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<br />oot'il <br /> <br />either a smaller scale or combined with one of the <br />other technologies. 9A~-lhFough cooling is a <br />technology with some favorable aspects (small <br />rates of evaporation, small capital cost, and small <br />plant-efficiency losses), as well as some un- <br />favorable aspects (damage to organisms from the <br />pumps and condensers and ecological changes due <br />to increased water temperatures). It is included in <br />this analysis to facilitate the comparison of a range <br />of development alternatives. In this manner, com- <br />binations of those options can be determined, <br />which would be a realistic compromise among <br />various economic, environmental, and social <br />objectives. <br />For the second analysis. the cooling mechanism <br />was assumed to he a cooling pond in the shape of a <br />long sinuous canal covering 4,230 acres (l.71O ha) <br />(fig. 3B). By simulation of the cooling process in <br />this pond, considering the range of conditions <br />prevailing in the Yampa River basin, the estimated <br />annual evaporation from the pond would be 4l,500 <br />acre-ft (51.2 million m3) (table 6). This evaporation <br />would be larger than for once-through cooling, <br />because this value includes both the natural and <br />the waste-heat-induced evaporation from the pond. <br />To compensate for the 41,500 acre-ft (51.2 mil- <br />lion m3) evaporative loss, a volume of water would <br />need to be withdrawn from the river. If the volume <br />of withdrawn water equaled the evaporation, then <br />the cooling water would accumulate dissolved <br />solids at a rate of 7,850 tons (7.120 t) per year. To <br />avoid this, an amount of water equal to 10 percent <br />of the evaporation rate would need to be constantly <br />removed from the cooling system and returned to <br />the river (this is called blowdown). Consequently, <br />the withdrawal rate would need to be 10 percent <br />greater than the evaporation rate. The annual <br />withdrawals would total 45, 700 acre-ft (56.3 million <br />m') and the dissolved-solids load of the river would <br />be unchanged due to this water use. The flow of the <br />Yampa River would be diminished by 3 percent, <br />and the dissolved-aolids concentration would in- <br />crease by 4 mg/L (table 6). <br />Compared with once-through cooling, the effects <br />on the river's biota using a cooling-pond system <br />would be very small. The withdrawal of water <br />would be 2 percent of that needed for once-through <br />cooling, and the blowdown would amount to 0.4 <br />percent of the total annual flow of the Yampa River <br />near Maybell. However, a pond system would af- <br />fect the terrestrial habitat by converting 4,230 <br />acres (1,710 ha) from land to water. It also would <br /> <br />have some effects on local climate, due to the vast <br />amount of heat and vapor transferred to the air <br />over this area. Once-through cooling, by com- <br />parison, would spread the effects over a stream <br />reach many miles in length. <br />A wet-cooling water tower rejects waste heat by <br />bringing the cooling water into contact with mov- <br />ing air as the water falls over baffles, causing it to <br />form small droplets. The water is taken from a col- <br />lecting basin at the base of the cooling tower, pas- <br />sed through the powerplant condenser, and <br />pumped to the top of the tower. As the water falls <br />through the tower, it moves past a large volume of <br />air driven either by fans or by natural buoyancy. <br />During this period of contact. some of the water <br />evaporates. In addition, the water is cooled by the <br />transfer of heat (conduction), The air leaving the <br />tower generally is saturated and is at a greater <br />temperature than it was when it entered the tower. <br />Because part of the water is evaporated as it <br />passes through the tower and a small amount <br />drifts out of the tower structure, water must con- <br />stantly be added to the system to keep the volume <br />of water in the system from decreasing. In addition, <br />some water must be added to prevent an excessive <br />increase of dissolved solids in the system (fig. 3C). <br />In a cooling tower, the fraction of waste heat that <br />is rejected by evaporation is an increasing function <br />of the ambient air temperature and a decreasing <br />function of the relative humidity and altitude. By <br />calculating the rate of evaporation for the range of <br />conditions typical of the Yamps River basin, the <br />annual rate of evaporation would be 40,400 acre-ft <br />(49.8 million m3) (table 6). This blowdown would <br />equal about 10 percent of the evaporation, so the <br />total rate of annual withdrawal from the river <br />would be 44,400 acre-ft (54.7 million m3). <br />Assuming an operating system with no direct <br />discharge of residuals to the river, the blowdown <br />(4,040 acre-ft or 5.0 million m3 per year) could be <br />used for transporting ash from the powerplant <br />boilers for discharge into a system of evaporation <br />ponds. For such a system, there is an unresolved <br />question as to the ultimate fate of the residue in the <br />evaporating ponds. Whether these residuals <br />(predominantly salts and sulfur compounds) can <br />be prevented from leaching back into the nearby <br />ground water or surface waters is unknown. An <br />ongoing study at the Hayden powerplant may <br />provide some site-specific information on the possi- <br />ble long-term effects of this form of disposal (S. R. <br />Ellis, written commun., 1978). <br /> <br />23 <br />