CN107718827A - A kind of seven-layer co-extrusion film and its production technology - Google Patents
A kind of seven-layer co-extrusion film and its production technology Download PDFInfo
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- CN107718827A CN107718827A CN201710952498.5A CN201710952498A CN107718827A CN 107718827 A CN107718827 A CN 107718827A CN 201710952498 A CN201710952498 A CN 201710952498A CN 107718827 A CN107718827 A CN 107718827A
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- temperature control
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- fuselage
- polyethylene
- polypropylene
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- 238000001125 extrusion Methods 0.000 title claims abstract description 40
- 238000005516 engineering process Methods 0.000 title claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 11
- -1 polyethylene Polymers 0.000 claims abstract description 112
- 239000004698 Polyethylene Substances 0.000 claims abstract description 81
- 229920000573 polyethylene Polymers 0.000 claims abstract description 81
- 239000004743 Polypropylene Substances 0.000 claims abstract description 29
- 229920001155 polypropylene Polymers 0.000 claims abstract description 29
- 229920006124 polyolefin elastomer Polymers 0.000 claims description 23
- 239000004925 Acrylic resin Substances 0.000 claims description 22
- 229920000178 Acrylic resin Polymers 0.000 claims description 22
- 239000002253 acid Substances 0.000 claims description 22
- 239000010647 garlic oil Substances 0.000 claims description 22
- 125000004079 stearyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 22
- KWUZCAVKPCRJPO-UHFFFAOYSA-N n-ethyl-4-(6-methyl-1,3-benzothiazol-2-yl)aniline Chemical compound C1=CC(NCC)=CC=C1C1=NC2=CC=C(C)C=C2S1 KWUZCAVKPCRJPO-UHFFFAOYSA-N 0.000 claims description 19
- 229920003210 poly(4-hydroxy benzoic acid) Polymers 0.000 claims description 18
- 239000004642 Polyimide Substances 0.000 claims description 13
- 239000003365 glass fiber Substances 0.000 claims description 13
- 229920001721 polyimide Polymers 0.000 claims description 13
- 229920001451 polypropylene glycol Polymers 0.000 claims description 13
- 229920000092 linear low density polyethylene Polymers 0.000 claims description 10
- MEYZYGMYMLNUHJ-UHFFFAOYSA-N tunicamycin Natural products CC(C)CCCCCCCCCC=CC(=O)NC1C(O)C(O)C(CC(O)C2OC(C(O)C2O)N3C=CC(=O)NC3=O)OC1OC4OC(CO)C(O)C(O)C4NC(=O)C MEYZYGMYMLNUHJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000004707 linear low-density polyethylene Substances 0.000 claims description 4
- 101000598921 Homo sapiens Orexin Proteins 0.000 claims description 3
- 101001123245 Homo sapiens Protoporphyrinogen oxidase Proteins 0.000 claims description 3
- 102100029028 Protoporphyrinogen oxidase Human genes 0.000 claims description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 3
- 239000005864 Sulphur Substances 0.000 claims description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims 4
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims 2
- 230000032683 aging Effects 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 2
- 239000010408 film Substances 0.000 description 32
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 9
- 229920003023 plastic Polymers 0.000 description 9
- 239000004033 plastic Substances 0.000 description 9
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 4
- 235000013305 food Nutrition 0.000 description 4
- 150000002083 enediols Chemical class 0.000 description 3
- 238000004806 packaging method and process Methods 0.000 description 3
- 238000004804 winding Methods 0.000 description 3
- BDAGIHXWWSANSR-UHFFFAOYSA-N Formic acid Chemical class OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 229920001233 Poly-4-hydroxybenzoate Polymers 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229960003742 phenol Drugs 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 1
- 229920000426 Microplastic Polymers 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 230000000845 anti-microbial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013410 fast food Nutrition 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 229910001416 lithium ion Inorganic materials 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000012788 optical film Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/16—Articles comprising two or more components, e.g. co-extruded layers
- B29C48/18—Articles comprising two or more components, e.g. co-extruded layers the components being layers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B33/00—Layered products characterised by particular properties or particular surface features, e.g. particular surface coatings; Layered products designed for particular purposes not covered by another single class
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions 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
