CN110330594A - Method for modifying polyethylene by crosslinking - Google Patents
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- 239000004698 Polyethylene Substances 0.000 title claims abstract description 93
- 238000004132 cross linking Methods 0.000 title claims abstract description 71
- 238000000034 method Methods 0.000 title claims abstract description 47
- -1 polyethylene Polymers 0.000 title claims abstract description 25
- 229920000573 polyethylene Polymers 0.000 title claims abstract description 21
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 claims abstract description 45
- 229910000077 silane Inorganic materials 0.000 claims abstract description 45
- 239000000463 material Substances 0.000 claims abstract description 16
- 238000012986 modification Methods 0.000 claims abstract description 14
- 230000004048 modification Effects 0.000 claims abstract description 14
- 239000011347 resin Substances 0.000 claims abstract description 12
- 229920005989 resin Polymers 0.000 claims abstract description 12
- 229920000642 polymer Polymers 0.000 claims abstract description 9
- 238000002360 preparation method Methods 0.000 claims abstract description 9
- 239000000126 substance Substances 0.000 claims abstract description 5
- 238000005411 Van der Waals force Methods 0.000 claims abstract description 4
- 239000002131 composite material Substances 0.000 claims abstract description 3
- 239000003963 antioxidant agent Substances 0.000 claims description 17
- 150000002978 peroxides Chemical class 0.000 claims description 15
- 239000003431 cross linking reagent Substances 0.000 claims description 14
- 230000008569 process Effects 0.000 claims description 14
- 239000003999 initiator Substances 0.000 claims description 12
- 239000003054 catalyst Substances 0.000 claims description 11
- 230000003078 antioxidant effect Effects 0.000 claims description 9
- 239000003112 inhibitor Substances 0.000 claims description 9
- 238000006116 polymerization reaction Methods 0.000 claims description 8
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 7
- 229920002521 macromolecule Polymers 0.000 claims description 7
- VSAWBBYYMBQKIK-UHFFFAOYSA-N 4-[[3,5-bis[(3,5-ditert-butyl-4-hydroxyphenyl)methyl]-2,4,6-trimethylphenyl]methyl]-2,6-ditert-butylphenol Chemical group CC1=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C(CC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)C(C)=C1CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 VSAWBBYYMBQKIK-UHFFFAOYSA-N 0.000 claims description 4
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical group CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 claims description 4
- 150000001336 alkenes Chemical class 0.000 claims description 4
- 150000004982 aromatic amines Chemical class 0.000 claims description 4
- 229920001577 copolymer Polymers 0.000 claims description 4
- 239000012975 dibutyltin dilaurate Substances 0.000 claims description 4
- 229920001519 homopolymer Polymers 0.000 claims description 4
- 150000004819 silanols Chemical class 0.000 claims description 4
- 239000003381 stabilizer Substances 0.000 claims description 4
- 230000009471 action Effects 0.000 claims description 3
- 238000007259 addition reaction Methods 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 238000012546 transfer Methods 0.000 claims description 3
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims description 3
- 229920002554 vinyl polymer Polymers 0.000 claims description 3
- 238000001125 extrusion Methods 0.000 abstract description 11
- 238000012545 processing Methods 0.000 abstract description 7
- 229920003020 cross-linked polyethylene Polymers 0.000 abstract description 5
- 239000004703 cross-linked polyethylene Substances 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 4
- 230000032683 aging Effects 0.000 abstract description 2
- 230000005855 radiation Effects 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 10
- 150000003254 radicals Chemical class 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 9
- 238000000354 decomposition reaction Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000007086 side reaction Methods 0.000 description 4
- 239000004594 Masterbatch (MB) Substances 0.000 description 3
- 230000000977 initiatory effect Effects 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 238000002715 modification method Methods 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 150000004756 silanes Chemical class 0.000 description 2
