CN107474428A - PVC composite modification materials and preparation method thereof - Google Patents

PVC composite modification materials and preparation method thereof Download PDF

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Publication number
CN107474428A
CN107474428A CN201710695883.6A CN201710695883A CN107474428A CN 107474428 A CN107474428 A CN 107474428A CN 201710695883 A CN201710695883 A CN 201710695883A CN 107474428 A CN107474428 A CN 107474428A
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parts
speed mixer
pvc composite
composite modification
modification materials
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郑云翠
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Wuhu Pilot New Mstar Technology Ltd
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Wuhu Pilot New Mstar Technology Ltd
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    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/04Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
    • C08L27/06Homopolymers or copolymers of vinyl chloride
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/24Crosslinking, e.g. vulcanising, of macromolecules
    • C08J3/246Intercrosslinking of at least two polymers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B3/00Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties
    • H01B3/18Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances
    • H01B3/30Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances plastics; resins; waxes
    • H01B3/44Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances plastics; resins; waxes vinyl resins; acrylic resins
    • H01B3/443Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances plastics; resins; waxes vinyl resins; acrylic resins from vinylhalogenides or other halogenoethylenic compounds
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2327/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
    • C08J2327/02Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
    • C08J2327/04Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
    • C08J2327/06Homopolymers or copolymers of vinyl chloride
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
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    • C08J2433/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
    • C08J2433/04Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters
    • C08J2433/06Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters of esters containing only carbon, hydrogen, and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • C08J2433/10Homopolymers or copolymers of methacrylic acid esters
    • C08J2433/12Homopolymers or copolymers of methyl methacrylate
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2433/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
    • C08J2433/18Homopolymers or copolymers of nitriles
    • C08J2433/20Homopolymers or copolymers of acrylonitrile
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    • C08J2483/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen, or carbon only; Derivatives of such polymers
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    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
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    • C08L2201/00Properties
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    • C08L2312/00Crosslinking

Abstract

PVC composite modification materials and preparation method thereof, it is material modified and preparation method thereof that it is related to a kind of PVC.A certain amount of unsaturated double-bond also be present on the strand material modified the invention aims to solve existing PVC, can form activated centre will cause poor ductility, easily cause melt to crush, and cause product surface coarse and lacklustre problem.PVC composite modification materials are prepared by polyvinyl chloride resin, low temperature toughener, impact modifier, processing aid, surfactant, compound stabilizer, covering agent, initiator and crosslinking agent in parts by weight.Preparation method:First, weigh;2nd, premix, obtain pre-composition;3rd, substep is mixed, obtains substep mixture;4th, it is mixed eventually, obtain mixed thing eventually;5th, extruding pelletization, PVC composite modification materials are obtained.Present invention is mainly used for prepare PVC composite modification materials.

Description

PVC composite modification materials and preparation method thereof
Technical field
It is material modified and preparation method thereof the present invention relates to a kind of PVC.
Background technology
It is known that the unmanageable characteristic of polyvinyl chloride resin shows that it is in thermal sensitivity, its processing temperature and decomposition temperature ratio It is closer to, low poor heat resistance, ageing resistance, melt calorific intensity, poor fluidity is present, easily produces thermal deformation, glass transition temperature Low and cryogenic property and impact strength is poor, interlaminar resin bonding force is not high, it is broken easily to occur melting, and processing characteristics is bad, So residence time of the resin in process equipment is longer than general resin, easily decomposed in the dead angle coking of equipment, cause to add The shortcomings of work difficult forming.Therefore in order to solve above-mentioned drawback, people employ copolymerized grafting, blending, enhancing, crosslinking etc. Physics and chemical method, are modified to it, prepare the PVC material of many excellent performances, make the field that it is applied to depth Development.
