CN110903576B - Preparation method of polyvinylidene fluoride composite material, polyvinylidene fluoride composite membrane, preparation method and application thereof - Google Patents

Preparation method of polyvinylidene fluoride composite material, polyvinylidene fluoride composite membrane, preparation method and application thereof Download PDF

Info

Publication number
CN110903576B
CN110903576B CN201911254086.XA CN201911254086A CN110903576B CN 110903576 B CN110903576 B CN 110903576B CN 201911254086 A CN201911254086 A CN 201911254086A CN 110903576 B CN110903576 B CN 110903576B
Authority
CN
China
Prior art keywords
polyvinylidene fluoride
fluoride composite
composite membrane
preparation
organic framework
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.)
Active
Application number
CN201911254086.XA
Other languages
Chinese (zh)
Other versions
CN110903576A (en
Inventor
覃慧
陈舒忆
王壹
聂胜强
成刚
罗军
陶泽志
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.)
Guiyang University
Original Assignee
Guiyang University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Guiyang University filed Critical Guiyang University
Priority to CN201911254086.XA priority Critical patent/CN110903576B/en
Publication of CN110903576A publication Critical patent/CN110903576A/en
Application granted granted Critical
Publication of CN110903576B publication Critical patent/CN110903576B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L27/00Materials for grafts or prostheses or for coating grafts or prostheses
    • A61L27/14Macromolecular materials
    • A61L27/16Macromolecular materials obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L27/00Materials for grafts or prostheses or for coating grafts or prostheses
    • A61L27/50Materials characterised by their function or physical properties, e.g. injectable or lubricating compositions, shape-memory materials, surface modified materials
    • A61L27/507Materials characterised by their function or physical properties, e.g. injectable or lubricating compositions, shape-memory materials, surface modified materials for artificial blood vessels
    • 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
    • B01D69/12Composite membranes; Ultra-thin membranes
    • 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
    • B01D71/30Polyalkenyl halides
    • B01D71/32Polyalkenyl halides containing fluorine atoms
    • B01D71/34Polyvinylidene fluoride
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2327/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
    • C08J2327/02Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
    • C08J2327/12Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • C08J2327/16Homopolymers or copolymers of vinylidene fluoride
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2487/00Characterised by the use of unspecified macromolecular compounds, obtained otherwise than by polymerisation reactions only involving unsaturated carbon-to-carbon bonds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/02Applications for biomedical use

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Dermatology (AREA)
  • General Health & Medical Sciences (AREA)
  • Veterinary Medicine (AREA)
  • Public Health (AREA)
  • Animal Behavior & Ethology (AREA)
  • Oral & Maxillofacial Surgery (AREA)
  • Transplantation (AREA)
  • Epidemiology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Polymers & Plastics (AREA)
  • Vascular Medicine (AREA)
  • Organic Chemistry (AREA)
  • External Artificial Organs (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The application provides a preparation method of a polyvinylidene fluoride composite material, a polyvinylidene fluoride composite membrane, a preparation method and application thereof, and belongs to the technical field of functional polymer materials. The preparation method of the polyvinylidene fluoride composite material comprises the following steps: dispersing a metal organic framework in a polar organic solvent, then adding polyvinylidene fluoride, and dispersing for 4-10h at the temperature of 50-70 ℃ to obtain a composite material. The preparation method of the polyvinylidene fluoride composite membrane comprises the steps of defoaming, curing and coating the polyvinylidene fluoride composite mixture in sequence. The polyvinylidene fluoride composite membrane prepared by the method has good adsorption capacity and certain blood compatibility, and can be used as a blood contact material.

