Vapor–liquid equilibria for the systems propane+m-cresol, propane+p-cresol, and propane+m-cresol+p-cresol at high pressures-Reference-Cited by-同舟云学术

Vapor–liquid equilibria for the systems propane+m-cresol, propane+p-cresol, and propane+m-cresol+p-cresol at high pressures

Published:1998-01 Issue:1-2 Volume:143 Page:125-141
ISSN:0378-3812
Container-title:Fluid Phase Equilibria
language:en
Short-container-title:Fluid Phase Equilibria

Author:

Lee Kuang-Rong,Tan Chung-Sung

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering

Reference15 articles.

1. W.B. Lone, T.B. McBride, J.F. Spears, J.H. Hall, US Patent No. 5,149,887, 1992.

2. A. Tasaka, H. Hosaka, I. Dohgame, US Patent No. 4,032,581, 1977.

3. Supercritical Fluid Extraction of Triglycerides

4. K.C. Chao, H.M. Lin, G.D. Nageshwar, Phase equilibrium in coal liquefaction processes, Research Project 367-2, Electric Power Research Institute, Palo Alto, CA, USA, 1980.

5. Gas-liquid equilibrium of carbon dioxide plus m-cresol and carbon dioxide plus quinoline at elevated temperatures

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