(GP/GT) for Additional Water Supply in the Lower Rio Grande

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ill-7 It is not surprising, therefore, that the development of the EDR process followed logically as an answer to these RO constraints, noting that current reversal in the EDR process on a set frequency is an elegant and efficient way to avoid (or at least greatly reduce) the advent of "concentration polarization". The one clear difference between the operational requirements of the RO Process as compared to the EDR Process is the much higher pressures at which RO operations have to be optimized. Pressure ranges from 400 to 1,000 psig are not uncommon, and these occasion higher fixed costs for electricity for pumping, in addition to the electrical power costs for the rest of the RO Process. It has been estimated that electrical costs for pumping alone can reach as high as 50 cents per thousand gallons. This is the reason that part of these costs are sought to be recovered by the inclusion of a power recovery turbine in the brine discharge line of RO plants. Approximately 20% of such losses are estimated to be reasonably recoverable. On balance, then, the overall operating costs of an RO plant as opposed to an EDR plant are higher for otherwise equivalent conditions. Process selection, however has to be influenced by the fact that EDR plants cannot cope with salinity conditions in excess of 6,000 ppm TDS, and this fact alone guarantees that there will always be a significant share of total installations that will accrue to the RO Process. Please see FIG. 4 for a flow diagram of the RO Process.
111-8 I Post treOJtmcnt chemicals Desalted + Drawback/flush permeate ~--p-
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KLEBER J. DENNY, INC. 312 Grandview
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KLEBER J. DENNY, INC. 312 Grandview
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FINAL REPORT ON TEXAS WATER DEVELOP
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REPORT ON TASK NO. I: CO-LOCATION S
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1-2 1. GP/GT Fairways Information p
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o s:: 011= m ,; .. f ; iI '& ri i'
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Table S Selected Formation Water An
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average depth of 10,033 feet, avera
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high, the sands are not thick enoug
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included distributary channel or de
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the eastern part of the study area,
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to coastal barrier sandstone on the
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within Reservoir Area B, the sand a
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Papadopulos, S. S., 1975, The Energ
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FLUID PROPERTIES Gas Gas Water Sol'
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only reason for selecting that limi
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Hidalgo Co. , , , ,, , ,, , ,,, , ,
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§ 8 10,116' ;;;- - ... : 10,695' F
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-r- ~~ '1- • r- ~~ .... . ~ 0 0 0
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MARK SAND (MINIMUM) Geo2 Fluid Prod
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BOND SAND (MINIMUM) Geo2 Fluid Prod
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EAST SAND (MINIMUM) Geo2 Fluid Prod
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MARK SAND (MINIMUM) Geo2 Fluid Prod
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BOND SAND (MINIMUM) Geo2 Fluid Prod
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EAST SAND (MAXIMUM) Geo2 Fluid Prod
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MARK SAND (MINIMUM) 1 5 Year Cumula
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BOND SAND (MINIMUM) 1 5 Year Cumula
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EAST SAND (MINIMUM) 1 5 Year Cumula
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jpH~j·:/·3,000 mgi1 TOS Sli,;,lly
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average depth of 10,033 feet, avera
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high, the sands are not thick enoug
Page 64 and 65: included distributary channel or de
Page 66 and 67: the eastern part of the study area,
Page 68 and 69: to coastal barrier sandstone on the
Page 70 and 71: Within Reservoir Area B, the sand a
Page 72 and 73: Papadopulos, S. S., 1975, The Energ
Page 74 and 75: FLUID PROPERTIES Gas Gas Water Sol'
Page 76 and 77: only reason for selecting that limi
Page 78 and 79: Matrix of Locations!') and Descript
Page 80 and 81: • , l L , ,, , ,, , , ,, ,, , ,,
Page 82 and 83: "i 8 10,116' II =1 -- ~ ~ -- iii: 1
Page 84 and 85: -I- 0; 0 0 .f: 0 -. - . '-I- - . r-
Page 86 and 87: MARK SAND (MINIMUM) Geo2 Fluid Prod
Page 88 and 89: BOND SAND (MINIMUM) Geo2 Fluid Prod
Page 90 and 91: EAST SAND (MINIMUM) Geo2 Fluid Prod
Page 92 and 93: MARK SAND (MINIMUM) Geo2 Fluid Prod
Page 94 and 95: BOND SAND (MINIMUM) Geo2 Fluid Prod
Page 96 and 97: EAST SAND (MAXIMUM) Geo2 Fluid Prod
Page 98 and 99: MARK SAND (MINIMUM) 1 5 Year Cumula
Page 100 and 101: BOND SAND (MINIMUM) 1 5 Year Cumula
Page 102 and 103: .,,'" - •• 0. _. ___ _ EAST SAN
Page 104 and 105: STARR COUNTY I -i'J- ~ 10 b .......
