DPF = W1.8µ0.2/20.000d4.8r
where:
| DPF | = | Frictional pressure loss, psi/lOO equivalent ft of Pipe |
| W | = | Flow rate, lb/hr |
| µ | = | Viscosity, cp |
| r | = | Density, lb/ft³ |
| d | = | Internal pipe diameter, in. |
This relationship holds for a Reynolds number range of 2,100 to 106. For smooth tubes (assumed for heat exchanger tubeside pressure drop calculations), a constant of 23,000 should be used instead of 20,000.
Source :
Branan, Carl R. "Estimating Pressure Drop," Clzenzicnl
Engineel-irzg, August 28. 1978.

1 comment:
would you have any idea if this correlation is applicable to gas flow?
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