CN103571186A - Waste CFRP (carbon fiber reinforced plastic) powder reinforced nylon composition and preparation method of nylon composition - Google Patents
Waste CFRP (carbon fiber reinforced plastic) powder reinforced nylon composition and preparation method of nylon composition Download PDFInfo
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- 239000000843 powder Substances 0.000 title claims abstract description 55
- 239000000203 mixture Substances 0.000 title claims abstract description 48
- 239000004677 Nylon Substances 0.000 title claims abstract description 46
- 229920001778 nylon Polymers 0.000 title claims abstract description 46
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- 239000004918 carbon fiber reinforced polymer Substances 0.000 title claims abstract 13
- 239000002699 waste material Substances 0.000 title abstract description 55
- 239000002131 composite material Substances 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims abstract description 12
- 239000002994 raw material Substances 0.000 claims abstract description 8
- 239000012756 surface treatment agent Substances 0.000 claims abstract description 6
- 239000000314 lubricant Substances 0.000 claims abstract description 5
- 239000002245 particle Substances 0.000 claims abstract description 5
- 238000002156 mixing Methods 0.000 claims abstract description 3
- 239000007822 coupling agent Substances 0.000 claims description 7
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 6
- 229920000571 Nylon 11 Polymers 0.000 claims description 5
- 229920002292 Nylon 6 Polymers 0.000 claims description 5
- 229920002302 Nylon 6,6 Polymers 0.000 claims description 5
- -1 Zinic stearas Chemical compound 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 5
- RKISUIUJZGSLEV-UHFFFAOYSA-N n-[2-(octadecanoylamino)ethyl]octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NCCNC(=O)CCCCCCCCCCCCCCCCC RKISUIUJZGSLEV-UHFFFAOYSA-N 0.000 claims description 5
- 239000006087 Silane Coupling Agent Substances 0.000 claims description 4
- 150000004645 aluminates Chemical class 0.000 claims description 4
- 229920006152 PA1010 Polymers 0.000 claims description 3
- 235000021355 Stearic acid Nutrition 0.000 claims description 3
- BGYHLZZASRKEJE-UHFFFAOYSA-N [3-[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxy]-2,2-bis[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxymethyl]propyl] 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)OCC(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 BGYHLZZASRKEJE-UHFFFAOYSA-N 0.000 claims description 3
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 3
- 239000008116 calcium stearate Substances 0.000 claims description 3
- 235000013539 calcium stearate Nutrition 0.000 claims description 3
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 3
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 3
- 239000008117 stearic acid Substances 0.000 claims description 3
- JHWNWJKBPDFINM-UHFFFAOYSA-N Laurolactam Chemical compound O=C1CCCCCCCCCCCN1 JHWNWJKBPDFINM-UHFFFAOYSA-N 0.000 claims description 2
- 229920000299 Nylon 12 Polymers 0.000 claims description 2
- UAUDZVJPLUQNMU-KTKRTIGZSA-N erucamide Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-KTKRTIGZSA-N 0.000 claims description 2
- SSDSCDGVMJFTEQ-UHFFFAOYSA-N octadecyl 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)CCC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 SSDSCDGVMJFTEQ-UHFFFAOYSA-N 0.000 claims description 2
- 238000005453 pelletization Methods 0.000 claims description 2
- 239000000835 fiber Substances 0.000 claims 9
- 238000013467 fragmentation Methods 0.000 claims 3
- 238000006062 fragmentation reaction Methods 0.000 claims 3
- 239000003112 inhibitor Substances 0.000 claims 3
- 230000003647 oxidation Effects 0.000 claims 3
- 238000007254 oxidation reaction Methods 0.000 claims 3
- 229920000305 Nylon 6,10 Polymers 0.000 claims 1
- 229920000049 Carbon (fiber) Polymers 0.000 abstract description 13
- 239000004917 carbon fiber Substances 0.000 abstract description 13
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 13
- 238000007873 sieving Methods 0.000 abstract description 7
- 239000003963 antioxidant agent Substances 0.000 abstract description 3
- 230000003078 antioxidant effect Effects 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 abstract description 2
- 238000001125 extrusion Methods 0.000 abstract description 2
- 239000008188 pellet Substances 0.000 abstract 1
- 238000012986 modification Methods 0.000 description 8
- 230000004048 modification Effects 0.000 description 8
- 239000003365 glass fiber Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 239000011256 inorganic filler Substances 0.000 description 4
- 229910003475 inorganic filler Inorganic materials 0.000 description 4
- 238000011056 performance test Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- JKIJEFPNVSHHEI-UHFFFAOYSA-N Phenol, 2,4-bis(1,1-dimethylethyl)-, phosphite (3:1) Chemical compound CC(C)(C)C1=CC(C(C)(C)C)=CC=C1OP(OC=1C(=CC(=CC=1)C(C)(C)C)C(C)(C)C)OC1=CC=C(C(C)(C)C)C=C1C(C)(C)C JKIJEFPNVSHHEI-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000007983 Tris buffer Substances 0.000 description 2
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- UAUDZVJPLUQNMU-UHFFFAOYSA-N Erucasaeureamid Natural products CCCCCCCCC=CCCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-UHFFFAOYSA-N 0.000 description 1
- OKOBUGCCXMIKDM-UHFFFAOYSA-N Irganox 1098 Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)NCCCCCCNC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 OKOBUGCCXMIKDM-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- FYHXNYLLNIKZMR-UHFFFAOYSA-N calcium;carbonic acid Chemical compound [Ca].OC(O)=O FYHXNYLLNIKZMR-UHFFFAOYSA-N 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011208 reinforced composite material Substances 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 description 1
Classifications
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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
- C08K13/00—Use of mixtures of ingredients not covered by one single of the preceding main groups, each of these compounds being essential
- C08K13/06—Pretreated ingredients and ingredients covered by the main groups C08K3/00 - C08K7/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
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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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- 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
- C08K9/00—Use of pretreated ingredients
- C08K9/04—Ingredients treated with organic substances
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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
- C08K9/00—Use of pretreated ingredients
- C08K9/04—Ingredients treated with organic substances
- C08K9/06—Ingredients treated with organic substances with silicon-containing compounds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
- C08L77/02—Polyamides derived from omega-amino carboxylic acids or from lactams thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
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- Chemical & Material Sciences (AREA)
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- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
本发明涉及一种废弃碳纤维复合材料粉增强尼龙组合物及其制备方法,包括以下步骤:(1)将废弃的CFRP材料破碎,过筛,得到粒径均匀的废弃CFRP粉末;(2)按上述配比,称取5-40份的废弃CFRP粉末在高混机中干燥处理,然后加入0.1-3份的表面处理剂对CFRP粉末表面处理;(3)再按配比称取60-95份尼龙,0.1-0.6份润滑剂,0.1-0.5份抗氧剂于高混机中,混合均匀;(4)将步骤(3)混合均匀的原料加入到双螺杆机中熔融共混,挤出,水冷,拉条切粒得废弃CFRP增强的尼龙组合物。与现有技术相比,本发明组合物密度低,减少了其对环境的污染,增加了其附加值,节约了资源,保护了环境点。The invention relates to a waste carbon fiber composite material powder reinforced nylon composition and a preparation method thereof, comprising the following steps: (1) crushing the waste CFRP material and sieving to obtain waste CFRP powder with uniform particle size; (2) according to the above Proportioning, weigh 5-40 parts of waste CFRP powder and dry it in a high mixer, then add 0.1-3 parts of surface treatment agent to treat the surface of CFRP powder; (3) weigh 60-95 parts of nylon according to the proportion , 0.1-0.6 parts of lubricant, 0.1-0.5 parts of antioxidant in a high mixer, and mix well; (4) Add the uniformly mixed raw materials in step (3) to a twin-screw machine for melt blending, extrusion, and water cooling , the strands were cut into pellets to obtain a waste CFRP-reinforced nylon composition. Compared with the prior art, the composition of the invention has low density, reduces its pollution to the environment, increases its added value, saves resources and protects the environment.
Description
技术领域technical field
本发明属于高分子材料回收技术领域,具体涉及一种废弃碳纤维复合材料粉增强尼龙组合物及其制备方法。The invention belongs to the technical field of polymer material recovery, and in particular relates to a waste carbon fiber composite material powder reinforced nylon composition and a preparation method thereof.
背景技术Background technique
碳纤维复合材料(CFRP)具有质轻、高强度、高模量等优异的性能,是其他玻璃纤维增强复合材料所无法比拟的,因此被广泛的应用于航空航天、汽车工业、轨道交通、新能源、体育用品等高新技术产业领域。随着经济的高速发展,CFRP在各个领域的使用量迅猛增长,所产生的废弃树脂也与日俱增,而废弃的CFRP中的成份都不可降解,若直接丢弃到环境中的话,一方面会给环境带来严重的污染;另一方面,这些废弃的CFRP中往往含有60%左右的高附加值碳纤维,而碳纤维的生产是一个高耗能的过程,若不加以回收利用也将造成资源的严重浪费。Carbon fiber composite materials (CFRP) have excellent properties such as light weight, high strength, and high modulus, which are unmatched by other glass fiber reinforced composite materials, so they are widely used in aerospace, automotive industry, rail transit, new energy , sporting goods and other high-tech industries. With the rapid development of the economy, the use of CFRP in various fields is increasing rapidly, and the waste resin produced is also increasing day by day, and the components in the waste CFRP are not degradable. If they are directly discarded into the environment, on the one hand, it will bring environmental harm On the other hand, these waste CFRP often contain about 60% of high value-added carbon fiber, and the production of carbon fiber is a high energy-consuming process, if it is not recycled, it will cause a serious waste of resources.
尼龙作为一种工程塑料,其具有很好的弹性,力学性能较好,耐磨,耐油性和加工性能良好,因此被广泛的应用于汽车,家电,电子电器,机械等领域。但是尼龙在使用过程中易脆化,抗冲击性能差,吸水率高,耐热性和强度稍低等缺陷,为了改善尼龙的这些性能,目前常用的方法是通过采用玻璃纤维或无机填料如碳酸钙,滑石粉等来填充改性尼龙。而玻璃纤维或无机填料密度较大,填充改性尼龙后得到组合物密度也随之大幅增加,这会导致产品的市场竞争力下降,同时,受玻璃纤维或无机填料本身性能限制,采用玻纤或无机填料增强改性的尼龙性能提高有限,在一些性能要求较高的场合应用将受限制。As an engineering plastic, nylon has good elasticity, good mechanical properties, wear resistance, oil resistance and good processing performance, so it is widely used in automobiles, home appliances, electronic appliances, machinery and other fields. However, nylon is prone to embrittlement during use, poor impact resistance, high water absorption, low heat resistance and low strength. In order to improve these properties of nylon, the commonly used method is to use glass fiber or inorganic fillers such as carbonic acid Calcium, talc, etc. to fill the modified nylon. However, the density of glass fiber or inorganic filler is relatively high, and the density of the composition obtained after filling modified nylon will also increase significantly, which will lead to a decline in the market competitiveness of the product. At the same time, due to the performance limitations of glass fiber or inorganic filler, glass fiber Or the performance of nylon modified by inorganic fillers is limited, and the application in some occasions with high performance requirements will be limited.
发明内容Contents of the invention
本发明的目的就是为了克服上述现有技术存在的缺陷而提供一种成本低、减少污染的废弃碳纤维复合材料粉增强尼龙组合物及其制备方法。The object of the present invention is to provide a waste carbon fiber composite material powder reinforced nylon composition with low cost and less pollution and a preparation method thereof in order to overcome the above-mentioned defects in the prior art.
本发明的目的可以通过以下技术方案来实现:一种废弃碳纤维复合材料粉增强尼龙组合物,其特征在于,该组合物包含以下重量份的组分制成:The purpose of the present invention can be achieved through the following technical solutions: a waste carbon fiber composite material powder reinforced nylon composition, characterized in that the composition comprises the following components by weight:
所述的尼龙为尼龙6(PA6)、尼龙66(PA66)、尼龙11(PA11)、尼龙12(PA12)、尼龙1010(PA1010)、尼龙610T(PA610T)中的一种或一种以上。The nylon is one or more of nylon 6 (PA6), nylon 66 (PA66), nylon 11 (PA11), nylon 12 (PA12), nylon 1010 (PA1010), and nylon 610T (PA610T).
所述的废弃CFRP粉末为将废弃的CFRP材料破碎所得,优选破碎后的粒径在40-400目之间。The waste CFRP powder is obtained by crushing waste CFRP materials, and the crushed particle size is preferably between 40-400 mesh.
由于废弃CFRP粉末的主要成分是碳纤维和树脂基体,树脂基体尤其以热固性树脂居多,其与尼龙表面的亲和性较差,所以两者往往不相容,采用表面处理剂对废弃CFRP粉末处理后可提高其表面亲和性,改善其与填充树脂的相容性。Since the main components of waste CFRP powder are carbon fiber and resin matrix, the resin matrix is mostly thermosetting resin, which has poor affinity with nylon surface, so the two are often incompatible. Surface treatment agent is used to treat waste CFRP powder. It can improve its surface affinity and improve its compatibility with filled resins.
所述的表面处理剂为硅烷偶联剂,钛酸酯偶联剂和铝酸酯偶联剂中的一种或一种以上。The surface treatment agent is one or more of silane coupling agent, titanate coupling agent and aluminate coupling agent.
所述的润滑剂为硬脂酸、硬脂酸锌、硬脂酸钙、聚乙烯腊、白油、乙撑双硬脂酰胺(EBS)、芥酸酰胺中的一种或一种以上。The lubricant is one or more of stearic acid, zinc stearate, calcium stearate, polyethylene wax, white oil, ethylene bisstearamide (EBS), and erucamide.
所述的抗氧剂为抗氧剂1010、抗氧剂1076、抗氧剂1098、抗氧剂168中的一种或一种以上。The antioxidant is one or more of antioxidant 1010, antioxidant 1076, antioxidant 1098, and antioxidant 168.
一种废弃碳纤维复合材料粉增强尼龙组合物的制备方法,其特征在于,包括以下步骤:A preparation method of waste carbon fiber composite material powder reinforced nylon composition, characterized in that it comprises the following steps:
(1)将废弃的CFRP材料破碎,过筛,得到粒径均匀的废弃CFRP粉末;(1) Crushing and sieving waste CFRP materials to obtain waste CFRP powders with uniform particle size;
(2)按上述配比,称取5-40份的废弃CFRP粉末在高混机中干燥处理,然后加入0.1-3份的表面处理剂对CFRP粉末表面处理;(2) According to the above ratio, weigh 5-40 parts of waste CFRP powder and dry it in a high mixer, and then add 0.1-3 parts of surface treatment agent to treat the surface of CFRP powder;
(3)再按配比称取60-95份尼龙,0.1-0.6份润滑剂,0.1-0.5份抗氧剂于高混机中,混合均匀;(3) Take by weighing 60-95 parts of nylon, 0.1-0.6 parts of lubricant, and 0.1-0.5 parts of antioxidant in a high-mixer, and mix evenly;
(4)将步骤(3)混合均匀的原料加入到双螺杆机中熔融共混,挤出,水冷,拉条切粒得废弃CFRP增强的尼龙组合物。(4) Add the homogeneously mixed raw materials in step (3) into a twin-screw machine for melt blending, extrusion, water cooling, strand cutting and pelletizing to obtain a waste CFRP reinforced nylon composition.
所述的步骤(2)中高混机的干燥温度为80-120℃,干燥时间为10-30min。The drying temperature of the high mixer in the step (2) is 80-120°C, and the drying time is 10-30min.
所述的步骤(4)的双螺杆挤出机为同向或异向双螺杆挤出机,挤出机温度为190-290℃,螺杆转速为150-400rpm,螺杆长径比L/D为30-50:1。The twin-screw extruder in the step (4) is a co-rotating or counter-rotating twin-screw extruder, the extruder temperature is 190-290°C, the screw speed is 150-400rpm, and the screw length-to-diameter ratio L/D is 30-50:1.
本发明的目的之一是提供一种废弃碳纤维复合材料粉增强尼龙组合物,该组合物采用回收的废弃碳纤维复合材料粉作为增强改性组分,以较低的成本实现了对尼龙的高性能改性,得到的组合物密度也低;同时该组合物使废弃的CFRP材料得以重新利用,减少了其对环境的污染,增加了其附加值,节约了资源,保护了环境。One of the objectives of the present invention is to provide a waste carbon fiber composite material powder reinforced nylon composition, which uses recycled waste carbon fiber composite material powder as a reinforcement modification component, and realizes high performance to nylon at a lower cost Modification, the density of the obtained composition is also low; at the same time, the composition enables the waste CFRP material to be reused, reduces its pollution to the environment, increases its added value, saves resources, and protects the environment.
