CN115093689A - Low-creep and stable-size PC film production process - Google Patents

Low-creep and stable-size PC film production process Download PDF

Info

Publication number
CN115093689A
CN115093689A CN202210732870.2A CN202210732870A CN115093689A CN 115093689 A CN115093689 A CN 115093689A CN 202210732870 A CN202210732870 A CN 202210732870A CN 115093689 A CN115093689 A CN 115093689A
Authority
CN
China
Prior art keywords
parts
mixture
creep
film
filler
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
CN202210732870.2A
Other languages
Chinese (zh)
Inventor
龙学文
陈光石
许义鹏
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.)
Anhui Chicheng Plastic Rubber Technology Co ltd
Original Assignee
Anhui Chicheng Plastic Rubber 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 Anhui Chicheng Plastic Rubber Technology Co ltd filed Critical Anhui Chicheng Plastic Rubber Technology Co ltd
Priority to CN202210732870.2A priority Critical patent/CN115093689A/en
Publication of CN115093689A publication Critical patent/CN115093689A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2369/00Characterised by the use of polycarbonates; Derivatives of polycarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2445/00Characterised by the use of homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic ring system; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2451/00Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
    • C08J2451/06Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2451/00Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
    • C08J2451/08Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers grafted on to macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • 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
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K2003/2237Oxides; Hydroxides of metals of titanium
    • C08K2003/2241Titanium dioxide
    • 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
    • C08K2201/011Nanostructured additives
    • 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
    • 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
    • C08K3/02Elements
    • C08K3/04Carbon
    • 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
    • C08K3/36Silica
    • 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
    • C08K5/00Use of organic ingredients
    • C08K5/0008Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
    • C08K5/0083Nucleating agents promoting the crystallisation of the polymer matrix
    • 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
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/20Carboxylic acid amides
    • 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
    • C08K9/00Use of pretreated ingredients

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

The invention relates to the technical field of PC films, and discloses a production process of a low-creep and stable-size PC film, which comprises the following raw materials in parts by weight: 100-200 parts of PC resin, 50-70 parts of cycloolefin copolymer, 5-10 parts of compatilizer, 7-13 parts of chain extender, 5-7 parts of toluene, 1-3 parts of nucleating agent, 10-30 parts of filler, 3-5 parts of toughening agent and 3-5 parts of dispersant. According to the production process of the low-creep and stable-size PC film, when the PC resin is produced, a large number of benzene ring structures are crosslinked on a linear chain or a branched chain of polypropylene in the stirring process to form a large number of gap structures, and after the filler is added, the gap structures are filled in gaps by the filler, and meanwhile, the graphene with electronegativity is adsorbed with the polypropylene, so that the graphene is inserted into the surface of the polypropylene to generate conductivity; the sodium polyacrylate modified polypropylene fiber has the advantages that the linear chain structure of the sodium polyacrylate is guaranteed, various additive components are stably introduced, and the oxidation resistance, heat resistance, flame retardance, strength, antistatic performance and creep resistance of the PP fiber are effectively improved.

