CN118271654A - A kind of anti-aging toughened and reinforced polyolefin plastic and preparation method thereof - Google Patents
A kind of anti-aging toughened and reinforced polyolefin plastic and preparation method thereof Download PDFInfo
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- CN118271654A CN118271654A CN202410491193.9A CN202410491193A CN118271654A CN 118271654 A CN118271654 A CN 118271654A CN 202410491193 A CN202410491193 A CN 202410491193A CN 118271654 A CN118271654 A CN 118271654A
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- 229920000098 polyolefin Polymers 0.000 title claims abstract description 66
- 230000003712 anti-aging effect Effects 0.000 title claims abstract description 51
- 229920003023 plastic Polymers 0.000 title claims abstract description 45
- 239000004033 plastic Substances 0.000 title claims abstract description 45
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- -1 polysiloxane Polymers 0.000 claims abstract description 70
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims abstract description 34
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 34
- 230000003014 reinforcing effect Effects 0.000 claims abstract description 30
- 239000004594 Masterbatch (MB) Substances 0.000 claims abstract description 27
- 229920001296 polysiloxane Polymers 0.000 claims abstract description 27
- 238000002156 mixing Methods 0.000 claims abstract description 23
- 238000006243 chemical reaction Methods 0.000 claims abstract description 22
- 238000001125 extrusion Methods 0.000 claims abstract description 12
- 238000005469 granulation Methods 0.000 claims abstract description 12
- 230000003179 granulation Effects 0.000 claims abstract description 12
- 239000003999 initiator Substances 0.000 claims abstract description 12
- 229920002545 silicone oil Polymers 0.000 claims abstract description 10
- 239000003960 organic solvent Substances 0.000 claims abstract description 5
- 238000010438 heat treatment Methods 0.000 claims abstract description 3
- 239000001257 hydrogen Substances 0.000 claims abstract 3
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract 3
- 239000004698 Polyethylene Substances 0.000 claims description 40
- 229920000573 polyethylene Polymers 0.000 claims description 40
- 239000004743 Polypropylene Substances 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 20
- 229920001155 polypropylene Polymers 0.000 claims description 19
- 229920002050 silicone resin Polymers 0.000 claims description 17
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 claims description 15
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 9
- 239000000155 melt Substances 0.000 claims description 7
- 239000000758 substrate Substances 0.000 claims description 7
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 6
- 239000004342 Benzoyl peroxide Substances 0.000 claims description 6
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 claims description 6
- 235000019400 benzoyl peroxide Nutrition 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- 239000003377 acid catalyst Substances 0.000 claims description 5
- 238000006392 deoxygenation reaction Methods 0.000 claims description 5
- 238000004821 distillation Methods 0.000 claims description 5
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 5
- 229920006124 polyolefin elastomer Polymers 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 4
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 claims description 2
- 239000008096 xylene Substances 0.000 claims description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims 2
- 239000012046 mixed solvent Substances 0.000 claims 1
- 230000032683 aging Effects 0.000 abstract description 41
- 239000000463 material Substances 0.000 abstract description 21
- 229920005989 resin Polymers 0.000 abstract description 9
- 239000011347 resin Substances 0.000 abstract description 9
- 150000001336 alkenes Chemical class 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 abstract description 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 abstract description 3
- 239000002861 polymer material Substances 0.000 abstract description 3
- 229910052710 silicon Inorganic materials 0.000 abstract description 3
- 239000010703 silicon Substances 0.000 abstract description 3
- 229920001002 functional polymer Polymers 0.000 abstract description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- 206010051246 Photodermatosis Diseases 0.000 abstract 1
- 230000008845 photoaging Effects 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 230000014759 maintenance of location Effects 0.000 description 44
- 230000000694 effects Effects 0.000 description 16
- 229920001684 low density polyethylene Polymers 0.000 description 16
- 239000004702 low-density polyethylene Substances 0.000 description 16
- 230000000052 comparative effect Effects 0.000 description 15
- 229920001903 high density polyethylene Polymers 0.000 description 10
- 239000004700 high-density polyethylene Substances 0.000 description 10
- 239000002131 composite material Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- XWJBRBSPAODJER-UHFFFAOYSA-N 1,7-octadiene Chemical compound C=CCCCCC=C XWJBRBSPAODJER-UHFFFAOYSA-N 0.000 description 4
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- 125000003342 alkenyl group Chemical group 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229920001912 maleic anhydride grafted polyethylene Polymers 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 230000002787 reinforcement Effects 0.000 description 3
- PRBHEGAFLDMLAL-UHFFFAOYSA-N 1,5-Hexadiene Natural products CC=CCC=C PRBHEGAFLDMLAL-UHFFFAOYSA-N 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 2
- 230000003078 antioxidant effect Effects 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 239000003431 cross linking reagent Substances 0.000 description 2
- NLDGJRWPPOSWLC-UHFFFAOYSA-N deca-1,9-diene Chemical compound C=CCCCCCCC=C NLDGJRWPPOSWLC-UHFFFAOYSA-N 0.000 description 2
- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 description 2
- PYGSKMBEVAICCR-UHFFFAOYSA-N hexa-1,5-diene Chemical compound C=CCCC=C PYGSKMBEVAICCR-UHFFFAOYSA-N 0.000 description 2
- 229960001545 hydrotalcite Drugs 0.000 description 2
- 229910001701 hydrotalcite Inorganic materials 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- VJHGSLHHMIELQD-UHFFFAOYSA-N nona-1,8-diene Chemical compound C=CCCCCCC=C VJHGSLHHMIELQD-UHFFFAOYSA-N 0.000 description 2
- 239000012744 reinforcing agent Substances 0.000 description 2
- 239000012745 toughening agent Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000004205 dimethyl polysiloxane Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- GEAWFZNTIFJMHR-UHFFFAOYSA-N hepta-1,6-diene Chemical compound C=CCCCC=C GEAWFZNTIFJMHR-UHFFFAOYSA-N 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 229920001911 maleic anhydride grafted polypropylene Polymers 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000012360 testing method Methods 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
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
- C08J3/22—Compounding polymers with additives, e.g. colouring using masterbatch techniques
- C08J3/226—Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
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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
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/04—Homopolymers or copolymers of ethene
- C08J2323/06—Polyethene
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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
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/10—Homopolymers or copolymers of propene
- C08J2323/12—Polypropene
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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
- C08J2483/00—Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen, or carbon only; Derivatives of such polymers
- C08J2483/10—Block- or graft-copolymers containing polysiloxane sequences
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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Abstract
Description
技术领域Technical Field
本发明属于功能聚合物材料技术领域,具体涉及一种抗老化增韧增强聚烯烃塑料及其制备方法。The invention belongs to the technical field of functional polymer materials, and in particular relates to an anti-aging toughened and reinforced polyolefin plastic and a preparation method thereof.
