Apparatus for creating gas-liquid interfacial contact conditions for highly efficient mass transfer

Claim 2

Apparatus for creating gas-liquid interfacial contact conditions for efficient mass transfer, comprising a gas-liquid contactor assembly with a first end and a second end and a longitudinal axis, including at least one coaxially aligned cylindrical porous tube with a first end and a second end, a longitudinal axis, an outer surface and an inner surface, and a hollow interior, said at least one porous tube being penetrated by a multiplicity of pores extending from said outer surface to said inner surface, each of said pores providing a passageway for the flow of gas therethrough to said interior of said at least one porous tube, and further including at least one nonporous outer jacket disposed concentric with said at least one porous tube and interconnected thereto so as to form at least one closed gas plenum, said at least one outer jacket having at least one gas inlet port disposed therein for introduction of gas to said at least one closed gas plenum formed thereby; liquid feeding means for feeding liquid to the interior of said at least one porous tube at said first end of said gas-liquid contactor assembly in a spiral flow pattern around and along said inner surface of said at least one porous tube from said first end to said second end of said gas-liquid contactor assembly; and a gas-liquid separator assembly including a nonporous cylindrical degassing tube, having a first end of the same inside diameter as said second end of said at least one porous tube at said second end of said gas-liquid contactor assembly, and a second end, disposed in coaxial alignment with said gas-liquid contactor assembly with said first end of said degassing tube connected to said second end of said porous tube at said second end of said gas-liquid contactor assembly so as to provide an uninterrupted flow path from said porous tube to and through said degassing tube, and including a gas outlet port with a first end and a second end, disposed in coaxial alignment with said gas-liquid contactor assembly and said degassing tube so as to provide a flow path for gas from said degassing tube into said gas outlet port.

Claim 3

The apparatus of claim 1, wherein said liquid feeding means comprises a liquid feed assembly including a nonporous extension tube of the same cross-sectional dimension and configuration as said at least one porous tube, having a first end and a second end, disposed in coaxial alignment with and interconnected at said second end thereof to said first end of said porous tube at said first end of said gas-liquid contactor assembly, said extension tube having a wall, an outer surface and an inner surface, and a hollow interior, and said extension tube further having a slot shaped aperture extending through said wall thereof for introduction of liquid therethrough, and further including a feed head having an inlet nipple and a slotted nozzle connected between said inlet nipple and said extension tube in communication with said slot shaped aperture.

Claim 4

The apparatus of claim 2, wherein said feed head of said liquid feed assembly further includes an acceleration chamber connected between said inlet nipple and said slotted nozzle, said acceleration chamber narrowing in cross-sectional area from said inlet nipple to said slotted nozzle so as to increase the velocity of liquid flowing therethrough.

Claim 5

The apparatus of claim 3, wherein said slotted nozzle is disposed relative to said extension tube such that liquid flowing from said slotted nozzle into said interior of said extension tube through said slot shaped aperture enters said extension tube tangential to the curvature of said inner surface thereof and at an angle relative to a plane perpendicular to the aligned longitudinal axes of said extension tube and said porous tube.

Claim 6

The apparatus of claim 4, wherein said feed head of said liquid feed assembly further includes a flow defining means for directing the flow of liquid in a spiral pattern around and along said inner surface of said extension tube toward said porous tube.

Claim 7

The apparatus of claim 5, wherein said flow defining means comprises a flow definer including a helical ramp to receive and direct the flow of liquid from said slotted nozzle, said helical ramp having a surface, an upstream edge, and a downstream edge, and further including a ledge extending from said surface and along said upstream edge of said helical ramp to maintain the flow of liquid along said surface of said helical ramp.

Claim 8

The apparatus of claim 1, wherein said gas outlet port has a side wall, and wherein said side wall of said gas outlet port narrows in proximity to said first end thereof to form a knife edge at said first end thereof.

Claim 9

The apparatus of claim 7, wherein said degassing tube increases in inside diameter adjacent to said second end thereof, and wherein the angle through which said side wall of said gas outlet port narrows is approximately equal to the angle through which said inside diameter of said degassing tube increases.

Claim 10

The apparatus of claim 1, wherein the inside diameter of said degassing tube is constant from said first end thereof to said second end thereof.

Claim 11

The apparatus of claim 8, wherein the inside diameter of said gas outlet port is approximately 80% of the inside diameter of said porous tube.

