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An apparatus for contacting large volumes of gas and liquid together on a microscope scale for mass transfer or transport processes wherein the contact between liquid and gas occurs at the interfaces of a multitude of gas bubbles. Multiple porous tubes assembled in a bundle inside a pressure vessel

An apparatus for contacting large volumes of gas and liquid together on a microscope scale for mass transfer or transport processes wherein the contact between liquid and gas occurs at the interfaces of a multitude of gas bubbles. Multiple porous tubes assembled in a bundle inside a pressure vessel terminate at each end in a tube sheet. A thin film helical liquid flow is introduced into the inside of each porous tube around and along its inside wall. Gas is sparged into the porous media and the liquid film so that an annular two phase flow with a uniform distribution of tiny gas bubbles results. The gas flow is segregated from the liquid flow without first passing through the porous media and through the liquid film. Nozzles at the lower end of the tubes divert liquid flow to a vessel and redirect the gas flow in a countercurrent direction.

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1. Apparatus for contacting large volumes of gas and liquid across a multitude of microscopic interfaces, comprising:at least one gas-liquid contactor assembly including an outer vessel having a central longitudinal axis circumscribed by a non-porous generally cylindrical side wall with first and se

1. Apparatus for contacting large volumes of gas and liquid across a multitude of microscopic interfaces, comprising:at least one gas-liquid contactor assembly including an outer vessel having a central longitudinal axis circumscribed by a non-porous generally cylindrical side wall with first and second ends, at least one gas inlet for introducing gas into said outer vessel, a plurality of elongate tubes within said outer vessel disposed in circumferential and radially spaced relation having longitudinal axes parallel to said outer vessel longitudinal axis, each of said tubes having a microscopically porous side wall with an inner surface surrounding a hollow interior and opposed first and second ends, first and second seal means engaged in sealing relation with said outer vessel and around said first and second ends of said tubes to form a pressurized gas chamber surrounding said tubes and a gas-liquid separator chamber isolated therefrom by said second seal means, said hollow interior of said tubes being in open fluid communication through said first and second seal means, and said second seal means having a plurality of orifices in coaxial alignment with said seconds ends of said tubes to provide an uninterrupted flow path from said second ends of said tubes;a liquid feed assembly connected with said outer vessel first end and in fluid communication with said first ends of said tubes and having liquid injection means for introducing liquid tangentially into said hollow interior of each of said tubes such that the liquid flows in a thin film in a spiral flow pattern around and along said inner surface of each of said tubes from said first ends to said second ends;a gas-liquid separator assembly in said outer vessel gas-liquid separator chamber including a plurality of target nozzles disposed in coaxial alignment with said seconds ends of said tubes and said orifices in said second seal means, each having a first end spaced relative to said orifices and configured and sized relative thereto to form an annular gas-liquid separator annulus that allows liquid to pass therethrough and redirects gas in a direction countercurrent to the direction of liquid flow above it;a gas exhaust assembly connected with said liquid feed assembly and including at least one gas duct having an interior connected in gas flow communication with said interior of said porous tubes for conducting redirected gas therefrom; anda liquid collection vessel having a first end connected with said outer vessel second end having an interior in fluid communication with said gas-liquid separator chamber and with said second ends of said tubes through said annular gas-liquid separator annulus to receive liquid passing through said annulus. 2. The apparatus according to claim 1, whereinsaid first seal means comprises a first disk-shaped tube sheet disposed in sealing relation between said first end of said outer vessel and said liquid feed assembly having a plurality of circumferentially spaced holes extending therethrough;said second seal means comprises a second disk-shaped tube sheet disposed within said outer vessel having an outer periphery engaged in sealing relation with an interior surface of said vessel side wall and having a plurality of circumferentially spaced holes extending therethrough; andsaid opposed first and second ends of each of said tubes have an exterior surface sealingly engaged in respective said holes in said first and second tube sheets, and an outer facing end of said holes provide an uninterrupted flow path coaxial with said interior of said tubes. 3. The apparatus according to claim 1, whereinsaid pressurized gas chamber of said outer vessel is divided into a plurality of segregated pressurized gas chambers each having a gas inlet for introducing gas therein, and each of said elongate tubes are disposed within a respective one of said pressurized gas chambers; wherebyeach of said elongate tubes may be individually supplied with gas at different pressures. 