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/06—Polyethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions 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
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/08—Copolymers of ethene
- C08L23/0807—Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
- C08L23/0815—Copolymers of ethene with aliphatic 1-olefins
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions 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
- C08L23/10—Homopolymers or copolymers of propene
- C08L23/12—Polypropene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/30—Properties of the layers or laminate having particular thermal properties
- B32B2307/31—Heat sealable
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/50—Properties of the layers or laminate having particular mechanical properties
- B32B2307/54—Yield strength; Tensile strength
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/50—Properties of the layers or laminate having particular mechanical properties
- B32B2307/582—Tearability
- B32B2307/5825—Tear resistant
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/70—Other properties
- B32B2307/726—Permeability to liquids, absorption
- B32B2307/7265—Non-permeable
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2203/00—Applications
- C08L2203/16—Applications used for films
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
Landscapes
- 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)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
The present invention provides a kind of seven-layer co-extrusion film, including the first polyethylene layer, the second polyethylene layer, the first polypropylene layer, the 3rd polyethylene layer, the second polypropylene layer, the 4th polyethylene layer and the 5th polyethylene layer being in contact successively, with good tear-proof and tensile strength, ageing resistace and anti-wear performance are improved, and have good market prospects.Simultaneously present invention also offers the production technology of the seven-layer co-extrusion film, using different-diameter screw rod and different zones temperature regulation, come produce relative to film layer, production process is simple, and cost of material is relatively low, and input and output are higher.
Description
Technical field
The present invention relates to plastic sheeting field, and in particular to a kind of seven-layer co-extrusion film and its production technology.
Background technology
Plastic sheeting is usually used in packing, and suitable for every field such as food, medicine, agricultural, industry and space flight and aviation, leads to
It is made frequently with polyvinyl chloride, polyethylene, polypropylene, polystyrene and other resins, plastics package and plastic packet product
Commercially shared share is increasing, particularly composite plastic flexible package, has been widely used for food, medicine, change
The fields such as work, wherein it is again maximum with packaging for foodstuff proportion, for example beverage packaging, quick-frozen food are packed, cooking food is packed,
Fast food packaging etc., these products are all brought great convenience to people's life, and Plastics in China product industry is also at soon
Fast developing stage, 2010 ~ 2011 be the plastic sheeting peak of investment phase, and production capacity acquisition time, and film overall productivity is kept for two
Several growth rate, high-end work uh scale are also progressively domesticizing, the field such as capactive film, lithium ion battery separator, optical film
Also begin to fast development.
Film species has monofilm, composite membrane and a co-extrusion film, the mechanical strength and case hardness of single thin film be relatively low,
The shortcomings of inflammable and poor heat resistance, limits its use range, and co-extrusion film market is more wide, wherein, multi-layer co-extruded technology is just
It is that raw material is directly used as using more than 3 kinds of plastic pellet (or plastic powders), makes every kind of modeling respectively by several extruders
After expecting fusion plastification, into same mouth mold (or by distributor, supplied after the plastics that each extruder is supplied are converged
Enter mouth mold), then by being processed further handling, multi-layer compound film is made.
Wherein, co-extrusion film can be used as winding film effect, and existing winding film is easily torn in use, while is made
Easy aging, breakage, influence using effect, it is difficult to meet demand during.
The content of the invention
(One)Technical problems to be solved
The problem to be solved in the present invention is that existing film strength is low, easy to aging, tear, and service life is shorter.
