CN108430613A - Amphoteric ion sulfone polymer blend and hollow-fibre membrane - Google Patents

Amphoteric ion sulfone polymer blend and hollow-fibre membrane Download PDF

Info

Publication number
CN108430613A
CN108430613A CN201680070265.6A CN201680070265A CN108430613A CN 108430613 A CN108430613 A CN 108430613A CN 201680070265 A CN201680070265 A CN 201680070265A CN 108430613 A CN108430613 A CN 108430613A
Authority
CN
China
Prior art keywords
polymer
independently
hollow
structural unit
alkyl
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.)
Granted
Application number
CN201680070265.6A
Other languages
Chinese (zh)
Other versions
CN108430613B (en
Inventor
周宏毅
M.J.米斯纳
袁卫
J-A.M.伯迪克
P.J.麦吉尔克
J.E.豪森
R.D.伯切斯基
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.)
Cytiva Sweden AB
Original Assignee
General Electric Co
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
Priority claimed from US14/958,937 external-priority patent/US20160136588A1/en
Application filed by General Electric Co filed Critical General Electric Co
Publication of CN108430613A publication Critical patent/CN108430613A/en
Application granted granted Critical
Publication of CN108430613B publication Critical patent/CN108430613B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • B01D71/66Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
    • B01D71/68Polysulfones; Polyethersulfones
    • 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
    • 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
    • B01D69/02Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
    • 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
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M1/00Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
    • A61M1/14Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis
    • A61M1/16Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2323/00Details relating to membrane preparation
    • B01D2323/12Specific ratios of components used
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2323/00Details relating to membrane preparation
    • B01D2323/36Introduction of specific chemical groups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/18Membrane materials having mixed charged functional groups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/34Molecular weight or degree of polymerisation

Abstract

Provided herein is the blends of the polymer suitable for preparing hollow-fibre membrane.Blend polymer includes the blend of the first polymer containing the sulfone polymer with amphoteric ion functional group and the second polymer containing sulfone polymer.

