Estimating Water Treatment Costs Volume 4 Computer User's Manual for Retrieving and Updating Cost Data

&EPA United States Environmental Protection Agency Municipal Environmental Research Laboratory Cincinnati OH 45268 EPA-600/2-79-162d August 1979 Research and Development Estimating Water Treatment Costs Volume 4 Computer User's Manual for Retrieving and Updating Cost Data ------- RESEARCH REPORTING SERIES Research reports of the Office of Research and Development, U.S. Environmental Protection Agency, have been grouped into nine series. These nine broad cate- gories were established to facilitate further development and application of en- vironmental technology. Elimination of traditional grouping was consciously planned to foster technology transfer and a maximum interface in related fields. The nine series are: 1. Environmental Health Effects Research 2. Environmental Protection Technology 3. Ecological Research 4, Environmental Monitoring 5. Socioeconomic Environmental Studies 6. Scientific and Technical Assessment Reports (STAR) 7. Interagency Energy-Environment Research and Development 8. "Special" Reports 9. Miscellaneous Reports This report has been assigned to the ENVIRONMENTAL PROTECTION TECH- NOLOGY series. This series describes research performed to develop and dem- onstrate instrumentation, equipment, and methodology to repair or prevent en- vironmental degradation from point and non-point sources of pollution. This work provides the new or improved technology required for the control and treatment of pollution-sources to meet environmental quality standards. This document is available to the public through the National Technical Informa- tion Service, Springfield, Virginia 22161. ------- EPA-600/2-79-162d August 1979 ESTIMATING WATER TREATMENT COSTS Volume 4. Computer User's Manual for Retrieving and Updating Cost Data by Thomas S. Lineck Robert C. Gumerman Russell L. Gulp Gulp/Wesner/Gulp Consulting Engineers Santa Ana, California 92707 Contract No. 68-03-2516 Project Officer Robert M. Clark Drinking Water Research Division Municipal Environmental Research Laboratory Cincinnati, Ohio 45268 MUNICIPAL ENVIRONMENTAL RESEARCH LABORATORY OFFICE OF RESEARCH AND DEVELOPMENT U.S. ENVIRONMENTAL PROTECTION AGENCY CINCINNATI, OHIO 45268 ------- DISCLAIMER This report has been reviewed by the Municipal Environmental Research Laboratory, U.S. Environmental Protection Agency, and approved for publica- tion. Approval does not signify that the contents necessarily reflect the views and policies of the U.S. Environmental Protection Agency, nor does mention of trade names or commercial products constitute endorsement or recommendation for use. ii ------- FOREWORD The U.S. Environmental Protection Agency (EPA) was created because of increasing public and government concern about the dangers of pollution to the health and welfare of the American people. Noxious air, foul water, and spoiled land are tragic testimonies to the deterioration of our natural environment. The complexity of that environment and the interplay of its components require a concentrated and integrated attack on the problem. Research and development is that necessary first step in problem solution, and it involves defining the problem, measuring its impact, and searching for solutions. The Municipal Environmental Research Laboratory develops new and improved technology and systems to prevent, treat, and manage wastewater and solid and hazardous water pollutant discharges from municipal and community sources to preserve and treat public drinking water supplies, and to minimize the adverse economic, social, health, and aesthetic effects of pollution. This publication is one of the products of that research—a most vital communications link between the researcher and the user community. The cost of water treatment processes that may be used by water supply systems to remove contaminants included in the National Interim Primary Drinking Water Regulations is of interest to the EPA, State and local agencies, and consulting engineers. This volume contains documentation and user information for the WATER program, a FORTRAN computer program that retrieves and updates cost information for the 72 large-system unit processes and the 27 small system processes presented in Volumes 1, 2, and 3 of this report. The WATER program is capable of determining costs for individual processes and complete treatment plants. Francis T. Mayo Director Municipal Environmental Research Laboratory iii ------- ABSTRACT This volume is the fourth in a series of four reports on estimating costs for water treatment as a function of system size and treatment efficiency. Volume 4 is a computer users manual and contains a FORTRAN computer program, WATER, that can be used for retrieval and updating of all cost data contained in the Volumes 1, 2 and 3. Volume 1 is the summary volume and discusses the cost estimating approaches utilized to develop the cost curves and the treatment techniques applicable for contaminant removal. It also presents a series of examples demonstrating the use of the cost curves applicable to large water supply systems with treatment capacities between 1 and 200 mgd. Information is included on virus and asbestos removal. Volume 2 presents cost curves for large water systems (1 to 200 mgd), and Volume 3 presents cost curves for small systems (2,500 gpd to 1 mgd). The WATER program determines costs by retrieving stored coefficients for a least squares polynomial fit of the cost curves presented in Volumes 1, 2, and 3, and by evaluating the polynomial expression for the desired process design parameter. Cost information is presented for construction and operation and maintenance, including energy, maintenance material and labor. The conceptual designs and assumptions used in formulating the cost information are presented in Volumes 1, 2, and 3. The program will compute costs for individual processes or for a series of processes. Capital costs are determined from construction costs by applying cost factors (input by the user) for engineering, sitework, sub- surface considerations, land, and standby power. The program computes general contractor overhead and profit, legal, fiscal, and administrative fees, and interest during construction based on the overall cost of the project. All construction costs are stored in terms of October 1978 dollars, and are updated by one of two methods, determined by the user. The program computes a weighted composite cost index for each process, using eight individual cost indices for excavation and sitework, manufactured equipment, concrete, steel, labor, pipe and valves, electrical equipment and instrumenta- tion, and housing - or the user may specify updating by use of the Engineering News Record Construction Cost Index. Operation and maintenance costs are determined from unit costs (input by the user) such as dollars per hour for labor and dollars per kilowatt hour for electricity. Maintenance material costs are stored as dollars per year and are updated using the Bureau of Labor Statistics Price Index. The user need not be an experienced programmer, but a familiarity with programming is recommended. This report was submitted in fulfillment of Contract No. 68-03-2516 by Gulp/Wesner/Gulp under the sponsorship of the U.S. Environmental Protection Agency. This report covers the period November 1, 1976 to January 1, 1979. It was completed as of July 2, 1979. iv ------- CONTENTS Foreword .... Abstract .... Figures .... Tables Acknowledgements 1. Introduction 2. Input Data Files 3. COST.DAT File Construction 4. PROCES.DAT File Construction 5. Program Output 6. Examples 7. Trouble Shooting Guide . . . 8. WATER Program Listing . . . . 9. CRV.DAT File iii iv vi vi vii 1 3 6 9 34 36 57 58 70 ------- FIGURES Number Page 1 PROCES.DAT Data Segments 17 2 Land Requirements for Conventional Plants 18 3 Land Requirements for Package Complete Treatment Plants 19 Number 1 2 3 4 5 6 TABLES COST.DAT File Example PROCES.DAT File Example Card-by-Card Explanation of COST.DAT File Process Cost Curves for Large and Small Water Treatment Systems Processes That Use Chemicals and Chemicals Used Process Parameter Units Page 4 5 6 10 15 22 vi ------- ACKNOWLEDGEMENTS This report was prepared under the direction of Dr. Robert M. Clark, Municipal Environmental Research Laboratory, Office of Research and Development. The report was prepared by Robert C. Gumerman, Russell L. Gulp, Sigurd P. Hansen, Thomas S. Lineck, and Bruce E. Burris of Gulp/Wesner/Gulp. Ms. Karin J. Wells of Gulp/Wesner/Gulp was responsible for typing of the final report. Mr. Ronald M. Dahman of Zurheide-Herrmann, Inc., was responsible for checking all unit costs. Dr. Isadore Nusbaum and Mr. Dean Owens were respective sub-consultants on the reverse osmosis and ion exchange curves. Special acknowledgement is given to Mr. Keith Carswell, Dr. Robert M. Clark, Mr. Jack De Marco, Dr. Gary Logsdon, Dr. 0. Thomas Love, Mr. Benjamin Lykins, Jr., Mr. Thomas J. Sorg, all of the EPA Municipal Environmental Research Laboratory, who reviewed the final report, and Mr. Paul Dorsey, also of the EPA Municipal Environmental Research Laboratory, who reviewed the computer program. Mrs. Anne Hamilton was the technical editor for all four volumes of this reportx , . vii ------- ------- SECTION 1 INTRODUCTION SCOPE This report is Volume 4 of a four-volume study that presents construction and operation and maintenance cost curves for 99 unit processes that are especially applicable (either individually or in combination) to the removal of contaminants listed in the National Interim Primary Drinking Water Regulations. This volume is a computer users manual and contains documenta- tion and user information for the WATER program, which is a FORTRAN computer program that retrieves and updates cost information for the 72 large and 27 small water supply systems presented in Volumes 1, 2, and 3 of this report. Costs are also determined for treatment plants, and they are input to the program as trains of individual processes. BACKGROUND The WATER program described here can be used as a valuable tool to facilitate retrieval and updating of the cost information presented in Volumes 1, 2, and 3 of this report. Since WATER has been designed to compute costs for entire treatment plants, cost determinations for competing treatment trains or regional variations in operating costs for a particular treatment train can be made quickly and accurately. The costs generated by this program are broken down into capital costs and operation and' maintenance costs. Capital costs include those for construction, engineering, sitework and interface piping, subsurface considera- tions, standby power, legal, fiscal and administrative services, interest during construction, and land. Operation and maintenance costs include those for electricity, labor, maintenance materials, diesel fuel, natural gas, and chemicals. Most costs are stored as coefficients of third-degree polynomial expressions determined by the method of least squares for the values in the cost tables presented in Volumes 1, 2, and 3. Therefore, the cost generated for a specific point in these tables could vary by as much as 10 to 15 percent from the value generated by the program, depending on the deviation of the values in the table from a smooth curve fit. In general, the 'differences between the costs generated by the program and the costs obtained through use of the cost curves in Volumes 1, 2, and 3, will be insignificant. The user need not be an experienced programmer, but a familiarity with programming is recommended. ------- PURPOSE AND OBJECTIVES The purpose of this volume is to present complete documentation and user information for the FORTRAN computer program, WATER, which retrieves and updates cost information for the large and small water supply treatment processes presented in Volumes 1, 2, and 3 of this report. The WATER program has been designed to facilitate the estimation of overall treatment plant costs as well as individual process costs. ------- SECTION 2 INPUT DATA FILES Three data files are necessary to run this program. Two of these files, COST.DAT and PROCES.DAT, are set up by the user. The third data file, CRV.DAT, is a construction and operation and maintenance data base containing information about each of the water treatment processes considered in this report. This file is an integral part of the program and must be established on the computing system with the main program. Once it is established, the general user should have no need to access the main program, WATER, or the data base, CRV.DAT. The first of the two data files to be constructed by the user is the COST.DAT file. Table 1 is an example listing of the COST.DAT file. This file basically contains all the cost information necessary to run the program. The variables in this file, called cost factors, must be input in the sequence shown in Table 1. A detailed explanation of the input format is given in the following section on COST.DAT File Construction. The second file to be constructed by the user is the PROCES.DAT file. Table 2 is an example listing of the PROCES.DAT file. This file contains information about each of the water treatment processes for which the user desires costs. A detailed explanation of the input format is given in a following section entitled, PROCES.DAT File Construction. ------- Table 1 COST.DAT File Example COSTS PRESENTED ARE CURRENT AS OF OCTOBER 1978 CAPITAL COST FACTORS (X OF CONSTRUCTION COST)* 1 ENGINEERING(X) =10* 2 SITEUORK, INTERFACE PIPING(%) =5* 3 SUBSURFACE CONSIDERATIONS(%) =00 4 STANDBY POWER(%) =00 5 INTEREST RATE(%> =7* 6 NUMBER OF YEARS =200 7 LAND COST, /ACRE =2000* UNIT COST FACTORS: 8 ELECTRICITY, /KWH = 03 9 LABOR, $/HR =10* 10 DIESEL FUEL, $/GAL =45 11 NATURAL GAS, $/CU FT =»0013 12 BLDNG ENERGY USE,KWH/SQ FT/YR =1026 COST INDEXES: 13 EXCAVATION(ENR SKILLED LABOR) 14 MANUFACTURED EQUIP (BLS #114) 15 CONCRETE (BLS #132) 16 STEEL (BLS #101,3) 17 LABOR (ENR SKILLED LABOR) 18 PIPE S VALVES (BLS #114901) 19 ELECTRICAL S INSTR (BLS #117) =1675 20 HOUSING (ENR BUILDING COST) =25476 21 PRODUCER PRICE INDEX =1997 22 ENR CONSTRUCTION, '67 BASE YR =00 OUTPUT(6 FOR LP,5 FOR TELETYPE) -5 PRINTOUT(DETAILED OR SUMMARY) "SUMMARY 9,2 75,125 =2470 =2213 =221 =262 =247 1 1 0 ------- Table 2 PROCES.DAT File Example ACRES=15 1,57,IN-PLANT PUMPING 2,50,35,75,35 3,75 * 0, TDH 1,60,PRESSURE ION EXCHANGE-SOFTENING 2,5,0,35,50,35 3,306,REGENERATION SALT 1,15,SODIUM HYDROXIDE FrEE» SYSTEMS 2>5035,6250,4380 3,2000,SODIUM HYDFi'OXiriE, 15 MG/L lil9CL2 FEED-CYLINDER STORAGE 2,50,35,630,440 3,3000,CHLORINE,15 MG/L 1,95,CLEARWELL STORAGE-GROUND LEVEL 2,50,35,500000 * 0,500000 * 0 1,93,FINISHED WATER PUMPING FACILITY 2,50,35,80,35 3,2000,TDH 000000000000000000000000000000000000000000 ACRES~00 1?11,LIME FEED-NO RECALCINATION 2,10,07,8.7,61 3,650,LIME,25 MG/L ------- , SECTION 3 COST.DAT FILE CONSTRUCTION To aid in understanding the format of this data file, the user is referred to Table 1, which must be constructed as shown. Cards 2, 10, and 16 are for user information only and are skipped by the program when reading this file. They must not be omitted, however, or the program will skip actual data. A card-by-card explanation of this file is given in Table 3. Table 3 Card-by-Card Explanation of COST.DAT File Card No. 3-9 10 11-15 16 Explanation First 48 characters printed "as is" on the program output. Intended to be used to denote valid data of cost information produced. For user information only. program. This line is skipped by the Capital cost factors as shown. Program read skips the first 34 characters then reads floating point number input. These values must start in Column 35 and must contain a decimal point. Percentage values, as indicated, must be percentages, not decimal values. Example: Engineering must be listed as 10.0 for 10 percent, not as 0.10. The program internally divides by 100. For user information only - skipped by program read. Unit cost factors as shown. As with lines 3-9, program read skips the first 34 characters. Values must begin in Column 35 and must contain decimal points. Units are as shown in Table 1. For user information only - skipped by program read. ------- Card No. 17-26 27 28 29-30 Explanation (continued) Cost indices as shown. As with lines 3-9 and 11-15, program read skips the first 34 characters. Values must hegin in Column 35 and must contain decimal points. These cost indices are used to update the cost data base stored in the CRV.DAT file. The user has the option of using the first eight cost indices listed (Excavation through Housing) to update the construction costs produced by the program, or he can use the ENR Construction Cost Index (line 26) in lieu of the first eight indices. Thfe computer will use the ENR Construction Cost Index if the value input is greater than zero. If the value input for the ENR Construction Cost Index is equal to zero, the computer will use the first eight indices. This card designates the location for program output. On most computer installations, a "5" designates the teletype or remote terminal. The program output is 132 characters wide, so it is suggested that the line printer be used if the teletype does not have the capacity to print 132 characters per line. The value for this variable must be an integer and must begin in Column 35. This card designates a detailed or summary output. See sections 5 (Program Output) and 6 (Examples) for an explanation and sample of these options. These cards are optional. The user may wish to run the program while varying only one of the cost factors in the COST.DAT file. Cost factors are numbered 1 through 22 for convenience. For example, cost factor number 9 is labor ($/hr). Thus if the user wants to determine the change in overall operations and maintenance cost based on the regional variation of the cost of electricity across the nation, he first inputs in card 29 the number of the cost factor and the additional number of values to be used for that cost factor. In this case, cards 29 and 30 are as follows for two additional values of cost factor number 9: Card 29: Card 30: 9,2 7.5,12.5 Card 30 contains the two additional values of labor ($/hr) namely, 7.5 and 12.5. Note that all input values begin in column one for lines 29 and 30, and that they are separated by a comma. Up to 10 additional values may be input. They must be floating point numbers with decimal points, but they can appear in any column as long as they are separated by a comma. ------- Card No. Explanation (continued) 29-30 Cards 29 and 30 shown in the listing of the COST.DAT file in continued Table 1 accomplish the following: The program computes all costs with the cost of labor ($/hr) at 10. Then the program is automatically rerun twice with the cost of labor ($/hr) at 7.5 and 12.5. This produces three complete printouts. If the user wants to run the program only once, without varying any of the 22 cost factors, cards 29 and 30 are omitted, and the designation of DETAILED or SUMMARY printout is the last card of the COST.DAT file. ------- SECTION 4 PROCES.DAT FILE CONSTRUCTION The PROCES.DAT file contains design and operating information about each of the processes for which the user may desire costs. Table 4 lists the processes for which costs are available and includes the process parameter range over which cost information is stored in the computer. For example, process 1 CL2 FEED - CYLINDER STORAGE, has cost information stored in the program data file over a range of 10 to 10,000 Ib/day of chlorine feed. Also shown in Table 4 are the number of chemicals used in the treatment process, the process type and the number of data cards. Chemical cost information is input along with process design and operating parameters, as explained later. The number of chemicals used in the process is listed in Table 4, and in most cases, the types of chemicals used will be obvious (for example, chlorine is used in process 1, CL2 FEED - CYLINDER STORAGE). For convenience, however, Table 5 lists the processes that use chemicals and the chemicals used. The Process Type listed in Table 4 denotes the way in which information is input to the computer, and the number of data cards indicates the number of cards necessary to input information for that process. There are a total of 11 process types. The input data for each type are described later in this section. Since the computer program is designed to determine individual process costs and plant costs by totaling the process costs, the PROCES.DAT file is assembled into what is here termed loosely as "segments" of data (Figure 1). THE ACRES= CARD Each data segment corresponds to a treatment plant and must begin with the ACRES= card. This card denotes the land area, in acres, required for the plant. If land costs are not to be included, the card should read ACRES=0.0, with the "A" in acres beginning in Column 1. For convenience, typical land area requirements are shown in Figures 2 and 3. PROCESS DATA CARDS Following the ACRES= card, data cards for the processes in the plant are assembled sequentially. There may be as many processes as desired, in any order, and processes may be input more than once. The set of process data cards preceded by the ACRES= card constitutes a segment of data (Figure 1). 9 ------- Table 4 Process Cost Curves for Large and Small Water Treatment Systems TREATMENT PROCESS - LARGE SYSTEMS 1 CL2 FEED-CYLINDER STORAGE 2 CL2 FEED-ON SITE STORAGE TANK 3 CU2 FEED FROM RAIL CAR 4 CHLORINE DIOXIDE GENERATING»FEED 5 OZONE GENERATION SYSTEMS A OZONE CONTACT CHAMBER 7 ON-SITE HYPOCHLORITE GENERATION B AI.UH FEED-LIOUID STOCK 9 ALUM FEED-DRY STOCK 10 POLYMER FEED SYSTEMS 11 LIME FEED-NO RECALCINATION 12 LIME FEED-UITH RECALCINATION 13 POTASSIUM PERMANGANATE FEED 14 SULFURIC ACID FEED SYSTEMS IS SODIUM HYDROXIDE FEED SYSTEMS 16 FERROUS SULFATE FEED SYSTEMS 17 FERRIC SULFATE FEED SYSTEMS 18 ANHYDROUS AMMONIA FEED FACILITY 19 AQUA AMMONIA FEED FACILITY 20 POWDERED ACTIVATED CARBON FEED 21 RAPID HlXr 0=300 22 RAPID HlXr G-600 23 RAPID MIXr G=900 24 FLOCCULATION-HORIZ PADDLEr G=20 25 FLOCCULATION-HORIZ PADDLEf G=50 24 FLOCCULATION-HORIZ PADDLEr G=BO 27 FLOCCULATION-VERT TURBINE. G=20 28 FLOCCULATION-VERT TURBINE. G=50 PARAMETER RANGE 10.0 2000.0 2OOO.O 10.0 10,0 460.0 10.0 5.4 10.0 1.0 10,0 1000.0 1.0 10,0 10.0 10.7 13.3 250.0 250.0 3.5 100.0 100.0 100.0 1800.0 1800.0 1800.0 1800.0 1800.0 TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO 10000 10000 10000 3500 3500 92000 10000 5400 5000 200 1000 10000 500 5000 10000 5350 6600 5000 5000 7000 20000 20000 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 .0 20000.0 1000000.0 1000000.0 500000, .0 25000.0 25000. ,0 NUMBER OF CHEMICALS LB/DAY LB/DAY LB/DAY LB/DAY LB/DAY CU FT LB/DAY LB/HR LB/HR LB/DAY LB/HR LB/HR LB/DAY GPD LB/DAY LB/HR LB/HR LB/DAY LB/DAY LB/HR CU FT CU FT CU FT CU FT CU FT CU FT CU FT CU FT 1 1 1 2 0 0 1 1 .1 1 1 1 1 1 1 1 1 1 1 1 0 0 0 0 0 0 0 0 PROCESS TYPE 1 1 1 1 1 1 1 1 1 10 1 8 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 NO. 1 CAR) 3 3 3 4 2 2 3 3 3 3 3 4 3 3 3 3 3 3 3 3 2 2 2 2 2 2 2 2 10 ------- Table 4 (Continued) TREATMENT PROCESS - LARGE SYSTEMS 29 FLOCCULATION-VERT TURBINE, G=80 30 CIRCULAR CLARIFIER-LIME SLUDGE 31 CIRC CLARIFIER-FECL3 & ALUM SLDG 32 RECTANGULAR CLARIFIER-LIME SLDG 33 RECT CLARIFIER-FECL3 X ALUM SLG 34 UPFLOW SOLIDS CONTACT CLARiG=70 35 UPFLOW SOLIDS CONTACT CLAR»G=11O 36 UPFLOW SOLIDS CONTACT CLAR>G=150 37 TUBE SETTLING MODULES 38 GRAVITY FILTRATION STRUCTURE 39 FILTRATION MEDIA-RAPID SAND 40 FILTRATION MEDIA-DUAL MEDIA 41 FILTRATION MEDIA-MIXED MEDIA 42 BACKWASH PUMPING FACILITIES OSM! 43 HYDRAULIC SURFACE WASH SYSTEMS 44 AIR-WATER BACKWASH FACILITIES 45 WASH WATER SURGE BASINS 46 FILTER MOD-RAP SAND TO HIGH RATE 47 CONTINUOUS AUTO. BACKWASH FILTER 48 RECARBONATION BASIN 49 RECARBONATION-LIQUin C02 FEED 50 RECARB-C02 FROM SUBMERGED BURNER 51 RECARBONATION-C02 FROM STACK GAS 52 MULTIPLE HEARTH RECALCINATION 53 CONTACT BASIN-DIRECT FILTRATION 54 PRESSURE DIATOMITE FILTERS 55 VACUUM DIATOMITE FILTERS PARAMETER RANGE 1800.0 707.0 707.0 240.0 240.0 255.0 255.0 255. 0 280.0 140.0 370.0 140.0 140.0 1260.0 1537.2 140.0 140.0 10000.0 140.0 360.0 770.0 380.0 500.0 25OO.O 179.0 2640.0 1.0 1.0 TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO 25000.0 31400.0 31400.0 4800.0 4800.0 14500.0 14500.0 14500.0 56000.0 28000.0 74800.0 29900.0 29900.0 23000.0 28060.0 28000.0 28000.0 500000.0 28000.0 70400.0 35200.0 15000.0 10000.0 50000.0 2930.0 528OO.O 200.0 200.0 NUMBER OF CHEMICALS CU FT SQ FT SO FT SQ FT SQ FT SQ FT SQ FT SQ FT SQ FT SQ FT SQ FT SQ FT SQ FT GPM SQ FT SQ FT SQ FT GAL SQ FT SQ FT CU FT LB/DAY LB/DAY LB/DAY SQ FT CU FT MGD MGD 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 o 0 0 0 1 0 0 0 0 3 3 PROCESS TYPE 1 3 3 3 3 3 3 3 . 1 1 1 1 1 1 1 1 1 1 1 3 1 3 1 3 3 2 2 NO. D CARD 2 3 3 3 3 3 3 3 2 2 2 2 2 2 2 2 2 2 2 3 3 3 2 3 3 5 5 11 ------- Table 4 (Continued) TREATMENT PROCESS - LARGE SYSTEMS 56 PRESSURE FILTRATION PLANTS 57 IN-PLANT PUMPING SB WASH UATER STORAGE TANKS 59 REVERSE OSMOSIS 60 PRESSURE ION EXCHANGE-SOFTENING 61 GRAVITY ION EXCHANGE-SOFTENING 62 PRESSURE ION EXCHANG-N03 REMOVAL 63 ACTIV, ALUMINA-FLUORIDE REMOVAL 64 GRAVITY GAC CONTACTORS-CONCRETE OIH: 65 GRAVITY GAC CONTACTORS-STEEL OIH: 66 PRESSURE CARBON CONTACTORS OXM: 67 CONVERT FILTER TO GAC CONTACTOR 68 GRANULAR ACT CARBON-CONSTR COST 69 MAKEUP CARBON COST-OSM ONLY 70 CAPPING SAND FILTER W/ANTHRACITE 71 REGIONAL GAC REGEN-TRANS S STOR OIH: 72 REGIONAL HULTI HEARTH GAC REGEN 73 MULTIPLE HEARTH GAC REGENERATION 74 INFRARED CARBON REGEN FURNACE 75 FLUIDIZED BED GAC REGENERATION 76 POWDERED CARD REGEN-FLUIDIZED BD 77 POWDERED CARB REGEN-ATOHIZED SUS 78 CHEN SLUDGE PUHPING-UNTHICKENED 79 CHEH SLUDGE PUMPING-THICKENED 80 GRAVITY SLUDGE THICKENER-LIME SI GRAV SLDO THICKENER-ALUM S FECL3 PARAMETER RANGE 140.0 1.0 21000.0 1.0. 1.1 1.5 1.1 0.7 350.0 140.0 6280.0 31400.0 390.0 157.0 370.0 10000.0 10000.0 350.0 1000.0 30000.0 27. 0 27.0 2400.0 6000.0 209.0 1000.0 20.0 5.0 314.0 314.0 TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO 28000.0 200.0 900000.0 200.0 123.0 150.0 12.3 135.0 10600.0 28000.0 14100.0 628000.0 2260.0 6790.0 70000.0 10000000.0 10000000.0 70000.0 20000.0 3000000.0 1510.0 1510.0 60000.0 24000.0 33400.0 1000O.O 10000.0 1250.0 17800.0 17800.0 SO FT MGD GAL MGD MGD MGD MGD MGD CU FT SO FT CU FT CU FT CU FT SO FT SO FT LB LB/YR SO FT CU FT LB/YR SQ FT SQ FT LB/DAY LB/DAY LB/DAY LB/DAY GPM GPM SQ FT SQ FT NUMBER OF CHEMICALS 0 0 0 3 1 1 1 2 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 PROCESS TYPE 1 5 1 2 1 1 1 2 4 4 4 1 1 1 1 6 12 3 1 3 1 1 1 1 3 3 NO. ] CAR] 2 3 2 5 3 3 3 4 3 3 3 2 2 2 2 3 4 3 2 3 2 2 2 2 3 3 12 ------- Table 4 (Continued) TREATMENT PROCESS - LARGE SYSTEMS 82 VACUUM FILTERS 83 BELT FILTER PRESS 84 FILTER PRESS 85 DECANTER CENTRIFUGES 86 BASKET CENTRIFUGES 87 SAND DRYING BEDS 88 SLUDGE DEUATERING LAGOONS OSM! 89 SLUDGE DISPOSAL-SANITARY SEWER 90 LIQUID SLUDGE HAULING 91 DEUATERED SLUDGE HAULING 92 RAW WATER PUMPING FACILITY 93 FINISHED WATER PUMPING FACILITY 94 CLEARWELL STORAGE-BELOW GROUND 95 CLEARWELL STORAGE-GROUND LEVEL 96 DIFFUSED AERATION BASIN 97 AERATION-AERATION TOWERS 98 ADMINrLAB & MAINTENANCE BUILDING TREATMENT PROCESS - SMALL SYSTEMS 99 PACKAGE COMPLETE TREATMENT PLANT 100 PACKAGE GRAVITY FILTER PLANTS 101 PACKAGE PRESSURE FILTRATION PLNT 102 FILTER MEDIA-RAPID SAND 103 FILTER MEDIA-DUAL MEDIA 104 FILTER MEDIA-MIXED MEDIA 105 FILTER MEDIA-MIXEDrINST U/MF SUP 106 PACKAGE PRESS DIATOMITE FILTERS PARAMETER RANGE 9.4 15.0 4.3 10.0 3600.0 5000.0 40000.0 25000.0 20.0 1.3 1000.0 1.0 1.5 10000.0 8500.0 1900.0 680.0 1.0 4.0 80.0 0.7 4.0 4.0 4.0 4.0 28000.0 TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO 1320.0 450.0 896.0 500.0 720000.0 40OOOO.O 8000000.0 5000000.0 10000.0 100.0 300000.0 200.0 300.0 7500000.0 9400000.0 380000.0 256000.0 200.0 1400.0 1400.0 350.0 280.0 280.0 280.0 280.0 1000000.0 SQ FT GPM CU FT GPM GPD SO FT CU FT CF/YR GPM MG/YR CY/YR MGD MGD GAL GAL CU FT CU FT MGD GPM GPM GPM SQ FT SQ FT SQ FT SQ FT GPD NUMBER OF CHEMICALS 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 4 4 4 0 0 0 0 4 PROCESS TYPE 1 1 1 3 1 1 1 11 7 7 5 5 1 1 1 1 1 9 9 9 1 1 1 1 2 NO. i CAR] 2 2 2 3 2 2 2 3 3 3 3 3 2 2 2 2 2 7 7 7 2 2 2 2 6 13 ------- Table 4 (Continued) TREATMENT PROCESS - SMALL SYSTEMS 107 PACKAGE VACUUM DIATOMITE FILTERS 108 PACKAGE ULTRAFILTRATION PLANTS 109 PACKAGE GRAN ACT CARBON COLUMNS 110 POTASSIUM PERMANGANATE FEED SYST 111 POtYMtR FEED SYSTEMS 112 POWDERED ACT CARBON FEED SYSTEMS 113 DIRECT FEED GAS CHLORINATION 111 SODIUM HYPOCHLORITE SOLUTN FEED 115 OZONE GENERATING AND FEED 116 OZONE CONTACT CHAMBER 117 CHLORINE DIOXIDE GENERATING/FEED 118 ULTRAVIOLET LIGHT DISINFECTION 11? REVERSE OSMOSIS 120 PRESSURE ION EXCHANGE-SOFTENING 121 PRESSURE ION EXCHANG-N03 REMOVAL 122 ACTIVATED ALUMINA FLUORIDE REMOV 123 BONE CHAR FLUORIDE REMOVAL 12-1 PACKAGE RAU UATER PUHPING-TDH=°50 125 PACKAGE HIGH SERVICE PUMP STATN 126 STEEL BACKUASH/CLEARWELL TANKS 127 LIQUID SLUDGE HAULING 128 DEUATERED SLUDGE HAULING 129 SLUDGE DISPOSAL-SANITARY SEUER 130 SLUDGE DEUATERING LAGOONS OSH: 131 SAND DRYING BEDS PARAMETER RANGE 30.0 2SOO.O 2500.0 0.1 0.1 1.0 0.1 0.1 0.5 850.0 0.1 10.0 2500.0 70000.0 70000.0 12700.0 16300.0 20.0 30.0 500.0 •68.0 100.0 50.0 1500.0 750.0 TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO TO 720.0 1000000.0 500000.0 10.0 10.0 10.0 100.0 100.0 10.0 13500.0 50.0 780.0 1000000.0 860000.0 830000.0 910000.0 800000.0 700.0 1100.0 30000.0 41100.0 50000.0 25000.0 30000.0 15000.0 NUMBER OF CHEMICALS GPM GPD GPU LB/DAY LB/DAY LB/HR LB/DAY LB/DAY LB/DAY GAL LB/DAY GPM GPD GPD GPD GPD GPD GPM GPM GAL GPD CY/YR GPD CU FT CF/YR 4 3 0 1 1 1 1 1 0 0 2 0 3 1 1 2 2 0 0 0 0 0 0 0 PROCESS TYPE 2 2 1 1 10 1 1 1 1 1 1 1 2 1 1 2 1 1 1 : 1 7 7 11 1 NO. 1 CAR] 6 5 2 3 3 3 3 3 2 2 4 2 5 3 3 4 4 2 2 2 3 3 3 2 200.0 TO 800.0 SQ FT 14 ------- Table 5 Processes that Use Chemicals and Chemicals Used TREATMENT PROCESS - LARGE SYSTEMS 1 CL2 FEED-CYLINDER STORAGE 2 CL2 FEED-ON SITE STORAGE TANK 3 CL2 FEED FROM RAIL CAR 4 CHLORINE DIOXIDE GENERATINGrFEED 7 ON-SITE HYPOCHLORITE GENERATION 8 ALUM FEED-LIQUID STOCK 9 ALUM FEED-DRY STOCK 10 POLYMER FEED SYSTEMS 11 LIME FEED-NO RECALCINATION 12 LIME FEED-UITH RECALCINATION 13 POTASSIUM PERMANGANATE FEED 14 SULFURIC ACID FEED SYSTEMS 15 SODIUM HYDROXIDE FEED SYSTEMS 16 FERROUS SULFATE FEED SYSTEMS 17 FERRIC SULFATE FEED SYSTEMS 18 ANHYDROUS AMMONIA FEED FACILITY 19 AQUA AMMONIA FEED FACILITY 20 POWDERED ACTIVATED CARBON FEED 49 RECARDONATION-LIQUID C02 FEED 54 PRESSURE DIATOMITE FILTERS 55 VACUUM DIATOMITE FILTERS 59 REVERSE OSMOSIS 60 PRESSURE ION EXCHANGE-SOFTENING 61 GRAVITY ION EXCHANGE-SOFTENING 62 PRESSURE ION EXCHANG-N03 REMOVAL 63 ACTIV. ALUMINA-FLUORIDE REMOVAL TREATMENT PROCESS - SMALL SYSTEMS 99 PACKAGE COMPLETE TREATMENT PLANT CHEMICALS USED CHLORINE CHLORINE CHLORINE CHLORINE»SALT SALT ALUM-LIQUID STOCK ALUM-DRY STOCK POLYMER LIME LIME POTASSIUM PERMANGANATE SULFURIC ACID SODIUM HYDROXIDE FERROUS SULFATE FERRIC SULFATE ANHYDROUS AMMONIA AQUACEOUS AMMONIA POWDERED ACTIVATED CARDON LIQUID CARBON DIOXIDE POLYMERr ALUMr DIATOMACEOUS EARTH POLYMER, ALUMT DIATOMACEOUS EARTH SULFURIC ACID» HEXAMETAPHOSPHATE, CHLORINE SALT SALT SALT SODIUM HYDROXIDE, SULFURIC ACID ALUM. POLYMER. SODA ASH. CHLORINE OR HYPOCHLORITE 15 ------- TREATMENT PROCESS - SMALL SYSTEMS 100 PACKAGE GRAVITY FILTER PLANTS 101 PACKAGE PRESSURE FILTRATION PLNT lOi PACKAGE PRESS DIATOMITE FILTERS 107 PACKAGE VACUUM DIATOMITE FILTERS 108 PACKAGE ULTRAFILTRATION PLANTS 110 POTASSIUM PERMANGANATE FEED SYST 111 POLYMER FEED SYSTEMS 112 POWDERED ACT CARBON FEED SYSTEMS 113 DIRECT FEED GAS CHLORINATION 114 SODIUM HYPOCHLORITE SOLUTN FEED 117 CHLORINE DIOXIDE GENERATING/FEED 117 REVERSE OSMOSIS 120 PRESSURE ION EXCHANGE-SOFTENING 121 PRESSURE ION EXCHANG-N03 REMOVAL 122 ACTIVATED ALUMINA FLUORIDE REMOV 123 BONE CHAR FLUORIDE REMOVAL Table 5 (Continued) CHEMICALS USED ALUM? POLYMER? SODA ASH* CHLORINE OR HYPOCHLORITE ALUM? POLYMER* SODA ASH? CHLORINE OR HYPOCHLORITE ALUMr POLYMER* CHLORINE. DIATOMACEOUS EARTH ALUM? POLYMER? CHLORINE? DIATOMACEOUS EARTH SULFURIC ACID? HEXAMETAPHOSPHATE? CHLORINE POTASSIUM PERMANGANATE POLYMER POUDERED ACTIVATED CARBON GASEOUS CHLORINE SODIUM HYPOCHLORITE CHLORINE? SALT SULFURIC ACID? HEXAMETAPHOSPHATEr CHLORINE SALT SALT SODIUM HYDROXIDE? SULFURIC ACID SODIUM HYDROXIDE? CARBONIC ACID 16 ------- PROCESS DATA CARDS. / PROCESS DATA CARDS. /"ACRES 2.0 / ooeeeoeeooot PROCESS DATA CARD: ACRES 1.0 THIRD DATA SEGMENT SECOND DATA SEGMENT FIRST DATA SEGMENT Figure 1. PROCES.DAT data segments. 17 ------- o o CM to f- o IO c cd \ 8 a ca o u. o •H 4-> a OJ o a CO a o o so cd o ra T3 0) rCl 60 a (U \ 10 1^- UJ a < _J a. o IO IO CM •H 3 a< 01 bO •H cd en M O ctf (U M ctf id T3 cd o ro O OJ 18 ------- CO I +J a I td CD CO $-1 DO •H saaov-QNvn 19 ------- THE ZERO CARD Segments of data in the PROCES.DAT file must be separated by a card containing a string of at least 15 zeros. (In some systems, a blank card may suffice). If cost data are desired for only one plant or segment of data, no ZERO card should be included. Inclusion of cost data for two or more plants requires that the PROCES.DAT file be arranged as shown in Figure 1, with ZERO cards between each segment. The last card in the PROCES.DAT file is the last card of the last segment of data. A Zero card must not be placed at the end of the file. A ZERO card is only placed between segments. PROCESS TYPES AND DATA INPUT The various process types require two to seven cards for data input. The First two cards of data for all process types are the same. Data card format and content are explained in the following pages. Type 1 Process Data Input Card 1-- The first card of data contains the following information starting in column 1: The card number (the integer 1) followed by a comma in column 2, the process number (integer) from Table 3 followed immediately by a comma, and finally, the process name. Examples: Card 1: 1,9,ALUM FEED - DRY STOCK Card 1: 1,21,RAPID MIX, G=300 Card 1: 1,131,SAND DRYING BEDS The commas are necessary to separate numbers and must not be omitted. The process name is optional, but, it is a useful identifier for the user when reviewing the PROCES.DAT file later. The comma preceding the process name is not optional Card 2~ The second card of data contains the following information starting in column 1: The card number (the integer 2) followed by a comma in column 2, the plant design flow in mgd (floating point) followed by a comma, the plant actual flow in mgd (floating point) followed by a comma, the process design parameter (floating point) followed by a comma, and the process operating parameter (floating point) 20 ------- Examples: Using the same three examples as used above for Card 1, assume the following: Example 1: Plant Design Flow = 10.0 mgd Plant Operating Flow = 7.0 mgd Alum Design Feed = 245 Ib/hr Alum Operating Feed = 170 Ib/hr Card 2: 2,10.0,7.0,245.0,170.0 Example 2: Plant Design Flow = 5.0 mgd Plant Operating Flow = 4.0 mgd Design Rapid Mix Volume = 464 cu ft Operating Rapid Mix Volume = 464 cu ft Card 2: 2,5.0,4.0,464.0,464.0 Example 3: Plant Design Flow = 0.5 mgd Plant Actual Flow =0.25 mgd Design Sand Drying Bed Area = 500.0 sq ft Operating Sand Drying Bed Area = 250.0 sq ft Card 2: 2,0.5,0.25,500.0,250.0 The process design and operating parameters have the units specified in Tables 4 and 6. The process design parameter is used to calculate construction costs, and the operating parameter is used to determine operation and maintenance costs. In some cases, these parameters have different units and/or ranges. In Table 4, for example, process 42 (BACKWASH PUMPING FACILITIES) has the unit gpm for the design parameter and sq ft for the operating parameter. Plant flows are always in mgd. All values are floating point (except the card number) and are separated by a comma. Notice that for some processes such as chemical feed and pumping, the numerical values of the design and operating parameters may be different, since the design parameter indicates capacity, and these processes generally do not operate at capacity. For other processes, such as basins, the design and operating parameters are identical. Operation and maintenance costs for any process operating at less than 100 percent time can be determined by inputing a proportionately lower value for the operating parameter. For example, operation and maintenance costs for a 500 sq ft furnace operating 70 percent of the time are determined by inputing a value of 350 for the operating parameter. Cards 3 and 4— The number of cards for a type 1 process is equal to 2 plus the number of chemicals. For example, process number 9, ALUM FEED - DRY STOCK, requires 2+1=3 cards. Process 21 (RAPID MIX, G=300) requires 2+0=2 cards. If a third or fourth card of data is required, it contains the following information: The number of the card (the integer 3 or 4) followed by a comma, the cost of the chemical(s) used in the process in dollars/ton (floating point) followed by a comma, and the name of the chemical used in the process (up to 24 characters). For most processes, the chemical(s) used will be 21 ------- Table 6 Process Parameter Units TREATMENT PROCESS - LARGE SYSTEMS 1 CL2 FEED-CYLINDER STORAGE LB/DttY 2 CL2 FEED-ON SITE STORAGE TANK LB/DAY 3 CL2 FEED FROM RAIL CAR LB/DAY 4 CHLORINE DIOXIDE GENERATINGFEED LB/DAY 5 OZONE GENERATION SYSTEMS LB/DAY 6 OZONE CONTACT CHAMBER CU FT 7 ON-SITE HYPOCHLORITE GENERATION LB/DAY 8 ALUM FEED-LIQUID STOCK LB/HR 9 ALUM FEED-DRY STOCK LB/HR 10 POLYMER FEED SYSTEMS LB/DAY 11 LIME FEED-NO RECALCINATION LB/HR 12 LIME FEED-UITH RECALCINATION LB/HR 13 POTASSIUM PERMANGANATE FEED LB/DAY 14 SULFURIC ACID FEED SYSTEMS GPD 15 SODIUM HYDROXIDE FEED SYSTEMS LB/DAY 16 FERROUS SULFATE FEED SYSTEMS LB/HR 17 FERRIC SULFATE FEED SYSTEMS LB/HR 18 ANHYDROUS AMMONIA FEED FACILITY LB/DAY 19 AQUA AMMONIA FEED FACILITY LB/DAY 20 POWDERED ACTIVATED CARBON FEED LB/HR 21 RAPID MIX G=300 CU FT 22 RAPID MIX* G=600 CU FT 23 RAPID MIXr G=900 CU FT 24 FLOCCULATION-HORIZ PADDLE* G=20 CU FT 25 FLOCCULATION-HORIZ PADDLE* G°»50 CU FT 26 FLOCCULATION-HORIZ PADDLE* G=80 CU FT 27 FLOCCULATION-VERT TURBINE* G=20 CU FT 28 FLOCCULATION-VERT TURBINE* G=50 CU FT UNITS OF CHLORINE OF CHLORINE OF CHLORINE OF CHLORINE DIOXIDE OF OZONE OF TOTAL CHAMBER VOLUME OF EQUIVALENT CHLORINE OF ALUM OF ALUM OF POLYMER OF LIME OF LIME OF PERMANGANATE OF SULFURIC ACID OF SODIUM HYDROXIDE OF FERROUS SULFATE OF FERRIC SULFATE OF AMMONIA OF AMMONIA OF POWDERED CARBON OF TOTAL BASIN VOLUME OF TOTAL BASIN VOLUME OF TOTAL BASIN VOLUME OF TOTAL BASIN VOLUME OF TOTAL BASIN VOLUME OF TOTAL BASIN VOLUME OF TOTAL BASIN VOLUME OF TOTAL BASIN VOLUME 22 ------- Table 6 (Continued) TREATMENT PROCESS - LARGE SYSTEMS 29 FLOCCULATION-VERT TURBINEr B=80 CU FT OF 30 CIRCULAR CLARIFIER-LIME SLUDGE SQ FT OF 31 CIRC CLARIFIER-FECL3 X ALUM SLDG SQ FT OF 32 RECTANGULAR CLARIFIER-LIME SLDG SQ FT OF 33 RECT CLARIFIER-FECL3 8 ALUM SLG SQ FT OF 34 UPFLOW SOLIDS CONTACT CLAR>G=70 SQ FT OF 35 UPFLOW SOLIDS CONTACT CLARi.G=110 SQ FT OF 36 UPFLOU SOLIDS CONTACT CLARf6=150 SQ FT OF 37 TUBE SETTLING MODULES SQ FT OF 38 GRAVITY FILTRATION STRUCTURE SQ FT OF 39 FILTRATION MEDIA-RAPID SAND SQ FT OF 40 FILTRATION MEDIA-DUAL MEDIA SQ FT OF 41 FILTRATION MEDIA-MIXED MEDIA SQ FT OF 42 BACKWASH PUMPING FACILITIES GPM OF O&M: SQ FT OF 43 HYDRAULIC SURFACE WASH SYSTEMS SQ FT OF 44 AIR-WATER BACKWASH FACILITIES SQ FT OF 45 WASH WATER SURGE BASINS GAL OF 46 FILTER MOD-RAP SAND TO HIGH RATE SQ FT OF 47 CONTINUOUS AUTO. BACKWASH FILTER SQ FT OF 48 RECARBONATION BASIN CU FT OF 49 RECARBONATION-LIQUID C02 FEED LB/DAY OF SO RECARB-C02 FROM SUBMERGED BURNER LB/DAY OF 51 RECARBONATION-C02 FROM STACK GAS LB/DAY OF 52 MULTIPLE HEARTH RECALCINATION SQ FT OF 53 CONTACT BASIN-DIRECT FILTRATION CU FT OF 54 PRESSURE DIATOMITE FILTERS MGD OF 53 VACUUM DIATOMITE FILTERS MGD OF UNITS TOTAL BASIN VOLUME SINGLE CLARIFIER AREA SINGLE CLARIFIER AREA SINGLE CLARIFIER AREA SINGLE CLARIFIER AREA SINGLE CLARIFIER AREA SINGLE CLARIFIER AREA SINGLE CLARIFIER AREA TOTAL TUBE MODULE AREA TOTAL FILTER AREA TOTAL FILTER AREA TOTAL FILTER AREA TOTAL FILTER AREA BACKWASH PUMPING CAPACITY TOTAL FILTER AREA TOTAL FILTER AREA TOTAL FILTER AREA BASIN VOLUME TOTAL FILTER AREA TOTAL FILTER AREA SINGLE BASIN VOLUME LIQUID CARBON DIOXIDE CARBON DIOXIDE FROM SINGLE BURNER SET CARBON DIOXIDE SINGLE FURNACE EFFECTIVE HEARTH AREA SINGLE BASIN AREA TOTAL FILTER FLOW TOTAL FILTER FLOW 23 ------- Table 6 (Continued) TREATMENT PROCESS - LARGE SYSTEMS 56 PRESSURE FILTRATION PLANTS 57 IN-PLANT PUMPING 58 WASH WATER STORAGE TANKS 59 REVERSE OSMOSIS 60 PRESSURE ION EXCHANGE-SOFTENING 61 GRAVITY ION EXCHANGE-SOFTENING 62 PRESSURE ION EXCHANG-NO3 REMOVAL 63 ACTIV. ALUMINA-FLUORIDE REMOVAL 64 GRAVITY GAC CONTACTORS-CONCRETE 65 GRAVITY GAC CONTACTORS-STEEL OSH: 66 PRESSURE CARBON CONTACTORS OSH! 67 CONVERT FILTER TO GAC CONTACTOR 68 GRANULAR ACT CARBON-CONSTR COST 69 MAKEUP CARBON COST-OSM ONLY 70 CAPPING SAND FILTER U/ANTHRACITE 71 REGIONAL GAC REGEN-TRANS 8 STOR OSH: 72 REGIONAL HULTI HEARTH GAC REGEN 73 MULTIPLE HEARTH GAC REGENERATION 74 INFRARED CARBON REGEN FURNACE 75 FLUIDIZED BED GAC REGENERATION 76 POWDERED CARB REGEN-FLUIDIZED BD 77 POWDERED CARB REGEN-ATOMIZED SUS 78 CHEH SLUDGE PUMPING-UNTHICKENED 79 CHEH SLUDGE PUHPING-THICKENED 80 GRAVITY SLUDGE THICKENER-LIME 81 GRAV SLDG THICKENER-ALUM 8 FECL3 UNITS SQ FT OF TOTAL FILTER AREA MGD OF TOTAL PLANT FLOW GAL OF TOTAL TANK VOLUME MGD OF TOTAL FLOW MGD OF TOTAL FLOW MGD OF TOTAL FLOW MGD OF TOTAL FLOW MGD OF TOTAL FLOW CU FT OF SINGLE CONTACTOR VOLUME SQ FT OF TOTAL CONTACTOR AREA CU FT OF SINGLE VOLUME CU FT OF TOTAL CONTACTOR VOLUME CU FT OF SINGLE CONTACTOR VOLUME SQ FT OF TOTAL CONTACTOR AREA SQ FT OF TOTAL FILTER AREA LB OF TOTAL CARBON WEIGHT LB/YR OF TOTAL CARBON WEIGHT SQ FT OF TOTAL FILTER AREA CU FT OF ON-SITE CARBON STORAGE CAPACITY LB/YR OF CARBON REGENERATED SQ FT OF SINGLE FURNACE EFFECTIVE HEARTH AREA SQ FT OF SINGLE FURNACE EFFECTIVE HEARTH AREA LB/DAY OF TOTAL CARBON WEIGHT LB/DAY OF CARBON FDR SINGLE FURNACE LB/DAY OF TOTAL CARBON WEIGHT LB/DAY OF TOTAL CARBON WEIGHT GPM OF SLUDGE PUMPING GPM OF SLUDGE PUMPING SQ FT OF SINGLE BASIN AREA SQ FT OF SINGLE BASIN AREA 24 ------- Table 6 (Continued) TREATMENT PROCESS - LARGE SYSTEMS 82 VACUUM FILTERS 83 BELT FILTER PRESS 84 FILTER PRESS 85 DECANTER CENTRIFUGES 86 BASKET CENTRIFUGES 87 SAND DRYING BEDS' 88 SLUDGE DEUATERING LAGOONS OSMJ 89 SLUDGE DISPOSAL-SANITARY SEWER 90 LIQUID SLUDGE HAULING 91 DEUATERED SLUDGE HAULING 92 RAW WATER PUMPING FACILITY 93 FINISHED WATER PUMPING FACILITY 94 CLEARWELL STORAGE-BELOW GROUND 95 CLEARWELL STORAGE-GROUND LEVEL 96 DIFFUSED AERATION BASIN 97 AERATION-AERATION TOUERS 98 ADMINrLAB X MAINTENANCE BUILDING TREATMENT PROCESS - SMALL SYSTEMS 99 PACKAGE COMPLETE TREATMENT PLANT 100 PACKAGE GRAVITY FILTER PLANTS 101 PACKAGE PRESSURE FILTRATION PLNT 102 FILTER MEDIA-RAPID SAND 103 FILTER MEDIA-DUAL MEDIA 104 FILTER MEDIA-MIXED MEDIA 105 fILTER MEDIA-MIXEDflNST U/MF SUP 106 PACKAGE PRESS DIATOMITE FILTERS UNITS SO FT OF TOTAL FILTER AREA GPM OF TOTAL SLUDGE PUMPING CU FT OF PRESS SLUDGE CAPACITY GPM OF SLUDGE PUMPING GPD OF SLUDGE PUMPING SO FT OF TOTAL BED AREA CU FT OF TOTAL LAGOON VOLUME CF/YR OF SLUDGE REMOVED GPM OF SLUDGE MG/YR OF SLUDGE CY/YR OF SLUDGE MOD OF TOTAL FLOW MGD OF TOTAL FLOW GAL OF CLEARUELL VOLUME GAL OF CLEARUELL VOLUME CU FT OF BASIN VOLUME CU FT OF TOWER VOLUME MGD OF PLANT FLOW GPM OF TOTAL FLOW GPM OF TOTAL FLOW GPM OF TOTAL FLOW SO FT OF TOTAL FILTER AREA SO FT OF TOTAL FILTER AREA SO FT OF TOTAL FILTER AREA SO FT OF TOTAL FILTER AREA GPD OF TOTAL FILTER FLOW 25 ------- Table 6 (Continued) TREATMENT PROCESS - SMALL SYSTEMS 107 PACKAGE VACUUM DIATOMITE FILTERS 108 PACKAGE ULTRAFILTRATION PLANTS 109 PACKAGE GRAN ACT CARBON COLUMNS 110 POTASSIUM PERMANGANATE FEED SYST 111 POLYMER FEED SYSTEMS 112 POWDERED ACT CARBON FEED SYSTEMS 113 DIRECT FEED GAS CHLORINATION 114 SODIUM HYPOCHLORITE SOLUTN FEED 115 OZONE GENERATING AND FEED 116 OZONE CONTACT CHAMBER 117 CHLORINE DIOXIDE GENERATING/FEED 118 ULTRAVIOLET LIGHT DISINFECTION 119 REVERSE OSMOSIS 120 PRESSURE ION EXCHANGE-SOFTENING 121 PRESSURE ION EXCHANG-N03 REMOVAL 122 ACTIVATED ALUMINA FLUORIDE REMOV 123 BONE CHAR FLUORIDE REMOVAL 124 PACKAGE RAU WATER PUMPING-TDH=50 125 PACKAGE HIGH SERVICE PUMP STATN 126 STEEL BACKUASH/CLEARWELL TANKS 127 LIQUID SLUDGE HAULING 128 DEUATERED SLUDGE HAULING 129 SLUDGE DISPOSAL-SANITARY SEWER 130 SLUDGE DEUATERING LAGOONS OSM: 131 SAND DRYING BEDS UNITS GPM OF TOTAL FILTER FLOW GPD OF TOTAL FLOW GPD OF TOTAL FLOW LB/DAY OF PERMANGANATE LB/DAY OF POLYMER LB/HR OF POWDERED CARBON LB/DAY OF CHLORINE LB/DAY OF EQUIVALENT CHLORINE LB/DAY OF OZONE GAL OF TOTAL CHAMBER VOLUME LB/DAY OF CHLORINE DIOXIDE GPM OF TOTAL FLOW GPD OF FLOW GPD OF FLOW GPD OF FLOW GPD OF FLOW GPD OF FLOW GPM OF FLOW GPM OF FLOW GAL OF TOTAL TANK VOLUME GPD OF SLUDGE CY/YR OF SLUDGE GPD OF SLUDGE CU FT OF TOTAL LAGOON VOLUME CF/YR OF SLUDGE REMOVED SO FT OF TOTAL BED AREA 26 ------- obvious. For example, process 9 (ALUM FEED - DRY STOCK) uses alum. For convenience, however, the processes that use chemicals and the names of the chemicals are shown in Table 5. Examples: Alum = $70.00/ton / Card 3: 3,70.00,ALUM Since the 24 characters immediately following the second comma are copied on the printout, other useful information may be included. For example, we could have written: Card 3: 3,70.00,ALUM (DOSE = 70 MG/L) Any characters following the 24th character will be ignored. Completed Examples— The following four examples show all cards necessary for data input of the processes shown. All data begin in column one. Card 1: 1,9,ALUM FEED - DRY STOCK Card 2: 2,10.0,7.0,245.0,170.0 Card 3: 3,70.0,ALUM (DOSE = 70 MG/L) Card 1: 1,21,RAPID MIX, G=300 Card 2: 2,5.0,4.0,464.0,464.0 Card 1: 1,131,SAND DRYING BEDS Card 2: 2,0.5,0.25,500.0,500.0 Card 1: 1,4,CHLORINE DIOXIDE GENERATING,FEED Card 2: 2,2.0,1.75,16.7,14.5 Card 3: 3,300.0,CHLORINE Card 4: 4,225.0,SODIUM CHLORITE The first three examples were explained above. The last example can be interpreted as follows: Total number of cards necessary is 2 + number of chemicals =2+2=4. Card 1: Process No. 4, CHLORINE DIOXIDE GENERATING - FEED Card 2: Design flow = 2.0 mgd, actual flow = 1.75 mgd, process design parameter = 16.7 Ib/day, process operating parameter =14.5 Ib/day Card 3: $300.00/ton for chlorine used in this process Card 4: $225.00/ton for sodium chlorite used in this process Type 2 Process Data Input The total number of data cards required for a type 2 process is 2 + number of chemicals. The first two cards of data are identical in format 27 ------- and content to a type 1 process. The remaining cards contain chemical cost and chemical feed information. For example, process 59 (REVERSE OSMOSIS) may use up to 3 chemicals: sulfuric acid, sodium hexameta phosphate, and chlorine. This process requires 2+3=5 cards of data with the following information: The card number (integer) followed by a comma, the cost of the chemical in $/ton (floating point) followed by a comma, the actual (not design) feed rate in Ib/day for the chemical (floating point) followed by a comma, and the name of the chemical (not to exceed 24 characters). The chemicals can be input in any order. If one or more of the chemicals is not used, an input of zeros for the chemical cost and the chemical feed rate will cause no information to be printed on the output for that chemical. To illustrate, the 5 data cards for process 59 (REVERSE OSMOSIS) may be constructed as follows: Card 1: 1,59,REVERSE OSMOSIS Card 2: 2,2.0,1.5,2.0,1.5 Card 3: 3,65.0,250.2,SULFURIC ACID,20 MG/L Card 4: 4,650.0,62.6,SODIUM HEXA P03,5 MG/L Card 5: 5,300.0,25.0,CHLORINE,2 MG/L Card 1: 1,59,REVERSE OSMOSIS Card 2: 2,2.0,1.5,2.0,1.5 Card 3: 3,650.0,62.5,SODIUM HEXA P03,5 MG/L Card 4: 4,65.0,125.1,SULFURIC ACID,10 MG/L Card 5: 5,0.0,0.0 Card 1: 1,59,REVERSE OSMOSIS Card 2: 2,2.0,1.5,2.0,1.5 Card 3: 3,0.0,0.0 Card 4: 4,0.0,0.0 Card 5: 5,0.0,0.0 Example 1, above, indicates the following: Card 3: $65.00/ton cost and 250.2 Ib/day feed rate for sulfuric acid at a dose of 20 mg/1 Card 4: $650.00/ton and 62.6 Ib/day feed rate for sodium hexameta phosphate at a dose of 5 mg/1 Card 5: $300.00/ton and 25.0 Ib/day feed rate for chlorine at 2 mg/1 Example 2, above, indicates the following: Card 3: $650.00/ton for sodium hexameta phosphate at a 5 mg/1 dose Card 4: $65.00/ton for sulfuric acid at a 10 mg/1 dose Card 5: No other chemicals used Example 3, above, indicates that no chemicals were used in this process since cards 3 to 5 contained zeros for the chemicals costs and feed rates. 28 ------- Type 3 Process Data Input The total number of cards required for a type 3 process is 3 + number of chemicals. The first two lines are identical in form and content to the first two lines of process type 1. Card 3 is very specific and must contain the number of units of the process in question for which costs are desired. For example, process 31 (CIRC CLARIFIER - FECL3 & ALUM SLDG), when input to the computer, calculates costs for a single clarifier. The program then multiplies the calculated costs for a single clarifier by the number of units indicated on card 3. To illustrate this, consider the following process data input. number of data cards =3+0=3. Total Card 1: 1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG Card 2: 2,1.0,0.9,1667.0,1667.0 Card 3: 3,1,UNIT Card 3 above contains the integer 3 beginning in column 1 followed by a comma, and the number of units (integer) for which costs are desired followed by a comma and the word UNIT or UNITS. The word QNIT(S) is optional, but the comma following the number of units is not. Costs could be obtained for three 1667.0 sq ft clarifiers by either of the following methods (more about this later): Card 1: 1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG Card 2: 2,3.0,2.7,1667.0,1667.0 Card 3: 3,3,UNIT or, Card 1: 1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG Card 2: 2,1.0,0.9,1667.0,1667.0 Card 3: 3,1,UNIT Card 1: 1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG Card 2: 2,1.0,0.9,1667.0,1667.0 Card 3: 3,1,UNIT Card 1: 1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG Card 2: 2,1.0,0.9,1667.0,1667.0 Card 3: 3,1,UNIT The above example shows that the design and operating flows in card 2 of each process represent the total flow for that process only. The first example, gives a total of 2.7 mgd (0.9 mgd/clarifier x 3 clarifiers), and the second example yields a flow of 0.9 mgd for each clarifier. If the number of chemicals for any type 3 process is greater than 1, the additional cards will contain chemical cost information identical in format and content to the third card of process type 1. 