CN102604293A - Thermoplastically processable polyvinyl alcohol composite and preparation method thereof - Google Patents
Thermoplastically processable polyvinyl alcohol composite and preparation method thereof Download PDFInfo
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- 239000004372 Polyvinyl alcohol Substances 0.000 title claims abstract description 64
- 229920002451 polyvinyl alcohol Polymers 0.000 title claims abstract description 64
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- 239000002131 composite material Substances 0.000 title abstract description 5
- XUMBMVFBXHLACL-UHFFFAOYSA-N Melanin Chemical compound O=C1C(=O)C(C2=CNC3=C(C(C(=O)C4=C32)=O)C)=C2C4=CNC2=C1C XUMBMVFBXHLACL-UHFFFAOYSA-N 0.000 claims abstract description 66
- 239000004014 plasticizer Substances 0.000 claims abstract description 9
- 230000004888 barrier function Effects 0.000 claims abstract description 8
- 239000000203 mixture Substances 0.000 claims description 28
- 238000012545 processing Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 239000012153 distilled water Substances 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 4
- 238000006136 alcoholysis reaction Methods 0.000 claims description 2
- 239000008187 granular material Substances 0.000 claims description 2
- 239000012456 homogeneous solution Substances 0.000 claims description 2
- 238000006116 polymerization reaction Methods 0.000 claims description 2
- 238000002844 melting Methods 0.000 abstract description 23
- 230000008018 melting Effects 0.000 abstract description 23
- 238000005979 thermal decomposition reaction Methods 0.000 abstract description 20
- 239000000463 material Substances 0.000 abstract description 4
- 238000010128 melt processing Methods 0.000 abstract description 4
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 238000013508 migration Methods 0.000 abstract 1
- 230000005012 migration Effects 0.000 abstract 1
- 238000012856 packing Methods 0.000 abstract 1
- 229920002978 Vinylon Polymers 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- 229920001169 thermoplastic Polymers 0.000 description 5
- 239000004416 thermosoftening plastic Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000007731 hot pressing Methods 0.000 description 3
- 239000010410 layer Substances 0.000 description 3
- 229920002521 macromolecule Polymers 0.000 description 3
- 238000011056 performance test Methods 0.000 description 3
- 239000002356 single layer Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 229920006257 Heat-shrinkable film Polymers 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000002828 fuel tank Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 231100000252 nontoxic Toxicity 0.000 description 2
- 230000003000 nontoxic effect Effects 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 2
- 239000004926 polymethyl methacrylate Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000071 blow moulding Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 229920006280 packaging film Polymers 0.000 description 1
- 239000012785 packaging film Substances 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 150000008442 polyphenolic compounds Chemical group 0.000 description 1
- 235000013824 polyphenols Nutrition 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000010129 solution processing Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000003017 thermal stabilizer Substances 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000002166 wet spinning Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/04—Particle-shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/92895—Barrel or housing
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
技术领域 technical field
本发明涉及一种可热塑性加工的聚乙烯醇组合物及其制备方法,该组合物用于薄膜产品,例如单层薄膜、多层共挤薄膜、双向拉伸薄膜、热收缩薄膜,各种中空容器,例如汽车油箱、瓶、桶等,各类管材,例如燃油或输油管,各类片材等的高阻隔产品。The invention relates to a polyvinyl alcohol composition capable of thermoplastic processing and a preparation method thereof. The composition is used for film products, such as single-layer film, multi-layer co-extruded film, biaxially stretched film, heat-shrinkable film, various hollow Containers, such as automobile fuel tanks, bottles, barrels, etc., various types of pipes, such as fuel or oil pipelines, and high barrier products such as various sheets.
