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

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III-34<br />

1. Group 1 through Group 4 waters conta<strong>in</strong> levels of boron <strong>in</strong> excess of 1.4 ppm which will cause severe<br />

problems <strong>for</strong> fruits, plants and o<strong>the</strong>r grow<strong>in</strong>g th<strong>in</strong>gs, but waters conta<strong>in</strong><strong>in</strong>g boron levels up to 45 ppm<br />

can be consumed by humans with no problems. Because only potable water <strong>for</strong> human consumption, as<br />

opposed to irrigation water, is under consideration here<strong>in</strong>, <strong>the</strong> impact of <strong>the</strong> presence of boron is ignored.<br />

However, if boron reduction is required, both EDR and RO could reduce same by hav<strong>in</strong>g <strong>the</strong> feedwater<br />

pH raised to 8.5 - 9.5.<br />

2. As regards silica (SiO,), <strong>the</strong> content of same <strong>in</strong> <strong>the</strong> Group 1 through 3 waters is such as to significantly<br />

limit <strong>the</strong> level of recovery of product water much more <strong>for</strong> <strong>the</strong> RO process than <strong>for</strong> <strong>the</strong> EDR process.<br />

The Group 4 waters conta<strong>in</strong> much lower levels of (SiO,), and <strong>for</strong> such waters its presence is not as<br />

adverse. Because high levels of product water recovery are essential to m<strong>in</strong>imize br<strong>in</strong>e disposal. most<br />

probably via <strong>in</strong>jection wells. <strong>the</strong> impact of (SiD,) <strong>in</strong> most of <strong>the</strong> ground waters under consideration is to<br />

give a substantial comparative advantage to EDR.<br />

3. The presence of calcium and bicarbonate <strong>in</strong> each "Group" of water at <strong>the</strong> "mean levels" <strong>in</strong>dicated <strong>in</strong> <strong>the</strong><br />

analyses can, to some extent, negatively impact both <strong>the</strong> RO and EDR processes. For RQ, <strong>the</strong> presence<br />

of such levels of <strong>the</strong>se constituents requires <strong>the</strong> feed<strong>in</strong>g of sulfuric acid to <strong>the</strong> feedwater <strong>in</strong> order to<br />

control <strong>the</strong> level of CaCo, scal<strong>in</strong>g <strong>in</strong> <strong>the</strong> RO br<strong>in</strong>e. In <strong>the</strong> case of Elm, with such levels of <strong>the</strong>se<br />

constituents <strong>in</strong> <strong>the</strong> feedwater, <strong>the</strong>ir impact is to necessitate an <strong>in</strong>crease <strong>in</strong> electrical power <strong>in</strong> order to<br />

ma<strong>in</strong>ta<strong>in</strong> higher water recovery levels.<br />

In summ3Q', both Alternatives A and B should be elim<strong>in</strong>ated from fur<strong>the</strong>r consideration on <strong>the</strong> grounds of technie.<br />

feasibility, whereas Alternative C and D, namely EDR and RO, should be carried <strong>for</strong>ward to Step 2. As regards rank,<br />

EDR appears to have an advantage over RO, primarily because of <strong>the</strong> impact of Si0 2 •<br />

Energy Forms<br />

At <strong>the</strong> outset it should be noted that both <strong>the</strong> EDR and RQ processes use electrical power as <strong>the</strong>ir energy source.<br />

Accord<strong>in</strong>gly, <strong>in</strong> evaluat<strong>in</strong>g <strong>the</strong> comparative technical feasibility associated with <strong>the</strong> three energy <strong>for</strong>ms, namely E(B),<br />

E(G), and E(P), <strong>the</strong> two important criteria are (a) <strong>the</strong> magnitude of <strong>the</strong> source of energy <strong>in</strong>sofar as its ability to power<br />

a sizable EDR or RQ plant and (b) <strong>the</strong> state of <strong>the</strong> technology associated with <strong>the</strong> trans<strong>for</strong>mation of each energy <strong>for</strong>m<br />

<strong>in</strong>to electrical power utiliz<strong>in</strong>g commercially available equipment. As regards <strong>the</strong> magnitude of <strong>the</strong> sources, this<br />

<strong>in</strong><strong>for</strong>mation is presented earlier <strong>in</strong> <strong>the</strong> Section under <strong>the</strong> head<strong>in</strong>g Order-of-Magnitude Projected Quantity Ranges, and <strong>the</strong><br />

evaluation <strong>for</strong> each <strong>for</strong>m is presented as follows:<br />

lliID - Based on <strong>the</strong> above mentioned projections, <strong>the</strong> quantities available from lliID are more than adequate,<br />

although higher temperatures would be more desirable. As regards <strong>the</strong> status of <strong>the</strong> technology, our one<br />

source of available literature(l) suggests that both <strong>the</strong> Kal<strong>in</strong>a Cycle System 12 and <strong>the</strong> Cascade Rank<strong>in</strong>e<br />

Cycle may be on <strong>the</strong> verge of commercial utilization <strong>for</strong> geo<strong>the</strong>rmal power generation, but that <strong>the</strong>re are<br />

still some unknowns.<br />

E.(Q) - Aga<strong>in</strong>, based on <strong>the</strong> above mentioned projections, <strong>the</strong> quantities of entra<strong>in</strong>ed natural gas are more than<br />

adequate. As regards <strong>the</strong> state of <strong>the</strong> technology, <strong>the</strong> use of gas turb<strong>in</strong>e generators such as those built<br />

by Stewart & Stevenson is very well established to provide an efficient conversion to electrical power.

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