CN111471254A - 一种可热熔对接焊聚氯乙烯管材及其制备方法 - Google Patents

一种可热熔对接焊聚氯乙烯管材及其制备方法 Download PDF

Info

Publication number
CN111471254A
CN111471254A CN202010474827.1A CN202010474827A CN111471254A CN 111471254 A CN111471254 A CN 111471254A CN 202010474827 A CN202010474827 A CN 202010474827A CN 111471254 A CN111471254 A CN 111471254A
Authority
CN
China
Prior art keywords
parts
pipe
chlorine content
chlorinated polyethylene
polyvinyl chloride
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202010474827.1A
Other languages
English (en)
Inventor
张双全
郝洪波
朱鹏飞
王贝贝
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kangtai Plastic Science and Technology Group Co Ltd
Original Assignee
Kangtai Plastic Science and Technology Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kangtai Plastic Science and Technology Group Co Ltd filed Critical Kangtai Plastic Science and Technology Group Co Ltd
Priority to CN202010474827.1A priority Critical patent/CN111471254A/zh
Publication of CN111471254A publication Critical patent/CN111471254A/zh
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/04Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
    • C08L27/06Homopolymers or copolymers of vinyl chloride
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion 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
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/9258Velocity
    • B29C2948/9259Angular velocity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/9258Velocity
    • B29C2948/926Flow or feed rate
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92609Dimensions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92609Dimensions
    • B29C2948/92666Distortion, shrinkage, dilatation, swell or warpage
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92895Barrel or housing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92904Die; Nozzle zone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92933Conveying, transporting or storage of articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92819Location or phase of control
    • B29C2948/92952Drive section, e.g. gearbox, motor or drive fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0005Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
    • B29K2105/0044Stabilisers, e.g. against oxydation, light or heat
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2023/00Tubular articles
    • B29L2023/22Tubes or pipes, i.e. rigid
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • 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
    • 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
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

本发明属于管材加工技术领域,具体涉及可热熔对接焊聚氯乙烯管材及其制备方法,按重量份数计,包括以下原料,PVC树脂50‑100份;PE树脂40‑99份;PVC增溶剂0.5‑15份;PE增溶剂0.5‑15份;钙锌稳定剂3‑8份;硬脂酸0.1‑2.0份;聚乙烯蜡0.1‑2份;ACR:0.5‑8份;增强剂0.5‑15份;纳米填充剂0.5‑15份;其中,所述PVC增溶剂为含氯量35‑37%的氯化聚乙烯、乙烯‑醋酸乙烯共聚物中的一种或两种的混合;所述PE增溶剂为含氯量40‑50%的氯化聚乙烯和含氯量60‑70%的氯化聚乙烯的混合物。在本发明中,管材的原料中加入大量的PE树脂,提高PVC管材的强度,并且,加入含氯量40‑50%的氯化聚乙烯和含氯量60‑70%的氯化聚乙烯作为PE增溶剂,提高PVC和PE的相容性,进而提高焊口处的力学性能和圆滑性。

