CN110041519B - Long-chain branch poly (arylene ether nitrile) anion exchange membrane and preparation method thereof - Google Patents

Long-chain branch poly (arylene ether nitrile) anion exchange membrane and preparation method thereof Download PDF

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CN110041519B
CN110041519B CN201910368274.9A CN201910368274A CN110041519B CN 110041519 B CN110041519 B CN 110041519B CN 201910368274 A CN201910368274 A CN 201910368274A CN 110041519 B CN110041519 B CN 110041519B
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焉晓明
查怀宁
贺高红
刘嘉霏
桑嘉悦
田震
代岩
潘昱
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Dalian University of Technology
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Abstract

The invention belongs to the technical field of alkaline anion exchange membranes, and relates to a long-chain branched poly (arylene ether nitrile) anion exchange membrane and a preparation method thereof. The prepared membrane not only has higher ionic conductivity, but also keeps good dimensional stability, and can be applied to alkaline fuel cells.

Description

Long-chain branch poly (arylene ether nitrile) anion exchange membrane and preparation method thereof
Technical Field
The invention belongs to the technical field of alkaline anion exchange membranes, and relates to a long-chain branched poly (arylene ether nitrile) anion exchange membrane and a preparation method thereof.
Background
With the increasing energy crisis and the worsening global environmental pollution, the development of clean and efficient new energy utilization by human beings is urgent. Fuel cells have attracted attention of many researchers in recent years due to their high energy conversion efficiency, environmental friendliness, and the like. The proton exchange membrane fuel cell has been developed greatly in recent years by virtue of its excellent performance, but the proton exchange membrane fuel cell greatly increases the production cost of the fuel cell and seriously hinders the development of the proton exchange membrane fuel cell because noble metal platinum is used as a catalyst. Compared with proton exchange membrane fuel cells, alkaline anion exchange membrane fuel cells have similar working principles, but can allow the use of fewer catalysts or non-noble metal catalysts under alkaline conditions, so that the cost is greatly reduced, and therefore, the alkaline anion exchange membrane fuel cells gradually become a hotspot of research in the field of fuel cells.
As a core component of an alkaline anion exchange membrane fuel cell, the alkaline anion exchange membrane has a shallower research than a proton exchange membrane, and has the following problems: low hydroxide ion conductivity, poor membrane dimensional stability, low alkaline stability, and the like. In order to improve the hydroxide conductivity of the basic anion-exchange membrane, long-chain branches can be introduced into the membrane structure, and partial research shows that the anion-exchange membrane with longer chain branches has more excellent performance in ion conductivity compared with the anion-exchange membrane with short chain branches. In order to improve the dimensional stability of the membrane, a crosslinking method is generally adopted, however, the crosslinking causes poor solubility of the product in an organic solvent, and is not beneficial to the preparation of the membrane. It has been shown that the introduction of cyano groups into the main chain of the film reduces the degree of water swelling of the film without sacrificing the solubility of the product.
Therefore, in order to simultaneously solve the problems of low hydroxide ion conductivity and poor membrane dimensional stability in the preparation of the existing anion exchange membrane material, the invention introduces cyano groups into the membrane, inhibits membrane swelling through enhanced intermolecular interaction and does not sacrifice membrane solubility on the other hand. In addition, a long branched chain structure is introduced by taking amino as a site on a polymer skeleton with nitrile groups, so that the microphase separation of hydrophilic-hydrophobic parts is further promoted, the generation of ion clusters is promoted, and a penetrating ion transmission channel is formed, so that the ion-conducting polymer has high ion conductivity and wide application prospect of fuel cells.
Disclosure of Invention
The invention aims to improve the hydroxide ion conductivity of an alkaline anion-exchange membrane and ensure the dimensional stability of the alkaline anion-exchange membrane, and provides a preparation method of a long side chain poly (arylene ether nitrile) anion-exchange membrane, which comprises the following steps: the poly (arylene ether nitrile) polymer with good solubility is successfully synthesized through polycondensation, then the long branched chain structure is introduced into the polymer by directly taking the amido of the polymer as a grafting site, and finally functionalization is carried out, so that a membrane material with a good ion conduction path is obtained, and finally a membrane is formed through a casting method. The prepared membrane not only has higher ionic conductivity, but also keeps good dimensional stability, and can be applied to alkaline fuel cells.
