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CN111234348B - Special material for buried polyethylene structural wall pipeline and preparation method thereof - Google Patents

Special material for buried polyethylene structural wall pipeline and preparation method thereof Download PDF

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CN111234348B
CN111234348B CN202010133610.4A CN202010133610A CN111234348B CN 111234348 B CN111234348 B CN 111234348B CN 202010133610 A CN202010133610 A CN 202010133610A CN 111234348 B CN111234348 B CN 111234348B
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polyethylene
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parts
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buried
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CN111234348A (en
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陈振树
黄险波
叶南飚
陈锬
宋晓庆
陈平绪
程杰
汪海
刘惠文
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Jiangsu Jinfa Renewable Resources Co ltd
Kingfa Science and Technology Co Ltd
Guangdong Kingfa Science and Technology Co Ltd
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Jiangsu Golden Hair Environmental Protection Technology Co ltd
Kingfa Science and Technology Co Ltd
Guangdong Kingfa Science and Technology Co Ltd
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/06Polyethene
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/08Copolymers of ethene
    • C08L23/0807Copolymers of ethene with unsaturated hydrocarbons only containing four or more carbon atoms
    • C08L23/0815Copolymers of ethene with unsaturated hydrocarbons only containing four or more carbon atoms with aliphatic 1-olefins containing one carbon-to-carbon double bond
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
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    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/18Applications used for pipes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C08L2205/025Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/06Properties of polyethylene
    • C08L2207/062HDPE
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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Abstract

本发明公开了一种埋地聚乙烯结构壁管道专用料,包含以下重量份的制备原料:管材级聚乙烯10~40份、中空级聚乙烯10~30份、注塑级聚乙烯3~10份、薄膜级线性聚乙烯20~45份、炭黑母粒4~6份、外观改善剂1~3份和耐环境应力开裂调节剂4~10份。本发明所述埋地聚乙烯结构壁管道专用料选择管材级聚乙烯、中空级聚乙烯、注塑级聚乙烯和薄膜级线性聚乙烯四种不同级别的聚乙烯,可以制得具有优异机械性能和外观性能的再生埋地聚乙烯结构壁管道。本发明还公开了所述埋地聚乙烯结构壁管道专用料的制备方法,采用该方法能够制得性能均一的埋地聚乙烯结构壁管道专用料。The invention discloses a special material for buried polyethylene structural wall pipes, comprising the following preparation raw materials in parts by weight: 10-40 parts of pipe-grade polyethylene, 10-30 parts of hollow-grade polyethylene, and 3-10 parts of injection-molded polyethylene , 20-45 parts of film-grade linear polyethylene, 4-6 parts of carbon black masterbatch, 1-3 parts of appearance improving agent and 4-10 parts of environmental stress cracking regulator. The special material for the buried polyethylene structural wall pipeline of the present invention is selected from four different grades of polyethylene: pipe grade polyethylene, hollow grade polyethylene, injection grade polyethylene and film grade linear polyethylene, which can be prepared with excellent mechanical properties and Appearance properties of recycled buried polyethylene structural wall pipes. The invention also discloses a preparation method of the special material for the buried polyethylene structure wall pipeline, and the method can prepare the special material for the buried polyethylene structure wall pipeline with uniform performance.

Description

一种埋地聚乙烯结构壁管道专用料及其制备方法Special material for buried polyethylene structural wall pipeline and preparation method thereof

技术领域technical field

本发明涉及高分子材料技术领域,具体涉及一种埋地聚乙烯结构壁管道专用料及其制备方法。The invention relates to the technical field of polymer materials, in particular to a special material for buried polyethylene structural wall pipes and a preparation method thereof.

背景技术Background technique

在各种管道的生产制造技术中,高密度聚乙烯(HDPE)埋地排水管的发展最为迅猛,根据现有生产技术分类,主要有两种工艺:直接挤出成型和缠绕-熔接成型,而应用最广的是直接挤出成型工艺制得的结构管。这类结构管是以HDPE为主要原料,分别由内、外挤出机共挤一次成型,其内壁平整、外壁呈梯形波纹状,内外壁之间有夹壁空心层的塑料管材。其具有重量轻、耐高压、环刚度大、韧性好、耐低温、耐腐蚀、施工快、寿命长等优点。Among the production and manufacturing technologies of various pipes, the development of high-density polyethylene (HDPE) buried drainage pipes is the most rapid. According to the classification of existing production technologies, there are mainly two processes: direct extrusion molding and winding-welding molding, while The most widely used is the structural pipe made by the direct extrusion molding process. This type of structural pipe is made of HDPE as the main raw material, which is co-extruded by the inner and outer extruders at one time. It has the advantages of light weight, high pressure resistance, high ring stiffness, good toughness, low temperature resistance, corrosion resistance, fast construction and long life.

埋地聚乙烯结构壁管道作为结构性管材,对材料的强度、刚度、使用寿命和成型要求较高,因此要求其必须要有适当的熔体流动速率、较高的机械性能、耐环境应力开裂及抗热氧老化性。国标GB/T 19472.1-2004对埋地用聚乙烯结构壁管道进行详细的规定。As a structural pipe, the buried polyethylene structural wall pipe has high requirements on the strength, stiffness, service life and molding of the material, so it must have an appropriate melt flow rate, high mechanical properties, and resistance to environmental stress cracking. and thermal oxidation resistance. The national standard GB/T 19472.1-2004 provides detailed regulations for buried polyethylene structural wall pipes.

为了制备性能满足国标的埋地聚乙烯结构壁管道专用料,目前国内大多采用的是以管材级聚乙烯树脂为基料,并在基料中添加少量HDPE管材回料、线性低密度聚乙烯、增强母粒、炭黑、抗氧剂、改性剂等混炼而成,如公布的专利CN 102494203 A,所用的树脂全部是聚乙烯新料,而在利用废旧聚乙烯材料生产埋地聚乙烯结构壁管道专用料的的报道和专利较少,公开号为CN 106832528 A的专利公开了一种HDPE再生改性材料的生产方法,但是其所涉及的废旧塑料没有具体的物性要求。In order to prepare special materials for buried polyethylene structural wall pipes whose performance meets the national standard, most of the domestic use is based on pipe-grade polyethylene resin, and a small amount of HDPE pipe material, linear low-density polyethylene, linear low-density polyethylene, etc. are added to the base material. Reinforced masterbatch, carbon black, antioxidants, modifiers, etc. are kneaded, such as the published patent CN 102494203 A, the resins used are all new polyethylene materials, and the use of waste polyethylene materials to produce buried polyethylene There are few reports and patents on special materials for structural wall pipes. The patent publication number CN 106832528 A discloses a production method of HDPE regenerated modified material, but the waste plastics involved have no specific physical property requirements.