Description

Low-creep and stable-size PC film production process
Technical Field
The invention relates to the technical field of PC films, in particular to a production process of a PC film with low creep and stable size.
Background
The PC film is a polycarbonate film for short, and is an amorphous, odorless, nontoxic, highly transparent colorless or yellowish thermoplastic engineering plastic.
At present, when a traditional PC film is produced, PC resin and a processing aid are usually added into a double-screw base machine to form a film, but the PC film produced by the method has the advantages of stable heat resistance and size and poor creep deformation resistance, and cannot meet the requirements of materials in the field with higher heat resistance requirements such as heat-releasing electric appliances, so that a low-creep and stable-size PC film production process is provided, and the problems are solved.
Disclosure of Invention
Technical problem to be solved
Aiming at the defects of the prior art, the invention provides a production process of a PC film with low creep deformation and stable size, and solves the problems that the heat resistance and the size stability of the material are poor, the creep deformation resistance is generally poor, and the requirements of the fields with higher heat resistance requirements, such as materials of heat-releasing electrical appliances and the like, cannot be met.
(II) technical scheme
The invention provides the following technical scheme: a production process of a low-creep and dimensionally stable PC film comprises the following raw materials in parts by weight: 100-200 parts of PC resin, 50-70 parts of cycloolefin copolymer, 5-10 parts of compatilizer, 7-13 parts of chain extender, 5-7 parts of toluene, 1-3 parts of nucleating agent, 10-30 parts of filler, 3-5 parts of flexibilizer and 3-5 parts of dispersant.
Preferably, the main chain of the cycloolefin copolymer is a cycloolefin, and the grafting monomer is one of maleic anhydride, maleic ester monomers, fumaric acid, fumaric ester monomers, acrylic acid, acrylate monomers, methacrylic acid, or methacrylate monomers.
Preferably, the compatilizer is prepared from maleic anhydride grafted polyphenyl ether and maleic anhydride grafted polyethylene according to a mass ratio of (1-3): (2-4).
Preferably, the cycloolefin copolymer is one or more of ethylene-norbornene copolymer (COC), styrene-norbornene Copolymer (COP), COC derivative, and COP derivative.
Preferably, the dispersant is modified ethylene bis fatty acid amide, and the nucleating agent is a beta-nucleating agent.
Preferably, the filler is a mixture of nano titanium dioxide, nano silicon dioxide and graphite, the mixing ratio of the nano titanium dioxide to the nano silicon dioxide to the graphite is 1.7:2:1,
a low creep, dimensionally stable PC film production process comprising the steps of:
s1, preparing the materials;
s2, adding the PC resin, the toluene and the filler into a stirrer, stirring at the speed of 800-1000r/min, introducing nitrogen to 0.5MPa, heating to 200 ℃ at the speed of 20 ℃/min, and then stirring at constant temperature for 60-80min to form a mixture A;
s3, adding mixture a into the hopper of an extruder, the temperature of the extruder being 1 stage: 170 ℃ and 180 ℃, 2 sections: 180 ℃ and 190 ℃ and 3 sections: 190 plus temperature to 200 ℃, starting an extruder after reaching the plasticizing temperature, wherein the speed of the extruder is 45-50RP, and extruding and stretching to obtain a mixture B.
S4, adding the cyclic olefin copolymer, the chain extender and the nucleating agent into a reaction kettle, mixing, and stirring at the rotation speed of 1200r/min for 40-60min to obtain a mixture C;
s5, adding the mixture C into a double-screw extruder to obtain a mixture D.
S6, placing the mixture D and the mixture B into a UV illumination box for illumination for 15-20 seconds;
s7, adding the mixture B, the mixture D and the rest materials after illumination into a double-screw granulator, extruding, granulating and drying to obtain slices;
and S8, melting and extruding the slices, cooling, and performing longitudinal stretching, transverse stretching and sizing after cooling to obtain the PC film with low creep and stable size.
(III) advantageous effects
Compared with the prior art, the invention provides a production process of a PC film with low creep and stable size, which has the following beneficial effects:
1. the low-creep and stable-size PC film production process can synthesize the advantageous properties of various unit graft copolymers, realize complementation among all components, make up the defect of single performance of the unit graft copolymers, and achieve the effect that one is added and one is larger than two.
2. According to the production process of the PC film with low creep and stable size, the compound is prepared by melting and mixing the graft copolymers with various units through a screw melting, mixing and extruding process, so that the advantages and properties of the graft copolymers with various units can be integrated, and the functional complementation among the graft copolymers with various units can be realized. The method has simple process, can solve the problem of single performance of the existing unit graft copolymer, and can also avoid the problems of high control difficulty and high crosslinking risk of the grafting process in the process of multi-graft copolymerization.
