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- W2045595514 abstract "Radial diffusional mass transfer is studied in a fluid flowing in fully developed laminar flow in an annular cylindrical reactor in which a first order heterogeneous reaction is taking place at the wall. The asymptotic behaviour of the concentration decrease far from the reactor inlet is especially investigated. Limiting values of Sherwood numbers are numerically determined and represented by semi-empirical expressions. Additivity relationships between homogeneous and heterogeneous contributions are established. Theoretical results are found in excellent agreement with those yielded by a new experimental method based on heterogeneous decomposition of ozone. Annular reactors exhibit a mass transfer efficiency which is noticeably higher than that of empty tubes. This efficiency may be characterized by three criteria related to inner space utilization, catalytic surface utilization and/or mechanical energy degradation." @default.
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- W2045595514 date "1977-01-01" @default.
- W2045595514 modified "2023-09-29" @default.
- W2045595514 title "Mass transfer in annular cylindrical reactors in laminar flow" @default.
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- W2045595514 doi "https://doi.org/10.1016/0009-2509(77)80243-1" @default.
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