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CN109821426B - A kind of preparation method and use of polyimide film containing binaphthalene structure - Google Patents

A kind of preparation method and use of polyimide film containing binaphthalene structure Download PDF

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CN109821426B
CN109821426B CN201910056350.2A CN201910056350A CN109821426B CN 109821426 B CN109821426 B CN 109821426B CN 201910056350 A CN201910056350 A CN 201910056350A CN 109821426 B CN109821426 B CN 109821426B
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polyimide film
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CN109821426A (en
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邓国雄
王一雷
薛松
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Tianjin University of Technology
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Abstract

本发明公开了一种含有联萘结构聚酰亚胺薄膜的制备方法及用途,用于O2/N2、CO2/N2分离。该聚酰亚胺分离膜采用具有不同侧基官能团联萘胺单体和二酸酐合成聚酰亚胺树脂薄膜,该聚酰亚胺树脂薄膜具有高气体透过量和高选择性的特点:在0.8MPa的工作压力下,对O2的透过系数超过300barrer,CO2的透过效率超过800barrer;对氮气的透过系数低于25barrer;O2/N2的选择性系数超过13,对CO2/N2的选择性系数超过68。该聚酰亚胺薄膜便显出优异的耐热性能(超过500℃)和力学性能。

Figure 201910056350

The invention discloses a preparation method and application of a polyimide film containing a binaphthalene structure, which is used for the separation of O 2 /N 2 and CO 2 /N 2 . The polyimide separation membrane uses binaphthylamine monomers with different pendant functional groups and dianhydrides to synthesize polyimide resin films. The polyimide resin films have the characteristics of high gas permeability and high selectivity: at 0.8 Under the working pressure of MPa, the permeability coefficient of O 2 exceeds 300 barrer, and the permeability efficiency of CO 2 exceeds 800 barrer; the permeability coefficient of nitrogen gas is less than 25 barrer; the selectivity coefficient of O 2 /N 2 exceeds 13, and the permeability coefficient of CO 2 The selectivity coefficient of /N 2 exceeds 68. The polyimide film exhibits excellent heat resistance (over 500°C) and mechanical properties.

Figure 201910056350

Description

Preparation method and application of polyimide film containing binaphthyl structure
Technical Field
The invention belongs to the technical field of chemical industry, and designs a preparation method and application of a polyimide gas separation film with high temperature resistance and organic solvent resistance, wherein the prepared gas separation film is suitable for CO in industrial waste gas2Recovery of gases, combustion-supporting combustion of air O2Film enrichment and the like.
Background
The energy crisis forces the high-energy consuming industry to abandon the original extensive production mode and draw together towards a more efficient energy-saving mode. The treatment of the industrial waste gas and the tail gas not only comprises the removal of smoke dust particles and acid gas, but also is an important step in industrial production because the emission reduction of greenhouse gas is increasingly strict in environmental protection requirements. The traditional process generally purifies the tail gas layer by layer through combining catalytic combustion with an activated carbon adsorption filtration process. The process not only consumes a large amount of energy, but also is tedious, low in efficiency and capable of improving the product cost. Gas membrane separation is a rapidly evolving gas separation technology. The membrane separation technology has the functions of separation, concentration, purification and refining, and has the characteristics of simple filtration process, easy control, molecular filtration and the like. Therefore, it has become one of the most important means for solving the energy and environmental problems in the fields of medicine, chemical industry, metallurgy, petroleum, water treatment, electronics, etc. If the membrane separation technology is applied to carbon dioxide removal and oxygen enrichment in air, energy consumption in the distillation process is reduced, the separation process does not involve phase change, the process is simple, the efficiency is high, and the membrane separation technology can be widely applied to gas separation. The polyimide material has the advantages of good solvent resistance, high temperature resistance, low thermal expansion coefficient and the like, and has good flexibility. Polyimide gas separation membranes have become an important choice for gas membrane separation, but the gas selectivity and the gas passing rate need to be further improved by changing the structure of a high molecular chain through different monomer structures, the gas separation efficiency is improved, and the energy consumption is reduced.
