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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
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<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
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