ctowles
Chemical
- Mar 31, 2006
- 1
I am working on a natural gas chilling application.
I’m calculating the head load (cooling load). We need to bring the natural gas from 70 F down to 28 F (at 750 psig). The natural gas is 12% CO2, 5% Ethane, 82% Methane, 1% other (mole%). Pure CO2 will condense from vapor to liquid during this temperature change at this pressure. This greatly impacts the heat load for the chiller. I’m wondering though, since the CO2 is mixed with Methane, and at a relatively high pressure where the gases are not ideal (compressibility, Z, for this mixture is .84) that the intermolecular forces/mixing properties may prevent the CO2 to condense.
What I really need is a CO2-Methane binary mixture vapor- liquid equilibrium chart. I haven’t been successful in finding that. I was wondering if someone could shed a little light on this subject. Thank you.
I’m calculating the head load (cooling load). We need to bring the natural gas from 70 F down to 28 F (at 750 psig). The natural gas is 12% CO2, 5% Ethane, 82% Methane, 1% other (mole%). Pure CO2 will condense from vapor to liquid during this temperature change at this pressure. This greatly impacts the heat load for the chiller. I’m wondering though, since the CO2 is mixed with Methane, and at a relatively high pressure where the gases are not ideal (compressibility, Z, for this mixture is .84) that the intermolecular forces/mixing properties may prevent the CO2 to condense.
What I really need is a CO2-Methane binary mixture vapor- liquid equilibrium chart. I haven’t been successful in finding that. I was wondering if someone could shed a little light on this subject. Thank you.