背景技术 Background technique
聚乙烯醇(PVA)是一种综合性能优异的可由非石油路线大规模生产的高分子聚合物,具有优异的耐油、耐溶剂及气体阻隔性,在烃类溶剂、农药、石油等包装运输方面具有独特优势。由于PVA高分子链相邻羟基间易形成大量的分子内和分子间氢键,使其热分解温度(200-250℃)与熔点(226℃)接近,熔融即分解,难以热塑加工。目前PVA的应用基于溶液加工成型,通过湿法纺丝、流延成膜制备纤维、薄膜等低维制品或用作助、辅材料,难以制备厚壁和形状复杂的三维制品,这极大地限制了PVA的应用与发展。Polyvinyl alcohol (PVA) is a high-molecular polymer with excellent comprehensive properties that can be produced on a large scale by non-petroleum routes. It has excellent oil resistance, solvent resistance and gas barrier properties. It is used in packaging and transportation of hydrocarbon solvents, pesticides, petroleum, etc. Has unique advantages. Since a large number of intramolecular and intermolecular hydrogen bonds are easily formed between the adjacent hydroxyl groups of the PVA polymer chain, its thermal decomposition temperature (200-250°C) is close to the melting point (226°C), and it decomposes when it melts, making it difficult for thermoplastic processing. At present, the application of PVA is based on solution processing and forming. It is difficult to prepare three-dimensional products with thick walls and complex shapes through wet spinning and casting to prepare low-dimensional products such as fibers and films or as auxiliary materials. The application and development of PVA.
目前,对于PVA熔融加工技术,JP77110782A报道了一种熔融吹塑聚乙烯醇的成膜方法,其技术采用大量水(含量大于40%)作为增塑剂,以降低PVA的熔点,使其在低于PVA的分解温度下实现吹塑成膜。但这种制备方法在实际生产中稳定性不好,由于大量水的存在,树脂在挤出过程中容易起泡,导致薄膜无法均匀成型。At present, for PVA melt processing technology, JP77110782A has reported a kind of film-forming method of melt blowing polyvinyl alcohol, and its technology adopts a large amount of water (content greater than 40%) as plasticizer, to reduce the melting point of PVA, make it in low Blow molding is realized at the decomposition temperature of PVA. However, this preparation method has poor stability in actual production. Due to the presence of a large amount of water, the resin is prone to foaming during extrusion, resulting in the inability to uniformly form the film.
而CN1368515公开了一种用于热塑加工聚乙烯醇薄膜的新型增速方法,该方法主要选择一种可聚合的酰胺类单体作为增塑剂,以及控制水在树脂中更多以结合水的形式存在,因而有效地降低了PVA树脂的加工温度,但是该方法选用的增塑剂具有一定的毒性,使制备的薄膜不适合做环保和食品包装膜。And CN1368515 discloses a kind of novel speed-increasing method that is used for thermoplastic processing polyvinyl alcohol film, and this method mainly selects a kind of polymerizable amides monomer as plasticizer, and controls water to be more in resin to bind water The form exists, thereby effectively reducing the processing temperature of PVA resin, but the plasticizer selected by this method has certain toxicity, so that the prepared film is not suitable for environmental protection and food packaging film.
要实现聚乙烯醇熔融加工,一般来说必须要加入大量的增塑剂才能显著降低PVA树脂的熔点,改善流动性。但是增塑剂大量的加入会造成PVA综合性能(刚性、强度、阻隔性能)的下降,而且增塑剂容易迁移污染包装物。因此最具应用前景的方法是添加少量助剂实现PVA的热塑加工。To achieve polyvinyl alcohol melt processing, generally speaking, a large amount of plasticizer must be added to significantly reduce the melting point of PVA resin and improve fluidity. However, the addition of a large amount of plasticizer will cause the decline of PVA's comprehensive performance (rigidity, strength, barrier performance), and the plasticizer is easy to migrate and pollute the packaging. Therefore, the most promising method is to add a small amount of additives to realize the thermoplastic processing of PVA.