背景技术Background technique
聚烯烃(PO)材料是指以由一种或几种烯烃聚合或共聚制得的聚合物为基材的材料,它主要包括聚乙烯(PE)、聚丙烯(PP)和聚烯烃弹性体(POE)、乙烯-醋酸乙烯共聚物(EVA)等。是一类产量最大、应用最多的高分子材料;其中以PE、PP最为重要。由于原料丰富、价格低廉、容易加工成型、综合性能优良等特点,在现实生活中应用最为广泛。Polyolefin (PO) materials refer to materials based on polymers obtained by polymerization or copolymerization of one or more olefins, which mainly include polyethylene (PE), polypropylene (PP), polyolefin elastomer (POE), ethylene-vinyl acetate copolymer (EVA), etc. It is a type of polymer material with the largest output and the most applications; among them, PE and PP are the most important. Due to the characteristics of abundant raw materials, low price, easy processing and molding, and excellent comprehensive performance, it is the most widely used in real life.
但常规的聚烯烃材料普遍存在耐高温性和耐候性较差的缺陷,长期使用易老化、易变形,通过改性可降低其缺陷。专利CN 112341689 B公开了一种耐热老化的聚乙烯复合材料,包含如下组分:聚乙烯、交联剂、抗氧剂、聚乙烯蜡、轻质碳酸钙、水滑石。该聚乙烯复合材料以聚乙烯为基础,在其中添加一定量的聚乙烯蜡、轻质碳酸钙、水滑石和交联剂和抗氧剂,利用各成分的相互作用提高了聚乙烯复合材料的热稳定性,使其可长时间在高于100℃的环境中工作。但过高含量无机材料的加入会降低聚乙烯材料的强度及韧性。专利CN114933756 B公开了一种耐老化聚乙烯材料,包括以下重量份的原料:90-110份聚乙烯、10-20份马来酸酐接枝聚乙烯以及5-10份有机-无机复合剂,所述有机-无机复合剂为钛酸酯-有机硅组合物修饰的抗紫外线金属氧化物。该专利主要利用钛酸酯-有机硅组合物修饰的抗紫外线金属氧化物对紫外线具备更为优良的屏蔽效果和吸收效果,从而有效提高聚乙烯的抗紫外老化性能。对聚乙烯材料的力学性能及热氧老化性能方面的改善作用有限。However, conventional polyolefin materials generally have the defects of poor high temperature resistance and weather resistance, and are prone to aging and deformation after long-term use. These defects can be reduced by modification. Patent CN 112341689 B discloses a heat-resistant polyethylene composite material, comprising the following components: polyethylene, a cross-linking agent, an antioxidant, polyethylene wax, light calcium carbonate, and hydrotalcite. The polyethylene composite material is based on polyethylene, to which a certain amount of polyethylene wax, light calcium carbonate, hydrotalcite, a cross-linking agent, and an antioxidant are added. The thermal stability of the polyethylene composite material is improved by the interaction of the components, so that it can work in an environment above 100°C for a long time. However, the addition of too high a content of inorganic materials will reduce the strength and toughness of the polyethylene material. Patent CN114933756 B discloses an aging-resistant polyethylene material, comprising the following raw materials by weight: 90-110 parts of polyethylene, 10-20 parts of maleic anhydride grafted polyethylene, and 5-10 parts of an organic-inorganic composite agent, wherein the organic-inorganic composite agent is an anti-ultraviolet metal oxide modified by a titanate-organosilicon composition. This patent mainly uses the anti-ultraviolet metal oxide modified by titanate-organic silicon composition to have better shielding and absorption effect on ultraviolet rays, thereby effectively improving the anti-ultraviolet aging performance of polyethylene. The improvement effect on the mechanical properties and thermal oxidation aging performance of polyethylene materials is limited.
另外,聚烯烃材料还存在韧性稍差的缺陷,通过添加相应的增韧剂可以改善聚烯烃材料韧性,常用的增韧剂有马来酸酐接枝聚乙烯/聚丙烯(PE/PP-g-MAH),但聚烯烃材料因缺少与马来酸酐进行反应的活性基团而无法形成弹性体部分,导致增韧效果稍差,另外PE/PP-g-MAH对聚烯烃材料耐老化性能的改善作用也非常有限。In addition, polyolefin materials also have the defect of slightly poor toughness. The toughness of polyolefin materials can be improved by adding corresponding toughening agents. Commonly used toughening agents include maleic anhydride grafted polyethylene/polypropylene (PE/PP-g-MAH). However, polyolefin materials cannot form an elastomer part due to the lack of active groups that react with maleic anhydride, resulting in slightly poor toughening effect. In addition, the effect of PE/PP-g-MAH on improving the aging resistance of polyolefin materials is also very limited.
因此,提供一种能够同时提升力学性能、耐高温老化和光老化性能,以拓宽其应用场景及耐用性的聚烯烃材料具有显著的研究价值和商业价值。Therefore, providing a polyolefin material that can simultaneously improve mechanical properties, high temperature aging resistance and light aging performance to broaden its application scenarios and durability has significant research value and commercial value.
发明内容Summary of the invention
针对以上现有技术存在的缺点和不足之处,本发明的首要目的在于提供一种抗老化增韧增强聚烯烃塑料的制备方法。In view of the shortcomings and deficiencies of the above prior art, the primary purpose of the present invention is to provide a method for preparing an anti-aging toughened and reinforced polyolefin plastic.
本发明的另一目的在于提供一种通过上述方法制备得到的抗老化增韧增强聚烯烃塑料。Another object of the present invention is to provide an anti-aging toughened and reinforced polyolefin plastic prepared by the above method.