Claim 12

The apparatus of claim 1, wherein said degassing tube decreases in inside diameter adjacent to said second end thereof.

Claim 13

The apparatus of claim 11, wherein the inside diameter of said gas outlet port is approximately 1/3 of the inside diameter of said porous tube.

Claim 14

The apparatus of claim 1, wherein said porous tube at said first end of said gas-liquid contactor assembly is open at said first end thereof and wherein the apparatus further includes a gas outlet duct disposed in coaxial alignment with said porous tube and interconnected to said first end thereof to receive gas from the interior of said porous tube through said first end thereof.

Claim 15

The apparatus of claim 13, wherein the inside diameter of said gas outlet port is approximately 1/6 of the inside diameter of said porous tube, and wherein the inside diameter of said gas outlet duct is approximately 1/6 of the inside diameter of said porous tube.

Claim 16

The apparatus of claim 1, further comprising a liquid collection assembly to receive liquid flowing from said second end of said degassing tube, including a liquid vessel with a hollow interior in liquid flow communication with said second end of said degassing tube.

Claim 17

The apparatus of claim 1, further comprising a gas discharge assembly to receive gas flowing from said second end of said gas outlet port, including a gas vessel with a hollow interior in gas flow communication with said second end of said gas outlet port.

Claim 18

The apparatus of claim 13, further comprising a liquid collection assembly to receive liquid from said gas-liquid contactor assembly, a first gas discharge assembly to receive gas flowing from said second end of said gas outlet port, including a first gas vessel with a hollow interior in gas flow communication with said second end of said gas outlet port, and a second gas discharge assembly to receive gas flowing from said interior of said porous tube through said gas outlet duct, including a second gas vessel with a hollow interior in gas flow communication with said gas outlet duct.

Claim 19

The apparatus of claim 17, wherein said liquid collection assembly, said first gas vessel, and said second gas vessel are interconnected in gas flow communication, so as to equalize pressure therein.

Claim 20

The apparatus of claim 1, wherein said gas-liquid contactor assembly is disposed with said longitudinal axis thereof generally perpendicular to the earth's gravitational field.

Claim 21

The apparatus of claim 1, wherein the number of said gas inlet ports is greater than one.

Claim 22

The apparatus of claim 20, wherein the number of said closed gas plenums formed by said at least one outer jacket is greater than one and wherein at least one gas inlet port is provided for introduction of gas to each of said closed gas plenums.

Claim 23

The apparatus of claim 1, wherein the cross-sectional dimension of said pores penetrating said at least one porous tube is within the range of about 0.5 micron to about 40 microns.

Claim 24

The apparatus of claim 1, wherein the cross-sectional dimension of said pores penetrating said at least one porous tube is within the range of about 0.5 micron to about 20 microns.

Claim 25

The apparatus of claim 1, wherein the cross-sectional dimension of said pores penetrating said at least one porous tube is within the range of about 0.5 micron to about 10 microns.

Claim 26

The apparatus of claim 1, wherein the number of said porous tubes is greater than one, with said porous tubes smoothly mated and interconnected end to end in coaxial alignment, the number of said outer jackets is equal to the number of said porous tubes, with each of said jacket sections connected around a respective one of said porous tubes in end to end in coaxial alignment to form a closed gas plenum associated with each of said porous tubes.

Claim 27

The apparatus of claim 2, wherein said extension tube has a curved inner surface, and wherein said slotted nozzle is disposed relative to said slot shaped aperture in said extension tube such that liquid flowing through said slotted nozzle and through said slot shaped aperture enters said extension tube tangential to the curvature of said inner surface of said extension tube.

Claim 28

The apparatus of claim 26, wherein said slot shaped aperture and said slotted nozzle are disposed relative to said extension tube such that the flow path followed by liquid entering said extension tube deviates at an angle from perpendicular to the aligned longitudinal axes of said extension tube and said porous tube, whereby the liquid flows in a film around said inner surfaces of said extension tube and said porous tube in a spiral flow path toward said second end of said gas-liquid contactor assembly.

Claim 29

The apparatus of claim 27, wherein the angle of deviation of said flow path of liquid entering said extension tube from perpendicular to the aligned longitudinal axes of said extension tube and said porous tube is such that the liquid flows around said inner surface of said at least one porous tube up to about 50 times between said first end and said second end of said gas-liquid contactor assembly.