然而,在国家科技进步和经济的快速发展的进程中,废旧聚乙烯制品种类繁多、总量庞大。如何循环利用这些废旧聚乙烯不仅是国家所鼓励和倡导的政策方向之一,而且是塑料改性企业的社会责任之一。根据长期生产经验,埋地聚乙烯结构壁管道专用料的原材料如果全部用废旧聚乙烯材料,挤出过程容易出现麻面、鼓包、气泡等挤出缺陷,同时很多生产塑料管道的厂家为了降本添加再生料而忽略产品质量,在使用再生料生产时对再生料的底料、来源、物性特点等了解不全,并且缺乏试验验证,出现了环刚度不够、韧性不够、耐环境应力开裂等现象,造成了工程返工、误期等事故。因此急需开发一种全部以废旧聚乙烯材料为原材料、性能满足国标、挤出外观合格的埋地聚乙烯结构壁管道专用料新技术。However, in the process of national scientific and technological progress and the rapid development of economy, there are many kinds of waste polyethylene products, and the total amount is huge. How to recycle these waste polyethylene is not only one of the policy directions encouraged and advocated by the state, but also one of the social responsibilities of plastic modification enterprises. According to long-term production experience, if all the raw materials of the special materials for buried polyethylene structural wall pipes are made of waste polyethylene materials, extrusion defects such as pockmarks, bulges, and air bubbles are prone to occur during the extrusion process. At the same time, many manufacturers of plastic pipes are in order to reduce costs. Adding recycled materials and ignoring the product quality, when using recycled materials for production, the bottom material, source, physical properties, etc. of recycled materials are not fully understood, and there is a lack of experimental verification. There are phenomena such as insufficient ring stiffness, insufficient toughness, and environmental stress cracking resistance. Accidents such as project rework and delay were caused. Therefore, it is urgent to develop a new technology for the special material for buried polyethylene structural wall pipes that uses waste polyethylene materials as raw materials, whose performance meets the national standard and whose extrusion appearance is qualified.

发明内容SUMMARY OF THE INVENTION

本发明的目的在于克服现有技术存在的不足之处而提供一种埋地聚乙烯结构壁管道专用料及其制备方法。The purpose of the present invention is to overcome the deficiencies existing in the prior art and provide a special material for buried polyethylene structural wall pipes and a preparation method thereof.

为实现上述目的,本发明采取的技术方案为:一种埋地聚乙烯结构壁管道专用料,包含以下重量份的制备原料:管材级聚乙烯10~40份、中空级聚乙烯10~30份、注塑级聚乙烯3~10份、薄膜级线性聚乙烯20~45份、炭黑母粒4~6份、外观改善剂1~3份和耐环境应力开裂调节剂4~10份。In order to achieve the above purpose, the technical solution adopted in the present invention is: a special material for buried polyethylene structural wall pipeline, comprising the following preparation raw materials in parts by weight: 10-40 parts of pipe-grade polyethylene and 10-30 parts of hollow-grade polyethylene , 3-10 parts of injection-molded polyethylene, 20-45 parts of film-grade linear polyethylene, 4-6 parts of carbon black masterbatch, 1-3 parts of appearance improver and 4-10 parts of environmental stress cracking regulator.

本发明所述埋地聚乙烯结构壁管道专用料选择四种不同级别的聚乙烯,以上述配比可以制得具有优异机械性能和外观性能的再生埋地聚乙烯结构壁管道。Four different grades of polyethylene are selected for the special material for the buried polyethylene structural wall pipeline of the present invention, and the regenerated buried polyethylene structural wall pipeline with excellent mechanical properties and appearance properties can be prepared with the above ratio.

优选地,所述管材级聚乙烯、中空级聚乙烯、注塑级聚乙烯和薄膜级线性聚乙烯均为回收树脂。管材级聚乙烯、中空级聚乙烯、注塑级聚乙烯、薄膜级线性聚乙烯各原料可以为新树脂,也可以为回收树脂,也可以为新树脂和回收树脂的混合物,优选均采用回收树脂,可以极大降低成本,采用本发明所述专用料的配方制得的埋地聚乙烯结构壁管道在各原料均采用废旧回收料的情况下,仍能保持较好的机械性能,全部满足国标要求,且挤出过程无外观缺陷,如气泡、鼓包、麻面、缩孔等。Preferably, the pipe-grade polyethylene, hollow-grade polyethylene, injection-molding-grade polyethylene and film-grade linear polyethylene are all recycled resins. The raw materials of pipe-grade polyethylene, hollow-grade polyethylene, injection-molding-grade polyethylene, and film-grade linear polyethylene can be new resins, recycled resins, or a mixture of new resins and recycled resins, preferably recycled resins. The cost can be greatly reduced, and the buried polyethylene structural wall pipeline prepared by using the formula of the special material of the present invention can still maintain good mechanical properties under the condition that all raw materials are used waste recycled materials, and all meet the requirements of the national standard. , and the extrusion process has no appearance defects, such as bubbles, bulging, pockmarks, shrinkage holes, etc.

管材级聚乙烯回收废料主要是指以高密度聚乙烯类管道破碎而来的一类破碎料,如燃气管、高密度聚乙烯波纹管、滴灌管、埋地钢质管道的防腐层、容积100L以上的聚乙烯大桶等。其来源较为纯净、性能优异,具有较高的耐环境应力开裂性能。Pipe-grade polyethylene recycling waste mainly refers to a type of crushed material obtained from high-density polyethylene pipes, such as gas pipes, high-density polyethylene corrugated pipes, drip irrigation pipes, anti-corrosion layers of buried steel pipes, and a volume of 100L. The above polyethylene vats, etc. Its source is relatively pure, its performance is excellent, and it has high resistance to environmental stress cracking.

