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Cooling tower packing efficiency

This paper points out important criteria for an efficient mass transfer packing. Also described is a new PVC packing for use in water/air or water/gas applications such as cooling towers. 4 refs, cited. [Pg.296]

A nuclear power plant produces 1000 MW of electricity with a power cycle thermodynamic efficiency of 30%. The heat rejected is removed by cooling water that enters the condenser at 293 K and is heated to 313 K. The hot water flows to two identical natural-draft cooling towers, where it is recooled to 293 K, and makeup water is added as necessary. The available air is at 298 K with a wet-bulb temperature of 285 K, and it will flow at a rate 1.2 times the minimum. Specialized packing will be used for which Kya is expected to be 1.0 kg/m3-s if the liquid mass velocity is at least 3.4 kg/m2-s and the gas mass velocity is at least 2.75 kg/m2-s. Compute the dimensions of the packed sections of the cooling towers and the makeup water requirement due to evaporation. [Pg.502]

In addition, these depths apply to packed beds with uniform liquid and gas distribution similar to that used in distillation columns. In many designs of commercial cooling towers, distribution is of a substantially lower quality. Thus, the packed depth specified must make allowance for these less efficient distributor designs. For large size dumped tower packings, the value of Hqg inay be 25% to 40% greater than that from Table 6-1 when commercial liquid distributors are used. [Pg.155]

Mass transfer of the ozone gas stream to the cooling-tower water is usually accomphshed through a venturi in a recirculation line connected to the sump of the cooling tower, where the temperature of the water is the lowest. Since the solubility of ozone is very temperature-dependent, the point of lowest temperature allows the maximum amount of ozone to be introduced in solution to the tower. Mass-transfer equipment can take other forms column-bubble diffiisers, positive-pressure injection (U-tube), turbine mixer tank, and packed tower. The coimtercurrent column-bubble contactor is the most efficient and cost-effective but is not always useful in a cooling-tower setting because of space constraints. ... [Pg.215]


See other pages where Cooling tower packing efficiency is mentioned: [Pg.270]    [Pg.221]    [Pg.526]    [Pg.280]    [Pg.403]    [Pg.463]    [Pg.327]    [Pg.245]    [Pg.280]    [Pg.280]    [Pg.280]    [Pg.227]    [Pg.463]    [Pg.155]    [Pg.156]    [Pg.273]    [Pg.433]    [Pg.312]    [Pg.313]    [Pg.115]    [Pg.231]    [Pg.192]    [Pg.16]    [Pg.91]    [Pg.273]    [Pg.1177]    [Pg.1208]    [Pg.231]    [Pg.296]    [Pg.225]    [Pg.231]    [Pg.231]    [Pg.1569]    [Pg.1644]    [Pg.211]    [Pg.288]    [Pg.174]    [Pg.1565]    [Pg.1640]    [Pg.133]    [Pg.436]    [Pg.473]   
See also in sourсe #XX -- [ Pg.406 ]

See also in sourсe #XX -- [ Pg.406 ]




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