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CN104194218A - Polyethylene-polyvinyl chloride blend-modified tube and preparation method thereof - Google Patents

Polyethylene-polyvinyl chloride blend-modified tube and preparation method thereof Download PDF

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Publication number
CN104194218A
CN104194218A CN201410439951.9A CN201410439951A CN104194218A CN 104194218 A CN104194218 A CN 104194218A CN 201410439951 A CN201410439951 A CN 201410439951A CN 104194218 A CN104194218 A CN 104194218A
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China
Prior art keywords
parts
polyethylene
pvc
tubing
districts
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CN201410439951.9A
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CN104194218B (en
Inventor
林云青
张双全
郝洪波
郑术友
周祖明
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Kangtai Plastic Technology Co ltd
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Kangtai Plastic Science and Technology Group Co Ltd
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Priority to CN201410439951.9A priority Critical patent/CN104194218B/en
Publication of CN104194218A publication Critical patent/CN104194218A/en
Priority to DE102015206943.5A priority patent/DE102015206943A1/en
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    • 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
    • B29C48/022Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
    • 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
    • B29C48/16Articles comprising two or more components, e.g. co-extruded layers
    • CCHEMISTRY; METALLURGY
    • 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
    • C08K3/01Use of inorganic substances as compounding ingredients characterized by their specific function
    • C08K3/013Fillers, pigments or reinforcing additives
    • CCHEMISTRY; METALLURGY
    • 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
    • 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
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/06PE, i.e. polyethylene
    • 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
    • B29K2027/00Use of polyvinylhalogenides or derivatives thereof as moulding material
    • B29K2027/06PVC, i.e. polyvinylchloride
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16LPIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
    • F16L9/00Rigid pipes
    • F16L9/12Rigid pipes of plastics with or without reinforcement

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

Abstract

The invention belongs to the field of drainage tubes, and particularly relates to a polyethylene-polyvinyl chloride blend-modified tube and a preparation method thereof. The polyethylene-polyvinyl chloride blend-modified tube aims to solve the technical problems of poor shock strength, high sensitivity to temperature, poor ring stiffness, higher cost and short service life in the existing tube. In order to solve the technical problems, the invention provides a polyethylene-polyvinyl chloride blend-modified tube which comprises the following components in parts by weight: 50-150 parts of polyethylene resin, 50-150 parts of polyvinyl chloride resin, 10-30 parts of nano material, 0.5-5 parts of pigment, 2-20 parts of leadless stabilizer, 1-20 parts of processing assistant, 1-5 parts of lubricant, 0.5-5 parts of antioxidant, 0.5-2 parts of photostabilizer, 1-25 parts of solubilizer, 1-15 parts of impact-resistant modifier, 1-15 parts of enhancer and 0.5-10 parts of coupling agent. The polyethylene-polyvinyl chloride blend-modified tube has the advantages of higher ring stiffness, favorable toughness, aging resistance and greatly higher shock strength.

Description

Tubing of polyethylene and blending modification of PVC and preparation method thereof
Technical field
The invention belongs to blowdown tubing field, be specifically related to tubing of polyethylene and blending modification of PVC and preparation method thereof.
Technical background
Along with the continuous propelling that Chinese Urbanization is built, the demand of buried pollution discharge drainage pipe is expanded thereupon, and the performance requriements of corrugated tube is improved thereupon, especially resistance to impact shock.Common extrusion type polyvinyl chloride (PVE) double-wall corrugated pipe exists ring stiffness better, and the cost of material is low, but resistance to impact shock is poor, more responsive to temperature.Common polythene (PE) corrugated pipe good toughness, but ring stiffness is poor, ensure that ring stiffness uses material more, waste resource.
At present, be badly in need of developing that a kind of ring stiffness is good, ageing-resistant, intensity is high, low temperature resistant, cost is low, the Environment Protection and Drainage of Pulled Water corrugated pipe of rice heavy and light, both met the engineerings such as general draining, blowdown, also can be for thering is the conveying of inner pressure medium.
Summary of the invention
The technical problem to be solved in the present invention is that existing tubing resistance to impact shock is poor, and more responsive to temperature, ring stiffness is poor, and cost is higher, and work-ing life is short.
The scheme that the present invention solves the problems of the technologies described above is to provide the tubing of a kind of polyethylene and blending modification of PVC.
