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Received August 16, 2016
Accepted February 6, 2017
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Quantitative structure-property relationship (QSPR) for prediction of CO2 Henry’s law constant in some physical solvents with consideration of temperature effects
Institute of Petroleum Engineering, Faculty of Chemical Engineering, College of Engineering, University of Tehran, Tehran, Iran
riahi@ut.ac.ir
Korean Journal of Chemical Engineering, May 2017, 34(5), 1405-1415(11), 10.1007/s11814-017-0018-0
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Abstract
Different types of physical solvents have been utilized for CO2 removal from natural gas in the sweetening process. In this work, quantitative structure-property relationship (QSPR) method is suggested to build powerful models to predict Henry’s law constant (HLC) for CO2 in physical solvents. Modeling the HLC for CO2 as a function of molecular descriptors was achieved by multiple linear regression and descriptor selection was by genetic algorithm. The main proposed model has two simple descriptors, including the number of hydroxyl groups and molecular weight of solvents at fixed temperature. Also, the effect of temperature was studied, and this operational variable was added to the mentioned simple descriptors. In this case, the data set is comprised of 77 HLC for CO2 in solvents and at different temperatures. Several internal and external validation methods demonstrated the excellent ability for prediction, and the average relative deviation of main model was 6.48.
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Shacham M, Elly M, Paster I, Brauner N, Chem. Eng. Sci., 97, 186 (2013)
O’Loughlin DR, English NJ, Chemosphere, 127, 1 (2015)
Gharagheizi F, Ilani-Kashkouli P, Mirkhani SA, Farahani N, Mohammadi AH, Ind. Eng. Chem. Res., 51(12), 4764 (2012)
English NJ, Carroll DG, J. Chem. Inf. Comput. Data, 41, 1150 (2001)
Xu J, Zhang H, Wang LX, Ye WX, Xu WL, Li ZC, Fluid Phase Equilib., 291(2), 111 (2010)
Sahoo S, Patel S, Mishra BK, Thermochim. Acta, 512(1-2), 273 (2011)
Goodarzi M, Ortiz EV, Coelho LS, Duchowicz PR, Atmos. Environ., 44, 3179 (2010)
Golzar K, Amjad-Iranagh S, Modarress H, Measurement, 46, 4206 (2013)
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http://www.hyper.com
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Talete SRL, Dragon for Windows (Software for Molecular Descriptor Calculation), Version 6 (2013).
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Golbraikh A, Tropsha A, J. Mol. Graph. Model, 20, 269 (2002)
XLSTAT software, XLSTAT-CCR module, Trial Version (2013).
Gramatica P, QSAR Comb. Sci., 26, 694 (2007)
Minovski N, Zuperl S, Drgan V, Novi M, Anal. Chim. Acta, 759, 28 (2013)
Galvao AC, Francesconi AZ, J. Supercrit. Fluids, 51(2), 123 (2009)
Xu Y, Schutte RP, Hepler LG, Can. J. Chem. Eng., 70, 569 (1992)
Rucker CH, Rucker G, Meringer M, J. Chem. Inf. Model, 47, 2345 (2007)
Singh P, Niederer JPM, Versteeg GF, Int. J. Greenh Gas Control, 1, 5 (2007)
Singh P, Niederer JPM, Versteeg GF, Chem. Eng. Res. Des., 87(2A), 135 (2009)
Kanegsberg B, Kanegsberg E, Handbook for Critical Cleaning: Cleaning Agents and Systems, 2nd Ed., CRC Press (2011).
Osmialowski K, Piekos R, J. Solution. Chem., 20, 241 (1991)
Makitra RG, Pristanski RE, Flyunt RI, Russ. J. Gen. Chem., 73, 1227 (2003)