CoolingTower.gif (471 × 303 pixels, file size: 4 KB, MIME type: image/gif)
Summary
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Diagram and model of a cooling tower system. Here are the governing relationships for the makeup flow rate, the evaporation and windage losses, the draw-off rate, and the concentration cycles in a wet cooling tower system: M = Make-up water in m3/hr A water balance around the entire system is: M = E + D + W Since the evaporated water (E) has no salts, a chloride balance around the system is: M (XM) = D (XC) + W (XC) = XC (D + W) and, therefore: XC / XM = Cycles = M / (D + W) = M / (M – E) = 1 + {E / (D + W)} From a simplified heat balance around the cooling tower: E = (C) (ΔT) (cp) / HV where: Windage losses (W), in the absence of manufacturer's data, may be assumed to be: W = 0.3 to 1.0 percent of C for a natural draft cooling tower
W = 0.1 to 0.3 percent of C for an induced draft cooling tower
W = about 0.01 percent of C if the cooling tower has windage drift eliminators Concentration cycles in petroleum refinery cooling towers usually range from 3 to 7. In some large power plants, the cooling tower concentration cycles may be much higher. (Note: Draw-off and blowdown are synonymous. Windage and drift are also synonymous.) |
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Own work I developed this image myself using the Paint program supplied with WindowsXP. |
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Date/Time | Thumbnail | Dimensions | User | Comment | |
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current | 17:25, 20 January 2006 | 471 × 303 (4 KB) | Mbeychok (talk | contribs) | I developed this image myself using the Paint program supplied with WindowsXP. |
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