Solubility of CO2 in the Mixed Solvent System of Alkanolamines and Poly(ethylene glycol) 200
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作者:
Li, Jun
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E China Univ Sci & Technol, State Key Lab Chem Engn, Sch Chem Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Sch Chem Engn, Shanghai 200237, Peoples R China
Li, Jun
[1
]
Chen, Lifang
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E China Univ Sci & Technol, State Key Lab Chem Engn, Sch Chem Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Sch Chem Engn, Shanghai 200237, Peoples R China
Chen, Lifang
[1
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Ye, Yinmei
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E China Univ Sci & Technol, Natl Engn Res Ctr Integrated Utilizat Salt Lake R, Sch Resources & Environm Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Sch Chem Engn, Shanghai 200237, Peoples R China
Ye, Yinmei
[2
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Qi, Zhiwen
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E China Univ Sci & Technol, State Key Lab Chem Engn, Sch Chem Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Sch Chem Engn, Shanghai 200237, Peoples R China
Qi, Zhiwen
[1
]
机构:
[1] E China Univ Sci & Technol, State Key Lab Chem Engn, Sch Chem Engn, Shanghai 200237, Peoples R China
[2] E China Univ Sci & Technol, Natl Engn Res Ctr Integrated Utilizat Salt Lake R, Sch Resources & Environm Engn, Shanghai 200237, Peoples R China
Mixed solvents of monoethanolamine (MEA), diglycolamine (DGA), diethanolamine (DEA), and N-methyldiethanolamine (MDEA) with poly(ethylene glycol) 200 (PEG200) as cosolvent were analyzed by thermal gravimetric analysis to select an available CO2 absorber. MEA-PEG200 has the lowest onset temperature (the temperature at which the weight loss begins) of 363 K and thus is not appropriate for CO2 capture at high temperature. The viscosities of the mixtures decrease as temperature increases, and are mainly decided by the viscosity of PEG200 at a high temperature. The solubility of CO2 in mixed solvents of alkanolamine (DGA, DEA, and MDEA) and PEG200 was measured over the range of pressure from (10 to 1600) kPa and temperature from (313.15 to 393.15) K in intervals of 40 K DEA and DGA solutions show relatively high CO2 capacity at 313.15 K owing to a chemical reaction with CO2, while MDEA solution presents the property of physical absorber. When temperature further increases to 393 K, the capacity decreases significantly. The solubility was correlated by Jou and Mather's model.
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Queens Univ Belfast, Sch Chem & Chem Engn, QUILL, Belfast BT9 5AG, Antrim, North IrelandUniv Alabama, Ctr Green Mfg, Tuscaloosa, AL 35487 USA
Rodriguez, Hector
;
Rogers, Robin D.
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Univ Alabama, Ctr Green Mfg, Tuscaloosa, AL 35487 USA
Univ Alabama, Dept Chem, Tuscaloosa, AL 35487 USA
Queens Univ Belfast, Sch Chem & Chem Engn, QUILL, Belfast BT9 5AG, Antrim, North IrelandUniv Alabama, Ctr Green Mfg, Tuscaloosa, AL 35487 USA
机构:
Queens Univ Belfast, Sch Chem & Chem Engn, QUILL, Belfast BT9 5AG, Antrim, North IrelandUniv Alabama, Ctr Green Mfg, Tuscaloosa, AL 35487 USA
Rodriguez, Hector
;
Rogers, Robin D.
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h-index: 0
机构:
Univ Alabama, Ctr Green Mfg, Tuscaloosa, AL 35487 USA
Univ Alabama, Dept Chem, Tuscaloosa, AL 35487 USA
Queens Univ Belfast, Sch Chem & Chem Engn, QUILL, Belfast BT9 5AG, Antrim, North IrelandUniv Alabama, Ctr Green Mfg, Tuscaloosa, AL 35487 USA