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40 matching references were found.

Mahmoud, R.; Solimando, R.; Bouroukba, M.; Rogalski, M., Solid-Liquid Equilibrium and Excess Enthalpy Measurements in Binary {Dibenzofuran or Xanthene + Normal Long-Chain Alkane} Systems, J. Chem. Eng. Data, 2000, 45, 3, 433-436, https://doi.org/10.1021/je9902084 . [all data]

Solimando, R.; Neau, E.; Peneloux, A.; Rogalski, M., Equations of state for representing PVT properties and vapor-liquid equilibria of hydrocarbons, Rev. Inst. Fr. Pet., 1995, 50, 791-805. [all data]

Solimando, R.; Rogalski, M.; Neau, E.; Peneloux, A., Modifying the Peng Robinson equation for a homogeneous representation of pure fluid PVT properties, Fluid Phase Equilib., 1995, 106, 59-80. [all data]

Durupt, N.; Aoulmi, A.; Bouroukba, M.; Rogalski, M., Heat capacities of liquid polycyclic aromatic hydrocarbons, Thermochim. Acta, 1995, 260, 87-94. [all data]

Aoulmi, A.; Bouroukba, M.; Solimando, R.; Rogalski, M., Thermodynamics of mixtures formed by polycyclic aromatic hydrocarbons with long chain alkanes, Fluid Phase Equilib., 1995, 110, 283-97. [all data]

Gierycz, P.; Malanowski, S.; Rogalski, M., Liquid-vapor equilibria and excess Gibbs energy of 1-methyl-2- pyrrolidinone + organic compounds, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1994, 22, 220-58. [all data]

Solimando, R.; Rogalski, M.; Neau, E.; Peneloux, A., Modeling of the phase behavior of mixtures in the critical region using the augmented Peng-Robinson equation of state, Fluid Phase Equilib., 1993, 82, 369-77. [all data]

Rogalski, M., Liquid-vapor equilibria and excess Gibbs energies of alkyl substituted pyridenes + alkyl substituted benzenes, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1993, 21, 258-317. [all data]

Rogalski, M.; Bylicki, A., Liquid-vapor equilibria and excess Gibbs energy of pyridene + ethylbezene, + propylbezene, or + butylbenzene, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1993, 21, 246-57. [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]

Nagata, I.; Rogalski, M.; Miyamoto, K., Correlation of binary coexistence curves of liquid-liquid equilibria over a wide temperature range using a new local composition model, Thermochim. Acta, 1993, 224, 59-69. [all data]

Rogalski, M.; Carrier, B.; Peneloux, A., Correlation and prediction of physical properties of hydrocarbons with the modified Peng-Robinson equation of state. 3. Thermal properties. A new significant characterizing parameter m, Ind. Eng. Chem. Res., 1991, 30, 1612-17. [all data]

Rogalski, M.; Mato, F.A.; Carrier, B., Vapor pressures of hydrocarbons: modeling, extrapolation and predictionn, Chem. Eng. Sci., 1991, 46, 2445-54. [all data]

Rogalski, M.; Carrier, B.; Solimando, R.; Peneloux, A., Correlation and predication of physical properties of hydrocarbons with the modified Peng-Robinson equation of state. 2. Representation of the vapor pressures and of the molar volumes, Ind. Eng. Chem. Res., 1990, 29, 659. [all data]

Rogalski, M.; Neau, E., A group contribution method for prediction of hydrocarbon saturated liquid volumes, Fluid Phase Equilib., 1990, 56, 59-69. [all data]

Carrier, B.; Rogalski, M.; Peneloux, A., Correlation and prediction of physical properties of hydrocarbons with the modified Peng-Robinson equation of state. 1. Low and medium vapor pressures, Ind. Eng. Chem. Res., 1988, 27, 1714-21. [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]

Kiciak, K.; Rogalski, M., Prediction of ternary vapour-liquid equilibria from binary data, Chem. Biochem. Eng. Q., 1987, 1, 4, 151. [all data]

Berro, C.; Neau, E.; Rogalski, M., Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1987, No. 2, 90. [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]

Rogalski, M.; Treszczanowicz, A.J., Vapor pressures and enthalpy of vaporization of 1-alkanols in terms of associated mixtures models, Fluid Phase Equilib., 1986, 27, 53. [all data]

Rogalski, M., Vapour pressures and excess Gibbs energies of (2-methylpyridine + methylbenzene), (2,4-dimethylpyridine + 1,2-dimethylbenzene), and (2,6-dimethylpyridine + 1,2- or 1,3- or 1,4-dimethylbenzene or, J. Chem. Thermodyn., 1985, 17, 1045. [all data]

