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

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2.2 The gas can be burned <strong>in</strong> a gas eng<strong>in</strong>e to produce<br />

electric power.<br />

3. The geopressured hot water is used <strong>in</strong> a b<strong>in</strong>ary module to<br />

produce electric power.<br />

The ma<strong>in</strong> components of <strong>the</strong> b<strong>in</strong>ary module are shown <strong>in</strong> Figure<br />

2. It consists of heat exchangers which transfer heat energy from<br />

<strong>the</strong> geo<strong>the</strong>rmal water to <strong>the</strong> work<strong>in</strong>g fluid. The heat supplied is<br />

sufficient to completely vaporize <strong>the</strong> work<strong>in</strong>g fluid at a relative<br />

high pressure. The vaporized work<strong>in</strong>g fluid is expanded through a<br />

turb<strong>in</strong>e where shaft power is produced to drive a generator. The<br />

work<strong>in</strong>g fluid <strong>the</strong>n flows to <strong>the</strong> condenser where heat is rejected to<br />

a heat s<strong>in</strong>k (such as <strong>the</strong> evaporation of water or ambient air). The<br />

liquid work<strong>in</strong>g fluid fr~m <strong>the</strong> condenser is pumped back to <strong>the</strong> heat<br />

exchanger, thus complet<strong>in</strong>g <strong>the</strong> cycle. The design of <strong>the</strong> b<strong>in</strong>ary<br />

module, <strong>in</strong>clud<strong>in</strong>g <strong>the</strong> selection of <strong>the</strong> work<strong>in</strong>g fluid, is tailored<br />

to match <strong>the</strong> resource temperature to provide <strong>the</strong> maximum<br />

utilization <strong>for</strong> that resource. The equipment layout <strong>for</strong> a b<strong>in</strong>ary<br />

module is shown <strong>in</strong> Figure 3.<br />

The characteristics <strong>for</strong> a representative geopressured<br />

resource are shown at <strong>the</strong> top of Table 1 along with <strong>the</strong> assumed<br />

sales rate <strong>for</strong> gas and electric power. Follow<strong>in</strong>g this are <strong>the</strong><br />

estimated costs <strong>for</strong> <strong>the</strong> equipment as outl<strong>in</strong>ed previously and <strong>the</strong><br />

revenue produced by.<strong>the</strong> different energy sources. option I is <strong>for</strong><br />

a plant <strong>in</strong> which <strong>the</strong> gas is sold directly. option II is <strong>for</strong> a<br />

plant <strong>in</strong> which <strong>the</strong> gas is burned to produce electricity. It should<br />

be noted that <strong>the</strong> b<strong>in</strong>ary module <strong>in</strong> Option II is larger than Option<br />

I. This is because <strong>the</strong> b<strong>in</strong>ary module <strong>in</strong> Option II uses some of <strong>the</strong><br />

waste heat from <strong>the</strong> gas eng<strong>in</strong>e <strong>in</strong> addition to that from <strong>the</strong><br />

geofluid.<br />

The results of this simplified model <strong>in</strong>dicate that while <strong>the</strong><br />

cost of option II (convert<strong>in</strong>g <strong>the</strong> gas to electricity) is higher<br />

than Option I, <strong>the</strong> <strong>in</strong>creased revenue has actually improved <strong>the</strong> rate<br />

of return. A detailed economic analysis with actual sales rates<br />

and costs are based on actual resource characteristics should be<br />

per<strong>for</strong>med be<strong>for</strong>e <strong>the</strong> f<strong>in</strong>al option is selected. This model<br />

<strong>in</strong>dicates that <strong>the</strong>re may be options that are superior to <strong>the</strong> direct<br />

sale of <strong>the</strong> gas.<br />

. ~<br />

.<br />

78

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