本发明目的通过以下技术方案实现:The purpose of the present invention is achieved through the following technical solutions:
一种抗老化增韧增强聚烯烃塑料的制备方法,包括如下制备步骤:A method for preparing anti-aging toughened and reinforced polyolefin plastics, comprising the following preparation steps:
(1)将端氢硅油与α,ω-二烯烃按摩尔比为1:2~2.2加入到有机溶剂中搅拌溶解均匀,氮气除氧后加入氯铂酸催化剂,然后升温至70~90℃搅拌反应,反应完成后减压蒸馏去除溶剂,得到烯烃封端改性聚硅氧烷(VPDMS);(1) adding hydrogen-terminated silicone oil and α,ω-diolefin in a molar ratio of 1:2 to 2.2 to an organic solvent and stirring to dissolve uniformly, adding chloroplatinic acid catalyst after nitrogen deoxygenation, and then heating to 70 to 90° C. and stirring to react, and after the reaction is completed, removing the solvent by reduced pressure distillation to obtain olefin-terminated modified polysiloxane (VPDMS);
(2)将聚烯烃(PO)、烯烃封端改性聚硅氧烷(VPDMS)、乙烯基MQ硅树脂(VMQ)和引发剂加入到挤出机中熔融共混反应后挤出造粒,得到抗老化增韧增强母粒;(2) adding polyolefin (PO), olefin-terminated modified polysiloxane (VPDMS), vinyl MQ silicone resin (VMQ) and an initiator into an extruder for melt blending and reaction, and then extruding and granulating to obtain an anti-aging toughening and reinforcing masterbatch;
(3)将步骤(2)所得抗老化增韧增强母粒与聚烯烃基材加入到挤出机中熔融共混挤出造粒,得到抗老化增韧增强聚烯烃塑料。(3) adding the anti-aging toughening and reinforcing masterbatch obtained in step (2) and the polyolefin substrate into an extruder for melt blending and extrusion granulation to obtain an anti-aging toughening and reinforcing polyolefin plastic.
优选地,步骤(1)中所述端氢硅油为重均分子量为1000~20000的端氢硅油,其25℃粘度为10~600mpa.s。Preferably, the hydrogen-terminated silicone oil in step (1) is a hydrogen-terminated silicone oil with a weight average molecular weight of 1000 to 20000 and a viscosity of 10 to 600 mPa.s at 25°C.
优选地,步骤(1)中所述α,ω=-二烯烃为碳原子数≥6的α,ω-二烯烃。如1,5-己二烯、1,6-庚二烯、1,7-辛二烯、1,8-壬二烯、1,9-癸二烯等。本发明通过采用碳原子数≥6的烯烃对聚硅氧烷进行封端改性,以达到增容增塑的效果,可显著提高长链聚硅氧烷与聚烯烃的相容性及改善固态产物的热塑性,从而提高长链聚硅氧烷与聚烯烃材料混合反应的接枝效率,同时烯烃封端改性聚硅氧烷能够与聚烯烃形成弹性体结构,并最终达到显著提高抗老化性及韧性的效果。Preferably, the α,ω=-diolefin in step (1) is an α,ω-diolefin with a carbon number of ≥6. Such as 1,5-hexadiene, 1,6-heptadiene, 1,7-octadiene, 1,8-nonadiene, 1,9-decadiene, etc. The present invention uses an olefin with a carbon number of ≥6 to end-cap and modify the polysiloxane to achieve the effect of volume expansion and plasticization, which can significantly improve the compatibility of long-chain polysiloxane and polyolefin and improve the thermoplasticity of the solid product, thereby improving the grafting efficiency of the mixed reaction of long-chain polysiloxane and polyolefin materials. At the same time, the olefin-end-capped modified polysiloxane can form an elastomeric structure with the polyolefin, and finally achieve the effect of significantly improving the aging resistance and toughness.
优选地,步骤(1)中所述有机溶剂为甲苯、二甲苯、石油醚、异丙醇、丁醇等。Preferably, the organic solvent in step (1) is toluene, xylene, petroleum ether, isopropanol, butanol, etc.
优选地,步骤(2)中所述聚烯烃为聚乙烯(PE)或聚丙烯(PP)。Preferably, the polyolefin in step (2) is polyethylene (PE) or polypropylene (PP).
优选地,步骤(2)中所述乙烯基MQ硅树脂为分子量为3000~8000g/mol,乙烯基含量为0.5~3.0wt%的乙烯基MQ硅树脂。其可通过商业购买得到,可采用溶剂型液体乙烯基MQ硅树脂或粉体乙烯基MQ硅树脂,如湖北新四海化工股份有限公司的5202P乙烯基VMQ树脂、5202S乙烯基VMQ树脂、5202N乙烯基VMQ树脂等。本发明采用乙烯基MQ硅树脂作为补强剂,可显著提高所得聚烯烃塑料的强度。并进一步在烯烃封端改性聚硅氧烷的增容作用下,其补强效果更为显著。Preferably, the vinyl MQ silicone resin in step (2) is a vinyl MQ silicone resin with a molecular weight of 3000-8000 g/mol and a vinyl content of 0.5-3.0 wt%. It can be purchased commercially, and solvent-based liquid vinyl MQ silicone resin or powdered vinyl MQ silicone resin can be used, such as 5202P vinyl VMQ resin, 5202S vinyl VMQ resin, 5202N vinyl VMQ resin, etc. of Hubei Xinsihai Chemical Co., Ltd. The present invention uses vinyl MQ silicone resin as a reinforcing agent, which can significantly improve the strength of the obtained polyolefin plastic. And further, under the compatibilization effect of olefin-terminated modified polysiloxane, its reinforcing effect is more significant.
优选地,步骤(2)中所述聚烯烃、烯烃封端改性聚硅氧烷、乙烯基MQ硅树脂加入的质量比为100:2~10:2~10。Preferably, in step (2), the mass ratio of the polyolefin, olefin-terminated modified polysiloxane and vinyl MQ silicone resin added is 100:2-10:2-10.
优选地,步骤(2)中所述引发剂为过氧化二异丙苯(DCP)、过氧化苯甲酰(BPO)或偶氮二异丁腈(AIBN);引发剂的加入量为聚烯烃质量的0.1%~0.5%。Preferably, the initiator in step (2) is dicumyl peroxide (DCP), benzoyl peroxide (BPO) or azobisisobutyronitrile (AIBN); the amount of the initiator added is 0.1% to 0.5% of the mass of the polyolefin.
优选地,步骤(2)中所述熔融共混反应的温度为180~220℃,时间为15~90min。Preferably, the temperature of the melt blending reaction in step (2) is 180 to 220° C., and the time is 15 to 90 minutes.
