CN1446852A - Method for preparing Inserted layers type nano composite material of polypropylene/montmorillonite - Google Patents
Method for preparing Inserted layers type nano composite material of polypropylene/montmorillonite Download PDFInfo
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- CN1446852A CN1446852A CN 03115233 CN03115233A CN1446852A CN 1446852 A CN1446852 A CN 1446852A CN 03115233 CN03115233 CN 03115233 CN 03115233 A CN03115233 A CN 03115233A CN 1446852 A CN1446852 A CN 1446852A
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- 239000004743 Polypropylene Substances 0.000 title claims abstract description 78
- -1 polypropylene Polymers 0.000 title claims abstract description 78
- 229920001155 polypropylene Polymers 0.000 title claims abstract description 78
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 title claims abstract description 53
- 229910052901 montmorillonite Inorganic materials 0.000 title claims abstract description 23
- 239000002114 nanocomposite Substances 0.000 title claims abstract description 17
- 239000000463 material Substances 0.000 title claims abstract description 16
- 238000000034 method Methods 0.000 title claims abstract description 15
- 239000004594 Masterbatch (MB) Substances 0.000 claims abstract description 29
- 239000002131 composite material Substances 0.000 claims abstract description 9
- 230000002687 intercalation Effects 0.000 claims abstract description 8
- 238000009830 intercalation Methods 0.000 claims abstract description 8
- 238000002360 preparation method Methods 0.000 claims abstract description 8
- 238000001125 extrusion Methods 0.000 claims description 30
- 239000000203 mixture Substances 0.000 claims description 23
- 239000003999 initiator Substances 0.000 claims description 10
- 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
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 claims description 6
- 235000019400 benzoyl peroxide Nutrition 0.000 claims description 6
- 239000000178 monomer Substances 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 229920001577 copolymer Polymers 0.000 claims description 5
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical group C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 238000007348 radical reaction Methods 0.000 claims description 4
- 150000003254 radicals Chemical class 0.000 claims description 4
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 3
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims description 3
- 150000001768 cations Chemical class 0.000 claims description 3
- 239000011229 interlayer Substances 0.000 claims description 3
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims description 3
- 239000011976 maleic acid Substances 0.000 claims description 3
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 3
- 230000004048 modification Effects 0.000 claims description 3
- 238000012986 modification Methods 0.000 claims description 3
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims description 3
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims description 2
- JBSLOWBPDRZSMB-FPLPWBNLSA-N dibutyl (z)-but-2-enedioate Chemical compound CCCCOC(=O)\C=C/C(=O)OCCCC JBSLOWBPDRZSMB-FPLPWBNLSA-N 0.000 claims description 2
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 claims 1
- 229920005606 polypropylene copolymer Polymers 0.000 abstract description 8
- 239000003607 modifier Substances 0.000 abstract 1
- 239000002994 raw material Substances 0.000 abstract 1
- 238000003756 stirring Methods 0.000 description 14
- 239000008187 granular material Substances 0.000 description 12
- 239000000047 product Substances 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000002156 mixing Methods 0.000 description 5
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 238000005341 cation exchange Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 229910001961 silver nitrate Inorganic materials 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- SRMJUSXGAMRMDL-UHFFFAOYSA-N 2,2,3,3,4,4-hexaaminohexanoic acid Chemical compound NC(C(C(C(=O)O)(N)N)(N)N)(CC)N SRMJUSXGAMRMDL-UHFFFAOYSA-N 0.000 description 1