(Two)Technical scheme
To solve the technical problem, the present invention provides a kind of seven-layer co-extrusion film, including the first polyethylene being in contact successively
Layer, the second polyethylene layer, the first polypropylene layer, the 3rd polyethylene layer, the second polypropylene layer, the 4th polyethylene layer and the 5th are poly-
Pvdf layer;First polyethylene layer is 80 ~ 90% polyethylene, 1 ~ 5% acrylic resin, 1 ~ 3% polyoxygenated third by mass percent
The double octadecyl esters of enediol, 1 ~ 5% garlic oil, 1 ~ 10% ekonol, 0.1 ~ 1% thio-2 acid are formed;Described second
Polyethylene layer is that 90 ~ 95% polyethylene and 5 ~ 10% polyolefin elastomers are formed by mass percent;First polypropylene layer
It is that 80 ~ 90% polypropylene, 5 ~ 10% glass fibres, 5 ~ 10% polyimides are formed by mass percent;3rd polyethylene layer by
Mass percent is that 90 ~ 95% LLDPEs and 5 ~ 10% polyolefin elastomers are formed;Second polypropylene layer
It is that 80 ~ 90% polypropylene, 5 ~ 10% glass fibres, 5 ~ 10% polyimides are formed by mass percent;4th polyethylene layer by
Mass percent is that 90 ~ 95% polyethylene and 5 ~ 10% polyolefin elastomers are formed;5th polyethylene layer is by quality percentage
Than for 80 ~ 90% polyethylene, 1 ~ 5% acrylic resin, 1 ~ 3% polyoxypropyleneglycol, 1 ~ 5% garlic oil, 1 ~ 10% poly- para hydroxybenzene
The double octadecyl esters of formic acid esters, 0.1 ~ 1% thio-2 acid are formed.
Further, first polyethylene layer is 80% polyethylene, 5% acrylic resin, 3% polyoxygenated by mass percent
The double octadecyl esters of propylene glycol, 2% garlic oil, 10% ekonol, 0.1% thio-2 acid are formed.
Further, the 5th polyethylene layer is 80% polyethylene, 5% acrylic resin, 3% polyoxy by mass percent
Change the double octadecyl esters of propylene glycol, 2% garlic oil, 10% ekonol, 0.1% thio-2 acid to form.
Or first polyethylene layer is 90% polyethylene, 2% acrylic resin, 3% polyoxygenated third by mass percent
The double octadecyl esters of enediol, 2% garlic oil, 3% ekonol, 0.1% thio-2 acid are formed.
Further, the 5th polyethylene layer is 90% polyethylene, 2% acrylic resin, 3% polyoxy by mass percent
Change the double octadecyl esters of propylene glycol, 2% garlic oil, 3% ekonol, 0.1% thio-2 acid to form.
Corresponding, present invention also offers a kind of production technology of seven-layer co-extrusion film, specifically include following steps:
S1:Weigh quantitative polyethylene, acrylic resin, polyoxypropyleneglycol, garlic oil, ekonol, sulphur
It is well mixed, is then put into respectively in two extruderses, extruder screw is straight in batch mixer for the double octadecyl esters of dipropionic acid
65mm is selected in footpath, and the temperature control of fuselage one is at 160 ~ 170 DEG C, and the temperature control of fuselage two is at 170 ~ 180 DEG C, the temperature of fuselage three
Degree control is at 175 ~ 185 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, and the temperature control of machine neck is at 190 ~ 200 DEG C, head
Temperature control at 200 ~ 210 DEG C;
S2:Weigh quantitative polyethylene and polyolefin elastomer is put into two extruderses respectively, the choosing of extruder screw diameter
With 65mm, the temperature control of fuselage one is at 150 ~ 160 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature control of fuselage three
System is at 165 ~ 175 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, and the temperature control of machine neck is at 190 ~ 200 DEG C, the temperature of head
Degree control is at 200 ~ 210 DEG C;
S3:Weigh quantitative polypropylene, glass fibre, polyimides to put into two extruderses respectively, extruder screw diameter
From 90mm, the temperature control of fuselage one is at 160 ~ 170 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature of fuselage three
Control at 170 ~ 180 DEG C, the temperature control of fuselage four at 185 ~ 195 DEG C, the temperature control of machine neck at 195 ~ 205 DEG C, head
Temperature control is at 210 ~ 220 DEG C;
S4:Weigh in quantitative LLDPE and polyolefin elastomer input extruder, extruder screw diameter
From 65mm, the temperature control of fuselage one is at 150 ~ 160 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature of fuselage three
Control at 165 ~ 175 DEG C, the temperature control of fuselage four at 180 ~ 190 DEG C, the temperature control of machine neck at 190 ~ 200 DEG C, head
Temperature control is at 200 ~ 210 DEG C;
S5:Above-mentioned seven tunic is cast by coextrusion mold by co-extrusion technology, obtains seven-layer co-extrusion film.
