2016•Industrial & Engineering Chemistry ResearchOpen access

Combined Effect of Temperature and pKa on the Kinetics of Absorption of Carbon Dioxide in Aqueous Alkanolamine and Carbonate Solutions with Carbonic Anhydrase

Nathalie J.M.C. Penders-van Elk, S. Martijn Oversteegen, Geert Frederik Versteeg

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Abstract

In present work the absorption of carbon dioxide in aqueous N -methyldiethanolamine, N, N -dimethylethanolamine, and triisopropanolamine solutions with and without the enzyme carbonic anhydrase has been studied in a stirred cell reactor at temperatures varying between 278 and 313 K, at an alkanolamine concentration of 1 kmol m –3 and carbonic anhydrase concentrations ranging from 0 to 2.4 kg m –3, respectively. The experimental data from these experiments have been used to fit the obtained rate constant for the enzymatic CO 2 hydration to the Brønsted relation: ln( k ) = A (p K a ) + B + C / T . In addition to the carbon dioxide absorption in the three tertiary alkanolamines, the absorption of carbon dioxide in next three solvents had been studied: 0.3 kmol m –3 potassium carbonate, 0.3 kmol m –3 sodium carbonate, and 0.2 kmol m –3 2-amino-2-methyl-1-propanol. The kinetics from these solvents are well predicted by the relation fitted to the data of the tertiary amines only.

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In present work the absorption of carbon dioxide in aqueous N -methyldiethanolamine, N, N -dimethylethanolamine, and triisopropanolamine solutions with and without the enzyme carbonic anhydrase has been studied in a stirred cell reactor at temperatures varying between 278 and 313 K, at an alkanolamine concentration of 1 kmol m –3 and carbonic anhydrase concentrations ranging from 0 to 2.4 kg m –3, respectively. The experimental data from these experiments have been used to fit the obtained rate constant for the enzymatic CO 2 hydration to the Brønsted relation: ln( k ) = A (p K a ) + B + C / T . In addition to the carbon dioxide absorption in the three tertiary alkanolamines, the absorption of carbon dioxide in next three solvents had been studied: 0.3 kmol m –3 potassium carbonate, 0.3 kmol m –3 sodium carbonate, and 0.2 kmol m –3 2-amino-2-methyl-1-propanol. The kinetics from these solvents are well predicted by the relation fitted to the data of the tertiary amines only.

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Available abstract

In present work the absorption of carbon dioxide in aqueous N -methyldiethanolamine, N, N -dimethylethanolamine, and triisopropanolamine solutions with and without the enzyme carbonic anhydrase has been studied in a stirred cell reactor at temperatures varying between 278 and 313 K, at an alkanolamine concentration of 1 kmol m –3 and carbonic anhydrase concentrations ranging from 0 to 2.4 kg m –3, respectively. The experimental data from these experiments have been used to fit the obtained rate constant for the enzymatic CO 2 hydration to the Brønsted relation: ln( k ) = A (p K a ) + B + C / T . In addition to the carbon dioxide absorption in the three tertiary alkanolamines, the absorption of carbon dioxide in next three solvents had been studied: 0.3 kmol m –3 potassium carbonate, 0.3 kmol m –3 sodium carbonate, and 0.2 kmol m –3 2-amino-2-methyl-1-propanol. The kinetics from these solvents are well predicted by the relation fitted to the data of the tertiary amines only.

Key concepts: Alkanolamine, Chemistry, Carbonic anhydrase, Carbon dioxide, Potassium carbonate, Aqueous solution, Carbonic acid, Inorganic chemistry

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Combined Effect of Temperature and pKa on the Kinetics of Absorption of Carbon Dioxide in Aqueous Alkanolamine and Carbonate Solutions with Carbonic Anhydrase — Research Paper | ScholarLens