3. According to the production process of the low-creep and stable-size PC film, the cyclic olefin copolymer mainly refers to a copolymer of norbornene and other olefins, a large number of norbornene chain segments exist on a macromolecular chain, the rotation of the molecular chain is difficult due to the huge steric hindrance effect of the norbornene chain segments, and then higher glass transition temperature and good rigidity are reflected, and meanwhile, the macromolecular chain segments are difficult to move and show lower creep property due to the fact that the rotation of the molecular chain segments is difficult
4. According to the production process of the low-creep and stable-size PC film, when the PP resin is produced, a large number of benzene ring structures are crosslinked on a linear chain or a branched chain of polypropylene in the stirring process to form a large number of gap structures, and after the filler is added, the gap structures are filled in gaps by the filler, and meanwhile, graphene with electronegativity is adsorbed with the polypropylene, so that the graphene is inserted into the surface of the polypropylene to generate conductivity; the sodium polyacrylate fiber has the advantages that the linear chain structure of the sodium polyacrylate is guaranteed, various addition components are stably introduced, and the oxidation resistance, heat resistance, flame retardance, strength, antistatic property and creep resistance of the PP fiber are effectively improved.
5. According to the production process of the low-creep and stable-size PC film, the nucleating agent is a beta-nucleating agent, a large number of beta-crystal forms are generated in the material, a large number of extended chain segments formed by connecting continuous molecular chains exist in a porous crystallization area of the beta-crystal forms, clear boundaries do not exist between spherulites, and a large number of silver streaks can be initiated and more energy can be absorbed when the PC film is stretched or impacted by external force. Meanwhile, the mutual interference of stress fields among the silver streaks enables the stress to be dispersed, so that the further development of cracks is prevented, the low-temperature impact performance of the material is improved, the modified ethylene bis fatty acid amide is used as a dispersing agent, a polar group of the dispersing agent and the long chain end of a silane coupling agent generate strong attraction through Van der Waals, the attraction is enough to enable the interface of two phases to disappear, so that one phase is formed, the phase has certain intermiscibility with polypropylene, the effect of a phase intermiscibility agent is achieved, the external force stretching or impact on a beta-crystal form can be increased, the interference of the silver streak stress fields is further promoted, the mechanical performance of the product is improved, and the creep resistance of the product is improved.
6. According to the production process of the PC film with low creep and stable size, the compatilizer is arranged, so that the polyphenyl ether and the PC resin are well compatible in any proportion, the polyethylene and the cycloolefin copolymer are high in compatibility, the high heat resistance of the polyphenyl ether can make up for the defect of insufficient heat resistance of the polyethylene, and the high reactivity of the maleic anhydride can well improve the compatibility of the cycloolefin copolymer and the PC system.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The first embodiment is as follows: a production process of a low-creep and dimensionally stable PC film comprises the following raw materials in parts by weight: 100 parts of PC resin, 50 parts of cycloolefin copolymer, 5 parts of compatilizer, 7 parts of chain extender, 5 parts of toluene, 1 part of nucleating agent, 10 parts of filler, 3 parts of flexibilizer and 3 parts of dispersant.
Further, the main chain of the cycloolefin copolymer is a cycloolefin, and the grafting monomer is one of maleic anhydride, maleic ester monomers, fumaric acid, fumaric ester monomers, acrylic acid, acrylate monomers, methacrylic acid, or methacrylate monomers.
Further, the compatilizer is prepared by mixing maleic anhydride grafted polyphenyl ether and maleic anhydride grafted polyethylene according to a mass ratio of 1: 2.
Further, the cycloolefin copolymer is one or more of ethylene-norbornene copolymer (COC), styrene-norbornene Copolymer (COP), COC derivatives and COP derivatives.
Further, the dispersant is modified ethylene bis fatty acid amide, and the nucleating agent is a beta-nucleating agent.
Further, the filler is a mixture of nano titanium dioxide, nano silicon dioxide and graphite, the mixing ratio of the nano titanium dioxide to the nano silicon dioxide to the graphite is 1.7:2:1,
a low creep, dimensionally stable PC film production process comprising the steps of:
s1, preparing the materials;
s2, adding the PC resin, the toluene and the filler into a stirrer, stirring at the speed of 800r/min, introducing nitrogen to 0.5MPa, heating to 200 ℃ at the speed of 20 ℃/min, and then stirring at constant temperature for 60min to form a mixture A;
