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Four different membrane modules were used to explore the impact of configuration on separation performance.
Recent researches on the fundamental transport data in the membrane modules were collected and compared.
CHF membrane modules were prepared for pilot plant testing and performance measured using CO2, O2, N2.
Inner skin hollow fiber pervaporation membrane modules were fabricated by a dynamic negative pressure layer-by-layer (LbL) technique.
The membrane modules were received as commercial modules from Air Products (US-Norway), and were coated in-situ at NTNU in Norway.
In Phase 2, all the membrane modules were aerated and polyhydroxyalkanoate (PHA) was utilized as carbon resource to promote the microbial growth.
Similar(46)
Established technologies based on specific membrane modules are also described.
Mathematical models of hollow-fibre and spiral-wound membrane modules are presented in this paper.
Improving mass transfer in membrane modules is always desirable, but not easily achieved under laminar regime.
The allocation of membrane area to the two membrane modules was optimized.
As membranes and membrane modules are becoming cheaper, operation below the threshold flux becomes more practical.
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