- SCPYDCQAZCOKTP-UHFFFAOYSA-N silanol Chemical compound [SiH3]O SCPYDCQAZCOKTP-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229940123457 Free radical scavenger Drugs 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 206010070834 Sensitisation Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005250 beta ray Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000010894 electron beam technology Methods 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- FWDBOZPQNFPOLF-UHFFFAOYSA-N ethenyl(triethoxy)silane Chemical compound CCO[Si](OCC)(OCC)C=C FWDBOZPQNFPOLF-UHFFFAOYSA-N 0.000 description 1
- NKSJNEHGWDZZQF-UHFFFAOYSA-N ethenyl(trimethoxy)silane Chemical compound CO[Si](OC)(OC)C=C NKSJNEHGWDZZQF-UHFFFAOYSA-N 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 230000005281 excited state Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000005251 gamma ray Effects 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000004719 irradiation crosslinked polyethylene Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000002516 radical scavenger Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000008313 sensitization Effects 0.000 description 1
- 230000001235 sensitizing effect Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 238000004018 waxing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F255/00—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00
- C08F255/02—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Graft Or Block Polymers (AREA)
Abstract
本发明属于材料改性技术领域,公开了一种聚乙烯交联改性的方法,聚乙烯交联改性的方法为PE的硅烷交联法,硅垸交联PE以PE为基础树脂,由硅垸为桥键材料,在聚合物大分子链间形成化学共价键以取代原先的范德华力,使分子构成三维立体网络,硅垸交联PE的制备包含接枝和交联两个阶段。本发明采用硅烷交联的方法,无需高昂的设备投入,可获得较高的挤出速度,并能减少开机阶段产生的废料,其交联的聚乙烯的耐老化能力要优于其他制备方法,技术简单且稳定的硅烷交联方式可以应用于较大范围的复合物加工。
The invention belongs to the technical field of material modification, and discloses a method for crosslinking and modifying polyethylene. The method for crosslinking and modifying polyethylene is the silane crosslinking method of PE. The silane crosslinked PE uses PE as the base resin. Silane is a bridge material, which forms chemical covalent bonds between polymer macromolecular chains to replace the original van der Waals force, making the molecules form a three-dimensional network. The preparation of silane crosslinked PE includes two stages of grafting and crosslinking. The present invention adopts the silane cross-linking method, which does not require expensive equipment investment, can obtain higher extrusion speed, and can reduce the waste generated during the start-up stage, and the aging resistance of the cross-linked polyethylene is better than other preparation methods. The technically simple and stable silane crosslinking method can be applied to a wide range of composite processing.
Description
技术领域technical field
本发明属于材料改性技术领域,尤其涉及一种聚乙烯交联改性的方法。The invention belongs to the technical field of material modification, and in particular relates to a method for cross-linking modification of polyethylene.
背景技术Background technique
目前,业内常用的现有技术是这样的:现代塑料具有非常优异的物理性能,只是受其相对较差的耐热性能的影响,在许多应用领域中使用寿命仍然有限,PE由于其结构特点,不能承受较高的使用温度,加之机械强度较低,限制了它在许多领域的应用。为了改善PE的耐热和力学性能,行之有效的方法是对其进行交联改性。At present, the existing technologies commonly used in the industry are as follows: modern plastics have very excellent physical properties, but are only affected by their relatively poor heat resistance, and their service life is still limited in many application fields. Due to its structural characteristics, PE It cannot withstand high operating temperature, and its low mechanical strength limits its application in many fields. In order to improve the heat resistance and mechanical properties of PE, an effective method is to modify it by cross-linking.
对于交联聚乙烯而言,正是因为其具有独特的三维网状分子结构,使其具有更加出色的性能。交联聚乙烯因其优异的机械加工性能使其被广泛应用于管材制造工业,并逐步取代诸如聚丙烯、聚氯乙烯及各种热塑性聚乙烯等非交联塑料管材。在要求更高的应用领域中,例如汽车制造业,交联聚乙烯材料可以用来替代成本更高的工程塑料。交联聚乙烯泡沫在汽车领域的应用,主要用途包括汽车内顶饰,行李箱、地垫、侧围板、隔热垫、门内护板、防水帘、遮阳板、打蜡盘、空调系统等。目前对于聚乙烯的交联改性方法有很多,但是在进行改性时往往需要投入高昂的设备,技术比较复杂,产生较多的废料,造成较大的经济损失。For cross-linked polyethylene, it is precisely because of its unique three-dimensional network molecular structure that it has more excellent performance. Cross-linked polyethylene is widely used in the pipe manufacturing industry due to its excellent mechanical processing properties, and gradually replaces non-cross-linked plastic pipes such as polypropylene, polyvinyl chloride and various thermoplastic polyethylenes. In more demanding applications, such as in the automotive industry, XLPE can be used as an alternative to more expensive engineering plastics. The application of cross-linked polyethylene foam in the automotive field, the main uses include automotive interior roofing, luggage, floor mats, side panels, heat insulation pads, door inner guards, waterproof curtains, sun visors, waxing plates, air conditioning systems Wait. At present, there are many cross-linking modification methods for polyethylene, but the modification often needs to invest in expensive equipment, the technology is more complicated, more waste materials are generated, and greater economic losses are caused.
