CN117748050A - Preparation method of high heat-resistant polyether ketone nitrile/polyvinylidene fluoride lithium battery diaphragm - Google Patents
Preparation method of high heat-resistant polyether ketone nitrile/polyvinylidene fluoride lithium battery diaphragm Download PDFInfo
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- 229920002981 polyvinylidene fluoride Polymers 0.000 title claims abstract description 79
- 239000002033 PVDF binder Substances 0.000 title claims abstract description 76
- PQXKHYXIUOZZFA-UHFFFAOYSA-M lithium fluoride Chemical compound [Li+].[F-] PQXKHYXIUOZZFA-UHFFFAOYSA-M 0.000 title claims abstract description 29
- 229920001643 poly(ether ketone) Polymers 0.000 title claims abstract description 22
- 150000002825 nitriles Chemical class 0.000 title claims abstract description 19
- 238000002360 preparation method Methods 0.000 title claims abstract description 5
- 239000000203 mixture Substances 0.000 claims abstract description 34
- 238000005191 phase separation Methods 0.000 claims abstract description 8
- 239000002904 solvent Substances 0.000 claims abstract description 8
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 72
- 239000000843 powder Substances 0.000 claims description 42
- 239000000243 solution Substances 0.000 claims description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 33
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 30
- 238000000034 method Methods 0.000 claims description 21
- 239000008367 deionised water Substances 0.000 claims description 18
- 229910021641 deionized water Inorganic materials 0.000 claims description 18
- 238000003756 stirring Methods 0.000 claims description 18
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 16
- 239000007787 solid Substances 0.000 claims description 13
- -1 4' -biphenol Chemical compound 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 8
- 239000012046 mixed solvent Substances 0.000 claims description 8
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- 238000010992 reflux Methods 0.000 claims description 6
- YOYAIZYFCNQIRF-UHFFFAOYSA-N 2,6-dichlorobenzonitrile Chemical compound ClC1=CC=CC(Cl)=C1C#N YOYAIZYFCNQIRF-UHFFFAOYSA-N 0.000 claims description 5
- LSQARZALBDFYQZ-UHFFFAOYSA-N 4,4'-difluorobenzophenone Chemical compound C1=CC(F)=CC=C1C(=O)C1=CC=C(F)C=C1 LSQARZALBDFYQZ-UHFFFAOYSA-N 0.000 claims description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 239000005357 flat glass Substances 0.000 claims description 5
- 239000011521 glass Substances 0.000 claims description 5
- 239000011259 mixed solution Substances 0.000 claims description 5
- 238000011282 treatment Methods 0.000 claims description 5
- 239000003054 catalyst Substances 0.000 claims description 4
- 239000000376 reactant Substances 0.000 claims description 4
- 230000001112 coagulating effect Effects 0.000 claims 2
- VCCBEIPGXKNHFW-UHFFFAOYSA-N biphenyl-4,4'-diol Chemical compound C1=CC(O)=CC=C1C1=CC=C(O)C=C1 VCCBEIPGXKNHFW-UHFFFAOYSA-N 0.000 claims 1
- 238000005266 casting Methods 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 238000002791 soaking Methods 0.000 claims 1
- 230000002194 synthesizing effect Effects 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 239000003792 electrolyte Substances 0.000 abstract description 12
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 abstract description 8
- 229910001416 lithium ion Inorganic materials 0.000 abstract description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 abstract description 5
- 238000010521 absorption reaction Methods 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 4
- 229920001577 copolymer Polymers 0.000 abstract description 3
- 239000011244 liquid electrolyte Substances 0.000 abstract description 3
- 238000010534 nucleophilic substitution reaction Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 abstract description 2
- 125000004093 cyano group Chemical group *C#N 0.000 abstract description 2
- 229910052760 oxygen Inorganic materials 0.000 abstract description 2
- 239000001301 oxygen Substances 0.000 abstract description 2
- 238000006068 polycondensation reaction Methods 0.000 abstract 1
- 230000000052 comparative effect Effects 0.000 description 36
- 238000002844 melting Methods 0.000 description 13
- 230000008018 melting Effects 0.000 description 13
- 238000005345 coagulation Methods 0.000 description 8
- 230000015271 coagulation Effects 0.000 description 8
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 7
- 229910052744 lithium Inorganic materials 0.000 description 7
- 239000002131 composite material Substances 0.000 description 6
- 229920000098 polyolefin Polymers 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000012528 membrane Substances 0.000 description 5
- 239000011148 porous material Substances 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 3
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 description 3
- 239000012965 benzophenone Substances 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000006482 condensation reaction Methods 0.000 description 3
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 238000001523 electrospinning Methods 0.000 description 3
- 238000010907 mechanical stirring Methods 0.000 description 3
- 230000007935 neutral effect Effects 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000012643 polycondensation polymerization Methods 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- BQCIDUSAKPWEOX-UHFFFAOYSA-N 1,1-Difluoroethene Chemical compound FC(F)=C BQCIDUSAKPWEOX-UHFFFAOYSA-N 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 238000002536 laser-induced breakdown spectroscopy Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 229920000090 poly(aryl ether) Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
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Abstract
Description
技术领域Technical field
本发明属于锂离子电池材料技术领域,具体涉及一种高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜的制备方法。The invention belongs to the technical field of lithium-ion battery materials, and specifically relates to a method for preparing a highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator.
