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...
Saved in:
Published in: | Industrial & engineering chemistry research Vol. 36; no. 3; pp. 896 - 902 |
---|---|
Main Authors: | , , , , |
Format: | Journal Article |
Language: | English |
Published: |
Washington, DC
American Chemical Society
01-03-1997
|
Subjects: | |
Online Access: | Get full text |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
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 |