优选地,步骤(3)中所述聚烯烃基材为聚乙烯(PE)、聚丙烯(PP)、聚烯烃弹性体(POE)或乙烯-醋酸乙烯共聚物(EVA)。Preferably, the polyolefin substrate in step (3) is polyethylene (PE), polypropylene (PP), polyolefin elastomer (POE) or ethylene-vinyl acetate copolymer (EVA).
优选地,步骤(3)中所述抗老化增韧增强母粒的加入量为聚烯烃基材质量的5%~15%。Preferably, the amount of the anti-aging toughening and reinforcing masterbatch added in step (3) is 5% to 15% of the mass of the polyolefin substrate.
一种抗老化增韧增强聚烯烃塑料,通过上述方法制备得到。An anti-aging toughened and reinforced polyolefin plastic is prepared by the method.
与现有技术相比,本发明的有益效果是:Compared with the prior art, the present invention has the following beneficial effects:
(1)本发明通过烯烃封端改性聚硅氧烷与聚烯烃进行接枝共聚反应制备抗老化增韧增强母粒,可在聚烯烃基材中引入化学接枝的长链聚硅氧烷,并可形成弹性体结构,显著提高聚烯烃塑料的耐老化性能和韧性。(1) The present invention prepares an anti-aging toughening and reinforcing masterbatch by grafting copolymerization of olefin-terminated modified polysiloxane with polyolefin, which can introduce chemically grafted long-chain polysiloxane into the polyolefin matrix and form an elastomeric structure, thereby significantly improving the aging resistance and toughness of polyolefin plastics.
(2)本发明通过引入乙烯基MQ硅树脂,并通过烯烃封端改性聚硅氧烷的增容作用,可在聚烯烃基材中形成交联网络,达到补强效果,显著提高所得聚烯烃塑料的强度。(2) The present invention can form a cross-linked network in the polyolefin substrate by introducing vinyl MQ silicone resin and using the compatibilizing effect of olefin-terminated modified polysiloxane to achieve a reinforcing effect and significantly improve the strength of the obtained polyolefin plastic.
具体实施方式Detailed ways
下面结合实施例对本发明作进一步详细的描述,但本发明的实施方式不限于此。The present invention is further described in detail below with reference to examples, but the embodiments of the present invention are not limited thereto.
实施例1Example 1
一种抗老化增韧增强聚烯烃塑料的制备方法,包括如下制备步骤:A method for preparing anti-aging toughened and reinforced polyolefin plastics, comprising the following preparation steps:
(1)将端氢硅油(市购,平均分子量为6000,H含量0.032%,25℃粘度为100mpa.s)与1,7-辛二烯按摩尔比为1:2.1加入到甲苯溶剂中搅拌溶解均匀,氮气除氧后加入氯铂酸催化剂溶液,然后升温至80℃搅拌反应5h,检测H含量反应完全后减压蒸馏去除溶剂及未反应原料,得到淡黄色粘稠液体状辛烯封端改性聚硅氧烷(VPDMS),测定产物烯基含量(以CH2=CH-计)为0.92wt.%。(1) Hydrogen-terminated silicone oil (commercially available, with an average molecular weight of 6000, a H content of 0.032%, and a viscosity of 100 mPa.s at 25°C) and 1,7-octadiene in a molar ratio of 1:2.1 were added to a toluene solvent and stirred to dissolve evenly. After nitrogen deoxygenation, a chloroplatinic acid catalyst solution was added, and then the temperature was raised to 80°C and stirred to react for 5 h. The H content was detected. After the reaction was complete, the solvent and unreacted raw materials were removed by reduced pressure distillation to obtain a light yellow viscous liquid octene-terminated modified polysiloxane (VPDMS). The alkenyl content of the product (in terms of CH2 =CH-) was measured to be 0.92 wt.%.
(2)将低密度聚乙烯(LDPE)、辛烯封端改性聚硅氧烷(VPDMS)、粉末乙烯基MQ硅树脂(5202P乙烯基VMQ树脂,分子量5150g/mol,乙烯基含量1.07wt%)和引发剂过氧化二异丙苯(DCP)加入到双螺杆挤出机中熔融共混反应后挤出造粒,得到抗老化增韧增强母粒。其中LDPE、VPDMS、VMQ加入的质量比为100:5:5,DCP的加入量为LDPE质量的0.4%。双螺杆挤出机中从喂料口至出口各区段温度分别控制为180℃、180℃、190℃、210℃、200℃和180℃,控制喂料转速使熔融共混反应控制为60min。(2) Low-density polyethylene (LDPE), octene-terminated modified polysiloxane (VPDMS), powdered vinyl MQ silicone resin (5202P vinyl VMQ resin, molecular weight 5150 g/mol, vinyl content 1.07 wt%) and initiator diisopropylbenzene peroxide (DCP) were added to a twin-screw extruder for melt blending reaction and extrusion granulation to obtain an anti-aging toughening and reinforcing masterbatch. The mass ratio of LDPE, VPDMS and VMQ added was 100:5:5, and the amount of DCP added was 0.4% of the mass of LDPE. The temperatures of each section from the feed port to the outlet of the twin-screw extruder were controlled to 180°C, 180°C, 190°C, 210°C, 200°C and 180°C, respectively, and the feed speed was controlled to control the melt blending reaction to 60 minutes.
(3)将步骤(2)所得抗老化增韧增强母粒与高密度聚乙烯(HDPE)加入到双螺杆挤出机中熔融共混挤出造粒,抗老化增韧增强母粒的加入量为HDPE质量的10%,双螺杆挤出机中从喂料口至出口各区段温度分别控制为170℃、170℃、185℃、200℃、180℃和175℃,得到抗老化增韧增强聚乙烯塑料。(3) adding the anti-aging toughening and reinforcing masterbatch obtained in step (2) and high-density polyethylene (HDPE) into a twin-screw extruder for melt blending and extrusion granulation, wherein the amount of the anti-aging toughening and reinforcing masterbatch added is 10% of the mass of HDPE, and the temperatures of each section from the feed port to the outlet of the twin-screw extruder are respectively controlled to be 170° C., 170° C., 185° C., 200° C., 180° C. and 175° C. to obtain an anti-aging toughening and reinforced polyethylene plastic.