Disclosure of Invention
The invention aims to provide a preparation method of a polyimide film for separating carbon dioxide or enriching oxygen in air. It has been found that by using a monomer with polyaminobinaphthyl structure synthesized from a variety of dicarboxylic anhydride molecules to synthesize polyamide acid polymers, different side chain groups of the polyaminobinaphthyl monomer can change the gas selectivity and permeability of the film. After appropriate heat treatment, a polyimide film having a high separation coefficient and a high gas permeation rate was obtained. O of polyimide film under 0.8MPa of operating pressure2/N2The separation coefficient can reach 14.92, and the oxygen transmission rate is 238.71 barrer; CO 22/N2The separation coefficient can reach 66.65, CO2Has a transmission rate of 836.12 barrer.
The invention adopts the following technical scheme:
1) the 1,1' -bi-2-naphthol is nitrified by nitric acid to obtain a gray yellow powdery compound.
2) And (2) reducing the gray powdery compound obtained in the step (1) in hydrogen with the palladium-carbon catalysis of less than 2bar to obtain a pink solid.
3) The synthesis of the polyimide resin containing the binaphthyl structure adopts any one of the following methods a) or b):
chemical imidization process: mixing the polyaminobinaphthyl compound obtained in the step 2) and a proper amount of hexafluorodianhydride in a molar ratio of 0.8-1.2: 1 into a dry round-bottom flask, and 3-8mL of N, N-dimethylacetamide is added under the condition of an ice-water bath. Then 1-6mL of triethylamine and 1-6mL of acetic anhydride are added for chemical imidization for 12-36 hours. After the reaction was complete, the solid was precipitated and collected in methanol, washed clean and dried under vacuum at 200 ℃ overnight.
The constant boiling imidization process: putting the polyaminobinaphthyl compound obtained in the step 2) and a proper amount of hexafluoro dianhydride (the molar ratio is 0.8-1.2) into a dry round-bottom flask filled with a certain solvent, and stirring for 5-30 minutes at 10-40 ℃ under the protection of nitrogen. The schlenk tube is then warmed to 50-80 ℃ and held for 0.5-2 hours until the solution is completely dissolved. Then adding a proper amount of isoquinoline and o-dichlorobenzene, and then refluxing at 180-240 ℃ for 2-14 hours. After the reaction was complete, the solid was collected by settling in methanol and dried under vacuum at 200 ℃ overnight.
4) Preparing a polyimide film: dissolving the binaphthyl polyimide resin synthesized in the step 3) in chloroform to prepare 2-8 wt% of casting solution. Filtering the membrane casting solution by a 0.45 mu m polytetrafluoroethylene filter membrane to remove insoluble substances, and then placing the filtrate in a culture dish and uniformly paving the culture dish at the bottom of the dish. The culture dish with the membrane casting liquid is sealed in a self-sealing bag to slowly volatilize the solvent until the membrane is formed, and finally all the solvent is removed in a vacuum oven at the temperature of 180 ℃ and 240 ℃ for 10-48 hours.
5) The prepared binaphthyl polyimide gas separation membrane is further subjected to heat treatment in a carbonization furnace under the protection of nitrogen. The heating rate is 2-10 ℃/min and the temperature is respectively kept at 300-800 ℃ for 0.5-4 hours. And naturally cooling to room temperature after the heat treatment is finished.
The invention has the advantages that:
1) the distance between high molecular chains in the polyimide film can be adjusted through different side chain groups of the polyamino binaphthyl, so that the gas selectivity of the film is adjusted.
2) The permeation rate of the film is adjusted by controlling the aging temperature.
3) O of polyimide film2/N2The separation coefficient can reach 14.92, and the oxygen transmission rate is 238.71 barrer; CO 22/N2The separation coefficient can reach 66.65, CO2Has a transmission rate of 836.12 barrer.
