Equilibrium Constants for the Liquid-Phase Synthesis of Isopropyl tert-Butyl Ether from 2-Propanol and Isobutene

Equilibrium constants for the liquid-phase addition of 2-propanol to isobutene to give isopropyl tert-butyl ether (IPTBE) were determined experimentally in the temperature range 303−353 K and at 1.6 MPa. To reach etherification equilibrium, the macroporous sulfonic resin Bayer K-2631 was used as the...

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Published in:Industrial & engineering chemistry research Vol. 36; no. 3; pp. 896 - 902
Main Authors: Calderón, Adela, Tejero, Javier, Izquierdo, José Felipe, Iborra, Montserrat, Cunill, Fidel
Format: Journal Article
Language:English
Published: Washington, DC American Chemical Society 01-03-1997
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Summary:Equilibrium constants for the liquid-phase addition of 2-propanol to isobutene to give isopropyl tert-butyl ether (IPTBE) were determined experimentally in the temperature range 303−353 K and at 1.6 MPa. To reach etherification equilibrium, the macroporous sulfonic resin Bayer K-2631 was used as the catalyst. The UNIFAC estimates of activity coefficients were used to describe the liquid-phase nonideality. The thermodynamic equilibrium constants and the enthalpy, free energy, and entropy changes of the reaction were given as a function of temperature. At 298.15 K, the standard molar reaction enthalpy Δr H°m(298.15 K) is −(22.9 ± 1.3) kJ·mol-1, in agreement with literature data, and the standard molar reaction entropy Δr S°m(298.15 K) and free energy Δr G°m(298.15 K) are −(60.3 ± 0.5) J·(mol·K)-1 and −(4.9 ± 1.4) kJ·mol-1, respectively. Finally, at 298.15 K the standard molar enthalpy of formation Δf H°m(l, 298.15 K) and the standard molar entropy of IPTBE S°m(l, 298.15 K) were estimated to be −(378.5 ± 2.7) kJ·mol-1 and 337.6 ± 1.5 J·(mol·K)-1, respectively.
Bibliography:ark:/67375/TPS-FZL4N079-R
Abstract published in Advance ACS Abstracts, January 15, 1997.
istex:64FF6C87C5F32F296C6ED48CF1846B1051BBB55E
ISSN:0888-5885
1520-5045
DOI:10.1021/ie960492h