Modeling Equilibrium Systems of Amine-Based CO2 Capture by Implementing Machine Learning Approaches

被引:21
作者
Ghiasi, Mohammad M. [1 ]
Abedi-Farizhendi, Saeid [2 ]
Mohammadi, Amir H. [1 ,3 ]
机构
[1] Univ KwaZulu Natal, Sch Engn, Discipline Chem Engn, Howard Coll Campus, Durban, South Africa
[2] Tarbiat Modares Univ, Dept Chem Engn, Tehran, Iran
[3] IRGCP, Paris, France
关键词
absorption; AdaBoost; amine solution; ANN; CO2; capture; modeling; HIGHER HEATING VALUE; CARBON-DIOXIDE; AQUEOUS-SOLUTIONS; HYDROGEN-SULFIDE; MLP-ANN; SOLUBILITY; ABSORPTION; PREDICTION; MONOETHANOLAMINE; MIXTURES;
D O I
10.1002/ep.13160
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Precise calculation of carbon dioxide equilibrium solubility in aqueous amine solutions is decisive in the success of establishment or maintenance of amine-based absorptive carbon dioxide capture processes. To implement the AdaBoost algorithm in conjunction with the classification and regression tree (AdaBoost-CART) aimed at developing models to accurately estimate the equilibrium absorption of carbon dioxide in ethanolamine solutions, experimental data for monoethanolamine (MEA), diethanolamine (DEA), and triethanolamine (TEA) systems were gathered from the literature. Furthermore, neural-based models were developed using the collected databank as the basis of comparison. The results of the presented models were compared to the results of the available models in the literature. It was found that the proposed AdaBoost-CART models for the investigated amine systems present more precise and reliable outputs compared to the results of the neural-based and literature models. In a respective order, the introduced AdaBoost-CART models for MEA, DEA, and TEA solutions show average absolute relative deviation percent of 0.51, 2.76, and 1.41 which indicate their reliability and superiority over other models. (c) 2019 American Institute of Chemical Engineers Environ Prog, 38:e13146, 2019
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页数:12
相关论文
共 39 条
[21]  
LEE JI, 1976, J APPL CHEM BIOTECHN, V26, P541
[22]   CO2 mass transfer and solubility in aqueous primary and secondary amine [J].
Li, Le ;
Rochelle, Gary .
12TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-12, 2014, 63 :1487-1496
[23]   Solubility of carbon dioxide in 30 mass % monoethanolamine and 50 mass % methyldiethanolamine solutions [J].
Ma'mun, S ;
Nilsen, R ;
Svendsen, HF ;
Juliussen, O .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2005, 50 (02) :630-634
[24]  
Maddox R.N., 1994, GAS LIQUID SWEETENIN
[25]  
Mason JW, 1936, T AM INST CHEM ENG, V32, P27
[26]  
Monteith K, 2011, 2011 INTERNATIONAL JOINT CONFERENCE ON NEURAL NETWORKS (IJCNN), P2657, DOI 10.1109/IJCNN.2011.6033566
[27]   Solubility of carbon dioxide in aqueous solutions of 2-amino-2-ethyl-1,3-propanediol [J].
Park, JY ;
Yoon, SJ ;
Lee, H ;
Yoon, JH ;
Shim, JG ;
Lee, JK ;
Min, BY ;
Eum, HM ;
Kang, MC .
FLUID PHASE EQUILIBRIA, 2002, 202 (02) :359-366
[28]   Correlation and prediction of the solubility of carbon dioxide in aqueous alkanolamine and mixed alkanolamine solutions [J].
Park, SH ;
Lee, KB ;
Hyun, JC ;
Kim, SH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (06) :1658-1665
[29]   High Throughput Screening of CO2 Solubility in Aqueous Monoamine Solutions [J].
Porcheron, Fabien ;
Gibert, Alexandre ;
Mougin, Pascal ;
Wender, Aurelie .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2011, 45 (06) :2486-2492
[30]   Estimation of Carbon Dioxide Equilibrium Adsorption Isotherms Using Adaptive Neuro-Fuzzy Inference Systems (ANFIS) and Regression Models [J].
Saghafi, Hamidreza ;
Arabloo, Milad .
ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY, 2017, 36 (05) :1374-1382