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• W4382791455 endingPage "1349" @default.
• W4382791455 startingPage "1341" @default.
• W4382791455 abstract "The removal of acid gas impurities from synthesis gas or natural gas can be achieved using several physical solvents. Examples of solvents applied on a commercial scale include methanol (Rectisol), poly(ethylene glycol) dimethyl ethers (Selexol), n-methyl-2-pyrrolidone (Purisol), and propylene carbonate (Fluor solvent). Continuous Fractional Component Monte Carlo (CFCMC) simulations in the osmotic ensemble were used to compute the Henry coefficients of the pure gases CO2, CH4, C2H6, CO, H2, N2, N2O, and H2S in the aforementioned solvents. The predicted Henry coefficients are in good agreement with the experimental results. The Monte Carlo method correctly predicts the gas solubility trend in these physical solvents, which obeys the following order: H2S > CO2 > C2H6 > CH4 > CO > N2 > H2. The gas separation selectivities for the precombustion process and the natural gas sweetening process are calculated from the pure gas Henry coefficients. The CO2/N2O analogy is verified for the solubility in these solvents." @default.
• W4382791455 created "2023-07-02" @default.
• W4382791455 creator A5039294022 @default.
• W4382791455 creator A5072421815 @default.
• W4382791455 creator A5091298778 @default.
• W4382791455 date "2023-06-30" @default.
• W4382791455 modified "2023-09-26" @default.
• W4382791455 title "Solubilities of CO₂, CH₄, C₂H₆, CO, H₂, N₂, N₂O, and H₂S in commercial physical solvents from Monte Carlo simulations" @default.
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• W4382791455 doi "https://doi.org/10.1080/08927022.2023.2228918" @default.
• W4382791455 hasPublicationYear "2023" @default.

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