Description

Preparation method of polyvinylidene fluoride composite material, polyvinylidene fluoride composite membrane, preparation method and application thereof
Technical Field
The application relates to the technical field of functional polymer materials, in particular to a preparation method of a polyvinylidene fluoride composite material, a polyvinylidene fluoride composite membrane, a preparation method and application thereof.
Background
Metal-Organic Frameworks (MOFs) are inorganic-Organic composites formed by self-assembly of Metal ions and Organic ligands with multiple functional groups into crystalline porous materials with periodic network structures. The metal organic framework material is mainly characterized by high porosity and huge specific surface area due to the combination of the properties of a periodic network hole structure and an organic material framework. In recent years, the application field of the metal organic framework material with controllable functional groups in the molecular structure is more and more extensive by designing and synthesizing the metal organic framework material. The catalyst has great application potential in the aspects of hydrogen storage, drug delivery, catalysis, selective separation and the like due to the characteristics of harmonious pore channel shape, size, obvious stability and the like.
The metal organic framework material MIL-100-Fe has good adsorption performance due to the polar functional group and molecular pores in the structure, but has poor film forming property, so the metal organic framework material MIL-100-Fe cannot be directly used for preparing the anti-pollution material.
Disclosure of Invention
The polyvinylidene fluoride composite membrane has good blood compatibility and can be used for preparing blood contact materials.
In a first aspect, an embodiment of the present application provides a preparation method of a polyvinylidene fluoride composite material, including: dispersing a metal organic framework material MIL-100-Fe in a polar organic solvent, then adding polyvinylidene fluoride, and dispersing for 4-10h at the temperature of 50-70 ℃ to obtain a composite material.
Wherein the structural formula of the metal organic framework material MIL-100-Fe is as follows:
Figure BDA0002309347960000021
in a second aspect, embodiments of the present application provide a preparation method of a polyvinylidene fluoride composite film, where the polyvinylidene fluoride composite material is subjected to defoaming, curing, and coating in sequence to obtain the polyvinylidene fluoride composite film.
In a third aspect, an embodiment of the present application provides a polyvinylidene fluoride composite film prepared by the above polyvinylidene fluoride composite film preparation method.
In a fourth aspect, the present application provides an application of a polyvinylidene fluoride composite membrane in preparation of a blood contact material.
The preparation method of the polyvinylidene fluoride composite material, the polyvinylidene fluoride composite film, the preparation method and the application of the polyvinylidene fluoride composite material provided by the embodiment of the application have the beneficial effects that:
the polyvinylidene fluoride composite membrane is prepared by defoaming, curing and coating the composite mixture, and the metal organic framework material MIL-100-Fe has good stability, and cannot be decomposed and precipitated from a polyvinylidene fluoride composite membrane matrix in the using process, so that the obtained polyvinylidene fluoride composite membrane has good adsorption performance without adding a pore-forming agent, has blood compatibility, can have the performance of resisting platelet activation and complement activation, and can be used as a blood contact material.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present application clearer, the technical solutions of the embodiments of the present application will be clearly and completely described below. The examples, in which specific conditions are not specified, were conducted under conventional conditions or conditions recommended by the manufacturer. The reagents or instruments used are not indicated by the manufacturer, and are all conventional products available commercially.
The preparation method of the polyvinylidene fluoride composite membrane provided by the embodiment of the application comprises the following steps:
s10, preparing a metal organic framework material MIL-100-Fe:
dispersing trimesic acid and ferric ions in a polar organic solvent, and reacting for 16-24h at the temperature of 110-130 ℃ to obtain the metal organic framework material MIL-100-Fe.
Wherein the molar ratio of the trimesic acid to the ferric ions is 1:4-1:6, so that the trimesic acid can be converted into the metal-organic framework material MIL-100-Fe more. For example: the molar ratio of the trimesic acid to the ferric ions is 1:4, 1:5 or 1: 6. Alternatively, the source of ferric ions may be FeCl3Or Fe (NO)3)3
Optionally, the polar organic solvent is a combination of one or more selected from the group consisting of N-methylpyrrolidone, dimethylacetamide, and N, N' -dimethylformamide. For example: the polar organic solvent is N-methyl pyrrolidone; the polar organic solvent is dimethylacetamide; the polar organic solvent is N, N' -dimethylformamide; the polar organic solvent is a mixture of N-methyl pyrrolidone and dimethylacetamide; the polar organic solvent is a mixture of N-methyl pyrrolidone and N, N' -dimethylformamide; the polar organic solvent is a mixture of N-methylpyrrolidone, dimethylacetamide and N, N' -dimethylformamide.