对本实施例所得聚乙烯塑料的拉伸强度(GB/T 1040-2018)、冲击强度(GB/T1843-2008)、抗热老化性能(GB/T 7141-2008,热老化条件为135℃,168h;然后测试拉伸强度保持率(老化后拉伸强度/老化前拉伸强度×100%)和冲击强度保持率(老化后冲击强度/老化前冲击强度×100%))、抗紫外老化性能(GB/T16422.3-2022,UVA-340(1A型)荧光紫外灯,按方法A的人工加速气候老化条件进行5个暴露循环;然后测试拉伸强度保持率和冲击强度保持率)。并以等量马来酸酐接枝聚乙烯(PE-g-MAH)替代VPDMS制备的聚乙烯作为对照组。The tensile strength (GB/T 1040-2018), impact strength (GB/T1843-2008), heat aging resistance (GB/T 7141-2008, heat aging conditions are 135°C, 168h; then the tensile strength retention (tensile strength after aging/tensile strength before aging × 100%) and impact strength retention (impact strength after aging/impact strength before aging × 100%)) of the polyethylene plastic obtained in this example are tested, and the ultraviolet aging resistance (GB/T16422.3-2022, UVA-340 (1A type) fluorescent ultraviolet lamp, 5 exposure cycles according to the artificial accelerated climate aging conditions of method A; then the tensile strength retention and impact strength retention are tested). The polyethylene prepared by replacing VPDMS with an equal amount of maleic anhydride grafted polyethylene (PE-g-MAH) is used as a control group.
测试结果显示本实施例所得聚乙烯塑料的拉伸强度为65.2MPa,冲击强度为77.9KJ/m2;热老化拉伸强度保持率为93.2%,冲击强度保持率为95.1%;紫外老化拉伸强度保持率为94.5%,冲击强度保持率为92.8%。而采用PE-g-MAH制备的聚乙烯塑料拉伸强度为62.6MPa,冲击强度为68.4KJ/m2;热老化拉伸强度保持率为82.6%,冲击强度保持率为79.8%;紫外老化拉伸强度保持率为81.2%,冲击强度保持率为85.0%。The test results show that the tensile strength of the polyethylene plastic obtained in this embodiment is 65.2MPa, and the impact strength is 77.9KJ/ m2 ; the tensile strength retention rate after heat aging is 93.2%, and the impact strength retention rate is 95.1%; the tensile strength retention rate after ultraviolet aging is 94.5%, and the impact strength retention rate is 92.8%. The polyethylene plastic prepared by PE-g-MAH has a tensile strength of 62.6MPa and an impact strength of 68.4KJ/ m2 ; the tensile strength retention rate after heat aging is 82.6%, and the impact strength retention rate is 79.8%; the tensile strength retention rate after ultraviolet aging is 81.2%, and the impact strength retention rate is 85.0%.
实施例2Example 2
一种抗老化增韧增强聚烯烃塑料的制备方法,包括如下制备步骤:A method for preparing anti-aging toughened and reinforced polyolefin plastics, comprising the following preparation steps:
(1)将端氢硅油(市购,平均分子量为18000,H含量0.011%,25℃粘度为500mpa.s)与1,9-癸二烯按摩尔比为1:2.0加入到甲苯溶剂中搅拌溶解均匀,氮气除氧后加入氯铂酸催化剂溶液,然后升温至90℃搅拌反应4h,检测H含量反应完全后减压蒸馏去除溶剂及未反应原料,得到白色固体状癸烯封端改性聚硅氧烷(VPDMS),测定产物烯基含量为0.30wt.%。(1) Hydrogen-terminated silicone oil (commercially available, with an average molecular weight of 18,000, a H content of 0.011%, and a viscosity of 500 mPa.s at 25°C) and 1,9-decadiene were added to a toluene solvent at a molar ratio of 1:2.0 and stirred to dissolve evenly. After nitrogen deoxygenation, a chloroplatinic acid catalyst solution was added, and then the temperature was raised to 90°C and stirred to react for 4 hours. The H content was detected. After the reaction was complete, the solvent and unreacted raw materials were removed by reduced pressure distillation to obtain a white solid decene-terminated modified polysiloxane (VPDMS). The alkenyl content of the product was measured to be 0.30 wt.%.
(2)将聚丙烯(PP)、癸烯封端改性聚硅氧烷(VPDMS)、粉末乙烯基MQ硅树脂(5202P乙烯基VMQ树脂,分子量5150g/mol,乙烯基含量1.07wt%)和引发剂过氧化苯甲酰(BPO)加入到双螺杆挤出机中熔融共混反应后挤出造粒,得到抗老化增韧增强母粒。其中PP、VPDMS、VMQ加入的质量比为100:2:2,BPO的加入量为PP质量的0.4%。双螺杆挤出机中从喂料口至出口各区段温度分别控制为180℃、180℃、190℃、210℃、200℃和180℃,控制喂料转速使熔融共混反应控制为60min。(2) Polypropylene (PP), decene-terminated modified polysiloxane (VPDMS), powdered vinyl MQ silicone resin (5202P vinyl VMQ resin, molecular weight 5150 g/mol, vinyl content 1.07 wt%) and initiator benzoyl peroxide (BPO) were added to a twin-screw extruder for melt blending reaction and extrusion granulation to obtain an anti-aging toughening and reinforcing masterbatch. The mass ratio of PP, VPDMS and VMQ added was 100:2:2, and the amount of BPO added was 0.4% of the mass of PP. The temperatures of each section from the feed port to the outlet of the twin-screw extruder were controlled to 180°C, 180°C, 190°C, 210°C, 200°C and 180°C, respectively, and the feed speed was controlled to control the melt blending reaction to 60 min.
(3)将步骤(2)所得抗老化增韧增强母粒与聚丙烯(PP)加入到双螺杆挤出机中熔融共混挤出造粒,抗老化增韧增强母粒的加入量为PP质量的15%,双螺杆挤出机中从喂料口至出口各区段温度分别控制为170℃、170℃、185℃、200℃、180℃和175℃,得到抗老化增韧增强聚丙烯塑料。(3) adding the anti-aging toughening and reinforcing masterbatch obtained in step (2) and polypropylene (PP) into a twin-screw extruder for melt blending and extrusion granulation, wherein the amount of the anti-aging toughening and reinforcing masterbatch added is 15% of the mass of PP, and the temperature of each section from the feed port to the outlet of the twin-screw extruder is controlled to be 170° C., 170° C., 185° C., 200° C., 180° C. and 175° C., respectively, to obtain an anti-aging toughening and reinforced polypropylene plastic.
