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<br />\1r'ELl DIAMETER (INCHES): <br />\lr"ElL DRILLING COST (!JFT): <br />SPECIRC CAPACITY GP,," <br /> <br />10 STATIC WATER LEVEL(FT): <br />$1~0 SYSTEM PRESSURE (PSI). <br />0,6 <br /> <br />850 <br />" <br /> <br />,,\ f\ 'i\ '\ <br />.-:' W,\" <br />'~'i\ <;:..'- <br /> <br />LARA~IIE. ro., mLLS AQUIFER _ SOUTHERN WELLnELD Table C7 . <br /> <br />DISCOL/Jl,"T RATE ('l>): <br />ANNUAll}.'FLATlON 'l . <br /> <br />~.oo<;W ENERGY COST SlKWH. <br />I ~O% <br /> <br />SO.O~ <br /> <br />I PROJECT YEAR: I 2 3 , , 6 7 8 , 10 II 12 13 I' I> 10 17 " " " TOTAL PR ESFJJT <br /> COST VAlut: <br />'PROD\JCTION (AFfYR): 360 360 360 360 360 360 360 360 360 360 360 360 l60 360 360 360 360 360 360 360 <br />AVa QPERLFHWELL{GPM): 225 '" 22l 225 225 22~ 225 225 22~ 225 225 225 225 m 215 ", 225 225 ", 225 <br />WELLS RfQliIRED: I 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 <br />TOTAL 'W"El..l5 ON LINE. I I I I I , I , , I I I I I I I I I I I <br />BACKUP WEW REQUIRED: 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 <br />AVERAGE WELL DEPTIl (FD: 2.650 2.650 2.650 2.MO 2.650 2.650 2.650 2.650 2.650 2.650 2.650 2.650 2.650 2.650 2,650 2.650 2.650 2.650 2.650 2.650 <br />l,I,"ElLCOST: S397.500 " " '0 '0 " " " '0 " " '0 " '0 '0 '0 " so " " $397.500 $397.500 <br />WELL RfDEVELOPME.VT COST: '0 " " '0 '0 " " so '0 S49.628 so so " '0 '0 " so so so .B1.019 $100.107 S52.:04 <br />PUMPING WATER LEVEL (FT): 1.115 1.255 1.285 1.315 ].3~5 1.315 1.405 1.~35 1.46:5 1.495 1.525 ].555 1.585 1.6]5 1,64:5 1.675 1.705 1.735 1.765 1.795 <br />AVERAGE IDH (FD: 1.463 U% U29 ],562 ].59:5 1.628 1.661 1.694 1.727 1.760 1.793 ].826 ],859 1.892 1.92:5 1.958 1.991 2.024 2.057 2.090 <br />PUMP HP REQUlREE:VWELL' 13' 142 14' 148 I>' '" I>7 160 164 107 170 173 176 179 182 '" 18' "2 '" 198 <br />[PUMPING EOUIP><ENT COST, S80.555 so SO so '0 '0 '0 " " " so so so '0 '0 " so " so " $80.555 $80.555 <br />PUMP REPLACE.\1ENTCOST: '0 " so " '0 SO B9.512 " " so '0 " '0 S43.JI9 so '0 so so so " $82.831 $52.458 <br />WEU &: PUMP COST. ~78.055 " '0 '0 '0 " $39.~12 so '0 $-19.628 so so so 543.319 so '0 " so so S~I.0/9 $66U93 S~82,7] 7 <br />PUMP\NGE;-"'ERGY COST: $74.1195 ".\6.5% 'S!i8.1:!8 $50.090 ~51.l'.l'.3 $.53.706 555.559 S57.~) S59.351 S6D(}1 \63.216 SM.28l 561.111 Vl9.383 S7L.479 $73.606 575,763 $77.9H S80.168 $82..1]1 $].285.797 5810.559 <br />TOTAL WELL&. EQUIP. COST: $555.638 549.347 $~1.]42 5;2.967 S5-1.82.3 S~6. 708 $98.137 $60.571 $62.549 $114.18-1 $66.594 S68.662 $70.761 $116.208 $75.049 577.239 $79A.59 $81.709 $83.990 5137.3S0 $1.947.390 51.393.:!76 <br />PIPELINE COST: 5[73.520 so so '0 '0 so so so '0 so '0 so so so '0 '0 so so so so 5173.520 5173.