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- W2371242951 abstract "A simulation model of flash separation unit is established using ChemCAD.Eight thermodynamic methods available in ChemCAD are investigated.The results indicate that API-SRK,SRK and Peng-Robinson are more suitable for calculating hydrogen solubility in hydrocarbons.Using m-xylene and hydrogen as feed stream components,the effect of feed flow ratio on the content of hydrogen in the product streams is studied.The results show that flash balance calculation can be achieved when the flow ratio is between 2/1 and 2664/1.Flash separator model is built to calculate solubility of hydrogen in hydrocarbons,m-xylene,cyclohexane,benzene,and benzene+cyclohexane with the flash separation temperature at 305.15 K,353 K,393 K and 433 K,respectively,and the pressure range from 8 to 5 MPa.The hydrogen solubility increases linearly with the pressure and the temperature.Simulation results are in good agreement with experimental results.Based on the results of this research,ChemCAD flash separator model can be more accurately calculate hydrogen solubility in hydrocarbons when thermodynamic methods and feed flow ratio are chosen correctly." @default.
- W2371242951 created "2016-06-24" @default.
- W2371242951 creator A5080129546 @default.
- W2371242951 date "2013-01-01" @default.
- W2371242951 modified "2023-09-24" @default.
- W2371242951 title "Calculation of hydrogen solubility in hydrocarbons by ChemCAD" @default.
- W2371242951 hasPublicationYear "2013" @default.
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