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Journal ArticleDOI

Diffusional boundary‐layer resistance for membranes with low porosity

Dermot M. Malone, +1 more
- 01 Mar 1977 - 
- Vol. 23, Iss: 2, pp 177-184
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TLDR
In this paper, diffusional mass transfer across membranes with uniform but low pore densities was studied experimentally as a function of stirring rate and pore area fraction, and the results were analyzed in terms of a stagnant film boundary-layer model specially formulated for a heterogeneous membrane containing discrete pores.
Abstract
Diffusional mass transfer across membranes with uniform but low pore densities was studied experimentally as a function of stirring rate and pore area fraction. The results were analyzed in terms of a stagnant film boundary-layer model specially formulated for a heterogeneous membrane containing discrete pores. The overall membrane diffusional resistance is linearly related to the inverse of the pore area fraction of the membranes for a constant stirring rate. An equivalent boundary-layer thickness can be defined which is independent of membrane properties but a unique function of stirrer speed. These experimental boundary-layer thicknesses are greater by a factor of 3 than those predicted by a published Sherwood number correlation determined for homogeneous surfaces, but the stirring rate dependence is in excellent agreement with this same correlation.

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Citations
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Characterisation and prediction of separation performance of nanofiltration membranes

TL;DR: In this article, the rejection of single electrolytes at six nanofiltration membranes has been experimentally studied using a model based on the extended Nernst-Planck equation, which accounts for the hindered nature of transport in the membranes.
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Microporous hollow fibre membrane modules as gas-liquid contactors. Part 1: Physical mass transfer processes. A specific application: mass transfer in highly viscous liquids

TL;DR: In this paper, a gas-liquid contactor with nonwetted microporous fibres in the laminar flow regime was studied and the active mass transfer area was found to be equal to the total membrane area, regardless the porosity of the fibres.
Journal ArticleDOI

Process for protein PEGylation.

TL;DR: This review article critically reviews the current state of the art in PEGylation and critical reviews the development of industrial scale processes which can meet the market requirements in terms of quality and costs.
Journal ArticleDOI

Proper accounting of mass transfer resistances in forward osmosis: Improving the accuracy of model predictions of structural parameter

TL;DR: In this article, the authors proposed a mathematical flux model in which ECP effects are accounted for, so that structural parameter (S ) can be more accurately measured and showed that changes in cross-flow velocity impact internal concentration polarization due to induced mixing within the support layer.
Book ChapterDOI

Membrane-Based Solvent Extraction

TL;DR: A mixer-settler arrangement provides a single equilibrium stage; a number of them connected together provide multistage extraction as mentioned in this paper, which creates a large interfacial area and increases the extraction rate considerably.
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