Problem 1.. tank at 101,325 Pa pressure to a distillation tower. The inner diameter of the pipe is 0.0243 m. The density of the feed is 749.7 kg/m and its vapor pressure is 68947.3 Pa. The friction loss in the suction line is 1.219 m. The net positiv "ction head required is 0.9 m. A feed rate of 0.0004246 m³/s of a hydrocarbon mixture at 70°C is being pumped from a , (a) Calculate the available net positive suction head if the pump is located 3.0 m above the liquid level. Will cavitation occur?

Refrigeration and Air Conditioning Technology (MindTap Course List)
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Author:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson
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Chapter40: Typical Operating Conditions
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Problem 1.
tank at 101,325 Pa pressure to a distillation tower. The inner diameter of the pipe is 0.0243 m. The density of the
feed is 749.7 kg/m² and its vapor pressure is 68947.3 Pa. The friction loss in the suction line is 1.219 m. The net
positiv ction head required is 0.9 m.
A feed rate of 0.0004246 m³/s of a hydrocarbon mixture at 70°C is being pumped from a
(a) Calculate the available net positive suction head if the pump is located 3.0 m above the
liquid level. Will cavitation occur?
, (b) Calculate if the pump will be able to provide sufficient NPSH to prevent cavitation if
Z1=0?
Transcribed Image Text:Problem 1. tank at 101,325 Pa pressure to a distillation tower. The inner diameter of the pipe is 0.0243 m. The density of the feed is 749.7 kg/m² and its vapor pressure is 68947.3 Pa. The friction loss in the suction line is 1.219 m. The net positiv ction head required is 0.9 m. A feed rate of 0.0004246 m³/s of a hydrocarbon mixture at 70°C is being pumped from a (a) Calculate the available net positive suction head if the pump is located 3.0 m above the liquid level. Will cavitation occur? , (b) Calculate if the pump will be able to provide sufficient NPSH to prevent cavitation if Z1=0?
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