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Author Topic: Mass fluxes and partial pressures of NH3 and H2O vapour  (Read 1890 times)

djb14128

  • Frequent Contributor
  • Posts: 19
Mass fluxes and partial pressures of NH3 and H2O vapour
« on: 27/05/20 12:17 »
Hi,

I'm just wondering if there is a way for me to calculate the partial pressures and fluxes of NH3-N and H2O (water) vapour using IPHREEQC.

Kind regards,
djb14128
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dlparkhurst

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Re: Mass fluxes and partial pressures of NH3 and H2O vapour
« Reply #1 on: 27/05/20 17:01 »
The partial pressures of NH3(g) and H2O(g) will appear in the "Saturation  indices" section of the output. For a gas, SI = log10(fugacity). Fugacity = pressure * phi / 1 atm.  For ideal gases, phi = 1. At low pressures fugacity will essentially equal pressure, even in Peng-Robinson calculations.


Not sure what you are looking for with the fluxes. PHREEQC will calculate mole transfers of NH3 if you specify a partial pressure with EQUILIBRIUM_PHASES, or if you react a solution with a GAS_PHASE. You usually cannot specify a partial pressure of H2O(g) because it is fixed at a given temperature; you can define H2O(g) as a component in a GAS_PHASE.
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djb14128

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  • Posts: 19
Re: Mass fluxes and partial pressures of NH3 and H2O vapour
« Reply #2 on: 28/05/20 09:14 »
Quote from: dlparkhurst on 27/05/20 17:01
The partial pressures of NH3(g) and H2O(g) will appear in the "Saturation  indices" section of the output. For a gas, SI = log10(fugacity). Fugacity = pressure * phi / 1 atm.  For ideal gases, phi = 1. At low pressures fugacity will essentially equal pressure, even in Peng-Robinson calculations.


Not sure what you are looking for with the fluxes. PHREEQC will calculate mole transfers of NH3 if you specify a partial pressure with EQUILIBRIUM_PHASES, or if you react a solution with a GAS_PHASE. You usually cannot specify a partial pressure of H2O(g) because it is fixed at a given temperature; you can define H2O(g) as a component in a GAS_PHASE.

Thanks.
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