Dh = u2/(2g)
DP(V) + Du2/(2g) + DZ + E = 0
where :
DP(V) + Du2/(2g) + DZ + E = 0
Dh | = | Head loss in feet of flowing fluid |
u | = | Velocity in ft/sec |
g | = | 32.2 ft/sec2 | P | = | Pressure, lb/ft2 | V | = | Specific volume, ft3/lb | Z | = | Elevation, feet | E | = | Head loss due to friction in feet of flowing fluid |
- Sizing the holes in a sparger
- Calculating leakage through a small hole
- Sizing a restriction orifice
- Calculating the flow with a pitot tube
- Orifice calculations
- Relating fitting losses, etc.
For compressible fluids one must be careful that when sonic or “choking” velocity is reached, further decreases in downstream pressure do not produce additional flow. This occurs at an upstream to downstream absolute pressure ratio of about 2 : 1. Critical flow due to sonic velocity has practically no application to liquids. The speed of sound in liquids is very high.
Still more mileage can be gotten out of Dh = u2/2g when using it with Equation 2, which is the famous Bernoulli equation. The terms are
- The PV change
- The kinetic energy change or “velocity head”
- The elevation change
- The friction loss
These contribute to the flowing head loss in a pipe. However, there are many situations where by chance, or on purpose, u2/2g head is converted to PV or vice versa.
We purposely change u2/2g to PV gradually in the following situations:
- Entering phase separator drums to cut down turbulence and promote separation
- Entering vacuum condensers to cut down pressure drop
Source :
Branan, C. R. The Process Engineer’s Pocket Handbook, Vol. 1, Gulf Publishing Co., Houston, Texas, p. 1, 1976.
Branan, C. R. The Process Engineer’s Pocket Handbook, Vol. 1, Gulf Publishing Co., Houston, Texas, p. 1, 1976.
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