The technical scheme of the invention is as follows:
a long-chain branched poly (arylene ether nitrile) anion exchange membrane has the following structure:
Figure BDA0002048971940000021
wherein: x is 0-0.9, and y is 1-0.1; n is an integer of 1-16;
r is an introduced functional group and is one of N-methylpyrrolidine, N-methylmorpholine, N-methylpiperidine, 1-methylimidazole, 2-methylimidazole, 1, 2-dimethylimidazole, trimethylamine, triethylamine, tris (2,4, 6-trimethoxyphenyl) phosphine, pyridine and guanidine.
The preparation method of the long-chain branched poly (arylene ether nitrile) anion exchange membrane comprises the following steps:
(1) and (3) synthesis of poly (arylene ether nitrile):
dissolving 2, 6-difluorobenzonitrile, 2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane and potassium carbonate in a solvent A to prepare a solution with the mass concentration of 150-400 g/L, adding toluene in an amount which is 0.5-1.5 times the volume of the solvent A, condensing and refluxing for 3-12 h at 120-150 ℃ in a protective gas atmosphere until water and toluene are completely removed, and then heating to 160 ℃ to react for 12-20 h; pouring the obtained solution into a precipitator A under vigorous stirring to precipitate a white filamentous product, then carrying out re-precipitation operation to further improve the purity of the product, namely re-dissolving the obtained filamentous product into the solvent A to prepare a solution with the mass concentration of 100-350 g/L, then carrying out re-precipitation on the solution by the precipitator A, repeating the re-precipitation operation for about 2-5 times, and finally carrying out vacuum drying to obtain the poly (arylene ether nitrile);
the content of the 2,6 difluorobenzonitrile: 2, 2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane: hexafluorobisphenol a: the molar ratio of potassium carbonate is 10: 10-1: 15;
dissolving 2, 6-difluorobenzonitrile, 2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane, hexafluorobisphenol a and potassium carbonate in a solvent a, and adding hexafluorobisphenol a while controlling the molar ratio of 2, 6-difluorobenzonitrile to hexafluorobisphenol a to not less than 10: 9.
the solvent A is one of N, N-dimethylacetamide and N-methylpyrrolidone;
the precipitant A is one of methanol, ethanol and water;
the temperature of the poly (arylene ether nitrile) vacuum drying is 30-100 ℃, and the time is more than 6 hours;
(2) preparing a long-chain branched poly (arylene ether nitrile) anion exchange membrane:
preparing a poly (arylene ether nitrile)/solvent B solution with the mass concentration of 30-100 g/L, adding NaH under the protection of inert gas, reacting for 2-8 h at 20-60 ℃, adding a monomer A containing a fatty chain, and reacting for 12-48 h at 40-80 ℃; pouring the reaction solution into a precipitator B under rapid stirring, repeatedly washing and drying by using a solvent C, dissolving the product in the solvent B to prepare a solution with the mass concentration of 50g/L, adding a certain amount of ionizing reagent, and reacting for 48-72 h at the temperature of 80-120 ℃ to obtain a casting solution; spreading a film on a clean glass plate by using a casting method for the film casting solution, drying, then taking off the film from the glass plate, soaking the film in a solvent D for 24-48 h to remove anions from Cl-Conversion to OH-And repeatedly washing with deionized water to remove residual alkali liquor, thus obtaining the long-chain branched poly (arylene ether nitrile) anion exchange membrane.
