The  resulting  BOD waste  load is 0.0025 kg/cu m (0.021 lb/1000 gal), and
 the  suspended  solids load  is 0.0005 kg/cu m (0.00042 lb/1000 gal).

               Costs:  Total investment cost:  $836,070
                      Total yearly cost:      $160,320

 An itemized breakdown of costs is presented in Table 346.   It is
 assumed that land costs $4100 per hectare ($1660 per acre).  It is
 further assumed  that three operators are required.

               Reduction Benefits:  BOD:  98.9 percent
                                    SS:  90.0 percent

 A cost efficiency curve is presented in Figure 327.

 Alternative A  28-XI - This alternative provides carbon adsorption in
 addition to the  treatment modules of Alternative A 28-VII.

The resulting  BOD waste load is 0.0025 kg/cu m (0.021 lb/1000 gal), and
 the suspended  solids load is 0.0005 kg/cu m (0.0042 lb/1000 gal).

              Costs:  Total investment cost: • $474,860
                      Total yearly cost:       $137,000

An itemized breakdown of costs  is presented in Table  347.   It is
assumed that land costs $41,000 per hectare ($16,600  per acre).   It
is further assumed that three operators are required.
                               1166

-------
DRAFT
                       TABLE 345

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-IX
                  (BEVERAGE. BASE SYRUP)
  ITEMIZED COST SUMMARY FOR KA8TEMTER TREATMENT  CHAIN
  DESIGN EFFICIENCY... 99.0 PERCENT BOD REDUCTION
  TREATMENT MCDULESi
                    B.
                    C.
                    L.
                    8.
                    N.
                    Z.
              .PUMPING STATION
              .EQIALIZATICN  BASIN
              .AERATED LAGOON
              .PUMPING STATION
              .DUAL MEDIA PRESSURE  PILTRA'N
              .ACTIVATED CARBON  ADSORPTICN
  INVESTMENT COSTS!
                 1.
                 5.
            .CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC LINER
                 TCTAL
YEARLY
OPERATING
        1.
        2.
        3.
        4.
        5.
                   COSTSi
                     LABOR
                     CHEMICALS
                     MAINTENANCE&SLPP'LIES
                     PVC LINER
                 TCTAL

  TCTAL YEARLY CCSTSl
                 1. YEARLY OPERATING COST
                 2. YEARLY INVESTMENT
                    COST RECOVERY
                 3. DEPRECIATION
                 TCTAL
                                         329670.00
                                           4160.00
                                          32970.00
                                          32970.00
                                           6300.00
                                         106070.00
                                          12490.00
                                          791BO.OO
                                              0,0
                                          23750.00
                                            270.00
                                         115690.00
                                  115690.00

                                   16240.00
                                   20100.00
                                  152030.00
                           1167

-------
oo
                     (T


                     _!
                     >-



                     >
                     HI
                             .t
                     «    S-3.3
                     a
                     <
                     o
                           111.C  !
                               oc.cs    «i.co
                                                                                         «7.ce     «e.:o
                                                                     EFFICIENCY



                                                            FIGURE 326



                                 INVESTNENT AND  YEARLY COSTS FOR SUBCATEGORY A 28, ALT.  I,  V, IX
                                                                                                                 iec.cc

-------
DRAFT
                       TABLE  346

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-X
                   (BEVERAGE BASE SYRUP)
ITEMIZED COST SUMMARY FOR WASTEKATEP  TREATMENT  CHAIN
DESIGN EFFICIENCY,.. 99.0 PERCENT  800  REDUCTION-
TREATMENT MOOULESj
                  Bl
                  e.
                  c.
                  K.
                  Q.
                  P-.
                  Y.
                  B.
                  N.
                  z,
  .CONTROL HGU8E
  .PUMPING STATION
  .EQUALIZATION BASIN
  .ACTIVATED SLUDGE
  .SLUDGE THICKENER
  .AEROBIC DIGESTOR
  .HOLDING TANK
  .PUMPING STATION
  .DUAL MEDIA PRESSURE FILTRA'N
  .ACTIVATED CARBON ADSORPTION'
INVESTMENT COSTS!
               1.
               2.
               3.
               4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
               TCTAL

YEARLY OPERATING COSTS!
               1.  LABOR
               2.  POWER
               3.  CHEMICALS
               4.  MAINTENANCE&SUPPLIES
               TCTAL
402410.00
353160.00
 40240.00
 40240.00
836070.00
                      37480.00
                      36730.00
                          0.0
                      28530..00
                      102740.00
TOTAL YEARLY CCSTSl
                1.  YEARLY  OPERATING  COST 102740.00
                2.  YEARLY  INVESTMENT
                   COST  RECOVERY           33440.00
                3.  DEPRECIATION            24140.00
                TCTAL                    . 160320.00
                            1169

-------
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8
    622.*
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    1(3.3
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                 «i.90     «z.ec    
-------
DRAFT
                        TABLE 347