本实施例所得聚丙烯塑料的拉伸强度为73.8MPa,冲击强度为60.2KJ/m2;热老化拉伸强度保持率为92.5%,冲击强度保持率为92.4%;紫外老化拉伸强度保持率为92.8%,冲击强度保持率为90.3%。而采用等量PP-g-MAH替代VPDMS制备的聚丙烯塑料拉伸强度为69.4MPa,冲击强度为48.7KJ/m2;热老化拉伸强度保持率为81.7%,冲击强度保持率为82.5%;紫外老化拉伸强度保持率为74.6%,冲击强度保持率为69.2%。The tensile strength of the polypropylene plastic obtained in this embodiment is 73.8MPa, and the impact strength is 60.2KJ/ m2 ; the tensile strength retention rate after heat aging is 92.5%, and the impact strength retention rate is 92.4%; the tensile strength retention rate after ultraviolet aging is 92.8%, and the impact strength retention rate is 90.3%. The tensile strength of the polypropylene plastic prepared by replacing VPDMS with the same amount of PP-g-MAH is 69.4MPa, and the impact strength is 48.7KJ/ m2 ; the tensile strength retention rate after heat aging is 81.7%, and the impact strength retention rate is 82.5%; the tensile strength retention rate after ultraviolet aging is 74.6%, and the impact strength retention rate is 69.2%.
实施例3Example 3
一种抗老化增韧增强聚烯烃塑料的制备方法,包括如下制备步骤:A method for preparing anti-aging toughened and reinforced polyolefin plastics, comprising the following preparation steps:
(1)将端氢硅油(市购,平均分子量为1000,H含量0.203%,25℃粘度为10mpa.s)与1,5-己二烯按摩尔比为1:2.2加入到甲苯溶剂中搅拌溶解均匀,氮气除氧后加入氯铂酸催化剂溶液,然后升温至70℃搅拌反应6h,检测H含量反应完全后减压蒸馏去除溶剂及未反应原料,得到淡黄色液体状己烯封端改性聚硅氧烷(VPDMS),测定产物烯基含量为4.76wt.%。(1) Hydrogen-terminated silicone oil (commercially available, with an average molecular weight of 1000, a H content of 0.203%, and a viscosity of 10 mPa.s at 25°C) and 1,5-hexadiene in a molar ratio of 1:2.2 were added to a toluene solvent and stirred to dissolve evenly. After nitrogen deoxygenation, a chloroplatinic acid catalyst solution was added, and then the temperature was raised to 70°C and stirred for reaction for 6 h. The H content was detected. After the reaction was complete, the solvent and unreacted raw materials were removed by reduced pressure distillation to obtain a light yellow liquid hexene-terminated modified polysiloxane (VPDMS). The alkenyl content of the product was measured to be 4.76 wt.%.
(2)将低密度聚乙烯(LDPE)、己烯封端改性聚硅氧烷(VPDMS)、粉末乙烯基MQ硅树脂(5202P乙烯基VMQ树脂,分子量3200g/mol,乙烯基含量1.12wt%)和引发剂过氧化二异丙苯(DCP)加入到双螺杆挤出机中熔融共混反应后挤出造粒,得到抗老化增韧增强母粒。其中PE、VPDMS、VMQ加入的质量比为100:10:10,DCP的加入量为LDPE质量的0.5%。双螺杆挤出机中从喂料口至出口各区段温度分别控制为180℃、180℃、190℃、210℃、200℃和180℃,控制喂料转速使熔融共混反应控制为60min。(2) Low-density polyethylene (LDPE), hexene-terminated modified polysiloxane (VPDMS), powdered vinyl MQ silicone resin (5202P vinyl VMQ resin, molecular weight 3200 g/mol, vinyl content 1.12 wt%) and initiator diisopropylbenzene peroxide (DCP) were added to a twin-screw extruder for melt blending reaction and extrusion granulation to obtain an anti-aging toughening and reinforcing masterbatch. The mass ratio of PE, VPDMS and VMQ added was 100:10:10, and the amount of DCP added was 0.5% of the mass of LDPE. The temperatures of each section from the feed port to the outlet of the twin-screw extruder were controlled to 180°C, 180°C, 190°C, 210°C, 200°C and 180°C, respectively, and the feed speed was controlled to control the melt blending reaction to 60 min.
(3)将步骤(2)所得抗老化增韧增强母粒与高密度聚乙烯(HDPE)加入到双螺杆挤出机中熔融共混挤出造粒,抗老化增韧增强母粒的加入量为HDPE质量的5%,双螺杆挤出机中从喂料口至出口各区段温度分别控制为170℃、170℃、185℃、200℃、180℃和175℃,得到抗老化增韧增强聚乙烯塑料。(3) adding the anti-aging toughening and reinforcing masterbatch obtained in step (2) and high-density polyethylene (HDPE) into a twin-screw extruder for melt blending and extrusion granulation, wherein the amount of the anti-aging toughening and reinforcing masterbatch added is 5% of the mass of HDPE, and the temperatures of each section from the feed port to the outlet of the twin-screw extruder are respectively controlled to be 170° C., 170° C., 185° C., 200° C., 180° C. and 175° C. to obtain an anti-aging toughening and reinforced polyethylene plastic.
本实施例所得聚乙烯塑料的拉伸强度为57.3MPa,冲击强度为68.6KJ/m2热老化拉伸强度保持率为96.0%,冲击强度保持率为96.7%;紫外老化拉伸强度保持率为95.7%,冲击强度保持率为94.2%。而采用等量PE-g-MAH替代VPDMS制备的聚乙烯塑料拉伸强度为53.1MPa,冲击强度为55.3KJ/m2;热老化拉伸强度保持率为79.3%,冲击强度保持率为80.7%;紫外老化拉伸强度保持率为76.9%,冲击强度保持率为79.2%。The tensile strength of the polyethylene plastic obtained in this embodiment is 57.3MPa, the impact strength is 68.6KJ/ m2, the heat aging tensile strength retention rate is 96.0%, the impact strength retention rate is 96.7%; the ultraviolet aging tensile strength retention rate is 95.7%, and the impact strength retention rate is 94.2%. The polyethylene plastic prepared by replacing VPDMS with an equal amount of PE-g-MAH has a tensile strength of 53.1MPa and an impact strength of 55.3KJ/ m2 ; the heat aging tensile strength retention rate is 79.3%, the impact strength retention rate is 80.7%; the ultraviolet aging tensile strength retention rate is 76.9%, and the impact strength retention rate is 79.2%.