Description

Amphoteric ion sulfone polymer blend and hollow-fibre membrane
Cross reference to related applications
The application is entitled " the Zwitterion-Functionalized Polymer submitted on November 19th, 2014 Hollow-Fiber Membranes And Associated Method (the functionalized polymeric hollow fibres of amphoteric ion Film and correlation technique) " U.S. Patent Application No. 14/547,306 part continuation application, entire contents are incorporated by reference into Herein.
Background
The disclosure generally relates to prepare the blend polymer of hollow-fibre membrane.Blend polymer includes at least one wraps The polymer of the group containing amphoteric ion.
Porous hollow fiber polymer film is used for many applications, such as haemodialysis, ultrafiltration, nanofiltration, reverse osmosis, gas point From, micro-filtration and pervaporation.For many in these applications, there is best selective and chemistry, heat and mechanical stability Film be ideal.In many applications (such as bio-separation or water filtering), there is improved hydrophily, improved biofacies Capacitive or it is low be stained in one or more films be also likely to be desirable.
Poly (arylene ether), especially polyether sulfone and polysulfones, due to its machinery, thermally and chemically stability and be commonly used as membrane material Material.However, these polymer are hydrophobic, and lack biocompatibility and aqueous using required hydrophily.Pass through polymerization Object blending has been carried out the hydrophilic improvement of film, such as depositing at a small amount of hydrophilic polymer such as polyvinylpyrrolidone (PVP) In lower manufacture perforated membrane.However, since PVP is water-soluble, it can slowly be leached from porous polymer matrix, generate product Changeability.Alternatively, hydrophily via the functionalization of main polymer chain and carboxyl, nitrile or polyethylene glycol functional group introducing and It realizes.However, these chemical modifications may be complicated, expensive and inefficient.In addition, addition functional group may make it difficult to Hollow-fibre membrane is manufactured by functionalized polymeric.Solve the problems, such as that a kind of method caused due to functional group is after fabrication by film Functionalization;But this method increases the manufacturing cost of film.
This field needs easy to process and/or manufacture film forming (including hollow-fibre membrane) but can also reduce protein combination And/or it is stained and provides the material of the good mechanical properties suitable for aqueous application.
It summarizes
Provided herein is the blend polymers for the certain limitations for mitigating the previously known method for manufacturing hollow-fibre membrane.This hair Bright blend improves the machinability of functionalized polymeric, and also reduces functionalized demand after the casting to film.
Provided herein is hollow-fibre membranes, and it includes the first polymers containing the sulfone polymer with amphoteric ion functional group With the blend of the second polymer containing sulfone polymer:
On the one hand, provided herein is hollow-fibre membranes, poly- it includes first containing the sulfone polymer with amphoteric ion functional group The blend of object and the second polymer containing sulfone polymer is closed, wherein including the sulfone polymer with amphoteric ion functional group First polymer includes the structural unit of the Formulas I A or Formulas I B that are connect with the structural unit of Formula II, and wherein includes sulfone polymer Second polymer includes the structural unit with Formula II, the structure of III, IV or V, the wherein knot of Formulas I A, IB, II, III, IV and V Structure is as described in following detailed description part.
Attached drawing
When refer to the attached drawing reading is described in detail below, these and other features, aspects and advantages of the invention will become more preferable Understand, wherein identical character represents identical part in all the appended drawings, wherein:
Fig. 1 shows the hollow-fibre membrane comprising heavy polymer and comprising claimed blend polymer Comparison between the cross section of hollow-fibre membrane.
Fig. 2 shows the comparison between the protein-binding matter (being stained) of hollow-fibre membrane:(1) high molecular weight polysulfones (PSU) (MW 54kg/mol) ultra filtration hollow fiber membrane, the hollow fibre of (2) high molecular weight polysulfones (PSU) (MW 54kg/mol) micro-filtration Film is tieed up, (3) include PSU (ZwPSU) micro-filtration hollow-fibre membrane of amphoteric ion group, and (4) include that the polymer of the present invention is blended The micro-filtration hollow-fibre membrane of object (MW 49.3kg/mol), and PSU (ZwPSU) micro-filtration of (5) comprising amphoteric ion group are hollow Tunica fibrosa.From heavy polymer to blend polymer, observe combine (ELISA) without influencing form and IgG or It influences minimum.
It is described in detail
Hollow-fibre membrane is commonly used in wherein needing the application of hydrophily and/or biocompatibility barrier.Amphoteric ion sulfone polymerize Object is hydrophilic and leads to low-protein combination and biodeterioration.However, amphoteric ion sulfone polymer tends to be difficult to Film forming, and gained film usually has the engineering properties of difference.The hydrophilic previous trial of improvement film containing sulfone polymer, which concentrates on, to gather It is functionalized after closing the manufacture of object and/or film.
In contrast, provided herein is the novel blend of the polymer comprising sulfone polymer and amphoteric ion sulfone polymer, It mitigates to functionalized needs after the manufacture of film.In addition, blend polymer as described herein can improve polymer network knot Structure simultaneously leads to better mechanical performance.Blend polymer as described herein also assigns improved machinability, to allow more Film, including hollow-fibre membrane is easily manufactured.In addition, blend polymer as described herein provides the desired hydrophily to film And/or biocompatibility.Therefore, by the way that the sulfone polymer of low amounts to be blended with amphoteric ion sulfone polymer, improve amphoteric ion The machinability of sulfone polymer film forming.In addition, the engineering properties of the film comprising the blend polymer significantly improves, protect simultaneously Hold film form and the low combination feature of film.Advantageously, film of the invention mitigates has with from matrix leaching water-soluble polymer such as PVP The problem of pass, to reduce product changeability.
Blend polymer as described herein provides film machinability (such as prepared paint viscosity (dope viscosity)) With the simple adjustment of engineering properties (such as high tensile elongation) and significantly improve, and also by with sulfone relatively inexpensive in blend Polymer replaces expensive amphoteric ion sulfone polymer to provide some cost reductions.
Certain terms
Approximating language as used herein, which can be applied to modification, in entire disclosure and claims may allow to change Any quantificational expression without leading to relative basic function variation.Therefore, for example " about " by one or more terms " substantially " value modified is not limited to specified exact value.In some cases, approximating language can correspond to for surveying The precision of the instrument of magnitude.In here and throughout the specification and claims book, scope limitation can be combined and/or mutually It changes, such range is identified and includes all subranges wherein included, unless context or language are indicated otherwise.
In following specification and claims, unless the context clearly indicates otherwise, otherwise singulative " one ", "one" and "the" include plural reference.As used herein, term "or" being not intended to be exhaustive property, and refer to it is existing at least Component mentioned by one, and include wherein may exist the case where combination of mentioned component, unless context is in addition bright Really instruction.
As used herein, " sulfone polymer " is comprising structure aryl-SO2One or more subelements of aryl it is any Polymer.In general, sulfone polymer is prepared via the reaction between bis-phenol and bis- (4- chlorphenyls) sulfones by eliminating sodium chloride:Sulfone is poly- It includes but not limited to polysulfones, polyarylsufone (or referred to as polyphenylsulphine or polyphenylsulfone), polyether sulfone etc. to close object.