背景技术Background technique
随着高性能锂离子电池技术的发展,对隔膜改性设计提出了更高的要求,隔膜作为重要的安全元件,对电池的安全性能和电化学性能起着关键作用。隔膜不仅能有效隔离正负极从而避免短路,而且还能为锂离子穿过液体电解质提供畅通无阻的通道。合格的隔膜应具有适当的孔隙率、良好的电化学稳定性和热稳定性。聚烯烃隔膜由于具有较高的机械性能,优异的电化学稳定性和低廉的价格等特点,是最常见的商业隔膜材料之一,例如聚丙烯(PP)和聚乙烯(PE)。但是,聚烯烃隔膜熔点低,电解质润湿差,在高温下容易发生严重的尺寸收缩,导致内部短路并进一步诱发LIBS热失控。With the development of high-performance lithium-ion battery technology, higher requirements have been put forward for separator modification design. As an important safety component, separators play a key role in the safety performance and electrochemical performance of batteries. The separator not only effectively isolates the positive and negative electrodes to avoid short circuits, but also provides an unobstructed path for lithium ions to pass through the liquid electrolyte. Qualified separators should have appropriate porosity, good electrochemical stability and thermal stability. Polyolefin separators are one of the most common commercial separator materials due to their high mechanical properties, excellent electrochemical stability and low price, such as polypropylene (PP) and polyethylene (PE). However, polyolefin separators have low melting points and poor electrolyte wetting, and are prone to severe dimensional shrinkage at high temperatures, leading to internal short circuits and further inducing thermal runaway in LIBS.
为了弥补聚烯烃隔膜的不足,满足高性能锂离子电池的需求,国内外研究人员主要采用对聚烯烃隔膜改性的方法,比如用化学接枝法和在表面进行无机或有机涂覆改性聚烯烃隔膜。然而,采用化学接枝改性的方法会增加后续处理步骤,同时容易导致膜微孔被阻塞;在PE隔膜表面涂覆无机纳米颗粒可以提高其热稳定性,但这种方法容易导致隔膜表面出现闭孔现象,并且制备过程难以精确控制。因此,开发一种新材料代替聚烯烃隔膜是当务之急。In order to make up for the shortcomings of polyolefin separators and meet the needs of high-performance lithium-ion batteries, domestic and foreign researchers mainly use methods to modify polyolefin separators, such as chemical grafting and inorganic or organic coating on the surface to modify polyolefin separators. Olefin separator. However, the use of chemical graft modification will increase the number of subsequent processing steps and easily cause the membrane pores to be blocked; coating the surface of the PE membrane with inorganic nanoparticles can improve its thermal stability, but this method can easily lead to the formation of pores on the membrane surface. Closed pore phenomenon, and the preparation process is difficult to accurately control. Therefore, developing a new material to replace polyolefin separators is a top priority.
申请号为201810504179.2的中国专利公开了一种锂离子动力电池用复合隔膜的制造方法,通过静电纺丝工艺将聚芳醚腈与聚乙烯醇的混合物制成无纺布纤维层,再引入官能团,在基材上涂覆无机粒子层来增强隔膜的耐热性,但这容易导致隔膜中的孔闭合,而且制造过程复杂,难以控制。申请号为202310804126.3的中国专利公开了一种功能化动力电池静电纺丝补锂隔膜的制备方法,采用静电纺丝技术将补锂剂和聚偏二氟乙烯静电纺丝隔膜相结合,增加了电解液的浸润性,但是由于聚偏二氟乙烯的高结晶度和界面电阻的影响,会限制电池的安全性能。Chinese patent application number 201810504179.2 discloses a method for manufacturing a composite separator for lithium-ion power batteries. The mixture of polyaryl ether nitrile and polyvinyl alcohol is made into a non-woven fiber layer through an electrospinning process, and then functional groups are introduced. Coating a layer of inorganic particles on the substrate enhances the heat resistance of the separator, but this easily causes the pores in the separator to close, and the manufacturing process is complex and difficult to control. The Chinese patent application number 202310804126.3 discloses a method for preparing a functional power battery electrospun lithium replenishing separator. It uses electrospinning technology to combine a lithium replenishing agent and a polyvinylidene fluoride electrospinning separator to increase electrolysis. However, due to the high crystallinity and interface resistance of polyvinylidene fluoride, the safety performance of the battery will be limited.
发明内容Contents of the invention
本发明的目的在于,针对背景技术存在的问题,提出了一种高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜的制备方法。本发明通过亲核取代缩聚反应合成聚醚酮腈共聚物,与聚偏二氟乙烯共混后,采用非溶剂致相分离法制备了高耐热锂电池隔膜,并通过制备不同复配比的聚醚酮腈/聚偏二氟乙烯隔膜研究聚醚酮腈对隔膜结构和性能的影响。此外,研究了不同退火处理制备的聚醚酮腈/聚偏二氟乙烯复合隔膜的热稳定性和电解液吸收率的变化。The purpose of the present invention is to propose a method for preparing a highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator in view of the problems existing in the background technology. The present invention synthesizes polyether ketone nitrile copolymer through nucleophilic substitution condensation polymerization reaction. After blending with polyvinylidene fluoride, a non-solvent induced phase separation method is used to prepare a high heat-resistant lithium battery separator, and by preparing different compound ratios Polyetherketonenitrile/polyvinylidene fluoride separator Study the effect of polyetherketonenitrile on the structure and performance of the separator. In addition, the changes in thermal stability and electrolyte absorption rate of polyetherketonenitrile/polyvinylidene fluoride composite separators prepared by different annealing treatments were studied.
