ES2096031T3 - Modulos de membrana de liquido con minimo espesor efectivo de membrana y procedimiento para fabricar los mismos. - Google Patents

Modulos de membrana de liquido con minimo espesor efectivo de membrana y procedimiento para fabricar los mismos.

Info

Publication number
ES2096031T3
ES2096031T3 ES92303501T ES92303501T ES2096031T3 ES 2096031 T3 ES2096031 T3 ES 2096031T3 ES 92303501 T ES92303501 T ES 92303501T ES 92303501 T ES92303501 T ES 92303501T ES 2096031 T3 ES2096031 T3 ES 2096031T3
Authority
ES
Spain
Prior art keywords
membrane
modules
liquid
membranes
minimum effective
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
ES92303501T
Other languages
English (en)
Inventor
Ravi Prasad
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CNA Holdings LLC
Original Assignee
Hoechst Celanese Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hoechst Celanese Corp filed Critical Hoechst Celanese Corp
Application granted granted Critical
Publication of ES2096031T3 publication Critical patent/ES2096031T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02—Hollow fibre modules
    • B01D63/04—Hollow fibre modules comprising multiple hollow fibre assemblies
    • B01D63/043—Hollow fibre modules comprising multiple hollow fibre assemblies with separate tube sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/22—Separation 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/38—Liquid-membrane separation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02—Hollow fibre modules
    • B01D63/021—Manufacturing thereof
    • B01D63/0233—Manufacturing thereof forming the bundle
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02—Hollow fibre modules
    • B01D63/026—Wafer type modules or flat-surface type modules
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02—Hollow fibre modules
    • B01D63/027—Twinned or braided type modules
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
    • B01D2313/21—Specific headers, end caps

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Manufacturing & Machinery (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • External Artificial Organs (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

MODULOS PARA UTILIZACION EN SEPARACIONES LIQUIDAS, ESPECIALMENTE EN SEPARACIONES DE MEMBRANA DE CONTENIDO LIQUIDO, MUESTRAN ESPESOR DE MEMBRANA EFECTIVA MINIMA. LOS MODULOS [10] TIENEN UNA CAPA MODULAR [C], Y AL MENOS UN PAR DE LAMINAS DE TEJIDO SUPERPUESTAS [12, 14] EN EL INTERIOR DE LA CAPA [C], ESTANDO LAS LAMINAS DE TEJIDO ONDULADAS Y ANIDADAS EN LA DIRECCION LONGITUDINAL DE LA CAPA. CADA LAMINA DE TEJIDO [12, 14] CONTIENE MEMBRANAS DE FIBRA HUECA DE EXTENSION EN FORMA DE URDIMBRE [FF'' FS]. LAS MEMBRANAS DE FIBRA HUECA [FF] EN EL INTERIOR DE LOS PLIEGUES DE UNA LAMINA DE TEJIDO [12] FORMARAN POR TANTO FILAS ALTERNAS CON LAS MEMBRANAS DE TEJIDOS HUECOS [FS] EN EL INTERIOR DE LOS PLIEGUES DE LA OTRA LAMINA DE TEJIDO [14] EN VIRTUD DE LA ONDULACION ANIDADA LONGITUDINAL. COMO RESULTADO, EL VALOR DE ESPESOR EFECTIVO DE LA MEMBRANA DEL MODULO SE REDUCE MEJORANDO POR ELLO LA EFICACIA DE LAS SEPARACIONES DE LIQUIDO.
ES92303501T 1991-04-22 1992-04-21 Modulos de membrana de liquido con minimo espesor efectivo de membrana y procedimiento para fabricar los mismos. Expired - Lifetime ES2096031T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/688,178 US5449457A (en) 1991-04-22 1991-04-22 Liquid membrane modules with minimal effective membrane thickness and methods of making the same

Publications (1)

Publication Number Publication Date
ES2096031T3 true ES2096031T3 (es) 1997-03-01

Family

ID=24763425

Family Applications (1)

Application Number Title Priority Date Filing Date
ES92303501T Expired - Lifetime ES2096031T3 (es) 1991-04-22 1992-04-21 Modulos de membrana de liquido con minimo espesor efectivo de membrana y procedimiento para fabricar los mismos.

Country Status (12)

Country Link
US (1) US5449457A (es)
EP (1) EP0515033B1 (es)
JP (1) JPH0751217B2 (es)
KR (1) KR950008629B1 (es)
AT (1) ATE146987T1 (es)
CA (1) CA2065879A1 (es)
DE (1) DE69216290T2 (es)
DK (1) DK0515033T3 (es)
ES (1) ES2096031T3 (es)
GR (1) GR3022209T3 (es)
NO (1) NO921535L (es)
TW (1) TW223665B (es)

