BR0306850A - Processo para produzir uma membrana hidrofóbica integralmente assimétrica, membrana hidrofóbica integralmente assimétrica, e, uso da mesma - Google Patents

Processo para produzir uma membrana hidrofóbica integralmente assimétrica, membrana hidrofóbica integralmente assimétrica, e, uso da mesma

Info

Publication number
BR0306850A
BR0306850A BR0306850-1A BR0306850A BR0306850A BR 0306850 A BR0306850 A BR 0306850A BR 0306850 A BR0306850 A BR 0306850A BR 0306850 A BR0306850 A BR 0306850A
Authority
BR
Brazil
Prior art keywords
membrane
separation
integrally asymmetric
hydrophobic membrane
producing
Prior art date
Application number
BR0306850-1A
Other languages
English (en)
Other versions
BR0306850B1 (pt
Inventor
Erich Kessler
Thomas Batzilla
Friedbert Wechs
Frank Wiese
Original Assignee
Membrana Gmbh
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 Membrana Gmbh filed Critical Membrana Gmbh
Publication of BR0306850A publication Critical patent/BR0306850A/pt
Publication of BR0306850B1 publication Critical patent/BR0306850B1/pt

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002—Organic membrane manufacture
    • B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
    • B01D67/0018—Thermally induced processes [TIPS]
    • 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
    • B01D53/228—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 characterised by specific membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002—Organic membrane manufacture
    • B01D67/0023—Organic membrane manufacture by inducing porosity into non porous precursor membranes
    • B01D67/0025—Organic membrane manufacture by inducing porosity into non porous precursor membranes by mechanical treatment, e.g. pore-stretching
    • B01D67/0027—Organic membrane manufacture by inducing porosity into non porous precursor membranes by mechanical treatment, e.g. pore-stretching by stretching
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002—Organic membrane manufacture
    • B01D67/0023—Organic membrane manufacture by inducing porosity into non porous precursor membranes
    • B01D67/003—Organic membrane manufacture by inducing porosity into non porous precursor membranes by selective elimination of components, e.g. by leaching
    • B01D67/0031—Organic membrane manufacture by inducing porosity into non porous precursor membranes by selective elimination of components, e.g. by leaching by elimination of at least one of the blocks of a block copolymer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/08—Hollow fibre membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/26—Polyalkenes
    • B01D71/262—Polypropylene
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C67/00—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
    • B29C67/20—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 for porous or cellular articles, e.g. of foam plastics, coarse-pored
    • B29C67/202—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 for porous or cellular articles, e.g. of foam plastics, coarse-pored comprising elimination of a solid or a liquid ingredient
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2323/00—Details relating to membrane preparation
    • B01D2323/38—Graft polymerization
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2325/00—Details relating to properties of membranes
    • B01D2325/02—Details relating to pores or porosity of the membranes
    • B01D2325/022—Asymmetric membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2325/00—Details relating to properties of membranes
    • B01D2325/02—Details relating to pores or porosity of the membranes
    • B01D2325/026—Sponge structure

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Thermal Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Analytical Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • External Artificial Organs (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

"PROCESSO PARA PRODUZIR UMA MEMBRANA HIDROFóBICA INTEGRALMENTE ASSIMéTRICA MEMBRANA HIDROFóBICA INTEGRALMENTE ASSIMéTRICA, E, USO DA MESMA". A invenção refere-se a um método para a produção de uma membrana poliolefinica hidrofóbica integralmente assimétrica com uma estrutura de suporte microporosa de poro aberto, esponjosa e uma camada de separação possuindo uma estrutura mais espessa por meio de um processo de separação de fases de líquido-líquido termalmente induzida. Uma solução de pelo menos uma poliolefina é extrusada para formar um corpo moldado. O solvente usado é tal que a temperatura de separação de uma solução a 25% em peso de poliolefina no citado solvente está entre 10<198>C e 70<198>C acima da temperatura de endurecimento. Após a desmoldagem, o corpo moldado é resfriado por um meio de resfriamento líquido que não dissolve o polímero em temperaturas de até a temperatura de ferramenta, até a separação de fases e o endurecimento da fase rica em polímero. A membrana integralmente assimétrica assim produzida possui uma porosidade que é maior do que 30% em volume - 75% em volume, uma estrutura de suporte microporosa de poro aberto, esponjosa destituída de macrovazios e possui poros isotrópicos em seu centro e pelo menos uma camada de separação possuindo um número máximo de poros > 100 arranjados sobre pelo menos uma sua superfície. A membrana e preferivelmente usada para processos de separação gasosa ou de transferência gasosa e especialmente para a oxigenação de sangue.
BRPI0306850-1A 2002-01-24 2003-01-08 processo para produzir uma membrana hidrofóbica integralmente assimétrica. BR0306850B1 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10202594 2002-01-24
PCT/EP2003/000084 WO2003061812A2 (de) 2002-01-24 2003-01-08 Polyolefinmembran mit integral asymmetrischer struktur und verfahren zu ihrer herstellung

Publications (2)

Publication Number Publication Date
BR0306850A true BR0306850A (pt) 2004-11-03
BR0306850B1 BR0306850B1 (pt) 2011-12-13

Family

ID=27588019

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0306850-1A BR0306850B1 (pt) 2002-01-24 2003-01-08 processo para produzir uma membrana hidrofóbica integralmente assimétrica.

