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Title: Equilibrium constants for the liquid-phase synthesis of isopropyl tert-butyl ether from 2-propanol and isobutene

Journal Article · · Industrial and Engineering Chemistry Research
DOI:https://doi.org/10.1021/ie960492h· OSTI ID:458468
; ; ; ;  [1]
  1. Univ. of Barcelona (Spain) Chemical Engineering Dept.

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 {Delta}{sub r}H{degree}{sub m}(298.15 K) is {minus}(22.9 {+-} 1.3) kJ/mol, in agreement with literature data, and the standard molar reaction entropy {Delta}{sub r}S{degree}{sub m}(298.15 K) and free energy {Delta}{sub r}G{degree}{sub m}(298.15 K) are {minus}(60.3 {+-} 0.5) J/mol{times}K and {minus}(4.9 {+-} 1.4) kJ/mol, respectively. Finally, at 298.15 K the standard molar enthalpy of formation {Delta}{sub f}H{degree}{sub m}(l, 298.15 K) and the standard molar entropy of IPTBE S{degree}{sub m}(l, 298.15 K) were estimated to be {minus}(378.5 {+-} 2.7) kJ/mol and 337.6 {+-} 1.5 J/(mol{times}K), respectively.

Sponsoring Organization:
DGICyT (Spain)
OSTI ID:
458468
Journal Information:
Industrial and Engineering Chemistry Research, Vol. 36, Issue 3; Other Information: PBD: Mar 1997
Country of Publication:
United States
Language:
English