Page 106 and 107: Net Sand Depth Thickness Sand Sand
Page 108 and 109: TABLE 5 TEXAS WATER DEVELOPMENT BOA
Page 110 and 111: ill-2 This process review is especi
Page 112 and 113: m-4 There are some built-in limitat
Page 116 and 117: ,,,,-,';8 .. - .. ~ Pretreatment Pr
Page 118 and 119: lli-9 Comparative Assumed Input Inr
Page 120 and 121: PRO-FORMA CALCULATIONS FOR REVERSE
Page 122 and 123: STEAM VENT EJECTOR • PRESSURE RED
Page 124 and 125: STEAM VENT EJECTOR I :> :>:> LfTl:>
Page 126 and 127: ID-16 a) The separate seawater inta
Page 128 and 129: 1lI-18 Data for the injection flow
Page 130 and 131: lli-20 (8) Thermal content of fluid
Page 132 and 133: ill-22 The primary environmental co
Page 134 and 135: ill-24 III. B-2 BRINE DISPOSAL VIA
Page 136 and 137: 1lI-26 to 10 centipoise if it is he
Page 138 and 139: 1II-28 1lI.B-S&6 BYPRODUCT SALTS RE
Page 140 and 141: II I-3~ BRINES mOlAl( DlCAtlYDlAI!
Page 142 and 143: 1II-32 2. Generally speaking, the s
Page 144 and 145: III-34 1. Group 1 through Group 4 w
Page 146 and 147: 1II-36 Based on this comparative da
Page 148 and 149: In-38 Section UlD - Pro-Forma Econo
Page 150 and 151: II I -40 Exhibit InD-2 Assumed Inpu
Page 152 and 153: 111-42 EXHIBIT llID-4 PRO-FORMA CAL
Page 154 and 155: Appendices
Page 156 and 157: Appendix A Preliminary Estimates of
Page 158 and 159: APPENDIX B
Page 160 and 161: -------- ThIs Underground Injection
Page 162 and 163: Federal Requirements - -"-J;' ... -
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Chapter II Summary of Injection Con
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.. ' a surface owner b. offset oper
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I. Special "Down Hole" Swvcys speci
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FLOWCHART: INJECTION/DISPOSAL WELL
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the applicant can show. by computat
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Criteria lor Determining the Adequa
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.I MODULAR POWER PLANTS FOR GEOPRES
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FIGURE 2 BINARY POWER MODULE··: .
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TABLE 1 GEOPRESSURED PLANT APPROXIM
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EGG-EP-8839 September 1991 Idaho Na
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EGG-EP-9839 Distribution Category:
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ACKNOWLEDGMENT Work supported by th
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APPENDIX A--SEATTLE TIMES EDITORIAL
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THE FEASIBILITY OF APPLYING GEOPRES
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University, January 10, 1990 with 6
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OF 35 50 100 150 200 250 300 I I I
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Desalination Plant Supply Well \ er
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for an extensive chicken hatching/r
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THE GEOPRESSURED RESOURCE Geopressu
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Production Co. has leased 4000 acre
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p' , ~"\ ,0 .~~ ~~ 'i ~ __ =:-~ 'l.
