2006
DOI: 10.1016/j.ijheatmasstransfer.2005.08.013
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Diffusion models and scale-up

Abstract: A model for mass transfer processes in column apparatuses has been done. The model may be modified for different volume source (chemical reaction, interphase mass transfer). The using of the average velocities and concentration permits to solve the scale-up problem. A hierarchical approach for model parameter identification has been proposed.

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Cited by 33 publications
(13 citation statements)
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“…Under these hydrodynamic conditions, velocity distributions in the gas and liquid phases in the column cannot be obtained. Only a qualitative theoretical analysis of the absorption kinetics can be carried out employing the diffusion type of model 5–9.…”
Section: Physical Absorptionmentioning
confidence: 99%
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“…Under these hydrodynamic conditions, velocity distributions in the gas and liquid phases in the column cannot be obtained. Only a qualitative theoretical analysis of the absorption kinetics can be carried out employing the diffusion type of model 5–9.…”
Section: Physical Absorptionmentioning
confidence: 99%
“…The mathematical model of the process is created by approximations of the mechanics of continua 5. The model is based on the convection‐diffusion equation 5–9, where the convective transfer in the medium elementary volume results from laminar or turbulent (as a result of large‐scale pulsations) flows, the diffusive transfer is molecular or turbulent (as a result of small‐scale pulsations), and the interphase mass transfer is a volume reaction.…”
Section: Physical Absorptionmentioning
confidence: 99%
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