综上所述,现有技术存在的问题是:目前对聚乙烯在进行改性时往往需要投入高昂的设备,技术比较复杂,产生较多的废料,造成较大的经济损失。To sum up, the problems existing in the prior art are: at present, expensive equipment needs to be invested in the modification of polyethylene, the technology is more complicated, more wastes are produced, and greater economic losses are caused.
发明内容Contents of the invention
针对现有技术存在的问题,本发明提供了一种聚乙烯交联改性的方法。Aiming at the problems in the prior art, the invention provides a method for crosslinking and modifying polyethylene.
本发明是这样实现的,一种聚乙烯交联改性的方法为:PE的硅烷交联法,硅垸交联PE以PE为基础树脂,由硅垸为桥键材料,在聚合物大分子链间形成化学共价键以取代原先的范德华力,使分子构成三维立体网络,硅垸交联PE的制备包含接枝和交联两个阶段。The present invention is achieved in this way, a polyethylene cross-linking modification method is: PE silane cross-linking method, silane cross-linked PE with PE as the base resin, with silane as the bridge material, in the polymer macromolecule A chemical covalent bond is formed between the chains to replace the original van der Waals force, so that the molecules form a three-dimensional network. The preparation of silane cross-linked PE includes two stages of grafting and cross-linking.
接枝阶段:过氧化物引发剂受热分解形成初级自由基,初级自由基夺取PE大分子链上的H原子形成PE大分子自由基,该自由基与乙烯基三烷氧基硅烷CH2=CH—Si(OR)3中的乙烯基进行加成反应,形成PE接枝硅垸活性大分子,该活性大分子通过夺取PE中的H原子实现链转移得到PE接枝硅垸产物即接枝料A;Grafting stage: The peroxide initiator is decomposed by heat to form primary free radicals, which capture the H atoms on the PE macromolecular chain to form PE macromolecular free radicals, which are combined with vinyltrialkoxysilane CH 2 =CH —The vinyl group in Si (OR) 3 undergoes an addition reaction to form a PE-grafted silane active macromolecule. The active macromolecule realizes chain transfer by capturing the H atom in PE to obtain a PE-grafted silane product, namely grafting Material A;
交联阶段:PE接枝硅烷产物在有机锡类催化剂的作用下水解生成硅醇,硅醇通过脱水或脱醇形成PE硅垸交联产物。Crosslinking stage: PE grafted silane products are hydrolyzed under the action of organotin catalysts to generate silanols, and silanols are dehydrated or dealcoholized to form PE silane crosslinked products.
进一步,所述基础树脂为干燥处理之后的烯烃的均聚物和共聚物。Further, the base resin is a homopolymer or copolymer of olefin after drying treatment.
进一步,所述引发剂为DCP,DCP的用量为0.05-0.5份。Further, the initiator is DCP, and the amount of DCP is 0.05-0.5 parts.
进一步,所述交联剂采用乙烯基不饱和硅烷,交联剂用量为0.5-4份之间。Further, the cross-linking agent adopts ethylenically unsaturated silane, and the dosage of the cross-linking agent is between 0.5-4 parts.
进一步,所述抗氧剂为抗氧剂330、168、1010、RD及其它芳香胺类稳定剂,也可采用复配抗氧剂,抗氧剂含量不大于1份。Further, the antioxidants are antioxidant 330, 168, 1010, RD and other aromatic amine stabilizers, and compound antioxidants can also be used, and the antioxidant content is not more than 1 part.
进一步,所述交联催化剂是二月桂酸二丁锡酯,其用量为份。Further, the crosslinking catalyst is dibutyltin dilaurate, and its consumption is share.