(Three)Beneficial effect
(1)Seven-layer co-extrusion film provided by the invention, using seven-layer co-extrusion technology, seven layer films produced, substantially increase
Raising is obtained in terms of film body intensity, tearing toughness and tensile strength, there are good market prospects.
(2)Seven-layer co-extrusion film provided by the invention, two layers of use modified polyethylene material of head and the tail is made, including poly- second
The double octadecyl esters of alkene, acrylic resin, polyoxypropyleneglycol, garlic oil, ekonol, thio-2 acid are formed,
The mixing of various raw material is improved using garlic oil, while brings anti-microbial property, utilizes acrylic resin and PPOX two
The double octadecyl esters of alcohol, thio-2 acid combine the light resistance and ageing resistace for improving polyethylene, ekonol with
Polyethylene, which combines, improves its wear-resisting, tear resistance, while the layer that finishes up has certain viscosity, has preferably winding function,
Intermediate layer tool polyethylene and polyolefin elastomer, LLDPE and polyolefin elastomer, have good resistance wet
Function, it can prevent vapor from penetrating into, corrosion has good heat sealability and mechanical performance, in addition to polypropylene, glass fibers
Dimension, polyimide layer, the polypropylene layer is located at the both sides in most intermediate layer, using this layer greatly improve overall tear resistance with
And tensile strength.
(3)The production technology of seven-layer co-extrusion film provided by the invention, using seven-layer co-extrusion technology, pass through specific temperature
And the setting of screw rod, to coordinate the shaping of above-mentioned film, moulding process is relatively simple, and production cost is relatively low, meets market need
Ask.
Brief description of the drawings
Fig. 1 is the schematic diagram of seven-layer co-extrusion film in the present invention.
Embodiment
With reference to embodiment, the embodiment of the present invention is described in further detail.Following examples are used for
Illustrate the present invention, but be not limited to the scope of the present invention.
Reference picture 1, the present invention provide a kind of seven-layer co-extrusion film, including the first polyethylene layer 1, second being in contact successively
Polyethylene layer 2, the first polypropylene layer 3, the 3rd polyethylene layer 4, the second polypropylene layer 5, the 4th polyethylene layer 6 and the 5th poly- second
Alkene layer 7;First polyethylene layer is 80 ~ 90% polyethylene, 1 ~ 5% acrylic resin, 1 ~ 3% polyoxygenated third by mass percent
The double octadecyl esters of enediol, 1 ~ 5% garlic oil, 1 ~ 10% ekonol, 0.1 ~ 1% thio-2 acid are formed;Described second
Polyethylene layer is that 90 ~ 95% polyethylene and 5 ~ 10% polyolefin elastomers are formed by mass percent;First polypropylene layer
It is that 80 ~ 90% polypropylene, 5 ~ 10% glass fibres, 5 ~ 10% polyimides are formed by mass percent;3rd polyethylene layer by
Mass percent is that 90 ~ 95% LLDPEs and 5 ~ 10% polyolefin elastomers are formed;Second polypropylene layer
It is that 80 ~ 90% polypropylene, 5 ~ 10% glass fibres, 5 ~ 10% polyimides are formed by mass percent;4th polyethylene layer by
Mass percent is that 90 ~ 95% polyethylene and 5 ~ 10% polyolefin elastomers are formed;5th polyethylene layer is by quality percentage
Than for 80 ~ 90% polyethylene, 1 ~ 5% acrylic resin, 1 ~ 3% polyoxypropyleneglycol, 1 ~ 5% garlic oil, 1 ~ 10% poly- para hydroxybenzene
The double octadecyl esters of formic acid esters, 0.1 ~ 1% thio-2 acid are formed.
