KR890016993A - Apparatus and method for removing water from hydrocarbon and halogenated hydrocarbon mixtures - Google Patents

Apparatus and method for removing water from hydrocarbon and halogenated hydrocarbon mixtures Download PDF

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KR890016993A
KR890016993A KR1019890006570A KR890006570A KR890016993A KR 890016993 A KR890016993 A KR 890016993A KR 1019890006570 A KR1019890006570 A KR 1019890006570A KR 890006570 A KR890006570 A KR 890006570A KR 890016993 A KR890016993 A KR 890016993A
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South Korea
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water
fiber
mixture
hydrocarbon
soluble substances
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KR1019890006570A
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Korean (ko)
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에이. 테일러 존
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에이. 테일러 존
세퍼레이션 다이나믹스, 인코포레이티드
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Priority claimed from US07/194,984 external-priority patent/US4857081A/en
Application filed by 에이. 테일러 존, 세퍼레이션 다이나믹스, 인코포레이티드 filed Critical 에이. 테일러 존
Publication of KR890016993A publication Critical patent/KR890016993A/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/36Pervaporation; Membrane distillation; Liquid permeation
    • B01D61/362Pervaporation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/08Thickening liquid suspensions by filtration
    • B01D17/085Thickening liquid suspensions by filtration with membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/22Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
    • B01D53/225Multiple stage diffusion
    • B01D53/227Multiple stage diffusion in parallel connexion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • B01D53/268Drying gases or vapours by diffusion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/04Hollow fibre modules comprising multiple hollow fibre assemblies
    • B01D63/046Hollow fibre modules comprising multiple hollow fibre assemblies in separate housings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/08Hollow fibre membranes
    • B01D69/081Hollow fibre membranes characterised by the fibre diameter
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/08Polysaccharides
    • B01D71/12Cellulose derivatives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2256/00Main component in the product gas stream after treatment
    • B01D2256/24Hydrocarbons
    • B01D2256/245Methane
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/50Specific extra tanks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/20Specific permeability or cut-off range

Abstract

내용 없음No content

Description

탄화수소 및 할로겐화탄화수소 혼합물로부터 물을 제거하는 장치 및 방법Apparatus and method for removing water from hydrocarbon and halogenated hydrocarbon mixtures

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

제 1 도는 본 발명에 따른 장치를 측면에서 본 단면도. 제 2 도는 본 발명에 따른 장치를 구성하는 하나의 섬유에 대한 부분적인 단면도. 제 3 도는 소제기류를 이송시키기 위하여 섬유 통로의 뚫린 단부를 형성하고 있는 섬유로서, 본 발명의 장치에 매립된 섬유에 대한 단부를 부분적으로 나타낸 사시도.1 is a cross-sectional side view of a device according to the invention. 2 is a partial cross-sectional view of one fiber constituting the device according to the invention. 3 is a perspective view partially showing the end of the fiber embedded in the device of the present invention, the fiber forming a perforated end of the fiber passageway for transporting the scavenging stream;

Claims (24)

