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CN1105742C - Special material for modifying PP-R plastics and its preparing process - Google Patents

Special material for modifying PP-R plastics and its preparing process Download PDF

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CN1105742C
CN1105742C CN00123963A CN00123963A CN1105742C CN 1105742 C CN1105742 C CN 1105742C CN 00123963 A CN00123963 A CN 00123963A CN 00123963 A CN00123963 A CN 00123963A CN 1105742 C CN1105742 C CN 1105742C
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plastics
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CN1304956A (en
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黄学伦
于好兴
王永选
王锡臣
黄志诚
张双全
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HAIXING PLASTICS PLANT ZHAOYUAN CITY
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Abstract

本发明涉及一种通过工程塑料改性的PP-R塑料专用料及其制备方法,本发明的改性PP-R塑料专用料,按重量份,包括PP-R树脂50-75份、工程塑料10-30份、增容剂1-10份、润滑剂0.5-3份,还可以加入高熔点聚丙烯7-20份、活性纳米材料1-5份,其制备方法包括混料、冷却、造粒、冷却切料四个步骤,本发明的改性PP-R塑料专用料制成的塑料制品具有耐高温、高强度、耐疲劳性和较长的使用寿命。The invention relates to a PP-R plastic special material modified by engineering plastics and a preparation method thereof. The modified PP-R plastic special material of the present invention comprises 50-75 parts of PP-R resin and 10 parts of engineering plastics in parts by weight. -30 parts, 1-10 parts of compatibilizer, 0.5-3 parts of lubricant, 7-20 parts of high melting point polypropylene and 1-5 parts of active nanomaterials can also be added. The preparation method includes mixing, cooling and granulation 1. Cooling and cutting four steps, the plastic products made of the modified PP-R plastic special material of the present invention have high temperature resistance, high strength, fatigue resistance and long service life.

Description

改性PP-R塑料专用料Modified PP-R plastic special material

本发明涉及一种通过工程塑料改性的PP-R塑料专用料。The invention relates to a PP-R plastic special material modified by engineering plastics.

目前国内外所用的PP-R是一种无毒、卫生的新型高分子化学材料,其为PP-R三型,是继PP-R二型之后的第三代产品,主要用先进的气相共聚法使乙烯和丙烯在分子链中随机聚合而成,但由于其本身分子结构的特性,使用温度范围较窄,当温度升高到玻璃化温度Tg时,分子链间空隙体积开始膨胀,主链单键内旋转势垒突然降低,链段开始进行位移运动,聚合物开始相态转变,此时在压力作用下,温度只要提高几度,形变值突然增大几十倍,模量下降3-4个数量级。若温度继续升高,高分子的热运动能量和分子间的空隙体积均达到可以使链段比较自由地进行相对位移运动。此时PP-R塑料已处于高弹态,塑料制品如果有压力或受到拉伸力作用时,链段就会进行相对更大的位移运动,致使高分子链从卷曲的构象变为伸展的构象。在宏观上,形变大,模量少,时间一长,就具行松驰特性,因此目前国内外用PP-R塑料制成的塑料制品,最高使用温度90-95℃,短时期使用为110℃,目前国家明文规定逐步取消镀锌管,最佳的替代产品为PP-R塑料管材,事实上沸水、锅炉蒸气、温泉的温度有时远大于95℃,长期使用就不能满足此要求。PP-R currently used at home and abroad is a non-toxic, hygienic new polymer chemical material, which is the third type of PP-R, which is the third generation product after the second type of PP-R. The method makes ethylene and propylene randomly polymerized in the molecular chain, but due to the characteristics of its own molecular structure, the use temperature range is narrow. When the temperature rises to the glass transition temperature Tg, the volume of the interstitial space between the molecular chains begins to expand, and the main chain The rotation barrier within the single bond suddenly decreases, the chain segment begins to move, and the polymer begins to change its phase state. At this time, under the action of pressure, as long as the temperature increases by a few degrees, the deformation value suddenly increases dozens of times, and the modulus decreases by 3- 4 orders of magnitude. If the temperature continues to rise, the thermal kinetic energy of the polymer and the volume of the inter-molecular voids can reach the relative displacement movement of the chain segments relatively freely. At this time, the PP-R plastic is already in a highly elastic state. If the plastic product is under pressure or tensile force, the chain segment will undergo a relatively larger displacement movement, causing the polymer chain to change from a curled conformation to an extended conformation. . Macroscopically, the deformation is large, the modulus is small, and it will relax after a long time. Therefore, the plastic products made of PP-R plastic at home and abroad have a maximum service temperature of 90-95°C, and a short-term use of 110°C. At present, the state expressly stipulates that galvanized pipes will be phased out, and the best alternative product is PP-R plastic pipes. In fact, the temperature of boiling water, boiler steam, and hot springs is sometimes much higher than 95°C, and long-term use cannot meet this requirement.