中空级聚乙烯回收废料主要指以高密度聚乙烯中空制件破碎而来的一类破碎料,如容积100L以内的聚乙烯中空桶、聚乙烯类奶瓶、日杂聚乙烯类瓶等。其机械性能较好、含极少量的PP杂料。Hollow-grade polyethylene recycling waste mainly refers to a type of crushed material obtained by crushing high-density polyethylene hollow parts, such as polyethylene hollow barrels with a volume of less than 100L, polyethylene milk bottles, daily miscellaneous polyethylene bottles, etc. It has good mechanical properties and contains a very small amount of PP miscellaneous materials.

注塑级聚乙烯回收废料主要由高密度聚乙烯瓶盖或者其他注塑制件(如啤酒框、周转筐等)破碎而来,其杂质较少、粒子光泽度较好、性能优良。Injection-grade polyethylene recycling waste is mainly broken by high-density polyethylene bottle caps or other injection-molded parts (such as beer boxes, turnover baskets, etc.), which have less impurities, better particle gloss and excellent performance.

薄膜级线性聚乙烯回收废料,主要是以LLDPE为主体的一类膜类再生造粒料。由于LLDPE的拉伸性能远高于LDPE,因此可以通过测试其拉伸性能来判断这类膜料的主体树脂。Film-grade linear polyethylene recycling waste is mainly a type of film-based recycled granulation material with LLDPE as the main body. Since the tensile properties of LLDPE are much higher than that of LDPE, the main resin of this type of film can be judged by testing its tensile properties.

优选地,所述埋地聚乙烯结构壁管道专用料包含以下重量份的制备原料:管材级聚乙烯15~30份、中空级聚乙烯10~20份、注塑级聚乙烯5~8份、薄膜级线性聚乙烯20~40份、炭黑母粒4~6份、外观改善剂1~3份和耐环境应力开裂调节剂5~8份。Preferably, the special material for buried polyethylene structural wall pipeline comprises the following raw materials by weight: 15-30 parts of pipe-grade polyethylene, 10-20 parts of hollow-grade polyethylene, 5-8 parts of injection-molded polyethylene, film 20-40 parts of grade linear polyethylene, 4-6 parts of carbon black masterbatch, 1-3 parts of appearance improver and 5-8 parts of environmental stress cracking resistance regulator.

优选地,所述管材级聚乙烯的熔体流动速率为0.1~0.5g/10min,所述管材级聚乙烯的熔体流动速率根据GB/T 3682使用5kg重量并在190℃下测量。Preferably, the melt flow rate of the pipe grade polyethylene is 0.1˜0.5 g/10min, and the melt flow rate of the pipe grade polyethylene is measured at 190° C. according to GB/T 3682 using a weight of 5 kg.

优选地,所述中空级聚乙烯的熔体流动速率为0.5~2.0g/10min,所述中空级聚乙烯的熔体流动速率根据GB/T 368 2使用5kg重量并在190℃下测量。Preferably, the melt flow rate of the hollow grade polyethylene is 0.5˜2.0 g/10min, and the melt flow rate of the hollow grade polyethylene is measured at 190° C. according to GB/T 368 2 using a weight of 5 kg.

优选地,所述注塑级聚乙烯的熔体流动速率为0.5~2.0g/10min,所述注塑级聚乙烯的熔体流动速率根据GB/T 3682使用2.16kg重量并在190℃下测量。Preferably, the melt flow rate of the injection molding grade polyethylene is 0.5˜2.0 g/10min, and the melt flow rate of the injection molding grade polyethylene is measured at 190° C. according to GB/T 3682 using a weight of 2.16 kg.

优选地,所述薄膜级线性聚乙烯的熔体流动速率为2.0~4.0g/10min,所述薄膜级线性聚乙烯根据GB/T 3682使用2.16kg重量并在190℃下测量。Preferably, the melt flow rate of the film-grade linear polyethylene is 2.0˜4.0 g/10min, and the film-grade linear polyethylene is measured at 190° C. according to GB/T 3682 using a weight of 2.16 kg.

优选地,所述管材级聚乙烯的密度为0.95~0.97g/cm3,根据GB/T 1040.2采用挤塑1BA型样条、厚度2mm、拉伸速度50mm/min进行拉伸性能测试:拉伸强度大于25MPa,伸长率大于600%。Preferably, the density of the pipe-grade polyethylene is 0.95-0.97 g/cm 3 . According to GB/T 1040.2, the tensile properties are tested by extruding 1BA type splines, with a thickness of 2 mm and a tensile speed of 50 mm/min: stretching The strength is greater than 25MPa, and the elongation is greater than 600%.

优选地,所述中空级聚乙烯的密度为0.95~0.97g/cm3,根据GB/T 1040.2采用挤塑1BA型样条、厚度2mm、拉伸速度50mm/min进行拉伸性能测试:拉伸强度大于22MPa,伸长率大于350%。Preferably, the density of the hollow-grade polyethylene is 0.95-0.97g/cm 3 . According to GB/T 1040.2, the tensile properties are tested by extruding a 1BA type spline, a thickness of 2 mm, and a tensile speed of 50 mm/min: stretching The strength is greater than 22MPa, and the elongation is greater than 350%.

优选地,所述注塑级聚乙烯的密度为0.95~0.97g/cm3,根据GB/T 1040.2模塑1A型样条、厚度4mm、拉伸速度50mm/min进行拉伸性能测试:拉伸强度大于20MPa,伸长率大于50%;根据GB/T 9341-2008测试的弯曲模量大于750MPa。Preferably, the density of the injection-molded polyethylene is 0.95-0.97 g/cm 3 , and the tensile properties are tested according to GB/T 1040.2 molding 1A-type splines, thickness 4 mm, and tensile speed 50 mm/min: tensile strength Greater than 20MPa, the elongation is greater than 50%; the flexural modulus tested according to GB/T 9341-2008 is greater than 750MPa.

优选地,所述薄膜级线性聚乙烯的密度为0.915~0.955g/cm3,根据GB/T 1040.2采用挤塑1BA型样条、厚度2mm、拉伸速度50mm/min进行拉伸性能测试:拉伸强度大于22MPa,伸长率大于500%。Preferably, the density of the film-grade linear polyethylene is 0.915-0.955g/cm 3 , and the tensile properties are tested according to GB/T 1040.2 using extruded 1BA type splines, thickness 2mm, and tensile speed 50mm/min: The tensile strength is greater than 22MPa, and the elongation is greater than 500%.

所述管材级聚乙烯、中空级聚乙烯、注塑级聚乙烯和薄膜级线性聚乙烯的灰分<2%,灰分测试条件为650±50℃下在马弗炉里灼烧2小时。The ash content of the pipe-grade polyethylene, hollow-grade polyethylene, injection-molding-grade polyethylene and film-grade linear polyethylene is less than 2%, and the ash content test conditions are burning in a muffle furnace at 650±50° C. for 2 hours.

优选地,所述炭黑母粒包含以下重量份的组分:薄膜级线性聚乙烯30~50份、炭黑40~45份、抗氧剂15~20份、分散剂1~3份和耐候剂1~3份;所述抗氧剂为受阻酚类抗氧剂和/或亚磷酸脂类抗氧剂,所述分散剂为PE蜡,所述耐候剂为紫外光吸收剂和受阻胺光稳定剂的混合物。Preferably, the carbon black masterbatch contains the following components in parts by weight: 30-50 parts of film-grade linear polyethylene, 40-45 parts of carbon black, 15-20 parts of antioxidant, 1-3 parts of dispersant and weather resistance The antioxidant is a hindered phenolic antioxidant and/or a phosphite antioxidant, the dispersing agent is PE wax, and the weathering agent is an ultraviolet light absorber and a hindered amine light Mixture of stabilizers.

所述薄膜级线性聚乙烯可以为新树脂也可以为回收树脂,优选采用回收树脂,其熔体流动速率为2.0~4.0g/10min,所述薄膜级线性聚乙烯根据GB/T 3682使用2.16kg重量并在190℃下测量,密度为0.915~0.955g/cm3,拉伸强度根据GB/T 1040.2采用挤塑1BA型样条、厚度2mm、拉伸速度50mm/min进行测试:拉伸强度大于22MPa,伸长率大于500%。在炭黑母粒中,薄膜级线性聚乙烯优选为造粒料。The film-grade linear polyethylene can be a new resin or a recycled resin, preferably a recycled resin, and its melt flow rate is 2.0-4.0g/10min. The film-grade linear polyethylene uses 2.16kg according to GB/T 3682 The weight is measured at 190°C, the density is 0.915~0.955g/cm 3 , and the tensile strength is tested according to GB/T 1040.2 using extruded 1BA type splines, thickness 2mm, and tensile speed 50mm/min: the tensile strength is greater than 22MPa, the elongation is greater than 500%. In the carbon black masterbatch, film grade linear polyethylene is preferably the pelletizing material.

优选地,所述外观改善剂为PE基氧化钙母粒。Preferably, the appearance improving agent is PE-based calcium oxide masterbatch.

优选地,所述耐环境应力开裂改善剂为乙烯-丁烯高聚物和/或乙烯-辛烯高聚物。Preferably, the environmental stress crack resistance improving agent is an ethylene-butene polymer and/or an ethylene-octene polymer.

优选地,所述抗氧剂为受阻酚类抗氧剂和亚磷酸脂类抗氧剂的混合物,所述受阻酚类抗氧剂和亚磷酸脂类抗氧剂的重量之比为3:2;和/或所述耐候剂为紫外吸收剂和受阻胺光稳定剂的重量之比为1:1。Preferably, the antioxidant is a mixture of hindered phenolic antioxidant and phosphite antioxidant, and the weight ratio of the hindered phenolic antioxidant to phosphite antioxidant is 3:2 ; and/or the weathering agent is that the weight ratio of the UV absorber and the hindered amine light stabilizer is 1:1.

本发明的目的还在于提供所述埋地聚乙烯结构壁管道专用料的制备方法,包括以下步骤:The object of the present invention is also to provide a preparation method of the special material for the buried polyethylene structural wall pipeline, comprising the following steps:

(1)将管材级聚乙烯、中空级聚乙烯和注塑级聚乙烯混合造粒,得破碎料;(1) mixing and granulating pipe-grade polyethylene, hollow-grade polyethylene and injection-molding-grade polyethylene to obtain crushed material;

(2)将薄膜级线性聚乙烯造粒,得薄膜造粒料;(2) granulating film grade linear polyethylene to obtain film granulation material;

(3)将破碎料、薄膜造粒料、炭黑母粒、外观改善剂和耐环境应力开裂调节剂混合均匀后投入上阶单螺杆挤出机,熔融挤出后流入下阶挤出机熔融挤出、水冷、切粒、过筛、烘干,得所述埋地聚乙烯结构壁管道专用料。(3) Mix the crushed material, film granulation material, carbon black masterbatch, appearance improver and environmental stress cracking resistance regulator evenly and put it into the upper-stage single-screw extruder. After melt extrusion, it flows into the lower-stage extruder to melt. Extrusion, water cooling, pelletizing, sieving and drying to obtain the special material for the buried polyethylene structural wall pipeline.

由于步骤(1)中的管材级聚乙烯、中空级聚乙烯和注塑级聚乙烯与步骤(2)的薄膜级线性聚乙烯的密度、粒径和尺寸相差较大,如果按照传统的“一锅混”混料工艺会导致破碎片和粒子分层,影响均匀性,导致成品性能波动、甚至不合格。因此,采用将步骤(1)中的管材级聚乙烯、中空级聚乙烯和注塑级聚乙烯与步骤(2)的薄膜级线性聚乙烯分别造粒后再混合,熔融挤出,能实现成品性能的均一性。Since the density, particle size and size of the pipe-grade polyethylene, hollow-grade polyethylene and injection-molded polyethylene in step (1) are quite different from those of the film-grade linear polyethylene in step (2), if the traditional "one-pot polyethylene" The blending process can cause broken flakes and particles to delaminate, affecting uniformity, resulting in fluctuations in finished product performance and even substandard results. Therefore, the performance of the finished product can be achieved by granulating the pipe-grade polyethylene, hollow-grade polyethylene and injection-molding-grade polyethylene in the step (1) and the film-grade linear polyethylene in the step (2), respectively, and then mixing and melt extrusion. uniformity.