Description

一种可热熔对接焊聚氯乙烯管材及其制备方法
技术领域
本发明属于管材加工技术领域,具体涉及可热熔对接焊聚氯乙烯管材及其制备方法。
背景技术
目前城市建设面积越来越多,新城镇建设,新农村建设,美丽乡村等等,随着水泥地面的范围越来越大,在多数情况下,铺设安装和维修地下给水、排水和电缆导管时,不能破坏地面设施,所以非开挖用管道越来越受欢迎。目前使用于非开挖的塑料管材,最多的是PE管道和MPP管道,PE和PP焊口强度很好,但PE和PP管道受石油价格波动影响非常大,有时价格比PVC树脂价格高100%。而针对PVC管材,由于现有技术对接焊的焊口强度低,焊口处不能圆滑过渡,容易把电缆线划伤,焊口冲击强度低,焊口弯折容易断裂,难以在实际工程中应用。
发明内容
本发明的目的在于:解决上述现有技术中的不足,提供一种可对接焊的PVC管材,焊接后的焊口强度高管材本体的强度,可以广泛作为城市乡村开挖和非开挖的给水管材,排水管材,通信管材,既可以节约管件和粘接成本,还可以减少承口部分的管材长度和节约胶圈,本发明为一种节能减排,性价比高的新管材。
为了实现上述目的,本发明采用的技术方案为:一种可热熔对接焊聚氯乙烯管材,按重量份数计,包括以下原料,
Figure BDA0002515529420000011
Figure BDA0002515529420000021
其中,所述PVC增溶剂为含氯量35-37%的氯化聚乙烯、乙烯-醋酸乙烯共聚物中的一种或两种的混合;
所述PE增溶剂为含氯量40-50%的氯化聚乙烯和含氯量60-70%的氯化聚乙烯的混合物。
进一步的,所述含氯量40-50%的氯化聚乙烯和含氯量60-70%的氯化聚乙烯的重量份数比为1:1。在本发明中,含氯量指的是氯化聚乙烯接枝的氯元素的质量分数。
进一步的,该管材的包括以下含量的原料,按重量份数计为:
Figure BDA0002515529420000022
Figure BDA0002515529420000031
进一步的,该管材的包括以下含量的原料,按重量份数计为:
Figure BDA0002515529420000032
进一步的,所述增强剂为丙烯腈-丁二烯-苯乙烯共聚物、甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物中一种或者两种共混物。
进一步的,所述填充剂为纳米碳酸钙、云母、石英砂、黏土、钛白粉、炭黑、石墨烯、滑石粉、二氧化硅中一种或者两种以上混合物。
一种上述可热熔对接焊聚氯乙烯管材的制备方法,包括以下步骤,
S1混料:将各原料加入到加热搅拌机中,搅拌均匀,待原料温度达到100-125℃后,将原料加入到冷却搅拌机中,搅拌,并将各原料冷却至28-42℃;
S2挤出成型:调节模具参数和挤出工艺参数,将上述步骤S1混合后的物料加入到挤出机中,挤出管材。
进一步的,在所述步骤S2中,管材的纵向拉伸比1:1.2~1.6,管材的环向拉伸比1:1.20~1.7,管材的压缩比1:12-25。在加工过程中,将纵向拉伸比控制在1:1.2~1.6,环向拉伸比控制在1:1.20~1.7,提高管材的拉伸强度和环向强度,而将压缩比控制在1:12-25,结合到管材的原料配方,提高PVC树脂和PE树脂的相溶性,进而提高焊口的强度和圆滑性。
进一步的,在所述步骤S2中,挤出机机筒温度,1区175-225℃,2区180-215℃,3区170-200℃,4区165-185℃,合流芯165-195℃。
进一步的,在所述步骤S2中,模具温度为1区175-190℃,2区180-195℃,3区180-200℃,口模温度175-215℃。
进一步的,在所述步骤S2中,挤出机主机螺杆转速8-40转/分钟,机筒的真空度0.04-0.1MPa,水箱中空管0.04-0.08MPa,牵引机速度0.1-5米/分钟。
进一步的,在本发明中,原料还包含抗氧剂1010:0.1-0.8份,紫外光吸收剂UV-531:0.5-5份。提高管材的抗氧化性和抗光照性,利于管材裸露安装,在夏季,可长期在工地上堆放。