29 ------- Type 4 Process Data Input The number of data cards required for type 4 processes (GAG Contactors) is 3 + number of chemicals or 3 + 0 = 3 cards of data. The first two cards of data are identical in format and content to type 1. The third data card is identical in form and content to the third data card of type 3 processes. Note, however, that the design process variable has the units of cu ft per single contactor volume, and the operating process variable has the units of total volume in cu ft or total area in sq ft (see Table 6). For example, consider the following data cards for process 65 (GRAVITY GAG CONTACTORS - STEEL): The design flow is 50.0 mgd, the actual flow is 30.0 mgd, the single contactor volume is 6,300 cu ft, the number of contactors is 22, and the total volume is 138,600 cu ft. Card 1: 1,65,GRAVITY GAG CONTACTORS - STEEL Card 2: 2,50.0,30.0,6300.0,138600.0 Card 3: 3,22,UNITS There are only 3 type 4 processes. All are granular activated carbon treatment. The operation and maintenance cost curves for each include the costs for backwash pumping for the contactors. The cost for backwash pumping is different for each type of contactor because of the variation in the pumping head. Therefore, when computing costs for a train of processes that includes any of the activated carbon contactors (processes 64, 65 or 66) and backwash pumping for these contactors (process 42), a zero must be input for the operating parameter of the backwash pumping curve. This will avoid duplication of the operation and maintenance costs for backwash pumping. Type 5 Process Data Input The number of data cards for type 5 is 3 + number of chemicals or 3+0=3. Type 5 processes consist of the various types of pumping facilities. Cards 1 and 2 are identical in format and content to cards 1 and 2 of type 1. Card 3 contains the integer 3 followed by a comma, the total dynamic pumping head in feet (floating point) followed by a comma, and the abbreviation TDH. For example, process 57 (IN PLANT PUMPING) for a 5.0 mgd plant with an actual flow of 3.0 mgd and a total dynamic head of 40 ft becomes: Card 1: 1,57,IN-PLANT PUMPING Card 2i 2,5.0,3.0,7.5,3.0 Card 3: 3,40.0,TDH In this case, a 7.5 mgd pumping capacity has been installed as shown in Card 2. The abbreviation TDH is optional, but the comma preceding it is not. Type 6 and 7 Process Data Input The number of data cards required for types 6 and 7 is 3 + number of chemicals =3+0=3. The first two data cards of types 6 and 7 are 30 ------- identical in format and content to type 1. The third card of data contains the number of one-way miles driven to the regeneration site or the sludge disposal site. Similar to previous processes; Card 3 contains the integer 3 followed by a comma, the number of one-way miles (floating point) followed by a comma, and the word MILES. The word MILES is optional, but the comma preceding it is not. Examples: Card 1: Card 2: Card 3: Card 1: Card 2: Card 3: 1,71,REGIONAL GAG REGEN-TRANS & STOR 2,1.0,0.9,1000.0,30000.0 3,10.0,MILES 1,90,LIQUID SLUDGE HAULING 2,1.0,1.0,1.3,1.3 3,15.0,MILES Type 8 Process Data Input The number of data cards for type 8 is 3 + number of chemicals = 3+1=4. The first two data cards are identical in format and content to the first two data cards of type 1. The third data card contains the integer 3 followed by a comma, the amount of makeup lime added to the recalcined lime is percent of lime feed rate (floating point) followed by a comma, and the words MAKEUP LIME %. The words MAKEUP LIME % are optional, but the preceding comma is not. The fourth card of data contains chemical cost information and is similar to the third card of type 1. Examples for 5% and 10% makeup lime: Card 1: 1,12,LIME FEED - WITH RECALCINATION Card 2: 2,30.0,25.0,3500.0,2606.0 Card 3: 3,5.0,MAKEUP LIME % Card 4: 4,40.0,LIME Card 1: 1,12,LIME FEED - WITH RECALCINATION Card 2: 2,30.0,25.0,3500.0,2606.0 Card 3: 3,10.0,MAKEUP LIME % Card 4: 4,40.0,LIME In the above examples, the cost of lime is $40.00/ton, the plant design flow is 30.0 mgd, and the design lime rate is 3500.0 Ib/hr. In the fourth data card, the word LIME is not optional. Chemical names following chemical cost information are not optional unless the amount or the cost of that chemical is zero. Type 9 Process Data Input The total number of data cards required for type 9 is 3 + number of chemicals =3+4=7. This process type includes the package treatment plants, which may use from zero to 4 chemicals, depending on the operators' requirements. The first two data cards are identical in format and content 31 ------- to the first two data cards of type 1. The third data card contains the integer 3 followed by a comma, the hydraulic loading on the package plant in gpm/sf (floating point) followed by a comma, and the abbreviation gpm/sf. The abbreviation, gpm/sf is optional, but the preceding comma is not. The fourth, fifth, sixth and seventh data cards contain chemical cost and chemical feed information with format and content identical to chemical information cards for type 2 processes. That is, they contain the card number (integer) followed by a comma, the cost of the chemical used is $/ton (floating point) followed by a comma, the chemical feed rate is Ib/day (floating point) followed by a comma, and the name of the chemical (up to 24 charaters long). If a chemical name is input exceeding 24 characters, the 25th and succeeding characters will be ignored. Example: Card 1: Card 2: Card 3: Card 4: Card 5: Card 6: Card 7: 1,99,PACKAGE COMPLETE TREATMENT PLANT 2,0.288,0.252,200.0,175.0 3,2.0,GPM/SF 4,70.0,147.0,ALUM,70 MG/L 5,4000.0,2.0,POLYMER,! MG/L($2/LB) 5,0.0,0.0 7,0.0,0.0 Type 10 Process Data Input The total number of cards for type 10 is 2 + number of chemicals = 2+1 = 3. The data card input is identical in format and content to type 1 for all cards with one exception. The chemical cost is input in $/lb instead of $/ton. Example: Card 1: Card 2: Card 3: 1,10,POLYMER FEED SYSTEMS 2,1.0,1.0,8.34,8.34 3,2.0, POLYMER,! MG/1 Refer to section on type 1 process data input for a discussion of format and content of data cards. Type 11 Process Data Input The total number of data cards for type 11 is 3 + number of chemicals = 3+0=3. The first two data cards are identical in format and content to the first two data cards of type 1. The third data card for process 11 contains the integer 3 followed by a comma, the sludge concentration in mg/1 (floating point) followed by a comma, and the abbreviation mg/1. The abbreviation mg/1 is optional, but the preceding comma is not. Example: 32 ------- Card 1: 1,89,SLUDGE DISPOSAL - SANITARY SEWER Card 2: 2,1.0,1.0,20.0,20..0 Card 3: 3,10000.0,MG/L Type 12 Process Data Input The total number of cards for type 12 is 4 + number of chemicals = 4+0=4. The first two data cards are identical in format and content to the first-two data cards of type 1. The third data card indicates the number of units and is identical to the third data card of type 3. The fourth data card indicates percent ownership of the regional facility and contains the integer 4 followed by a comma, the percent ownership (floating point) followed by a comma, and the optional words % OWNERSHIP. The comma preceding % OWNERSHIP is not optional. Example: Card 1: Card 2: Card 3: Card 4: 1,72,REGIONAL MULTI HEARTH GAG REGEN 2,5.0,3.5,800.0,560.0 3,2,UNITS 4,10.0% OWNERSHIP 33 ------- SECTION 5 PROGRAM OUTPUT DETAILED OR SUMMARY Program output is controlled by both the COST.DAT file and the PROCES.DAT file. The main option available to the user is determined in line 28 of the COST.DAT file. The two options available are the DETAILED or SUMMARY printout. Sample printouts for each of the options are shown in Examples 1 through 3 in Section 6. Note that if the user chooses the DETAILED printout, he gets all the information contained in the SUMMARY plus a detailed cost breakdown for each process. REPETITIVE OUTPUT Program output is also controlled, in part, by the way in which the COST.DAT and PROCES.DAT files are constructed. In Section 3, COST.DAT File Construction, it was shown that two additional cards of data could be added (cards 29 and 30) to the file to cause the program to be rerun. Card 29 designates which cost factor is to be changed during the rerun, and card 30 contains the values to be used during the rerun. In other words, if cards 29 and 30 were added to the COST.DAT file with the following information, Card 29: Card 30: 8,2 0.02,0.04 the program would be rerun twice using the existing PROCES.DAT file and the new values, 0.02 and 0.04, of cost factor number 8, ELECTRICITY, $/kwh. This has the same effect as running the program three times. This is, three complete program output listings will be generated: One complete output computing costs with the original cost of electricity, one complete output computing costs with electricity at $0.02/kwh, and one complete output computing costs with electricity at $0.04/kwh. In Section 4, PROCES.DAT File Construction, it was shown that data were input or assembled as segments, with a segment representing costs for one treatment plant. A complete program output includes computed costs listed separately for each data segment, with a listing of the COST.DAT file following the output for the final data segment. Therefore, if the PROCES.DAT file were constructed with five data segments and the COST.DAT file contained cards of 29 and 30, as shown above, the printout generated by the program would consist of: 34 ------- 1st data segment cost 2nd data segment cost 3rd data segment cost 4th data segment cost 5th data segment cost information information information information information Listing of COST.DAT values used 1st data segment cost information 5th data segment cost information Listing of COST.DAT values used (as above except electricity = $0,02/kwh) 1st data segment cost information 5th data segment cost information Listing of COST. DAT values used (as above except electricity = $0.04/kwh) Examples of the above program outputs are shown in Section 6, Examples. COST EXTRAPOLATION FOR OUT-OF-RANGE INPUTS Table 4 lists the processes for which costs are available and the design and operating parameter ranges over which these costs are valid. If the user attempts to obtain costs for process parameters outside the valid range, the program will extrapolate the stored costs and notify the user of this condi- tion on the printout. The extrapolation is accomplished by evaluating the following equation for y after first computing the constants GI and G£ from stored cost data: Iny Inx Where x is the input process parameter (out of range) and y is the extrapolated cost at x. When plotted on log-log paper, this results in a linear extrapolation of the cost curve. See Section 6, EXAMPLES, for a sample printout of extrapolated costs. 35 ------- SECTION 6 EXAMPLES The following examples have been constructed to demonstrate the options of input and output available. Each example is arranged with a table of the plant and process assumptions followed by copies of the actual COST.DAT and PROCES.DAT files and the program output. EXAMPLE 1 Example 1 contains one segment of data with five treatment processes in the PROCES.DAT file. The COST.DAT file contains the DETAILED printout option and the use of the ENR Construction Cost Index. The COST.DAT and PROCES.DAT files are shown along with the printout generated by these inputs. EXAMPLE 2 Example 2 contains two segments of data with 17 and 4 treatment processes, respectively, in the PROCES.DAT file. The COST.DAT file contains the SUMMARY printout option and does not use the ENR Construction Cost Index. The COST.DAT and PROCES.DAT files are shown along with the printouts generated by these inputs. EXAMPLE 3 Example 3 contains two segments of data with 6 and 1 treatment processes, respectively, in the PROCES.DAT file. The COST.DAT file contains the SUMMARY printout option and does not use the ENR Construction Cost Index. The COST.DAT file also contains lines 29 and 30, which causes additional printouts varying the cost of labor to include $7.50/hr and $12.50/hr. The COST.DAT and PROCES.DAT files are shown along with the printouts generated by these inputs. 36 ------- COST.DAT File Example 1 COSTS PRESENTED ARE CURRENT AS OF OCTOBER 1978 CAPITAL COST FACTORS (% OF CONSTRUCTION COST): 1 ENGINEERINGS) 2 SITEWQRK* INTERFACE PIPING(%) 3 SUBSURFACE CONSIDERATIONS(%) 4 STANDBY POWER(%) 5 INTEREST RATE(%) 6 NUMBER OF YEARS 7 LAND COST* S/ACRE UNIT COST FACTORS: 8 ELECTRICITY. /KWH 9 LABOR /HR 10 DIESEL FUEL $/GAL 11 NATURAL GAS* /CU FT 12 BLDNG ENERGY USEKWH/S« FT/YR COST INDEXES: 13 EXCAVATION(ENR SKILLED LABOR) 14 MANUFACTURED EQUIP (BLS 114) 15 CONCRETE (BLS 132> 16 STEEL (BLS #101.3) 17 LABOR (ENR SKILLED LABOR) 18 PIPE & VALVES (BLS #114901) 19 ELECTRICAL X INSTR (BLS 117) 20 HOUSING (ENR BUILDING COST) 21 PRODUCER PRICE INDEX 22 ENR CONSTRUCTION* '67 BASE YR OUTPUT(6 FOR LP5 FOR TELETYPE) PRINTOUT(BETAILED OR SUMMARY) -10 -5* =00 =00 =7* =200 =2000 = 10. = 45 =,0013 =102.6 =2470 =221 » 3 =2211 =262 1 =2470 =2364 =1675 =25476 =1997 =265,38 =5 -DETAILED 37 ------- PROCES.DAT File Example 1 ACRES-0»25 1»124,PACKAGE RAW WATER PUMPING~TDH=50 2rO1010072105,0,500 It99vPACKAGE COMPLETE TREATMENT PLANT 201010.072,700500 3,5.0GPM/SF 4700120ALUM» 20 MG/L 5 4000. * 0 * 15 POLYMER(42/LB)»0»25 MG/L 6y300»0»l8fCHLORINE)- 3 MG/L 7rOOrO.O^ 1» 126.STEEL BACKWASH/CLEARWELL TANKS f> 2>0101»0»072»15000Of 15000.0 1» 125s-PACKAGE HIGH SERVICE PUMP STATN 2f0101,0.072»1050,500 1r131,SAND DRYING BEDS 20»1010.072* 50005000 38 ------- **** COST ESTIMATE FOR PACKAGE RAW UATER PUMPING-TDH=50 PROCESS FLOW PROCESS PARAMETER CAPITAL COST CONSTRUCTION OTHER RELATED COSTS DESIGN 0.101 MGD 105.00 GPM OPERATING 0.072 MGD 50.00 GPM DOLLARS 15653. 5691. OXM COST PROCESS CAPITAL COST 21344. CTS/1000 GAL TREATED ELECTRICAL ENERGY (2 '* 0.030/KUH MAINTENANCE MATERIAL LABOR @ $10.000/HR DIESEL FUEL 0 $ 0.450/GAL NATURAL GAS 0 * .0013/CU FT CHEMICALS 0.662 0.237 2.043 0.000 0.000 O.OOO COST SUMMARY OXM DEBT (3 20.0 YRS AND PROCESS OS« COST 7.0 7. PROCESS TOTAL COST 2.943 2.943 7.666 10.609 DOLLARS/YR 174. 62. 537. 0. 0. 0. 773. 773. 2015. 2788. ***** COST ESTIMATE FOR PACKAGE COMPLETE TREATMENT PLANT PROCESS FLOW PROCESS PARAMETER CAPITAL COST CONSTRUCTION OTHER RELATED COSTS DESIGN 0.101 MGD 70.OO GPM DOLLARS 87293. 31736. OPERATING 0.072 MGD 50.00 GPM OXM COST PROCESS CAPITAL COST 119029. CTS/1000 GAL TREATED ELECTRICAL ENERGY B * 0.030/KUH MAINTENANCE MATERIAL LABOR ------- ***** COST ESTIMATE FOR STEEL BACKUASH/CLEARUELL TANKS PROCESS FLOW PROCESS PARAMETER CAPITAL COST CONSTRUCTION OTHER RELATED COSTS DESIGN 0.101 MBD 15000.00 GAL OPERATING 0.072 HGD 15000.00 GAL DOLLARS 14896. 5415. OSH COST PROCESS CAPITAL COST 20311. CTS/1000 GAL TREATED ELECTRICAL ENERGY 8 * 0.030/KUH MAINTENANCE MATERIAL LABOR 0 $10.000/HR DIESEL FUEL S $ 0.450/GAL NATURAL GAS B * ,0013/CU FT CHEMICALS COST SUMMARY OSM DEBT S 20.0 YRS AND PROCESS OSM COST 7.0 % PROCESS TOTAL COST 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 7.295 7.295 DOLLARS/YR 0. 0. 0. 0. 0. 0. 0. 1917. 1917. ***** COST ESTIMATE FOR PACKAGE HIGH SERVICE PUMP STATN PROCESS FLOW PROCESS PARAMETER CAPITAL COST CONSTRUCTION OTHER RELATED COSTS DESIGN 0.101 MGD 105.00 GPM DOLLARS 11866. 4314. OPERATING 0.072 MGD 50.00 GPM OSM COST PROCESS CAPITAL COST 16181. CTS/1000 GAL TREATED ELECTRICAL ENERGY 0 $ 0.030/KUH MAINTENANCE MATERIAL LABOR B 10.000/HR DIESEL FUEL t> 0.450/GAL NATURAL GAS e * ,0013/CU FT CHEMICALS PROCESS OSM COST COST SUMMARY OSM DEBT I 20.0 YRS AND 7.0 X PROCESS TOTAL COST 0.819 0.118 3.973 0.000 0.000 0.000 4.910 4.910 5.812 10.722 DOLLARS/YR 215. 31. 1044. 0. 0. 0. 1290. 1290. 1527. 2818. 40 ------- ****** COST ESTIMATE FOR SAND DRYING BEDS PROCESS FLOW PROCESS PARAMETER CAPITAL COST CONSTRUCTION OTHER RELATED COSTS DESIGN 0.101 MGD 500.00 SQ FT OPERATING 0.072 MGD 500.00 SQ FT DOLLARS 3763. 1368. OSM COST PROCESS CAPITAL COST 5130. CTS/1000 GAL TREATED ELECTRICAL ENERGY 8 $ 0.030/KWH MAINTENANCE MATERIAL LABOR e S10.000/HR DIESEL FUEL @ * 0,450/GAL NATURAL GAS 0 * .0013/CU FT CHEMICALS COST SUMMARY O&M DEBT B 20.0 YRS AND PROCESS OXM COST 7.0 Z PROCESS TOTAL COST 0.000 0.076 9.701 O.O6S 0.000 0.000 9.845 9.845 1.843 11.688 DOLLARS/YR 0. 20. 2549. 18. 0. 0, 2587. 2587. 484. 3072. 41 ------- ***** TOTAL COST ESTIMATE FOR WATER TREATMENT PLANT CAPITAL COST CONSTRUCTION SITEUORKfINTERFACE PIPINGrROADS 8 5.0 7. TOTAL CONSTRUCTION COST GEN CONTRACTOR OVERHEAD & PROFIT S 12.0 7. SUBTOTAL ENGINEERING 8 10.0 7. SUBTOTAL LAND* 0.25 ACRES 0 $ 2000/ACRE LEGAL»FISCAL» S ADMINISTRATIVE INTEREST DURING CONSTRUCTION TOTAL CAPITAL COST DOLLARS 133471. 6674. 140145. 16817. 156962. 15696. 172659. 500. 6057. 2780, 181995. OSM COST ELECTRICAL ENERGY ------- :NT PROCESSES x H- - or J. 3 tn i- tn a CJ CO O H O O IH 1- va -DOLLARS COSTS- CAPITAL 08M CO t- CC CO 1- o tn u z a u CO z HI t- cc i 1- UI J£ O •I ce CN H CO iH 1- o ooooo n "TNS3O1XO in O PS ixiHOoino3 o* ^ * S3cos3inorx o- co M S3S3ins3CMiH Md:x:cn H. o onceuoz HI ui - u - •• z in _i o B) o. M r>i « co z to - u z -i -i o in co ui wo: i- coo ooooo in -i u.3 o -•• -T 1-1 ui o •» (a i— .j u - _j ui _!_] O U. CO Z z z _i x: a ui a. a. « o. a 3 co to to co co co co o o o o o -^ mo o in o o o rx o oo 3 in o 1-1 in ui cc 1-1 HI - a> •»• in o i£ix in uiui u u. u. u. u ce en I-I— X UJ D 3-it-aaocn a a. • "C uiuiMoooauici: •• <> CDCDOrxoO 13 Q £ O •«4M u. u: _j o: >^ ce-j co co 1- X UI 1 U. M X3 CO UI u » u. z HI _J UI fl; •. _\| ^ i- ce ui o; to u a tn 3 z ui a) uj H- a _I «HI - UI en -CO z 3=> Q a: HI UI CO Z UI CD H- 04 - U, ------- COST.DAT File Example 2 COSTS PRESENTED ARE CURRENT AS OF OCTOBER 1978 CAPITAL COST FACTORS (% OF CONSTRUCTION COST): 1 ENGINEERINGS) =10* 2 SITEWQRK* INTERFACE PIPINGS) =5* 3 SUBSURFACE CONSIDERATIONS(%) 4 STANDBY POWERS) 5 INTEREST RATE(%) 6 NUMBER OF YEARS 7 LAND COST* /ACRE UNIT COST FACTORS: 8 ELECTRICITYr /KWH 9 LABOR, $/HR 10 DIESEL FUEL* /GAL 11 NATURAL GAS $/CU FT 12 BLDNG ENERGY USE,KWH/SQ FT/YR COST INDEXES: 13 EXCAVATION(ENR SKILLED LABOR) =2470 14 MANUFACTURED EQUIP (BLS 114) =2213 15 CONCRETE (BLS #132) =2211 16 STEEL (BLS 1013) =2621 17 LABOR (ENR SKILLED LABOR) =2470 18 PIPE S VALVES (BLS 114901) =2364 19 ELECTRICAL S INSTR (BLS 117) =1675 20 HOUSING (ENR BUILDING COST) =25476 21 PRODUCER PRICE INDEX =199,7 22 ENR CONSTRUCTION* '67 BASE YR =00 OUTPUT(6 FOR LP»5 FOR TELETYPE) =5 PRINTOUT(DETAILED OR SUMMARY) =SUMMARY =00 =00 tfny =200 =2000* = ,03 = 10* = »45 =0013 =1026 44 ------- PROCESS.DAT File Example 2 ACRES=13.0 IrSrALUM FEED-LIQUID STOCK 2r40,Or 28.Or 556.Or 350.0 3r70rALUMr40 MG/L 1,15rSODIUM HYDROXIDE FEED SYSTEMS 2r40.Or28.Or5000.Or3300.0 3r200.0rSODIU« HYDROXIDErlS MG/L IrlOrPOLYMER FEED SYSTEMS 2r40.Or 28.Or 67.Or 45.0 3r2.0rPOLYMERr0.25 MG/L lr22rRAPID MIXr G=600 2 r 40 . 0 r 28 .0 r 2785 . 0 r 2785 . O 1r25rFLOCCULATION-HORIZ PADDLErG=50 2. 40. Or 28.Or 13000.0» 13000.0 lr33rRECT CLARIFIER-FECL3 & ALUM SLG 2r40. Or28.Or 4444.Or 4444.0 3r9rUNITS IrSSrGRAVITY FILTRATION STRUCTURE 2r40.Or 28.Or 5560.Or 5560.0 lr41rFILTRATION MEDIA-MIXED MEDIA 2r40.Or 28.Or 5560.Or5560.0 Ir43rHYDRAULIC SURFACE HASH 2r40.0r28.0r5560.0r5560.0 lr42rBACKUASH PUMPING FACILITIES 2r40.Or28.Or 10010.Or 5560.0 lr45rWASH WATER SURGE BASINS 2r40.Or28.Or200000.Or 200000.0 lrlrCL2 FEED-CYLINDER STORAGE 2r40.Or 28.Or670.Or 450.0 3r300.0rCHLORINEr2MG/L lr94rCLEARUELL STORAGE-BELOUI GROUND 2 r 40.0 r 28.0 r 2500000.0 r 2500000.0 lr93rFINISHED WATER PUMPING FACILITY 2r40.Or 28.Or 55.Or 28.0 3r250.OrTDH IrSlrGRAM SLDG THICKENERrALUM 8 FECL3 2r40.Or 28.Or 850.Or 850.0 3rlrUNIT lr86rBASKET CENTRIFUGES 2 r 40.0 r 28.0 r115000.0 r 70000.0 lr91rDEUATERED SLUDGE HAULING 2 r 40.0 r 28.0 r 200OO.0 r12000.0 3r20.0rMILES 000000000000000000000000000000000000000 ACRES=1.5 lr59rREMERSE OSMOSIS 2r5.0r3.5r5.0r3.5 3r65.0rl042.5rSULFURIC ACIDr25 MG/L 4r650.0r208.5rSODIUM HEXA P03r5 MG/L 5r300.Or29.2rCHLORINErl MG/L lr94rCLEARUELL STORAGE-BELOU GROUND 2r5.Or 3.5r300000.Or 300000.0 lrlrCL2 FEED-CYLINDER STORAGE 2r5.0r3.5r63.0r44.0 3r300.0rCHLORINErl.5 MG/L lr93rFINISHED WATER PUMPING FACILITY 2r5.0r3.5r8.0r3.5 3r200.0rTDH 45 ------- o •o o cs CM ^- o* CD H «r to o sj w T-I o in co wo in co-o in in in win -r* o^o TH 1-1 to o i-t CM CM -l - - * zo (B a. wo Z CD - I- <»> ZP3 CO LJr4 U a CJ - CJ Ik CO OO OOO OOOOO Hin in M «r co IXO CM OCM M oooooooooo z a: w H- H OOOOO OOOOO _ UI CO UI - CO ££0 o rx S3lnOCSS3- - eo CE H I- CO UI O H 3 o en ui z - i-t cj MI y: CD =1 Z O _lT-C M . cnxicjcnPuQjM i SCM >H3<:.XCO £6CL CEII « ZZ U.BJ CCIZI-Ul COX aiui cEouiauizcnui n CO V -i in - • —I Q QCEOU1-- <£ -! d; ^UI COU.XA3CJ cju, o ma CO UI u a 46 _ ------- II II II II II II II II II cnorxooooo _i M TH _1 CD UI • \ f- U. t3 en X U. 3 3 i- x ui - Z M Ul O i£ •• - 11 >. u a. u. ------- en LI en en Ul g 1 i g s » >- Of f 1- cn s -1 -J«r « l- o o I- § o •1 1- x a en ui I-Q u i en z u •» Q * en K- Qh- co o 00 -JM (D en en Ul §; so tn ^ o co in ts IH •v in co rs • • • • n < o CM rs c in os o •o in is -o is m n co • • • • ro TH o o rs o in o »«4 o o* in IS O -O CO » O O rt o in 1-4 ^* IH oo is ^- •0 «r PI M ro o v -o O* 1-4 CM 1-4 CO PI 1-4 N in CO O W CO o so o o o ro o o o o o o o o in in in in • • • » ro ro ro ro _i O -1 X O O O OX CO O O O ogz oo o • z • • • in in m in_iin in •. x - Ul2 3 ^IIj o xiu o UIM M Z K ZU 3 sec aa:u. U. MCD 3 «O -J o _i o a: _i eo 3 OX _1 OXZ en enu ui i-cj M « en a. OCDC3UICCO3U1 U.U.U.CDUIU.Q.UI en « o u. Mzzzttzzo: cnooaoMouio zxxxeo>-x-» » M * LU _ 1 _l M a: u u u. o CM •o 00 IS ^ W r^ PI •O PI IS o rs PI «r o rs w in o is M «r co VH in o co CM rs m ^ PI o PI o rs -o co ~H ro rs o PI in CM s» ro ro 1-4 1-4 ro ro PI ro -1 K. M CO CO ZOi 1 Ul OZ Ul Ml- i- 3 M a: zcn o o o a: o Q z i- Q. 1-4 ui - >Z 0 -J° 05 £u M in « CD Z CO • CJZ 1- MZ r< CO M co ui MO: ui a -a O "•_! o r OM co PI -I CO Ul X ui aco a ui_i z _i(o i- co o 1-4 N O n ~ 0> -rtl- - CO a: IH co u O 1-4 _l « a co 5 co "^M i _ Li] CO H w Ul CJ -'Q-i!.:^!!!:!-! ui a co _i z a: ZIE — co - >-ce _i tno i-x ui - * ZM ui ace » «. M » O u- U. -co a: a Z3 3 OCt: Ul CDI-«<:r-ZZZ UICOCOCOMZ-1_1 l- l«l x Ul 48 ------- COST.DAT File Example 3 COSTS PRESENTED ARE CURRENT AS OF OCTOBER 1978 CAPITAL COST FACTORS S OF CONSTRUCTION COST): 1 ENGINEERINGS) 2 SITEUORK* INTERFACE PIPINGS) 3 SUBSURFACE CONSIDERATIONSS) 4 STANDBY POWERS) 5 INTEREST RATES) 6 NUMBER OF YEARS 7 LAND COST? /ACRE UNIT COST FACTORS: 8 ELECTRICITYr $/KUH LABOR» /HR DIESEL FUEL* NATURAL GAS? BLDNG ENERGY $/GAL /CU FT USEfKUH/SQ FT/YR 9 10 11 12 COST INDEXES: 13 EXCAVATION ------- PROCES.DAT File Example 3 ACRES=15 157IN-PLANT PUMPING 2503,57535 3750TDH 160PRESSURE ION EXCHANGE-SOFTENING 25,0355035 330,6REGENERATION SALT 115SODIUM HYDROXIDE FEED SYSTEMS 2 5 * 0 * 3 * 5 * 625.0 * 438 * 0 32000SODIUM HYDROXIDE 15 MG/l. 11CL2 FEED-CYLINDER STORAGE 25,035630440 3300«0CHLQRINE1«5 MG/L 195CLEARWELL STORAGE-GROUND LEVEL 2503550000005000000 193FINISHED WATER PUMPING FACILITY 25.0358035 32000TDH 000000000000000000000000000000000000000000 ACRES=0«0 111LIME FEED-NO RECALCINATION 2100,78761 3650LIME25 MG/L 50 ------- Ul en en in u o a: a. a: ui a: a u. cc •I x: -1 -i - 1 a x at _i CD rs 03 O to 03 ii O in ON -0 o ON IS - ^ a « _i O IS n CM ro rs n CM O Is •rt rs ro co rt O o o o in O 03 O n 03 O CM - -r mm CM CSrH Ul ^ CJ en ui X Ul Ci 2 o «r CM o rs <»• in is -o ois -o o- -o cs o -o - 2 o _i cj 04 O. M in •<£ CD 2 CD • O 2 _1 1- 00 2 i-J CO M - M h- Ul ffl Z i- o i- N^ ui oo u. a: _i a: en - X •o 03-o -o o «* 03 -"1-eN M 03 in in« -- u: _i en CD i- x ui •$.&. n x z) CD ui CJ v U. 2 l-i -I Ul u. - _i - 20 a: • _i i- M M en o n ui w ui i co csm to o -o ion -o is in ii ^0 ^ 11 i-l O O in ONO in ii r-i o o co ON is -oro in o CM IS 11 11 N in n in £LO OXOMC3OU1O S • Z V->O 1- _I I- h- I- • =iinaxa:x>xco«xo a. is M o a o u o so •o >- o i o _i CM t- LLI-X-Q-_IQ zua:o ouiouiuiu - z n ui oo: M - u ii. u. iK ^ - en ui o irnui a: z 3 a D o; ui M ui co z ui a CD t- « ------- ini- CSM CO. 3S L Ult- a cn uz o u U) IS -in «X!S CJ-rt UI I U n « u ii n ii « n-H u. a:. • <* a: w j 2 a; : _i ui a, cj a: s n CD Ui a: 2 cj ) i- 1-1 rs i cj cn a : o - - •• Z O_l n a. M o V. -J CO CD i- x ui in Q ce « 2 3 Z3 CS w ui cn 2 CD H m <1 ui co co cn M UI — cn a: i^ cn ui u — a: a: - a: » >. u. <: t- i— o ui co co a: o ui a: -i u a: ui ui m a a H s: 2 z 2 3 « ------- _j - - Z O _i a a. i-i in «£ CD z CD - cj z i- VSZ -H CO I-I co Ui i-i a: - X U. Z! Ui o - a CJ ^ _l U- CD 2 CD 2 £ CJ <[ UJ, i-< 03 2 ~" o oo o o o CO M H Ul OS 2 i— CJ 1- ~ UJ «) •X u. a: _i IK en <: 3 u uj o uj o 2 2 ui a n. x-x o t- • S3 a: ix o r-j • vC CO S3 S3 O T-I co ^ r-i re co in in T-t -q- in r-j .. >. k >- >- ce _i tn CD H- I ui - - => Ul I UI X UJ UJ i- a: f- 2 _i u. ui to x: ui M c 2 > =3 CD a: a en ui 03 i-i - x to ix w o a o u o S3 >- o i O _i ui x * a * _i n a: o o ui o ui 33 re z o uj o 3 x to.- rs r-j u. re a; a co w <£ i- uj Tft a TS- r-j ts ui to r-j _i S3 •c: u"3 M CO tn T-I ui i- •c CO 3: -o 3 re uj i! CO X CO o re c-4 ^r o r-j co CN in re o S3 re TH SD rx in T-I S3 "3- T-I T-I O O in o SD in T-i c-r S3 o to CN ix sj re in o r-j ix TH T-i rx in TH in CO T-i r-J re en UJ o o !£. i. i- CD 2 i- iii cj tn o u 000. OOOOO ooooooino OblOOIXO^O n n ii n n CO CO 2 2 >-i O a. M w h- a. -i a: ui ui cj a ui ^ M ~ ^. en a: U. 03 15 is! 03 UJ CJ ~a:z--'a:a:<: j^uioa;ui'iux -^V-tJUJh-UI- 2 i-i ui o a: - - i-i ». u a. u. - en a: o uioa:ffiuia: ------- en en 1 1 I g i -« g Lu >- C£ 22 t- § u J 12 O 1- o o o XOJ enui J™ O u en tn O£ OW o oJ fi: W So. _)« -JU Q 1 en t~ C£ en h- o tn "§ u g ARAHETER OPERATI CL tn en 1§ ^5 Q ^ Q h" C9U X<£ §§ ifS Ul Q tn en Ul 8 cu •a m ^* •o CO CM n . a: X 0) _J o o Ul O CO T* z cu ea z a w 1- h- - 1 a o o 0 o UJrt to •c Z 0 CD 1- M CO O a o z o h-1 1- i M CO U en _i Ul - >- (E _i tn t3 i- I ui - en ceo uioicnco>- ------- . ui ~ co PI S3 PI o TH co o rx PI ia CN ix co in -o co ii n Pi co Ul tn tn ui u o a: o- m o. IX o ^" M o ix o o* o -o - - Z O _i £Xi a. M 113 Ml- Ul » Z i- u i- --• ui oo - >- a: _i co CD i- x ui «a: l-i \ O CD Ui u « u. z w _iui a; » _i - z>. Ul -3to a:o i to ui co n0 T TH 1H O O in o-o in n PI <3O CO CK ix -on in o Pi IX ~t rt IX in IH in a.ix i-ioaocjo ^o >- o i o _i ui • x • a • _i a:o GUIOUI •« o 3 O PJ t-l PJ 13 O tOHPlM«Tln-0 to _J Ul « u I- O o a: i- a. z Ul a: a: co a u cn o u omooixono 1H Pi O o II II II II II II CD CO zz l-l O a. M M 1- a. - z *-» ui o ar »• •• HI » u a. u. -cn ce o uicococni-iz_i-i 55 ------- KENT PROCESS K- • G£ I j— 8	AS UJ • ess £» M _J »•* * ^ 77513. 3.899 2.864 J FT CHEMICALS r$ 0. 1737, N ONWOOIOJttt O o inooo rjinii-i »- o OO-IHN orsitn cn N cv4r»m M i rv « tfl 1 P. CD i ! SE ! .j K s^s CD cn 2: a: _i - ^z o_i a n a. w o H a: UI i- - CK X X -J o o 0 o UI n CD Z a: z a C3 H- Hl CO O UI ' o o 1-1 z o HI jj z HI CO CJ cn _i in i CJ CJ 0 UI a! cc o z 1 a UI UI u. UI M -J T-I CO IX 0- IH C£ UI a H- CJ O u. o CO ^ ^ w t- uioa z u a. 1— CJ(— ^'UIOUHICOUI <: ^ a: _icn co H- X UI • z HI uio a: » •• HI •. CJO. U, - cn a: o Z 3 3 CS CC. UI MuicozuiAaa uicncocoHiz-i-i 56 ------- SECTION 7 TROUBLE SHOOTING GUIDE The WATER program is designed to check the PROCES.DAT file before computing process costs to assure that all necessary data cards are present. If an error exists in this file, the program will print the type of error and the line number in which the error occurred. The program also checks the length of the COST.DAT file to assure that it contains either 28 or 30 cards. The following self-explanatory error messages are contained in the program: 1. FORTRAN read error in card of the PROCES.DAT file. This card should contain the word "ACRES=" followed by a floating point 2. number of 15 digits or less. Error - card with "ACRES=" is missing or misspelled. of the PROCES.DAT file. Check card FORTRAN read error in card of the PROCES.DAT file. This card should contain the integer 1 followed by a comma, the process number, and name. Error - this should be the first data card of a process and should begin with the integer 1 in column 1. Check card of the PROCES.DAT file. 5. Error in card number. of the PROCES.DAT file. _ Processes are numbered 1 through 28 in Table is an invalid process of the program manual. 6. Error in card 7. of the PROCES.DAT file. Card number was expected for process , which requires cards of data. Error - not enough data in the COST.DAT file; this file should have either 28 or 30 cards. In addition to the error messages, the program also notifies the user when his input data exceed the valid range of the stored cost data. In this case, the computer extrapolates the stored data. See example 3 in Section 6 for a sample listing of this situation. Errors may arise that will not cause an error message or program inter- ruption if the required commas between the input data values are forgotten. In this case, erroneous input values will result. If this happens, check the PROCES.DAT file for required commas. 57 ------- SECTION 8 WATER PROGRAM LISTING The WATER program is written specifically for the DEC PDP-1170 IAS computing system. Because this FORTRAN program may not be compatible with all systems, it may be necessary to modify the opening and closing of data files. Also, FORMAT statements do not contain the Holerith or H-conversion; instead they transmit alphanumeric data by enclosing it directly in quotation marks. 58 ------- WATER PROGRAM INTEGER OfREPEATrREDO REAL M»L»MAINTrLABOR»LFAFEE LOGICAL DLIMITrOLIMIT DIMENSION TDH<10)»TMILEK10)rGPMSFK10)»AMAKUP<10>r : AMGLC10>fVAR<22>rVARVALaO>,IRANGE<150>»NPU50)»APCENTUO) DIMENSION NCHEM<75)»CMNAM<75»3)rCMCST<75>»CMAMT<75>»ITYPE<150> DIMENSION SAVEH10) DOUBLE PRECISION OUTPUT»PROCES»DETAILEDfDXUrOXUrCMNAM»CH£CKl»CHECK DIMENSION CONSTRC150>>ELECTR<150)>MAINT<150)rLABOR<150>» : DIESEL< 150> »GAS< 150) f CHEM< 150>»QD< ISO) »GA< 150>fDPV< 150) i : OPV<150)fPROCAP<150)rCTSTOM<150>jCTSDEB<150)rCTSTL<150>> t NUMUN<150)»DXIK150> jQXUClSO) DIMENSION C<4>»E<4)>M<4)»L<4)fD<4>»G<4>»F<8>»B<4> DIMENSION PROCESU50,4)rCTS<150> COMMON NUMUN»N/A/TOP,BOTTOMrC,BfCI/B/OTOPrOBOT»ErM»L»B»GfCR9 COMMON/C/ENGR»SITE r SUBSUR i STNB Y r RATE. YE ARS t CL AND r ELEC r : HOURLYrFUELrGASCST»ENFTfCIliCI2,CI3»CI4>CI5rCI6»CI7»CI8»CI9r J CI10 EQUIVALENCE 'ACRES=V OPENSITErSUBSUR>STNBY.RATE»YEARS,CLAND RE AD < 1,101, END=240) ELEC r HOURLY r FUEL, G ASCST , ENFT READCI8»CI9jCHO READ<1»103»END=240) OfOUTPUT READ(lflOS»END=450) IVNrlW IF(IVN.LE.O.OR.IVN.GT.22) GOTO 620 READ(lrl06»END=240> < VARVAL< II ) »11=1 rlW) 450 IVV=IW+1 CLOSE DO 610 REDO=1»IVV IF(REDO.GT.l) VAR(IVN)=VARVAL NCASE=0 ILINE=0 198 ILINE=ILINE+1 READ(2il51»END=251fERR=210> CHECKfACRES IF NCHCK»NP <1) IF GOTO 245 IF5 OPEN(UNIT=3»NAME='CRV.DAT'tTYPE='OLD'tACCESS='DIRECT'f i FORM='FORMATTED'»ASSOCIATEVARIABLE=IZN) READ(3'IZ»153) (PROCESdfll > r 11 = 1 r4> iNCHEMd) »ITYPE<1> CLOSEITYPE 200 NCARD=2+NCHEM<1> GOTO 203 201 NCARD=3+NCHEM(1) GOTO 203 202 NCARD=4+NCHEM<1) 203 DO 205 Il=2fNCARD ILINE=ILINE+1 RE AD < 2 ,154 r END=235 , ERR=235 > NCHCK IF(NCHCK.NE.Il) GOTO 235 205 CONTINUE GOTO 199 210 URITE(0»370) ILINE GOTO 1000 215 MRITE<0»371> ILINE GOTO 1000 220 URITE<0»372> ILINE GOTO 1000 225 WRITE(Or373) ILINE GOTO 1000 230 URITE(Of374) ILINE»NP<1> GOTO 1000 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 59 ------- WATER PROGRAM (CONTINUED) ) ,NCARD 235 URITE(Or375> ILINErIlFNP , ,12 GOTO 1000 240 URITE(Or376> GOTO 1000 245 NCASE=NCASE+1 GOTO 198 250 NCASE=NCASE-H 251 CLOSE OPEN DO 600 REPEAT=1,NCAS£ ICHEH2=0 ITDH=0 IMILES=0 IMAKUP=0 IGPH=0 IHGL=0 IPCENT=0 N=0 IPAGE=0 TCOST=0.0 TCTSE=0.0 TCTSH=0.0 TCTSL=0.0 TCTSD=0.0 TCTSG=0.0 TCTSC-0.0 TE-0.0 TH-0.0 TL-0.0 TD=0.0 TG=0.0 TC=0.0 SUM1=0.0 SUH2=O.O SUM3=0.0 SUM4=0.0 SUH5=0.0 READ<2,127) ACRES 500 RE AD (2 r 110FEND=531) NP »IiPVOPV MrL READC3'IZ+3 r!21) D,G READ<3'IZ+4 ,122) B,F CLOSE(UNIT=3) IFCITYPE(N).EQ.4.0R.ITYPE(N).EQ.6) GOTO 501 OBOT=BOTTOMPROP OTOP=TOPPROP GOTO 502 501 OBOT=PROP OTOP=IRATIO(10.0IEXP) 502 DLIMIT=DPV(N).LT. BOTTOM. OR. DPVCN) .GT.TOP OLIMIT=OPV(N).LT.OBOT.OR.OPV(N).GT.OTOP RATIO=IRATIO ( 10 . 0*IEXP ) CI=F<1)CR1 + F(2)CR2 + F(3)CR3 + F(4)CR4 + F(5)CR5 + F<6)CR6 + F(7)CR7 + F(8)CR8 IF(CI.LT.O.Ol) CI=CR9 IF(CRIO.GT.O.O) CI=CR10 CHEM(N)=0.0 NUMUN ------- WATER PROGRAM (CONTINUED) 505 CONSTR+C(2>DPV+C<3)W1+C<4>W2)NUMUNCI BLBEN = +B<2>DPVW1+B<4>U2>EL£CENFT/102.6 FLFCTR < N ) = (E (1 > +E < ?"> OP V < N ) +E ( 3 ) U3+E < 4 > W4 > NUMUN < N) ELEC MAINT(N) ^U3iMC4)U4)NUMUNCR9 LABOR < N) = < L < 1 > iL < 2 ) OPU < N > +L < 3 ) U3+L < 4 ) U4 ) NUMUN < N > HOURLY MFSEL = OPV+D<3)W3-H:i(4)U4)NUMUNFUEL GAS < N ) = < G (1> +G < 2 ) OPy < N > +G(3)U34 G < 4 > U4 > NUMUN < N > GASCST IF(DLIMIT) CALL ORANGE CALL ORANGEXELECTR(N)»MAINT(N),LABORi : (3AS(N)rOPV DO 515 Il=:CHEMlfICHEM2 READ(2rill) CMCST(Il)r(CMNAM(IlrI2)>I2=lr3) CMAMTRATia365./2000. CHEH(N)==CHEM(N)+CMCST(I1)CMAMT(I1) : TYPE 10 IF(ITYPE(N).EG.10) CHEM(N)=CHEM(N)2000.0 515 CONTINUE GOTO 526 ; TYPE 2* 520 ICHEM1=ICHEM2+1 ICHEM2=ICHEM2+NCHEM(N > DO 522 I1 = ICHEM1»ICHEM2 READ<2f113) CMCST+M(2)OPV(N)+M(3)U3+M(4)U4)CR9 LABOR(N)=BLDEN,OPV(N)) 528 IF=1 ELECTR(N)=ELECTR(N)+BLDEN DIESEL=0.0 GOTO 526 C TYPE 5 530 ITDH=ITDH+1 READ(2rl23) TDH(ITDH) BLriEN=BLIiEN102.6/ELEC/ENFTCI ELECTR=0.0 DENOM=D<1)-D<2) SLOPE=(CONSTR < N)-BLDEN)/BENOM BEE= < C<1> BLDEN-D < 2)CONSTR < N)>/DENOH CONSTR (N)=SLOPETDH< ITDH) + BEE BLDEN=0.0 GOTO 526 C TYPE 6* 535 IMILES=IMILES+1 READ<2,123> TMILE1(IMILES) TMILES=TMILE1(IMILES) IF LABOR<14.71+TMILES/17.0) DIESEL (N)=DIESEL < N > TMILES CHEM ------- MATER PROGRAM (CONTINUED) C TYPE 7 540 IHILES=IHILES+1 READ<2,123) TMILE1 (IMILES) THILES=TMILE1 ( IMILES) ELECTR ( N > =ELECTR ( N > /ELECCI SLOPE=(ELECTR(N)-CONSTR=SLOPETMILES + BEE IF(TMILES.LE.20> LABOR (N)=LABOR(N>(0. 667+0. 0667TMILES> IF(TMILES.GT.20> LABOR (N)=LABOR(N>< 1 ,0+0.05TMILES> MAINT(N)=MAINT(N)TMILES/5.0 GAS(N>=0.0 DIESEL(N)=DIESEL(N>TMILES/5.0 ELECTR(N)=0.0 BLDEN=0.0 CHEM(N>=0.0 GOTO 526 C TYPE 8 545 IMAKUP=IMAKUP+1 READ(2,123> AMAKUP(IMAKUP) ICHEM2=ICHEM2+1 READ(2rlll) CMCST(ICHEM2) r (CMNAM(ICHEM2»I1 ) , 11=1 ,3) CMAMT(ICHEM2)=OPV(N>RATIO365./2000.AMAKUP(IMAKUP>/100. CHEM(N)=CMCST(ICHEM2)CMAMT(ICHEM2> GOTO 526 C TYPE 9 550 IGPH=IGPM+1 READ<2rl23> GPMSFKIGPM) GPMSF=GPMSF1 ( IGPM) IF(GPMSF.EQ.O.O) GPMSF=2.0 W1=DPV(N)/GPMSF U2=U12 W3=U13 BOTTOM=BOTTOM/2 . 0 TOP=TOP/5.0 DLIMIT=U1,LT. BOTTOM. OR. Ul.GT. TOP CONSTR(N)=CI BLDEN=+B(2>UH-B(3)U2+B(4)W3)ELECENFT/102.6 IF(DLIMIT) CALL DRANBECCONSTRCN) rBLDENfUi ) U1=OPV(N>/GPMSF U3=U1*3 ELECTR = UH-E(3)W2+E<4)U3)ELEC MAINTU2+M<4>U3)CR9 LABORU2+L<4)U3)HOURLY OLIMIT=U1.LT. BOTTOM. OR. Ul.GT. TOP IF(OLIMIT) CALL ORANGE (ELECTR(N) rMAINT(N) ,LABOR(N) ,DIESEL r : GAS(N),W1) IF(DLIMIT.OR.OLIMIT) IRANGE(N)=1 ELECTR ( N) =ELECTR ( N > GPMSF/2 . 0+BLDEN DIESEL=0.0 GAS(N)=0.0 ICHEM1=ICHEM2+1 ICHEM2=ICHEM2+NCHEM < N ) BO 548 Il=ICHEMlfICHEM2 READ(2»113> CMCST(Il)rCMAMT(Il),(CMNAM(Il»I2)rI2=lr3) CMAMT365./2000. 548 CHEM(N)=CHEM(N)+CMCST(I1>CMAMT(I1) GOTO 526 TYPE 11 554 IMGL=IMGL+1 READ(2rl23) AMGL(IMGL) SAVE1(IMGL)=CONSTR(N)AMGL(IMGL>/D(1) CONSTR(N)=0.0 DIESEL =0.0 GOTO 526 TYPE 12* 557 IPCENT=IPCENT+1 READ(27l23) APCENT(IPCENT) CONSTR(N)=CONSTR(N>APCENT(IPCENT)/100. ELECTR ( N > =ELECTR ( N ) APCENT ( IPCENT ) /1 00 , MAINT(N) =MAINT(N) APCENT(IPCENT)/100. LABOR/100. DIESEL(N>=DIESEL(N)APCENT(IPCENT)/100. GAS=0.0 GOTO 526 526 TCOST=TCOST+CONSTR(N) GOTO 500 235 236 237 238 239 240 241 242 243 244 245 246 247 248 249 250 251 252 253 254 255 256 257 258 259 260 261 262 263 264 265 266 267 268 269 270 271 272 273 274 275 276 277 278 279 280 281 282 283 284 285 286 287 288 289 290 291 292 293 294 295 296 297 298 299 300 301 302 303 304 305 306 307 308 309 310 311 312 313 62 ------- WATER PROGRAM OHP=10. IF GOTO 551 IF(SUBTL3.LE.O.O) GOTO 552 LFAFEE=60.0+. 0447SUBTL.3-6.406E-BSUBTL3*2+3.673E-14SUBTL3*3 BR=SUBTL3/1.E4 CSTINT= <1.75+.252BR-2.105E-3BR2+9.013E-6BR*3)/ : 24.RATESUBTL3/100. GOTO 555 551 LFAFEE=125570. +6.823E-4SUBTL3-115564. EXP (-6.015E-8SUBTL3) BR=SUBTL3/1.E6 CSTINT= < 16.03+1.02BR-1.188E-2BR*2+3. 7E-5BR*3 > / : 24.RATESUBTL3/100. GOTO 555 552 LFAFEE=0.0 CSTINT=0.0 555 TCAP=SUBTL3 + CSTLND + LFAFEE + CSTINT W1=(1.+RATE/100.) DEBT=TCAPRATE/100.W1YEARS/(W1YEARS-1.) IMGL=0 DO 570 1 = 1.N IF(TCOST.LE.O.O) GOTO 556 GOTO 558 556 U2=0.0 GOTO 559 558 U2=CONSTR CTSLAB=LABOR CTSDIE=DIESEL /CTS(I) CTSCHE=CHEM /CTS =PRBEBT/CTS(I> CTSTOM (I) =CTSELE+CTSMAI+CTSLAB+CTSHIE+CTSGAS+CTSCHE IF IM6L=IMGL+1 IF.EG,11> TOM=SAVE1 TL=TL + LABOR(I) p TD=TD + DIESEL WRITE (0.300) IF(IPAGE.EQ.O) IPAGE=2 : OPVr «RITE<0.302) CONSTR(I)FOTHERrPROCAP(I> GOTO 565 314 315 316 317 318 319 320 321 322 323 324 325 326 327 328 329 330 331 332 333 334 335 336 337 338 339 340 341 342 343 344 345 346 347 348 349 350 351 352 353 354 355 356 357 358 359 360 361 362 363 364 365 366 367 368 369 370 371 372 373 374 375 376 377 378 379 380 381 382 383 384 385 386 387 388 389 390 391 392 63 ------- UATER PROGRAM (CONTINUED) 540 IF=C1D/NUMUN QA rGD ,DPV . 565 570 571 575 578 580 581 582 583 700 705 710 715 720 725 aD=QD(I>NUMUN QA(I)=QA(I)NUMUN NUMUN(I>rCONSTR.OTHER»PROCAP.NUMUN URITE<0»305> ELECrCTSELE.ELECTR .CTSMAI»MAINT< I> .HOURLY. : CTSLABrLABOR(I).FUEL.CTSDIE.DIESEL URITE (0 » 306 > GASCST t CTSGAS , GAS < I ) , CTSCHE t CHEM < I > > CTSTOM ( I ) , TOM URITE CTSTOM .TOM» YEARS .RATE»CTSDEB(I > .PRDEBT. : CTSTL URITE<0308> TCOSTrSITE.CSTSIT IFCSUBSUR.GT.O.) WRITE<0»309> SUBSUR.CSTSUB IFtSTNBY.GT.O.) URITE<0.310> STNBY.CSTSTN WRITECOfSll) SUBTLl»OHP»CSTOHPfSUBTL2»ENGRfCSTENG»SUBTL3 ICLAND=CLAND IFCACRES.GT.O.) URITE(Or312) ACRES jICLANDf CSTLND URITE(0»313) LFAFEE»CSTINT»TCAP URITE(Of314) ELEC»TCTSE»TEfTCTSHrTHfHOURLY»TCTSLfTL»FUELrTCTSDrTD URITE(0»315) GASCST f TCTSGrTGrTCTSCfTCf SUH2rSUM4 URITE(0>316) SUM2 » SUM4 » YEARS j RATE rSU«l» DEBT » SUMS f SUMS ICHEM2=0 ITDH=0 IHILES=0 IMAKUP=0 IGPM=0 IMGL=0 IPCENT=0 13=0 WRITE GOTO 578 URITE N URITE<0»319) DO 590 1=1 rN IF(I3-45) 583 r 580 r 581 IF(N-I) 581.583.581 IF GOTO 583 13=0 URITE<0,300) URITE N URITE<0.319> 13=13+8 URITE(Or320) IF (PROCES .QA .DPV 13=13+1 GOTO < 735 .735.700. 705. 710. 715.715, 720. 725. 735. 730. 732) ITYPE( I) URITECOr331) NUMUN(I) 13=13+1 GOTO 735 U3=DPU(I)NUMUN(I)7.48/OD(I)/694.44 WRITE(Of332) W3 U3=DPV(I)NUMUN(I) URITE(Of341) U3FNUMUNCI) 13=13+3 GOTO 735 ITDH=ITDH+1 URITE(Or333> TDH(ITDH) 13=13+1 GOTO 735 IMILES=IMILES+1 WRITE(Or334> TMILE1 (IMILES) 13=13+1 GOTO 735 IHAKUP=IMAKUP+1 ' URITE336) GPHSFKIGPM) 13=13+1 GOTO 735 393 394 395 396 397 398 399 400 401 402 403 404 405 406 407 408 409 410 411 412 413 414 415 416 417 418 419 420 421 422 423 424 425 426 427 428 429 430 431 432 433 434 435 436 437 438 439 440 441 442 443 444 445 446 447 448 449 450 451 452 453 454 455 456 457 458 459 460 461 462 463 464 465 466 467 468 469 470 471 472 64 ------- WATER PROGRAM (CONTINUED) 730 IMGL=IMGL+1 WRITE(Or337> AMGL(IMGL) 13=13+1 GOTO 735 732 IPCENT=IPCENT+1 URITE(0»331> NUMUN(I) WRITE(0>339> APCENT(IPCENT) 13=13+2 GOTO 735 735 IF.LE,0.0> GOTO 585 WRITE(Or321) CMCST(I2)j(CMNAM(I2fI4)rI4=l>3) 13=13+1 GOTO 585 584 URITE(Qf328> CMCST(12)'i(CMNAH(1214)r14=1r3> 13=13+1 585 CONTINUE 590 CONTINUE URITE(0»322> TCOSTrTCAPSUM2i>SUM1,SUM3 13=13+4 SUM6=CSTSIT+CSTSUB+CSTSTN WRITE (0,329) SUM6 r OHP j CSTQHP r CSTENG > ACRES r CSTLNDtL.FAFEE r i CSTINTfTCAP 13=13+11 TE=TE/ELEC TL=TL/HOURLY TD=TD/FUEL TG=TG/GASCST WRITE(0>330) TE,TMfTLfTDrTG»TC 13=13+3 IF(N-l.EQ.O) GOTO 7778 IF(I3--60.GT.O) WRITE(Or300) URITE(0»351) 13=13+2 DO 7777 1=1iN IF(13-63.LT.O) GOTO 7776 WRITE(0»300) WRITE(O»354> 7776 TMP1=ELECTR(I)/ELEC TMP2=LAEOR(I)/HOURLY TMP3=DIESEL(I)/FUEL TMP4=GAS(I)/GASCST WRITE(0,350) I.TMP1»MAINT(I),TMP2,TMP3,TMP4.CHEM(I) 7777 13=13+1 7778 18=0 DO 592 1=1»N 592 I8=I8+IRANGE(I) IFdS.EG.O) GOTO 593 IF(58-I3-I8.LT.O> URITE(0»300) IF(58-I3-I8.LT.O> 13=0 18=0 593 DO 596 1=1rN IF(IRANGE(I>.EQ.O) GOTO 596 IF(IS.GT.O) GOTO 594 IF(I3-63.EQ.O> WRITE(0,30O) IF(I3-63.EQ.O) 13=0 URITE(Oi352) 18=18+1 13=13+4 594 IZ=1+(NP(I)-1>5 OPEN(UNIT=3 »NAME='CRM.DAT',TYPE='OLD'tACCESS='DIRECT'r : FORM='FORMATTED'»ASSOCIATEVARIABLE=IZN) READ(3'IZ,125) BOTTOM r TOP fPROP,IRATIO,IEXP CLOSE(UNIT=3) IF(ITYPE(I).EQ.4.0R.ITYPE(I).EQ.6) GOTO 597 OBOT=BOTTOMPROP OTOP=TOPPROP GOTO 595 597 OBOT=PROP OTOP=IRATIO(10.0IEXP) 595 URITE(Or353) I r (PROCESd , II > tll = l »4> ,BOTTOM?TOPrDXU(I> rDPMd ) t : OBOT,OTOPrOXU(I)»OPM(I) 13=13+1 473 474 475 476 477 478 479 480 4B1 482 483 484 485 486 487 488 489 490 491 492 493 494 495 496 497 498 499 500 501 502 503 504 505 506 507 508 509 510 511 512 513 514 515 516 517 518 519 520 521 522 523 524 525 526 527 528 529 530 531 532 533 534 535 536 537 538 539 540 541 542 543 544 545 546 547 548 549 550 65 ------- HATER PROGRAM (CONTINUED) 596 CONTINUE 551 OPEN(UNIT=lrNAME='COST.DAT'rTYPE='QLD') 552 IF(I3.GT.47> URITE(Or300> 553 READ(lrl04> BrF 554 WRITE(Or323) BrF 555 URITE(Or324) ENGRrELECrCIlrSITErHOURLYrCI2 556 WRITE(0»325) SUBSURrFUELrCI3rSTNBYrGASCST»CI4rRATErENFTrCI5 557 WRITE(Or326) YEARSrCI6rACRESrCI7rCLANDrCI8rCI9 558 IF(CIIO.GT.O.OI) WRITE (Or327) CI10 559 CLOSE(UNIT=1> 560 600 CONTINUE 561 CUOSE(UNIT=2) 562 610 CONTINUE 563 GOTO 1000 564 620 WRITE(Or338) IVN 565 1000 STOP 566 100 FORMAT(//6(34XrF9.2/)r34XrF9.2) 567 101 FORMAT(/4(34XrF9.2/)r34XrF9.2) 568 102 FORMAT(/9(34XrF9.2/)r34XrF9.2) 569 103 FORMAT(34XfIl/34XrA8) 570 1O4 FORMAT(4A4r8A4) 571 105 FORMAT(Irll) 572 106 FORMAT(10F) 573 110 FORMAT(2XrI> 574 111 FORMAT(2XrFr3A8) 575 113 FORMAT(2Xr2FfSAB) 576 114 FORMAT(2XrIrF) 577 115 FORMAT(2Xr4F) 578 120 FORMAT(4A8r2A6r3E9.2rI4rI2iIlrI2) 579 121 FORMAT<4E10.2r4E10.2) 580 122 FORMAT<4E10.2r8F5.3) 581 123 FORMAT(2XrF) 582 125 FORMAT(44Xr3E9.2rI4rI2) 583 127 FORMAT(6XrF) 584 151 FORMAT(-A6rF> 585 152 FORMAT(2I) 586 153 FORMAT(4A8r45XrIlrI2> 587 154 FORMATU) 588 300 FORMAT(1H1) 589 301 FORMAT(//' ** COST ESTIMATE FOR '4A8//T48r'DESIGN'T66r 590 : 'OPERATING'/Tl2r 'PROCESS FLOWT41 rF10.3r ' MGD'T61rF10.3r 591 t ' HGD'/T12r'PROCESS PARAMETER'T41rF10.2r!X»A6rT61FF10.2rIXrA6/) 592 302 FORMAT(T8r'CAPITAL COST'T55r'DOLLARS'// 593 S T12r'CONSTRUCTION'T52rF11.0/T12f'OTHER RELATED COSTS'T52rFll.O/ 594 ! T53r' '/T30r'PROCESS CAPITAL COST'T52rFll .O// 595 t TBr'OSM COST'T49r'CTS/1000 GAL TREATED'TSlr'DOLLARS/YR'/) 596 303 FORMAT(//' *** COST ESTIMATE FOR'r!Xr4A8r' CI3r' UNITS)'// 597 : T47r'DESIGN'T63r'OPERATING'/ 598 : T12r'PROCESS FLOW (PER UNIT)'T41rFll.3r' MGD'rT61rFll,3r' MGD'/ 599 5 T12r'PROCESS PARAMETER (PER UNIT)'T41rFll.2rlXrA6rT61rFll.2r 600 : !XrA6/) 601 304 FORMAT(T8r'CAPITAL COST (TOTAL FOR'I3r' UNITS)'T55»'DOLLARS'// 602 S T12r'CONSTRUCTION'T52rF11.0/T12r'OTHER RELATED COSTS'T52rFll.O/ 603 : T53r' '/T30r'PROCESS CAPITAL COST'T52rFll .O// 604 : TSr'OSM COST (TOTAL FOF'ISr' UNITS)'T49r'CTS/1000 GAL TREATED' 605 t T81r'DOLLARS/YR'/) 606 305 FORMAT(T12r'ELECTRICAL ENERGY B 'F6.3r'/KUH'T53rF10.3rT79r 607 Fll.0/T12r'MAINTENANCE MATERIAL'T53rF10.3rT79rFll .O/ 608 T12r'LABOR B 'F6.3r'/HR'T53rF10.3rT79rFll.O/ 609 T12r'DIESEL FUEL S 'F6.3r'/GAL'T53>F10.3rT79rFll.0) 610 FORMAT(T12r'NATURAL GAS @ 'F6.4r'/CU FT'T53rF10.3rT79rFll.O/ 611 T12r'CHEMICALS'T53rF10.3rT79rFll.O/ 612 T53 r ' ' T80 r' ' /T34 r 613 'PROCESS OSM COST'F13.3rT79rF11.0/> 614 307 FORMAT(T8r'COST SUMMARY'// 615 J T12r'08M'T52rF11.3rT79rF11.0/T12r'DEBT @' 616 : FS.lr' YRS AND'FS.lr' %'T52rFll.3rT79 rFll.O/ 617 * TS3» '—»-.-•—.«.••—.-——'T8O» '———•———.—.———'/ &IQ : T32r'PROCESS TOTAL COST'T52»F11.3rT79 rFll.O) 619 308 FORMAT(//' ***** TOTAL COST ESTIMATE FOR WATER TREATMENT PLANT' 620 S ///T8r'CAPITAL COST'T55r'DOLLARS'// 621 : T12r'CONSTRUCTION'T52rF11.0/ 622 ! T12r'SITEUORKrINTERFACE PIPINGrROADS O'FS.lt' %'T52rF11.0) 623 309 FORMAT(T12r'SUBSURFACE CONSIDERATIONS S'FS.lr' %'T52rF11.0> 624 310 FORMAT(T12r'STANDBY POWER S'FS.lr' X'T52rF11.0) . : 625 306 66 ------- WATER PROGRAM (CONTINUED) 311 FORMAT(T53r' '/T27»'TOTAL CONSTRUCTION COST'T52rFll .O// 626 J T12»'GEN CONTRACTOR OVERHEAD S PROFIT @'F5.1r' %'T55»F8.0/ 627 } T53»' '/T42r'SUBTOTAL'T52»F11.O// 628 : T12i'ENGINEERING B'F5.1»' Z'T52»F11.0/T53r' '/ 629 : T42»'SUBTOTAL'T52rF11.0/> 630 312 FORMAT(T12r'LAND,'F7.2»' ACRES 6 'I6»'/ACRE'T52»F11.0) 631 313 FORMAT(T12r'LEGAL,FISCAL, S ADMINISTRATIVE'T52,F11.O/ 632 : T12r'INTEREST DURING CONSTRUCTION'T52,F11.O/ 633 . T53,' '/T32,'TOTAL CAPITAL COST'T52,F11.0//) 634 314 FORMAT(T8,'OSM COST'T49,'CTS/1000 GAL TREATED' 635 t T81r'DOLLARS/YR'// 636 : T12,'ELECTRICAL ENERGY 644 316 FORMATFll.l»lXA6»F10.1»lXfA6fF10.0»Fll.O» 656 : 3F8.3) 657 321 FORMAT 660 323 FORMAT(///1X»4A4»8A4/) 661 324 FORMAT 'T34» '-' 663 : F8.2»T47>'ELECTRICITY* $/KUH'T80»'='F6.2rT91f'EXCAVATION' 664 :,' (ENR SKILLED LABOR)='F7.l/T5f'SITEUORK.INTERFACE PIPING(X) =' 665 : F8.2,T47r'LABORr /HR'T80»'='F6.2fT91.'MANUFACTURED EQUIP' 666 t,' '='F6.3»T91»'CONCRETE '='F8.2rT47>'NATURAL GASf /CU FT'T80» 670 • ' = 'F6.4»T91»'STEEL 681 329 FORMAT(//T56»'SITEWORK»SUBSURFACErSTNBY POWER'fT88»F10. 0/T66r 682 J 'GEN CON OH S P.'rF5.1r'%',T88fF10.0/T76r'ENGINEERING'.T88.F10.0/ 683 : T69r'LAND»'»F7.2»' ACRES'rT88>F10.0/ 684 : T69»'LEGALrFISCAL»ADMIN'»T88rF10.0/T70r'INT DURING CONSTR'» 685 : T88»F10.0/T87»' '/T74»'TOTAL CAPITAL'» T88»F10.0) 686 330 FORMAT(//' TOTAL OXM:'»T21»'KWH'»8Xf'MATERIALSr'»9X»'LABORrHR'r 687 5 9X»'DIESELfGAL'r9Xr'NAT GAS.CU FT'»9X»'CHEMICALSf'/ 688 : T16»F11.0,5X»F10.08XVF9.0r9XrF10.0,9X,F13.0rlOX»F10.0> 689 331 FORMAT(T7i'NUMBER OF UNITS ='»I3> 690 332 FORMAT(T7»'EMPTY BED CONTACT TIME AT DESIGN FLOW ='»F5.1»' MIN') 691 333 FORMAT(T7r'TBH ='rF6.1»' FEET') 692 334 FORMAT(T7r'ONE WAY MILES ='»F6.1) 693 335 FORMAT(T7»'MAKEUP LIME.='rF6.1,' %') 694 336 FORMAT(T7»'LOADING RATE ='»F5.1f' GPM/SO FT') 695 337 FORMAT(T7f'SLUDGE CONCENTRATION ='»F8.0>' MG/L') 696 338 FORMATC PROGRAM EXIT. CHECK THE 'COST.DAT" FILE'rI6f' IS NOT' 697 J ' A VALID COST FACTOR NUMBER.') 698 339 FORMAT(T7>'COSTS CALCULATED FOR'rF7.2»' 7. OWNERSHIP OF REGIONAL' 699 : ' FACILITY') 700 341 FORMAT 703 351 FORMAT(/' PROCESS OXM') 704 67 ------- UATER PROGRAM (CONTINUED) 352 FORMATC/' COSTS FOR THE FOLLOWING PROCESSES HAVE BEEN' 705 : ' EXTRAPOLATED. VALID RANGES FOR INPUT DATA AREt'// 706 i T17r 'PROCESS' fT43r 'DESIGN RANGE' 7 T69r 'YOUR INPUT' rT86» 707 : 'OPERATING RANGE' >T114r 'YOUR INPUT') 708 353 FORMAT(lX7l2rlX»4A8fF9.1>' TO' >F11 . 1 , !X»A6rFll .1 , F13. 1 » ' TO'r 709 I Fll.lrlXrA6rFll.l) 710 354 FORHAT(//' PROCESS OXM' rT21 r 'KUH' rSXf 'MATERIALS,' ,9X, 'LABOR* HR' , 711 : 9Xf 'DIESELrGAL'»9X» 'NAT GASfCU FT' f9X» 'CHEMICALS,' > 712 37O FORHATC FORTRAN READ ERROR IN CARD',I5f' OF THE PROCES.DAT FILE.' 713 : ' THIS CARD SHOULD CONTAIN THE WORD 'ACRES' FOLLOWED BY'/ 714 : ' A FLOATING POINT NUMBER OF 15 DIGITS OR LESS') 715 371 FORMAT<' ERROR-CARD WITH 'ACRES=' MISSING OR MISSPELLED.'/ 716 : ' CHECK CARD'rI5»' OF THE PROCES.DAT FILE.') 717 372 FORMAT<' FORTRAN READ ERROR IN CARD'»I5»' OF THE PROCES.DAT' 718 : ' FILE'/' THIS CARD SHOULD CONTAIN THE INTEGER "1" ' 719 : 'FOLLOWED BY'/' A COMMAr THE PROCESS NUMBER AND THE PROCESS' 720 : ' NAME') 721 373 FORMAT' ERROR-THIS SHOULD BE THE FIRST DATA CARD'/' OF A' 722 : ' PROCESS AND SHOULD BEGIN WITH THE INTEGER '!' IN COLUMN I'/ 723 ; ' CHECK CARD'fI5»' OF THE PROCES.DAT FILE') 724 374 FORMAT<' ERROR IN CARD'rISj' OF THE PROCESrDAT FILE'/lXfI5» 725 I ' IS AN INVALID PROCESS NUMBER. PROCESSES'/' ARE NUMBERED' 726 J ' 0 THRU 129 IN TABLE 2 OF THE PROGRAM MANUAL') 727 375 FORMATC ERROR IN CARD'.ISr' OF THE PROCES.DAT FILE'/' CARD' 728 : ' NO.'flSr' WAS EXPECTED FOR PROCESS' r I4» !Xf4A8> ' r WHICH' 729 : ' REQUIRES' r!3»' CARDS OF DATA.') 730 376 FORMATC ERROR-NOT ENOUGH DATA IN THE COST. DAT FILE.'/ 731 : ' THIS FILE SHOULD HAVE EITHER 28 OR 30 CARDS') 732 END 733 SUBROUTINE DRANGEC Ylf Y2,X> 734 DIMENSION C<4)»B<4)fNUMUN(150)jVAR(22) 735 COMMON NUMUNrN/A/TOP»BOTTOM»C»B»CI 736 COMMON/C/ENGR r SITE » SUBSUR , STNBY » RATE , YEARS > CLAND , ELEC » 737 : HQURLY7FUEL»GASCSTrENFTrCIlrCI2rCI3rCI4rCI5rCI6»CI7rCI8rCI9* 738 S CI10 739 EQUIVALENCE X1+C<3)X1*2+CC4>X1*3) 752 C2=(C(1)+C(2>X2+C(3)X22+C(4)X2*3) 753 Bl= B<1)+B(2)X1+B<3)X12+B(4)X1*3 754 B2= B(1)+B(2)X2+B(3)X22+B(4)X2*3 755 ALX1=ALOG(X1> 756 ALX2=ALOG -ALOG ( Cl ) > /DENOM 763 Y1=EXPNUMUNCI 764 120 IF GOTO 125 765 Y2=0.0 766 GOTO 130 767 125 AB1= /DENOM 769 Y2=EXP < AB1+AB2ALOG ELECENFT/102 . 6 770 130 RETURN /71 END 772 SUBROUTINE ORANGE < Yl , Y2, Y3r Y4r Y5»X) 773 REAL H,L r/4 DIMENSION E<4)»M(4)rL(4)»D(4)>G(4)rNUMUN(150)»VAR(22> 775 COMMON NUMUNfN/B/OTOPfOBQT>E,MrL»DrGrCR9 776 COMMON/C/ENGR , SI TE , SUBSUR » STNBY , RATE , YEARS r CLAND , ELEC , 777 ', HOURLY»FUELrGASCSTjENFTTCIlfCI2rCI3»CI4iCI5jCI6rCI7rCI8»CI9r 778 ! CI10 779 EQUIVALENCE(ENGRfVAR(l)> 780 Fl(AlfA2) = (ALOG(Al)ALX2-ALOG=(ALOG(A2)-ALOG )/DENOM 782 IF(X.LE.O.O) GOTO 98 7B,5 GOTO 99 7S4 68 ------- WATER PROGRAM (CONTINUED) 98 Yl=--0.0 Y2--0.0 Y3=0.0 Y4=0.0 Y5--0.0 GOTO 160 99 IF(X-OTOP.GT.O.O) GOTO 100 X1=OBOT X2<=2.0OBOT GOTO 110 100 X1=OTOP X2= ( OTOP-f OBOT ) /2 . 