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Author:Wichterle

65 matching references were found.

Fárková, J.; Wichterle, I., Vapour pressures of some ethyl and propyl esters of fatty acids, Fluid Phase Equilibria, 1993, 90, 1, 143-148, https://doi.org/10.1016/0378-3812(93)85009-B . [all data]

Linek, J.; Wichterle, I., Liquid-vapour equilibrium. LIX. The systems diisopropyl ether-acrylic acid, isopropyl acetate-acrylic acid, acrylic acid-2-ethylhexanol and methyl isobutyl ketone-acrylic acid, Collect. Czech. Chem. Commun., 1973, 38, 7, 1846-1852, https://doi.org/10.1135/cccc19731846 . [all data]

Linek, J.; Wichterle, I.; Marsh, K.N., Vapor-liquid Equilibria for Water + Diacetone Alcohol, Ethyl Methanoate + Water, and Ethyl Methanoate + Phenol, J. Chem. Eng. Data, 1996, 41, 1219-22. [all data]

Linek, J.; Wichterle, I.; Marsh, K.N., Vapor-liquid Equilibria for N-Methyl-3-pyrrolidone + Benzene, + Toluene, and + Methylcyclohexane, J. Chem. Eng. data, 1996, 41, 1212-8. [all data]

Linek, J.; Wichterle, I., Isobaric vapor-liquid equilibria in six binary systems containing hexane + a pentanol isomer at 27, 53, and 93 kPa, ELDATA Int. Electron. J. Phys.-Chem. Data, 1995, 1, 265-274. [all data]

Farkova, J.; Linek, J.; Wichterle, I., Isothermal vapor-liquid equilibria and excess volumes in the methanol- aliphatic ether systems, Fluid Phase Equilib., 1995, 109, 53-65. [all data]

Farkova, J.; Wichterle, I., Vapor-liquid equilibria of 1,1,2,2-tetrachloroethane + some n-alkyl n- alkanoates, ELDATA Int. Electron. J. Phys.-Chem. Data, 1995, 1, 13-22. [all data]

Farkova, J.; Wichterle, I., Isothermal vapor-liquid equilibria in five methanol + aliphatic ether systems at temperatures from 310.15 to 333.15 K, ELDATA Int. Electron. J. Phys.-Chem. Data, 1995, 1, 121-9. [all data]

Farkova, J.; Wichterle, I., Vapor pressures of some ethyl and propyl esters of fatty acids, Fluid Phase Equilib., 1993, 90, 143-8. [all data]

Bernatova, S.; Linek, J.; Wichterle, I., Vapor-liquid equilibrium in the butyl alcohol-n-decane system at 85, 100 and 115 .degree.C, Fluid Phase Equilib., 1992, 74, 127-32. [all data]

Wolfova, J.; Linek, J.; Wichterle, I., Vapor-liquid equilibria in the heptane-2-pentanol and heptane-2-methyl-1- butanol systems at 75, 85 and 95.degree.C, Fluid Phase Equilib., 1991, 64, 281-9. [all data]

Wolfova, J.; Linek, J.; Wichterle, I., Vapor-liquid equilibria in the heptane - 3-pentanol and heptane - 2-methyl-2-butanol systems at constant temperature, Fluid Phase Equilib., 1990, 54, 69. [all data]

Wichterle, I., Liquid-vapour equilibrium: xxxv vapour-liquid equilibria in system heptane - toluene - p-xylene and in systems heptane - toluene - extractive agent, Collect. Czech. Chem. Commun., 1965, 30, 3388. [all data]

Wichterle, I.; Hala, E., Semimicrodetermination of vapor-liquid equilibrium, Ind. Eng. Chem. Fundam., 1963, 2, 155. [all data]

Wichterle, I.; Wagner, Z., Nonclassical behavior of binary mixtures in gas-liquid critical region and its quantitative description, Collect. Czech. Chem. Commun., 1989, 54, 2863. [all data]

Machova, I.; Linek, J.; Wichterle, I., Vapour-liquid equilibria in the heptane - 1-penthanol and heptane-3-methyl-1--butanol systems at 75, 85 and 95 Celcius, Fluid Phase Equilib., 1988, 41, 257-67. [all data]

Wagner, Z.; Wichterle, I., High-pressure vapour-liquid equilibrium in systems containing carbon dioxide, 1-hexene, and n-hexane, Fluid Phase Equilib., 1987, 33, 109. [all data]

Machova, I.; Polednova, J.; Wichterle, I., Vapor-liquid equilibriums in the system chlorobenzene-ethylbenzene, Chem. Prum., 1986, 36, 462. [all data]

Wichterle, I.; Linek, J.; Hala, E., Vapor-Liquid Equilibrium Data Bibliography, Suppl. 4, Elsevier, New York, 1985. [all data]

Polednova, J.; Wichterle, I., Vapour-liquid equilibrium in the acetone + water system at 101.325 kpa., Fluid Phase Equilib., 1984, 17, 115-21. [all data]