Present invention also offers a kind of production technology of seven-layer co-extrusion film, comprise the following steps:
S1:Weigh quantitative polyethylene, acrylic resin, polyoxypropyleneglycol, garlic oil, ekonol, sulphur
It is well mixed, is then put into respectively in two extruderses, extruder screw is straight in batch mixer for the double octadecyl esters of dipropionic acid
65mm is selected in footpath, and the temperature control of fuselage one is at 160 ~ 170 DEG C, and the temperature control of fuselage two is at 170 ~ 180 DEG C, the temperature of fuselage three
Degree control is at 175 ~ 185 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, and the temperature control of machine neck is at 190 ~ 200 DEG C, head
Temperature control at 200 ~ 210 DEG C;
S2:Weigh quantitative polyethylene and polyolefin elastomer is put into two extruderses respectively, the choosing of extruder screw diameter
With 65mm, the temperature control of fuselage one is at 150 ~ 160 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature control of fuselage three
System is at 165 ~ 175 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, and the temperature control of machine neck is at 190 ~ 200 DEG C, the temperature of head
Degree control is at 200 ~ 210 DEG C;
S3:Weigh quantitative polypropylene, glass fibre, polyimides to put into two extruderses respectively, extruder screw diameter
From 90mm, the temperature control of fuselage one is at 160 ~ 170 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature of fuselage three
Control at 170 ~ 180 DEG C, the temperature control of fuselage four at 185 ~ 195 DEG C, the temperature control of machine neck at 195 ~ 205 DEG C, head
Temperature control is at 210 ~ 220 DEG C;
S4:Weigh in quantitative LLDPE and polyolefin elastomer input extruder, extruder screw diameter
From 65mm, the temperature control of fuselage one is at 150 ~ 160 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature of fuselage three
Control at 165 ~ 175 DEG C, the temperature control of fuselage four at 180 ~ 190 DEG C, the temperature control of machine neck at 190 ~ 200 DEG C, head
Temperature control is at 200 ~ 210 DEG C;
S5:Above-mentioned seven tunic is cast by coextrusion mold by co-extrusion technology, obtains seven-layer co-extrusion film.
With reference to specific embodiment, the present invention will be further elaborated:
Embodiment 1
First, weigh by weight 80 parts of polyethylene, 5 parts of acrylic resins, 3 parts of polyoxypropyleneglycols, 2 portions of garlic oils, 10 parts
Ekonol and the double octadecyl esters of 0.1 part of thio-2 acid are well mixed in batch mixer, are then thrown respectively
Enter in two extruderses, extruder screw diameter selects 65mm, and the temperature control of fuselage one is at 160 ~ 170 DEG C, the temperature of fuselage two
Degree control is at 170 ~ 180 DEG C, and the temperature control of fuselage three is at 175 ~ 185 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, machine
The temperature control of neck is at 190 ~ 200 DEG C, and the temperature control of head is at 200 ~ 210 DEG C;Simultaneously weigh by weight 90 parts of polyethylene with
And 10 parts of polyolefin elastomers are put into two extruderses respectively, extruder screw diameter selects 65mm, the temperature control of fuselage one
System is at 150 ~ 160 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, and the temperature control of fuselage three is at 165 ~ 175 DEG C, fuselage four
Temperature control at 180 ~ 190 DEG C, the temperature control of machine neck is at 190 ~ 200 DEG C, and the temperature control of head is at 200 ~ 210 DEG C;Together
Thing weighs 80 parts of polypropylene, 10 parts of glass fibres, 10 parts of polyimides and put into respectively in two extruderses, extruder screw diameter
From 90mm, the temperature control of fuselage one is at 160 ~ 170 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature of fuselage three
Control at 170 ~ 180 DEG C, the temperature control of fuselage four at 185 ~ 195 DEG C, the temperature control of machine neck at 195 ~ 205 DEG C, head
Temperature control is at 210 ~ 220 DEG C;90 parts of LLDPEs and 10 parts of polyolefin elastomer input extrusions are weighed simultaneously
In machine, extruder screw diameter selects 65mm, and the temperature control of fuselage one is at 150 ~ 160 DEG C, and the temperature control of fuselage two is 160
~ 170 DEG C, the temperature control of fuselage three is at 165 ~ 175 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, the temperature control of machine neck
At 190 ~ 200 DEG C, the temperature control of head is at 200 ~ 210 DEG C;Finally by co-extrusion technology by above-mentioned seven tunic be cast co-extrusion into
Type, obtain seven-layer co-extrusion film.
