CN114643083A - Monolithic polytrifluorochloroethylene bipolar membrane containing metal phthalocyanine derivative water dissociation catalyst and preparation method thereof - Google Patents

Monolithic polytrifluorochloroethylene bipolar membrane containing metal phthalocyanine derivative water dissociation catalyst and preparation method thereof Download PDF

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CN114643083A
CN114643083A CN202210241576.1A CN202210241576A CN114643083A CN 114643083 A CN114643083 A CN 114643083A CN 202210241576 A CN202210241576 A CN 202210241576A CN 114643083 A CN114643083 A CN 114643083A
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polytrifluorochloroethylene
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陈晓
黄雪红
金延超
陈日耀
林思涵
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Fujian Normal University
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    • B01J39/00Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
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    • B01J41/08Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
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Abstract

The invention discloses a monolithic polytrifluorochloroethylene bipolar membrane containing metal phthalocyanine derivative water dissociation catalyst and a preparation method thereof, belonging to the field of electrically driven membranes.

Description

Monolithic polytrifluorochloroethylene bipolar membrane containing metal phthalocyanine derivative water dissociation catalyst and preparation method thereof
Technical Field
The invention relates to a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst and a preparation method thereof, belonging to the technical field of electrically driven membranes.
Background
The bipolar membrane is a composite membrane material compounded by an anion exchange membrane, a cation exchange membrane and an intermediate catalyst layer. Under the action of an electric field, water molecules in the middle layer of the bipolar membrane are subjected to water dissociation to generate hydrogen ions and hydroxyl, so that the purpose of acid and alkali production is achieved. The theoretical potential of acid and alkali produced by the water dissociation of the bipolar membrane is 0.828V, and the theoretical voltage of acid and alkali produced by the electrolysis of water is 2.057V. In addition, the water dissociation rate of the bipolar membrane intermediate layer is about 5000 ten thousand times faster than that in the ordinary case. Therefore, the bipolar membrane technology has the characteristics of low energy consumption, high efficiency, no pollution of products and the like, and is widely applied to various fields of acid and alkali production and recovery, ocean chemical industry, pollution treatment, organic synthesis and the like.
Aromatic carbon skeletons such as polyaryletherketone and the like are commonly used bipolar membrane substrate materials at present, and quaternary ammonium functional groups are common functional groups of anion exchange membranes in bipolar membranes. However, the carbon-oxygen bond in the aromatic carbon skeleton is easily degraded by the attack of hydroxyl, and because of the attack of hydroxyl, the quaternary ammonium functional group is destroyed due to hoffman reaction, affinity substitution reaction and the like, so that the acid-base concentration generated by the bipolar membrane electrodialysis is generally low. Therefore, the control of the acid-base concentration is crucial to the application of acid-base generated by the bipolar membrane. On the other hand, the existing bipolar membrane is formed by compounding an anion exchange membrane, a cation exchange membrane and an intermediate catalyst layer, and due to the difference of physicochemical properties of different layers, the bipolar membrane is easy to peel off in the use process, so that the service life of the bipolar membrane is further shortened.
Disclosure of Invention
In order to solve the problems in the prior art, the invention provides a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst and a preparation method thereof.
The technical scheme of the invention is as follows:
one of the purposes of the invention is to provide a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst, wherein one side of the bipolar membrane is introduced with a sulfonic acid group, and the other side of the bipolar membrane is introduced with a quaternary ammonium group;
the structural formula of the cation exchange membrane in the bipolar membrane is as follows: the structural formula of the cation exchange membrane in the bipolar membrane is as follows:
Figure BDA0003542300450000021
the anion exchange membrane has the structural formula:
Figure BDA0003542300450000022
the structural formula of the intermediate interfacial catalyst is as follows:
Figure BDA0003542300450000023
wherein n is the polymerization degree of the main chain of the polytrifluorochloroethylene basal membrane, m is the polymerization degree of the polybromomethylstyrene side chain, and n and m are integers which are not zero.
The invention also aims to provide a preparation method of the monolithic polytrifluorochloroethylene bipolar membrane containing the metal phthalocyanine derivative water dissociation catalyst, which comprises the following steps:
s1, preparing a polychlorotrifluoroethylene grafted polymethyl styrene copolymer: dissolving polychlorotrifluoroethylene in an organic solvent I, introducing nitrogen to remove oxygen, heating, mixing according to the molar ratio of polychlorotrifluoroethylene, a methyl styrene monomer, CuBr and bipyridine or pentamethyl diethylenetriamine being 1 (20-100): 1:2, reacting for 5-40 h at constant temperature under the protection of nitrogen, pouring the reaction liquid into an alcohol-water mixed solvent with the volume ratio of 1:1, and precipitating to obtain a grafted combination; leaching the precipitate with alcohol water for multiple times, soaking in running water for 24h, filtering, and drying to obtain polychlorotrifluoroethylene grafted polymethyl styrene graft polymer (PCTFE-g-PMST);
s2, bromination: dissolving the polychlorotrifluoroethylene grafted polymethyl styrene graft polymer prepared in the step S1 in an organic solvent II, adding a brominating agent and an initiator, boiling and refluxing for 4-6 h under the conditions of heating and stirring, stopping heating and stirring after full reaction, precipitating white floccules in anhydrous methanol or isopropanol, washing to remove impurities, and drying to obtain a bromomethylated polymer (PCTFE-g-BrPMST);
s3, preparing a base film: dissolving the bromomethylated polymer prepared in the step S2 in N-dimethyl pyrrolidone, casting the solution on a clean glass plate after the polymer is completely dissolved, and drying to prepare a polychlorotrifluoroethylene grafted bromomethylated styrene base film;
s4, introducing ion exchange groups on two sides of the base membrane: placing the polychlorotrifluoroethylene grafted bromomethylated styrene base membrane prepared in the step S3 in a reactor, respectively soaking two side surfaces of the base membrane in a sulfonation reagent and a negative membrane functional reaction reagent, introducing nitrogen to remove air in the reactor, sealing the reactor, and placing the reactor in a constant-temperature water bath kettle at the temperature of 20-70 ℃ for reacting for 40-60 hours;
s5, preparing a bipolar membrane: after the negative film functionalization reaction is finished, continuing the sulfonation reaction at 20-90 ℃, and keeping the sulfonation reaction time for 50-72 h longer than the negative film functionalization reaction time; and (2) introducing sulfonic acid groups through sulfonation reaction, removing reaction liquid on one side of the cathode membrane, changing the reaction liquid into intermediate interface layer catalyst reaction liquid and cathode membrane functional reagent mixed solution for continuous reaction, introducing anion exchange groups and sulfonic acid groups into two sides of the base membrane respectively, introducing metal phthalocyanine derivatives and anion exchange groups into a thin layer between the two sides, and removing residual reaction liquid in the base membrane after the reaction is finished to obtain the monolithic polytrifluorochloroethylene bipolar membrane containing the metal phthalocyanine derivative water dissociation catalyst.
