ahog
- 4
- 1
Hi all,
I'm calculating the temperature drop of a gas during a throttling process. When using ideal gas theory, of course throttling is an isothermal process. Now i want to consider a real gas.
My problem: I have a gas, for example containing N2, O2 and H2O in the gaseous phase at a certain temperature and pressure. When considering pure components at system temperature and pressure, N2 and O2 are gaseous and H2O is liquid. In reality, the H2O partial pressure is below the saturation pressure, so H2O is also gaseous. Now I'm using partial pressures for enthalpy calculation of the mixture.
My question: Is it the right approach? Do I always have to use partial pressures, even when considering nearly ideal gases like N2 and O2, because they do show very small deviations from ideal gas law?
Thanks in advance.
I'm calculating the temperature drop of a gas during a throttling process. When using ideal gas theory, of course throttling is an isothermal process. Now i want to consider a real gas.
My problem: I have a gas, for example containing N2, O2 and H2O in the gaseous phase at a certain temperature and pressure. When considering pure components at system temperature and pressure, N2 and O2 are gaseous and H2O is liquid. In reality, the H2O partial pressure is below the saturation pressure, so H2O is also gaseous. Now I'm using partial pressures for enthalpy calculation of the mixture.
My question: Is it the right approach? Do I always have to use partial pressures, even when considering nearly ideal gases like N2 and O2, because they do show very small deviations from ideal gas law?
Thanks in advance.
Last edited by a moderator: