CN113019155A - Composite microfiltration membrane - Google Patents
Composite microfiltration membrane Download PDFInfo
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- CN113019155A CN113019155A CN202110325201.9A CN202110325201A CN113019155A CN 113019155 A CN113019155 A CN 113019155A CN 202110325201 A CN202110325201 A CN 202110325201A CN 113019155 A CN113019155 A CN 113019155A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0013—Casting processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
Abstract
A composite microfiltration membrane is characterized by comprising at least one layer of composite ultrafiltration membrane; the filter membrane has the advantages of good safety, high puncture resistance and tensile strength, and good heat resistance and porosity.
Description
Technical Field
The invention relates to a composite microfiltration membrane.
Background
The application is application number 201810805152.7, the invention name is a composite ultrafiltration membrane and a divisional application of a preparation method and application thereof, and the disclosure of the parent application is fully introduced.
The industrial application of the ultrafiltration membrane is very wide, and the ultrafiltration membrane becomes one of novel chemical unit operations. For use in the separation, concentration, purification of biologics, pharmaceuticals and food industries; also used for terminal treatment devices in blood treatment, wastewater treatment and ultrapure water preparation. The ultrafiltration membrane is successfully used for the concentration and purification of Chinese herbal medicines and the research and development and the use of water purification equipment in China, particularly the PVC alloy ultrafiltration membrane researched and developed in China overcomes the world problem of the industrial production of high-quality ultrafiltration membranes by common PVC materials, reduces the production cost and the operation energy consumption of the ultrafiltration membrane, improves the filtration performance and the service life of the ultrafiltration membrane, and is listed as an energy-saving emission-reduction recommended product by the state intellectual property bureau. With the progress of the technology, the screening function of the ultrafiltration membrane is improved and strengthened, and the contribution to the human society is increased.
The structure of the ultrafiltration membrane is divided into symmetrical and asymmetrical. The former is isotropic without a skin layer, and the pores in all directions are the same, belonging to deep filtration; the filter has a compact surface layer and a bottom layer mainly of a finger-shaped structure, the surface layer is 0.1 micron or less in thickness and has micropores arranged in order, and the bottom layer is 200-250 microns in thickness and belongs to surface layer filtration. Ultrafiltration membranes used commercially are typically asymmetric membranes. The membrane material of the ultrafiltration membrane mainly comprises cellulose and derivatives thereof, polycarbonate, polyvinyl chloride, polyvinylidene fluoride, polysulfone, polyacrylonitrile, polyamide, polysulfone amide, sulfonated polysulfone, crosslinked polyvinyl alcohol, modified acrylic acid polymer and the like.
Disclosure of Invention
The invention adopts the following technical scheme:
a composite micro-filtration membrane is characterized by comprising at least one layer of composite ultra-filtration membrane;
the preparation method of the composite ultrafiltration membrane comprises the following steps:
step one, placing the composite ultrafiltration membrane base membrane into 20% hydrogen peroxide solution and 0.6% piperazine hexahydrate aqueous solution, soaking for 40-60min at 40-60 ℃, taking out the base membrane, washing for 3-6 times by using deionized water, and drying;
step two, mixing vinyl tri-tert-butoxy silane, maleic anhydride, tert-butyl hydroperoxide and ethanol according to the mass ratio of 1-3:2-4:0.5-4:10-20, and uniformly stirring to prepare a mixed solution;
step three, placing the base membrane dried in the step one into the mixed solution in the step two, heating to 50-70 ℃ under the protection of nitrogen, treating for 4-6h, naturally cooling to normal temperature, adjusting the pH value of the solution to 5-6 by adopting acetic acid, continuously soaking for 30-60min, removing, flushing for 3-6 times by adopting deionized water, and drying in vacuum;
step four, drying the membrane dried in the step three in an oven at the temperature of 80 ℃ for 30-60min to obtain a composite ultrafiltration membrane;
