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Thread: natural gas, water dew point with Prode, best model ?

  1. #1

    natural gas, water dew point with Prode, best model ?

    Prode Properties includes several thermodynamic models which allow to calculate water phase condensation in natural gas,
    I have found that Soave Redlich Kwong or Peng Robinson with temperature dependent BIPs gives accurate results for water + HC,
    however Prode includes also ISO 18453 (specific for natural gas + water), GERG 2008, Peng Robinson with cpomplex mixing rules such as Wong Sandler, CPA two versions including association etc. etc.
    which is the best option ?

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  3. #2

    Re: natural gas, water dew point with Prode, best model ?

    For natural gas Peng Robinson with temperature dependent parameters is accurate,
    if your mixture includes polar non-hydrocarbons alternatives could be CPA or a EOS
    based on complex rules,
    for best accuracy consider data regression utility !
    Prode Properties includes many thermodynamic models
    which allow to solve multi phase vapor-liquid-solid equilibria,
    it is difficult to suggest a model without knowing exact composition.

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