As used herein, " sulfone polymer with amphoteric ion functional group " or " amphoteric ion sulfone polymer " are comprising knot Structure aryl-SO2One or more subelements of aryl simultaneously have one or more subelements comprising amphoteric ion functional group Any polymer.
Terms used herein " hollow-fibre membrane " refer to the film knot based on fiber for including the separating layer for being present in surface Structure.Hollow-fibre membrane can use " inside and outside " or " in outer " mechanism to work.Term " hollow-fibre membrane " and " film " are herein It is used interchangeably, unless the context clearly indicates otherwise.
Term " alkyl " refers to the linear or branched alkyl group with 1 to 12 carbon atom in chain.The example of alkyl includes Methyl (Me) ethyl (Et), n-propyl, isopropyl, butyl, isobutyl group, sec-butyl, tertiary butyl (tBu), amyl, isopentyl, uncle Amyl, hexyl, isohesyl etc..
" naphthenic base " refers to monocycle or polycyclic non-aromatic hydrocarbon group with 3 to 12 carbon atoms.Naphthenic base it is non-limiting Example includes cyclopropyl, cyclobutyl, cyclopenta, cyclohexyl, 1- methylcyclopropyl groups, 2- methylcyclopentyls, octahydro -1H- indenes, decahydro Naphthalene etc..
Term " aryl " indicates monocycle or bicyclic aromatic hydrocarbon ring structure.Aryl rings can have 6 or 10 carbon originals in ring Son.
Described herein is hollow-fibre membrane, poly- it includes first containing the sulfone polymer with amphoteric ion functional group Close the blend of object and the second polymer containing sulfone polymer.
On the one hand, hollow-fibre membrane includes the first polymer containing the sulfone polymer with amphoteric ion functional group and contains There is the blend of the second polymer of sulfone polymer, wherein the comprising the sulfone polymer with amphoteric ion functional group first polymerization Object includes the structural unit of the Formulas I A or Formulas I B that are connect with the structural unit of Formula II:
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;
K is 0 to 10;
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;With
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
On the other hand, hollow-fibre membrane include containing with amphoteric ion functional group sulfone polymer first polymer and The blend of second polymer containing sulfone polymer, wherein comprising sulfone polymer second polymer include with Formula II, The structural unit of the structure of III, IV or V,
Wherein
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;With
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
A and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
In some embodiments of above-mentioned hollow-fibre membrane, include the of the sulfone polymer with amphoteric ion functional group One polymer includes the structural unit of the Formulas I A or Formulas I B that are connect with the structural unit of Formula II:
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;
K is 0 to 10;
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;With
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;
M and n is each independently 0 or 1;With
The second polymer for wherein including sulfone polymer includes the structural unit with Formula II, IV or V structure
In some embodiments of above-mentioned hollow-fibre membrane, including first of the sulfone polymer with amphoteric ion functional group is poly- Close the structural unit that object includes Formula IV:
Wherein w is 0,1,2 or 3.
In some embodiments of above-mentioned hollow-fibre membrane, include the of the sulfone polymer with amphoteric ion functional group One polymer includes the structural unit of Formula VII:
Wherein P+Q=1, P=0.30-0.50, Q=0.50-0.70.
In some embodiments of above-mentioned hollow-fibre membrane, the amphoteric ion functionalization knot of the Formulas I B in first polymer The molar fraction of structure unit is less than about 50 moles of % of the total mole number of the unit of Formulas I B and Formula II in first polymer.Upper In some embodiments for stating hollow-fibre membrane, mole of the amphoteric ion functionalized structure unit of the Formulas I B in first polymer Within the scope of about 30 moles of % to about 50 moles of % of the total mole number of the unit of Formulas I B and Formula II of the score in first polymer.
In some embodiments of above-mentioned hollow-fibre membrane, include the of the sulfone polymer with amphoteric ion functional group The molecular weight of one polymer is in the range of about 10000g/mol to about 80000g/mol.
In some embodiments of above-mentioned hollow-fibre membrane, including the second polymer of sulfone polymer contains Formula II Structural unit polysulfones.
In some embodiments of above-mentioned hollow-fibre membrane, including the second polymer of sulfone polymer contains formula IV Structural unit polyphenylsulphine.
In some embodiments of above-mentioned hollow-fibre membrane, including the second polymer of sulfone polymer contains Formula V Structural unit polyether sulfone.
In some embodiments of above-mentioned hollow-fibre membrane, including the amount of the second polymer of sulfone polymer is in film The about 0.5 weight % to about 5 weight % of the total weight of polymer.
In some embodiments of above-mentioned hollow-fibre membrane, including the molecular weight of the second polymer of sulfone polymer is about In the range of 50000g/mol to about 80000g/mol.
In some embodiments of above-mentioned hollow-fibre membrane, include the of the sulfone polymer with amphoteric ion functional group One polymer includes the structural unit for the Formulas I B being connect with the structural unit of Formula II, and includes the second polymer packet of sulfone polymer Structural unit containing Formula II
In some embodiments of above-mentioned hollow-fibre membrane, including first of the sulfone polymer with amphoteric ion functional group is poly- It includes the structural unit of Formulas I B connect with the structural unit of Formula II to close object, and include the second polymer of sulfone polymer includes formula The structural unit of IV
In some embodiments of above-mentioned hollow-fibre membrane, including first of the sulfone polymer with amphoteric ion functional group is poly- It includes the structural unit of Formulas I B connect with the structural unit of Formula II to close object, and include the second polymer of sulfone polymer includes formula The structural unit of V
Provided herein is the hollow fiber membrane modules for including multiple hollow-fibre membranes, wherein including the sulfone with amphoteric ion functional group The first polymer of polymer includes the structural unit of Formulas I B being connect with the structural unit of Formula II, and includes the of sulfone polymer Dimerization object includes the structural unit of Formula II.The haemodialysis comprising hollow fiber membrane module or blood filtration dress is also provided herein It sets, wherein the first polymer comprising the sulfone polymer with amphoteric ion functional group includes to be connect with the structural unit of Formula II The structural unit of Formulas I B, and include that the second polymer of sulfone polymer includes the structural unit of Formula II.
Provided herein is the hollow fiber membrane modules for including multiple hollow-fibre membranes, wherein comprising having amphoteric ion functional group The first polymer of sulfone polymer include the structural unit of Formulas I B being connect with the structural unit of Formula II, and include sulfone polymer Second polymer include the structural unit of formula IV.The haemodialysis comprising hollow fiber membrane module or blood mistake is also provided herein Device is filtered, wherein the first polymer comprising the sulfone polymer with amphoteric ion functional group includes to connect with the structural unit of Formula II The structural unit of the Formulas I B connect, and include that the second polymer of sulfone polymer includes the structural unit of formula IV.
Provided herein is the hollow fiber membrane modules for including multiple hollow-fibre membranes, wherein comprising having amphoteric ion functional group The first polymer of sulfone polymer include the structural unit of Formulas I B being connect with the structural unit of Formula II, and include sulfone polymer Second polymer include the structural unit of Formula V.The haemodialysis comprising hollow fiber membrane module or blood mistake is also provided herein Device is filtered, wherein the first polymer comprising the sulfone polymer with amphoteric ion functional group includes to connect with the structural unit of Formula II The structural unit of the Formulas I B connect, and include that the second polymer of sulfone polymer includes the structural unit of Formula V.