s3, adding mixture a into the hopper of an extruder, the temperature of the extruder being 1 stage: 170 ℃ and 2 stages: 180 ℃ and 3 stages: and (3) starting an extruder after the temperature reaches 190 ℃ and reaches the plasticizing temperature, wherein the speed of the extruder is 45RP, and extruding and stretching to obtain a mixture B.
S4, adding the cyclic olefin copolymer, the chain extender and the nucleating agent into a reaction kettle, mixing, and stirring at the rotation speed of 1200r/min for 40min to obtain a mixture C;
s5, adding the mixture C into a double-screw extruder to obtain a mixture D.
S6, placing the mixture D and the mixture B into a UV illumination box for illumination, wherein the illumination time is 15 seconds;
s7, adding the illuminated mixture B, the illuminated mixture D and the rest materials into a double-screw granulator, extruding, granulating and drying to obtain slices;
and S8, melting and extruding the slices, cooling, and performing longitudinal stretching, transverse stretching and sizing after cooling to obtain the PC film with low creep deformation and stable size.
Example two:
a production process of a low-creep and dimensionally stable PC film comprises the following raw materials in parts by weight: 150 parts of PC resin, 60 parts of cycloolefin copolymer, 8 parts of compatilizer, 10 parts of chain extender, 6 parts of toluene, 2 parts of nucleating agent, 20 parts of filler, 4 parts of toughening agent and 4 parts of dispersant.
Further, the main chain of the cycloolefin copolymer is a cycloolefin, and the grafting monomer is one of maleic anhydride, maleic ester monomers, fumaric acid, fumaric ester monomers, acrylic acid, acrylate monomers, methacrylic acid, or methacrylate monomers.
Further, the compatilizer is prepared by mixing maleic anhydride grafted polyphenyl ether and maleic anhydride grafted polyethylene according to a mass ratio of 2: 3, and (3).
Further, the cycloolefin copolymer is one or more of ethylene-norbornene copolymer (COC), styrene-norbornene Copolymer (COP), COC derivatives and COP derivatives.
Further, the dispersing agent is modified ethylene bis fatty acid amide, and the nucleating agent is a beta-nucleating agent.
Further, the filler is a mixture of nano titanium dioxide, nano silicon dioxide and graphite, the mixing ratio of the nano titanium dioxide to the nano silicon dioxide to the graphite is 1.7:2:1,
a low creep, dimensionally stable PC film production process comprising the steps of:
s1, preparing the materials;
s2, adding the PC resin, the toluene and the filler into a stirrer, stirring at the speed of 900r/min, introducing nitrogen to 0.5MPa, heating to 200 ℃ at the speed of 20 ℃/min, and then stirring at constant temperature for 70min to form a mixture A;
s3, adding mixture a into the hopper of an extruder, the temperature of the extruder being 1 stage: 175 ℃, 2 stages: 185 ℃ and 3 stages: and (3) starting an extruder after reaching the plasticizing temperature of 195 ℃, wherein the speed of the extruder is 47RP, and extruding and stretching to obtain a mixture B.
S4, adding the cyclic olefin copolymer, the chain extender and the nucleating agent into a reaction kettle, mixing, and stirring for 50min at the rotating speed of 1200r/min to obtain a mixture C;
s5, adding the mixture C into a double-screw extruder to obtain a mixture D.
S6, placing the mixture D and the mixture B into a UV illumination box for illumination for 18 seconds;
s7, adding the illuminated mixture B, the illuminated mixture D and the rest materials into a double-screw granulator, extruding, granulating and drying to obtain slices;
and S8, melting and extruding the slices, cooling, and performing longitudinal stretching, transverse stretching and sizing after cooling to obtain the PC film with low creep and stable size.
Example three: a production process of a low-creep and dimensionally stable PC film comprises the following raw materials in parts by weight: 200 parts of PC resin, 70 parts of cycloolefin copolymer, 10 parts of compatilizer, 13 parts of chain extender, 7 parts of toluene, 3 parts of nucleating agent, 30 parts of filler, 5 parts of toughening agent and 5 parts of dispersant.
Further, the main chain of the cycloolefin copolymer is a cycloolefin, and the grafting monomer is one of maleic anhydride, maleic ester monomers, fumaric acid, fumaric ester monomers, acrylic acid, acrylate monomers, methacrylic acid, or methacrylate monomers.
Further, the compatilizer is prepared by mixing maleic anhydride grafted polyphenyl ether and maleic anhydride grafted polyethylene according to a mass ratio of 3: 4.
Further, the cycloolefin copolymer is one or more of ethylene-norbornene copolymer (COC), styrene-norbornene Copolymer (COP), COC derivatives and COP derivatives.
Further, the dispersing agent is modified ethylene bis fatty acid amide, and the nucleating agent is a beta-nucleating agent.
Further, the filler is a mixture of nano titanium dioxide, nano silicon dioxide and graphite, the mixing ratio of the nano titanium dioxide to the nano silicon dioxide to the graphite is 1.7:2:1,
a low creep, dimensionally stable PC film production process comprising the steps of:
s1, preparing the materials;
s2, adding the PC resin, the toluene and the filler into a stirrer, stirring at the speed of 1000r/min, introducing nitrogen to 0.5MPa, heating to 200 ℃ at the speed of 20 ℃/min, and then stirring at constant temperature for 80min to form a mixture A;
