misterd
Chemical
- Apr 9, 2001
- 34
We are trying to size a control valve to feed an heat exchanger. The inlet pressure is 100 psig for a flowrate estimated at 195 lb/hr. What is the rule or how can I figure the dP across the valve? From what I understand, the steam trap will keep the pressure in the heat exchanger. Should I size the control valve with a dP of 2 psig?
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