The solvent B is one of N, N-dimethylformamide, N, N-dimethylacetamide, N-methylpyrrolidone and dimethyl sulfoxide;
the amount of the added substances of the NaH is 2-6 times of the amount of the substances of the amido substituted repeating units in the poly (arylene ether nitrile);
the structure of the monomer A containing the fatty chain is Cl- (CH)2)n-Br, added in a quantity of substance 1.5 to 3 times the quantity of substance of NaH; wherein n is a positive integer of 1-16;
the precipitant B is one of acetone, ethyl acetate and ethanol;
the solvent C is one of methanol, ethanol and water;
the product is repeatedly washed by the solvent C for 3-5 times;
the temperature required in the drying step after the product is repeatedly filtered and washed by the solvent C is 40-100 ℃, and the time is more than 8 hours;
the ionizing reagent is one of N-methylpyrrolidine, N-methylmorpholine, N-methylpiperidine, 1-methylimidazole, 2-methylimidazole, 1, 2-dimethylimidazole, trimethylamine, triethylamine, tris (2,4, 6-trimethoxyphenyl) phosphine, pyridine and guanidine;
the amount of substances added into the ionizing reagent is 1.5-3 times of the amount of substances of the monomer A containing the fatty chain;
the solvent D is one of KOH and NaOH;
the number of times of repeatedly washing the membrane by the deionized water is 3-5;
the drying temperature of the film formed by the casting method is 50-80 ℃, and the time is 24-48 hours; the thickness of the film formed by the casting method is within the range of 30-60 mu m.
The invention has the beneficial effects that:
(1) due to the existence of nitrile groups in the ion side chain poly (arylene ether nitrile) anion exchange membrane, the membrane swelling can be effectively inhibited by enhancing the dipole-dipole intermolecular interaction.
(2) The long branched chain structure can improve the mobility of the branched chain, effectively promote the microphase separation of hydrophilic and hydrophobic phases in the membrane, and better form an ion transmission channel, thereby improving the conductivity.
(3) The ion exchange capacity of the anionic membrane can be achieved by preparing poly (arylene ether nitriles) with different degrees of amino substitution.
(4) The poly (arylene ether nitrile) has good solubility in various solvents, and the solvent selection range is wide.
(5) The amido in the amido substituted poly (arylene ether nitrile) can be directly used as a functional reaction site, and the reaction step is simple.
Detailed Description
The present invention will be described in further detail with reference to examples, but the embodiments of the present invention are not limited thereto.
Example 1
Synthesis of Polyarylethernitrile 1.4050g (10mmol) of 2, 6-difluorobenzonitrile, 0.7475g (2mmol) of 2, 2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane, 2.7447g (8mmol) of hexafluorobisphenol A and 1.3961g (10mmol) of potassium carbonate were placed in a 50mL three-necked flask, a mixed solution of 5mL of toluene and 9mL of N, N-dimethylacetamide was added thereto, the temperature was gradually raised to 140 ℃ under a protective gas atmosphere, the mixture was cooled and refluxed for about 4 hours until water was completely removed, and then the temperature was raised to 160 ℃ and reacted for about 15 hours. Slowly pouring the product into ethanol solution under mechanical stirring after the reaction is finished, separating out a filamentous polymer product, then further improving the purity of the product, carrying out re-separation operation, namely re-dissolving the obtained filamentous product into N, N-dimethylacetamide to prepare a solution with the mass concentration of 100g/L, then separating out the solution again through the ethanol solution, repeating the re-separation operation for about 3 times, and finally carrying out vacuum drying to obtain the polyarylether nitrile;
the preparation of the long-chain branched poly (arylene ether nitrile) anion exchange membrane comprises the steps of weighing 0.4g of poly (arylene ether nitrile) product obtained in the previous step under the protection of nitrogen, adding the poly (arylene ether nitrile) product into a 50mL single-neck flask, dissolving the poly (arylene ether nitrile) product with 10mL of N, N-dimethylacetamide, adding 0.02172g of NaH after the polymer is fully dissolved, reacting the reaction system at 60 ℃ for 5h, then adding 0.1653mL of 1, 6-dibromohexane, and reacting the system at 60 ℃ for 48 h. After the reaction is finished, the product is precipitated by ethanol, repeatedly washed and dried to obtain a white powder product, then the white powder product is dissolved by 8ml of N-methylpyrrolidone, namely the solution with the mass concentration of 50g/L is prepared, 1ml of N-methylpiperidine is added, and the reaction system reacts for 3 days at the temperature of 100 ℃. And obtaining the casting solution. Then casting the casting solution to form a film; finally, the membrane was soaked in 1M KOH solution for 36h to remove anions from Cl-Conversion to OH-. And finally, repeatedly washing with deionized water to remove residual alkali, thereby obtaining the long-chain branched poly (arylene ether nitrile) anion exchange membrane.