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- VBIIFPGSPJYLRR-UHFFFAOYSA-M Stearyltrimethylammonium chloride Chemical compound [Cl-].CCCCCCCCCCCCCCCCCC[N+](C)(C)C VBIIFPGSPJYLRR-UHFFFAOYSA-M 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 125000005211 alkyl trimethyl ammonium group Chemical group 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- PSLWZOIUBRXAQW-UHFFFAOYSA-M dimethyl(dioctadecyl)azanium;bromide Chemical compound [Br-].CCCCCCCCCCCCCCCCCC[N+](C)(C)CCCCCCCCCCCCCCCCCC PSLWZOIUBRXAQW-UHFFFAOYSA-M 0.000 description 1
- REZZEXDLIUJMMS-UHFFFAOYSA-M dimethyldioctadecylammonium chloride Chemical compound [Cl-].CCCCCCCCCCCCCCCCCC[N+](C)(C)CCCCCCCCCCCCCCCCCC REZZEXDLIUJMMS-UHFFFAOYSA-M 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 238000004299 exfoliation Methods 0.000 description 1
- 229910017059 organic montmorillonite Inorganic materials 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920005653 propylene-ethylene copolymer Polymers 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 239000004945 silicone rubber Substances 0.000 description 1
- SZEMGTQCPRNXEG-UHFFFAOYSA-M trimethyl(octadecyl)azanium;bromide Chemical compound [Br-].CCCCCCCCCCCCCCCCCC[N+](C)(C)C SZEMGTQCPRNXEG-UHFFFAOYSA-M 0.000 description 1
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Abstract
本发明是一种聚丙烯/蒙脱土纳米复合材料的制备方法。现有技术获得的复合材料性能不令人满意,且工艺复杂。本发明聚丙烯/蒙脱土插层型纳米复合材料的原材料包括:等规聚丙烯、层间距不同的有机改性蒙脱土(TJ1、TJ2、TJ3、TJ4)、接枝改性聚丙烯、接枝改性聚丙烯共聚物。以接枝改性聚丙烯或接枝改性聚丙烯共聚物为改性剂,用母料法熔融插层制备了聚丙烯/蒙脱土插层型纳米复合材料。本发明方法获得的复合材料力学性能明显提高,并且材料的加工性能也有所改善。The invention is a preparation method of polypropylene/montmorillonite nanocomposite material. The performance of the composite material obtained by the prior art is not satisfactory, and the process is complicated. The raw materials of the polypropylene/montmorillonite intercalation nanocomposite of the present invention include: isotactic polypropylene, organically modified montmorillonite (TJ1, TJ2, TJ3, TJ4) with different layer spacings, grafted modified polypropylene, Graft modified polypropylene copolymer. Polypropylene/montmorillonite intercalated nanocomposites were prepared by melt intercalation by masterbatch method with graft modified polypropylene or graft modified polypropylene copolymer as modifier. The mechanical property of the composite material obtained by the method of the invention is obviously improved, and the processing performance of the material is also improved.
Description
技术领域technical field
本发明涉及一种有机改性蒙脱土填充聚丙烯形成插层型纳米复合材料的制备方法。The invention relates to a preparation method of organically modified montmorillonite filled with polypropylene to form an intercalated nanocomposite material.
背景技术Background technique
本发明现有技术涉及到的专利有CN1163288A、CN1247206A、CN1267682A、US5910523。专利CN1163288A是有关蒙脱土填充硅橡胶形成复合材料。专利CN1247206A采用直接熔融共混法,用经十六烷基三甲基溴化铵或六氨基己酸进行阳离子交换的蒙脱土填充聚丙烯形成复合材料,采用直接熔融共混法,材料的混合均匀性较差,得到的复合材料性能相对较低。专利CN1267682A、US5910523是用液相插层反应接枝改性的聚丙烯在液相反应器中插入蒙脱土片层,得到聚丙烯/蒙脱土纳米复合材料,该工艺过程复杂,并且要用到大量的有机溶剂,给环境带来了严重的污染。The patents related to the prior art of the present invention are CN1163288A, CN1247206A, CN1267682A, US5910523. Patent CN1163288A is about montmorillonite filled with silicone rubber to form a composite material. Patent CN1247206A adopts the direct melt blending method, and uses the montmorillonite filled polypropylene with cation-exchanged cetyltrimethylammonium bromide or hexaaminocaproic acid to form a composite material, adopts the direct melt blending method, and the mixing of materials The homogeneity is poor and the resulting composites have relatively low properties. Patents CN1267682A and US5910523 use liquid-phase intercalation reaction graft-modified polypropylene to insert montmorillonite sheets in a liquid-phase reactor to obtain polypropylene/montmorillonite nanocomposites. The process is complicated and requires A large amount of organic solvents have brought serious pollution to the environment.