Rogalski, M., Vapour pressures and excess Gibbs energies of {(3-methylpyridine or 3-ethylpyridine) + (methyl- or ethyl- or propyl- or butyl-benzene)} at T = 373.15 K, J. Chem. Thermodyn., 1985, 17, 921. [all data]

Rogalski, M., Correlation of vapor pressures of pure substances in homologous series, Thermochim. Acta, 1985, 90, 125. [all data]

Rogalski, M., Vapour pressures and excess Gibbs energies of (2,4,6-trimethylpyridine + 1,2,4- or 1,3,5-trimethylbenzene or n-propylbenzene or isoporpylbenzene or n-butylbenzene or isobutylbenzene at T = 373.1, J. Chem. Thermodyn., 1985, 17, 1051. [all data]

Rogalski, M.; Bylicki, A., Vapour pressures and excess Gibbs energies of {pyridine + (methyl- or benzene)} at T = 373.15 k, J. Chem. Thermodyn., 1985, 17, 915. [all data]

Gierycz, P.; Rogalski, M.; Malanowski, S., Vapor-liquid equilibria in binary systems formed by N-methylpyrrolidone with hydrocarbons and hydroxyl derivatives, Fluid Phase Equilib., 1985, 22, 107-22. [all data]

Berro, C.; Rogalski, M.; Peneloux, A., A new ebulliometric technique. vapor-liquid equilibria in the binary systems ethanol + n-heptane and ethanol + n-nonane., Fluid Phase Equilib., 1982, 8, 55. [all data]

Berro, C.; Rogalski, M.; Peneloux, A., Excess Gibbs energies and excess volumes of 1-butanol-n-hexane and 2- methyl-1-propanol-n-hexane binary systems, J. Chem. Eng. Data, 1982, 27, 352. [all data]

Berro, C.; Neau, E.; Rogalski, M., Vapor-liquid equilibrium of the systems 1-propanol + 2,2,4- trimethylpentane and 2-propanol + n-hexane., Fluid Phase Equilib., 1981, 7, 41. [all data]

Rogalski, M., A New Method for COrrelating Vapor-Liquid Equilibrium in Strongly Nonideal Systems in Intern. Symp. Vapor-Liquid Equil. Multicomp. Systems, Warszawa-Jablonna, Nov. 2-6, 1975, p 99, 1980. [all data]

Rogalski, M.; Malanowski, S., Ebulliometers modified for the accurate determination of vapor-liquid equilibrium, Fluid Phase Equilib., 1980, 5, 97-111. [all data]

Rogalski, M.; Stryjek, R., Mutual solubility of binary n-hexadecane and polar compound systems., Bull. Acad. Pol. Sci., Ser. Sci. Chim., 1980, 28, 139-47. [all data]

Stryjek, R.; Rogalski, M.; Treszczanowicz, T.; Luszczyk, M., Vapor-Liquid Equilibrium and Mutual Solubility of the B- Methoxypropionitrile-Water System, Bull. Acad. Pol. Sci., Ser. Sci. Chim., 1978, 26, 327-35. [all data]

Maczynski, A.; Maczynska, Z.; Rogalski, M., Binary systems of hydrocarbons and related non-oxygen compounds. in Verified Vapor-Liquid Equilibrium Data, Vol. 2, Thermody- namical Data for Technology, Ser. A, Polish Sci. Pub., Warsaw, 1978. [all data]

Bylicki, A.; Kozdon, A.F.; Rogalski, M., Comparative measurements of benzene density, Bull. Acad. Pol. Sci., Ser. Sci. Chim., 1978, 26, 877-81. [all data]

Rogalski, M.; Malanowski, S., A new equation for correlation of vapour-liquid equilibrium data of strongly non-ideal mixtures, Fluid Phase Equilib., 1977, 1, 137. [all data]

Rogalski, M.; Rybakiewicz, K.; Malanowski, S., Rapid and accurate method for determination of vapor-liquid equilibrium., Ber. Bunsen-Ges. Phys. Chem., 1977, 81, 1070-3. [all data]

Judeinstein, P.; Berdagué, P.; Bayle, J.P.; Rogalska, E.; Rogalski, M.; Petit-Jean, D.; Guermouche, M.H., Synthesis and properties of two new liquid crystals: an analytical and thermodynamic study, J. Chromatogr. A, 1999, 859, 1, 59-67, https://doi.org/10.1016/S0021-9673(99)00755-4 . [all data]

Kozlowska, M.K.; Dománska, U.; Lempert, M.; Rogalski, M., Determination of thermodynamic properties of isotactic poly(1-butene) at infinite dilution using density and inverse gas chromatography, J. Chromatogr. A, 2005, 1068, 2, 297-305, https://doi.org/10.1016/j.chroma.2005.01.090 . [all data]