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-XI
                   (BEVERAGE BASE  SYRUP)
ITEMIZED COST SUMMARY FOR HASTEkATER  TREATMENT  CHAIN
DESIGN EFFICIENCY... 99.0 PERCENT  BCD  REDUCTION
TREATMENT MODULES;
INVESTMENT COSTS:
               1.
               2.
               3.
               4.
                  81..CONTROL  HCL5E
                  B...PUMPING  STATION
                  C...EQUALIZATION BASIN
                  K...ACTIVATED  SLUDGE
                  o...SLUDGE THICKENER
                  S...VACUUM FILTRATION
                  Y...HOLDING  TA*K
                  B.f.PUMPING  STATION1
                  N...DUAL MEDIA  PRESSURE  FILTRA'N
                  Z...ACTIVATED  CARBCN A
                   CCN8TRUCTICN
                   LAND
                   ENGINEERING
                   CONTINGENCY
               TOTAL
YEARLY OPERATING
               i.
               2.
               3.
               4.
                   LABOR
                   POWER
                   CHEMICALS
                   MAINTENANCE&SL'PPLIES
               TOTAL

TOTAL YEARLY COSTS*
               1. YEARLY OPERATING  COST
               2. YEARLY INVESTMENT
                  COST RECOVERY
               3. DEPRECIATION
               TOTAL
373500.00
 26660.00
 37350.00
 37350.00
474860.00
 37480.00
 30890.00
  3060.00
 24170.00
 95600.00
                                          95600.00

                                          18990.00
                                          22410.00
                                         137000.00
                          1171

-------
  DRAFT
              Reduction Benefits:  BOD:  98.9 percent
                                    SS:  90.0 percent

A cost efficiency curve is presented in Figure  328.

Alternative A 28-XII - This alternative provides carbon adsorption in
addition to the treatment modules of Alternative A 28-VIII.

The resulting BOD waste load is 0.0025 kg/cu m (0.021 lb/1000 gal),
and the suspended solids load is 0.005 kg/cu m (0.0042 lb/1000 gal).

              Costs:  Total investment cost:  $661,470
                      Total yearly cost:      $175,630

An itemized breakdown of costs is presented in Table 348.   It is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that three operators are required.

              Reduction Benefits:  BOD:  98.3 percent
                                    SS:  90.0 percent

A cost efficiency curve is presented in Figure  329.
Alternative A 28-XIII - This alternative consists of a pumping station,
a flow equalization tank, and spray irrigation of the raw waste effluent.

The resulting BOD waste load is 0.0 kg/cu m (0.0 lb/1000 gal), and
the suspended solids load is 0.0 kg/cu m (0.0 lb/1000 gal).

              Costs:  Total investment cost:  $192,790
                      Total yearly cost:      $ 27,360

An itemized breakdown of costs is presented in Table 349.   It.  is
assumed that land costs $4100 per hectare ($1660 per acre).  It is
further assumed that one-half time operator is required.

              Reduction Benefits:  BOD:  100 percent
                                    SS:  100 percent
Cost and Reduction Benefits of Alternative Treatment Techno!ocn'.es for
Subcategory A 30 - Instant Tea

A model plant representative of subcategory A 30 was developed in Section
V for  the purpose of applying control and treatment alternatives.  In
Section VII, eight alternatives were selected as being applicable engi-
neering alternatives.  These alternatives provide for various levels of
waste  reductions for the model plant which produces 9.1 kkg (10 ton) of
soluble "instant" tea per day.

Alternative A 30-1 - This alternative assumes no treatment and no reduc-
tion in the waste load.  It is estimated that the effluent from a 9.1
llg (10 ton) per day plant is 454 cu m  (0.12 MG) per day.  The 300 waste
                               117?

-------
VI
5


b
S
*-s
V
      Iil7.il
       ««,C
                                         ^ » • „ .    ^ • » V -    ' C * V V    T « t v V    ^ t » ^ J
                                            EFFICIENCY


                                    FIGURE 328


           INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 28, ALT.  Ill,  VI,  XI

-------
DRAFT
                       TABLE 348

        ITEMIZED COST SUMMARY FOR  ALTERNATIVE A28-XII
                  (BEVERAGE BASE SYRUP)
ITEMIZED COST  SUMMARY  FOR  I*ASTE*ATER  TREATMENT CHAIN
DESIGN EFFICIENCY... 99.0  PERCENT  BCD REDUCTION

TREATMENT  MODULES*
                   Bi..CONTROL  HCLSE
                   B...PUMPING  STATION
                   C...EQUALIZATION BASIN
                   *... ACTIVATED  SLLDGE
                   Q...SLLDGE  THICKENER
                   R...AERC5IC  DIGESTQR
                   T...SANP DRYING-PEDS
                   Y...HOLDING  TANK
                   P...PUMPING  STATION
                   N...DUAL MEDIA PRESSURE FIURA'N
                   z...ACTIVATED  CAPBCN ACSCRPTK^