最近,Macromolecules,20 11,44,9499-9507:“Thermooxidative Stabilizationof Polymers Using Natural and Synthetic Melanins”一文中报道了黑色素(Melanin)可作为聚甲基丙烯酸甲酯的高效热稳定剂大幅度提高聚合物的热分解温度,少量(0.5~5wt%)黑色素能使PMMA的热分解温度提高50~90℃。但是至今没有研究将黑色素用于聚乙烯的体系,用于改善聚乙烯醇的熔融加工性能。Recently, Macromolecules, 20 11, 44, 9499-9507: "Thermooxidative Stabilization of Polymers Using Natural and Synthetic Melanins" reported that melanin (Melanin) can be used as a high-efficiency thermal stabilizer of polymethyl methacrylate to greatly improve the thermal stability of polymers. Thermal decomposition temperature, a small amount (0.5-5wt%) of melanin can increase the thermal decomposition temperature of PMMA by 50-90°C. However, there has been no research on the use of melanin in polyethylene systems to improve the melt processability of polyvinyl alcohol.
发明内容 Contents of the invention
黑色素是一种含有多酚和氨基结构的生物大分子,广泛存在于动植物中,在人体中起到抗氧化作用,可以迅速捕获高分子链断裂产生的烷基自由基、烷氧自由基以及过氧化自由基,防止聚合物热氧化降解。Melanin is a biomacromolecule containing polyphenols and amino structures. It is widely found in animals and plants and plays an antioxidant role in the human body. It can quickly capture the alkyl radicals, alkoxyl radicals and Peroxide free radicals to prevent thermal oxidative degradation of polymers.
基于以上原因,本发明人利用黑色素改性PVA,所得PVA复合材料的熔点降低、热分解温度升高,获得宽熔融加工窗口,实现熔融加工,该材料经熔融加工后,黑色素的添加量小,而且,黑色素属于生物大分子,无毒,所得聚乙烯醇组合物的综合性能优异。Based on the above reasons, the present inventor utilizes melanin to modify PVA, the melting point of the obtained PVA composite material decreases, the thermal decomposition temperature increases, and a wide melting processing window is obtained to realize melting processing. After the material is melt processed, the amount of melanin added is small, Moreover, melanin belongs to biological macromolecules and is non-toxic, and the obtained polyvinyl alcohol composition has excellent comprehensive properties.
本发明的目的是提供一种可热塑加工的聚乙烯醇组合物,该组合物中含有少量黑色素,综合性能优异。The purpose of the present invention is to provide a thermoplastically processable polyvinyl alcohol composition, which contains a small amount of melanin and has excellent comprehensive properties.
本发明的另一个目的是提供该组合物的制备方法。Another object of the present invention is to provide a method for the preparation of the composition.
本发明的一种聚乙烯醇组合物,其特征在于该组合物复合的以下组分:聚乙烯醇、黑色素,聚乙烯醇∶黑色素之间重量比为(85~99.8)∶(15~0.2)。A kind of polyvinyl alcohol composition of the present invention is characterized in that the following components of this composition compound: polyvinyl alcohol, melanin, polyvinyl alcohol: the weight ratio between melanin is (85~99.8): (15~0.2) .
本发明中的聚乙烯醇,其特征在于聚乙烯醇的聚合度为1700~2400,醇解度为92~100%。The polyvinyl alcohol in the present invention is characterized in that the degree of polymerization of the polyvinyl alcohol is 1700-2400, and the degree of alcoholysis is 92-100%.
本发明中的黑色素包括现有技术所公开的各种类型的天然提取黑色素、化学合成和生物发酵法制备的类黑色素。The melanin in the present invention includes various types of naturally extracted melanin disclosed in the prior art, and melanoids prepared by chemical synthesis and biological fermentation.
本发明中一种聚乙烯醇组合物的制备方法,其特征在于包含有以下步骤之一的方法制备而得:A preparation method of a polyvinyl alcohol composition in the present invention is characterized in that it is prepared by a method comprising one of the following steps:
(a)将聚乙烯醇、黑色素按一定比例加入搅拌机中,充分混合均匀,再将所得预混料放入双螺杆挤出机中,加工温度控制在170~250℃,经熔融塑化造粒。(a) Add polyvinyl alcohol and melanin into the mixer in a certain proportion, mix thoroughly and evenly, then put the obtained premix into a twin-screw extruder, control the processing temperature at 170-250°C, and melt, plasticize and granulate .
