CN117046327A - Hollow fiber membrane with good biocompatibility and application thereof - Google Patents

Hollow fiber membrane with good biocompatibility and application thereof Download PDF

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Publication number
CN117046327A
CN117046327A CN202311309320.0A CN202311309320A CN117046327A CN 117046327 A CN117046327 A CN 117046327A CN 202311309320 A CN202311309320 A CN 202311309320A CN 117046327 A CN117046327 A CN 117046327A
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Prior art keywords
hollow fiber
fiber membrane
aromatic
grafted
membrane according
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CN202311309320.0A
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Chinese (zh)
Inventor
杨正根
付守军
徐凌燕
吴硕莹
练明
陈校园
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Guangzhou Kangsheng Biotechnology Co ltd
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Guangzhou Kangsheng Biotechnology Co ltd
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Priority to CN202311309320.0A priority Critical patent/CN117046327A/en
Publication of CN117046327A publication Critical patent/CN117046327A/en
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    • 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
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0002Organic membrane manufacture
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/36Hydrophilic membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/58Biocompatibility of membrane

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Artificial Filaments (AREA)

Abstract

The invention discloses a hollow fiber membrane with good biocompatibility, which comprises a polysulfone/polyethersulfone matrix component and a grafted aromatic hydrophobic polymer with the mass content of 30-100% of the matrix component, wherein the preparation method of the grafted aromatic hydrophobic polymer comprises the following steps: dissolving aromatic diamine in an organic solvent, adding aromatic dianhydride, performing polymerization reaction for 4-10h, adding polyamine, stirring and dissolving, performing secondary reaction for 2-4 h, and finally adding an anticoagulant containing carboxyl, and performing grafting reaction for 12-48h to obtain the grafted aromatic hydrophobic polymer. The hollow fiber membrane has stable performance, can effectively reduce deposition of prothrombin, fibrin and the like, obviously improves anticoagulation effect and greatly improves biocompatibility.

