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Relevant bibliographies by topics / Fugacity coefficient

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Journal articles

Academic literature on the topic 'Fugacity coefficient'

Author: Grafiati

Published: 4 June 2021

Last updated: 15 February 2022

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Journal articles on the topic "Fugacity coefficient"

1

Hu, Jiawen, Rong Wang, and Shide Mao. "Some useful expressions for deriving component fugacity coefficients from mixture fugacity coefficient." Fluid Phase Equilibria 268, no. 1-2 (2008): 7–13. http://dx.doi.org/10.1016/j.fluid.2008.03.007.

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2

CHEN, Fei-Wu, Cong Qian Gu, Wei-Lan Qian, and Xu-Qin Li. "The Fugacity Coefficient of Non-Ideal Gas and Activity Coefficient of Non-Ideal Solution." University Chemistry 32, no. 8 (2017): 66–70. http://dx.doi.org/10.3866/pku.dxhx201701025.

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3

Callegaro, Sara, Kalotina Geraki, Andrea Marzoli, Angelo De Min, Victoria Maneta, and Don R. Baker. "The quintet completed: The partitioning of sulfur between nominally volatile-free minerals and silicate melts." American Mineralogist 105, no. 5 (2020): 697–707. http://dx.doi.org/10.2138/am-2020-7188.

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Abstract Magmatic systems are dominated by five volatiles, namely H2O, CO2, F, Cl, and S (the igneous quintet). Multiple studies have measured partitioning of four out of these five volatiles (H2O, CO2, F, and Cl) between nominally volatile-free minerals and melts, whereas the partitioning of sulfur is poorly known. To better constrain the behavior of sulfur in igneous systems we measured the partitioning of sulfur between clinopyroxene and silicate melts over a range of pressure, temperature, and melt composition from 0.8 to 1.2 GPa, 1000 to 1240 °C, and 49 to 66 wt% SiO2 (13 measurements). A

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4

Parsafar, Gholamabbas, and F. Madani. "An analytical expression for the fugacity coefficient of the supercritical fluids." High Temperatures-High Pressures 35/36, no. 5 (2003): 529–39. http://dx.doi.org/10.1068/htjr122.

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5

Szarawara, Jósef, and Andrzej Gawdzik. "Method of calculation of fugacity coefficient from cubic equations of state." Chemical Engineering Science 44, no. 7 (1989): 1489–94. http://dx.doi.org/10.1016/0009-2509(89)80025-9.

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6

Míka, Vladimír. "A generalized treatment of cubic equations of state." Collection of Czechoslovak Chemical Communications 54, no. 11 (1989): 2879–95. http://dx.doi.org/10.1135/cccc19892879.

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From the formula proposed for the van Waals type equations of state, general expressions for the compressibility factor, the departure functions and the fugacity coefficient are derived. Easy construction of the formula needed is possible for any of the equations listed in the paper. The method is applicable to other equations of this type.

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7

Amaya-Tapia, A., S. Y. Larsen, and M. Lassaut. "Third Bose fugacity coefficient in one dimension, as a function of asymptotic quantities." Annals of Physics 326, no. 2 (2011): 406–25. http://dx.doi.org/10.1016/j.aop.2010.10.004.

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8

Zhao, Weilong, Hao Wu, Jing Wen, Xin Guo, Yongsheng Zhang, and Ruirui Wang. "Simulation Study on the Influence of Gas Mole Fraction and Aqueous Activity under Phase Equilibrium." Processes 7, no. 2 (2019): 58. http://dx.doi.org/10.3390/pr7020058.

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This work explored the influence of gas mole fraction and activity in aqueous phase while predicting phase equilibrium conditions. In pure gas systems, such as CH4, CO2, N2 and O2, the gas mole fraction in aqueous phase as one of phase equilibrium conditions was proposed, and a simplified correlation of the gas mole fraction was established. The gas mole fraction threshold maintaining three-phase equilibrium was obtained by phase equilibrium data regression. The UNIFAC model, the predictive Soave-Redlich-Kwong equation and the Chen-Guo model were used to calculate aqueous phase activity, the f

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9

Zhou, Li, and Yaping Zhou. "Determination of compressibility factor and fugacity coefficient of hydrogen in studies of adsorptive storage." International Journal of Hydrogen Energy 26, no. 6 (2001): 597–601. http://dx.doi.org/10.1016/s0360-3199(00)00123-3.

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10

Palencia Muñoz, Miguel Fernando, Natalia Prieto-Jiménez, and Germán González Silva. "Liquid balance - steam for methanol mixing - Benzen using the Peng Robinson and Van-Laar models." Respuestas 24, no. 1 (2019): 34–41. http://dx.doi.org/10.22463/0122820x.1807.

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This paper is related to the procedure for calculating curves dew point and bubble point of a binary system, consisting of the methanol and benzene mixture to 45°C, using the Peng-Robinson cubic equation to calculate the fugacity coefficient of gas i in the mixture, and Van Laar model to calculate the activity coefficient of component i in the liquid mixture. Then a comparison between the theoretical data with the experimental data and later with the commercial simulator Hysys-Aspen, which applies the model of Wilson. The simulation was validated with experimental data,in addition to comparing

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