Embodiment 2
First, weigh by weight 90 parts of polyethylene, 2 parts of acrylic resins, 3 parts of polyoxypropyleneglycols, 2 portions of garlic oils, 3 parts it is poly-
P-hydroxybenzoate and the double octadecyl esters of 0.1 part of thio-2 acid are well mixed in batch mixer, are then put into respectively
In two extruderses, extruder screw diameter selects 65mm, and the temperature control of fuselage one is at 160 ~ 170 DEG C, the temperature of fuselage two
Control is at 170 ~ 180 DEG C, and the temperature control of fuselage three is at 175 ~ 185 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, machine neck
Temperature control at 190 ~ 200 DEG C, the temperature control of head is at 200 ~ 210 DEG C;Simultaneously weigh by weight 90 parts of polyethylene and
10 parts of polyolefin elastomers are put into two extruderses respectively, and extruder screw diameter selects 65mm, the temperature control of fuselage one
At 150 ~ 160 DEG C, the temperature control of fuselage two at 160 ~ 170 DEG C, the temperature control of fuselage three at 165 ~ 175 DEG C, fuselage four
Temperature control is at 180 ~ 190 DEG C, and the temperature control of machine neck is at 190 ~ 200 DEG C, and the temperature control of head is at 200 ~ 210 DEG C;Colleague
Weigh 80 parts of polypropylene, 10 parts of glass fibres, 10 parts of polyimides to put into two extruderses respectively, the choosing of extruder screw diameter
With 90mm, the temperature control of fuselage one is at 160 ~ 170 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature control of fuselage three
System is at 170 ~ 180 DEG C, and the temperature control of fuselage four is at 185 ~ 195 DEG C, and the temperature control of machine neck is at 195 ~ 205 DEG C, the temperature of head
Degree control is at 210 ~ 220 DEG C;90 parts of LLDPEs and 10 parts of polyolefin elastomer input extruders are weighed simultaneously
Interior, extruder screw diameter selects 65mm, the temperature control of fuselage one at 150 ~ 160 DEG C, the temperature control of fuselage two 160 ~
170 DEG C, the temperature control of fuselage three is at 165 ~ 175 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, the temperature control of machine neck
At 190 ~ 200 DEG C, the temperature control of head is at 200 ~ 210 DEG C;Finally by co-extrusion technology by above-mentioned seven tunic be cast co-extrusion into
Type, obtain seven-layer co-extrusion film.
