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The membrane module achieved a maximum H2 flux of 1.79×10−2 mg H2/m2 s, which was sufficient to completely remove 16.4 mg/L NO3−-N from a synthetic groundwater with no NO2− accumulation.
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Cross flow microfiltration membrane modules ensured almost complete separation and recycle of cells without much fouling problem whereas composite nanofiltration membrane module helped achieve 96% recovery and recycle of unconverted sugars along with high degree of purity.
When its first module achieved orbit in 1986, Mir was the pride of the Soviet Union.
In overall, greater flux enhancements with modified hollow fiber membranes modules were achieved at higher feed temperatures.
Using these criteria, Global Up and CNV Up modules achieved high-quality networks.
Therefore, higher efficiency improvements can be achieved if membrane module designs with reduced pressure drop are used.
As most of the industrial membrane separation units use hollow fiber modules, having a proper model for simulating this type of membrane module is very useful in achieving guidelines for design and characterization of membrane separation units.
This is not possible to achieve for a static non-vibrating membrane module.
A comparative performance analysis is then achieved between a porous and a dense membrane module.
By selecting 347 and 104 membrane module, minimum and maximum values of flow rate for each membrane module would be achieved, respectively.
For the specific hollow fiber membrane module in the present study, the inlet holes should be evenly distributed at the cross section to achieve uniform flow distribution in the module.
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