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Environmental Problems Associated With The Use of Cooling Towers DAVID L. BRENCHLEY, Assistant Professor School of Civil Engineering Purdue University West Lafayette, Indiana PETER R. WESTLIN, Engineer Environmental Protection Agency Research Triangle Park, North Carolina INTRODUCTION The demand for energy continues to grow; at present the need for electrical energy is doubling every seven years. This increase is due both to the population growth and the per capita increase in consumption. This energy need must be produced by some sort of thermodynamic process. Hence the second law of thermodynamics becomes of particular interest. This law essentially limits the efficiency of powerplants to about 30 or 40 percent and thereby necessitates rejection of 60 to 70 percent of the energy as low grade waste heat. The people using energy conversion processes are therefore faced with the dilemma of how and where to reject heat. They must maintain efficient design and yet still keep peace with the populace. In the past, lakes and rivers have served as intermediate sinks for this waste energy. The local result has been increased water temperatures often referred to as "thermal pollution" or "thermal enrichment", depending upon one's point of view. Eventually the water cools by transferring the energy to the atmosphere. Cooling ponds and cooling towers are used to enhance this energy transfer process to the atmosphere and thereby relieve the thermal stressing of local watercourses. Recent water quality standards (1) on water effluents allow a 5 F (2.8K) increase in open rivers and streams. The allowable increase for lakes is 3 F (1.7K). For estuaries and coastal waters a 1.5 F (0.8K) is allowed during the months of June, July and August, while a 4 F (2.2K) is permitted during the rest of the year. The maximum water temperature allowed in all cases is 90 F (306K). This type of regulation makes it extremely difficult to use the watercourses as heat sinks. Typically condensers for powerplant operations are designed on a 10 to 30 F (5.6 to 14.8 K) temperature rise. If the condensers were to be designed for the 1.5 to 3 F (0.8 to 1.7 K) allowable increase, the water pumping cost would be excessive. This obvious conflict thus explains the increased use of cooling ponds and cooling towers. The cooling ponds seem to find application only in certain circumstances because of the large land area requirements. Cooling towers are devices which transfer the waste energy directly to the atmosphere. The towers may be mechanical or natural draft and may be wet or dry. The most common types are natural and mechanical draft wet-type towers. In these devices the hot water comes in contact with the ambient air. The water is cooled by two mechanisms: 1) sensible heat exchange and 2) latent heat of evaporation. During summer operations the cooling is due almost totally to evaporation while under winter conditions, possibly one-third is due to sensible heat exchange. At larger power plant installations these cooling towers discharge thousands of gallons per minute of water to the atmosphere. Some of the water is in the form of "drift", but mist eliminators generally limit this to 0.1 percent of the water flow rate. A greater portion of the water leaves the tower as a vapor. The evaporative loss is on the order of 1 percent of the water flow rate for each 10 F(5.6K) cooling of the process water. Dry cooling towers rely completely on sensible heat exchange; the gas and liquid streams do not come into direct contact. Large quantities of air must be moved through the device in order to accomplish the necessary heat transfer. Like an automobile radiator, a 55
Object Description
Purdue Identification Number | ETRIWC197204 |
Title | Environmental problems associated with the use of cooling towers |
Author |
Brenchley, David L. Westlin, Peter R. |
Date of Original | 1972 |
Conference Title | Proceedings of the 27th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,20246 |
Extent of Original | p. 55-66 |
Series | Engineering extension series no. 141 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Date Digitized | 2009-06-08 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page0055 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | Environmental Problems Associated With The Use of Cooling Towers DAVID L. BRENCHLEY, Assistant Professor School of Civil Engineering Purdue University West Lafayette, Indiana PETER R. WESTLIN, Engineer Environmental Protection Agency Research Triangle Park, North Carolina INTRODUCTION The demand for energy continues to grow; at present the need for electrical energy is doubling every seven years. This increase is due both to the population growth and the per capita increase in consumption. This energy need must be produced by some sort of thermodynamic process. Hence the second law of thermodynamics becomes of particular interest. This law essentially limits the efficiency of powerplants to about 30 or 40 percent and thereby necessitates rejection of 60 to 70 percent of the energy as low grade waste heat. The people using energy conversion processes are therefore faced with the dilemma of how and where to reject heat. They must maintain efficient design and yet still keep peace with the populace. In the past, lakes and rivers have served as intermediate sinks for this waste energy. The local result has been increased water temperatures often referred to as "thermal pollution" or "thermal enrichment", depending upon one's point of view. Eventually the water cools by transferring the energy to the atmosphere. Cooling ponds and cooling towers are used to enhance this energy transfer process to the atmosphere and thereby relieve the thermal stressing of local watercourses. Recent water quality standards (1) on water effluents allow a 5 F (2.8K) increase in open rivers and streams. The allowable increase for lakes is 3 F (1.7K). For estuaries and coastal waters a 1.5 F (0.8K) is allowed during the months of June, July and August, while a 4 F (2.2K) is permitted during the rest of the year. The maximum water temperature allowed in all cases is 90 F (306K). This type of regulation makes it extremely difficult to use the watercourses as heat sinks. Typically condensers for powerplant operations are designed on a 10 to 30 F (5.6 to 14.8 K) temperature rise. If the condensers were to be designed for the 1.5 to 3 F (0.8 to 1.7 K) allowable increase, the water pumping cost would be excessive. This obvious conflict thus explains the increased use of cooling ponds and cooling towers. The cooling ponds seem to find application only in certain circumstances because of the large land area requirements. Cooling towers are devices which transfer the waste energy directly to the atmosphere. The towers may be mechanical or natural draft and may be wet or dry. The most common types are natural and mechanical draft wet-type towers. In these devices the hot water comes in contact with the ambient air. The water is cooled by two mechanisms: 1) sensible heat exchange and 2) latent heat of evaporation. During summer operations the cooling is due almost totally to evaporation while under winter conditions, possibly one-third is due to sensible heat exchange. At larger power plant installations these cooling towers discharge thousands of gallons per minute of water to the atmosphere. Some of the water is in the form of "drift", but mist eliminators generally limit this to 0.1 percent of the water flow rate. A greater portion of the water leaves the tower as a vapor. The evaporative loss is on the order of 1 percent of the water flow rate for each 10 F(5.6K) cooling of the process water. Dry cooling towers rely completely on sensible heat exchange; the gas and liquid streams do not come into direct contact. Large quantities of air must be moved through the device in order to accomplish the necessary heat transfer. Like an automobile radiator, a 55 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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