采用双阶挤出机组生产埋地聚乙烯结构壁管道专用料,上阶单螺杆挤出机能够有效地对废旧聚乙烯破碎料进行塑化、除杂和自然排气,下阶挤出机通过设计螺杆组合能够改善各组分的分散性和相容性,设置真空系统能进一步脱挥,从而制得光泽度高、切面无气孔的再生埋地聚乙烯结构壁管道专用料。The two-stage extruder is used to produce the special material for buried polyethylene structural wall pipes. The upper-stage single-screw extruder can effectively plasticize, remove impurities and naturally exhaust the waste polyethylene crushed materials. The lower-stage extruder can pass The design of the screw combination can improve the dispersibility and compatibility of each component, and the vacuum system can be set up to further devolatilize, so as to obtain the special material for regenerated buried polyethylene structural wall pipes with high gloss and no pores on the cut surface.

优选地,所述炭黑母粒的制备方法为:将薄膜级聚乙烯、炭黑、抗氧剂、分散剂和耐候剂在高混机中低转速混合均匀后,投入密炼机中,密炼温度160~175℃,密炼时间10~15分钟;然后将密炼好的物料团经锥双螺杆喂入单螺杆挤出机进行磨面风冷造粒,单螺杆挤出机的温度170~190℃。Preferably, the preparation method of the carbon black masterbatch is as follows: after the film-grade polyethylene, carbon black, antioxidant, dispersant and weathering agent are uniformly mixed in a high-speed mixer at a low speed, put into an internal mixer, and dense The mixing temperature is 160~175℃, and the mixing time is 10~15 minutes; then the mixed material mass is fed into the single-screw extruder through the conical twin-screw for grinding and air-cooling granulation. The temperature of the single-screw extruder is 170 ~190°C.

优选地,步骤(1)中,所述造粒用的挤出机为单螺杆熔融挤出造粒机,各温区的温度为160~200℃,单螺杆的换网器和机头的温度为200~210℃,换网器的滤网目数为60+80目。Preferably, in step (1), the extruder used for granulation is a single-screw melt extrusion granulator, the temperature of each temperature zone is 160-200°C, and the temperature of the single-screw screen changer and the head is The temperature is 200~210℃, and the mesh number of the screen changer is 60+80 mesh.

优选地,步骤(3)中,所述混合所用的设备为容积大于5m3的立式混料机或卧式混料机,以提高混合的均匀性。Preferably, in step (3), the equipment used for the mixing is a vertical mixer or a horizontal mixer with a volume greater than 5 m 3 to improve the uniformity of mixing.

优选地,步骤(3)中,上阶单螺杆挤出机至少有一个排气口,单螺杆的输送段采用深螺槽设计以提高喂料量;熔融压缩段先采用分离型螺杆设计实现固液分离提高塑化能力,然后在靠近排气段的地方设置斜槽屏障段(长度为1~2D)以增加熔融、混炼效果;排气段为了提高脱挥效率采用深螺槽设计;在计量段中设置较深螺槽较短导程以增加熔体的环状混合效果。Preferably, in step (3), the upper-stage single-screw extruder has at least one exhaust port, and the conveying section of the single-screw adopts a deep screw groove design to increase the feeding amount; the melt-compression section first adopts a separate screw design to achieve solidification. The liquid separation improves the plasticizing capacity, and then a chute barrier section (1-2D in length) is set near the exhaust section to increase the melting and mixing effect; the exhaust section adopts a deep screw groove design in order to improve the devolatilization efficiency; In the metering section, a deeper screw groove and a shorter lead are set to increase the annular mixing effect of the melt.

优选地,一阶机单螺杆机的各区段温度为:固体输送段180℃、熔融压缩段220~240℃、排气段225℃、均化段215~225℃、滤板220℃、出料管220℃;Preferably, the temperature of each section of the first-stage single-screw machine is: 180°C for the solid conveying section, 220-240°C for the melt-compression section, 225°C for the exhaust section, 215-225°C for the homogenization section, 220°C for the filter plate, and 220°C for the discharge. Tube 220℃;

所述步骤(3)中,下阶挤出机为单螺杆挤出机或双螺杆挤出机,若为单螺杆,其螺杆结构宜采用较深螺杆、较短导程的结构,以提高熔体的环状混合效果;若为双螺杆,其螺杆组合通过设计多段式的45°啮合区域以提高各组分的分散和相容性。排气口加装抽真空设备,真空度为-0.08MPa,各温区的温度为190~200℃,模头210℃。In the step (3), the lower-stage extruder is a single-screw extruder or a twin-screw extruder. If it is a single-screw, the screw structure should be a deeper screw and a shorter lead to improve the melting point. The annular mixing effect of the body; if it is a twin screw, the screw combination of the multi-stage 45° meshing area is designed to improve the dispersion and compatibility of each component. The exhaust port is equipped with vacuum equipment, the vacuum degree is -0.08MPa, the temperature of each temperature zone is 190-200℃, and the die head is 210℃.

本发明的有益效果在于:本发明提供了一种埋地聚乙烯结构壁管道专用料及其制备方法。本发明所述埋地聚乙烯结构壁管道专用料选择管材级聚乙烯、中空级聚乙烯、注塑级聚乙烯和薄膜级线性聚乙烯四种不同级别的聚乙烯,可以制得具有优异机械性能和外观性能的再生埋地聚乙烯结构壁管道。The beneficial effects of the present invention are as follows: the present invention provides a special material for buried polyethylene structural wall pipes and a preparation method thereof. The special material for the buried polyethylene structural wall pipeline of the present invention is selected from four different grades of polyethylene: pipe grade polyethylene, hollow grade polyethylene, injection grade polyethylene and film grade linear polyethylene, which can be prepared with excellent mechanical properties and Appearance properties of recycled buried polyethylene structural wall pipes.