本发明的目的旨在改进上述已有技术的不足,而提供一种耐高温、具有高强度、耐疲劳性和使用寿命长的改性PP-R塑料专用料。The purpose of the present invention is to improve the deficiencies of the above-mentioned prior art, and provide a modified PP-R plastic special material with high temperature resistance, high strength, fatigue resistance and long service life.

为了达到上述目的,本发明是这样实现的:改性PP-R塑料专用料,按重量份,包括PP-R树脂50-75份、工程塑料10-30份、增容剂1-10份、润滑剂0.5-3份。In order to achieve the above object, the present invention is achieved in this way: modified PP-R plastic special material, by weight, includes 50-75 parts of PP-R resin, 10-30 parts of engineering plastics, 1-10 parts of compatibilizer, Lubricant 0.5-3 parts.

本发明改性的PP-R塑料专用料的优选方案,按重量份,包括PP-R树脂55-70份、工程塑料12-25份、增容剂3-8份、润滑剂0.5-2.5份。The preferred version of the modified PP-R plastic special material of the present invention includes 55-70 parts of PP-R resin, 12-25 parts of engineering plastics, 3-8 parts of compatibilizer, and 0.5-2.5 parts of lubricant by weight. .

本发明改性的PP-R塑料专用料的最佳方案,按重量份,包括PP-R树脂67份、工程塑料15.5份、增容剂6.8份、润滑剂0.65份。The best solution of the modified PP-R plastic special material of the present invention comprises 67 parts of PP-R resin, 15.5 parts of engineering plastics, 6.8 parts of compatibilizer and 0.65 parts of lubricant in parts by weight.

本发明所述的改性PP-R塑料专用料,所述的工程塑料为聚甲醛、聚酰胺、聚碳酸酯、聚酰胺-聚苯醚共混物、聚酰胺/苯乙烯-马来酸酐共聚物与聚苯醚共混物、聚苯醚-聚酰胺共混物、聚酰胺/苯乙烯-马来酸酐共聚物、聚酯,可单用也可为任意两种及两种以上的混合;所述的增容剂为乙烯-丙烯酸酯类共聚物、甲基丙烯酸酯-丁苯弹性体接枝共聚物、乙烯-醋酸乙烯共聚物、EPDM(商品代号)、马来酸酐接枝聚烯烃共聚物、美国生产的商品代号C803、日本生产的商品代号HTNA01,可单用也可为任意两种及两种以上的混合;所述的润滑剂为聚乙烯蜡、硬脂酸、硬脂酸单甘酯,可单用也可为任意两种及两种以上的混合。The modified PP-R plastic special material of the present invention, the engineering plastics are polyoxymethylene, polyamide, polycarbonate, polyamide-polyphenylene ether blend, polyamide/styrene-maleic anhydride copolymer Polyphenylene ether blends, polyphenylene ether-polyamide blends, polyamide/styrene-maleic anhydride copolymers, and polyesters can be used alone or in combination of any two or more; The compatibilizer is ethylene-acrylate copolymer, methacrylate-styrene-butadiene elastomer graft copolymer, ethylene-vinyl acetate copolymer, EPDM (product code), maleic anhydride grafted polyolefin copolymer Commodity, product code C803 produced in the United States, product code HTNA01 produced in Japan, can be used alone or in combination of any two or more; the lubricant is polyethylene wax, stearic acid, stearic acid alone Glycerides can be used alone or in combination of any two or more.