Another aspect, provided herein is comprising the first polymer containing the sulfone polymer with amphoteric ion functional group and contain There is the composition of the blend of the second polymer of sulfone polymer.
In some embodiments, provided herein is a kind of compositions, and it includes contain the sulfone with amphoteric ion functional group The blend of the first polymer of polymer and second polymer containing sulfone polymer, wherein comprising having amphoteric ion function The first polymer of the sulfone polymer of group includes the structural unit for the Formulas I B being connect with the structural unit of Formula II, and includes sulfone polymerization The second polymer of object includes the structural unit of Formula II
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;
K is 0 to 10;
R3It independently is hydrogen atom, C with Y1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
In some embodiments, provided herein is a kind of compositions, and it includes contain the sulfone with amphoteric ion functional group The blend of the first polymer of polymer and second polymer containing sulfone polymer, wherein comprising having amphoteric ion function The first polymer of the sulfone polymer of group includes the structural unit for the Formulas I B being connect with the structural unit of Formula II, and includes sulfone polymerization The second polymer of object includes the structural unit of formula IV
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;
K is 0 to 10;
R3It independently is hydrogen atom, C with Y1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
In some embodiments, provided herein is a kind of compositions, and it includes contain the sulfone with amphoteric ion functional group The blend of the first polymer of polymer and second polymer containing sulfone polymer, wherein comprising having amphoteric ion function The first polymer of the sulfone polymer of group includes the structural unit for the Formulas I B being connect with the structural unit of Formula II, and includes sulfone polymerization The second polymer of object includes the structural unit of Formula V
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;
K is 0 to 10;
R3It independently is hydrogen atom, C with Y1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or virtue Basic ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
The method for being used to form hollow-fibre membrane as described herein is also provided herein comprising:
(A) cast-solution that the blend comprising first polymer and second polymer is provided, wherein in the cast-solution Total polymer content is less than about 20 weight % of the cast-solution;With
(B) cast-solution is squeezed out to form the hollow-fibre membrane by circular passage.
In alternative embodiment, cast-solution can have in the cast-solution less than about 50 weight % of cast-solution Total polymer content.In a further embodiment, cast-solution can have the about 10 weight % to about 30 weights for cast-solution Measure the total polymer content in the cast-solution of %.It should be understood that the actual content of polymer in film may not always with pour The amount for casting the polymer in solution (coating) is identical.Only it is used as explanation, 2.5 weight % sulfone polymers (second polymer) in film Content can include amphoteric ion official by 0.4 weight % sulfone polymers in cast-solution together with 15.6 weight % in cast-solution The sulfone polymer that can be rolled into a ball generates.
In certain embodiments, include the total polymer weight in film by the hollow-fibre membrane that above-mentioned steps (B) are formed About 0.5 weight % to about 5 weight % amount second polymer.In other embodiments, in being formed by above-mentioned steps (B) Empty fiber membrane includes the second polymer of the amount of the about 0.5 weight % to about 3 weight % of the total polymer weight in film.
Sulfone polymer as described herein is synthesized using any suitable technology known in the art and/or there is amphoteric ion The sulfone polymer of functional group.In certain embodiments, sulfone polymer by make at least one aromatic dihydroxy compound with extremely A kind of few aromatic dihalide compound compound is reacted to synthesize.In aromatic dihydroxy compound and aromatic dihalide compound compound extremely It is a kind of less that the appropriate functional group (such as piperazine amide group) that can be converted into amphoteric ion functional group can be used to be functionalized.One In a little embodiments, aromatic dihydroxy compound can be functionalized with suitable functional group.In addition, aromatic dihydroxy compound and At least one of aromatic dihalide compound compound can include sulfone part.In some embodiments, aromatic dihalide compound It can includes sulfone part to close object.
The Exemplary aromatic dihalide compounds that can be used include bis- (chlorphenyl) sulfones of 4,4'-, 2,4'- bis- (chlorobenzenes Base) sulfone, 2,4- bis- (chlorphenyl) sulfones, 4,4'- bis- (fluorophenyl) sulfones, 2,4'- bis- (fluorophenyl) sulfones, 2,4- bis- (fluorophenyl) sulfones, 4,4'- bis- (chlorphenyl) sulfoxides, 2,4'- bis- (chlorphenyl) sulfoxides, 2,4- bis- (fluorophenyl) sulfoxides, 4,4'- bis- (fluorophenyls) are sub- Sulfone, 2,4'- bis- (fluorophenyl) sulfoxides, 2,4- bis- (fluorophenyl) sulfoxides, 4,4'- bis- (fluorophenyl) ketone, 2,4'- bis- (fluorophenyls) Ketone, 2,4- bis- (fluorophenyl) ketone, 1,3- bis- (4- fluoro benzoyls) benzene, bis- (4- fluoro benzoyls) benzene of Isosorbide-5-Nitrae-, 4,4'- bis- (4- Chlorphenyl) phenyl phosphine oxide, 4,4'- bis- (4- fluorophenyls) phenyl phosphine oxides, 4,4'- bis- (4- fluorophenylSulphonyls) -1,1'- connection Benzene, 4,4'- bis- (4- Chlorophenylsulfonyls) -1,1'- biphenyl, 4,4'- bis- (4- fluorophenyls sulfoxide) -1,1'- biphenyl, 4,4'- is bis- (4- chlorophenyls) -1,1'- biphenyl and combinations thereof.
The non-limiting examples for the suitable aromatic dihydroxy compounds that can be used include 4,4'- dihydroxy phenyl sulfones, 2, 4'- dihydroxy phenyl sulfones, 4,4'- dihydroxy phenyl sulfoxides, 2,4'- dihydroxy phenyl sulfoxides, bis- (3,5- dimethyl -4- hydroxyls Phenyl) sulfoxide, bis- (3,5- dimethyl -4- hydroxy phenyls) sulfones, 4,4- (phenyl phosphino-) bis-phenols, 4,4'- oxygroup bis-phenols, 4,4'- Thiobisphenol, 4,4'- dihydroxy benaophenonels, 4,4'- dihydroxy benzenes methylmethanes, quinhydrones, isophthalic bis-phenol, 5- cyano -1,3- bis- Hydroxy benzenes, 4- cyano -1,3- dihydroxy benzenes, 2- cyano-Isosorbide-5-Nitrae-dihydroxy benzenes, 2- methoxyhydroquinons, 2,2'- bis-phenols, 4,4'- is bis- Phenol, 2,2'- dimethyl bisphenols, 2,2', 6,6'- tetramethyl bis-phenols, 2,2', 3,3', 6,6'- hexamethyl bis-phenols, 3,3', 5,5'- Tetrabromobisphenol, 2', 6,6'- tetramethyl bis-phenols, 4,4'- isopropylidene bisphenols (bisphenol-A), bis- (2, the 6- dimethyl of 4,4'- isopropylidenes Phenol) (bisphenol-A), 4,4'- isopropylidenes are bis- (2- methylphenols), and 4,4'- isopropylidenes are bis- (2- chavicols), 4,4'- isopropylidenes are bis- (2- allyl -6- methylphenols), 4,4'(1,3- phenylenediisopropylidenes) bis-phenol (bis-phenol M), 4, 4'- isopropylidenes are bis- (3- phenylphenols), 4,4'- isopropylidenes-bis- (2- phenylphenols), and 4,4'- (Isosorbide-5-Nitrae-phenylene two is sub- different Propyl) bis-phenol (bis-phenol P), 4,4'- ethylidene bis-phenols (bis-phenol E), 4,4'- oxygroup bis-phenols, 4,4'- thiobisphenols, 4,4'- is thio Bis- (2,6- xylenols), 4,4'- sulfonyldiphenols, 4,4'- sulfonyls bis- (2,6- xylenols), 4,4'- sulfenyls Base bis-phenol, 4,4'- hexafluoroisopropyli,enes) bis-phenol (bisphenol AF), 4,4'- hexafluoroisopropyli,enes) bis- (2,6- xylenols), 4, 4'- (1- phenyl-ethylenes) bis-phenol (bisphenol-ap), 4,4'- (1- phenyl-ethylenes) are bis- (2,6- xylenol), bis- (4- hydroxyls Phenyl) -2,2- dichloroethylene (bisphenol-c), bis- (4- hydroxy phenyls) methane (Bisphenol F) are bis- (2,6- dimethyl -4- hydroxy phenyls) Methane, 2,2- bis- (4- hydroxy phenyls) butane, 3,3- bis- (4- hydroxy phenyls) pentanes, 4,4'- (cyclopentylene) bis-phenols, 4,4'- (cyclohexylidene) bis-phenol (bisphenol Z), 4,4'- (cyclohexylidenes) are bis- (2- methylphenols), 4,4'- (sub- cyclo-dodecyl) bis-phenols, 4,4'- (two rings [2.2.1] heptamethylene) bis-phenols, 4,4'- (9H- fluorenes -9,9- diyl) bis-phenols, 3,3'- bis- (4- hydroxy phenyls) are different Benzofuran -1 (3H) -one, 1- (4- hydroxy phenyls) -3,3'- dimethyl -2,3- dihydro -1H- indenes -5- alcohol, 1- (hydroxyl -3 4-, 5- 3,5-dimethylphenyls) -1,3,3', 4,6- pentamethyl -2,3- dihydro -1H- indenes -5- alcohol, 3,3,3', 3'- tetramethyls -2,2', 3, 3'- tetrahydrochysenes -1,1'- spiral shell [indenes] -5,6'- glycol (spirobindene is full), dihydroxy benaophenonel (bis-phenol K), thiobisphenol (bis-phenol S), bis- (4- hydroxy phenyls) diphenyl methanes, bis- (4- hydroxyphenoxies) -4,4'- biphenyl, 4,4'- bis- (4- hydroxy phenyls) two Phenyl ether, 9,9- bis- (3- methyl -4- hydroxy phenyls) fluorenes, N- phenyl -3,3- is bis--(4- hydroxy phenyls) phthalimide and A combination thereof.