4. The apparatus according to claim 1, whereinat least one of said tubes has a hollow interior of a diameter different from the diameter of at least another one of said tubes. 5. The apparatus according to claim 1, whereinat least one of said tubes has a hollow interior that is tapered along its length between its said opposed first and second ends. 6. The apparatus according to claim 1, whereinat least one of said tubes has a microscopically porous side wall of different porosity from at least another one of said tubes. 7. The apparatus according to claim 1, whereinsaid liquid feed assembly and said gas exhaust assembly comprises a plurality of liquid inlet and gas exhaust nozzles, each having a nozzle housing with generally cylindrical side wall having a reduced diameter exhaust opening at a first end thereof and a larger interior diameter at a second end thereof with a rectangular liquid inlet nozzle aperture through said side wall tangential to its said interior diameter to establish tangential fluid flow of a thin film of incoming liquid; anda vortex finder disposed in said nozzle housing having a central bore through its center coaxial with said exhaust opening to provide a flow path for exhausting return gas, said central bore circumscribed by a generally cylindrical side wall positioned concentrically in said nozzle housing interior diameter in radially inward spaced relation thereto to establish vortex fluid flow of said thin film of incoming liquid, and said vortex finder side wall providing a physical separation between the incoming liquid and the return gas. 8. The apparatus according to claim 7, whereinsaid liquid injection nozzle aperture of said nozzles have a cross sectional area sized to produce a thin film of incoming liquid having a thickness in the range of from about 5% to about 28% of the inside diameter of said inner surface of said tubes. 9. The apparatus according to claim 7, further comprising:a cylindrical erosion resistant liner positioned concentrically in said interior diameter of said nozzle housing and having a cylindrical side wall surrounding an interior diameter with a rectangular liquid inlet aperture extending therethrough tangential to its said interior diameter and aligned in fluid communication with said liquid inlet nozzle aperture to receive liquid therefrom and establish tangential fluid flow of a thin film of the incoming liquid; andsaid liner interior diameter is spaced radially outward from said vortex finder side wall to establish vortex fluid flow of said thin film of incoming liquid. 10. The apparatus according to claim 7, further comprising:a generally dome shaped liquid feed and gas exhaust vessel having a first end connected in sealing relation with said outer vessel first end and an enclosed interior divided into a separate liquid chamber at said first end and a gas exhaust chamber at a second end by a divider plate having a central liquid inlet bore and a plurality of circumferentially spaced gas exhaust bores extending therethrough in radially spaced relation thereto;said liquid chamber surrounding said plurality of liquid inlet and gas exhaust nozzles, and each of said plurality of circumferentially spaced gas exhaust bores in said divider plate engaged in sealing relation with a respective said reduced diameter exhaust opening in a respective said nozzle housing; anda liquid inlet conduit having a first end exterior of said vessel extending in sealed relation through said gas exhaust chamber and having a second end connected in fluid communication with said central liquid inlet bore; whereinliquid is introduced through said liquid inlet conduit into said liquid chamber and fed simultaneously to the liquid inlet nozzle aperture in the side wall of the housing of said plurality of liquid inlet and gas exhaust nozzles, and return gas from each of said plurality of tubes is exhausted through each said central bore of said vortex finder, said exhaust bor e in said nozzle housing, and through respective said gas exhaust bores in said divider plate into said exhaust gas chamber. 11. The apparatus according to claim 10, further comprising:a conduit connected in fluid communication between the interior of said liquid collection vessel and the interior of said liquid feed and gas exhaust vessel to equalize gas pressure therebetween. 12. The apparatus according to claim 7, whereineach said nozzle housing has an outwardly extending liquid inlet conduit in fluid communication with said rectangular liquid inlet nozzle aperture; andliquid is introduced individually to at least one of said plurality of said liquid inlet and gas exhaust nozzles through said liquid inlet conduit and said liquid inlet nozzle aperture in the side wall of said nozzle housing, and return gas is exhausted through said central bore of said vortex finder and said exhaust bore in said nozzle housing; wherebyliquid may be introduced into selected ones of said tubes. 13. The apparatus according to claim 12, whereinliquid is introduced individually to each of said plurality of said liquid inlet and gas exhaust nozzles through said liquid inlet conduit and said liquid inlet nozzle aperture in the side wall of said nozzle housing, and return gas from each of said plurality of tubes is exhausted through each said central bore of said vortex finder and said exhaust bore in said nozzle housing; wherebyliquid may be introduced into each or groups of said tubes at different velocities. 