Huang Rongrong, Gu Feiyan, Zhang Bing and Hou Yujun(Y. C. Hou)(Chemical Engineering Thermodynamics Laboratory, et al. Phase Equilibria for the Binary System of Water-Isobutyl Aldehyde[J]. CIESC Journal, 1985, (1).
DOI:
Huang Rongrong, Gu Feiyan, Zhang Bing and Hou Yujun(Y. C. Hou)(Chemical Engineering Thermodynamics Laboratory, et al. Phase Equilibria for the Binary System of Water-Isobutyl Aldehyde[J]. CIESC Journal, 1985, (1).DOI:
Phase Equilibria for the Binary System of Water-Isobutyl Aldehyde
Equilibrium properities of the partially miscible system of water and isobutyl aldehyde were difficult to measure due to the latters chemical activity
and as such
the accuracy of literature data is generally poor. Effective steps were taken in the present work to prevent oxidation and polymerization of isobutyl aldehyde
thereby insuring good reproducibility of the data obtained. In this work
vapor-liquid equilibrium and liquid-liquid equilibrium data for this binary system
measured at 760 mm Hg
are correlated by using both the NRTL equation and the multiparameter Wilson equation (Mitsuyasu method). Three sets of binary parameters for each equation are determined in the following manner: (1)based on VLE experimental data alone
(2)based on LLE experimental data alone and(3) based on both VLE and LLE data. The vapor compositions calculated from these two equations with the three sets of binary parameters all agree well with the experimental data.
Study on flash evaporation characteristics as well as thermodynamic variation performance in liquid hydrogen tank during on-orbit venting
Thermo-oxidative degradation characteristics of TPT backsheet from end-of-life photovoltaic modules
Controlled synthesis of Bi2MoO6/MoO3 composite fibers via in-situ hydrothermal method and their high-efficiency photocatalytic hydrogen production performance
Research progress of ionic liquids in separation of aromatics/alkanes and olefins/alkanes
A hybrid modeling and optimization strategy for sequential simulated moving bed