INVESTMENT CCSTSl
                1.   CCNSTRUCTICN          547620.00
                2.   LAND                    4330.00
                3.   ENGINEERING           54760.00
                4.   CONTINGENCY           54760.00
                TCTAL                     661470.00

YEARLY OPERATING CCSTSt
                1.   LABO»                  37480.00
                2,   POWER                  36730.00
                3.   CHEMICALS                  0.0
                4.   MAINTEKANCE&SLPPHES  42100.00
                TCTAL                     116310.00

TOTAL YEARLY CCSTS:
                1.  YEARLY  OPERATING COST 116310.00
                2.  YEARLY  INVESTMENT
                   CC.8T  RECOVERY           26^60.00
                3.  DEPRECIATION           32860.00
                TCTAL                     175630.00
                         1174

-------
                   8

                   u.
                   o
     55*.
Ul
z
t-t


I-
                   a
                   <
                   u
                        :«?.
     13?.C
                            
-------
DRAFT
                       TABLE 349

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A28-XIII
                   (BEVERAGE BASE SYRUP)
 ITEMIZED COST  SUMMARY  FOR  M8TFMTER TREATMENT CHAIN'
 DESIGN EFFICIENCY...100.0  PERCENT BOO REDUCTION
 TREATMENT MODULESt
                    Y...HOLDING TANK
                    U... SPRAY  IRRIGATION
INVESTMENT CCSTSt
               1.
               2.
               3.
               4.  CONTINGENCY
               TOTAL
                     CCNSTRUCTICN
                     LAND
YEARLY
OPERATING
        1.
        2,
        3.
        4.
                   CCSTSt
                     LABOR
                     CHEMICALS
                     PAINTENAMCEHSLPPLIES
                 TOTAL

 TOTAL YEARLY  COST?:
                 1.  YEARLY  CFFPATIKG CCST
                 2.  YEARLY  INV
                    CCST  RECOVERY
                 3.  DEPRECIATION
                 TCTAL
                                  13289C.OO
                                   33320.OP
                                   132
-------
DRAFT

loaTTs" 1>0.0 kg/kkg (100.0 Ib/ton), and the suspended solids load is
37.5 kg/kkg (75.0 Ib/ton).

Alternatlve A 30-11 - This alternative consists of a pumping station,
a flow equalization tank, primary clarification, a complete-mix activated
sludge basin, sludge thickening, aerobic digestion and vacuum filtration.

The resulting BOD waste load is 2.00 kg/kkg (4.0 Ib/ton), and the sus-
pended solids load is 5.50 kg/kkg (11.0 Ib/ton).

               Costs:  Total investment cost:   $358,430
                       Total yearly cost:      $ 97,010

An itemized breakdown of costs is presented in Table 350.  It is
that land costs $41,000 per hectare ($16,600 per acre).  It is further
assumed that one operator is required.

               Reduction Benefits:  BOD:  96.0 percent
                                     SS:  85.3 percent

Alternative A 30-111 - This alternative replaces the vacuum filtration
module of alternative A 30-11 with sand drying beds.

The resulting BOD waste load is 2.00 kg/kkg (4.00 Ib/ton) and the suspen-
ded solids load is 5.5 kg/kkg (11.0 Ib/ton).

               Cost:  Total investment cost:  $402,290
                      Total yearly cost:      $103,830

An itemized breakdown of costs is presented in Table 351.  It is
that land costs $20,510 per hectare ($8,330 per acre).   It is further
assumed that one operator is required.

               Reduction Benefits:  BOD:  96.0 percent
                                     SS:  85.3 percent

Alternative A 30-IV - This  alternative consists of a pumping station,
a flow equalization tank and aerated lagoon.

The resulting BOD waste load is 2.0 kg/kkg (4.0 Ib/ton) and the suspended
solids load is 5.5 kg/kkg (11.0 Ib/ton).

               Costs:  Total investment cost:   $359,080
                       Total yearly cost:      $140,200

An itemized breakdown of costs is presented in Table 352.  It is
that land costs $4,100 per hectare ($1,660 per acre).  It is further
assumed that one half-time operator is required.