공급지, 건조된 탄화수소 유체의 저장소, 내,외표면을 갖는 다수의 섬유 및 공급지로부터 탄화수소 유체를 섬유의 제 1 표면을 따라 접촉시켜 저장소로 이송시키는 수단으로 구성된 탄화수소 혼합물로부터 물과 수용성 물질을 제거하기 위한 장치에 있어서, 섬유는 자립형인 확산수단을 이루고, 비다공성 동암모늄 셀룰로오스 막은 연속된 표면을 이루고 있어서 탄화수소 혼합물로부터 물과 수용성 물질만이 확산되도록하고, 섬유의 길이를 따라 탄화수소 혼합물이 한번 통과하는 동안 탄화수소 혼합물로부터 최소한 95%의 물과 수용성 물질을 제거하는 확산활동을 갖는 물 제거수단을 포함하고 있는 장치.To remove water and water-soluble substances from a hydrocarbon mixture consisting of a feed source, a reservoir of dried hydrocarbon fluid, a plurality of fibers having an inner and outer surface, and means for contacting the hydrocarbon fluid along the first surface of the fiber to the reservoir from the feed source. For the apparatus, the fibers comprise freestanding diffusion means and the non-porous copper ammonium cellulose membrane forms a continuous surface such that only water and water-soluble materials diffuse from the hydrocarbon mixture, and the hydrocarbon mixture passes once along the length of the fiber. And water removal means having a diffusion activity to remove at least 95% of water and water-soluble substances from the hydrocarbon mixture. 제 1 항에 있어서, 각각의 섬유는 내,외표면 사이의 평균 두께가 9.5 내지 10.5 미크론을 이루고 있는 장치.The device of claim 1, wherein each fiber has an average thickness of between 9.5 and 10.5 microns between the inner and outer surfaces. 제 2 항에 있어서, 상기 물 제거수단은 섬유의 제 2 표면을 따라 흐르는 소제 기류를 포함하고 있는 장치.3. An apparatus according to claim 2, wherein said water removing means comprises a sweep stream of air flowing along the second surface of the fiber. 제 3 항에 있어서, 상기 제 1 표면은 섬유의 외표면을 이루고 상기 제 2 표면은 내표면을 이루고 있는 장치.4. The device of claim 3, wherein the first surface comprises an outer surface of the fiber and the second surface comprises an inner surface. 탄화수소 혼합물로부터 물과 수용성 물질을 제거하는 방법에 있어서, 다수의 중공체인 비다공성 동암모늄 셀룰로오스로 만들어진 섬유의 연속된 자립형 표면을 따라 탄화수소 혼합물이 직접 접촉되도록 이를 이송시키고, 탄화수소 유체가 섬유 표면과 접촉함에 따라 탄화수소 혼합물로부터 단지 물과 수용성 물질만을 확산에 의해서 섬유내부로 선택적으로 통과시키며, 탄화수소 혼합물로부터 물과 수용성 물질을 최소한 95% 제거하는 확산 활성을 갖는 섬유의 내부로 확산된 물과 수용성 물질을 제거한 단계로 이루어진 방법.A method of removing water and water-soluble substances from a hydrocarbon mixture, the hydrocarbon mixture is brought into direct contact along a continuous freestanding surface of a fiber made of a plurality of hollow nonporous ammonium cellulose, and the hydrocarbon fluid contacts the fiber surface. Thereby selectively passing only water and water-soluble substances from the hydrocarbon mixture into the fiber by diffusion, and water and water-soluble substances diffused into the fiber having a diffusion activity that removes at least 95% of water and water-soluble substances from the hydrocarbon mixture. The method consists of the steps removed. 제 5 항에 있어서, 물과 수용성 물질을 제거하는 수단은 탄화수소 혼합물의 흐름과 반대방향으로 소제기류를 통과시키는 방법.6. The method of claim 5, wherein the means for removing water and water-soluble substances is passed through the scrub stream in a direction opposite to that of the hydrocarbon mixture. 제 6 항에 있어서, 탄화수소 혼합물을 섬유의 외표면을 따라 이송시키고, 내표면을 따라 물과 수용성 물질을 제거하는 방법.The method of claim 6, wherein the hydrocarbon mixture is transferred along the outer surface of the fiber and water and water soluble substances are removed along the inner surface. 제 7 항에 있어서, 외표면으로부터 내표면까지의 9.5 내지 10.5 미크론되는 평균 두께를 가로질러 확산되는 물과 수용성 물질을 투과시키는 방법.8. The method of claim 7, wherein the water and water soluble material diffuses across an average thickness of 9.5 to 10.5 microns from the outer surface to the inner surface. 