Phase equilibrium properties of binary and ternary systems containing di-isopropyl ether + 1-butanol + benzene at 313.15 K |
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| Institution: | 1. Department of Microbiology and Immunology, University of Texas Medical Branch, Galveston, TX, USA;2. World Reference Center for Emerging Viruses and Arboviruses, University of Texas Medical Branch, Galveston, TX, USA;3. Rochal Industries LLC, San Antonio, TX, USA;4. Institute for Human Infections and Immunity, University of Texas Medical Branch, Galveston, TX, USA |
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| Abstract: | (Vapour + liquid) equilibria data of (di-isopropyl ether + 1-butanol + benzene), (di-isopropyl ether + 1-butanol) and (1-butanol + benzene) have been measured at T = 313.15 K using an isothermal total pressure cell. Data reduction by Barker’s method provides correlations for the excess molar Gibbs energy using the Margules equation for the binary systems and the Wohl expansion for the ternary. The Wilson, NRTL and UNIQUAC models have been applied successfully to both the binary and the ternary systems reported here. |
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