具体实施方式Detailed ways

为更好地说明本发明的目的、技术方案和优点,下面将结合具体实施例对本发明作进一步说明。In order to better illustrate the purpose, technical solutions and advantages of the present invention, the present invention will be further described below with reference to specific embodiments.

实施例和对比例所述埋地聚乙烯结构壁管道专用料的制备原料配方见表2和表3。The preparation raw material formulations of the special materials for buried polyethylene structural wall pipes described in Examples and Comparative Examples are shown in Table 2 and Table 3.

实施例和对比例中,所述管材级聚乙烯破碎料、中空级聚乙烯破碎料、注塑级聚乙烯破碎料均为回收树脂,经过分拣、破碎、清洗、脱水所得,薄膜级线性聚乙烯造粒料为回收的线性聚乙烯类薄膜分拣、破碎、清洗、脱水所得。In the examples and comparative examples, the pipe-grade polyethylene crushed material, hollow-grade polyethylene crushed material, and injection-molded polyethylene crushed material are all recycled resins, obtained after sorting, crushing, cleaning, and dehydration, and film-grade linear polyethylene is obtained. The granulation material is obtained by sorting, crushing, cleaning and dehydrating the recovered linear polyethylene film.

所述管材级聚乙烯破碎料均选自具有以下特征的聚乙烯材料:熔体流动速率为0.1~0.5g/10min(根据GB/T 3682使用5kg重量并在190℃下测量),密度为0.95~0.97g/cm3,根据GB/T 1040.2采用挤塑1BA型样条、厚度2mm、拉伸速度50mm/min进行拉伸性能测试:拉伸强度大于25MPa,伸长率大于600%。The pipe-grade polyethylene crushed materials are all selected from polyethylene materials with the following characteristics: the melt flow rate is 0.1-0.5g/10min (according to GB/T 3682, using a weight of 5kg and measuring at 190°C), and the density is 0.95 ~0.97g/cm 3 , according to GB/T 1040.2, using extruded 1BA type splines, thickness 2mm, tensile speed 50mm/min for tensile property test: tensile strength is greater than 25MPa, elongation is greater than 600%.

所述中空级聚乙烯均选自具有以下特征的聚乙烯材料:熔体流动速率为0.5~2.0g/10min(根据GB/T 368 2使用5kg重量并在190℃下测量),密度为0.95~0.97g/cm3,根据GB/T 1040.2采用挤塑1BA型样条、厚度2mm、拉伸速度50mm/min进行拉伸性能测试:拉伸强度大于22MPa,伸长率大于350%。The hollow-grade polyethylenes are all selected from polyethylene materials with the following characteristics: a melt flow rate of 0.5 to 2.0 g/10min (according to GB/T 368 2 using a 5 kg weight and measured at 190°C), and a density of 0.95 to 0.95 0.97g/cm 3 , according to GB/T 1040.2, using extruded 1BA spline, thickness 2mm, tensile speed 50mm/min for tensile property test: tensile strength is greater than 22MPa, elongation is greater than 350%.

所述注塑级聚乙烯均选自具有以下特征的聚乙烯材料:熔体流动速率为0.5~2.0g/10min(根据GB/T 3682使用2.16kg重量并在190℃下测量),密度为0.95~0.97g/cm3,根据GB/T 1040.2模塑1A型样条、拉伸速度50mm/min进行拉伸性能测试:拉伸强度大于20MPa,伸长率大于50%;根据GB/T 9341-2008测试的弯曲模量大于750MPa。The injection-molding polyethylene is selected from polyethylene materials with the following characteristics: melt flow rate of 0.5~2.0g/10min (according to GB/T 3682 using 2.16kg weight and measured at 190°C), density of 0.95~ 0.97g/cm 3 , according to GB/T 1040.2 molding 1A spline, tensile speed 50mm/min for tensile property test: tensile strength greater than 20MPa, elongation greater than 50%; according to GB/T 9341-2008 The tested flexural modulus was greater than 750 MPa.

所述薄膜级线性聚乙烯均选自具有以下特征的聚乙烯材料:熔体流动速率为2.0~4.0g/10min(根据GB/T 3682使用2.16kg重量并在190℃下测量),密度为0.915~0.955g/cm3,根据GB/T 1040.2采用挤塑1BA型样条、厚度2mm、拉伸速度50mm/min进行拉伸性能测试:拉伸强度大于22MPa,伸长率大于500%。The film-grade linear polyethylenes are all selected from polyethylene materials with the following characteristics: a melt flow rate of 2.0 to 4.0 g/10min (according to GB/T 3682 using a weight of 2.16 kg and measured at 190°C), and a density of 0.915 ~0.955g/cm 3 , according to GB/T 1040.2, using extruded 1BA spline, thickness 2mm, tensile speed 50mm/min for tensile property test: tensile strength is greater than 22MPa, elongation is greater than 500%.

所述炭黑母粒包含以下重量份的组分:薄膜级线性聚乙烯40份、炭黑43份、抗氧剂18份、分散剂2份和耐候剂2份;所述薄膜级线性聚乙烯均选自具有以下特征的聚乙烯材料:熔体流动速率为2.0~4.0g/10min(根据GB/T 3682使用2.16kg重量并在190℃下测量),密度为0.915~0.955g/cm3,根据GB/T 1040.2采用挤塑1BA型样条、厚度2mm、拉伸速度50mm/min进行拉伸性能测试:拉伸强度大于22MPa,伸长率大于500%。The carbon black masterbatch comprises the following components in parts by weight: 40 parts of film-grade linear polyethylene, 43 parts of carbon black, 18 parts of antioxidant, 2 parts of dispersant and 2 parts of weathering agent; the film-grade linear polyethylene All are selected from polyethylene materials with the following characteristics: melt flow rate is 2.0~4.0g/10min (according to GB/T 3682 using 2.16kg weight and measured at 190℃), density is 0.915~0.955g/cm 3 , According to GB/T 1040.2, extruded 1BA type splines, thickness 2mm, tensile speed 50mm/min are used for tensile property test: tensile strength is greater than 22MPa, elongation is greater than 500%.