本发明的有益效果是:
在本发明中,管材的原料中加入大量的PE树脂,提高PVC管材的强度,并且,加入含氯量40-50%的氯化聚乙烯和含氯量60-70%的氯化聚乙烯作为PE增溶剂,提高PVC和PE的相容性,即较高氯含量的氯化聚乙烯,与PVC分子的接触面积大,氯化聚乙烯与PVC分子之间形成“桥梁”,PE树脂的分子链与PVC树脂的分子量交叉缠绕,提高相容性。在热熔对接焊时,由于管材中PE树脂和PVC树脂的相容高,熔融后的加工温区间变宽,使得焊口处圆滑,焊口处的拉伸强度、抗冲击强度、耐压性等均有所提高。并且,在本发明中,利用大量的PE树脂,对PVC进行改性,提高PVC管材和焊口的强度。
具体实施方式
实施例1:
按以下配方,配置管材原料:
PVC树脂75份;PE树脂50份;氯化聚乙烯(氯含量36%)10份;乙烯-醋酸乙烯共聚物3份;氯化聚乙烯(氯含量48%)4份;氯化聚乙烯(氯含量60%)4份;钙锌稳定剂3份;硬脂酸0.5份;聚乙烯蜡0.8份;ACR1.5份;丙烯腈-丁二烯-苯乙烯共聚物2.8份;纳米钛白粉1.0份。
按照以上发明中配方份数称量,将料加入高速搅拌机中,混合10分钟,混料温度达到105℃,放入冷却搅拌机中冷却到32℃,装袋下道工序备用。
调节模具参数:纵向拉伸比1:1.3,环向拉伸比1.25,压缩比1:12。3、挤出工艺参数:
挤出机机筒温度:1区190℃,2区180℃,3区175℃,4区165℃,合流芯170℃。
模具温度:1区180℃,2区185℃,3区195℃,口模温度195℃。
主机螺杆转速14转/分钟,机筒真空度0.08MPa,水箱中空管0.04MPa,牵引机速度0.5米/分钟。
经挤出成型,得到dn110x4.2mm,的管材,管材长度6米/根。
实施例2:
按以下配方,配置管材原料:
PVC树脂75份,PE树脂40份,氯化聚乙烯(氯含量36%)11份,乙烯-醋酸乙烯共聚物4份,氯化聚乙烯(氯含量48%)3.5份,氯化聚乙烯(氯含量60%)3.5份,钙锌稳定剂3.8份,硬脂酸0.6份,聚乙烯蜡0.7份,ACR 1.8份,丙烯腈-丁二烯-苯乙烯共聚物5.0份,甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物5.0份,纳米钛白粉3.0份,
按上述配方中的份数称量,将各原料加入高速搅拌机中,混合10分钟,混料温度达到105℃,放入冷却搅拌机中冷却到32℃,装袋下道工序备用。
调节模具参数:纵向拉伸比1:1.3,环向拉伸比1.25,压缩比1:12。
挤出工艺参数:
挤出机机筒温度:1区190℃,2区180℃,3区175℃,4区165℃,合流芯170℃。
模具温度:1区180℃,2区185℃,3区195℃,口模温度195℃。
主机螺杆转速25转/分钟,机筒真空度0.08MPa,水箱中空管0.04MPa,牵引机速度0.6米/分钟,
得到规格为dn110x5.3mm的管材,管材长度6米/根。
实施例3:
按照以下重量份数,配置管材原料:
PVC树脂75份;PE树脂55份;氯化聚乙烯(氯含量36%)12份;乙烯-醋酸乙烯共聚物4份,氯化聚乙烯(氯含量48%)4.5份,氯化聚乙烯(氯含量60%)4.5份,钙锌稳定剂4.0份,硬脂酸0.4份,聚乙烯蜡0.8份,ACR,1.8份,甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物1.0份,纳米二氧化硅1.5份,纳米钛白粉1.5份。
按照上述各原料的重要份数,将各原料加入高速搅拌机中,混合10分钟,待混料温度达到110℃,放入冷却搅拌机中冷却到35℃,装袋下道工序备用。
调节模具参数:纵向拉伸比1:1.3,环向拉伸比1.25,压缩比1:13。
挤出工艺参数:
挤出机机筒温度:1区190℃,2区180℃,3区175℃,4区165℃,合流芯170℃。
