Relevant bibliographies by topics / Electrolyte-NRTL model

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Academic literature on the topic 'Electrolyte-NRTL model'

Author: Grafiati
Published: 4 June 2021
Last updated: 1 February 2022

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Journal articles on the topic "Electrolyte-NRTL model"

1

Chen, Chau-Chyun, and Yuhua Song. "Generalized electrolyte-NRTL model for mixed-solvent electrolyte systems." AIChE Journal 50, no. 8 (2004): 1928–41. http://dx.doi.org/10.1002/aic.10151.

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2

Hossain, Nazir, Sanjoy K. Bhattacharia, and Chau-Chyun Chen. "Temperature dependence of interaction parameters in electrolyte NRTL model." AIChE Journal 62, no. 4 (2015): 1244–53. http://dx.doi.org/10.1002/aic.15080.

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3

Lin, Yu-Jeng, Nazir Hossain, and Chau-Chyun Chen. "Modeling dissociation of ionic liquids with electrolyte NRTL model." Journal of Molecular Liquids 329 (May 2021): 115524. http://dx.doi.org/10.1016/j.molliq.2021.115524.

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4

Yansen Hartanto, Tri Partono Adhi, and Antonius Indarto. "EVALUASI KESETIMBANGAN KELARUTAN GAS KARBON DIOKSIDA (CO2) DALAM PELARUT ALKANOLAMINA MENGGUNAKAN SIMULATOR PROSES." Jurnal Teknik Kimia USU 4, no. 4 (2015): 1–7. http://dx.doi.org/10.32734/jtk.v4i4.1506.

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Acid gas removal to remove carbon dioxide (CO2) in natural gas is one of the most important processes. The common removal process of CO2 from natural gas by using alkanolamine solution This process was adopted as basic module in commercial process simulation tools with various equilibrium models. Thus, this study was focused to evaluate the validity in certain operating condition and equilibrium model that produced by commercial simulation tools. The model in this study included coefficient activity model based on Kent-Eisenberg, Li-Mather, and Electrolyte Non Random Two Liquid (NRTL). The evaluation was conducted by doing analysis from simulation result and experiment data that have been used as reference. Furthermore, validation test in absorption process simulation was done to compare column temperature profile. The overall conclusions show that electrolyte NRTL gives the most accurate result.
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5

Bollas, G. M., C. C. Chen, and P. I. Barton. "Refined electrolyte-NRTL model: Activity coefficient expressions for application to multi-electrolyte systems." AIChE Journal 54, no. 6 (2008): 1608–24. http://dx.doi.org/10.1002/aic.11485.

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6

Chen, Chau-Chyun. "Representation of solid-liquid equilibrium of aqueous electrolyte systems with the electrolyte NRTL model." Fluid Phase Equilibria 27 (January 1986): 457–74. http://dx.doi.org/10.1016/0378-3812(86)87066-2.

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7

Chen, Chau-Chyun, Paul M. Mathias, and Hasan Orbey. "Use of hydration and dissociation chemistries with the electrolyte–NRTL model." AIChE Journal 45, no. 7 (1999): 1576–86. http://dx.doi.org/10.1002/aic.690450719.

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8

Sadeghi, Rahmat. "Modification of the NRTL and Wilson models for the representation of phase equilibrium behavior of aqueous amino acid – electrolyte solutions." Canadian Journal of Chemistry 86, no. 12 (2008): 1126–37. http://dx.doi.org/10.1139/v08-166.

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The extended NRTL and Wilson local composition models for amino acid solutions have been modified for the representation of the phase equilibrium behavior of aqueous amino acid – electrolyte solutions by considering cells with random composition for the reference Gibbs energies or enthalpies of local composition cells with a central amino acid molecule and also with a central ion. These new local composition models, which have a molecular thermodynamic framework, have been used to model the vapor–liquid and solid–liquid equilibrium behavior of amino acids and small peptides in aqueous solutions as functions of temperature, ionic strength, and amino acid compositions. The utility of the models is demonstrated with a successful representation of the activity coefficients and the solubility of several amino acids in different aqueous solutions.Key words: amino acid, NRTL, Wilson, activity coefficient, solubility, aqueous solution.
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9

Zhang, Ying, and Chau-Chyun Chen. "Thermodynamic Modeling for CO2Absorption in Aqueous MDEA Solution with Electrolyte NRTL Model." Industrial & Engineering Chemistry Research 50, no. 1 (2011): 163–75. http://dx.doi.org/10.1021/ie1006855.

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10

Que, Huiling, and Chau-Chyun Chen. "Thermodynamic Modeling of the NH3–CO2–H2O System with Electrolyte NRTL Model." Industrial & Engineering Chemistry Research 50, no. 19 (2011): 11406–21. http://dx.doi.org/10.1021/ie201276m.

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