所述炭黑母粒的制备方法为:将薄膜级聚乙烯、炭黑、抗氧剂、分散剂和耐候剂在高混机中低转速混合均匀后,投入密炼机中,密炼温度160~175℃,密炼时间10~15分钟;然后将密炼好的物料团经锥双螺杆喂入单螺杆挤出机进行磨面风冷造粒,单螺杆挤出机的温度170~190℃。所述抗氧剂为受阻酚类抗氧剂和亚磷酸脂类抗氧剂的混合物,所述受阻酚类抗氧剂和亚磷酸脂类抗氧剂的重量之比为3:2,所述分散剂为PE蜡,所述耐候剂为紫外光吸收剂和受阻胺光稳定剂的混合物,紫外光吸收剂和受阻胺光稳定剂的重量之比为1:1。其中,受阻酚类抗氧剂购自天津利安隆新材料股份有限公司,型号为RIANOX 1010;亚磷酸脂类抗氧剂购自天津利安隆新材料股份有限公司,型号为RIANOX 168;PE蜡购自广州恒石进出口贸易有限公司,型号为CS-12N;紫外光吸收剂购自氰特工程材料(上海)有限公司,型号为UV-531;受阻胺光稳定剂购自艾迪科(中国)投资有限公司,型号为LA-402AF。The preparation method of the carbon black master batch is as follows: after the film grade polyethylene, carbon black, antioxidant, dispersant and weather resistance agent are uniformly mixed in a high mixer at a low speed, then put into an internal mixer, and the internal mixing temperature is 160 °C. ~175℃, the mixing time is 10~15 minutes; then the mixed material mass is fed into the single-screw extruder through the conical twin-screw for grinding and air-cooling granulation. The temperature of the single-screw extruder is 170~190℃ . The antioxidant is a mixture of a hindered phenolic antioxidant and a phosphite antioxidant, and the weight ratio of the hindered phenolic antioxidant to the phosphite antioxidant is 3:2, and the The dispersing agent is PE wax, the weathering agent is a mixture of an ultraviolet light absorber and a hindered amine light stabilizer, and the weight ratio of the ultraviolet light absorber and the hindered amine light stabilizer is 1:1. Among them, hindered phenolic antioxidants were purchased from Tianjin Rianlong New Materials Co., Ltd., model RIANOX 1010; phosphite antioxidants were purchased from Tianjin Rianlong New Materials Co., Ltd., model RIANOX 168; PE wax was purchased from from Guangzhou Hengshi Import and Export Trading Co., Ltd., model CS-12N; UV absorber purchased from Cytec Engineering Materials (Shanghai) Co., Ltd., model UV-531; hindered amine light stabilizer purchased from Adico (China) ) Investment Co., Ltd., model LA-402AF.

外观改善剂为PE基氧化钙母粒,购自广州绿鑫环保科技有限公司,商品型号为NDM-1008。The appearance improving agent is PE-based calcium oxide masterbatch, which was purchased from Guangzhou Lvxin Environmental Protection Technology Co., Ltd., and the commodity model is NDM-1008.

耐环境应力开裂改善剂为乙烯-丁烯高聚物和/或乙烯-辛烯高聚物,购自宁波能之光新材料科技股份有限公司,商品型号为MC218。The environmental stress cracking resistance improver is ethylene-butene polymer and/or ethylene-octene polymer, purchased from Ningbo Nengzhiguang New Material Technology Co., Ltd., and the commodity model is MC218.

实施例和对比例所述埋地聚乙烯结构壁管道专用料的制备方法包括以下步骤:The preparation method of the special material for the buried polyethylene structural wall pipeline described in the embodiment and the comparative example comprises the following steps:

(1)将管材级聚乙烯破碎料、中空级聚乙烯破碎料和注塑级聚乙烯破碎料清洗、脱水后装袋备用,将低密度聚乙烯薄膜分拣、破碎、清洗、脱水后,经单螺杆挤出机熔融挤出造粒备用,单螺杆熔融挤出造粒的各温区的温度为160~200℃,单螺杆的换网器和机头的温度为200~210℃,换网器的滤网目数为60+80目;(1) The pipe-grade polyethylene crushed material, hollow-grade polyethylene crushed material and injection-molded polyethylene crushed material are cleaned, dehydrated and then bagged for use. After sorting, crushing, cleaning and dehydration of the low-density polyethylene film, the The temperature of each temperature zone of the single-screw melt extrusion and granulation is 160-200°C, and the temperature of the screen changer and the head of the single-screw is 200-210°C. The mesh number of the filter is 60+80 mesh;

(2)将处理后的管材级聚乙烯破碎料、中空级聚乙烯破碎料和注塑级聚乙烯破碎料按配方比例称取重量,投入容积为5m3的立式混料罐混30min后,投入振动下料计量秤的料仓中;将薄膜级聚乙烯造粒料、专用功能炭黑母粒、外观改善剂和耐环境应力开裂改善剂按配方比例称取重量,投入容积为2m3的卧式混料罐混20min后,投入另外一台计量秤(可以为振动下料计量秤或螺杆下料计量秤)的料仓中。按配方比例设置两台计量秤的下料比例或重量,物料会按照比例准确下料至上阶单螺杆挤出机的下料口中;(2) The treated pipe grade polyethylene crushed material, hollow grade polyethylene crushed material and injection-molded polyethylene crushed material are weighed according to the formula proportions, put into a vertical mixing tank with a volume of 5 m after mixing for 30 minutes, and then put into In the silo of the vibrating unloading weighing scale; weigh the film-grade polyethylene granules, the special functional carbon black masterbatch, the appearance improver and the environmental stress cracking resistance improver according to the formula proportions, and put them into a 2m3 horizontal container. After 20 minutes of mixing in the type mixing tank, put it into the silo of another weighing scale (which can be a vibrating feeding weighing scale or a screw feeding weighing scale). Set the feeding ratio or weight of the two weighing scales according to the formula ratio, and the material will be accurately fed into the feeding port of the upper-stage single-screw extruder according to the proportion;

(3)物料进入上阶单螺杆挤出机经历了固体输送、熔融塑化、熔融混合和熔体除杂过滤四个过程,其挤出温度为180~230℃,过滤板上的滤网目数为80+100目;除杂后的熔体流入下阶单螺杆或双螺杆挤出机的下料口,其造粒温度为170~200℃,切粒方式为水拉条或者水下磨面热切,然后过筛、在线烘干、包装,即得到所述埋地聚乙烯结构壁管道专用料。(3) The material enters the upper-stage single-screw extruder and undergoes four processes: solid conveying, melt plasticization, melt mixing and melt impurity removal and filtration. The number is 80+100 mesh; the melt after removal of impurities flows into the feeding port of the next-stage single-screw or twin-screw extruder. The surface is eagerly cut, then sieved, dried online, and packaged to obtain the special material for buried polyethylene structural wall pipes.

