Hollow fiber apparatus and use thereof for fluids separations and heat and mass transfers
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
B01D-053/22
F28D-015/00
F28F-001/00
B01D-001/22
B64D-037/32
F28F-021/06
F28D-007/16
B01D-063/02
F28F-009/02
F28D-007/02
F28D-021/00
출원번호
US-0492757
(2012-06-08)
등록번호
US-9623369
(2017-04-18)
발명자
/ 주소
Bikson, Benjamin
Etter, Stephen
Ching, Nathaniel
출원인 / 주소
POROGEN CORPORATION
대리인 / 주소
Cronin, Christopher J.
인용정보
피인용 횟수 :
0인용 특허 :
36
초록▼
A hollow fiber fluid separation device includes a hollow fiber cartridge, comprising a plurality of hollow fiber membranes arranged around a central tubular core, a first tubesheet and a second tubesheet encapsulating respective distal ends of the hollow fiber bundle. The tubesheets have boreholes i
A hollow fiber fluid separation device includes a hollow fiber cartridge, comprising a plurality of hollow fiber membranes arranged around a central tubular core, a first tubesheet and a second tubesheet encapsulating respective distal ends of the hollow fiber bundle. The tubesheets have boreholes in fluid communication with bores of the hollow fiber membrane. In at least one of the tubesheets, the boreholes are formed radially and are in communication with the central tubular core. The hollow fiber fluid separation device can be utilized in liquid separation applications such as ultrafiltration and in gas separation processes such as air separation. The design disclosed herein is light weight and compact and is particularly advantageous at high operating temperatures when the pressure of the feed fluid introduced into the bores of hollow fibers is higher than the pressure on the shell side of the device.
대표청구항▼
1. A fluid separation apparatus comprising: a) a cartridge including a hollow fiber membrane bundle, comprising a plurality of hollow fibers arranged around a substantially tubular core member, a first tubesheet and a second tubesheet encapsulating respective distal ends of the hollow fiber bundle,
1. A fluid separation apparatus comprising: a) a cartridge including a hollow fiber membrane bundle, comprising a plurality of hollow fibers arranged around a substantially tubular core member, a first tubesheet and a second tubesheet encapsulating respective distal ends of the hollow fiber bundle, said tubesheets having, respectively, first boreholes formed radially in the first tubesheet and second boreholes formed radially in the second tubesheet, wherein the first boreholes and the second boreholes are in fluid communication with bores of the hollow fiber membranes;b) a housing surrounding the cartridge, wherein the housing has: i. a first port for introducing a feed fluid, the first port being in fluid communication with the first boreholes;ii. a second port for removal of non-permeate portion of the feed fluid, the second port being in fluid communication with the second boreholes; andiii. a third port for removal of permeate fluid from a shell side of hollow fiber membranes,wherein at least one of the first boreholes or at least one of the second boreholes is directly connected by perforations with an interior of the substantially tubular core member. 2. The apparatus of claim 1 wherein the feed fluid is a gas mixture. 3. The apparatus of claim 2 wherein the gas mixture is compressed air. 4. The apparatus of claim 1, wherein the hollow fiber membranes are asymmetric or composite. 5. The apparatus of claim 3, wherein compressed air is separated into nitrogen enriched for the non-permeated portion and oxygen enriched for the permeate fluid. 6. The apparatus of claim 5, wherein the apparatus generates the nitrogen enriched air on board aircraft. 7. The apparatus of claim 1, wherein the core member is hollow and has one or more openings formed in a wall thereof to provide a fluid communication conduit. 8. The apparatus of claim 1 wherein the hollow fibers are arranged around said core member by helical winding. 9. The apparatus of claim 8, wherein the hollow fibers are deposited at a wind angle within the range of from about 5° to about 6020 . 10. The apparatus of claim 8 wherein the hollow fibers are wound at a lower wind angle in a section of the bundle being encapsulated by the terminal tubesheets, as compared to the wind angle of hollow fibers in a section of the bundle disposed between the terminal tubesheets. 11. The apparatus of claim 1, wherein the first boreholes or the second boreholes are cylindrical, elliptical or oval. 12. The apparatus of claim 11, wherein the first boreholes or the second boreholes are formed at an angle to the surface of the tubesheet. 13. The apparatus of claim 1, wherein the flow direction of the permeate fluid is substantially axial and counter-current to the flow direction of the fluid in the hollow fiber bores. 14. An aircraft comprising the apparatus of claim 1. 15. The apparatus of claim 1, wherein: said first tubesheet is provided with a first pair of aligned circumferential grooves adapted and configured to receive a first pair of O-ring seals;a diameter of said first tubesheet is reduced in a portion of said first tubesheet in between the grooves of said first pair in comparison to remaining portions of said first tubesheet; andsaid first boreholes emerge at a surface of said first tubesheet in the reduced diameter portion of said first tubesheet. 16. The apparatus of claim 15, wherein: said second tubesheet is provided with a first pair of aligned circumferential grooves adapted and configured to receive a second pair of O-ring seals;a diameter of said second tubesheet is reduced in a portion of said second tubesheet in between the grooves of said second pair in comparison to remaining portions of said second tubesheet; andsaid second boreholes emerge at a surface of said second tubesheet in the reduced diameter portion of said second tubesheet. 17. The apparatus of claim 1, wherein said first boreholes comprise a plurality of aligned rows of boreholes. 18. The apparatus of claim 17, wherein said second boreholes comprise a plurality of aligned rows of boreholes. 19. The apparatus of claim 1, wherein diameters of said first boreholes are wider closer to an exterior of said first tubesheet and narrower closer to an interior of said first tubesheet. 20. The apparatus of claim 1, wherein diameters of said second boreholes are wider closer to an exterior of said second tubesheet and narrower closer to an interior of said second tubesheet. 21. A hollow fiber device comprising: a hollow fiber bundle formed around a central substantially tubular core member, including a plurality of hollow fiber membranes, a first tubesheet and a second tubesheet encapsulating respective distal ends of the hollow fiber bundle, the first tubesheet and the second tubesheet having, respectively, first boreholes formed radially in the first tubesheet and second boreholes formed radially in the second tubesheet, wherein the first and the second boreholes are in fluid communication with bores of the hollow fiber membranes, and wherein at least one of the first boreholes or the second boreholes is directly connected by perforations with a hollow interior of the central substantially tubular core member. 22. A process for gas separation, the process comprising: a) directing a feed gas mixture to a bore side of a hollow fiber bundle that contains a plurality of hollow fiber membranes arranged around a core member, wherein the feed gas mixture is introduced through the core member, the core member being directly connected by perforations to first boreholes formed radially in a first tubesheet at a first end of the hollow fiber bundle, said first boreholes being in fluid communication with bores of the hollow fiber membranes;b) separating more permeable components of the feed gas by permeation through the hollow fiber membranes;c) recovering a fraction of less permeable gas components from the core member, the core member being directly connected by perforations to second boreholes formed radially in the second tubesheet at a second end of the hollow fiber bundle, said second boreholes being in fluid communication with bores of the hollow fibers; andd) recovering a fraction of more permeable components of the feed gas from a shell side of the hollow fiber bundle. 23. The process of claim 22, wherein the gas separation process is air separation process. 24. The process of claim 23, wherein a non-permeate gas is nitrogen enriched air and a permeate gas is oxygen enriched air. 25. The process of claim 24, wherein the nitrogen enriched air is directed into fuel tank on board aircraft.
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