本发明所述的改性PP-R塑料专用料,也可加入高熔点聚丙烯7-20份。The modified PP-R plastic special material of the present invention can also add 7-20 parts of high melting point polypropylene.

另外,本发明所述的改性PP-R塑料专用料,还可加入活性纳米材料1-5份。In addition, 1-5 parts of active nanomaterials can also be added to the modified PP-R plastic special material of the present invention.

本发明所述的改性PP-R塑料专用料,可同时加入高熔点聚丙烯7-20份和活性纳米材料1-5份。The modified PP-R plastic special material of the present invention can simultaneously add 7-20 parts of high melting point polypropylene and 1-5 parts of active nanomaterials.

本发明所述的改性PP-R塑料专用料,所述的活性纳米材料为二氧化硅、二氧化钛、碳酸钙。In the modified PP-R plastic special material of the present invention, the active nanomaterials are silicon dioxide, titanium dioxide and calcium carbonate.

本发明的改性PP-R塑料专用料,其制备方法依次包括下列步骤:Modified PP-R plastic special material of the present invention, its preparation method comprises the following steps successively:

a,混料:将各种粉状原料配好后,加入高速搅拌机,搅拌到60-100℃;a. Mixing: After mixing various powdery raw materials, add them to a high-speed mixer and stir to 60-100°C;

b,冷却:将上述混料自动排入冷搅机中,冷却至20-40℃,备用;b. Cooling: automatically discharge the above-mentioned mixture into the cold mixer, cool to 20-40°C, and set aside;

c,造粒:将备好的料加入造粒机,经挤出造粒;c, granulation: put the prepared material into the granulator, and extrude to granulate;

d,冷却切粒:冷切水温为20-45℃;切粒后成为改性PP-R塑料专用料;其中造粒过程造粒机的机筒温度为:输送段:180-195℃;压缩段:190-195℃;熔融段:190-195℃;计量段:190-198℃;机头温度为:机头体190-210℃;口模:190-255℃。d. Cooling and granulation: the temperature of cold cutting water is 20-45°C; after granulation, it becomes a special material for modified PP-R plastics; the barrel temperature of the granulator during the granulation process is: conveying section: 180-195°C; compression Section: 190-195°C; melting section: 190-195°C; metering section: 190-198°C; head temperature: head body 190-210°C; die: 190-255°C.

本发明的改性PP-R塑料专用料,是采用工程塑料对PP-R树脂进行改性,使之形成错综复杂的分子构象,通过分子链互相缠绕在一起,减少应力集中,减少取向,纵横平衡,从而使改性后的PP-R塑料的耐热性、强度,耐疲劳性,使用寿命提高。The modified PP-R plastic special material of the present invention uses engineering plastics to modify PP-R resin to form an intricate molecular conformation, and the molecular chains are entangled with each other to reduce stress concentration, reduce orientation, and balance vertically and horizontally. , so that the heat resistance, strength, fatigue resistance and service life of the modified PP-R plastic are improved.

本发明的改性PP-R塑料专用料与已有技术相比,具有积极效果,采用塑料制品常规的测试工具和手段,测得用改性的PP-R塑料专用料制得的管材最高使用温度为100-123.5℃,比目前的PP-R塑料最高使用温度90-95℃高10-28.5℃;短期使用温度125-131.8℃,比目前的PP-R塑料高15-21.8℃;其拉伸强度≥29MPa,比目前的PP-R塑料拉伸强度大3-6MPa;在0℃时,冲击试验28J,高于目前的PP-R塑料15J;此外其邵氏硬度>75,洛氏硬度>65,弯曲模量>885MPa,弯曲应力>33.5MPa,拉伸弹性模量>818MPa。Compared with the prior art, the modified PP-R plastic special material of the present invention has a positive effect. Using conventional testing tools and means for plastic products, it is measured that the pipe made of the modified PP-R plastic special material has the highest service life. The temperature is 100-123.5°C, which is 10-28.5°C higher than the current maximum use temperature of 90-95°C PP-R plastic; the short-term use temperature is 125-131.8°C, which is 15-21.8°C higher than the current PP-R plastic; Tensile strength ≥ 29MPa, 3-6MPa greater than the current PP-R plastic tensile strength; at 0°C, the impact test is 28J, higher than the current PP-R plastic 15J; in addition, its Shore hardness > 75, Rockwell hardness >65, flexural modulus >885MPa, flexural stress >33.5MPa, tensile modulus >818MPa.