进一步,所述阻聚剂在接枝过程中加入复配阻聚剂。Further, the polymerization inhibitor is added into a complex polymerization inhibitor during the grafting process.
综上所述,本发明的优点及积极效果为:本发明采用硅烷交联的方法,无需高昂的设备投入,可获得较高的挤出速度,并能减少开机阶段产生的废料,其交联的聚乙烯的耐老化能力要优于其他制备方法,技术简单且稳定的硅烷交联方式可以应用于较大范围的复合物加工。To sum up, the advantages and positive effects of the present invention are: the present invention adopts the method of silane cross-linking, which does not require expensive equipment investment, can obtain higher extrusion speed, and can reduce the waste generated during the start-up stage, and its cross-linking The aging resistance of polyethylene is superior to other preparation methods, and the simple and stable silane crosslinking method can be applied to a wide range of composite processing.
附图说明Description of drawings
图1是本发明实施例提供的硅垸交联PE的制备方法流程图。Fig. 1 is a flow chart of the preparation method of silane crosslinked PE provided by the embodiment of the present invention.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。In order to make the object, technical solution and advantages of the present invention more clear, the present invention will be further described in detail below in conjunction with the examples. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.
下面结合附图对本发明的应用原理做详细描述。The application principle of the present invention will be described in detail below in conjunction with the accompanying drawings.
本发明实施例提供的聚乙烯交联改性的方法为:PE的硅烷交联法,硅垸交联PE以PE为基础树脂,由硅垸为桥键材料,在聚合物大分子链间形成化学共价键以取代原先的范德华力,使分子构成三维立体网络,硅垸交联PE的制备包含接枝和交联两个阶段(如图1所示)。The method for cross-linking modification of polyethylene provided in the embodiments of the present invention is: silane cross-linking method of PE, silane cross-linked PE uses PE as the base resin, and silane is used as the bridging material to form between polymer macromolecular chains. Chemical covalent bonds are used to replace the original van der Waals force, so that the molecules form a three-dimensional network. The preparation of silane cross-linked PE includes two stages of grafting and cross-linking (as shown in Figure 1).
S101:接枝阶段:过氧化物引发剂受热分解形成初级自由基,初级自由基夺取PE大分子链上的H原子形成PE大分子自由基,该自由基与乙烯基三烷氧基硅烷CH2=CH—Si(OR)3中的乙烯基进行加成反应,形成PE接枝硅垸活性大分子,该活性大分子通过夺取PE中的H原子实现链转移得到PE接枝硅垸产物即接枝料A。S101: Grafting stage: The peroxide initiator is decomposed by heat to form a primary free radical, which captures the H atom on the PE macromolecular chain to form a PE macromolecular free radical, which is combined with vinyltrialkoxysilane CH 2 The vinyl group in =CH—S i (OR) 3 undergoes an addition reaction to form a PE-grafted silane active macromolecule, and the active macromolecule realizes chain transfer by capturing the H atom in PE to obtain a PE-grafted silane product, namely Grafting material A.
S102:交联阶段:PE接枝硅烷产物在有机锡类催化剂的作用下水解生成硅醇,硅醇通过脱水或脱醇形成PE硅垸交联产物。S102: Cross-linking stage: the PE grafted silane product is hydrolyzed under the action of an organotin catalyst to generate silanol, and the silanol is dehydrated or dealcoholized to form a PE silane cross-linked product.
本发明实施例提供的基础树脂为干燥处理之后的烯烃的均聚物和共聚物。The base resins provided in the embodiments of the present invention are homopolymers and copolymers of olefins after drying treatment.
本发明实施例提供的引发剂为DCP,DCP的用量为0.05-0.5份。The initiator provided in the embodiment of the present invention is DCP, and the dosage of DCP is 0.05-0.5 parts.
本发明实施例提供的交联剂采用乙烯基不饱和硅烷,交联剂用量为0.5-4份之间。The cross-linking agent provided in the embodiment of the present invention adopts vinyl unsaturated silane, and the dosage of the cross-linking agent is between 0.5-4 parts.
本发明实施例提供的抗氧剂为抗氧剂330、168、1010、RD及其它芳香胺类稳定剂,也可采用复配抗氧剂,抗氧剂含量不大于1份。The antioxidants provided in the examples of the present invention are antioxidant 330, 168, 1010, RD and other aromatic amine stabilizers. Compound antioxidants can also be used, and the antioxidant content is not more than 1 part.