Claim 30

The apparatus of claim 27, wherein the angle of deviation of said flow path of liquid entering said extension tube from perpendicular to the aligned longitudinal axes of said extension tube and said porous tube is such that the liquid flows around said inner surface of said at least one porous tube between about 10 and about 50 times between said first end and said second end of said gas-liquid contactor assembly.

Claim 31

The apparatus of claim 27, wherein the angle of deviation of said flow path of liquid entering said extension tube from perpendicular to the aligned longitudinal axes of said extension tube and said porous tube is such that the liquid flows around said inner surface of said at least one porous tube between about 10 and about 40 times between said first end and said second end of said gas-liquid contactor assembly.

Claim 32

Apparatus for creating gas-liquid interfacial contact conditions for efficient mass transfer, comprising a gas-liquid contactor assembly with a first end and a second end and a longitudinal axis, including at least one coaxially aligned cylindrical porous tube with a first end and a second end, a longitudinal axis, an outer surface and an inner surface, and a hollow interior chamber, said at least one porous tube being penetrated by a multiplicity of pores extending from said outer surface to said inner surface, and further including at least one nonporous outer jacket disposed concentric with said at least one porous tube and interconnected thereto so as to form at least one closed gas plenum, said at least one outer jacket having at least one gas inlet port disposed therein for introduction of gas to said at least one closed gas plenum formed thereby; a liquid feed assembly including a nonporous extension tube of the same cross-sectional dimension and configuration as said at least one porous tube, disposed in coaxial alignment with and interconnected to said first end of said porous tube at said first end of said gas-liquid contactor assembly, said extension tube having a slot shaped aperture therein for introduction of liquid therethrough, and further including a feed head having an inlet nipple and a slotted nozzle connected between said inlet nipple and said extension tube in communication with said slot shaped aperture, for feeding liquid to the interior of said extension tube and said porous tube in a spiral flow pattern around and along said inner surface of said at least one porous tube; a gas-liquid separator assembly including a nonporous cylindrical degassing tube, having a first end of the same inside diameter and configuration as said second end of said porous tube at said second end of said gas-liquid contactor assembly, and a second end, disposed in coaxial alignment with said gas-liquid contactor assembly with said first end of said degassing tube connected to said second end of said porous tube at said second end of said gas-liquid contactor assembly so as to provide an uninterrupted flow path from said porous tube to and through said degassing tube, and further including a cylindrical gas outlet port with a first end and a second end, disposed in coaxial alignment with said gas-liquid contactor assembly and said degassing tube, said gas outlet port having a continuous side wall with an outer surface and an inner surface, with an outside diameter less than the inside diameters of said at least one porous tube and said degassing tube, with said side wall of said gas outlet port narrowing in proximity to said first end thereof to form a knife edge at said first end thereof, said gas outlet port being disposed with said first end thereof in proximity to said second end of said degassing tube; a liquid collection assembly to receive liquid flowing from said second end of said degassing tube, including a liquid vessel with a hollow interior in liquid flow communication with said second end of said degassing tube; a first gas discharge assembly to receive gas flowing from said second end of said gas outlet port, including a first gas vessel with a hollow interior in gas flow communication with said second end of said gas outlet port; and a second gas discharge assembly to receive gas flowing from said first end of said porous tube at said first end of said gas-liquid contactor assembly, including a gas outlet duct in gas flow communication with said interior chamber of said porous tube through said first end thereof, and a second gas vessel with a hollow interior in gas flow communication with said gas outlet duct.