s3, adding mixture a into the hopper of an extruder, the temperature of the extruder being 1 stage: 180 ℃ and 2 stages: 190 ℃ and 3 stages: and (3) starting an extruder after the temperature reaches 200 ℃ and reaching the plasticizing temperature, wherein the speed of the extruder is 50RP, and extruding and stretching to obtain a mixture B.
S4, adding the cyclic olefin copolymer, the chain extender and the nucleating agent into a reaction kettle, mixing, and stirring for 60min at the rotating speed of 1200r/min to obtain a mixture C;
s5, adding the mixture C into a double-screw extruder to obtain a mixture D.
S6, placing the mixture D and the mixture B into a UV illumination box for illumination for 15-20 seconds;
s7, adding the mixture B, the mixture D and the rest materials after illumination into a double-screw granulator, extruding, granulating and drying to obtain slices;
s8, melting and extruding the slices, cooling, longitudinally stretching, transversely stretching and shaping after cooling to obtain the PC film with low creep and stable size
In summary, the low-creep and dimensionally stable PC film production process 1 provides a graft copolymer composite that can integrate the advantageous properties of a plurality of unit graft copolymers, complement each other, make up for the defect of single performance of the unit graft copolymer, and achieve the effect of one plus one over two.
2. According to the production process of the PC film with low creep and stable size, the compound is prepared by melting and mixing the graft copolymers with various units through a screw melting, mixing and extruding process, so that the advantages and properties of the graft copolymers with various units can be integrated, and the functional complementation among the graft copolymers with various units can be realized. The method has simple process, can solve the problem of single performance of the existing unit graft copolymer, and can also avoid the problems of high control difficulty and high crosslinking risk of the grafting process in the process of multi-graft copolymerization.
3. In the production process of the low-creep and stable-size PC film, the cycloolefin copolymer mainly refers to a copolymer of norbornene and other olefins, a large amount of norbornene chain segments exist on a macromolecular chain, the rotation of the molecular chain is difficult due to the huge steric hindrance effect of the norbornene chain segments, and then higher glass transition temperature and good rigidity are reflected, and meanwhile, the macromolecular chain segments are difficult to move and show lower creep property due to the difficult rotation of the molecular chain segments,
4. according to the production process of the low-creep and stable-size PC film, when the PP resin is produced, a large number of benzene ring structures are crosslinked on a linear chain or a branched chain of polypropylene in the stirring process to form a large number of gap structures, and then the filler is added, so that the gap structures are filled in gaps of the filler, and simultaneously, graphene with electronegativity is adsorbed with the polypropylene, so that the graphene is inserted into the surface of the polypropylene, and the conductivity is generated; the sodium polyacrylate fiber has the advantages that the linear chain structure of the sodium polyacrylate is guaranteed, various addition components are stably introduced, and the oxidation resistance, heat resistance, flame retardance, strength, antistatic property and creep resistance of the PP fiber are effectively improved.
5. According to the production process of the low-creep and stable-size PC film, the nucleating agent is a beta-nucleating agent, a large number of beta-crystal forms are generated in the material, a large number of extended chain segments formed by connecting continuous molecular chains exist in a porous crystallization area of the beta-crystal forms, clear boundaries do not exist between spherulites, and a large number of silver streaks can be initiated and more energy can be absorbed when the PC film is stretched or impacted by external force. Meanwhile, the mutual interference of stress fields among the silver stripes enables the stress to be dispersed, so that the further development of cracks is prevented, the low-temperature impact performance of the material is improved, the modified ethylene bis-fatty acid amide is used as a dispersing agent, a polar group of the dispersing agent and the long chain end of a silane coupling agent generate strong attraction through Van der Waals, the attraction is enough to enable the interface of two phases to disappear, so that one phase is formed, the phase has certain intermiscibility with polypropylene, the function of a phase dissolving agent is realized, the external force stretching or impact on a beta-crystal form can be increased, the interference of the stress fields of the silver stripes is further promoted, the mechanical performance of the product is improved, and the creep resistance of the product is improved.
6. Although the embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and alterations can be made herein without departing from the principles and spirit of the invention, and it is intended that the scope of the present invention be limited by the appended claims and their equivalents.

