CN108047999A - A kind of multi-layer co-extruded hose adhering resin and preparation method thereof - Google Patents

A kind of multi-layer co-extruded hose adhering resin and preparation method thereof Download PDF

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Publication number
CN108047999A
CN108047999A CN201711433068.9A CN201711433068A CN108047999A CN 108047999 A CN108047999 A CN 108047999A CN 201711433068 A CN201711433068 A CN 201711433068A CN 108047999 A CN108047999 A CN 108047999A
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CN
China
Prior art keywords
adhering resin
layer
extruded hose
mass parts
extruded
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
CN201711433068.9A
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Chinese (zh)
Inventor
李楠
毕宏江
杨少辉
肖传富
欧阳贵
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.)
SHANGHAI BANZAN MACROMOLECULE MATERIAL CO Ltd
Original Assignee
SHANGHAI BANZAN MACROMOLECULE MATERIAL CO Ltd
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Publication date
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Priority to CN201711433068.9A priority Critical patent/CN108047999A/en
Publication of CN108047999A publication Critical patent/CN108047999A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J123/00Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers
    • C09J123/02Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers not modified by chemical after-treatment
    • C09J123/04Homopolymers or copolymers of ethene
    • C09J123/08Copolymers of ethene
    • C09J123/0807Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
    • C09J123/0815Copolymers of ethene with aliphatic 1-olefins
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/02Non-macromolecular additives
    • C09J11/04Non-macromolecular additives inorganic
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/02Non-macromolecular additives
    • C09J11/06Non-macromolecular additives organic
    • 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
    • C08K2201/00Specific properties of additives
    • C08K2201/014Additives containing two or more different additives of the same subgroup in C08K
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/08Stabilised against heat, light or radiation or oxydation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/16Applications used for films
    • 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
    • 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
    • C08L2207/062HDPE
    • 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
    • C08L2207/066LDPE (radical process)

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Laminated Bodies (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

The present invention, which provides one kind, has environmental stress resistance high strength multi-layer co-extrusion hose special bonding resin and preparation method thereof, which includes following raw material components and mass parts:100 parts of LLDPE, 1~3 part of Glycidyl methacrylate acid lipid, 0.05~0.2 part of di-tert-butyl peroxide, 15~30 parts of Glycidyl methacrylate acid lipid grafted linear low-density polyethylenes, 15~25 parts of high density polyethylene (HDPE)s, 15~25 parts of low density polyethylene (LDPE)s, 5~10 parts of nitrocellulose.The adhering resin has the performance that UV resistant, weatherability, peel strength are big, bonding is stable persistently, the range of work is wide.