聚丙烯作为一种最常用的通用塑料,具有较优良的综合性能,但是与传统工程塑料相比存在强度和弹性摸量较低,耐候性差,收缩率大,耐热性较差等特点。而聚丙烯/有机改性蒙脱土复合材料具有较高的冲击韧性和弹性模量,较好的耐热性及突出的阻隔性,在汽车、航天航空领域具有广阔的应用前景。As one of the most commonly used general-purpose plastics, polypropylene has excellent comprehensive properties, but compared with traditional engineering plastics, it has the characteristics of lower strength and elastic modulus, poor weather resistance, large shrinkage rate, and poor heat resistance. The polypropylene/organically modified montmorillonite composite material has high impact toughness and elastic modulus, good heat resistance and outstanding barrier properties, and has broad application prospects in the fields of automobiles and aerospace.
在基于聚丙烯的有机/无机纳米杂化材料体系中,经过表面化学修饰的层状硅酸盐材料,如:有机蒙脱土在聚丙烯基体中形成插层或剥离型的结构,达到纳米分散水平,材料的力学性能(强度、韧性)及耐热性可同时提高,且加工性能有所改善。但是现有技术中尚无一种令人满意的制备方法。In the polypropylene-based organic/inorganic nano-hybrid material system, the surface chemically modified layered silicate material, such as: organic montmorillonite forms an intercalation or exfoliation structure in the polypropylene matrix to achieve nano-dispersion Level, the mechanical properties (strength, toughness) and heat resistance of the material can be improved at the same time, and the processing performance has been improved. But there is no satisfactory preparation method in the prior art.
发明内容Contents of the invention
本发明的目的是提供一种方法简单、工艺上容易实现、成本不高、性能良好的制备聚丙烯/蒙脱土插层型的纳米复合材料方法。The purpose of the present invention is to provide a method for preparing polypropylene/montmorillonite intercalated nano-composite material with simple method, easy technical realization, low cost and good performance.
本发明的聚丙烯/蒙脱土插层型的纳米复合材料制备时先制得接枝改性聚丙烯,再将接枝改性聚丙烯与有机改性蒙脱土熔融共混得母料,最后将聚丙烯和母料熔融共混得到产品。制备的具体条件是:将聚丙烯、接枝单体、自由基反应引发剂经高速搅拌机混合,用双螺杆挤出机熔融共混,进行反应挤出,挤出温度是180-230℃,得接枝改性聚丙烯,其中各组成的重量份数是:When preparing the polypropylene/montmorillonite intercalated nanocomposite material of the present invention, graft modified polypropylene is first prepared, then graft modified polypropylene and organically modified montmorillonite are melt-blended to obtain a masterbatch, and finally The polypropylene and masterbatch are melt blended to obtain the product. The specific conditions for the preparation are: mixing polypropylene, grafted monomers and free radical reaction initiators through a high-speed mixer, melt blending with a twin-screw extruder, and performing reactive extrusion. The extrusion temperature is 180-230° C. to obtain Graft modified polypropylene, wherein the parts by weight of each composition are:
聚丙烯: 1.0Polypropylene: 1.0
接枝单体: 0.01~0.1Graft monomer: 0.01~0.1
引发剂: 0.001~0.01。Initiator: 0.001~0.01.
将上述接枝改性聚丙烯与有机改性蒙脱土经高速搅拌机混合,用双螺杆挤出机熔融共混,挤出温度是180-230℃,得母料,各组成的重量份数是:Mix the above-mentioned graft-modified polypropylene and organically-modified montmorillonite through a high-speed mixer, melt and blend them with a twin-screw extruder, and the extrusion temperature is 180-230°C to obtain a masterbatch. The parts by weight of each composition are :
接枝改性聚丙烯: 1.0Graft modified polypropylene: 1.0
有机改性蒙脱土: 0.15~0.35。Organic modified montmorillonite: 0.15~0.35.
将聚丙烯和母料,经高速搅拌机混合,用双螺杆挤出机熔融共混,挤出温度是180-230℃,得产品。各组成的重量份数是:The polypropylene and the masterbatch are mixed through a high-speed mixer, melted and blended with a twin-screw extruder, and the extrusion temperature is 180-230°C to obtain the product. The parts by weight of each composition are:
聚丙烯: 1.0Polypropylene: 1.0
母料: 0.05~0.35。Masterbatch: 0.05~0.35.
上述聚丙烯是等规聚丙烯,其熔融指数约为3.7克/分左右。The aforementioned polypropylene is an isotactic polypropylene having a melt index of about 3.7 g/min.
接枝改性后聚丙烯的熔融指数为3.0-3.7克/分。The melt index of polypropylene after graft modification is 3.0-3.7 g/min.
