-
Calculate internal pipe diameter at floe temperature:
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Calculate correction factor for steam quality (For lliquid, water, and steam, Fs=1):
-
Calculate orifice diameter at flow temperature.
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For Venturi tubes and Nozzles:
-
For orifice plates:
-
-
Calculate b - ratio:
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Checking for Critical flow and some initial calculations.
Liquid /Water case
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Calculate downstream pressure:
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If the the flow is critical. If not then the floe is sub-critical.
-
For critical flow:
-
For sub-critical flow:
Classic Venturi tube:
-
-
-
Nozzles
-
Orifice plates:
-
Calculate first estimate for flow rate (W0 [kg/s]):
-
-
Gas/Steam case
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Calculate critical pressure ratio and define whether the flow is critical.
If the the flow is critical. If not the flow is sub-critical.
-
-
Initial calculation for critical flow.
-
Gas Expansion factor:
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First estimate for flow rate (W0 [1b/h], T[R], D[in], P1[psi-a])
-
-
Initial calculations for sub-critical flow.
Differential pressure to be used in flow rat calculation:
-
For classical Venturi tube:
-
For Nozzles:
-
For orifice plates:
-
-
Gas expansion factor:
-
For Venturi tubes and nozzles:
where
-
For orifice plates:
-
First estimate for flow rate (W0[kg/s]):
-
-
-
Calculate Reynolds number.
-
For gas/steam critical flow (Bore Reynolds number):
-
For liquid/water and gas/steam sub-critical flow (Pipe Reynolds number):
-
-
Calculate discharge coefficient. See Appendix.
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For orifices in the case of gas/steam sub-critical flow, calculate DP and gas expansion factor:
-
Calculate new flow rate:
-
For gas/steam at critical flow:
-
For other cases (W[kg/s]):
-
-
Repeat steps 6 to 10 until the relative change in the flow rate is less than 0.0001.