The tubing of above-mentioned polyethylene and blending modification of PVC, its component comprises by weight: 50~150 parts of polyvinyl resins, 50~150 parts of polyvinyl chloride (PVC) RESINS, 10~30 parts of nano materials, 0.5~5 part of pigment, without 2~20 parts of lead stabilizers, 1~20 part of processing aid, 1~5 part of lubricant, oxidation inhibitor 0.5-5 part, 0.5~2 part of photostabilizer, expanding material 1-25 part, 1~15 part of anti-impact modifier, 1~15 part of toughener, 0.5~10 part of coupling agent.
In the tubing of above-mentioned polyethylene and blending modification of PVC, the density 0.930~0.965g/cm of described polyvinyl resin 3, melting index (190 DEG C/5.0kg)≤0.5g/10min, yield strength 24~28MPa, elongation at break 350~450%, the oxidation induction time 30~60min 200 DEG C time.
In the tubing of above-mentioned polyethylene and blending modification of PVC, the apparent density>=0.45g/cm of described polyvinyl chloride (PVC) RESINS 3, viscosity number 80~110ml/g, whiteness (160 DEG C, after 10min)>=74%, heat-stable time is not less than 4 minutes, remaining VCM≤1.0mg/kg, 100g resin plasticizer absorbed dose>=19g, the polymerization degree is 750~1100, K value 60~68.
In the tubing of above-mentioned polyethylene and blending modification of PVC, described nano material is at least one in outsourcing process wollastonite, calcium carbonate, talcum powder, mica, barium sulfate, titanium dioxide or the whisker of activation treatment;
In the tubing of above-mentioned polyethylene and blending modification of PVC, described pigment is titanium dioxide, carbon black, ultramarine, at least one in ultramarine, red pigment, violet pigment, yellow ultramarine, gray paint, brown pigments, coffee-like pigment too.
In the tubing of above-mentioned polyethylene and blending modification of PVC, described any one without in lead stabilizer calcium zinc stabilizer, organotin stabilizer or rare-earth stabilizer.
In the tubing of above-mentioned polyethylene and blending modification of PVC, described processing aid be acrylic acid fat high-molecular copolymer (ACR), phthalic acid Diisooctyl or or polycthylene grafted muriate at least one.
In the tubing of above-mentioned polyethylene and blending modification of PVC, described lubricant is at least one in stearic acid, paraffin, polyethylene wax, oxidized polyethlene wax, silicone oil, white oil or stearic amide.
In the tubing of above-mentioned polyethylene and blending modification of PVC, described oxidation inhibitor is at least one in phosphite antioxidant, sulfuric acid oxidation inhibitor or Hinered phenols antioxidant.
In the tubing of above-mentioned polyethylene and blending modification of PVC, described photostabilizer is at least one in benzophenone, benzene potassium acid esters, azimidobenzene, salicylate, dithiocarbamic acid nickel salt, thiobisphenol, phosphate monoester nickel, hindered amine, zinc oxide or ferric oxide.
In the tubing of above-mentioned polyethylene and blending modification of PVC, described expanding material is ethylene-vinyl acetate copolymer, glycidyl methacrylate radiation grafting thing, styrene-maleic anhydride copolymer, ethylene-propylene copolymer, acrylonitrile-butadiene-styrene (ABS) grafts, polypropylene-caprolactone graft copolymer, polypropylene-phenylethene grafted copolymer, maleic anhydride graft copolymer, macromole silane coupling agent, macromole aluminium titanium coupling agent, macromole titanate coupling agent, polypropylene-methacrylic acid ester graft copolymer, polypropylene-acrylonitrile graft copolymer, 1-chloro-4-methyl-benzene graft copolymer, acrylic acid epoxy ester graft copolymer, at least one in chlorinatedpolyethylene or MALEIC ANHYDRIDE graft copolymer.
In the tubing of above-mentioned polyethylene and blending modification of PVC, described anti-impact modifier is at least one in chlorinatedpolyethylene, ethylene-vinyl acetate copolymer, acrylonitrile-butadiene-styrene copolymer, methacrylate butadi ene styrene copolymer, acrylic resin, plexiglass, nitrile rubber or styrene-butadiene rubber(SBR).
In the tubing of above-mentioned polyethylene and blending modification of PVC, described toughener is at least one in Graphene, white carbon black, glass fibre, asbestos, carbon fiber, boron fibre, aramid fiber, Stainless Steel Fibre.
In the tubing of above-mentioned polyethylene and blending modification of PVC, described coupling agent is at least one in titanate coupling agent, aluminate coupling agent, aluminium titanium coupling agent or silane coupling agent.
The present invention also provides the preparation method of the tubing of above-mentioned polyethylene and blending modification of PVC, comprises the following steps:
A, expanding material, the toughener of the coupling agent of polyvinyl resin, total umber 50%, total umber 50% are weighed according to weight part after, stir 5~20 minutes at 60~100 DEG C, then be cooled to 30~38 DEG C, after granulation, obtain standby material I;
B, by polyvinyl chloride (PVC) RESINS, stablizer, pigment, modifier, remaining coupling agent, after oxidation inhibitor, photostabilizer, remaining expanding material, anti-impact modifier are weighed according to weight part, stir 7~30 minutes at 110~135 DEG C, be then cooled to 30~43 DEG C, obtain standby material II;
C, by standby material I and standby material II mix and blend 5~15 minutes, temperature reaches after 60~80 DEG C, then is cooled to 32~38 DEG C, extrudes the tubing that obtains polyethylene and blending modification of PVC.
Wherein, in the preparation method of the tubing of above-mentioned polyethylene and blending modification of PVC, the processing parameter of granulation is as follows described in step b: processing temperature: 165~175 DEG C, machine barrel 1st district, 2 170~185 DEG C, districts, 3 180~185 DEG C, districts, 4 180~195 DEG C, districts; 170~180 DEG C, mould 1st district, 180~190 DEG C, mould 2nd district, 185~235 DEG C, mould 3rd district; Main-machine screw rotating speed is 5~40 turn/min, and cutter machine rotating speed is 5~150 turn/min.
Wherein, in the preparation method of the tubing of above-mentioned polyethylene and blending modification of PVC, extruding described in step c is the method that adopts the two-layer co-extrusion of same mould to be integrated.
Wherein, in the preparation method of the tubing of above-mentioned polyethylene and blending modification of PVC, the processing parameter of extruding described in step c is as follows:
Inwall machine and outer wall machine barrel zone temperature: 1 170~180 DEG C, district, 2 180~185 DEG C, districts, 3 180~190 DEG C, districts, 4 185~195 DEG C, districts, 5 190~205 DEG C, districts, 6 200~215 DEG C, districts, 7 200~220 DEG C, districts, 8 200~225 DEG C, districts, 9 210~225 DEG C, districts, 205~225 DEG C of heads, 200~235 DEG C of materials;
Outer wall main-machine screw rotating speed is 5~40r/min, main frame electric current 50-200A, and inwall engine speed is 5~30 turn/min, and electric current is 40~180A, and pulling speed is 0.1~5 meter/min.
The tubing of polyethylene provided by the invention and blending modification of PVC, there is good high impact properties and ring stiffness, combine the advantage of polythene material good toughness and pvc material good rigidly, make that this tubing is strong and unyielding to be had both, and creep resistance is good, can keep for a long time rigidity, greatly improve the ability of opposing settlement of foundation.Even by Tube flatting, also there will not be cracking, its bending elastic modulus has improved 50~60% than existing polytene corrugated tube, ring stiffness has improved 30~40% than existing polytene corrugated tube, resistance of oxidation has improved 30~45% than existing polytene corrugated tube, resistance to impact shock has improved 3~8 times than existing polyvinyl chloride corrugated tube, and resistance to low temperature is reduced to-15~-25 DEG C, and material cost has reduced by 15~30% than existing polytene corrugated tube.The tubing of polyethylene provided by the invention and blending modification of PVC, has realized that comprehensive strength is high, the ideal effect of comprehensive cost, has embodied good cost performance, has the good market competitiveness.
Embodiment
The tubing of polyethylene and blending modification of PVC, its component comprises by weight: 50~150 parts of polyvinyl resins, 50~150 parts of polyvinyl chloride (PVC) RESINS, 10~30 parts of nano materials, 0.5~5 part of pigment, without 2~20 parts of lead stabilizers, 1~20 part of processing aid, 1~5 part of lubricant, oxidation inhibitor 0.5-5 part, 0.5~2 part of photostabilizer, expanding material 1-25 part, 1~15 part of anti-impact modifier, 1~15 part of toughener, 0.5~10 part of coupling agent.
The preparation method of the tubing of above-mentioned polyethylene and blending modification of PVC, comprises the following steps:
A, expanding material, the toughener of the coupling agent of polyvinyl resin, total umber 50%, total umber 50% are weighed according to weight part after, stir 5~20 minutes at 60~100 DEG C, then be cooled to 30~38 DEG C, after granulation, obtain standby material I;
B, by polyvinyl chloride (PVC) RESINS, stablizer, pigment, modifier, remaining coupling agent, after oxidation inhibitor, photostabilizer, remaining expanding material, anti-impact modifier are weighed according to weight part, stir 7~30 minutes at 110~135 DEG C, be then cooled to 30~43 DEG C, obtain standby material II;
C, by standby material I and standby material II mix and blend 5~15 minutes, temperature reaches after 60~80 DEG C, then is cooled to 32~38 DEG C, extrudes the tubing that obtains polyethylene and blending modification of PVC.
Wherein, in the preparation method of the tubing of above-mentioned polyethylene and blending modification of PVC, the processing parameter of granulation is as follows described in step b:
Processing temperature: 165~175 DEG C, machine barrel 1st district, 2 170~185 DEG C, districts, 3 180~185 DEG C, districts, 4 180~195 DEG C, districts; 170~180 DEG C, mould 1st district, 180~190 DEG C, mould 2nd district, 185~235 DEG C, mould 3rd district;
Main-machine screw rotating speed is 5~40 turn/min, and cutter machine rotating speed is 5~150 turn/min.
Wherein, in the preparation method of the tubing of above-mentioned polyethylene and blending modification of PVC, extruding described in step c is the method that adopts the two-layer co-extrusion of same mould to be integrated.
Wherein, in the preparation method of the tubing of above-mentioned polyethylene and blending modification of PVC, the processing parameter of extruding described in step c is as follows:
Inwall machine and outer wall machine barrel zone temperature: 1 170~180 DEG C, district, 2 180~185 DEG C, districts, 3 180~190 DEG C, districts, 4 185~195 DEG C, districts, 5 190~205 DEG C, districts, 6 200~215 DEG C, districts, 7 200~220 DEG C, districts, 8 200~225 DEG C, districts, 9 210~225 DEG C, districts, 205~225 DEG C of heads, 200~235 DEG C of materials;
Outer wall main-machine screw rotating speed is 5~40r/min, main frame electric current 50-200A, and inwall engine speed is 5~30 turn/min, and electric current is 40~180A, and pulling speed is 0.1~5 meter/min.
Embodiment 1
Adopt the polyethylene of following weight proportion and the tubing of blending modification of PVC:
150 parts of polyvinyl chloride (PVC) RESINS, 75 parts of polyvinyl resins, 25 parts, active nano barium sulfate, 1 part of carbon black, 6 parts of calcium zinc stabilizers, ACR is 10 parts, 1 part of polyethylene wax, 1 part, paraffin, 0.5 part of phosphite antioxidant, 0.5 part of light-stability agent benzophenone, 3 parts of acrylic acid epoxy ester graft copolymers, 10 parts of 5 parts of chlorinatedpolyethylenees of ethylene-vinyl acetate copolymer, 10 parts, glass fibre, 1 part of titanate coupling agent.
Adopt following preparation method:
By polyvinyl resin, coupling agent (total umber 50%), expanding material (total umber 50%), toughener is weighed to add in homogenizer according to weight part and is stirred 10 minutes, temperature reaches 65 DEG C, enter cooler, be cooled to 38 degree, then granulation obtains standby material I.
By polyvinyl chloride (PVC) RESINS, stablizer, pigment, modifier, coupling agent (upper operation remaining 50%), oxidation inhibitor, photostabilizer, expanding material (upper operation remaining 50%), anti-impact modifier is weighed according to weight part, in heating homogenizer, stir 15 minutes, temperature reaches after 120 DEG C, enters in cooling and stirring machine and is cooled to 36 DEG C of packs, obtains standby material II.
Standby material I is stirred 7 minutes together with standby material II in stirrer, when temperature reaches 70 DEG C, enter the cooling 36 DEG C of packs of cooler, be integrated by the method co-extrusion of the two-layer coextrusion of same mould, obtain the tubing of polyethylene and blending modification of PVC.
Wherein, tablets press working process parameter is as follows:
Processing temperature: 165 DEG C, machine barrel 1st district, 2 185 DEG C, districts, 3 180 DEG C, districts, 4 185 DEG C, districts, 180 DEG C, mould 1st district, 180 DEG C, mould 2nd district, 235 DEG C, mould 3rd district;
Main-machine screw rotating speed: 20 turn/min, cutter machine turns 25 turn/min.
Wherein, corrugated tube forcing machine inwall and outer wall processing parameter are as follows:
Inwall machine and outer wall machine barrel zone temperature: 1 175 DEG C, district, 2 180 DEG C, districts, 3 190 DEG C, districts, 4 190 DEG C, districts, 5 205 DEG C, districts, 6 200 DEG C, districts, 7 200 DEG C, districts, 8 225 DEG C, districts, 9 225 DEG C, districts, 225 DEG C of heads, 230 DEG C of materials;
Outer wall main-machine screw rotating speed is 30r/min, and main frame electric current is 1400A, and inwall engine speed is 18 turn/min, and electric current is 80A, and pulling speed is 0.5 meter/min.
Embodiment 2
Adopt the polyethylene of following weight proportion and the tubing of blending modification of PVC:
100 parts of polyvinyl chloride (PVC) RESINS, 75 parts of polyvinyl resins, 25 parts of active nano talcum powder, 1 part of titanium dioxide, 3 parts of organotin stabilizers, ACR is 10 parts, 1 part of polyethylene wax, 1 part, paraffin, phosphite antioxidant 168 is 0.5 part, 0.5 part of photostabilizer azimidobenzene, 2 parts of macromole silane coupling agents, 5 parts of 1-chloro-4-methyl-benzene graft copolymers, 5 parts of nitrile rubbers, 5 parts of chlorinatedpolyethylenees, 5 parts of Graphenes, 1 part of titanate coupling agent.
Preparation method and working process parameter are with embodiment 1.
Embodiment 3
The polyethylene of embodiment 1,2 preparation and PVC modified tubing, its performance test is as table 1:
The performance test of table 1 polyethylene and PVC modified tubing
Polyethylene provided by the invention and PVC modified tubing, ring stiffness is improved, and good toughness, ageing-resistant, has greatly improved resistance to impact shock.

Claims (10)

1. the tubing of polyethylene and blending modification of PVC, its component comprises by weight: 50~150 parts of polyvinyl resins, 50~150 parts of polyvinyl chloride (PVC) RESINS, 10~30 parts of nano materials, 0.5~5 part of pigment, without 2~20 parts of lead stabilizers, 1~20 part of processing aid, 1~5 part of lubricant, oxidation inhibitor 0.5-5 part, 0.5~2 part of photostabilizer, expanding material 1-25 part, 1~15 part of anti-impact modifier, 1~15 part of toughener, 0.5~10 part of coupling agent.
2. the tubing of polyethylene according to claim 1 and blending modification of PVC, is characterized in that: the density 0.930~0.965g/cm of described polyvinyl resin 3, melting index≤0.5g/10min when 190 DEG C/5.0kg, surrenders strong 24~28MPa, elongation at break 350~450%, the oxidation induction time 30~60min 200 DEG C time.
3. the tubing of polyethylene according to claim 1 and blending modification of PVC, is characterized in that: the apparent density>=0.45g/cm of described polyvinyl chloride (PVC) RESINS 3, viscosity number 80~110mL/g, whiteness (160 DEG C, after 10min)>=74%, heat-stable time is not less than 4 minutes, remaining VCM≤1.0mg/kg, 100g resin plasticizer absorbed dose>=19g, the polymerization degree is 750~1100, K value 60~68.
4. the tubing of polyethylene according to claim 1 and blending modification of PVC, is characterized in that: described nano material is through at least one in the wollastonite of activation treatment, calcium carbonate, talcum powder, mica, barium sulfate, titanium dioxide or whisker;
Described pigment is titanium dioxide, carbon black, ultramarine, at least one in ultramarine, red pigment, violet pigment, yellow ultramarine, gray paint, brown pigments, coffee-like pigment too;
Described any one without in lead stabilizer calcium zinc stabilizer, organotin stabilizer or rare-earth stabilizer;
Described processing aid be acrylic acid fat high-molecular copolymer, phthalic acid Diisooctyl or or polycthylene grafted muriate at least one;
Described lubricant is at least one in stearic acid, paraffin, polyethylene wax, oxidized polyethlene wax, silicone oil, white oil or stearic amide;
Described oxidation inhibitor is at least one in phosphite antioxidant, sulfuric acid oxidation inhibitor or Hinered phenols antioxidant;
Described photostabilizer is at least one in benzophenone, benzene potassium acid esters, azimidobenzene, salicylate, dithiocarbamic acid nickel salt, thiobisphenol, phosphate monoester nickel, hindered amine, zinc oxide or ferric oxide.