为实现上述目的,本发明采用的技术方案如下:In order to achieve the above objects, the technical solutions adopted by the present invention are as follows:
一种高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜的制备方法,包括以下步骤:A method for preparing a highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator, including the following steps:
步骤1、合成聚醚酮腈:Step 1. Synthesis of polyetherketonenitrile:
1.1在带温度计、分水器、冷凝回流装置和机械搅拌装置的三颈瓶中加入4,4’-联苯二酚、2,6-二氯苯甲腈和4,4’-二氟二苯甲酮作为反应物,加入碳酸钾作为催化剂,得到混合物粉末;在分水器中注入甲苯;其中,4,4’-二氟二苯甲酮、4,4’-联苯二酚、2,6-二氯苯甲腈和碳酸钾的摩尔比为1:3:(2.1~2.4):4.2;1.1 Add 4,4'-biphenyldiphenol, 2,6-dichlorobenzonitrile and 4,4'-difluorodiphenol to a three-necked flask equipped with a thermometer, water separator, condensation reflux device and mechanical stirring device. Benzophenone is used as a reactant, potassium carbonate is added as a catalyst to obtain a mixture powder; toluene is injected into the water separator; among them, 4,4'-difluorobenzophenone, 4,4'-biphenyldiphenol, 2 , the molar ratio of 6-dichlorobenzonitrile and potassium carbonate is 1:3: (2.1~2.4): 4.2;
1.2在步骤1.1得到的混合物粉末中加入N-甲基吡咯烷酮和甲苯的混合溶剂,搅拌混合均匀,得到混合液A;混合溶剂中,N-甲基吡咯烷酮和甲苯的体积比为3:1;其中,步骤1.1在分水器中注入的甲苯和步骤1.2在混合物粉末中加入的甲苯的摩尔比为1:(1.35~1.8);1.2 Add a mixed solvent of N-methylpyrrolidone and toluene to the mixture powder obtained in step 1.1, stir and mix evenly to obtain mixed liquid A; in the mixed solvent, the volume ratio of N-methylpyrrolidone and toluene is 3:1; where , the molar ratio of the toluene injected in the water separator in step 1.1 and the toluene added to the mixture powder in step 1.2 is 1: (1.35~1.8);
1.3步骤1.2得到的混合液A在140℃下加热回流2~5h,释放分水器中的甲苯,然后升温至150~159℃并在150~159℃下保温1~2h、升温至160~169℃并在160~169℃下保温1~2h、升温至170~179℃并在170~179℃下保温1~2h、升温至180~190℃并在180~190℃下保温1~2h,进行脱水缩合反应,待粘度不再增加时,得到的反应液倒入去离子水中,搅拌,得到条状固体;1.3 The mixed liquid A obtained in step 1.2 is heated and refluxed at 140°C for 2 to 5 hours to release the toluene in the water separator, then the temperature is raised to 150 to 159°C and kept at 150 to 159°C for 1 to 2 hours, and the temperature is raised to 160 to 169 ℃ and keep it at 160~169°C for 1~2h, raise the temperature to 170~179°C and keep it at 170~179°C for 1~2h, raise the temperature to 180~190°C and keep it at 180~190°C for 1~2h, proceed Dehydration and condensation reaction. When the viscosity no longer increases, pour the resulting reaction solution into deionized water and stir to obtain a strip solid;
1.4步骤1.3得到的条状固体在10wt%的盐酸溶液中浸泡24h后,粉碎,再采用去离子水洗涤3~5次至溶液呈中性;洗涤后的粉末置于烘箱中100℃干燥24~48h,得到聚醚酮腈粉末;1.4 The strip solid obtained in step 1.3 is soaked in 10wt% hydrochloric acid solution for 24 hours, then crushed, and then washed with deionized water 3 to 5 times until the solution becomes neutral; the washed powder is dried in an oven at 100°C for 24 to After 48h, polyetherketonenitrile powder was obtained;
步骤2、配制聚醚酮腈/聚偏二氟乙烯共混热溶液:Step 2. Prepare polyetherketonenitrile/polyvinylidene fluoride hot blend solution:
2.1在三颈瓶中加入N-甲基吡咯烷酮和步骤1得到的聚醚酮腈粉末,在140~150℃下加热搅拌2~5h,得到均匀的溶液B;2.1 Add N-methylpyrrolidone and the polyetherketonenitrile powder obtained in step 1 into a three-necked bottle, heat and stir at 140-150°C for 2-5 hours to obtain a uniform solution B;
2.2在步骤2.1得到的溶液B中加入聚偏二氟乙烯和N-甲基吡咯烷酮,继续在140~150℃下加热搅拌2h,得到聚醚酮腈/聚偏二氟乙烯共混热溶液;其中,聚醚酮腈与聚偏二氟乙烯的质量比为1:(0.25~4),聚醚酮腈粉末与聚偏二氟乙烯的混合固体粉末和N-甲基吡咯烷酮的固液比为1g:(15~35)mL;2.2 Add polyvinylidene fluoride and N-methylpyrrolidone to solution B obtained in step 2.1, and continue heating and stirring at 140 to 150°C for 2 hours to obtain a polyetherketonenitrile/polyvinylidene fluoride hot blend solution; where , the mass ratio of polyetherketonenitrile and polyvinylidene fluoride is 1: (0.25~4), the solid-liquid ratio of the mixed solid powder of polyetherketonenitrile powder and polyvinylidene fluoride and N-methylpyrrolidone is 1g (15~35)mL;
步骤3、采用非溶剂致相分离法制备高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜:Step 3. Use a non-solvent-induced phase separation method to prepare a highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator:
3.1将步骤2得到的聚醚酮腈/聚偏二氟乙烯共混热溶液倒在干净、平整的玻璃板上,用四面涂膜器浇铸出湿膜;3.1 Pour the polyetherketonenitrile/polyvinylidene fluoride hot blend solution obtained in step 2 onto a clean, flat glass plate, and use a four-sided film applicator to cast a wet film;
3.2将步骤3.1得到的带湿膜的玻璃板直接浸入凝固浴中10~20min,脱离形成具有多孔结构的隔膜,然后将隔膜浸泡于去离子水中;其中,凝固浴为体积比1:1的无水乙醇和去离子水的混合液;3.2 Directly immerse the glass plate with the wet film obtained in step 3.1 into the coagulation bath for 10 to 20 minutes to separate and form a separator with a porous structure, and then soak the separator in deionized water; where, the coagulation bath is a non-porous membrane with a volume ratio of 1:1. A mixture of hydroethanol and deionized water;
3.3将步骤3.2处理后得到的隔膜在室温下晾干,即可得到所述高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜。3.3 Dry the separator obtained after the treatment in step 3.2 at room temperature to obtain the high heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator.
与现有技术相比,本发明的有益效果为:Compared with the prior art, the beneficial effects of the present invention are:
本发明提供的一种高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜的制备方法,通过亲核取代缩聚反应合成聚醚酮腈共聚物,与聚偏二氟乙烯共混后,采用非溶剂致相分离获得高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜。该电池隔膜中,聚醚酮腈可以降低共混膜的结晶度,且聚醚酮主链上的极性羧基和氧醚键增强了其与液体电解质的亲和力,聚醚酮腈中氰基的引入有助于提高电解质的吸收率,拓宽电化学窗口,使得该隔膜具有高离子电导率、良好的电解质润湿性和较强的耐热性。The invention provides a method for preparing a highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator. The polyetherketonenitrile copolymer is synthesized through a nucleophilic substitution condensation polymerization reaction. After blending with polyvinylidene fluoride, A highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator was obtained using non-solvent-induced phase separation. In this battery separator, polyetherketonenitrile can reduce the crystallinity of the blend film, and the polar carboxyl groups and oxygen ether bonds on the polyetherketone main chain enhance its affinity with the liquid electrolyte. The cyano group in polyetherketonenitrile The introduction helps to increase the absorption rate of the electrolyte and broaden the electrochemical window, making the separator have high ionic conductivity, good electrolyte wettability and strong heat resistance.
附图说明Description of drawings
图1为步骤1聚醚酮腈的合成路线;Figure 1 is the synthesis route of polyetherketonenitrile in step 1;
图2为实施例3制备的聚醚酮腈/聚偏二氟乙烯锂电池隔膜和对比例8的电解液润湿性;Figure 2 shows the electrolyte wettability of the polyetherketonenitrile/polyvinylidene fluoride lithium battery separator prepared in Example 3 and Comparative Example 8;
图3为实施例1~3、对比例4~6制备的聚醚酮腈/聚偏二氟乙烯锂电池隔膜和对比例7、对比例8的耐热稳定性;Figure 3 shows the heat resistance stability of polyetherketonenitrile/polyvinylidene fluoride lithium battery separators prepared in Examples 1 to 3 and Comparative Examples 4 to 6 and Comparative Examples 7 and 8;
图4为实施例3制备的聚醚酮腈/聚偏二氟乙烯锂电池隔膜和对比例8的电池循环性能。Figure 4 shows the battery cycle performance of the polyetherketonenitrile/polyvinylidene fluoride lithium battery separator prepared in Example 3 and Comparative Example 8.
具体实施方式Detailed ways
下面结合附图和实施例,详述本发明的技术方案。The technical solution of the present invention will be described in detail below with reference to the accompanying drawings and examples.
实施例1Example 1
一种高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜的制备方法,包括以下步骤:A method for preparing a highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator, including the following steps:
步骤1、合成聚醚酮腈:Step 1. Synthesis of polyetherketonenitrile:
1.1在带温度计、分水器、冷凝回流装置和机械搅拌装置的三颈瓶中加入4,4’-联苯二酚、2,6-二氯苯甲腈和4,4’-二氟二苯甲酮作为反应物,加入碳酸钾作为催化剂,得到混合物粉末;在分水器中注入甲苯;其中,4,4’-二氟二苯甲酮、4,4’-联苯二酚、2,6-二氯苯甲腈和碳酸钾的摩尔比为1:3:2.2:4.2;1.1 Add 4,4'-biphenyldiphenol, 2,6-dichlorobenzonitrile and 4,4'-difluorodiphenol into a three-necked flask equipped with a thermometer, water separator, condensation reflux device and mechanical stirring device. Benzophenone is used as a reactant, potassium carbonate is added as a catalyst to obtain a mixture powder; toluene is injected into the water separator; among them, 4,4'-difluorobenzophenone, 4,4'-biphenyldiphenol, 2 , the molar ratio of 6-dichlorobenzonitrile and potassium carbonate is 1:3:2.2:4.2;
1.2在步骤1.1得到的混合物粉末中加入N-甲基吡咯烷酮和甲苯的混合溶剂,搅拌混合均匀,得到混合液A;混合溶剂中,N-甲基吡咯烷酮和甲苯的体积比为3:1;其中,步骤1.1在分水器中注入的甲苯和步骤1.2在混合物粉末中加入的甲苯的摩尔比为1:1.8;1.2 Add a mixed solvent of N-methylpyrrolidone and toluene to the mixture powder obtained in step 1.1, stir and mix evenly to obtain mixed liquid A; in the mixed solvent, the volume ratio of N-methylpyrrolidone and toluene is 3:1; where , the molar ratio of the toluene injected in the water separator in step 1.1 and the toluene added to the mixture powder in step 1.2 is 1:1.8;
1.3步骤1.2得到的混合液A在140℃下加热回流3h,每8~10min释放3~5mL分水器中的甲苯,然后以2~5℃/min的升温速率升温至155℃并在155℃下保温2h、升温至165℃并在165℃下保温2h、升温至175℃并在175℃下保温2h、升温至185℃并在185℃下保温2h,进行脱水缩合反应,待粘度不再增加时,得到的反应液倒入去离子水中,搅拌,得到条状固体;1.3 Mixed solution A obtained in step 1.2 is heated to reflux at 140°C for 3 hours, releasing 3 to 5 mL of toluene in the water separator every 8 to 10 minutes, and then heated to 155°C at a heating rate of 2 to 5°C/min and heated at 155°C. Keep the temperature at 165°C for 2 hours, raise the temperature to 165°C and keep it at 165°C for 2 hours, raise the temperature to 175°C and keep it at 175°C for 2 hours, raise the temperature to 185°C and keep it at 185°C for 2 hours, and carry out dehydration and condensation reaction until the viscosity no longer increases. When, the reaction solution obtained is poured into deionized water and stirred to obtain a strip solid;
1.4步骤1.3得到的条状固体在10wt%的盐酸溶液中浸泡24h后,粉碎,再采用去离子水洗涤3~5次至溶液呈中性;洗涤后的粉末置于烘箱中100℃干燥36h,得到聚醚酮腈粉末;1.4 The strip solid obtained in step 1.3 is soaked in 10wt% hydrochloric acid solution for 24 hours, then crushed, and then washed with deionized water 3 to 5 times until the solution becomes neutral; the washed powder is dried in an oven at 100°C for 36 hours. Polyetherketonenitrile powder is obtained;
步骤2、配制聚醚酮腈/聚偏二氟乙烯共混热溶液:Step 2. Prepare polyetherketonenitrile/polyvinylidene fluoride hot blend solution:
2.1在三颈瓶中加入N-甲基吡咯烷酮和步骤1得到的聚醚酮腈粉末,在150℃下加热搅拌5h,得到均匀的溶液B;其中,1g聚醚酮腈粉末中加入10mL的N-甲基吡咯烷酮;2.1 Add N-methylpyrrolidone and the polyetherketonenitrile powder obtained in step 1 into a three-necked flask, heat and stir at 150°C for 5 hours to obtain a uniform solution B; add 10 mL of N to 1g of polyetherketonenitrile powder. - Methylpyrrolidone;
2.2在步骤2.1得到的溶液B中加入聚偏二氟乙烯和N-甲基吡咯烷酮,继续在150℃下加热搅拌2h,得到聚醚酮腈/聚偏二氟乙烯共混热溶液;其中,聚醚酮腈与聚偏二氟乙烯的质量比为1:(0.25~4),1g聚醚酮腈粉末与聚偏二氟乙烯的混合固体粉末中加入16.25mL的N-甲基吡咯烷酮;2.2 Add polyvinylidene fluoride and N-methylpyrrolidone to the solution B obtained in step 2.1, and continue to heat and stir at 150°C for 2 hours to obtain a polyetherketonenitrile/polyvinylidene fluoride blend hot solution; where, poly(vinylidene fluoride) and N-methylpyrrolidone are added. The mass ratio of ether ketone nitrile and polyvinylidene fluoride is 1: (0.25~4), and 16.25 mL of N-methylpyrrolidone is added to 1g of the mixed solid powder of polyether ketone nitrile powder and polyvinylidene fluoride;
步骤3、采用非溶剂致相分离法制备高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜:Step 3. Use a non-solvent-induced phase separation method to prepare a highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator:
3.1将步骤2得到的聚醚酮腈/聚偏二氟乙烯共混热溶液倒在干净、平整的玻璃板上,用四面涂膜器浇铸出湿膜;3.1 Pour the polyetherketonenitrile/polyvinylidene fluoride hot blend solution obtained in step 2 onto a clean, flat glass plate, and use a four-sided film applicator to cast a wet film;
3.2将步骤3.1得到的带湿膜的玻璃板直接浸入凝固浴中15min,脱离形成具有多孔结构的隔膜,然后将隔膜浸泡于去离子水中;其中,凝固浴为体积比1:1的无水乙醇和去离子水的混合液;3.2 Directly immerse the glass plate with wet film obtained in step 3.1 into the coagulation bath for 15 minutes to separate and form a separator with a porous structure, and then soak the separator in deionized water; where the coagulation bath is absolute ethanol with a volume ratio of 1:1 and deionized water mixture;
3.3将步骤3.2处理后得到的隔膜在室温下晾干,即可得到所述高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜。3.3 Dry the separator obtained after the treatment in step 3.2 at room temperature to obtain the high heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator.
实施例2Example 2
本实施例与实施例1相比,区别在于:Compared with Embodiment 1, the differences between this embodiment and Embodiment 1 are:
步骤2配制聚醚酮腈/聚偏二氟乙烯共混热溶液的过程调整为:The process of preparing the polyetherketonenitrile/polyvinylidene fluoride hot blend solution in step 2 is adjusted as follows:
2.1在三颈瓶中加入N-甲基吡咯烷酮和步骤1得到的聚醚酮腈粉末,在150℃下加热搅拌5h,得到均匀的溶液B;其中,1g聚醚酮腈粉末中加入10mL的N-甲基吡咯烷酮;2.1 Add N-methylpyrrolidone and the polyetherketonenitrile powder obtained in step 1 into a three-necked flask, heat and stir at 150°C for 5 hours to obtain a uniform solution B; add 10 mL of N to 1g of polyetherketonenitrile powder. - Methylpyrrolidone;
2.2在步骤2.1得到的溶液B中加入聚偏二氟乙烯和N-甲基吡咯烷酮,继续在150℃下加热搅拌2h,得到聚醚酮腈/聚偏二氟乙烯共混热溶液;其中,聚醚酮腈与聚偏二氟乙烯的质量比为1:(0.25~4),1g聚醚酮腈粉末与聚偏二氟乙烯的混合固体粉末中加入20mL的N-甲基吡咯烷酮;其余过程与实施例1完全相同。2.2 Add polyvinylidene fluoride and N-methylpyrrolidone to the solution B obtained in step 2.1, and continue to heat and stir at 150°C for 2 hours to obtain a polyetherketonenitrile/polyvinylidene fluoride blend hot solution; where, poly(vinylidene fluoride) and N-methylpyrrolidone are added. The mass ratio of ether ketone nitrile and polyvinylidene fluoride is 1: (0.25~4). 20 mL of N-methylpyrrolidone is added to 1g of the mixed solid powder of polyether ketone nitrile powder and polyvinylidene fluoride; the rest of the process is as follows Example 1 is exactly the same.
实施例3Example 3
本实施例与实施例1相比,区别在于:Compared with Embodiment 1, the differences between this embodiment and Embodiment 1 are:
步骤2配制聚醚酮腈/聚偏二氟乙烯共混热溶液的过程调整为:The process of preparing the polyetherketonenitrile/polyvinylidene fluoride hot blend solution in step 2 is adjusted as follows:
2.1在三颈瓶中加入N-甲基吡咯烷酮和步骤1得到的聚醚酮腈粉末,在150℃下加热搅拌5h,得到均匀的溶液B;其中,1g聚醚酮腈粉末中加入10mL的N-甲基吡咯烷酮;2.1 Add N-methylpyrrolidone and the polyetherketonenitrile powder obtained in step 1 into a three-necked flask, heat and stir at 150°C for 5 hours to obtain a uniform solution B; among which, add 10mL of N to 1g of polyetherketonenitrile powder. -Methylpyrrolidone;
2.2在步骤2.1得到的溶液B中加入聚偏二氟乙烯和N-甲基吡咯烷酮,继续在150℃下加热搅拌2h,得到聚醚酮腈/聚偏二氟乙烯共混热溶液;其中,聚醚酮腈与聚偏二氟乙烯的质量比为1:(0.25~4),1g聚醚酮腈粉末与聚偏二氟乙烯的混合固体粉末中加入35mL的N-甲基吡咯烷酮;其余过程与实施例1完全相同。2.2 Add polyvinylidene fluoride and N-methylpyrrolidone to the solution B obtained in step 2.1, and continue to heat and stir at 150°C for 2 hours to obtain a polyetherketonenitrile/polyvinylidene fluoride blend hot solution; where, poly(vinylidene fluoride) and N-methylpyrrolidone are added. The mass ratio of ether ketone nitrile and polyvinylidene fluoride is 1: (0.25~4). 35 mL of N-methylpyrrolidone is added to 1g of the mixed solid powder of polyether ketone nitrile powder and polyvinylidene fluoride; the rest of the process is as follows Example 1 is exactly the same.
对比例1Comparative example 1
步骤1、将聚偏二氟乙烯和N-甲基吡咯烷酮混合,在150℃下加热搅拌2h,得到聚偏二氟乙烯热溶液;其中,1g聚偏二氟乙烯粉末中加入10mL的N-甲基吡咯烷酮;Step 1. Mix polyvinylidene fluoride and N-methylpyrrolidone, heat and stir at 150°C for 2 hours to obtain a hot polyvinylidene fluoride solution; add 10 mL of N-methylpyrrolidone to 1g of polyvinylidene fluoride powder. pyrrolidone;
步骤2、采用非溶剂致相分离法制备聚偏二氟乙烯锂电池隔膜:Step 2. Use non-solvent induced phase separation method to prepare polyvinylidene fluoride lithium battery separator:
2.1将步骤1得到的聚偏二氟乙烯热溶液倒在干净、平整的玻璃板上,用四面涂膜器浇铸出湿膜;2.1 Pour the polyvinylidene fluoride hot solution obtained in step 1 onto a clean, flat glass plate, and use a four-sided film applicator to cast a wet film;
2.2将步骤2.1得到的带湿膜的玻璃板直接浸入凝固浴中15min,脱离形成隔膜,然后将隔膜浸泡于去离子水中;其中,凝固浴为体积比1:1的无水乙醇和去离子水的混合液;2.2 Directly immerse the glass plate with wet film obtained in step 2.1 into the coagulation bath for 15 minutes to separate and form a separator, and then soak the separator in deionized water; where the coagulation bath is absolute ethanol and deionized water with a volume ratio of 1:1 mixture;
2.3将步骤2.2处理后得到的隔膜在室温下晾干,即可得到聚偏二氟乙烯锂电池隔膜。2.3 Dry the separator obtained after step 2.2 at room temperature to obtain a polyvinylidene fluoride lithium battery separator.
对比例2Comparative example 2
本对比例与实施例1的区别在于:步骤3.3中,将步骤3.2处理后得到的隔膜在室温下晾干,然后在120℃下热处理5h;其余步骤与实施例1相同。The difference between this comparative example and Example 1 is that in step 3.3, the separator obtained after step 3.2 is dried at room temperature and then heat-treated at 120°C for 5 hours; the remaining steps are the same as in Example 1.
对比例3Comparative example 3
本对比例与实施例2的区别在于:步骤3.3中,将步骤3.2处理后得到的隔膜在室温下晾干,然后在120℃下热处理5h;其余步骤与实施例2相同。The difference between this comparative example and Example 2 is that in step 3.3, the separator obtained after step 3.2 is dried at room temperature and then heat-treated at 120°C for 5 hours; the remaining steps are the same as in Example 2.
对比例4Comparative example 4
本对比例与实施例3的区别在于:步骤3.3中,将步骤3.2处理后得到的隔膜在室温下晾干,然后在120℃下热处理5h;其余步骤与实施例3相同。The difference between this comparative example and Example 3 is that in step 3.3, the separator obtained after step 3.2 is dried at room temperature and then heat-treated at 120°C for 5 hours; the remaining steps are the same as in Example 3.
对比例5Comparative example 5
本对比例与实施例3的区别在于:步骤3.3中,将步骤3.2处理后得到的隔膜在室温下晾干,然后在200℃下热处理2h;其余步骤与实施例3相同。The difference between this comparative example and Example 3 is that in step 3.3, the separator obtained after step 3.2 is dried at room temperature and then heat-treated at 200°C for 2 hours; the remaining steps are the same as in Example 3.
对比例6Comparative example 6
本对比例与对比例1的区别在于:步骤2.3中,将步骤2.2处理后得到的隔膜在室温下晾干,然后在120℃下热处理5h;其余步骤与对比例1完全相同。The difference between this comparative example and Comparative Example 1 is that in step 2.3, the separator obtained after step 2.2 is dried at room temperature and then heat-treated at 120°C for 5 hours; the remaining steps are exactly the same as in Comparative Example 1.
对比例7Comparative example 7
一种聚醚酮腈锂电池隔膜,其制备方法包括:A polyetherketone nitrile lithium battery separator, the preparation method of which includes:
步骤1、合成聚醚酮腈:Step 1. Synthesis of polyetherketonenitrile:
1.1在带温度计、分水器、冷凝回流装置和机械搅拌装置的三颈瓶中加入4,4’-联苯二酚、2,6-二氯苯甲腈和4,4’-二氟二苯甲酮作为反应物,加入碳酸钾作为催化剂,得到混合物粉末;在分水器中注入甲苯;其中,4,4’-二氟二苯甲酮、4,4’-联苯二酚、2,6-二氯苯甲腈和碳酸钾的摩尔比为1:3:2.2:4.2;1.1 Add 4,4'-biphenyldiphenol, 2,6-dichlorobenzonitrile and 4,4'-difluorodiphenol to a three-necked flask equipped with a thermometer, water separator, condensation reflux device and mechanical stirring device. Benzophenone is used as a reactant, potassium carbonate is added as a catalyst to obtain a mixture powder; toluene is injected into the water separator; among them, 4,4'-difluorobenzophenone, 4,4'-biphenyldiphenol, 2 , the molar ratio of 6-dichlorobenzonitrile and potassium carbonate is 1:3:2.2:4.2;
1.2在步骤1.1得到的混合物粉末中加入N-甲基吡咯烷酮和甲苯的混合溶剂,搅拌混合均匀,得到混合液A;混合溶剂中,N-甲基吡咯烷酮和甲苯的体积比为3:1;其中,步骤1.1在分水器中注入的甲苯和步骤1.2在混合物粉末中加入的甲苯的摩尔比为1:1.8;1.2 Add a mixed solvent of N-methylpyrrolidone and toluene to the mixture powder obtained in step 1.1, stir and mix evenly to obtain mixed liquid A; in the mixed solvent, the volume ratio of N-methylpyrrolidone and toluene is 3:1; where , the molar ratio of the toluene injected in the water separator in step 1.1 and the toluene added to the mixture powder in step 1.2 is 1:1.8;
1.3步骤1.2得到的混合液A在140℃下加热回流3h,每8~10min释放3~5mL分水器中的甲苯,然后以2~5℃/min的升温速率升温至155℃并在155℃下保温2h、升温至165℃并在165℃下保温2h、升温至175℃并在175℃下保温2h、升温至185℃并在185℃下保温2h,进行脱水缩合反应,待粘度不再增加时,得到的反应液倒入去离子水中,搅拌,得到条状固体;1.3 Mixed solution A obtained in step 1.2 is heated to reflux at 140°C for 3 hours, releasing 3 to 5 mL of toluene in the water separator every 8 to 10 minutes, and then heated to 155°C at a heating rate of 2 to 5°C/min and heated at 155°C. Keep the temperature at 165°C for 2 hours, raise the temperature to 165°C and keep it at 165°C for 2 hours, raise the temperature to 175°C and keep it at 175°C for 2 hours, raise the temperature to 185°C and keep it at 185°C for 2 hours, and carry out dehydration and condensation reaction until the viscosity no longer increases. When, the reaction solution obtained is poured into deionized water and stirred to obtain a strip solid;
1.4步骤1.3得到的条状固体在10wt%的盐酸溶液中浸泡24h后,粉碎,再采用去离子水洗涤3~5次至溶液呈中性;洗涤后的粉末置于烘箱中100℃干燥36h,得到聚醚酮腈粉末;1.4 The strip solid obtained in step 1.3 is soaked in 10wt% hydrochloric acid solution for 24 hours, then crushed, and then washed with deionized water 3 to 5 times until the solution becomes neutral; the washed powder is dried in an oven at 100°C for 36 hours. Polyetherketonenitrile powder is obtained;
步骤2、配制聚醚酮腈热溶液:Step 2. Prepare polyetherketonenitrile hot solution:
在三颈瓶中加入N-甲基吡咯烷酮和步骤1得到的聚醚酮腈粉末,在150℃下加热搅拌5h,得到聚醚酮腈热溶液;其中,1g聚醚酮腈粉末中加入10mL的N-甲基吡咯烷酮;Add N-methylpyrrolidone and the polyetherketonenitrile powder obtained in step 1 into a three-necked flask, heat and stir at 150°C for 5 hours to obtain a polyetherketonenitrile hot solution; where, 10 mL of polyetherketonenitrile powder is added to 1g of polyetherketonenitrile powder. N-methylpyrrolidone;
步骤3、采用非溶剂致相分离法制备聚醚酮腈锂电池隔膜:Step 3. Use non-solvent induced phase separation method to prepare polyetherketone nitrile lithium battery separator:
3.1将步骤2得到的聚醚酮腈热溶液倒在干净、平整的玻璃板上,用四面涂膜器浇铸出湿膜;3.1 Pour the hot polyetherketonenitrile solution obtained in step 2 onto a clean, flat glass plate, and use a four-sided film applicator to cast a wet film;
3.2将步骤3.1得到的带湿膜的玻璃板直接浸入凝固浴中15min,脱离形成隔膜,然后将隔膜浸泡于去离子水中;其中,凝固浴为体积比1:1的无水乙醇和去离子水的混合液;3.2 Directly immerse the glass plate with wet film obtained in step 3.1 into the coagulation bath for 15 minutes to separate and form a separator, and then soak the separator in deionized water; where the coagulation bath is absolute ethanol and deionized water with a volume ratio of 1:1 mixture;
3.3将步骤3.2处理后得到的隔膜在室温下晾干,即可得到所述聚醚酮腈锂电池隔膜。3.3 Dry the separator obtained after the treatment in step 3.2 at room temperature to obtain the polyetherketone nitrile lithium battery separator.
对比例8Comparative example 8
市售的商用Celgard 2400隔膜。Commercially available Celgard 2400 separator.
以上实施例和对比例制备得到的锂电池隔膜,检测其各项性能,结果如表1和表2所示。Various properties of the lithium battery separators prepared in the above examples and comparative examples were tested, and the results are shown in Table 1 and Table 2.
表1电池隔膜熔点及熔融焓Table 1 Melting point and melting enthalpy of battery separator
表2电池隔膜性能Table 2 Battery separator performance
从表1可以看出,随着聚偏二氟乙烯比例的增加,熔融焓增加,这表明聚偏二氟乙烯可以促进复合隔膜结晶。并且复合薄膜的结晶度比聚偏二氟乙烯的小,这是由于聚偏二氟乙烯的非晶区增加,而较低的结晶度可以提高导电率。部分复合隔膜经120℃处理后,聚偏二氟乙烯的熔点几乎没有受到影响,但结晶度有所降低。为了确认复合隔膜的结晶度,将实施例3在200℃的高温烘箱中处理2h后,观察到实施例3中聚偏二氟乙烯的熔点变为两个点分别为166.9℃和179℃,聚偏二氟乙烯组分的熔点提高了10%,这是由于聚偏二氟乙烯中α相含量的上升所致。表2可以看出,与对比例7相比,本发明实施例制备的高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜具有良好的耐热性,还具有55.54%~89.86%的高孔隙率、210%~435%的高效电解液吸液率和0.301~0.600*10-3S/cm的离子电导率。As can be seen from Table 1, as the proportion of polyvinylidene fluoride increases, the melting enthalpy increases, which indicates that polyvinylidene fluoride can promote the crystallization of the composite separator. Moreover, the crystallinity of the composite film is smaller than that of polyvinylidene fluoride, which is due to the increase in the amorphous area of polyvinylidene fluoride, and lower crystallinity can improve conductivity. After some composite separators are treated at 120°C, the melting point of polyvinylidene fluoride is almost not affected, but the crystallinity is reduced. In order to confirm the crystallinity of the composite separator, after treating Example 3 in a high-temperature oven at 200°C for 2 hours, it was observed that the melting point of polyvinylidene fluoride in Example 3 changed to two points, 166.9°C and 179°C respectively. The melting point of the vinylidene fluoride component increased by 10%, which was due to the increase in the alpha phase content in polyvinylidene fluoride. As can be seen from Table 2, compared with Comparative Example 7, the highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator prepared in the embodiment of the present invention has good heat resistance, and also has 55.54% to 89.86% High porosity, high-efficiency electrolyte absorption rate of 210% to 435% and ionic conductivity of 0.301 to 0.600*10 -3 S/cm.
图2为实施例3制备的聚醚酮腈/聚偏二氟乙烯锂电池隔膜和对比例8的电解液润湿性;由图2可知,本发明实施例制备的高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜表现出良好的电解质润湿性,电解质可以很好地铺展在薄膜上。与对比例7和对比例8相比,本发明制备的高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜具有更高的电解质润湿性。Figure 2 shows the electrolyte wettability of the polyetherketonenitrile/polyvinylidene fluoride lithium battery separator prepared in Example 3 and Comparative Example 8; it can be seen from Figure 2 that the high heat-resistant polyetherketonenitrile prepared in Examples of the present invention /Polyvinylidene fluoride lithium battery separator shows good electrolyte wettability, and the electrolyte can be spread well on the film. Compared with Comparative Examples 7 and 8, the highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator prepared by the present invention has higher electrolyte wettability.
图3为实施例1~3、对比例4~6制备的聚醚酮腈/聚偏二氟乙烯锂电池隔膜和对比例7、对比例8的耐热稳定性;由图3可知,与对比例7和对比例8相比,本发明制备的高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜具有良好的阻燃性和耐热性,能满足锂离子安全标准。Figure 3 shows the heat resistance stability of the polyetherketonenitrile/polyvinylidene fluoride lithium battery separators prepared in Examples 1 to 3 and Comparative Examples 4 to 6 and Comparative Examples 7 and 8; as can be seen from Figure 3, the Compared with Example 7 and Comparative Example 8, the highly heat-resistant polyetherketonenitrile/polyvinylidene fluoride lithium battery separator prepared by the present invention has good flame retardancy and heat resistance and can meet lithium ion safety standards.
图4为实施例3制备的聚醚酮腈/聚偏二氟乙烯锂电池隔膜和对比例8的电池循环性能;由图4可知,与对比例8相比,本发明实施例制备的高耐热聚醚酮腈/聚偏二氟乙烯锂电池隔膜组装的电池比容量相对较高,达到约160mAh g-1,在0.5C电流密度下的初始放电比容量169.1mAh g-1。循环45次后,电池的容量保持率为86.64%,电池放电比容量为146.5mAhg-1。本发明耐高温聚醚酮腈/聚偏二氟乙烯薄膜作为锂离子电池隔膜,电池性能显著优于Celgard 2400隔膜。Figure 4 shows the battery cycle performance of the polyetherketonenitrile/polyvinylidene fluoride lithium battery separator prepared in Example 3 and Comparative Example 8; it can be seen from Figure 4 that compared with Comparative Example 8, the high-resistant membrane prepared in the Example of the present invention has The specific capacity of the battery assembled with the thermal polyetherketonenitrile/polyvinylidene fluoride lithium battery separator is relatively high, reaching about 160mAh g -1 , and the initial discharge specific capacity is 169.1mAh g -1 at a current density of 0.5C. After 45 cycles, the battery's capacity retention rate was 86.64%, and the battery's specific discharge capacity was 146.5mAhg -1 . The high-temperature-resistant polyetherketonenitrile/polyvinylidene fluoride film of the present invention is used as a lithium-ion battery separator, and the battery performance is significantly better than the Celgard 2400 separator.
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