Polyvinyl chloride (PVC) is to polymerize obtained polymer by monomer of vinyl chloride, belongs to thermoplastic, has chemistry Stability is good, and high mechanical properties, electrical apparatus insulation be excellent, fire retardant self-extinguishment, lower-price characteristic.But due in strand Syndiotactic containing short distance, belong to amorphous polymer, in the course of the polymerization process due to chain transfer reaction and disproportionated reaction occurs A number of unsaturated end group and side chain can be produced, a small amount of end group is the residue of initiator, and the presence of these miscellaneous structures makes PVC Heat endurance decline, temperature in use is not high, fragility is big, can not resist cold, low temperature impact strength is low, in the presence of heat, oxygen and light Easy to aging, the shortcomings of degrading, using modified mode, it is also easy to make that product surface is rough, dimensional stability is bad, shadow The processing characteristics of product is rung, the prior cost that improves adds expense.In order to solve the above problems, being badly in need of one kind can solve The certainly appearance of the new PVC modified products of drawbacks described above.Therefore by the modification to PVC composites, materials for construction is produced Product forms, apply and produce plastic material product by checking, this kind of material in plastic door-window industry, further increase PVC Tensile strength, dimensional stability, low-temperature impact toughness and the electrical property of material product, reduce thermal deformation and high-temerature creep, resistance to The performances such as degraded, the shortcomings of improving the stress concentration of product, be cracked, avoid what plastic material used in low-temperature cold area Defect, reduce molecular particle size diameter and control one setting state, improve tensile yield strength and low temperature impact strength, improve it The transparency and glossiness, processing temperature during shaping is reduced, so as to extend the service life of product, this materials application is in agriculture In industry, building, chemical industry, electric, machinery and daily life, purposes is extremely wide, especially with the plastics of this kind of material production Section bar is successfully applied to be used under the larger environment of the temperature difference, achieves good effect.But point material modified existing PVC A certain amount of unsaturated double-bond in subchain also be present, can form activated centre will cause poor ductility, easily cause melt to crush, Cause product surface coarse and lacklustre problem.
The content of the invention
Also exist on the strand material modified the invention aims to solve existing PVC a certain amount of unsaturated double Key, can form activated centre will cause poor ductility, easily cause melt to crush, and cause product surface coarse and lacklustre ask Topic, and PVC composite modification materials and preparation method thereof are provided.
PVC composite modification materials are in parts by weight by 60~85 parts of polyvinyl chloride resin, 3.5~10 parts of low temperature toughener, 4 ~9 parts of impact modifier, 2~5 parts of processing aid, 0.5~1 part of surfactant, 2~5 parts of compound stabilizer, 2 ~5 parts of covering agent, 0.1~0.5 part of initiator and 0.5~4.5 part of crosslinking agent are prepared.
The preparation method of PVC composite modification materials, is specifically realized by the following steps:
First, weigh:Weigh in parts by weight 60~85 parts polyvinyl chloride resin, 3.5~10 parts of low temperature toughener, 4~9 parts Impact modifier, 2~5 parts of processing aid, 0.5~1 part of surfactant, 2~5 parts of compound stabilizer, 2~5 parts Covering agent, 0.1~0.5 part of initiator and 0.5~4.5 part of crosslinking agent;
2nd, premix:By weighed in step 1 60~85 parts of polyvinyl chloride resin, 2~5 parts of compound stabilizer and 2~5 parts Covering agent be sequentially placed into high-speed mixer, mixed in the case where temperature is 70 DEG C~80 DEG C and rotating speed is 10r/min~15r/min 5min~15min, obtain pre-composition;
3rd, substep is mixed:By weighed in step 1 3.5~10 parts of low temperature toughener, 2~5 parts of processing aid and 4~ 9 parts of impact modifier is sequentially placed into high-speed mixer, and high-speed mixer design temperature is 110 DEG C, starts high-speed mixer Mixed in the case where rotating speed is 10r/min~15r/min, when the mixing temperature of high-speed mixer reaches 70~80 DEG C, addition 0.5~ 1 part of surfactant, continue to mix, blowing when reaching 110 DEG C to the mixing temperature of high-speed mixer, obtain substep and mix Thing;
4th, it is mixed eventually:The substep mixture that the pre-composition and step 3 that step 2 obtains obtain is sequentially placed into high-speed mixer In, sequentially add 0.5~4.5 part of the crosslinking agent and 0.1~0.5 part of initiator weighed in step 1, high-speed mixer Design temperature is 70~80 DEG C, starts high-speed mixer and is mixed in the case where rotating speed is 10r/min~15r/min, works as high-speed mixer Mixing temperature stop mixing when reaching 70~80 DEG C, obtain mixed thing eventually;
5th, extruding pelletization:End that step 4 is obtained mixes thing and is transferred in extruder, pass sequentially through extruder shearing, Mixing, kneading and cooling pelletization, obtain PVC composite modification materials;Technological temperature difference of the extrusion from material mouth at mouth mold For:1st area:160~165 DEG C, 2nd area:165~170 DEG C, 3rd area:175~180 DEG C, 4th area:180~185 DEG C, 5th area:185~190 DEG C, 6th area:195~205 DEG C, melt pressure is no more than 10MPa.