Description

Hollow fiber membrane with good biocompatibility and application thereof
Technical Field
The invention relates to the field of biological materials, in particular to a hollow fiber membrane with good biocompatibility and application thereof.
Background
Polysulfone/polyethersulfone is a polymer material with excellent comprehensive properties, has excellent heat resistance, physical and mechanical properties, insulating properties, relatively good biocompatibility and the like, and has been widely used in a plurality of fields. Polysulfone/polyethersulfone also has good film forming and filtration properties, and thus is one of the most common hollow fiber membrane preparation materials.
However, the polysulfone/polyethersulfone membrane material has strong hydrophobic effect and strong polarity of sulfur and oxygen atoms existing in the structure, so that the polysulfone/polyethersulfone membrane material has strong adhesion effect on blood platelets and the like when being applied to clinical blood contact, and the porous structure of the fibrous membrane material is easy to deposit prothrombin and fibrin in pores of the fibrous membrane, so that a coagulation system is activated, thrombus is induced to form, protein pollution is easy to occur after long-term use, and further a pore blocking phenomenon occurs.
In order to improve the anticoagulation and anti-pollution performance of the polysulfone/polyethersulfone membrane material, three methods are mainly adopted: (1) Performing body modification, namely performing anticoagulation modification on a polysulfone/polyether sulfone material body, and then preparing a fibrous membrane; (2) Surface modification, grafting self-anticoagulation polymer on the surface of the fiber by a chemical method, a photochemical method or a plasma technology, or coating the self-anticoagulation polymer on the surface by a physical method; (3) Blending modification, namely blending polysulfone/polyether sulfone with self-coagulation-resistant functional polymer to form spinning solution, and finally spinning to form a film.
The polysulfone/polyethersulfone bulk material has stable performance, is very difficult to modify, and is generally applied to hollow fiber membrane materials with smaller diameters by surface grafting and coating modification, so that the mass production and the application are difficult to realize. At present, a physical blending modification method is mainly adopted to improve the anticoagulation performance of the polysulfone/polyether sulfone fibrous membrane. For example, polyvinyl pyrrolidone (PVP), a zwitterionic compound (MPC of polyphosphoester) and a sulfonated functional polymer are mixed into a polysulfone/polyethersulfone film-forming liquid, and finally spun into a film. However, the hydrophilic additive can be slowly separated out in the use process of the hollow fiber membrane obtained by the modification method, and the performance stability is not high; even if amphiphilic polymers are used, the problem of large phase separation still exists, and the strength and mechanical properties of the fiber membrane are easily reduced, so that the filtration stability of the membrane is reduced.
Disclosure of Invention
The invention aims to overcome at least one defect of the prior art and provide a hollow fiber membrane with good biocompatibility and application thereof.
The technical scheme adopted by the invention is as follows:
in a first aspect, the present invention provides a hollow fiber membrane with good biocompatibility, the components of the hollow fiber membrane comprise a polysulfone/polyethersulfone matrix component and a grafted aromatic hydrophobic polymer with a mass content of 30% -100% of the matrix component, wherein the preparation method of the grafted aromatic hydrophobic polymer comprises the following steps:
1) Dissolving aromatic diamine in an organic solvent, adding aromatic dianhydride, and carrying out polymerization reaction for 4-10h to obtain a polyamic acid solution;
2) Adding polyamine into the polyamic acid solution prepared in the step 1), stirring and dissolving, and carrying out secondary reaction for 2-4 h;
3) Adding an anticoagulant containing carboxyl into the solution obtained in the step 2), and carrying out grafting reaction for 12-48 hours to obtain the grafted aromatic hydrophobic polymer.
In some examples, the aromatic dianhydride of step 1) is selected from any one of 3,3',4, 4' -benzophenone tetracarboxylic dianhydride, 4, 4' -hexafluoroisopropylidene-phthalic anhydride, 3',4, 4' -biphenyl tetracarboxylic dianhydride, 1, 2',4, 5' -pyromellitic anhydride, 3',4, 4' -diphenylsulfone tetracarboxylic dianhydride, or phthalic anhydride.
In some examples, the aromatic diamine of step 1) is selected from any one of 3,3' -dimethyl-4, 4' -diphenyl methane diamine, 4, 4' -diamino diphenyl methane, 4, 4' -diphenyl methane diisocyanate, or 4, 4' -diamino diphenyl ether, p-phenylenediamine.