通过以上实施例1~3的结果可以看出,本发明采用VPDMS和VMQ对聚烯烃塑料进行化学接枝及共混改性,相比PE/PP-g-MAH和VMQ改性,可以显著提高聚乙烯塑料的抗热老化性能和抗紫外老化性能,同时对材料的韧性改善作用更为显著。另外在VPDMS的增容作用下,VMQ的补强效果更为显著。From the results of Examples 1 to 3 above, it can be seen that the present invention uses VPDMS and VMQ to chemically graft and blend polyolefin plastics, which can significantly improve the heat aging resistance and UV aging resistance of polyethylene plastics compared to PE/PP-g-MAH and VMQ modification, and at the same time, the toughness improvement effect of the material is more significant. In addition, under the volume expansion effect of VPDMS, the reinforcement effect of VMQ is more significant.
对比例1Comparative Example 1
本对比例与实施例1相比,未加入VMQ,采用等量VPDMS替代(即抗老化增韧增强母粒中LDPE、VPDMS加入的质量比为100:10),其余相同。Compared with Example 1, this comparative example does not add VMQ, but uses an equal amount of VPDMS instead (that is, the mass ratio of LDPE and VPDMS added to the anti-aging toughening and reinforcing masterbatch is 100:10), and the rest is the same.
本实施例所得聚乙烯塑料的拉伸强度为46.5MPa,冲击强度为70.2KJ/m2;热老化拉伸强度保持率为88.5%,冲击强度保持率为87.8%;紫外老化拉伸强度保持率为90.1%,冲击强度保持率为89.6%。The polyethylene plastic obtained in this example has a tensile strength of 46.5 MPa and an impact strength of 70.2 KJ/m 2 ; a heat aging tensile strength retention rate of 88.5% and an impact strength retention rate of 87.8%; a UV aging tensile strength retention rate of 90.1% and an impact strength retention rate of 89.6%.
通过本对比例与实施例1的比较结果可以看出,本发明通过引入VMQ作为补强剂,可以显著提高聚烯烃材料的力学强度,并对材料的韧性及耐老化性能的提升具有一定的协同作用。By comparing the results of this comparative example with Example 1, it can be seen that the present invention can significantly improve the mechanical strength of polyolefin materials by introducing VMQ as a reinforcing agent, and has a certain synergistic effect on improving the toughness and aging resistance of the material.
对比例2Comparative Example 2
本对比例与实施例1相比,辛烯封端改性聚硅氧烷(VPDMS)在步骤(3)中加入,具体制备步骤如下:Compared with Example 1, in this comparative example, octene-terminated modified polysiloxane (VPDMS) is added in step (3), and the specific preparation steps are as follows:
步骤(1)同实施例1。Step (1) is the same as in Example 1.
(2)将低密度聚乙烯(LDPE)、粉末乙烯基MQ硅树脂(5202P乙烯基VMQ树脂,分子量5150g/mol,乙烯基含量1.07wt%)和引发剂过氧化二异丙苯(DCP)加入到双螺杆挤出机中熔融共混反应后挤出造粒,得到增强母粒。其中LDPE、VMQ加入的质量比为100:5,DCP的加入量为LDPE质量的0.4%。双螺杆挤出机中从喂料口至出口各区段温度分别控制为180℃、180℃、190℃、210℃、200℃和180℃,控制喂料转速使熔融共混反应控制为60min。(2) Low density polyethylene (LDPE), powdered vinyl MQ silicone resin (5202P vinyl VMQ resin, molecular weight 5150 g/mol, vinyl content 1.07 wt%) and initiator diisopropylbenzene peroxide (DCP) were added to a twin-screw extruder for melt blending reaction and extrusion granulation to obtain a reinforced masterbatch. The mass ratio of LDPE and VMQ added was 100:5, and the amount of DCP added was 0.4% of the mass of LDPE. The temperature of each section from the feed port to the outlet of the twin-screw extruder was controlled to 180°C, 180°C, 190°C, 210°C, 200°C and 180°C, respectively, and the feed speed was controlled to control the melt blending reaction to 60 minutes.
(3)将步骤(2)所得增强母粒与步骤(1)所得辛烯封端改性聚硅氧烷(VPDMS)和高密度聚乙烯(HDPE)加入到双螺杆挤出机中熔融共混挤出造粒,VPDMS的加入量为增强母粒质量的5%,增强母粒的加入量为HDPE质量的10%,双螺杆挤出机中从喂料口至出口各区段温度分别控制为170℃、170℃、185℃、200℃、180℃和175℃,得到增强聚乙烯塑料。(3) adding the reinforcing masterbatch obtained in step (2), the octene-terminated modified polysiloxane (VPDMS) obtained in step (1) and high-density polyethylene (HDPE) into a twin-screw extruder for melt blending and extrusion granulation, wherein the amount of VPDMS added is 5% of the mass of the reinforcing masterbatch, and the amount of the reinforcing masterbatch added is 10% of the mass of the HDPE. The temperatures of the sections from the feed port to the outlet of the twin-screw extruder are respectively controlled to be 170° C., 170° C., 185° C., 200° C., 180° C. and 175° C. to obtain a reinforced polyethylene plastic.
本对比例所得聚乙烯塑料的拉伸强度为61.7MPa,冲击强度为64.5KJ/m2;热老化拉伸强度保持率为85.1%,冲击强度保持率为83.8%;紫外老化拉伸强度保持率为84.3%,冲击强度保持率为87.4%。The polyethylene plastic obtained in this comparative example has a tensile strength of 61.7 MPa and an impact strength of 64.5 KJ/m 2 ; the heat aging tensile strength retention rate is 85.1%, and the impact strength retention rate is 83.8%; the UV aging tensile strength retention rate is 84.3%, and the impact strength retention rate is 87.4%.
通过本对比例与实施例1的比较结果可以看出,通过预先将VPDMS与聚烯烃材料进行化学接枝反应,并进一步形成交联弹性体结构,可显著提高所得聚烯烃材料的抗老化性能及韧性。且在VPDMS的增容作用下,VMQ的补强效果更为显著。It can be seen from the comparison between this comparative example and Example 1 that by chemically grafting VPDMS with polyolefin materials in advance and further forming a cross-linked elastic structure, the anti-aging performance and toughness of the obtained polyolefin materials can be significantly improved. Moreover, under the volume expansion effect of VPDMS, the reinforcement effect of VMQ is more significant.