The reaction can carry out in the presence of alkali metal compound in polar non-solute, and optionally in catalyst In the presence of carry out.The basic salt of alkali metal compound can be used for realizing the reaction between dihalo and dihydroxy aromatic compounds. Exemplary compounds include alkali metal hydroxide, such as, but not limited to lithium hydroxide, sodium hydroxide, potassium hydroxide, hydroxide Rubidium and cesium hydroxide;Alkali carbonate, such as, but not limited to lithium carbonate, sodium carbonate, potassium carbonate, rubidium carbonate and cesium carbonate;With Alkali metal hydrogencarbonate, such as, but not limited to lithium bicarbonate, sodium bicarbonate, saleratus, rubidium bicarbonate and caesium bicarbonate.These The combination of compound can also be used for realizing reaction.
Some examples of aprotic polar solvent include but not limited to n,N-Dimethylformamide, N, N- diethyl formyls Amine, n,N-dimethylacetamide, N, N- diethyl acetamides, N, N- Valpromides, N, N- dimethyl benzamides, N- first Base -2-Pyrrolidone (NMP), N- ethyl-2-pyrrolidones, N- isopropyls -2-Pyrrolidone, N- isobutyl groups -2-Pyrrolidone, N- n-propyls -2-Pyrrolidone, N- normal-butyls -2-Pyrrolidone, n-cyclohexyl-2-pyrrolidone, N- methyl -3- methyl -2- Pyrrolidones, N- ethyl -3- methyl-pyrrolidons, N- methyl -3,4,5- trimethyls -2-Pyrrolidone, N- methyl -2- piperidines Ketone, N- ethyl -2- piperidones, N- isopropyl -2- piperidones, N- methyl -6- methyl -2- piperidones, N- methyl -3- ethyl piperidines Ketone, dimethyl sulfoxide (DMSO) (DMSO), diethyl sulfoxide, sulfolane, 1- methyl-1s-oxo sulfolane, 1- ethyl -1- oxo ring fourths Sulfone, 1- phenyl -1- oxo sulfolane, N, N'- dimethyl-imidazolinones (DMI), diphenyl sulphone (DPS) and combinations thereof.Solvent ready for use Amount is typically the amount for being enough to dissolve dihalo and dihydroxy aromatic compounds.
The reaction can be about 100 DEG C to about 300 DEG C in some embodiments, be about 120 in some embodiments DEG C to about 200 DEG C, and it is to carry out at a temperature of about 150 DEG C to about 200 DEG C ranges in specific embodiments.Reaction mixture It is further starting reaction mixture can be added to by the way that the solvent of azeotropic mixture will be formed with water together with polar non-solute It is dry.The example of this solvent includes toluene, benzene, dimethylbenzene, ethylbenzene and chlorobenzene.By azeotropic drying remove remaining water it Afterwards, reaction can carry out at above-mentioned raised temperature.The reaction usually carries out about 1 hour to about 72 in some embodiments The period of hour, and about 1 hour to about 10 hours period is carried out in specific embodiments.
After completion of the reaction, polymer can be detached with inorganic salts, be deposited in non-solvent and by filtering and drying receipts Collection.The example of non-solvent includes water, methanol, ethyl alcohol, propyl alcohol, butanol, acetone, methyl ethyl ketone, methyl iso-butyl ketone (MIBK) and its group It closes.
The glass transition temperature T of polymer as described hereingIt in one embodiment can be at about 120 DEG C to about In the range of 280 DEG C, and in another embodiment can be in the range of about 140 DEG C to about 200 DEG C.Polymer can be into One step passes through the weight average molecular weight (M that is obtained from gel permeation chromatography based on polystyrene standardsw) characterize.Implement at one In scheme, the M of polymerwIt can be in the range of about 10000 grams/mol (g/mol) be to about 100000g/mol.At another In embodiment, MwIt can be in the range of about 10000g/mol to about 75000g/mol.In another embodiment, MwIt can With in the range of about 40000g/mol to about 55000g/mol.In another embodiment, MwIt can be in about 50000g/ In the range of mol to about 80000g/mol.
Mechanical test is carried out by using Instron (model 4202).In typical test, the one of about 2 inches of length Section hollow-fibre membrane is fitted into a pair of of air-actuated jaw, and gauge length is made to be exactly 1 inch.Test sample is with the rate of 0.5 inch/min It stretches, and stops test when sample burst.Include sample modulus, peak load and maximum elongation from the data of test record Rate, load and elongation at break.
Polymer and film including polymer blend as described herein can further pass through its respective Hydrophilic Characterization of Hydrophilic. In some embodiments, the contact angle of the sulfone polymer with amphoteric ion functional group and water is less than about 80 degree, in glass base It is measured on surface on material as the polymer of film casting.In some embodiments, the sulfone with amphoteric ion functional group is poly- The contact angle for closing object and water is less than about 50 degree, is measured on the surface as the polymer of film casting on the glass substrate.Specific Embodiment in, with amphoteric ion functional group sulfone polymer and water contact angle be less than about 30 degree, on the glass substrate It is measured on the surface of polymer as film casting.
It is prepared by methods known in the art according to the film of the embodiments described herein.Suitable technology includes but not It is limited to:Dry phase separation membrane forming process;Wetting phase seperation film forming process;Dry-wetting phase seperation film forming process;Thermal inactive film Forming process.In addition, after film formation, film can be subjected to film adjustment process or processing procedure before it is used to detach application. Exemplary process may include thermal annealing to mitigate the stress or pre-equilibration in the similar solution of the feeding flow of contact with film.
In one embodiment, film can be prepared by mutually converting.Phase transfer process includes 1) steam induction phase point From (VIPS), also referred to as " dry method casting " or " air casting ";2) liquid induction phase separation (LIPS), main referred to as " immersion is poured Casting " or " wet caste ";With 3) heating consumers (TIPS), commonly referred to as " melt casting ".Phase transfer process can generate Asymmetric membrane integral into cortex.In some embodiments, film can be crosslinked to provide additional support.
Film can be designed and manufactured as having specific pore size so that the solute that size is more than pore size may not be able to lead to It crosses.In one embodiment, pore size can be in the range of about 0.5 nanometer to about 100 nanometers.In another embodiment In, pore size can be in the range of about 1 nanometer to about 25nm.
The method to form hollow-fibre membrane as described herein is also provided herein.This method includes providing comprising foregoing The cast-solution of blend polymer and solvent.This method further includes squeezing out cast-solution by circular passage to form hollow fibre Tie up film.The non-limiting examples of suitable solvent include n-methyl-2-pyrrolidone, dimethylacetylamide, dimethylformamide, and four Hydrogen furans, methyl ethyl ketone, formyl piperidine or combinations thereof.
In some embodiments, cast-solution may further include selected from polymer such as polyvinylpyrrolidone and gather The additive of ethylene glycol;Anti-solvent, such as water, alcohol, glycol, glycol ethers and salt;Alkali halide;And combinations thereof.In some realities Apply in scheme, additive may include alkali metal bromide, such as, but not limited to lithium bromide, sodium bromide, potassium bromide, cesium bromide or A combination thereof.
In some embodiments, additive can be deposited with the amount (total amount) within the scope of about 0.1 weight % to about 30 weight % It is in cast-solution.In addition, the sulfone polymer and sulfone polymer comprising amphoteric ion functional group are with the cast-solution The amount of about 10 weight % to about 30 weight % of weight be present in the cast-solution.
In some embodiments, above-mentioned any hollow-fibre membrane blend includes at least one other polymer. Other polymer can be blended with above-mentioned blend polymer to assign heterogeneity, such as better heat resistance, biofacies Capacitive etc..It is generated when mutually conversion furthermore, it is possible to which other polymer is added in cast-solution during film is formed with changing Phase inversion membrane structure form, such as asymmetric membrane structure.In some cases, polymer in addition can be kept in Sulfone polymer in most telolemma and/or the additive (such as PVP, PEG etc.) for losing but not being completely removed in the fabrication process. Such film is recognized as in the range of embodiment presented herein.
