In this paper the transport processes in Membrane Distillation (MD) are described by reformulation of the conventional theories of heat and mess transfer. This analysis highlights the sources of potential inefficiency in the MD process and provides a rationale for future developments. The theory is
Determination of membrane properties for use in the modelling of a membrane distillation module
✍ Scribed by Caroliene M. Guijt; Imre G. Rácz; Tom Reith; AndréB. de Haan
- Publisher
- Elsevier Science
- Year
- 2000
- Tongue
- English
- Weight
- 458 KB
- Volume
- 132
- Category
- Article
- ISSN
- 0011-9164
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✦ Synopsis
Membrane distillation carded out in a counter current flow module, in which latent heat is recovered by heating the incoming cold seawater with the condensing product water flow, is a promising technology for low cost seawater desalination. The membranes used in this module are hydrophobic (polypropylene, polyethylene) and highly permeable fibre membranes. For modelling purposes the Knudsen diffusion and viscous flow membrane characteristics (K0 and Bo respectively) of five fibre membranes are determined. This paper presents a new, specially developed method for the determination of Ko and B0 values of highly permeable fibre membranes with single gas permeation experiments through a short dead end fibre. In order to be able to make use of a reliable method to determine the values of K0 and B~ it is essential that the pressure inside the permeable part of the membrane is constant. To determine the conditions at which the pressure drop in the permeable part of the membrane fibre is negligible, this part is reduced in length until the values of K0 and/3o become constant For all membranes the gases He, N2 and CO2 were used. The gases N2 and CO2 lead to consistent values of K0 and Bo. Helium gives less accurate results due to its low molecular weight. The three polypropylene membranes have a similar structure and have therefore about the same values for K0 and B0. The same was found for the two polyethylene fibres.
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