the preparation method of the composite ultrafiltration membrane base membrane comprises the following steps:
step A, preparation of nanoparticle matrix
a. Mixing silica sol, absolute ethyl alcohol and LiNO30.2 mol/L of Ni (NO)3)2Mixing the water solution in a mass ratio of 2-8:10-30:1-2:1-2, stirring for 2-5h by using a magnetic stirrer to form uniform sol,
b. b, heating the sol obtained in the step a in a water bath, and carrying out gelation treatment for 5-10h at the heating temperature of 40-70 ℃ to obtain gel;
c. placing the gel in a high-pressure reaction kettle, reacting at 120 deg.C for 1-2h, heating to 150 deg.C, reacting for 1-2h, heating to 200 deg.C again, reacting for 10-20min, cooling to room temperature, placing the solid in a high-temperature furnace, and placing in N2∶H2Under the reducing atmosphere condition of 95: 5, heat treatment is carried out for 3-6h at the temperature of 500-1+And Ni2+Doped SiO2A nanoparticle matrix;
step B, preparation of surface modified nano material
a. B, placing the nanoparticle matrix prepared in the step A into deionized water, and stirring for 15-30 hours by magnetic force to prepare suspension with the mass percentage concentration of 5-10% for later use;
b. mixing m-phenylenediamine, acetic acid, a silane coupling agent, N-methylpyrrolidone, a first compound and deionized water according to the mass ratio of 2-5:1-2:0.5-2:2-4:5-8:30-60, and stirring for 3-6h to prepare a first solution for later use;
the silane coupling agent is prepared by mixing aminopropyltrimethoxysilane and vinyl aminopropyltrimethoxysilane in a mass ratio of 1-2: 2-3;
the first compound may be selected from: methanesulfonic acid, 1-naphthalenesulfonic acid, 2-naphthalenesulfonic acid, benzenesulfonic acid, methanesulfonic acid, ethanesulfonic acid, 1-propanesulfonic acid, 4-borabenzenesulfonic acid, methanesulfonic acid methyl ester, methanesulfonic acid ethyl ester, aminomethanesulfonic acid, 1-anthraquinone sulfonic acid, 2-anthraquinone sulfonic acid, vinylsulfonic acid, thiophene-2-sulfonic acid, quinoline-8-sulfonic acid, benzenesulfonic acid methyl ester, benzenesulfonic acid ethyl ester, p-toluenesulfonic acid, pyridine-4-sulfonic acid, methanesulfonic acid methyl ester;
c. mixing the suspension prepared in the step a and the first solution prepared in the step b, placing the mixture in an oil bath at the temperature of 80-150 ℃, stirring for 30-60min, cooling to room temperature, introducing nitrogen, standing for 10-30min, adding the first mixed solution and a catalyst, heating to 60-70 ℃, refluxing for 4-6h, filtering a reaction product in vacuum, washing for 3-6 times by using ethanol, and drying in vacuum to obtain a surface-modified nano material for later use;
the first mixed solution consists of vinyl pyrrolidone and sodium acetate in a mass ratio of 1-5: 2-4;
the catalyst is PtxCoyA chemical catalyst, wherein x/y = 1.5-2;
the mass ratio of the suspension prepared in the step a, the first solution prepared in the step b, the first mixed solution and the catalyst is 2-3:5-8:1-2: 0.2-0.5;
step C, preparation of composite ultrafiltration membrane base membrane
B, placing the polymer solution and the surface modified nano material prepared in the step B into a container, stirring for 20-60min, stopping stirring to obtain a casting solution, standing, casting the casting solution on glass to form a film after the casting solution is completely bubble-free, heating to 50-90 ℃, vacuum-drying for 10-20 h, lifting the dried film, and hot-pressing at the temperature of 100-150 ℃ and the pressure of 3-9 MPa; cutting the hot-pressed membrane, and stretching to obtain a composite ultrafiltration membrane base membrane;
the polymer solution is prepared by mixing polyether sulfone, polyether sulfone ketone and a second compound according to the mass ratio of 1-4:2-5: 1-2;
the second compound is selected from: hexanenitrile, nonanenitrile, octanenitrile, octadecanenitrile, decanedionitrile, n-heptanonitrile, isobutyronitrile, p-tolunitrile, bromoxynil, 3-chlorobenzonitrile, o-chlorobenzonitrile, 5-hexenenitrile, 2-naphthylacetonitrile, 2-furancarbonitrile, isovaleronitrile, o-iodobenzonitrile, 2-bromoxynil, p-fluorobenzonitrile, 1-naphthylacetonitrile, 2-naphthylcarbonitrile, 1-naphthylcarbonitrile;
the stretching in the step C is longitudinal stretching at the temperature of 100-120 ℃, and then natural cooling to room temperature; heating to 130-140 ℃ and transversely stretching at the stretching speed of 2-4m/s and the stretching ratio of 10-20 times; and (3) after stretching, placing the membrane at 150 ℃ for heat setting for 10-60 minutes to obtain the composite ultrafiltration membrane base membrane.
2. The composite microfiltration membrane according to claim 1, wherein the mass ratio of the hydrogen peroxide solution to the piperazine hexahydrate aqueous solution in the first step is 4-7: 1-2.
3. The composite microfiltration membrane according to claim 1, wherein in the second step, vinyltri-tert-butoxysilane, maleic anhydride, tert-butyl hydroperoxide and ethanol are mixed in a mass ratio of 2:3:1: 18.
4. The composite microfiltration membrane according to claim 1, wherein in the third step, the dried basement membrane in the first step is placed in the mixed solution in the second step, the temperature is raised to 60 ℃ under the protection of nitrogen for treatment for 6 hours, the basement membrane is naturally cooled to normal temperature, the pH value of the solution is adjusted to 5.5 by using acetic acid, the solution is continuously soaked for 40 minutes, deionized water is removed for washing for 3-6 times, and the membrane is dried in vacuum.
5. A composite microfiltration membrane according to claim 1, wherein step four: and (4) drying the membrane dried in the step three in an oven at the temperature of 80 ℃ for 50min to obtain the composite ultrafiltration membrane.
Has the advantages that:
the membrane has the characteristics of easy preparation and operation, high water permeability, high salt retardation rate and long service life; the nano material has good dispersibility, gives the film the advantages of high flux and low pollution, does not need an additional pore-forming agent, is environment-friendly, and can be widely applied to the fields of water treatment and chemical separation.
Detailed Description
The invention will be further illustrated with reference to the following specific examples.
A composite microfiltration membrane, characterized in that the method comprises the steps of:
step one, placing the composite ultrafiltration membrane base membrane into 20% hydrogen peroxide solution and 0.6% piperazine hexahydrate aqueous solution, soaking for 40-60min at 40-60 ℃, taking out the base membrane, washing for 3-6 times by using deionized water, and drying;
step two, mixing vinyl tri-tert-butoxy silane, maleic anhydride, tert-butyl hydroperoxide and ethanol according to the mass ratio of 1-3:2-4:0.5-4:10-20, and uniformly stirring to prepare a mixed solution;
step three, placing the base membrane dried in the step one into the mixed solution in the step two, heating to 50-70 ℃ under the protection of nitrogen, treating for 4-6h, naturally cooling to normal temperature, adjusting the pH value of the solution to 5-6 by adopting acetic acid, continuously soaking for 30-60min, removing, flushing for 3-6 times by adopting deionized water, and drying in vacuum;
and step four, drying the membrane dried in the step three in an oven at the temperature of 80 ℃ for 30-60min to obtain the composite ultrafiltration membrane.
In the step one, the mass ratio of the hydrogen peroxide solution to the piperazine hexahydrate aqueous solution is 4-7: 1-2.
And in the second step, mixing vinyl tri-tert-butyloxysilane, maleic anhydride, tert-butyl hydroperoxide and ethanol in a mass ratio of 2:3:1: 18.
And step three, placing the base film dried in the step one into the mixed solution in the step two, heating to 60 ℃ under the protection of nitrogen, treating for 6 hours, naturally cooling to normal temperature, adjusting the pH value of the solution to 5.5 by adopting acetic acid, continuously soaking for 40min, removing, flushing for 3-6 times by adopting deionized water, and drying in vacuum.
Step four: and (4) drying the membrane dried in the step three in an oven at the temperature of 80 ℃ for 50min to obtain the composite ultrafiltration membrane.
The composite ultrafiltration membrane is characterized by being prepared by adopting the method.
A composite microfiltration membrane characterised in that it comprises at least one composite ultrafiltration membrane as hereinbefore described.
A composite nanofiltration membrane, which is characterized by comprising at least one layer of the composite ultrafiltration membrane.
The application of the composite ultrafiltration membrane in water treatment and chemical separation.
The preparation method of the composite ultrafiltration membrane base membrane in the first step of the invention comprises the following steps:
step A, preparation of nanoparticle matrix
a. Mixing silica sol, absolute ethyl alcohol and LiNO30.2 mol/L of Ni (NO)3)2The aqueous solution is mixed according to the mass ratio of 2-8:10-30:1-2:1-2, and a magnetic stirrer is adopted for stirring 2-After 5h, a uniform sol is formed,
b. b, heating the sol obtained in the step a in a water bath, and carrying out gelation treatment for 5-10h at the heating temperature of 40-70 ℃ to obtain gel;
c. placing the gel in a high-pressure reaction kettle, reacting at 120 deg.C for 1-2h, heating to 150 deg.C, reacting for 1-2h, heating to 200 deg.C again, reacting for 10-20min, cooling to room temperature, placing the solid in a high-temperature furnace, and placing in N2∶H2Under the reducing atmosphere condition of 95: 5, heat treatment is carried out for 3-6h at the temperature of 500-1+And Ni2+Doped SiO2A nanoparticle matrix;
step B, preparation of surface modified nano material
a. B, placing the nanoparticle matrix prepared in the step A into deionized water, and stirring for 15-30 hours by magnetic force to prepare suspension with the mass percentage concentration of 5-10% for later use;
b. mixing m-phenylenediamine, acetic acid, a silane coupling agent, N-methylpyrrolidone, a first compound and deionized water according to the mass ratio of 2-5:1-2:0.5-2:2-4:5-8:30-60, and stirring for 3-6h to prepare a first solution for later use;
the silane coupling agent is prepared by mixing aminopropyltrimethoxysilane and vinyl aminopropyltrimethoxysilane in a mass ratio of 1-2: 2-3;
the structural formula of the first compound is shown in the formula (1)
Wherein R1 is selected from benzene ring, methyl, ethyl, hydroxy, propyl, ester group, amino, aryl, aralkyl, heteroaryl, vinyl, thienyl, naphthyl, pyridyl, halogen;
r2 is selected from hydrogen, halogen, methyl, ethyl;
c. mixing the suspension prepared in the step a and the first solution prepared in the step b, placing the mixture in an oil bath at the temperature of 80-150 ℃, stirring for 30-60min, cooling to room temperature, introducing nitrogen, standing for 10-30min, adding the first mixed solution and a catalyst, heating to 60-70 ℃, refluxing for 4-6h, filtering a reaction product in vacuum, washing for 3-6 times by using ethanol, and drying in vacuum to obtain a surface-modified nano material for later use;
the first mixed solution consists of vinyl pyrrolidone and sodium acetate in a mass ratio of 1-5: 2-4;
the catalyst is PtxCoyA chemical catalyst, wherein x/y = 1.5-2;
the mass ratio of the suspension prepared in the step a, the first solution prepared in the step b, the first mixed solution and the catalyst is 2-3:5-8:1-2: 0.2-0.5;
step C, preparation of composite ultrafiltration membrane base membrane
B, placing the polymer solution and the surface modified nano material prepared in the step B into a container, stirring for 20-60min, stopping stirring to obtain a casting solution, standing, casting the casting solution on glass to form a film after the casting solution is completely bubble-free, heating to 50-90 ℃, vacuum-drying for 10-20 h, lifting the dried film, and hot-pressing at the temperature of 100-150 ℃ and the pressure of 3-9 MPa; cutting the hot-pressed membrane, and stretching to obtain a composite ultrafiltration membrane base membrane;
the polymer solution is prepared by mixing polyether sulfone, polyether sulfone ketone and a second compound according to the mass ratio of 1-4:2-5: 1-2;
the structural formula of the second compound is shown in formula (2)
Wherein R3 is selected from alkyl, aryl, aralkyl, heteroaryl, hydrocarbyl, naphthyl;
the stretching in the step C is longitudinal stretching at the temperature of 100-120 ℃, and then natural cooling to room temperature; heating to 130-140 ℃ and transversely stretching at the stretching speed of 2-4m/s and the stretching ratio of 10-20 times; placing the stretched film at 150 ℃ for heat setting for 10-60 minutes to obtain a composite ultrafiltration membrane base film;
the first compound in the present invention may be selected from: methanesulfonic acid, 1-naphthalenesulfonic acid, 2-naphthalenesulfonic acid, benzenesulfonic acid, methanesulfonic acid, ethylsulfonic acid, 1-propanesulfonic acid, 4-borabenzenesulfonic acid, methanesulfonic acid methyl ester, methanesulfonic acid ethyl ester, aminomethanesulfonic acid, 1-anthraquinone sulfonic acid, 2-anthraquinone sulfonic acid, vinylsulfonic acid, thiophene-2-sulfonic acid, quinoline-8-sulfonic acid, benzenesulfonic acid methyl ester, benzenesulfonic acid ethyl ester, p-toluenesulfonic acid, pyridine-4-sulfonic acid, methanesulfonic acid methyl ester, and the like.
The second compound in the present invention may be selected from: hexanenitrile, nonanenitrile, octanenitrile, octadecanenitrile, decanedionitrile, n-heptanenitrile, isobutyronitrile, p-tolunitrile, bromoxynil, 3-chlorobenzonitrile, o-chlorobenzonitrile, 5-hexenenitrile, 2-naphthaleneacetonitrile, 2-furancarbonitrile, isovaleronitrile, o-iodoxynil, 2-bromoxynil, p-fluorobenzonitrile, 1-naphthaleneacetonitrile, 2-naphthalenecarbonitrile, 1-naphthalenecarbonitrile, and the like.
The silica used in step A was dissolved in JN30 type silica sol.
The composite ultrafiltration membrane of the invention is researched:
1. step A, preparation of surface modified nano material, adding PtxCoyAn alloy catalyst is creatively adopted, x/y =1.5-2, and research shows that the first compound and the silane coupling agent are combined to form a branch on the surface of the nanoparticle in the presence of a first mixed solution after the catalyst is added, a reticular molecular bond is formed between the first compound and the silane coupling agent, the branch is firmly arranged on the surface of the nanoparticle, and the branch ratio after the catalyst is added exceeds 25-40% of that without the catalyst; thereby improving the bonding performance between the composite ultrafiltration membrane and a polymer matrix and improving the stability of the composite ultrafiltration membrane;
2. the first compound is added in the modification of the nanoparticles, and the first compound and the silane coupling agent are combined to be capable of being on the surface of the branched nanoparticles; the self-made polymer solution is adopted in the composite ultrafiltration membrane base membrane, the second compound is added in the polymer solution, the second compound can enter between the first compound and the silane coupling agent to form a reticular molecular bond to be consolidated to form a more stable reticular compound, and the nano particles and the polymer matrix form a molecular bond to be combined together, so that the bonding strength of an interface is enhanced, and the chlorine resistance of the composite ultrafiltration membrane is effectively improved through the later heat treatment on the base membrane; the addition of the second compound enables an additional nanoscale channel to be provided between the nanoparticle and the polymer interface, so that the water flux of the composite membrane is effectively improved; under the condition of room temperature, the operating pressure is 0.5Mpa, and the flux of 2g/L MgSO4 aqueous solution is tested, and can reach 38.2L/(m 2. n), and the retention rate is 97.6%.
3. Researches show that when the reverse osmosis basement membrane is respectively soaked by alkaline and acidic aqueous solutions, the performance of the reverse osmosis basement membrane is improved, and after the reverse osmosis basement membrane is soaked in 1000ppm NaClO aqueous solution for 10 hours, the rejection rate of NaCl is still as high as 97.8-99.7%, and the preference is 99.1%; the water flux reaches 1.92-2.16M3/M2D, preferably 1.99M3/M2.d。
4. Found by the study that Li1+And Ni2+Co-doped with SiO2The nano particles can promote doped ions to better enter crystal lattices of the matrix to play a role in charge compensation and effectively enhance the transfer of crystal lattice energy, so that the strength of the film is greatly enhanced, the tensile strength can reach 80-89N, and Li is not adopted1+And Ni2+The tensile strength of the film prepared by doping the elements is 70-76N.
It should be understood that these examples are for illustrative purposes only and are not intended to limit the scope of the present invention. Further, it should be understood that various changes or modifications of the present invention may be made by those skilled in the art after reading the teaching of the present invention, and such equivalents may fall within the scope of the present invention as defined in the appended claims.
Claims (5)
1. A composite microfiltration membrane is characterized by comprising at least one layer of composite ultrafiltration membrane;
the preparation method of the composite ultrafiltration membrane comprises the following steps:
step one, placing the composite ultrafiltration membrane base membrane into 20% hydrogen peroxide solution and 0.6% piperazine hexahydrate aqueous solution, soaking for 40-60min at 40-60 ℃, taking out the base membrane, washing for 3-6 times by using deionized water, and drying;
step two, mixing vinyl tri-tert-butoxy silane, maleic anhydride, tert-butyl hydroperoxide and ethanol according to the mass ratio of 1-3:2-4:0.5-4:10-20, and uniformly stirring to prepare a mixed solution;
step three, placing the base membrane dried in the step one into the mixed solution in the step two, heating to 50-70 ℃ under the protection of nitrogen, treating for 4-6h, naturally cooling to normal temperature, adjusting the pH value of the solution to 5-6 by adopting acetic acid, continuously soaking for 30-60min, removing, flushing for 3-6 times by adopting deionized water, and drying in vacuum;
step four, drying the membrane dried in the step three in an oven at the temperature of 80 ℃ for 30-60min to obtain a composite ultrafiltration membrane;
the preparation method of the composite ultrafiltration membrane base membrane comprises the following steps:
step A, preparation of nanoparticle matrix
a. Mixing silica sol, absolute ethyl alcohol and LiNO30.2 mol/L of Ni (NO)3)2Mixing the water solution in a mass ratio of 2-8:10-30:1-2:1-2, stirring for 2-5h by using a magnetic stirrer to form uniform sol,
b. b, heating the sol obtained in the step a in a water bath, and carrying out gelation treatment for 5-10h at the heating temperature of 40-70 ℃ to obtain gel;
c. placing the gel in a high-pressure reaction kettle, reacting at 120 deg.C for 1-2h, heating to 150 deg.C, reacting for 1-2h, heating to 200 deg.C again, reacting for 10-20min, cooling to room temperature, placing the solid in a high-temperature furnace, and placing in N2∶H2Under the reducing atmosphere condition of 95: 5, heat treatment is carried out for 3-6h at the temperature of 500-1+And Ni2+Doped SiO2A nanoparticle matrix;
step B, preparation of surface modified nano material
a. B, placing the nanoparticle matrix prepared in the step A into deionized water, and stirring for 15-30 hours by magnetic force to prepare suspension with the mass percentage concentration of 5-10% for later use;
b. mixing m-phenylenediamine, acetic acid, a silane coupling agent, N-methylpyrrolidone, a first compound and deionized water according to the mass ratio of 2-5:1-2:0.5-2:2-4:5-8:30-60, and stirring for 3-6h to prepare a first solution for later use;
the silane coupling agent is prepared by mixing aminopropyltrimethoxysilane and vinyl aminopropyltrimethoxysilane in a mass ratio of 1-2: 2-3;
the first compound may be selected from: methanesulfonic acid, 1-naphthalenesulfonic acid, 2-naphthalenesulfonic acid, benzenesulfonic acid, methanesulfonic acid, ethanesulfonic acid, 1-propanesulfonic acid, 4-borabenzenesulfonic acid, methanesulfonic acid methyl ester, methanesulfonic acid ethyl ester, aminomethanesulfonic acid, 1-anthraquinone sulfonic acid, 2-anthraquinone sulfonic acid, vinylsulfonic acid, thiophene-2-sulfonic acid, quinoline-8-sulfonic acid, benzenesulfonic acid methyl ester, benzenesulfonic acid ethyl ester, p-toluenesulfonic acid, pyridine-4-sulfonic acid, methanesulfonic acid methyl ester;
c. mixing the suspension prepared in the step a and the first solution prepared in the step b, placing the mixture in an oil bath at the temperature of 80-150 ℃, stirring for 30-60min, cooling to room temperature, introducing nitrogen, standing for 10-30min, adding the first mixed solution and a catalyst, heating to 60-70 ℃, refluxing for 4-6h, filtering a reaction product in vacuum, washing for 3-6 times by using ethanol, and drying in vacuum to obtain a surface-modified nano material for later use;
the first mixed solution consists of vinyl pyrrolidone and sodium acetate in a mass ratio of 1-5: 2-4;
the catalyst is PtxCoyA chemical catalyst, wherein x/y = 1.5-2;
the mass ratio of the suspension prepared in the step a, the first solution prepared in the step b, the first mixed solution and the catalyst is 2-3:5-8:1-2: 0.2-0.5;
step C, preparation of composite ultrafiltration membrane base membrane
B, placing the polymer solution and the surface modified nano material prepared in the step B into a container, stirring for 20-60min, stopping stirring to obtain a casting solution, standing, casting the casting solution on glass to form a film after the casting solution is completely bubble-free, heating to 50-90 ℃, vacuum-drying for 10-20 h, lifting the dried film, and hot-pressing at the temperature of 100-150 ℃ and the pressure of 3-9 MPa; cutting the hot-pressed membrane, and stretching to obtain a composite ultrafiltration membrane base membrane;
the polymer solution is prepared by mixing polyether sulfone, polyether sulfone ketone and a second compound according to the mass ratio of 1-4:2-5: 1-2;
the second compound is selected from: hexanenitrile, nonanenitrile, octanenitrile, octadecanenitrile, decanedionitrile, n-heptanonitrile, isobutyronitrile, p-tolunitrile, bromoxynil, 3-chlorobenzonitrile, o-chlorobenzonitrile, 5-hexenenitrile, 2-naphthylacetonitrile, 2-furancarbonitrile, isovaleronitrile, o-iodobenzonitrile, 2-bromoxynil, p-fluorobenzonitrile, 1-naphthylacetonitrile, 2-naphthylcarbonitrile, 1-naphthylcarbonitrile;
the stretching in the step C is longitudinal stretching at the temperature of 100-120 ℃, and then natural cooling to room temperature; heating to 130-140 ℃ and transversely stretching at the stretching speed of 2-4m/s and the stretching ratio of 10-20 times; and (3) after stretching, placing the membrane at 150 ℃ for heat setting for 10-60 minutes to obtain the composite ultrafiltration membrane base membrane.
2. The composite microfiltration membrane according to claim 1, wherein the mass ratio of the hydrogen peroxide solution to the piperazine hexahydrate aqueous solution in the first step is 4-7: 1-2.
3. The composite microfiltration membrane according to claim 1, wherein in the second step, vinyltri-tert-butoxysilane, maleic anhydride, tert-butyl hydroperoxide and ethanol are mixed in a mass ratio of 2:3:1: 18.
4. The composite microfiltration membrane according to claim 1, wherein in the third step, the dried basement membrane in the first step is placed in the mixed solution in the second step, the temperature is raised to 60 ℃ under the protection of nitrogen for treatment for 6 hours, the basement membrane is naturally cooled to normal temperature, the pH value of the solution is adjusted to 5.5 by using acetic acid, the solution is continuously soaked for 40 minutes, deionized water is removed for washing for 3-6 times, and the membrane is dried in vacuum.
5. A composite microfiltration membrane according to claim 1, wherein step four: and (4) drying the membrane dried in the step three in an oven at the temperature of 80 ℃ for 50min to obtain the composite ultrafiltration membrane.
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| CN202110325201.9A CN113019155A (en) | 2018-07-20 | 2018-07-20 | Composite microfiltration membrane |
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| CN201810805152.7A CN108905626B (en) | 2018-07-20 | 2018-07-20 | Composite ultrafiltration membrane and preparation method and application thereof |
| CN202110325201.9A CN113019155A (en) | 2018-07-20 | 2018-07-20 | Composite microfiltration membrane |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113797953A (en) * | 2021-09-29 | 2021-12-17 | 广州珠矶科技有限公司 | Preparation and application method of nano catalyst for repairing organic pollution of underground water |
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| US5112491A (en) * | 1991-03-01 | 1992-05-12 | E. I. Du Pont De Nemours And Company | Management of waste solution containing photoresist materials |
| DE29623801U1 (en) * | 1995-03-03 | 1999-11-11 | Alltech Associates Inc | Apparatus for the electrochemical modification of chromatographic material |
| CN100584437C (en) * | 2007-06-13 | 2010-01-27 | 海南立昇净水科技实业有限公司 | Hydrophilic polyvinylidene fluoride hollow fiber microporous membrane and preparation method thereof |
| CN101185848B (en) * | 2007-08-29 | 2010-12-01 | 江南大学 | Unsymmetrical network shape pore structure hollow fiber film and preparation method thereof |
| JP5648245B2 (en) * | 2011-03-08 | 2015-01-07 | 日本表面化学株式会社 | Method for forming chromium-free metal protective film and treatment agent for forming chromium-free metal protective film |
| CN102888016B (en) * | 2012-09-12 | 2014-03-05 | 常州大学 | Preparation method of lithium-ion secondary battery diaphragm with crosslinking composite layer |
| CN102941027B (en) * | 2012-11-30 | 2014-11-19 | 艾特克控股集团有限公司 | Method for producing high-flux ultra-filtration membrane |
| CN105214521B (en) * | 2014-06-25 | 2017-08-04 | 天津大学 | A kind of polyetherimide amine composite nanofiltration membrane and preparation method |
| CN106166450A (en) * | 2016-08-08 | 2016-11-30 | 贵阳时代沃顿科技有限公司 | A kind of high temperature resistant accurate molecular cut off ultrafilter membrane and preparation method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113797953A (en) * | 2021-09-29 | 2021-12-17 | 广州珠矶科技有限公司 | Preparation and application method of nano catalyst for repairing organic pollution of underground water |
| CN113797953B (en) * | 2021-09-29 | 2023-07-04 | 广州珠矶科技有限公司 | Preparation and application methods of nano catalyst for repairing organic pollution of underground water |
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| CN108905626A (en) | 2018-11-30 |
| CN108905626B (en) | 2021-06-08 |
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