The anion-exchange membrane obtained in this example had the following structure:
Figure BDA0002048971940000061
tests show that the ion conductivity of the long-chain branched poly (arylene ether nitrile) anion-exchange membrane prepared in the embodiment at 20 ℃ is 19mS cm-1The water absorption rate is 35 percent, the swelling degree is 16 percent, the film is not degraded after being soaked in 1mol/L KOH solution for 500 hours at the temperature of 60 ℃, and the film shows more excellent performance.
Example 2
Synthesis of Polyarylethernitrile 1.4050g (10mmol) of 2, 6-difluorobenzonitrile, 0.7475g (2mmol) of 2, 2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane, 2.7447g (8mmol) of hexafluorobisphenol A and 1.3961g (10mmol) of potassium carbonate were placed in a 50mL three-necked flask, a mixed solution of 5mL of toluene and 9mL of N, N-dimethylacetamide was added thereto, the temperature was gradually raised to 140 ℃ under a protective gas atmosphere, the mixture was cooled and refluxed for about 4 hours until water was completely removed, and then the temperature was raised to 160 ℃ and reacted for about 15 hours. Slowly pouring the product into ethanol solution under mechanical stirring after the reaction is finished, separating out a filamentous polymer product, then further improving the purity of the product, carrying out re-separation operation, namely re-dissolving the obtained filamentous product into N, N-dimethylacetamide to prepare a solution with the mass concentration of 100g/L, then separating out the solution again through the ethanol solution, repeating the re-separation operation for about 3 times, and finally carrying out vacuum drying to obtain the polyarylether nitrile;
the preparation of the long-chain branched poly (arylene ether nitrile) anion exchange membrane comprises the steps of weighing 0.4g of poly (arylene ether nitrile) product obtained in the previous step under the protection of nitrogen, adding the poly (arylene ether nitrile) product into a 50mL single-neck flask, dissolving the poly (arylene ether nitrile) product with 10mL of N, N-dimethylacetamide, adding 0.02172g of NaH after the polymer is fully dissolved, reacting the reaction system at 60 ℃ for 5h, then adding 0.2050mL of 1, 10-dibromohexane, and reacting the system at 60 ℃ for 48 h. After the reaction is finished, the product is precipitated by ethanol, repeatedly washed and dried to obtain a white powder product, then the white powder product is dissolved by 8ml of N-methylpyrrolidone, namely the solution with the mass concentration of 50g/L is prepared, 1ml of N-methylpiperidine is added, and the reaction system reacts for 3 days at the temperature of 100 ℃. And obtaining the casting solution.Then casting the casting solution to form a film; finally, the membrane was soaked in 1M KOH solution for 36h to remove anions from Cl-Conversion to OH-. And finally, repeatedly washing with deionized water to remove residual alkali, thereby obtaining the long-chain branched poly (arylene ether nitrile) anion exchange membrane.
The anion-exchange membrane obtained in this example had the following structure:
Figure BDA0002048971940000071
tests show that the ion conductivity of the long-chain branched poly (arylene ether nitrile) anion-exchange membrane prepared in the embodiment at 20 ℃ is 16mS cm-1The water absorption rate is 33 percent, the swelling degree is 13 percent, the film is not degraded after being soaked in 1mol/L KOH solution for 500 hours at the temperature of 60 ℃, and the film shows more excellent performance.
