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

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Desalination Desalination is a proven technology using conventional energy forms. As the relative cost of water increases, desalination will become a more viable option -- not only to extract the potable water from geopressured resources in inland areas, but also from the ocean for near-coastal and other demands. Fresh water can potentially be removed from geopressured fluids to meet critical freshwater needs in the water scarce regions of California, the lower Rio Grande Valley of Texas, and other areas, both nationally and internationally. G. S. Nitschke (Boeing, WA) and J. A. Harris (Wichita State University) proposed a system that will use the pressure gradient of the reservoir to produce electricity by way of a pressure reduction turbine and generator combination. The natural gas would be separated for sale or on-site use, and the thermal energy would be used to produce potable water through a multi-effect distillation unit. In turn, the remalnlng saturated brines could be sold. The brine is ideal for solar ponds that utilize binary power generators, a method effectively proven in Israel. Solar pond power could be used for further water production in a conventional reverse osmosis desalination scheme fed with seawater. It is suggested that such a scheme could produce as much as 40% of the total water load in California (Nitschke and Harris, 1990). F. J. Spencer (International Management Services) has identified six areas of use that he is encouraging for utilization of geopressured resources, particularly in the entire lower Rio Grande Valley, south TX, in the coming decade. The proposed areas are: 1. Recover dissolved methane and sell it as pipeline gas 2. Use the geopressured fluid or gas pressure or both to drive turbines for power production 3. Use the steam content of the geopressured fluid to drive conventional turbines for power production 20
4. Use the heat in the fluid for many industrial processes 5. Use the fluid directly depending on salinity, for both aquaculture and industry 6. Desalinate the fluid and use the salts contained in the fluid as starting points for chemicals (Spencer, 1990). 21
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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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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
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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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Matrix of Locations!') and Descript
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• , l L , ,, , ,, , , ,, ,, , ,,
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"i 8 10,116' II =1 -- ~ ~ -- iii: 1
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-I- 0; 0 0 .f: 0 -. - . '-I- - . r-
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EAST 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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.,,'" - •• 0. _. ___ _ EAST SAN
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STARR COUNTY I -i'J- ~ 10 b .......
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Net Sand Depth Thickness Sand Sand
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TABLE 5 TEXAS WATER DEVELOPMENT BOA
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ill-2 This process review is especi
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m-4 There are some built-in limitat
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ill-7 It is not surprising, therefo
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,,,,-,';8 .. - .. ~ Pretreatment Pr
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lli-9 Comparative Assumed Input Inr
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PRO-FORMA CALCULATIONS FOR REVERSE
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STEAM VENT EJECTOR • PRESSURE RED
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STEAM VENT EJECTOR I :> :>:> LfTl:>
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ID-16 a) The separate seawater inta
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1lI-18 Data for the injection flow
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lli-20 (8) Thermal content of fluid
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ill-22 The primary environmental co
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ill-24 III. B-2 BRINE DISPOSAL VIA
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1lI-26 to 10 centipoise if it is he
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1II-28 1lI.B-S&6 BYPRODUCT SALTS RE
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II I-3~ BRINES mOlAl( DlCAtlYDlAI!
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1II-32 2. Generally speaking, the s
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III-34 1. Group 1 through Group 4 w
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1II-36 Based on this comparative da
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In-38 Section UlD - Pro-Forma Econo
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II I -40 Exhibit InD-2 Assumed Inpu
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111-42 EXHIBIT llID-4 PRO-FORMA CAL
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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;' ... -
Page 164 and 165: Chapter II Summary of Injection Con
Page 166 and 167: .. ' a surface owner b. offset oper
Page 168 and 169: I. Special "Down Hole" Swvcys speci
Page 170 and 171: FLOWCHART: INJECTION/DISPOSAL WELL
Page 172 and 173: the applicant can show. by computat
Page 174 and 175: Criteria lor Determining the Adequa
Page 176 and 177: .I MODULAR POWER PLANTS FOR GEOPRES
Page 178 and 179: FIGURE 2 BINARY POWER MODULE··: .
Page 180 and 181: TABLE 1 GEOPRESSURED PLANT APPROXIM
Page 182 and 183: EGG-EP-8839 September 1991 Idaho Na
Page 184 and 185: EGG-EP-9839 Distribution Category:
Page 186 and 187: ACKNOWLEDGMENT Work supported by th
Page 188 and 189: APPENDIX A--SEATTLE TIMES EDITORIAL
Page 190 and 191: THE FEASIBILITY OF APPLYING GEOPRES
Page 192 and 193: University, January 10, 1990 with 6
Page 194 and 195: OF 35 50 100 150 200 250 300 I I I
Page 196 and 197: Desalination Plant Supply Well \ er
Page 198 and 199: for an extensive chicken hatching/r
Page 200 and 201: THE GEOPRESSURED RESOURCE Geopressu
Page 202 and 203: Production Co. has leased 4000 acre
Page 204 and 205: p' , ~"\ ,0 .~~ ~~ 'i ~ __ =:-~ 'l.
Page 208 and 209: --- r/< N N EIII ... IK:ltI' 011 ,,
Page 210 and 211: Sacramento Valley and San Joaquin V
Page 212 and 213: Gas Use and Sales Gas contained in
Page 214 and 215: Sulfur Fraschtng Sulfur can be reco
Page 216 and 217: Coal Desulfurization and Preparatio
Page 218 and 219: films. Today, nearly half of the br
Page 220 and 221: Waste gases Chlorinator Chlorine Di
Page 222 and 223: POTENTIAL AGRICULTURE/AQUACULTURE A
Page 224 and 225: The University of Southwestern loui
Page 226 and 227: Snapping turtles are important comp
Page 228 and 229: ECONOMIC CONSIDERATIONS This sectio
Page 230 and 231: economic techniques because cash fl
Page 232 and 233: Assuming a geopressured well can pr
Page 234 and 235: Table 3. Agriculture/aquaculture fi
Page 236 and 237: Circular Tank 90' Diam. 80'F Bypass
Page 238 and 239: Potable water for agriculture and a
Page 240 and 241: DESALINATION/AGRICULTURE/AQUACULTUR
Page 242 and 243: REFERENCES Carlson, R. A., P. H. Po
Page 244 and 245: APPENDIX A SEATTLE TIMES EDITORIAL
Page 246 and 247: APPENDIX B HEATING REQUIREMENTS FOR
Page 248 and 249: temperature and the heat gain curve
Page 250 and 251: Thermal Refuge Heating Requirements
Page 252 and 253: APPENDIX C INTEGRATED APPLICATIONS
Page 254 and 255: 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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(GP/GT) for Additional Water Supply in the Lower Rio Grande

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