14. The apparatus according to claim 13, whereinsaid pressurized gas chamber of said outer vessel is divided into a plurality of segregated pressurized gas chambers each having a gas inlet for introducing gas therein, and each of said elongate tubes are disposed within a respective one of said pressurized gas chambers; wherebygas at different pressures may be supplied individually to each or groups of said elongate tubes. 15. The apparatus according to claim 12, further comprising:a hollow cylindrical erosion resistant liner positioned concentrically within each said liquid inlet conduit. 16. The apparatus according to claim 1, further comprising:a second gas-liquid contactor assembly disposed between the first stated gas-liquid contactor section and said liquid feed section;said second gas-liquid contactor section including a second outer vessel having a central longitudinal axis circumscribed by a non-porous generally cylindrical side wall with a first end connected with said liquid feed section and a second end connected with said first end of the first stated gas liquid contactor section, at least one gas inlet for introducing gas into said second outer vessel, a second plurality of elongate tubes within said second outer vessel disposed in circumferential and radially spaced relation having longitudinal axes axially aligned with said longitudinal axes of the first stated plurality of tubes, each of said second tubes having a microscopically porous side wall with an inner surface surrounding a hollow interior and opposed first and second ends, third seal means engaged in sealing relation between said first and second outer vessel and around said first and second ends of said first and second plurality of tubes to form a second pressurized gas chamber surrounding said second plurality of tubes, said hollow interior of said first and second plurality of tubes being in open fluid communication through said third seal means; wherebygas at different pressures may be supplied individually to said first and said second plurality of tubes. 17. The apparatus according to claim 1, whereineach of said tubes has a microscopically porous side wall of sufficient porosity to produce up to about 50 psig differential gas pressure measured across the porous media. 18. The apparatus according to claim 1, whereinsaid microscopically porous side wall of each of said tubes contains a surface active catalytic material in proximity to its said inner surface. 19. The apparatus according to claim 1, whereinsaid inner surface of each of said tubes is surface treated to enhance fluid flow characteristics. 20. The apparatus according to claim 1, further comprising:gas baffle means in said pressurized chamber of said outer vessel to inhibit the incoming gas stream from impinging directly on the exterior surface of said tubes and facilitate even gas distribution along the exterior surfaces thereof. 21. The apparatus according to claim 1, further comprising:liquid motion baffle means in said liquid collection vessel to mitigate sloshing. 22. The apparatus according to claim 1, further comprising:heating means in said liquid collection vessel for heating liquid contained therein. 23. The apparatus according to claim 1, whereinsaid porous side wall of at least one of said tubes is connected with an electrical source to function as a resistance heating element. 24. The apparatus according to claim 1, further comprising:an ultraviolet emitting light source disposed inside and along the central axis of at least one of said porous tubes. 25. The apparatus according to claim 1, whereinsaid gas exhaust assembly contains a gas scrubber section near the exit of the gas after it has been in contact with the liquid to scrub out entrained liquid from the gas prior to exiting the vessel, and means for returning the scrubbed out liquid to said liquid collection vessel. 26. The apparatus according to claim 1, whereinsaid gas-liquid separator assembly includes sensor means for monitoring the gas-liquid flow pattern in said gas-liquid contactor section. 27. The apparatus according to claim 1, further comprising:filter means disposed between said gas inlet and said porous side wall of said tubes for filtering gas introduced into said outer vessel. 28. The apparatus according to claim 1, wherein said target nozzles of said gas-liquid separator assembly are spaced relative to said orifices and configured and sized relative thereto to form an annular gas-liquid separator annulus that allows liquid to pass therethrough and redirects gas in a direction countercurrent and co-current to the direction of liquid flow above allowing the gas to travel toward either of said first ends and second ends of each of said tubes. 29. The apparatus according to claim 1, whereinsaid liquid collection vessel has a liquid outlet connected in fluid communication with a said liquid inlet of a liquid feed assembly of a second apparatus as recited in claim 1 for introducing gas thereto; wherebya first and a second said apparatus are operated in series. 30. The apparatus according to claim 1, whereinsaid liquid inlet of said liquid feed assembly is connected in parallel with a said liquid inlet of a said liquid feed assembly of a second apparatus as recited in claim 1 and both are joined to a common liquid supply source; andsaid gas inlet of said gas-liquid contactor assembly is connected in parallel with a said gas inlet of a gas-liquid contactor assembly of a second apparatus as recited in claim 1 and both are joined to a common gas supply source; wherebya first and a second said apparatus are operated in parallel.