Mixing trimesic acid and FeCl3Dispersing in a polar organic solvent, and reacting for 16-24h at the temperature of 110-130 ℃ to obtain the metal organic framework material MIL-100-Fe. The reaction temperature is high, so that the metal organic framework material MIL-100-Fe is obtained through reaction. Further, the temperature of the reaction may be 110 ℃, 120 ℃ or 130 ℃; the reaction time may be 16h, 20h or 24 h.
After the reaction is completed, the reaction is stopped, partial impurities (such as trimesic acid) which are not reacted can exist in the product, the reaction liquid is cooled to 20 ℃, the unreacted trimesic acid is washed by ethanol, and then the drying is carried out at the temperature of 80 ℃, and then the grinding is carried out to obtain the metal organic framework material MIL-100-Fe.
Wherein the structural formula of the metal organic framework material MIL-100-Fe is as follows:
Figure BDA0002309347960000041
the obtained metal organic framework material MIL-100-Fe has good stability, polar functional groups and molecular pores, and a good adsorption function.
S20, preparing a polyvinylidene fluoride composite material:
dispersing a metal organic framework material MIL-100-Fe in a polar organic solvent, then adding polyvinylidene fluoride, and dispersing for 4-10h at the temperature of 50-70 ℃ to obtain a composite material.
The reaction is carried out at such a temperature that the two are combined to avoid separation of the metal organic framework material MIL-100-Fe from the polyvinylidene fluoride. Here, the polar organic solvent is the same as the polar organic solvent in step S10, and the description thereof is omitted.
Optionally, the mass ratio of the metal-organic framework material MIL-100-Fe to the polyvinylidene fluoride is 1:1.5-1:4, so that the metal-organic framework material MIL-100-Fe and the polyvinylidene fluoride can be combined more firmly, and the effects of adsorption and blood compatibility are better. For example: the mass ratio of the metal organic framework material MIL-100-Fe to the polyvinylidene fluoride is 1:1.5, 1:2, 1:2.5, 1:3, 1:3.5 or 1: 4.
Further, the mass ratio of the metal organic framework material MIL-100-Fe to the polar organic solvent is 1:7-1:16, so that the raw materials can be fully mixed in the organic solvent for reaction. For example: the mass ratio of the metal organic framework material MIL-100-Fe to the polar organic solvent is 1:7, 1:8, 1:10, 1:12, 1:14 or 1: 16.
In some embodiments, the reaction temperature to prepare the composite may be 50 ℃, 55 ℃, 60 ℃, 65 ℃ or 70 ℃. The reaction time for preparing the composite material may be 4h, 6h, 8h or 10 h.
Further, in order to enable the metal organic framework material MIL-100-Fe to be dispersed in the polar organic solvent more uniformly, the metal organic framework material MIL-100-Fe can be dispersed in an ultrasonic dispersion mode (the dispersion is more uniform), polyvinylidene fluoride is added after the dispersion, and then the mixture is stirred for 4-10 hours at the temperature of 60 ℃ to react, so that a composite material is obtained.
S30, preparing a polyvinylidene fluoride composite membrane:
and (3) defoaming, curing and coating the polyvinylidene fluoride composite mixture in sequence to obtain the polyvinylidene fluoride composite membrane.
The polyvinylidene fluoride composite mixed material is defoamed and cured to obtain the modified casting solution. The defoaming may be performed by vacuum defoaming, and the aging treatment is to allow the vacuum defoamed material to stand for a certain period of time to age to obtain a casting solution.
And then, coating on a spin coating machine by adopting a spin coating method, and separating the membrane from the spin coating machine by adopting a liquid-liquid phase separation method to obtain the polyvinylidene fluoride composite membrane. Wherein, the thickness of the polyvinylidene fluoride composite membrane is 50-100 μm, so that the adsorption effect of the composite membrane is better, and the blood compatibility is more obvious. For example: the thickness of the polyvinylidene fluoride composite membrane is 50 μm, 60 μm, 70 μm, 100 μm, 80 μm, 90 μm or 100 μm.
Alternatively, the non-solvent used in the liquid-liquid phase separation method is distilled water, the spin-coating speed is 200r/min, 400r/min, 600r/min, 800r/min or 1000r/min, and the spin-coating time is 20s, 40s, 60s, 80s or 90 s.
The metal organic framework material MIL-100-Fe of the polyvinylidene fluoride composite membrane prepared by the preparation method has good stability, cannot be decomposed and separated out from a polyvinylidene fluoride composite membrane matrix in the using process, can stably exist in the polyvinylidene fluoride composite membrane matrix, and can permanently modify the polyvinylidene fluoride membrane.
The polyvinylidene fluoride composite membrane obtained can have good adsorption performance without adding pore-forming agent, has blood compatibility, and can have the performance of resisting platelet activation and complement activation.
The polyvinylidene fluoride composite membrane can be used for preparing blood contact materials, such as: can be used for preparing artificial blood vessel or blood purification membrane.
The present application is described in detail below with reference to specific examples, but is not limited thereto.
The main reagent information mentioned in the following examples is shown in table 1:
table 1 information on the main reagents used in the examples
Figure BDA0002309347960000061
Example 1
A preparation method of a polyvinylidene fluoride composite membrane comprises the following steps:
(1) 0.21g of trimesic acid and 0.675g of FeCl3Dispersing in 50mL DMF (N, N' -dimethylformamide), reacting at 120 deg.C for 20 hr, stopping reaction, cooling to 20 deg.CWashing unreacted trimesic acid by using ethanol, drying at 80 ℃ to obtain a crystal A, and grinding the crystal A by using a mortar to obtain powder A, wherein the powder A is the metal organic framework material MIL-100-Fe.
(2) Adding 0.5g of metal organic framework material MIL-100-Fe and 8g N-methyl pyrrolidone into a reactor, ultrasonically dispersing for 2h at normal temperature, adding 1.5g of polyvinylidene fluoride into the reactor, and stirring for 4h at 60 ℃ to obtain a composite material.
(3) And (3) carrying out vacuum defoaming and standing curing treatment on the composite mixture to obtain the modified casting solution.
(4) And (3) coating the modified casting solution on a spin coater by adopting a spin coating method (the spin coating speed is 200r/min, and the spin coating time is 20s), and obtaining the polyvinylidene fluoride composite membrane with the thickness of 75 microns by a liquid-liquid phase separation method (non-solvent distilled water is used).
And detecting the adsorption capacity of the polyvinylidene fluoride composite membrane. Wherein, the detection mode of the adsorption capacity is as follows: preparing a standard aqueous solution of a dye, and making a concentration-absorbance standard curve by an ultraviolet-visible spectrophotometer under a characteristic wavelength; immersing 5g of polyvinylidene fluoride composite membrane into 100mL of dye aqueous solution with the concentration of 20mg/mL at room temperature, starting timing, taking out the dye solution immersed in the membrane every half hour, and measuring the absorbance of the dye solution by using an ultraviolet visible spectrophotometer until the absorbance is not reduced any more; determining the dye concentration in the final dye solution through a standard curve, comparing the dye concentration with the concentration of the original solution before adsorption, and calculating the adsorption quantity.
The adsorption capacity of the polyvinylidene fluoride membrane to Victoria blue is 50 mg/g; the adsorption capacity to methylene blue is 55 mg/g; the adsorption capacity to methyl orange is 30 mg/g; the adsorption amount of Congo red is 60 mg/g.
And detecting the blood compatibility of the polyvinylidene fluoride composite membrane. The contents of platelet 4 factor (PF4) and complement C3a in plasma after contacting polyvinylidene fluoride composite membrane with plasma for 30 min. PF4 and C3a test methods were carried out according to the methods described in the documents Shengqiang Nie, Hui Qin, Chong Cheng, Weifeng Zhao, Shudong Sun, Baihai Su, Changsheng Zhao, Zhongwei Gu, Blood activity and compatibility on single-molecular-layer biological interface, journal of Materials Chemistry B,2014,2,4911, using ELISA kits such as the human plasma PF4 and C3a test kits produced by the company R & D.
The content of PF4 in the polyvinylidene fluoride composite membrane is 37ng/mL after the polyvinylidene fluoride composite membrane is contacted with plasma for 30min (38 ng/mL of plasma which is not contacted with the composite membrane); PF4 content was 10ng/mL (15 ng/mL for plasma not contacted with the composite membrane), and there was no significant difference before and after contact. Therefore, the polyvinylidene fluoride composite membrane can have the performance of resisting platelet activation and complement activation, and can be used for preparing blood contact materials.
Comparative example 1
The preparation method of the polyvinylidene fluoride composite membrane provided in the comparative example 1 is different from that of the example 1 in that: and (3) adding 5% of vinyl pyrrolidone (PVP-K30) serving as a pore-foaming agent into the step (2). The other steps are consistent in method.
The method for detecting the adsorption capacity of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the polyvinylidene fluoride composite membrane provided by the comparative example 1 has an adsorption capacity of 55mg/g to Victoria blue; the adsorption capacity to methylene blue is 57 mg/g; the adsorption capacity to methyl orange is 42 mg/g; the adsorption amount of Congo red is 60 mg/g. The comparative example 1 shows that although the pore-foaming agent is added in the preparation process, the adsorption capacity of the polyvinylidene fluoride composite membrane on pollutants in wastewater is not improved, and the polyvinylidene fluoride composite membrane can have good adsorption capacity without adding the pore-foaming agent.
Example 2
A preparation method of a polyvinylidene fluoride composite membrane comprises the following steps:
(1) 0.21g of trimesic acid and 0.675g of FeCl3Dispersing the mixture into 50mL of DMF (N, N' -dimethylformamide), reacting at 120 ℃ for 20h, stopping the reaction, cooling to 20 ℃, washing unreacted trimesic acid with ethanol, drying at 80 ℃ to obtain a crystal A, and grinding the crystal A with a mortar to obtain powder A, wherein the powder A is the metal organic framework material MIL-100-Fe.
(2) Adding 1g of metal organic framework material MIL-100-Fe and 7.5g N-methyl pyrrolidone into a reactor, ultrasonically dispersing for 2h at normal temperature, adding 1.5g of polyvinylidene fluoride into the reactor, and stirring for 4h at 60 ℃ to obtain a composite material.