               Reduction Benefits:  BOD:  96.0 percent
                                     SS:  85.3 percent
                                1177

-------
DRAFT
                       TABLE  350

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A30-II
                      (INSTANT TEA)
 ITEMIZED COST 8LMKARY  FOR  WASTEfcATER  TREATMENT CHAIN
 DESIGN EFFICIENCY... 95.0  PERCENT  BOD REDUCTION
 TREATMENT MODULES!
                    Bl
                    B.
                    C.
                    E.
                    K.
                    S.
                    Y,
                     .CONTROL HOUSE
                     .PUMPING STATION
                     .EQUALIZATION BASIN
                     .CLARIFIER
                     .ACTIVATED SLUDGE
                     .SLUDGE TMICKENEP
                     .AEROBIC DICES TOR
                     .VACUUM FILTRATION
                     .HOLDING TANK
 INVESTMENT CCSTSt
                 1.
                 2.
                 3.
    CONSTRUCTION
    LAND
    FNPINEERING
4.  CONTINGENCY
TOTAL
 YEARLY
       OPERATING
               1.
               2.
               3.
               a.
  COSTSi
    LABOR
    PO'^EP
    CHEMICALS
    MAINTENANCE&SLPPLIES
               TOTAL

TOTAL YEARLY CCSTSJ
               i. YEARLY OPERATING COST
               2. YEARLY INVESTMENT
                  COST RECOVERY
               3. DEPRECIATION
               TOTAL
                                         273700.00
                                          29990.00
                                          27370.00
                                          27370.00
                                         358U30.00
                                           37480.00
                                           18990.00
                                            2670.00
                                            7110.00
                                           66250.00
                                           66250,00
                                                i.OO
                                           16420.00
                                           97010.00
                         1178

-------
DRAFT
                       TABLE 351

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A30-III
                      (INSTANT TEA)
 ITEMIZED  COST  SUMMARY FOP WA9TFMTER TREATMENT CHAIN
 DESIGN  EFFICIENCY... 95.0 PERCENT BOD REDUCTION
 TREATMENT MODULES!
                   Bl
                   8.
                   C.
                   E.
                   K.
                   0.
                   P-.
                   T.
                   Y.
  .CONTROL HCL'SE
  .PUMPING STATION
  .EQUALIZATION BASIN
  .CLARIFIED
  .ACTIVATED SLUDGE
  .SLtOGg THICKENER
  .AER08IC OIGESTOR
  .SANp DRYING BEDS
  .HOLDING TANK
 INVESTMENT COSTSI
                i.
                2.
                3.
                4.
CCNSTPUCTIC^
LAND
ENGINEERING
CONTINGENCY
                TOTAL
YEARLY OPERATING
               1.
               2.
               3.
               4.
                  COSTS*
                    LABOR
                    PCWEP
                    CHEMICALS
                    MAINTENANCE&SLPPLIES
                TCTAL

 TOTAL YEARLY CCSTSi
                1. VEARLY OPERATING  COST
                2. YEARLY INVESTMENT
                   COST PFCCVFRY
                3. DEPRECIATION
                TCTAL
318580.00
 l
-------
DRAFT
                       TABLE  352

        ITEMIZED  COST SUMMARY FOR ALTERNATIVE A30-IV
                      (INSTANT TEA)
  ITEMIZED COST SUMMARY FOR WASTEMTEP TREATMENT CHAIN
  DESIGN EFFICIENCY... 95.0 PERCENT BOO REDUCTION
  TREATMENT MODULFSt
                    B...PUMPING STATION
                    C...EQUALIZATION BASIN
                    L...AERATED LAGOON
  INVESTMENT CCSTSI
                 i.
                 2.
                 3.
                 4.
                 5.
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
                   PVC LINEP
               TOTAL

YEARLY OPERATING COSTS;
               1.  LABOR
                   2D t^ IAJ IT U
                0  r Vi I" t ™
               3.  CHEMICALS
               4.  MAINTENANCE&SIPPLIES
               5.  PVC LINER
               TOTAL
288570.00
  4660.00
 PP860.00
 28660.00
  8130.00
359080.00
                                            12490.00
                                            87UO.OO
                                                0.0
                                            8180.00
                                             310.00
                                           108120.00
  TOTAL  YEARLY COSTS!
                 1. YEARLY OPERATING COST 108120.00
                 2. YEARLY INVESTMENT
                    COST RECOVERY           14360.00
                 3. DEPRECIATION            17720.00
                 TOTAL                    140200,00
                         1180

-------
  DRAFT
Alternative A 30-V - This alternative provides dual  media filtration
in addition to the treatment modules of Alternative  A 30-11.

The resulting BOD waste load is 1.0 kg/kkg (2.0 Ib/ton), and  the
suspneded solids load is 1.0 kg/kkg (2.0 Ib/ton).

               Costs:  Total investment cost:   $382,030
                       Total yearly cost:      $103,680

An itemized breakdown of costs is presented in Table 353.  It is
assumed that land costs $4100 per hectare ($1660 per acre).   It
is further assumed that one operator is required.

               Reduction Benefits:  BOD:  98.0 percent
                                     SS:  97.3 percent

A cost efficiency curve is presented in Figure 330.

Alternative A 30-VI - This alternative provides dual media filtration
in addition to the treatment modules of Alternative  A 30-1II.

The resulting BOD waste load is 1.0 kg/kkg (2.0 Ib/ton).

