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The characteristic channel size of micromixers is in the submillimeter range.
The effects the channel size and the channel length are particularly considered.
For all solutions a significant viscosity dependence on channel size was observed.
The transition to turbulence is not affected by the channel size.
Channel size can be tuned over wide limits by adjusting temperature and lipid identity.
Hence, the flow velocity is almost the same in a certain range of the channel size.
We also used CFD to investigate the effects of the channel size and the flow of the dispersed phase on MC emulsification using asymmetric straight flow-through MCs with a characteristic channel size of 5 400 μm.
The degree of activity enhancement due to the channel shape decreases as the channel size is reduced from 2 to 1 mm, because the catalyst utilization is increased with decreasing the channel size.
Results also show that the temperature, channel size, and air flow rate influence each other, and the performance cannot be improved infinitely by increasing the channel size, and thus the cathode flow field should be optimized.
This method was based on a systematic reduction of wall channel size based on a predetermined correlation between column's back pressure and wall channel size of a particular monolith pore size.
The flexibility in channel size and dimension allows tailoring the monolith reactor to the specific needs of the individual application.
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