(3) And (3) carrying out vacuum defoaming and standing curing treatment on the composite mixture to obtain the modified casting solution.
(4) And (3) coating the modified casting solution on a spin coater by adopting a spin coating method (the spin coating speed is 1000r/min, and the spin coating time is 30s), and obtaining the polyvinylidene fluoride composite membrane with the thickness of 50 mu m by a liquid-liquid phase separation method (non-solvent distilled water used).
The method for detecting the adsorption capacity of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the adsorption capacity of the polyvinylidene fluoride composite membrane to Victoria blue is 100 mg/g; the adsorption capacity to methylene blue is 103 mg/g; the adsorption capacity to methyl orange is 65 mg/g; the adsorption amount of Congo red was 105 mg/g.
The method for detecting the blood compatibility of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the content of PF4 in the polyvinylidene fluoride composite membrane is 35ng/mL (38 ng/mL in the plasma which is not contacted with the composite membrane) after 30min of contact between the polyvinylidene fluoride composite membrane and the plasma; the PF4 content was 15ng/mL (15 ng/mL for plasma not contacted with the composite membrane), and there was no significant difference before and after contact. Therefore, the polyvinylidene fluoride composite membrane can have the performance of resisting platelet activation and complement activation, and can be used for preparing blood contact materials.
Comparative example 2
The preparation method of the polyvinylidene fluoride composite membrane provided by the comparative example 2 is different from that of the example 2 in that: and (3) adding 5% of vinyl pyrrolidone (PVP-K30) serving as a pore-foaming agent into the step (2). The other steps are consistent in method.
The method for detecting the adsorption capacity of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the polyvinylidene fluoride composite membrane provided by the comparative example 2 has the adsorption capacity of 110mg/g to Victoria blue; the adsorption capacity to methylene blue is 100 mg/g; the adsorption capacity to methyl orange is 70 mg/g; the adsorption amount of Congo red is 116 mg/g. The comparative example 2 shows that although the pore-foaming agent is added in the preparation process, the adsorption capacity of the pore-foaming agent on pollutants in wastewater is not improved, and the polyvinylidene fluoride composite membrane can have good adsorption capacity without adding the pore-foaming agent.
Example 3
A preparation method of a polyvinylidene fluoride composite membrane comprises the following steps:
(1) 0.21g of trimesic acid and 0.675g of FeCl3Dispersing the mixture into 50mL of DMF (N, N' -dimethylformamide), reacting at 120 ℃ for 20h, stopping the reaction, cooling to 20 ℃, washing unreacted trimesic acid with ethanol, drying at 80 ℃ to obtain a crystal A, and grinding the crystal A with a mortar to obtain powder A, wherein the powder A is the metal organic framework material MIL-100-Fe.
(2) Adding 1g of metal organic framework material MIL-100-Fe and 7g N-methyl pyrrolidone into a reactor, performing ultrasonic dispersion for 2 hours at normal temperature, adding 2g of polyvinylidene fluoride into the reactor, and stirring for 4 hours at 60 ℃ to obtain a composite material.
(3) And (3) carrying out vacuum defoaming and standing curing treatment on the composite mixture to obtain the modified casting solution.
(4) And (3) coating the modified casting solution on a spin coater by adopting a spin coating method (the spin coating speed is 300r/min, and the spin coating time is 90s), and obtaining the polyvinylidene fluoride composite membrane with the thickness of 100 mu m by a liquid-liquid phase separation method (non-solvent distilled water used).
The method for detecting the adsorption capacity of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the absorption capacity of the polyvinylidene fluoride composite membrane to Victoria blue is 70 mg/g; the adsorption capacity to methylene blue is 80 mg/g; the adsorption capacity to methyl orange is 40 mg/g; the adsorption capacity to Congo red was 80 mg/g.
The method for detecting the blood compatibility of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the content of PF4 in the polyvinylidene fluoride composite membrane is 38ng/mL (38 ng/mL in the plasma which is not contacted with the composite membrane) after 30min of contact between the polyvinylidene fluoride composite membrane and the plasma; PF4 level was 14ng/mL (15 ng/mL for plasma not contacted with the composite membrane), and there was no significant difference before and after contact. Therefore, the polyvinylidene fluoride composite membrane can have the performance of resisting platelet activation and complement activation, and can be used for preparing blood contact materials.
Comparative example 3
The preparation method of the polyvinylidene fluoride composite membrane provided by the comparative example 3 is different from that of the example 3 in that: and (3) adding 5% of vinyl pyrrolidone (PVP-K30) serving as a pore-foaming agent into the step (2). The other steps are consistent in method.
