On the CO2 absorption kinetics, loading capacity, and catalytic desorption of aqueous solutions of N-methyl-D-glucamine

被引:4
|
作者
Sarode, Urvashi K. [1 ]
Vaidya, Prakash D. [1 ,2 ]
机构
[1] Inst Chem Technol, Dept Chem Engn, Mumbai, India
[2] Inst Chem Technol, Dept Chem Engn, Nathalal Parekh Marg, Mumbai 400019, India
来源
关键词
absorption; amino sugar; carbon dioxide; equilibrium; kinetics; regeneration; CARBON-DIOXIDE REMOVAL; SOLUBILITY; MONOETHANOLAMINE; ETHYLENEDIAMINE; EQUILIBRIUM; CAPTURE; SINGLE; PLANT; WATER;
D O I
10.1002/cjce.24865
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
CO2 separation with harmful chemicals will damage the environment. It is essential to explore greener solvents that are producible from renewable resources such as biomass. The suitability of N-methyl-D-glucamine (MG), also known as meglumine, for capturing CO2, was explored in this work. This nontoxic amino sugar, which is derived from sorbitol, represents a renewable bio-solvent. It was found that MG is especially reactive with CO2. Trials were performed in a stirred cell reactor with a flat gas-liquid interface between 303 and 313 K. The values of the pseudo-first-order reaction rate constant, reaction orders, and activation energy were found. The loading capacity (alpha) of 0.5 M MG solution was measured at T = 308 K. For a typical value of alpha = 0.524 mol CO2/mol MG, the corresponding equilibrium partial pressure of CO2 was 22 kPa. Finally, it was found that the catalyst Al2O3 aided in the desorption of CO2-loaded MG solutions. Desorption efficiency using Al2O3 was higher (74%) than that achieved without this catalyst (45%). It is thus clear that MG represents a potential solvent for improved CO2 separation from gases.
引用
收藏
页码:5956 / 5966
页数:11
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