CN105085978A - Production method for PE gas pipe - Google Patents

Production method for PE gas pipe Download PDF

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Publication number
CN105085978A
CN105085978A CN201510281502.0A CN201510281502A CN105085978A CN 105085978 A CN105085978 A CN 105085978A CN 201510281502 A CN201510281502 A CN 201510281502A CN 105085978 A CN105085978 A CN 105085978A
Authority
CN
China
Prior art keywords
temperature
production method
gas line
starting material
line production
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
CN201510281502.0A
Other languages
Chinese (zh)
Inventor
王幼芳
冷建波
吴品玲
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.)
GUANGXI GOLD BEACH PIPE INDUSTRY TECHNOLOGY Co Ltd
Original Assignee
GUANGXI GOLD BEACH PIPE INDUSTRY TECHNOLOGY 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 GUANGXI GOLD BEACH PIPE INDUSTRY TECHNOLOGY Co Ltd filed Critical GUANGXI GOLD BEACH PIPE INDUSTRY TECHNOLOGY Co Ltd
Priority to CN201510281502.0A priority Critical patent/CN105085978A/en
Publication of CN105085978A publication Critical patent/CN105085978A/en
Pending legal-status Critical Current

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Classifications

    • 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
    • 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
    • C08K3/34Silicon-containing compounds
    • C08K3/346Clay
    • 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
    • C08L23/06Polyethene
    • 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
    • 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
    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/06Properties of polyethylene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2310/00Masterbatches

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Dispersion Chemistry (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

The invention provides a production method for a PE gas pipe. The production method comprises the following steps: S1, putting 95-97% of PE resin powder, 2-3% of color masterbatch and 1-4% of a clay nano composite material into a drying mixer to be dried and stirred to form raw materials, wherein the drying temperature is 60-80 DEG C, the mixing time is longer than 2 hours, and the water content of the raw materials is less than 0.015%; S2, putting the dried raw materials into a stripper to be melted, extruded and granulated; and S3, inputting the granulated material in the step 2 into an extruder to be melted and extruded, and spraying water to cool the extruded material through a cooling water channel, wherein the temperature of a screw charge barrel of the stripper ranges from 175 DEG C to 220 DEG C, the temperature at the nose part ranges from 185 DEG C to 200 DEG C, and the temperature at a neck mould ranges from 190 DEG C to 210 DEG C. The product produced by the method is good in flame retardance and flexibility, low-temperature-resistant, high-temperature-resistant, strong in quick crack growth breaking tenacity and good in crushing resistance.

Description

A kind of PE gas line production method
Technical field
The present invention relates to tubing field, particularly relate to a kind of PE gas line production method.
Background technology
PE material, due to advantages such as its intensity are high, high temperature resistant, erosion resistance is good, nontoxic, is widely used in water pipe and gas line manufacture field.Because it can't get rusty, flame retardant resistance is strong, so be the desirable tubing as gas line; Wherein PE material has corrosion-resistant relative to steel pipe, not easily the performance such as cooperating microorganisms.
Along with the further expansion of urban construction, PE gas line also will be further applied in more in rugged environment, such as, in the low temperature continued, acid or alkali environment, so need the performance further promoting PE gas line, but PE gas line in process of production due to adopt can be different manufacturing process, the assembled watch produced reveals different characteristics, such as splitting resistance.
Summary of the invention
The technical problem to be solved in the present invention is: the PE gas line production method providing a kind of elongation at break high.
For achieving the above object, the invention provides a kind of PE gas line production method, described PE gas line production method comprises the following steps:
Step 1: PE resin-oatmeal 95%-97%, look female 2%-3%, clay nanocomposites 1 ~ 4% are put into drying blendor oven dry together and stirred formation starting material, starting material bake out temperature 60 DEG C-80 DEG C, compounding time continues more than 2 hours, after high temperature mixing, starting material moisture content is less than 0.015%.
Step 2: by the starting material in step 1, drops in shedder and melt extrudes granulation;
Step 3: the granulation material described in step 2 is dropped into forcing machine and extrudes through melting, die orifice, and through cooling trough spraying cooling, obtain PE gas line;
Wherein, the actual temperature on described shedder screw cylinder controls between 175 DEG C-220 DEG C, and head spot temperature controls between 185 DEG C-200 DEG C, and die temperature controls between 190 DEG C-210 DEG C.
Further, described spraying cooling water temperature is between 20 DEG C-40 DEG C, and vacuum pressure is between 0.1-0.8Mpa.
Further, described PE resin-oatmeal is the special mixed ingredients of Borealis HE3490LS.
Further, described clay nanocomposites is phyllosilicate nano material, comprises montmorillonite.
Beneficial effect of the present invention:
The PE gas line that method provided by the invention is produced has good flame retardant resistance, snappiness, low temperature resistant, high temperature resistant, and it is strong that rapid crack increases fracture toughness property, and crushing resistance is good.
Embodiment
For further setting forth the technique means and effect thereof that the present invention takes, be described in detail below in conjunction with the preferred embodiments of the present invention.
The video interphone terminal video intercom extension set of what the specific embodiment of the invention provided the invention provides a kind of detectable smog.
For achieving the above object, the invention provides a kind of PE gas line production method, comprise the following steps:
Step 1: PE resin-oatmeal 95%-97%, look female 2%-3%, clay nanocomposites 1 ~ 4% are put into drying blendor oven dry together and stirred formation starting material, starting material bake out temperature 60 DEG C-80 DEG C, compounding time continues more than 2 hours, after high temperature mixing, starting material moisture content is less than 0.015%.
Step 2: by the starting material in step 1, drops in shedder and melt extrudes granulation;
Step 3: the granulation material described in step 2 is dropped into forcing machine and extrudes through melting, die orifice, and through cooling trough spraying cooling, obtain PE gas line;
Wherein, the actual temperature on described shedder screw cylinder controls between 175 DEG C-220 DEG C, and head spot temperature controls between 185 DEG C-200 DEG C, and die temperature controls between 190 DEG C-210 DEG C.
In the present embodiment, described starting material melt flow rate (MFR): 0.22g/10min, density: 0.959g/cm3, oxidation induction time can reach 128min, tensile strength: 25MPa, elongation at break: 600%.
Further, described spraying cooling water temperature is between 20 DEG C-40 DEG C, and vacuum pressure is between 0.1-0.8Mpa.
Further, described PE resin-oatmeal is the special mixed ingredients of Borealis HE3490LS.
In the present embodiment, the special mixed ingredients of described Borealis HE3490LS has good resistance to cleavage, Heat stability is good, and anti-uvioresistant is strong, the features such as good processing characteristics, all technical parameter is also all obviously better than the raw material of the PE100 of domestic petrochemical industry producer.
Further, described clay nanocomposites is phyllosilicate nano material, comprises montmorillonite.
In the present embodiment, increase clay nanocomposites has very strong mechanics and strengthens the property, and can increase drag in the two-dimensional direction.
In the present embodiment, the described montmorillonite regenerating easily of employing utilizes, and its mechanical property can be improved equally in regeneration.The clay nanocomposites filler particles increased in addition is little, can make to comprise the surface of plastic products made brighter and cleaner.
In addition, according to the experimental demonstration repeatedly of the broken material sample of the goods to method for product and same materials, find that this raw material second stage employ performance is without obvious decline, can be used in the production of PE water service pipe, its PE water service pipe produced enough can meet requirements.
The above, for the person of ordinary skill of the art, can make other various corresponding change and distortion according to technical scheme of the present invention and technical conceive, and all these change and be out of shape the protection domain that all should belong to the claims in the present invention.

