110th Anniversary: Accurate Modeling of the Simultaneous Absorption of H2S and CO2 in Aqueous Amine Solvents

被引:17
作者
Alkhatib, Ismail I. I. [1 ,2 ]
Pereira, Luis M. C. [1 ]
Vega, Lourdes F. [1 ,2 ]
机构
[1] Khalifa Univ Sci & Technol, Gas Res Ctr, Chem Engn Dept, PO 127788, Abu Dhabi, U Arab Emirates
[2] Khalifa Univ Sci & Technol, Ctr Catalysis & Separat CeCaS, Res & Innovat Ctr CO2 & H2 RICH, PO 127788, Abu Dhabi, U Arab Emirates
关键词
EQUATION-OF-STATE; VAPOR-LIQUID-EQUILIBRIA; POLYATOMIC FLUID MIXTURES; GAS-ALKANOLAMINE SYSTEMS; HYDROGEN-SULFIDE; CARBON-DIOXIDE; ACID GAS; N-METHYLDIETHANOLAMINE; PHASE-EQUILIBRIA; DIETHANOLAMINE SOLUTIONS;
D O I
10.1021/acs.iecr.9b00862
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We present results concerning the application of soft statistical associating fluid theory (soft-SAFT), a molecular-based equation, for modeling the absorption of carbon dioxide and hydrogen sulfide in several aqueous amines, including monoethanolamine, diethanolamine, and N-methyldiethanolamine, at conditions of relevance for acid gas separation. The chemisorption of CO2 and H2S in aqueous amines was modeled through the formation of physically bounded CO2-amine and H2S-amine aggregates by explicitly considering strong intermolecular association forces. This approach eliminates the need to consider all speciation reactions, significantly reducing the number of fitted parameters required to describe the absorption process while providing a direct connection between each amine and the chemical reaction with the acid gases. The model predicts the absorption of H2S for different amine concentrations in excellent agreement with data, showing high extrapolative capability. Soft-SAFT is also used to predict the simultaneous absorption of H2S and CO2 in aqueous amines and results compared with experimental literature data and predictions from the recommended thermodynamic models implemented in the Aspen Plus (version 10) process simulator. Results show that soft-SAFT provides comparable levels of accuracy as the e-NRTL thermodynamic model recommended in the process simulator, with the added advantages of higher transferability and predictive capabilities, being a reliable model for the screening of high-performance solvents for acid gas separation when limited experimental data are available.
引用
收藏
页码:6870 / 6886
页数:17
相关论文
共 95 条
[1]   Sensitivity analysis of the rate-based CO2 absorber model using amine solutions (MEA, MDEA and AMP) in packed columns [J].
Afkhamipour, Morteza ;
Mofarahi, Masoud .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2014, 25 :9-22
[2]   A rate-based model for the design of gas absorbers for the removal Of CO2 and H2S using aqueous solutions of MEA and DEA [J].
Al-Baghli, NA ;
Pruess, SA ;
Yesavage, VF ;
Selim, MS .
FLUID PHASE EQUILIBRIA, 2001, 185 (1-2) :31-43
[3]   Modeling the solubility of CO2 and H2S in DEA-MDEA alkanolamine solutions using the electrolyte-UNIQUAC model [J].
Al-Rashed, Osama A. ;
Ali, Sami H. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2012, 94 :71-83
[4]   HYDROGEN SULPHIDE ABSORPTION IN AQUEOUS MONOETHANOLAMINE SOLUTIONS [J].
ASTARITA, G ;
BALZANO, C .
CHEMICAL ENGINEERING SCIENCE, 1965, 20 (12) :1101-&
[5]   MODEL OF VAPOR-LIQUID-EQUILIBRIA FOR AQUEOUS ACID GAS-ALKANOLAMINE SYSTEMS .2. REPRESENTATION OF H2S AND CO2 SOLUBILITY IN AQUEOUS MDEA AND CO2 SOLUBILITY IN AQUEOUS MIXTURES OF MDEA WITH MEA OR DEA [J].
AUSTGEN, DM ;
ROCHELLE, GT ;
CHEN, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (03) :543-555
[6]   MODEL OF VAPOR LIQUID EQUILIBRIA FOR AQUEOUS ACID GAS ALKANOLAMINE SYSTEMS USING THE ELECTROLYTE NRTL EQUATION [J].
AUSTGEN, DM ;
ROCHELLE, GT ;
PENG, X ;
CHEN, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (07) :1060-1073
[7]   PHASE-EQUILIBRIUM PROPERTIES OF SYSTEM CARBON DIOXIDE-HYDROGEN SULFIDE [J].
BIERLEIN, JA ;
KAY, WB .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (03) :618-624
[8]   Prediction of binary and ternary diagrams using the statistical associating fluid theory (SAFT) equation of state [J].
Blas, FJ ;
Vega, LF .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (02) :660-674
[9]  
Blas FJ, 1997, MOL PHYS, V92, P135, DOI 10.1080/00268979709482082
[10]   Online NMR Spectroscopic Study of Species Distribution in MDEA-H2O-CO2 and MDEA-PIP-H2O-CO2 [J].
Boettinger, Wolfram ;
Maiwald, Michael ;
Hasse, Hans .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (20) :7917-7926