Drawings
FIG. 1 monomer chemical Structure of polyimide resin
FIG. 2 is a schematic view of the chemical structure of a polyimide resin
FIG. 3 scanning electron micrograph of polyimide film
Detailed description of the preferred embodiments
The invention is further illustrated by the following specific embodiments in conjunction with the accompanying drawings:
according to the invention for O2/N2And CO2/N2The preparation method of the system gas separation membrane mainly comprises the following steps: the preparation method comprises the following steps of synthesis of a polyamino biphenyl monomer, preparation of biphenyl polyimide resin, preparation of a biphenyl polyimide casting solution and a film, and carbonization treatment of the biphenyl polyimide film.
Example 1:
0.62mL of concentrated nitric acid was added dropwise to an acetic acid solution containing 1.0g of 1,1' -bi-2-naphthol dissolved therein, and the mixture was stirred at room temperature for 1 hour. The mixture was then poured into ice water and the solid collected by filtration. The solid and 10% Pd/C catalyst were added to N, N-dimethylformamide solvent and reacted at room temperature under magnetic stirring in a hydrogen atmosphere of 2bar for 24 hours. After filtering through diatomite, pouring the filtrate into deionized water for sedimentation to obtain the biphenyldiamine monomer. Under the ice-water bath, 1.26mmol of biphenyldiamine monomer, 1.28mmol of hexafluoro dianhydride and 4.0mL of N, N-dimethylacetamide are put into a three-necked bottle and are stirred uniformly by magnetic force. Stirring was continued at 40 ℃ for 4 hours, and then 3mL of triethylamine and 3mL of anhydride were added and reacted at room temperature for 24 hours. After the reaction was complete, the solid was precipitated into methanol and collected, washed clean and dried under vacuum at 200 ℃ overnight. The binaphthyl polyimide resin was dissolved in chloroform to prepare a 5 wt% casting solution, and insoluble matter was filtered off through a 0.45 μm polytetrafluoroethylene filter. And uniformly spreading the membrane casting solution on the bottom of the dish in a culture dish, sealing the dish in a self-sealing bag, and slowly volatilizing the solvent until the membrane is formed. Finally, the polyimide film is subjected to vacuum oven at 200 ℃ for 10 hours to remove all the solvent. The prepared binaphthyl polyimide gas separation membrane is further subjected to heat treatment in a carbonization furnace under the protection of nitrogen. The temperature was raised at 5 ℃/min for 30 minutes at 550 ℃. And naturally cooling to room temperature after the heat treatment is finished. O of polyimide film at 0.8MPa2/N2The separation coefficient can reach 12.70, CO2/N2The separation coefficient can reach 53.28; n is a radical of2,O2And CO2Through the use ofRates were 12.40, 157.53 and 660.98 barrers, respectively.
Example 2:
0.62mL of concentrated nitric acid was added dropwise to an acetic acid solution containing 1.0g of 1,1' -bi-2-naphthol dissolved therein, and the mixture was stirred at room temperature for 1 hour. The mixture was then poured into ice water and the solid collected by filtration. The solid obtained and a 10% Pd/C catalyst were added to N, N dimethylformamide solvent and reacted at room temperature under magnetic stirring in a hydrogen atmosphere of 2bar for 24 hours. After filtering through diatomite, pouring the filtrate into deionized water for sedimentation to obtain the biphenyldiamine monomer. Under the ice-water bath, 1.26mmol of biphenyldiamine monomer, 1.28mmol of 3,3 ', 4, 4' -benzophenonetetracarboxylic dianhydride and 4.0mL of N, N-dimethylacetamide were put into a three-necked flask and stirred by magnetic force. Stirring was continued at 40 ℃ for 4 hours, and then 3mL of triethylamine and 3mL of anhydride were added and reacted at room temperature for 24 hours. After the reaction was complete, the solid was precipitated into methanol and collected, washed clean and dried under vacuum at 200 ℃ overnight. The binaphthyl polyimide resin was dissolved in chloroform to prepare a 5 wt% casting solution, and insoluble matter was filtered off through a 0.45 μm polytetrafluoroethylene filter. And uniformly spreading the membrane casting solution on the bottom of the dish in a culture dish, sealing the dish in a self-sealing bag, and slowly volatilizing the solvent until the membrane is formed. Finally, the polyimide film is subjected to vacuum oven at 200 ℃ for 10 hours to remove all the solvent. The prepared binaphthyl polyimide gas separation membrane is further subjected to heat treatment in a carbonization furnace under the protection of nitrogen. The temperature was raised at 5 ℃/min for 30 minutes at 550 ℃. And naturally cooling to room temperature after the heat treatment is finished. O of polyimide film at 0.8MPa2/N2The separation coefficient can reach 11.58, CO2/N2The separation coefficient can reach 39.36; n is a radical of2,O2And CO2The transmission rates were 13.24, 153.40 and 521.27 barrers, respectively.