               Costs:  Total investment cost:   $463,070
                       Total yearly cost:      $120.500

An itemized breakdown of costs is presented in Table 354.  It is
assumed that land costs $20,510 per hectare ($8330 per acre).  It
is further assumed that three operators are required.

               Reduction Benefits:  BOD:  98.0 percent
                                     SS:  97.3 percent

A cost efficiency curve is presented in Figure 331.

Alternative A 30-VII  - This alternative provides dual media  filtration
in addition to the treatment modules of Alternative  A 30-IV.

The resulting BOD waste load is 1.0 kg/kkg (2.0 Ib/ton), and  the
suspended solids load is 1.0 kg/kkg (2.0 Ib/ton).

               Costs:  Total investment cost:   $424,650
                       Total yearly cost:      $148,560

An itemized breakdown of costs is presented in Table 355.  It is
assumed that land costs $4100 per hectare ($1660 per acre).   It
is further assumed that one half-time operator is required.

               Reduction Benefits:  BOD:  98.0 percent
                                     SS:  97.3 percent

A cost efficiency curve is presented in Figure 332.
                                1181

-------
DRAFT
                       TABLE  353

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A30 -V
                      (INSTANT TEA)
  ITEMIZED COST SUMMARY FQR WA3TEMTER TREATMENT  CHAIN
  DESIGN EFFICIENCY... 97.5 PERCENT BOO REDUCTION
  TREATMENT MODULES!
                    Bl
                    8.
                    C.
                    E.
                    K.
                    0.
                    R.
                    S.
                    Y.
                    8.
                    N.
  .CONTROL HCUSE
  .PUMPING STATION
  .EQUALIZATION BASIN
  .CLARIFIER
  .ACTIVATED SLUDGE
  .SLUDGE THICKENER
  .AERCRIC DIGESTQR
  .VACUUM FILTRATION
  .HOLDING TANK
  .PUMPING STATION
  .DUAL MEDIA PRESSURE FJLTRA'N
  INVESTMENT CCSTSi
                 1.
                 2.
                 I.
                 4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                 TOTAL

  YEARLY OPERATING CCSTS*
                 i.  LABOR
                 a.  PC*ER
                 3.  CHEMICALS
                 «.  MAINTENANCE&SUPPLIES
                 TOTAL

  TOTAL YEARLY COSTS*
                 1. YEARLY OPERATING COST
                 2. YEARLY INVESTMENT
                    COST RECOVERY
                 3. DEPRECIATION
                 TOTAL
293360.00
 29990.00
 29340.00
 29340.00
382030.00
                      37480.00
                      23240.00
                       2670.00
                       7410.00
                      70800.00
                      70800.00

                      15280,00
                      17600.00
                     103680.00
                           1182

-------
      sai.o
CO
o:
      J2S.I
      2t«.»
In

8
      a«c.o
211.«
      H«.2
      129.*
Q.

3
             «i.ce    <2.eo     <>. ee
                                                             **'°°    *7*ee
                                                   FIGURE 330


                       INVEST^€^T^ AND YEARLY COSTS FOR SUBCATEGORY A 30.  ALT. n,  v

-------
DRAFT
                       TABLE  354

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A30-VI
                      (INSTANT TEA)
 ITEMIZED COST BLEARY PHR UA9TEMTER TREATMENT  CHAIN
 DESIGN EFFICIENCY... 97.5 PERCENT BOD REDUCTION
 TREATMENT MODULES*
                   81
                   8.
                   C.
                   E.
                   K.
                   G.
                   R.
                   T.
                   V.
                   B.
                   N.
.CONTROL HCU3E
.PUMPING STATION
.FQLALI7ATION PASIN
.CLARIFIER
.ACTIVATED SLUDGE
.SLUDGE THICKENER
.AFPCPIC DIRESTCR
.SAND DRYING BEDS
.HOLDING TANK
.PUMPING STATION
.DUAL MEDIA PRESSURE FILTRA'N
 INVESTMENT COSTS*
                1.
                2.
                3.
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
 YEARLY OPERATING CCSTSf
                1.  LABOR
                2,  PC'WER
                3.  CHEMICALS
                4.  MAJNTf-NANCERSUPPLIES
                TOTAL

 TOTAL YEARLY COSTS!
                i. YEARLY OPERATING COST
                2. YEARLY INVESTMENT
                   COST RECOVERY
                3. DEPRECIATION
                TOTAL
                   338240.00
                    19990.00
                    33820.00
                    33820.00
                   425870.00
                    37480.00
                    20880.00
                        0.0
                    14820.00
                    73180.00
                    73180.00

                    17030.00
                    20290.00
                   110500.00
                           1184

-------
(fl
o:
u.
o
8
>-
^^

>-
u
         .8
       '.*•?.<
         . 3
u      ic3.e  i
                                                                                           :eo>cs
                                      FIGURE  331
          INVESTMENT AND YEARLY COSTS FOR SUBCATEGORY A 30, ALT.  30 III. VI