0 110 X12=X12 X13=X13 X22=X2#2 X23=X23 El=E-tE<2)Xl+E<3)X12+E<4>X13 E2=E<1)+E(2)X2+E< 3 > X22+E < 4 >X23 ALX2=ALOG(X2) ALX1<=ALQG(X1> 11ENOM=ALX2--AL.X1 IF(E1.GT.O.O.AND.E2.GT.O.O) GOTO 115 Yl=0,0 GOTO 120 115 AE1-FKE1»E2> AE2=F2 Y1=EXP 120 TM1-M<1> H-i<2)Xl+M(3)X12+M<4)X13 TM2-M(1)+M(2)X2+H(3)X22+M< 4)X23 IF GOTO 135 Y3=0.0 GOTO 140 135 AL.1=F1(TL1»TL2) AL2=F2(TL1»TL2) Y3=EXP ( Al_ 1+AL2ALOG ( X ) ) HOURLYKcNUMUN (N ) 140 Dl=D(l)+n(2)Xl+D<3)X12+D(4)X13 Il2=D< 1) +D ( 2 ) X2+D'< 3 ) X22+D ( 4 ) X23 IF GOTO 145 Y4=0.0 GOTO ISO 145 ADl=FKDlrIi2) An2=F2(Ill»ri2) Y4=EXP < ADI +AD2ALOG (X) ) FUELNUMUN < N ) 150 Gl=G(l)+G(2)XH-G(3)X12tG(4)X13 G2=G(1)+G < 2)X2+G < 3)X22+G(4)X23 IF(Gl.GT.O.O.ANn.G2.GT.O.O) GOTO 155 Y5=0,0 GOTO 160 155 AGl--FKGlfG2) AG2=F2(G1»G2) Y5=EXP(AG1+AG2ALOG ------- SECTION 9 CRV.DAT FILE The CRV.DAT file contains all the cost information for the water treatment processes. The WATER program reads this file in a random or direct access mode. Each line of data contains 80 characters, so that if a record length of 80 is established on the system, the location of the first line of data of any process is given by: (NP-1) x 5 + 1 where NP is the number of the process shown in Table 4. For example, data for process 21, RAPID MIX, G=300, begins at line (21-1) x 5 + 1 = 101 and continues through line 105. If the CRV.DAT is not established on the computing system as a random or direct access formatted file, the WATER program will have to be modified accordingly. A copy of the CRV.DAT file is given on the following pages. The file is 655 lines long and contains 52,400 characters. Some systems may include a carraige return and line feed at the end of each line of data. In this case, the file will contain 82 characters per line and a total of 53,710. characters. 70 ------- CFW.DAT FILE CL2 FEED-CYLINDER STORAGE 1.20E+04 9.43E+01 -1.44E-02 1.53E+03 2.39E+00 -4.38E-04 0,OOE+OO O.OOE+00 O.OOE+00 8.19E+03 1.13E+02 -1.22E-02 CL2 FEED-ON SITE STORAGE TANK 1.83E+05 -7.18E-01 4.15E+03 2.14E-01 O.OOE+00 O.OOE+00 -2.63E+02 3.23E+00 CL2 FEED FROM RAIL CAR 1.52E+05 2.44E+00 3.75E-04 4.15E+03 2.14E-01 3.55E-05 O.OOE+00 O.OOE+00 O.OOE+00 -2.63E+02 3.23E+OO -3.1SE-04 1.97E-03 -7.97E-OS 3.55E-05 -1.61E-09 O.OOE+00 3.15E-04 LB/DAVLB/DAY l.OOE+01 l.OOE+04 l.OOE+00 1 101 8.69E-07 5.45E+02 9.98E-01 7.14E-04 -5.05E-08 2.68E-08 4.01E+02 7.93E-01 -5.59E-05 2.66E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 8.03E-07 0.00 0.50 0.00 0.00 0.06 0.04 0.06 0.34 LB/DAYLB/DAY 2.00E+03 l.OOE+04 l.OOE+00 1 101 9.13E+02 1.84E-01 1.22E-04 -6.32E-09 6.3SE+02 1.92E-01 -2.55E-05 1.14E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 9.92E-09 0.00 0,81 0.00 0.02 0.08 0.03 0.05 0.01 LB/DAYLB/DAY 2.00E+03 l.OOE+04 l.OOE+00 1 101 1.94E-08 9.13E+02 1.84E-01 1.22E-04 -6.32E-09 1.61E-09 6.96E+03 3.80E-01 -4.92E-OS 2.12E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 9.92E--09 0.00 0.82 0.00 0.00 0.06 0.04 0.06 0.02 CHLORINE DIOXIDE GENERATINGrFEEDLB/DAYLB/DAY l.OOE+01 3.50E+03 l.OOE+00 17-1201 2.74E+04 2.55E+02 -7.17E-02 1.47E+03 5.30E+00 -1.70E-03 O.OOE+00 O.OOE+00 O.OOE+00 1.28E+04 6.SOE+01 -2.20E-02 OZONE GENERATION SYSTEMS 4.12E+04 1.78E+03 -7.83E-01 1.26E+03 1.83E+01 -6.29E-03 O.OOE+00 O.OOE+00 O.OOE+00 8.09E-06 2.94E+03 6.31E+00 2.61E-04 -8.13E-08 1.89E-07 5.88E+02 1.85E+00 -3.19E-04 2.99E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.72E-06 0.00 0.41 0.00 0.00 0.32 0.02 0.03 0.22 LB/DAYLB/DAY l.OOE+01 3.50E+03 l.OOE+00 1 1 1.31E-04 1.75E+04 3.33E+03 -6.98E-01 1.55E-04 9.52E-07 4.74E+02 1.06E+00 -1.37E-05 -2.61E-08 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 6.71E+03 1.60E+01 1.06E-02 -1.58E-06 0.00 0.79 0.00 0.00 0.17 0.00 0.00 0,04 OZONE CONTACT CHAMBER 4.06E+03 4.93E+00 -1.04E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00, O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 CU FT CU FT 4.60E+02 9.20E+04 l.OOE+00 1 1 8.00E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 4.15E-06 O.OOE+00 -3.30E-02 4.46E-06 O.OOE+00 -3.57E-02 3.38E-01 1.72E+00 -2.04E-02 O.OOE+00 O.OOE+00 -1.49E-01 O.OOE+00 O.OOE+00 0.06 0.00 0.19 0.32 0.43 0.00 0.00 0.00 ON-SITE HYPOCHLORITE GENERATION LB/DAYLB/DAY l.OOE+01 l.OOE+04 l.OOE+00 35-1101 1.S8E+04 3.58E+02 -S.97E-02 3.37E-06 -4.90E+01 9.16E+02 -4.97E-03 3.67E-07 6.49E-08 3.76E+02 8.98E-01 -1.21E-04 6.59E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 8.54E-07 0.00 0.60 0.00 0.00 0.21 0.00 0.06 0.13 LB/HR LB/HR 5.40E+00 5.40E+03 l.OOE+00 24 101 5.16E-06 3.24E+03 4.26E+00 1.80E-05 5.24E-07 -1.17E-09 6.15E+01 6.92E-03 9.17E-06 -3.44E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.32E-06 0.00 0,42 0.00 0.00 0.08 0.03 0.12 0.35 LB/HR LB/HR l.OOE+01 5.00E+03 l.OOE+00 24 101 7.40E-06 4.84E+03 2.28E+00 -7.93E-04 1.07E-07 3.40E-09 2.68E+02 8.11E-01 2.87E-O5 -4.02E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00, 5.87E-06 0.00 0,40 0.00 0.00 0.03 0.07 0.06 0.44 LB/DAYLB/DAY l.OOE+00 2.00E+02 l.OOE+00 1 110 -9.09E-04 1.73E+04 3.37E-03 1.05E-05 6.28E-OB 8.58E-05 1.96E+02 3.33E-01 -2.16E-03 7.20E-06 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 4.68E-04 O.OO 0.69 O.OO 0.00 O.O4 0.01 0.07 0.19 LB/HR LB/HR l.OOE+01 l.OOE+03 l.OOE+00 24 101 2.44E-04 3.25E+03 9.61E+00 -1.47E-02 7.94E-06 2.64E-06 5.20E+02 5.53E+00 -9.68E-O3 5.68E-06 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.22E+04 1.67E+01 6.71E-02 -4.20E-05 0.00 0.53 0.00 0.00 0.02 0.13 0.07 0,49 LIME FEED-WITH RECALCINATION LB/HR LB/HR l.OOE+03 l.OOE+04 l.OOE+00 24 108 2.12E-07 1.35E+03 4.00E+00 -4.51E-04 3.34E-08 6.99E+02 1.47E+00 -1.76E-04 8.88E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 8.73E-09 0.00 0.67 0.00 O.OO 0.02 0.05 0.10 0.16 LB/DAYLB/DAY 1.OOE+OO S.OOE+02 l.OOE+00 1 101 4.13E-05 3.08E+03 2.OOE+OO 1.56E-02 -1.17E-05 6.97E-07 2.06E+02 2.57E+00 -9.02E-03 1.03E-05 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 5.69E-05 0.00 0.33 0.00 0.00 0.06 0.10 0.33 0.18 GPD GPU l.OOE+01 5.00E+03 l.OOE+00 153-1101 7.24E-07 1.60E+03 -1.53E-01 2.54E-04 -3.15E-08 1.57E-09 7.88E+01 1.60E-01 -3.34E-05 4.67E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO .11 0.11 0.22 0.10 1. OOE+OO 1 101 3.20E+03 8.66E-01 -3.39E-05 -2.79E-10 1.20E+02 1.59E-02 -3.08E-06 3.03E^10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.39E-07 0.00 0.39 0.00 0.00 0.05 0.05 0.18 0.33 LB/HR LB/HR 1.07E+01 5.35E+03 l.OOE+00 24 101 4.61E-06 4.70E+03 2.09E+00 -5.59E-04 6.54E-08 6.45E-09 2.67E+02 7.95E-01 -4.06E-O5 8.10E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 4.44E-06 0.00 0.38 0.00 0.00 0.03 0.06 O.O6 0,47 9.23E+02 1.06E+01 -9.70E-04 O.OOE+00 O.OOE+00 O.OOE+00 4.85E+03 8.09E+01 -1.50E-02 ALUM FEED-LIQUID STOCK 1.91E+04 1.14E+02 -3.86E-02 7.38E+01 6.3OE-02 O.OOE+00 O.OOE+OO 5.43E+03 8.22E+O1 ALUM FEED-DRY STOCK 2.09E+04 1.40E+02 -4.64E-02 1.99E+02 1.30E-01 O.OOE+00 O.OOE+00 5.67E+03 9.81E+01 POLYMER FEED SYSTEMS 2.00E+04 1.73E+01 2.59E+02 O.OOE+00 7.99E+03 2.26E+01 LIME FEED-NO RECALCINATION 4.37E+04 2.84E+02 -4.56E-01 7.02E+02 2.52E+00 -4.47E-03 O.OOE+00 O.OOE+00 O.OOE+00 1.30E-05 -7.11E-10 O.OOE+00 O.OOE+00 5.98E+04 2.30E+01 -3.54E-O3 1.35E+03 -2.61E-03 O.OOE+00 O.OOE+00 1.63E+04 7.24E+00 -3.31E-04 POTASSIUM PERMANGANATE FEED 9.63E+O3 2.41E+01 -4.69E-02 7.24E+01 3.48E-01 -6.92E-04 O.OOE+00 O.OOE+OO O.OOE+00 1.45E+03 1.61E+01 -4.65E-02 SULFURIC ACID FEED SYSTEMS 8.60E+03 2.26E+01 -5.78E-03 6.48E+01 4.90E-02 -1.46E-05 O.OOE+00 O.OOE+00 O.OOE+00 2.88E+03 -9.94E-01 3.52E-04 -3.79E-08 0.00 0.46 0.00 0.00 0. SODIUM HYDROXIDE FEED SYSTEMS LB/DAYLB/DAY l.OOE+01 l.OOE+04 1.44E+O4 1.39E+02 7.94E+00 -4.89E-04 2.86E-02 O.OOE+00 4.34E-08 O.OOE+00 1.06E+03 1.47E+01 -2.03E-03 FERROUS SULFATE FEED SYSTEMS 1.96E+04 1.20E+02 -3.21E-02 1.85E+02 1.26E-01 -1.86E-05 O.OOE+00 O.OOE+00 O.OOE+00 5.71E+03 8.93E+01 -2.89E-02 2.28E-06 -1.33E-10 O.OOE+00 O.OOE+00 71 ------- CRV.DAT FILE (CONTINUED) FERRIC SULFATE FEED SYSTEMS LB/HR LB/HR 1.33E+01 6.60E+03 l.OOE+00 24 101 1.95E+04 9.79E+01 -2.26E-02 2.68E-06 4.79E+03 1.57E+00 -2.19E-04 1.46E-08 1.88E+02 4.81E-02 3.59E-OS -2.62E-09 2.72E+02 S.38E-01 7.17E-05 -B.18E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 5.80E+03 6.71E+01 -1.41E-02 1.76E-06 0.00 0.38 0.00 0.00 0.03 0.06 0.06 0.47 ANHYDROUS AMMONIA FEED FACILITY LB/DAYLB/DAY 2.50E+02 5.00E+03 l.OOE+00 1 101 1.85E+04 5.70E+01 -1.68E-02 1.89E-06 -9.13E+01 3.41E+00 3.13E-03 -4.49E-07 6.59E-08 4.57E+02 2.27E-01 -5.25E-05 5.71E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.46E-07 0.00 0.55 0.00 0.00 0.15 0.10 0.11 0.09 LB/DAYLB/DAY 2.50E+02 5.00E+03 l.OOE+00 34-1101 3.58E-07 5.70E+02 4.73E-07 -2.01E-10 1.69E-14 5.43E-09 1.52E+02 1.26E-07 -5.51E-11 4.55E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.71 0.00 0.00 0.06 0.05 0.18 0.00 LB/HR LB/HR 3.50E+00 7.00E+03 l.OOE+00 24 101 5.35E-06 7.94E+03 1.36E+03 -3.62E-01 3.10E-05 3.07E-07 9.29E+02 2.04E+00 -3.98E-04 4.50E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.94E-13 0.01 0.44 0.02 0.04 0.05 0.15 0.24 0.05 CU FT CU FT l.OOE+02 2.00E+04 l.OOE+00 1 1 2.16E-04 -4.63E-09 -9.19E-04 5.09E+01 -7.63E-10 1.48E-13 1.45E-02 -4.44E-07 2.21E-11 4.54E+02 -6.88E-03 9.09E-06 -2.95E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.03 0.31 0.07 0.11 0.18 0.00 0.30 0.00 CU FT CU FT l.OOE+02 2.00E+04 l.OOE+00 1 1 15E-04 -9.31E-10 1.50E+01 1.02E+02 1.23E-05 -1.90E-10 2.21E-11 O.OOE+00 2.27E+03 2.48E+00 -6.03E-04 O.OOE+00 O.OOE+00 O.OOE+00 9.44E+03 2.53E+00 -1.05E-03 AQUA AMMONIA FEED FACILITY 8.94E+03 1.58E+01 -3.50E-03 3.99E+01 2.52E-01 -5.49E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 POWDERED ACTIVATED CARBON FEED 7.01E+04 3.07E+02 -6.09E-02 2.00E+01 -3.67E-03 O.OOE+OO O.OOE+00 7.39E-06 -4.71E-09 2.36E+03 O.OOE+00 1.03E+04 RAPID MIX» G=300 1.38E+04 7.45E+00 2.05E+01 O.OOE+00 O.OOE+00 RAPID MIXr 1.41E+04 2.0SE+01 O.OOE+00 O.OOE+00 RAPID MIXi G=900 1.41E+04 1.99E+01 2.05E+01 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 G=60O 1.05E+01 1 1.45E-02 -4.44E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.46E-05 1.45E-02 -4.44E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 4.54E+02 -6.88E-03 9.09E-06 -2.95E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.02 0.40 0.06 0.09 0.17 0.00 0.26 0.00 CU FT CU FT l.OOE+02 2.00E+04 l.OOE+00 1 1 1.90E-09 -7.51E+01 3.40E+02 -7.42E-05 2.91E-09 4.54E+02 -6.88E-03 9.09E-06 -2.95E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.29E+04 3.66E+02 O.OOE+00 O.OOE+00 3.80E+00 -5.18E-06 3.70E-02 -2.61E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.21E-11 O.OOE+00 O.OOE+00 0.01 0.60 0.04 0.06 0.12 0.00 0.17 0.00 FLOCCULATION-HORIZ PADDLE, G=20 CU FT CU FT 1.80E+03 l.OOE+06 l.OOE+00 1 1 3.40E+04 3.41E+00 -4.93E-06 3.32E-12 -2.55E+01 1.98E-01 -8.37E-09 8.71E-15 3.66E+02 3.70E-02 -2.61E-08 1.77E-14 1.30E+02 2.68E-03 -5.51E-09 3.76E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.04 0.24 0.12 0.17 0.25 0.00 0.18 0.00 FLOCCULATION-HORIZ PADDLEr G=50 CU FT CU FT 1.80E+03 l.OOE+06 l.OOE+00 1 1 3.51E-12 -7.31E+01 1.19E+00 -1.71E-08 1.57E-14 1.77E-14 1.30E+02 2.68E-03 -5.51E-09 3.76E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.04 0.27 0.10 0.17 0.26 0.00 0.16 0.00 FLOCCULATION-HORIZ PADDLEr G=80 CU FT CU FT 1.80E+03 5.00E+05 l.OOE+00 1 1 2.S2E+04 S.56E+00 -1.69E-05 2.25E-11 4.58E+01 3.36E+00 6.58E-09 -3.07E-14 3.66E402 3.70E-02 -2.61E-08 1.77E-14 1.30E+02 2.68E-03 -5.51E-09 3.76E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 0.02 0.34 0.08 0.13 0.24 0.00 0.19 0.00 FLOCCULATION-VERT TURBINE G=20 CU FT CU FT 1.80E+03 2.50E+04 l.OOE+00 1 1 1.11E+04 1.17E+01 .-3.61E-04 4.46E-09 -2.55E+01 1.98E-01 -8.37E-09 8.71E-15 1.77E-14 1.30E+02 2.68E-03 -5.51E-09 3.76E-15 O.OOE+00 O.OOE+00 FLOCCULATION-VERT TURBINE, G=50 CU FT CU FT 1.80E+03 2.50E+04 l.OOE+00 1 1 1.11E+04 1.17E+01 -3.61E-04 4.46E-09 -7.31E+01 1.19E+00 -1.71E-08 1.57E-14 3.66E+02 3.70E-02 -2.61E-08 1.77E-14 1.30E+02 2.68E-03 -5.51E-09 3.76E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.03 0.18 0.09 0.14 0.25 0.00 0.32 0.00 FLOCCULATION-VERT TURBINE? G=80 CU FT CU FT 1.80E+03 2.50E+04 l.OOE+00 1 1 1.04E+04 1.22E+01 -4.31E-04 6.92E-09 1.77E-14 O.OOE+00 3.66E+02 O.OOE+00 O.OOE+00 3.70E-02 -2.61E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.02 0.27 0.07 0.12 0.27 0.00 0.26 0.00 3.66E+02 3.70E-02 -2.61E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 CIRCULAR CLARIFIER-LIME SLUDGE 5.83E+04 3.63E+01 -4.99E-04 1.01E+02 2.14E-01 -6.35E-06 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 4.21E+01 3.37E+00 -2.54E-08 2.87E-14 1.30E+02 2.68E-03 -5.51E-09 3.76E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.03 0.23 0.09 0.15 0.29 0.00 0.22 0.00 SQ FT SO FT 7.07E+02 3.14E+04 l.OOE+00 1 3 6.35E-09 4.64E+03 4.18E-01 -2.09E-06 -4.35E-11 1.14E-10 1.35E+02 2.24E-02 -6.61E-07 1.01E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.02 0.31 0.08 0.37 0.14 0.05 0.03 0.00 CIRC CLARIFIER-FECL3 8 ALUM SLDGSO FT SQ FT 7.07E+02 3.14E+04 l.OOE+00 1 3 5.83E+04 3.63E+01 -4.99E-04 6.35E-09 3.09E+03 3.79E-01 -9.65E-06 1.84E-10 1.01E+02 2.14E-01 -6.35E-06 1.14E-10 1.35E+02 2.24E-02 -6.61E-07 1.01E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.02 0.31 0.08 0.37 0.14 0.05 0.03 0.00 RECTANGULAR CLARIFIER-LIME SLDG SQ FT SQ FT 2.40E+02 4.80E+03 l.OOE+00 1 3 7.38E-07 3.04E+03 9.62E-01 1.40E-04 1.40E-08 3.64E-09 O.OOE+00 6.43E+01 -6.31E-03 1.32E-01 -2.13E-06 O.OOE+OO O.OOE+00 2.38E+04 2.53E+02 O.OOE+00 O.OOE+00 O.OOE+00 RECT CLARIFIER-FECL3 2.38E+04 6.43E+01 -6.31E-03 2.S3E+02 1.32E-01 -2.13E-06 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 1.49E+02 8.61E-02 -4.09E-06 3.63E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.04 0.27 0.10 0.25 0.21 0.11 0.02 0.00 ALUM SLG SQ FT SQ FT 2.40E+02 4.80E+03 l.OOE+00 1 3 7.38E-07 3.08E+03 8.15E-01 -4.68E-05 2.35E-08 3.64E-09 1.49E+02 8.61E-02 -4.09E-06 3.63E-1Q O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+OO 0.04 O.27 0.1O 0.25 0.21 O.ll 0.02 O.OO 72 ------- CRV.DAT FILE (CONTINUED) UPFLOW SOLIDS CONTACT CLAR.G=70 SQ FT SO FT 2.55E+02 1.45E+04 l.OOE+00 1 3 6.59E+04 5.44E+01 -2.29E-03 2.52E-08 5.92E+03 8.73E+00 -2.79E-04 1.82E-08 5.04E+02 2.71E-01 -1.57E-05 3.90E-10 4.23E+02 7.33E-02 -7.32E-06 2.47E-10 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.04 0.53 0.07 0.10 0.25 0.00 0.01 0.00 UPFLOW SOLIDS CONTACT CLARrG=110SQ FT SQ FT 2.55E+02 1.45E+04 l.OOE+00 1 3 6.59E+04 5.44E+01 -2.29E-03 2.52E-08 2.82E+03 5.04E+02 2.71E-01 -1.57E-05 3.90E-10 4.23E+02 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.04 0.53 UPFLOU SOLIDS CONTACT CLARrG=150SQ FT SQ 6.59E+04 5.44E+O1 -2.29E-03 5.04E+02 2.71E-01 -1.57E-O5 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 TUBE SETTLING MODULES SQ FT SQ 2.86E+03 2.55E+01 -2.00E-04 1.91E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.09E+01 -1.32E-03 8.80E-08 7.33E-02 -7.32E-06 2.47E-10 O.OOE+00 O.OOE+00 O.OOE+00 0.07 0.1O 0.25 0.00 0.01 O.OO FT 2.55E+02 1.45E+04 l.OOE+00 1 3 2.52E-08 7.68E+03 2.22E+01 2.14E-03 -1.15E-07 3.90E-10 4.23E+02 7.33E-02 -7.32E-06 2.47E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 GRAVITY FILTRATION STRUCTURE 1.16E+05 3.92E+02 -2.04E-02 , 4.31E+02 2.78E+00 -1.37E-04 O.OOE+00 O.OOE+00 O.OOE+00 1.72E+04 1.93E+02 -4.11E-03 FILTRATION MEDIA-RAPID SAND 3.80E+03 7.99E+00 -3.52E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 FILTRATION MEDIA-DUAL. MEDIA 2.8'2E+03 2.03E+01 -7.01E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 FILTRATION MEDIA-MIXED MEDIA 4.68E+03 2.91E+01 -6.82E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 BACKWASH PUMPING FACILITIES 2.98E+04 1.05E+01 -1.29E-04 6.23E+02 6.64E-01 -4.19E-05 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO HYDRAULIC SURFACE WASH SYSTEMS 2.60E+04 2.91E+01 -1.05E-03 2.08E+02 4.85E-02 -2.86E-06 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+OO o;ooE+oo AIR-UATER BACKWASH FACILITIES 7.04E+04 4.24E+01 -2.34E-03 6.23E+O2 6.64E-01 -4.19E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OD O.OOE+OO O.OOE+00 UAS.H WATER SURGE BASINS 1.88E+04 3.33E+00 -1.04E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 -O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.04 0.53 0.07 0.10 0.25 0.00 0.01 0.00 FT 2.80E+02 5.60E+04 l.OOE+00 1 1 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.50 0,00 0 SQ FT SQ ,33 0.17 0.00 0.00 0.00 FT 1.40E+02 2.80E+04 l.OOE+00 1 1 4.82E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.03E-09 B.46E+02 8.04E-01 -3.28E-05 9.39E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 8.71E-08 0.01 0.16 0.07 0.05 0.24 0.24 0.07 0.16 SQ FT SQ FT 3.70E+02 7.48E+04 l.OOE+00 1 1 3.78E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 O.OO SQ FT SQ FT 1.40E+02 2.99E+04 l.OOE+00 1 1 1.68E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 SQ FT SQ FT 1.40E+02 2.99E+04 l.OOE+00 1 1 1.63E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 GPM SQ FT 1.26E+03 2.30E+04 1.22E+00 1 1 5.53E-10 -5.92E-01 2.39E+01 -2.50E-06 1.74E-10 8.85E-10 1.93E+02 2.47E-02 -1.32E-06 2.36E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0,00 0.49 0.00 0.00 0.06 0.23 0.22 0.00 SQ FT SQ FT 1.40E+02 2.80E+04 l.OOE+00 1 1 3.21E-08 3.41E+02 1.40E+O1 -5.15E-05 2.16E-09 5.82E-11 7.03E+01 6.70E-02 -5.02E-06 1.28E-10 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.52 O.OO 0.00 O.O8 O.1O 0.30 0.00 SQ FT SQ FT 1.40E+02 2.80E+04 l.OOE+00 1 1 5.58E-08 7.00E+00 2.42E+01 1.39E-06 6.57E-11 8.85E-10 1.94E+02 2.58E-02 -1.46E-06 2.72E-11 O.OOE+OO O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO 0.00 0.41 O.OO 0.00 0.09 0.39 0.11 0.00 GAL GAL l.OOE+04 5.00E+O5 l.OOE+00 1 1 1.11E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.01 0.00 0.30 0.18 0.44 0.05 0.00 0.02 FILTER MOD-RAP SAND TO HIGH RATESQ FT SQ FT 1.40E+02 2.80E+04 l.OOE+00 1 1 2.05E+04 3.28E+01 -1.41E-03 3.21E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0,00 O.OO 0.38 0.45 0.17 0.00 CONTINUOUS AUTO. BACKWASH FILTERSQ FT SQ FT 3.60E+02,7.04E+04 l.OOE+00 1 1 O.OOE+OO O.OOE+00 1.54E+05 1.76E+02 5.09E+02 5.35E-01 O.OOE+00 O.OOE+OO 5.67E+04 1.53E+02 RECARBONATION BASIN 5.42E+03 3.95E+00 -1.28E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 RECARBONATION-LIQUID C02 FEED 3.96E+04 2.01E+01 -1.41E-03 2.48E+03 1.19E+00 -9.17E-O5 O.OOE+00 O.OOE+00 O.OOE+OO 9.83E+03 1.34E+00 -1.22E-04 1.77E-03 -1.75E-08 1.62E-06 -2.49E-11 O.QOE+00 O.OOE+00 3.50E-03 -3 CU FT CU 2.41E-09 O.OOE+OO 7.32E+02 7.00E+02 O.OOE+00 29E-08 O.01 0.50 8.33E+00 1.80E-04 -1.79E-09 6.51E-02 8.76E-06 -8.79E-11 O.OOE+00 O.OOE+00 O.OOE+00 0.07 0.03 0.15 0.03 0.02 0.19 FT 7.70E+02 3.52E+04 l.OOE+00 1 3 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+OO O.OOE+00 O.OOE+00 0.07 0.00 0.20 0.32 0.39 0.02 0.00 0.00 LB/DAYLB/DAY 3.80E+02 1.50E+04 l.OOE+00 1 101 7.69E-08 -7.1"6E+01 1.90E+01 -3.18E-04 1.53E-08 3.06E-09 7.14E+01 2.52E-02 -1.4SE-06 4.43E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 5.38E-09 0.00 0.59 0.00 0.00 0.21 0.09 0.00 0.11 73 ------- CRV.BAT FILE (CONTINUED) RECARB-C02 FROM SUBMERGED BURNERLB/DAVLB/DAY 5.00E+02 1.OOE+04 l.OOE+00 1 3 5.05E+04 6.33E+00 1.58E-04 -2.34E-OB 1.71E+04 7.14E+01 -8.45E-03 4.76E-07 1.36E+03 4.31E-01 -6.59E-05 3.S7E-09 8.00E+01 -6.73E-09 4.09E-12 6.88E-16 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 8.65E+03 3.14E+03 5.61E-03 -4.81E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.56 0.00 0.00 0.20 0.17 0.07 0.00 RECARBONATION-C02 FROM STACK GASLB/DAYLB/BAY 2.50E+03 5.00E+04 l.OOE+00 1 1 8.84E+03 1.13E+01 -3.89E-04 4.68E-09 -1.05E+02 1.74E+01 -5.38E-06 8.69E-11 7.90E-11 O.OOE+00 1.28E+03 3.09E-01 -7.47E-06 O.OOE+00 O.OOE+00 O.OOE+0'0 O.OOE+00 O.OOE+00 O.OOE+00 MULTIPLE HEARTH RECALCINATION 4.89E+OS 2.27E+03 -8.47E-01 3.26E+03 1.67E+01 -4.01E-03 O.OOE+OO O.OOE+00 O.OOE+00 1.78E+03 3.08E+01 -1.45E-02 3.17E+01 2.88E-02 -6.18E-07 6.60E-12 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.42 0.00 0.00 0.27 0.15 0,16 0.00 SQ FT SO FT 1.79E+02 2.93E+03 l.OOE+00 1 3 1.28E-04 1.75E+05 9.27E+02 -4.21E-01 1.3SE-04 8.45E-07 1.10E+03 1.13E+01 -3.23E-03 5.39E-07 O.OOE+00 1.76E+07 4.8SE+04 2.44E+01 -2.17E-03 2.47E-06 0.00 0.63 0.00 0.00 0.27 0.01 0.01 0, CONTACT BASIN-DIRECT FILTRATION CU FT CU FT 2.64E+03 5.28E+04 l.OOE+00 1.06E+04 O.OOE+00 O.OOE+00 O.OOE+00 08 3 3.83E+00 -7.18E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 MGC 7.27E+04 1.09E+02 -4.53E-01 -1.63E+03 3.91E+02 -6.72E-01 O.OOE+00 O.OOE+OO 1.66E+04 -1.84E+01 PRESSURE DIATOMITE FILTERS 2.03E+05 1.10E+03 O.OOE+00 1.42E+05 VACUUM DIATOMITE FILTERS 4.83E+04 1.01E+05 -5.06E+01 2.95E+02 4.49E+02 -5.04E-01 O.OOE+00 O.OOE+00 O.OOE+00 1.52E+04 6.17E+04 -1.06E+02 PRESSURE FILTRATION PLANTS :>.23E+05 2.01E+02 2.57E-02 -6.69E-07 5.17E+02 4.94E+00 -1.89E-04 4.09E-09 O.OOE+00 O.OOE+00 2.01E+05 2.11E+01 IN-PLANT PUMPING 2.23E+04 5.47E+03 -1.53E+01 2.13E+02 1.32E+02 3.50E+01 7.50E+01 2.23E+04 5.47E+03 -1.53E+01 WASH WATER STORAGE TANKS 2.12E+03 3.89E-01 -3.82E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 REVERSE OSMOSIS 2.46E+05 5.32E+05 -1 2.26E+04 O.OOE+OO 2.17E+O4 8.33E+04 -1.09E+02 7.16E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.07 0,00 0.20 0.34 0.39 0.00 0.00 0.00 MGD l.OOE+00 2.00E+02 l.OOE+00 1 302 1.27E+05 -2.42E+02 9.40E-01 1.58E-03 2.39E+03 6.09E+02 -5.47E+00 1.64E-02 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 6.76E-02 0.01 0.62 0.01 0.01 0.15 0.04 0.07 0.09 MGD MGD l.OOE+00 2.00E+02 l.CfOE+00 1 302 2.09E-01 7.54E+03 5.64E+04 1.80E+01 -6.34E-02 2.96E-07 2.39E+03 6.09E+02 -5.47E+00 1.64E-02 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.75E-01 0.01 0,32 0.01 0.01 0.22 0.22 0.05 0,16 SO FT SQ FT 1.4OE+02 2.80E+04 l.OOE+00 1 1 2.90E+03 2.34E+02 2.36E-04 -S.36E-09 1.25E+03 1.37E+00 -6.16E-05 1.32E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 9.00E-03 -2.26E-07 0.01 0,45 0.01 0.01 0.07 0.25 0.12 0.08 MGD MGD l.OOE+00 2.00E+02 l.OOE+00 1 5 6.48E-02 1.41E+02 5.24E+04 1.64E+00 -4.S9E-03 4.54E-01 -2.49E-03 5.09E+02 2.20E+01 -1.90E-02 1.24E-04 4.00E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 6.48E-02 0.01 0.22 0.02 0.03 0.28 0.27 0.11 0.06 GAL GAL 2.10E+04 9.00E+05 l.OOE+00 1 1 2.98E-13 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.02 0.00 0.01 0.43 0.54 0.00 0.00 0,00 MGD MGD l.OOE+00 2.00E+02 l.OOE+00 1 302 4.28E+00 2.24E+05 2.19E+06 3.69E+02 -1.27E+00 2.46E-01 1.81E+03 9.13E+01 -6.70E-01 2.30E-03 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO 3.49E-01 0.00 0.61 0.00 0.00 0.12 0.00 0.15 0.12 PRESSURE ION EXCHANGE-SOFTENING MGD MGD 1.10E+00 1.23E+02 l.OOE+00 490 1101 4.95E+04 8.59E+04 2.76E+02 -2.03E+00 -1.15E+00 2.06E+03 -7.18E-02 5.50E-04 1.26E-02 -S.BSE-'OS 2.11E+03 1.28E+02 -8.5BE.-01 4.75E-03 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 5.68E-08 O.OOE+00 O.OOE+00 O.OOE+00 .50E+03 6.85E+04 -7.22E+01 O.OOE+OO O.OOE+00 2.38E+02 O.OOE+00 2.S9E+04 4.33E+03 O.OOE+00 2.78E+04 GRAVITY ION EXCHANGE-SOFTENING 1.17E+05 6.81E+04 -2.15E+02 l.OBE+03 3.93E+03 -2.31E+00 O.OOE+00 O.OOE+00 O.OOE+00 1.69E+04 1.82E+04 -4.30E+01 1.88E+02 -1.63E+00 0.01 0.52 O.O1 0.01 0,01 0.16 0.16 0.12 MGD MGD 1.50E+00 1.50E+02 l.OOE+00 49O 1101 7.80E-01 -1.53E+00 9.81E+02 4.15E-02 -3.23E-04 8.75E-03 2.11E+03 1.08E+02 -1.96E-01 1.07E-03 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.16E-01 0.01 0.59 0.04 0.03 0.09 0.10 0.06 0.08 PRESSURE ION EXCHANG-N03 REMOVALMGD MGD 1.10E+00 1.23E+01 l.OOE+00 121'2101 2.04E+05 2.28E+04 3.35E+04 -1.72E+03 -8.31E-01 1.73E+03 -2.09E+00 1.28E-01 2.43E+03 2.08E+04 5.64E+02 -3.15E+01 2.06E+03 1.05E+02 l.OOE+01 -7.74E-01 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.48E+04 2.82E+04 1.70E+02 -4.61E+01 0.01 0.68 0.01 0.01 0.11 0.06 0.06 0.06 ACTIV. ALUMINA-FLUORIDE REMOVAL MGD MGD 7.00E-01 1.35E+02 l.OOE+00 1 202 4.46E+04 5.97E+04 1.94E+02 -1.05E+00 9.29E+00 6.22E-01 -7.15E-03 4.36E-05 6.16E+02 1.60E+03 1.98E+01 -1.14E-01 2.41E+03 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.35E+03 2.09E+04 -8.13E-01 -2.39E-01 0.00 0.52 6.26E+01 7.21E-01 -2.60E-03 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.12 0.16 0.05 0.. 15 GRAVITY GAG CONTACTORS-CONCRETE CU FT SO FT 3.50E+02 1.06E+04 1.40E+02 28 3004 6.47E+04 4.31E+02 O.OOE+00 1.72E+04 5.83E+01 -6.53E-03 2.78E+00 -1.37E-04 O.OOE+00 O.OOE+00 1.93E+02 -4.11E-03 GRAVITY GAC CONTACTORS-STEEL 1.41E+04 2.68E+01 -3.93E-04 5.46E+02 1.61E-01 -3.12E-07 O.OOE+00 O.OOE+00 O.OOE+00 -4.52E+03 2.17E+01 -1.22E-05 PRESSURE CARBON CONTACTORS 3.94E+04 7.63E+01 -2.69E-02 9.25E+02 4.10E+00 1.60E-04 O.OOE+00 O.OOE+00 O.OOE+00 4.59E+04 3.97E+02 -6.00E-02 2.96E-07 9.41E+00 4.86E+00 1.20E-06 -2.55E-11 3.03E-09 8.46E+02 8.04E-01 -3.28E-05 9.39E1-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 8.71E-08 0.01 0.14 0.05 0.03 0.20 0.41 0.02 0.14 CU FT CU FT 6.28E+03 1.41E+04 3.14E+04 '628'3004 7.46E-09 -8.24E+01 3.86E-01 -2.13E-08 2.85E-14 3.21E-13 2.32E+03 1.89E-02 9.37E-08 -9.64E-14 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.. OOE+00 1.26E-11 0.01 0.43 0.01 0.01 0.08 0.19 0.66 6..21 CU FT SQ FT 3.90E+02 2.26E+03 1.57E+02 679,1004 4.52E-06 1.21E+02 5.OOE+00 2.12E-04 -1.41E-08 2.88E-09 8.90E+02 7.30E-01 3.52E-05 -3.07E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+OO 6.91E-06 0.01 0.47 0.01 0.01 0.06 0.17 0.10 0.17 74 ------- CRV.DAT FILE (CONTINUED) O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 MAKEUP CARBON COST-O&M ONLY O.OOE+00 O.OOE+00 O.OOE+00 CONVERT FILTER TO GAC CONTACTOR SB FT SO FT 3.70E+02 7.00E+04 l.OOE+00 1 1 2.03E+04 5.10E+01 -2.52E-04 1.97E-09 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.12 0.00 0.00 0.25 0.61 0.02 0.00 GRANULAR ACT CARBON-CONSTR COST LB LB l.OOE+04 l.OOE+07 l.OOE+00 1 1 1.02E+03 6.07E-01 -6.54E-09 -5.61E-17 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 LB/YR LB/YR l.OOE+04 l.OOE+07 l.OOE+00 1 1 O.OOE+OO O.OOE+OO O.OOE+00 O.OOE+OO O.OOE+00 1.02E+03 6.07E-01 -6.54E-09 -5.61E-17 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 O.OO 0.00 O.OO 0.00 0.00 0.00 0.00 CAPPING SAND FILTER U/ANTHRACITESQ FT SQ FT 3.SOE+02 7.00E+04 l.OOE+00 1 1 4.08E+02 6.17E+00 -9.55E-06 9.53E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO 0.00 O.OO 0.68 0.00 0.32 O.OO 0.00 O.OO REGIONAL GAC REGEN-TRANS 8 STOR CU FT LB/YR l.OOE+03 2.00E+04 3.OOE+O4 3 6006 1.83E+04 7.21E+00 1.87E-03 -6.84E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.46E-03 1.99E-05 1.35E-13 -1.14E-21 -1.16E-02 2.30E-05 7.07E-14 4.37E-21 -9.54E-03 1.93E-05 4.O8E-14 2.60E-21 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO 0.01 0.16 0.02 0.39 0.37 O.OS 0.00 0.00 REGIONAL MULTI HEARTH GAC REGEN SQ FT SQ FT 2.70E+01 1.51E+03 l.OOE+00 1 12 4.68E+05 3.74E+03 -2.71E+00 B.31E-04 2.49E+05 1.26E+03 -8.58E-01 3.22E-04 2.48E+03 2.78E+01 -2.9SE-02 1.13E-05 2.51E+02 2.19E+01 -1.46E-02 4.94E-06 O.OOE+00 1.69E+06 1.59E+05 -4.87E+01 2.29E-02 2.78E+01 -2.9SE-02 O.OOE+00 O.OOE+00 -2.95E-02 O.OOE+00 2.48E+03 2.78E+01 O.OOE+00 O.OOE+00 1.39E+04 2.17E+01 1.89E-02 -1.25E-05 0.00 INFRARED CARBON REGEN FURNACE 2.19E+05 3.15E+01 -3.64E-04 6.06E+03 1.24E+00 -2.46E-05 O.OOE+00 O.OOE+00 O.OOE+00 -3.49E+00 3.31E+00 -7.03E-05 FLUIDIZED BED GAC REGENERATION 7.74E+05 3.19E+01 -S.94E-04 1.09E+04 8.46E-01 -3.46E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+00 1.39E+04 2.17E+01 1.89E-02 -1.25E-05 0.00 0.53 0.00 0.00 0,28 0.02 0.01 0.16 MULTIPLE HEARTH'GAC REGENERATIONSQ FT SQ FT 2.70E+01 1.51E+03 l.OOE+00 1 3 4.68E+05 3.74E+03 -2.71E+00 8.31E-04 2.49E+05 1.26E+03 -8.58E-01 3.22E-04 1.13E-05 2.51E+02 2.19E+01 -1.46E-02 4.94E-06 O.OOE+00 1.69E+06 1.59E+05 -4.87E+01 2.29E-02 0.53 0.00 0.00 0.28 0.02 0.01 0.16 LB/DAYLB/DAY 2.40E+03 6.00E+04 l.OOE+00 1 1 4.03E-09 -6.19E+04 3.28E+02 -4.27E-03 6.50E-08 1.95E-10 2.03E+03 1.14E-01 2.17E-06 -2.35E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 6.95E-10 0.00 0.64 0.00 0.00 0.18 0.01 0,08 0.09 LB/DAYLB/DAY 6.00E+03 2.40E+04 l.OOE+00 1 3 5.97E-09 -4.60E+00 2.10E+01 -1.98E-O8 1.43E-12 6.28E-10 2.39E+03 -5.59E-02 7.67E-06 -1.65E-10 O.OOE+00 -1.64E+05 1.14E+03 -4.05E-03 9.73E-OB O.OOE+00 O.OO 0.68 O.OO O.OO 0,22 O.OO 0.01 O.O9 POWDERED CARB REGEN-FLUIDIZED BDLB/DAYLB/DAY 2.09E+02 3.34E+04 l.OOE+00 1 1 5.74E+05 3.28E+02 -1.56E-02 3.01E-07 -1.89E+03 4.52E+02 -1.91E-02 3.84E-07 2.59E+03 2.35E-01 -7.94E-06 1.44E-10 1.20E+03 2.82E-02 5.15E-06 -1.12E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.89E+05 3.49E+03 -4.93E-02 9.28E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.49 0.00 O.OO 0.35 O.OO 0.15 O.01 POWDERED CARB REGEN-ATOMIZED SUSLB/DAYLB/DAY l.OOE+03 l.OOE+04 l.OOE+00 1 1 1.04E+05 2.29E+02 -4.87E-03 2.13E-07 2.03E+04 2.23E+01 4.30E-03 -2.28E-07 1.93E+03 4.43E-02 2.41E-05 -1.69E-09 9.04E+02 1.28E-01 -1.23E-05 5.60E-10 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+OO -2.98E+O5 6.42E+03 -1.21E-01 3.27E-06 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.76 O.OO 0.00 0,00 0.00 0.12 0.12 CHEM SLUDGE PUMPING-UNTHICKENED 0PM GPM 2.00E+01 l.OOE+04 l.OOE+00 1 1 3.28E+04 6.07E+01 -9.22E-03 5.49E-07 2.36E+00 6.39E+01 3.07E-OS -2.00E-09 6.00E-08 1.07E+02 3.08E-01 -5»16E-05 2.91E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.75E-08 0.01 0.15 0.06 0.06 0.24 0.23 0.14 0.11 0PM GPM 5.00E+00 1.25E+03 l.OOE+00 1 1 1.17E-04 2.98E+03 4.62E+02 -2.14E-01 9.60E-05 1.47E-05 O.OOE+00 7.70E-07 2.27E+03 7.39E+00 -9.64E-04 O.OOE+00 O.OOE+00 O.OOE+00 9.71E+03 3.26E+00 -5.88E-04 CHEM SLUDGE PUMPING-THICKENED 8.46E+03 1.69E+Q2 -2.43E-01 1.10E+O3 2.21E+O1 -3.06E-02 O.OOE+00 O.OOE+00 O.OOE+00 4.95E+03 6.05E+00 -2.38E-03 GRAVITY SLUDGE THICKENER-LIME 4.18E+04 4.06E+01 -3.99E-03 9.36E+01 1.59E-01 1.17E-O6 -1.63E-10 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 9.36E+01 1.59E-01 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 VACUUM FILTERS '1.62E+05 7.36E+02 -2.69E-01 1.63E+03 1.52E+02 -1.66E-01 O.OOE+OO O.OOE+00 O.OOE+00 4.77E+01 9.40E-01 -1.26E-03 5.90E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.64 0.00 0.00 0.13 0.04 0.07 0.12 SQ FT SQ FT 3.14E+02 1.78E+04 l.OOE+00 1 3 1.58E-07 2.83E+03 1.44E+00 1.11E-04 -4.34E-09 1.16E+02 3.59E-02 -2.69E-06 8.67E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 00 3 2.76E+03 1.69E+00 -8.49E-05 4.05E-09 1.16E+02 3.59E-02 -2.69E-06 8.67E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.03 0.41 O.12 0.16 0.27 0.00 0.01 0.00 SQ FT SQ FT 9.40E+00 1.32E+03 l.OOE+00 1 1 7.78E+04 1.50E+03 1.84E-01 -7.19E-06 6.12E+02 1.58E+O1 -1.39E-02 5.99E-06 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 0.03 0.41 0.12 0.16 0.27 0.00 0.01 0 GRAV SLDG THICKENER-ALUM £ FECL3SQ FT SQ FT 3.14E+02 1.78E+04 l.OOE+00 1 4V18E+04 4.06E+01 -3.99E-03 1.58E-07 1.17E-06 -1.63E-10 O.OOE+00 O.OOE+00 1.12E-04 7.35E-05 O.OOE+00 1.27E+05 3.81E+02 -5.67E-01 3.18E-04 0.00 0.46 O.OO 0.00 0.16 0.02 0.02 0.34 75 ------- CRM.DAT FILE (CONTINUED) BELT FILTER PRESS 1.20E+05 5.65E+03 5.71E+02 5.25E+01 O.OOE+00 O.OOE+00 O.OOE+00 9.79E+04 1.34E+03 -3.83E+00 FILTER PRESS 2.03E+05 5.06E+03 -1.03E+01 9.57E+02 2.88E+01 -4.96E-02 O.OOE+00 O.OOE+00 O.OOE+00 1.32E+05 1.92E+03 -4.14E+00 DECANTER CENTRIFUGES 1.47E+05 1.92E+03 -4.01E+00 6.39E+02 9.18E+01 -3.09E-01 O.OOE+00 O.OOE+00 O.OOE+00 9.86E+04 7.87E+02 -1.62E+00 BASKET CENTRIFUGES 1.7SE+05 7.66E-01 1.71E+03 1.30E-02 O.OOE+00 O.OOE+00 7.76E+04 8.30E-01 SAND DRYING BEDS 7.4SE+03 2.97E+00 -7.41E+00 -1.7SE-04 GPM GPM 1.50E+01 4.50E+02 l.OOE+00 1 1 1.13E+01 -1.82E-02 4.69E+04 3.40E+03 8.73E+00 -1.31E-02 1.23E-01 -2.09E-04 8.03E+02 1.75E+01 2.87E-02 -2.76E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 6.90E-03 0.00 0.69 O.OO 0.00 0.21 0.02 0.01 0.07 CU FT CU FT 4.30E+00 8.96E+02 l.OOE+00 1 1 7.89E-03 1.66E+04 1.92E+03 -2.34E+00 1.93E-03 3.64E-05 7.00E+03 7.33E+00 5.26E-02 -3.01E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.05E-03 0.00 0.61 0.00 0.00 0.18 0.01 0.01 0.19 GPM GPM l.OOE+01 5.00E+02 l.OOE+00 1 3 4.02E-03 5.16E+02 1.16E+03 8.29E-01 -1.05E-03 3.67E-04 5.64E+02 1.72E+01 -6.16E-02 7.64E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.20E-03 0.00 0.48 0.00 0.00 0.17 0.04 0.03 0.28 GPD GPD 3.60E+03 7.20E+05 l.OOE+00 1 1 6.13E-06 -6.15E-12 6.08E+04 7.85E-01 1.11E-05 -1.07E-11 8.22E-08 -7.34E-14 4.78E+03 -4.13E-02 1.38E-07 -1.38E-13 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.17E-05 -1.15E-11 0.00 0.53 0.00 0.00 0.17 0.05 0.01 0.24 SQ FT SQ FT 5.00E+03 4.00E+05 l.OOE+00 1 1 5.07E-07 -6.77E-12 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.16E-02 -9.43E-09 1.83E-14 5.74E+02 2.84E-02 6.47E-08 -9.80E-14 6.00E-02 1.12E-13 -2.90E-19 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.06 0.00 0.08 0.02 0.64 0.20 0.00 0.00 SLUDGE DEUATERING LAGOONS CU FT CF/YR 4.00E+04 8.00E+06 6.25E-01 1 1 6.79E+03 8.13E-02 -2.06E-09 -2.55E-17 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 4.22E+01 S.85E-04 -8.68E-11 -2.92E-20 1.80E+01 7.71E-03 -3.45E-10 -2.32E-18 7.S4E+00 9.27E-03 -1.55E-10 -1.17E-18 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.51 0.00 0,04 0.01 0.28 0.16 0.00 0.00 GPM GPM 2.00E+01 l.OOE+04 l.OOE+00 1 11 2.55E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 MG/YR MG/YR 1.25E+00 l.OOE+02 l.OOE+00 1 7 6.4SE+01 -3.71E-01 5.65E+04 1.76E+04 -5.40E+01 4.24E-01 4.53E-02 -2.70E-04 -9.35E-01 2.09E+02 4.07E-02 -3.77E-04 4.17E-01 -3.05E-03 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 CY/YR CY/YR l.OOE+03 3.00E+05 l.OOE+00 1 7 1.98E-11 4.10E+04 4.59E+00 -1.83E-05 4.27E-11 8.96E+01 2.93E-02 1.11E-07 -2.74E-13 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 SLUDGE DISPOSAL-SANITARY SEWER 4.94E+01 8.43E+02 -2.11E-04 O.OOE+00 O.OOE+00 O.OOE+00 5.00E+03 O.OOE+00 O.OOE+00 O.OOE+00 LIQUID SLUDGE HAULING 7.23E+04 2.03E+03 7.33E+00 5.94E+02 6.53E+01 5.07E+02 O.OOE+00 O.OOE+00 DEUATERED SLUDGE HAULING 4.S6E+04 1.34E+00 -7.65E-06 1.21E+02 9.79E-02 1.31E+02 8.85E-02 O.OOE+00 O.OOE+00 1.27E-07 -3.05E-13 7.88E-08 -1.95E-13 3.00E+01 1.97E+04 l.OOE+02 4.89E-04 5.O6E+03 -8.25E+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0,00 0.00 0.00 RAW WATER PUMPING FACILITY MGD MGD l.OOE+00 2.00E+02 l.OOE+00 1 5 1.92E+04 3.43E+03 -2.89E+00 8.85E-03 -5.38E-03 4.49E+04 -9.78E-05 -1.42E-07 2.17E+02 1.33E+02 2.80E-01 -1.63E-03 4.99E+02 2.37E+01 -3.57E-02 1.66E-04 1.34E-05 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.51E-02 0.00 0.42 0.00 0.00 0.17 0.32 0.09 0.00 FINISHED WATER PUMPING FACILITY MGD MGD 1.50E+00 3.00E+02 l.OOE+00 1 5 3.75E+04 2.82E+03 1.50E+01 -3.27E-02 8.19E-04 5.00E+04 8.10E-05 -3.33E-07 1.97E-04 5.06E+02 2.13E+01 5.23E-03. 1.22E-05 4.28E-04 O.OOE+00 O.OOE+00 0'. OOE+00 O.OOE+00 5.27E-02 0.00 0.41 0.00 0,00 0.11 0,22 0.26 0.00 GAL GAL l.OOE+04 7.SOE+06 l.OOE+00 1 1 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.S9E+02 1.47E+02 -1.36E-01 l.OOE+02 3.00E+02 -2.19E-03 4.07E+04 8.88E+03 -2.05E+01 CLEARUELL STORAGE-BELOW GROUND 3.10E+04 4.22E-01 -2.78E-08 -1.39E-17 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.01 0.00 0.3S 0,17 0.44 0..00 0.03 0.00 CLEARUELL STORAGE-GROUND LEVEL GAL GAL 8.50E+03 9.40E+06 l.OOE+00 1 1 2.70E+04 2.07E-01 -9.72E-09 -3.95E-17 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 DIFFUSED AERATION BASIN 5.43E+04 2.99E+01 -9.75E-05 2.98E+03 1.61E-01 -5.72E-07 O.OOE+00 O.OOE+00 O.OOE+00 1.47E+04 S.73E-01 -2.71E-06 AERATION-AERATION TOWERS 2.45E+04 1.36E+01 -6.96E-05 S.48E+02 7.07E-02 2.19E-07 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 ADHINrLAB S 1.83E+04 1.80E+03 O.OOE+OO 4.16E+04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.71 0.08 0.06 0.01 0.09 0.05 0.00 CU FT CU FT 1.90E+03 3.BOE+05 l.OOE+00 1 1 1.75E-10 -6.46E+02 1.48E+02 3.14E-OS -6.90E-11 8.65E-13 1.30E+03 1.27E-01 -3.12E-07 6.54E-13 0,OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 5.08E-12 0.01 0.61 0.02 0.03 0.16 0.00 0.15 0.02 CU FT CU FT 6.80E+02 2.S6E+05 l.OOE+00 1 1 1.76E-10 -4.02E+03 1.07E+01 -7.18E-06 2.11E-11 •4.83E-13 4.68E+01 1.03E-02 -5.01E-08 1.38E-13 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0,OOE+00 ..... O.OOE+00 0.01 0.67 0.06 0.08 0.14 0.00 0.04 0.00 MAINTENANCE BUILDINGMGD MGD l.OOE+00 2.00E+02 l.OOE+00 1 1 6.96E+03 -5.69E+01 1.65E-01 O.OOE+00 O.OOE+00 O.OOE+00 O.'OOE+OO 2.52E+02 -1.71E+00 4.52E-03 1.28E+03 2.68E+02 -2.42E+00 7.31E-03 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0,OOE+00 O.OOE+00 1.59E+04 -1.30E+02 3.76E-01 0.00 0.00 0.00 0.00 0.00 0.00 0.00 1.00 76 ------- ORV.DAT FILE (CONTINUED) GPM 4.00E+00 1.40E+03 l.OOE+00 1 409 1.81E-02 7.27E+01 1.30E+02 -4.88E-01 1.36E-03 4.70E-04 1.25E+Q3 4.87E+01' -3.26E-01 7.33E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 8.99E-03 0.01 0.44 0.01 0,00 0.09 0.02 0.18 0.25 GPM GPM 8.00E+01 1.40E+03 l.OOE+00 1 409 2.65E-02 -9.69E+01 1.06E+02 -1.38E-01 4.04E-04 1.49E-04 2.68E+03 4.41E+00 3.56E-02 -1.06E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 4.41E-02 0.01 0.22 0.15 0.00 0.08 0.06 0.17 0.31 PACKAGE PRESSURE FILTRATION PLNTGPM GPM 7.00E-01 3.50E+02 l.OOE+00 1 409 1.82E+04 5.01E+03 -1.03E+02 8.27E-01 7.09E+00 1.22E+02 8.55E-01 -1.01E-02 4.64E+01 1.97E+01 -4.43E-01 3.58E-03 3.57E+02 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.40E+04 1.75E+03 6.24E+00 -1.64E-01 0.01 0.43 0.01-0.00 0.13 0.02 0.12 0.28 PACKAGE COMPLETE TREATMENT PLANTBPM 5.70E+04 2.27E+03 -7.84E+00 2.85E+02 3.75E+01 -2.28E-01 O.OOE+00 O.OOE+00 O.OOE+00 2.80E+04 1.98E+03 -4.70E+00 PACKAGE GRAVITY FILTER PLANTS 9.17E+04 1.84E+03 ^-9.25E+00 7.49E+02 1.01E+01 -5.35E-02 O.OOE+00 O.OOE+00 O.OOE+00 9.05E+04 2.20E+03 -1.68E+01 5.17E+00 -6.18E-02 O.OOE+00 O.OOE+00 9.14E-04 O.OOE+00 FILTER MEDIA-RAPID -SAND 4.50E+01 4.71E+01 -1.85E-01 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 FILTER MEDIA-DUAL MEDIA 9.56E+01 5.56E+01 -1.34E-O1 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 FILTER MEDIA-MIXED MEDIA 1.41E+02 8.11E+01 -1.54E-01 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 SO FT SO FT 4.00E+00 2.80E+02 l.OOE+00 1 1 4.30E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 O.OQ 0.00 0.00 SO FT SO FT 4.00E+00 2.80E+02 l.OOE+00 1 1 3.15E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE100 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OO 0.00 0.00 0.00 0.00 0.00 0.00 0.00 SO FT SQ FT 4.00E+00 2.80E+02 l.OOE+00 1 1 2.91E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 FILTER MEDIA-MIXEDrlNST U/MF SUPSQ FT SQ FT 4.00E+00 2.80E+02 l.OOE+00 1 1 1.08E+03 8.91E+01 -2.18E-01 4.42E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO. O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 PACKAGE PRESS DIATOMITE FILTERS GPD GPD 4.43E+04 8.79E-02 1.07E-07 -7.25E-14 1.09E+02 1.66E-03 -2.33E-09 O.OOE+00 O.OOE+00 O.OOE+OO 2.29E+04 9.16E-02 -1.05E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 2.80E+04 l.OOE+06 l.OOE+00 1 402 1.58E+01 4.86E-02 1.39E-10 2.87E-15 1.32E-15 6.27E+02 2.06E-03 -2.20E-09 2.41E-15 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 '6.71E-14 0.01 0.55 0.01 0.01 0.09 0.04 0.05 0.24 GPM PACKAGE VACUUM DIATOMITE FILTERSGPM 4.39E+04 3.15E+02 -4.98E-01 7.10E+01 2.83E+00 -5.79E-03 O.OOE+00 O.OOE+OO O.OOE+00 2.26E+04 1.22E+02 -1-.45E-01 PACKAGE ULTRAFILTRATION PLANTS 9.01E+03 9.28E-01 -8.97E-07 3.08E+01 6.74E-02 1.90E-08 O.OOE+00 O.OOE+OO O.OOE+00 1.01E+04 3.05E-01 -2.48E-07 PACKAGE GRAN ACT CARBON COLUMNS GPD GPD 8.79E+03 3.50E-01 -1.09E-06 1.29E-12 -1 3.00E+01 7.20E+02 l.OOE+00 1 402 4.57E-04 6.00E+03 1.17E+02 7.13E-02 -1.70E-04 4.40E-06 6.54E+02 2.45E+00 -1.36E-03 3.23E--06 O.OQE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 1.09E-04 0.01 0.65 0.01 0.01 0.05 0.05 0.02 0,20 GPD GPD 2.50E+03 l.OOE+06 l.OOE+00 1 302 5.66E-13 1.15E+03 7.39E-02 -4.18E-08 2.75E-14 1.47E-14 3.52E+02 6.76E-04 2.97E-10 -2.26E-16 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO 2.24E-13 0,01 0.64 0.01 0.00 0,07 0.01 0.13 0.13 2.50E+03 5.00E+05 l.OOE+00 1 1 16E+01 5.27E-02 -9.29E-08 1.67E-13 8.11E+01 7.40E-03 1.93E-08 -3.00E-14 9.62E+01 7.32E-04 -1.37E-09 1.12E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 5.27E+03 3.54E-01 -1.09E-06 1.11E-12 0.01 0.25 0.02 0.00 0.22 0.15 0.03 0.32 POTASSIUM PERMANGANATE FEED SYSTLB/DAVLB/DAY l.OOE-01 l.OOE+01 l.OOE+00 1 101 7.36E+03 -9.62E-03 5.00E+01 -6.52E-05 O.OOE+00 O.OOE+OO 2.05E+03 -2.66E-03 POLYMER FEED SYSTEMS 6.09E-04 4.10E-06 O.OOE+00 1.65E-04 8.27E-05 1.80E+03 -2.34E-03 1.49E-04 2.05E-05 5.70E-07 1.01E+02 -1.32E-04 8.18E-06 1.16E-06 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.36E-05 0.00 0.22 O.OO 0.00 0,05 0.05 0.03 0.65 LB/DAYLB/DAY l.OOE-01 l.OOE+01 l.OOE+00 1 110 1.90E+04 -9.51E-03 -1.19E-03 -2.62E-05 1.73E+04 -8.79E-03 -1.07E-03 -2.58E-05 2.40E+02 -1.23E-04 -1.51E-05 -3.20E-07 1.98E+02 -1.04E-04 -1.24E-05 -2.76E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 8.21E+03 -4.17E-03 -5.61E-04 -1.32E-05 O.OO 0.67 0.00 0.00 0.04 0.02 0.07 0.20 POWDERED ACT CARBON FEED SYSTEMSLB/HR LB/HR l.OOE+00 l.OOE+01 l.OOE+00 1 101 2.93E+03 4.68E+02 -5.01E+01 2.29E+00 1.95E+03 1.69E+02 -8.96E+00 9.72E-01 6.91E-02 1.34E+02 7.33E+01 -7.12E+00 3.98E-01 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OO 0.79 0.00 0.00 0.11 0.00 0.10 0.00 LB/DAYLB/DAY l.OOE-01 l.OOE+02 l.OOE+00 . 1 101 4.87E-08 1.63E+03 1.48E-04 6.99E-06 1.85E-08 4.72E-10 1.83E+02 1.64E-05 7.79E-07 2.09E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.93E-08 0.00 0.35 0.00 0.00 0.08 0.03 0.05 0.49 SODIUM HYPOCHLORITE SOLUTN FEED LB/DAYLB/DAY l.OOE-01 1.00E+O2 l.OOE+00 1 101 4.31E+03 3.92E-04 1.84E-05' 4.87E-08 5.70E+02 5.15E-05 2.44E-06 6.37E-09 2.00E+01 1.81E-06 8.51EM>8 2.36E-10 3.6SE+02 3.33E-05 1.55E-06 4.27E-09 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 2.56E+03 2.32E-O4 1.09E-05 2.93E-08 0.00 0.29 0.00 0.00 0.08 0.08 0.05 0.50 3.89E+O1 1.24E+01 -1.12E+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 DIRECT FEED GAS CHLORINATION 4.'31E+03 3.92E-04 1.84E-05 4.00E+01 3.62E-06 1.70E-O7 O.OOE+00 O.OOE+00 O.OOE+00 2.56E+03 2.32E-04 1.09E-05 77 ------- CRV.DAT FILE (CONTINUED) OZONE GENERATING AND FEED LB/DAYLB/DAY S.OOE-01 l.OOE+01 l.OOE+00 1 1 2.10E+04 2.55E+03 -8.76E+00 -3.49E-01 3.78E+02 4.37E+03 -7.69E+00 -3.22E+00 1.11E+02 1.77E+01 1.49E-02 3.37E-04 3.42E+02 5.98E+01 -6.71E+00 2.81E-01 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 6.57E+03 O.OOE+00 O.OOE+00 4.02E-03 -1.14E-03 -4.66E-06 0.00 0.68 0,00 0.00 0.11 0.00 0.00 0.21 GAL GAL 8.50E+02 1.35E+04 l.OOE+00 1 1 -8.89E-09 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.84 0.03 0.01 0.12 0.00 0,00 0.00 OZONE CONTACT CHAMBER 9.27E+02 -3.12E-02 1.84E-04 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 CHLORINE DIOXIDE GENERATING/FEEDLB/DAYLB/DAY l.OOE-01 5.00E+01 l.OOE+00 9.67E+03 7V32E-04 -2.92E-05 l.OOE+02 7.72E-06 -3.08E-07 O.OOE+00 O.OOE+00 O.OOE+00 4.10E+03 3.18E-04 -1.24E-05 ULTRAVIOLET LIGHT DISINFECTION 3.38E+03 3.36E+01 1.58E-03 5.93E-07 1.24E+03 6.05E-09 3.65E+02 O.OOE+00 O.OOE+00 2.52E-07 0.00 0.48 201 9.50E-05 -3.82E-06 7.70E-08 2.78E-05 -1.10E-06 2.22E-08 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.07 0.06 0.05 0,34 5.91E+01 4.07E+00 O.OOE+00 O.OOE+00 9.65E+03 6.48E+00 -3.9OE-03 REVERSE OSMOSIS 9.96E+03 1.41E+00 -1.71E-06 8.34E+00 9.66E-02 O.OOE+00 O.OOE+00 GPM GPM 1.45E-06 3.80E-04 -3.25E-07 O.OOE+00 O.OOE+00 2.54E-09 -1.84E-15 O.OOE+00 O.OOE+00 l.OOE+01 7.80E+02 l.OOE+00 1 1 2.80E+01 4.17E+01 -7.22E-03 7.24E-06 2.31E+01 1.69E-02 3.17E-05 -2.87E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.'OOE+OO 2.08E-06 0.01 0.72 0.02 0.00 0.03 0.04 0.04 0.14 GPD GPD 2.50E+03 l.OOE+06 l.OOE+00 1 302 1.06E-12 1.68E+03 2.65E+00 -6.22E-07 3.79E-13 7.56E+02 3.97E-03 -6.28E-09 3.40E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 7.64E+03 7.78E-02 4.61E-08 -2.63E-14 0.00 0.71 0.00 0.00 0.14 0.00 0.09 0.06 PRESSURE ION EXCHANGE-SOFTENING GPD GPD 7.00E+04 8.60E+05 l.OOE+00 49-4101 5.39E+04 1.59E-01 -1.44E-07 8.54E-14 7.54E+00 1.87E-03 2.87E-10 -2.06E-16 3.89E+02 4.50E-03 -7.15E-10 3.65E-16 8.08E+02 3.01E-03 -3.92E-09 2.21E-15 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 1.02E+04 4.93E-02 -3.67E-08 1.75E-14 0.01 0.32 0.02 0.03 0.10 0.15 0.26 0.11 PRESSURE ION EXCHANG-N03 REMOVALGPD GPD 7.00E+04 8.30E+05 l.OOE+00 121-41O1 5.29E+04 2.16E-01 -1.56E-07 1.03E-13 -1.40E+01 2.03E-03 -4.25E-10 3.07E-16 2.8SE+02 2.32E-02 -3.52E-09 2.49E-15 7.92E+02 3.29E-03 -4.69E-09 2.81E-1S O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.00E+O4 5.2BE-02 -4.35E-08 2.22E-14 0.01 0.49 0.01 0.01 0.06 0.12 0.21 0.09 ACTIVATED ALUMINA FLUORIDE REMOVGPD GPD 1.27E+04 9.10E+05 l.OOE+00 1 202 3.79E+04 2.46E-01 -3.71E-07 2.25E-13 8.07E-01 2.73E-05 -7.66E-11 7.95E-17 2.33E-16 7.75E+02 4.41E-03 -7.96E-09 4.94E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.96E-14 0.00 0.29 0,00 0.00 0.12 0.20 0.29 0.10 GPD GPD 1.63E+04 8.00E+05 l.OOE+00 952-6201 7.81E-14 1.66E+01 1.66E-04 9.52E-10 -7.61E-16 2.31E-15 7.47E+02 3.97E-03 -6.53E-09 4.23E-15 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.86E+04 4.99E-02 1.45E-07 -1.35E-13 0.00 0.33 0.00 0.00 0.13 0.15 0.21 0.18 PACKAGE RAU WATER PUMPING-TDH=50GPM GPM 2.00E+01 7.00E+02 l.OOE+00 1 1 1.04E+04 '6.20E+01 -1.25E-01 1.05E-04 4.81E-01 1.16E+02 8.61E-04 -9.36E-07 4.13E+01 4.71E-01 -1.06E-03 8.36E-07 4.83E+01 1.11E-01 -6.50E-05 7.86E-08 O.OOE+00 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+0'0 0.07 0.59 0.05 0.00 0.17 0.08 0.04 0.00 PACKAGE HIGH SERVICE PUMP STATN GPM GPM 3.00E+01 1.10E+03 l.OOE+00 1 1 1.05E+04 1.32E+01 -1.68E-03 -8.47E-07 -6.08E+02 1.47E+02 1.79E-01 -1.24E-04 2.84E+01 S.46E-02 -4.27E-05 4.00E-08 9.75E+01 1.48E-01 -1.97E-04 9.20E-08 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.80 0.00 0.00 0.12 0.06 0.02 0.00 GAL GAL 5.00E+02 3.00E+04 l.OOE+00 1 1 8.89E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.01 0.00 0.04 0.89 0.06 0.00 0.00 0.00 GPD GPD 6.80E+01 4.11E+04 l.OOE+00 1 7 4.93E-09 4.06E+04 1.10E+01 -2.45E-04 3.41E-09 2.68E+01 3.53E-02 3.98E-06 -7.15E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 3.B9E+02 2.56E-03 -8.74E-10 O.OOE+00 O.OOE+00 O.OOE+00 6.90E+03 3.41E-02 -2.26E-08 BONE CHAR FLUORIDE REMOVAL 5.37E+04 2.18E-01 -1.53E-07 5.21E+02 5.02E-03 -3.36E-09 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 STEEL BACKUASH/CLEARUELL TANKS 9.23E+02 1.36E+00 -4.19E-05 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 LIQUID SLUDGE HAULING 3.97E+04 7.39E+00 -3.13E-04 3.96E+01 1.54E-01 4.04E+01 1.33E-01 5.69E-06 -1.01E-10 5.53E-06 -1.02E-10 O.OOE+00 O.OOE+OO O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 BEUATERED SLUDGE HAULING CY/YR CY/YR l.OOE+02 5.00E+04 l.OOE+00 1 7 2.84E+03 4.26E-01 -1.01E-05 8.12E-11 3.02E+04 8.54E+00 -2.40E-04 2.79E-09 1.92E+02 5.09E-02 3..29E-06 -4.47E-11 6.40E+00 6.09E-02 -1.74E-06 2.62E-11 6.20E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 GPD GPD 5.00E+01 2.50E+04 l.OOE+00 1 11 5.50E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 7.03E+00 1.55E-01 -4.18E-06 O.OOE+00 O.OOE+00 O.OOE+00 SLUDGE DISPOSAL-SANITARY SEWER -1.69E-O2 2.40E-01 -1.63E-06 O.OOE+00 O.OOE+00 O.OOE+00 5.00E+03 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 78 ------- CPU.DAT FILE (CONTINUED) SLUDGE DEUATERING LAGOONS 1.63E+03 2.48E-01 -1.12E-05 4.60E+01 5.63E-O3 -4.40E-O7 1.85E+00 1.06E-02 3.90E-07 O.OOE+00 O.OOE+00 O.OOE+00 SAND DRYING BEDS 9.18E+02 5.80E+00 1.77E-04 3.33E+00 3.33E-02 3.68E-09 2.33E+01 3.33E-02 8.64E-09 O.OOE+00 O.OOE+00 O.OOE+00 CU FT CF/YR 1.50E+03 3.00E+04 S.OOE-01 1 1 2.63E-10 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 1.29E-11 1.49E+01 1.28E-04 1.35E-06 -5.36E-11 -1.74E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 0.31 0.00 0.13 0.00 0.29 0.27 0.00 0.00 SO FT SQ FT 2.00E+02 8.00E+02 l.OOE+00 1 1 -7.98E-07 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 6.99E-13 1.11E+02 2.40E-01 -3.73E-06 1.99E-07 -1.09E-11 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.OOE+00 O.O5 0.00 0.37 0.05 0.24 0.29 0.00 0.00 79 ------- TECHNICAL REPORT DATA (Please read Instructions on the reverse before completing) 1. REPORT NO. EPA-600/2-79-162d 2. 3. RECIPIENT'S ACCESSION NO. 4. TITLE AND SUBTITLE ESTIMATING WATER TREATMENT COSTS Volume 4. Computer User's Manual for Retrieving and Updating Cost Data 5. REPORT DATE August 1979 (Issuing Date) 6. PERFORMING ORGANIZATION CODE 7. AUTHOR(S) Thomas S. Lineck, Robert C. Gumerman, and Russell L. Gulp 8. PERFORMING ORGANIZATION REPORT NO. 9. PERFORMING ORGANIZATION NAME AND ADDRESS Culp/Wesner/Culp Consulting Engineers 2232 S.E. Bristol, Suite 210 Santa Ana, California 92707 1O. PROGRAM ELEMENT NO. 1CC614, SOS 1, Task 38 11. CONTRACT/GRANT NO. 68-03-2516 12. SPONSORING AGENCY NAME AND ADDRESS Municipal Environmental Research Laboratory—Gin.,OH Office of Research and Development U.S. Environmental Protection Agency Cincinnati, Ohio 45268 13: TYPE OF REPORT AND PERIOD COVERED Final 14. SPONSORING AGENCY CODE EPA/600/14 15. SUPPLEMENTARY NOTES Proj ect Officer: Robert M. Clark See also EPA-600/2-78-182 (NTIS PB284274/AS); Volume 1, Volume 2, EPA-600/2-79-162b; and Volume 3, EPA-600/2-79- (513) 684-7488. EPA-600/2-79-162a; •162c. 16. ABSTRACT This report discusses unit processes and combinations of unit processes that are capable of removing contaminants included in the National Interim Primary Drinking Water Regulations. Construction and operation and maintenance cost curves are presented for 99 unit processes that are considered to be especially applicable to contaminant removal. The report is divided into four volumes. Volume 1 is a summary volume. Volume 2 presents cost curves applicable to large water supply systems with treatnnent capacities between 1 and 200 mgd, as well as information on virus and asbestos removal. Volume 3 includes cost curves applicable to flows of 2,500 gpd to 1 mgd. And Volume 4 is a computer program user's manual for the curves included in the report. For each unit process included in this report, conceptual designs were formulated, and construction cost curves were checked for accuracy by a second consulting engineering firm, Zurheide-Herrmann, Inc., using cost-estimating techniques similar to those used by general contractors in preparing their bids. Operation and maintenance requirements were determined individually for three categories: Energy, maintenance material, and labor. Energy requirements for the building and the process are presented separately. Costs are in October 1978 dollars. 17, KEY WORDS AND DOCUMENT ANALYSIS DESCRIPTORS b.lDENTIFIERS/OPEN ENDED TERMS c. cos AT I Field/Group Economic analysis, Environmental engineering, Operating costs, Computer programming, Water treatment, Cost indexes, Water supply, Cost estimates, Cost analysis Energy costs, Cost curves, Safe Drinking Water Act, Interim primary standards, Unit processes, Treatment efficiency 13B 18. DISTRIBUTION STATEMENT Release to Public 19. SECURITY CLASS (ThisReport) Unclassified 21. NO. OF PAGES 88 20."SECURITY CLASS (Thispage) Unclassified 22. PRICE EPA Form 2220-1 (Rev. 4-77) 80 •AT U.S. GOVERNMENT PRINTING OFFICE: 1980--757-064/0174 -------


