Simultaneous absorption of carbon dioxide and hydrogen sulfide into aqueous blends of 2-amino-2-methyl-1-propanol and diethanolamine |
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| Authors: | B.P. Mandal |
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| Affiliation: | a Department of Chemical Engineering, Indian Institute of Technology Guwahati, North Guwahati 781039, India
b Separation Science Laboratory, Cryogenic Engineering Centre, Indian Institute of Technology Kharagpur, Kharagpur 721302, India |
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| Abstract: | This work presents an experimental and theoretical investigation of the simultaneous absorption of CO2 and H2S into aqueous blends of 2-amino-2-methyl-1-propanol (AMP) and diethanolamine (DEA). The effect of contact time, temperature and amine concentration on the rate of absorption and the selectivity were studied by absorption experiments in a wetted wall column at atmospheric pressure and constant feed gas ratio. The diffusion-reaction processes for CO2 and H2S mass transfer in blended amines are modeled according to Higbie's penetration theory with the assumption that all reactions are reversible. The blended amine solvent (AMP+DEA+H2O) has been found to be an efficient mixed solvent for simultaneous absorption of CO2 and H2S. By varying the relative amounts of AMP and DEA the blended amine solvent can be used as an H2S-selective solvent or an efficient solvent for total removal of CO2 and H2S from the gas streams. Predicted results, based on the kinetics-equilibrium-mass transfer coupled model developed in this work, are found to be in good agreement with the experimental results of rates of absorption of CO2 and H2S into (AMP+DEA+H2O) of this work. |
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| Keywords: | Absorption Modeling Carbon dioxide Hydrogen sulfide 2-Amino-2-methyl-1-propanol Diethanolamine |
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