本发明实施例提供的交联催化剂是二月桂酸二丁锡酯,其用量为0.02-~0.15份。The cross-linking catalyst provided in the embodiment of the present invention is dibutyltin dilaurate, and its dosage is 0.02-0.15 parts.
本发明实施例提供的阻聚剂在接枝过程中加入复配阻聚剂。In the polymerization inhibitor provided in the embodiment of the present invention, a complex polymerization inhibitor is added during the grafting process.
下面结合具体实施例对本发明作进一步描述。The present invention will be further described below in conjunction with specific embodiments.
实施例1Example 1
影响硅烷接枝交联PE的因素有:Factors affecting silane grafted cross-linked PE are:
基础树脂:烯烃的均聚物和共聚物都可被不饱和硅垸接枝交联。不同PE因其结构不同,接枝前后熔体流动速率下降的程度是不同的。具体生产中,单独的一种树脂很难满足综合性能要求,通常采用几种树脂共混的办法来调节树脂的基本特性,以希望达到预期的PE交联制品。另外,硅烷接枝对聚合物的含水量有严格要求。硅垸遇到聚合物中的水分会发生水解并产生预交联,将严重影响产品的质量。所以聚合物在使用前要进行干燥处理。Base resin: Homopolymers and copolymers of olefins can be grafted and cross-linked by unsaturated silanes. Due to their different structures, different PEs have different degrees of decrease in melt flow rate before and after grafting. In specific production, it is difficult for a single resin to meet the comprehensive performance requirements, and the method of blending several resins is usually used to adjust the basic characteristics of the resin in order to achieve the expected PE cross-linked products. In addition, silane grafting has strict requirements on the water content of the polymer. When silane encounters moisture in the polymer, it will be hydrolyzed and pre-crosslinked, which will seriously affect the quality of the product. Therefore, the polymer should be dried before use.
引发剂:硅烷接枝交联PE常用的引发剂为DCP,其分解温度及半衰期都能满足PE树脂与有机硅单体熔融接枝反应条件。当其它条件一定的情况下,随着DCP用量的增加,PE接枝效率有所变化。DCP的用量一般为0.05-0.5份。Initiator: The commonly used initiator for silane grafting and crosslinking PE is DCP, whose decomposition temperature and half-life can meet the conditions of melt grafting reaction between PE resin and organosilicon monomer. When other conditions are constant, the PE grafting efficiency changes with the increase of DCP dosage. The dosage of DCP is generally 0.05-0.5 parts.
交联剂:交联剂一般采用乙烯基不饱和硅垸作为交联剂,包括乙烯基三甲氧基硅垸和乙烯基三乙氧基硅烷。交联剂用量一般在0.5-4份之间。Crosslinking agent: The crosslinking agent generally uses vinyl unsaturated silane as the crosslinking agent, including vinyltrimethoxysilane and vinyltriethoxysilane. The dosage of crosslinking agent is generally between 0.5-4 parts.
抗氧剂:抗氧剂若在接枝之前加入,会对硅垸接枝反应产生明显影响,尤其是自由基的捕获剂类型的抗氧剂,因为它们会捕获PE自由基,抑制接枝反应。所以接枝过程中抗氧剂的添加要慎重,应选择合适的抗氧剂。常用的抗氧剂有抗氧剂330、168、1010、RD及其它芳香胺类稳定剂,也可采用复配抗氧剂。一般抗氧剂含量不大于1份。Antioxidant: If the antioxidant is added before grafting, it will have a significant impact on the silane grafting reaction, especially the free radical scavenger type antioxidant, because they will capture PE free radicals and inhibit the grafting reaction . Therefore, the addition of antioxidants in the grafting process should be cautious, and appropriate antioxidants should be selected. Commonly used antioxidants include antioxidant 330, 168, 1010, RD and other aromatic amine stabilizers, and compound antioxidants can also be used. Generally, the antioxidant content is not more than 1 part.
