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The present calculations were confined to the fully developed mass transfer region far downstream from the tube inlet, where <Sh> and Sh* are both independent of axial position.
The most active mass transfer region are consist of relative high Re and high CO2 volume fraction according to the fitting results, and the Sh decrease intensely when Re decrease, especially when Re is below 0.1.
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These slow mass transfer regions are vulnerable to be contaminated by transuranic elements.
However, at low methanol solution flow rates, a larger open ratio yielded a higher power density at higher current densities, corresponding to the mass transfer limitation region.
The reaction dominated mass transfer regime was confirmed by the plateau region experiment and calculations of mass transfer.
The resistance to mass transfer inside this region during bioPd(0) preparation should not be neglected.
The extent of mass transfer in this region can be quantified.
The data also indicate the occurrence of a great degree of mass transfer in the region immediate downstream of the nozzle tip.
The model partitions the pore space into "mobile" and "immobile" flow regions with first-order mass transfer between these two regions (i.e, "physical" nonequilibrium or PNE).
The PCNE model allows for partitioning open space in solution conduits into mobile and immobile flow regions with first-order mass transfer between the two regions to represent physical nonequilibrium in the conduit.
The first one is plug flow mass transfer in semi-infinite region.
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