为了更好地理解与实施,下面结合实施例详细说明本发明。For better understanding and implementation, the present invention will be described in detail below in conjunction with the examples.

实施例1,将PP-R树脂(RA130E)67Kg、聚甲醛15.5Kg、乙烯-丙烯酸酯类共聚物6.8Kg、聚乙烯蜡0.65Kg配好后,加入高速搅拌机,搅拌至温度为80℃时,自动排入冷搅机中,冷却至30℃,而后加入温度已设定好的造粒机,造粒机的机筒温度为:输送段:185℃;压缩段:190℃;熔融段:192℃;计量段:194℃;机头温度为:机头体195℃;口模:220℃,经挤出造粒,而后冷却切粒,冷切水温为30℃,切粒后成为改性PP-R塑料专用料。Example 1, after preparing 67Kg of PP-R resin (RA130E), 15.5Kg of polyoxymethylene, 6.8Kg of ethylene-acrylate copolymer, and 0.65Kg of polyethylene wax, add it to a high-speed mixer and stir until the temperature is 80°C. It is automatically discharged into the cold mixer, cooled to 30°C, and then added to the granulator whose temperature has been set. The barrel temperature of the granulator is: conveying section: 185°C; compression section: 190°C; melting section: 192 ℃; metering section: 194°C; head temperature: head body 195°C; die: 220°C, extruded and granulated, then cooled and pelletized, the temperature of the cold cutting water is 30°C, and it becomes modified PP after pelletizing -R plastic special material.

实施例2,将PP-R树脂(RA130E)50Kg、聚酰胺/苯乙烯-马来酸酐共聚物10Kg、甲基丙烯酸-丁苯弹性体接枝共聚物1Kg、硬脂酸0.25Kg、聚乙烯蜡0.25Kg配好后,加入高速搅拌机,搅拌至温度为60℃时,自动排入冷搅机中,冷却至20℃,而后加入温度已设定好的造粒机,造粒机的机筒温度为:输送段:180℃;压缩段:190℃;熔融段:190℃;计量段:190℃;机头温度为:机头体190℃;口模:190℃,经挤出造粒,而后冷却切粒,冷切水温为20℃,切粒后成为改性PP-R塑料专用料。Embodiment 2, with PP-R resin (RA130E) 50Kg, polyamide/styrene-maleic anhydride copolymer 10Kg, methacrylic acid-butadiene styrene elastomer graft copolymer 1Kg, stearic acid 0.25Kg, polyethylene wax After the 0.25Kg is prepared, add it to the high-speed mixer, stir until the temperature is 60°C, automatically discharge it into the cold mixer, cool it to 20°C, and then add the granulator whose temperature has been set, the barrel temperature of the granulator For: conveying section: 180°C; compression section: 190°C; melting section: 190°C; metering section: 190°C; head temperature: head body 190°C; Cooling and pelletizing, the temperature of cold cutting water is 20°C, after pelletizing, it becomes special material for modified PP-R plastics.