Lancka, M.; Wichterle, I., Vapor-liquid equilibrium in the 2-butanone + water system at 101.325 kpa., Fluid Phase Equilib., 1984, 18, 245-252. [all data]

Lencka, M.; Wichterle, I., Vapor-liquid equilibrium in the 2-butanone-water system at 101.325 kPa, Fluid Phase Equilib., 1984, 18, 245. [all data]

Uchytil, P.; Wichterle, I., Liquid-Vapor critical region of the most volatile component of a ternary System I. Vapour-liquid equilibria in the ethane-propane-n-butane system system., Fluid Phase Equilib., 1983, 15, 209-17. [all data]

Lhotak, V.; Wichterle, I., Vapor-liquid equilibria in the ethane + propane + n-butane system at high pressures., Fluid Phase Equilib., 1983, 12, 307-309. [all data]

Wichterle, I.; Linek, J.; Hala, E., Vapor-Liquid Equilibrium Data Bibliography, Suppl. 3, Elsevier, New York, 1982. [all data]

Lhotak, V.; Wichterle, I., Vapor-liquid equilibria in the ethane + n-butane system at high pressures., Fluid Phase Equilib., 1981, 6, 229. [all data]

Beranek, P.; Wichterle, I., Vapor-liquid equilibria in the propane + n-butane system at high pressures., Fluid Phase Equilib., 1981, 6, 279-82. [all data]

Wichterle, I., The Experimental Techniques for Determinating High-Pressure Vapor-Liquid Equilibrium in Intern. Symp. Vapor-Liquid Equil. Multicomp. Systems, Warszawa-Jablonna, Nov. 2-6, 1975, p 163, 1980. [all data]

Wichterle, I., High pressure vapour-liquid equilibrium: vi experimental technique, Fluid Phase Equilib., 1979, 2, 293. [all data]

Wichterle, I., Vapour-liquid equilibrium correlation procedure in high pressure region, Collect. Czech. Chem. Commun., 1979, 44, 3515. [all data]

Wichterle, I.; Linek, J.; Hala, E., Vapor-Liquid Equilibrium Data Bibliography, Suppl. 2, Elsevier, New York, 1979. [all data]

Rajiah, A.; Wichterle, I., Vapour-liquid equilibrium in tetrachloromethane + isobutyl alcohol system, Collect. Czech. Chem. Commun., 1979, 44, 2006. [all data]

Wichterle, I., High pressure vapour-liquid equilibrium: V quantitative description, Fluid Phase Equilib., 1978, 2, 143. [all data]

Wichterle, I., High pressure vapour-liquid equilibrium: IV quantitative description, Fluid Phase Equilib., 1978, 2, 59. [all data]

Wichterle, I.; Lenek, J., Vapor-liquid equilibrium data bibliography: supplement I, J. Am. Chem. Soc., 1977, 99, 5229. [all data]

Lnenickova, J.; Wichterle, I., Vapour-liquid equilibrium in toluene + aliphatic c(4) alcohol systems, Collect. Czech. Chem. Commun., 1977, 42, 1907. [all data]

Drahos, J.; Wichterle, I.; Hala, E., A generalized method for calculation and prediction of vapour-liquid equilibria at high pressures, Fluid Phase Equilib., 1977, 1, 173. [all data]

Wichterle, I., Computations of vapour-liquid equilibrium in the critical region, Collect. Czech. Chem. Commun., 1976, 41, 3188. [all data]

Wichterle, I.; Linek, J.; Hala, E., Vapor-Liquid Equilibrium Data Bibliography, Suppl. 1, Elsevier, New York, 1976. [all data]

Wichterle, I.; Lnenickova, J., , Vyskumna Zprava 4/75, UTZCHTCSAV, Praha, 1975. [all data]

Miksovsky, J.; Wichterle, I., Vapour-Liquid Equilibria in the Ethane-Proane System at High Pressures, Collect. Czech. Chem. Commun., 1975, 40, 365. [all data]

Vejrosta, J.; Wichterle, I., The propane - pentane system at high pressures, Collect. Czech. Chem. Commun., 1974, 39, 1246. [all data]

Vejrosta, J.; Wichterle, I.; Wicar, S., Semimicrostill for the determination of high pressure vapor- liquid equilibrium, Collect. Czech. Chem. Commun., 1974, 39, 206. [all data]

Wichterle, I., Vapor-liquid equilibrium data bibliography a system of computer documentation, J. Chem. Doc., 1974, 14, 39. [all data]

Linek, J.; Wichterle, I., Liquid-vapour equilibrium in the ternary isopropyl acetate + water + acetic acid and isopropyl acetate + water + acrylic acid systems at 200 torr, Collect. Czech. Chem. Commun., 1974, 39, 3395-3402. [all data]

Linek, J.; Wichterle, I., Liquid-vapour equilibrium in the ternary water + acetic acid + 2- ethylhexanol and water + acrylic acid + 2-ethylhexanol systems at 50 torr, Collect. Czech. Chem. Commun., 1974, 39, 3403-3408. [all data]

Wichterle, I.; Linek, J.; Hala, E., Vapor-Liquid Equilibrium Data Bibliography, Elsevier: New York, pp 1053, 1973. [all data]

Linek, J.; Hlavaty, K.; Wichterle, I., Liquid-liquid equilibria in the ternary acrylic acid + extraction solvent + water systems, Collect. Czech. Chem. Commun., 1973, 38, 1840-1845. [all data]

Linek, J.; Wichterle, I., Liquid-vapour equilibrium lx the system acetic acid - acrylic acid at 200 torr, Collect. Czech. Chem. Commun., 1973, 38, 1853-1857. [all data]

Wichterle, I.; Kobayashi, R., Vapor-liquid equilibrium of methane-ethane-propane system at low temperatures and high pressures., J. Chem. Eng. Data, 1972, 17, 13-18. [all data]

Linek, J.; Prochazka, K.; Wichterle, I., Liquid-vapour equilibrium liv systems ethyl acetate - benzene, ethyl acetate - toluene and ethyl acetate - ethylbenzene, Collect. Czech. Chem. Commun., 1972, 37, 3010-3014. [all data]

Linek, J.; Wichterle, I.; Polednova, J., Liquid-vapour equilibrium: liii the systems benzene + diisopropyl ether, dipropyl ether + toluene and dipropyl ether + ethylbenzene, Collect. Czech. Chem. Commun., 1972, 37, 2820-2829. [all data]

Wichterle, I.; Linek, J., Antoine Vapor Pressure Constants of Pure Compounds, Academia, Praha, 1971. [all data]

Wichterle, I.; Salsburg, Z.W.; Chappelear, P.S.; Kobayashi, R., "Unexpected" vapor-liquid equilibria behavior in the critical region and some theoretical implications of critical exponents, Chem. Eng. Sci., 1971, 26, 1141-1144. [all data]

Wichterle, I.; Chappelear, P.S.; Kobayashi, R., Determination of critical exponents from measurements of binary vapor- liquid equilibrium in the neighborhood of the critical line, J. Comput. Phys., 1971, 7, 606. [all data]

Wichterle, I.; Kobayashi, R., , Monogr. Low Temperature VLE, Rice University, Houston, TX, 1970. [all data]

Wichterle, I.; Boublikova, L., Semimicromethod for determination of partial pressures of solutions., Ind. Eng. Chem. Fundam., 1969, 8, 585. [all data]

Hala, E.; Wichterle, I.; Linek, J., , Recommended Test Mixtures for Distillation Columns, Eur- op. Fed. Chem. Eng., Zuiderweg, F. J., Ed., Inst. Chem. Eng.: London, 1969. [all data]

Bernatová, Svatoslava; Wichterle, Ivan, Isothermal vapour--liquid equilibrium in the binary tert-butanol or 2,2,4-trimethylpentane+1-tert-butoxy-2-propanol, and in the ternary tert-butanol+2,2,4-trimethylpentane+1-tert-butoxy-2-propanol systems, Fluid Phase Equilibria, 2001, 189, 1-2, 111-118, https://doi.org/10.1016/S0378-3812(01)00574-X . [all data]

Constantinescu, Dana; Wichterle, Ivan, Isothermal vapour--liquid equilibria and excess molar volumes in the binary ethanol + methyl propanoate or methyl butanoate systems, Fluid Phase Equilibria, 2002, 203, 1-2, 71-82, https://doi.org/10.1016/S0378-3812(02)00173-5 . [all data]

Dahmani, Omar; Wichterle, Ivan; Ait-Kaci, Ahmed, Isothermal vapour-liquid equilibria for binary systems of chloroalkanes with heptane, toluene and methylcyclohexane at 323.15 and 333.15 K, Fluid Phase Equilibria, 1996, 124, 1-2, 135-146, https://doi.org/10.1016/S0378-3812(96)03106-8 . [all data]

Linek, Jan; Wichterle, Ivan; Marsh, Kenneth N., Vapor-Liquid Equilibria for N- Methyl-2-pyrrolidone + Benzene, +Toluene, +Heptane, and +Methylcyclohexane, J. Chem. Eng. Data, 1996, 41, 6, 1212-1218, https://doi.org/10.1021/je9601826 . [all data]

Wichterle, O.; Vogel, J., Chem. Listy, 1954, 48, 1225. [all data]

Wichterle, O.; Kobayashi, R., Vapor-Liquid Equilibrium of Methane-Propane Systems at Low Temperatures and High Pressures, J. Chem. Eng. Data, 1972, 17, 4. [all data]

Wichterle, O.; Kobayashi, R., Vapor-Liquid Equilibrium of Methane-Ethane System at Low Temperatures and High Pressures, J. Chem. Eng. Data, 1972, 17, 9. [all data]