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In particular, its high gas liquid mass transfer efficiency is proved by plentiful experimental data.
One method is to invent novel distillation column internals of excellent performance on high gas liquid mass transfer efficiency, including new and efficient trays, random and structured packings [5, 6, 7, 8].
The change from hydrophilicity to hydrophobicity gave the reactor a higher mass transfer efficiency.
First, a higher agitation rate was used to promote mass transfer efficiency.
The new model incorporates mass transfer efficiency and convective heat transfer along the packed bed.
Characterization of multiphase dispersions is required as it determines mass transfer efficiency and bioreactor homogeneity.
Annular reactors exhibit a mass transfer efficiency which is noticeably higher than that of empty tubes.
The hydrodynamic performance and mass transfer efficiency were compared with classical packing materials used in distillation.
Pressure drop and mass transfer efficiency can also be affected by liquid velocity.
Mass transfer efficiency based on quality of mixing has also been enunciated in this work.
For modules with the same densities, the different packing irregularity led to different mass transfer efficiency.
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