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The model was subsequently used to compare the effect of module length and number of stages on the design performance of a 110,000 m3/day NF plant.
At the same time, using the optimized hollow fiber module length and packing density in the DCMD process, ultra pure water with a low salinity of 0.062 g/L was attained at a condition of high energy efficiency (EE).
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The hTLR10 N-terminal domain was composed of 1 4 LRR modules, with each LRR module length being around 24 residues and the structurally important asparagine ladder being conserved.
It has been observed that for given feed temperature and concentration, the optimum module length can be tuned by changing F/P ratio.
The low stage cut (5-10 %) set in the experimental measurements means that the differences between the mixture selectivity and the single gas selectivity cannot be attributed to the eventual presence of partial pressure profiles along the module length, but only to the interactions occurring among gases and membrane.
Under a given set of operating conditions, there exists a module length (named as optimum module length) where the net thermal energy consumption and overall permeate productivity are optimum.
More importantly, total thermal efficiency decreased with increasing module length, thus a short module was better used for high efficiency of VMD.
The optimum module length has been analyzed as function of feed to permeate flow rate (F/P) ratio, feed temperature and concentration.
In this paper, a cross-flow model for hyperfiltration is developed by considering mass balance at a differential element of the cross-flow module and then integrating the expression over the whole module to get the module length.
Variations of bulk concentration, bulk velocity, retentate channel pressure, permeate flux, permeate concentration, etc., along the module length are obtained after solving the design equations numerically.
It is represented by a decrease in the total water production beyond a number of stages or a certain module length.
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