Example 3
Synthesis of Polyarylethernitrile 1.4050g (10mmol) of 2, 6-difluorobenzonitrile, 1.495g (4mmol) of 2, 2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane, 2.0585g (6mmol) of hexafluorobisphenol A and 1.3961g (10mmol) of potassium carbonate were placed in a 50mL three-necked flask, a mixed solution of 5mL of toluene and 9mL of N, N-dimethylacetamide was added thereto, the temperature was gradually raised to 140 ℃ under a protective gas atmosphere, and after cooling and refluxing for about 4 hours, water was completely removed, and then the temperature was raised to 160 ℃ and reacted for about 15 hours. Slowly pouring the product into ethanol solution under mechanical stirring after the reaction is finished, separating out a filamentous polymer product, then further improving the purity of the product, carrying out re-separation operation, namely re-dissolving the obtained filamentous product into N, N-dimethylacetamide to prepare a solution with the mass concentration of 100g/L, then separating out the solution again through the ethanol solution, repeating the re-separation operation for about 3 times, and finally carrying out vacuum drying to obtain the polyarylether nitrile;
the preparation of the long-chain branched poly (arylene ether nitrile) anion exchange membrane comprises the steps of weighing 0.4g of poly (arylene ether nitrile) product obtained in the previous step under the protection of nitrogen, adding the poly (arylene ether nitrile) product into a 50mL single-neck flask, dissolving the poly (arylene ether nitrile) product with 10mL of N, N-dimethylacetamide, adding 0.04344g of NaH after the polymer is fully dissolved, reacting the reaction system at 60 ℃ for 5 hours, and then adding 0.3306m of NaHl of 1, 6-dibromohexane, and reacting the system at 60 ℃ for 48 hours. After the reaction is finished, the product is precipitated by ethanol, repeatedly washed and dried to obtain a white powder product, then the white powder product is dissolved by 8ml of N-methylpyrrolidone, namely the solution with the mass concentration of 50g/L is prepared, 2ml of N-methylpiperidine is added, and the reaction system reacts for 3 days at the temperature of 100 ℃. And obtaining the casting solution. Then casting the casting solution to form a film; finally, the membrane was soaked in 1M KOH solution for 36h to remove anions from Cl-Conversion to OH-. And finally, repeatedly washing with deionized water to remove residual alkali, thereby obtaining the long-chain branched poly (arylene ether nitrile) anion exchange membrane.
The anion-exchange membrane obtained in this example had the following structure:
Figure BDA0002048971940000081
tests show that the ion conductivity of the long-chain branched poly (arylene ether nitrile) anion-exchange membrane prepared in the embodiment at 20 ℃ is 28mS cm-1The water absorption rate is 51 percent, the swelling degree is 23 percent, the film is not degraded after being soaked in 1mol/L KOH solution for 500 hours at the temperature of 60 ℃, and the film shows more excellent performance.

Claims (9)

1. A preparation method of a long-chain branch poly (arylene ether nitrile) anion exchange membrane is characterized in that the structure of the long-chain branch poly (arylene ether nitrile) anion exchange membrane is as follows:
Figure FDA0003068585310000011
wherein: x is 0-0.9, and y is 1-0.1; n is an integer of 1-16;
r is an introduced functional group and is one of N-methylpyrrolidine, N-methylmorpholine, N-methylpiperidine, 1-methylimidazole, 2-methylimidazole, 1, 2-dimethylimidazole, trimethylamine, triethylamine, pyridine and guanidine;
the preparation method comprises the following steps:
(1) and (3) synthesis of poly (arylene ether nitrile):
dissolving 2, 6-difluorobenzonitrile, 2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane and potassium carbonate in a solvent A to prepare a solution with the mass concentration of 150-400 g/L, adding toluene in an amount which is 0.5-1.5 times the volume of the solvent A, condensing and refluxing for 3-12 h at 120-150 ℃ in a protective gas atmosphere until water and toluene are completely removed, and then heating to 160 ℃ to react for 12-20 h; pouring the obtained solution into a precipitator A under vigorous stirring to precipitate a white filamentous product, then carrying out re-precipitation operation to further improve the purity of the product, namely re-dissolving the obtained filamentous product into the solvent A to prepare a solution with the mass concentration of 100-350 g/L, then separating the solution out through the precipitator A again, repeating the re-precipitation operation for 2-5 times, and finally carrying out vacuum drying to obtain the poly (arylene ether nitrile);