Claims (4)

1. a PE gas line production method, is characterized in that, comprises the following steps:
Step 1: PE resin-oatmeal 95%-97%, look female 2%-3%, clay nanocomposites 1 ~ 4% are put into drying blendor oven dry together and stirred formation starting material, starting material bake out temperature 60 DEG C-80 DEG C, compounding time continues more than 2 hours, after high temperature mixing, starting material moisture content is less than 0.015%;
Step 2: by the starting material in step 1, drops in shedder and melt extrudes granulation;
Step 3: the granulation material described in step 2 is dropped into forcing machine and extrudes through melting, die orifice, and through cooling trough spraying cooling, obtain PE gas line;
Wherein, the actual temperature on described shedder screw cylinder controls between 175 DEG C-220 DEG C, and head spot temperature controls between 185 DEG C-200 DEG C, and die temperature controls between 190 DEG C-210 DEG C.
2. PE gas line production method according to claim 1, is characterized in that, described spraying cooling water temperature is between 20 DEG C-40 DEG C, and vacuum pressure is between 0.1-0.8Mpa.
3. PE gas line production method according to claim 1, is characterized in that, described PE resin-oatmeal is the special mixed ingredients of Borealis HE3490LS.
4. PE gas line production method according to claim 1, it is characterized in that, described clay nanocomposites is phyllosilicate nano material, comprises montmorillonite.
CN201510281502.0A 2015-05-28 2015-05-28 Production method for PE gas pipe Pending CN105085978A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510281502.0A CN105085978A (en) 2015-05-28 2015-05-28 Production method for PE gas pipe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510281502.0A CN105085978A (en) 2015-05-28 2015-05-28 Production method for PE gas pipe

Publications (1)

Publication Number Publication Date
CN105085978A true CN105085978A (en) 2015-11-25

Family

ID=54567366

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510281502.0A Pending CN105085978A (en) 2015-05-28 2015-05-28 Production method for PE gas pipe

Country Status (1)

Country Link
CN (1) CN105085978A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107189172A (en) * 2017-07-14 2017-09-22 长兴佳能高分子材料有限公司 A kind of PE tubing production technology
CN109206710A (en) * 2018-08-27 2019-01-15 四川省海维塑胶有限公司 A kind of production technology of buried combustion gas PE tubing

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107189172A (en) * 2017-07-14 2017-09-22 长兴佳能高分子材料有限公司 A kind of PE tubing production technology
CN109206710A (en) * 2018-08-27 2019-01-15 四川省海维塑胶有限公司 A kind of production technology of buried combustion gas PE tubing

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Application publication date: 20151125