实施例和对比例的性能测试方法见表1:The performance testing method of embodiment and comparative example is shown in Table 1:

表1Table 1

Figure BDA0002395743600000091
Figure BDA0002395743600000091

测试结果见表2和表3。The test results are shown in Table 2 and Table 3.

表2Table 2

Figure BDA0002395743600000092
Figure BDA0002395743600000092

Figure BDA0002395743600000101
Figure BDA0002395743600000101

表3table 3

Figure BDA0002395743600000102
Figure BDA0002395743600000102

由表2、3可知,实施例1~7所述埋地聚乙烯结构壁管道专用料具有满足GB/T19472.1-2004的专用料指标。It can be seen from Tables 2 and 3 that the special materials for buried polyethylene structural wall pipes described in Examples 1 to 7 have the special material indexes that meet GB/T19472.1-2004.

最后所应当说明的是,以上实施例仅用以说明本发明的技术方案而非对本发明保护范围的限制,尽管参照较佳实施例对本发明作了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的实质和范围。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention and not to limit the protection scope of the present invention. Although the present invention is described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that, The technical solutions of the present invention may be modified or equivalently replaced without departing from the spirit and scope of the technical solutions of the present invention.

Claims (3)

1. The special material for the buried polyethylene structure wall pipeline is characterized by comprising the following preparation raw materials in parts by weight: 10-40 parts of pipe grade polyethylene, 10-30 parts of hollow grade polyethylene, 3-10 parts of injection grade polyethylene, 20-45 parts of film grade linear polyethylene, 4-6 parts of carbon black master batch, 1-3 parts of appearance improver and 4-10 parts of environmental stress cracking resistance regulator;
the melt flow rate of the pipe grade polyethylene is 0.1-0.5 g/10min, the melt flow rate of the pipe grade polyethylene is measured at 190 ℃ according to GB/T3682 with the weight of 5kg, and the density of the pipe grade polyethylene is 0.95-0.97 g/cm 3 According to GB/T1040.2, an extrusion molding 1BA type sample strip, the thickness of the sample strip is 2mm, and the tensile speed is 50mm/min is adopted for carrying out tensile property test: the tensile strength is more than 25MPa, and the elongation is more than 600 percent;
the melt flow rate of the hollow-grade polyethylene is 0.5-2.0 g/10min, and the hollow-grade polyethyleneThe melt flow rate of the ethylene is measured according to GB/T3682 using a weight of 5kg and at 190 ℃, and the density of the hollow-grade polyethylene is 0.95-0.97 g/cm 3 According to GB/T1040.2, an extrusion molding 1BA type sample strip, the thickness of the sample strip is 2mm, and the tensile speed is 50mm/min is adopted for carrying out tensile property test: the tensile strength is more than 22MPa, and the elongation is more than 350 percent;
the melt flow rate of the injection-grade polyethylene is 0.5-2.0 g/10min, the melt flow rate of the injection-grade polyethylene is measured at 190 ℃ by using 2.16kg of weight according to GB/T3682, and the density of the injection-grade polyethylene is 0.95-0.97 g/cm 3 Tensile properties were measured according to GB/T1040.2 moulding of 1A type bars, thickness 4mm, tensile speed 50 mm/min: the tensile strength is more than 20MPa, and the elongation is more than 50 percent; the flexural modulus tested according to GB/T9341-2008 is more than 750 MPa;
the melt flow rate of the film-grade linear polyethylene is 2.0-4.0 g/10min, the film-grade linear polyethylene is measured at 190 ℃ according to GB/T3682 with a weight of 2.16kg, and the density of the film-grade linear polyethylene is 0.915-0.955 g/cm 3 According to GB/T1040.2, an extrusion molding 1BA type sample strip, the thickness of the sample strip is 2mm, and the tensile speed is 50mm/min is adopted for carrying out tensile property test: the tensile strength is more than 22MPa, and the elongation is more than 500 percent;
the carbon black master batch comprises the following components in parts by weight: 30-50 parts of film-grade linear polyethylene, 40-45 parts of carbon black, 15-20 parts of antioxidant, 1-3 parts of dispersant and 1-3 parts of weather resistant agent; the antioxidant is hindered phenol antioxidant and/or phosphite antioxidant, the dispersing agent is PE wax, and the weather-resistant agent is a mixture of an ultraviolet light absorber and a hindered amine light stabilizer;
the appearance improver is PE-based calcium oxide master batch;
the environmental stress cracking resistance improver is an ethylene-butene high polymer and/or an ethylene-octene high polymer.
2. The special material for the buried polyethylene structure wall pipeline as claimed in claim 1, wherein the antioxidant is a mixture of hindered phenol antioxidant and phosphite antioxidant, and the weight ratio of the hindered phenol antioxidant to the phosphite antioxidant is 3: 2; and/or the weather resisting agent is an ultraviolet absorbent and the hindered amine light stabilizer with the weight ratio of 1: 1.
3. The method for preparing the special material for the buried polyethylene structure wall pipeline as claimed in claim 1 or 2, is characterized by comprising the following steps:
(1) mixing and granulating the pipe-grade polyethylene, the hollow-grade polyethylene and the injection-grade polyethylene to obtain a crushed material;
(2) granulating the film-grade linear polyethylene to obtain film granulating materials;
(3) uniformly mixing the crushed material, the film granulating material, the carbon black master batch, the appearance improver and the environmental stress cracking resistance regulator, then putting the mixture into an upper-stage single-screw extruder, and flowing the mixture into a lower-stage extruder after melt extrusion for melt extrusion, water cooling, granulating, sieving and drying to obtain the special material for the buried polyethylene structural wall pipeline.
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