对比例3Comparative Example 3
本对比例与实施例1相比,粉末乙烯基MQ硅树脂(VMQ)在步骤(3)中加入,具体制备步骤如下:Compared with Example 1, powdered vinyl MQ silicone resin (VMQ) is added in step (3) in this comparative example. The specific preparation steps are as follows:
步骤(1)同实施例1。Step (1) is the same as in Example 1.
(2)将低密度聚乙烯(LDPE)、辛烯封端改性聚硅氧烷(VPDMS)和引发剂过氧化二异丙苯(DCP)加入到双螺杆挤出机中熔融共混反应后挤出造粒,得到抗老化增韧增强母粒。其中LDPE、VPDMS加入的质量比为100:5,DCP的加入量为LDPE质量的0.4%。双螺杆挤出机中从喂料口至出口各区段温度分别控制为180℃、180℃、190℃、210℃、200℃和180℃,控制喂料转速使熔融共混反应控制为60min。(2) Low-density polyethylene (LDPE), octene-terminated modified polysiloxane (VPDMS) and initiator diisopropylbenzene peroxide (DCP) were added to a twin-screw extruder for melt blending and reaction, and then extruded and granulated to obtain an anti-aging toughening and reinforcing masterbatch. The mass ratio of LDPE and VPDMS added was 100:5, and the amount of DCP added was 0.4% of the mass of LDPE. The temperatures of each section from the feed port to the outlet of the twin-screw extruder were controlled to 180°C, 180°C, 190°C, 210°C, 200°C and 180°C, respectively, and the feed speed was controlled to control the melt blending reaction to 60 minutes.
(3)将步骤(2)所得抗老化增韧增强母粒与粉末乙烯基MQ硅树脂(5202P乙烯基VMQ树脂,分子量5150g/mol,乙烯基含量1.07wt%)和高密度聚乙烯(HDPE)加入到双螺杆挤出机中熔融共混挤出造粒,VMQ的加入量为抗老化增韧增强母粒质量的5%,抗老化增韧增强母粒的加入量为HDPE质量的10%,双螺杆挤出机中从喂料口至出口各区段温度分别控制为170℃、170℃、185℃、200℃、180℃和175℃,得到增强聚乙烯塑料。(3) The anti-aging toughening and reinforcing masterbatch obtained in step (2) is added to a twin-screw extruder for melt blending and extrusion granulation, wherein the amount of VMQ added is 5% of the mass of the anti-aging toughening and reinforcing masterbatch, and the amount of the anti-aging toughening and reinforcing masterbatch added is 10% of the mass of HDPE. The temperatures of each section from the feed port to the outlet of the twin-screw extruder are respectively controlled to 170° C., 170° C., 185° C., 200° C., 180° C. and 175° C. to obtain a reinforced polyethylene plastic.
本对比例所得聚乙烯塑料的拉伸强度为53.8MPa,冲击强度为69.0KJ/m2;热老化拉伸强度保持率为90.6%,冲击强度保持率为91.4%;紫外老化拉伸强度保持率为92.2%,冲击强度保持率为89.5%。The polyethylene plastic obtained in this comparative example has a tensile strength of 53.8 MPa and an impact strength of 69.0 KJ/m 2 ; the heat aging tensile strength retention rate is 90.6%, and the impact strength retention rate is 91.4%; the UV aging tensile strength retention rate is 92.2%, and the impact strength retention rate is 89.5%.
通过本对比例与实施例1的比较结果可以看出,通过预先将VMQ在VPDMS增容作用下与聚烯烃材料进行化学接枝反应,可显著提高VMQ的补强效果。It can be seen from the comparison results of this comparative example and Example 1 that the reinforcement effect of VMQ can be significantly improved by chemically grafting VMQ with polyolefin materials under the compatibilization effect of VPDMS in advance.
对比例4Comparative Example 4
本对比例与实施例1相比,采用乙烯基含量相同的端乙烯基聚二甲基硅氧烷(市购,平均分子量为6000,乙烯基含量为0.92wt.%,25℃粘度为100mpa.s)替代辛烯封端改性聚硅氧烷(VPDMS),其余相同。Compared with Example 1, this comparative example uses vinyl-terminated polydimethylsiloxane with the same vinyl content (commercially available, with an average molecular weight of 6000, a vinyl content of 0.92wt.%, and a viscosity of 100mPa.s at 25°C) to replace octene-terminated modified polysiloxane (VPDMS), and the rest is the same.
本对比例所得聚乙烯塑料的拉伸强度为62.1MPa,冲击强度为60.3KJ/m2;热老化拉伸强度保持率为84.7%,冲击强度保持率为84.5%;紫外老化拉伸强度保持率为85.6%,冲击强度保持率为88.2%。The polyethylene plastic obtained in this comparative example has a tensile strength of 62.1 MPa and an impact strength of 60.3 KJ/m 2 ; the heat aging tensile strength retention rate is 84.7%, and the impact strength retention rate is 84.5%; the UV aging tensile strength retention rate is 85.6%, and the impact strength retention rate is 88.2%.
通过本对比例与实施例1的比较结果可以看出,用于接枝改性的VPDMS中碳链过短,其与聚烯烃的相容性较差,同时对VMQ的增容效果也较差,导致所得聚烯烃材料的力学性能和抗老化性能均出现明显的降低。By comparing the results of this comparative example with Example 1, it can be seen that the carbon chain in the VPDMS used for grafting modification is too short, and its compatibility with polyolefins is poor. At the same time, the volume expansion effect on VMQ is also poor, resulting in a significant decrease in the mechanical properties and anti-aging properties of the obtained polyolefin material.
上述实施例为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其它的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。The above embodiments are preferred implementation modes of the present invention, but the implementation modes of the present invention are not limited to the above embodiments. Any other changes, modifications, substitutions, combinations, and simplifications that do not deviate from the spirit and principles of the present invention should be equivalent replacement methods and are included in the protection scope of the present invention.
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Effective date of registration: 20240923 Address after: Room 101-301, Building 10, Block B, Wanyang Zhongchuang City, No.1 Shuangyang Road, Yangqiao Town, Boluo County, Huizhou City, Guangdong Province 516000 Applicant after: Guangdong Junmao Plastic Raw Materials Co.,Ltd. Country or region after: China Address before: 516100 Yangqiao Town, Boluo County, Huizhou City, Guangdong Province Shuangyang Road, Wanyang Zhongchuang City Applicant before: Guangdong Jinyuan Plastic Technology Co.,Ltd. Country or region before: China |
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