模具温度:1区180℃,2区185℃,3区195℃,口模温度195℃。
主机螺杆转速18转/分钟,机筒真空度0.08MPa,水箱中空管0.04MPa,牵引机速度0.8米/分钟。
得到规格为dn110x3.2mm的管材,管材的长度6米/根。
实施例4:
按照以下重量份数,配置管材原料:
PVC树脂50份;PE树脂99份;氯化聚乙烯(氯含量37%)12份,氯化聚乙烯(氯含量50%)4.5份,氯化聚乙烯(氯含量70%)4.5份,钙锌稳定剂4.0份,硬脂酸0.4份,聚乙烯蜡0.8份,ACR,1.8份,甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物1.0份,纳米钛白粉0.5份。
按照实施例1所述的模具参数和挤出参数,挤出成型管材。
实施例5:
按照以下重量份数,配置管材原料:
PVC树脂100份;PE树脂40份;氯化聚乙烯(氯含量35%)3份,乙烯-醋酸乙烯共聚物10份,氯化聚乙烯(氯含量50%)6.5份,氯化聚乙烯(氯含量60%)6.5份,钙锌稳定剂3份,硬脂酸1份,聚乙烯蜡0.8份,ACR,1.8份,甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物1.0份,纳米碳酸钙1.5份,纳米钛白粉4份。
按照实施例1所述的模具参数和挤出参数,挤出成型管材。
实施例6:
按照以下重量份数,配置管材原料:
PVC树脂80份;PE树脂60份;氯化聚乙烯(氯含量35%)3份,氯化聚乙烯(氯含量50%)3份,氯化聚乙烯(氯含量60%)3份,钙锌稳定剂5份,硬脂酸2份,聚乙烯蜡0.1份,ACR,0.5份,甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物1.0份,纳米碳酸钙1.5份,纳米钛白粉3份。
按照实施例1所述的模具参数和挤出参数,挤出成型管材。
实施例7:
按照以下重量份数,配置管材原料:
PVC树脂80份;PE树脂60份;氯化聚乙烯(氯含量35%)15份,乙烯-醋酸乙烯共聚物2份,氯化聚乙烯(氯含量50%)5份,氯化聚乙烯(氯含量60%)5份,钙锌稳定剂5份,硬脂酸2份,聚乙烯蜡0.1份,ACR,0.5份,甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物1.0份,纳米石英砂1份,纳米钛白粉10份。
按照实施例2中的模具参数和挤出参数,挤出成型管材。
实施例8:
PVC树脂65份;PE树脂75份;乙烯-醋酸乙烯共聚物18份,氯化聚乙烯(氯含量50%)5份,氯化聚乙烯(氯含量60%)5份,钙锌稳定剂5份,硬脂酸2份,聚乙烯蜡0.1份,ACR,0.5份,甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物1.0份,纳米云母5份,纳米钛白粉3份。
按照实施例2中的模具参数和挤出参数,挤出成型管材。
实施例9:
PVC树脂65份;PE树脂75份;乙烯-醋酸乙烯共聚物18份,氯化聚乙烯(氯含量50%)5份,氯化聚乙烯(氯含量60%)5份,钙锌稳定剂5份,硬脂酸2份,聚乙烯蜡0.1份,ACR,0.5份,甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物1.0份,纳米云母5份,纳米炭黑5份。
按照实施例2中的模具参数和挤出参数,挤出成型管材。
实施例10:
PVC树脂50份;PE树脂40份;氯化聚乙烯(氯含量35%)0.5份,乙烯-醋酸乙烯共聚物,1份,氯化聚乙烯(氯含量45%)6份,氯化聚乙烯(氯含量60%)6份,钙锌稳定剂3份,硬脂酸2份,聚乙烯蜡0.1份,ACR,8份,甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物1.0份,丙烯腈-丁二烯-苯乙烯共聚物5份,纳米石墨烯3份,纳米滑石粉5份。
按照实施例2中的模具参数和挤出参数,挤出成型管材。
对比例1:
在实施例1的基础上,所加入的氯化聚乙烯总量为18份,其氯化聚乙烯的氯含量为10%,其余的原料和份数与实施例1的相同,模具参数和挤出工艺参数与实施例1的也相同。
对比例2:
在实施例1的基础上,所加入的氯化聚乙烯总量为18份,其氯化聚乙烯的氯含量为20%,其余的原料和份数与实施例1的相同,模具参数和挤出工艺参数与实施例1的也相同。
对比例3:
按照以下配方,配置各原料
PVC树脂100份;钙锌稳定剂3份;硬脂酸0.5份;聚乙烯蜡0.8份;ACR 1.5份;丙烯腈-丁二烯-苯乙烯共聚物2.8份;纳米钛白粉1.0份。
按照实施例1的模具参数和挤出工艺参数,挤出成型得到管材。
实施例4:
PVC树脂100份;PE树脂10份,氯化聚乙烯(氯含量10%)10份,钙锌稳定剂3份;硬脂酸0.5份;聚乙烯蜡0.8份;ACR 1.5份;丙烯腈-丁二烯-苯乙烯共聚物2.8份;纳米钛白粉1.0份。
按照实施例1的模具参数和挤出工艺参数,挤出成型得到管材。
实验例:
将上述实施例1-10和对比例1-4得到的管材,依次标号为1-10号和对比1-4号。将得到的管材进行热熔对接焊,即1号管材和1号管材焊接,2号管材和2号管材焊接。焊接后,分别测定各管材焊口的强度、焊口断裂伸长率、焊口冲击强度、焊口折弯度、焊口耐压性,并观察焊口的外观是否圆滑,得到的结果如表1所示。
其中,焊口冲击强度指的是,将焊口在0℃冷冻1小时后,以冲击高2米,锤头半径45mm进行焊口冲击强度测试。焊口耐压性能测试:向焊接后的管材中通入20℃的温水,在公称压力42MPa环应力下,进行液压试验,得到焊口的耐压性能。
表1实施例1-10管材的焊口和对比例1-4管材的焊口的力学性能
Figure BDA0002515529420000101
Figure BDA0002515529420000111
从上述表1中,可以得出,实施例1-10的管材焊口,其焊口的拉伸强度在42.7-48.5Mpa,断裂伸长率175-280%,在进行低温摆锤冲击试验时,实施例1-10的焊口均为破裂,并且,实施例1-10的焊口,在弯折45°后,焊口不断裂,通水后焊口处无渗漏,向焊接后的管材中通入20℃的温水,在公称压力42MPa环应力下,进行液压试验,实施例1-10的焊口处在1小时内均无破裂和渗漏,并且,实施例1-10的焊口处圆滑。
在对比例1-4号中,焊口的拉伸强度在37.5-40.1Mpa,实施例1-10号的焊口处的拉伸强度明显高于对比例1-4的拉伸强度,并且,结合实施例1和对比例1,对比例1中添加的增溶剂氯化聚乙烯的氯含量10%,其余的均与实施例1的相同,由于对比例1中增容剂的氯含量较低,且氯化聚乙烯的种类单一,使得管材中的PVC树脂和PE树脂的相容性较差,溶入到PVC树脂分子中的PE树脂的量较少,PE树脂改性性能较弱,在热熔焊接时,热熔后的管材中的PE树脂难以再融入到PVC树脂中,使得焊口处的拉伸强度要低于管材本体的强度(对比例1的断裂位置为焊口,实施例1的断裂位置为管材)。而在对比实施例1中,加入的增容剂分别为氯含量36%、48%、60%的氯化聚乙烯,其氯含量较高,可将大量的PE树脂溶入到PVC树脂中,明显的提高管材焊口处的强度。同时,由于PE树脂的溶入量增大,热熔后管材的加工温度区间变宽,使得焊接后的焊口处更加的圆滑,焊口的耐压性、抗冲击强度和弯折性均有提高。
同样的,结合到实施例1和对比例2,在对比例2中,氯化聚乙烯的氯含量为20%,相对与对比例1,增加了氯化聚乙烯的氯含量,但从对比例2的管材的焊口性能来看,焊口的拉伸强度、断裂伸长率、抗冲击性能、弯折性能、耐压性能均比实施例1-10的焊口的性能差。
结合实施例1和对比例3,在对比例3中,未加入PE树脂以及增溶剂,即为普通的PVC管材,从表1中,可以看出,对比例3的管材焊口的力学性能明显差与实施例1-10的管材焊口。
综上所述,本发明提高的PVC管材,其具有优异的热熔对接焊性能,焊口处的力学性能明显优于现有的PVC管材。

