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

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

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EVALUATION OF AUTO DESALINATION<br />

As with all process feasibility evaluations, background <strong>in</strong><strong>for</strong>mation must be obta<strong>in</strong>ed<br />

which determ<strong>in</strong>es <strong>the</strong> feasibility of <strong>the</strong> various process units. In <strong>the</strong> case of <strong>the</strong> <strong>GP</strong>/<strong>GT</strong><br />

application, <strong>the</strong> follow<strong>in</strong>g wellhead <strong>in</strong><strong>for</strong>mation was provided by <strong>the</strong> Project Manager,<br />

based upon historical data from <strong>the</strong> McAllen Ranch wellfield:<br />

Wellhead Temperature: 265°F<br />

Entra<strong>in</strong>ed Gas 25 ftl/bbl<br />

Daily Feed 1.0 MGD<br />

Chemical Analysis see attached<br />

Br<strong>in</strong>e Disposal Via Injection Well (o<strong>the</strong>rs)<br />

M<strong>in</strong>imum System Recovery 75%<br />

Wellhead Pressure 1000 PSI<br />

• Produce <strong>Water</strong> Quality SDWA Standards<br />

Based upon <strong>the</strong> temperature, pressure, and entra<strong>in</strong>ed gas <strong>in</strong><strong>for</strong>mation, all membrane<br />

systems can be precluded from fur<strong>the</strong>r consideration without significant additional<br />

process equipment to cool and degas <strong>the</strong> streams. The elevated pressure can be<br />

reduced by <strong>the</strong> utilization of an energy recovery system to both recover <strong>the</strong> <strong>GP</strong> energy<br />

and depressurize <strong>the</strong> stream.<br />

Immediately after depressurization, a s<strong>in</strong>gle-staged flash unit without a condenser can<br />

be applied to remove <strong>the</strong> entra<strong>in</strong>ed (miscible and immiscible) gases from <strong>the</strong> stream.<br />

This energy source can be recovered or utilized <strong>for</strong> o<strong>the</strong>r energy production on-site.<br />

Based upon standard <strong>the</strong>rmodynamic design, <strong>the</strong> heat loss from wellhead,<br />

depressurization, through <strong>the</strong>se units is estimated to be 15-20°, result<strong>in</strong>g <strong>in</strong> a flow to<br />

<strong>the</strong> desal<strong>in</strong>ation system at a temperature of approximately 245-250 0.<br />

The basic concept of <strong>the</strong> autodesal<strong>in</strong>ation system has been to utilize <strong>the</strong> <strong>GT</strong> aspect of<br />

<strong>the</strong> flows. Instead of <strong>the</strong> usual system of heat sources and exchangers throughout <strong>the</strong><br />

process, <strong>the</strong> stream arrives at an elevated temperature, which <strong>the</strong>n provides <strong>the</strong><br />

<strong>the</strong>rmal energy to drive <strong>the</strong> multi-effect unit.<br />

Prior to <strong>the</strong> actual design of a multi-effect distillation system, attention must be made<br />

to <strong>the</strong> feedwater chemistry, <strong>the</strong> br<strong>in</strong>e chemistry, and <strong>the</strong> number of effects. The<br />

physical chemistry of <strong>the</strong> flows across <strong>the</strong> various effects determ<strong>in</strong>es <strong>the</strong> per<strong>for</strong>mance,<br />

scale deposition, and corrosivity of <strong>the</strong> system.<br />

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