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Author:Mehra, V.S.

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11 matching references were found.

Mehra, V.S.; Thodos, G., Vapor-liquid equilibrium constants for the ethane - n-butane - n-heptane system at 150, 200, and 250f, J. Chem. Eng. Data, 1966, 11, 365-72. [all data]

Mehra, V.S.; Thodos, G., Vapor-liquid equilibrium in the ethane - n-heptane system, J. Chem. Eng. Data, 1965, 10, 211-4. [all data]

Mehra, V.S.; Thodos, G., Vapor-liquid equilibrium in the ethane - n-butane system, J. Chem. Eng. Data, 1965, 10, 307-9. [all data]

Mehra, V.S.; Thodos, G., Critical Temperatures and Critical Pressures for the Ethan-n-Butane-n- Pentane System, J. Appl. Chem., 1964, 14, 265. [all data]

Mehra, V.S., Vapor-liquid equilibrium constants for ethane + n-butane + n-pentane and ethane + n-butane + n-heptane systems, Ph.D. Dissertation, Northwestern University, Evanston, IL, 1963. [all data]

Mehra, V.S.; Thodos, G., Vapor-Liquid Equilibrium Constants for the Ethane-n-Butane-n-Pentane System at 200 deg, 250 deg, and 300 deg F., J. Chem. Eng. Data, 1963, 8, 1-8. [all data]

Mehra, V.S.; Brown, G.M.; Thodos, G., Vapour-liquid equilibrium constants up to the critical point for binary hydrocarbon systems, Chem. Eng. Sci., 1962, 17, 33. [all data]

Mehra, V.S.; Thodos, G., The methane - propane - n-pentane system, J. Chem. Eng. Data, 1962, 7, 497-8. [all data]

Mehra, V.S.; Thodos, G., The prediction of vapor-liquid equilibrium constants for binary hydrocarbon systems in the critical region, AIChE J., 1962, 8, 604. [all data]

Mehra, V.S.; Thodos, G., Fugacity coefficients of n-butane, J. Chem. Eng. Data, 1961, 6, 366-7. [all data]

Mehra, V.S.; Thodos, G., Vapor-Liquid Equilibrium Constants for the Ethane-n-Butane-n-Heptane System at 300 deg and 350 deg F, J. Chem. Eng. Data, 1968, 13, 155-60. [all data]