实施例3,将PP-R树脂(RA130E)75Kg、聚酰胺-聚苯醚共混物15Kg、聚酰胺15Kg、乙烯-醋酸乙烯共聚物5Kg、马来酸酐接枝聚烯烃共聚物5Kg、硬脂酸单甘酯1Kg、聚乙烯蜡1Kg、硬脂酸1Kg,配好后,加入高速搅拌机,搅拌至温度为100℃时,自动排入冷搅机中,冷却至40℃,而后加入温度已设定好的造粒机,造粒机的机筒温度为:输送段:195℃;压缩段:195℃;熔融段:195℃;计量段:198℃;机头温度为:机头体210℃;口模:255℃,经挤出造粒,而后冷却切粒,冷切水温为45℃,切粒后成为改性PP-R塑料专用料。Embodiment 3, PP-R resin (RA130E) 75Kg, polyamide-polyphenylene ether blend 15Kg, polyamide 15Kg, ethylene-vinyl acetate copolymer 5Kg, maleic anhydride grafted polyolefin copolymer 5Kg, stearin 1Kg of monoglyceride, 1Kg of polyethylene wax, and 1Kg of stearic acid. After preparation, add to a high-speed blender, stir until the temperature is 100°C, automatically discharge into the cold blender, cool to 40°C, and then add The barrel temperature of the fixed granulator is: conveying section: 195°C; compression section: 195°C; melting section: 195°C; metering section: 198°C; head temperature: head body 210°C Die: 255°C, extruded and granulated, and then cooled and cut into pellets. The temperature of the cold cutting water is 45°C. After pelletizing, it becomes a special material for modified PP-R plastics.

实施例4,将PP-R树脂(RA130E)70Kg、聚甲醛8Kg、聚碳酸酯8Kg、聚酰胺/苯乙烯-马来酸酐共聚物与聚苯醚共混物9Kg、高熔点聚丙烯7Kg、二氧化硅1Kg、EPDM 3Kg、乙烯-醋酸乙烯共聚物3Kg、乙烯-丙烯酸酯类共聚物3Kg、聚乙烯蜡1.0Kg配好后,加入高速搅拌机,搅拌至温度为75℃时,自动排入冷搅机中,冷却至25℃,而后加入温度已设定好的造粒机,造粒机的机筒温度为:输送段:192℃;压缩段:194℃;熔融段:195℃;计量段:195℃;机头温度为:机头体205℃;口模:245℃,经挤出造粒,而后冷却切粒,冷切水温为40℃,切粒后成为改性PP-R塑料专用料。Example 4, PP-R resin (RA130E) 70Kg, polyoxymethylene 8Kg, polycarbonate 8Kg, polyamide/styrene-maleic anhydride copolymer and polyphenylene ether blend 9Kg, high melting point polypropylene 7Kg, two Silicon oxide 1Kg, EPDM 3Kg, ethylene-vinyl acetate copolymer 3Kg, ethylene-acrylic acid ester copolymer 3Kg, polyethylene wax 1.0Kg After mixing, add to a high-speed mixer, stir until the temperature is 75°C, and then automatically discharge into the cold stirring In the machine, cool to 25°C, and then add the granulator whose temperature has been set. The barrel temperature of the granulator is: conveying section: 192°C; compression section: 194°C; melting section: 195°C; metering section: 195°C; head temperature: head body 205°C; die: 245°C, extruded and granulated, then cooled and cut into pellets, the cold cutting water temperature is 40°C, after pelletizing, it becomes a special material for modified PP-R plastics .

实施例5,将PP-R树脂(RA130E)60Kg、聚酰胺/苯乙烯-马来酸酐共聚物10Kg、聚酰胺10Kg、高熔点聚丙烯15Kg、马来酸酐接枝烯烃共聚物5Kg、硬脂酸2.0Kg配好后,加入高速搅拌机,搅拌至温度为90℃时,自动排入冷搅机中,冷却至35℃,而后加入温度已设定好的造粒机,造粒机的机筒温度为:输送段:190℃;压缩段:192℃;熔融段:193℃;计量段:195℃;机头温度为:机头体200℃;口模:240℃,经挤出造粒,而后冷却切粒,冷切水温为40℃,切粒后成为改性PP-R塑料专用料。Embodiment 5, with PP-R resin (RA130E) 60Kg, polyamide/styrene-maleic anhydride copolymer 10Kg, polyamide 10Kg, high melting point polypropylene 15Kg, maleic anhydride graft olefin copolymer 5Kg, stearic acid After 2.0Kg is prepared, add it to a high-speed mixer and stir until the temperature is 90°C, then automatically discharge it into the cold mixer, cool it to 35°C, and then add it to the granulator whose temperature has been set. The temperature of the barrel of the granulator For: conveying section: 190°C; compression section: 192°C; melting section: 193°C; metering section: 195°C; head temperature: head body 200°C; Cooling and pelletizing, the temperature of cold cutting water is 40°C, after pelletizing, it becomes special material for modified PP-R plastics.

