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The mathematical model of multicomponent mixture mass transfer in membrane contactor has been developed.

An internally-cooled parallel-plate membrane contactor has been proposed, designed, and used for liquid desiccant air dehumidification.

The idea of interfacial membrane contactor has been utilized for the catalytic wet air oxidation of phenol under mild conditions.

A internally-cooled hexagonal parallel-plate membrane contactor has been proposed and employed for liquid desiccant air dehumidification, which contains a series of internally-cooled hexagonal parallel-plate membrane channels (IHPMC) for the liquid desiccant stream.

It indicates that the hollow fiber membrane contactor has a great potential in the area of CO2 separation from flue gas when absorbent's concentration and liquid gas pressure difference are designed elaborately.

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With the recent introduction of thin and chemically resistant membrane contactors based on Teflon AF-2400 (poly(tetrafluoroethylene- co-2,2-bis trisfluoromethyl -4,5-difluoro-1,3-dioxole)) co-2,2-bis trisfluoromethyl -4,5-difluoro-1,3-dioxolef membrane co-2,2-bis trisfluoromethyl -4,5-difluoro-1,3-dioxole

Five different membrane contactors have been fabricated and series of experiments have been conducted to validate the mathematical model.

Microporous hollow fiber gas liquid membrane contactors have a fixed and well-defined gas liquid interfacial area.

Ceramic hollow fibre membrane contactors have been applied to carbon dioxide stripping from monoethanolamine (MEA) solution at high temperature where most polymeric membranes would fail to operate.

Membrane contactors have been used in a wide range of applications, since they offer a number of advantages over the conventional dispersed phase contactors, such as the absence of emulsions, no flooding at high flow rates or unloading at low flow rates.

Such tube-in-tube membrane contactors have now been applied in several important synthetic reactions and are becoming a generally accepted tool of mesoscale flow chemistry.

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