5. the tubing of polyethylene according to claim 1 and blending modification of PVC, it is characterized in that: described expanding material is ethylene-vinyl acetate copolymer, glycidyl methacrylate radiation grafting thing, styrene-maleic anhydride copolymer, ethylene-propylene copolymer, acrylonitrile-butadiene-styrene (ABS) grafts, polypropylene-caprolactone graft copolymer, polypropylene-phenylethene grafted copolymer, maleic anhydride graft copolymer, macromole silane coupling agent, macromole aluminium titanium coupling agent, macromole titanate coupling agent, polypropylene-methacrylic acid ester graft copolymer, polypropylene-acrylonitrile graft copolymer, 1-chloro-4-methyl-benzene graft copolymer, acrylic acid epoxy ester graft copolymer, at least one in chlorinatedpolyethylene or MALEIC ANHYDRIDE graft copolymer.
6. the tubing of polyethylene according to claim 1 and blending modification of PVC, is characterized in that: described anti-impact modifier is at least one in chlorinatedpolyethylene, ethylene-vinyl acetate copolymer, acrylonitrile-butadiene-styrene copolymer, methacrylate butadi ene styrene copolymer, acrylic resin, plexiglass, nitrile rubber or styrene-butadiene rubber(SBR);
Described toughener is at least one in Graphene, white carbon black, glass fibre, asbestos, carbon fiber, boron fibre, aramid fiber, Stainless Steel Fibre;
Described coupling agent is at least one in titanate coupling agent, aluminate coupling agent, aluminium titanium coupling agent or silane coupling agent.
7. the preparation method of the tubing of polyethylene and blending modification of PVC described in claim 1~6, comprises the following steps:
A, expanding material, the toughener of the coupling agent of polyvinyl resin, total umber 50%, total umber 50% are weighed according to weight part after, stir 5~20 minutes at 60~100 DEG C, then be cooled to 30~38 DEG C, after granulation, obtain standby material I;
B, by polyvinyl chloride (PVC) RESINS, stablizer, pigment, modifier, remaining coupling agent, after oxidation inhibitor, photostabilizer, remaining expanding material, anti-impact modifier are weighed according to weight part, stir 7~30 minutes at 110~135 DEG C, be then cooled to 30~43 DEG C, obtain standby material II;
C, by standby material I and standby material II mix and blend 5~15 minutes, temperature reaches after 60~80 DEG C, then is cooled to 32~38 DEG C, extrudes the tubing that obtains polyethylene and blending modification of PVC.
8. the preparation method of the tubing of polyethylene and blending modification of PVC according to claim 7, it is characterized in that: described in step b, the processing parameter of granulation is as follows: processing temperature: 165~175 DEG C, machine barrel 1st district, 2 170~185 DEG C, districts, 3 180~185 DEG C, districts, 4 180~195 DEG C, districts; 170~180 DEG C, mould 1st district, 180~190 DEG C, mould 2nd district, 185~235 DEG C, mould 3rd district; Main-machine screw rotating speed is 5~40 turn/min, and cutter machine rotating speed is 5~150 turn/min.
9. the preparation method of the tubing of polyethylene and blending modification of PVC according to claim 7, is characterized in that: extruding described in step c is the method that adopts the two-layer co-extrusion of same mould to be integrated.
10. the preparation method of the tubing of polyethylene and blending modification of PVC according to claim 7, is characterized in that: the processing parameter of extruding described in step c is as follows:
Inwall machine and outer wall machine barrel zone temperature: 1 170~180 DEG C, district, 2 180~185 DEG C, districts, 3 180~190 DEG C, districts, 4 185~195 DEG C, districts, 5 190~205 DEG C, districts, 6 200~215 DEG C, districts, 7 200~220 DEG C, districts, 8 200~225 DEG C, districts, 9 210~225 DEG C, districts, 205~225 DEG C of heads, 200~235 DEG C of materials;
Outer wall main-machine screw rotating speed is 5~40r/min, main frame electric current 50-200A, and inwall engine speed is 5~30 turn/min, and electric current is 40~180A, and pulling speed is 0.1~5 meter/min.
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