Description

A kind of multi-layer co-extruded hose adhering resin and preparation method thereof
Technical field
The present invention relates to a kind of multi-layer co-extruded hose adhering resin and preparation method thereof, more particularly to a kind of resistance to environment should Power high strength multi-layer co-extrusion hose adhering resin, belongs to adhering resin field.
Background technology
As China's expanding economy and consumption mode constantly change, packaging industry needs various types of high functions, specially With the packing film of change, such as the fresh-keeping function for improving food occurred in the market, the high-barrier of extension article shelf-life Property packaging film, cosmetics composite soft tube, electronic device transportation and packing etc..The film article of these high functionalities is multi-layer co-extruded The result of thin film technique development.Multi-layer co-extruded film is mainly characterized by economy, and functional, intensity is high.Such as PVDC is to oxygen Gas and vapor have very high barrier property, but its price is high, and process can generate harmful chlorine, therefore use The film of the materials coextrusion blow such as PA and LDPE, LLDPE, HDPE, not only meets barrier property, but also meets the necessary machinery of packaging Intensity, cost performance is reasonable, has the higher market competitiveness.So multi-layer co-extruded composite soft tube is exactly to absorb layers of material Advantage meets cost-effective, the feature of environmental protection dispatched from the factory from production and processing to finished product to meet requirement of the product to each performance indicator It is good to wait requirement.
The so-called multi-layer co-extruded plural layers for being exactly extruded into sharp interface layer simultaneously by a die head, and wherein Bonding between layers of material is just particularly important, and comparative maturity is with ethene-vinyl acetate, ethylene, propylene on the market The copolymers such as acid, ethylene methacrylic acid are as adhesive layer, but this adhesive lacks heat resistance, while cost is also higher. And the research of modified PE or MODIFIED PP hot melt adhesive at home is also fewer, it is few applied to just more seeming for composite soft tube packaging See, the functional molecular distribution uniformity difficulty that mainly modified PE is grafted when either PP hot melt adhesive is coextruded in PE or PP, How being evenly distributed of graft is ensured, peeling force is big and stablizes persistently, and environmental stress resistance is strong etc., it is necessary to it does further Research and discussion.
The content of the invention
The present invention in view of the deficienciess of the prior art, the present invention provides one kind there is environmental stress resistance high strength multi-layer to be total to Hose special bonding resin and preparation method thereof is squeezed, the adhering resin is big, viscous with UV resistant, weatherability, peel strength It connects and stablizes performance lasting, that the range of work is wide.
The technical solution that the present invention solves above-mentioned technical problem is as follows:A kind of multi-layer co-extruded hose adhering resin, it is described Adhering resin includes following raw material components and mass parts:
The present invention is further arranged to, and the adhering resin further includes 0.2~1 mass parts vinyl bis-stearamides.
The present invention is further arranged to, and the adhering resin further includes 0.1~0.5 mass parts benzotriazole uvioresistant Agent.
The present invention is further arranged to, and the adhering resin further includes 10~20 mass parts modified sodium silicate powder.
The present invention is further arranged to, and the adhering resin further includes 0.5~2 mass parts talcum powder.
The present invention is further arranged to, and the adhering resin further includes 1~4 mass parts calcium-zinc composite stabilizing agent.
The present invention is further arranged to, and the adhering resin further includes 0.3~0.6 mass parts resistance phenolic antioxidant.
The present invention is further arranged to, and the resistance phenolic antioxidant is the one or more in 1010,1076 or B215.
The present invention also provides the preparation method of multi-layer co-extruded hose adhering resin, step is as follows:(1) prepared by masterbatch: By LLDPE, Glycidyl methacrylate acid lipid, initiator di-tert-butyl peroxide prior to being uniformly mixed in high-speed mixer, Then fusion-grafting is carried out in double screw extruder, rotating speed 1000rpm, 4th area of processing temperature point are respectively 190 DEG C, and 200 DEG C, 210 DEG C, 220 DEG C, extrusion, water cooling, air-dried, pelletizing to obtain the final product;(2) prepared by adhering resin:Remaining component is uniformly mixed, 180~210 DEG C are granulated by the way that double screw extruder is extruded and are dried to obtain the adhering resin.
The multi-layer co-extruded composite soft tube of the present invention is modified with adhering resin by LLDPE linear low density polyethylene, Chemical graft polar micromolecules group on nonpolar polyethylene analysis chain, realizes the high-barriers such as vistanex and PA/EVOH Property resin bonding, had both remained the mechanical property of vistanex, low temperature resistant, ageing-resistant, resistant to chemical etching, and can realize PA/ The high barrier of EVOH ensure that the practicability and security of composite soft tube.
Graft modification linear low density polyethylene used in the present invention is compared with conventional ethylene-ethyl acrylate copolymer system application It is less, but compared with ethylene-ethyl acrylate copolymer, environmental stress resistance is good, at low cost, easy to process, and it is fine with nitric acid Dimension is known as preferable compatibility, and the toughness of composite soft tube can be remarkably reinforced.
Dispersant vinyl bis-stearamides used in the present invention are mainly used for the wettability of regulation system, while can change Dispersiveness between kind formulatory agents makes the homogeneity that adhering resin is bonded more preferably more stable.
The adhering resin of the present invention also has excellent processing performance, is applicable to Multi-layer co-extrusion film-blowing (above blow/under blow) Technique.
The safe and healthy non-poisonous material of the present invention generates.
Specific embodiment
The technical solution in the embodiment of the present invention is clearly and completely described below, it is clear that described embodiment Only part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, the common skill in this field Art personnel all other embodiments obtained without making creative work belong to the model that the present invention protects It encloses.
Embodiment one:
It is prepared by masterbatch:By LLDPE, Glycidyl methacrylate acid lipid, initiator di-tert-butyl peroxide prior at a high speed It is uniformly mixed in mixer, fusion-grafting, rotating speed 1000rpm, processing temperature point four is then carried out in double screw extruder Area is respectively 190 DEG C, and 200 DEG C, 210 DEG C, 220 DEG C, extrusion, water cooling, air-dried, pelletizing to obtain the final product.
It is prepared by adhering resin:
It will grafting masterbatch, high density polyethylene (HDPE), low density polyethylene (LDPE), nitrocellulose, dispersant vinyl stearic bicine diester Amine, benzotriazole UV resistant agent, modified sodium silicate powder, talcum powder, heat stabilizer calcium-zinc composite stabilizing agent, resistance phenols resist Oxygen agent in the position that suitably feeds, is added in more than ratio by the method for multiple spot multichannel, carries out mixed at high speed to being uniformly mixed, It is granulated by the way that double screw extruder is extruded at 180~210 DEG C and is dried to obtain the adhering resin.
The tensile strength of adhering resin made from the present embodiment is 23.44MPa, and it is 6.91N/mm to glue PA peel strengths
Embodiment two:
It is prepared by masterbatch:By LLDPE, Glycidyl methacrylate acid lipid, initiator di-tert-butyl peroxide prior at a high speed It is uniformly mixed in mixer, fusion-grafting, rotating speed 1000rpm, processing temperature point four is then carried out in double screw extruder Area is respectively 190 DEG C, and 200 DEG C, 210 DEG C, 220 DEG C, extrusion, water cooling, air-dried, pelletizing to obtain the final product.
It is prepared by adhering resin:
It will grafting masterbatch, high density polyethylene (HDPE), low density polyethylene (LDPE), nitrocellulose, dispersant vinyl stearic bicine diester Amine, benzotriazole UV resistant agent, modified sodium silicate powder, talcum powder, heat stabilizer calcium-zinc composite stabilizing agent, resistance phenols resist Oxygen agent in the position that suitably feeds, is added in more than ratio by the method for multiple spot multichannel, carries out mixed at high speed to being uniformly mixed, It is granulated by the way that double screw extruder is extruded at 180~210 DEG C and is dried to obtain the adhering resin.
The tensile strength of adhering resin made from the present embodiment is 24.21MPa, and it is 7.03N/mm to glue PA peel strengths
Embodiment three:
It is prepared by masterbatch:By LLDPE, Glycidyl methacrylate acid lipid, initiator di-tert-butyl peroxide prior at a high speed It is uniformly mixed in mixer, fusion-grafting, rotating speed 1000rpm, processing temperature point four is then carried out in double screw extruder Area is respectively 190 DEG C, and 200 DEG C, 210 DEG C, 220 DEG C, extrusion, water cooling, air-dried, pelletizing to obtain the final product.
It is prepared by adhering resin:
It will grafting masterbatch, high density polyethylene (HDPE), low density polyethylene (LDPE), nitrocellulose, dispersant vinyl stearic bicine diester Amine, benzotriazole UV resistant agent, modified sodium silicate powder, talcum powder, heat stabilizer calcium-zinc composite stabilizing agent, resistance phenols resist Oxygen agent in the position that suitably feeds, is added in more than ratio by the method for multiple spot multichannel, carries out mixed at high speed to being uniformly mixed, It is granulated by the way that double screw extruder is extruded at 180~210 DEG C and is dried to obtain the adhering resin.
The tensile strength of adhering resin made from the present embodiment is 23.01MPa, and it is 6.86N/mm to glue EVOH peel strengths
The foregoing is merely presently preferred embodiments of the present invention, is not intended to limit the invention, it is all the present invention spirit and Within principle, any modifications, equivalent replacements and improvements are made should all be included in the protection scope of the present invention.