交联催化剂:交联催化剂最常用的催化剂是二月桂酸二丁锡酯(DBDTL),其用量为份。加入交联催化剂一般有两种形式,一种是直接加人到PE料中或者以母料形式加入;另一种是在制品的外表面涂上一层催化剂,第一种方法使用较多。Cross-linking catalyst: The most commonly used catalyst for cross-linking catalyst is dibutyltin dilaurate (DBDTL), and its dosage is share. There are generally two forms of adding cross-linking catalysts, one is directly added to PE material or added in the form of masterbatch; the other is to coat a layer of catalyst on the outer surface of the product, the first method is used more.
阻聚剂:阻聚剂在硅垸接枝和交联过程中不可避免地发生很多副反应,这些副反应对交联PE的加工和储存不利,所以应尽量减少这类反应的发生。为了降低这些副反应,采取的途径是在接枝过程中加入复配阻聚剂。Polymerization inhibitor: In the process of silane grafting and crosslinking, polymerization inhibitors inevitably have many side reactions. These side reactions are unfavorable to the processing and storage of crosslinked PE, so the occurrence of such reactions should be minimized. In order to reduce these side reactions, the approach taken is to add compound inhibitors during the grafting process.
实施例2Example 2
影响硅烷接枝交联PE的因素有:Factors affecting silane grafted cross-linked PE are:
(1)影响PE硅烷接枝工艺的因素(1) Factors affecting PE silane grafting process
影响PE硅烷接枝的主要工艺因素是挤出温度和挤出速度。接枝反应的速度主要取决于接枝引发剂的分解速度,而接枝引发剂的分解速度又强烈地依赖于挤出温度。随着温度升高,引发剂的半衰期降低,提高挤出温度有利于提高接枝反应速度。但挤出温度过高,硅烷单体挥发,降低了接枝率。PE硅烷接枝反应温度一般控制在190-210℃之间。挤出机转速决定物料在挤出机中停留的时间(反应时间)和混合效果。停留时间太短,过氧化物分解不完全,降低接枝率,残留过氧化物会直接影响接枝料的长期稳定性以及制品的成型性和外观。停留时间过长,挤出物料的黏度增加而影响加工性能。一般来说,工艺上要求PE在挤出机中的平均停留时间应控制在引发剂分解半衰期的5-10倍。喂料速度不仅对滞留时间有一定影响,而且喂料速度不同,螺槽的填充程度不同,因而影响螺杆对物料的混合和剪切作用。喂料过快,挤出的物料出料不均匀,表面不光滑,呈竹节状,工艺性能差。喂料太慢,经济性不合算。The main process factors affecting PE silane grafting are extrusion temperature and extrusion speed. The speed of the grafting reaction mainly depends on the decomposition speed of the grafting initiator, and the decomposition speed of the grafting initiator strongly depends on the extrusion temperature. As the temperature increased, the half-life of the initiator decreased, and increasing the extrusion temperature was beneficial to increase the rate of grafting reaction. However, if the extrusion temperature is too high, the silane monomer will volatilize, reducing the grafting rate. The temperature of PE silane grafting reaction is generally controlled between 190-210°C. The speed of the extruder determines the residence time of the material in the extruder (reaction time) and the mixing effect. If the residence time is too short, the decomposition of peroxide will be incomplete, and the grafting rate will be reduced. The residual peroxide will directly affect the long-term stability of the grafted material and the formability and appearance of the product. If the residence time is too long, the viscosity of the extruded material will increase and affect the processing performance. Generally speaking, the process requires that the average residence time of PE in the extruder should be controlled at 5-10 times the decomposition half-life of the initiator. The feeding speed not only has a certain influence on the residence time, but also the filling degree of the screw groove is different with different feeding speeds, thus affecting the mixing and shearing effect of the screw on the material. If the feeding is too fast, the extruded material will be discharged unevenly, the surface will be rough and bamboo-shaped, and the process performance will be poor. Feeding is too slow, and the economy is not cost-effective.
(2)硅垸接枝交联PE制备的两种工艺:(2) Two processes for the preparation of silane grafted cross-linked PE:
一步法:起源于M0n0sil技术,它是通过特制的精密计量系统,将原料一次性进入专门设计的反应挤出机中,一步完成接枝和成型的工艺。One-step method: Originated from M0n0sil technology, it uses a special precision metering system to feed raw materials into a specially designed reaction extruder at one time, and completes the grafting and molding process in one step.
