tc112
Mechanical
- Jun 13, 2006
- 6
I am trying to verify the actual volumetric flow rate in a test rig we have setup. The unit is a waste gas combustion device used to burn vapors from oil storage tank batteries. The test rig is flowing C3H6 (Propylene) at 10 oz/sq in, approx. 60 deg F, and at a rate that is supposed to be around 90 CFM. I originally purchased an expensive PD rotary gas flow meter that fit the application perfectly, except that I didn't yet understand that the definition of a standard cubic foot varies based on the gas composition. My meter was only setup for a range of SG from .55 to .87 (C3H6 SG=1.453) and is reading much lower that I had expected. I also tried to verify the flow rate using a thermal mass flow meter (hot wire anemometer), but come to find out it had been calibrated in air and the correction factor the manufacturer gave me adjusted the flow rate up by approx. 55%, this doesn't seem right to me. I have tried to correct the numbers I have for both the meter and the anemometer using the Ideal Gas Law without success. Should the molar flow rate be the same regardless of gas composition for the same P, V, and T? I have been using the universal gas constant for my molar flow rate calcs and corrected density calcs but should I be using the Individual gas constant instead?? From what I have done so far it looks like for a given temp and pressure, the cu ft/lbmol is the same for all gases??