Further, in the step S1, the methylstyrene monomer is any one of 4-methylstyrene, 2-methylstyrene, 3-methylstyrene, 2, 4-dimethylstyrene, 3, 4-dimethylstyrene, 2,3, 4-trimethylstyrene, 3,4, 5-trimethylstyrene, 2,4, 6-trimethylstyrene, 2,3,4, 5-tetramethylstyrene, 2,3,4, 6-tetramethylstyrene, and 2,3,4,5, 6-pentamethylstyrene monomer.
Further, in the step S1, the organic solvent i is any one or a combination of two of N, N-dimethylacetamide, dimethylsulfoxide, N-methylpyrrolidone and N, N-dimethylformamide in any ratio.
Further, in the step S2, the organic solvent ii is any one or a combination of two of 1, 2-dichloroethane, chlorobenzene and carbon tetrachloride in any proportion.
Further, the solvent of the sulfonation reagent in the step S4 is any one of sodium phenolsulfonate, sodium hydroxybenzenesulfonate, sodium hydroxysulfonate, sodium 2-hydroxysulfonate, sodium 3-hydroxysulfonate, sodium 4-hydroxysulfonate, sodium mercaptoethylsulfonate or sodium mercaptopropylsulfonate, and the solution of the sulfonation reagent is one of distilled water, THF, DMF, DMAc, NMP and DMSO or a mixture of two of them in any proportion.
Further, in step S4, the solvent of the reaction reagent for negative membrane functionalization is any one of trimethylamine, triethylamine, dimethylimidazole, trimethylimidazole, methylethylimidazole, dimethylpropylimidazole, dimethylbutylimidazole, tetramethylimidazole, trimethylethylimidazole, methylethylimidazole, pentamethylguanidine, tetramethylethylguanidine, tetramethylpropylguanidine, tetramethylbutylguanidine, tetramethylhexylguanidine, or N-methylmorpholine, and the solution of the reaction reagent for negative membrane functionalization is one of distilled water, THF, DMF, DMAc, NMP, and DMSO or a combination of two of them at any ratio.
Further, the intermediate interface layer catalyst reaction liquid is an alcohol/water solution containing a metal phthalocyanine derivative.
Further, the phthalocyanine is any one of hydroxyl substituent phthalocyanine, amino substituent phthalocyanine, phthalocyanine containing transition metal hydroxyl substituent or phthalocyanine containing transition metal amino substituent.
Further, the metal phthalocyanine derivative central ion may be any one of inorganic metal ions.
Compared with the prior art, the invention has the beneficial effects that:
(1) the invention provides a preparation method of a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst, which comprises the steps of polymerizing by ATRP, brominating polytrifluorochloroethylene grafted methyl styrene polymer by NBS to control the molecular weight of side chains of polymethyl styrene, obtaining bromomethylation polymer after bromination, further forming a base membrane material, introducing sulfonic acid groups and anion exchange groups by utilizing the reaction of bromomethyl and corresponding reagents, forming the monolithic bipolar membrane simultaneously provided with anion and cation exchange membrane layers, omitting a membrane forming process in the preparation process of the traditional bipolar membrane, and avoiding the use of carcinogenic substance chloromethyl ether.
(2) According to the invention, the bromomethyl of the side chain of the bipolar membrane reacts with the metal phthalocyanine derivative, so that the polytrifluorochloroethylene side chain is bonded with the metal phthalocyanine derivative to be used as a bipolar membrane middle layer water dissociation catalyst, the prepared bipolar membrane has low resistance and low transmembrane voltage, and the water dissociation catalyst is not easy to run off.
(3) The monolithic bipolar membrane prepared by the method provided by the invention has the advantages that the problems of bubbling, cracking and the like which are easily caused in the using process of the sandwich bipolar membrane can be avoided even if the monolithic bipolar membrane is used for a long time.
Detailed Description
The invention is further described in connection with the preferred embodiments, and the endpoints of the ranges and any values disclosed in the present invention are not limited to the precise range or value, and such ranges or values should be understood to encompass values close to such ranges or values; for numerical ranges, each range between its endpoints and individual point values, and each individual point value can be combined with each other to give one or more new numerical ranges, and such numerical ranges should be construed as specifically disclosed herein.
Materials, reagents and the like used in the following examples are commercially available unless otherwise specified;
the experimental procedures in the following examples are conventional unless otherwise specified.