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3902232B2 (ja) * 1995-11-30 2007-04-04 テルモ カーディオバスキュラー システムズコーポレイション 多層中空繊維本体およびその製法
US5693230A (en) * 1996-01-25 1997-12-02 Gas Research Institute Hollow fiber contactor and process
EP0963239B1 (de) * 1997-02-04 2002-07-31 MAT Adsorption Technologies GmbH & Co. KG Membranmodul enthaltend mindestens zwei gruppen von hohlfasermembranen und verfahren zu seiner herstellung
US6432586B1 (en) 2000-04-10 2002-08-13 Celgard Inc. Separator for a high energy rechargeable lithium battery
US6558450B2 (en) * 2001-03-22 2003-05-06 Celgard Inc. Method for debubbling an ink
US6616841B2 (en) * 2001-06-21 2003-09-09 Celgard Inc. Hollow fiber membrane contactor
US7105089B2 (en) * 2003-03-13 2006-09-12 3M Innovative Properties Company Liquid—liquid extraction system and method
US7122709B2 (en) * 2003-03-13 2006-10-17 3M Innovative Properties Company Method for obtaining ethanol
US7264725B2 (en) * 2004-03-04 2007-09-04 Celgard Inc. Hollow fiber membrane contactor and method of making same
US7638049B2 (en) * 2004-03-30 2009-12-29 Celgard Inc. Three-port high performance mini hollow fiber membrane contactor
USD538749S1 (en) 2004-04-09 2007-03-20 Celgard Inc. Three-port high performance mini hollow fiber membrane contactor
CN106040003A (zh) * 2011-06-03 2016-10-26 3M创新有限公司 平板接触器和方法
WO2013090061A1 (en) 2011-12-14 2013-06-20 3M Innovative Properties Company Methods of producing butanol from non-cellulosic biomass
CA2969317C (en) * 2014-12-24 2023-06-13 Dic Corporation Hollow-fiber degassing module and inkjet printer
DE102019101740B4 (de) * 2019-01-24 2021-08-05 Dr. Ing. H.C. F. Porsche Aktiengesellschaft Verfahren zur Herstellung eines Mikrokanalbündel-Wärmetauschers
IT202000004138A1 (it) 2020-02-27 2021-08-27 Univ Degli Studi Di Roma “La Sapienza” Contattore anulare.

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3342729A (en) * 1964-12-09 1967-09-19 Dow Chemical Co Permeability separatory cell and apparatus and method of using the same
US3557962A (en) * 1968-06-28 1971-01-26 North American Rockwell Reverse osmosis fabric
BE793624A (fr) * 1972-01-10 1973-05-02 Baxter Laboratories Inc Dispositif pour le transfert de masses, presentant une membrane de diffision tubulaire enroulee
US4087327A (en) * 1976-04-12 1978-05-02 Monsanto Company Mammalion cell culture process
US4425234A (en) * 1979-07-30 1984-01-10 Hospal Ltd. Hollow fiber separatory device
DE3277363D1 (en) * 1981-06-29 1987-10-29 Baxter Travenol Lab Microporous hollow fiber membrane assembly and its method of manufacture
AU565652B2 (en) * 1982-02-19 1987-09-24 Dow Chemical Company, The Hollow fibre oxygenator element
FR2525487B1 (es) * 1982-04-27 1988-04-22 Hospal Sodip
US4460641A (en) * 1983-03-21 1984-07-17 Celanese Corporation Microporous hollow fibers as protectants against toxic agents
US4789468A (en) * 1984-08-28 1988-12-06 The Trustees Of The Stevens Institute Of Technology Immobilized-interface solute-transfer apparatus
US4750918A (en) * 1985-05-28 1988-06-14 The Trustees Of The Stevens Institute Of Technology Selective-permeation gas-separation process and apparatus
EP0264696A3 (de) * 1986-10-13 1989-03-15 Akzo N.V. Vorrichtung zum Stoffaustausch
DE3803693A1 (de) * 1987-03-10 1988-09-22 Akzo Gmbh Mehrlagiger hohlfadenwickelkoerper
JPH0696098B2 (ja) * 1988-05-27 1994-11-30 株式会社クラレ 中空糸型流体処理装置
JP2725311B2 (ja) * 1988-10-13 1998-03-11 大日本インキ化学工業株式会社 中空糸膜型気液接触装置
JP2002086329A (ja) * 2000-09-13 2002-03-26 Mori Seiki Co Ltd 工作機械の熱変位補正量算出方法及び熱変位補正量算出装置

Also Published As

Publication number Publication date
US5449457A (en) 1995-09-12
DE69216290D1 (de) 1997-02-13
EP0515033A1 (en) 1992-11-25
KR950008629B1 (ko) 1995-08-03
NO921535L (no) 1992-10-23
DE69216290T2 (de) 1997-05-28
JPH05123541A (ja) 1993-05-21
KR920019404A (ko) 1992-11-19
NO921535D0 (no) 1992-04-21
CA2065879A1 (en) 1992-10-23
TW223665B (es) 1994-05-11
GR3022209T3 (en) 1997-04-30
EP0515033B1 (en) 1997-01-02
JPH0751217B2 (ja) 1995-06-05
DK0515033T3 (es) 1997-03-03
ATE146987T1 (de) 1997-01-15

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