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<br />WATER-USE AND RESIDUALS <br />IMPLICA TIONS OF <br />COAL-CONVERSION AND <br />TRANSPORTATION ALTERNATIVES <br /> <br />By ROBERT M. HIRSCH <br /> <br />Each coal. use alternative has a set of implica. <br />tions regarding discharge of residuals into the en. <br />vironment and use of water (Gold and others, <br />1977). In this chapter, a comparative analysis is <br />made of alternative cooling systems in power- <br />plants. Then, assuming a fixed amount of coal <br />production, relative water-use implications are <br />compared in use of this coal for electric-power <br />generation, coal gasification, or a coal-slurry <br />pipeline. Finally, a comparison of total residuals <br />discharged as a result of the seven assumed coal. <br />development plans gives some insight into the pos- <br />sible environmental problems confronting resource <br />managers in the Yampa River basin. <br />A coal.burning powerplant generating electricity <br />must reject a vast amount of waste heat into the <br />environment. For every megawatt-hour (MWh) of <br />electricity produced, approximately 6.2 million <br />Btu (6.5 billion joules) of heat is produced. There <br />are five major methods available for dealing with <br />this residual. Four of these methoda-{)nce-through <br />cooling, cooling ponds, wet-cooling towers, and <br />dry-cooling towers-were investigated to determine <br />their implications for the use of water and energy as <br />well as for the residuals produced in the heat. <br />production process. A fifth method not examined <br />here is the beneficial use of waste heat. <br />The relative amounts of the heat load rejected by <br />each mechanism are dependent upon: (1) the type <br />of cooling device used; (2) climatic conditions <br />(temperature, humidity, and wind); (3) hydrologic <br />conditions (quantity and temperature of available <br />water); and (4) certain plant.operating conditions. <br />The first three of these methods rely, to varying <br />degrees, on evaporation as a cooling mechanism. <br />For each kilogram of water evaporated. a water <br />body loses 2,400 Btu (2.5 million joules) of heat. As <br />a consequence of this evaporation, there is not just <br />an addition of moisture to the atmosphere and loss <br />of surface water available for other uses, but there <br />also will be an increase in the concentration of dis- <br />solved and suspended solids in the remaining <br /> <br />,;~:t$ <br /> <br />, <br /> <br />water. Thus, the consequences of heat-rejection <br />methods involve changes in atmospheric condi. <br />tions, water availability, and water quality. <br />Schematics of the four cooling systems con- <br />sidered in this analysis are shown in figure 3. In the <br />comparative analysis, the results of which are sum. <br />marized in table 6, it was assumed that the cooling <br />systems would be installed at a complex of <br />powerplants using 12.5 million tons (11.3 million t) <br />of coal annually and that the total plant-generating <br />capacity would be about 4,000 MW, with operating <br />efficiency of 39 percent and a load factor of 83 per- <br />cent (I. C. James II, E. D. Attanasi, T. Maddock <br />III, S. H. Chiang, B. T. Bower, and N. C. Matalas, <br />written commun., 1978). <br />For once-through cooling, the annual flow <br />diverted from the river would average 3,580 ft'/s <br />(101 m'/s) or total 2.l5 million acre-ft (2.65 billion <br />m') (table 6). This water would be pumped from <br />the river, passed through the powerplant con- <br />densers where it would be heated, and then <br />returned to the river (fig. 3A). Because the three <br />physical mechanisms of heat loss (evaporation, <br />conduction, and long-wave radiation) proceed at <br />rates which are increasing functions of water <br />temperature. the river would begin to cool and <br />gradually return to its natural temperature. In the <br />reach of the river affected by this elevated <br />temperature, there would likely be changes in the <br />number and variety of aquatic species. <br />Because the evaporation rate of a free-water sur. <br />face is an increasing function of water temperature, <br />the evaporation rate for the river will be larger than <br />it would be if no waste heat had been discharged to <br />the river. The rate of water evaporation at- <br />tributable to the powerplant is this difference <br />between the actual rate and the natural rate of <br />evaporation, integrated over the surface area of the <br />river. The rate of water evaporation is an increasing <br />function of wind speed, natural water temperature, <br />and altitude. <br />By computing the rate of water evaporation for <br />the various climatic and hydrologic conditions as- <br />sumed to exist throughout the year. the annual <br />evaporation by a hypothetical 4.000-MW power- <br />plant located on the Yampa River would be 27.800 <br />acre-ft (34.3 million m3), or 1 percent of the annual <br />withdrawal rate (table 6). This would result in a <br />2,7-percent decrease in the mean annual flow of the <br /> <br />20 <br />