In the following examples, poly (vinylidene fluoride-chlorotrifluoroethylene) was used as the polychlorotrifluoroethylene, and the resulting polychlorotrifluoroethylene-grafted polymethylstyrene copolymer was a poly (vinylidene fluoride-chlorotrifluoroethylene) -grafted polymethylstyrene copolymer.
Example 1
A monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst, wherein one side of the bipolar membrane is introduced with sulfonic acid groups, and the other side of the bipolar membrane is introduced with quaternary ammonium groups; the structural formula of the cation exchange membrane in the bipolar membrane is as follows:
Figure BDA0003542300450000051
the anion exchange membrane has the structural formula:
Figure BDA0003542300450000052
the structural formula of the intermediate interfacial catalyst is as follows:
Figure BDA0003542300450000061
wherein n is the polymerization degree of the main chain of the polytrifluorochloroethylene basal membrane, m is the polymerization degree of the polybromomethylstyrene side chain, and n and m are integers which are not zero.
Example 2
A monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst, comprising the steps of:
s1, preparing a polychlorotrifluoroethylene grafted polymethyl styrene copolymer (PCTFE-g-PMST): weighing 20g of polychlorotrifluoroethylene, dissolving in 200mL of N-methylpyrrolidone, introducing nitrogen to remove oxygen, heating to 110 ℃, adding 144.1g of 4-methylstyrene, 8.72g of CuBr and 9.52g of bipyridine into a reaction system, reacting at constant temperature for 40 hours under the protection of nitrogen, pouring the reaction solution into an alcohol-water mixed solvent with the volume ratio of 1:1, and precipitating to obtain a graft conjugate; leaching the precipitate with alcohol water for multiple times, then soaking the precipitate in running water for 24 hours to remove copper ions and bipyridine, filtering and drying the precipitate, putting the precipitate into a Soxhlet extractor to be extracted with toluene for 10 hours to completely remove homopolymer polystyrene, and putting the precipitate into a vacuum drying oven at 80 ℃ to be dried for 24 hours to prepare the polytrifluorochloroethylene grafted polymethylstyrene graft polymer, wherein the reaction formula is as follows:
Figure BDA0003542300450000062
s2, bromination: weighing 10g of polychlorotrifluoroethylene grafted polymethylstyrene graft polymer, dissolving in 150mL of chlorobenzene, adding 9.04g N-bromosuccinimide as a brominating agent and 0.9g of dicumyl peroxide as an initiator, boiling and refluxing for 6h under the conditions of 130 ℃ and stirring, gradually changing the solution into orange red along with the reaction, continuing to react for a period of time after the orange red fades, stopping heating and stirring, precipitating white floccule in anhydrous methanol or isopropanol, extracting the white floccule in a Soxhlet extractor with acetone for 20h to remove impurities, and drying to obtain the bromomethylation polymer, wherein the reaction formula is as follows:
Figure BDA0003542300450000071
s3, preparing a base film: dissolving the bromomethylated polymer prepared in the step S2 in N-dimethyl pyrrolidone, casting the bromomethylated polymer on a clean glass plate after the polymer is completely dissolved, and drying to prepare the polychlorotrifluoroethylene grafted bromomethylated styrene base film;
s4, introducing ion exchange groups on two sides of the base membrane: placing the polychlorotrifluoroethylene grafted bromomethylated styrene basement membrane prepared in the step S3 in a reactor, and respectively soaking two side surfaces of the basement membrane in a sulfonation reagent and a negative membrane functional reaction reagent, wherein the solvent of the sulfonation reagent is sodium p-phenolate sodium benzenesulfonate, and the solution is a mixed solution of distilled water and DMF (sodium p-phenolate sodium benzenesulfonate: H)2The mass ratio of O to DMF is 1:8:2), the solvent of the negative membrane functionalization reaction reagent is trimethylamine, and the solution is a mixed solution of distilled water and DMF (trimethylamine: H)2The mass ratio of O to DMF is 1:9:1), and the basement membrane separates the two reagents; introducing nitrogen to remove air in the reactor, sealing the reactor, and placing the reactor in a constant-temperature water bath kettle at 70 ℃ for reaction;
s5, preparing a bipolar membrane: after the cathode membrane functionalization reaction is finished for 50 hours, continuing the sulfonation reaction at 90 ℃, maintaining the sulfonation reaction for 65 hours, introducing sulfonic acid groups into the sulfonation reaction, removing reaction liquid on one side of the cathode membrane, changing the reaction liquid into amino phthalocyanine iron alcohol/water solution, continuing the reaction for 10 hours, introducing anion exchange groups into bromomethyl on the outer layer of the cathode basement membrane and a cathode membrane functionalization reagent, introducing phthalocyanine into the bromomethyl on the inner layer of the cathode basement membrane and amino phthalocyanine iron through reaction, introducing a water dissociation catalyst into a cathode interface layer and an anode interface layer, and removing residual reaction liquid in the basement membrane after the reaction is finished to obtain the single-chip type polytrifluorochloroethylene bipolar membrane containing the phthalocyanine derivative water dissociation catalytic groups, wherein the ion exchange capacity of the anode is 1-2.5mmol/g, the ion exchange capacity of the cathode is 0.8-3.2mmol/g, and the specific reaction formula is as follows:
Figure BDA0003542300450000081
example 3
A preparation method of a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst comprises the following steps:
s1, preparing a polychlorotrifluoroethylene grafted polymethyl styrene copolymer (PCTFE-g-PMST): weighing 20g of polychlorotrifluoroethylene, dissolving in 200mL of dimethyl sulfoxide, introducing nitrogen to remove oxygen, heating to 110 ℃, adding 180.1g of 2-methylstyrene, 8.72g of CuBr and 21.13g of pentamethyldiethylenetriamine into a reaction system, reacting for 5 hours at constant temperature under the protection of nitrogen, pouring the reaction solution into an alcohol-water mixed solvent with the volume ratio of 1:1, and precipitating to obtain a graft conjugate; leaching the precipitate with alcohol water for multiple times, then soaking the precipitate in running water for 24 hours to remove copper ions and pentamethyldiethylenetriamine, filtering and drying the precipitate, putting the precipitate into a Soxhlet extractor, extracting the precipitate with toluene for 10 hours to completely remove homopolymer polystyrene, and putting the precipitate into a vacuum drying oven at 80 ℃ to dry the precipitate for 24 hours to prepare the polychlorotrifluoroethylene grafted polymethylstyrene graft polymer, wherein the reaction formula is as follows:
Figure BDA0003542300450000082
s2, bromination: weighing 10g of polychlorotrifluoroethylene grafted polymethylstyrene graft polymer, dissolving in 160mL of 1, 2-dichloroethane, adding 10.84g N-bromosuccinimide as a brominating agent and 1.08g of dicumyl peroxide as an initiator, boiling and refluxing for 5h under the conditions of 130 ℃ and stirring, gradually changing the solution into orange red along with the reaction, continuing the reaction for a period of time after the orange red fades, stopping heating and stirring, precipitating white floccules in anhydrous methanol or isopropanol, extracting the white floccules in a Soxhlet extractor with acetone for 20h to remove impurities, and drying to obtain the bromomethylated polymer, wherein the reaction formula is shown in example 1:
s3, preparing a base film: dissolving the bromomethylated polymer prepared in the step S2 in N-dimethyl pyrrolidone, casting the solution on a clean glass plate after the polymer is completely dissolved, and drying to prepare a polychlorotrifluoroethylene grafted bromomethylated styrene base film;
s4, introducing ion exchange groups on two sides of the base membrane: placing the polychlorotrifluoroethylene grafted bromomethylated styrene basement membrane prepared in the step S3 in a reactor, and respectively soaking two side surfaces of the basement membrane in a sulfonation reagent and a negative membrane functional reaction reagent, wherein the solvent of the sulfonation reagent is sodium p-phenolate sodium benzenesulfonate, and the solution is a mixed solution of distilled water and THF (sodium p-phenolate sodium benzenesulfonate: H)2THF is in a mass ratio of 1:7:3), the solvent of the quaternization reagent is dimethylimidazole, and the solution is a mixed solution of distilled water and THF (dimethylimidazole: H)2THF in a mass ratio of 1:8:2), and the base membrane separates the two reagents; introducing nitrogen to remove air in the reactor, sealing the reactor, and placing the reactor in a constant-temperature water bath kettle at 20 ℃ for reaction;
s5, preparing a bipolar membrane: after the cathode membrane functionalization reaction is finished for 60 hours, continuing the sulfonation reaction at 20 ℃ for 72 hours; removing reaction liquid on one side of the cathode membrane, changing the reaction liquid into amino iron phthalocyanine alcohol/water solution, continuing to react for 8 hours, introducing an anion exchange group into bromomethyl on the outer layer of the cathode basement membrane and a cathode membrane functional reagent, introducing phthalocyanine into the bromomethyl on the inner layer of the cathode basement membrane and the amino iron phthalocyanine by reaction, introducing a water dissociation catalyst into a cathode interface layer and an anode interface layer, and removing residual reaction liquid in the basement membrane after the reaction is finished to obtain the monolithic polytrifluorochloroethylene bipolar membrane containing the phthalocyanine derivative water dissociation catalytic group, wherein the specific reaction formula is as follows:
Figure BDA0003542300450000101
example 4
A preparation method of a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst comprises the following steps:
s1, preparing a polychlorotrifluoroethylene grafted polymethyl styrene copolymer (PCTFE-g-PMST): weighing 20g of polychlorotrifluoroethylene, dissolving in 200mL of N, N-dimethylformamide, introducing nitrogen to remove oxygen, heating to 110 ℃, adding 172.9g of 3-methyl styrene, 8.72g of CuBr and 21.13g of pentamethyl diethylenetriamine into a reaction system, reacting for 24 hours at constant temperature under the protection of nitrogen, pouring the reaction solution into an alcohol-water mixed solvent with the volume ratio of 1:1, and precipitating to obtain a grafting combination; leaching the precipitate with alcohol water for multiple times, then soaking the precipitate in running water for 24 hours to remove copper ions and pentamethyldiethylenetriamine, filtering and drying the precipitate, placing the precipitate in a Soxhlet extractor to extract the precipitate for 10 hours with toluene to completely remove homopolymer polystyrene, and placing the precipitate in a vacuum drying oven at 80 ℃ to dry the precipitate for 24 hours to prepare the polychlorotrifluoroethylene grafted polymethylstyrene graft polymer, wherein the reaction formula is as shown in example 2;
s2, bromination: weighing 10g of polychlorotrifluoroethylene grafted polymethylstyrene graft polymer, dissolving in 160mL of carbon tetrachloride, adding 10.04g N-bromosuccinimide as a brominating agent and 1.0g of dicumyl peroxide as an initiator, boiling and refluxing for 4h under the conditions of 130 ℃ and stirring, gradually changing the solution into orange red along with the reaction, continuing to react for a period of time after the orange red fades, stopping heating and stirring, precipitating white floccule in anhydrous methanol or isopropanol, extracting the white floccule in a Soxhlet extractor with acetone for 20h to remove impurities, and drying to obtain the bromomethylation polymer, wherein the reaction formula is shown in example 1:
s3, preparing a base film: dissolving the bromomethylated polymer prepared in the step S2 in N-dimethyl pyrrolidone, casting the solution on a clean glass plate after the polymer is completely dissolved, and drying to prepare a polychlorotrifluoroethylene grafted bromomethylated styrene base film;