The method for detecting the adsorption capacity of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the polyvinylidene fluoride composite membrane provided by the comparative example 3 has an adsorption capacity of 75mg/g to victoria blue; the adsorption capacity to methylene blue is 79 mg/g; the adsorption capacity to methyl orange is 50 mg/g; the adsorption amount of Congo red is 85 mg/g. The comparative example 3 shows that although the pore-foaming agent is added in the preparation process, the adsorption capacity of the composite polyvinylidene fluoride membrane on pollutants in wastewater is not improved, and the polyvinylidene fluoride composite membrane can have good adsorption capacity without adding the pore-foaming agent.
Example 4
The difference between the preparation method of the polyvinylidene fluoride composite membrane provided in the embodiment 4 and the embodiment 3 is that: and (3) replacing the polar organic solvent in the step (2) with N, N' -dimethylformamide. The other steps are consistent in method.
The method for detecting the adsorption capacity of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the adsorption capacity of the polyvinylidene fluoride composite membrane to Victoria blue is 65 mg/g; the adsorption capacity to methylene blue is 87 mg/g; the adsorption capacity to methyl orange is 38 mg/g; the adsorption amount of Congo red is 75 mg/g.
The method for detecting the blood compatibility of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the content of PF4 in the polyvinylidene fluoride composite membrane is 47ng/mL (44 ng/mL in the plasma which is not contacted with the composite membrane) after 30min of contact between the polyvinylidene fluoride composite membrane and the plasma; PF4 level was 17ng/mL (18 ng/mL for plasma not contacted with composite membrane), with no significant difference before and after contact. Therefore, the polyvinylidene fluoride composite membrane can have the performance of resisting platelet activation and complement activation, and can be used for preparing blood contact materials.
Example 5
The difference between the preparation method of the polyvinylidene fluoride composite membrane provided in the embodiment 5 and the embodiment 3 is that: the step (2) is as follows: adding 1g of metal organic framework material MIL-100-Fe and 7g N-methyl pyrrolidone into a reactor, performing ultrasonic dispersion for 2h at normal temperature, adding 2g of polyvinylidene fluoride into the reactor, and stirring for 10h at 50 ℃ to obtain a composite material. The polar organic solvent in (1) is replaced by N, N' -dimethylformamide. The other steps are consistent in method.
The method for detecting the adsorption capacity of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the absorption capacity of the polyvinylidene fluoride composite membrane to Victoria blue is 60 mg/g; the adsorption capacity to methylene blue is 85 mg/g; the adsorption capacity to methyl orange is 40 mg/g; the adsorption amount of Congo red was 76 mg/g.
The method for detecting the blood compatibility of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the content of PF4 in the polyvinylidene fluoride composite membrane is 45ng/mL (44 ng/mL in the plasma which is not contacted with the composite membrane) after 30min of contact between the polyvinylidene fluoride composite membrane and the plasma; PF4 level was 20ng/mL (18 ng/mL for plasma not contacted with composite membrane), and there was no significant difference before and after contact. Therefore, the polyvinylidene fluoride composite membrane can have the performance of resisting platelet activation and complement activation, and can be used for preparing blood contact materials.
Example 6
The difference between the preparation method of the polyvinylidene fluoride composite membrane provided in the embodiment 6 and the embodiment 3 is that: the step (2) is as follows: adding 1g of metal organic framework material MIL-100-Fe and 7g N-methyl pyrrolidone into a reactor, performing ultrasonic dispersion for 2h at normal temperature, adding 2g of polyvinylidene fluoride into the reactor, and stirring for 4.5h at 70 ℃ to obtain a composite material. The polar organic solvent in (1) is replaced by N, N' -dimethylformamide. The other steps are consistent in method.
The method for detecting the adsorption capacity of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the adsorption capacity of the polyvinylidene fluoride composite membrane to Victoria blue is 65 mg/g; the adsorption capacity to methylene blue is 88 mg/g; the adsorption capacity to methyl orange is 36 mg/g; the adsorption amount of Congo red is 72 mg/g.
The method for detecting the blood compatibility of the polyvinylidene fluoride composite membrane is consistent with the method provided by the embodiment 1, and the obtained result is as follows: the content of PF4 in the polyvinylidene fluoride composite membrane is 42ng/mL (44 ng/mL in the plasma which is not contacted with the composite membrane) after 30min of contact between the polyvinylidene fluoride composite membrane and the plasma; PF4 content was 15ng/mL (18 ng/mL for plasma not contacted with the composite membrane), and there was no significant difference before and after contact. Therefore, the polyvinylidene fluoride composite membrane can have the performance of resisting platelet activation and complement activation, and can be used for preparing blood contact materials.
The embodiments described above are some, but not all embodiments of the present application. The detailed description of the embodiments of the present application is not intended to limit the scope of the claimed application, but is merely representative of selected embodiments of the application. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present application.

Claims (8)

1. A preparation method of a polyvinylidene fluoride composite film is characterized by comprising the following steps: dispersing a metal organic framework material MIL-100-Fe in a polar organic solvent, then adding polyvinylidene fluoride, and dispersing for 4-10h at the temperature of 50-70 ℃ to obtain a polyvinylidene fluoride composite material;
wherein the structural formula of the metal organic framework is as follows:
Figure 207302DEST_PATH_IMAGE001
wherein no pore-forming agent is added into the polyvinylidene fluoride composite material;
the mass ratio of the metal organic framework material MIL-100-Fe to the polyvinylidene fluoride is 1:1.5-1: 4; the mass ratio of the metal organic framework material MIL-100-Fe to the polar organic solvent is 1:7-1: 16;
and (3) defoaming, curing and coating the polyvinylidene fluoride compound mixture in sequence.
2. The method according to claim 1, wherein the polar organic solvent is one or more selected from the group consisting of N-methylpyrrolidone, dimethylacetamide, and N, N' -dimethylformamide.
3. The method of claim 1 or 2, wherein the method of preparing the metal-organic framework material MIL-100-Fe comprises: dispersing trimesic acid and ferric ions in a polar organic solvent, and reacting for 16-24h at the temperature of 110-130 ℃.
4. The method according to claim 3, wherein the molar ratio of the trimesic acid to the ferric ions is 1:4 to 1: 6.
5. A polyvinylidene fluoride composite film produced by the production method according to any one of claims 1 to 4.
6. The polyvinylidene fluoride composite film according to claim 5, wherein the thickness of the polyvinylidene fluoride composite film is 50 to 100 μm.
7. Use of the polyvinylidene fluoride composite membrane of claim 5 or 6 in the preparation of a blood contact material.
8. Use of a polyvinylidene fluoride composite membrane according to claim 7, wherein the blood contact material is an artificial blood vessel or a blood purification membrane.
CN201911254086.XA 2019-12-09 2019-12-09 Preparation method of polyvinylidene fluoride composite material, polyvinylidene fluoride composite membrane, preparation method and application thereof Active CN110903576B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201911254086.XA CN110903576B (en) 2019-12-09 2019-12-09 Preparation method of polyvinylidene fluoride composite material, polyvinylidene fluoride composite membrane, preparation method and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201911254086.XA CN110903576B (en) 2019-12-09 2019-12-09 Preparation method of polyvinylidene fluoride composite material, polyvinylidene fluoride composite membrane, preparation method and application thereof

Publications (2)

Publication Number Publication Date
CN110903576A CN110903576A (en) 2020-03-24
CN110903576B true CN110903576B (en) 2021-09-14

Family

ID=69823814

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201911254086.XA Active CN110903576B (en) 2019-12-09 2019-12-09 Preparation method of polyvinylidene fluoride composite material, polyvinylidene fluoride composite membrane, preparation method and application thereof

Country Status (1)

Country Link
CN (1) CN110903576B (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105498553A (en) * 2015-12-11 2016-04-20 华南理工大学 Polyvinylidene fluoride and metal-organic framework composite ultra-filtration membrane and preparation and application
CN108893873A (en) * 2018-07-05 2018-11-27 贵阳学院 A kind of anticoagulation tunica fibrosa and its preparation method and application

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20180043656A1 (en) * 2017-09-18 2018-02-15 LiSo Plastics, L.L.C. Oriented Multilayer Porous Film

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105498553A (en) * 2015-12-11 2016-04-20 华南理工大学 Polyvinylidene fluoride and metal-organic framework composite ultra-filtration membrane and preparation and application
CN108893873A (en) * 2018-07-05 2018-11-27 贵阳学院 A kind of anticoagulation tunica fibrosa and its preparation method and application

Also Published As

Publication number Publication date
CN110903576A (en) 2020-03-24

Similar Documents

Publication Publication Date Title
Yin et al. Free-standing ZIF-71/PDMS nanocomposite membranes for the recovery of ethanol and 1-butanol from water through pervaporation
Zhang et al. Improving the hydrostability of ZIF-8 membrane by biomolecule towards enhanced nanofiltration performance for dye removal
CN109763333B (en) Method for preparing metal organic framework through modified carrier
CN110237728B (en) Mixed matrix membrane compounded by metal organic framework and polymer with micropores as well as preparation method and application of mixed matrix membrane
CN103585891A (en) Compression-resistant microporous membrane and preparation method thereof
US20210179450A1 (en) Membrane for water purification
CN106268348A (en) A kind of preparation method of super-hydrophobic polyphenylene sulfide film
CN110252154A (en) A kind of graphene oxide/graphite phase carbon nitride composite membrane preparation method of glycine modification
CN110280150A (en) A kind of preparation method of the porous base composite ultrafiltration membrane material of high anti-pollution Kynoar
CN106279672A (en) From tool micro-porous copolymers, its preparation method and application
Bhat et al. Pervaporation‐aided dehydration and esterification of acetic acid with ethanol using 4A zeolite‐filled cross‐linked sodium alginate‐mixed matrix membranes
CN113150304A (en) Mixed body metal-organic framework material and preparation method and application thereof
CN110903576B (en) Preparation method of polyvinylidene fluoride composite material, polyvinylidene fluoride composite membrane, preparation method and application thereof
CN105085324A (en) Betaine type amphoteric ioncompound containing isocyanate groups and preparation method thereof
CN104741009B (en) The preparation method and applications of salicylic acid molecular engram acetyl cellulose blend film
CN110152503A (en) A kind of preparation method for the solvent resistant nanofiltration membrane that graphene oxide is compound with tool microporous polymer certainly
JPS6178402A (en) Separation of organic liquid mixture
CN105642130A (en) Ionic liquid modified mesoporous molecular sieve/polymer composite film and preparation and application thereof
CN116808848A (en) Organic/inorganic MOF hybrid mixed matrix membrane with high separation performance, preparation method and application
CN109865501A (en) A kind of compound membrane preparation method for organic dyestuff in Adsorption water
Zhu et al. Electrostatic spray deposition of boronate affinity imprinted membrane to be used as adsorption separation material
Pathak et al. Polymers of Intrinsic Microporosity Based on Dibenzodioxin Linkage: Design, Synthesis, Properties, and Applications
CN113856494A (en) Preparation and application of metal organic framework filled mixed matrix membrane with photoresponse
JP2020531259A (en) Method for producing a composition for forming a gas separation membrane active layer, a composition for forming a gas separation membrane active layer produced thereby, a method for producing a gas separation membrane, and a gas separation membrane.
JPS62114628A (en) Separation membrane

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
GR01 Patent grant
GR01 Patent grant