In some embodiments, the other polymer of blending is hydrophilic polymer.Suitable hydrophilic polymer Non-limiting examples include polyvinylpyrrolidone (PVP), polyoxazolines, polyethylene glycol, polypropylene glycol, polyglycols monoesters, The polymer of polyethylene glycol and polypropylene glycol, water-soluble cellulose derivative, polysorbate, polyethylene oxide-polycyclic oxygen third Alkane polymer, polyethyleneimine and combinations thereof.In some embodiments, cast-solution blend can include other polymerization Object, such as polyether urethane, polyamide, polyether-amide, polyacrylonitrile and combinations thereof.
Film as described herein can be used for various applications, such as bio-separation, Water warfare, blood filtration, haemodialysis, super Filter, nanofiltration, gas separation, micro-filtration, reverse osmosis and pervaporation.In specific embodiments, film can have and wherein need to change Application in the bio-pharmaceuticals and biomedical sector of kind hydrophily and biocompatibility.
In some embodiments, provided herein is the hollow-fibre membranes for bio-separation.Suitable for bio-separation Empty fiber membrane part is combined by protein and is characterized.In some embodiments, hollow-fibre membrane provided herein has and is less than About 30ng/cm2Protein combine.The film is made of blend polymer as described herein.On the other hand, provided herein is one Kind bio-separation device comprising multiple porous hollow fibers that perforated membrane provided herein is constituted.
In some embodiments, film as described herein is used for haemodialysis.Dialysis refers to being realized by one or more films Process, wherein mainly driving conveying by the pressure difference of the thickness across one or more films.Haemodialysis refers to dialysis Process, wherein not needing biologically and/or toxic solute is removed such as metabolin and by-product from blood.Haemodialysis Film is that low molecular weight solutes (usually less than 5,000 dalton) such as urea, kreatinin, uric acid, electrolyte and water is allowed to pass through, But prevent higher molecular weight protein and blood cell component by perforated membrane.Closer to the blood for representing renal glomerulus filtering Liquid filtering needs even higher infiltrative film so that and molecular weight is less than 50,000 dalton and in some cases less than 20, The solute of 000 dalton passes through completely.
Blend polymer as described herein assigns required engineering properties to manufacture and to support during use porous Hollow fiber film structure.In addition, blend polymer assigns thermal property appropriate, to reduce or prevent high-temp steam sterilizing mistake Degradation during journey.In addition, blend polymer and film have best biocompatibility so that protein be stained minimum and The thrombosis of processed blood will not occur.
Embodiment
Unless otherwise stated, chemicals is purchased from Aldrich and Sloss Industries and uses as former state. Bruker Avance 400(1H, 400 MHz) H NMR spectroscopy is recorded on spectrometer, and shifted with reference to residual solvent.Molecular weight is with number Average molecular weight (Mn) or weight average molecular weight (Mw) report, and analyzed equipped with UV detectors by gel permeation chromatography (GPC) It is measured on 200 instruments of Perkin Elmer Series.Polymer heat analysis is in the Perkin equipped with TAC7/DX thermal analyzers It carries out on Elmer DSC7 and is handled using Pyris softwares.
Glass transition temperature is recorded in second of heat scan.What is assessed using VCA optima softwares Contact-angle measurement is carried out on VCA 2000 (Advanced Surface Technology, Inc.) instrument.Polymer film is by the future From appropriate solution such as dimethyl sulfoxide (DMSO) (DMSO), the film of n-methyl-2-pyrrolidone (NMP) and dimethylacetylamide (DMAC) It is cast on clean glass slide and evaporates solvent and obtain.On the both sides (towards air and towards glass slide) of film determine with The advancing contact angle (73 dynes/cm) of water.It is assumed that since surface is more smooth, the side towards glass slide obtain always compared with Low value.
The synthesis of sulfone polymer with amphoteric ion functional group
The preparation of the polymer of formula (VII) and amphoteric ion (one-pot synthesis, the 3.25 moles of % chains ends for being finally derived as 45 moles of % Only agent) it carries out as follows:It feeds to the 5.0L three-neck flasks equipped with overhead mechanical stirrer, brachycephaly distilling apparatus and nitrogen entrance double Phenol A (BPA) (228.1g, 1.000 moles), N methyl piperazine bis-phenol amide (301.17g, 0.8182 mole), to cumyl benzene Phenol (12.468g, 0.0591 mole) and 1.60L N-Methyl pyrrolidones (NMP), leaching is in oil bath.The mixture is at room temperature Stirring, is then added portionwise potassium carbonate (401.5g, 2.909 moles), is subsequently added into 0.800L toluene.The mixture is slow Under nitrogen stream then heating is azeotroped off remaining water with dry reaction mixture to remove toluene.Oil bath temperature is from 125-150 DEG C gradually rise with remove most of toluene (> 90%).Then slurry is cooled to room temperature, the difluoro as solid is then added Reaction temperature is simultaneously gradually increased to 165 DEG C by diphenyl sulfone (469.63g, 1.8482 moles).During heating, at about 100 DEG C Observe mild heat release.Heating mixture and every two hours sampling are until reach required molecular weight (8-10 hours).Anti- Reaction viscosity increases during should running, and shows opaque light gray.When reaching required molecular weight, diluted with 0.8 liter of NMP Reactant is simultaneously cooled to 50 DEG C.Then 1,3-propane sultone (149.7g, 1.227 moles) and reaction mixture is gradual is added It is heated to 80 DEG C.Reaction is completed in ~ 4 hours.After the addition is complete, reaction color is shoaled gradually as greyish white mill base material.It is based on Solution viscosity, can further diluted reaction mixture.Then use high speed blender by mixture precipitation to 12.0L water, Generate white precipitate.Precipitation is collected by filtration, then repulped 6 hours in 5.0 heating water (40-50 DEG C).Pass through filtering Collect solid.It is initially dried 24 hours in 50 DEG C of polymer being dried to obtain under nitrogen purge under vacuum, then in 80- About 950 grams of polymer (~ 95% rate of recovery) after re-dry is dried for 24 hours with offer under full vacuum at 100 DEG C.
The casting of hollow-fibre membrane is carried out using methods known in the art and using method described herein.Polymer is total Mixed object by preparing polymer dissolving in a suitable solvent.By the way that blend polymer and any optional additive is molten Solution prepares the coating solution for hollow-fibre membrane of casting in a suitable solvent.
The test that protein combines
Nonspecific protein knot is measured using the immunoglobulin protein marked with horseradish peroxidase (HRP) functional group It closes.1 inch strip of each doughnut is placed in 35 × 10mm culture dishes and in phosphate buffered saline (PBS) (pH=7.4) Thoroughly washing from fiber to remove remaining glycerine, salt or pore-foaming agent.It is replaced with 10 μ g/ml HRP- protein solutions of 2ml PBS.After impregnating 2 hours, antibody-solutions are removed, and fiber is fully washed with PBS.Then fiber is cut into quarter, and by this Quarter is transferred to the hole of 24 orifice plates containing 0.5ml 50mM citrate-phosphate buffers (CPB) (pH=5) jointly In.Sample impregnates 30 minutes.
It is replaced with the 0.5ml solution based on CPB for containing 0.5mg/ml o-phenylenediamines (OPD) and 0.015% hydrogen peroxide CPB.HRP labels on protein convert OPD to the dissolved compound of yellow.After 3 minutes, low capacity one is transferred the solution into In secondary property cuvette.Absorbance is measured at 450nm to quantify the amount of the OPD of conversion, with non-specific adsorption to film surface On protein amount it is directly proportional.The amount passes through film surface product (including cross section of inner cavity and exocoel and exposure) normalization. As a result it shows in fig. 2.
Although having only illustrated and described certain features of the present invention herein, those skilled in the art will expect many modifications And variation.It is therefore understood that appended claims are intended to all such modifications that covering is fallen within the true spirit of the invention And variation.