s4, introducing ion exchange groups on two sides of the base membrane: placing the polychlorotrifluoroethylene grafted bromomethylated styrene basement membrane prepared in the step S3 in a reactor, and respectively soaking two side surfaces of the basement membrane in a sulfonation reagent and a negative membrane functional reaction reagent, wherein the solvent of the sulfonation reagent is sodium p-phenolate sodium benzenesulfonate, and the solution is a mixed solution of distilled water and DMAc (sodium p-phenolate sodium benzenesulfonate: H)2The mass ratio of O to DMAc is 1:7:3), the solvent of the negative membrane functionalization reaction reagent is trimethyl imidazole, and the solution is a mixed solution of distilled water and DMAc (trimethyl imidazole: H)2DMAc is in a mass ratio of 1:8:2), and the base membrane separates the two reagents; introducing nitrogen to remove air in the reactor, sealing the reactor, and placing the reactor in a constant-temperature water bath kettle at 50 ℃ for reaction;
s5, preparing a bipolar membrane: after the negative film functionalization reaction is finished for 40 hours, continuing the sulfonation reaction at 80 ℃ for 50 hours; removing reaction liquid on one side of the negative film, changing the reaction liquid into amino phthalocyanine copper alcohol/water solution, continuously reacting for 10 hours, introducing quaternary ammonium groups into a bromomethyl group on the outer layer of the negative basement film and a quaternizing agent, introducing phthalocyanine by reacting the bromomethyl group on the inner layer of the negative basement film with the amino phthalocyanine copper, introducing a water dissociation catalyst into the negative interface layer and the positive interface layer, and removing residual reaction liquid in the basement film after the reaction is finished to obtain the monolithic polytrifluorochloroethylene bipolar film containing the metal phthalocyanine derivative water dissociation catalyst, wherein the specific reaction formula is as follows:
Figure BDA0003542300450000121
example 5
A preparation method of a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst comprises the following steps:
s1, preparing a polychlorotrifluoroethylene grafted polymethyl styrene copolymer (PCTFE-g-PMST): weighing 20g of polychlorotrifluoroethylene, dissolving in 200mL of N, N-dimethylacetamide, introducing nitrogen to remove oxygen, heating to 110 ℃, adding 172.9g of 3-methylstyrene, 8.72g of CuBr and 21.13g of pentamethyldiethylenetriamine into a reaction system, reacting for 36 hours at constant temperature under the protection of nitrogen, pouring the reaction solution into an alcohol-water mixed solvent with the volume ratio of 1:1, and precipitating to obtain a graft conjugate; leaching the precipitate with alcohol water for multiple times, then soaking the precipitate in running water for 24 hours to remove copper ions and pentamethyldiethylenetriamine, filtering and drying the precipitate, placing the precipitate in a Soxhlet extractor to extract the precipitate for 10 hours with toluene to completely remove homopolymer polystyrene, and placing the precipitate in a vacuum drying oven at 80 ℃ to dry the precipitate for 24 hours to prepare the polychlorotrifluoroethylene grafted polymethylstyrene graft polymer, wherein the reaction formula is as shown in example 2;
s2, bromination: weighing 10g of polychlorotrifluoroethylene grafted polymethylstyrene graft polymer, dissolving the polychlorotrifluoroethylene grafted polymethylstyrene graft polymer in 150mL of mixed solvent of carbon tetrachloride and chlorobenzene, adding 10.04g N-bromosuccinimide as a brominating agent and 1.0g of dicumyl peroxide as an initiator, boiling and refluxing for 6h under the conditions of 130 ℃ and stirring, gradually changing the solution into orange red along with the reaction, continuing to react for a period of time after the orange red fades, stopping heating and stirring, precipitating white floccule in anhydrous methanol or isopropanol, extracting the white floccule in a Soxhlet extractor with acetone for 20h to remove impurities, and drying to obtain the bromomethylated polymer, wherein the reaction formula is shown in example 1:
s3, preparing a base film: dissolving the bromomethylated polymer prepared in the step S2 in N-dimethyl pyrrolidone, casting the bromomethylated polymer on a clean glass plate after the polymer is completely dissolved, and drying to prepare the polychlorotrifluoroethylene grafted bromomethylated styrene base film;
s4, introducing ion exchange groups on two sides of the base membrane: placing the polychlorotrifluoroethylene grafted bromomethylated styrene base membrane prepared in the step S3 in a reactor, and respectively soaking two side surfaces of the base membrane in a sulfonation reagent and a negative membrane functional reaction reagent, wherein the solvent of the sulfonation reagent is sodium p-phenolate sodium benzenesulfonate, and the solution is a mixed solution of distilled water and NMP (sodium p-phenolate sodium benzenesulfonate: H)2The mass ratio of O to NMP is 1:7:3), the solvent of the negative membrane functionalization reaction reagent is pentamethylguanidine, and the solution is a mixed solution of distilled water and NMP (pentamethylguanidine: H)2The mass ratio of O to NMP is 1:8:2), and the base membrane separates the two reagents; after nitrogen is introduced to remove air in the reactorSealing the reactor, and placing the reactor in a constant-temperature water bath kettle at 60 ℃ for reaction;
s5, preparing a bipolar membrane: after the negative film functionalization reaction is finished for 40h, continuing the sulfonation reaction at 50 ℃ for 50 h; removing reaction liquid on one side of a quaternary anion membrane, changing the reaction liquid into amino phthalocyanine copper alcohol/water solution, continuing to react for 8 hours, introducing an anion exchange group into bromomethyl on the outer layer of a cathode basement membrane and a cathode membrane functional reaction reagent, introducing phthalocyanine into the bromomethyl on the inner layer of the cathode basement membrane and the amino phthalocyanine copper through reaction, introducing a water dissociation catalyst into a cathode interface layer and an anode interface layer, removing residual reaction liquid in the basement membrane after the reaction is finished, and obtaining the monolithic polytrifluorochloroethylene bipolar membrane containing the metal phthalocyanine derivative water dissociation catalyst, wherein the specific reaction formula is as follows:
