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- W2298711213 abstract "Due to the need to meet stringent environmental regulations and to minimize capital and operating costs, the design and operation of coke-oven gas (COG) desulfurization processes must be optimized. For H2S Scrubbers, this paper presents a rigorous rate model that accounts for not only mass and heat transfer mechanisms, but also complex and reversible chemical reactions involving H2S, CO2, NH3 and associated ions. The model need not use a chemical enhancement factor based on simplified reaction mechanisms. This model can be extended to simulation of NH3 scrubbers, deacifiers and NH3 stills of COG desulfurization processes. The model establishes liquid-film concentration profiles of individual components and temperature profile. For a typical industrial H2S scrubber, the predicted absorption efficiency for H2S, CO2, and NH3 is 86.4% and 60.2%, respectively." @default.
- W2298711213 created "2016-06-24" @default.
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- W2298711213 date "2002-03-01" @default.
- W2298711213 modified "2023-09-23" @default.
- W2298711213 title "Modelling chemical absorption for a coke-oven-gas H2S scrubber" @default.
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- W2298711213 doi "https://doi.org/10.6967/jcice.200203.0181" @default.
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