Claim 33

Apparatus for creating gas-liquid interfacial contact conditions for efficient mass transfer, comprising a gas-liquid contactor assembly with a first end and a second end and a longitudinal axis, including at least one coaxially aligned cylindrical porous tube with a first end and a second end, a longitudinal axis, an outer surface and an inner surface, and a hollow interior chamber, said at least one porous tube being penetrated by a multiplicity of pores extending from said outer surface to said inner surface, and further including at least one nonporous outer jacket disposed concentric with said at least one porous tube and interconnected thereto so as to form at least one closed gas plenum, said at least one outer jacket having at least one gas inlet port disposed therein for introduction of gas to said at least one closed gas plenum formed thereby; a liquid feed assembly including a nonporous extension tube of the same cross-sectional dimension and configuration as said at least one porous tube, disposed in coaxial alignment with and interconnected to said first end of said porous tube at said first end of said gas-liquid contactor assembly, said extension tube having a slot shaped aperture therein for introduction of liquid therethrough, and further including a feed head having an inlet nipple and a slotted nozzle connected between said inlet nipple and said extension tube in communication with said slot shaped aperture, for feeding liquid to the interior of said extension tube and said porous tube in a spiral flow pattern around and along said inner surface of said at least one porous tube; a gas-liquid separator assembly including a nonporous cylindrical degassing tube, having a first end of the same inside diameter and configuration as said second end of said porous tube at said second end of said gas-liquid contactor assembly, and a second end, disposed in coaxial alignment with said gas-liquid contactor assembly with said first end of said degassing tube connected to said second end of said porous tube at said second end of said gas-liquid contactor assembly so as to provide an uninterrupted flow path from said porous tube to and through said degassing tube, and further including a cylindrical gas outlet port with a first end and a second end, disposed in coaxial alignment with said gas-liquid contactor assembly and said degassing tube, said gas outlet port having a continuous side wall with an outer surface and an inner surface, with an outside diameter less than the inside diameters of said at least one porous tube and said degassing tube, with said side wall of said gas outlet port narrowing in proximity to said first end thereof to form a knife edge at said first end thereof, said gas outlet port being disposed with said first end thereof in proximity to said second end of said degassing tube; a liquid collection assembly to receive liquid flowing from said second end of said degassing tube, including a liquid vessel with a hollow interior in liquid flow communication with said second end of said degassing tube; a first gas discharge assembly to receive gas flowing from said second end of said gas outlet port, including a first gas vessel with a hollow interior in gas flow communication with said second end of said gas outlet port; and a second gas discharge assembly to receive gas flowing from said first end of said porous tube at said first end of said gas-liquid contactor assembly, including a gas outlet duct in gas flow communication with said interior chamber of said porous tube through said first end thereof, and a second gas vessel with a hollow interior in gas flow communication with said gas outlet duct.

Claim 34

The apparatus of claim 31, wherein the inside diameter of said gas outlet port is approximately 1/6 of the inside diameter of said at least one porous tube, and wherein the inside diameter of said gas outlet duct is approximately 1/6 of the inside diameter of said at least one porous tube.

Claim 35

The apparatus of claim 31, wherein the sum of the inside diameter of said gas outlet port and the inside diameter of said gas outlet duct is approximately 1/3 of the inside diameter of said at least one porous tube.

Claim 36

The apparatus of claim 31, wherein the number of said gas inlet ports is greater than one.

Claim 37

The apparatus of claim 34, wherein the number of said closed gas plenums formed by said at least one outer jacket is greater than one and wherein at least one gas inlet port is provided for introduction of gas to each of said closed gas plenums.

Claim 38

The apparatus of claim 35, wherein the number of said porous tubes is equal to the number of said closed gas plenums.

Claim 39

The apparatus of claim 31, wherein the cross-sectional dimension of said pores penetrating said at least one porous tube is within the range of about 0.5 micron to about 40 microns.

Claim 40

The apparatus of claim 31, wherein the cross-sectional dimension of said pores penetrating said at least one porous tube is within the range of about 0.5 micron to about 20 microns.

Claim 41

The apparatus of claim 31, wherein the cross-sectional dimension of said pores penetrating said at least one porous tube is within the range of about 0.5 micron to about 10 microns.

Claim 42

The apparatus of claim 31, wherein said degassing tube is of constant inside diameter from said first end thereof to said second end thereof.

Claim 43

The apparatus of claim 31, wherein said degassing tube decreases in inside diameter from said first end thereof to said second end thereof.

Claim 44

The apparatus of claim 31, wherein said degassing tube increases in inside diameter from said first end thereof to said second end thereof.

Claim 45

The apparatus of claim 31, wherein said liquid vessel, said first gas vessel, and said second gas vessel are interconnected in gas flow communication so as to equalize pressure thereamong.

Claim 46

The apparatus of claim 31, further comprising a pressure equalizing means for the purpose of equalizing the internal pressures in said liquid vessel, said first gas vessel, and said second gas vessel.

Claim 47

The apparatus of claim 44, wherein said pressure equalizing means includes a first conduit connected between said first gas vessel and said second gas vessel, and a second conduit connected between said first conduit and said liquid vessel.