引发剂是自由基反应引发剂,如过氧化二异丙苯、过氧化二苯甲酰等。The initiator is a free radical reaction initiator, such as dicumyl peroxide, dibenzoyl peroxide and the like.
有机改性蒙脱土可用现有技术方法改性、阳离子交换剂如16-18碳烷基铵盐,16烷基三甲基溴化铵等。The organically modified montmorillonite can be modified by prior art methods, cation exchangers such as 16-18 carbon alkyl ammonium salts, 16 alkyl trimethyl ammonium bromide and the like.
本发明的聚丙烯可以是共聚物经接枝改性、如丙烯-乙烯共聚物、丙烯-丙烯腈共聚物的接枝产物等,与有机改性蒙脱土熔融共混,制得母料。也可以用市售的接枝改性聚丙烯共聚物GMG0101。The polypropylene of the present invention can be grafted and modified copolymers, such as grafted products of propylene-ethylene copolymers and propylene-acrylonitrile copolymers, which are melt-blended with organically modified montmorillonite to obtain a masterbatch. Commercially available graft-modified polypropylene copolymer GMG0101 can also be used.
接枝改性聚丙烯或聚丙烯共聚物的接枝单体可以是下述中任一种:马来酸酐、马来酸、马来酸二丁酯、丙烯酸、丙烯酰胺、甲基丙烯酸丁酯或者是它们的复配物。The graft monomer of graft modified polypropylene or polypropylene copolymer can be any of the following: maleic anhydride, maleic acid, dibutyl maleate, acrylic acid, acrylamide, butyl methacrylate Or a combination of them.
本发明接枝反应引发剂是自由基反应引发剂,过氧化二异丙苯或过氧化二苯甲酰是本发明较好的引发剂。The grafting reaction initiator of the present invention is a free radical reaction initiator, and dicumyl peroxide or dibenzoyl peroxide are preferred initiators of the present invention.
有机改性蒙脱土的阳离子交换剂以16-18碳烷基铵盐或双16-18碳烷基铵盐为好,所用方法与现有技术同样。The cation exchanger of organically modified montmorillonite is preferably 16-18 carbon alkyl ammonium salt or double 16-18 carbon alkyl ammonium salt, and the method used is the same as the prior art.
经改性后的蒙脱土经x-光衍射分析,其层间距是2.0-4.0nm,该层间距的蒙脱土插入聚丙烯后,不仅使复合材料力学性能提高,且加工性能也良好。After the modified montmorillonite is analyzed by X-ray diffraction, the interlayer spacing is 2.0-4.0nm. After the interlayer montmorillonite is inserted into polypropylene, not only the mechanical properties of the composite material are improved, but also the processing performance is also good.
蒙脱土改性后,经研磨过筛至粒径是20-100μm与接枝改性聚丙烯熔融共混获得母料效果良好。After the montmorillonite is modified, it is grinded and sieved to a particle size of 20-100 μm and melt-blended with grafted modified polypropylene to obtain a masterbatch with good effect.
本发明所制得的聚丙烯/蒙脱土插层型纳米复合材料中,有机改性蒙脱土在聚丙烯基体中分散均匀,形成了插层结构,复合材料具有很好的综合性能。冲击强度提高10~124%,拉伸强度提高10~30%,维卡软化点提高20℃左右,其性能见表1。In the polypropylene/montmorillonite intercalation nanocomposite material prepared by the invention, the organically modified montmorillonite is uniformly dispersed in the polypropylene matrix to form an intercalation structure, and the composite material has good comprehensive performance. The impact strength is increased by 10-124%, the tensile strength is increased by 10-30%, and the Vicat softening point is increased by about 20°C. The properties are shown in Table 1.
附图说明Description of drawings
图1是聚丙烯/蒙脱土插层型纳米复合材料的性能。Figure 1 shows the properties of polypropylene/montmorillonite intercalated nanocomposites.
具体实施方式Detailed ways
实施例1Example 1
100g聚丙烯4.2g马来酸酐0.84g过氧化二苯甲酰共混,用双螺杆挤出机挤出造粒,挤出温度为160-190℃,得接枝改性聚丙烯;再将100g接枝改性聚丙烯与25g有机改性蒙脱土混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得母料;然后将100g聚丙烯5.9g母料混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得产品。其性能见表1。100g polypropylene, 4.2g maleic anhydride and 0.84g dibenzoyl peroxide are blended, extruded and granulated with a twin-screw extruder, and the extrusion temperature is 160-190°C to obtain graft modified polypropylene; then 100g Graft modified polypropylene is mixed with 25g of organically modified montmorillonite, stirred with a high-speed mixer, extruded and granulated with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain a masterbatch; then 100g of polypropylene Mix 5.9 g of the masterbatch, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220° C. to obtain the product. Its performance is shown in Table 1.