In some examples, the molar ratio of aromatic dianhydride to aromatic diamine is: (1-1.05): 1.
in some examples, the polyamine of step 2) is selected from one or more of ethylenediamine, propylenediamine, tris (2-aminoethyl) amine, and quaternium.
In some examples, the molar ratio of the polyamine to the aromatic dianhydride is (2 to 2.05): 1.
in some examples, the organic solvent in step 1) is selected from at least one of dimethyl sulfoxide, N-methyl-2-pyrrolidone, N-dimethylformamide, and N, N-dimethylacetamide.
In some examples, the anticoagulant containing a carboxyl group is selected from heparin or heparin analogues.
In some examples, the method of making a hollow fiber membrane comprises the steps of: stirring and dissolving polysulfone/polyether sulfone, grafted aromatic hydrophobic polymer, water-soluble pore-forming agent and spinning solution solvent at 80-180 ℃, centrifugally filtering, standing at 40-80 ℃ for 2-24 hours to defoam to obtain spinning solution, and carrying out dry spinning or wet spinning, washing, stretching and drying on the spinning solution to obtain the modified hollow fiber membrane.
In some examples, the mass ratio of each component in the spinning solution is: 20-60 parts of polysulfone/polyether sulfone, 20-40 parts of grafted aromatic hydrophobic polymer, 0.1-10 parts of water-soluble pore-forming agent and 100-300 parts of spinning solution solvent.
In a second aspect, the invention provides an application of a hollow fiber membrane with good biocompatibility in preparing a blood purification material.
The beneficial effects of the invention are as follows:
according to some examples of the invention, the aromatic hydrophobic polymer grafted with the anticoagulant is blended with polysulfone/polyethersulfone for modification, and the anticoagulant group is directly obtained on the surface of the prepared hollow fiber membrane, so that the subsequent anticoagulant modification of the hollow fiber membrane is not needed, and the purpose of continuous anticoagulant modification is realized.
According to some examples of the invention, the grafted aromatic hydrophobic polymer has obvious hydrophobicity, good blending effect with polysulfone/polyethersulfone, difficult phase separation and stable performance of the hollow fiber membrane;
in some examples of the invention, the grafted aromatic hydrophobic polymer and polysulfone/polyethersulfone are blended, and the surface side branches have a large amount of amino groups, so that the hydrophilic effect of the hollow fiber membrane can be additionally improved and the biocompatibility can be improved according to the similar compatibility principle.
Detailed Description
The hollow fiber membrane with good biocompatibility comprises a polysulfone/polyethersulfone matrix component and a grafted aromatic hydrophobic polymer with the mass content of 30-100% of the matrix component, wherein the preparation method of the grafted aromatic hydrophobic polymer comprises the following steps:
1) Dissolving aromatic diamine in an organic solvent, adding aromatic dianhydride, and carrying out polymerization reaction for 4-10h to obtain a polyamic acid solution;
2) Adding polyamine into the polyamic acid solution prepared in the step 1), stirring and dissolving, and carrying out secondary reaction for 2-4 h;
3) Adding an anticoagulant containing carboxyl into the solution obtained in the step 2), and carrying out grafting reaction for 12-48 hours to obtain the grafted aromatic hydrophobic polymer.
In some examples, the aromatic dianhydride of step 1) is selected from any one of 3,3',4, 4' -benzophenone tetracarboxylic dianhydride, 4, 4' -hexafluoroisopropylidene-phthalic anhydride, 3',4, 4' -biphenyl tetracarboxylic dianhydride, 1, 2',4, 5' -pyromellitic anhydride, 3',4, 4' -diphenylsulfone tetracarboxylic dianhydride, or phthalic anhydride. The raw materials have wide sources and good stability.
In some examples, the aromatic diamine of step 1) is selected from any one of 3,3' -dimethyl-4, 4' -diphenyl methane diamine, 4, 4' -diamino diphenyl methane, 4, 4' -diphenyl methane diisocyanate, or 4, 4' -diamino diphenyl ether, p-phenylenediamine. These aromatic diamines are relatively widely available and have good stability.
In some examples, the molar ratio of aromatic dianhydride to aromatic diamine is: (1-1.05): 1, thus ensuring a sufficient reaction.
In some examples, the polyamine of step 2) is selected from one or more of ethylenediamine, propylenediamine, tris (2-aminoethyl) amine, and quaternium.
In some examples, the molar ratio of the polyamine to the aromatic dianhydride is (2 to 2.05): 1.
in some examples, the organic solvent in step 1) is selected from at least one of dimethyl sulfoxide, N-methyl-2-pyrrolidone, N-dimethylformamide, and N, N-dimethylacetamide.
The existence of carboxyl is more beneficial to the anticoagulant grafting reaction. In some examples, the anticoagulant containing a carboxyl group is selected from heparin or heparin analogues. Heparin or heparin analogues have good anticoagulation effect and safety is verified in a long-term use process.
