The issue of water vapor content in saturated gas
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What are the reasons why the saturation water vapor content in the crude gas as specified in the process package is much higher than the value calculated based on the saturated vapor pressure of water?
Is it related to temperature and partial pressure?
The question is whether saturated crude gas contains other components, whereas the process package only lists gas and water as the main components.
Are it the other components in crude gas that reduce the vapor pressure of water?
For a saturated gas, simply dividing the found saturated vapor pressure by the total pressure gives the vapor partial pressure! What other factors need to be taken into account here?
There are no factors to consider anymore,,,
Is the compressibility factor of the gas having a significant impact? How to correct it?