(b)将聚乙烯醇放入蒸馏水中配置成均匀溶液,再将黑色素和碱性物质按一定的重量比加入,经搅拌混合均匀、干燥后得到聚乙烯醇组合物。(b) Put polyvinyl alcohol into distilled water to form a homogeneous solution, then add melanin and alkaline substances in a certain weight ratio, stir and mix evenly, and dry to obtain a polyvinyl alcohol composition.
以上所述的聚乙烯醇组合物,可利用各类单层或多层可热塑性加工的挤出加工设备,制作各类含该组合物的薄膜,包括:单层薄膜、多层共机薄膜、双向拉伸薄膜、热收缩薄膜;中空容器,包括:汽车油箱、瓶、桶;各类管材,包括燃油或输油管,各类片材等一切利用该材料制作的高阻隔产品。The above-mentioned polyvinyl alcohol composition can utilize various single-layer or multi-layer extrusion processing equipment that can be thermoplastically processed to produce various films containing the composition, including: single-layer film, multi-layer co-organic film, Biaxially stretched film, heat-shrinkable film; hollow containers, including: automotive fuel tanks, bottles, barrels; various types of pipes, including fuel or oil pipelines, various sheets, and other high-barrier products made of this material.
本发明的有益效果:Beneficial effects of the present invention:
(1)本发明加入少量的黑色素,在提高聚乙烯醇的热分解温度同时又降低聚乙烯醇的熔点,获得较宽的熔融加工窗口实现热塑加工;(1) The present invention adds a small amount of melanin, increases the thermal decomposition temperature of polyvinyl alcohol and reduces the melting point of polyvinyl alcohol at the same time, obtains wider melt processing window and realizes thermoplastic processing;
(2)由于加入黑色素的量小,且黑色素属于生物大分子,具有以下优点:一方面,所制备的聚乙烯醇组合物环保、无毒,而且助剂不易析出,可用于各种产品;另一方面,黑色素对聚乙烯醇的综合性能影响小,拉伸性能保持在较高的水平;(2) Because the amount of melanin added is small, and melanin belongs to biological macromolecules, it has the following advantages: on the one hand, the prepared polyvinyl alcohol composition is environmentally friendly and non-toxic, and the auxiliary agent is not easy to separate out, so it can be used in various products; On the one hand, melanin has little effect on the comprehensive properties of polyvinyl alcohol, and the tensile properties remain at a high level;
(3)该方法简单可行、易于操作。(3) The method is simple, feasible and easy to operate.
具体实施方式 Detailed ways
下面结合实施例进一步描述本发明,本发明的范围不受这些实施例的限制。本发明的范围在权利要求书中提出。Further describe the present invention below in conjunction with embodiment, the scope of the present invention is not limited by these embodiment. The scope of the present invention is set forth in the claims.
实施例1Example 1
称取99.5g聚乙烯醇(中石化四川维尼纶厂,牌号1799)与900g蒸馏水在95℃下加热溶解,然后将0.5g黑色素加入溶液中搅拌混合均匀,随后将混合溶液倒入容器中,在60℃下真空干燥得到样品,进行热压成型制备标准样条,按GB-13022标准进行拉伸性能测试,采用热失重分析仪和差失扫描量热仪测试其热分解温度、熔点。Weigh 99.5g of polyvinyl alcohol (Sinopec Sichuan Vinylon Factory, brand 1799) and 900g of distilled water to dissolve under heating at 95°C, then add 0.5g of melanin into the solution and stir to mix evenly, then pour the mixed solution into a container, The samples were obtained by vacuum drying at ℃, and the standard specimens were prepared by hot pressing. The tensile properties were tested according to the GB-13022 standard. The thermal decomposition temperature and melting point were tested by a thermogravimetric analyzer and a differential scanning calorimeter.
所得薄膜的拉伸强度为60MPa,断裂伸长率为267%,热分解温度为255℃,熔点为226℃。The tensile strength of the obtained film was 60 MPa, the elongation at break was 267%, the thermal decomposition temperature was 255°C, and the melting point was 226°C.
实施例2Example 2
称取95g聚乙烯醇(中石化四川维尼纶厂,牌号1799)与900g蒸馏水在95℃下加热溶解,然后将黑色素(自制)5g加入溶液中搅拌混合均匀,随后将混合溶液倒入容器中,在60℃下真空干燥得到样品,进行热压成型制备标准样条,按GB-13022标准进行拉伸性能测试,采用热失重分析仪和差失扫描量热仪测试其热分解温度、熔点。Weigh 95g of polyvinyl alcohol (Sinopec Sichuan Vinylon Factory, brand 1799) and 900g of distilled water to dissolve under heating at 95°C, then add 5g of melanin (self-made) into the solution and stir to mix evenly, then pour the mixed solution into a container, Vacuum-dried at 60°C to obtain samples, and then hot-pressed to prepare standard specimens. The tensile properties were tested according to the GB-13022 standard. The thermal decomposition temperature and melting point were tested by thermogravimetric analyzer and differential scanning calorimeter.
所得薄膜的拉伸强度为56MPa,断裂伸长率为320%,热分解温度为271℃,熔点为212℃。The tensile strength of the obtained film was 56MPa, the elongation at break was 320%, the thermal decomposition temperature was 271°C, and the melting point was 212°C.
实施例3Example 3
分别称取聚乙烯醇(中石化四川维尼纶厂,牌号1799)475g、黑色素25g加入搅拌机中,充分混合均匀,再将预混料放入双螺杆挤出机中,螺杆温度为220~225℃,螺杆转速为100rpm,挤出造粒,在进行热压成型制备标准样条,按GB-13022标准进行拉伸性能测试,采用热失重分析仪和差失扫描量热仪测试其热分解温度、熔点。Weigh 475g of polyvinyl alcohol (Sinopec Sichuan Vinylon Factory, brand 1799) and 25g of melanin into a mixer, mix well, and then put the premix into a twin-screw extruder with a screw temperature of 220-225°C. The screw speed is 100rpm, extruded and granulated, the standard sample is prepared by hot pressing, the tensile performance test is carried out according to the GB-13022 standard, and the thermal decomposition temperature and melting point are tested by a thermogravimetric analyzer and a differential scanning calorimeter. .
所得薄膜的拉伸强度为55MPa,断裂伸长率为270%,热分解温度为270℃,熔点为211℃。The tensile strength of the obtained film was 55 MPa, the elongation at break was 270%, the thermal decomposition temperature was 270°C, and the melting point was 211°C.
实施例4Example 4
分别称取聚乙烯醇(中石化四川维尼纶厂,牌号1799)450g、黑色素50g加入搅拌机中,充分混合均匀,再将预混料放入双螺杆挤出机中,螺杆温度为215~222℃,螺杆转速为100rpm,挤出造粒,在进行热压成型制备标准样条,按GB-13022标准进行拉伸性能测试,采用热失重分析仪和差失扫描量热仪测试其热分解温度、熔点。Weigh 450g of polyvinyl alcohol (Sinopec Sichuan Vinylon Factory, brand 1799) and 50g of melanin into a mixer, mix well, and then put the premix into a twin-screw extruder with a screw temperature of 215-222°C. The screw speed is 100rpm, extruded and granulated, the standard sample is prepared by hot pressing, the tensile performance test is carried out according to the GB-13022 standard, and the thermal decomposition temperature and melting point are tested by a thermogravimetric analyzer and a differential scanning calorimeter. .
所得薄膜的拉伸强度为53MPa,断裂伸长率为250%,热分解温度为281℃,熔点为205℃。The tensile strength of the obtained film was 53 MPa, the elongation at break was 250%, the thermal decomposition temperature was 281°C, and the melting point was 205°C.