&EPA
            United States
            Environmental Protection
            Agency
            Municipal Environmental Research
            Laboratory
            Cincinnati OH 45268
EPA-600/2-79-162d
August 1979
            Research and Development
Estimating Water
Treatment Costs

Volume 4
Computer User's
Manual for
Retrieving  and
Updating Cost Data

-------
                 RESEARCH  REPORTING SERIES

 Research reports of the Office of Research and Development, U.S. Environmental
 Protection Agency, have been grouped into nine series. These nine broad cate-
 gories were established to facilitate further development and application of en-
 vironmental technology. Elimination  of  traditional grouping was  consciously
 planned to foster technology transfer and a maximum interface in related fields.
 The nine series are:

      1.   Environmental Health Effects Research
      2.   Environmental Protection Technology
      3.   Ecological Research
      4,   Environmental Monitoring
      5.   Socioeconomic Environmental Studies
      6.   Scientific and Technical Assessment Reports (STAR)
      7.   Interagency Energy-Environment Research and Development
      8.   "Special" Reports
      9.   Miscellaneous Reports

 This report has been assigned to the ENVIRONMENTAL PROTECTION TECH-
 NOLOGY series. This series describes research performed to develop and dem-
 onstrate instrumentation, equipment,  and methodology to repair or prevent en-
 vironmental degradation from point and non-point sources of pollution. This work
 provides the new or improved technology required for the control and treatment
 of pollution-sources to meet environmental quality standards.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia 22161.

-------
                                      EPA-600/2-79-162d
                                      August  1979
     ESTIMATING WATER TREATMENT COSTS

   Volume 4.   Computer User's Manual for
     Retrieving and Updating Cost Data
                    by

             Thomas S. Lineck
            Robert C.  Gumerman
              Russell  L.  Gulp

             Gulp/Wesner/Gulp
           Consulting  Engineers
       Santa Ana, California  92707
          Contract No. 68-03-2516
              Project Officer

              Robert M. Clark
     Drinking Water Research Division
Municipal Environmental Research Laboratory
          Cincinnati, Ohio  45268
MUNICIPAL ENVIRONMENTAL RESEARCH LABORATORY
    OFFICE OF RESEARCH AND DEVELOPMENT
   U.S. ENVIRONMENTAL PROTECTION AGENCY
          CINCINNATI, OHIO  45268

-------
                                 DISCLAIMER
     This report has been reviewed by the Municipal Environmental Research
Laboratory, U.S. Environmental Protection Agency, and approved for publica-
tion.  Approval does not signify that the contents necessarily reflect the
views and policies of the U.S. Environmental Protection Agency, nor does
mention of trade names or commercial products constitute endorsement or
recommendation for use.
                                     ii

-------
                                  FOREWORD
     The U.S. Environmental Protection Agency (EPA) was created because of
increasing public and government concern about the dangers of pollution to
the health and welfare of the American people.  Noxious air, foul water, and
spoiled land are tragic testimonies to the deterioration of our natural
environment.  The complexity of that environment and the interplay of its
components require a concentrated and integrated attack on the problem.

     Research and development is that necessary first step in problem
solution, and it involves defining the problem, measuring its impact, and
searching for solutions.  The Municipal Environmental Research Laboratory
develops new and improved technology and systems to prevent,  treat,  and
manage wastewater and solid and hazardous water pollutant discharges from
municipal and community sources to preserve and treat public drinking water
supplies, and to minimize the adverse economic, social, health, and aesthetic
effects of pollution.  This publication is one of the products of that
research—a most vital communications link between the researcher and the
user community.

     The cost of water treatment processes that may be used by water supply
systems to remove contaminants included in the National Interim Primary
Drinking Water Regulations is of interest to the EPA, State and local agencies,
and consulting engineers.  This volume contains documentation and user
information for the WATER program, a FORTRAN computer program that retrieves
and updates cost information for the 72 large-system unit processes and
the 27 small system processes presented in Volumes 1, 2, and 3 of this
report.  The WATER program is capable of determining costs for individual
processes and complete treatment plants.
                                      Francis T. Mayo
                                      Director
                                      Municipal Environmental Research
                                        Laboratory
                                     iii

-------
                                   ABSTRACT

    This volume is the fourth in a series of four reports on estimating costs
for water treatment as a function of system size and treatment efficiency.
Volume 4 is a computer users manual and contains a FORTRAN computer program,
WATER, that can be used for retrieval and updating of all cost data
contained in the Volumes 1, 2 and 3.  Volume 1 is the summary volume and
discusses the cost estimating approaches utilized to develop the cost curves
and the treatment techniques applicable for contaminant removal.  It also
presents a series of examples demonstrating the use of the cost curves
applicable to large water supply systems with treatment capacities between
1 and 200 mgd.  Information is included on virus and asbestos removal.
Volume 2 presents cost curves for large water systems (1 to 200 mgd), and
Volume 3 presents cost curves for small systems (2,500 gpd to 1 mgd).

    The WATER program determines costs by retrieving stored coefficients for
a least squares polynomial fit of the cost curves presented in Volumes 1,
2, and 3, and by evaluating the polynomial expression for the desired process
design parameter.  Cost information is presented for construction and
operation and maintenance, including energy, maintenance material and labor.
The conceptual designs and assumptions used in formulating the cost information
are presented in Volumes 1, 2, and 3.
    The program will compute costs for individual processes or for a series
of processes.  Capital costs are determined from construction costs by
applying cost factors (input by the user) for engineering, sitework, sub-
surface considerations, land, and standby power.  The program computes general
contractor overhead and profit, legal, fiscal, and administrative fees, and
interest during construction based on the overall cost of the project.

