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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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A review of <strong>the</strong> data <strong>for</strong> <strong>the</strong> wellhead stream immediately f<strong>in</strong>ds several problems <strong>in</strong> <strong>the</strong><br />

<strong>for</strong>m of scale <strong>for</strong>m<strong>in</strong>g salts. The Langelier Index f<strong>in</strong>ds that <strong>for</strong> all conditions <strong>in</strong> excess<br />

of pH 7.0, scale will <strong>for</strong>m. The elevated total dissolved solids level of this stream<br />

(> 9,800 mgtl TDS) <strong>in</strong>dicates <strong>the</strong> Stiff-Davis Index should perhaps apply. A review of<br />

<strong>the</strong> Stiff-Davis plot <strong>for</strong> <strong>the</strong>se conditions f<strong>in</strong>ds significant scale <strong>for</strong>mation at pH greater<br />

than 7.0 and at temperatures less than 233 0 F.<br />

A review of <strong>the</strong> plots <strong>for</strong> several constituents f<strong>in</strong>ds immediate problems <strong>in</strong> scale<br />

<strong>for</strong>mation with Silica at all pH conditions at temperatures less than 183 0 F, Aragonite<br />

at all temperatures at pH conditions greater than 7.0, Barite under 183 0 F, Calcite at<br />

all temperatures at pH greater than 7.0, Siderite at all conditions, and Strontianite at<br />

all temperatures at pH greater than 7.5.<br />

In summary, <strong>the</strong> scal<strong>in</strong>g potential of <strong>the</strong> feed water source precludes <strong>the</strong> implementation<br />

of a multi-effect desal<strong>in</strong>ation process without significant additional process<br />

control systems <strong>for</strong> pH and temperature management.<br />

In an ef<strong>for</strong>t to fur<strong>the</strong>r understand <strong>the</strong> per<strong>for</strong>mance of <strong>the</strong> <strong>GP</strong>t<strong>GT</strong> feed waters under <strong>the</strong><br />

McAllen Ranch operational conditions, a second run was made at 75% water recovery,<br />

a concentration factor of 4.0.<br />

A review of <strong>the</strong> data <strong>for</strong> <strong>the</strong> 75% recovery stream aga<strong>in</strong> immediately f<strong>in</strong>ds several<br />

problems <strong>in</strong> <strong>the</strong> <strong>for</strong>m of scale <strong>for</strong>m<strong>in</strong>g salts. The Langelier Index f<strong>in</strong>ds that <strong>for</strong> all<br />

conditions <strong>in</strong> excess of pH 6.33, scale will <strong>for</strong>m. The elevated total dissolved solids<br />

level of this stream (> 36,500 mg/l TDS) <strong>in</strong>dicates <strong>the</strong> Stiff-Davis Index should perhaps<br />

apply. A review of <strong>the</strong> Stiff-Davis plot <strong>for</strong> <strong>the</strong>se conditions f<strong>in</strong>ds significant scale<br />

<strong>for</strong>mation at all pH greater than 6.0 and at all temperatures less than 250 0 F.<br />

A review of <strong>the</strong> plots <strong>for</strong> several constituents f<strong>in</strong>ds immediate problems <strong>in</strong> scale<br />

<strong>for</strong>mation with Silica at all pH conditions at all temperatures less than 233 0 F,<br />

Amorphous Iron Hydroxide at all temperatures when <strong>the</strong> pH is greater than 6.5.<br />

Anhydrite under all conditions, Aragonite at all temperatures at all pH conditions<br />

greater than 5.5, Barite under 217 0<br />

F, Calcite at all temperatures at all pH levels<br />

greater than 6.0, Siderite at all conditions, and Strontianite at all conditions.<br />

In summary, <strong>the</strong> scal<strong>in</strong>g potential of <strong>the</strong> br<strong>in</strong>e reject stream will result <strong>in</strong> significant<br />

scale <strong>for</strong>mation and deposition with<strong>in</strong> <strong>the</strong> system, with what appears to be significant<br />

deposition (as noted <strong>in</strong> <strong>the</strong> Momentary Excess plots) <strong>in</strong> effects after Effect No.6.<br />

Even with <strong>the</strong> addition of significant additional process control systems <strong>for</strong> pH and<br />

temperature management, <strong>the</strong> implementation of <strong>the</strong> multi-effect distillation system on<br />

<strong>the</strong> <strong>GP</strong>t<strong>GT</strong> feedwaters <strong>in</strong> technically unfeasible at this time.<br />

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