实施例2Example 2
100g聚丙烯1.2g马来酸0.14g过氧化二异丙苯,用双螺杆挤出机挤出造粒,挤出温度为160-190℃,得接枝改性聚丙烯;再将100g接枝改性聚丙烯与15g有机改性蒙脱土混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得母料;然后将100g聚丙烯17.6g母料混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得产品。其性能见表1。100g polypropylene, 1.2g maleic acid, 0.14g dicumyl peroxide, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 160-190°C to obtain grafted modified polypropylene; then graft 100g Modified polypropylene is mixed with 15g of organically modified montmorillonite, stirred with a high-speed mixer, extruded and granulated with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain a masterbatch; then 100g of polypropylene 17.6g The masterbatch is mixed, stirred with a high-speed mixer, extruded and granulated with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain the product. Its performance is shown in Table 1.
实施例3Example 3
100g聚丙烯10g丙烯酸1.0g过氧化二苯甲酰共混,用双螺杆挤出机挤出造粒,挤出温度为160-190℃,得接枝改性聚丙烯;再将100g接枝改性聚丙烯与35g有机改性蒙脱土混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得母料;然后将100g聚丙烯33.3g母料混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得产品。其性能见表1。100g of polypropylene, 10g of acrylic acid, and 1.0g of dibenzoyl peroxide are blended, extruded and granulated with a twin-screw extruder, and the extrusion temperature is 160-190°C to obtain graft-modified polypropylene; Mix permanent polypropylene with 35g of organically modified montmorillonite, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain a masterbatch; then mix 100g of polypropylene with 33.3g of masterbatch Mix the materials, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain the product. Its performance is shown in Table 1.
实施例4Example 4
100g聚丙烯4.2g甲基丙烯酸丁酯0.84g过氧化二苯甲酰共混,用双螺杆挤出机挤出造粒,挤出温度为160-190℃,得接枝改性聚丙烯;再将100g接枝改性聚丙烯与25g有机改性蒙脱土混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得母料;然后将100g聚丙烯35.0g母料混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得产品。其性能见表1。100g of polypropylene, 4.2g of butyl methacrylate, and 0.84g of dibenzoyl peroxide are blended, extruded and granulated with a twin-screw extruder, and the extrusion temperature is 160-190°C to obtain grafted modified polypropylene; Mix 100g of grafted modified polypropylene with 25g of organically modified montmorillonite, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain a masterbatch; then 100g 35.0 g of polypropylene master batches were mixed, stirred with a high-speed mixer, extruded and granulated with a twin-screw extruder, and the extrusion temperature was 180-220° C. to obtain the product. Its performance is shown in Table 1.
实施例5Example 5
将100g接枝改性聚丙烯共聚物(乙烯-丙烯共聚物)与25g有机改性蒙脱土混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得母料;然后将100g聚丙烯、5.9g母料混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得产品。其性能见表1。Mix 100g of graft modified polypropylene copolymer (ethylene-propylene copolymer) with 25g of organically modified montmorillonite, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220 °C to obtain a masterbatch; then mix 100g polypropylene and 5.9g masterbatch, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain the product. Its performance is shown in Table 1.
实施例6Example 6
将100g接枝改性聚丙烯共聚物(市售GMG0101)与25g有机改性蒙脱土混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得母料;然后将100g聚丙烯、17.6g母料混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得产品。其性能见表1。Mix 100g of graft-modified polypropylene copolymer (commercially available GMG0101) with 25g of organically modified montmorillonite, stir with a high-speed mixer, extrude and pelletize with a twin-screw extruder, and the extrusion temperature is 180-220°C. Obtain the masterbatch; then mix 100g of polypropylene and 17.6g of the masterbatch, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain the product. Its performance is shown in Table 1.