Claims (28)

1. a kind of hollow-fibre membrane it includes the first polymer containing the sulfone polymer with amphoteric ion functional group and contains The blend of the second polymer of sulfone polymer.
2. the hollow-fibre membrane of claim 1, wherein described first comprising the sulfone polymer with amphoteric ion functional group is poly- Close the structural unit that object includes the Formulas I A or Formulas I B that are connect with the structural unit of Formula II:
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;
K is 0 to 10;
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;With
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
3. the hollow-fibre membrane of claim 1, wherein the second polymer comprising sulfone polymer include with Formula II, III, The structural unit of IV or IV structures:
Wherein
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;With
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
A and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
4. the hollow-fibre membrane of claim 1, wherein described first comprising the sulfone polymer with amphoteric ion functional group is poly- Close the structural unit that object includes the Formulas I A or Formulas I B that are connect with the structural unit of Formula II:
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;
K is 0 to 10;
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;With
Y' and R' is each independently hydrogen, C1-C20Alkyl or aryl ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;
M and n is each independently 0 or 1;With
The wherein described second polymer comprising sulfone polymer includes the structural unit with Formula II, the structure of IV or V:
5. the hollow-fibre membrane of claim 2, wherein described first comprising the sulfone polymer with amphoteric ion functional group is poly- Close the structural unit that object includes Formula IV:
Wherein w is 0,1,2 or 3.
6. the hollow-fibre membrane of claim 2, wherein described first comprising the sulfone polymer with amphoteric ion functional group is poly- Close the structural unit that object includes Formula VII:
Wherein P+Q=1, P=0.30-0.50, Q=0.50-0.70.
7. the hollow-fibre membrane of claim 6, wherein the amphoteric ion functionalized structure list of the Formulas I B in the first polymer About 30 moles of % to about 50 of the total mole number of the unit of Formulas I B and Formula II of the molar fraction of member in the first polymer rub Within the scope of your %.
8. the hollow-fibre membrane of claim 1, wherein described first comprising the sulfone polymer with amphoteric ion functional group is poly- The molecular weight of object is closed in the range of about 10000g/mol to about 80000g/mol.
9. the hollow-fibre membrane of claim 3, wherein the second polymer comprising sulfone polymer includes the knot containing Formula II The polysulfones of structure unit.
10. the hollow-fibre membrane of claim 3, wherein the second polymer comprising sulfone polymer includes the knot containing formula IV The polyphenylsulphine of structure unit.
11. the hollow-fibre membrane of claim 3, wherein the second polymer comprising sulfone polymer includes the knot containing Formula V The polyether sulfone of structure unit.
12. the hollow-fibre membrane of claim 1, wherein the amount of the second polymer comprising sulfone polymer is in the film The about 0.5 weight % to about 5 weight % of total polymer weight.
13. the hollow-fibre membrane of claim 1, wherein the molecular weight of the second polymer comprising sulfone polymer is about In the range of 50000g/mol to about 80000g/mol.
14. the hollow-fibre membrane of claim 4, wherein described first comprising the sulfone polymer with amphoteric ion functional group is poly- Close the structural unit that object includes the Formulas I B being connect with the structural unit of Formula II, and the second polymer packet comprising sulfone polymer Structural unit containing Formula II
15. the hollow-fibre membrane of claim 4, wherein described first comprising the sulfone polymer with amphoteric ion functional group is poly- Close the structural unit that object includes the Formulas I B being connect with the structural unit of Formula II, and the second polymer packet comprising sulfone polymer Structural unit containing formula IV
16. the hollow-fibre membrane of claim 4, wherein described first comprising the sulfone polymer with amphoteric ion functional group is poly- Close the structural unit that object includes the Formulas I B being connect with the structural unit of Formula II, and the second polymer packet comprising sulfone polymer Structural unit containing Formula V
17. a kind of hollow fiber membrane module, it includes the hollow-fibre membranes of multiple claims 14.
18. a kind of haemodialysis or blood filter device, it includes the hollow fiber membrane modules of claim 17.
19. a kind of hollow fiber membrane module, it includes the hollow-fibre membranes of multiple claims 15.
20. a kind of haemodialysis or blood filter device, it includes the hollow fiber membrane modules of claim 19.
21. a kind of hollow fiber membrane module, it includes the hollow-fibre membranes of multiple claims 16.
22. a kind of haemodialysis or blood filter device, it includes the hollow fiber membrane modules of claim 21.
23. a kind of composition it includes the first polymer containing the sulfone polymer with amphoteric ion functional group and contains sulfone The blend of the second polymer of polymer.
24. the composition of claim 23, wherein first polymerization comprising the sulfone polymer with amphoteric ion functional group Object includes the structural unit for the Formulas I B being connect with the structural unit of Formula II, and the second polymer comprising sulfone polymer includes The structural unit of Formula II:
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;
K is 0 to 10;
R3It independently is hydrogen atom, C with Y1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
25. the composition of claim 23, wherein first polymerization comprising the sulfone polymer with amphoteric ion functional group Object includes the structural unit for the Formulas I B being connect with the structural unit of Formula II, and the second polymer comprising sulfone polymer includes The structural unit of formula IV:
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;
K is 0 to 10;
R3It independently is hydrogen atom, C with Y1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
26. the composition of claim 23, wherein first polymerization comprising the sulfone polymer with amphoteric ion functional group Object includes the structural unit for the Formulas I B being connect with the structural unit of Formula II, and the second polymer comprising sulfone polymer includes The structural unit of Formula V:
Wherein
R1And R2It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base, C3-C12 Naphthenic base or aryl rings;
K is 0 to 10;
R3It independently is hydrogen atom, C with Y1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R4It is key, C1-C12Alkyl, C3-C12Naphthenic base or aryl rings;
R5And R6It independently is hydrogen atom, halogen atom, nitro, C at each occurrence1-C12Alkyl, C3-C12Naphthenic base or aryl Ring;
A, a' and b independently is 0,1,2,3 or 4 at each occurrence;With
M and n is each independently 0 or 1.
27. a kind of method for the hollow-fibre membrane forming claim 1, including:
(A) cast-solution that the blend comprising first polymer and second polymer is provided, wherein in the cast-solution Total polymer content is less than about 20% weight of the cast-solution;With
(B) cast-solution is squeezed out to form the hollow-fibre membrane by circular passage.
28. the method for claim 27, wherein the hollow-fibre membrane includes about 0.5 weight of the total polymer weight in the film % is measured to the second polymer of the amount of about 5 weight %.
CN201680070265.6A 2015-12-04 2016-12-02 Zwitterionic sulfone polymer blend and hollow fiber membranes Active CN108430613B (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US14/958,937 US20160136588A1 (en) 2014-11-19 2015-12-04 Zwitterionic sulfone polymer blend and hollow-fiber membrane
US14/958937 2015-12-04
PCT/US2016/064576 WO2017096140A1 (en) 2015-12-04 2016-12-02 Zwitterionic sulfone polymer blend and hollow-fiber membrane