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Desalination Desalination is a prov
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--- r/< N N EIII ... IK:ltI' 011 ,,
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Sacramento Valley and San Joaquin V
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Gas Use and Sales Gas contained in
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Sulfur Fraschtng Sulfur can be reco
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Coal Desulfurization and Preparatio
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films. Today, nearly half of the br
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Waste gases Chlorinator Chlorine Di
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POTENTIAL AGRICULTURE/AQUACULTURE A
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The University of Southwestern loui
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Snapping turtles are important comp
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ECONOMIC CONSIDERATIONS This sectio
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economic techniques because cash fl
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Assuming a geopressured well can pr
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Table 3. Agriculture/aquaculture fi
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Circular Tank 90' Diam. 80'F Bypass
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Potable water for agriculture and a
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DESALINATION/AGRICULTURE/AQUACULTUR
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REFERENCES Carlson, R. A., P. H. Po
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APPENDIX A SEATTLE TIMES EDITORIAL
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APPENDIX B HEATING REQUIREMENTS FOR
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temperature and the heat gain curve
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Thermal Refuge Heating Requirements
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APPENDIX C INTEGRATED APPLICATIONS
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ANALYSIS OF WELL: Large Volume. Mod
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ANALYSIS OF WELL: large Volume, Mod
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ANALYSIS OF ~ELL: Large Volume. MOd
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APPENDIX D PRELIMINARY FEASIBILITY
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DES/ON • CONS(JI..TlNO • F',..,
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Des/oN • CONS
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Des/ON • CONS(.Jl..rINQ • F,A.S
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RED EWALD,lnc. 10,000 GALLON RACEWA
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",CUND F:;:SH C;LTURE TANKS ~.:::~
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~c:!~ ?:~:~.~ ?.I'n~ -: 1'DS-; mS-!
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* Texas A uaculture Association * A
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-----------------------------------
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RED EWALD. Ute. -- Round Fish Cultu
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PORTABLE MODULAR FISH HATCHERY SYST
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B & J Water- Well Ser-vice 419 East
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APPENDIX F COMPARATIVE PERFORMANCE
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BffiLIOGRAPHIC DATA SHEET for repor
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factors, utility costs, cash flow,
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afforded by low electridty rates al
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PRODUCTION LOSSES: With any type of
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deposits. minimum monthly customer
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conservative figure. This rate is u
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Other Capital Equipment YlETAL BUIL
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SECTION 3a. ~OTE 1 :-"-:ET CASH l1'
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TABLE 8·25. ASSl.;;-'1PT!O:\'S FOR
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TABLE B·26. GRED;HOUSE C.u>IT AL C
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.1 ~I ~ · ~ · ~ .. · · ~ ~ " -
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APPENDIX E
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Assumed Efficiency = 0.90 Constant
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EVALUATION OF AUTO DESALINATION As
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A review of the data for the wellhe
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J. McNutt & Associates, Inc. McAlle
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DownHole SAT(tm) SURFACE WATER DEPO
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DownHole SAT(tm) SURFACE WATER CHEM
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DownHole SAT(tm) SURFACE WATER MOME
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en C 0 09'8 -- += "0 c 0 U "0 X (])
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(/) c o += x -- (]) D -c 5 c u - D
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Degree of Supersaturation (E-01 ) 0
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(/) c - 0 (]) -- += > D (]) c -.J 0
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(/) c - 0 (]) 09'8 += -- > '"0 (])
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(/) c 0 - 09'8 -- :f= (]) -0 c > (]
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(/) c 0 09'8 -- =t= - C > 0 (]) U -
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C/) c 0 - 09'8 += (]) .- D c (]) >
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en - Cl) > Cl) C ..J o += C "'0 --
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APPENDIX G
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McPJlen Ranch, 7 t :> W:lter Recove
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c ~ (J) 09'8 0 (J) (]J 0 (1) U C2::
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McAJlen Ranch, 75'10 WJter Recovery
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IVlcPJlen I-
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c CJ) CJ) (]) ~ 0 U 0 X w & ~ ~ -m
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J) rJ) (1) u x W 09'8 ~o .. ..c. o
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c ~ 0 09'8 U) 0 U) (]) CJ.) ~ U ~ X
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McAJlen Ranch, 7510 W:1ter Recovery
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c ~ - 09'8 0 (]) 0 > Q) (]) -V ..J
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c ~ o
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c ~ 09"8 0 - (]) 0 > (]) (]) 0::: .
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c ~ 09'8 0 - 0 Cl) (1) > ~ Cl) ~ ..
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c ~ - 09'8 0 C]) 0 > (]) C]) v --1
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c ~ o (]) y - (l.) > (l.) ..J C o .
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00'8 ... .c U c -8 c (l) - ~ 5 - x
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c ~ X 0 Q.) u (}) -0 ""V - C ~ ~ c
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APPENDIX G 4 DEC 1993 TO: MR. KLEBE
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PRELIMINARY EDR/RO COSTS & PERFORMA
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GROUP 1 CONDITIONS 195,000 gpd bypa
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CASE 3 CONDITIONS 214,000 gpd bypas
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BUDGET CAPITAL COST REVIEW ---costs
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0H16D REVIEW OP O~11 COSTS .'.(1) -
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From: CANYON n,DUSTRIES, INC. 206 5
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