Claims (7)

1. A production process of a low-creep and dimensionally stable PC film is characterized by comprising the following raw materials in parts by weight: 100-200 parts of PC resin, 50-70 parts of cycloolefin copolymer, 5-10 parts of compatilizer, 7-13 parts of chain extender, 5-7 parts of toluene, 1-3 parts of nucleating agent, 10-30 parts of filler, 3-5 parts of toughening agent and 3-5 parts of dispersant.
2. The process of claim 1, wherein the cyclic olefin copolymer backbone is a cyclic olefin, and the grafting monomer is one of maleic anhydride, maleic ester monomer, fumaric acid, fumaric ester monomer, acrylic acid, acrylic ester monomer, methacrylic acid, or methacrylic ester monomer.
3. The process for producing a low-creep dimensionally stable PC film according to claim 1, wherein the compatibilizer is prepared by mixing maleic anhydride-grafted polyphenylene ether and maleic anhydride-grafted polyethylene in a mass ratio of (1-3): (2-4).
4. The process of claim 1, wherein the cycloolefin copolymer is one or more of ethylene-norbornene copolymer (COC), styrene-norbornene Copolymer (COP), COC derivatives, and COP derivatives.
5. The process of claim 1, wherein the dispersant is a modified ethylene bis fatty acid amide and the nucleating agent is a β -nucleating agent.
6. The process of claim 1, wherein the filler is a mixture of nano titanium dioxide, nano silica and graphite in a ratio of 1.7:2: 1.
7. The process of claim 1, comprising the steps of:
s1, preparing the materials;
s2, adding PC resin, toluene and filler into a stirrer, stirring at the speed of 800-1000r/min, introducing nitrogen to 0.5MPa, heating to 200 ℃ at the speed of 20 ℃/min, and then stirring at constant temperature for 60-80min to form a mixture A;
s3, adding mixture a into the hopper of an extruder, the temperature of the extruder being 1 stage: 170 ℃ and 180 ℃, 2 sections: 180 ℃ and 190 ℃ and 3 sections: 190 ℃ and 200 ℃, starting an extruder after the plasticizing temperature is reached, wherein the speed of the extruder is 45-50RP, and performing extrusion and stretching to obtain a mixture B.
S4, adding the cyclic olefin copolymer, the chain extender and the nucleating agent into a reaction kettle, mixing, and stirring at the rotation speed of 1200r/min for 40-60min to obtain a mixture C;
s5, adding the mixture C into a double-screw extruder to obtain a mixture D.
S6, placing the mixture D and the mixture B into a UV illumination box for illumination for 15-20 seconds;
s7, adding the mixture B, the mixture D and the rest materials after illumination into a double-screw granulator, extruding, granulating and drying to obtain slices;
and S8, melting and extruding the slices, cooling, and performing longitudinal stretching, transverse stretching and sizing after cooling to obtain the PC film with low creep and stable size.
CN202210732870.2A 2022-06-27 2022-06-27 Low-creep and stable-size PC film production process Pending CN115093689A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202210732870.2A CN115093689A (en) 2022-06-27 2022-06-27 Low-creep and stable-size PC film production process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202210732870.2A CN115093689A (en) 2022-06-27 2022-06-27 Low-creep and stable-size PC film production process