Example 3:
0.62mL of concentrated nitric acid was added dropwise to an acetic acid solution containing 1.0g of 1,1' -bi-2-naphthol dissolved therein, and the mixture was stirred at room temperature for 1 hour. The mixture was then poured into ice water and the solid collected by filtration. The solid obtained and a 10% Pd/C catalyst were added to N, N dimethylformamide solvent and reacted at room temperature under magnetic stirring in a hydrogen atmosphere of 2bar for 24 hours. After the mixture is filtered by the diatomite,pouring the filtrate into deionized water for sedimentation to obtain the biphenyldiamine monomer. Under ice-water bath, 1.26mmol of biphenyldiamine monomer, 1.28mmol of 4, 4' -diphenyl ether dianhydride and 4.0mL of dimethylacetamide were put into a three-necked flask and stirred by magnetic force. Stirring was continued at 40 ℃ for 4 hours, and then 3mL of triethylamine and 3mL of anhydride were added and reacted at room temperature for 24 hours. After the reaction was complete, the solid was precipitated into methanol and collected, washed clean and dried under vacuum at 200 ℃ overnight. The binaphthyl polyimide resin was dissolved in chloroform to prepare a 5 wt% casting solution, and insoluble matter was filtered off through a 0.45 μm polytetrafluoroethylene filter. And uniformly spreading the membrane casting solution on the bottom of the dish in a culture dish, sealing the dish in a self-sealing bag, and slowly volatilizing the solvent until the membrane is formed. Finally, the polyimide film is subjected to vacuum oven at 200 ℃ for 10 hours to remove all the solvent. The prepared binaphthyl polyimide gas separation membrane is further subjected to heat treatment in a carbonization furnace under the protection of nitrogen. The temperature was raised at 5 ℃/min for 30 minutes at 550 ℃. And naturally cooling to room temperature after the heat treatment is finished. O of polyimide film at 0.8MPa2/N2The separation coefficient can reach 6.29, CO2/N2The separation coefficient can reach 22.23; n is a radical of2,O2And CO2The transmission rates were 14.33, 90.11 and 318.52barrer, respectively.
Example 4:
0.62mL of concentrated nitric acid was added dropwise to an acetic acid solution containing 1.0g of 1,1' -bi-2-naphthol dissolved therein, and the mixture was stirred at room temperature for 1 hour. The mixture was then poured into ice water and the solid collected by filtration. The solid obtained and a 10% Pd/C catalyst were added to N, N dimethylformamide solvent and reacted at room temperature under magnetic stirring in a hydrogen atmosphere of 2bar for 24 hours. After filtering through diatomite, pouring the filtrate into deionized water for sedimentation to obtain the biphenyldiamine monomer. 4.8mmol of biphenyldiamine monomer, 4.8mmol of hexafluoro dianhydride and 7.25 mmol of LN-methyl pyrrolidone are added into a three-necked flask, stirred for 15 minutes at room temperature under the protection of nitrogen, and then heated to 60 ℃ and stirred for 30 minutes. After a drop of isoquinoline and 5mL of o-dichlorobenzene were added to the reaction system, the temperature was raised to 190 ℃ for 12 hours. After the reaction was complete, the solid was precipitated into methanol and collected, washed clean and dried under vacuum at 200 ℃ overnight. The binaphthyl polyimide resin was dissolved in chloroform to prepare5 wt% of the casting solution, and insoluble matter was filtered off through a 0.45 μm polytetrafluoroethylene filter. And uniformly spreading the membrane casting solution on the bottom of the dish in a culture dish, sealing the dish in a self-sealing bag, and slowly volatilizing the solvent until the membrane is formed. Finally, the polyimide film is subjected to a vacuum oven at 200 ℃ for 24 hours to remove all the solvent. The prepared binaphthyl polyimide gas separation membrane is further subjected to heat treatment in a carbonization furnace under the protection of nitrogen. The temperature was raised at 5 ℃/min for 30 minutes at 550 ℃. And naturally cooling to room temperature after the heat treatment is finished. O of polyimide film at 0.8MPa2/N2The separation coefficient can reach 5.13, CO2/N2The separation coefficient can reach 33.94; n is a radical of2,O2And CO2The transmission rates were 2.02, 10.36 and 68.5barrer, respectively.
