A coke packed humidifier is to be designed to cool 3,000 cfm of saturated air from 150 to 75 °F at barometric pressure. Cooling water at 50°F will be allowed to heat up to 100°F. Gas velocity will be 3,000 lb of dry air per sq ft of total cross section. Water velocity is 1,200 lb/h per sq ft of total cross section. Over-all coefficient of sensible heat transfer from air to water = 300 BTU/h ft³ °F. Calculate the height and diameter of cooling tower required. Round your answers to the nearest 0.05 ft.

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Chapter8: Natural Convection
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A coke packed humidifier is to be designed to cool 3,000 cfm of saturated air from 150 to 75 °F at
barometric pressure. Cooling water at 50°F will be allowed to heat up to 100°F. Gas velocity will
be 3,000 lb of dry air per sq ft of total cross section. Water velocity is 1,200 lb/h per sq ft of total
cross section. Over-all coefficient of sensible heat transfer from air to water = 300 BTU/h ft³.°F.
Calculate the height and diameter of cooling tower required. Round your answers to the nearest
0.05 ft.
Transcribed Image Text:A coke packed humidifier is to be designed to cool 3,000 cfm of saturated air from 150 to 75 °F at barometric pressure. Cooling water at 50°F will be allowed to heat up to 100°F. Gas velocity will be 3,000 lb of dry air per sq ft of total cross section. Water velocity is 1,200 lb/h per sq ft of total cross section. Over-all coefficient of sensible heat transfer from air to water = 300 BTU/h ft³.°F. Calculate the height and diameter of cooling tower required. Round your answers to the nearest 0.05 ft.
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