In some examples, the method of making a hollow fiber membrane comprises the steps of: stirring and dissolving polysulfone/polyether sulfone, grafted aromatic hydrophobic polymer, water-soluble pore-forming agent and spinning solution solvent at 80-180 ℃, centrifugally filtering, standing at 40-80 ℃ for 2-24 hours to defoam to obtain spinning solution, and carrying out dry spinning or wet spinning, washing, stretching and drying on the spinning solution to obtain the modified hollow fiber membrane.
In some examples, the mass ratio of each component in the spinning solution is: 20-60 parts of polysulfone/polyether sulfone, 20-40 parts of grafted aromatic hydrophobic polymer, 0.1-10 parts of water-soluble pore-forming agent and 100-300 parts of spinning solution solvent.
The following disclosure provides many different embodiments, or examples, for implementing different aspects of the invention.
The preparation method of the grafted aromatic hydrophobic polymer of examples 1 to 3 in the present invention is as follows:
1. and (3) measuring a certain amount of strong polar solvent, gradually adding a certain amount of diamine under the protection of nitrogen, stirring for 2 hours until the diamine is completely dissolved, gradually adding dianhydride, and stirring for 4-10 hours to obtain the polyamic acid stock solution. Wherein each substance and the content thereof are shown in the following table 1.
2. Adding polyamine to the solution obtained in the step (1), wherein the molar ratio of the polyamine to the aromatic dianhydride in the step (1) is 2.05:1, stirring for 2 hours to dissolve, and then continuing stirring for 4-10 hours.
3. Adding 10mg of heparin/heparin analogue into the solution obtained in the step (2), fully stirring and dissolving, and soaking for 12-48 hours to obtain the aromatic hydrophobic polymer solution.
TABLE 1
The preparation methods of the modified hollow fiber membranes in the examples and comparative examples of the present invention are as follows:
1) According to the raw material components and mass ratio in Table 2, polysulfone/polyether sulfone, blending resin, water-soluble pore-forming agent and spinning solution solvent are respectively weighed, stirred and dissolved at 100 ℃ to form transparent solution, centrifugally filtered, and kept stand at 80 ℃ for 4 hours to defoam to obtain spinning solution.
2) Extruding the spinning solution obtained in the step 1 from a spinneret at an extrusion speed of 3-15mL/min by using spinning equipment, performing air bath of 5-50cm in air, performing solidification molding in a water bath of 20-50 ℃, winding and molding at a speed of 5-50m/min, soaking the molded fiber filaments in water, removing residual solvent and unreacted raw materials, and drying to obtain the hollow fiber membrane.
Wherein the water-soluble pore-forming agent can be at least one selected from polyethylenimine, polyethylene glycol 800, polyethylene glycol 1000, polyethylene glycol 2000, polyvinylpyrrolidone, polyacrylic acid, polyvinyl alcohol, tween-20, tween-60, tween-80, sodium sorbate, potassium sorbate, sodium citrate, sodium laurate, sodium alginate, sodium lysinate, sodium ethylenediamine tetraacetate, sodium N-tetradecanecarbonate, sodium dodecylsulfonate, sodium octoate, sodium caproate, sodium propionate, sodium acetate, sodium oxalate, lithium acetate, sodium chloride, lithium chloride, calcium chloride or copper chloride, and the spinning solution solvent is at least one selected from dimethyl sulfoxide, N-methyl-2-pyrrolidone, N-dimethylformamide and N, N-dimethylacetamide.
TABLE 2
Performance tests were then performed on examples 4-7 and comparative examples 1-2, with the test results shown in table 3 below:
TABLE 3 Table 3
Conclusion:
it can be seen that the hollow fiber membrane prepared by the invention has no obvious change in ultrafiltration coefficient and does not affect dialysis performance compared with the fiber membrane of comparative example 1 which is not subjected to hydrophilic modification; the water contact angle is obviously reduced, and the hydrophilicity is obviously improved; the pure water flux recovery rate is obviously improved after hemodialysis, which indicates that the modified hollow fiber membrane reduces deposition of prothrombin, fibrin and the like; APTT (activated partial thromboplastin time) is obviously prolonged and anticoagulation effect is obviously improved.
The hydrophilicity and anticoagulation effect are also increased to some extent as compared with a hollow fiber membrane modified with only polyvinylpyrrolidone.
The above description of the present invention is further illustrated in detail and should not be taken as limiting the practice of the present invention. It is within the scope of the present invention for those skilled in the art to make simple deductions or substitutions without departing from the concept of the present invention.