Example 5:
0.62mL of concentrated nitric acid was added dropwise to an acetic acid solution containing 1.0g of 1,1' -bi-2-naphthol dissolved therein, and the mixture was stirred at room temperature for 1 hour. The mixture was then poured into ice water and the solid collected by filtration. The solid obtained and a 10% Pd/C catalyst were added to N, N dimethylformamide solvent and reacted at room temperature under magnetic stirring in a hydrogen atmosphere of 2bar for 24 hours. After filtering through diatomite, pouring the filtrate into deionized water for sedimentation to obtain the biphenyldiamine monomer. 4.8mmol of biphenyldiamine monomer, 4.8mmol of hexafluoro dianhydride and 7.25 mmol of LN-methyl pyrrolidone are added into a three-necked flask, stirred for 15 minutes at room temperature under the protection of nitrogen, and then heated to 60 ℃ and stirred for 30 minutes. After a drop of isoquinoline and 5mL of o-dichlorobenzene were added to the reaction system, the temperature was raised to 190 ℃ for 12 hours. After the reaction was complete, the solid was precipitated into methanol and collected, washed clean and dried under vacuum at 200 ℃ overnight. The binaphthyl polyimide resin was dissolved in chloroform to prepare a 5 wt% casting solution, and insoluble matter was filtered off through a 0.45 μm polytetrafluoroethylene filter. And uniformly spreading the membrane casting solution on the bottom of the dish in a culture dish, sealing the dish in a self-sealing bag, and slowly volatilizing the solvent until the membrane is formed. Finally, the polyimide film is subjected to a vacuum oven at 200 ℃ for 24 hours to remove all the solvent. The prepared binaphthyl polyimide gas separation membrane is further subjected to heat treatment in a carbonization furnace under the protection of nitrogen. The temperature was raised at 5 ℃/min for 30 minutes at 550 ℃. And naturally cooling to room temperature after the heat treatment is finished. Polyimide at 0.8MPaO of imine film2/N2The separation coefficient can reach 13.81, CO2/N2The separation coefficient can reach 66.65; n is a radical of2,O2And CO2The transmission rates were 12.54, 173.29 and 836.12 barrers, respectively.
The invention is shown in figure 1, which shows the chemical structure of the monomer of the polyimide resin, wherein figure 1a is the chemical structure of the polyamino binaphthyl monomer, and figure 1b is the chemical structure of the dianhydride monomer. FIG. 2 shows a schematic diagram of the chemical structure of the polyimide resin prepared by the present invention, and a scanning electron micrograph of the polyimide resin is shown in FIG. 3.