Publications (2)

Publication Number Publication Date
CN108430613A true CN108430613A (en) 2018-08-21
CN108430613B CN108430613B (en) 2022-02-11

Family

ID=58797853

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201680070265.6A Active CN108430613B (en) 2015-12-04 2016-12-02 Zwitterionic sulfone polymer blend and hollow fiber membranes

Country Status (4)

Country Link
EP (1) EP3383524A4 (en)
JP (1) JP6983159B2 (en)
CN (1) CN108430613B (en)
WO (1) WO2017096140A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114786795A (en) * 2019-12-05 2022-07-22 索尔维特殊聚合物美国有限责任公司 Process for preparing poly (aryl ether sulfone) (PAES) polymers

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10851241B2 (en) 2014-11-19 2020-12-01 Cytiva Sweden Ab Zwitterion-functionalized multicomponent copolymers and associated polymer blends and membranes
WO2019219486A1 (en) * 2018-05-15 2019-11-21 General Electric Company Zwitterion-functionalized multicomponent copolymers and associated polymer blends and membranes
CN114941184A (en) * 2022-06-29 2022-08-26 山东海科创新研究院有限公司 Preparation method of spinning solution, spinning solution and filtering membrane

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4758343A (en) * 1985-09-20 1988-07-19 Toray Industries, Inc. Interfacially synthesized reverse osmosis membrane
US4970034A (en) * 1988-09-23 1990-11-13 W. R. Grace & Co.-Conn. Process for preparing isotropic microporous polysulfone membranes
JP2003320229A (en) * 2002-04-30 2003-11-11 Asahi Kasei Corp Modified hollow fiber membrane
JP2005137996A (en) * 2003-11-05 2005-06-02 Toyobo Co Ltd Permselective separation membrane
US20100044314A1 (en) * 2008-08-25 2010-02-25 General Electric Company Polyarylether compositions bearing zwitterion functionalities
CN102029117A (en) * 2009-09-29 2011-04-27 中国科学院大连化学物理研究所 Method for modifying surface of ultrafiltration membrane
CN102294176A (en) * 2011-08-17 2011-12-28 浙江大学 High permeability nanofiltration membrane containing zwitterion and preparation method thereof
CN104208766A (en) * 2014-08-26 2014-12-17 东华大学 High-stain-resistance polyether sulfone blood purifier and manufacturing method thereof
CN104607068A (en) * 2015-01-20 2015-05-13 苏州信望膜技术有限公司 Bio-adhesion-resistant porous separation membrane as well as preparation method and application thereof
CN104804195A (en) * 2015-01-13 2015-07-29 西北大学 Mussel-adhered and cytomembrane antifouling double-bionic multi-armed PEG and preparation method thereof

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5043398A (en) * 1989-05-12 1991-08-27 Hoechst Celanese Corporation Grafting of functional compounds onto functional oxymethylene polymer backbones, with diisocyanate coupling agents, and the graft polymers thereof
US5071448A (en) * 1990-12-05 1991-12-10 Union Carbide Industrial Gases Technology Corporation Semipermeable membranes based on certain sulfonated substituted polysulfone polymers
JP2008284521A (en) * 2007-05-21 2008-11-27 Takuma Co Ltd Method of manufacturing hollow fiber type amphoteric charge membrane
EP2253367B1 (en) * 2009-05-20 2014-11-19 Gambro Lundia AB Membranes having improved performance
JP6109492B2 (en) * 2012-05-22 2017-04-05 株式会社ダイセル NF flat membrane and its manufacturing method
US9440198B2 (en) * 2014-05-16 2016-09-13 General Electric Company Zwitterion-functionalized block copolymer membranes and associated block copolymer composition
US9085542B1 (en) * 2014-06-12 2015-07-21 General Electric Company Method for synthesis of N-methyl piperazine diphenolamide and related composition
US20160136587A1 (en) * 2014-11-19 2016-05-19 General Electric Company Zwitterion-functionalized copolymer hollow-fiber membranes and associated method

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4758343A (en) * 1985-09-20 1988-07-19 Toray Industries, Inc. Interfacially synthesized reverse osmosis membrane
US4970034A (en) * 1988-09-23 1990-11-13 W. R. Grace & Co.-Conn. Process for preparing isotropic microporous polysulfone membranes
JP2003320229A (en) * 2002-04-30 2003-11-11 Asahi Kasei Corp Modified hollow fiber membrane
JP2005137996A (en) * 2003-11-05 2005-06-02 Toyobo Co Ltd Permselective separation membrane
US20100044314A1 (en) * 2008-08-25 2010-02-25 General Electric Company Polyarylether compositions bearing zwitterion functionalities
CN102029117A (en) * 2009-09-29 2011-04-27 中国科学院大连化学物理研究所 Method for modifying surface of ultrafiltration membrane
CN102294176A (en) * 2011-08-17 2011-12-28 浙江大学 High permeability nanofiltration membrane containing zwitterion and preparation method thereof
CN104208766A (en) * 2014-08-26 2014-12-17 东华大学 High-stain-resistance polyether sulfone blood purifier and manufacturing method thereof
CN104804195A (en) * 2015-01-13 2015-07-29 西北大学 Mussel-adhered and cytomembrane antifouling double-bionic multi-armed PEG and preparation method thereof
CN104607068A (en) * 2015-01-20 2015-05-13 苏州信望膜技术有限公司 Bio-adhesion-resistant porous separation membrane as well as preparation method and application thereof

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
IDRIS A ET AL.: "novel high performance hollow fiber ultrafiltration membranes spun from LiBr droped solutions", 《DESALINATION》 *
ZHANG Q ET AL.: "novel zwitterionic poly(arylene ether sulfone)s as antifouling membrane material", 《JOURNAL OR MEMBRANE SCIENCE》 *
ZHANG QIANG ET AL.: "synthesis and characterization of novel cardo poly(aryl ether sulfone) bearing zwitterionic side groups for proton exchange membranes", 《INTERNATION JOURNAL OF HYDROGEN ENERGY》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114786795A (en) * 2019-12-05 2022-07-22 索尔维特殊聚合物美国有限责任公司 Process for preparing poly (aryl ether sulfone) (PAES) polymers

Also Published As

Publication number Publication date
JP6983159B2 (en) 2021-12-17
EP3383524A1 (en) 2018-10-10
EP3383524A4 (en) 2019-07-24
WO2017096140A1 (en) 2017-06-08
JP2019501013A (en) 2019-01-17
CN108430613B (en) 2022-02-11

Similar Documents

Publication Publication Date Title
CN108430613A (en) Amphoteric ion sulfone polymer blend and hollow-fibre membrane
CA2949193C (en) Zwitterion-functionalized block copolymer membranes and associated block copolymer composition
US7681741B2 (en) Functional polyarylethers
WO2013156598A1 (en) Ultrafiltration membranes fabricated from sulfonated polyphenylenesulfones
AU2014307032A1 (en) Process for making polyarylethers and use in membrane preparation
US20210322933A1 (en) Zwitterion-functionalized copolymer hollow-fiber membranes and associated method
US20160136589A1 (en) Zwitterionic sulfone polymer flat sheet membrane
US20160136588A1 (en) Zwitterionic sulfone polymer blend and hollow-fiber membrane
JP2023126212A (en) Membrane manufacturing with cosolvent in polymer dope solution
EP3383523A1 (en) Zwitterionic sulfone polymer flat sheet membrane
WO2008073537A1 (en) Functional polyaryleters
US20230001362A1 (en) Process for preparing a poly(aryl ether sulfone) (paes) polymer
KR20150033378A (en) A novel preparation method of hydrophilic membrane having excellent water permeability, size exclusion selectivity, and anti-fouling using the blend solution of PVDF and partially sulfonated polyarylene-based polymers
EP3794056A1 (en) Zwitterion-functionalized multicomponent copolymers and associated polymer blends and membranes
EP3571242B1 (en) New membranes
WO2024078975A1 (en) Polyarylethersulfone copolymer having improved hydrophilicity
WO2018197341A1 (en) Aromatic sulfone polymers comprising (per)fluoropolyether segments
WO2015024958A1 (en) Polyarylnitrile copolymer membranes
KR20230119135A (en) Bio-based sulfone copolymer free of BPA and BPS
JP2024502866A (en) A new method for separating propylene from gas mixtures (GM) containing propylene and propane

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
CB02 Change of applicant information

Address after: uppsala

Applicant after: Stoivan Sweden Ltd.

Address before: uppsala

Applicant before: GE HEALTHCARE BIO-SCIENCES AB

CB02 Change of applicant information
TA01 Transfer of patent application right

Effective date of registration: 20201028

Address after: uppsala

Applicant after: GE HEALTHCARE BIO-SCIENCES AB

Address before: New York State, USA

Applicant before: General Electric Co.

TA01 Transfer of patent application right
GR01 Patent grant
GR01 Patent grant