Refer to Figure P19.69. Answer the following questions. Explain each answer. At what flowrate is NPSHA =
Question:
Refer to Figure P19.69. Answer the following questions. Explain each answer.
At what flowrate is NPSHA = 3.2 m? Comment on the feasibility of operating at this flowrate.
At what flowrate does the pump produce 33.5 m of head? What is the system frictional loss at this flowrate? What is the pressure drop across the control valve at this flowrate?
At what flowrate does cavitation become a problem?
What is the maximum possible flowrate?
If the source and destination pressures are identical, what is the elevation difference between source and destination?
At a flowrate of 1 L/s, what is the system frictional head loss?
At a flowrate of 1 L/s, what head is developed by the pump?
At a flowrate of 1 L/s, what is the head loss across the control valve?
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