实施例7Example 7
将100g接枝改性聚丙烯共聚物与25g有机改性蒙脱土混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得母料;然后将100g聚丙烯、33.3g母料混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得产品。其性能见表1。Mix 100g of graft-modified polypropylene copolymer with 25g of organically modified montmorillonite, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain a masterbatch; then Mix 100g of polypropylene and 33.3g of masterbatch, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain the product. Its performance is shown in Table 1.
实施例8Example 8
将100g接枝改性聚丙烯共聚物(丙烯-丙烯腈共聚物)与25g有机改性蒙脱土混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得母料;然后将100g聚丙烯、35g母料混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得产品。其性能见表1。Mix 100g of graft-modified polypropylene copolymer (propylene-acrylonitrile copolymer) with 25g of organically modified montmorillonite, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180~ 220°C to obtain a masterbatch; then mix 100g polypropylene and 35g masterbatch, stir with a high-speed mixer, extrude and granulate with a twin-screw extruder, and the extrusion temperature is 180-220°C to obtain the product. Its performance is shown in Table 1.
实施例9Example 9
100g聚丙烯和5.3g有机改性蒙脱土TJ4混合,用高速搅拌机搅拌,用双螺杆挤出机挤出造粒,挤出温度为180~220℃,得产品。其性能见表1。100g of polypropylene and 5.3g of organically modified montmorillonite TJ4 were mixed, stirred with a high-speed mixer, extruded and granulated with a twin-screw extruder, and the extrusion temperature was 180-220°C to obtain the product. Its performance is shown in Table 1.
实施例10(对比例)Embodiment 10 (comparative example)
100g聚丙烯在加工设备上加热,挤出温度为180~220℃,得对比样品,其性能见表1。100g of polypropylene was heated on the processing equipment, and the extrusion temperature was 180-220°C to obtain comparative samples, whose properties are shown in Table 1.
实施例11Example 11
将阳离子交换总容量为80meq/100g的蒙脱土2.0g,加水80ml,待分散均匀后,高速搅拌40min,得悬浮液。10g十八烷基三甲基氯化铵或双十八烷基二甲基氯化铵溶于25ml水中,得溶液。上述悬浮液加热至80℃,滴加上述溶液,温度维持在80℃,保温1小时,倒去上层清液,抽滤,用蒸馏水洗涤多次,用0.2%硝酸银溶液检测滤液至无氯离子,干燥,研磨,过筛,得有机改性蒙脱土,其粒径为20μm。Add 2.0 g of montmorillonite with a total capacity of cation exchange of 80 meq/100 g, add 80 ml of water, wait for uniform dispersion, and stir at high speed for 40 min to obtain a suspension. Dissolve 10g of octadecyltrimethylammonium chloride or dioctadecyldimethylammonium chloride in 25ml of water to obtain a solution. Heat the above suspension to 80°C, add the above solution dropwise, maintain the temperature at 80°C, keep warm for 1 hour, pour off the supernatant, filter with suction, wash with distilled water for several times, and detect the filtrate with 0.2% silver nitrate solution until there is no chloride ion , dried, ground, and sieved to obtain an organically modified montmorillonite with a particle size of 20 μm.
实施例12Example 12
将阳离子交换总容量为100meq/100g的蒙脱土3.0g,加水120ml,待分散均匀后,高速搅拌40min,得悬浮液。5g十八烷基三甲基溴化铵或双十八烷基二甲基溴化铵溶于25ml水中,得溶液。上述悬浮液加热至80℃,滴加上述溶液,温度维持在80℃,保温1小时,倒去上层清液,抽滤,用蒸馏水洗涤多次,用0.2%硝酸银溶液检测滤液至无氯离子,干燥,研磨,过筛,得有机改性蒙脱土,其粒径为100μm。Add 3.0 g of montmorillonite with a total capacity of cation exchange of 100 meq/100 g, add 120 ml of water, and stir at high speed for 40 min after uniform dispersion to obtain a suspension. Dissolve 5g of octadecyltrimethylammonium bromide or dioctadecyldimethylammonium bromide in 25ml of water to obtain a solution. Heat the above suspension to 80°C, add the above solution dropwise, maintain the temperature at 80°C, keep warm for 1 hour, pour off the supernatant, filter with suction, wash with distilled water for several times, and detect the filtrate with 0.2% silver nitrate solution until there is no chloride ion , dried, ground, and sieved to obtain an organically modified montmorillonite with a particle size of 100 μm.
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