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Gas/steam at critical flow |
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Gas/steam at subcritical flow | ![]() |
Liquid | ![]() |
A0 | Minimum required flow cross sectional area | (mm²) |
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Qm | Mass Flow rate | (kg/h) |
C |
Function for isentropic exponent k
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V0 | Specific volume at practical release pressure and temperature | (m³/kg) |
P0 | Release pressure | (bar a) |
α | Release coefficient (In general, apply 0.62) | |
T0 | Release temperature | (K) |
Z0 | Compressibility coefficient at practical release pressure and temperature (If there is no available data, Z0=0.1) |
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M | Mol weight | kg/kmol |
x | Dryness of wet steam | |
Kb |
Viscosity correction factor related to Reynold's number(Re) If the liquid viscosity is less than that of water at 20°C, kv=1.0 (Refer to Fig 1. Capacity correction factor for viscosity) |
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Kv |
Correction factor for reduction in the theoretical capacity as increase of the back pressure in subcritical flow (Refer to table 2. Capacity correction factor for back pressure) |
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Re | Reynold's number
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μ | Viscosity of the liquid | |
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(bar a) |
Pb | Back pressure (pressure at outlet) | (psia) |
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