Country Status (9)

Country Link
US (1) US7429343B2 (pt)
EP (1) EP1469935B1 (pt)
JP (1) JP4217627B2 (pt)
CN (1) CN1301149C (pt)
AT (1) ATE337080T1 (pt)
BR (1) BR0306850B1 (pt)
CA (1) CA2477190C (pt)
DE (1) DE50304738D1 (pt)
WO (1) WO2003061812A2 (pt)

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JP5076320B2 (ja) * 2006-01-11 2012-11-21 東洋紡績株式会社 ポリフッ化ビニリデン系中空糸型微多孔膜の製造方法
US8652332B2 (en) * 2009-01-09 2014-02-18 Massachusetts Institute Of Technology Liquid filtration using pressure difference across a hydrophobic membrane
CN102416300B (zh) * 2010-09-28 2014-03-12 中国石油化工股份有限公司 一种聚丙烯平板分离膜的制备方法
CN102755840B (zh) * 2011-04-25 2014-08-06 中国石油化工股份有限公司 一种平板聚丙烯分离膜的制备方法
AT511431B1 (de) * 2011-06-01 2012-12-15 Univ Wien Tech Herstellung asymmetrischer membranen
WO2012174649A1 (en) * 2011-06-20 2012-12-27 Dmf Medical Incorporated An anesthetic circuit and a method for using the anesthetic circuit
WO2014094139A1 (en) 2012-12-22 2014-06-26 Dmf Medical Incorporated An anesthetic circuit having a hollow fiber membrane
EP3618943A1 (de) * 2014-11-03 2020-03-11 3M Innovative Properties Company Mikroporöse polyvinylidenfluorid-flachmembran und ihre herstellung
WO2016136396A1 (ja) * 2015-02-27 2016-09-01 富士フイルム株式会社 ガス分離膜、ガス分離モジュール、ガス分離装置、及びガス分離方法
WO2016136395A1 (ja) * 2015-02-27 2016-09-01 富士フイルム株式会社 ガス分離非対称膜、ガス分離モジュール、ガス分離装置、及びガス分離方法
JP6349026B2 (ja) * 2015-02-27 2018-06-27 富士フイルム株式会社 ガス分離膜、ガス分離モジュール、ガス分離装置、ガス分離方法、及びガス分離非対称膜の製造方法
EP3235558A1 (en) * 2016-04-21 2017-10-25 3M Innovative Properties Company of 3M Center Hollow fiber membrane for use in an anesthetic circuit
CN106823806B (zh) * 2017-03-23 2020-04-28 南京膜材料产业技术研究院有限公司 一种规则四层结构的纳滤膜、制备方法及在高浓度盐分离过程中的应用
CN108099185B (zh) * 2017-12-07 2020-11-13 浙江海洋大学 一种基于3d打印快速在基体上制备超疏水表面方法
CN108211809B (zh) * 2017-12-13 2020-12-08 浙江长兴求是膜技术有限公司 一种永久亲水的聚偏氟乙烯膜及其制造方法
CN108211808B (zh) * 2017-12-13 2020-12-08 浙江长兴求是膜技术有限公司 一种食品级聚偏氟乙烯膜及其制造方法
US20200139309A1 (en) 2018-11-01 2020-05-07 Entegris, Inc. Porous polyethylene filter membrane with asymmetric pore structure, and related filters and methods
CN110538582A (zh) * 2019-09-09 2019-12-06 杭州科百特过滤器材有限公司 一种非对称聚烯烃膜的制备方法
JP7851241B2 (ja) * 2019-10-10 2026-04-24 インテグリス・インコーポレーテッド 多孔質ポリマー膜並びに関連したフィルタ及び方法
CN111888946B (zh) * 2020-08-17 2022-08-30 杭州科百特科技有限公司 一种用于血液氧合的非对称疏水性聚烯烃中空纤维膜及其制备方法与用途
CN112535956B (zh) * 2020-11-17 2022-09-23 上海翊科聚合物科技有限公司 一种用于氧合膜的超疏水聚烯烃中空纤维膜及其制备方法
CN114733361B (zh) * 2021-01-07 2024-06-14 杭州费尔新材料有限公司 一种聚烯烃中空纤维膜的制备方法
KR20240000455A (ko) 2021-04-28 2024-01-02 도레이 카부시키가이샤 분리막 및 그 제조 방법
CN120897793A (zh) 2023-04-05 2025-11-04 东丽株式会社 分离膜、其制造方法、作为脱气用和注气用的至少一者的膜组件、以及作为脱气用和注气用的至少一者的装置

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Also Published As

Publication number Publication date
US7429343B2 (en) 2008-09-30
DE50304738D1 (de) 2006-10-05
US20050145107A1 (en) 2005-07-07
WO2003061812A3 (de) 2004-02-05
EP1469935B1 (de) 2006-08-23
EP1469935A2 (de) 2004-10-27
CA2477190A1 (en) 2003-07-31
BR0306850B1 (pt) 2011-12-13
JP2005515061A (ja) 2005-05-26
WO2003061812A2 (de) 2003-07-31
CA2477190C (en) 2011-07-26
JP4217627B2 (ja) 2009-02-04
CN1622850A (zh) 2005-06-01
CN1301149C (zh) 2007-02-21
ATE337080T1 (de) 2006-09-15

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Legal Events

Date Code Title Description
B06A Patent application procedure suspended [chapter 6.1 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]

Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 08/01/2003, OBSERVADAS AS CONDICOES LEGAIS.

B25A Requested transfer of rights approved