Figure BDA0003542300450000141
example 6
A preparation method of a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst comprises the following steps:
s1, preparing a polychlorotrifluoroethylene grafted polymethyl styrene copolymer (PCTFE-g-PMST): weighing 20g of polychlorotrifluoroethylene, dissolving in 200mL of N-methylpyrrolidone, introducing nitrogen to remove oxygen, heating to 110 ℃, adding 144.1g of 2-methylstyrene, 8.72g of CuBr and 9.52g of bipyridine into a reaction system, reacting for 20 hours at constant temperature under the protection of nitrogen, pouring the reaction solution into an alcohol-water mixed solvent with the volume ratio of 1:1, and precipitating to obtain a graft conjugate; leaching the precipitate with alcohol water for multiple times, then soaking the precipitate in running water for 24 hours to remove copper ions and bipyridine, filtering and drying the precipitate, placing the precipitate in a Soxhlet extractor to be extracted with toluene for 10 hours to completely remove homopolymer polystyrene, and placing the precipitate in a vacuum drying oven at 80 ℃ to be dried for 24 hours to prepare the polytrifluorochloroethylene grafted polymethylstyrene graft polymer, wherein the reaction formula is shown in example 1:
s2, bromination: weighing 10g of polychlorotrifluoroethylene grafted polymethylstyrene graft polymer, dissolving in 150mL of a mixed solvent of 1, 2-dichloroethane and chlorobenzene, adding 10.04g N-bromosuccinimide as a brominating agent and 1.0g of dicumyl peroxide as an initiator, boiling and refluxing for 4h under the conditions of 130 ℃ and stirring, gradually changing the solution into orange red along with the reaction, continuing to react for a period of time after the orange red fades, stopping heating and stirring, precipitating white floccule in anhydrous methanol or isopropanol, putting the white floccule into a Soxhlet extractor, extracting with acetone for 20h to remove impurities, and drying to obtain the bromomethylated polymer, wherein the reaction formula is shown in example 1:
s3, preparing a base film: dissolving the bromomethylated polymer prepared in the step S2 in N-dimethyl pyrrolidone, casting the solution on a clean glass plate after the polymer is completely dissolved, and drying to prepare a polychlorotrifluoroethylene grafted bromomethylated styrene base film;
s4, introducing ion exchange groups on two sides of the base membrane: placing the polychlorotrifluoroethylene grafted bromomethylated styrene basement membrane prepared in the step S3 in a reactor, and respectively soaking two side surfaces of the basement membrane in a sulfonation reagent and a negative membrane functional reaction reagent, wherein the solvent of the sulfonation reagent is sodium p-phenolate sodium benzenesulfonate, and the solution is a mixed solution of distilled water and DMSO (sodium p-phenolate sodium benzenesulfonate: H)2DMSO is 1:7:3 in mass ratio, the solvent of the negative membrane functionalization reaction reagent is N-methylmorpholine, and the solution is a mixed solution of distilled water and DMSO (N-methylmorpholine: H)2DMSO is 1:8:2) by mass, and the base membrane separates the two reagents; introducing nitrogen to remove air in the reactor, sealing the reactor, and placing the reactor in a constant-temperature water bath kettle at 60 ℃ for reaction; the bromomethyl on the positive basal membrane reacts with a sulfonation reagent to introduce sulfonic acid groups, and the bromomethyl on the negative basal membrane reacts with a negative membrane functionalization reaction reagent to introduce anion exchange groups, namely quaternary ammonium groups;
s5, preparing a bipolar membrane: after the negative membrane functionalization reaction is finished for 10 hours, continuing the sulfonation reaction at 45 ℃ until 20 hours are finished; removing reaction liquid on one side of a negative film, changing the reaction liquid into amino cobalt phthalocyanine alcohol/water solution, continuing to react for 8 hours, introducing an anion exchange group into bromomethyl on the outer layer of the negative basement membrane and a negative film functionalized reaction reagent, introducing phthalocyanine into the bromomethyl on the inner layer of the negative basement membrane through reaction with the amino cobalt phthalocyanine, introducing a water dissociation catalyst into a negative interface layer and a positive interface layer, and removing residual reaction liquid in the basement membrane after the reaction is finished to obtain the monolithic polytrifluorochloroethylene bipolar membrane containing the metal phthalocyanine derivative water dissociation catalyst, wherein the specific reaction formula is as follows:
Figure BDA0003542300450000161
in addition to the above embodiments, the methylstyrene monomer in step S1 in the present invention may be any one of 2, 4-dimethylstyrene, 3, 4-dimethylstyrene, 2,3, 4-trimethylstyrene, and 3,4, 5-trimethylstyrene monomer; the organic solvent I can also be the combination of two of N, N-dimethylacetamide, dimethyl sulfoxide, N-methylpyrrolidone and N, N-dimethylformamide in any proportion; the solvent of the sulfonation reagent in the step S4 can be any one of sodium hydroxybenzenesulfonate, sodium hydroxysulfonate, 2-sodium hydroxysulfonate, 3-sodium hydroxysulfonate, 4-sodium hydroxysulfonate, sodium mercaptoethylsulfonate or sodium mercaptopropylsulfonate; the solvent of the quaternization reagent can be any one of triethylamine, methyl ethyl imidazole, dimethyl propyl imidazole, dimethyl butyl imidazole, tetramethyl imidazole, trimethyl ethyl imidazole, methyl ethyl imidazole, tetramethyl ethyl guanidine, tetramethyl propyl guanidine, tetramethyl butyl guanidine and tetramethyl hexyl guanidine; the phthalocyanine can also be any one of hydroxyl substituent phthalocyanine, amino substituent phthalocyanine and transition metal-containing hydroxyl substituent phthalocyanine.