本发明的另一目的是提供一种上述废弃碳纤维复合材料粉增强尼龙组合物的制备方法,该制备方法加工操作简单。Another object of the present invention is to provide a method for preparing the above-mentioned waste carbon fiber composite material powder reinforced nylon composition, which is simple in processing and operation.
与现有技术相比,本发明组合物采用回收的废弃碳纤维复合材料粉作为增强改性组分,以较低的成本实现了对尼龙的高性能改性,得到的废弃CFRP复合材料粉增强尼龙组合物密度低,力学性能优异,采用回收的废弃CFRP复合材料粉作为增强改性组分,以较低的成本实现了对尼龙的高性能改性;同时该组合物使废弃的CFRP材料得以重新利用,减少了其对环境的污染,增加了其附加值,节约资源,保护环境;得到的组合物可以广泛的应用于汽车、电子电器、家电、机械等产品零部件。Compared with the prior art, the composition of the present invention adopts recycled waste carbon fiber composite material powder as a reinforcing modification component, and realizes high-performance modification of nylon at a lower cost, and the obtained waste CFRP composite material powder reinforces nylon The composition has low density and excellent mechanical properties. Recycled waste CFRP composite powder is used as the reinforcing modification component to achieve high-performance modification of nylon at a lower cost; at the same time, the composition enables waste CFRP materials to be regenerated Utilization reduces its pollution to the environment, increases its added value, saves resources, and protects the environment; the obtained composition can be widely used in product parts such as automobiles, electronic appliances, home appliances, and machinery.
具体实施方式Detailed ways
下面结合具体实施例对本发明进行详细说明。The present invention will be described in detail below in conjunction with specific embodiments.
以下实施例中,拉伸性能测试标准为ASTM D638,弯曲性能测试标准为ASTMD790,Izod缺口冲击强度测试标准为ASTM D256。In the following examples, the tensile performance test standard is ASTM D638, the bending performance test standard is ASTM D790, and the Izod notched impact strength test standard is ASTM D256.
实施例1Example 1
(1)将废弃CFRP材料破碎,过筛得400目的废弃CFRP粉末。(1) Crushing waste CFRP materials and sieving to obtain 400-mesh waste CFRP powder.
(2)称取20份废弃CFRP粉末于高混机中100℃干燥20min,然后加入0.1份硅烷偶联剂KH550表面处理废弃CFRP粉末。(2) Weigh 20 parts of waste CFRP powder and dry it in a high mixer at 100°C for 20 min, then add 0.1 part of silane coupling agent KH550 to surface treat the waste CFRP powder.
(3)称取80份PA66,0.1份硬脂酸钙,0.3份抗氧剂1010,0.1份抗氧剂168于高混机中混合均匀。(3) Weigh 80 parts of PA66, 0.1 part of calcium stearate, 0.3 part of antioxidant 1010, and 0.1 part of antioxidant 168, and mix them uniformly in a high mixer.
(4)将混合均匀的原料加入双螺杆挤出机中,熔融共混,挤出,拉条切粒得所需的废弃CFRP粉末增强尼龙组合物,双螺杆挤出机各区温度为:一区220℃,二区230℃,三区240℃,四区250℃,五区260℃,六区270℃,七区280℃,八区280℃,九区290℃,十区290℃,机头285℃;螺杆转速350rpm,长径比L/D=30/1。(4) Add the uniformly mixed raw materials into the twin-screw extruder, melt and blend, extrude, and pelletize the strands to obtain the required waste CFRP powder reinforced nylon composition. The temperature in each zone of the twin-screw extruder is: Zone 1 220°C, 230°C in zone 2, 240°C in zone 3, 250°C in zone 4, 260°C in zone 5, 270°C in zone 6, 280°C in zone 7, 280°C in zone 8, 290°C in zone 9, 290°C in zone 10, machine head 285°C; screw speed 350rpm, aspect ratio L/D=30/1.
实施例2Example 2
(1)将废弃CFRP材料破碎,过筛得200目的废弃CFRP粉末。(1) Crushing waste CFRP materials and sieving to obtain 200-mesh waste CFRP powder.
(2)称取10份废弃CFRP粉末于高混机中80℃干燥30min,然后加入1份硅烷偶联剂KH560表面处理废弃CFRP粉末。(2) Weigh 10 parts of waste CFRP powder and dry it in a high mixer at 80°C for 30 minutes, then add 1 part of silane coupling agent KH560 to surface treat the waste CFRP powder.
