2. Consider the following piping system, which has a mass flowrate of 12 kg/s: Liquid level 4.1 m Open to Atmosphere Duction=4.026-inch edischarge 555J/kg Discharge 3.068-inch 1.2 m Pressure in Vessel = 3.4 bar = 3.4×10³ Pa 5.8 m Liquid level 2.9m

Structural Analysis
6th Edition
ISBN:9781337630931
Author:KASSIMALI, Aslam.
Publisher:KASSIMALI, Aslam.
Chapter2: Loads On Structures
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Solve last three parts where density of fluid is 900kg/m3

2. Consider the following piping system, which has a mass flowrate of 12 kg/s:
Liquid level
4.1 m
Open to Atmosphere
Storage Tank
Disuction=4.026-inch
Pump
0.6 m
e suction 65J/kg
e discharge 555 J/kg
Discharge 3.068-inch
1.2 m
Determine the velocity in the discharge side.
e. Determine the velocity on the suction side.
f.
Determine the pressure at Point 3 (the inlet to the pump).
Pressure in Vessel = 3.4 bar = 3.4×105 Pa
5.8 m
g. Determine the work required for the pump (which is 65% efficient).
h. Determine the pressure at Point 4 (the discharge of the pump).
Liquid level
2.9 m
Process Vessel
Transcribed Image Text:2. Consider the following piping system, which has a mass flowrate of 12 kg/s: Liquid level 4.1 m Open to Atmosphere Storage Tank Disuction=4.026-inch Pump 0.6 m e suction 65J/kg e discharge 555 J/kg Discharge 3.068-inch 1.2 m Determine the velocity in the discharge side. e. Determine the velocity on the suction side. f. Determine the pressure at Point 3 (the inlet to the pump). Pressure in Vessel = 3.4 bar = 3.4×105 Pa 5.8 m g. Determine the work required for the pump (which is 65% efficient). h. Determine the pressure at Point 4 (the discharge of the pump). Liquid level 2.9 m Process Vessel
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