Claims (9)

1. a kind of multi-layer co-extruded hose adhering resin, which is characterized in that the adhering resin includes following raw material components and matter Measure part:
2. multi-layer co-extruded hose adhering resin according to claim 1, which is characterized in that the adhering resin further includes 0.2~1 mass parts vinyl bis-stearamides.
3. multi-layer co-extruded hose adhering resin according to claim 1, which is characterized in that the adhering resin further includes 0.1~0.5 mass parts benzotriazole UV resistant agent.
4. multi-layer co-extruded hose adhering resin according to claim 1, which is characterized in that the adhering resin further includes 10~20 mass parts modified sodium silicate powder.
5. multi-layer co-extruded hose adhering resin according to claim 1, which is characterized in that the adhering resin further includes 0.5~2 mass parts talcum powder.
6. multi-layer co-extruded hose adhering resin according to claim 1, which is characterized in that the adhering resin further includes 1~4 mass parts calcium-zinc composite stabilizing agent.
7. multi-layer co-extruded hose adhering resin according to claim 1, which is characterized in that the adhering resin further includes 0.3~0.6 mass parts hinder phenolic antioxidant.
8. multi-layer co-extruded hose adhering resin according to claim 7, which is characterized in that it is described resistance phenolic antioxidant be 1010th, the one or more in 1076 or B215.
9. according to the preparation method of any multi-layer co-extruded hose adhering resins of claim 1-8, which is characterized in that step It is rapid as follows:(1) prepared by masterbatch:By LLDPE, Glycidyl methacrylate acid lipid, initiator di-tert-butyl peroxide prior to height It is uniformly mixed in fast mixer, fusion-grafting, rotating speed 1000rpm, processing temperature point is then carried out in double screw extruder 4th area are respectively 190 DEG C, and 200 DEG C, 210 DEG C, 220 DEG C, extrusion, water cooling, air-dried, pelletizing to obtain the final product;(2) prepared by adhering resin:It will Remaining component is uniformly mixed, and is granulated by the way that double screw extruder is extruded at 180~210 DEG C and is dried to obtain the bonding tree Fat.
CN201711433068.9A 2017-12-26 2017-12-26 A kind of multi-layer co-extruded hose adhering resin and preparation method thereof Pending CN108047999A (en)

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CN201711433068.9A CN108047999A (en) 2017-12-26 2017-12-26 A kind of multi-layer co-extruded hose adhering resin and preparation method thereof

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Application Number Priority Date Filing Date Title
CN201711433068.9A CN108047999A (en) 2017-12-26 2017-12-26 A kind of multi-layer co-extruded hose adhering resin and preparation method thereof

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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102086357A (en) * 2010-12-16 2011-06-08 广州市合诚化学有限公司 Adhesive resin used for steel band reinforced polyethylene spiral corrugated pipe and preparation method thereof

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102086357A (en) * 2010-12-16 2011-06-08 广州市合诚化学有限公司 Adhesive resin used for steel band reinforced polyethylene spiral corrugated pipe and preparation method thereof

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Application publication date: 20180518

RJ01 Rejection of invention patent application after publication