Eakapong
Materials
- Apr 24, 2011
- 3
Hi,
I am finding the calculation method for the maximum leak rate of a gas/liquid mixture through clearance between tube and tubesheet of an air-finned cooler. The fluid contains 79% H2 gas, 19% liquid hydrocarbon, and 2% liquid water at 181 barg and 168 degC. There is a 0.15 mm clearance between tube (25.4 mm OD) and its bore (25.7 mm OD). Fluid would leak through this clearance to the atmospheric.
I tried the orifice flow equation (Q = C*A*sqrt(2*(P1-P2)/Density)). As the clearance is very small comparing with the upstream area (header box), C=0.6 was assumed). By substitute P1=18.1 MPa and P2=0 MPa with average density of fluid at 42.8 kg/m3, I got flow rate 0.00664 m3/sec (6.6 litre/sec). This flow rate means the fluid is leaking at velocity of 551 m/s!!! This is unbelievable and I believe I did something wrong. Can anyone suggest please?
Thank you so much.
I am finding the calculation method for the maximum leak rate of a gas/liquid mixture through clearance between tube and tubesheet of an air-finned cooler. The fluid contains 79% H2 gas, 19% liquid hydrocarbon, and 2% liquid water at 181 barg and 168 degC. There is a 0.15 mm clearance between tube (25.4 mm OD) and its bore (25.7 mm OD). Fluid would leak through this clearance to the atmospheric.
I tried the orifice flow equation (Q = C*A*sqrt(2*(P1-P2)/Density)). As the clearance is very small comparing with the upstream area (header box), C=0.6 was assumed). By substitute P1=18.1 MPa and P2=0 MPa with average density of fluid at 42.8 kg/m3, I got flow rate 0.00664 m3/sec (6.6 litre/sec). This flow rate means the fluid is leaking at velocity of 551 m/s!!! This is unbelievable and I believe I did something wrong. Can anyone suggest please?
Thank you so much.