Claims (10)

1. The hollow fiber membrane with good biocompatibility is characterized in that the components of the hollow fiber membrane comprise polysulfone/polyethersulfone matrix components and grafted aromatic hydrophobic polymers with the mass content of 30% -100% of the matrix components, wherein the preparation method of the grafted aromatic hydrophobic polymers comprises the following steps:
1) Dissolving aromatic diamine in an organic solvent, adding aromatic dianhydride, and carrying out polymerization reaction for 4-10h to obtain a polyamic acid solution;
2) Adding polyamine into the polyamic acid solution prepared in the step 1), stirring and dissolving, and carrying out secondary reaction for 2-4 h;
3) Adding an anticoagulant containing carboxyl into the solution obtained in the step 2), and carrying out grafting reaction for 12-48 hours to obtain the grafted aromatic hydrophobic polymer.
2. The hollow fiber membrane according to claim 1, wherein the aromatic dianhydride of step 1) is selected from any one of 3,3',4, 4' -benzophenone tetracarboxylic dianhydride, 4, 4' -hexafluoroisopropylidene-phthalic anhydride, 3',4, 4' -biphenyl tetracarboxylic dianhydride, 1, 2',4, 5' -pyromellitic anhydride, 3',4, 4' -diphenylsulfone tetracarboxylic dianhydride or phthalic anhydride.
3. The hollow fiber membrane according to claim 1, wherein the aromatic diamine of step 1) is selected from any one of 3,3' -dimethyl-4, 4' -diphenyl methane diamine, 4, 4' -diaminodiphenyl methane, 4, 4' -diphenyl methane diisocyanate, 4, 4' -diaminodiphenyl ether and p-phenylenediamine.
4. A hollow fiber membrane according to claim 2 or 3, characterized in that the molar ratio of aromatic dianhydride to aromatic diamine is: (1-1.05): 1.
5. the hollow fiber membrane of claim 1, wherein the polyamine of step 2) is selected from one or more of ethylenediamine, propylenediamine, tris (2-aminoethyl) amine, and quaternium.
6. The hollow fiber membrane according to claim 2 or 5, wherein the molar ratio of the polyamine to the aromatic dianhydride is (2 to 2.05): 1.
7. the hollow fiber membrane according to claim 1, wherein the organic solvent in step 1) is selected from at least one of dimethyl sulfoxide, N-methyl-2-pyrrolidone, N-dimethylformamide, and N, N-dimethylacetamide; and/or
The anticoagulant containing carboxyl groups is selected from heparin or heparin analogues.
8. The hollow fiber membrane according to claim 1, wherein the preparation method of the hollow fiber membrane comprises the steps of: stirring and dissolving polysulfone/polyether sulfone, grafted aromatic hydrophobic polymer, water-soluble pore-forming agent and spinning solution solvent at 80-180 ℃, centrifugally filtering, standing at 40-80 ℃ for 2-24 hours to defoam to obtain spinning solution, and carrying out dry spinning or wet spinning, washing, stretching and drying on the spinning solution to obtain the modified hollow fiber membrane.
9. The hollow fiber membrane according to claim 8, wherein the mass ratio of each component in the spinning solution is: 20-60 parts of polysulfone/polyether sulfone, 20-40 parts of grafted aromatic hydrophobic polymer, 0.1-10 parts of water-soluble pore-forming agent and 100-300 parts of spinning solution solvent.
10. Use of a hollow fiber membrane according to any one of claims 1 to 9 with good biocompatibility for the preparation of a blood purification material.
CN202311309320.0A 2023-10-11 2023-10-11 Hollow fiber membrane with good biocompatibility and application thereof Pending CN117046327A (en)

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CN202311309320.0A CN117046327A (en) 2023-10-11 2023-10-11 Hollow fiber membrane with good biocompatibility and application thereof

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Application Number Priority Date Filing Date Title
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