(3)称取90份PA12,0.3份EBS,0.1份抗1076,0.1份抗168于高混机中混合均匀。(3) Weigh 90 parts of PA12, 0.3 part of EBS, 0.1 part of anti-1076, 0.1 part of anti-168 and mix them evenly in a high mixer.
(4)将混合均匀的原料加入双螺杆挤出机中,熔融共混,挤出,拉条切粒得所需的废弃CFRP粉末增强尼龙组合物,双螺杆挤出机各区温度为:一区220℃,二区230℃,三区240℃,四区250℃,五区260℃,六区270℃,七区280℃,八区280℃,九区290℃,十区290℃,机头285℃;螺杆转速250rpm,长径比L/D=40/1。(4) Add the uniformly mixed raw materials into the twin-screw extruder, melt and blend, extrude, and pelletize the strands to obtain the required waste CFRP powder reinforced nylon composition. The temperature in each zone of the twin-screw extruder is: Zone 1 220°C, 230°C in zone 2, 240°C in zone 3, 250°C in zone 4, 260°C in zone 5, 270°C in zone 6, 280°C in zone 7, 280°C in zone 8, 290°C in zone 9, 290°C in zone 10, machine head 285°C; screw speed 250rpm, aspect ratio L/D=40/1.
实施例3Example 3
(1)将废弃CFRP材料破碎,过筛得80目的废弃CFRP粉末。(1) Crushing the waste CFRP material and sieving to obtain 80-mesh waste CFRP powder.
(2)称取30份废弃CFRP粉末于高混机中120℃干燥10min,然后加入3份钛酸酯偶联剂异丙基三(十二烷基苯磺酰基)钛酸酯表面处理废弃CFRP粉末。(2) Weigh 30 parts of waste CFRP powder and dry it in a high mixer at 120°C for 10 minutes, then add 3 parts of titanate coupling agent isopropyl tris(dodecylbenzenesulfonyl) titanate to surface treat waste CFRP powder.
(3)称取70份PA6,0.6份聚乙烯蜡,0.3份抗1098,0.2份抗168于高混机中混合均匀。(3) Weigh 70 parts of PA6, 0.6 parts of polyethylene wax, 0.3 parts of anti-1098, 0.2 parts of anti-168 and mix them evenly in a high mixer.
(4)将混合均匀的原料加入双螺杆挤出机中,熔融共混,挤出,拉条切粒得所需的废弃CFRP粉末增强尼龙组合物,双螺杆挤出机各区温度为;一区220℃,二区230℃,三区240℃,四区250℃,五区260℃,六区270℃,七区280℃,八区280℃,九区290℃,十区290℃,机头285℃;螺杆转速400rpm,长径比L/D=50/1。(4) Add the homogeneously mixed raw materials into the twin-screw extruder, melt and blend, extrude, and pelletize the strands to obtain the required waste CFRP powder reinforced nylon composition. The temperature in each zone of the twin-screw extruder is; 220°C, 230°C in zone 2, 240°C in zone 3, 250°C in zone 4, 260°C in zone 5, 270°C in zone 6, 280°C in zone 7, 280°C in zone 8, 290°C in zone 9, 290°C in zone 10, machine head 285°C; screw speed 400rpm, aspect ratio L/D=50/1.
实施例4Example 4
(1)将废弃CFRP材料破碎,过筛得300目的废弃CFRP粉末。(1) Crushing the waste CFRP material and sieving to obtain 300 mesh waste CFRP powder.
(2)称取40份废弃CFRP粉末于高混机中120℃干燥10min,然后加入3份铝酸酯偶联剂二硬脂酰氧异丙基铝酸酯表面处理废弃CFRP粉末。(2) Weigh 40 parts of waste CFRP powder and dry it in a high mixer at 120°C for 10 min, then add 3 parts of aluminate coupling agent distearoyloxyisopropyl aluminate to surface treat the waste CFRP powder.
(3)称取60份PA11,0.5份白油,0.3份抗1076,0.2份抗168于高混机中混合均匀。(3) Weigh 60 parts of PA11, 0.5 parts of white oil, 0.3 parts of anti-1076, 0.2 parts of anti-168 and mix them evenly in a high mixer.
