Abstract
Membranes which give high fluxes without selectivities provide a large interfacial area between fluid phases which is independent of the normal constraints of loading and flooding. These membranes offer a largely unexplored route to separation process intensification. Three examples are given in the paper. First, studies of hollow fiber blood oxygenators show that flows which are only a few percent from uniform can reduce overall mass transfer by an order of magnitude. Second, flat sheet membrane evaporators promise the performance of a centrifugal evaporator at a fraction of that unit's cost. Third, distillation in hollow fibers means that the height of the transfer units can be smaller than 0.1 cm, indeed as small as desired.
| Original language | English (US) |
|---|---|
| Pages (from-to) | 98-102 |
| Number of pages | 5 |
| Journal | Journal of Chemical Technology and Biotechnology |
| Volume | 78 |
| Issue number | 2-3 |
| DOIs | |
| State | Published - Feb 2003 |
Keywords
- Blood oxygenators
- Membrane distillation
- Membrane evaporator
- Separation
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