实施例6,将PP-R树脂(RA130E)55Kg、聚酰胺/苯乙烯-马来酸酐共聚物4Kg、聚苯醚-聚酰胺共混物4KG、聚酰胺/苯乙烯-马来酸酐共聚物与聚苯醚4Kg、二氧化硅3Kg、C803 3.0Kg、聚乙烯蜡1.5Kg配好后,加入高速搅拌机,搅拌至温度为70℃时,自动排入冷搅机中,冷却至28℃,而后加入温度已设定好的造粒机,造粒机的机筒温度为:输送段:182℃;压缩段:191℃;熔融段:192℃;计量段:192℃;机头温度为:机头体195℃;口模:200℃,经挤出造粒,而后冷却切粒,冷切水温为35℃,切粒后成为改性PP-R塑料专用料。Embodiment 6, PP-R resin (RA130E) 55Kg, polyamide/styrene-maleic anhydride copolymer 4Kg, polyphenylene ether-polyamide blend 4KG, polyamide/styrene-maleic anhydride copolymer and After mixing 4Kg of polyphenylene ether, 3Kg of silicon dioxide, 3.0Kg of C803, and 1.5Kg of polyethylene wax, add it to a high-speed mixer, stir until the temperature reaches 70°C, then automatically discharge it into the cold blender, cool to 28°C, and then add The temperature of the granulator has been set. The barrel temperature of the granulator is: conveying section: 182°C; compression section: 191°C; melting section: 192°C; metering section: 192°C; head temperature: head Body 195°C; Die: 200°C, extruded and granulated, and then cooled and cut into pellets. The temperature of the cold cutting water is 35°C. After pelletizing, it becomes a special material for modified PP-R plastics.

实施例7,将PP-R树脂(RA130E)65Kg、聚酯18Kg、高熔点聚丙烯20Kg、二氧化钛5Kg、HTNAO1 8Kg、硬脂酸单甘酯2.5Kg配好后,加入高速搅拌机,搅拌至温度为75℃时,自动排入冷搅机中,冷却至25℃,而后加入温度已设定好的造粒机,造粒机的机筒温度为:输送段:188℃;压缩段:192℃;熔融段:194℃;计量段:196℃;机头温度为:机头体198℃;口模:235℃,经挤出造粒,而后冷却切粒,冷切水温为30℃,切粒后成为改性PP-R塑料专用料。Embodiment 7, after PP-R resin (RA130E) 65Kg, polyester 18Kg, high melting point polypropylene 20Kg, titanium dioxide 5Kg, HTNAO1 8Kg, stearic acid monoglyceride 2.5Kg are prepared, add high-speed mixer, stir until temperature is At 75°C, it will be automatically discharged into the cold mixer, cooled to 25°C, and then added to the granulator whose temperature has been set. The barrel temperature of the granulator is: conveying section: 188°C; compression section: 192°C; Melting section: 194°C; metering section: 196°C; machine head temperature: machine head body 198°C; die: 235°C, extruded and granulated, then cooled and pelletized, the temperature of the cold cutting water is 30°C, after pelletizing Become a special material for modified PP-R plastics.

本发明的改性PP-R塑料专用料,可用通用的塑料加工设备和工艺,经挤出机制成塑料管,广泛用于建筑物内的冷热水系统、采暖系统、中央空调系统、输送或排放化学介质等,另外还可以按常规工艺制成各种塑料容器。The modified PP-R plastic special material of the present invention can be made into plastic pipes through extruders with general plastic processing equipment and techniques, and is widely used in cold and hot water systems, heating systems, central air-conditioning systems, transportation or Discharge chemical media, etc., and can also be made into various plastic containers according to conventional processes.