Embodiment 3
First, weigh by weight 85 parts of polyethylene, 5 parts of acrylic resins, 3 parts of polyoxypropyleneglycols, 2 portions of garlic oils, 5 parts it is poly-
P-hydroxybenzoate and the double octadecyl esters of 0.1 part of thio-2 acid are well mixed in batch mixer, are then put into respectively
In two extruderses, extruder screw diameter selects 65mm, and the temperature control of fuselage one is at 160 ~ 170 DEG C, the temperature of fuselage two
Control is at 170 ~ 180 DEG C, and the temperature control of fuselage three is at 175 ~ 185 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, machine neck
Temperature control at 190 ~ 200 DEG C, the temperature control of head is at 200 ~ 210 DEG C;Simultaneously weigh by weight 90 parts of polyethylene and
10 parts of polyolefin elastomers are put into two extruderses respectively, and extruder screw diameter selects 65mm, the temperature control of fuselage one
At 150 ~ 160 DEG C, the temperature control of fuselage two at 160 ~ 170 DEG C, the temperature control of fuselage three at 165 ~ 175 DEG C, fuselage four
Temperature control is at 180 ~ 190 DEG C, and the temperature control of machine neck is at 190 ~ 200 DEG C, and the temperature control of head is at 200 ~ 210 DEG C;Colleague
Weigh 80 parts of polypropylene, 10 parts of glass fibres, 10 parts of polyimides to put into two extruderses respectively, the choosing of extruder screw diameter
With 90mm, the temperature control of fuselage one is at 160 ~ 170 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature control of fuselage three
System is at 170 ~ 180 DEG C, and the temperature control of fuselage four is at 185 ~ 195 DEG C, and the temperature control of machine neck is at 195 ~ 205 DEG C, the temperature of head
Degree control is at 210 ~ 220 DEG C;90 parts of LLDPEs and 10 parts of polyolefin elastomer input extruders are weighed simultaneously
Interior, extruder screw diameter selects 65mm, the temperature control of fuselage one at 150 ~ 160 DEG C, the temperature control of fuselage two 160 ~
170 DEG C, the temperature control of fuselage three is at 165 ~ 175 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, the temperature control of machine neck
At 190 ~ 200 DEG C, the temperature control of head is at 200 ~ 210 DEG C;Finally by co-extrusion technology by above-mentioned seven tunic be cast co-extrusion into
Type, obtain seven-layer co-extrusion film.
Coordinate above-described embodiment, compared with the polyethylene film common with the market, obtain a result as follows:
Project | Polyethylene film | Embodiment 1 | Embodiment 2 | Embodiment 3 |
Tensile strength Mpa | 9.2 | 27.1 | 29.3 | 28.5 |
Tearing toughness MPa | 7.1 | 12.6 | 14.4 | 13.9 |
From table results, film tearing toughness of the invention and tensile strength are above polyethylene common on the market
Film, meanwhile, the tensile strength and tearing toughness highest of embodiment 2.
In summary, the restricted embodiment that it is the present invention that above-mentioned embodiment, which is not, all those skilled in the art
The modification carried out on the basis of the substantive content of the present invention or equivalent deformation, the technology category in the present invention.
Claims (6)
1. a kind of seven-layer co-extrusion film, including the first polyethylene layer, the second polyethylene layer, the first polypropylene being in contact successively
Layer, the 3rd polyethylene layer, the second polypropylene layer, the 4th polyethylene layer and the 5th polyethylene layer;
First polyethylene layer is 80 ~ 90% polyethylene, 1 ~ 5% acrylic resin, 1 ~ 3% PPOX by mass percent
The double octadecyl esters of glycol, 1 ~ 5% garlic oil, 1 ~ 10% ekonol, 0.1 ~ 1% thio-2 acid are formed;
Second polyethylene layer is that 90 ~ 95% polyethylene and 5 ~ 10% polyolefin elastomers are formed by mass percent;
First polypropylene layer is 80 ~ 90% polypropylene, 5 ~ 10% glass fibres, 5 ~ 10% polyimides structures by mass percent
Into;
3rd polyethylene layer is 90 ~ 95% LLDPEs and 5 ~ 10% polyolefin elastomers by mass percent
Form;
Second polypropylene layer is 80 ~ 90% polypropylene, 5 ~ 10% glass fibres, 5 ~ 10% polyimides structures by mass percent
Into;
4th polyethylene layer is that 90 ~ 95% polyethylene and 5 ~ 10% polyolefin elastomers are formed by mass percent;
5th polyethylene layer is 80 ~ 90% polyethylene, 1 ~ 5% acrylic resin, 1 ~ 3% PPOX by mass percent
The double octadecyl esters of glycol, 1 ~ 5% garlic oil, 1 ~ 10% ekonol, 0.1 ~ 1% thio-2 acid are formed.