Publications (1)

Publication Number Publication Date
CN115093689A true CN115093689A (en) 2022-09-23

Family

ID=83292556

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202210732870.2A Pending CN115093689A (en) 2022-06-27 2022-06-27 Low-creep and stable-size PC film production process

Country Status (1)

Country Link
CN (1) CN115093689A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116082582A (en) * 2022-09-30 2023-05-09 安捷利(番禺)电子实业有限公司 Modified plastic and low-dielectric pure adhesive film prepared from same

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4855357A (en) * 1988-10-12 1989-08-08 General Electric Company Low-temperature impact blends of polycarbonate, graft copolymer and rigid copolymer
CN101353474A (en) * 2008-07-07 2009-01-28 苏州奥美光学材料有限公司 Liquid crystal optical highly transparent polycarbonate film and sheet material, and manufacturing method thereof
CN101367992A (en) * 2008-09-25 2009-02-18 上海交通大学 Method of manufacturing polycarbonate/polyester alloy
CN103483796A (en) * 2013-09-29 2014-01-01 太仓市鸿运包装材料有限公司 Scratching-resistant and flame-retardant PC (polycarbonate) film material and preparation method thereof
CN106147182A (en) * 2015-04-01 2016-11-23 合肥杰事杰新材料股份有限公司 A kind of low water suction fire-retardant scratch resistant polycarbonate composite and preparation method thereof
WO2018107969A1 (en) * 2016-12-15 2018-06-21 金发科技股份有限公司 Pc/abs composition, preparation method therefor and use thereof
CN109880333A (en) * 2017-12-06 2019-06-14 万华化学集团股份有限公司 A kind of polycarbonate compositions and preparation method thereof
CN110240755A (en) * 2019-05-17 2019-09-17 武汉金牛经济发展有限公司 A kind of PPR pipe with low-temperature impact resistance toughness
CN113845684A (en) * 2021-09-15 2021-12-28 安徽坤涂新材料科技有限公司 Production process of wear-resistant PC glass plate
WO2022057206A1 (en) * 2020-09-18 2022-03-24 金发科技股份有限公司 Polycarbonate alloy composition, preparation method therefor and use thereof