比较例1:Comparative example 1:
称取100g聚乙烯醇(中石化四川维尼纶厂,牌号1799)与900g蒸馏水在95℃下加热溶解,然后将溶液倒入容器中,在60℃下真空干燥得到样品,进行裁剪制备标准样条,按GB-13022标准进行拉伸性能测试,采用热失重分析仪和差失扫描量热仪测试其热分解温度、熔点。Weigh 100g of polyvinyl alcohol (Sinopec Sichuan Vinylon Factory, brand 1799) and 900g of distilled water, heat and dissolve at 95°C, then pour the solution into a container, dry it in vacuum at 60°C to obtain a sample, and cut it to prepare a standard sample. The tensile performance test was carried out according to the GB-13022 standard, and the thermal decomposition temperature and melting point were tested by a thermogravimetric analyzer and a differential scanning calorimeter.
所得薄膜的拉伸强度为58MPa,断裂伸长率为312%,热分解温度为233℃,熔点为231℃。The tensile strength of the obtained film was 58MPa, the elongation at break was 312%, the thermal decomposition temperature was 233°C, and the melting point was 231°C.
与比较例1相比,由于实施例1中加入重量比为0.5%的黑色素,实施例1中的热分解温度提高了22℃,熔点降低了5℃,而且,拉伸强度和断裂伸长率变化不大。与比较例1相比,由于实施例2中加入重量比为5%的黑色素,实施例2中的热分解温度提高了38℃,熔点降低了19℃,而且拉伸强度和断裂伸长率变化不大。与比较例1相比,实施例中加入的黑色素越多,其热分解温度提高得越多,熔点降低得越多,热分解温度与熔点的差值越大,越有利于熔融加工,同时,其拉伸性能变化不大,维持在较高水平。Compared with Comparative Example 1, due to the addition of 0.5% melanin by weight in Example 1, the thermal decomposition temperature in Example 1 has increased by 22 ° C, and the melting point has decreased by 5 ° C. Moreover, the tensile strength and elongation at break Has not changed much. Compared with Comparative Example 1, due to the addition of 5% melanin by weight in Example 2, the thermal decomposition temperature in Example 2 increased by 38°C, the melting point decreased by 19°C, and the tensile strength and elongation at break changed not big. Compared with Comparative Example 1, the more melanin added in the embodiment, the more the thermal decomposition temperature increases, the more the melting point decreases, and the larger the difference between the thermal decomposition temperature and the melting point is, the more conducive to melting processing. At the same time, Its tensile properties did not change much and remained at a high level.
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CN105524384A (en) * | 2014-09-29 | 2016-04-27 | 中国石油化工集团公司 | Melt-processable polyvinyl alcohol masterbatch and preparation method thereof |
CN106884213A (en) * | 2017-04-11 | 2017-06-23 | 大连天马可溶制品有限公司 | A kind of low temperature water-soluble polyvinyl alcohol long filament and preparation method thereof |
CN111004406A (en) * | 2019-12-30 | 2020-04-14 | 北京林业大学 | Preparation method of novel anti-ultraviolet and anti-oxidation film |
US20210269450A1 (en) * | 2018-06-21 | 2021-09-02 | Steven Baranowitz | Impact resistant material |
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CN101233196A (en) * | 2005-07-15 | 2008-07-30 | 艾姆基希薄膜株式会社 | Process for producing melanin, melanin produced by the process, functional film containing the melanin, and process for producing the same |
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CN105524384A (en) * | 2014-09-29 | 2016-04-27 | 中国石油化工集团公司 | Melt-processable polyvinyl alcohol masterbatch and preparation method thereof |
CN105524384B (en) * | 2014-09-29 | 2019-03-26 | 中国石油化工集团公司 | A kind of melt-processable polyvinyl alcohol master batch and preparation method thereof |
CN106884213A (en) * | 2017-04-11 | 2017-06-23 | 大连天马可溶制品有限公司 | A kind of low temperature water-soluble polyvinyl alcohol long filament and preparation method thereof |
US20210269450A1 (en) * | 2018-06-21 | 2021-09-02 | Steven Baranowitz | Impact resistant material |
CN111004406A (en) * | 2019-12-30 | 2020-04-14 | 北京林业大学 | Preparation method of novel anti-ultraviolet and anti-oxidation film |
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