To solve the problems of lower removal efficiency of organic sulfide and large amount of by-products in the traditional wet desulfurization process
a novel wet catalytic hydrolysis system of carbonyl sulfide was developed. The system was constr
ucted with application of polyethylene glycol dimethyl ether (NHD)
N
-methyldiethanolamine (MDEA)
and water as desulfurization agent with optimal compositions of 25% MDEA/15% H
2
O/60% NHD. The effect of the desulfurization operation parameters
reaction temperature
gas concentration and gas flow rate on the desulfurization of COS was investigated. Furthermore the possible mechanism and kinetic of the desulfurization process were proposed and determined in reference of the results of GC and IC. The results show that the removal efficiency of COS is above 80% under low temperature (298.15—343.15 K) and normal pressure. The absorption process conforms to pseudo-first-order reaction kinetics. The organic solvent contents in the developed desulfurization system is more than 85%
which can effectively avoid the production of by-products and consumption of alkali in the desulfurization system
and is expected to be treated as an alternative for COS removal with high desulfurization efficiency.
关键词
Keywords
references
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