처음의 수분을 함유한 탄화수소 혼합물을 비다공성 섬유의 한쪽면과 접촉되도록 이송시켜서 탄화수소 혼합물로부터 물과 수용성 물질을 제거하는 방법에 있어서, 투막으로서 동암모늄 셀룰로오스 계통의 물질로 만들어진 자립형 섬유를 적용하고, 섬유의 내부로 가로질러 확산하는 물과 수용성 물질의 투막경도를 유지시키고, 섬유를 한번 통과하는 동안 탄화수소 혼합물로부터 물과 수용성 물질을 최소한 95% 제거하도록 확산시키는 단계로 이루어진 방법.A method of removing water and water-soluble substances from a hydrocarbon mixture by transferring the first water-containing hydrocarbon mixture into contact with one side of the non-porous fiber, applying a self-supporting fiber made of a copper ammonium cellulose-based material as a permeation membrane, Maintaining the diaphragm hardness of water and water soluble materials diffusing across the interior of the fiber and diffusing to remove at least 95% of the water and water soluble materials from the hydrocarbon mixture during one pass through the fiber. 중공체 섬유를 이용하여 수분을 함유한 탄화수소 기류를 건조시키는 방법에 있어서, 탄화수소는 통과시키지 않는 비다공성 중공체의 친수성 동암모늄으로 재생된 셀룰로오스 섬유를 설치하고, 수분을 함유한 탄화수소 기류를 섬유의 외표면과 접촉하도록 하여 기류에 있는 수증기는 섬유에 의해서 흡수되어 섬유통로로 확산시키고, 섬유를 통과한 물을 제거하기 위하여 섬유통로를 통하여 소재 기류를 통과시켜서 섬유로부터 건조기체를 제거하는 단계로 이루어진 방법.In the method of drying a water-containing hydrocarbon stream using hollow fiber, a cellulose fiber regenerated from hydrophilic copper ammonium of a non-porous hollow body which does not pass hydrocarbon is provided, and the water-containing hydrocarbon stream is Water vapor in the air stream is brought into contact with the outer surface to be absorbed by the fiber and diffused into the fiber path, and a dry material is removed from the fiber by passing a material air stream through the fiber path to remove water passing through the fiber. Way. 제10항에 있어서, 소재 기류를 수분을 함유한 기체와 반대방향으로 이동시키는 방법.The method of claim 10 wherein the material air stream is moved in a direction opposite to the water-containing gas. 제11항에 있어서, 섬유는 동암모늄 셀룰로오스로 이루어지고 수분을 함유한 기체는 주로 메탄으로 구성된 방법.The method of claim 11, wherein the fibers consist of copper ammonium cellulose and the water-containing gas consists primarily of methane. 제12항에 있어서, 물에 대한 섬유막의 투과성은 20ml/hr.mmHg.m2이상이 되도록 한 방법.The method of claim 12, wherein the permeability of the fiber membrane to water is at least 20 ml / hr.mmHg.m 2 . 중공체 섬유를 사용하여 탄화수소의 습한 기류를 건조시키는 방법에 있어서, 동암모늄 셀룰로오스로 만들어진 비다공성의 자립형 중공체 섬유를 적용하고, 습한 탄화수소 기류를 섬유의 외표면에 접촉되도록 이송시켜서 기류를 함유된 수분이 흡수되어 섬유통로로 확산시키며, 섬유통로로 흡수된 물을 제거하고, 건조된 기체를 분리하는 단계로 이루어진 방법.In a method of drying a wet air stream of hydrocarbons using hollow fiber, a non-porous, self-supporting hollow fiber made of copper ammonium cellulose is applied, and the wet hydrocarbon air stream is brought into contact with the outer surface of the fiber to contain the air stream. Absorbing moisture to diffuse into the fiber passage, removing the water absorbed into the fiber passage, and separating the dried gas. 제14항에 있어서, 섬유를 구성하는 물질은 물에 대하여 20ml/hr.mmHg.m2이상의 투과성을 갖도록 하는 방법.The method of claim 14, wherein the material constituting the fibers has a permeability of at least 20 ml / hr.mmHg.m 2 with respect to water. 제15항에 있어서, 습한 기류가 대체로 메탄으로 이루어진 방법.16. The method of claim 15, wherein the humid air stream is generally comprised of methane. 물과 탄화수소 또는 할로겐화 탄화수소 혼합물로부터 물을 분리하는 장치에 있어서, 동암모늄 셀룰로오스로 만들어진 비다공성의 자립형 중공체의 내외표면을 가진 섬유로 이루어진 격막을 포함하고 있는 분리수단; 탄화수소나 할로겐화탄화수소 및 물의 혼합물을 상기 섬유의 한면과 접촉되도록 하여 섬유의 다른면으로 물을 흡수 확산시키도록 혼합물을 이송시키는 제 1 도관; 섬유의 다른면으로부터 물을 제거하는 제거수단으로 이루어진 장치.An apparatus for separating water from a mixture of water and hydrocarbons or halogenated hydrocarbons, the apparatus comprising: separating means including a diaphragm comprising fibers with inner and outer surfaces of a nonporous, self-supporting hollow body made of copper ammonium cellulose; A first conduit for bringing a mixture of hydrocarbons or halogenated hydrocarbons and water into contact with one side of the fiber to direct absorption of the diffusion of water to the other side of the fiber; A device comprising removal means for removing water from the other side of the fiber. 