两步法:来源于道康宁公司的Sioplase技术。第一步是硅烷接枝PE粒料和催化母料的混炼挤出制备,第二步是接枝PE粒料和催化母料与PE—起挤出成型,制品在热水或低压蒸汽下进行交联。Two-step method: Sioplase technology from Dow Corning. The first step is the mixing and extrusion preparation of silane-grafted PE pellets and catalytic masterbatch. The second step is to extrude the grafted PE pellets and catalytic masterbatch together with PE. The products are heated under hot water or low-pressure steam to cross-link.
下面结合具体实施例对其他交联方法作进一步描述。Other cross-linking methods will be further described below in conjunction with specific examples.
(1)高能辐射交联法(1) High energy radiation crosslinking method
辐射交联法(PE-Xc)是通过β射线或γ射线照射已成型产品,使聚乙烯分子间形成C-C交联键。所得制品纯净,电气性能优越,但辐射发生装置昂贵,辐射线穿透能力有限,不适宜制作厚壁制品或结构复杂的制品,多用于电缆料、热收缩管和特种薄膜的生产。The radiation crosslinking method (PE-Xc) is to irradiate the molded product with β-ray or γ-ray to form C-C crosslinking bonds between polyethylene molecules. The resulting product is pure and has superior electrical properties, but the radiation generating device is expensive and the penetration of radiation is limited. It is not suitable for making thick-walled products or products with complex structures. It is mostly used in the production of cable materials, heat-shrinkable tubes and special films.
PE是一种典型的可辐射交联聚合物。伹如何加速辐射交联、抑制副反应、降低达到所需凝胶含量时的辐照剂量(也就是PE的敏化辐射问题)已成为当前研究的重点。PE is a typical radiation crosslinkable polymer. How to accelerate radiation crosslinking, suppress side reactions, and reduce the radiation dose to achieve the required gel content (that is, the sensitizing radiation problem of PE) has become the focus of current research.
PE敏化辐射问题的一般方法是在PE中加入增敏剂和敏化剂(也有人将增敏剂和敏化剂统称为敏化剂或增感剂),或者改变辐照气氛(如在乙炔、四氟乙烯气氛中)。The general method of PE sensitization to radiation problems is to add sensitizers and sensitizers to PE (some people refer to sensitizers and sensitizers collectively as sensitizers or sensitizers), or to change the irradiation atmosphere (such as in Acetylene, tetrafluoroethylene atmosphere).
PE高能辐射交联法的优缺点:Advantages and disadvantages of PE high energy radiation crosslinking method:
优点:良好的加工稳定性;制成品纯净。Advantages: good processing stability; finished product is pure.
缺点:昂贵的辅助加工设备;要求较高的工作环境;只适用于薄壁产品;难于完成盘管的交联。Disadvantages: expensive auxiliary processing equipment; demanding working environment; only suitable for thin-walled products; difficult to complete cross-linking of coils.
(2)PE的过氧化物交联(2) Peroxide crosslinking of PE
过氧化物交联具有适应性强、交联制品性能好等优点,因而获得了工业应用。Peroxide crosslinking has the advantages of strong adaptability and good performance of crosslinked products, so it has been applied in industry.
过氧化物交联与辐射交联不同之处在于:Peroxide crosslinking differs from radiation crosslinking in that:
其交联过程必须有交联剂,即过氧化物存在;The crosslinking process must have a crosslinking agent, that is, the presence of peroxide;
交联反应必须在一定温度下进行。The crosslinking reaction must be carried out at a certain temperature.
当交联剂是单纯过氧化物时,其反应过程如下:过氧化物受热分解生成自由基,自由基进攻PE大分子链,夺取分子链上的氢原子,生成PE大分子链自由基;PE大分子链自由基具有高度反应活性,当两个PE分子链自由基相遇时,便相互结合,形成高分子链间的化学键而交联。When the cross-linking agent is pure peroxide, the reaction process is as follows: peroxide is decomposed by heat to generate free radicals, which attack PE macromolecular chains, capture hydrogen atoms on the molecular chains, and generate PE macromolecular chain free radicals; Macromolecular chain free radicals are highly reactive. When two PE molecular chain free radicals meet, they combine with each other to form chemical bonds between polymer chains and cross-link.
