CN117069999A - A method for catalytically degrading carbon fiber reinforced resin matrix composite materials - Google Patents
A method for catalytically degrading carbon fiber reinforced resin matrix composite materials Download PDFInfo
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- 229920000049 Carbon (fiber) Polymers 0.000 title claims abstract description 101
- 239000004917 carbon fiber Substances 0.000 title claims abstract description 101
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 90
- 229920005989 resin Polymers 0.000 title claims abstract description 60
- 239000011347 resin Substances 0.000 title claims abstract description 60
- 238000000034 method Methods 0.000 title claims abstract description 53
- 239000011159 matrix material Substances 0.000 title claims abstract description 42
- 239000002131 composite material Substances 0.000 title claims abstract description 40
- 230000000593 degrading effect Effects 0.000 title claims abstract description 6
- 239000000835 fiber Substances 0.000 claims abstract description 49
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000000463 material Substances 0.000 claims abstract description 31
- 239000003054 catalyst Substances 0.000 claims abstract description 26
- 239000000805 composite resin Substances 0.000 claims abstract description 20
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims abstract description 10
- 235000003891 ferrous sulphate Nutrition 0.000 claims abstract description 6
- 239000011790 ferrous sulphate Substances 0.000 claims abstract description 6
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims abstract description 6
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims abstract description 6
- ONIKNECPXCLUHT-UHFFFAOYSA-N 2-chlorobenzoyl chloride Chemical compound ClC(=O)C1=CC=CC=C1Cl ONIKNECPXCLUHT-UHFFFAOYSA-N 0.000 claims abstract description 5
- WETWJCDKMRHUPV-UHFFFAOYSA-N acetyl chloride Chemical compound CC(Cl)=O WETWJCDKMRHUPV-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000012346 acetyl chloride Substances 0.000 claims abstract description 5
- 229910052943 magnesium sulfate Inorganic materials 0.000 claims abstract description 5
- 235000019341 magnesium sulphate Nutrition 0.000 claims abstract description 5
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 claims abstract description 5
- 229960001763 zinc sulfate Drugs 0.000 claims abstract description 5
- 229910000368 zinc sulfate Inorganic materials 0.000 claims abstract description 5
- 230000015556 catabolic process Effects 0.000 claims description 16
- 238000006731 degradation reaction Methods 0.000 claims description 16
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 15
- 230000003197 catalytic effect Effects 0.000 claims description 9
- 239000002904 solvent Substances 0.000 claims description 8
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 7
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 6
- 238000004321 preservation Methods 0.000 claims description 5
- LXEJRKJRKIFVNY-UHFFFAOYSA-N terephthaloyl chloride Chemical compound ClC(=O)C1=CC=C(C(Cl)=O)C=C1 LXEJRKJRKIFVNY-UHFFFAOYSA-N 0.000 claims description 5
- 229920002302 Nylon 6,6 Polymers 0.000 claims description 4
- 229920005992 thermoplastic resin Polymers 0.000 claims description 4
- 229920001187 thermosetting polymer Polymers 0.000 claims description 4
- 229920002292 Nylon 6 Polymers 0.000 claims description 3
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 3
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 claims description 2
- 239000004695 Polyether sulfone Substances 0.000 claims description 2
- 239000011304 carbon pitch Substances 0.000 claims description 2
- 239000003822 epoxy resin Substances 0.000 claims description 2
- 239000005007 epoxy-phenolic resin Substances 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims description 2
- 229920001568 phenolic resin Polymers 0.000 claims description 2
- 229920000647 polyepoxide Polymers 0.000 claims description 2
- 229920006393 polyether sulfone Polymers 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 229920006305 unsaturated polyester Polymers 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 claims 2
- 238000001035 drying Methods 0.000 claims 1
- 238000004064 recycling Methods 0.000 abstract description 32
- 238000012545 processing Methods 0.000 abstract description 10
- 239000000126 substance Substances 0.000 abstract description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- GFAUNYMRSKVDJL-UHFFFAOYSA-N formyl chloride Chemical compound ClC=O GFAUNYMRSKVDJL-UHFFFAOYSA-N 0.000 abstract 1
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 abstract 1
- 238000011084 recovery Methods 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 9
- 239000002699 waste material Substances 0.000 description 8
- 239000000047 product Substances 0.000 description 7
- 230000014759 maintenance of location Effects 0.000 description 6
- 239000011259 mixed solution Substances 0.000 description 5
- 238000005303 weighing Methods 0.000 description 5
- 238000005265 energy consumption Methods 0.000 description 4
- 238000000197 pyrolysis Methods 0.000 description 3
- 238000009864 tensile test Methods 0.000 description 3
- MQJKPEGWNLWLTK-UHFFFAOYSA-N Dapsone Chemical group C1=CC(N)=CC=C1S(=O)(=O)C1=CC=C(N)C=C1 MQJKPEGWNLWLTK-UHFFFAOYSA-N 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- AUSGLDHLCBXRML-UHFFFAOYSA-N bis(oxiran-2-ylmethyl) 2-[(3-methyloxiran-2-yl)methyl]butanedioate Chemical group C(C1CO1)OC(=O)CC(CC1C(C)O1)C(=O)OCC1CO1 AUSGLDHLCBXRML-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
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- 238000012805 post-processing Methods 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000002352 steam pyrolysis Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000013475 authorization Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- ITZGNPZZAICLKA-UHFFFAOYSA-N bis(oxiran-2-ylmethyl) 7-oxabicyclo[4.1.0]heptane-3,4-dicarboxylate Chemical compound C1C2OC2CC(C(=O)OCC2OC2)C1C(=O)OCC1CO1 ITZGNPZZAICLKA-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
- C08K7/02—Fibres or whiskers
- C08K7/04—Fibres or whiskers inorganic
- C08K7/06—Elements
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Abstract
本发明涉及一种催化降解碳纤维增强树脂基复合材料的方法,其解决了传统化学回收法处理时间长、工序复杂、纤维受损严重等技术问题,其包括如下步骤:S1、将需降解的碳纤维树脂基复合材料裁剪之后,放入第一组催化剂中,常压下保温处理;所述第一组催化剂为硫酸亚铁、硫酸镁、硫酸锌中的一种或几种;S2、将所述步骤S1处理后的碳纤维树脂基复合材料取出后,清洗,干燥后,放入第二组催化剂中,常温下保温处理;所述第二组催化剂为乙酰氯、邻氯苯甲酰氯、对苯二甲酰氯的一种或几种;S3、将产物取出,用乙醇清洗,得到表面清洁的再生碳纤维。本发明可用于碳纤维增强树脂基复合材料的回收处理。
The invention relates to a method for catalytically degrading carbon fiber-reinforced resin-based composite materials, which solves the technical problems of traditional chemical recycling methods such as long processing time, complex processes, and serious fiber damage. It includes the following steps: S1. Carbon fiber to be degraded After the resin-based composite material is cut, it is put into the first group of catalysts and heat-maintained under normal pressure; the first group of catalysts is one or more of ferrous sulfate, magnesium sulfate, and zinc sulfate; S2. After the carbon fiber resin-based composite material treated in step S1 is taken out, cleaned and dried, it is placed in a second set of catalysts and kept at room temperature; the second set of catalysts are acetyl chloride, o-chlorobenzoyl chloride, and terephthalate. One or more forms of formyl chloride; S3. Take out the product and clean it with ethanol to obtain regenerated carbon fiber with a clean surface. The invention can be used for recycling of carbon fiber reinforced resin matrix composite materials.
Description
技术领域Technical field
本发明涉及一种碳纤维增强树脂基复合材料的回收方法,具体地说,涉及一种催化降解碳纤维增强树脂基复合材料的方法。The present invention relates to a method for recycling carbon fiber reinforced resin matrix composite materials, and specifically to a method for catalytically degrading carbon fiber reinforced resin matrix composite materials.
背景技术Background technique
碳纤维是一种轻质高强的纤维,利用碳纤维制备的碳纤维复合材料具有高比强度、高比模量、耐腐蚀等优点,被广泛用在体育用品、轨道交通、航空航天等领域。Carbon fiber is a lightweight and high-strength fiber. Carbon fiber composite materials prepared from carbon fiber have the advantages of high specific strength, high specific modulus, corrosion resistance, etc., and are widely used in sporting goods, rail transportation, aerospace and other fields.
随着碳纤维复合材料的用量逐年增加,将会有越来越多的复合材料达到生命使用周期,碳纤维复合材料中的碳纤维价值较高,如果通过传统的焚烧或者填埋无疑会对碳纤维资源造成巨大浪费,并且也会对环境造成污染。所以这些废料急需回收处理。然而,由于经过回收处理得到的纤维通常呈现短切状态、分散性较差,并且在经历回收处理过程后,纤维的表面会出现众多表面缺陷,因此和树脂基体的界面结合性能较差,导致回收纤维的应用范围受到限制,因此现有的回收纤维一般作为填料使用。As the amount of carbon fiber composite materials increases year by year, more and more composite materials will reach the end of their life cycle. The carbon fiber in carbon fiber composite materials has a high value. If it is burned or landfilled through traditional methods, it will undoubtedly cause huge damage to carbon fiber resources. Wasteful and polluting the environment. Therefore, these waste materials are in urgent need of recycling. However, since the fibers obtained by recycling are usually in a chopped state and have poor dispersion, and after the recycling process, many surface defects will appear on the surface of the fiber, so the interface bonding performance with the resin matrix is poor, resulting in recycling The application range of fibers is limited, so existing recycled fibers are generally used as fillers.
目前已经有多种用于回收碳纤维复合材料的方法,回收过程中将树脂基体降解、剥离其中的纤维,从而实现回收碳纤维的目的。降解方法主要包括机械回收、热解回收、化学回收等。There are currently a variety of methods for recycling carbon fiber composite materials. During the recycling process, the resin matrix is degraded and the fibers are stripped away, thereby achieving the purpose of recycling carbon fibers. Degradation methods mainly include mechanical recycling, pyrolysis recycling, chemical recycling, etc.
机械回收目前作为一种较为成熟的回收方法,其过程一般包括碾压、切碎、研磨等物理手段对复合材料进行粉碎、筛分,回收得到的纤维可以无需任何后处理过程直接使用。但是纤维在机械回收过程中由于受到挤压、切割等物理作用后力学性能会有较大损伤,并且处理后的纤维形态较差,所以经过机械回收后得到的再生纤维,其应用领域严重受限。热降解法是目前发展的最为完善的回收方法、也是唯一成功工业化的方法。热降解法包括流化床回收、热解回收、超热蒸汽回收。热解回收法主要是在氧化、热量的作用下分解树脂,尽管回收效率高,且回收纤维的种类多样,但是回收过程需要巨大的能量消耗,且部分液相副产物对环境、人体有毒害作用。Mechanical recycling is currently a relatively mature recycling method. The process generally includes crushing and screening of composite materials by physical means such as rolling, chopping, and grinding. The recovered fibers can be used directly without any post-processing. However, the mechanical properties of fibers will be greatly damaged due to physical effects such as extrusion and cutting during the mechanical recycling process, and the fiber shape after treatment is poor. Therefore, the application fields of regenerated fibers obtained after mechanical recycling are severely limited. . Thermal degradation method is the most complete recycling method currently developed and the only method that has been successfully industrialized. Thermal degradation methods include fluidized bed recovery, pyrolysis recovery, and superheated steam recovery. The pyrolysis recycling method mainly decomposes resin under the action of oxidation and heat. Although the recycling efficiency is high and the types of recycled fibers are diverse, the recycling process requires huge energy consumption, and some liquid by-products are toxic to the environment and human body. .
化学法回收不需要过高的处理温度,将废弃物浸泡在有机溶液中,在一定温度条件下树脂分子在溶剂作用下裂解为可溶解的小分子,从而剥离出碳纤维。可以选择的溶剂范围十分广泛,根据回收溶液状态的不同,可以分为溶解催化回收和超临界溶剂回收法。但是目前多数化学回收方法需要用到强酸、强碱等强氧化性试剂,对回收设备要求高,且造成环境污染,同时伴随回收时间长、回收工艺复杂等问题,部分回收方法需要高温高压,且在处理过后需要对纤维进行复杂的后处理工序才能得到表面较为清洁的再生纤维。Chemical recycling does not require excessive processing temperatures. The waste is soaked in an organic solution. Under certain temperature conditions, the resin molecules are cracked into soluble small molecules under the action of the solvent, thereby peeling off the carbon fibers. The range of solvents that can be selected is very wide. According to the different states of the recovery solution, it can be divided into dissolution catalytic recovery and supercritical solvent recovery methods. However, most current chemical recovery methods require the use of strong oxidizing reagents such as strong acids and alkalis, which require high recovery equipment and cause environmental pollution. At the same time, they are accompanied by problems such as long recovery time and complex recovery processes. Some recovery methods require high temperature and high pressure, and After treatment, the fiber needs to undergo complex post-processing procedures to obtain regenerated fiber with a cleaner surface.
授权公告号为114044936B的中国发明专利公开了一种催化水蒸汽热解回收碳纤维树脂基复合材料的方法,其解决了现有水蒸汽热解法温度高、处理时间长、碳纤维受损严重的问题,其包括如下步骤:S1、将两组催化剂按照预设比例放入反应容器;S2、将需降解的碳纤维复合材料裁剪之后放入所述S1步骤的催化剂中,通入水蒸汽,在常压下,保温;S3、将产物取出,用超声清洗,得到表面清洁的回收碳纤维。The Chinese invention patent with authorization announcement number 114044936B discloses a method for catalytic steam pyrolysis to recover carbon fiber resin matrix composite materials, which solves the problems of high temperature, long processing time and serious damage to carbon fibers in the existing steam pyrolysis method. , which includes the following steps: S1. Put the two sets of catalysts into the reaction vessel according to the preset ratio; S2. Cut the carbon fiber composite material to be degraded and put it into the catalyst of step S1, add water vapor, and heat it under normal pressure. , heat preservation; S3. Take out the product and clean it with ultrasonic to obtain recycled carbon fiber with clean surface.
上述方法主要存在以下问题:The above methods mainly have the following problems:
(1)反应温度过高,容易产生更多能耗;(1) The reaction temperature is too high, which easily produces more energy consumption;
(2)该方法得到的再生纤维由于高温环境而产生力学性能下降,导致其应用领域受到严重限制;(2) The mechanical properties of the regenerated fiber obtained by this method are reduced due to the high temperature environment, resulting in serious limitations in its application fields;
(3)该方法是针对于特殊气体环境中的催化降解,不具有通常气体环境中的普适性。(3) This method is aimed at catalytic degradation in special gas environments and does not have universal applicability in ordinary gas environments.
发明内容Contents of the invention
本发明就是为了解决现有技术反应温度高、处理时间长、工序复杂、纤维受损严重等技术问题,提供一种在较低的温度下、更快、更完全地催化降解碳纤维增强树脂基复合材料的方法。The purpose of the present invention is to solve the technical problems of the existing technology such as high reaction temperature, long processing time, complex procedures, and serious fiber damage, and provide a method for catalytically degrading carbon fiber reinforced resin matrix composites at a lower temperature faster and more completely. Materials methods.
为此,本发明提供一种催化降解碳纤维增强树脂基复合材料的方法,其包括如下步骤:S1、将需降解的碳纤维树脂基复合材料裁剪之后,放入第一组催化剂中,常压下保温处理;所述第一组催化剂为硫酸亚铁、硫酸镁、硫酸锌中的一种或几种,浓度为1~5mol/L;S2、将所述步骤S1处理后的碳纤维树脂基复合材料取出后,用乙醇清洗,干燥后,放入第二组催化剂中,常温下保温处理;所述第二组催化剂为乙酰氯、邻氯苯甲酰氯、对苯二甲酰氯的一种或几种,溶剂为乙醇、四氢呋喃、N,N-二甲基甲酰胺的一种或几种;所述第二组催化剂中溶质和溶剂的质量比为1:(1~5);S3、将产物取出,用乙醇清洗,得到表面清洁的再生碳纤维。To this end, the present invention provides a method for catalytically degrading carbon fiber-reinforced resin-based composite materials, which includes the following steps: S1. After cutting the carbon fiber-reinforced resin-based composite materials to be degraded, put them into the first group of catalysts and keep them warm under normal pressure. Processing; the first group of catalysts is one or more of ferrous sulfate, magnesium sulfate, and zinc sulfate, with a concentration of 1 to 5 mol/L; S2. Take out the carbon fiber resin-based composite material processed in step S1 Then, wash with ethanol, dry, put into the second group of catalysts, and keep it at room temperature; the second group of catalysts is one or more of acetyl chloride, o-chlorobenzoyl chloride, and terephthaloyl chloride. The solvent is one or more of ethanol, tetrahydrofuran, and N,N-dimethylformamide; the mass ratio of solute and solvent in the second group of catalysts is 1: (1-5); S3, take out the product, Clean with ethanol to obtain regenerated carbon fiber with clean surface.
优选的,所述步骤S1中,裁剪后的碳纤维树脂基复合材料的厚度为1~20mm。Preferably, in step S1, the thickness of the cut carbon fiber resin matrix composite material is 1 to 20 mm.
优选的,所述步骤S1中,碳纤维树脂基复合材料在第一组催化剂中于常压下,保温30~200min,温度为50~150℃。温度越高、或者保温时间越长,则树脂的清除率越高,但是过高的处理温度或处理时间可能对纤维造成不可逆的性能损伤。Preferably, in step S1, the carbon fiber resin matrix composite material is kept in the first group of catalysts under normal pressure for 30 to 200 minutes at a temperature of 50 to 150°C. The higher the temperature or the longer the holding time, the higher the resin removal rate. However, excessively high processing temperature or processing time may cause irreversible performance damage to the fiber.
优选的,所述步骤S1中,所述碳纤维树脂基复合材料的树脂基体为热固性树脂、热塑性树脂,热固性树脂包括环氧树脂、酚醛树脂和不饱和聚酯;热塑性树脂包括聚醚砜、尼龙6、尼龙66。Preferably, in the step S1, the resin matrix of the carbon fiber resin matrix composite material is a thermosetting resin or a thermoplastic resin. The thermosetting resin includes epoxy resin, phenolic resin and unsaturated polyester; the thermoplastic resin includes polyethersulfone, nylon 6 , Nylon 66.
优选的,所述步骤S1中,所述的碳纤维树脂基复合材料的碳纤维形态包括短切纤维、连续纤维、碳纤维布或者粉末纤维。Preferably, in step S1, the carbon fiber form of the carbon fiber resin matrix composite material includes chopped fibers, continuous fibers, carbon fiber cloth or powder fibers.
优选的,所述步骤S1中,所述碳纤维树脂基复合材料的纤维为聚丙烯腈基碳纤维或沥青基碳纤维。Preferably, in step S1, the fibers of the carbon fiber resin matrix composite material are polyacrylonitrile-based carbon fibers or pitch-based carbon fibers.
优选的,所述步骤S2中,碳纤维树脂基复合材料在第二组催化剂中于常压下,保温60~300min;温度为50~200℃。温度越高、或者保温时间越长,则树脂的清除率越高,但是过高的处理温度或处理时间可能对纤维造成不可逆的性能损伤。Preferably, in step S2, the carbon fiber resin matrix composite material is kept in the second group of catalysts under normal pressure for 60 to 300 minutes; the temperature is 50 to 200°C. The higher the temperature or the longer the holding time, the higher the resin removal rate. However, excessively high processing temperature or processing time may cause irreversible performance damage to the fiber.
本发明具有以下有益效果:The invention has the following beneficial effects:
(1)本发明中的催化剂可以催化降解废弃碳纤维树脂基复合材料中的树脂基体,可以使树脂基体充分降解,参与杂质被清除;(1) The catalyst in the present invention can catalyze the degradation of the resin matrix in the waste carbon fiber resin matrix composite material, and can fully degrade the resin matrix and remove impurities involved;
(2)本发明提供的方法,分步降解复合材料,所选用的催化剂能高效断裂树脂体系中的特定化学键,第一组催化剂起到;所述的第二组催化剂为特选的几种催化剂,可以有效降解树脂;(2) The method provided by the invention degrades composite materials step by step. The selected catalyst can efficiently break specific chemical bonds in the resin system. The first group of catalysts plays a role; the second group of catalysts are several specially selected catalysts. , can effectively degrade resin;
(3)本发明提供的方法,反应过程不需要过高的温度,并且回收效率较高。这种方法所能得到的回收碳纤维的力学性能保留率能达到95%以上,且纤维与树脂基体的界面性能不会有明显的降低;(3) The method provided by the present invention does not require excessively high temperatures during the reaction process, and the recovery efficiency is high. The mechanical property retention rate of recycled carbon fiber that can be obtained by this method can reach more than 95%, and the interface properties between the fiber and the resin matrix will not be significantly reduced;
(4)本发明处理后的纤维利用乙醇就可以洗净,无需其他溶剂,减少了工序,也降低了环境污染。(4) The fiber treated in the present invention can be washed with ethanol without the need for other solvents, which reduces the number of processes and environmental pollution.
附图说明Description of the drawings
图1是本发明中添加硫酸锌和乙酰氯/乙醇的条件下回收得到的纤维表面SEM图;Figure 1 is an SEM image of the fiber surface recovered under the conditions of adding zinc sulfate and acetyl chloride/ethanol in the present invention;
图2是本发明中添加硫酸镁和对苯二甲酰氯/乙醇条件下回收得到的纤维表面SEM图。Figure 2 is an SEM image of the fiber surface recovered under the conditions of adding magnesium sulfate and terephthaloyl chloride/ethanol in the present invention.
具体实施方式Detailed ways
下面结合实施例对本发明做进一步描述。The present invention will be further described below in conjunction with examples.
实施例1Example 1
所选废弃的碳纤维树脂基复合材料中的碳纤维为东丽T700,纤维单丝拉伸强度为4.90GPa,树脂基体为4,5-环氧己烷-1,2-二甲酸二缩水甘油酯(TDE-85),固化剂为4,4`-二氨基二苯基甲烷(DDM),碳纤维为PAN基纤维,碳纤维的形态为连续纤维,其中碳纤维重量含量为60%。The carbon fiber in the selected waste carbon fiber resin matrix composite material is Toray T700, the fiber single filament tensile strength is 4.90GPa, and the resin matrix is 4,5-epoxyhexane-1,2-dicarboxylic acid diglycidyl ester ( TDE-85), the curing agent is 4,4`-diaminodiphenylmethane (DDM), the carbon fiber is PAN-based fiber, the form of the carbon fiber is continuous fiber, and the carbon fiber weight content is 60%.
本实施例提供一种回收废弃的碳纤维树脂基复合材料中碳纤维的方法,具体步骤如下:This embodiment provides a method for recycling carbon fibers in discarded carbon fiber resin matrix composite materials. The specific steps are as follows:
1、将10mm厚的碳纤维树脂复合材料裁剪成适当大小,并放入反应装置中;1. Cut the 10mm thick carbon fiber resin composite material into appropriate size and put it into the reaction device;
2、将材料放入1mol/L的硫酸镁中于100℃处理60min,利用乙醇洗净后放入乙酰氯/N,N-二甲基甲酰胺混合溶液中,混合质量比为1:2,于200℃保温150min;2. Put the material into 1 mol/L magnesium sulfate and treat it at 100°C for 60 minutes. Wash it with ethanol and put it into an acetyl chloride/N, N-dimethylformamide mixed solution. The mixing mass ratio is 1:2. Insulated at 200℃ for 150min;
3、将产物取出,用乙醇超声洗净。3. Take out the product and wash it ultrasonically with ethanol.
通过对处理前后对材料进行称重,发现树脂的降解率约为98%。根据ASTM-D3379标准,对碳纤维进行单丝拉伸测试,得到的单丝拉伸强度为4.81GPa,力学强度保留率为98.2%。By weighing the material before and after treatment, it was found that the degradation rate of the resin was approximately 98%. According to the ASTM-D3379 standard, the carbon fiber was subjected to a single-filament tensile test. The obtained single-filament tensile strength was 4.81GPa, and the mechanical strength retention rate was 98.2%.
实施例2Example 2
所选废弃的碳纤维树脂基复合材料中的碳纤维为短切东丽T700,纤维拉伸强度为4.90GPa,树脂基体为尼龙6,,碳纤维为PAN基纤维,碳纤维的形态为短切纤维,其中碳纤维重量含量为60%。The carbon fiber in the selected waste carbon fiber resin-based composite material is chopped Toray T700, the fiber tensile strength is 4.90GPa, the resin matrix is nylon 6, the carbon fiber is PAN-based fiber, the form of the carbon fiber is chopped fiber, among which the carbon fiber The weight content is 60%.
本实施例提供一种回收废弃的碳纤维树脂基复合材料中碳纤维的方法,具体步骤如下:This embodiment provides a method for recycling carbon fibers in discarded carbon fiber resin matrix composite materials. The specific steps are as follows:
1、将4mm厚的碳纤维树脂复合材料裁剪成适当大小,并放入反应装置中;1. Cut the 4mm thick carbon fiber resin composite material into appropriate size and put it into the reaction device;
2、将材料放入2mol/L的硫酸亚铁中于50℃处理30min,利用乙醇洗净后放入对苯二甲酰氯/四氢呋喃混合溶液中,混合质量比为1:5,于50℃保温300min;2. Put the material into 2 mol/L ferrous sulfate and treat it at 50°C for 30 minutes. Wash it with ethanol and put it into a mixed solution of terephthaloyl chloride/tetrahydrofuran. The mixing mass ratio is 1:5 and keep it warm at 50°C. 300min;
3、将产物取出,用乙醇超声洗净。3. Take out the product and wash it ultrasonically with ethanol.
通过对处理前后对材料进行称重,发现树脂的降解率约为96%。根据ASTM-D790标准,对回收纤维重新与树脂配合制备成复合材料,测得弯曲强度为2.96Gpa,力学强度保留率为95.7%。By weighing the material before and after treatment, it was found that the degradation rate of the resin was approximately 96%. According to the ASTM-D790 standard, the recycled fibers were combined with resin to prepare composite materials. The measured bending strength was 2.96Gpa, and the mechanical strength retention rate was 95.7%.
实施例3Example 3
所选废弃的碳纤维树脂基复合材料中的碳纤维为东丽T800,纤维拉伸强度为5.49GPa,树脂基体为4,5-环氧己烷-1,2-二甲酸二缩水甘油酯(TDE-85),固化剂为二氨基二苯砜(DDS),碳纤维为PAN基纤维,碳纤维的形态为连续纤维,其中碳纤维重量含量为60%。The carbon fiber in the selected waste carbon fiber resin matrix composite material is Toray T800, the fiber tensile strength is 5.49GPa, and the resin matrix is 4,5-epoxyhexane-1,2-dicarboxylic acid diglycidyl ester (TDE- 85), the curing agent is diaminodiphenyl sulfone (DDS), the carbon fiber is PAN-based fiber, the form of the carbon fiber is continuous fiber, and the carbon fiber weight content is 60%.
本实施例提供一种回收废弃的碳纤维树脂基复合材料中碳纤维的方法,具体步骤如下:This embodiment provides a method for recycling carbon fibers in discarded carbon fiber resin matrix composite materials. The specific steps are as follows:
1、将20mm厚的碳纤维树脂复合材料裁剪成适当大小,并放入反应装置中;1. Cut the 20mm thick carbon fiber resin composite material into appropriate size and put it into the reaction device;
2、将材料放入5mol/L的硫酸亚铁中于50℃处理200min,利用乙醇洗净后放入对苯二甲酰氯/乙醇混合溶液中,混合质量比为1:3,于120℃保温100min;2. Put the material into 5 mol/L ferrous sulfate and treat it at 50°C for 200 minutes. Wash it with ethanol and put it into a terephthaloyl chloride/ethanol mixed solution. The mixing mass ratio is 1:3 and keep it warm at 120°C. 100min;
3、将产物取出,用乙醇超声洗净。3. Take out the product and wash it ultrasonically with ethanol.
通过对处理前后对材料进行称重,发现树脂的降解率约为96%。根据ASTM-D3379标准,对碳纤维进行单丝拉伸测试,得到的单丝拉伸强度为5.32GPa,力学强度保留率为96.9%。By weighing the material before and after treatment, it was found that the degradation rate of the resin was approximately 96%. According to the ASTM-D3379 standard, the carbon fiber was subjected to a single-filament tensile test. The obtained single-filament tensile strength was 5.32GPa, and the mechanical strength retention rate was 96.9%.
实施例4Example 4
所选废弃的碳纤维树脂基复合材料中的碳纤维为短切东丽T800,纤维拉伸强度为5.49GPa,树脂基体尼龙66,碳纤维为PAN基纤维,碳纤维的形态为短切纤维,其中碳纤维重量含量为60%。The carbon fiber in the selected waste carbon fiber resin-based composite material is chopped Toray T800, the fiber tensile strength is 5.49GPa, the resin matrix is nylon 66, the carbon fiber is PAN-based fiber, the form of the carbon fiber is chopped fiber, and the carbon fiber weight content is 60%.
本实施例提供一种回收废弃的碳纤维树脂基复合材料中碳纤维的方法,具体步骤如下:This embodiment provides a method for recycling carbon fibers in discarded carbon fiber resin matrix composite materials. The specific steps are as follows:
1、将20mm厚的碳纤维树脂复合材料裁剪成适当大小,并放入反应装置中;1. Cut the 20mm thick carbon fiber resin composite material into appropriate size and put it into the reaction device;
2、将材料放入2mol/L的硫酸锌中于200℃处理50min,利用乙醇洗净后放入邻氯苯甲酰氯/N,N-二甲基甲酰胺混合溶液中,混合质量比为1:1,于150℃保温60min;2. Put the material into 2 mol/L zinc sulfate and treat it at 200°C for 50 minutes. Wash it with ethanol and put it into the o-chlorobenzoyl chloride/N, N-dimethylformamide mixed solution. The mixing mass ratio is 1 :1, keep at 150℃ for 60min;
3、将产物取出,用乙醇超声洗净。3. Take out the product and wash it ultrasonically with ethanol.
通过对处理前后对材料进行称重,发现树脂的降解率约为99%。根据ASTM-D790标准,对回收纤维重新与树脂配合制备成复合材料,测得弯曲强度为3.23Gpa,力学强度保留率为97.6%。By weighing the material before and after treatment, it was found that the degradation rate of the resin was approximately 99%. According to the ASTM-D790 standard, the recycled fibers were combined with resin to prepare composite materials. The measured bending strength was 3.23Gpa, and the mechanical strength retention rate was 97.6%.
实施例5Example 5
所选废弃的碳纤维树脂基复合材料中的碳纤维为东丽T700,纤维拉伸强度为4.90GPa,树脂基体尼龙66,碳纤维为PAN基纤维,碳纤维的形态为短切纤维,其中碳纤维重量含量为60%。The carbon fiber in the selected waste carbon fiber resin-based composite material is Toray T700, the fiber tensile strength is 4.90GPa, the resin matrix is nylon 66, the carbon fiber is PAN-based fiber, the form of the carbon fiber is chopped fiber, and the carbon fiber weight content is 60 %.
本实施例提供一种回收废弃的碳纤维树脂基复合材料中碳纤维的方法,具体步骤如下:This embodiment provides a method for recycling carbon fibers in discarded carbon fiber resin matrix composite materials. The specific steps are as follows:
1、将1mm厚的碳纤维树脂复合材料裁剪成适当大小,并放入反应装置中;1. Cut the 1mm thick carbon fiber resin composite material into appropriate size and put it into the reaction device;
2、将材料放入2mol/L的硫酸亚铁中于100℃处理150min,利用乙醇洗净后放入邻氯苯甲酰氯/N,N-二甲基甲酰胺混合溶液中,混合质量比为1:4,于120℃保温200min;2. Put the material into 2 mol/L ferrous sulfate and treat it at 100°C for 150 minutes. Wash it with ethanol and put it into the o-chlorobenzoyl chloride/N,N-dimethylformamide mixed solution. The mixing mass ratio is 1:4, keep at 120℃ for 200min;
3、将产物取出,用乙醇超声洗净。3. Take out the product and wash it ultrasonically with ethanol.
通过对处理前后对材料进行称重,发现树脂的降解率约为97%。根据ASTM-D3379标准,对碳纤维进行单丝拉伸测试,得到的单丝拉伸强度为4.83GPa,力学强度保留率为98.6%。By weighing the material before and after treatment, it was found that the degradation rate of the resin was approximately 97%. According to the ASTM-D3379 standard, the carbon fiber was subjected to a single-filament tensile test. The obtained single-filament tensile strength was 4.83GPa, and the mechanical strength retention rate was 98.6%.
与现有的碳纤维回收技术相比,本发明回收效率高、能量消耗低、处理温度低,解决了化学回收工艺操作时间长、能耗高的问题,相比于其他传统单用催化剂的回收方法,这种方法能够更有效地降解树脂,同时两步处理分别有不同的作用,能更高效地进行回收。Compared with the existing carbon fiber recycling technology, the present invention has high recycling efficiency, low energy consumption and low processing temperature. It solves the problems of long operation time and high energy consumption of the chemical recycling process. Compared with other traditional recovery methods using only catalysts, , this method can degrade the resin more effectively, and at the same time, the two-step treatment has different effects and can be recycled more efficiently.
在回收过后纤维的状态保持良好,表面没有出现明显的缺陷结构,纤维本身的力学性能得到了极大程度的保留。碳纤维在回收过后还保留同样的形态,使其仍然具有一定的利用价值。After recycling, the fiber remains in good condition, with no obvious defect structure on the surface, and the mechanical properties of the fiber itself are retained to a great extent. Carbon fiber retains the same form after recycling, making it still valuable.
惟以上所述者,仅为本发明的具体实施例而已,当不能以此限定本发明实施的范围,故其等同组件的置换,或依本发明专利保护范围所作的等同变化与修改,皆应仍属本发明权利要求书涵盖之范畴。However, the above are only specific embodiments of the present invention, and should not be used to limit the scope of the present invention. Therefore, the replacement of equivalent components, or equivalent changes and modifications made in accordance with the patent protection scope of the present invention, should be It still falls within the scope of the claims of the present invention.
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