-------
 DRAFT
                        TABLE 355

         ITEMIZED COST SUMMARY FOR ALTERNATIVE A30-VII
                      (INSTANT TEA)
ITEMIZED COST SUMMARY FOR WASTEKATER  TREATMENT  CHAIN
DESIGN EFFICIENCY.,. 97.5 PERCENT BOD REDUCTION
TREATMENT MODULES!
                  8...PUMPING STATION
                  C...EOUALIZATICN BASIN  '
                  L...AERATED LAGOON
                  R...PUMPING STATION
                  N...DUAL MEDIA PRESSURE  FILTRA»N
INVESTMENT COSTSI
               i.
               2.
               3.
               4.
               5.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
PVC LINER
               TOTAL

YEARLY OPERATING COSTSl
               1.  LABOR
               2.  POWER
               3.  CHEMICALS
               4,  MAINTENANCE&SUPPLIES
5.  PVC
TOTAL
                       LINER
                         306230.00
                          46650.00
                          30620.00
                          30620.00
                           6130.00
                         424650.00
                      12490.00
                      91390,00
                          0.0
                       8460.00
                        310.00
                     112670.00
TOTAL YEARLY COSTSI
               1. YEARLY OPERATING COST  112670.00
               2. YEARLY INVESTMENT
                  COST RECOVERY           16990.00
               3. DEPRECIATION            18900.00
               TOTAL                     148560.00
                           1186

-------
00
           to


           i
           co
           o


           I
           o
           o
                 • 13.0
                 I«*. 5
      J»«.0
                 JJ9.5
                 3U.O
•-«     asj.s






^     2la.e
                 22S.S
                  tta.s
                  lao.o
                      90.00     41.00     42.00    41.00    4a^QO    4S.09     «».00     47.00     48.00    4V.00    100.00






                                                            FIGURE 332




                               INVESTMEm- AND YEARLY COSTS  FOR SUBCATEGORY A  30. ALT.  A 30 IV

-------
  DRAFT


Alternative A 3Q-VIII - This alternative provides dual media filtration
in addition to the treatment modules of Alternative A 30-IV.

The resulting BOD waste load is 1.0 kg/kkg (2.0 Ib/ton).

               Costs:  Total investment cost:  $223,650
                       Total yearly cost:      $ 30,250

An itemized breakdown of costs is presented in Table 356.  It is
assumed that land costs $4100 per hectare ($1660 per acre).   It
is further assumed that one half-time operator is required.

               Reduction Benefits:  BOD:  100 percent
                                     SS:  100 percent

Cost and Reduction Benefits of Alternative Treatment Technologies
for Subcategory C 8 - Coffee Roasting with Wet Scrubbers

A model plant representative of Subcategory C 8 was developed in
Section V for the purpose of applying control and treatment alter-
natives.  In Section VII, four alternatives were selected as being
applicable engineering alternatives.  These alternatives provide
for various levels of waste reductions for the model plant which
consumes 60 kkg (65 ton) of coffee beans per day.
  f
Alternative C 8-1  - This alternative assumes no treatment and no
reduction in the waste load.  It is estimated that the effluent from
a 60 kkg (65 ton) per day plant is 64.3 cu m/day (0.017 MGD).  The
BOD concentration is 350 mg/1, and the suspended solids concentration
is 200 mg/1.

               Costs:               0
               Reduction Benefits:  None

Alternative C 8-II - This alternative consists of a pumping station,
caustic neutralization, a primary clarifier, an activated sludge
system, sludge thickening, vacuum filtration, and sludge storage and
hauling.  A control house is provided.

The resulting BOD waste load is 0.038 kg/kkg (0.076 Ib/ton), and
the suspended solids load is 0.066 kg/kkg (0.13 Ib/ton).

               Costs:  Total investment cost:  $181,710
                       Total yearly cost:      $ 78,600

An itemized breakdown of costs is presented in Table 357.  It is
assumed that land costs $41,000 per hectare ($16,600 per acre).  It
is further assumed that two operators are required.

               Reduction Benefits:  BOD:  90 percent
                                     SS:  70 percent
                                1188

-------
DRAFT
                       TABLE 356

        ITEMIZED COST SUMMARY FOR ALTERNATIVE A30-VIII
                      (INSTANT TEA)
 ITEMIZED COST SUMMARY FOR WA8TEKATER  TREATMENT  CHAIN
 DESIGN EFFICIENCY...100.0 PERCENT BOD  REDUCTION

 TREATMENT MODULES}
                   Y...HOLDING
                   U...SPRAY IRRIGATION
 INVESTMENT COSTSf
                1.
                2.
                3.
                   CONSTRUCTION
                   LAND
                   ENGINEERING
               4,  CONTINGENCY
               TCTAL
YEARLY
OPERATING
        1.
        2.
        3.
        4.
                  COSTS;
                    LABOR
                    POER
                    CHEMICALS
                    MAINTENANCE&SLPPLIES
                TCTAL