过氧化物交联所用的交联剂为有机过氧化物,常用的品种主要有DCP,BPO等。用过氧化物交联PE时,挤出温度必须保持很低,一旦挤出温度高于过氧化物的分解温度,早期的交联可能导致出现焦化,影响制品的质量甚至损坏设备,该温度极限严格限制着可交联PE的挤出速度,而且在挤出制品时,要有专用的挤出机和高压连续交联管道,这就限制了该技术在中、小企业的应用。The crosslinking agent used in peroxide crosslinking is organic peroxide, and the commonly used varieties mainly include DCP, BPO and so on. When crosslinking PE with peroxide, the extrusion temperature must be kept very low. Once the extrusion temperature is higher than the decomposition temperature of peroxide, early crosslinking may cause coking, affect the quality of the product or even damage the equipment. The temperature limit The extrusion speed of cross-linkable PE is strictly limited, and when extruding products, there must be a special extruder and high-pressure continuous cross-linking pipeline, which limits the application of this technology in small and medium-sized enterprises.
PE的过氧化物交联的优缺点Advantages and disadvantages of peroxide crosslinking of PE
优点:较高的交联度;较好的柔性。Advantages: higher degree of cross-linking; better flexibility.
缺点:对生产设备要求较高,要高温,易造成聚乙烯分子断链,生产速度较慢,效率较低。Disadvantages: high requirements for production equipment, high temperature, easy to cause chain breakage of polyethylene molecules, slow production speed and low efficiency.
(3)PE的紫外光照交联(3) UV light crosslinking of PE
紫外光也能使PE发生交联,紫外光交联是通过光引发剂吸收紫外光能量后转变为激发态,然后在PE链上夺氢产生自由基而引发PE交联的。Ultraviolet light can also cause PE to crosslink. Ultraviolet light crosslinking is transformed into an excited state after the photoinitiator absorbs the energy of ultraviolet light, and then hydrogen abstraction on the PE chain generates free radicals to initiate PE crosslinking.
PE的紫外光照交联的突破性进展Breakthrough progress in UV crosslinking of PE
①选用高功率高压汞灯代替低压汞灯,不仅提高了光强,而且使其发射波长范围适合于所用的光引发剂的吸收;①Using high-power high-pressure mercury lamps instead of low-pressure mercury lamps not only increases the light intensity, but also makes the emission wavelength range suitable for the absorption of the photoinitiator used;
②采用熔融态进行交联,一方面使紫外光容易穿透PE厚样品,另一方面由于温度的提高增加了待交联的大分子自由基的运动性,从而加快了反应速度,提高了交联的均匀性;②Cross-linking in a molten state, on the one hand, makes it easy for ultraviolet light to penetrate thick PE samples; Uniformity of joint;
③采用多官能团交联剂与光引发剂配合的高效引发体系,使交联过程在最初引发阶段的短时间内完成,不仅提高了交联引发速度,而且将交联的深度由0.3mm提高到3mm以上。③The high-efficiency initiation system of multifunctional crosslinking agent and photoinitiator is used to complete the crosslinking process in a short time at the initial initiation stage, which not only improves the crosslinking initiation speed, but also increases the crosslinking depth from 0.3mm to 3mm or more.
PE的紫外光照交联的优点Advantages of UV crosslinking of PE
紫外光交联技术有其独特的优点,在技术原理上它类似于高能电子束辐射法,但是它采用低能的紫外光作为辐射源,设备易得,投资费用低,操作简单,防护容易。因此,PE的紫外光交联技术越来越受到人们的重视,特别在发展交联电线以及各种低压交联电缆方面具有较大的市场竞争力,为PE交联技术开辟出一条新路。Ultraviolet light cross-linking technology has its unique advantages. It is similar to the high-energy electron beam radiation method in terms of technical principle, but it uses low-energy ultraviolet light as the radiation source. The equipment is easy to obtain, the investment cost is low, the operation is simple, and the protection is easy. Therefore, more and more people pay more and more attention to the ultraviolet light cross-linking technology of PE, especially in the development of cross-linked wires and various low-voltage cross-linked cables, which have great market competitiveness and open up a new way for PE cross-linking technology.
以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present invention should be included in the protection of the present invention. within range.
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