The above-mentioned embodiments are only preferred embodiments of the present invention, but the embodiments of the present invention are not limited by the above-mentioned embodiments, and any other changes, modifications, substitutions, combinations, and simplifications which do not depart from the spirit and principle of the present invention should be regarded as equivalent replacements within the protection scope of the present patent.

Claims (10)

1. A monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst, characterized in that: introducing a sulfonic acid group into one surface of the bipolar membrane, and introducing a quaternary ammonium group into the other surface of the bipolar membrane; the structural formula of the cation exchange membrane in the bipolar membrane is as follows:
Figure FDA0003542300440000011
the anion exchange membrane has the structural formula:
Figure FDA0003542300440000012
the structural formula of the intermediate interfacial catalyst is as follows:
Figure FDA0003542300440000013
wherein n is the polymerization degree of the main chain of the polytrifluorochloroethylene base membrane, m is the polymerization degree of the polybromomethylstyrene side chain, and n and m are integers which are not zero.
2. A preparation method of a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst is characterized by comprising the following steps:
s1, preparing a polychlorotrifluoroethylene grafted polymethyl styrene copolymer: dissolving polychlorotrifluoroethylene in an organic solvent I, introducing nitrogen to remove oxygen, heating, mixing according to the molar ratio of polychlorotrifluoroethylene, a methyl styrene monomer, CuBr and bipyridine or pentamethyl diethylenetriamine being 1 (20-100): 1:2, reacting for 5-40 h at constant temperature under the protection of nitrogen, pouring the reaction liquid into an alcohol-water mixed solvent with the volume ratio of 1:1, and precipitating to obtain a grafted combination; leaching the precipitate with alcohol water for multiple times, soaking in running water for 24h, filtering, and drying to obtain the polychlorotrifluoroethylene grafted polymethyl styrene graft polymer;
s2, bromination: dissolving the polychlorotrifluoroethylene grafted polymethyl styrene polymer prepared in the step S1 in an organic solvent II, adding a brominating agent and an initiator, boiling and refluxing for 4-6 h under the conditions of heating and stirring, stopping heating and stirring after full reaction, precipitating white floccules in anhydrous methanol or isopropanol, washing to remove impurities, and drying to obtain a bromomethylation polymer;
s3, preparing a base film: dissolving the bromomethylated polymer prepared in the step S2 in N-dimethyl pyrrolidone, casting the solution on a clean glass plate after the polymer is completely dissolved, and drying to prepare a polychlorotrifluoroethylene grafted bromomethylated styrene base film;
s4, introducing ion exchange groups on two sides of a base membrane: placing the polychlorotrifluoroethylene grafted bromomethylated styrene base membrane prepared in the step S3 in a reactor, respectively soaking two side surfaces of the base membrane in a sulfonation reagent and a negative membrane functional reaction reagent, introducing nitrogen to remove air in the reactor, sealing the reactor, and placing the reactor in a constant-temperature water bath kettle at the temperature of 20-70 ℃ for reacting for 40-60 hours;
s5, preparing a bipolar membrane: after the negative film functionalization reaction is finished, continuing the sulfonation reaction at 20-90 ℃, and keeping the sulfonation reaction time for 50-72 h longer than the negative film functionalization reaction time; and (2) introducing sulfonic acid groups through sulfonation reaction, removing reaction liquid on one side of the cathode membrane, changing the reaction liquid into intermediate interface layer catalyst reaction liquid and cathode membrane functional reagent mixed solution for continuous reaction, introducing anion exchange groups and sulfonic acid groups into two sides of the base membrane respectively, introducing metal phthalocyanine derivatives and anion exchange groups into a thin layer between the two sides, and removing residual reaction liquid in the base membrane after the reaction is finished to obtain the monolithic polytrifluorochloroethylene bipolar membrane containing the metal phthalocyanine derivative water dissociation catalyst.
3. The method for preparing a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst according to claim 2, wherein: in step S1, the methylstyrene monomer is any one of 4-methylstyrene, 2-methylstyrene, 3-methylstyrene, 2, 4-dimethylstyrene, 3, 4-dimethylstyrene, 2,3, 4-trimethylstyrene, 3,4, 5-trimethylstyrene, 2,4, 6-trimethylstyrene, 2,3,4, 5-tetramethylstyrene, 2,3,4, 6-tetramethylstyrene, and 2,3,4,5, 6-pentamethylstyrene monomer.
4. The method for preparing a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst according to claim 2, wherein: in the step S1, the organic solvent I is any one or a combination of two of N, N-dimethylacetamide, dimethyl sulfoxide, N-methylpyrrolidone and N, N-dimethylformamide in any proportion.
5. The method for preparing a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst according to claim 2, wherein: and in the step S2, the organic solvent II is any one or a combination of two of 1, 2-dichloroethane, chlorobenzene and carbon tetrachloride in any proportion.
6. The method for preparing a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst according to claim 2, wherein: the solvent of the sulfonation reagent in the step S4 is any one of sodium phenolsulfonate, sodium hydroxybenzenesulfonate, sodium hydroxysulfonate, sodium 2-hydroxysulfonate, sodium 3-hydroxysulfonate, sodium 4-hydroxysulfonate, sodium mercaptoethylsulfonate or sodium mercaptopropylsulfonate, and the solution of the sulfonation reagent is one of distilled water, THF, DMF, DMAc, NMP and DMSO or a mixture of two of them in any proportion.