Claims (9)

1.一种可热熔对接焊聚氯乙烯管材,其特征在于:按重量份数计,包括以下原料,
Figure FDA0002515529410000011
其中,所述PVC增溶剂为含氯量35-37%的氯化聚乙烯、乙烯-醋酸乙烯共聚物中的一种或两种的混合;
所述PE增溶剂为含氯量40-50%的氯化聚乙烯和含氯量60-70%的氯化聚乙烯的混合物。
2.根据权利要求1所述的可热熔对接焊聚氯乙烯管材,其特征在于:所述含氯量40-50%的氯化聚乙烯和含氯量60-70%的氯化聚乙烯的重量份数比为1:1。
3.根据权利要求1所述的可热熔对接焊聚氯乙烯管材,其特征在于:所述增强剂为丙烯腈-丁二烯-苯乙烯共聚物、甲基丙烯酸甲酯-丁二烯-苯乙烯共聚物中一种或者两种共混物。
4.根据权利要求1所述的可热熔对接焊聚氯乙烯管材,其特征在于:所述填充剂为纳米级的碳酸钙、云母、石英砂、黏土、钛白粉、炭黑、石墨烯、滑石粉、二氧化硅中一种或者两种以上混合物。
5.一种如权利要求1-4任一所述的可热熔对接焊聚氯乙烯管材的制备方法,其特征在于:包括以下步骤,
S1混料:将各原料加入到搅拌机中,搅拌均匀,待原料温度达到100-125℃后,将原料加入到冷却搅拌机中,搅拌,并将各原料冷却至28-42℃;
S2挤出成型:调节模具参数和挤出工艺参数,将上述步骤S1混合后的物料加入到挤出机中,挤出管材。
6.根据权利要求5所述的可热熔对接焊聚氯乙烯管材的制备方法,其特征在于:在所述步骤S2中,管材的纵向拉伸比1:1.2~1.6,管材的环向拉伸比1:1.20~1.7,管材的压缩比1:12-25。
7.根据权利要求1所述的可热熔对接焊聚氯乙烯管材的制备方法,其特征在于:在所述步骤S2中,挤出机机筒温度,1区175-225℃,2区180-215℃,3区170-200℃,4区165-185℃,合流芯165-195℃。
8.根据权利要求1所述的可热熔对接焊聚氯乙烯管材的制备方法,其特征在于:在所述步骤S2中,模具温度为1区175-190℃,2区180-195℃,3区180-200℃,口模温度175-215℃。
9.根据权利要求1所述的可热熔对接焊聚氯乙烯管材的制备方法,其特征在于:在所述步骤S2中,挤出机主机螺杆转速8-40转/分钟,机筒的真空度0.04-0.1MPa,水箱中空管0.04-0.08MPa,牵引机速度0.1-5米/分钟。
CN202010474827.1A 2020-05-29 2020-05-29 一种可热熔对接焊聚氯乙烯管材及其制备方法 Pending CN111471254A (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010474827.1A CN111471254A (zh) 2020-05-29 2020-05-29 一种可热熔对接焊聚氯乙烯管材及其制备方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010474827.1A CN111471254A (zh) 2020-05-29 2020-05-29 一种可热熔对接焊聚氯乙烯管材及其制备方法