Claims (6)

1.一种含有联萘结构聚酰亚胺薄膜的制备方法,其特征在于包括以下步骤:1. a preparation method containing a polyimide film of binaphthalene structure is characterized in that comprising the following steps: 1)6,6-二硝基-1,1'-联-2-萘酚制备:冰水浴条件下将0.4-0.8mL硝酸加入到0.6-1.5g的1,1'-联-2-萘酚醋酸溶液中,然后在10-40℃下持续搅拌1-4小时,反应结束后,混合液倒入冰水中,过滤收集得到灰黄色固体粉末;1) Preparation of 6,6-dinitro-1,1'-bi-2-naphthol: add 0.4-0.8 mL of nitric acid to 0.6-1.5 g of 1,1'-bi-2-naphthalene under ice-water bath conditions phenolic acetic acid solution, and then continue stirring at 10-40 ° C for 1-4 hours. After the reaction is completed, the mixture is poured into ice water, and the gray-yellow solid powder is collected by filtration; 2)6,6-二氨基-1,1'-联-2-萘酚制备:将步骤1)所得化合物和2%-10%Pd/C催化剂加入到N,N-二甲基甲酰胺中,在磁力搅拌均匀,然后在1-2bar氢气氛中室温反应12-48个小时,反应结束后,用硅藻土过滤并浓缩得到产物;2) Preparation of 6,6-diamino-1,1'-bi-2-naphthol: add the compound obtained in step 1) and 2%-10% Pd/C catalyst to N,N-dimethylformamide , stir evenly with magnetic force, then react at room temperature for 12-48 hours in a hydrogen atmosphere of 1-2bar, after the reaction, filter and concentrate with diatomaceous earth to obtain the product; 3)含有联萘结构聚酰亚胺树脂的合成,采用以下a)或b)中任一方法:3) The synthesis of polyimide resin containing binaphthalene structure adopts any method in the following a) or b): a)化学亚胺化过程:称取步骤2)中合成多氨基联萘胺单体和六氟二酐以摩尔比为0.8-1.2:1加入到干燥圆底烧瓶中,冰水浴的条件下再加入3-8mL的N,N-二甲基乙酰胺,搅拌均匀后,升温至40℃继续反应4小时,然后加入1-6mL三乙胺和1-6mL醋酸酐进行化学亚胺化共12-36小时,反应结束后,在甲醇中沉淀并收集固体,清洗干净120-200℃真空干燥过夜;a) Chemical imidization process: Weigh the polyaminobinaphthylamine monomer synthesized in step 2) and hexafluorodianhydride in a molar ratio of 0.8-1.2:1 and add it to a dry round-bottomed flask, and then add it in an ice-water bath. Add 3-8 mL of N,N-dimethylacetamide, stir evenly, heat up to 40°C and continue the reaction for 4 hours, then add 1-6 mL of triethylamine and 1-6 mL of acetic anhydride for chemical imidization for a total of 12- After 36 hours, after the reaction is completed, precipitate and collect the solid in methanol, clean and dry under vacuum at 120-200 °C overnight; b)恒沸亚胺化过程:将步骤2)中所得多氨基联萘胺单体与六氟二酐按照摩尔比1:1放入装有5-15mLN-甲基吡咯烷酮三口瓶中,在10-40℃,氮气保护下搅拌5-30分钟,然后升温至50-80℃并保持0.5-2个小时,直到溶液完全澄清透明,然后加入1-5滴异喹啉和3-8mL邻二氯苯,然后在180-240℃回流2-14个小时,反应结束后,在甲醇中沉降收集固体,在200℃度真空干燥过夜;b) azeotropic imidization process: put the polyaminobinaphthylamine monomer and hexafluorodianhydride obtained in step 2) into a three-necked flask containing 5-15mL of N-methylpyrrolidone according to a molar ratio of 1:1, and at 10 -40°C, stir for 5-30 minutes under nitrogen protection, then warm up to 50-80°C and hold for 0.5-2 hours until the solution is completely clear, then add 1-5 drops of isoquinoline and 3-8mL of o-dichloro Benzene, then refluxed at 180-240°C for 2-14 hours, after the reaction was completed, the solid was collected by sedimentation in methanol, and vacuum-dried at 200°C overnight; 4)聚酰亚胺薄膜制备:将步骤3)中a)或b)合成的联萘聚酰亚胺树脂溶解于氯仿中配制成2-10wt%铸膜液,铸膜液使用聚四氟乙烯滤膜过滤,将滤液置于培养皿中均匀铺平皿底,平铺有铸膜液的培养皿被封在自封袋中缓慢挥发溶剂直至成膜,最后在180-240℃真空烘箱中10-48小时脱除全部溶剂;4) Preparation of polyimide film: the binaphthalene polyimide resin synthesized in step 3) in a) or b) is dissolved in chloroform to prepare a 2-10 