Claims (10)

1, special material for modifying PP-R plastics by weight, comprises PP-R resin 50-75 part, engineering plastics 10-30 part, expanding material 1-10 part, lubricant 0.5-3 part.
2, by the described special material for modifying PP-R plastics of claim 1, by weight, comprise PP-R resin 55-70 part, engineering plastics 12-25 part, expanding material 3-8 part, lubricant 0.5-2.5 part.
3, by the described special material for modifying PP-R plastics of claim 1, by weight, comprise 67 parts of PP-R resins, 15.5 parts in engineering plastics, 6.8 parts of expanding materials, 0.65 part of lubricant.
4, by claim 1 or 2 or 3 described special material for modifying PP-R plastics, it is characterized in that described engineering plastics are polyoxymethylene, polymeric amide, polycarbonate, polyamide-polyphenylene ether blend, polymeric amide/styrene-maleic anhydride copolymer and polyphenylene ether blend, polyphenylene ether-polyamide blend, polymeric amide/styrene-maleic anhydride copolymer, polyester, can be singly with also can be any two kinds and two or more mixing.
5, by claim 1 or 2 or 3 described special material for modifying PP-R plastics, it is characterized in that described expanding material is ethylene-acrylate copolymer, methacrylic ester-butadiene-styrene elastomer graft copolymer, ethylene-vinyl acetate copolymer, terpolymer EP rubber EPDM, maleic anhydride graft polyolefin copolymer, polymeric amide/rubber blend C803, polymeric amide/rubber blend HTNA01, can be singly with also can be any two kinds and two or more mixing.
6, by claim 1 or 2 or 3 described special material for modifying PP-R plastics, it is characterized in that described lubricant is polyethylene wax, stearic acid, stearic acid monoglycerides, can be singly with also can be any two kinds and two or more mixing.
7, by the described special material for modifying PP-R plastics of claim 1, it is characterized in that also can adding high-melting-point polypropylene 7-20 part.
8, by the described special material for modifying PP-R plastics of claim 1, it is characterized in that also can adding active nano material 1-5 part.
9, by the described special material for modifying PP-R plastics of claim 7, it is characterized in that also can adding active nano material 1-5 part.
10, by claim 8 or 9 described special material for modifying PP-R plastics, it is characterized in that described nano material is silicon-dioxide, titanium dioxide, lime carbonate.
CN00123963A 2000-10-25 2000-10-25 Special material for modifying PP-R plastics and its preparing process Expired - Fee Related CN1105742C (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0259960A2 (en) * 1986-09-01 1988-03-16 Imperial Chemical Industries Plc Polymer additive concentrate
EP0330015A2 (en) * 1988-02-20 1989-08-30 BASF Aktiengesellschaft Thermoplastic polypropylene polyamide compounds, process for their manufacture and their use
DE4404492A1 (en) * 1993-12-06 1995-06-14 Becker Plastics Gmbh Multilayer composite tube for hot water, sanitary applications etc.
JPH1011828A (en) * 1996-06-21 1998-01-16 So Fukada Magneto-optical recorded data reproducing device
DE29801191U1 (en) * 1998-01-26 1998-04-09 ALPHACAN Omniplast GmbH, 35630 Ehringshausen Street drain
CN1265969A (en) * 2000-04-07 2000-09-13 余杭市康运塑业有限公司 Atactic copolypropylene pipe with marking line and making method thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0259960A2 (en) * 1986-09-01 1988-03-16 Imperial Chemical Industries Plc Polymer additive concentrate
EP0330015A2 (en) * 1988-02-20 1989-08-30 BASF Aktiengesellschaft Thermoplastic polypropylene polyamide compounds, process for their manufacture and their use
DE4404492A1 (en) * 1993-12-06 1995-06-14 Becker Plastics Gmbh Multilayer composite tube for hot water, sanitary applications etc.
JPH1011828A (en) * 1996-06-21 1998-01-16 So Fukada Magneto-optical recorded data reproducing device
DE29801191U1 (en) * 1998-01-26 1998-04-09 ALPHACAN Omniplast GmbH, 35630 Ehringshausen Street drain
CN1265969A (en) * 2000-04-07 2000-09-13 余杭市康运塑业有限公司 Atactic copolypropylene pipe with marking line and making method thereof

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