 TCTAL YEARLY COSTS!
                1. YEARLY OPERATING COST
                2, YEARLY INVESTMENT
                   COST RECCVFRY
                3. DEPRECIATION
                TOTAL
                                  15C420.00
                                   ^3150,00
                                   150^0.00
                                   15040.00
                                  223650.00
                                           6250.00
                                           1840.00
                                              0.0
                                           4190.00
                                          12280.00
                                   12280.00

                                    8950.00
                                    9020.00
                                   30250.00
                             1189

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DRAFT
                       TABLE 357

         ITEMIZED COST SUMMARY FOR ALTERNATIVE C8-II
            (COFFEE ROASTING WITH WET SCRUBBERS)
    ITEMIZED  COST  SUMMARY FOR WASTEMTER TREATMENT CHAIN
    DESIGN  EFFICIENCY.,.90.0 PERCENT BOD REDUCTION
    TREATMENT  MODULES!
                      Bl
                      B.
                      G.
                      E.
                      H.
                      I.
                      K.
                      S.
                      Y.
.CONTROL HOUSE
.PUMPING STATION
.CAUSTIC NEUTRALIZATION
.CLARIFIER
.NITROGEN ADDITION
.PHOSPHORUS ADDITION
.ACTIVATED SLUDGE
.VACUUM FILTRATION
.HOLDING TANK
    INVESTMENT  COSTSl
                   1.
                   2.
                   3.
    CONSTRUCTION
    LAND
    ENGINEERING
4.  CONTINGENCY
TOTAL
    YEARLY  OPERATING  COSTSl
                   1.   LABOR
                   2.   PCWER
                   3.   CHEMICALS
                   «•   MAINTENANCE&SUPPLIES
                   TOTAL
                   129210.00
                    26660.00
                    12920.00
                    12920.00
                   181710.00
                    24990.00
                     5200,00
                    16860.00
                    16510.00
                    63580.00
   TOTAL  YEARLY  COSTS:
                   1.  YEARLY  OPERATING COST  63580.00
                   2.  YEARLY  INVESTMENT
                      COST  RECOVERY           7270,00
                   3.  DEPRECIATION             7750.00
                   TOTAL                      78600.00
                          1190

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  DRAFT


Alternative C 8-III - This alternative consists of Alternative C 8-II
with the addition of dual media filtration.

The resulting BOD waste load is 0.019 kg/kkg (0.038 Ib/ton),  and the
suspended solids load is 0.018 kg/kkg (0.035 Ib/ton).

               Costs:  Total investment cost:   $207,430
                       Total yearly cost:       $ 85,260

An itemized breakdown of costs is presented in Table 358.   It is
assumed that land costs $41,000 per hectare ($16,600 per acre).   It
is further assumed that two operators are  required.

               Reduction Benefits:  BOD:  95 percent
                                     SS:  92 percent

A cost efficiency curve is presented in Figure 333.

Alternative C 8-IV - This alternative consists of a pumping station,
caustic neutralization, nutrient addition, and aerated lagoons.

The resulting BOD waste load is 0.038 kg/kkg (0.076 Ib/ton),  and the
suspended solids load is 0.11 kg/kkg (0.22 Ib/ton).

               Costs:  Total investment cost:   $218,760
                       Total yearly cost:       $ 67,090

An itemized breakdown of costs is presented in Table 359.   It is
assumed that land costs $4100 per hectare  ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD: 90 percent
                                     SS: 50 percent

Alternative C 8-V - This alternative consists of Alternative C 8-1V
with the addition of dual media filtration.

The resulting BOD waste load is 0.019 kg/kkg (0.038 Ib/ton),  and the
suspended solids load is 0.031 kg/kkg (0.062 Ib/ton).

               Costs:  Total investment cost:   $244,470
                       Total yearly cost:       $ 73,750

An itemized breakdown of costs is presented in Table 360.   It is
assumed that land costs $4100 per hectare  ($1660 per acre).  It is
further assumed that two operators are required.

               Reduction Benefits:  BOD:  95 percent
                                     SS:  86 percent

A cost efficiency curve is presented in Figure 334.
                                 1191

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DRAFT
                       TABLE 358

         ITEMIZED COST SUMMARY FOR ALTERNATIVE C8-III
            (COFFEE ROASTING WITH WET SCRUBBERS)
    ITEMIZED COST SUMMARY FOR WASTEMTER TREATMENT  CHAIN
    DESIGN EFFICIENCY...95.0 PERCENT BOD REDUCTION
    TREATMENT MODULES*
                      Bl
                      B.
                      6.
                      E.
                      H,
                      I.
                      K.
                      S.
                      Y.
                      8.
                      N.
  .CONTROL HOUSE
  .PUMPING STATION
  .CAUSTIC NEUTRALIZATION
  .CLARIPIER
  .NITROGEN ADDITION
  .PHOSPHORUS ADDITION
  .ACTIVATED SLUDGE
  .VACUUM FILTRATION
  .HOLDING TANK
  .PUMPING STATION
  .DUAL MEDIA PRESSURE FILTRA'N
    INVESTMENT CCSTSl
                   1.
                   2.
                   3.
                   4.
CONSTRUCTION
LAND
ENGINEERING
CONTINGENCY
                   TOTAL