제17항에 있어서, 상기 제거수단은 종력에 의해서 섬유의 다른면으로부터 물을 제거하기 위한 제 2 도관을 포함하고 있는 장치.18. The apparatus of claim 17, wherein the removal means comprises a second conduit for removing water from the other side of the fiber by the end force. 제18항에 있어서, 상기 분리수단은 혼합물을 취하는 섬유의 한쪽면과 통하는 혼합물 유입구와 섬유의 다른면과 제 2 도관 살이의 유체통로에 잇는 물 유출구 및 섬유의 첫번째 면과 통하고 하우징으로부터 혼합물을 빼내기위해 혼합물 유입구와는 이격된 혼합물 유출구를 포함하고 있으며, 혼합물 유입구로 혼합물을 재순환시키고 상기 섬유의 첫번째 면을 통과함에 따라 물을 제거함으로서 계속 혼합물의 농도를 증가시키는 재순환수단을 포함하고 있는 장치.19. The method of claim 18, wherein the separating means communicates the mixture from the housing and communicates with the first inlet of the fiber and the water inlet connected to a mixture inlet to one side of the fiber taking the mixture and to a fluid passageway between the other side of the fiber and the second conduit. And a recirculation means comprising a mixture outlet separate from the mixture inlet for withdrawal and continuing to increase the concentration of the mixture by recycling the mixture to the mixture inlet and removing water as it passes through the first side of the fiber. 제19항에 있어서, 상기 재순환수단은 혼합물을 재순환시키기 위한 저장수단을 포함하며, 이 저장수단은 이곳으로 부가적인 혼합물을 주입시키기 위한 유입구 및 부가된 혼합물의 양을 선택적으로 조절하는 밸브수단을 포함하고 있는 장치.20. The apparatus of claim 19, wherein the recirculation means comprises a storage means for recycling the mixture, the storage means comprising an inlet for injecting additional mixture therein and valve means for selectively adjusting the amount of the added mixture. Device. 물과 탄화수소 또는 할로겐화 탄화수소 혼합물로부터 물을 분리하는 방법에 있어서, 이 혼합물을 내외표면을 갖고 동암모늄 셀룰로오스로 이루어진 비다공성 자립형의 중공체 섬유로 구성된 섬유다발의 한면과 접촉되도록 통과시키고, 혼합물로부터 물을 섬유에 흡수시켜서 섬유의 반대편으로 물을 확산시키며, 섬유의 다른면으로부터 물을 제거하고, 섬유의 처음면으로부터 남아 있는 혼합물을 제거하는 단계로 이루어진 방법.In a method for separating water from a mixture of water and a hydrocarbon or halogenated hydrocarbon, the mixture is passed through contact with one side of a fiber bundle composed of nonporous, self-supporting hollow fiber composed of copper ammonium cellulose, having an inner and outer surface, and water from the mixture. Absorbing the fibers to diffuse water to the opposite side of the fibers, removing water from the other side of the fiber, and removing the remaining mixture from the initial side of the fiber. 제21항에 있어서, 물을 제거하는 단계를 중력에 의하는 방법.The method of claim 21, wherein removing water is by gravity. 제22항에 있어서, 섬유의 처음면으로부터 제거된 혼합물을 다시 처음면으로 재순환시키고, 섬유를 통과함에 따라 물을 제거시킴으로써 혼합물의 농도를 통과시키는 단계를 포함하고 있는 방법.23. The method of claim 22 including passing the concentration of the mixture by recycling the mixture removed from the initial side of the fiber back to the initial side and removing the water as it passes through the fiber. 제23항에 있어서, 재순환 단계는 섬유의 두번째 면으로부터 제거된 혼합물을 저장하며 선택적으로 부가되는 혼합물과 저장된 혼합물을 혼합시키고, 선택적으로 섬유의 처음면으로 저장된 혼합물을 이송시키는 방법.The method of claim 23, wherein the recycling step stores the mixture removed from the second side of the fiber, optionally mixes the added mixture with the stored mixture, and optionally transfers the stored mixture to the first side of the fiber. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019890006570A 1988-05-17 1989-05-17 Apparatus and method for removing water from hydrocarbon and halogenated hydrocarbon mixtures KR890016993A (en)

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