Publications (1)

Publication Number Publication Date
CN111471254A true CN111471254A (zh) 2020-07-31

Family

ID=71765410

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010474827.1A Pending CN111471254A (zh) 2020-05-29 2020-05-29 一种可热熔对接焊聚氯乙烯管材及其制备方法

Country Status (1)

Country Link
CN (1) CN111471254A (zh)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112321964A (zh) * 2020-10-30 2021-02-05 山东国塑科技实业有限公司 高阻燃耐老化聚氯乙烯复合通信管及其制备方法
CN113881170A (zh) * 2021-11-12 2022-01-04 阿姆斯壮地面材料(中国)有限公司 一种含pvdf(聚偏氟乙烯)的焊线材料的制备方法

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104194218A (zh) * 2014-09-01 2014-12-10 康泰塑胶科技集团有限公司 聚乙烯和聚氯乙烯共混改性的管材及其制备方法
CN105001356A (zh) * 2015-08-07 2015-10-28 芜湖融汇化工有限公司 一种pvc/hdpe增容用氯化聚乙烯、制备方法及其应用

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104194218A (zh) * 2014-09-01 2014-12-10 康泰塑胶科技集团有限公司 聚乙烯和聚氯乙烯共混改性的管材及其制备方法
CN105001356A (zh) * 2015-08-07 2015-10-28 芜湖融汇化工有限公司 一种pvc/hdpe增容用氯化聚乙烯、制备方法及其应用

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112321964A (zh) * 2020-10-30 2021-02-05 山东国塑科技实业有限公司 高阻燃耐老化聚氯乙烯复合通信管及其制备方法
CN113881170A (zh) * 2021-11-12 2022-01-04 阿姆斯壮地面材料(中国)有限公司 一种含pvdf(聚偏氟乙烯)的焊线材料的制备方法

Similar Documents

Publication Publication Date Title
CN111471254A (zh) 一种可热熔对接焊聚氯乙烯管材及其制备方法
CN102417671B (zh) 一种高强度pvc非开挖管件的制备工艺
CN103059474B (zh) 一种木塑复合发泡板及其制备方法
CN100395301C (zh) 大口径聚乙烯管道接口密封用纳米复合热熔胶
CN104558800B (zh) 一种塑料防水板及其制备方法
WO2013149369A1 (zh) 聚乙烯电缆导管
CN102002191B (zh) Ppr/evoh/poe共混高抗冲阻透管材和制造方法
CN101532591A (zh) Upvc管材、件及其制备方法
CN104761794B (zh) 一种杜仲胶形状记忆高分子复合材料及其制备方法
CN104212046B (zh) 多孔梅花管及其制备方法
CN107778690A (zh) 高抗冲性pvc管及其生产方法
CN104629221B (zh) 一种聚氯乙烯内衬管
CN102827439A (zh) 一种pvc-m抗冲击管材
CN107778618A (zh) 抗菌高抗冲性pe给水管及其生产方法
CN104629211A (zh) Pvc-u穿线管材及其制备方法
CN103554601A (zh) 一种高密度聚乙烯双壁波纹管
CN107540916A (zh) 一种用于市政排水的pe管材及其制备方法
CN106893525A (zh) 一种用于钢管防腐用粘接树脂及其制备方法
CN103511765B (zh) 一种中空壁塑钢缠绕排水管材的制造方法
CN107033436A (zh) 抗静电阻燃管材及其制备方法
CN106977799A (zh) 复合再生塑料及其制备方法
CN104292391A (zh) 一种不饱和酸酐接枝氯化聚乙烯熔融生产法
CN106832698A (zh) 一种氯化聚氯乙烯管材组合物及管材制备方法
CN109082000A (zh) 一种原位反应增容合成的复合防水卷材及其制备方法
CN110591231A (zh) 一种高强度高韧性的mpp电力管及其制备方法

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20200731

RJ01 Rejection of invention patent application after publication