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Author:Heidemann, R.A.

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11 matching references were found.

Abdel-Ghani, R.M.; Heidemann, R.A., Comparison of «DELTA»g excess mixing rules for multi-phase equilibria in some ternary systems, Fluid Phase Equilib., 1996, 116, 495-502. [all data]

Heidemann, R.A.; Kokal, S.L., Combined excess free energy models and equations of state, Fluid Phase Equilib., 1990, 56, 17-37. [all data]

Michelsen, M.L.; Heidemann, R.A., Calculation of Tri-Critical Points, Fluid Phase Equilib., 1988, 39, 53. [all data]

Heidemann, R.A.; Fredenslund, A., Vapor-liquid equilibria in complex mixtures, Inst. Chem. Eng. Symp. Ser., 1988, No. 104, A291-A322. [all data]

Rizvi, S.S.H.; Heidemann, R.A., Vapor-liquid equilibria in the ammonia-water system, J. Chem. Eng. Data, 1987, 32, 183. [all data]

Dilay, G.W.; Heidemann, R.A., Calculation of Joule-Thomson inversion curves from equations of stat, Ind. Eng. Chem. Fundam., 1986, 25, 152. [all data]

Evelein, K.A.; Moore, R.G.; Heidemann, R.A., Correlation of the phase behavior in the systems hydrogen sulfide + water and carbon dioxide + water, I&EC Proc. Des. Develop., 1976, 15, 423. [all data]

Heidemann, R.A.; Mandhane, J.M., Ternary liquid-liquid equilibria the van laar equation, Chem. Eng. Sci., 1975, 30, 425. [all data]

Heidemann, R.A., Three-phase equilibria using equations of state, AIChE J., 1974, 20, 847. [all data]

Mandhane, J.M.; Heidemann, R.A., Nrtl parameters for the ternary system butanol + butyl acetate + water, Can. J. Chem. Eng., 1973, 51, 381. [all data]

Heidemann, R.A.; Mandhane, J.M., Some properties of the nrtl equation in correlating liquid-liquid equilibrium data, Chem. Eng. Sci., 1973, 28, 1213. [all data]