wt% casting solution, and the casting solution uses polytetrafluoroethylene Filter the membrane, place the filtrate in a petri dish and evenly spread the bottom of the dish. The petri dish with the casting solution is sealed in a self-sealing bag and slowly evaporate the solvent until the film is formed. Finally, put it in a vacuum oven at 180-240 °C for 10-48 Remove all the solvent in hours; 5)制备的联萘聚酰亚胺气体分离膜在氮气保护下于碳化炉内进一步进行热处理,升温速率为2-10℃/min在300-800℃维持0.5-4小时,热处理结束后自然降温到室温;5) The prepared binaphthalene polyimide gas separation membrane is further heat-treated in a carbonization furnace under nitrogen protection, the heating rate is 2-10°C/min, and the temperature is maintained at 300-800°C for 0.5-4 hours, and the temperature is naturally lowered after the heat treatment. to room temperature; 所得聚酰亚胺树脂具有如下结构通式:The obtained polyimide resin has the following general structural formula:
Figure FDA0003057360960000021
Figure FDA0003057360960000021
R:-OH,-CH3,-COOH,-OCH3,-OCOCH3,-COOCH3 R:-OH,-CH 3 ,-COOH,-OCH 3 ,-OCOCH3,-COOCH 3 Ar:
Figure FDA0003057360960000022
Ar:
Figure FDA0003057360960000022
2.根据权利要求1所述的含有联萘结构聚酰亚胺薄膜的制备方法,其特征在于步骤1)和2)具有多氨基联萘单体分子的合成,通过硝化、还原等步骤得到具有不同侧链的多氨基修饰联萘单体。2. the preparation method that contains binaphthalene structure polyimide film according to claim 1 is characterized in that step 1) and 2) have the synthesis of polyamino binaphthyl monomer molecule, obtain by steps such as nitration, reduction with Polyamino-modified binaphthyl monomers with different side chains. 3.根据权利要求1所述的含有联萘结构聚酰亚胺薄膜的制备方法,其特征在于步骤4)中在经过0.45μm聚四氟乙烯滤膜过滤后将滤液置于培养皿被封在自封袋中缓慢挥发溶剂直至成膜,最后在180-240℃真空烘箱中12-48小时脱除全部溶剂。3. the preparation method that contains binaphthalene structure polyimide film according to claim 1 is characterized in that in step 4), after filtering through 0.45 μm polytetrafluoroethylene filter membrane, the filtrate is placed in a petri dish to be sealed in the filtrate. The solvent is slowly evaporated in the ziplock bag until the film is formed, and finally all the solvent is removed in a vacuum oven at 180-240°C for 12-48 hours. 4.一种含有联萘结构聚酰亚胺薄膜的用途,其特征在于用于CO2/N2分离,所述的含有联萘结构聚酰亚胺薄膜为权利要求1-3任一项所制备的薄膜。4. The purposes of a polyimide film containing a binaphthyl structure, characterized in that it is used for CO 2 /N separation, and the polyimide film containing a binaphthyl structure is any one of claims 1-3. prepared films. 5.根据权利要求4所述的含有联萘结构聚酰亚胺薄膜的用途,其特征在于:在0.8MPa的压力下,聚酰亚胺薄膜的N2/CO2的分离系数为20-70;N2的气体通量为10-20barrer,CO2的气体通量为500-800barrer。5. The purposes of the polyimide film containing binaphthalene structure according to claim 4, characterized in that: under the pressure of 0.8MPa, the separation coefficient of N 2 /CO 2 of the polyimide film is 20-70 ; the gas flux of N 2 is 10-20 barrer and the gas flux of CO 2 is 500-800 barrer. 6.根据权利要求5所述的含有联萘结构聚酰亚胺薄膜的用途,其特征在于:在薄膜测试15-30天后,同样压力下测试气体分离系数变化维持在±3%。6 . The use of the polyimide film containing a binaphthalene structure according to claim 5 , wherein the variation of the test gas separation coefficient is maintained at ±3% under the same pressure after the film is tested for 15-30 days. 7 .
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