~20 <br />TRfATME.'lT COST: 52.934 $2.978 $3.022 53.066 $3.\10 $3.1~ $3.198 S3.2~2 $3.286 53.330 $3.374 $3.-118 $3.462 S3.506 53.550 $3.594 53,6:38 53.682 $3.726 53.7/0 $67.().~2 $42.944 <br />EASEMEi'o"T COSTS. , S3.600 $3.65-1 53.708 $3.761 $3.816 $3.810 $3.924 $3.978 S-1.032 5-1.086 Soi.I40 5-1.194 5-4.248 S-1.302 14.356 54.-110 $4.464 S-1.518 S-1.572 S-l626 $82..260 552.e91 <br />ITOTALCO:>JSTRUCTlON COST: $651.575 so so '0 so so $39.512 so '0 $-19.623 '0 so so $013.319 so so so so '0 S5].079 5835.113 $156J'37 <br />ICONTlr>:GE....ClES. 565.1~8 so '0 so so so $3.951 so '0 $-1.963 '0 so so $-\.332 so so so so so S5.10& $8305]] $75.t>24 <br />1~'GINEERIN"'''GMTCOST' 579.163 $-\.660 $4.833 $.5.009 $~.188 55.371 S9.902 $5.7.1-1 $5.936 $]1.589 $6.328 $6.52.8 $6.132 511.703 57.148 $7.361 $7.576 57.795 58.017 $]3.860 $220.-141 $]64.~42 <br />TOTAL CAPITAL COST: $795.896 $4.660 $..U33 $5.009 S5.188 55.371 553.366 S5.7-<4 55.936 $66.180 $6.328 $6.523 $6.732 $59.35-1 $7.148 57.361 $7.516 $7.795 58.017 570.OJ7 $U06.]09 $1.039,/)46 <br />,O&.\{ LABOR. 5UP. MTRLS: 598.313 $12.115 512..565 $13.023 $13.490 SI3.963 $19.226 $1-1.935 $15,~33 $11.943 $16.452 516.913 $17.502 523.281 $]8.585 $19.138 $19.698 $20.267 $20,844 527.609 1435.356 $302J50 <br />TOTAL 0&.\1 COST: 5179.742 $65.3-13 567.623 $69,9-'12 572.198 $7-1.693 $81.907 S79.598 $82.107 590.660 S87.242 $89.866 592.529 5]00.472 $97.970 $100.7-18 $103,5&1 $106.-118 $109.3\0 SI]8.-I2.2 $1.870.-155 SI.208.J.44 <br />ESTIMATED WELLFTELD COST: 5975.6)8 $70.003 57V.56 $7-1.951 S77.487 $SO.()6.-I $135.:!73 585.342 585.043 $156.8-10 593.569 $96.39-1 599.261 $159.826 S105.118 $108.108 5111.140 $II.Il.213 $117.327 $188A69 S3.009,522 S2.20.U47 <br />COST PER A.CRE.FOOT: SUIO '19' S201 5208 5215 S212 $376 $237 $245 ,m $260 5265 $276 ...... $292 $300 $309 $317 5326 S~2.~ , <br />COST PER 1.0000GA.L: $8.32 SO.6O SO.62 so 64 so 66 $0.68 $11.5 $013 $Q.75 51.3-1 so 80 $082 .$0.85 $l.36 SO.90 SO.92- SO" so 97 $1.00 51.61 <br />PROJECT YEAR: I 2 ) , , 6 7 , , 10 II 12 Il " " 16 17 18 19 201 TOTAL PRESE.1'lT <br /> COST VALUf <br /> <br />i <br /> <br />I <br />I <br />i <br /> <br />,.. <br />" <br />f <br /> <br />ARSTYEARCAPITALCOST(SlAF $2.211 <br />NPV ALL COSTS EXaPT YEAR ONE carr ($/1000 GAL): SO 55 <br /> <br />50lJTHER..-.; WELLfIELD WEIGJ-ITEO ... VERAGE 'fEAR ONE CAPIT AI.. COST (y~ $ 1.671 <br /> <br />HRS Water Consultants, Inc. <br />July, 1995 <br /> <br />,j <br /> <br />t' <br />[' <br />I <br />