(4)将混合均匀的原料加入双螺杆挤出机中,熔融共混,挤出,拉条切粒得所需的废弃CFRP粉末增强尼龙组合物,双螺杆挤出机各区温度为:一区220℃,二区230℃,三区240℃,四区250℃,五区260℃,六区270℃,七区280℃,八区280℃,九区290℃,十区290℃,机头285℃;螺杆转速400rpm,长径比L/D=50/1。(4) Add the uniformly mixed raw materials into the twin-screw extruder, melt and blend, extrude, and pelletize the strands to obtain the required waste CFRP powder reinforced nylon composition. The temperature in each zone of the twin-screw extruder is: Zone 1 220°C, 230°C in zone 2, 240°C in zone 3, 250°C in zone 4, 260°C in zone 5, 270°C in zone 6, 280°C in zone 7, 280°C in zone 8, 290°C in zone 9, 290°C in zone 10, machine head 285°C; screw speed 400rpm, aspect ratio L/D=50/1.
实施例5Example 5
(1)将废弃CFRP材料破碎,过筛得200目的废弃CFRP粉末。(1) Crushing waste CFRP materials and sieving to obtain 200-mesh waste CFRP powder.
(2)称取5份废弃CFRP粉末于高混机中100℃干燥20min,然后加入0.2份钛酸酯偶联剂异丙基三(十二烷基苯磺酰基)钛酸酯表面处理废弃CFRP粉末。(2) Weigh 5 parts of waste CFRP powder and dry it in a high mixer at 100°C for 20 minutes, then add 0.2 parts of titanate coupling agent isopropyl tris(dodecylbenzenesulfonyl) titanate to surface treat waste CFRP powder.
(3)称取95份PA1010,0.3份硬脂酸,0.3份抗1010,0.1份抗168于高混机中混合均匀。(3) Weigh 95 parts of PA1010, 0.3 part of stearic acid, 0.3 part of anti-1010, 0.1 part of anti-168 and mix them evenly in a high mixer.
(4)将混合均匀的原料加入双螺杆挤出机中,熔融共混,挤出,拉条切粒得所需的废弃CFRP粉末增强尼龙组合物,双螺杆挤出机各区温度为:一区220℃,二区230℃,三区240℃,四区250℃,五区260℃,六区270℃,七区280℃,八区280℃,九区290℃,十区290℃,机头285℃;螺杆转速150rpm,长径比L/D=30/1。(4) Add the uniformly mixed raw materials into the twin-screw extruder, melt and blend, extrude, and pelletize the strands to obtain the required waste CFRP powder reinforced nylon composition. The temperature in each zone of the twin-screw extruder is: Zone 1 220°C, 230°C in zone 2, 240°C in zone 3, 250°C in zone 4, 260°C in zone 5, 270°C in zone 6, 280°C in zone 7, 280°C in zone 8, 290°C in zone 9, 290°C in zone 10, machine head 285°C; screw speed 150rpm, aspect ratio L/D=30/1.
各实施例力学性能测试结果如下表1所示:The mechanical property test results of each embodiment are shown in Table 1 below:
表1力学性能测试结果Table 1 Mechanical property test results
从上表中力学性能测试结果分析可知,采用回收CFRP粉增强的尼龙组合物强度高,力学性能优异,符合对性能要求较高的场合使用。From the analysis of the mechanical performance test results in the above table, it can be seen that the nylon composition reinforced with recycled CFRP powder has high strength and excellent mechanical properties, which is suitable for use in occasions with high performance requirements.
上述的对实施例的描述是为便于该技术领域的普通技术人员能理解和应用本发明。熟悉本领域技术的人员显然可以容易地对实施例做出各种修改,并把此说明的一般原理应用到其他实施例中而不必经过创造性的劳动。因此,本发明不限于这里的实施例,本领域技术人员根据本发明的揭示,不脱离本发明范畴所做出的改进和修改都应该在本发明的保护范围之内。The above description of the embodiments is for those of ordinary skill in the art to understand and apply the present invention. It is obvious that those skilled in the art can easily make various modifications to the embodiment, and apply the general principles described in this description to other embodiments without creative effort. Therefore, the present invention is not limited to the embodiments herein. Improvements and modifications made by those skilled in the art according to the disclosure of the present invention without departing from the scope of the present invention should fall within the protection scope of the present invention.
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