    YEARLY  OPERATING COSTSi
                   1.   LABOR
                   2.   POWER
                   3.   CHEMICALS
                   4.   MAINTENANCE&SUPPLltS
                   TOTAL

    TOTAL YEARLY  CCSTSl
                   1.  YEARLY OPERATING COST
                   2.  YEARLY INVESTMENT
                      COST RECOVERY
                   3.  DEPRECIATION
                   TOTAL
150650.00
 26660.00
 15060.00
 15060.00
207430.00
                      24990.00
                       7530.00
                      16660.00
                      18520.00
                      67920.00
                      67920.00

                       8300.00
                       9040,00
                      85260.00
                          1192

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 10




 o


 b

 
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DRAFT
                       TABLE  359

         ITEMIZED COST SUMMARY FOR ALTERNATIVE C8-IV
            (COFFEE ROASTING WITH WET SCRUBBERS)
ITEMIZED  COST  SUMMARY  FOR  WASTEMTER TREATMENT CHAIN
DESIGN EFFICIENCY... 90.0  PERCENT BCD REDUCTION
TREATMENT  MODULES!
                   Bl..CONTROL
                   B...PUMPING
                       HOUSE
                       STATION
                   H...NITROGEN  ADDITION
                   I...PHCSPHORUS ADDITION
                   L...AERATED LAGCCN
INVESTMENT  CCSTSl
                1.
                2.
                3.
                4.
                5.
            CONSTRUCTION
            LAND
            ENGINEERING
            CONTINGENCY
            PVC
                TOTAL
YEARLY
OPERATING
        1.
        2.
        3.
        4.
COSTSl
  LABOR
                    CHEMICALS
                    MAINTPNAK'CERSLPPLIES
                    PVC  LINER
                TOTAL

TOTAL  VEARLY  COSTSt
                i.  YFAPUY  OPERATING COST
                2.  YEARLY  INVESTMENT
                   COST  RECOVERY
                3.  DEPRECIATION
                TOTAL
                        154980.00
                        26320.00
                        15500.00
                        15500.00
                         4460.00
                        218760.00
24990.00
 2210.00
15140.00
 6210.00
  270.00
48820.00
                                   48820.00

                                    8750.00
                                    9520.00
                                   67090.00

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DRAFT
                     TABLE 360

        ITEMIZED COST SUMMARY FOR ALTERNATIVE C8-V
                   (EGG PROCESSING)
ITEMIZED COST SUMMARY  FOR  WASTEKATER  TREATMENT CHAIN
DESIGN EFFICIENCY... 95.0  PERCENT  BOO REDUCTION
TREATMENT MCDULESi
                  Bl..CONTROL  HOUSE
                  B...PUMPING  STATION

                  H...NITROGEN ADDITION
                  I...PHOSPHORUS  ADDITION
                  L...AERATED  LAGOON
                  B,.'.PUMPING  STATION
                  N...DUAL  MEDIA  PRESSURE  FILTRA'N
INVESTMENT COSTSt
                1.
                2.
                3.
                4.
                5;
                   CONSTRUCTION
                   LAND
                   ENGINEERING
                   CONTINGENCY
                   PVC LINER
               TOTAL

YEARLY OPERATING CCSTSl
               !•  LABOR
               2D  POWER
               30  CHEMICALS
               40  MAJNTENANCE&SUPPIIES
               5Q  PVC LINER
            ,   TOTAL

TOTAL YEARLY COSTS!
               1, YEARLY OPERATING  COST
               2, YEARLY INVESTMENT
                  COST .RECOVERY
               3, DEPRECIATION
               TOTAL
176410.00
 28320.00
 176*10.00
 17640.00
  4460.00
244470.00
                                          24990.00
                                           4540.00
                                          15140.00
                                           6220,00
                                            270.00
                                          53160.00
                                          53160.00

                                           9780.00
                                          10610.00
                                          73750.00
                         1195

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                  tn
                  9E
                  in
2
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o
                            10.*
                            tat.i
                                  c
                             ITI.I
                             IM.I
                             III.*
                             »?.» IT
                                 M.e»    ft.ee
                                                         «».»•     *

                                                       EFFICIENCY
«T.ee    te.ee    ««.ee   iee.ee
                                                           FIGURE 334

                                  INVESTMENT AND YEARLY COSTS FOR SUBCATEGQRY Ce, AUT» V

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