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- W2034298943 abstract "Abstract A theoretical analysis using the surface-renewal and film-penetration models, which includes gas-phase resistance to mass transfer, is presented for the rate of absorption of a gas and its transfer to the bulk liquid in the case where the solute gas undergoes a first-order chemical reaction in the liquid phase. It reveals that: a. The fraction of absorbed gas transported to the bulk liquid depends upon the Hatta number Ha in case of the surface-renewal model and on Ha as well as a dimensionless hydrodynamic parameter in case of the film-penetration model. b. The widely assumed law of addition of resistances is valid for the surface-renewal and film-penetration models. c. The reaction influences both the overall mass-transfer coefficient and the nature of the driving force, i.e. the increased rate of absorption due to the reaction is not solely due to the enhancement factor multiplying the liquid-phase mass-transfer coefficient for physical absorption as has been conventionally assumed in the lite..." @default.
- W2034298943 created "2016-06-24" @default.
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- W2034298943 date "2010-02-04" @default.
- W2034298943 modified "2023-10-01" @default.
- W2034298943 title "A Theoretical Analysis of Dissolved-Gas Transfer to the Bulk Liquid in Gas Absorption with a First-Order Reaction" @default.
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- W2034298943 doi "https://doi.org/10.1080/00194500903315476" @default.
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