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4855357A (en) * 1988-10-12 1989-08-08 General Electric Company Low-temperature impact blends of polycarbonate, graft copolymer and rigid copolymer
CN101353474A (en) * 2008-07-07 2009-01-28 苏州奥美光学材料有限公司 Liquid crystal optical highly transparent polycarbonate film and sheet material, and manufacturing method thereof
CN101367992A (en) * 2008-09-25 2009-02-18 上海交通大学 Method of manufacturing polycarbonate/polyester alloy
CN103483796A (en) * 2013-09-29 2014-01-01 太仓市鸿运包装材料有限公司 Scratching-resistant and flame-retardant PC (polycarbonate) film material and preparation method thereof
CN106147182A (en) * 2015-04-01 2016-11-23 合肥杰事杰新材料股份有限公司 A kind of low water suction fire-retardant scratch resistant polycarbonate composite and preparation method thereof
WO2018107969A1 (en) * 2016-12-15 2018-06-21 金发科技股份有限公司 Pc/abs composition, preparation method therefor and use thereof
CN109880333A (en) * 2017-12-06 2019-06-14 万华化学集团股份有限公司 A kind of polycarbonate compositions and preparation method thereof
CN110240755A (en) * 2019-05-17 2019-09-17 武汉金牛经济发展有限公司 A kind of PPR pipe with low-temperature impact resistance toughness
WO2022057206A1 (en) * 2020-09-18 2022-03-24 金发科技股份有限公司 Polycarbonate alloy composition, preparation method therefor and use thereof
CN113845684A (en) * 2021-09-15 2021-12-28 安徽坤涂新材料科技有限公司 Production process of wear-resistant PC glass plate

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
郭峰;李传峰;汪文睿;杨爱武;: "环烯烃共聚物的应用", 现代塑料加工应用, no. 02, pages 60 - 63 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116082582A (en) * 2022-09-30 2023-05-09 安捷利(番禺)电子实业有限公司 Modified plastic and low-dielectric pure adhesive film prepared from same

Similar Documents

Publication Publication Date Title
TWI705094B (en) Recycle pet foaming material and method for manufacturing the same
CN102040808B (en) Glass fiber enhanced PET/PBT (Polyethylene Terephthalate)/(Polybutylene Terephthalate) alloy with high glossiness and low warping degree and preparation method thereof
CN102070884B (en) Fire resistant glass fiber reinforced polyethylene terephthalate/polybutylece terephthalate alloy and preparation method thereof
CN103589058A (en) Reinforced polypropylene composite material and preparation method thereof
CN102329479A (en) Glass fiber reinforced PBT (Poly Butylenes Terephthalate)/PP (Polypropylene) alloy material and preparation method thereof
CN102702705A (en) Toughened polylactic acid/polyolefin elastomer composite material and preparation method thereof
CN115093689A (en) Low-creep and stable-size PC film production process
CN113462130A (en) Polyester composition with high melt viscosity and preparation method thereof
CN109401045B (en) Special material for high-performance functionalized alloy modified polypropylene corrugated pipe and preparation method thereof
CN112266591A (en) Preparation method of carbon fiber reinforced polylactic acid 3D printing material
CN111154241A (en) Reinforced flame-retardant low-warpage PBT (polybutylene terephthalate) composite material and preparation method thereof
CN110229497B (en) Bio-based polyurethane/polylactic acid alloy film blowing material and preparation method thereof
CN113773580A (en) High-toughness PP composite material and preparation method thereof
CN107383744B (en) Polypropylene modified material for waste household appliances and preparation method thereof
CN115558204B (en) Low-shrinkage high-gloss V0-grade halogen-free flame-retardant polypropylene composite material and preparation method thereof
CN115368496B (en) Phosphonic acid group modified polyvinyl alcohol, preparation method and application thereof
CN110951222A (en) High-impact-resistance regenerated PET material and preparation method thereof
CN113980436B (en) Modified polyester transparent composite material and preparation method thereof
CN115286867A (en) Nano compatibilized polypropylene polystyrene composition and preparation method thereof
CN105017764A (en) Composite material of halogen-free flame-retardant reinforced PA66/recycled PET bottle-grade chips and preparation method thereof
CN113462150A (en) Flame-retardant nylon composite material and preparation method thereof
CN112662147A (en) High-performance ternary compound biodegradable film
CN114836009B (en) Low-temperature heat-shrinkable film and preparation method thereof
CN113136093B (en) Preparation method of reinforced polybutylene terephthalate material
CN103044885A (en) Halogen-free flame-retardant low-temperature resistant polycarbonate and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination