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Wisniewska, B., Liquid-vapor equilibrium. Ethylbenzene-propylbenzene system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1996, 24, 40-67. [all data]

Wisniewska, B.; Gregorowicz, J.; Malanowski, S., Development of a vapor-liquid equilibrium apparatus to work at pressures up to 3 MPa, Fluid Phase Equilib., 1993, 86, 173-86. [all data]

Rogalski, M.; Chylinski, K.; Wisniewska, B., liquid-vapor equilibia of quinoline + trans-decalin, + decane, or + butylbenzene, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1993, 21, 318-26. [all data]

Wisniewska, B.; Malanowski, S., Prediction of phase equilibria for hydrocarbon systems in a wide range of pressure and temperature by AEOS equation of state, Fluid Phase Equilib., 1990, 56, 89-95. [all data]

Wisniewska, B., Vapor pressures and excess Gibbs energies of {ethylbenzene + (methyl or n-propyl- or isopropyl- or n-butyl- or 1,2-dimethyl- or 1,4-dimethyl- or 1,2,4-trimethylbenzene or methylcyclohexane or heptane, J. Chem. Thermodyn., 1987, 19, 897. [all data]

Rogalski, M.; Chylinski, K.; Wisniewska, B., Vapor Pressures and Excess Gibbs Energies of {Quinoline + (trans- bicyclo[4.4.0]decane or n-decane or n-butylbenzene} at T = 393.15K and Excess Volumes of (quinoline+n-buthylbenzene) at T = 298.15K, J. Chem. Thermodyn., 1987, 19, 57. [all data]

Wisniewska, B.; Lencka, M.; Rogalski, M., Vapour pressures of 2,4-, 2,6-, and 3,5-dimethylpyridine at temperatures from 267 to 360 K, J. Chem. Thermodyn., 1986, 18, 703-8. [all data]