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- W2355626352 abstract "High pressure vapor-liquid phase equilibrium data of 2-butanol in CO2 from 323. 2 K to 353. 2 K were measured by constant-volume visual method. The phase equilibrium model was established by Peng-Robinson equation of state together with van der Waals-2 mixing rule. The solubility equation was correlated by Chrastil semi-empirical equation. Model parameters were calculated by least-squares optimization procedure. The solubility equation obtained was c = ρ3.3617 ·exp( 2198. 8193 /T + 6. 5545) ,and the solubility heat of the system was 18. 2809 kJ/mol." @default.
- W2355626352 created "2016-06-24" @default.
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- W2355626352 date "2010-01-01" @default.
- W2355626352 modified "2023-09-25" @default.
- W2355626352 title "High Pressure Phase Equilibrium Model of 2-Butanol in CO_2" @default.
- W2355626352 hasPublicationYear "2010" @default.
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