    All construction costs are stored in terms of October 1978 dollars, and
are updated by one of two methods, determined by the user.  The program
computes a weighted composite cost index for each process, using eight
individual cost indices for excavation and sitework, manufactured equipment,
concrete, steel, labor, pipe and valves, electrical equipment and instrumenta-
tion, and housing - or the user may specify updating by use of the Engineering
News Record Construction Cost Index.  Operation and maintenance costs are
determined from unit costs (input by the user) such as dollars per hour for
labor and dollars per kilowatt hour for electricity.  Maintenance material
costs are stored as dollars per year and are updated using the Bureau of
Labor Statistics Price Index.
    The user need not be an experienced programmer, but a familiarity with
programming is recommended.  This report was submitted in fulfillment of
Contract No. 68-03-2516 by Gulp/Wesner/Gulp under the sponsorship of the
U.S. Environmental Protection Agency.  This report covers the period November
1, 1976 to January 1, 1979.  It was completed as of July 2, 1979.
                                      iv

-------
                                  CONTENTS
Foreword ....
Abstract ....
Figures  ....
Tables 	
Acknowledgements
    1. Introduction  	
    2. Input Data Files  	
    3. COST.DAT File Construction
    4. PROCES.DAT File Construction
    5. Program Output  	
    6. Examples  	
    7. Trouble Shooting Guide  . .   .
    8. WATER Program Listing . . .   .
    9. CRV.DAT File  	
iii
 iv
 vi
 vi
vii

  1
  3
  6
  9
 34
 36
 57
 58
 70

-------
                                   FIGURES

Number                                                            Page

    1     PROCES.DAT Data Segments                                  17

    2     Land Requirements for Conventional Plants                 18

    3     Land Requirements for Package Complete Treatment Plants   19
Number

   1

   2

   3

   4


   5

   6
                          TABLES



COST.DAT File Example

PROCES.DAT File Example

Card-by-Card Explanation of COST.DAT File

Process Cost Curves for Large and Small Water Treatment
  Systems

Processes That Use Chemicals and Chemicals Used

Process Parameter Units
Page

  4

  5

  6


 10

 15

 22
                                 vi

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                              ACKNOWLEDGEMENTS
    This report was prepared under the direction of Dr. Robert M. Clark,
Municipal Environmental Research Laboratory, Office of Research and
Development.  The report was prepared by Robert C. Gumerman, Russell L. Gulp,
Sigurd P. Hansen, Thomas S. Lineck, and Bruce E. Burris of Gulp/Wesner/Gulp.
Ms. Karin J. Wells of Gulp/Wesner/Gulp was responsible for typing of the
final report.

    Mr. Ronald M. Dahman of Zurheide-Herrmann, Inc., was responsible for
checking all unit costs.  Dr. Isadore Nusbaum and Mr. Dean Owens were
respective sub-consultants on the reverse osmosis and ion exchange curves.

    Special acknowledgement is given to Mr. Keith Carswell, Dr. Robert M.
Clark, Mr. Jack De Marco, Dr. Gary Logsdon, Dr. 0. Thomas Love, Mr. Benjamin
Lykins, Jr., Mr. Thomas J. Sorg, all of the EPA Municipal Environmental
Research Laboratory, who reviewed the final report, and Mr. Paul Dorsey,
also of the EPA Municipal Environmental Research Laboratory, who reviewed
the computer program.

    Mrs. Anne Hamilton was the technical editor for all four volumes of
this reportx ,                   .
                                     vii

-------

-------
                                  SECTION 1

                                INTRODUCTION
SCOPE

     This report is Volume 4 of a four-volume study that presents construction
and operation and maintenance cost curves for 99 unit processes that are
especially applicable (either individually or in combination) to the removal
of contaminants listed in the National Interim Primary Drinking Water
Regulations.  This volume is a computer users manual and contains documenta-
tion and user information for the WATER program, which is a FORTRAN computer
program that retrieves and updates cost information for the 72 large and 27
small water supply systems presented in Volumes 1, 2, and 3 of this report.
Costs are also determined for treatment plants, and they are input to the
program as trains of individual processes.

BACKGROUND

     The WATER program described here can be used as a valuable tool to
facilitate retrieval and updating of the cost information presented in
Volumes 1, 2, and 3 of this report.  Since WATER has been designed to compute
costs for entire treatment plants, cost determinations for competing treatment
trains or regional variations in operating costs for a particular treatment
train can be made quickly and accurately.

     The costs generated by this program are broken down into capital costs
and operation and' maintenance costs.  Capital costs include those for
construction, engineering, sitework and interface piping, subsurface considera-
tions, standby power, legal, fiscal and administrative services, interest
during construction, and land.  Operation and maintenance costs include those
for electricity, labor, maintenance materials, diesel fuel, natural gas, and
chemicals.  Most costs are stored as coefficients of third-degree polynomial
expressions determined by the method of least squares for the values in the
cost tables presented in Volumes 1, 2, and 3.  Therefore, the cost generated
for a specific point in these tables could vary by as much as 10 to 15
percent from the value generated by the program, depending on the deviation
of the values in the table from a smooth curve fit.  In general, the
'differences between the costs generated by the program and the costs obtained
through use of the cost curves in Volumes 1, 2, and 3, will be insignificant.

     The user need not be an experienced programmer, but a familiarity
with programming is recommended.

-------
PURPOSE AND OBJECTIVES

     The purpose of this volume is to present complete documentation and
user information for the FORTRAN computer program, WATER, which retrieves
and updates cost information for the large and small water supply treatment
processes presented in Volumes 1, 2, and 3 of this report.  The WATER
program has been designed to facilitate the estimation of overall treatment
plant costs as well as individual process costs.

-------
                                  SECTION 2

                              INPUT DATA FILES
     Three data files are necessary to run this program.   Two of these files,
COST.DAT and PROCES.DAT, are set up by the user.  The third data file,
CRV.DAT, is a construction and operation and maintenance data base containing
information about each of the water treatment processes considered in this
report.  This file is an integral part of the program and must be established
on the computing system with the main program.  Once it is established,
the general user should have no need to access the main program, WATER, or
the data base, CRV.DAT.

     The first of the two data files to be constructed by the user is the
COST.DAT file.  Table 1 is an example listing of the COST.DAT file.  This
file basically contains all the cost information necessary to run the
program.  The variables in this file, called cost factors, must be input
in the sequence shown in Table 1.  A detailed explanation of the input
format is given in the following section on COST.DAT File Construction.

     The second file to be constructed by the user is the PROCES.DAT file.
Table 2 is an example listing of the PROCES.DAT file.  This file contains
information about each of the water treatment processes for which the user
desires costs.  A detailed explanation of the input format is given in a
following section entitled, PROCES.DAT File Construction.

-------
      Table 1

COST.DAT File Example
COSTS PRESENTED ARE CURRENT AS OF OCTOBER 1978
CAPITAL COST FACTORS  (X OF CONSTRUCTION COST)*
 1 ENGINEERING(X)                =10*
 2 SITEUORK, INTERFACE PIPING(%) =5*
 3 SUBSURFACE CONSIDERATIONS(%)  =0*0
 4 STANDBY POWER(%)              =0*0
 5 INTEREST RATE(%>              =7*
 6 NUMBER OF YEARS               =20*0
 7 LAND COST, */ACRE             =2000*
UNIT COST FACTORS:
 8 ELECTRICITY, */KWH            = *03
 9 LABOR, $/HR                   =10*
10 DIESEL FUEL, $/GAL            =*45
11 NATURAL GAS, $/CU FT          =»0013
12 BLDNG ENERGY USE,KWH/SQ FT/YR =102*6
COST INDEXES:
13 EXCAVATION(ENR SKILLED LABOR)
14 MANUFACTURED EQUIP (BLS #114)
15 CONCRETE (BLS #132)
16 STEEL (BLS #101,3)
17 LABOR (ENR SKILLED LABOR)
18 PIPE S VALVES (BLS #114*901)
19 ELECTRICAL S INSTR (BLS #117) =167*5
20 HOUSING (ENR BUILDING COST)    =254*76
21 PRODUCER PRICE INDEX          =199*7
22 ENR CONSTRUCTION, '67 BASE YR =0*0
OUTPUT(6 FOR LP,5 FOR TELETYPE)  -5
PRINTOUT(DETAILED OR SUMMARY)     "SUMMARY
9,2
7*5,12*5
=247*0
=221*3
=221
=262
=247
                      1
                      1
                      0

-------
                  Table 2

           PROCES.DAT File Example
ACRES=1*5
1,57,IN-PLANT PUMPING
2,5*0,3*5,7*5,3*5
3,75 * 0, TDH
1,60,PRESSURE ION EXCHANGE-SOFTENING
2,5,0,3*5,5*0,3*5
3,30*6,REGENERATION SALT
1,15,SODIUM HYDROXIDE FrEE» SYSTEMS
2>5*0*3*5,625*0,438*0
3,200*0,SODIUM HYDFi'OXiriE, 15 MG/L
lil9CL2 FEED-CYLINDER STORAGE
2,5*0,3*5,63*0,44*0
3,300*0,CHLORINE,1*5 MG/L
1,95,CLEARWELL STORAGE-GROUND LEVEL
2,5*0,3*5,500000 * 0,500000 * 0
1,93,FINISHED WATER PUMPING FACILITY
2,5*0,3*5,8*0,3*5
3,200*0,TDH
000000000000000000000000000000000000000000
ACRES~0*0
1?11,LIME FEED-NO RECALCINATION
2,1*0,0*7,8.7,6*1
3,65*0,LIME,25 MG/L

-------
                                ,  SECTION 3

                         COST.DAT FILE CONSTRUCTION
     To aid in understanding the format of this data file, the user is
referred to Table 1, which must be constructed as shown.  Cards 2, 10,
and 16 are for user information only and are skipped by the program when
reading this file.  They must not be omitted, however, or the program will
skip actual data.  A card-by-card explanation of this file is given in
Table 3.

                                   Table 3
                  Card-by-Card Explanation of COST.DAT File
Card No.
     3-9
     10

     11-15




     16
                           Explanation

First 48 characters printed "as is" on the program output.
Intended to be used to denote valid data of cost information
produced.
                For user information only.
                program.
                            This line is skipped by the
Capital cost factors as shown.  Program read skips the first
34 characters then reads floating point number input.  These
values must start in Column 35 and must contain a decimal
point.  Percentage values, as indicated, must be percentages,
not decimal values.  Example:  Engineering must be listed
as 10.0 for 10 percent, not as 0.10.  The program internally
divides by 100.

For user information only - skipped by program read.

Unit cost factors as shown.  As with lines 3-9, program
read skips the first 34 characters.  Values must begin in
Column 35 and must contain decimal points.  Units are as
shown in Table 1.

For user information only - skipped by program read.

-------
Card No.
   17-26
   27
   28
   29-30
                  Explanation (continued)

Cost indices as shown.  As with lines 3-9 and 11-15, program
read skips the first 34 characters.  Values must hegin in
Column 35 and must contain decimal points.  These cost
indices are used to update the cost data base stored in the
CRV.DAT file.  The user has the option of using the first
eight cost indices listed (Excavation through Housing) to
update the construction costs produced by the program, or
he can use the ENR Construction Cost Index (line 26) in
lieu of the first eight indices.  Thfe computer will use the
ENR Construction Cost Index if the value input is greater
than zero.  If the value input for the ENR Construction Cost
Index is equal to zero, the computer will use the first
eight indices.

This card designates the location for program output.  On
most computer installations, a "5" designates the teletype
or remote terminal.  The program output is 132 characters wide,
so it is suggested that the line printer be used if the
teletype does not have the capacity to print 132 characters
per line.  The value for this variable must be an integer and
must begin in Column 35.

This card designates a detailed or summary output.  See
sections 5 (Program Output) and 6 (Examples) for an
explanation and sample of these options.

These cards are optional.  The user may wish to run the
program while varying only one of the cost factors in the
COST.DAT file.  Cost factors are numbered 1 through 22 for
convenience.  For example, cost factor number 9 is labor
($/hr).  Thus if the user wants to determine the change in
overall operations and maintenance cost based on the regional
variation of the cost of electricity across the nation, he
first inputs in card 29 the number of the cost factor and
the additional number of values to be used for that cost
factor.  In this case, cards 29 and 30 are as follows for
two additional values of cost factor number 9:
                                      Card 29:
                                      Card 30:
                                9,2
                                7.5,12.5
                Card 30 contains the two additional values of labor ($/hr)
                namely, 7.5 and 12.5.

                Note that all input values begin in column one for lines
                29 and 30, and that they are separated by a comma.

                Up to 10 additional values may be input.  They must be
                floating point numbers with decimal points, but they can
                appear in any column as long as they are separated by a comma.

-------
Card No.
Explanation (continued)
 29-30         Cards 29 and 30 shown in the listing of the COST.DAT file in
continued      Table 1 accomplish the following:  The program computes all
               costs with the cost of labor ($/hr) at 10.  Then the program
               is automatically rerun twice with the cost of labor ($/hr)
               at 7.5 and 12.5.  This produces three complete printouts.

               If the user wants to run the program only once, without
               varying any of the 22 cost factors, cards 29 and 30 are
               omitted, and the designation of DETAILED or SUMMARY printout
               is the last card of the COST.DAT file.

-------
                                  SECTION 4

                        PROCES.DAT FILE CONSTRUCTION
     The PROCES.DAT file contains design and operating information about
each of the processes for which the user may desire costs.  Table 4 lists
the processes for which costs are available and includes the process
parameter range over which cost information is stored in the computer.
For example, process 1 CL2 FEED - CYLINDER STORAGE, has cost information
stored in the program data file over a range of 10 to 10,000 Ib/day of
chlorine feed.  Also shown in Table 4 are the number of chemicals used in
the treatment process, the process type and the number of data cards.

     Chemical cost information is input along with process design and
operating parameters, as explained later.  The number of chemicals used
in the process is listed in Table 4, and in most cases, the types of
chemicals used will be obvious (for example, chlorine is used in process
1, CL2 FEED - CYLINDER STORAGE).  For convenience, however, Table 5 lists
the processes that use chemicals and the chemicals used.

     The Process Type listed in Table 4 denotes the way in which information
is input to the computer, and the number of data cards indicates the number
of cards necessary to input information for that process.  There are a total
of 11 process types.  The input data for each type are described later in
this section.

     Since the computer program is designed to determine individual process
costs and plant costs by totaling the process costs, the PROCES.DAT file
is assembled into what is here termed loosely as "segments" of data
(Figure 1).

THE ACRES= CARD

     Each data segment corresponds to a treatment plant and must begin with
the ACRES= card.  This card denotes the land area, in acres, required for
the plant.  If land costs are not to be included, the card should read
ACRES=0.0, with the "A" in acres beginning in Column 1.  For convenience,
typical land area requirements are shown in Figures 2 and 3.

PROCESS DATA  CARDS

     Following the ACRES= card, data cards for the processes in the plant
are assembled sequentially.  There may be as many processes as desired,  in
any order, and processes may be input more than once.  The set of process
data cards preceded by the ACRES= card constitutes a segment of data
 (Figure 1).

                                      9

-------
                                             Table 4
        Process  Cost Curves for Large  and Small  Water  Treatment  Systems
   TREATMENT PROCESS - LARGE SYSTEMS

  1 CL2 FEED-CYLINDER STORAGE
  2 CL2 FEED-ON SITE STORAGE TANK
  3 CU2 FEED FROM RAIL CAR
  4 CHLORINE DIOXIDE GENERATING»FEED
  5 OZONE GENERATION SYSTEMS
  A OZONE CONTACT CHAMBER
  7 ON-SITE HYPOCHLORITE GENERATION
  B AI.UH FEED-LIOUID STOCK
  9 ALUM FEED-DRY STOCK
 10 POLYMER FEED SYSTEMS
 11 LIME FEED-NO RECALCINATION
 12 LIME FEED-UITH RECALCINATION
 13 POTASSIUM PERMANGANATE FEED
 14 SULFURIC ACID FEED SYSTEMS
 IS SODIUM HYDROXIDE FEED SYSTEMS
 16 FERROUS SULFATE FEED SYSTEMS
 17 FERRIC SULFATE FEED SYSTEMS
 18 ANHYDROUS AMMONIA FEED FACILITY
 19 AQUA AMMONIA FEED FACILITY
 20 POWDERED ACTIVATED CARBON FEED
 21 RAPID HlXr  0=300
 22 RAPID HlXr  G-600
 23 RAPID MIXr  G=900
 24 FLOCCULATION-HORIZ PADDLEr  G=20
 25 FLOCCULATION-HORIZ PADDLEf  G=50
24 FLOCCULATION-HORIZ PADDLEr  G=BO
27 FLOCCULATION-VERT  TURBINE.  G=20
28 FLOCCULATION-VERT  TURBINE.  G=50
PARAMETER RANGE
10.0
2000.0
2OOO.O
10.0
10,0
460.0
10.0
5.4
10.0
1.0
10,0
1000.0
1.0
10,0
10.0
10.7
13.3
250.0
250.0
3.5
100.0
100.0
100.0
1800.0
1800.0
1800.0
1800.0
1800.0
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
10000
10000
10000
3500
3500
92000
10000
5400
5000
200
1000
10000
500
5000
10000
5350
6600
5000
5000
7000
20000
20000
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
20000.0
1000000.0
1000000.0
500000,
.0
25000.0
25000.
,0
NUMBER OF
CHEMICALS
LB/DAY
LB/DAY
LB/DAY
LB/DAY
LB/DAY
CU FT
LB/DAY
LB/HR
LB/HR
LB/DAY
LB/HR
LB/HR
LB/DAY
GPD
LB/DAY
LB/HR
LB/HR
LB/DAY
LB/DAY
LB/HR
CU FT
CU FT
CU FT
CU FT
CU FT
CU FT
CU FT
CU FT
1
1
1
2
0
0
1
1
.1
1
1
1
1
1
1
1
1
1
1
1
0
0
0
0
0
0
0
0
PROCESS
TYPE
1
1
1
1
1
1
1
1
1
10
1
8
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
NO. 1
CAR)
3
3
3
4
2
2
3
3
3
3
3
4
3
3
3
3
3
3
3
3
2
2
2
2
2
2
2
2
                                                   10

-------
                                       Table  4  (Continued)
   TREATMENT PROCESS - LARGE SYSTEMS


29 FLOCCULATION-VERT TURBINE, G=80

30 CIRCULAR CLARIFIER-LIME SLUDGE

31 CIRC CLARIFIER-FECL3 & ALUM SLDG

32 RECTANGULAR CLARIFIER-LIME SLDG

33 RECT CLARIFIER-FECL3 X ALUM SLG

34 UPFLOW SOLIDS CONTACT CLARiG=70

35 UPFLOW SOLIDS CONTACT CLAR»G=11O

36 UPFLOW SOLIDS CONTACT CLAR>G=150

37 TUBE SETTLING MODULES

38 GRAVITY FILTRATION STRUCTURE

39 FILTRATION MEDIA-RAPID SAND

40 FILTRATION MEDIA-DUAL MEDIA

41 FILTRATION MEDIA-MIXED MEDIA

42 BACKWASH PUMPING FACILITIES
        OSM!

43 HYDRAULIC SURFACE WASH SYSTEMS

44 AIR-WATER BACKWASH FACILITIES

45 WASH WATER SURGE BASINS

46 FILTER MOD-RAP SAND TO HIGH RATE

47 CONTINUOUS AUTO. BACKWASH FILTER

48 RECARBONATION BASIN

49 RECARBONATION-LIQUin C02  FEED

50 RECARB-C02 FROM  SUBMERGED BURNER

51 RECARBONATION-C02  FROM STACK GAS

52 MULTIPLE HEARTH  RECALCINATION

53 CONTACT  BASIN-DIRECT FILTRATION

54 PRESSURE DIATOMITE FILTERS

55 VACUUM  DIATOMITE FILTERS
PARAMETER RANGE
1800.0
707.0
707.0
240.0
240.0
255.0
255.0
255. 0
280.0
140.0
370.0
140.0
140.0
1260.0
1537.2
140.0
140.0
10000.0
140.0
360.0
770.0
380.0
500.0
25OO.O
179.0
2640.0
1.0
1.0
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
25000.0
31400.0
31400.0
4800.0
4800.0
14500.0
14500.0
14500.0
56000.0
28000.0
74800.0
29900.0
29900.0
23000.0
28060.0
28000.0
28000.0
500000.0
28000.0
70400.0
35200.0
15000.0
10000.0
50000.0
2930.0
528OO.O
200.0
200.0
NUMBER OF
CHEMICALS
CU FT
SQ FT
SO FT
SQ FT
SQ FT
SQ FT
SQ FT
SQ FT
SQ FT
SQ FT
SQ FT
SQ FT
SQ FT
GPM
SQ FT
SQ FT
SQ FT
GAL
SQ FT
SQ FT
CU FT
LB/DAY
LB/DAY
LB/DAY
SQ FT
CU FT
MGD
MGD
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
o
0
0
0
1
0
0
0
0
3
3
PROCESS
TYPE
1
3
3
3
3
3
3
3 .
1
1
1
1
1
1
1
1
1
1
1
3
1
3
1
3
3
2
2
NO. D
CARD
2
3
3
3
3
3
3
3
2
2
2
2
2
2
2
2
2
2
2
3
3
3
2
3
3
5
5
                                                   11

-------
                                        Table 4  (Continued)
    TREATMENT PROCESS - LARGE SYSTEMS
 56  PRESSURE FILTRATION PLANTS
 57  IN-PLANT PUMPING
 SB  WASH UATER STORAGE TANKS
 59  REVERSE OSMOSIS
 60  PRESSURE ION EXCHANGE-SOFTENING
 61  GRAVITY ION EXCHANGE-SOFTENING
 62  PRESSURE ION EXCHANG-N03 REMOVAL
 63  ACTIV, ALUMINA-FLUORIDE REMOVAL
 64  GRAVITY GAC CONTACTORS-CONCRETE
        OIH:
 65  GRAVITY GAC CONTACTORS-STEEL
        OIH:
 66  PRESSURE CARBON CONTACTORS
        OXM:
 67  CONVERT FILTER TO GAC CONTACTOR
 68  GRANULAR ACT CARBON-CONSTR COST
 69  MAKEUP CARBON COST-OSM ONLY
 70  CAPPING SAND FILTER W/ANTHRACITE
 71  REGIONAL GAC REGEN-TRANS S STOR
        OIH:
 72  REGIONAL HULTI HEARTH GAC REGEN
 73  MULTIPLE HEARTH GAC REGENERATION
 74  INFRARED CARBON REGEN FURNACE
 75  FLUIDIZED BED GAC REGENERATION
 76  POWDERED CARD REGEN-FLUIDIZED BD
 77  POWDERED CARB REGEN-ATOHIZED SUS
 78 CHEN SLUDGE PUHPING-UNTHICKENED
 79 CHEH SLUDGE PUMPING-THICKENED
 80 GRAVITY SLUDGE THICKENER-LIME
SI GRAV SLDO THICKENER-ALUM S FECL3
PARAMETER RANGE
140.0
1.0
21000.0
1.0.
1.1
1.5
1.1
0.7
350.0
140.0
6280.0
31400.0
390.0
157.0
370.0
10000.0
10000.0
350.0
1000.0
30000.0
27. 0
27.0
2400.0
6000.0
209.0
1000.0
20.0
5.0
314.0
314.0
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
28000.0
200.0
900000.0
200.0
123.0
150.0
12.3
135.0
10600.0
28000.0
14100.0
628000.0
2260.0
6790.0
70000.0
10000000.0
10000000.0
70000.0
20000.0
3000000.0
1510.0
1510.0
60000.0
24000.0
33400.0
1000O.O
10000.0
1250.0
17800.0
17800.0
SO FT
MGD
GAL
MGD
MGD
MGD
MGD
MGD
CU FT
SO FT
CU FT
CU FT
CU FT
SO FT
SO FT
LB
LB/YR
SO FT
CU FT
LB/YR
SQ FT
SQ FT
LB/DAY
LB/DAY
LB/DAY
LB/DAY
GPM
GPM
SQ FT
SQ FT
NUMBER OF
CHEMICALS
0
0
0
3
1
1
1
2
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
PROCESS
TYPE
1
5
1
2
1
1
1
2
4
4
4
1
1
1
1
6
12
3
1
3
1
1
1
1
3
3
NO. ]
CAR]
2
3
2
5
3
3
3
4
3
3
3
2
2
2
2
3
4
3
2
3
2
2
2
2
3
3
                                                   12

-------
                                        Table 4  (Continued)
    TREATMENT  PROCESS  -  LARGE SYSTEMS


 82 VACUUM FILTERS

 83 BELT FILTER  PRESS

 84 FILTER PRESS

 85 DECANTER CENTRIFUGES

 86 BASKET CENTRIFUGES

 87 SAND DRYING  BEDS

 88 SLUDGE DEUATERING  LAGOONS
         OSM!

 89 SLUDGE DISPOSAL-SANITARY SEWER

 90 LIQUID SLUDGE HAULING

 91 DEUATERED  SLUDGE HAULING

 92 RAW WATER  PUMPING  FACILITY

 93 FINISHED WATER  PUMPING  FACILITY

 94 CLEARWELL  STORAGE-BELOW GROUND

 95 CLEARWELL  STORAGE-GROUND LEVEL

 96 DIFFUSED AERATION  BASIN

 97 AERATION-AERATION  TOWERS

 98 ADMINrLAB  &  MAINTENANCE BUILDING


    TREATMENT  PROCESS  -  SMALL SYSTEMS


 99 PACKAGE COMPLETE TREATMENT PLANT

100 PACKAGE GRAVITY FILTER  PLANTS

101 PACKAGE PRESSURE FILTRATION PLNT

102 FILTER MEDIA-RAPID SAND

103 FILTER MEDIA-DUAL  MEDIA

104 FILTER MEDIA-MIXED MEDIA

105 FILTER MEDIA-MIXEDrINST U/MF SUP

106 PACKAGE PRESS DIATOMITE FILTERS
PARAMETER RANGE
9.4
15.0
4.3
10.0
3600.0
5000.0
40000.0
25000.0
20.0
1.3
1000.0
1.0
1.5
10000.0
8500.0
1900.0
680.0
1.0
4.0
80.0
0.7
4.0
4.0
4.0
4.0
28000.0
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
1320.0
450.0
896.0
500.0
720000.0
40OOOO.O
8000000.0
5000000.0
10000.0
100.0
300000.0
200.0
300.0
7500000.0
9400000.0
380000.0
256000.0
200.0
1400.0
1400.0
350.0
280.0
280.0
280.0
280.0
1000000.0
SQ FT
GPM
CU FT
GPM
GPD
SO FT
CU FT
CF/YR
GPM
MG/YR
CY/YR
MGD
MGD
GAL
GAL
CU FT
CU FT
MGD
GPM
GPM
GPM
SQ FT
SQ FT
SQ FT
SQ FT
GPD
NUMBER OF
CHEMICALS
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
4
4
4
0
0
0
0
4
PROCESS
TYPE
1
1
1
3
1
1
1
11
7
7
5
5
1
1
1
1
1
9
9
9
1
1
1
1
2
NO. i
CAR]
2
2
2
3
2
2
2
3
3
3
3
3
2
2
2
2
2
7
7
7
2
2
2
2
6
                                                    13

-------
                                        Table 4  (Continued)
    TREATMENT PROCESS - SMALL SYSTEMS

107 PACKAGE VACUUM DIATOMITE FILTERS
108 PACKAGE ULTRAFILTRATION PLANTS
109 PACKAGE GRAN ACT CARBON COLUMNS
110 POTASSIUM PERMANGANATE FEED SYST
111 POtYMtR FEED SYSTEMS
112 POWDERED ACT CARBON FEED SYSTEMS
113 DIRECT FEED GAS CHLORINATION
111 SODIUM HYPOCHLORITE SOLUTN FEED
115 OZONE GENERATING AND FEED
116 OZONE CONTACT CHAMBER
117 CHLORINE DIOXIDE GENERATING/FEED
118 ULTRAVIOLET LIGHT DISINFECTION
11? REVERSE OSMOSIS
120 PRESSURE ION EXCHANGE-SOFTENING
121 PRESSURE ION EXCHANG-N03 REMOVAL
122 ACTIVATED ALUMINA FLUORIDE REMOV
123 BONE CHAR FLUORIDE REMOVAL
12-1 PACKAGE RAU UATER PUHPING-TDH=°50
125 PACKAGE HIGH SERVICE PUMP STATN
126 STEEL BACKUASH/CLEARWELL TANKS
127 LIQUID SLUDGE HAULING
128 DEUATERED SLUDGE HAULING
129 SLUDGE DISPOSAL-SANITARY SEUER
130 SLUDGE DEUATERING LAGOONS
         OSH:
131 SAND DRYING BEDS
PARAMETER RANGE
30.0
2SOO.O
2500.0
0.1
0.1
1.0
0.1
0.1
0.5
850.0
0.1
10.0
2500.0
70000.0
70000.0
12700.0
16300.0
20.0
30.0
500.0
•68.0
100.0
50.0
1500.0
750.0
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
TO
720.0
1000000.0
500000.0
10.0
10.0
10.0
100.0
100.0
10.0
13500.0
50.0
780.0
1000000.0
860000.0
830000.0
910000.0
800000.0
700.0
1100.0
30000.0
41100.0
50000.0
25000.0
30000.0
15000.0
NUMBER OF
CHEMICALS
GPM
GPD
GPU
LB/DAY
LB/DAY
LB/HR
LB/DAY
LB/DAY
LB/DAY
GAL
LB/DAY
GPM
GPD
GPD
GPD
GPD
GPD
GPM
GPM
GAL
GPD
CY/YR
GPD
CU FT
CF/YR
4
3
0
1
1
1
1
1
0
0
2
0
3
1
1
2
2
0
0
0
0
0
0
0
PROCESS
TYPE
2
2
1
1
10
1
1
1
1
1
1
1
2
1
1
2
1
1
1 :
1
7
7
11
1
NO. 1
CAR]
6
5
2
3
3
3
3
3
2
2
4
2
5
3
3
4
4
2
2
2
3
3
3
2
                                              200.0  TO
                                                              800.0  SQ FT
                                                   14

-------
                                             Table 5



                   Processes that  Use Chemicals and  Chemicals  Used
   TREATMENT  PROCESS  -  LARGE SYSTEMS






 1 CL2 FEED-CYLINDER  STORAGE




 2 CL2 FEED-ON SITE STORAGE TANK




 3 CL2 FEED FROM  RAIL CAR




 4 CHLORINE DIOXIDE GENERATINGrFEED




 7 ON-SITE HYPOCHLORITE GENERATION




 8 ALUM FEED-LIQUID STOCK




 9 ALUM FEED-DRY  STOCK




10 POLYMER FEED SYSTEMS




11 LIME FEED-NO RECALCINATION




12 LIME FEED-UITH RECALCINATION




13 POTASSIUM  PERMANGANATE FEED




14 SULFURIC ACID  FEED SYSTEMS




15 SODIUM HYDROXIDE FEED SYSTEMS




16 FERROUS SULFATE FEED SYSTEMS




17 FERRIC SULFATE FEED  SYSTEMS



18 ANHYDROUS  AMMONIA  FEED FACILITY




19 AQUA AMMONIA FEED  FACILITY



20 POWDERED ACTIVATED CARBON FEED




49 RECARDONATION-LIQUID C02 FEED




54 PRESSURE DIATOMITE FILTERS




55 VACUUM DIATOMITE FILTERS




59 REVERSE OSMOSIS




60 PRESSURE ION EXCHANGE-SOFTENING




61 GRAVITY ION EXCHANGE-SOFTENING




62 PRESSURE ION EXCHANG-N03 REMOVAL




63 ACTIV. ALUMINA-FLUORIDE REMOVAL






   TREATMENT  PROCESS  -  SMALL SYSTEMS






99 PACKAGE COMPLETE TREATMENT  PLANT
    CHEMICALS USED






CHLORINE




CHLORINE




CHLORINE




CHLORINE»SALT




SALT




ALUM-LIQUID STOCK




ALUM-DRY STOCK




POLYMER




LIME




LIME




POTASSIUM PERMANGANATE




SULFURIC ACID




SODIUM HYDROXIDE




FERROUS SULFATE




FERRIC SULFATE




ANHYDROUS AMMONIA




AQUACEOUS AMMONIA



POWDERED ACTIVATED CARDON




LIQUID CARBON DIOXIDE




POLYMERr ALUMr DIATOMACEOUS  EARTH




POLYMER, ALUMT DIATOMACEOUS  EARTH




SULFURIC ACID» HEXAMETAPHOSPHATE, CHLORINE




SALT




SALT




SALT




SODIUM HYDROXIDE, SULFURIC ACID
                                           ALUM. POLYMER. SODA ASH.  CHLORINE OR  HYPOCHLORITE
                                                  15

-------
    TREATMENT PROCESS - SMALL SYSTEMS





100 PACKAGE GRAVITY FILTER PLANTS



101 PACKAGE PRESSURE FILTRATION PLNT



lOi PACKAGE PRESS DIATOMITE FILTERS



107 PACKAGE VACUUM DIATOMITE FILTERS



108 PACKAGE ULTRAFILTRATION PLANTS



110 POTASSIUM PERMANGANATE FEED SYST



111 POLYMER FEED SYSTEMS



112 POWDERED ACT CARBON FEED SYSTEMS



113 DIRECT FEED GAS CHLORINATION



114 SODIUM HYPOCHLORITE SOLUTN FEED



117 CHLORINE DIOXIDE GENERATING/FEED



117 REVERSE OSMOSIS



120 PRESSURE ION EXCHANGE-SOFTENING



121 PRESSURE ION EXCHANG-N03 REMOVAL



122 ACTIVATED ALUMINA FLUORIDE REMOV



123 BONE CHAR FLUORIDE REMOVAL
Table 5  (Continued)






            CHEMICALS USED





        ALUM? POLYMER? SODA ASH*  CHLORINE  OR HYPOCHLORITE



        ALUM? POLYMER* SODA ASH?  CHLORINE  OR HYPOCHLORITE



        ALUMr POLYMER* CHLORINE.  DIATOMACEOUS EARTH



        ALUM? POLYMER? CHLORINE?  DIATOMACEOUS EARTH



        SULFURIC ACID? HEXAMETAPHOSPHATE?  CHLORINE



        POTASSIUM PERMANGANATE



        POLYMER




        POUDERED ACTIVATED CARBON



        GASEOUS CHLORINE



        SODIUM HYPOCHLORITE



        CHLORINE? SALT



        SULFURIC ACID? HEXAMETAPHOSPHATEr  CHLORINE



        SALT



        SALT



        SODIUM HYDROXIDE?  SULFURIC ACID



        SODIUM HYDROXIDE?  CARBONIC ACID
                                              16

-------
                                   PROCESS
                                DATA CARDS.
                       /
                      PROCESS
                   DATA CARDS.
           /"ACRES 2.0
         / ooeeeoeeooot
        PROCESS
      DATA CARD:
ACRES 1.0
THIRD DATA SEGMENT
                                         SECOND DATA SEGMENT
                                 FIRST DATA SEGMENT
                Figure 1.   PROCES.DAT data segments.
                                  17

-------
 THE ZERO CARD

      Segments of data in the PROCES.DAT file must be separated by a card
 containing a string of at least 15 zeros.   (In some systems,  a blank card
 may suffice).

      If cost data are desired for only one plant or segment of data,  no ZERO
 card should be included.   Inclusion of cost data for two or more  plants
 requires that the PROCES.DAT file be arranged as shown in Figure  1,  with
 ZERO cards between each segment.

      The last card in the PROCES.DAT file  is the last card of the last
 segment of data.   A Zero card must not be  placed at the end of the file.
 A ZERO card is only placed between segments.

 PROCESS TYPES AND DATA INPUT

      The various  process  types require two to seven cards  for  data input.
 The First two cards of data for all process types are the same.   Data card
 format and content are explained  in the following pages.

 Type 1 Process Data Input

 Card 1--

      The first card of data contains  the following information starting in
 column 1:   The card number (the integer 1)  followed by  a comma in column
 2,  the process number  (integer) from Table 3  followed immediately by  a
 comma,  and finally,  the process name.

      Examples:

      Card  1:   1,9,ALUM FEED -  DRY  STOCK
      Card  1:   1,21,RAPID  MIX,  G=300
      Card  1:   1,131,SAND  DRYING BEDS

      The commas are  necessary  to separate  numbers  and must not be omitted.
The  process name  is  optional,  but,  it  is a useful  identifier for  the user
when reviewing the PROCES.DAT  file  later.  The comma preceding the process
name is not optional

Card  2~

     The second card of data contains the  following information starting in
column  1:  The card number  (the integer 2) followed by a comma in column 2,
the plant design flow  in mgd (floating point) followed by a comma, the plant
actual flow in mgd  (floating point) followed by a  comma, the process design
parameter  (floating point)  followed by a comma, and the process operating
parameter  (floating point)
                                     20

-------
     Examples:  Using the same three examples as used above for Card 1,
                assume the following:

     Example 1:  Plant Design Flow = 10.0 mgd
                 Plant Operating Flow = 7.0 mgd
                 Alum Design Feed = 245 Ib/hr
                 Alum Operating Feed = 170 Ib/hr
     Card 2:     2,10.0,7.0,245.0,170.0

     Example 2:  Plant Design Flow = 5.0 mgd
                 Plant Operating Flow = 4.0 mgd
                 Design Rapid Mix Volume = 464 cu ft
                 Operating Rapid Mix Volume = 464 cu ft
     Card 2:     2,5.0,4.0,464.0,464.0

     Example 3:  Plant Design Flow = 0.5 mgd
                 Plant Actual Flow =0.25 mgd
                 Design Sand Drying Bed Area = 500.0 sq ft
                 Operating Sand Drying Bed Area = 250.0 sq ft
     Card 2:     2,0.5,0.25,500.0,250.0

     The process design and operating parameters have the  units  specified
in Tables 4 and 6.  The process design parameter is used to calculate
construction costs, and the operating parameter is used to determine operation
and maintenance costs.  In some cases, these parameters have different units
and/or ranges.  In Table 4, for example, process 42 (BACKWASH PUMPING
FACILITIES) has the unit gpm for the design parameter and sq ft for the
operating parameter.  Plant flows are always in mgd.  All values are floating
point (except the card number) and are separated by a comma.  Notice that
for some processes such as chemical feed and pumping, the numerical values
of the design and operating parameters may be different, since the design
parameter indicates capacity, and these processes generally do not operate
at capacity.  For other processes, such as basins, the design and operating
parameters are identical.  Operation and maintenance costs for any process
operating at less than 100 percent time can be determined by inputing a
proportionately lower value for the operating parameter.  For example,
operation and maintenance costs for a 500 sq ft furnace operating 70 percent
of the time are determined by inputing a value of 350 for the operating
parameter.

Cards 3 and 4—

     The number of cards for a type 1 process is equal to 2 plus the number
of chemicals.  For example, process number 9, ALUM FEED - DRY STOCK, requires
2+1=3 cards.  Process 21 (RAPID MIX, G=300) requires 2+0=2 cards.

     If a third or fourth card of data is required, it contains the following
information:  The number of the card (the integer 3 or 4) followed by a comma,
the cost of the chemical(s) used in the process in dollars/ton (floating
point) followed by a comma, and the name of the chemical used in the process
(up to 24 characters).  For most processes, the chemical(s) used will be
                                       21

-------
                                 Table  6
                      Process  Parameter Units
   TREATMENT PROCESS - LARGE SYSTEMS

  1 CL2 FEED-CYLINDER STORAGE             LB/DttY
  2 CL2 FEED-ON SITE STORAGE TANK         LB/DAY
  3 CL2 FEED FROM RAIL CAR                LB/DAY
  4 CHLORINE DIOXIDE GENERATING*FEED      LB/DAY
  5 OZONE GENERATION SYSTEMS              LB/DAY
  6 OZONE CONTACT CHAMBER                 CU FT
  7 ON-SITE HYPOCHLORITE GENERATION       LB/DAY
  8 ALUM FEED-LIQUID STOCK                LB/HR
  9 ALUM FEED-DRY STOCK                   LB/HR
10 POLYMER FEED SYSTEMS                  LB/DAY
11 LIME FEED-NO RECALCINATION            LB/HR
12 LIME FEED-UITH RECALCINATION          LB/HR
13 POTASSIUM PERMANGANATE FEED           LB/DAY
14 SULFURIC ACID FEED SYSTEMS            GPD
15 SODIUM HYDROXIDE FEED SYSTEMS         LB/DAY
16 FERROUS SULFATE FEED SYSTEMS          LB/HR
17 FERRIC SULFATE FEED SYSTEMS           LB/HR
18 ANHYDROUS AMMONIA FEED FACILITY       LB/DAY
19 AQUA AMMONIA FEED FACILITY            LB/DAY
20 POWDERED ACTIVATED CARBON FEED        LB/HR
21 RAPID MIX*  G=300                      CU FT
22 RAPID MIX*  G=600                      CU FT
23 RAPID MIXr  G=900                      CU FT
24 FLOCCULATION-HORIZ PADDLE*  G=20       CU FT
25 FLOCCULATION-HORIZ PADDLE*  G°»50       CU FT
26 FLOCCULATION-HORIZ PADDLE*  G=80       CU FT
27 FLOCCULATION-VERT TURBINE*  G=20       CU FT
28 FLOCCULATION-VERT TURBINE*  G=50       CU FT
      UNITS

OF CHLORINE
OF CHLORINE
OF CHLORINE
OF CHLORINE DIOXIDE
OF OZONE
OF TOTAL CHAMBER VOLUME
OF EQUIVALENT CHLORINE
OF ALUM
OF ALUM
OF POLYMER
OF LIME
OF LIME
OF PERMANGANATE
OF SULFURIC ACID
OF SODIUM HYDROXIDE
OF FERROUS SULFATE
OF FERRIC SULFATE
OF AMMONIA
OF AMMONIA
OF POWDERED CARBON
OF TOTAL BASIN VOLUME
OF TOTAL BASIN VOLUME
OF TOTAL BASIN VOLUME
OF TOTAL BASIN VOLUME
OF TOTAL BASIN VOLUME
OF TOTAL BASIN VOLUME
OF TOTAL BASIN VOLUME
OF TOTAL BASIN VOLUME
                                 22

-------
                               Table  6 (Continued)
   TREATMENT PROCESS - LARGE SYSTEMS
29 FLOCCULATION-VERT TURBINEr B=80       CU FT  OF
30 CIRCULAR CLARIFIER-LIME SLUDGE        SQ FT  OF
31 CIRC CLARIFIER-FECL3 X ALUM SLDG      SQ FT  OF
32 RECTANGULAR CLARIFIER-LIME SLDG       SQ FT  OF
33 RECT CLARIFIER-FECL3 8 ALUM SLG       SQ FT  OF
34 UPFLOW SOLIDS CONTACT CLAR>G=70       SQ FT  OF
35 UPFLOW SOLIDS CONTACT CLARi.G=110      SQ FT  OF
36 UPFLOU SOLIDS CONTACT CLARf6=150      SQ FT  OF
37 TUBE SETTLING MODULES                 SQ FT  OF
38 GRAVITY FILTRATION STRUCTURE          SQ FT  OF
39 FILTRATION MEDIA-RAPID SAND           SQ FT  OF
40 FILTRATION MEDIA-DUAL MEDIA           SQ FT  OF
41 FILTRATION MEDIA-MIXED MEDIA          SQ FT  OF
42 BACKWASH PUMPING FACILITIES           GPM    OF
        O&M:                             SQ FT  OF
43 HYDRAULIC SURFACE WASH SYSTEMS        SQ FT  OF
44 AIR-WATER BACKWASH FACILITIES         SQ FT  OF
45 WASH WATER SURGE BASINS               GAL    OF
46 FILTER MOD-RAP SAND TO HIGH RATE      SQ FT  OF
47 CONTINUOUS AUTO. BACKWASH FILTER      SQ FT  OF
48 RECARBONATION BASIN                   CU FT  OF
49 RECARBONATION-LIQUID C02 FEED         LB/DAY OF
SO RECARB-C02 FROM SUBMERGED BURNER      LB/DAY OF
51 RECARBONATION-C02 FROM STACK GAS      LB/DAY OF
52 MULTIPLE HEARTH RECALCINATION         SQ FT  OF
53 CONTACT BASIN-DIRECT FILTRATION       CU FT  OF
54 PRESSURE DIATOMITE FILTERS            MGD    OF
53 VACUUM DIATOMITE FILTERS              MGD    OF
   UNITS

TOTAL BASIN VOLUME
SINGLE CLARIFIER AREA
SINGLE CLARIFIER AREA
SINGLE CLARIFIER AREA
SINGLE CLARIFIER AREA

SINGLE CLARIFIER AREA
SINGLE CLARIFIER AREA

SINGLE CLARIFIER AREA
TOTAL TUBE MODULE AREA
TOTAL FILTER AREA
TOTAL FILTER AREA
TOTAL FILTER AREA
TOTAL FILTER AREA
BACKWASH PUMPING CAPACITY
TOTAL FILTER AREA
TOTAL FILTER AREA

TOTAL FILTER AREA
BASIN VOLUME
TOTAL FILTER AREA
TOTAL FILTER AREA
SINGLE BASIN VOLUME
LIQUID CARBON DIOXIDE
CARBON DIOXIDE FROM SINGLE BURNER SET
CARBON DIOXIDE

SINGLE FURNACE EFFECTIVE HEARTH AREA
SINGLE BASIN AREA
TOTAL FILTER FLOW
TOTAL FILTER FLOW
                                         23

-------
                               Table  6  (Continued)
   TREATMENT PROCESS - LARGE SYSTEMS

56 PRESSURE FILTRATION PLANTS
57 IN-PLANT PUMPING
58 WASH WATER STORAGE TANKS
59 REVERSE OSMOSIS
60 PRESSURE ION EXCHANGE-SOFTENING
61 GRAVITY ION EXCHANGE-SOFTENING
62 PRESSURE ION EXCHANG-NO3 REMOVAL
63 ACTIV. ALUMINA-FLUORIDE REMOVAL
64 GRAVITY GAC CONTACTORS-CONCRETE
65 GRAVITY GAC CONTACTORS-STEEL
        OSH:
66 PRESSURE CARBON CONTACTORS
        OSH!
67 CONVERT FILTER TO GAC CONTACTOR
68 GRANULAR ACT CARBON-CONSTR COST
69 MAKEUP CARBON COST-OSM ONLY
70 CAPPING SAND FILTER U/ANTHRACITE
71 REGIONAL GAC REGEN-TRANS 8 STOR
        OSH:
72 REGIONAL HULTI HEARTH GAC REGEN
73 MULTIPLE HEARTH GAC REGENERATION
74 INFRARED CARBON REGEN FURNACE
75 FLUIDIZED BED GAC REGENERATION
76 POWDERED CARB REGEN-FLUIDIZED BD
77 POWDERED CARB REGEN-ATOMIZED SUS
78 CHEH SLUDGE PUMPING-UNTHICKENED
79 CHEH SLUDGE PUHPING-THICKENED
80 GRAVITY SLUDGE THICKENER-LIME
81 GRAV SLDG THICKENER-ALUM 8 FECL3
             UNITS

SQ FT  OF TOTAL FILTER AREA
MGD    OF TOTAL PLANT FLOW
GAL    OF TOTAL TANK VOLUME
MGD    OF TOTAL FLOW
MGD    OF TOTAL FLOW

MGD    OF TOTAL FLOW
MGD    OF TOTAL FLOW
MGD    OF TOTAL FLOW

CU FT  OF SINGLE CONTACTOR VOLUME
SQ FT  OF TOTAL CONTACTOR AREA

CU FT  OF SINGLE VOLUME
CU FT  OF TOTAL CONTACTOR VOLUME
CU FT  OF SINGLE CONTACTOR VOLUME
SQ FT  OF TOTAL CONTACTOR AREA
SQ FT  OF TOTAL FILTER AREA
LB     OF TOTAL CARBON WEIGHT

LB/YR  OF TOTAL CARBON WEIGHT

SQ FT  OF TOTAL FILTER AREA
CU FT  OF ON-SITE CARBON STORAGE CAPACITY
LB/YR  OF CARBON REGENERATED
SQ FT  OF SINGLE FURNACE EFFECTIVE HEARTH AREA
SQ FT  OF SINGLE FURNACE EFFECTIVE HEARTH AREA
LB/DAY OF TOTAL CARBON WEIGHT
LB/DAY OF CARBON FDR SINGLE FURNACE
LB/DAY OF TOTAL CARBON WEIGHT
LB/DAY OF TOTAL CARBON WEIGHT
GPM    OF SLUDGE PUMPING
GPM    OF SLUDGE PUMPING

SQ FT  OF SINGLE BASIN AREA
SQ FT  OF SINGLE BASIN AREA
                                         24

-------
                      Table  6 (Continued)
   TREATMENT PROCESS - LARGE SYSTEMS

82 VACUUM FILTERS
83 BELT FILTER PRESS
84 FILTER PRESS
85 DECANTER CENTRIFUGES
86 BASKET CENTRIFUGES
87 SAND DRYING BEDS'
88 SLUDGE DEUATERING LAGOONS
        OSMJ
89 SLUDGE DISPOSAL-SANITARY SEWER
90 LIQUID SLUDGE HAULING
91 DEUATERED SLUDGE HAULING
92 RAW WATER PUMPING FACILITY
93 FINISHED WATER  PUMPING FACILITY
94 CLEARWELL STORAGE-BELOW GROUND
95 CLEARWELL STORAGE-GROUND LEVEL
96 DIFFUSED AERATION BASIN
97 AERATION-AERATION TOUERS
98 ADMINrLAB X MAINTENANCE BUILDING
   TREATMENT PROCESS - SMALL  SYSTEMS
99 PACKAGE  COMPLETE  TREATMENT PLANT
100 PACKAGE  GRAVITY FILTER PLANTS
101 PACKAGE  PRESSURE  FILTRATION PLNT
102 FILTER MEDIA-RAPID  SAND
103 FILTER MEDIA-DUAL MEDIA
104 FILTER MEDIA-MIXED  MEDIA
105 fILTER MEDIA-MIXEDflNST U/MF SUP
106 PACKAGE PRESS DIATOMITE FILTERS
             UNITS

SO FT  OF TOTAL FILTER AREA
GPM    OF TOTAL SLUDGE PUMPING
CU FT  OF PRESS SLUDGE CAPACITY
GPM    OF SLUDGE PUMPING
GPD    OF SLUDGE PUMPING

SO FT  OF TOTAL BED AREA
CU FT  OF TOTAL LAGOON VOLUME
CF/YR  OF SLUDGE REMOVED
GPM    OF SLUDGE
MG/YR  OF SLUDGE
CY/YR  OF SLUDGE
MOD    OF TOTAL FLOW
MGD    OF TOTAL FLOW
GAL    OF CLEARUELL VOLUME
GAL    OF CLEARUELL VOLUME
CU FT  OF BASIN VOLUME
CU FT  OF TOWER VOLUME
MGD    OF PLANT FLOW
GPM    OF TOTAL FLOW
GPM    OF TOTAL FLOW
GPM    OF TOTAL FLOW
SO FT  OF TOTAL FILTER AREA

SO FT  OF TOTAL FILTER AREA
SO FT  OF TOTAL FILTER AREA
SO FT  OF TOTAL FILTER AREA
GPD    OF TOTAL FILTER FLOW
                                    25

-------
                      Table  6  (Continued)
     TREATMENT  PROCESS - SMALL SYSTEMS

 107  PACKAGE VACUUM DIATOMITE FILTERS
 108  PACKAGE ULTRAFILTRATION PLANTS
 109  PACKAGE GRAN ACT CARBON COLUMNS
 110  POTASSIUM  PERMANGANATE FEED SYST
 111  POLYMER FEED SYSTEMS
 112  POWDERED ACT CARBON FEED SYSTEMS
 113  DIRECT FEED GAS CHLORINATION
 114  SODIUM HYPOCHLORITE SOLUTN FEED
 115  OZONE GENERATING AND FEED
 116  OZONE CONTACT CHAMBER
 117  CHLORINE DIOXIDE GENERATING/FEED
 118  ULTRAVIOLET LIGHT DISINFECTION
 119  REVERSE OSMOSIS
 120  PRESSURE ION EXCHANGE-SOFTENING
 121  PRESSURE ION EXCHANG-N03 REMOVAL
 122  ACTIVATED ALUMINA FLUORIDE REMOV
 123  BONE CHAR FLUORIDE REMOVAL
 124  PACKAGE RAU WATER PUMPING-TDH=50
 125 PACKAGE HIGH SERVICE PUMP STATN
 126 STEEL BACKUASH/CLEARWELL TANKS
 127 LIQUID SLUDGE HAULING
 128 DEUATERED SLUDGE HAULING
129 SLUDGE DISPOSAL-SANITARY SEWER
130 SLUDGE DEUATERING LAGOONS
         OSM:
131 SAND DRYING BEDS
              UNITS

 GPM    OF  TOTAL FILTER FLOW
 GPD    OF  TOTAL FLOW
 GPD    OF  TOTAL FLOW
 LB/DAY  OF  PERMANGANATE
 LB/DAY  OF  POLYMER
 LB/HR   OF  POWDERED CARBON
 LB/DAY  OF  CHLORINE

 LB/DAY  OF  EQUIVALENT CHLORINE
 LB/DAY  OF  OZONE
 GAL    OF  TOTAL CHAMBER VOLUME
 LB/DAY  OF  CHLORINE DIOXIDE
 GPM    OF  TOTAL FLOW
 GPD    OF  FLOW
 GPD    OF  FLOW
 GPD    OF  FLOW
 GPD    OF  FLOW
 GPD    OF  FLOW
 GPM    OF  FLOW
 GPM     OF  FLOW
 GAL     OF  TOTAL TANK VOLUME
 GPD     OF SLUDGE
 CY/YR  OF SLUDGE
 GPD    OF SLUDGE
CU FT  OF TOTAL LAGOON VOLUME
CF/YR  OF SLUDGE REMOVED
SO FT  OF TOTAL BED  AREA
                                 26

-------
obvious.  For example, process 9 (ALUM FEED - DRY STOCK) uses alum.  For
convenience, however, the processes that use chemicals and the names of the
chemicals are shown in Table 5.

     Examples:  Alum = $70.00/ton
                             /
     Card 3:    3,70.00,ALUM

Since the 24 characters immediately following the second comma are copied on
the printout, other useful information may be included.  For example, we
could have written:

     Card 3:    3,70.00,ALUM (DOSE = 70 MG/L)

Any characters following the 24th character will be ignored.

Completed Examples—

     The following four examples show all cards necessary for data input
of the processes shown.  All data begin in column one.

     Card 1:    1,9,ALUM FEED - DRY STOCK
     Card 2:    2,10.0,7.0,245.0,170.0
     Card 3:    3,70.0,ALUM  (DOSE = 70 MG/L)

     Card 1:    1,21,RAPID MIX, G=300
     Card 2:    2,5.0,4.0,464.0,464.0

     Card 1:    1,131,SAND DRYING BEDS
     Card 2:    2,0.5,0.25,500.0,500.0

     Card 1:    1,4,CHLORINE DIOXIDE GENERATING,FEED
     Card 2:    2,2.0,1.75,16.7,14.5
     Card 3:    3,300.0,CHLORINE
     Card 4:    4,225.0,SODIUM CHLORITE

     The first three examples were explained above.  The last example can
be interpreted as follows:

     Total number of cards necessary is 2 + number of chemicals =2+2=4.

     Card 1:    Process No.  4, CHLORINE DIOXIDE GENERATING - FEED
     Card 2:    Design flow  = 2.0 mgd, actual flow = 1.75 mgd, process
                design parameter = 16.7 Ib/day, process operating parameter
                =14.5 Ib/day
     Card 3:    $300.00/ton  for chlorine used in this process
     Card 4:    $225.00/ton  for sodium chlorite used in this process

Type 2 Process Data Input

     The total number of data cards required for a type 2 process is 2 +
number of chemicals.  The first two cards of data are identical in format
                                      27

-------
and content to a type 1 process.  The remaining cards contain chemical cost
and chemical feed information.  For example, process 59 (REVERSE OSMOSIS)
may use up to 3 chemicals:  sulfuric acid, sodium hexameta phosphate, and
chlorine.  This process requires 2+3=5 cards of data with the following
information:  The card number (integer) followed by a comma, the cost of the
chemical in $/ton (floating point) followed by a comma, the actual (not design)
feed rate in Ib/day for the chemical (floating point) followed by a comma,
and the name of the chemical (not to exceed 24 characters).  The chemicals
can be input in any order.  If one or more of the chemicals is not used, an
input of zeros for the chemical cost and the chemical feed rate will cause
no information to be printed on the output for that chemical.  To illustrate,
the 5 data cards for process 59 (REVERSE OSMOSIS) may be constructed as
follows:

     Card 1:    1,59,REVERSE OSMOSIS
     Card 2:    2,2.0,1.5,2.0,1.5
     Card 3:    3,65.0,250.2,SULFURIC ACID,20 MG/L
     Card 4:    4,650.0,62.6,SODIUM HEXA P03,5 MG/L
     Card 5:    5,300.0,25.0,CHLORINE,2 MG/L

     Card 1:    1,59,REVERSE OSMOSIS
     Card 2:    2,2.0,1.5,2.0,1.5
     Card 3:    3,650.0,62.5,SODIUM HEXA P03,5 MG/L
     Card 4:    4,65.0,125.1,SULFURIC ACID,10 MG/L
     Card 5:    5,0.0,0.0

     Card 1:    1,59,REVERSE OSMOSIS
     Card 2:    2,2.0,1.5,2.0,1.5
     Card 3:    3,0.0,0.0
     Card 4:    4,0.0,0.0
     Card 5:    5,0.0,0.0

     Example 1, above, indicates the following:

     Card 3:  $65.00/ton cost and 250.2 Ib/day feed rate for
              sulfuric acid at a dose of 20 mg/1

     Card 4:  $650.00/ton and 62.6 Ib/day feed rate for
              sodium hexameta phosphate at a dose of 5 mg/1

     Card 5:  $300.00/ton and 25.0 Ib/day feed rate for
              chlorine at 2 mg/1

     Example 2, above, indicates the following:

     Card 3:  $650.00/ton for sodium hexameta phosphate at a 5 mg/1 dose
     Card 4:  $65.00/ton for sulfuric acid at a 10 mg/1 dose
     Card 5:  No other chemicals used

     Example 3, above, indicates that no chemicals were used in this process
     since cards 3 to 5 contained zeros for the chemicals  costs and feed
     rates.
                                     28

-------
Type 3 Process Data Input

     The total number of cards required for a type 3 process is 3 + number
of chemicals.  The first two lines are identical in form and content to the
first two lines of process type 1.  Card 3 is very specific and must contain
the number of units of the process in question for which costs are desired.
For example, process 31 (CIRC CLARIFIER - FECL3 & ALUM SLDG), when input to
the computer, calculates costs for a single clarifier.  The program then
multiplies the calculated costs for a single clarifier by the number of units
indicated on card 3.
     To illustrate this, consider the following process data input.
number of data cards =3+0=3.
Total
     Card 1:    1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG
     Card 2:    2,1.0,0.9,1667.0,1667.0
     Card 3:    3,1,UNIT

     Card 3 above contains the integer 3 beginning in column 1 followed by
a comma, and the number of units (integer) for which costs are desired
followed by a comma and the word UNIT or UNITS.  The word QNIT(S) is optional,
but the comma following the number of units is not.  Costs could be obtained
for three 1667.0 sq ft clarifiers by either of the following methods (more
about this later):

     Card 1:    1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG
     Card 2:    2,3.0,2.7,1667.0,1667.0
     Card 3:    3,3,UNIT

or,

     Card 1:    1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG
     Card 2:    2,1.0,0.9,1667.0,1667.0
     Card 3:    3,1,UNIT
     Card 1:    1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG
     Card 2:    2,1.0,0.9,1667.0,1667.0
     Card 3:    3,1,UNIT
     Card 1:    1,31,CIRC CLARIFIER - FECL3 & ALUM SLDG
     Card 2:    2,1.0,0.9,1667.0,1667.0
     Card 3:    3,1,UNIT

     The above example shows that the design and operating flows in card 2
of each process represent the total flow for that process only.  The first
example, gives a total of 2.7 mgd (0.9 mgd/clarifier x 3 clarifiers), and
the second example yields a flow of 0.9 mgd for each clarifier.

     If the number of chemicals for any type 3 process is greater than 1,
the additional cards will contain chemical cost information identical in
format and content to the third card of process type 1.
                                    29

-------
Type 4 Process Data Input

     The number of data cards required for type 4 processes (GAG Contactors)
is 3 + number of chemicals or 3 + 0 = 3 cards of data.  The first two cards
of data are identical in format and content to type 1.  The third data card
is identical in form and content to the third data card of type 3 processes.
Note, however, that the design process variable has the units of cu ft per
single contactor volume, and the operating process variable has the units of
total volume in cu ft or total area in sq ft (see Table 6).  For example,
consider the following data cards for process 65 (GRAVITY GAG CONTACTORS -
STEEL):  The design flow is 50.0 mgd, the actual flow is 30.0 mgd, the single
contactor volume is 6,300 cu ft, the number of contactors is 22, and the total
volume is 138,600 cu ft.

     Card 1:    1,65,GRAVITY GAG CONTACTORS - STEEL
     Card 2:    2,50.0,30.0,6300.0,138600.0
     Card 3:    3,22,UNITS

     There are only 3 type 4 processes.  All are granular activated carbon
treatment.  The operation and maintenance cost curves for each include the
costs for backwash pumping for the contactors.  The cost for backwash pumping
is different for each type of contactor because of the variation in the pumping
head.  Therefore, when computing costs for a train of processes that includes
any of the activated carbon contactors (processes 64, 65 or 66) and backwash
pumping for these contactors (process 42), a zero must be input for the
operating parameter of the backwash pumping curve.  This will avoid
duplication of the operation and maintenance costs for backwash pumping.

Type 5 Process Data Input

     The number of data cards for type 5 is 3 + number of chemicals or
3+0=3.  Type 5 processes consist of the various types of pumping
facilities.  Cards 1 and 2 are identical in format and content to cards
1 and 2 of type 1.  Card 3 contains the integer 3 followed by a comma, the
total dynamic pumping head in feet (floating point) followed by a comma, and
the abbreviation TDH.

     For example, process 57 (IN PLANT PUMPING) for a 5.0 mgd plant with an
actual flow of 3.0 mgd and a total dynamic head of 40 ft becomes:

     Card 1:    1,57,IN-PLANT PUMPING
     Card 2i    2,5.0,3.0,7.5,3.0
     Card 3:    3,40.0,TDH

     In this case, a 7.5 mgd pumping capacity has been installed as shown in
Card 2.  The abbreviation TDH is optional, but the comma preceding it is not.

Type 6 and 7 Process Data Input

     The number of data cards required for types 6 and 7 is 3 + number of
chemicals =3+0=3.  The first two data cards of types 6 and 7 are
                                     30

-------
identical in format and content to type 1.  The third card of data contains
the number of one-way miles driven to the regeneration site or the sludge
disposal site.  Similar to previous processes; Card 3 contains the integer
3 followed by a comma, the number of one-way miles (floating point) followed
by a comma, and the word MILES.  The word MILES is optional, but the comma
preceding it is not.
     Examples:

     Card 1:
     Card 2:
     Card 3:

     Card 1:
     Card 2:
     Card 3:
1,71,REGIONAL GAG REGEN-TRANS & STOR
2,1.0,0.9,1000.0,30000.0
3,10.0,MILES

1,90,LIQUID SLUDGE HAULING
2,1.0,1.0,1.3,1.3
3,15.0,MILES
Type 8 Process Data Input

     The number of data cards for type 8 is 3 + number of chemicals =
3+1=4.  The first two data cards are identical in format and content to
the first two data cards of type 1.  The third data card contains the integer
3 followed by a comma, the amount of makeup lime added to the recalcined
lime is percent of lime feed rate (floating point) followed by a comma, and
the words MAKEUP LIME %.  The words MAKEUP LIME % are optional, but the
preceding comma is not.  The fourth card of data contains chemical cost
information and is similar to the third card of type 1.

     Examples for 5% and 10% makeup lime:

     Card 1:    1,12,LIME FEED - WITH RECALCINATION
     Card 2:    2,30.0,25.0,3500.0,2606.0
     Card 3:    3,5.0,MAKEUP LIME %
     Card 4:    4,40.0,LIME

     Card 1:    1,12,LIME FEED - WITH RECALCINATION
     Card 2:    2,30.0,25.0,3500.0,2606.0
     Card 3:    3,10.0,MAKEUP LIME %
     Card 4:    4,40.0,LIME

     In the above examples, the cost of lime is $40.00/ton, the plant design
flow is 30.0 mgd, and the design lime rate is 3500.0 Ib/hr.  In the fourth
data card, the word LIME is not optional.  Chemical names following chemical
cost information are not optional unless the amount or the cost of that
chemical is zero.

Type 9 Process Data Input

     The total number of data cards required for type 9 is 3 + number of
chemicals =3+4=7.  This process type includes the package treatment
plants, which may use from zero to 4 chemicals, depending on the operators'
requirements.  The first two data cards are identical in format and content
                                      31

-------
to the first two data cards of type 1.  The third data card contains the
integer 3 followed by a comma, the hydraulic loading on the package plant in
gpm/sf (floating point) followed by a comma, and the abbreviation gpm/sf.
The abbreviation, gpm/sf is optional, but the preceding comma is not.  The
fourth, fifth, sixth and seventh data cards contain chemical cost and chemical
feed information with format and content identical to chemical information
cards for type 2 processes.  That is, they contain the card number (integer)
followed by a comma, the cost of the chemical used is $/ton (floating point)
followed by a comma, the chemical feed rate is Ib/day (floating point)
followed by a comma, and the name of the chemical (up to 24 charaters long).
If a chemical name is input exceeding 24 characters, the 25th and succeeding
characters will be ignored.
     Example:

     Card 1:
     Card 2:
     Card 3:
     Card 4:
     Card 5:
     Card 6:
     Card 7:
1,99,PACKAGE COMPLETE TREATMENT PLANT
2,0.288,0.252,200.0,175.0
3,2.0,GPM/SF
4,70.0,147.0,ALUM,70 MG/L
5,4000.0,2.0,POLYMER,! MG/L($2/LB)
5,0.0,0.0
7,0.0,0.0
Type 10 Process Data Input

     The total number of cards for type 10 is 2 + number of chemicals =
2+1 = 3.

     The data card input is identical in format and content to type 1 for
all cards with one exception.  The chemical cost is input in $/lb instead of
$/ton.
     Example:

     Card 1:
     Card 2:
     Card 3:
1,10,POLYMER FEED SYSTEMS
2,1.0,1.0,8.34,8.34
3,2.0, POLYMER,! MG/1
     Refer to section on type 1 process data input for a discussion of format
and content of data cards.

Type 11 Process Data Input

     The total number of data cards for type 11 is 3 + number of chemicals =
3+0=3.  The first two data cards are identical in format and content to
the first two data cards of type 1.  The third data card for process 11
contains the integer 3 followed by a comma, the sludge concentration in mg/1
(floating point) followed by a comma, and the abbreviation mg/1.  The
abbreviation mg/1 is optional, but the preceding comma is not.

     Example:
                                     32

-------
     Card 1:    1,89,SLUDGE DISPOSAL - SANITARY SEWER
     Card 2:    2,1.0,1.0,20.0,20..0
     Card 3:    3,10000.0,MG/L

Type 12 Process Data Input

     The total number of cards for type 12 is 4 + number of chemicals =
4+0=4.  The first two data cards are identical in format and content to
the first-two data cards of type 1.  The third data card indicates the number
of units and is identical to the third data card of type 3.  The fourth data
card indicates percent ownership of the regional facility and  contains  the
integer 4 followed by a comma, the percent ownership (floating point) followed
by a comma, and the optional words % OWNERSHIP.  The comma preceding
% OWNERSHIP is not optional.
     Example:

     Card 1:
     Card 2:
     Card 3:
     Card 4:
1,72,REGIONAL MULTI HEARTH GAG REGEN
2,5.0,3.5,800.0,560.0
3,2,UNITS
4,10.0% OWNERSHIP
                                     33

-------
                                   SECTION 5

                                PROGRAM OUTPUT
 DETAILED OR SUMMARY

      Program output is  controlled by both the  COST.DAT  file  and  the PROCES.DAT
 file.   The main option  available to  the  user is  determined in  line 28  of  the
 COST.DAT file.   The two options  available are  the  DETAILED or  SUMMARY  printout.
 Sample  printouts for each of the options are shown in Examples 1  through
 3  in  Section 6.   Note that if the user chooses the DETAILED  printout,  he
 gets  all the information contained in the SUMMARY  plus  a detailed cost
 breakdown for each  process.

 REPETITIVE OUTPUT

      Program output is  also  controlled,  in part, by the way  in which the
 COST.DAT and PROCES.DAT files are constructed.   In Section 3,  COST.DAT
 File  Construction,  it was shown  that two additional cards of data could be
 added (cards 29  and 30)  to the file  to cause the program to  be rerun.
 Card  29 designates  which cost factor  is  to be  changed during the  rerun,
 and card 30 contains  the values  to be used during  the rerun.   In  other
 words,  if cards  29  and  30 were added to  the COST.DAT file with the following
 information,
     Card 29:
     Card 30:
8,2
0.02,0.04
the program would be rerun twice using the existing PROCES.DAT file and the
new values, 0.02 and 0.04, of cost factor number 8, ELECTRICITY, $/kwh.  This
has the same effect as running the program three times.  This is, three
complete program output listings will be generated:  One complete output
computing costs with the original cost of electricity, one complete output
computing costs with electricity at $0.02/kwh, and one complete output
computing costs with electricity at $0.04/kwh.

     In Section 4, PROCES.DAT File Construction, it was shown that data
were input or assembled as segments, with a segment representing costs for
one treatment plant.  A complete program output includes computed costs
listed separately for each data segment, with a listing of the COST.DAT
file following the output for the final data segment.  Therefore, if the
PROCES.DAT file were constructed with five data segments and the COST.DAT
file contained cards of 29 and 30, as shown above, the printout generated
by the program would consist of:
                                     34

-------
     1st data segment cost
     2nd data segment cost
     3rd data segment cost
     4th data segment cost
     5th data segment cost
           information
           information
           information
           information
           information
     Listing of COST.DAT values used

     1st data segment cost information
     5th data segment cost information
     Listing of COST.DAT values used (as above except electricity = $0,02/kwh)

     1st data segment cost information
     5th data segment cost information
     Listing of COST. DAT values used (as above except electricity = $0.04/kwh)

     Examples of the above program outputs are shown in Section 6, Examples.

COST EXTRAPOLATION FOR OUT-OF-RANGE INPUTS

     Table 4 lists the processes for which costs are available and the design
and operating parameter ranges over which these costs are valid.  If the user
attempts to obtain costs for process parameters outside the valid range, the
program will extrapolate the stored costs and notify the user of this condi-
tion on the printout.  The extrapolation is accomplished by evaluating the
following equation for y after first computing the constants GI and G£ from
stored cost data:
Iny
                              Inx
                Where x is the input process parameter (out of range) and
                y is the extrapolated cost at x.

     When plotted on log-log paper, this results in a linear extrapolation
of the cost curve.  See Section 6, EXAMPLES, for a sample printout of
extrapolated costs.
                                      35

-------
                                  SECTION  6

                                  EXAMPLES
     The following examples have been constructed to demonstrate the options
of  input and output available.  Each example is arranged with a table of the
plant and process assumptions followed by copies of the actual COST.DAT and
PROCES.DAT files and the program output.

EXAMPLE 1

     Example 1 contains one segment of data with five treatment processes in
the PROCES.DAT file.  The COST.DAT file contains the DETAILED printout option
and the use of the ENR Construction Cost Index.  The COST.DAT and PROCES.DAT
files are shown along with the printout generated by these inputs.

EXAMPLE 2

     Example 2 contains two segments of data with 17 and 4 treatment
processes, respectively, in the PROCES.DAT file.  The COST.DAT file contains
the SUMMARY printout option and does not use the ENR Construction Cost
Index.  The COST.DAT and PROCES.DAT files are shown along with the printouts
generated by these inputs.

EXAMPLE 3

     Example 3 contains two segments of data with 6 and 1 treatment
processes, respectively, in the PROCES.DAT file.  The COST.DAT file contains
the SUMMARY printout option and does not use the ENR Construction Cost Index.
The COST.DAT file also contains lines 29 and 30, which causes additional
printouts varying the cost of labor to include $7.50/hr and $12.50/hr.
The COST.DAT and PROCES.DAT files are shown along with the printouts
generated by these inputs.
                                    36

-------
                 COST.DAT File

                   Example 1
COSTS PRESENTED ARE CURRENT AS OF OCTOBER 1978
CAPITAL COST FACTORS (% OF CONSTRUCTION COST):
 1 ENGINEERINGS)
 2 SITEWQRK* INTERFACE PIPING(%)
 3 SUBSURFACE CONSIDERATIONS(%)
 4 STANDBY POWER(%)
 5 INTEREST RATE(%)
 6 NUMBER OF YEARS
 7 LAND COST* S/ACRE
UNIT COST FACTORS:
 8 ELECTRICITY. */KWH
 9 LABOR * */HR
10 DIESEL FUEL* $/GAL
11 NATURAL GAS* */CU FT
12 BLDNG ENERGY USE*KWH/S« FT/YR
COST INDEXES:
13 EXCAVATION(ENR SKILLED LABOR)
14 MANUFACTURED EQUIP (BLS *114)
15 CONCRETE  (BLS *132>
16 STEEL (BLS #101.3)
17 LABOR (ENR SKILLED LABOR)
18 PIPE & VALVES (BLS #114*901)
19 ELECTRICAL X INSTR (BLS *117)
20 HOUSING  (ENR BUILDING COST)
21 PRODUCER  PRICE  INDEX
22 ENR CONSTRUCTION*  '67 BASE  YR
OUTPUT(6 FOR LP*5 FOR TELETYPE)
PRINTOUT(BETAILED OR  SUMMARY)
-10*
-5*
=0*0
=0*0
=7*
=20*0
=2000*
= 10.
= *45
=,0013
=102.6

=247*0
=221 » 3
=221*1
=262* 1
=247*0
=236*4
=167*5
=254*76
=199*7
=265,38
=5
-DETAILED
                      37

-------
             PROCES.DAT File

               Example 1
ACRES-0»25
1»124,PACKAGE RAW WATER PUMPING~TDH*=50
2rO*101*0*072*105,0,50*0
It99vPACKAGE COMPLETE TREATMENT  PLANT
2*0*101*0.072,70*0*50*0
3,5.0*GPM/SF
4*70*0*12*0*ALUM» 20 MG/L
5 * 4000. * 0 * 15 *POLYMER(42/LB)»0»25 MG/L
6y300»0»l*8fCHLORINE)- 3 MG/L
7rO*OrO.O^
1» 126.STEEL BACKWASH/CLEARWELL TANKS f>
2>0*101»0»072»15000*Of 15000.0
1» 125s-PACKAGE HIGH SERVICE PUMP  STATN
2f0*101,0.072»105*0,50*0
1r131,SAND DRYING BEDS
2*0»101*0.072* 500*0*500*0
                  38

-------
***** COST ESTIMATE FOR PACKAGE RAW UATER PUMPING-TDH=50
          PROCESS FLOW
          PROCESS PARAMETER
      CAPITAL COST
          CONSTRUCTION
          OTHER RELATED COSTS
   DESIGN
 0.101 MGD
105.00 GPM
OPERATING
0.072 MGD
50.00 GPM
                                                     DOLLARS
            15653.
             5691.
      OXM COST
                            PROCESS CAPITAL COST       21344.

                                               CTS/1000 GAL TREATED
          ELECTRICAL ENERGY (2 '* 0.030/KUH
          MAINTENANCE MATERIAL
          LABOR @ $10.000/HR
          DIESEL FUEL 0 $ 0.450/GAL
          NATURAL GAS 0 * .0013/CU FT
          CHEMICALS
             0.662
             0.237
             2.043
             0.000
             0.000
             O.OOO
      COST SUMMARY
          OXM
          DEBT (3 20.0 YRS AND
                                PROCESS OS« COST
                               7.0 7.

                              PROCESS TOTAL COST
                                                        2.943
             2.943
             7.666
                                                       10.609
               DOLLARS/YR

                    174.
                     62.
                    537.
                      0.
                      0.
                      0.

                    773.
                    773.
                   2015.
                                                                                   2788.
***** COST ESTIMATE FOR PACKAGE COMPLETE TREATMENT PLANT
          PROCESS FLOW
          PROCESS PARAMETER
      CAPITAL COST
          CONSTRUCTION
          OTHER RELATED COSTS
   DESIGN
 0.101 MGD
 70.OO GPM
                                                     DOLLARS
            87293.
            31736.
OPERATING
0.072 MGD
50.00 GPM
      OXM COST
                            PROCESS CAPITAL COST      119029.

                                               CTS/1000 GAL TREATED
          ELECTRICAL ENERGY B * 0.030/KUH
          MAINTENANCE MATERIAL
          LABOR 
-------
***** COST ESTIMATE FOR STEEL BACKUASH/CLEARUELL TANKS
          PROCESS FLOW
          PROCESS PARAMETER

      CAPITAL COST

          CONSTRUCTION
          OTHER RELATED COSTS
                DESIGN
              0.101 MBD
           15000.00 GAL
        OPERATING
        0.072 HGD
     15000.00 GAL
                       DOLLARS
                         14896.
                          5415.
      OSH COST
                            PROCESS CAPITAL COST       20311.

                                               CTS/1000 GAL TREATED
          ELECTRICAL ENERGY 8 * 0.030/KUH
          MAINTENANCE MATERIAL
          LABOR 0 $10.000/HR
          DIESEL FUEL S $ 0.450/GAL
          NATURAL GAS B * ,0013/CU FT
          CHEMICALS
      COST SUMMARY
          OSM
          DEBT S 20.0 YRS AND
  PROCESS OSM COST




 7.0 %

PROCESS TOTAL COST
                          0.000
                          0.000
                          0.000
                          0.000
                          0.000
                          0.000

                          0.000
0.000
7.295
                                                        7.295
                       DOLLARS/YR

                              0.
                              0.
                              0.
                              0.
                              0.
                              0.
   0.
1917.
                                                                                   1917.
***** COST ESTIMATE FOR PACKAGE HIGH SERVICE PUMP STATN
          PROCESS FLOW
          PROCESS PARAMETER

      CAPITAL COST

          CONSTRUCTION
          OTHER RELATED COSTS
                DESIGN
              0.101 MGD
             105.00 GPM
                       DOLLARS
                         11866.
                          4314.
        OPERATING
        0.072 MGD
        50.00 GPM
      OSM COST
                            PROCESS CAPITAL COST       16181.

                                               CTS/1000 GAL TREATED
          ELECTRICAL ENERGY 0 $ 0.030/KUH
          MAINTENANCE MATERIAL
          LABOR B *10.000/HR
          DIESEL FUEL t> * 0.450/GAL
          NATURAL GAS e * ,0013/CU FT
          CHEMICALS

                                PROCESS OSM COST

      COST SUMMARY

          OSM
          DEBT I 20.0 YRS AND  7.0 X

                              PROCESS TOTAL COST
                          0.819
                          0.118
                          3.973
                          0.000
                          0.000
                          0.000
                          4.910
                          4.910
                          5.812
                                                       10.722
                       DOLLARS/YR

                            215.
                             31.
                           1044.
                              0.
                              0.
                              0.
                                                     1290.
                           1290.
                           1527.
                                                                                   2818.
                                         40
-------
****** COST ESTIMATE FOR SAND DRYING BEDS
          PROCESS FLOW
          PROCESS PARAMETER

      CAPITAL COST

          CONSTRUCTION
          OTHER RELATED COSTS
   DESIGN
 0.101 MGD
500.00 SQ FT
 OPERATING
 0.072 MGD
500.00 SQ FT
          DOLLARS
             3763.
             1368.
      OSM COST
                            PROCESS CAPITAL COST        5130.

                                               CTS/1000 GAL TREATED
          ELECTRICAL ENERGY 8 $ 0.030/KWH
          MAINTENANCE MATERIAL
          LABOR e S10.000/HR
          DIESEL FUEL @ * 0,450/GAL
          NATURAL GAS 0 * .0013/CU FT
          CHEMICALS
      COST SUMMARY
          O&M
          DEBT B 20.0 YRS AND
                                PROCESS OXM COST
                               7.0 Z

                              PROCESS TOTAL COST
             0.000
             0.076
             9.701
             O.O6S
             0.000
             0.000
                                                        9.845
             9.845
             1.843
                                                       11.688
                DOLLARS/YR

                       0.
                      20.
                    2549.
                      18.
                       0.
                       0,

                    2587.
                    2587.
                     484.
                                                                                   3072.
                                            41
-------
***** TOTAL COST ESTIMATE FOR WATER TREATMENT PLANT
      CAPITAL COST

          CONSTRUCTION
          SITEUORKfINTERFACE PIPINGrROADS 8  5.0 7.

                         TOTAL CONSTRUCTION COST

          GEN CONTRACTOR OVERHEAD & PROFIT S 12.0 7.

                                        SUBTOTAL

          ENGINEERING 8 10.0 7.

                                        SUBTOTAL

          LAND*   0.25 ACRES 0 $  2000/ACRE
          LEGAL»FISCAL» S ADMINISTRATIVE
          INTEREST DURING CONSTRUCTION

                              TOTAL CAPITAL COST
      DOLLARS

       133471.
         6674.

       140145.

        16817.

       156962.

        15696.

       172659.

          500.
         6057.
         2780,

       181995.
      OSM COST
          ELECTRICAL ENERGY 
-------



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COST.DAT File


  Example 2
COSTS PRESENTED ARE CURRENT AS OF OCTOBER 1978
CAPITAL COST FACTORS (% OF CONSTRUCTION COST):
 1 ENGINEERINGS)                =10*
 2 SITEWQRK* INTERFACE PIPINGS) =5*
 3 SUBSURFACE CONSIDERATIONS(%)
 4 STANDBY POWERS)
 5 INTEREST RATE(%)
 6 NUMBER OF YEARS
 7 LAND COST* */ACRE
UNIT COST FACTORS:
 8 ELECTRICITYr */KWH
 9 LABOR, $/HR
10 DIESEL FUEL* */GAL
11 NATURAL GAS* $/CU FT
12 BLDNG ENERGY USE,KWH/SQ FT/YR
COST INDEXES:
13 EXCAVATION(ENR SKILLED LABOR) =247*0
14 MANUFACTURED EQUIP (BLS *114) =221*3
15 CONCRETE (BLS #132)           =221*1
16 STEEL (BLS *101*3)            =262*1
17 LABOR (ENR SKILLED LABOR)     =247*0
18 PIPE S VALVES (BLS *114*901)  =236*4
19 ELECTRICAL S INSTR (BLS *117) =167*5
20 HOUSING (ENR BUILDING COST)   =254*76
21 PRODUCER PRICE INDEX          =199,7
22 ENR CONSTRUCTION* '67 BASE YR =0*0
OUTPUT(6 FOR LP»5 FOR TELETYPE)  =5
PRINTOUT(DETAILED OR SUMMARY)     =SUMMARY
                =0*0

                =0*0
                tfn**y

                =20*0

                =2000*


                = ,03

                = 10*

                = »45

                =*0013

                =102*6
    44
-------
          PROCESS.DAT File

              Example 2
ACRES=13.0
IrSrALUM FEED-LIQUID STOCK
2r40,Or 28.Or 556.Or 350.0
3r70rALUMr40 MG/L
1,15rSODIUM HYDROXIDE FEED SYSTEMS
2r40.Or28.Or5000.Or3300.0
3r200.0rSODIU« HYDROXIDErlS MG/L
IrlOrPOLYMER FEED SYSTEMS
2r40.Or 28.Or 67.Or 45.0
3r2.0rPOLYMERr0.25 MG/L
lr22rRAPID MIXr G=600
2 r 40 . 0 r 28 .0 r 2785 . 0 r 2785 . O
1r25rFLOCCULATION-HORIZ PADDLErG=50
2. 40. Or 28.Or 13000.0» 13000.0
lr33rRECT CLARIFIER-FECL3 & ALUM SLG
2r40. Or28.Or 4444.Or 4444.0
3r9rUNITS
IrSSrGRAVITY FILTRATION STRUCTURE
2r40.Or 28.Or 5560.Or 5560.0
lr41rFILTRATION MEDIA-MIXED MEDIA
2r40.Or 28.Or 5560.Or5560.0
Ir43rHYDRAULIC SURFACE HASH
2r40.0r28.0r5560.0r5560.0
lr42rBACKUASH PUMPING FACILITIES
2r40.Or28.Or 10010.Or 5560.0
lr45rWASH WATER SURGE BASINS
2r40.Or28.Or200000.Or 200000.0
lrlrCL2 FEED-CYLINDER STORAGE
2r40.Or 28.Or670.Or 450.0
3r300.0rCHLORINEr2MG/L
lr94rCLEARUELL STORAGE-BELOUI GROUND
2 r 40.0 r 28.0 r 2500000.0 r 2500000.0
lr93rFINISHED WATER PUMPING FACILITY
2r40.Or 28.Or 55.Or 28.0
3r250.OrTDH
IrSlrGRAM SLDG THICKENERrALUM 8 FECL3
2r40.Or 28.Or 850.Or 850.0
3rlrUNIT
lr86rBASKET CENTRIFUGES
2 r 40.0 r 28.0 r115000.0 r 70000.0
lr91rDEUATERED SLUDGE HAULING
2 r 40.0 r 28.0 r 200OO.0 r12000.0
3r20.0rMILES
000000000000000000000000000000000000000
ACRES=1.5
lr59rREMERSE OSMOSIS
2r5.0r3.5r5.0r3.5
3r65.0rl042.5rSULFURIC ACIDr25 MG/L
4r650.0r208.5rSODIUM HEXA P03r5 MG/L
5r300.Or29.2rCHLORINErl MG/L
lr94rCLEARUELL STORAGE-BELOU GROUND
2r5.Or 3.5r300000.Or 300000.0
lrlrCL2 FEED-CYLINDER STORAGE
2r5.0r3.5r63.0r44.0
3r300.0rCHLORINErl.5 MG/L
lr93rFINISHED WATER PUMPING FACILITY
2r5.0r3.5r8.0r3.5
3r200.0rTDH
                    45
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                 COST.DAT File


                   Example 3
COSTS PRESENTED ARE CURRENT AS OF OCTOBER 1978
CAPITAL COST FACTORS S OF CONSTRUCTION COST):
 1 ENGINEERINGS)
 2 SITEUORK* INTERFACE PIPINGS)
 3 SUBSURFACE CONSIDERATIONSS)
 4 STANDBY POWERS)
 5 INTEREST RATES)
 6 NUMBER OF YEARS
 7 LAND COST? */ACRE
UNIT COST FACTORS:
 8 ELECTRICITYr $/KUH
   LABOR» */HR
   DIESEL FUEL*
   NATURAL GAS?
   BLDNG ENERGY
$/GAL
*/CU FT
USEfKUH/SQ
                           FT/YR
 9
10
11
12
COST INDEXES:
13 EXCAVATION 
-------
               PROCES.DAT File

                  Example 3
ACRES=1*5
1*57*IN-PLANT PUMPING
2*5*0*3,5*7*5*3*5
3*75*0*TDH
1*60*PRESSURE ION EXCHANGE-SOFTENING
2*5,0*3*5*5*0*3*5
3*30,6*REGENERATION SALT
1*15*SODIUM HYDROXIDE FEED SYSTEMS
2 * 5 * 0 * 3 * 5 * 625.0 * 438 * 0
3*200*0*SODIUM HYDROXIDE* 15 MG/l.
1*1*CL2 FEED-CYLINDER STORAGE
2*5,0*3*5*63*0*44*0
3*300«0*CHLQRINE*1«5 MG/L
1*95*CLEARWELL STORAGE-GROUND LEVEL
2*5*0*3*5*500000*0*500000*0
1*93*FINISHED WATER PUMPING FACILITY
2*5.0*3*5*8*0*3*5
3*200*0*TDH
000000000000000000000000000000000000000000
ACRES=0«0
1*11*LIME FEED-NO RECALCINATION
2*1*0*0,7*8*7*6*1
3*65*0*LIME*25 MG/L
                    50
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KENT PROCESS
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-------
                                  SECTION 7

                           TROUBLE SHOOTING GUIDE
     The WATER program is designed to check the PROCES.DAT file before
computing process costs to assure that all necessary data cards are present.
If an error exists in this file, the program will print the type of error
and the line number in which the error occurred.  The program also checks
the length of the COST.DAT file to assure that it contains either 28 or 30
cards.  The following self-explanatory error messages are contained in the
program:

     1.  FORTRAN read error in card 	 of the PROCES.DAT file.  This card
         should contain the word "ACRES=" followed by a floating point
     2.
number of 15 digits or less.

Error - card with "ACRES=" is missing or misspelled.
    of the PROCES.DAT file.
                                             Check card
         FORTRAN read error in card 	 of the PROCES.DAT file.  This card
         should contain the integer 1 followed by a comma, the process
         number, and name.

         Error - this should be the first data card of a process and should
         begin with the integer 1 in column 1.  Check card 	 of the
         PROCES.DAT file.
     5.
Error in card
number.
     	 of the PROCES.DAT file.  _
Processes are numbered 1 through 28 in Table
is an invalid process
           of the
         program manual.
     6.  Error in card
     7.
              	 of the PROCES.DAT file.  Card number 	 was
expected for process 	, which requires 	 cards of data.

Error - not enough data in the COST.DAT file; this file should
have either 28 or 30 cards.
     In addition to the error messages, the program also notifies the user
when his input data exceed the valid range of the stored cost data.  In this
case, the computer extrapolates the stored data.  See example 3 in Section 6
for a sample listing of this situation.

     Errors may arise that will not cause an error message or program inter-
ruption if the required commas between the input data values are forgotten.
In this case, erroneous input values will result.  If this happens, check
the PROCES.DAT file for required commas.

                                     57

-------
                                  SECTION 8

                            WATER PROGRAM LISTING
     The WATER program is written specifically for the DEC PDP-1170 IAS
computing system.  Because this FORTRAN program may not be compatible with
all systems, it may be necessary to modify the opening and closing of data
files.  Also, FORMAT statements do not contain the Holerith or H-conversion;
instead they transmit alphanumeric data by enclosing it directly in quotation
marks.
                                     58

-------
                      WATER PROGRAM
    INTEGER OfREPEATrREDO
    REAL M»L»MAINTrLABOR»LFAFEE
    LOGICAL DLIMITrOLIMIT
    DIMENSION TDH<10)»TMILEK10)rGPMSFK10)»AMAKUP<10>r
   : AMGLC10>fVAR<22>rVARVALaO>,IRANGE<150>»NPU50)»APCENTUO)
    DIMENSION NCHEM<75)»CMNAM<75»3)rCMCST<75>»CMAMT<75>»ITYPE<150>
    DIMENSION SAVEH10)
    DOUBLE PRECISION OUTPUT»PROCES»DETAILEDfDXUrOXUrCMNAM»CH£CKl»CHECK
    DIMENSION CONSTRC150>>ELECTR<150)>MAINT<150)rLABOR<150>»
   : DIESEL< 150> »GAS< 150) f CHEM< 150>»QD< ISO) »GA< 150>fDPV< 150) i
   : OPV<150)fPROCAP<150)rCTSTOM<150>jCTSDEB<150)rCTSTL<150>>
   t NUMUN<150)»DXIK150> jQXUClSO)
    DIMENSION C<4>»E<4)>M<4)»L<4)fD<4>»G<4>»F<8>»B<4>
    DIMENSION PROCESU50,4)rCTS<150>
    COMMON NUMUN»N/A/TOP,BOTTOMrC,BfCI/B/OTOPrOBOT»ErM»L»B»GfCR9
    COMMON/C/ENGR»SITE r SUBSUR i STNB Y r RATE. YE ARS t CL AND r ELEC r
   : HOURLYrFUELrGASCST»ENFTfCIliCI2,CI3»CI4>CI5rCI6»CI7»CI8»CI9r
   J CI10
    EQUIVALENCE  'ACRES=V
    OPENSITErSUBSUR>STNBY.RATE»YEARS,CLAND
    RE AD < 1,101, END=240) ELEC r HOURLY r FUEL, G ASCST , ENFT
    READCI8»CI9jCHO
    READ<1»103»END=240) OfOUTPUT
    READ(lflOS»END=450) IVNrlW
    IF(IVN.LE.O.OR.IVN.GT.22) GOTO 620
    READ(lrl06»END=240> < VARVAL< II ) »11=1 rlW)
450 IVV=IW+1
    CLOSE
    DO 610 REDO=1»IVV
    IF(REDO.GT.l) VAR(IVN)=VARVAL
    NCASE=0
    ILINE=0
198 ILINE=ILINE+1
    READ(2il51»END=251fERR=210> CHECKfACRES
    IF NCHCK»NP <1)
    IF GOTO 245
    IF*5
    OPEN(UNIT=3»NAME='CRV.DAT'tTYPE='OLD'tACCESS='DIRECT'f
    i FORM='FORMATTED'»ASSOCIATEVARIABLE=IZN)
    READ(3'IZ»153)  (PROCESdfll > r 11 = 1 r4> iNCHEMd) »ITYPE<1>
    CLOSEITYPE
200 NCARD=2+NCHEM<1>
    GOTO 203
201 NCARD=3+NCHEM(1)
    GOTO 203
202 NCARD=4+NCHEM<1)
203 DO  205 Il=2fNCARD
    ILINE=ILINE+1
    RE AD < 2 ,154 r END=235 , ERR=235 >  NCHCK
    IF(NCHCK.NE.Il)  GOTO  235
205 CONTINUE
    GOTO 199
210 URITE(0»370) ILINE
    GOTO 1000
215 MRITE<0»371> ILINE
    GOTO 1000
220 URITE<0»372> ILINE
    GOTO 1000
225 WRITE(Or373) ILINE
    GOTO 1000
230 URITE(Of374) ILINE»NP<1>
    GOTO 1000
 1
 2
 3
 4
 5
 6
 7
 8
 9
10
11
12
13
14
15
16
17
18
19
20
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                                   59

-------
                                WATER PROGRAM (CONTINUED)
) ,NCARD
 235 URITE(Or375> ILINErIlFNP ,  ,12
     GOTO 1000
 240 URITE(Or376>
     GOTO 1000
 245 NCASE=NCASE+1
     GOTO 198
 250 NCASE=NCASE-H
 251 CLOSE
     OPEN
     DO 600 REPEAT=1,NCAS£
     ICHEH2=0
     ITDH=0
     IMILES=0
     IMAKUP=0
     IGPH=0
     IHGL=0
     IPCENT=0
     N=0
     IPAGE=0
     TCOST=0.0
     TCTSE=0.0
     TCTSH=0.0
     TCTSL=0.0
     TCTSD=0.0
     TCTSG=0.0
     TCTSC-0.0
     TE-0.0
     TH-0.0
     TL-0.0
     TD=0.0
     TG=0.0
     TC=0.0
     SUM1=0.0
     SUH2=O.O
     SUM3=0.0
     SUM4=0.0
     SUH5=0.0
     READ<2,127)  ACRES
 500 RE AD (2 r 110FEND=531)  NP »IiPVOPV MrL
     READC3'IZ+3   r!21) D,G
     READ<3'IZ+4   ,122) B,F
     CLOSE(UNIT=3)
     IFCITYPE(N).EQ.4.0R.ITYPE(N).EQ.6) GOTO  501
     OBOT=BOTTOM*PROP
     OTOP=TOP*PROP
     GOTO 502
501  OBOT=PROP
     OTOP=IRATIO*(10.0**IEXP)
502  DLIMIT=DPV(N).LT. BOTTOM. OR. DPVCN) .GT.TOP
    OLIMIT=OPV(N).LT.OBOT.OR.OPV(N).GT.OTOP
    RATIO=IRATIO* ( 10 . 0**IEXP )
    CI=F<1)*CR1 + F(2)*CR2 + F(3)*CR3 + F(4)*CR4 + F(5)*CR5 +
       F<6)*CR6 + F(7)*CR7 + F(8)*CR8
     IF(CI.LT.O.Ol) CI=CR9
     IF(CRIO.GT.O.O) CI=CR10
    CHEM(N)=0.0
    NUMUN
-------
                                  WATER PROGRAM (CONTINUED)
 505 CONSTR+C(2>*DPV+C<3)*W1+C<4>*W2)*NUMUN*CI
     BLBEN    = +B<2>*DPV*W1+B<4>*U2>*EL£C*ENFT/102.6
     FLFCTR < N ) = (E (1 > +E < ?"> *OP V < N ) +E ( 3 ) *U3+E < 4 > *W4 > *NUMUN < N) *ELEC
     MAINT(N) ^*U3iMC4)*U4)*NUMUN*CR9
     LABOR < N) = < L < 1 > iL < 2 ) *OPU < N > +L < 3 ) *U3+L < 4 ) *U4 ) *NUMUN < N > *HOURLY
     MFSEL = *OPV+D<3)*W3-H:i(4)*U4)*NUMUN*FUEL
     GAS < N )   = < G (1> +G < 2 ) *OPy < N > +G(3)*U34 G < 4 > *U4 > *NUMUN < N > *GASCST
     IF(DLIMIT) CALL ORANGE CALL ORANGEXELECTR(N)»MAINT(N),LABORi
    : (3AS(N)rOPV
     DO 515 Il=:CHEMlfICHEM2
     READ(2rill) CMCST(Il)r(CMNAM(IlrI2)>I2=lr3)
     CMAMT*RATia*365./2000.
     CHEH(N)==CHEM(N)+CMCST(I1)*CMAMT(I1)
:               **TYPE 10**
     IF(ITYPE(N).EG.10) CHEM(N)=CHEM(N)*2000.0
 515 CONTINUE
     GOTO 526
;              **TYPE  2**
 520 ICHEM1=ICHEM2+1
     ICHEM2=ICHEM2+NCHEM(N >
     DO  522  I1 = ICHEM1»ICHEM2
     READ<2f113) CMCST+M(2)*OPV(N)+M(3)*U3+M(4)*U4)*CR9
     LABOR(N)=BLDEN,OPV(N))
  528 IF=1
      ELECTR(N)=ELECTR(N)+BLDEN
      DIESEL=0.0
      GOTO 526
C             **TYPE 5**
  530 ITDH=ITDH+1
      READ(2rl23) TDH(ITDH)
      BLriEN=BLIiEN*102.6/ELEC/ENFT*CI
      ELECTR=0.0
      DENOM=D<1)-D<2)
      SLOPE=(CONSTR < N)-BLDEN)/BENOM
      BEE= < C<1> *BLDEN-D < 2)*CONSTR < N)>/DENOH
      CONSTR (N)=SLOPE*TDH< ITDH) + BEE
      BLDEN=0.0
      GOTO 526
C            **TYPE 6**
  535 IMILES=IMILES+1
      READ<2,123> TMILE1(IMILES)
      TMILES=TMILE1(IMILES)

      IF LABOR*<14.71+TMILES/17.0)
      DIESEL (N)=DIESEL < N > *TMILES
      CHEM
-------
                               MATER PROGRAM  (CONTINUED)
C             **TYPE  7**
  540  IHILES=IHILES+1
       READ<2,123) TMILE1 (IMILES)
       THILES=TMILE1 ( IMILES)
       ELECTR ( N > =ELECTR ( N > /ELEC*CI
       SLOPE=(ELECTR(N)-CONSTR=SLOPE*TMILES + BEE
       IF(TMILES.LE.20> LABOR (N)=LABOR(N>*(0. 667+0. 0667*TMILES>
       IF(TMILES.GT.20> LABOR (N)=LABOR(N>*< 1 ,0+0.05*TMILES>
       MAINT(N)=MAINT(N)*TMILES/5.0
       GAS(N>=0.0
       DIESEL(N)=DIESEL(N>*TMILES/5.0
       ELECTR(N)=0.0
       BLDEN=0.0
       CHEM(N>=0.0
       GOTO 526
C               **TYPE 8**
  545  IMAKUP=IMAKUP+1
      READ(2,123> AMAKUP(IMAKUP)
       ICHEM2=ICHEM2+1
      READ(2rlll) CMCST(ICHEM2) r (CMNAM(ICHEM2»I1 ) , 11=1 ,3)
      CMAMT(ICHEM2)=OPV(N>*RATIO*365./2000.*AMAKUP(IMAKUP>/100.
      CHEM(N)=CMCST(ICHEM2)*CMAMT(ICHEM2>
      GOTO 526
C                **TYPE 9**
  550 IGPH=IGPM+1
      READ<2rl23> GPMSFKIGPM)
      GPMSF=GPMSF1 ( IGPM)
      IF(GPMSF.EQ.O.O) GPMSF=2.0
      W1=DPV(N)/GPMSF
      U2=U1**2
      W3=U1**3
      BOTTOM=BOTTOM/2 . 0
      TOP=TOP/5.0
      DLIMIT=U1,LT. BOTTOM. OR. Ul.GT. TOP
      CONSTR(N)=*CI
      BLDEN=+B(2>*UH-B(3)*U2+B(4)*W3)*ELEC*ENFT/102.6
      IF(DLIMIT)  CALL  DRANBECCONSTRCN) rBLDENfUi )
      U1=OPV(N>/GPMSF
      U3=U1**3
      ELECTR = *UH-E(3)*W2+E<4)*U3)*ELEC
      MAINT*U2+M<4>*U3)*CR9
      LABOR*U2+L<4)*U3)*HOURLY
      OLIMIT=U1.LT. BOTTOM. OR. Ul.GT. TOP
      IF(OLIMIT) CALL ORANGE (ELECTR(N) rMAINT(N) ,LABOR(N) ,DIESEL r
     :  GAS(N),W1)
      IF(DLIMIT.OR.OLIMIT)  IRANGE(N)=1
      ELECTR ( N) =ELECTR ( N > *GPMSF/2 . 0+BLDEN
      DIESEL=0.0
      GAS(N)=0.0
      ICHEM1=ICHEM2+1
      ICHEM2=ICHEM2+NCHEM < N )
      BO 548 Il=ICHEMlfICHEM2
      READ(2»113> CMCST(Il)rCMAMT(Il),(CMNAM(Il»I2)rI2=lr3)
      CMAMT*365./2000.
 548  CHEM(N)=CHEM(N)+CMCST(I1>*CMAMT(I1)
     GOTO 526
              **TYPE  11**
 554  IMGL=IMGL+1
     READ(2rl23) AMGL(IMGL)
     SAVE1(IMGL)=CONSTR(N)*AMGL(IMGL>/D(1)
     CONSTR(N)=0.0
     DIESEL =0.0
     GOTO 526
              **TYPE  12**
 557 IPCENT=IPCENT+1
     READ(27l23) APCENT(IPCENT)
     CONSTR(N)=CONSTR(N>*APCENT(IPCENT)/100.
     ELECTR ( N > =ELECTR ( N ) *APCENT ( IPCENT ) /1 00 ,
     MAINT(N)  =MAINT(N) *APCENT(IPCENT)/100.
     LABOR/100.
     DIESEL(N>=DIESEL(N)*APCENT(IPCENT)/100.
     GAS=0.0
     GOTO 526
 526 TCOST=TCOST+CONSTR(N)
     GOTO 500
 235
 236
 237
 238
 239
 240
 241
 242
 243
 244
 245
 246
 247
 248
 249
 250
 251
 252
 253
 254
 255
 256
 257
 258
 259
 260
 261
 262
 263
 264
 265
 266
 267
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 273
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 279
 280
 281
 282
 283
 284
 285
 286
 287
 288
 289
 290
 291
 292
 293
 294
 295
 296
 297
 298
 299
 300
 301
 302
 303
 304
 305
 306
 307
 308
309
310
311
312
313
                                    62
-------
                               WATER  PROGRAM   OHP=10.
    IF GOTO 551
    IF(SUBTL3.LE.O.O) GOTO 552
    LFAFEE=60.0+. 0447*SUBTL.3-6.406E-B*SUBTL3**2+3.673E-14*SUBTL3**3
    BR=SUBTL3/1.E4
    CSTINT= <1.75+.252*BR-2.105E-3*BR**2+9.013E-6*BR**3)/
   : 24.*RATE*SUBTL3/100.
    GOTO 555
551 LFAFEE=125570. +6.823E-4*SUBTL3-115564. *EXP (-6.015E-8*SUBTL3)
    BR=SUBTL3/1.E6
    CSTINT= < 16.03+1.02*BR-1.188E-2*BR**2+3. 7E-5*BR**3 > /
   :       24.*RATE*SUBTL3/100.
    GOTO 555
552 LFAFEE=0.0
    CSTINT=0.0
555 TCAP=SUBTL3 + CSTLND + LFAFEE + CSTINT
    W1=(1.+RATE/100.)
    DEBT=TCAP*RATE/100.*W1**YEARS/(W1**YEARS-1.)
    IMGL=0
    DO 570 1 = 1.N
    IF(TCOST.LE.O.O) GOTO 556
    GOTO 558
556 U2=0.0
    GOTO 559
558 U2=CONSTR
    CTSLAB=LABOR 
    CTSDIE=DIESEL /CTS(I)
    CTSCHE=CHEM /CTS  =PRBEBT/CTS(I>
    CTSTOM (I) =CTSELE+CTSMAI+CTSLAB+CTSHIE+CTSGAS+CTSCHE
    IF IM6L=IMGL+1
    IF.EG,11> TOM=SAVE1
    TL=TL  + LABOR(I)              p
    TD=TD  + DIESEL WRITE  (0.300)
    IF(IPAGE.EQ.O)  IPAGE=2
    :  OPVr
     «RITE<0.302)  CONSTR(I)FOTHERrPROCAP(I>
     GOTO 565
314
315
316
317
318
319
320
321
322
323
324
325
326
327
328
329
330
331
332
333
334
335
336
337
338
339
340
341
342
343
344
345
346
347
348
349
350
351
352
353
354
355
356
357
358
359
360
361
362
363
364
365
366
367
368
369
370
371
372
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374
375
376
377
378
379
380
381
382
383
384
385
386
387
388
389
390
391
392
                                     63
-------
UATER PROGRAM (CONTINUED)
540 IF=C1D/NUMUN
    QA  rGD ,DPV .
565
570
571
575
578
580
581
582
583



700


705





710



715



720



725
    aD=QD(I>*NUMUN
    QA(I)=QA(I)*NUMUN NUMUN(I>rCONSTR.OTHER»PROCAP.NUMUN
    URITE<0»305> ELECrCTSELE.ELECTR .CTSMAI»MAINT< I> .HOURLY.
   :  CTSLABrLABOR(I).FUEL.CTSDIE.DIESEL
    URITE (0 » 306 > GASCST t CTSGAS , GAS < I ) , CTSCHE t CHEM < I > > CTSTOM ( I ) , TOM
    URITE CTSTOM .TOM» YEARS .RATE»CTSDEB(I > .PRDEBT.
   :  CTSTL
    URITE<0*308> TCOSTrSITE.CSTSIT
    IFCSUBSUR.GT.O.)  WRITE<0»309>  SUBSUR.CSTSUB
    IFtSTNBY.GT.O.) URITE<0.310> STNBY.CSTSTN
    WRITECOfSll) SUBTLl»OHP»CSTOHPfSUBTL2»ENGRfCSTENG»SUBTL3
    ICLAND=CLAND
    IFCACRES.GT.O.) URITE(Or312) ACRES jICLANDf CSTLND
    URITE(0»313) LFAFEE»CSTINT»TCAP
    URITE(Of314) ELEC»TCTSE»TEfTCTSHrTHfHOURLY»TCTSLfTL»FUELrTCTSDrTD
    URITE(0»315) GASCST f TCTSGrTGrTCTSCfTCf SUH2rSUM4
    URITE(0>316) SUM2 » SUM4 » YEARS j RATE rSU«l» DEBT » SUMS f SUMS
    ICHEM2=0
    ITDH=0
    IHILES=0
    IMAKUP=0
    IGPM=0
    IMGL=0
    IPCENT=0
    13=0
   WRITE
   GOTO 578
   URITE N
   URITE<0»319)
   DO 590 1=1 rN
   IF(I3-45)  583 r 580 r 581
   IF(N-I) 581.583.581
   IF  GOTO 583
   13=0
   URITE<0,300)
   URITE N
   URITE<0.319>
   13=13+8
   URITE(Or320) IF (PROCES .QA .DPV
   13=13+1
   GOTO < 735 .735.700. 705. 710. 715.715, 720. 725. 735. 730. 732) ITYPE( I)
   URITECOr331) NUMUN(I)
   13=13+1
   GOTO 735
   U3=DPU(I)*NUMUN(I)*7.48/OD(I)/694.44
   WRITE(Of332)  W3
   U3=DPV(I)*NUMUN(I)
   URITE(Of341) U3FNUMUNCI)
   13=13+3
   GOTO 735
   ITDH=ITDH+1
   URITE(Or333>  TDH(ITDH)
   13=13+1
   GOTO 735
   IMILES=IMILES+1
   WRITE(Or334>  TMILE1 (IMILES)
   13=13+1
   GOTO 735
   IHAKUP=IMAKUP+1                   '
   URITE336)  GPHSFKIGPM)
   13=13+1
   GOTO 735
                                                393
                                                394
                                                395
                                                396
                                                397
                                                398
                                                399
                                                400
                                                401
                                                402
                                                403
                                                404
                                                405
                                                406
                                                407
                                                408
                                                409
                                                410
                                                411
                                                412
                                                413
                                                414
                                                415
                                                416
                                                417
                                                418
                                                419
                                                420
                                                421
                                                422
                                                423
                                                424
                                                425
                                                426
                                                427
                                                428
                                                429
                                                430
                                                431
                                                432
                                                433
                                                434
                                                435
                                                436
                                                437
                                                438
                                                439
                                                440
                                                441
                                                442
                                                443
                                                444
                                                445
                                                446
                                                447
                                                448
                                                449
                                                450
                                                451
                                                452
                                                453
                                                454
                                                455
                                                456
                                                457
                                                458
                                                459
                                                460
                                                461
                                                462
                                                463
                                                464
                                                465
                                                466
                                                467
                                                468
                                                469
                                                470
                                                471
                                                472
        64
-------
                              WATER PROGRAM (CONTINUED)
 730 IMGL=IMGL+1
     WRITE(Or337> AMGL(IMGL)
     13=13+1
     GOTO 735
 732 IPCENT=IPCENT+1
     URITE(0»331> NUMUN(I)
     WRITE(0>339> APCENT(IPCENT)
     13=13+2
     GOTO 735
 735 IF.LE,0.0> GOTO 585
     WRITE(Or321) CMCST(I2)j(CMNAM(I2fI4)rI4=l>3)
     13=13+1
     GOTO 585
 584 URITE(Qf328> CMCST(12)'i(CMNAH(12*14)r14=1r3>
     13=13+1
 585 CONTINUE
 590 CONTINUE
     URITE(0»322> TCOSTrTCAP*SUM2i>SUM1,SUM3
     13=13+4
     SUM6=CSTSIT+CSTSUB+CSTSTN
     WRITE (0,329) SUM6 r OHP j CSTQHP r CSTENG > ACRES r CSTLNDtL.FAFEE r
    i CSTINTfTCAP
     13=13+11
     TE=TE/ELEC
     TL=TL/HOURLY
     TD=TD/FUEL
     TG=TG/GASCST
     WRITE(0>330) TE,TMfTLfTDrTG»TC
     13=13+3
     IF(N-l.EQ.O) GOTO 7778
     IF(I3--60.GT.O) WRITE(Or300)
     URITE(0»351)
     13=13+2
     DO 7777 1=1iN
     IF(13-63.LT.O) GOTO 7776
     WRITE(0»300)
     WRITE(O»354>

7776 TMP1=ELECTR(I)/ELEC
     TMP2=LAEOR(I)/HOURLY
     TMP3=DIESEL(I)/FUEL
     TMP4=GAS(I)/GASCST
     WRITE(0,350) I.TMP1»MAINT(I),TMP2,TMP3,TMP4.CHEM(I)
7777 13=13+1
7778 18=0
     DO 592 1=1»N
 592 I8=I8+IRANGE(I)
     IFdS.EG.O) GOTO 593
     IF(58-I3-I8.LT.O> URITE(0»300)
     IF(58-I3-I8.LT.O> 13=0
     18=0
 593 DO 596 1=1rN
     IF(IRANGE(I>.EQ.O) GOTO 596
     IF(IS.GT.O) GOTO 594
     IF(I3-63.EQ.O> WRITE(0,30O)
     IF(I3-63.EQ.O) 13=0
     URITE(Oi352)
     18=18+1
     13=13+4
 594 IZ=1+(NP(I)-1>*5
     OPEN(UNIT=3 »NAME='CRM.DAT',TYPE='OLD'tACCESS='DIRECT'r
    : FORM='FORMATTED'»ASSOCIATEVARIABLE=IZN)
     READ(3'IZ,125) BOTTOM r TOP fPROP,IRATIO,IEXP
     CLOSE(UNIT=3)
     IF(ITYPE(I).EQ.4.0R.ITYPE(I).EQ.6)  GOTO 597
     OBOT=BOTTOM*PROP
     OTOP=TOP*PROP
     GOTO 595
 597 OBOT=PROP
     OTOP=IRATIO*(10.0**IEXP)
 595 URITE(Or353) I r (PROCESd , II > tll = l »4> ,BOTTOM?TOPrDXU(I> rDPMd ) t
    : OBOT,OTOPrOXU(I)»OPM(I)
     13=13+1
473
474
475
476
477
478
479
480
4B1
482
483
484
485
486
487
488
489
490
491
492
493
494
495
496
497
498
499
500
501
502
503
504
505
506
507
508
509
510
511
512
513
514
515
516
517
518
519
520
521
522
523
524
525
526
527
528
529
530
531
532
533
534
535
536
537
538
539
540
541
542
543
544
545
546
547
548
549
550
                                   65
-------
                      HATER PROGRAM (CONTINUED)
 596 CONTINUE                                                               551
     OPEN(UNIT=lrNAME='COST.DAT'rTYPE='QLD')                                552
     IF(I3.GT.47> URITE(Or300>                                              553
     READ(lrl04> BrF                                                        554
     WRITE(Or323) BrF                                                       555
     URITE(Or324) ENGRrELECrCIlrSITErHOURLYrCI2                             556
     WRITE(0»325) SUBSURrFUELrCI3rSTNBYrGASCST»CI4rRATErENFTrCI5            557
     WRITE(Or326) YEARSrCI6rACRESrCI7rCLANDrCI8rCI9                         558
     IF(CIIO.GT.O.OI) WRITE (Or327) CI10                                    559
     CLOSE(UNIT=1>                                                          560
 600 CONTINUE                                                               561
     CUOSE(UNIT=2)                                                          562
 610 CONTINUE                                                               563
     GOTO 1000                                                              564
 620 WRITE(Or338) IVN                                                       565
1000 STOP                                                                   566
 100 FORMAT(//6(34XrF9.2/)r34XrF9.2)                                        567
 101 FORMAT(/4(34XrF9.2/)r34XrF9.2)                                         568
 102 FORMAT(/9(34XrF9.2/)r34XrF9.2)                                         569
 103 FORMAT(34XfIl/34XrA8)                                                  570
 1O4 FORMAT(4A4r8A4)                                                        571
 105 FORMAT(Irll)                                                           572
 106 FORMAT(10F)                                                            573
 110 FORMAT(2XrI>                                                           574
 111 FORMAT(2XrFr3A8)                                                       575
 113 FORMAT(2Xr2FfSAB)                                                      576
 114 FORMAT(2XrIrF)                                                         577
 115 FORMAT(2Xr4F)                                                          578
 120 FORMAT(4A8r2A6r3E9.2rI4rI2iIlrI2)                                      579
 121 FORMAT<4E10.2r4E10.2)                                                  580
 122 FORMAT<4E10.2r8F5.3)                                                   581
 123 FORMAT(2XrF)                                                           582
 125 FORMAT(44Xr3E9.2rI4rI2)                                                583
 127 FORMAT(6XrF)                                                           584
 151 FORMAT(-A6rF>                                                           585
 152 FORMAT(2I)                                                             586
 153 FORMAT(4A8r45XrIlrI2>                                                  587
 154 FORMATU)                                                              588
 300 FORMAT(1H1)                                                            589
 301 FORMAT(//' ***** COST ESTIMATE FOR '4A8//T48r'DESIGN'T66r              590
    : 'OPERATING'/Tl2r 'PROCESS FLOWT41 rF10.3r ' MGD'T61rF10.3r              591
    t '  HGD'/T12r'PROCESS PARAMETER'T41rF10.2r!X»A6rT61FF10.2rIXrA6/)       592
 302 FORMAT(T8r'CAPITAL COST'T55r'DOLLARS'//                                593
    S T12r'CONSTRUCTION'T52rF11.0/T12f'OTHER RELATED COSTS'T52rFll.O/       594
    ! T53r'	'/T30r'PROCESS CAPITAL COST'T52rFll .O//               595
    t TBr'OSM COST'T49r'CTS/1000 GAL TREATED'TSlr'DOLLARS/YR'/)             596
 303 FORMAT(//' ***** COST ESTIMATE FOR'r!Xr4A8r' CI3r' UNITS)'//          597
    : T47r'DESIGN'T63r'OPERATING'/                                          598
    : T12r'PROCESS FLOW (PER UNIT)'T41rFll.3r' MGD'rT61rFll,3r' MGD'/       599
    5 T12r'PROCESS PARAMETER (PER UNIT)'T41rFll.2rlXrA6rT61rFll.2r          600
    : !XrA6/)                                                               601
 304 FORMAT(T8r'CAPITAL COST (TOTAL FOR'I3r' UNITS)'T55»'DOLLARS'//         602
    S T12r'CONSTRUCTION'T52rF11.0/T12r'OTHER RELATED COSTS'T52rFll.O/       603
    : T53r'	'/T30r'PROCESS CAPITAL COST'T52rFll .O//               604
    : TSr'OSM COST (TOTAL FOF'ISr' UNITS)'T49r'CTS/1000 GAL TREATED'        605
    t T81r'DOLLARS/YR'/)                                                    606
 305 FORMAT(T12r'ELECTRICAL ENERGY B *'F6.3r'/KUH'T53rF10.3rT79r            607
      Fll.0/T12r'MAINTENANCE MATERIAL'T53rF10.3rT79rFll .O/                  608
      T12r'LABOR B *'F6.3r'/HR'T53rF10.3rT79rFll.O/                         609
      T12r'DIESEL FUEL S *'F6.3r'/GAL'T53>F10.3rT79rFll.0)                  610
     FORMAT(T12r'NATURAL GAS @ *'F6.4r'/CU FT'T53rF10.3rT79rFll.O/          611
      T12r'CHEMICALS'T53rF10.3rT79rFll.O/                                   612
        T53 r '	' T80 r'	' /T34 r                             613
      'PROCESS OSM COST'F13.3rT79rF11.0/>                                    614
 307 FORMAT(T8r'COST SUMMARY'//                                             615
    J T12r'08M'T52rF11.3rT79rF11.0/T12r'DEBT @'                             616
    : FS.lr'  YRS AND'FS.lr' %'T52rFll.3rT79 rFll.O/                         617
    *  TS3» '—»-.-•—.«.••—.-——'T8O» '———•———.—.———'/                                  &IQ
    :  T32r'PROCESS TOTAL COST'T52»F11.3rT79 rFll.O)                        619
 308 FORMAT(//' ***** TOTAL COST ESTIMATE FOR WATER TREATMENT PLANT'        620
    S ///T8r'CAPITAL COST'T55r'DOLLARS'//                                   621
    : T12r'CONSTRUCTION'T52rF11.0/                                          622
    ! T12r'SITEUORKrINTERFACE PIPINGrROADS O'FS.lt'  %'T52rF11.0)            623
 309 FORMAT(T12r'SUBSURFACE CONSIDERATIONS S'FS.lr'  %'T52rF11.0>            624
 310 FORMAT(T12r'STANDBY POWER S'FS.lr' X'T52rF11.0)              .    :    625
306
                                  66
-------
                         WATER PROGRAM (CONTINUED)
311 FORMAT(T53r'	'/T27»'TOTAL CONSTRUCTION COST'T52rFll .O//      626
   J T12»'GEN CONTRACTOR OVERHEAD S PROFIT @'F5.1r' %'T55»F8.0/            627
   } T53»'	'/T42r'SUBTOTAL'T52»F11.O//                           628
   : T12i'ENGINEERING B'F5.1»' Z'T52»F11.0/T53r'	'/              629
   : T42»'SUBTOTAL'T52rF11.0/>                                             630
312 FORMAT(T12r'LAND,'F7.2»' ACRES 6 *'I6»'/ACRE'T52»F11.0)                631
313 FORMAT(T12r'LEGAL,FISCAL, S ADMINISTRATIVE'T52,F11.O/                  632
   : T12r'INTEREST DURING CONSTRUCTION'T52,F11.O/                          633
   . T53,'	'/T32,'TOTAL CAPITAL COST'T52,F11.0//)                634
314 FORMAT(T8,'OSM COST'T49,'CTS/1000 GAL TREATED'                         635
   t T81r'DOLLARS/YR'//                                                    636
   : T12,'ELECTRICAL ENERGY                                     644
316 FORMATFll.l»lX*A6»F10.1»lXfA6fF10.0»Fll.O»         656
   : 3F8.3)                                                                657
321 FORMAT                                     660
323 FORMAT(///1X»4A4»8A4/)                                                 661
324 FORMAT 'T34» '-'        663
   : F8.2»T47>'ELECTRICITY* $/KUH'T80»'='F6.2rT91f'EXCAVATION'             664
   :,' (ENR SKILLED LABOR)='F7.l/T5f'SITEUORK.INTERFACE PIPING(X) ='       665
   : F8.2,T47r'LABORr */HR'T80»'='F6.2fT91.'MANUFACTURED EQUIP'            666
   t,' '='F6.3»T91»'CONCRETE '='F8.2rT47>'NATURAL GASf */CU FT'T80»       670
   • ' = 'F6.4»T91»'STEEL                                      681
329 FORMAT(//T56»'SITEWORK»SUBSURFACErSTNBY POWER'fT88»F10. 0/T66r          682
   J 'GEN CON OH S P.'rF5.1r'%',T88fF10.0/T76r'ENGINEERING'.T88.F10.0/     683
   : T69r'LAND»'»F7.2»' ACRES'rT88>F10.0/                                  684
   : T69»'LEGALrFISCAL»ADMIN'»T88rF10.0/T70r'INT DURING CONSTR'»           685
   : T88»F10.0/T87»'	'/T74»'TOTAL CAPITAL'» T88»F10.0)           686
330 FORMAT(//' TOTAL OXM:'»T21»'KWH'»8Xf'MATERIALSr*'»9X»'LABORrHR'r       687
   5 9X»'DIESELfGAL'r9Xr'NAT GAS.CU FT'»9X»'CHEMICALSf*'/                  688
   : T16»F11.0,5X»F10.0*8XVF9.0r9XrF10.0,9X,F13.0rlOX»F10.0>               689
331 FORMAT(T7i'NUMBER OF UNITS ='»I3>                                      690
332 FORMAT(T7»'EMPTY BED CONTACT TIME AT DESIGN FLOW ='»F5.1»' MIN')       691
333 FORMAT(T7r'TBH ='rF6.1»' FEET')                                        692
334 FORMAT(T7r'ONE WAY MILES ='»F6.1)                                      693
335 FORMAT(T7»'MAKEUP LIME.='rF6.1,' %')                                   694
336 FORMAT(T7»'LOADING RATE ='»F5.1f' GPM/SO FT')                          695
337 FORMAT(T7f'SLUDGE CONCENTRATION ='»F8.0>'  MG/L')                       696
338 FORMATC PROGRAM EXIT.  CHECK THE 'COST.DAT" FILE'rI6f' IS NOT'        697
   J ' A VALID COST FACTOR NUMBER.')                                       698
339 FORMAT(T7>'COSTS CALCULATED FOR'rF7.2»' 7.  OWNERSHIP OF REGIONAL'       699
   : ' FACILITY')                                                          700
341 FORMAT                                             703
351 FORMAT(/' PROCESS OXM')                                                704
                                  67
-------
                               UATER PROGRAM (CONTINUED)
352 FORMATC/' COSTS FOR THE FOLLOWING PROCESSES HAVE BEEN'                 705
   : ' EXTRAPOLATED.  VALID RANGES FOR INPUT DATA AREt'//                  706
   i T17r 'PROCESS' fT43r 'DESIGN RANGE' 7 T69r 'YOUR INPUT' rT86»                707
   : 'OPERATING RANGE' >T114r 'YOUR INPUT')                                  708
353 FORMAT(lX7l2rlX»4A8fF9.1>' TO' >F11 . 1 , !X»A6rFll .1 , F13. 1 » ' TO'r          709
   I Fll.lrlXrA6rFll.l)                                                    710
354 FORHAT(//' PROCESS OXM' rT21 r 'KUH' rSXf 'MATERIALS,*' ,9X, 'LABOR* HR' ,      711
   : 9Xf 'DIESELrGAL'»9X» 'NAT GASfCU FT' f9X» 'CHEMICALS,*' >                  712
37O FORHATC FORTRAN READ ERROR IN CARD',I5f' OF THE PROCES.DAT FILE.'     713
   : ' THIS CARD SHOULD CONTAIN THE WORD 'ACRES' FOLLOWED BY'/             714
   : ' A FLOATING POINT NUMBER OF 15 DIGITS OR LESS')                      715
371 FORMAT<' ERROR-CARD WITH 'ACRES=' MISSING OR MISSPELLED.'/             716
   : ' CHECK CARD'rI5»' OF THE PROCES.DAT FILE.')                          717
372 FORMAT<' FORTRAN READ ERROR IN CARD'»I5»' OF THE PROCES.DAT'           718
   : ' FILE'/' THIS CARD SHOULD CONTAIN THE INTEGER "1" '                  719
   : 'FOLLOWED BY'/' A COMMAr THE PROCESS NUMBER AND THE PROCESS'          720
   : ' NAME')                                                              721
373 FORMAT*' ERROR-THIS SHOULD BE THE FIRST DATA CARD'/' OF A'             722
   : ' PROCESS AND SHOULD BEGIN WITH THE INTEGER '!' IN COLUMN I'/         723
   ; ' CHECK CARD'fI5»' OF THE PROCES.DAT FILE')                           724
374 FORMAT<' ERROR IN CARD'rISj' OF THE PROCESrDAT FILE'/lXfI5»            725
   I ' IS AN INVALID PROCESS NUMBER.  PROCESSES'/' ARE NUMBERED'           726
   J ' 0 THRU 129 IN TABLE 2 OF THE PROGRAM MANUAL')                       727
375 FORMATC ERROR IN CARD'.ISr' OF THE PROCES.DAT FILE'/' CARD'           728
   : ' NO.'flSr' WAS EXPECTED FOR PROCESS' r I4» !Xf4A8> ' r WHICH'             729
   : ' REQUIRES' r!3»' CARDS OF DATA.')                                     730
376 FORMATC ERROR-NOT ENOUGH DATA IN THE COST. DAT FILE.'/                 731
   : ' THIS FILE SHOULD HAVE EITHER 28 OR 30 CARDS')                       732
    END                                                                    733
    SUBROUTINE DRANGEC Ylf Y2,X>                                             734
    DIMENSION C<4)»B<4)fNUMUN(150)jVAR(22)                                 735
    COMMON NUMUNrN/A/TOP»BOTTOM»C»B»CI                                     736
    COMMON/C/ENGR r SITE » SUBSUR , STNBY » RATE , YEARS > CLAND , ELEC »                 737
   : HQURLY7FUEL»GASCSTrENFTrCIlrCI2rCI3rCI4rCI5rCI6»CI7rCI8rCI9*          738
   S CI10                                                                  739
    EQUIVALENCE *X1+C<3)*X1**2+CC4>*X1**3)                                752
    C2=(C(1)+C(2>*X2+C(3)*X2**2+C(4)*X2**3)                                753
    Bl= B<1)+B(2)*X1+B<3)*X1**2+B(4)*X1**3                                 754
    B2= B(1)+B(2)*X2+B(3)*X2**2+B(4)*X2**3                                 755
    ALX1=ALOG(X1>                                                          756
    ALX2=ALOG -ALOG ( Cl ) > /DENOM                                          763
    Y1=EXP*NUMUN*CI                                    764
120 IF GOTO 125                                   765
    Y2=0.0                                                                 766
    GOTO 130                                                               767
125 AB1= /DENOM                                          769
    Y2=EXP < AB1+AB2*ALOG  *ELEC*ENFT/102 . 6                                770
130 RETURN                                                                 /71
    END                                                                    772
    SUBROUTINE ORANGE < Yl , Y2, Y3r Y4r Y5»X)                                    773
    REAL H,L                                                               r/4
    DIMENSION E<4)»M(4)rL(4)»D(4)>G(4)rNUMUN(150)»VAR(22>                   775
    COMMON NUMUNfN/B/OTOPfOBQT>E,MrL»DrGrCR9                               776
    COMMON/C/ENGR , SI TE , SUBSUR » STNBY , RATE , YEARS r CLAND , ELEC ,                 777
   ',  HOURLY»FUELrGASCSTjENFTTCIlfCI2rCI3»CI4iCI5jCI6rCI7rCI8»CI9r          778
   !  CI10                                                                  779
    EQUIVALENCE(ENGRfVAR(l)>                                               780
    Fl(AlfA2) = (ALOG(Al)*ALX2-ALOG=(ALOG(A2)-ALOG )/DENOM                                    782
    IF(X.LE.O.O) GOTO 98                                                   7B,5
    GOTO 99                                                                7S4
                                 68
-------
                            WATER PROGRAM  (CONTINUED)
 98 Yl=--0.0
    Y2--0.0
    Y3=0.0
    Y4=0.0
    Y5--0.0
    GOTO 160
 99 IF(X-OTOP.GT.O.O) GOTO 100
    X1=OBOT
    X2<=2.0*OBOT
    GOTO 110
100 X1=OTOP
    X2= ( OTOP-f OBOT ) /2 . 0
110 X12=X1**2
    X13=X1**3
    X22=X2#*2
    X23=X2**3
    El=E-tE<2)*Xl+E<3)*X12+E<4>*X13
    E2=E<1)+E(2)*X2+E< 3 > *X22+E < 4 >*X23
    ALX2=ALOG(X2)
    ALX1<=ALQG(X1>
    11ENOM=ALX2--AL.X1
    IF(E1.GT.O.O.AND.E2.GT.O.O)  GOTO  115
    Yl=0,0
    GOTO 120
115 AE1-FKE1»E2>
    AE2=F2
    Y1=EXP
120 TM1-M<1> H-i<2)*Xl+M(3)*X12+M<4)*X13
    TM2-M(1)+M(2)*X2+H(3)*X22+M< 4)*X23
    IF  GOTO 135
    Y3=0.0
    GOTO 140
135 AL.1=F1(TL1»TL2)
    AL2=F2(TL1»TL2)
    Y3=EXP ( Al_ 1+AL2*ALOG ( X ) ) *HOURLYKcNUMUN (N )
140 Dl=D(l)+n(2)*Xl+D<3)*X12+D(4)*X13
    Il2=D< 1) +D ( 2 ) *X2+D'< 3 ) *X22+D ( 4 ) *X23
    IF  GOTO 145
    Y4=0.0
    GOTO  ISO
145 ADl=FKDlrIi2)
    An2=F2(Ill»ri2)
    Y4=EXP < ADI +AD2*ALOG (X) ) *FUEL*NUMUN < N )
150 Gl=G(l)+G(2)*XH-G(3)*X12tG(4)*X13
    G2=G(1)+G < 2)*X2+G < 3)*X22+G(4)*X23
    IF(Gl.GT.O.O.ANn.G2.GT.O.O)  GOTO 155
    Y5=0,0
    GOTO  160
155 AGl--FKGlfG2)
    AG2=F2(G1»G2)
    Y5=EXP(AG1+AG2*ALOG
-------
                                  SECTION 9

                                CRV.DAT FILE
     The CRV.DAT file contains all the cost information for the water treatment
processes.  The WATER program reads this file in a random or direct access
mode.  Each line of data contains 80 characters, so that if a record length
of 80 is established on the system, the location of the first line of data
of any process is given by:

                          (NP-1) x 5 + 1

where NP is the number of the process shown in Table 4.  For example, data
for process 21, RAPID MIX, G=300, begins at line (21-1) x 5 + 1 = 101 and
continues through line 105.  If the CRV.DAT is not established on the
computing system as a random or direct access formatted file, the WATER
program will have to be modified accordingly.

     A copy of the CRV.DAT file is given on the following pages.  The file
is 655 lines long and contains 52,400 characters.  Some systems may include
a carraige return and line feed at the end of each line of data.  In this
case, the file will contain 82 characters per line and a total of 53,710.
characters.
                                     70
-------
                        CFW.DAT FILE
CL2 FEED-CYLINDER STORAGE
  1.20E+04  9.43E+01 -1.44E-02
  1.53E+03  2.39E+00 -4.38E-04
  0,OOE+OO  O.OOE+00  O.OOE+00
  8.19E+03  1.13E+02 -1.22E-02
CL2 FEED-ON SITE STORAGE TANK
  1.83E+05 -7.18E-01
  4.15E+03  2.14E-01
  O.OOE+00  O.OOE+00
 -2.63E+02  3.23E+00
CL2 FEED FROM RAIL CAR
  1.52E+05  2.44E+00  3.75E-04
  4.15E+03  2.14E-01  3.55E-05
  O.OOE+00  O.OOE+00  O.OOE+00
 -2.63E+02  3.23E+OO -3.1SE-04
                      1.97E-03 -7.97E-OS
                      3.55E-05 -1.61E-09
                      O.OOE+00
                      3.15E-04
                                LB/DAVLB/DAY l.OOE+01 l.OOE+04 l.OOE+00   1  101
                                8.69E-07  5.45E+02  9.98E-01  7.14E-04 -5.05E-08
                                2.68E-08  4.01E+02  7.93E-01 -5.59E-05  2.66E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                8.03E-07 0.00 0.50 0.00 0.00 0.06 0.04 0.06 0.34
                                LB/DAYLB/DAY 2.00E+03 l.OOE+04 l.OOE+00   1  101
                                          9.13E+02  1.84E-01  1.22E-04 -6.32E-09
                                          6.3SE+02  1.92E-01 -2.55E-05  1.14E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                9.92E-09 0.00 0,81 0.00 0.02 0.08 0.03 0.05 0.01
                                LB/DAYLB/DAY 2.00E+03 l.OOE+04 l.OOE+00   1  101
                                1.94E-08  9.13E+02  1.84E-01  1.22E-04 -6.32E-09
                                1.61E-09  6.96E+03  3.80E-01 -4.92E-OS  2.12E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                9.92E--09 0.00 0.82 0.00 0.00 0.06 0.04 0.06 0.02
CHLORINE DIOXIDE GENERATINGrFEEDLB/DAYLB/DAY l.OOE+01 3.50E+03 l.OOE+00  17-1201
  2.74E+04  2.55E+02 -7.17E-02
  1.47E+03  5.30E+00 -1.70E-03
  O.OOE+00  O.OOE+00  O.OOE+00
  1.28E+04  6.SOE+01 -2.20E-02
OZONE GENERATION SYSTEMS
  4.12E+04  1.78E+03 -7.83E-01
  1.26E+03  1.83E+01 -6.29E-03
  O.OOE+00  O.OOE+00  O.OOE+00
                                8.09E-06  2.94E+03  6.31E+00  2.61E-04 -8.13E-08
                                1.89E-07  5.88E+02  1.85E+00 -3.19E-04  2.99E-08
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                2.72E-06 0.00 0.41 0.00 0.00 0.32 0.02 0.03 0.22
                                LB/DAYLB/DAY l.OOE+01 3.50E+03 l.OOE+00   1    1
                                1.31E-04  1.75E+04  3.33E+03 -6.98E-01  1.55E-04
                                9.52E-07  4.74E+02  1.06E+00 -1.37E-05 -2.61E-08
                                O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00
  6.71E+03  1.60E+01  1.06E-02 -1.58E-06 0.00 0.79 0.00 0.00 0.17 0.00 0.00 0,04
OZONE CONTACT CHAMBER
  4.06E+03  4.93E+00 -1.04E-04
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00,  O.OOE+00
  O.OOE+00  O.OOE+00
                      O.OOE+00
                      O.OOE+00
                                CU FT CU FT  4.60E+02 9.20E+04 l.OOE+00   1    1
                                8.00E-10  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                      4.15E-06
                      O.OOE+00
                     -3.30E-02
                      4.46E-06
                      O.OOE+00
                     -3.57E-02

                      3.38E-01
            1.72E+00 -2.04E-02
            O.OOE+00  O.OOE+00
                     -1.49E-01
                                O.OOE+00
                                O.OOE+00 0.06 0.00 0.19 0.32 0.43 0.00 0.00 0.00
ON-SITE HYPOCHLORITE GENERATION LB/DAYLB/DAY l.OOE+01 l.OOE+04 l.OOE+00  35-1101
  1.S8E+04  3.58E+02 -S.97E-02  3.37E-06 -4.90E+01  9.16E+02 -4.97E-03  3.67E-07
                                6.49E-08  3.76E+02  8.98E-01 -1.21E-04  6.59E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00
                                8.54E-07 0.00 0.60 0.00 0.00 0.21 0.00 0.06 0.13
                                LB/HR LB/HR  5.40E+00 5.40E+03 l.OOE+00  24  101
                                5.16E-06  3.24E+03  4.26E+00  1.80E-05  5.24E-07
                               -1.17E-09  6.15E+01  6.92E-03  9.17E-06 -3.44E-10
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                3.32E-06 0.00 0,42 0.00 0.00 0.08 0.03 0.12 0.35
                                LB/HR LB/HR  l.OOE+01 5.00E+03 l.OOE+00  24  101
                                7.40E-06  4.84E+03  2.28E+00 -7.93E-04  1.07E-07
                                3.40E-09  2.68E+02  8.11E-01  2.87E-O5 -4.02E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00,
                                5.87E-06 0.00 0,40 0.00 0.00 0.03 0.07 0.06 0.44
                                LB/DAYLB/DAY l.OOE+00 2.00E+02 l.OOE+00   1  110
                               -9.09E-04  1.73E+04  3.37E-03  1.05E-05  6.28E-OB
                                8.58E-05  1.96E+02  3.33E-01 -2.16E-03  7.20E-06
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                4.68E-04 O.OO 0.69 O.OO 0.00 O.O4 0.01 0.07 0.19
                                LB/HR LB/HR  l.OOE+01 l.OOE+03 l.OOE+00  24  101
                                2.44E-04  3.25E+03  9.61E+00 -1.47E-02  7.94E-06
                                2.64E-06  5.20E+02  5.53E+00 -9.68E-O3  5.68E-06
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  2.22E+04  1.67E+01  6.71E-02 -4.20E-05 0.00 0.53 0.00 0.00 0.02 0.13 0.07 0,49
LIME FEED-WITH RECALCINATION    LB/HR LB/HR  l.OOE+03 l.OOE+04 l.OOE+00  24  108
                                2.12E-07  1.35E+03  4.00E+00 -4.51E-04  3.34E-08
                                          6.99E+02  1.47E+00 -1.76E-04  8.88E-09
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                8.73E-09 0.00 0.67 0.00 O.OO 0.02 0.05 0.10 0.16
                                LB/DAYLB/DAY 1.OOE+OO S.OOE+02 l.OOE+00   1  101
                                4.13E-05  3.08E+03  2.OOE+OO  1.56E-02 -1.17E-05
                                6.97E-07  2.06E+02  2.57E+00 -9.02E-03  1.03E-05
                                O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00
                                5.69E-05 0.00 0.33 0.00 0.00 0.06 0.10 0.33 0.18
                                GPD   GPU    l.OOE+01 5.00E+03 l.OOE+00 153-1101
                                7.24E-07  1.60E+03 -1.53E-01  2.54E-04 -3.15E-08
                                1.57E-09  7.88E+01  1.60E-01 -3.34E-05  4.67E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO
                                                              .11 0.11 0.22 0.10
                                                               1. OOE+OO   1  101
                                          3.20E+03  8.66E-01 -3.39E-05 -2.79E-10
                                          1.20E+02  1.59E-02 -3.08E-06  3.03E^10
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                1.39E-07 0.00 0.39 0.00 0.00 0.05 0.05 0.18 0.33
                                LB/HR LB/HR  1.07E+01 5.35E+03 l.OOE+00  24  101
                                4.61E-06  4.70E+03  2.09E+00 -5.59E-04  6.54E-08
                                6.45E-09  2.67E+02  7.95E-01 -4.06E-O5  8.10E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                4.44E-06 0.00 0.38 0.00 0.00 0.03 0.06 O.O6 0,47
  9.23E+02  1.06E+01 -9.70E-04
  O.OOE+00  O.OOE+00  O.OOE+00
  4.85E+03  8.09E+01 -1.50E-02
ALUM FEED-LIQUID STOCK
  1.91E+04  1.14E+02 -3.86E-02
  7.38E+01  6.3OE-02
  O.OOE+00  O.OOE+OO
  5.43E+03  8.22E+O1
ALUM FEED-DRY STOCK
  2.09E+04  1.40E+02 -4.64E-02
  1.99E+02  1.30E-01
  O.OOE+00  O.OOE+00
  5.67E+03  9.81E+01
POLYMER FEED SYSTEMS
  2.00E+04  1.73E+01
  2.59E+02
  O.OOE+00
  7.99E+03  2.26E+01
LIME FEED-NO RECALCINATION
  4.37E+04  2.84E+02 -4.56E-01
  7.02E+02  2.52E+00 -4.47E-03
  O.OOE+00  O.OOE+00  O.OOE+00
                      1.30E-05 -7.11E-10
                      O.OOE+00  O.OOE+00
  5.98E+04  2.30E+01 -3.54E-O3
  1.35E+03 -2.61E-03
  O.OOE+00  O.OOE+00
  1.63E+04  7.24E+00 -3.31E-04
POTASSIUM PERMANGANATE FEED
  9.63E+O3  2.41E+01 -4.69E-02
  7.24E+01  3.48E-01 -6.92E-04
  O.OOE+00  O.OOE+OO  O.OOE+00
  1.45E+03  1.61E+01 -4.65E-02
SULFURIC ACID FEED SYSTEMS
  8.60E+03  2.26E+01 -5.78E-03
  6.48E+01  4.90E-02 -1.46E-05
  O.OOE+00  O.OOE+00  O.OOE+00
  2.88E+03 -9.94E-01  3.52E-04 -3.79E-08 0.00 0.46 0.00 0.00 0.
SODIUM HYDROXIDE FEED SYSTEMS   LB/DAYLB/DAY l.OOE+01 l.OOE+04
  1.44E+O4
  1.39E+02
            7.94E+00 -4.89E-04
            2.86E-02
            O.OOE+00
                                4.34E-08
  O.OOE+00
  1.06E+03   1.47E+01 -2.03E-03
FERROUS SULFATE FEED SYSTEMS
  1.96E+04   1.20E+02 -3.21E-02
  1.85E+02   1.26E-01 -1.86E-05
  O.OOE+00   O.OOE+00  O.OOE+00
  5.71E+03   8.93E+01 -2.89E-02
                      2.28E-06 -1.33E-10
                      O.OOE+00  O.OOE+00
                                       71
-------
                                CRV.DAT FILE (CONTINUED)
 FERRIC SULFATE FEED SYSTEMS     LB/HR LB/HR  1.33E+01  6.60E+03  l.OOE+00   24   101
   1.95E+04  9.79E+01 -2.26E-02  2.68E-06   4.79E+03  1.57E+00  -2.19E-04   1.46E-08
   1.88E+02  4.81E-02  3.59E-OS -2.62E-09   2.72E+02  S.38E-01  7.17E-05 -B.18E-09
   O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00   O.OOE+OO  O.OOE+00  O.OOE+00   O.OOE+00
   5.80E+03  6.71E+01 -1.41E-02  1.76E-06  0.00 0.38 0.00  0.00  0.03  0.06 0.06  0.47
 ANHYDROUS AMMONIA  FEED FACILITY LB/DAYLB/DAY 2.50E+02  5.00E+03  l.OOE+00    1   101
   1.85E+04  5.70E+01 -1.68E-02  1.89E-06  -9.13E+01  3.41E+00  3.13E-03 -4.49E-07
                                 6.59E-08   4.57E+02  2.27E-01  -5.25E-05   5.71E-09
                                 O.OOE+00   O.OOE+00  O.OOE+00  O.OOE+00   O.OOE+00
                                 1.46E-07  0.00 0.55 0.00  0.00  0.15  0.10 0.11  0.09
                                 LB/DAYLB/DAY 2.50E+02  5.00E+03  l.OOE+00   34-1101
                                 3.58E-07   5.70E+02  4.73E-07  -2.01E-10   1.69E-14
                                 5.43E-09   1.52E+02  1.26E-07  -5.51E-11   4.55E-15
                                 O.OOE+00   O.OOE+00  O.OOE+00  O.OOE+00   O.OOE+00
                                 O.OOE+00  0.00 0.71 0.00  0.00  0.06  0.05 0.18  0.00
                                 LB/HR LB/HR  3.50E+00  7.00E+03  l.OOE+00   24   101
                                 5.35E-06   7.94E+03  1.36E+03  -3.62E-01   3.10E-05
                                 3.07E-07   9.29E+02  2.04E+00  -3.98E-04   4.50E-08
                                 O.OOE+00   O.OOE+00  O.OOE+00  O.OOE+00   O.OOE+00
                                 3.94E-13  0.01 0.44 0.02  0.04  0.05  0.15 0.24  0.05
                                 CU  FT CU  FT  l.OOE+02  2.00E+04  l.OOE+00    1     1
                       2.16E-04 -4.63E-09  -9.19E-04  5.09E+01  -7.63E-10   1.48E-13
             1.45E-02 -4.44E-07  2.21E-11   4.54E+02 -6.88E-03  9.09E-06 -2.95E-10
                                 O.OOE+00   O.OOE+00  O.OOE+00  O.OOE+00   O.OOE+00
                                 O.OOE+00  0.03 0.31 0.07  0.11  0.18  0.00 0.30  0.00
                                 CU  FT CU  FT  l.OOE+02  2.00E+04  l.OOE+00    1     1
                         15E-04 -9.31E-10   1.50E+01  1.02E+02  1.23E-05 -1.90E-10
                                 2.21E-11
                                 O.OOE+00
  2.27E+03  2.48E+00 -6.03E-04
  O.OOE+00  O.OOE+00  O.OOE+00
  9.44E+03  2.53E+00 -1.05E-03
AQUA AMMONIA FEED FACILITY
  8.94E+03  1.58E+01 -3.50E-03
  3.99E+01  2.52E-01 -5.49E-05
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
POWDERED ACTIVATED CARBON FEED
  7.01E+04  3.07E+02 -6.09E-02
            2.00E+01 -3.67E-03
            O.OOE+OO  O.OOE+00
            7.39E-06 -4.71E-09
   2.36E+03
   O.OOE+00
   1.03E+04
RAPID  MIX»  G=300
   1.38E+04   7.45E+00
   2.05E+01
   O.OOE+00
   O.OOE+00
RAPID  MIXr
   1.41E+04
   2.0SE+01
   O.OOE+00
   O.OOE+00
RAPID  MIXi  G=900
   1.41E+04   1.99E+01
   2.05E+01
   O.OOE+00
   O.OOE+00
                      O.OOE+00
                      O.OOE+00
            O.OOE+00
            O.OOE+00
           G=60O
            1.05E+01   1
            1.45E-02 -4.44E-07
            O.OOE+00   O.OOE+00
            O.OOE+00   O.OOE+00
                      2.46E-05
            1.45E-02 -4.44E-07
            O.OOE+00  O.OOE+00
            O.OOE+00  O.OOE+00
                                          4.54E+02 -6.88E-03  9.09E-06 -2.95E-10
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.02 0.40 0.06 0.09 0.17 0.00 0.26 0.00
                                CU FT CU FT  l.OOE+02 2.00E+04 l.OOE+00   1    1
                                1.90E-09 -7.51E+01  3.40E+02 -7.42E-05  2.91E-09
                                          4.54E+02 -6.88E-03  9.09E-06 -2.95E-10
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  3.29E+04
  3.66E+02
  O.OOE+00
  O.OOE+00
            3.80E+00 -5.18E-06
            3.70E-02 -2.61E-08
            O.OOE+00  O.OOE+00
            O.OOE+00  O.OOE+00
                                2.21E-11
                                O.OOE+00
                                O.OOE+00 0.01 0.60 0.04 0.06 0.12 0.00 0.17 0.00
FLOCCULATION-HORIZ PADDLE, G=20 CU FT CU FT  1.80E+03 l.OOE+06 l.OOE+00   1    1
  3.40E+04  3.41E+00 -4.93E-06  3.32E-12 -2.55E+01  1.98E-01 -8.37E-09  8.71E-15
  3.66E+02  3.70E-02 -2.61E-08  1.77E-14  1.30E+02  2.68E-03 -5.51E-09  3.76E-15
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.04 0.24 0.12 0.17 0.25 0.00 0.18 0.00
FLOCCULATION-HORIZ PADDLEr G=50 CU FT CU FT  1.80E+03 l.OOE+06 l.OOE+00   1    1
                                3.51E-12 -7.31E+01  1.19E+00 -1.71E-08  1.57E-14
                                1.77E-14  1.30E+02  2.68E-03 -5.51E-09  3.76E-15
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.04 0.27 0.10 0.17 0.26 0.00 0.16 0.00
FLOCCULATION-HORIZ PADDLEr G=80 CU FT CU FT  1.80E+03 5.00E+05 l.OOE+00   1    1
  2.S2E+04  S.56E+00 -1.69E-05  2.25E-11  4.58E+01  3.36E+00  6.58E-09 -3.07E-14
  3.66E402  3.70E-02 -2.61E-08  1.77E-14  1.30E+02  2.68E-03 -5.51E-09  3.76E-15
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00 0.02 0.34 0.08 0.13 0.24 0.00 0.19 0.00
FLOCCULATION-VERT TURBINE* G=20 CU FT CU FT  1.80E+03 2.50E+04 l.OOE+00   1    1
  1.11E+04  1.17E+01 .-3.61E-04  4.46E-09 -2.55E+01  1.98E-01 -8.37E-09  8.71E-15
                                1.77E-14  1.30E+02  2.68E-03 -5.51E-09  3.76E-15
                                O.OOE+00
                                O.OOE+00
FLOCCULATION-VERT TURBINE, G=50 CU FT CU FT  1.80E+03 2.50E+04 l.OOE+00   1    1
  1.11E+04  1.17E+01 -3.61E-04  4.46E-09 -7.31E+01  1.19E+00 -1.71E-08  1.57E-14
  3.66E+02  3.70E-02 -2.61E-08  1.77E-14  1.30E+02  2.68E-03 -5.51E-09  3.76E-15
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.03 0.18 0.09 0.14 0.25 0.00 0.32 0.00
FLOCCULATION-VERT TURBINE? G=80 CU FT CU FT  1.80E+03 2.50E+04 l.OOE+00   1    1
  1.04E+04  1.22E+01 -4.31E-04  6.92E-09
                                1.77E-14
                                O.OOE+00
  3.66E+02
  O.OOE+00
  O.OOE+00
            3.70E-02 -2.61E-08
            O.OOE+00  O.OOE+00
            O.OOE+00  O.OOE+00
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                         0.02 0.27 0.07 0.12 0.27 0.00 0.26 0.00
  3.66E+02  3.70E-02 -2.61E-08
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
CIRCULAR CLARIFIER-LIME SLUDGE
  5.83E+04  3.63E+01 -4.99E-04
  1.01E+02  2.14E-01 -6.35E-06
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
                                          4.21E+01   3.37E+00  -2.54E-08   2.87E-14
                                          1.30E+02   2.68E-03  -5.51E-09   3.76E-15
                                          O.OOE+00   O.OOE+00   O.OOE+00   O.OOE+00
                                O.OOE+00 0.03 0.23  0.09  0.15  0.29  0.00  0.22  0.00
                                SQ  FT SO FT  7.07E+02  3.14E+04 l.OOE+00   1     3
                                6.35E-09  4.64E+03   4.18E-01  -2.09E-06  -4.35E-11
                                1.14E-10  1.35E+02   2.24E-02  -6.61E-07   1.01E-11
                                O.OOE+00  O.OOE+00   O.OOE+00   O.OOE+00   O.OOE+00
                                O.OOE+00 0.02 0.31 0.08 0.37 0.14 0.05 0.03 0.00
CIRC CLARIFIER-FECL3 8 ALUM SLDGSO FT SQ FT  7.07E+02 3.14E+04 l.OOE+00   1    3
  5.83E+04  3.63E+01 -4.99E-04  6.35E-09  3.09E+03  3.79E-01 -9.65E-06  1.84E-10
  1.01E+02  2.14E-01 -6.35E-06  1.14E-10  1.35E+02  2.24E-02 -6.61E-07  1.01E-11
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.02 0.31 0.08 0.37 0.14 0.05 0.03 0.00
RECTANGULAR CLARIFIER-LIME SLDG SQ FT SQ FT  2.40E+02 4.80E+03 l.OOE+00   1    3
                                7.38E-07  3.04E+03  9.62E-01  1.40E-04  1.40E-08
                                3.64E-09
                                O.OOE+00
           6.43E+01  -6.31E-03
           1.32E-01  -2.13E-06
           O.OOE+OO   O.OOE+00
  2.38E+04
  2.53E+02
  O.OOE+00
  O.OOE+00  O.OOE+00
RECT CLARIFIER-FECL3
  2.38E+04  6.43E+01 -6.31E-03
  2.S3E+02  1.32E-01 -2.13E-06
  O.OOE+00  O.OOE+00
  O.OOE+OO  O.OOE+00
                                          1.49E+02  8.61E-02 -4.09E-06  3.63E-10
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                      O.OOE+00  O.OOE+00 0.04 0.27 0.10 0.25 0.21 0.11 0.02 0.00
                       ALUM SLG SQ FT SQ FT  2.40E+02 4.80E+03 l.OOE+00   1    3
                                7.38E-07  3.08E+03  8.15E-01 -4.68E-05  2.35E-08
                                3.64E-09  1.49E+02  8.61E-02 -4.09E-06  3.63E-1Q
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                      O.OOE+00
                      O.OOE+OO
                                O.OOE+OO 0.04 O.27 0.1O 0.25 0.21 O.ll 0.02 O.OO

                                       72
-------
                        CRV.DAT FILE (CONTINUED)
UPFLOW SOLIDS CONTACT CLAR.G=70 SQ FT SO FT  2.55E+02 1.45E+04 l.OOE+00   1    3
  6.59E+04  5.44E+01 -2.29E-03  2.52E-08  5.92E+03  8.73E+00 -2.79E-04  1.82E-08
  5.04E+02  2.71E-01 -1.57E-05  3.90E-10  4.23E+02  7.33E-02 -7.32E-06  2.47E-10
  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.04 0.53 0.07 0.10 0.25 0.00 0.01 0.00
UPFLOW SOLIDS CONTACT CLARrG=110SQ FT SQ FT  2.55E+02 1.45E+04 l.OOE+00   1    3
  6.59E+04  5.44E+01 -2.29E-03  2.52E-08  2.82E+03
  5.04E+02  2.71E-01 -1.57E-05  3.90E-10  4.23E+02
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.04 0.53
UPFLOU SOLIDS CONTACT CLARrG=150SQ FT SQ
  6.59E+04  5.44E+O1 -2.29E-03
  5.04E+02  2.71E-01 -1.57E-O5
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
TUBE SETTLING MODULES           SQ FT SQ
  2.86E+03  2.55E+01 -2.00E-04  1.91E-09
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                                   2.09E+01 -1.32E-03  8.80E-08
                                                   7.33E-02 -7.32E-06  2.47E-10
                                                   O.OOE+00   O.OOE+00  O.OOE+00
                                                   0.07 0.1O 0.25 0.00  0.01 O.OO
                                        FT   2.55E+02  1.45E+04 l.OOE+00   1     3
                               2.52E-08   7.68E+03  2.22E+01   2.14E-03  -1.15E-07
                               3.90E-10   4.23E+02  7.33E-02 -7.32E-06  2.47E-10
                                          O.OOE+00  O.OOE+00   O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
GRAVITY FILTRATION STRUCTURE
  1.16E+05  3.92E+02 -2.04E-02
 , 4.31E+02  2.78E+00 -1.37E-04
  O.OOE+00  O.OOE+00  O.OOE+00
  1.72E+04  1.93E+02 -4.11E-03
FILTRATION MEDIA-RAPID SAND
  3.80E+03  7.99E+00 -3.52E-05
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
FILTRATION MEDIA-DUAL. MEDIA
  2.8'2E+03  2.03E+01 -7.01E-04
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+OO  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
FILTRATION MEDIA-MIXED MEDIA
  4.68E+03  2.91E+01 -6.82E-04
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
BACKWASH PUMPING FACILITIES
  2.98E+04  1.05E+01 -1.29E-04
  6.23E+02  6.64E-01 -4.19E-05
  O.OOE+00  O.OOE+OO  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+OO
HYDRAULIC SURFACE WASH SYSTEMS
  2.60E+04  2.91E+01 -1.05E-03
  2.08E+02  4.85E-02 -2.86E-06
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+OO  O.OOE+OO  o;ooE+oo
AIR-UATER BACKWASH FACILITIES
  7.04E+04  4.24E+01 -2.34E-03
  6.23E+O2  6.64E-01 -4.19E-05
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+OD  O.OOE+OO  O.OOE+00
UAS.H  WATER SURGE BASINS
  1.88E+04  3.33E+00 -1.04E-05
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  -O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00
                                         0.04  0.53  0.07  0.10  0.25  0.00  0.01  0.00
                                         FT  2.80E+02  5.60E+04  l.OOE+00   1     1
                                          O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                          O.OOE+00   O.OOE+OO  O.OOE+00   O.OOE+00
                                          O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00  0.00  0.50  0,00  0
                                SQ  FT  SQ
                                                         ,33  0.17  0.00  0.00  0.00
                                         FT   1.40E+02  2.80E+04  l.OOE+00    1     1
                                4.82E-07   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                3.03E-09   B.46E+02   8.04E-01  -3.28E-05   9.39E-10
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                8.71E-08  0.01  0.16  0.07  0.05  0.24  0.24 0.07  0.16
                                SQ  FT  SQ  FT   3.70E+02  7.48E+04  l.OOE+00    1     1
                                3.78E-10   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+OO   O.OOE+00
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00  0.00 0.00  0.00  0.00  0.00  0.00 0.00  O.OO
                                SQ  FT  SQ  FT   1.40E+02  2.99E+04  l.OOE+00    1     1
                                1.68E-08   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00  0.00 0.00  0.00  0.00  0.00  0.00 0.00  0.00
                                SQ  FT  SQ  FT   1.40E+02  2.99E+04  l.OOE+00    1     1
                                1.63E-08   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00  0.00 0.00  0.00  0.00  0.00  0.00 0.00  0.00
                                GPM   SQ  FT   1.26E+03  2.30E+04  1.22E+00    1     1
                                5.53E-10  -5.92E-01   2.39E+01  -2.50E-06   1.74E-10
                                8.85E-10   1.93E+02   2.47E-02  -1.32E-06   2.36E-11
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00  0,00 0.49  0.00  0.00  0.06  0.23 0.22  0.00
                                SQ  FT  SQ  FT   1.40E+02  2.80E+04  l.OOE+00    1     1
                                3.21E-08   3.41E+02   1.40E+O1  -5.15E-05   2.16E-09
                                5.82E-11   7.03E+01   6.70E-02  -5.02E-06   1.28E-10
                                O.OOE+00   O.OOE+OO   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+00  0.00 0.52  O.OO  0.00  O.O8  O.1O 0.30  0.00
                                SQ  FT  SQ  FT   1.40E+02  2.80E+04  l.OOE+00    1     1
                                5.58E-08   7.00E+00   2.42E+01   1.39E-06   6.57E-11
                                8.85E-10   1.94E+02   2.58E-02  -1.46E-06   2.72E-11
                                O.OOE+OO   O.OOE+OO   O.OOE+00  O.OOE+00   O.OOE+00
                                O.OOE+OO  0.00 0.41  O.OO  0.00  0.09  0.39 0.11  0.00
                                GAL   GAL    l.OOE+04  5.00E+O5  l.OOE+00    1     1
                                1.11E-11   O.OOE+00   O.OOE+00   O.OOE+00   O.OOE+00
                                O.OOE+00   O.OOE+00   O.OOE+00   O.OOE+00   O.OOE+00
                                O.OOE+00   O.OOE+00   O.OOE+00   O.OOE+00   O.OOE+00
                                O.OOE+00  0.01 0.00  0.30  0.18  0.44  0.05  0.00  0.02
 FILTER MOD-RAP SAND TO HIGH RATESQ FT SQ FT  1.40E+02 2.80E+04 l.OOE+00   1    1
   2.05E+04  3.28E+01 -1.41E-03  3.21E-08  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
   O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
   O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                                    O.OOE+00  O.OOE+00  O.OOE+00
                                                    O.OOE+OO  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.00 0.00 0,00 O.OO 0.38 0.45 0.17 0.00
CONTINUOUS AUTO. BACKWASH FILTERSQ FT SQ FT  3.60E+02,7.04E+04 l.OOE+00   1    1
          O.OOE+OO
          O.OOE+00
   1.54E+05  1.76E+02
   5.09E+02  5.35E-01
   O.OOE+00  O.OOE+OO
   5.67E+04  1.53E+02
 RECARBONATION BASIN
   5.42E+03  3.95E+00 -1.28E-04
   O.OOE+00  O.OOE+00  O.OOE+00
   O.OOE+00  O.OOE+00  O.OOE+00
   O.OOE+00  O.OOE+00  O.OOE+00
 RECARBONATION-LIQUID C02 FEED
   3.96E+04  2.01E+01 -1.41E-03
   2.48E+03  1.19E+00 -9.17E-O5
   O.OOE+00  O.OOE+00  O.OOE+OO
   9.83E+03  1.34E+00 -1.22E-04
                      1.77E-03 -1.75E-08
                      1.62E-06 -2.49E-11
                      O.QOE+00  O.OOE+00
                      3.50E-03 -3
                                CU FT CU
                                2.41E-09
                                O.OOE+OO
          7.32E+02
          7.00E+02
          O.OOE+00
  29E-08 O.01 0.50
 8.33E+00  1.80E-04 -1.79E-09
 6.51E-02  8.76E-06 -8.79E-11
 O.OOE+00  O.OOE+00  O.OOE+00
0.07 0.03 0.15 0.03 0.02 0.19
         FT  7.70E+02 3.52E+04 l.OOE+00   1    3
          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+OO  O.OOE+00
O.OOE+00 0.07 0.00 0.20 0.32 0.39 0.02 0.00 0.00
LB/DAYLB/DAY 3.80E+02 1.50E+04 l.OOE+00   1  101
7.69E-08 -7.1"6E+01  1.90E+01 -3.18E-04  1.53E-08
3.06E-09  7.14E+01  2.52E-02 -1.4SE-06  4.43E-11
O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
5.38E-09 0.00 0.59 0.00 0.00 0.21 0.09 0.00 0.11
                                       73
-------
                           CRV.BAT  FILE  (CONTINUED)
 RECARB-C02 FROM SUBMERGED BURNERLB/DAVLB/DAY 5.00E+02 1.OOE+04 l.OOE+00   1    3
   5.05E+04  6.33E+00  1.58E-04 -2.34E-OB  1.71E+04  7.14E+01 -8.45E-03  4.76E-07
   1.36E+03  4.31E-01 -6.59E-05  3.S7E-09  8.00E+01 -6.73E-09  4.09E-12  6.88E-16
   O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  8.65E+03  3.14E+03  5.61E-03 -4.81E-07
   O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.00 0.56 0.00 0.00 0.20 0.17 0.07 0.00
 RECARBONATION-C02 FROM STACK GASLB/DAYLB/BAY 2.50E+03 5.00E+04 l.OOE+00   1    1
   8.84E+03  1.13E+01 -3.89E-04  4.68E-09 -1.05E+02  1.74E+01 -5.38E-06  8.69E-11
                                 7.90E-11
                                 O.OOE+00
   1.28E+03  3.09E-01 -7.47E-06
   O.OOE+00  O.OOE+00  O.OOE+0'0
   O.OOE+00  O.OOE+00  O.OOE+00
 MULTIPLE HEARTH RECALCINATION
   4.89E+OS  2.27E+03 -8.47E-01
   3.26E+03  1.67E+01 -4.01E-03
   O.OOE+OO  O.OOE+00  O.OOE+00
   1.78E+03  3.08E+01 -1.45E-02
                                           3.17E+01  2.88E-02 -6.18E-07  6.60E-12
                                           O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                 O.OOE+00 0.00 0.42 0.00 0.00 0.27 0.15 0,16 0.00
                                 SQ FT SO FT  1.79E+02 2.93E+03 l.OOE+00   1    3
                                 1.28E-04  1.75E+05  9.27E+02 -4.21E-01  1.3SE-04
                                 8.45E-07  1.10E+03  1.13E+01 -3.23E-03  5.39E-07
                                 O.OOE+00  1.76E+07  4.8SE+04  2.44E+01 -2.17E-03
                                 2.47E-06 0.00 0.63 0.00 0.00 0.27 0.01 0.01 0,
 CONTACT BASIN-DIRECT FILTRATION CU FT CU FT  2.64E+03 5.28E+04 l.OOE+00
   1.06E+04
   O.OOE+00
   O.OOE+00
   O.OOE+00
                                                                               08
                                                                                3
             3.83E+00 -7.18E-05
             O.OOE+00  O.OOE+00
             O.OOE+00  O.OOE+00
             O.OOE+00  O.OOE+00
                                 MGC
             7.27E+04  1.09E+02 -4.53E-01 -1.63E+03
             3.91E+02 -6.72E-01
             O.OOE+00  O.OOE+OO
             1.66E+04 -1.84E+01
 PRESSURE DIATOMITE FILTERS
   2.03E+05
   1.10E+03
   O.OOE+00
   1.42E+05
 VACUUM DIATOMITE FILTERS
   4.83E+04  1.01E+05 -5.06E+01
   2.95E+02  4.49E+02 -5.04E-01
   O.OOE+00  O.OOE+00  O.OOE+00
   1.52E+04  6.17E+04 -1.06E+02
PRESSURE FILTRATION PLANTS
  :>.23E+05  2.01E+02  2.57E-02 -6.69E-07
  5.17E+02  4.94E+00 -1.89E-04  4.09E-09
  O.OOE+00  O.OOE+00
  2.01E+05  2.11E+01
IN-PLANT PUMPING
  2.23E+04  5.47E+03 -1.53E+01
  2.13E+02  1.32E+02
  3.50E+01  7.50E+01
  2.23E+04  5.47E+03 -1.53E+01
WASH WATER STORAGE TANKS
  2.12E+03  3.89E-01 -3.82E-07
  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00
REVERSE OSMOSIS
  2.46E+05  5.32E+05 -1
  2.26E+04
  O.OOE+OO
  2.17E+O4  8.33E+04 -1.09E+02
                                 7.16E-10  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                 O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO
                                 O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                 O.OOE+00 0.07 0,00 0.20 0.34 0.39 0.00 0.00 0.00
                                       MGD    l.OOE+00 2.00E+02 l.OOE+00   1  302
                                                     1.27E+05 -2.42E+02  9.40E-01
                                 1.58E-03  2.39E+03  6.09E+02 -5.47E+00  1.64E-02
                                 O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00
                                 6.76E-02 0.01 0.62 0.01 0.01 0.15 0.04 0.07 0.09
                                 MGD   MGD    l.OOE+00 2.00E+02 l.CfOE+00   1  302
                                 2.09E-01  7.54E+03  5.64E+04  1.80E+01 -6.34E-02
                                 2.96E-07  2.39E+03  6.09E+02 -5.47E+00  1.64E-02
                                 O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                 3.75E-01 0.01 0,32 0.01 0.01 0.22 0.22 0.05 0,16
                                SO FT SQ FT   1.4OE+02 2.80E+04 l.OOE+00   1    1
                                          2.90E+03  2.34E+02  2.36E-04 -S.36E-09
                                          1.25E+03  1.37E+00 -6.16E-05  1.32E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                      9.00E-03 -2.26E-07 0.01 0,45 0.01 0.01 0.07 0.25 0.12 0.08
                                MGD   MGD     l.OOE+00 2.00E+02 l.OOE+00   1    5
                                6.48E-02  1.41E+02  5.24E+04  1.64E+00 -4.S9E-03
                      4.54E-01 -2.49E-03  5.09E+02  2.20E+01 -1.90E-02  1.24E-04
                                4.00E-10  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                6.48E-02 0.01 0.22 0.02 0.03 0.28 0.27 0.11 0.06
                                GAL   GAL     2.10E+04 9.00E+05 l.OOE+00   1    1
                                2.98E-13  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.02 0.00 0.01 0.43 0.54 0.00 0.00 0,00
                                MGD   MGD     l.OOE+00 2.00E+02 l.OOE+00   1  302
                                4.28E+00  2.24E+05  2.19E+06  3.69E+02 -1.27E+00
                                2.46E-01  1.81E+03  9.13E+01 -6.70E-01  2.30E-03
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO
                                3.49E-01 0.00 0.61 0.00 0.00 0.12 0.00 0.15 0.12
PRESSURE ION EXCHANGE-SOFTENING MGD   MGD     1.10E+00 1.23E+02 l.OOE+00 490 1101
  4.95E+04  8.59E+04  2.76E+02 -2.03E+00 -1.15E+00  2.06E+03 -7.18E-02  5.50E-04
                      1.26E-02 -S.BSE-'OS  2.11E+03  1.28E+02 -8.5BE.-01  4.75E-03
                      O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                      O.OOE+00
                      5.68E-08
                      O.OOE+00
                      O.OOE+00
                      O.OOE+00

                       .50E+03
            6.85E+04 -7.22E+01
            O.OOE+OO  O.OOE+00
  2.38E+02
  O.OOE+00
  2.S9E+04
            4.33E+03
            O.OOE+00
            2.78E+04
GRAVITY ION EXCHANGE-SOFTENING
  1.17E+05  6.81E+04 -2.15E+02
  l.OBE+03  3.93E+03 -2.31E+00
  O.OOE+00  O.OOE+00  O.OOE+00
  1.69E+04  1.82E+04 -4.30E+01
                      1.88E+02 -1.63E+00 0.01 0.52 O.O1 0.01 0,01 0.16 0.16 0.12
                                MGD   MGD    1.50E+00 1.50E+02 l.OOE+00 49O 1101
                                7.80E-01 -1.53E+00  9.81E+02  4.15E-02 -3.23E-04
                                8.75E-03  2.11E+03  1.08E+02 -1.96E-01  1.07E-03
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                1.16E-01 0.01 0.59 0.04 0.03 0.09 0.10 0.06 0.08
PRESSURE ION EXCHANG-N03 REMOVALMGD   MGD    1.10E+00 1.23E+01 l.OOE+00 121'2101
  2.04E+05  2.28E+04  3.35E+04 -1.72E+03 -8.31E-01  1.73E+03 -2.09E+00  1.28E-01
  2.43E+03  2.08E+04  5.64E+02 -3.15E+01  2.06E+03  1.05E+02  l.OOE+01 -7.74E-01
  O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  2.48E+04  2.82E+04  1.70E+02 -4.61E+01 0.01 0.68 0.01 0.01 0.11 0.06 0.06 0.06
ACTIV. ALUMINA-FLUORIDE REMOVAL MGD   MGD    7.00E-01 1.35E+02 l.OOE+00   1  202
  4.46E+04  5.97E+04  1.94E+02 -1.05E+00  9.29E+00  6.22E-01 -7.15E-03  4.36E-05
  6.16E+02  1.60E+03  1.98E+01 -1.14E-01  2.41E+03
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  3.35E+03  2.09E+04 -8.13E-01 -2.39E-01 0.00 0.52
                                                    6.26E+01  7.21E-01 -2.60E-03
                                                    O.OOE+00  O.OOE+00  O.OOE+00
                                                   0.00 0.00 0.12 0.16 0.05 0.. 15
GRAVITY GAG CONTACTORS-CONCRETE CU FT SO FT  3.50E+02 1.06E+04 1.40E+02  28 3004
  6.47E+04
  4.31E+02
  O.OOE+00
  1.72E+04
            5.83E+01 -6.53E-03
            2.78E+00 -1.37E-04
            O.OOE+00  O.OOE+00
            1.93E+02 -4.11E-03
GRAVITY GAC CONTACTORS-STEEL
  1.41E+04  2.68E+01 -3.93E-04
  5.46E+02  1.61E-01 -3.12E-07
  O.OOE+00  O.OOE+00  O.OOE+00
 -4.52E+03  2.17E+01 -1.22E-05
PRESSURE CARBON CONTACTORS
  3.94E+04  7.63E+01 -2.69E-02
  9.25E+02  4.10E+00  1.60E-04
  O.OOE+00  O.OOE+00  O.OOE+00
  4.59E+04  3.97E+02 -6.00E-02
                                2.96E-07  9.41E+00  4.86E+00  1.20E-06 -2.55E-11
                                3.03E-09  8.46E+02  8.04E-01 -3.28E-05  9.39E1-10
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                8.71E-08 0.01 0.14 0.05 0.03 0.20 0.41 0.02 0.14
                                CU FT CU FT  6.28E+03 1.41E+04 3.14E+04 '628'3004
                                7.46E-09 -8.24E+01  3.86E-01 -2.13E-08  2.85E-14
                                3.21E-13  2.32E+03  1.89E-02  9.37E-08 -9.64E-14
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  0.. OOE+00
                                1.26E-11 0.01 0.43 0.01 0.01 0.08 0.19 0.66 6..21
                                CU FT SQ FT  3.90E+02 2.26E+03 1.57E+02 679,1004
                                4.52E-06  1.21E+02  5.OOE+00  2.12E-04 -1.41E-08
                                2.88E-09  8.90E+02  7.30E-01  3.52E-05 -3.07E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+OO
                                6.91E-06 0.01 0.47 0.01 0.01 0.06 0.17 0.10 0.17
                                        74
-------
                        CRV.DAT FILE (CONTINUED)
  O.OOE+00  O.OOE+00  O.OOE+OO
  O.OOE+00  O.OOE+00  O.OOE+00
MAKEUP CARBON COST-O&M ONLY
  O.OOE+00  O.OOE+00  O.OOE+00
CONVERT FILTER TO GAC CONTACTOR SB FT SO FT  3.70E+02 7.00E+04 l.OOE+00   1    1
  2.03E+04  5.10E+01 -2.52E-04  1.97E-09  O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+OO
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.00 0.12 0.00 0.00 0.25 0.61 0.02 0.00
GRANULAR ACT CARBON-CONSTR COST LB    LB     l.OOE+04 l.OOE+07 l.OOE+00   1    1
  1.02E+03  6.07E-01 -6.54E-09 -5.61E-17  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
                                LB/YR LB/YR  l.OOE+04 l.OOE+07 l.OOE+00   1    1
                                O.OOE+OO  O.OOE+OO  O.OOE+00  O.OOE+OO  O.OOE+00
  1.02E+03  6.07E-01 -6.54E-09 -5.61E-17  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.00 O.OO 0.00 O.OO 0.00 0.00 0.00 0.00
CAPPING SAND FILTER U/ANTHRACITESQ FT SQ FT  3.SOE+02 7.00E+04 l.OOE+00   1    1
  4.08E+02  6.17E+00 -9.55E-06  9.53E-11  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO 0.00 O.OO 0.68 0.00 0.32 O.OO 0.00 O.OO
REGIONAL GAC REGEN-TRANS 8 STOR CU FT LB/YR  l.OOE+03 2.00E+04 3.OOE+O4   3 6006
  1.83E+04  7.21E+00  1.87E-03 -6.84E-08  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  2.46E-03  1.99E-05  1.35E-13 -1.14E-21 -1.16E-02  2.30E-05  7.07E-14  4.37E-21
 -9.54E-03  1.93E-05  4.O8E-14  2.60E-21  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO 0.01 0.16 0.02 0.39 0.37 O.OS 0.00 0.00
REGIONAL MULTI HEARTH GAC REGEN SQ FT SQ FT  2.70E+01 1.51E+03 l.OOE+00   1   12
  4.68E+05  3.74E+03 -2.71E+00  B.31E-04  2.49E+05  1.26E+03 -8.58E-01  3.22E-04
  2.48E+03  2.78E+01 -2.9SE-02  1.13E-05  2.51E+02  2.19E+01 -1.46E-02  4.94E-06
                                O.OOE+00  1.69E+06  1.59E+05 -4.87E+01  2.29E-02
            2.78E+01 -2.9SE-02
            O.OOE+00  O.OOE+00
                     -2.95E-02
                      O.OOE+00
  2.48E+03  2.78E+01
  O.OOE+00  O.OOE+00
  1.39E+04  2.17E+01  1.89E-02 -1.25E-05 0.00
INFRARED CARBON REGEN FURNACE
  2.19E+05  3.15E+01 -3.64E-04
  6.06E+03  1.24E+00 -2.46E-05
  O.OOE+00  O.OOE+00  O.OOE+00
 -3.49E+00  3.31E+00 -7.03E-05
FLUIDIZED BED GAC REGENERATION
  7.74E+05  3.19E+01 -S.94E-04
  1.09E+04  8.46E-01 -3.46E-05
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+OO  O.OOE+OO  O.OOE+OO
  O.OOE+00
  1.39E+04  2.17E+01  1.89E-02 -1.25E-05 0.00 0.53 0.00 0.00 0,28 0.02 0.01 0.16
MULTIPLE HEARTH'GAC REGENERATIONSQ FT SQ FT  2.70E+01 1.51E+03 l.OOE+00   1    3
  4.68E+05  3.74E+03 -2.71E+00  8.31E-04  2.49E+05  1.26E+03 -8.58E-01  3.22E-04
                                1.13E-05  2.51E+02  2.19E+01 -1.46E-02  4.94E-06
                                O.OOE+00  1.69E+06  1.59E+05 -4.87E+01  2.29E-02
                                              0.53 0.00 0.00 0.28 0.02 0.01 0.16
                                LB/DAYLB/DAY 2.40E+03 6.00E+04 l.OOE+00   1    1
                                4.03E-09 -6.19E+04  3.28E+02 -4.27E-03  6.50E-08
                                1.95E-10  2.03E+03  1.14E-01  2.17E-06 -2.35E-11
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                6.95E-10 0.00 0.64 0.00 0.00 0.18 0.01 0,08 0.09
                                LB/DAYLB/DAY 6.00E+03 2.40E+04 l.OOE+00   1    3
                                5.97E-09 -4.60E+00  2.10E+01 -1.98E-O8  1.43E-12
                                6.28E-10  2.39E+03 -5.59E-02  7.67E-06 -1.65E-10
                                O.OOE+00 -1.64E+05  1.14E+03 -4.05E-03  9.73E-OB
                                O.OOE+00 O.OO 0.68 O.OO O.OO 0,22 O.OO 0.01 O.O9
POWDERED CARB REGEN-FLUIDIZED BDLB/DAYLB/DAY 2.09E+02 3.34E+04 l.OOE+00   1    1
  5.74E+05  3.28E+02 -1.56E-02  3.01E-07 -1.89E+03  4.52E+02 -1.91E-02  3.84E-07
  2.59E+03  2.35E-01 -7.94E-06  1.44E-10  1.20E+03  2.82E-02  5.15E-06 -1.12E-10
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  1.89E+05  3.49E+03 -4.93E-02  9.28E-07
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.00 0.49 0.00 O.OO 0.35 O.OO 0.15 O.01
POWDERED CARB REGEN-ATOMIZED SUSLB/DAYLB/DAY l.OOE+03 l.OOE+04 l.OOE+00   1    1
  1.04E+05  2.29E+02 -4.87E-03  2.13E-07  2.03E+04  2.23E+01  4.30E-03 -2.28E-07
  1.93E+03  4.43E-02  2.41E-05 -1.69E-09  9.04E+02  1.28E-01 -1.23E-05  5.60E-10
  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+OO -2.98E+O5  6.42E+03 -1.21E-01  3.27E-06
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.00 0.76 O.OO 0.00 0,00 0.00 0.12 0.12
CHEM SLUDGE PUMPING-UNTHICKENED 0PM   GPM    2.00E+01 l.OOE+04 l.OOE+00   1    1
  3.28E+04  6.07E+01 -9.22E-03  5.49E-07  2.36E+00  6.39E+01  3.07E-OS -2.00E-09
                                6.00E-08  1.07E+02  3.08E-01 -5»16E-05  2.91E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                3.75E-08 0.01 0.15 0.06 0.06 0.24 0.23 0.14 0.11
                                0PM   GPM    5.00E+00 1.25E+03 l.OOE+00   1    1
                                1.17E-04  2.98E+03  4.62E+02 -2.14E-01  9.60E-05
                                1.47E-05
                                O.OOE+00
                                7.70E-07
  2.27E+03  7.39E+00 -9.64E-04
  O.OOE+00  O.OOE+00  O.OOE+00
  9.71E+03  3.26E+00 -5.88E-04
CHEM SLUDGE PUMPING-THICKENED
  8.46E+03  1.69E+Q2 -2.43E-01
  1.10E+O3  2.21E+O1 -3.06E-02
  O.OOE+00  O.OOE+00  O.OOE+00
  4.95E+03  6.05E+00 -2.38E-03
GRAVITY SLUDGE THICKENER-LIME
  4.18E+04  4.06E+01 -3.99E-03
  9.36E+01  1.59E-01  1.17E-O6 -1.63E-10
  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00
  9.36E+01  1.59E-01
  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
VACUUM FILTERS
 '1.62E+05  7.36E+02 -2.69E-01
  1.63E+03  1.52E+02 -1.66E-01
  O.OOE+OO  O.OOE+00  O.OOE+00
                                          4.77E+01  9.40E-01 -1.26E-03  5.90E-07
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                         0.00 0.64 0.00 0.00 0.13 0.04 0.07 0.12
                                SQ FT SQ FT  3.14E+02 1.78E+04 l.OOE+00   1    3
                                1.58E-07  2.83E+03  1.44E+00  1.11E-04 -4.34E-09
                                          1.16E+02  3.59E-02 -2.69E-06  8.67E-11
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                                                              00
                                                                               3
                                          2.76E+03  1.69E+00 -8.49E-05  4.05E-09
                                          1.16E+02  3.59E-02 -2.69E-06  8.67E-11
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.03 0.41 O.12 0.16 0.27 0.00 0.01 0.00
                                SQ FT SQ FT  9.40E+00 1.32E+03 l.OOE+00   1    1
                                          7.78E+04  1.50E+03  1.84E-01 -7.19E-06
                                          6.12E+02  1.58E+O1 -1.39E-02  5.99E-06
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00 0.03 0.41 0.12 0.16 0.27 0.00 0.01 0
GRAV SLDG THICKENER-ALUM £ FECL3SQ FT SQ FT  3.14E+02 1.78E+04 l.OOE+00   1
  4V18E+04  4.06E+01 -3.99E-03  1.58E-07
                      1.17E-06 -1.63E-10
                      O.OOE+00  O.OOE+00
                                1.12E-04
                                7.35E-05
                                O.OOE+00
  1.27E+05  3.81E+02 -5.67E-01  3.18E-04 0.00 0.46 O.OO 0.00 0.16 0.02 0.02 0.34
                                      75
-------
                              CRM.DAT FILE (CONTINUED)
BELT FILTER PRESS
   1.20E+05  5.65E+03
   5.71E+02  5.25E+01
   O.OOE+00  O.OOE+00  O.OOE+00
   9.79E+04  1.34E+03 -3.83E+00
FILTER PRESS
   2.03E+05  5.06E+03 -1.03E+01
   9.57E+02  2.88E+01 -4.96E-02
   O.OOE+00  O.OOE+00  O.OOE+00
   1.32E+05  1.92E+03 -4.14E+00
DECANTER CENTRIFUGES
   1.47E+05  1.92E+03 -4.01E+00
   6.39E+02  9.18E+01 -3.09E-01
   O.OOE+00  O.OOE+00  O.OOE+00
   9.86E+04  7.87E+02 -1.62E+00
BASKET CENTRIFUGES
   1.7SE+05  7.66E-01
   1.71E+03  1.30E-02
   O.OOE+00  O.OOE+00
   7.76E+04  8.30E-01
SAND DRYING BEDS
   7.4SE+03  2.97E+00
 -7.41E+00
 -1.7SE-04
                                GPM   GPM    1.50E+01 4.50E+02 l.OOE+00   1    1
                      1.13E+01 -1.82E-02  4.69E+04  3.40E+03  8.73E+00 -1.31E-02
                      1.23E-01 -2.09E-04  8.03E+02  1.75E+01  2.87E-02 -2.76E-05
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                6.90E-03 0.00 0.69 O.OO 0.00 0.21 0.02 0.01 0.07
                                CU FT CU FT  4.30E+00 8.96E+02 l.OOE+00   1    1
                                7.89E-03  1.66E+04  1.92E+03 -2.34E+00  1.93E-03
                                3.64E-05  7.00E+03  7.33E+00  5.26E-02 -3.01E-05
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                3.05E-03 0.00 0.61 0.00 0.00 0.18 0.01 0.01 0.19
                                GPM   GPM    l.OOE+01 5.00E+02 l.OOE+00   1    3
                                4.02E-03  5.16E+02  1.16E+03  8.29E-01 -1.05E-03
                                3.67E-04  5.64E+02  1.72E+01 -6.16E-02  7.64E-05
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                1.20E-03 0.00 0.48 0.00 0.00 0.17 0.04 0.03 0.28
                                GPD   GPD    3.60E+03 7.20E+05 l.OOE+00   1    1
                      6.13E-06 -6.15E-12  6.08E+04  7.85E-01  1.11E-05 -1.07E-11
                      8.22E-08 -7.34E-14  4.78E+03  -4.13E-02  1.38E-07 -1.38E-13
                      O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                      1.17E-05 -1.15E-11 0.00 0.53 0.00 0.00 0.17 0.05 0.01 0.24
                                SQ FT SQ FT  5.00E+03 4.00E+05 l.OOE+00   1    1
                      5.07E-07 -6.77E-12  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
            3.16E-02 -9.43E-09  1.83E-14  5.74E+02  2.84E-02  6.47E-08 -9.80E-14
            6.00E-02  1.12E-13 -2.90E-19  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.06 0.00 0.08 0.02 0.64 0.20 0.00 0.00
SLUDGE DEUATERING LAGOONS       CU FT CF/YR  4.00E+04 8.00E+06 6.25E-01   1    1
  6.79E+03  8.13E-02 -2.06E-09 -2.55E-17  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  4.22E+01  S.85E-04 -8.68E-11 -2.92E-20  1.80E+01  7.71E-03 -3.45E-10 -2.32E-18
  7.S4E+00  9.27E-03 -1.55E-10 -1.17E-18  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.51 0.00 0,04 0.01 0.28 0.16 0.00 0.00
                                GPM   GPM    2.00E+01 l.OOE+04 l.OOE+00   1   11
                                2.55E-08  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
                                MG/YR MG/YR  1.25E+00 l.OOE+02 l.OOE+00   1    7
                      6.4SE+01 -3.71E-01  5.65E+04  1.76E+04 -5.40E+01  4.24E-01
                      4.53E-02 -2.70E-04 -9.35E-01  2.09E+02  4.07E-02 -3.77E-04
                      4.17E-01 -3.05E-03  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                      O.OOE+00  O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
                                CY/YR CY/YR  l.OOE+03 3.00E+05 l.OOE+00   1    7
                                1.98E-11  4.10E+04  4.59E+00 -1.83E-05  4.27E-11
                                          8.96E+01  2.93E-02  1.11E-07 -2.74E-13
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
SLUDGE DISPOSAL-SANITARY SEWER
  4.94E+01  8.43E+02 -2.11E-04
  O.OOE+00  O.OOE+00  O.OOE+00
  5.00E+03  O.OOE+00
  O.OOE+00  O.OOE+00
LIQUID SLUDGE HAULING
  7.23E+04  2.03E+03
  7.33E+00  5.94E+02
  6.53E+01  5.07E+02
  O.OOE+00  O.OOE+00
DEUATERED SLUDGE HAULING
  4.S6E+04  1.34E+00 -7.65E-06
  1.21E+02  9.79E-02
  1.31E+02  8.85E-02
                      O.OOE+00
                      O.OOE+00
                      1.27E-07 -3.05E-13
                      7.88E-08 -1.95E-13
  3.00E+01
  1.97E+04
            l.OOE+02  4.89E-04
            5.O6E+03 -8.25E+00
  O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00 0.00 0.00 0.00 0.00 0.00 0,00 0.00 0.00
RAW WATER PUMPING FACILITY      MGD   MGD    l.OOE+00 2.00E+02 l.OOE+00   1    5
  1.92E+04  3.43E+03 -2.89E+00  8.85E-03 -5.38E-03  4.49E+04 -9.78E-05 -1.42E-07
  2.17E+02  1.33E+02  2.80E-01 -1.63E-03  4.99E+02  2.37E+01 -3.57E-02  1.66E-04
                                1.34E-05  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                3.51E-02 0.00 0.42 0.00 0.00 0.17 0.32 0.09 0.00
FINISHED WATER PUMPING FACILITY MGD   MGD    1.50E+00 3.00E+02 l.OOE+00   1    5
  3.75E+04  2.82E+03  1.50E+01 -3.27E-02  8.19E-04  5.00E+04  8.10E-05 -3.33E-07
                                1.97E-04  5.06E+02  2.13E+01  5.23E-03. 1.22E-05
                                4.28E-04  O.OOE+00  O.OOE+00  0'. OOE+00  O.OOE+00
                                5.27E-02 0.00 0.41 0.00 0,00 0.11 0,22 0.26 0.00
                                GAL   GAL    l.OOE+04 7.SOE+06 l.OOE+00   1    1
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  1.S9E+02  1.47E+02 -1.36E-01
  l.OOE+02  3.00E+02 -2.19E-03
  4.07E+04  8.88E+03 -2.05E+01
CLEARUELL STORAGE-BELOW GROUND
  3.10E+04  4.22E-01 -2.78E-08 -1.39E-17
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00 0.01 0.00 0.3S 0,17 0.44 0..00 0.03 0.00
CLEARUELL STORAGE-GROUND LEVEL  GAL   GAL    8.50E+03 9.40E+06 l.OOE+00   1    1
  2.70E+04  2.07E-01 -9.72E-09 -3.95E-17  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
DIFFUSED AERATION BASIN
  5.43E+04  2.99E+01 -9.75E-05
  2.98E+03  1.61E-01 -5.72E-07
  O.OOE+00  O.OOE+00  O.OOE+00
  1.47E+04  S.73E-01 -2.71E-06
AERATION-AERATION TOWERS
  2.45E+04  1.36E+01 -6.96E-05
  S.48E+02  7.07E-02  2.19E-07
  O.OOE+OO  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
ADHINrLAB S
  1.83E+04
  1.80E+03
  O.OOE+OO
  4.16E+04
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.00 0.71 0.08 0.06 0.01 0.09 0.05 0.00
                                CU FT CU FT  1.90E+03 3.BOE+05 l.OOE+00   1    1
                                1.75E-10 -6.46E+02  1.48E+02  3.14E-OS -6.90E-11
                                8.65E-13  1.30E+03  1.27E-01 -3.12E-07  6.54E-13
                                0,OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                5.08E-12 0.01 0.61 0.02 0.03 0.16 0.00 0.15 0.02
                                CU FT CU FT  6.80E+02 2.S6E+05 l.OOE+00   1    1
                                1.76E-10 -4.02E+03  1.07E+01 -7.18E-06  2.11E-11
                                •4.83E-13  4.68E+01  1.03E-02 -5.01E-08  1.38E-13
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  0,OOE+00
                          .....  O.OOE+00 0.01 0.67 0.06 0.08 0.14 0.00 0.04 0.00
            MAINTENANCE BUILDINGMGD   MGD    l.OOE+00 2.00E+02 l.OOE+00   1    1
            6.96E+03 -5.69E+01  1.65E-01  O.OOE+00  O.OOE+00  O.OOE+00  O.'OOE+OO
            2.52E+02 -1.71E+00  4.52E-03  1.28E+03  2.68E+02 -2.42E+00  7.31E-03
            O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  0,OOE+00  O.OOE+00
            1.59E+04 -1.30E+02  3.76E-01 0.00 0.00 0.00 0.00 0.00 0.00 0.00 1.00
                                       76
-------
                              ORV.DAT FILE  (CONTINUED)
                                      GPM    4.00E+00  1.40E+03  l.OOE+00    1  409
                                1.81E-02  7.27E+01  1.30E+02 -4.88E-01   1.36E-03
                                4.70E-04  1.25E+Q3  4.87E+01' -3.26E-01   7.33E-04
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00   O.OOE+00
                                8.99E-03 0.01 0.44 0.01 0,00 0.09 0.02 0.18  0.25
                                GPM   GPM    8.00E+01 1.40E+03 l.OOE+00   1  409
                                2.65E-02 -9.69E+01  1.06E+02 -1.38E-01  4.04E-04
                                1.49E-04  2.68E+03  4.41E+00  3.56E-02 -1.06E-04
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                4.41E-02 0.01 0.22 0.15 0.00 0.08 0.06 0.17 0.31
PACKAGE PRESSURE FILTRATION PLNTGPM   GPM    7.00E-01 3.50E+02 l.OOE+00   1  409
  1.82E+04  5.01E+03 -1.03E+02  8.27E-01  7.09E+00  1.22E+02  8.55E-01 -1.01E-02
  4.64E+01  1.97E+01 -4.43E-01  3.58E-03  3.57E+02
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  2.40E+04  1.75E+03  6.24E+00 -1.64E-01 0.01 0.43 0.01-0.00 0.13 0.02 0.12 0.28
PACKAGE COMPLETE TREATMENT PLANTBPM
  5.70E+04  2.27E+03 -7.84E+00
  2.85E+02  3.75E+01 -2.28E-01
  O.OOE+00  O.OOE+00  O.OOE+00
  2.80E+04  1.98E+03 -4.70E+00
PACKAGE GRAVITY FILTER PLANTS
  9.17E+04  1.84E+03 ^-9.25E+00
  7.49E+02  1.01E+01 -5.35E-02
  O.OOE+00  O.OOE+00  O.OOE+00
  9.05E+04  2.20E+03 -1.68E+01
                                                    5.17E+00 -6.18E-02
                                                    O.OOE+00  O.OOE+00
                                                                        9.14E-04
                                                                        O.OOE+00
FILTER MEDIA-RAPID -SAND
  4.50E+01  4.71E+01 -1.85E-01
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+OO
  O.OOE+00  O.OOE+00  O.OOE+00
FILTER MEDIA-DUAL MEDIA
  9.56E+01  5.56E+01 -1.34E-O1
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
FILTER MEDIA-MIXED MEDIA
  1.41E+02  8.11E+01 -1.54E-01
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
                                SO FT SO FT  4.00E+00 2.80E+02 l.OOE+00   1    1
                                4.30E-04  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00
                                O.OOE+00 0.00 0.00 0.00 0.00 0.00 O.OQ 0.00 0.00
                                SO FT SO FT  4.00E+00 2.80E+02 l.OOE+00   1    1
                                3.15E-04  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE100
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 O.OO 0.00 0.00 0.00 0.00 0.00 0.00 0.00
                                SO FT SQ FT  4.00E+00 2.80E+02 l.OOE+00   1    1
                                2.91E-04  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
FILTER MEDIA-MIXEDrlNST U/MF SUPSQ FT SQ FT  4.00E+00 2.80E+02 l.OOE+00    1     1
  1.08E+03  8.91E+01 -2.18E-01  4.42E-04  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00
                                O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+OO. O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
PACKAGE PRESS DIATOMITE FILTERS GPD   GPD
  4.43E+04  8.79E-02  1.07E-07 -7.25E-14
  1.09E+02  1.66E-03 -2.33E-09
  O.OOE+00  O.OOE+00  O.OOE+OO
  2.29E+04  9.16E-02 -1.05E-07
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
                                             2.80E+04 l.OOE+06 l.OOE+00   1  402
                                          1.58E+01  4.86E-02  1.39E-10  2.87E-15
                                1.32E-15  6.27E+02  2.06E-03 -2.20E-09  2.41E-15
                                O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                '6.71E-14 0.01 0.55 0.01 0.01 0.09 0.04 0.05 0.24
                                      GPM
PACKAGE VACUUM DIATOMITE FILTERSGPM
  4.39E+04  3.15E+02 -4.98E-01
  7.10E+01  2.83E+00 -5.79E-03
  O.OOE+00  O.OOE+OO  O.OOE+00
  2.26E+04  1.22E+02 -1-.45E-01
PACKAGE ULTRAFILTRATION PLANTS
  9.01E+03  9.28E-01 -8.97E-07
  3.08E+01  6.74E-02  1.90E-08
  O.OOE+00  O.OOE+OO  O.OOE+00
  1.01E+04  3.05E-01 -2.48E-07
PACKAGE GRAN ACT CARBON COLUMNS GPD   GPD
  8.79E+03  3.50E-01 -1.09E-06  1.29E-12 -1
                                             3.00E+01  7.20E+02  l.OOE+00    1   402
                                4.57E-04  6.00E+03   1.17E+02  7.13E-02 -1.70E-04
                                4.40E-06  6.54E+02   2.45E+00  -1.36E-03   3.23E--06
                                O.OQE+00  O.OOE+OO   O.OOE+00  O.OOE+00   O.OOE+00
                                1.09E-04 0.01 0.65  0.01  0.01  0.05  0.05 0.02  0,20
                                GPD   GPD    2.50E+03  l.OOE+06  l.OOE+00    1   302
                                5.66E-13  1.15E+03   7.39E-02  -4.18E-08   2.75E-14
                                1.47E-14  3.52E+02   6.76E-04  2.97E-10 -2.26E-16
                                O.OOE+OO  O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+OO
                                2.24E-13 0,01 0.64  0.01  0.00  0,07  0.01 0.13  0.13
                                             2.50E+03  5.00E+05  l.OOE+00    1     1
                                             16E+01   5.27E-02  -9.29E-08   1.67E-13
  8.11E+01  7.40E-03   1.93E-08 -3.00E-14   9.62E+01   7.32E-04  -1.37E-09   1.12E-15
  O.OOE+00  O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00   O.OOE+00   O.OOE+00   O.OOE+00
  5.27E+03  3.54E-01 -1.09E-06  1.11E-12 0.01  0.25  0.02  0.00  0.22  0.15  0.03  0.32
POTASSIUM PERMANGANATE FEED SYSTLB/DAVLB/DAY l.OOE-01  l.OOE+01  l.OOE+00   1   101
   7.36E+03 -9.62E-03
   5.00E+01 -6.52E-05
   O.OOE+00  O.OOE+OO
   2.05E+03 -2.66E-03
POLYMER FEED SYSTEMS
                       6.09E-04
                       4.10E-06
                       O.OOE+00
                       1.65E-04
                                8.27E-05  1.80E+03 -2.34E-03  1.49E-04  2.05E-05
                                5.70E-07  1.01E+02 -1.32E-04  8.18E-06  1.16E-06
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                2.36E-05 0.00 0.22 O.OO 0.00 0,05 0.05 0.03 0.65
                                LB/DAYLB/DAY l.OOE-01 l.OOE+01 l.OOE+00   1  110
  1.90E+04 -9.51E-03 -1.19E-03 -2.62E-05  1.73E+04 -8.79E-03 -1.07E-03 -2.58E-05
  2.40E+02 -1.23E-04 -1.51E-05 -3.20E-07  1.98E+02 -1.04E-04 -1.24E-05 -2.76E-07
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  8.21E+03 -4.17E-03 -5.61E-04 -1.32E-05 O.OO 0.67 0.00 0.00 0.04 0.02 0.07 0.20
POWDERED ACT CARBON FEED SYSTEMSLB/HR LB/HR  l.OOE+00 l.OOE+01 l.OOE+00   1  101
  2.93E+03  4.68E+02 -5.01E+01  2.29E+00  1.95E+03  1.69E+02 -8.96E+00  9.72E-01
                                6.91E-02  1.34E+02  7.33E+01 -7.12E+00  3.98E-01
                                O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 O.OO 0.79 0.00 0.00 0.11 0.00 0.10 0.00
                                LB/DAYLB/DAY l.OOE-01 l.OOE+02 l.OOE+00  . 1  101
                                4.87E-08  1.63E+03  1.48E-04  6.99E-06  1.85E-08
                                4.72E-10  1.83E+02  1.64E-05  7.79E-07  2.09E-09
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                2.93E-08 0.00 0.35 0.00 0.00 0.08 0.03 0.05 0.49
SODIUM HYPOCHLORITE SOLUTN FEED LB/DAYLB/DAY l.OOE-01 1.00E+O2 l.OOE+00   1  101
  4.31E+03  3.92E-04  1.84E-05' 4.87E-08  5.70E+02  5.15E-05  2.44E-06  6.37E-09
  2.00E+01  1.81E-06  8.51EM>8  2.36E-10  3.6SE+02  3.33E-05  1.55E-06  4.27E-09
  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  2.56E+03  2.32E-O4  1.09E-05  2.93E-08 0.00 0.29 0.00 0.00 0.08 0.08 0.05 0.50
   3.89E+O1   1.24E+01  -1.12E+00
   O.OOE+00   O.OOE+00   O.OOE+00
   O.OOE+00   O.OOE+00   O.OOE+00
 DIRECT  FEED  GAS  CHLORINATION
   4.'31E+03   3.92E-04   1.84E-05
   4.00E+01   3.62E-06   1.70E-O7
   O.OOE+00   O.OOE+00   O.OOE+00
   2.56E+03   2.32E-04   1.09E-05
                                       77
-------
                               CRV.DAT FILE  (CONTINUED)
 OZONE GENERATING AND FEED       LB/DAYLB/DAY S.OOE-01 l.OOE+01 l.OOE+00   1    1
   2.10E+04  2.55E+03 -8.76E+00 -3.49E-01  3.78E+02  4.37E+03 -7.69E+00 -3.22E+00
   1.11E+02  1.77E+01  1.49E-02  3.37E-04  3.42E+02  5.98E+01 -6.71E+00  2.81E-01
                                 O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
   O.OOE+00
   6.57E+03
             O.OOE+00  O.OOE+00
             4.02E-03 -1.14E-03 -4.66E-06 0.00 0.68 0,00 0.00 0.11 0.00 0.00 0.21
                                 GAL   GAL    8.50E+02 1.35E+04 l.OOE+00   1    1
                                -8.89E-09  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                 O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                 O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                 O.OOE+00 0.00 0.84 0.03 0.01 0.12 0.00 0,00 0.00
 OZONE CONTACT CHAMBER
   9.27E+02 -3.12E-02  1.84E-04
   O.OOE+00  O.OOE+00  O.OOE+00
   O.OOE+00  O.OOE+00  O.OOE+00
   O.OOE+00  O.OOE+00  O.OOE+00
 CHLORINE DIOXIDE GENERATING/FEEDLB/DAYLB/DAY l.OOE-01  5.00E+01  l.OOE+00
   9.67E+03  7V32E-04 -2.92E-05
   l.OOE+02  7.72E-06 -3.08E-07
   O.OOE+00  O.OOE+00  O.OOE+00
   4.10E+03  3.18E-04 -1.24E-05
 ULTRAVIOLET LIGHT DISINFECTION
   3.38E+03  3.36E+01   1.58E-03
                                 5.93E-07  1.24E+03
                                 6.05E-09  3.65E+02
                                 O.OOE+00  O.OOE+00
                                 2.52E-07 0.00 0.48
                                                                              201
                                                     9.50E-05  -3.82E-06   7.70E-08
                                                     2.78E-05  -1.10E-06   2.22E-08
                                                     O.OOE+00   O.OOE+00   O.OOE+00
                                                    0.00  0.00  0.07  0.06  0.05  0,34
   5.91E+01   4.07E+00
   O.OOE+00   O.OOE+00
   9.65E+03   6.48E+00 -3.9OE-03
 REVERSE OSMOSIS
   9.96E+03   1.41E+00 -1.71E-06
   8.34E+00   9.66E-02
   O.OOE+00   O.OOE+00
                                 GPM   GPM
                                 1.45E-06
                       3.80E-04 -3.25E-07
                       O.OOE+00  O.OOE+00
                       2.54E-09  -1.84E-15
                       O.OOE+00   O.OOE+00
                                              l.OOE+01  7.80E+02  l.OOE+00    1     1
                                           2.80E+01   4.17E+01  -7.22E-03   7.24E-06
                                           2.31E+01   1.69E-02  3.17E-05 -2.87E-08
                                           O.OOE+00   O.OOE+00  O.OOE+00   O.'OOE+OO
                                2.08E-06 0.01 0.72  0.02 0.00  0.03 0.04 0.04 0.14
                                GPD    GPD     2.50E+03  l.OOE+06  l.OOE+00    1  302
                                1.06E-12   1.68E+03   2.65E+00  -6.22E-07   3.79E-13
                                           7.56E+02   3.97E-03  -6.28E-09   3.40E-15
                                           O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
  7.64E+03  7.78E-02  4.61E-08 -2.63E-14 0.00 0.71  0.00 0.00  0.14 0.00 0.09 0.06
PRESSURE ION EXCHANGE-SOFTENING GPD    GPD     7.00E+04  8.60E+05  l.OOE+00  49-4101
  5.39E+04  1.59E-01 -1.44E-07  8.54E-14   7.54E+00   1.87E-03  2.87E-10 -2.06E-16
  3.89E+02  4.50E-03 -7.15E-10  3.65E-16   8.08E+02   3.01E-03  -3.92E-09   2.21E-15
  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00   O.OOE+OO   O.OOE+00  O.OOE+00   O.OOE+00
  1.02E+04  4.93E-02 -3.67E-08  1.75E-14 0.01 0.32  0.02 0.03  0.10 0.15 0.26 0.11
PRESSURE ION EXCHANG-N03 REMOVALGPD    GPD     7.00E+04  8.30E+05  l.OOE+00  121-41O1
  5.29E+04  2.16E-01 -1.56E-07  1.03E-13 -1.40E+01   2.03E-03  -4.25E-10   3.07E-16
  2.8SE+02  2.32E-02 -3.52E-09  2.49E-15   7.92E+02   3.29E-03  -4.69E-09   2.81E-1S
  O.OOE+OO  O.OOE+00  O.OOE+00  O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
  1.00E+O4  5.2BE-02 -4.35E-08  2.22E-14 0.01 0.49  0.01 0.01  0.06 0.12 0.21 0.09
ACTIVATED ALUMINA FLUORIDE REMOVGPD    GPD    1.27E+04  9.10E+05  l.OOE+00   1  202
  3.79E+04  2.46E-01 -3.71E-07  2.25E-13   8.07E-01   2.73E-05  -7.66E-11   7.95E-17
                                2.33E-16   7.75E+02   4.41E-03  -7.96E-09   4.94E-15
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
                                1.96E-14 0.00 0.29  0,00 0.00  0.12 0.20 0.29 0.10
                                GPD    GPD    1.63E+04  8.00E+05  l.OOE+00  952-6201
                                7.81E-14   1.66E+01   1.66E-04  9.52E-10 -7.61E-16
                                2.31E-15   7.47E+02   3.97E-03  -6.53E-09   4.23E-15
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
  1.86E+04  4.99E-02  1.45E-07 -1.35E-13 0.00 0.33  0.00 0.00  0.13 0.15 0.21 0.18
PACKAGE RAU WATER PUMPING-TDH=50GPM    GPM    2.00E+01  7.00E+02  l.OOE+00   1    1
  1.04E+04 '6.20E+01 -1.25E-01  1.05E-04   4.81E-01   1.16E+02  8.61E-04 -9.36E-07
  4.13E+01  4.71E-01 -1.06E-03  8.36E-07   4.83E+01   1.11E-01  -6.50E-05   7.86E-08
  O.OOE+00  O.OOE+00  O.OOE+OO  O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00   O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+0'0 0.07 0.59  0.05 0.00  0.17 0.08 0.04 0.00
PACKAGE HIGH SERVICE PUMP STATN GPM    GPM    3.00E+01  1.10E+03  l.OOE+00   1    1
  1.05E+04  1.32E+01 -1.68E-03 -8.47E-07 -6.08E+02   1.47E+02  1.79E-01 -1.24E-04
  2.84E+01  S.46E-02 -4.27E-05  4.00E-08   9.75E+01   1.48E-01 -1.97E-04  9.20E-08
                                O.OOE+00   O.OOE+00   O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.00 0.80 0.00 0.00 0.12 0.06 0.02 0.00
                                GAL    GAL    5.00E+02 3.00E+04  l.OOE+00   1    1
                                8.89E-10   O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00   O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.01 0.00 0.04 0.89 0.06 0.00 0.00 0.00
                                GPD   GPD    6.80E+01 4.11E+04  l.OOE+00   1    7
                                4.93E-09  4.06E+04   1.10E+01 -2.45E-04  3.41E-09
                                          2.68E+01  3.53E-02  3.98E-06 -7.15E-11
                                          O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
  3.B9E+02  2.56E-03 -8.74E-10
  O.OOE+00  O.OOE+00  O.OOE+00
  6.90E+03  3.41E-02 -2.26E-08
BONE CHAR FLUORIDE REMOVAL
  5.37E+04  2.18E-01 -1.53E-07
  5.21E+02  5.02E-03 -3.36E-09
  O.OOE+OO  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
STEEL BACKUASH/CLEARUELL TANKS
  9.23E+02  1.36E+00 -4.19E-05
  O.OOE+00  O.OOE+OO  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
LIQUID SLUDGE HAULING
  3.97E+04  7.39E+00 -3.13E-04
  3.96E+01  1.54E-01
  4.04E+01  1.33E-01
                      5.69E-06 -1.01E-10
                      5.53E-06 -1.02E-10
  O.OOE+00  O.OOE+OO  O.OOE+00  O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
BEUATERED SLUDGE HAULING        CY/YR CY/YR  l.OOE+02 5.00E+04 l.OOE+00   1    7
  2.84E+03  4.26E-01 -1.01E-05  8.12E-11  3.02E+04  8.54E+00 -2.40E-04  2.79E-09
  1.92E+02  5.09E-02  3..29E-06 -4.47E-11  6.40E+00  6.09E-02 -1.74E-06  2.62E-11
                                6.20E-11  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
                                GPD   GPD    5.00E+01 2.50E+04 l.OOE+00   1   11
                                5.50E-11  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
                                O.OOE+00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
  7.03E+00  1.55E-01 -4.18E-06
  O.OOE+00  O.OOE+00  O.OOE+00
SLUDGE DISPOSAL-SANITARY SEWER
 -1.69E-O2  2.40E-01 -1.63E-06
  O.OOE+00  O.OOE+00  O.OOE+00
  5.00E+03  O.OOE+00  O.OOE+00
  O.OOE+00  O.OOE+00  O.OOE+00
                                       78
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                           CPU.DAT FILE (CONTINUED)
SLUDGE DEUATERING LAGOONS
  1.63E+03  2.48E-01 -1.12E-05
  4.60E+01  5.63E-O3 -4.40E-O7
  1.85E+00  1.06E-02  3.90E-07
  O.OOE+00  O.OOE+00  O.OOE+00
SAND DRYING BEDS
  9.18E+02  5.80E+00  1.77E-04
  3.33E+00  3.33E-02  3.68E-09
  2.33E+01  3.33E-02  8.64E-09
  O.OOE+00  O.OOE+00  O.OOE+00
 CU FT CF/YR  1.50E+03 3.00E+04 S.OOE-01   1    1
 2.63E-10  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
 1.29E-11  1.49E+01  1.28E-04  1.35E-06 -5.36E-11
-1.74E-11  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
 O.OOE+00 0.31 0.00 0.13 0.00 0.29 0.27 0.00 0.00
 SO FT SQ FT  2.00E+02 8.00E+02 l.OOE+00   1    1
-7.98E-07  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
 6.99E-13  1.11E+02  2.40E-01 -3.73E-06  1.99E-07
-1.09E-11  O.OOE+00  O.OOE+00  O.OOE+00  O.OOE+00
 O.OOE+00 O.O5 0.00 0.37 0.05 0.24 0.29 0.00 0.00
                                      79
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                                   TECHNICAL REPORT DATA
                            (Please read Instructions on the reverse before completing)
1. REPORT NO.
 EPA-600/2-79-162d
                             2.
                                                           3. RECIPIENT'S ACCESSION NO.
4. TITLE AND SUBTITLE
 ESTIMATING WATER TREATMENT COSTS
 Volume 4.  Computer User's Manual for Retrieving
 and Updating Cost Data     	
              5. REPORT DATE
               August  1979  (Issuing Date)
              6. PERFORMING ORGANIZATION CODE
7. AUTHOR(S)
 Thomas S. Lineck,  Robert C. Gumerman, and
 Russell L.  Gulp
                                                           8. PERFORMING ORGANIZATION REPORT NO.
9. PERFORMING ORGANIZATION NAME AND ADDRESS
 Culp/Wesner/Culp
 Consulting  Engineers
 2232 S.E. Bristol,  Suite 210
 Santa Ana,  California  92707
              1O. PROGRAM ELEMENT NO.
               1CC614,  SOS  1,  Task 38
              11. CONTRACT/GRANT NO.

               68-03-2516
12. SPONSORING AGENCY NAME AND ADDRESS
 Municipal Environmental Research Laboratory—Gin.,OH
 Office of Research and Development
 U.S. Environmental Protection Agency
 Cincinnati,  Ohio  45268
              13: TYPE OF REPORT AND PERIOD COVERED
               Final      	
              14. SPONSORING AGENCY CODE
               EPA/600/14
15. SUPPLEMENTARY NOTES   Proj ect Officer:  Robert M.  Clark
 See also  EPA-600/2-78-182 (NTIS PB284274/AS); Volume 1,
 Volume  2,  EPA-600/2-79-162b; and Volume  3,  EPA-600/2-79-
               (513)  684-7488.
               EPA-600/2-79-162a;
              •162c.
16. ABSTRACT
      This  report discusses unit processes  and combinations of unit processes  that  are
 capable  of removing contaminants included  in the National Interim Primary Drinking
 Water Regulations.   Construction and operation and maintenance cost curves are
 presented  for 99 unit processes that are considered to be especially applicable to
 contaminant removal.  The report is divided  into four volumes.  Volume 1 is a summary
 volume.  Volume 2 presents cost curves  applicable to large water supply systems with
 treatnnent  capacities between 1 and 200  mgd,  as well as information on virus and
 asbestos removal.  Volume 3 includes cost  curves applicable to flows of 2,500 gpd  to
 1 mgd.   And Volume 4 is a computer program user's manual for the curves included in
 the report.   For each unit process included  in this report, conceptual designs  were
 formulated,  and construction cost curves were checked for accuracy by a second
 consulting engineering firm, Zurheide-Herrmann, Inc., using cost-estimating techniques
 similar  to those used by general contractors in preparing their bids.  Operation and
 maintenance requirements were determined individually for three categories:   Energy,
 maintenance material, and labor.  Energy requirements for the building and the  process
 are presented separately.  Costs are in October 1978 dollars.
17,
                                KEY WORDS AND DOCUMENT ANALYSIS
                  DESCRIPTORS
                                              b.lDENTIFIERS/OPEN ENDED TERMS
                            c. cos AT I Field/Group
 Economic analysis, Environmental
 engineering,  Operating costs, Computer
 programming,  Water treatment, Cost indexes,
 Water  supply, Cost estimates, Cost analysis
 Energy costs, Cost  curves,
 Safe Drinking Water Act,
 Interim primary standards,
 Unit processes, Treatment
 efficiency
13B
18. DISTRIBUTION STATEMENT
 Release to Public
                                              19. SECURITY CLASS (ThisReport)
                                                 Unclassified
                            21. NO. OF PAGES
                                   88
 20."SECURITY CLASS (Thispage)
    Unclassified
                                                                         22. PRICE
EPA Form 2220-1 (Rev. 4-77)
80
                                                         •AT U.S. GOVERNMENT PRINTING OFFICE: 1980--757-064/0174
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