the content of the 2,6 difluorobenzonitrile: 2, 2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane: the molar ratio of potassium carbonate is 10: 10-1: 15;
the solvent A is one of N, N-dimethylacetamide and N-methylpyrrolidone;
the precipitant A is one of methanol, ethanol and water;
(2) preparing a long-chain branched poly (arylene ether nitrile) anion exchange membrane:
preparing a poly (arylene ether nitrile)/solvent B solution with the mass concentration of 30-100 g/L, adding NaH under the protection of inert gas, reacting for 2-8 h at 20-60 ℃, adding a monomer A containing a fatty chain, and reacting for 12-48 h at 40-80 ℃; pouring the reaction solution into a precipitator B under rapid stirring, repeatedly washing and drying by using a solvent C, dissolving the product in the solvent B to prepare a solution with the mass concentration of 50g/L, adding a certain amount of ionizing reagent, and reacting for 48-72 h at the temperature of 80-120 ℃ to obtain a casting solution; spreading a film on a clean glass plate by using a casting method for the film casting solution, drying, then taking off the film from the glass plate, soaking the film in a solvent D for 24-48 h to remove anions from Cl-Conversion to OH-Repeatedly washing with deionized water to remove residual alkali liquor, and obtaining the long-chain branched poly (arylene ether nitrile) anion exchange membrane;
the amount of the added substances of the NaH is 2-6 times of the amount of the substances of the amido substituted repeating units in the poly (arylene ether nitrile);
the structure of the monomer A containing the fatty chain is Cl- (CH)2)n-Br, added in a quantity of substance 1.5 to 3 times the quantity of substance of NaH; wherein n is a positive integer of 1-16;
the amount of substances added into the ionizing reagent is 1.5-3 times of the amount of substances of the monomer A containing the fatty chain;
the solvent B is one of N, N-dimethylformamide, N, N-dimethylacetamide, N-methylpyrrolidone and dimethyl sulfoxide;
the precipitant B is one of acetone and ethyl acetate;
the solvent C is one of methanol, ethanol and water;
the ionizing reagent is one of N-methylpyrrolidine, N-methylmorpholine, N-methylpiperidine, 1-methylimidazole, 2-methylimidazole, 1, 2-dimethylimidazole, trimethylamine, triethylamine, pyridine and guanidine;
the solvent D is one of KOH and NaOH.
2. The production method according to claim 1, wherein 2, 6-difluorobenzonitrile, 2-bis (3-amino-4-hydroxyphenyl) hexafluoropropane and potassium carbonate are dissolved in a solvent a, and hexafluorobisphenol a is added while controlling the molar ratio of 2, 6-difluorobenzonitrile to hexafluorobisphenol a to not less than 10: 9.
3. the production method according to claim 1 or 2, wherein in the step (1), the temperature of the polyarylene ether nitrile in vacuum drying is 30 to 100 ℃ and the time is 6 hours or more.
4. The preparation method according to claim 1 or 2, wherein in the step (2), the product is repeatedly washed by the solvent C for 3 to 5 times, and the temperature required in the drying step after repeatedly filtering and washing the product by the solvent C is 40 to 100 ℃ for 8 hours or more.
5. The preparation method according to claim 3, wherein in the step (2), the product is repeatedly washed by the solvent C for 3 to 5 times, and the temperature required in the drying step after repeatedly filtering and washing the product by the solvent C is 40 to 100 ℃ for 8 hours or more.
6. The preparation method according to claim 1,2 or 5, wherein in the step (2), the drying temperature for the film formed by the casting method is 50-80 ℃ and the time is 24-48 hours; the thickness of the film formed by the casting method is within the range of 30-60 mu m.
7. The preparation method according to claim 3, wherein in the step (2), the drying temperature of the film formed by the casting method is 50-80 ℃ and the time is 24-48 hours; the thickness of the film formed by the casting method is within the range of 30-60 mu m.
8. The preparation method according to claim 4, wherein in the step (2), the drying temperature of the film formed by the casting method is 50-80 ℃ and the time is 24-48 hours; the thickness of the film formed by the casting method is within the range of 30-60 mu m.
9. The method according to claim 1,2, 5, 7 or 8, wherein in the step (2), the deionized water is repeatedly used for washing the film for 3-5 times.
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