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Journal ArticleDOI

A general approach to modelling membrane modules

James Marriott, +1 more
- 01 Nov 2003 - 
- Vol. 58, Iss: 22, pp 4975-4990
TLDR
In this paper, mathematical models of hollow-fibre and spiral-wound membrane modules were developed from rigorous mass, momentum and energy balances and can be used to describe a generic membrane separation, in contrast to most existing models which are typically process specific and are only valid within a limited operating range.
About
This article is published in Chemical Engineering Science.The article was published on 2003-11-01. It has received 178 citations till now. The article focuses on the topics: Mathematical model.

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Citations
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Journal ArticleDOI

Computational fluid dynamics applied to membranes: State of the art and opportunities

TL;DR: This paper reviews the improvements that have been achieved concerning the membranes used for microfiltration, ultraFiltration, nanofiltration/reverse osmosis processes during the last decades and reviews the state of the art computational fluid dynamics methods applied to membranes processes.
Journal ArticleDOI

Developments in Membrane Research: from Material via Process Design to Industrial Application

TL;DR: The aim of this review paper is to give an overview of the research activities of GKSS in the field of polymer based membranes by describing different classes of polymeric materials for membranes, and the characterization of membranes.
Journal ArticleDOI

Modeling the impacts of feed spacer geometry on reverse osmosis and nanofiltration processes

TL;DR: In this article, a multi-scale modeling approach was proposed to link microscopic and macroscopic transport phenomena in spiral wound elements. And the impacts of feed spacer geometry on full-scale reverse osmosis (RO) and nanofiltration (NF) system performance were investigated.
Journal ArticleDOI

Thermodynamic and thermoeconomic analyses of seawater reverse osmosis desalination plant with energy recovery

TL;DR: In this article, an energy recovery Pelton turbine is integrated with the desalination plant, and the effects of the system components irreversibilities on the economics and cost of product water are parametrically studied through the thermoeconomic analysis.
Journal ArticleDOI

Modeling submerged hollow-fiber membrane filtration for wastewater treatment

TL;DR: In this article, a model for submerged outside-in hollow-fiber MF/UF filtration for wastewater treatment is presented, which integrates the major influence factors on medium scale of granularity.
References
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Journal ArticleDOI

Viscous flow relative to arrays of cylinders

TL;DR: In this paper, the free-surface model was extended to the case of flow relative to cylinders and shown to be in good agreement with existing data on beds of fibers of various types and flow through bundles of heat-exchanger tubes.
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Mass transfer and pressure loss in spiral wound modules

TL;DR: In this paper, the authors present some experimental data for pressure drop and mass transfer characteristics in spiral wound elements and in spacer-filled flow channels and the experimental results and the computer program were used to calculate the performance of a spiral wound element and its possible design variations.
Journal ArticleDOI

Modeling permeation of binary mixtures through zeolite membranes

TL;DR: In this paper, the authors used the empirical Vignes relation for the prediction of the binary Maxwell-Stefan surface diffusivity, and showed that the importance of incorporation of adsorbate-adsorbate interactions in the model is clearly shown, both for transient and steady-state mixture permeation.
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Modeling multicomponent gas separation using hollow‐fiber membrane contactors

TL;DR: In this article, a model for multicomponent gas separation using hollow-fiber contactors was developed for simulation of cocurrent, countercurrent, and crossflow contacting patterns with permeate purging (or sweep).
Journal ArticleDOI

Gas separation by high‐flux, asymmetric hollow‐fiber membrane

TL;DR: A mathematical model of multicomponent permeation systems with high-flux, asymmetric hollow-fiber membranes is presented in this paper, which takes into account the permeate pressure variation inside the fiber.
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