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

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111-42<br />

EXHIBIT llID-4<br />

PRO-FORMA CALCULATIONS FOR REVERSE OSMOSIS PROCESS (RO)<br />

USING <strong>GP</strong>IFI' POWER @ SO.32lKWHR<br />

Cost Elements<br />

Capital<br />

COStsf($x 1 ()()Q)<br />

Annual<br />

Costs' ($x I ()()Q)<br />

<strong>Water</strong> Costs,<br />

$'1.000 gal.<br />

Capital Costs<br />

1.<br />

2.<br />

3.<br />

4.<br />

5.<br />

Plant and Equipment(2)<br />

Feedwater Pretreatment<br />

Feedwater <strong>Supply</strong>OJ<br />

<strong>Water</strong> Transmission<br />

Br<strong>in</strong>e Disposal<br />

$3.990<br />

o<br />

1.760<br />

820<br />

1.279<br />

$457.54<br />

o<br />

201.82<br />

94.03<br />

146.67<br />

$0.2773<br />

o<br />

0.1223<br />

0.0570<br />

0.0889<br />

Total Capital Costs<br />

$ 7,849.0<br />

$ 900.06<br />

$ 0.5455<br />

Operation and Ma<strong>in</strong>tenance Costs<br />

6. Operat<strong>in</strong>g and Ma<strong>in</strong>tenance Labor<br />

a. Plant and Equipment(2)<br />

b. Feedwater Pretreatment<br />

c. Feedwater <strong>Supply</strong><br />

d. <strong>Water</strong> Transmission<br />

e. Br<strong>in</strong>e Disposal<br />

Total Operat<strong>in</strong>g and Ma<strong>in</strong>tenance Labor<br />

7. O<strong>the</strong>r Operation and Ma<strong>in</strong>tenance Costs<br />

a. Payroll Extras (15% of 6a)<br />

b. General and Adm<strong>in</strong>istrative Overhead (30% of 6a + 7a)<br />

c. Supplies and Ma<strong>in</strong>tenance Materials<br />

d. Membrane Assembly or Replacement Tub<strong>in</strong>g(2)<br />

e. Chemicals(2)<br />

f. Fuel or Steam<br />

g. Electric Power<br />

Plant and Equipment(2)<br />

Feedwater <strong>Supply</strong><br />

<strong>Water</strong> Transmission<br />

Total O<strong>the</strong>r Operation and Ma<strong>in</strong>tenance Costs<br />

Total Operation and Ma<strong>in</strong>tenance Costs<br />

Total <strong>Water</strong> Cost (fotal Capital Plus 0, & M. Costs)<br />

$'1.000 gal.<br />

0.060<br />

o<br />

.029 .<br />

n r,u)<br />

0.21<br />

$ 0.299<br />

0.009<br />

0.021<br />

0.03<br />

0.165<br />

0.039<br />

n.el l )<br />

o<br />

0.104<br />

0.051<br />

$ 0.419<br />

$ .718<br />

$ 1.2635<br />

(1) none required<br />

(2) Based on recent <strong>in</strong>fonnation from lonics. Inc., cost <strong>in</strong>fonnation <strong>in</strong>cludes effect of 80.5%/19.5% blend<strong>in</strong>g; <strong>the</strong>re<strong>for</strong>e. actual plant size equal to<br />

4 MGD. and a water recovery factor of 82.5%. A factor of 20% has been added to cover <strong>in</strong>direct capital costs comprised of <strong>in</strong>terest dur<strong>in</strong>!!<br />

construction. eng<strong>in</strong>eer<strong>in</strong>g and cont<strong>in</strong>gencies. Also. a factor has been added <strong>for</strong> land COlt. No 20% factor added <strong>for</strong> M&O related costs<br />

(3) Based on a recent study by R.W. Harden Assoc. Total of 11 wells and a land coat factor added.

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