7. The method for preparing a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst according to claim 2, wherein: the solvent of the negative membrane functionalization reactant in the step S4 is any one of trimethylamine, triethylamine, dimethylimidazole, trimethylimidazole, methylethylimidazole, dimethylpropylimidazole, dimethylbutylimidazole, tetramethylimidazole, trimethylethylimidazole, methylethylimidazole, pentamethylguanidine, tetramethylethylguanidine, tetramethylpropylguanidine, tetramethylbutylguanidine, tetramethylhexylguanidine, or N-methylmorpholine, and the solution of the negative membrane functionalization reactant in the quaternary step S4 is one or a combination of two of distilled water, THF, DMF, DMAc, NMP, and DMSO in any proportion.
8. The method for preparing a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst according to claim 2, wherein: the intermediate interface layer catalyst reaction liquid is an alcohol/water solution containing a metal phthalocyanine derivative.
9. The method for preparing a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst of claim 8, wherein: the phthalocyanine is any one of hydroxyl substituent phthalocyanine, amino substituent phthalocyanine, phthalocyanine containing transition metal hydroxyl substituent or phthalocyanine containing transition metal amino substituent.
10. The method for preparing a monolithic polytrifluorochloroethylene bipolar membrane containing a metal phthalocyanine derivative water dissociation catalyst as claimed in claim 9, wherein: the metal phthalocyanine derivative central ion can be any one of inorganic metal ions.
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Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1041955A (en) * 1988-10-17 1990-05-09 阿托化学公司 Block and graft copolymer and its production and application
CN101899675A (en) * 2009-10-13 2010-12-01 福建师范大学 Bipolar membrane and preparation method thereof
CN105985495A (en) * 2015-02-04 2016-10-05 浙江大学 Cationic functional fluorine-containing polymer and preparation method thereof
WO2017205458A1 (en) * 2016-05-24 2017-11-30 Vanderbilt University Nanofiber-based bipolar membranes, fabricating methods and applications of same
CN111495215A (en) * 2020-05-12 2020-08-07 福建师范大学 Preparation method of monolithic polyarylethersulfone ketone bipolar membrane with side chain containing phthalocyanine water dissociation catalytic group
CN111499916A (en) * 2020-05-12 2020-08-07 福建师范大学 Preparation method of monolithic polyaryletherketone bipolar membrane with phthalocyanine group-containing side group
CN111530313A (en) * 2020-05-12 2020-08-14 福建师范大学 Preparation method of side group bonded phthalocyanine catalytic group monolithic polysulfone bipolar membrane
CN111530312A (en) * 2020-05-12 2020-08-14 福建师范大学 Preparation method of single-sheet type polysulfone bipolar membrane with side group bonded with porphyrin group
CN111530298A (en) * 2020-05-12 2020-08-14 福建师范大学 Preparation method of monolithic polyarylethersulfone ketone bipolar membrane containing phthalocyanine water dissociation catalytic group
CN111617644A (en) * 2020-05-12 2020-09-04 福建师范大学 Preparation method of monolithic polyaryletherketone bipolar membrane with side chain containing porphyrin water dissociation catalytic group

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1041955A (en) * 1988-10-17 1990-05-09 阿托化学公司 Block and graft copolymer and its production and application
CN101899675A (en) * 2009-10-13 2010-12-01 福建师范大学 Bipolar membrane and preparation method thereof
CN105985495A (en) * 2015-02-04 2016-10-05 浙江大学 Cationic functional fluorine-containing polymer and preparation method thereof
WO2017205458A1 (en) * 2016-05-24 2017-11-30 Vanderbilt University Nanofiber-based bipolar membranes, fabricating methods and applications of same
CN111495215A (en) * 2020-05-12 2020-08-07 福建师范大学 Preparation method of monolithic polyarylethersulfone ketone bipolar membrane with side chain containing phthalocyanine water dissociation catalytic group
CN111499916A (en) * 2020-05-12 2020-08-07 福建师范大学 Preparation method of monolithic polyaryletherketone bipolar membrane with phthalocyanine group-containing side group
CN111530313A (en) * 2020-05-12 2020-08-14 福建师范大学 Preparation method of side group bonded phthalocyanine catalytic group monolithic polysulfone bipolar membrane
CN111530312A (en) * 2020-05-12 2020-08-14 福建师范大学 Preparation method of single-sheet type polysulfone bipolar membrane with side group bonded with porphyrin group
CN111530298A (en) * 2020-05-12 2020-08-14 福建师范大学 Preparation method of monolithic polyarylethersulfone ketone bipolar membrane containing phthalocyanine water dissociation catalytic group
CN111617644A (en) * 2020-05-12 2020-09-04 福建师范大学 Preparation method of monolithic polyaryletherketone bipolar membrane with side chain containing porphyrin water dissociation catalytic group

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
CHEN RIYAO ET AL.: "Preparation and characterization of mSA/mCS bipolar membranes modified by CuTsPc and CuTAPc", 《JOURNAL OF MEMBRANE SCIENCE》, vol. 355, no. 1, pages 1 - 6, XP027018833 *
LIU YAOXING ET AL.: "Treatment of raffinate generated via copper ore hydrometallurgical processing using a bipolar membrane electrodialysis system", 《CHEMICAL ENGINEERING JOURNAL》, vol. 382, pages 122956 *
陈丽金等: "具有不同取代基数量铁酞菁衍生物改性双极膜的性能研究", 《应用化工》, vol. 42, no. 4, pages 661 - 664 *

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