2. a kind of seven-layer co-extrusion film according to claim 1, it is characterised in that first polyethylene layer is by quality percentage
Than for 80% polyethylene, 5% acrylic resin, 3% polyoxypropyleneglycol, 2% garlic oil, 10% ekonol, 0.1%
The double octadecyl esters of thio-2 acid are formed.
3. a kind of seven-layer co-extrusion film according to claim 1, it is characterised in that the 5th polyethylene layer is by quality percentage
Than for 80% polyethylene, 5% acrylic resin, 3% polyoxypropyleneglycol, 2% garlic oil, 10% ekonol, 0.1%
The double octadecyl esters of thio-2 acid are formed.
4. a kind of seven-layer co-extrusion film according to claim 1, it is characterised in that first polyethylene layer is by quality percentage
Than for 90% polyethylene, 2% acrylic resin, 3% polyoxypropyleneglycol, 2% garlic oil, 3% ekonol, 0.1%
The double octadecyl esters of thio-2 acid are formed.
5. a kind of seven-layer co-extrusion film according to claim 1, it is characterised in that the 5th polyethylene layer is by quality percentage
Than for 90% polyethylene, 2% acrylic resin, 3% polyoxypropyleneglycol, 2% garlic oil, 3% ekonol, 0.1%
The double octadecyl esters of thio-2 acid are formed.
6. a kind of production technology of seven-layer co-extrusion film, it is characterised in that comprise the following steps:
S1:Weigh quantitative polyethylene, acrylic resin, polyoxypropyleneglycol, garlic oil, ekonol, sulphur
It is well mixed, is then put into respectively in two extruderses, extruder screw is straight in batch mixer for the double octadecyl esters of dipropionic acid
65mm is selected in footpath, and the temperature control of fuselage one is at 160 ~ 170 DEG C, and the temperature control of fuselage two is at 170 ~ 180 DEG C, the temperature of fuselage three
Degree control is at 175 ~ 185 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, and the temperature control of machine neck is at 190 ~ 200 DEG C, head
Temperature control at 200 ~ 210 DEG C;
S2:Weigh quantitative polyethylene and polyolefin elastomer is put into two extruderses respectively, the choosing of extruder screw diameter
With 65mm, the temperature control of fuselage one is at 150 ~ 160 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature control of fuselage three
System is at 165 ~ 175 DEG C, and the temperature control of fuselage four is at 180 ~ 190 DEG C, and the temperature control of machine neck is at 190 ~ 200 DEG C, the temperature of head
Degree control is at 200 ~ 210 DEG C;
S3:Weigh quantitative polypropylene, glass fibre, polyimides to put into two extruderses respectively, extruder screw diameter
From 90mm, the temperature control of fuselage one is at 160 ~ 170 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature of fuselage three
Control at 170 ~ 180 DEG C, the temperature control of fuselage four at 185 ~ 195 DEG C, the temperature control of machine neck at 195 ~ 205 DEG C, head
Temperature control is at 210 ~ 220 DEG C;
S4:Weigh in quantitative LLDPE and polyolefin elastomer input extruder, extruder screw diameter
From 65mm, the temperature control of fuselage one is at 150 ~ 160 DEG C, and the temperature control of fuselage two is at 160 ~ 170 DEG C, the temperature of fuselage three
Control at 165 ~ 175 DEG C, the temperature control of fuselage four at 180 ~ 190 DEG C, the temperature control of machine neck at 190 ~ 200 DEG C, head
Temperature control is at 200 ~ 210 DEG C;
S5:Above-mentioned seven tunic is cast by coextrusion mold by co-extrusion technology, obtains seven-layer co-extrusion film.
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CN109159519A (en) * | 2018-09-11 | 2019-01-08 | 嘉兴鹏翔包装材料有限公司 | A kind of high sealing-strength bidirection stretching polyolefine heat-shrinkable film |
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2017
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN109159519A (en) * | 2018-09-11 | 2019-01-08 | 嘉兴鹏翔包装材料有限公司 | A kind of high sealing-strength bidirection stretching polyolefine heat-shrinkable film |
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