Advantages of the present invention:
First, it is using polyvinyl chloride resin as carrier according to PVC plastic when processing PVC material the characteristics of the technology of the present invention The characteristics of, multi-component plastics are prepared into using various plastic additives are added, changes formula and uses exclusive fiber distributed architecture, carry The creep-resistant property of high material, low temperature impact properties are improved, the plastic material and product of degree difference and multiple functions is made, carries The applicability of high product.
2nd, in enhancing composite modification material of the invention, mutually tied with polymeric material by intermolecular or chemical bond force Close, the basic performance of the property of its own and polymeric material is combined together, mutually twined with polymer in reinforcing material In the active force of knot, both are made to have sufficient affinity to reach the purpose of enhancing with it.Therefore modified PVC composites, tool There is the features such as density is low, intensity is high, processing is fast, recyclable, belong to high-performance, low cost, green advanced composite material (ACM), And part instead of expensive engineering plastics.
3rd, the PVC composite modification materials that prepare of the present invention, overcome PVC to it is thermo-responsive, heat endurance is poor, resistance to ag(e)ing And deformation resistance difference shortcoming, product tensile strength is improved, dimensional stability, impact flexibility, heat endurance and electrical property, is reduced The performance such as thermal deformation and high-temerature creep, improves product stress concentration, the shortcomings of cracking, so as to extending product using life etc. Prepare the product material of excellent performance.With contrasting afterwards before modified, ageing properties are improved by tensile strength 4.5MPa before modified To 7.6MPa, impact brittle temperature has original -20 DEG C to bring up to -40 DEG C.
4th, compared with existing PVC material, PVC is crosslinked the tensile strength for being favorably improved material.
5th, compared with existing PVC material, PVC is crosslinked the heat endurance for being favorably improved material.
6th, compared with existing PVC material, PVC composite modification materials prepared by the present invention improve the electrical insulating property of material.
Embodiment
Embodiment one:Present embodiment is PVC composite modification materials, in parts by weight by 60~85 parts of PVC Resin, 3.5~10 parts of low temperature toughener, 4~9 parts of impact modifier, 2~5 parts of processing aid, 0.5~1 part of surface Activating agent, 2~5 parts of compound stabilizer, 2~5 parts of covering agent, 0.1~0.5 part of initiator and 0.5~4.5 part of crosslinking Agent is prepared.
The heat endurance of polyvinyl chloride resin, an important factor for determining its quality, processing characteristics can be directly affected and using the longevity Life, research PVC is exactly to consider the molecular structure of polyvinyl chloride resin inherently, and this structure result in possessing have it is unstable because Element, therefore the present invention increases the viscoplasticity of PVC melts on the basis of original modification, so as to improve die swelling and improve molten Body intensity, improve the molecular structure of polymer, crystallinity, the direction of micro-crystallization, crosslinking degree etc., so as to by linear branched structure Become tridimensional network, make polymer more preferable to obdurability, impact, it is stronger to raising PVC performance, meet one Needs under a little specific conditions, extend PVC application scenario.
Embodiment two:The difference of present embodiment and embodiment one is:Described polyvinyl chloride resin is hard Polyvinyl chloride resin of the angle value 70.Other are identical with embodiment one.
Embodiment three:Present embodiment is with one of embodiment one or two difference:Described covering Agent is rutile titanium dioxide.Other are identical with embodiment one or two.
Embodiment four:Present embodiment is with one of embodiment one to three difference:Described low temperature Toughener is PNBR.Other are identical with embodiment one to three.
Embodiment five:Present embodiment is with one of embodiment one to four difference:Described anti-impact Modifying agent is MBS.Other are identical with embodiment one to four.
Embodiment six:Present embodiment is with one of embodiment one to five difference:Described processing Auxiliary agent is acrylonitritrile-styrene resin.Other are identical with embodiment one to five.
Embodiment seven:Present embodiment is with one of embodiment one to six difference:Described surface Activating agent is polyoxy base silane.Other are identical with embodiment one to six.
Embodiment eight:Present embodiment is with one of embodiment one to seven difference:Described initiation Agent is cumyl peroxide.Other are identical with embodiment one to seven.
Embodiment nine:Present embodiment is with one of embodiment one to eight difference:Described crosslinking Agent is double maleamic acids.Other are identical with embodiment one to eight.
Embodiment ten:Present embodiment is the preparation method of PVC composite modification materials, specifically according to the following steps Complete:
First, weigh:Weigh in parts by weight 60~85 parts polyvinyl chloride resin, 3.5~10 parts of low temperature toughener, 4~9 parts Impact modifier, 2~5 parts of processing aid, 0.5~1 part of surfactant, 2~5 parts of compound stabilizer, 2~5 parts Covering agent, 0.1~0.5 part of initiator and 0.5~4.5 part of crosslinking agent;
2nd, premix:By weighed in step 1 60~85 parts of polyvinyl chloride resin, 2~5 parts of compound stabilizer and 2~5 parts Covering agent be sequentially placed into high-speed mixer, mixed in the case where temperature is 70 DEG C~80 DEG C and rotating speed is 10r/min~15r/min 5min~15min, obtain pre-composition;
3rd, substep is mixed:By weighed in step 1 3.5~10 parts of low temperature toughener, 2~5 parts of processing aid and 4~ 9 parts of impact modifier is sequentially placed into high-speed mixer, and high-speed mixer design temperature is 110 DEG C, starts high-speed mixer Mixed in the case where rotating speed is 10r/min~15r/min, when the mixing temperature of high-speed mixer reaches 70~80 DEG C, addition 0.5~ 1 part of surfactant, continue to mix, blowing when reaching 110 DEG C to the mixing temperature of high-speed mixer, obtain substep and mix Thing;
4th, it is mixed eventually:The substep mixture that the pre-composition and step 3 that step 2 obtains obtain is sequentially placed into high-speed mixer In, sequentially add 0.5~4.5 part of the crosslinking agent and 0.1~0.5 part of initiator weighed in step 1, high-speed mixer Design temperature is 70~80 DEG C, starts high-speed mixer and is mixed in the case where rotating speed is 10r/min~15r/min, works as high-speed mixer Mixing temperature stop mixing when reaching 70~80 DEG C, obtain mixed thing eventually;
5th, extruding pelletization:End that step 4 is obtained mixes thing and is transferred in extruder, pass sequentially through extruder shearing, Mixing, kneading and cooling pelletization, obtain PVC composite modification materials;Technological temperature difference of the extrusion from material mouth at mouth mold For:1st area:160~165 DEG C, 2nd area:165~170 DEG C, 3rd area:175~180 DEG C, 4th area:180~185 DEG C, 5th area:185~190 DEG C, 6th area:195~205 DEG C, melt pressure is no more than 10MPa.
Plastics are raw materials based on synthetic resin (high-molecular compound or polymer), and polymer determines the basic of plastics Performance, and the performance of plastics is not only decided by the molecular structure of polymer, and the direction of crystallinity, micro-crystallization, intermolecular hydrogen bonding, Crosslinking degree etc. significantly affects, and PVC plastic is a kind of uneven anisotropic material, therefore modified emphasis is to carry The interface adhesion of high PVC and each component, make that there is good compatibility between polar molecule surface and some auxiliary agent interfaces, So that reaching intermolecular between surface between the surface of material and each auxiliary agent of plastics merges or produces chemical crosslinking, will The material of different component is appropriate to be combined together, and is produced the new material more excellent than homogenous material performance, is made the firm of material Property is perfectly combined with toughness, ensure that the stability and practicality of product.
PVC composite modification materials described in present embodiment use special chemical polymerization techniques and exclusive production work Skill, the technique manufacturing method that product crosslinking, compatible and processing, scattered multiple functions are integrated solve that PVC is many to be lacked Fall into, it is dispersed in polyvinyl chloride resin by adding a certain amount of various auxiliary agents, give full play to the toughness reinforcing with core-shell structure, increase It is potent to answer, make PVC particles by modified to have excellent shock resistance and comprehensive mechanical property, solve traditional toughness reinforcing While technology later stage co-blending elastic body is to material toughness reinforcing, performance loss and lubricating system precipitation of rigidity aspect etc. is also brought to ask Topic, improves its heat endurance, degradation resistance, low-temperature impact resistance.The key issue of present embodiment is to improve its PVC gel Content, only abundant gel, can just obtain excellent products appearance and and mechanical property, with its reach PVC material heat resistance with Degradation resistance and cold temperature impact.
PVC in process, the chemical reaction most importantly between macromolecule, be active group on strand collision What probability determined, collision probability is higher, and intermolecular reaction is easier, and reaction rate is also bigger, if the concentration of crosslinking is too It is low, reaction effective collision probability that can be cumbersome can be made just to reduce, reaction is difficult.Therefore macromolecule often draws in high-temperature heating The main chain risen disconnects, and makes reaction mechanism more complicated, and shearing force can cause chain to break and generate free radical, therefore in present embodiment The middle chemical method using modification by copolymerization, low temperature toughener is added in polyvinyl chloride resin, be adhered to by longer strand On polyvinyl chloride resin particle, by the heat of outside and shear transfer to resin, promote resin melting to make its plasticizing, reach the mesh of plasticizing , eliminate traditional polyvinyl chloride resin at low temperature product embrittlement, to it is thermo-responsive, heat endurance is poor, resistance to ag(e)ing, deformation resistance On the basis of the performances such as difference, by the way that to the composite modified of PVC material, mechanical property, the stretching for further increasing PVC material are strong Degree, dimensional stability, impact flexibility, the performance such as thermal deformation and high-temerature creep, degradation resistant is reduced, improve the stress collection of product In, cracking the shortcomings of, the PVC creep-resistant properties after crosslinking are good, product is reduced change during long-term use Shape, heat distortion temperature raising, good weatherability, the decomposition and chain rupture for not easily causing polymer, improve PVC high temperature tensile strengths, soft Change temperature and viscoplasticity, with the development of triazines cross-linking technology, the palliating degradation degree in PVC cross-linking processes reduces, to improving PVC Performance it is stronger, meet the needs under some specific conditions, extend PVC application scenario, so as to extend product Service life, its application field is developed to depth direction, be particularly suitable for using under the obvious environment that colds and heat succeed each other.Using Modified PVC composite of the present invention is compared with the material that traditional polyvinyl chloride resin produces, and low temperature impact strength improves 60%, glass Glass temperature improves 37 DEG C so that product does not ftracture at low temperature, has reached the characteristic used under suitable low temperature.
Embodiment 11:The difference of present embodiment and embodiment ten is:Described in step 1 Polyvinyl chloride resin is polyvinyl chloride resin of the hardness number 70.Other are identical with embodiment ten.
Embodiment 12:The difference of present embodiment and one of embodiment ten or 11 is:Step Covering agent described in one is rutile titanium dioxide.Other are identical with embodiment ten or 11.
Embodiment 13:Present embodiment is with the difference of embodiment ten to one of 12:Step 1 Described in low temperature toughener be PNBR.Other are identical with embodiment ten to 12.
Embodiment 14:Present embodiment is with the difference of embodiment one to one of 13:Step 1 Described in impact modifier be MBS.Other with embodiment ten to 13 is identical.
Embodiment 15:Present embodiment is with the difference of embodiment one to one of 14:Step 1 Described in processing aid be acrylonitritrile-styrene resin.Other are identical with embodiment ten to 14.
Embodiment 16:Present embodiment is with the difference of embodiment one to one of 15:Step 1 Described in surfactant be polyoxy base silane.Other are identical with embodiment ten to 15.
Embodiment 17:Present embodiment is with the difference of embodiment one to one of 16:Step 1 Described in initiator be cumyl peroxide.Other are identical with embodiment ten to 16.
Embodiment 18:Present embodiment is with the difference of embodiment one to one of 17:Step 1 Described in crosslinking agent be double maleamic acids.Other are identical with embodiment ten to 17.
Using following verification experimental verifications effect of the present invention
Embodiment 1:The preparation method of PVC composite modification materials, is specifically realized by the following steps:
First, weigh:85 parts of polyvinyl chloride resin, 3.5 parts of low temperature toughener, 4 parts impact-resistant modified is weighed in parts by weight Agent, 2 parts of processing aid, 0.5 part of surfactant, 2 parts of compound stabilizer, 2 parts of covering agent, 0.5 part of initiator With 0.5 part of crosslinking agent;
2nd, premix:By weighed in step 1 85 parts of polyvinyl chloride resin, 2 parts of compound stabilizer and 2 parts of covering agent according to It is secondary to be put into high-speed mixer, 10min is mixed in the case where temperature is 80 DEG C and rotating speed is 10r/min, obtains pre-composition;
3rd, substep is mixed:By weighed in step 1 3.5 parts of low temperature toughener, 2 parts of processing aid and 4 parts of anti-impact Modifying agent is sequentially placed into high-speed mixer, and high-speed mixer design temperature is 110 DEG C, is started high-speed mixer and is in rotating speed Mixed under 10r/min, when the mixing temperature of high-speed mixer reaches 80 DEG C, add 0.5 part of surfactant, continue to mix Close, blowing when reaching 110 DEG C to the mixing temperature of high-speed mixer, obtain substep mixture;
4th, it is mixed eventually:The substep mixture that the pre-composition and step 3 that step 2 obtains obtain is sequentially placed into high-speed mixer In, sequentially add 0.5 part of the crosslinking agent weighed in step 1 and 0.5 part of initiator, high-speed mixer design temperature are 80 DEG C, start high-speed mixer and mixed in the case where rotating speed is 10r/min, stopped when the mixing temperature of high-speed mixer reaches 80 DEG C Mixing, obtain mixed thing eventually;
5th, extruding pelletization:End that step 4 is obtained mixes thing and is transferred in extruder, pass sequentially through extruder shearing, Mixing, kneading and cooling pelletization, obtain PVC composite modification materials;Technological temperature difference of the extrusion from material mouth at mouth mold For:1st area:160~165 DEG C, 2nd area:165~170 DEG C, 3rd area:175~180 DEG C, 4th area:180~185 DEG C, 5th area:185~190 DEG C, 6th area:195~205 DEG C, melt pressure is no more than 10MPa.
Polyvinyl chloride resin described in the present embodiment step 1 is polyvinyl chloride resin of the hardness number 70.
Low temperature toughener described in the present embodiment step 1 is the europeanized powder for learning 's production of Yi Li Nitrile rubber.
Impact modifier described in the present embodiment step 1 is the methyl-prop of the auspicious specialization work Materials Co., Ltd production in Qingdao sea E pioic acid methyl ester-BS.
Processing aid described in the present embodiment step 1 be Zhenjiang Qi Mei industry Chemical Co., Ltd. production acrylonitrile- Styrol copolymer.
Surface compatilizer described in the present embodiment step 1 is the polyoxy base silane of Zhong Jie chemical companies of Changshu City production.
Compound stabilizer described in the present embodiment step 1 is the stable composition of Zhejiang Province Chuanhua Co., Ltd's production Agent.
Covering agent described in the present embodiment step 1 is the rutile of Henan Baililian Chemical Co., Ltd.'s production Type titanium dioxide.
Initiator described in the present embodiment step 1 is the cumyl peroxide of Shanghai Hao Hua Chemical Co., Ltd.s.
Crosslinking agent described in the present embodiment step 1 comes for the span of Beijing Yi Taiwei plastic materials Co., Ltd production Amic acid.
Embodiment 2:The preparation method of PVC composite modification materials, is specifically realized by the following steps:
First, weigh:Weigh in parts by weight 80 parts polyvinyl chloride resin, 5 parts of low temperature toughener, 5 parts of impact modifier, 3 parts of processing aid, 0.5 part of surfactant, 3 parts of compound stabilizer, 2 parts of covering agent, 0.5 part of initiator and 1 The crosslinking agent of part;
2nd, premix:By weighed in step 1 80 parts of polyvinyl chloride resin, 3 parts of compound stabilizer and 2 parts of covering agent according to It is secondary to be put into high-speed mixer, 10min is mixed in the case where temperature is 80 DEG C and rotating speed is 10r/min, obtains pre-composition;
3rd, substep is mixed:Weighed in step 15 parts of low temperature toughener, 3 parts of processing aid and 5 parts of anti-impact are changed Property agent be sequentially placed into high-speed mixer, high-speed mixer design temperature is 110 DEG C, and it in rotating speed is 10r/ to start high-speed mixer Mixed under min, when the mixing temperature of high-speed mixer reaches 80 DEG C, add 0.5 part of surfactant, continue to mix, extremely The blowing when mixing temperature of high-speed mixer reaches 110 DEG C, obtain substep mixture;
4th, it is mixed eventually:The substep mixture that the pre-composition and step 3 that step 2 obtains obtain is sequentially placed into high-speed mixer In, 1 part of the crosslinking agent and 0.5 part of initiator weighed in step 1 is sequentially added, high-speed mixer design temperature is 80 DEG C, start high-speed mixer and mixed in the case where rotating speed is 10r/min, stopped when the mixing temperature of high-speed mixer reaches 80 DEG C mixed Close, obtain mixed thing eventually;
5th, extruding pelletization:End that step 4 is obtained mixes thing and is transferred in extruder, pass sequentially through extruder shearing, Mixing, kneading and cooling pelletization, obtain PVC composite modification materials;Technological temperature difference of the extrusion from material mouth at mouth mold For:1st area:160~165 DEG C, 2nd area:165~170 DEG C, 3rd area:175~180 DEG C, 4th area:180~185 DEG C, 5th area:185~190 DEG C, 6th area:195~205 DEG C, melt pressure is no more than 10MPa.
Polyvinyl chloride resin described in the present embodiment step 1 is polyvinyl chloride resin of the hardness number 70.
Low temperature toughener described in the present embodiment step 1 is the europeanized powder for learning 's production of Yi Li Nitrile rubber.
Impact modifier described in the present embodiment step 1 is the methyl-prop of the auspicious specialization work Materials Co., Ltd production in Qingdao sea E pioic acid methyl ester-BS.
Processing aid described in the present embodiment step 1 be Zhenjiang Qi Mei industry Chemical Co., Ltd. production acrylonitrile- Styrol copolymer.
Surface compatilizer described in the present embodiment step 1 is the polyoxy base silane of Zhong Jie chemical companies of Changshu City production.
Compound stabilizer described in the present embodiment step 1 is the stable composition of Zhejiang Province Chuanhua Co., Ltd's production Agent.
Covering agent described in the present embodiment step 1 is the rutile of Henan Baililian Chemical Co., Ltd.'s production Type titanium dioxide.
Initiator described in the present embodiment step 1 is the cumyl peroxide of Shanghai Hao Hua Chemical Co., Ltd.s.
Crosslinking agent described in the present embodiment step 1 comes for the span of Beijing Yi Taiwei plastic materials Co., Ltd production Amic acid.
Embodiment 3:The preparation method of PVC composite modification materials, is specifically realized by the following steps:
First, weigh:70 parts of polyvinyl chloride resin, 8 parts of low temperature toughener, 7.4 parts impact-resistant modified is weighed in parts by weight Agent, 4 parts of processing aid, 1 part of surfactant, 4 parts of compound stabilizer, 3 parts of covering agent, 0.1 part of initiator and 2.5 parts of crosslinking agent;
2nd, premix:By weighed in step 1 70 parts of polyvinyl chloride resin, 4 parts of compound stabilizer and 2 parts of covering agent according to It is secondary to be put into high-speed mixer, 10min is mixed in the case where temperature is 80 DEG C and rotating speed is 10r/min, obtains pre-composition;
3rd, substep is mixed:By weighed in step 18 parts of low temperature toughener, 4 parts of processing aid and 7.4 parts of anti-impact Modifying agent is sequentially placed into high-speed mixer, and high-speed mixer design temperature is 110 DEG C, is started high-speed mixer and is in rotating speed Mixed under 10r/min, when the mixing temperature of high-speed mixer reaches 80 DEG C, add 1 part of surfactant, continue to mix, Blowing when reaching 110 DEG C to the mixing temperature of high-speed mixer, obtains substep mixture;
4th, it is mixed eventually:The substep mixture that the pre-composition and step 3 that step 2 obtains obtain is sequentially placed into high-speed mixer In, sequentially add 2.5 parts of the crosslinking agent weighed in step 1 and 0.1 part of initiator, high-speed mixer design temperature are 80 DEG C, start high-speed mixer and mixed in the case where rotating speed is 10r/min, stopped when the mixing temperature of high-speed mixer reaches 80 DEG C Mixing, obtain mixed thing eventually;
5th, extruding pelletization:End that step 4 is obtained mixes thing and is transferred in extruder, pass sequentially through extruder shearing, Mixing, kneading and cooling pelletization, obtain PVC composite modification materials;Technological temperature difference of the extrusion from material mouth at mouth mold For:1st area:160~165 DEG C, 2nd area:165~170 DEG C, 3rd area:175~180 DEG C, 4th area:180~185 DEG C, 5th area:185~190 DEG C, 6th area:195~205 DEG C, melt pressure is no more than 10MPa.
Polyvinyl chloride resin described in the present embodiment step 1 is polyvinyl chloride resin of the hardness number 70.
Low temperature toughener described in the present embodiment step 1 is the europeanized powder for learning 's production of Yi Li Nitrile rubber.
Impact modifier described in the present embodiment step 1 is the methyl-prop of the auspicious specialization work Materials Co., Ltd production in Qingdao sea E pioic acid methyl ester-BS.
Processing aid described in the present embodiment step 1 be Zhenjiang Qi Mei industry Chemical Co., Ltd. production acrylonitrile- Styrol copolymer.
Surface compatilizer described in the present embodiment step 1 is the polyoxy base silane of Zhong Jie chemical companies of Changshu City production.
Compound stabilizer described in the present embodiment step 1 is the stable composition of Zhejiang Province Chuanhua Co., Ltd's production Agent.
Covering agent described in the present embodiment step 1 is the rutile of Henan Baililian Chemical Co., Ltd.'s production Type titanium dioxide.
Initiator described in the present embodiment step 1 is the cumyl peroxide of Shanghai Hao Hua Chemical Co., Ltd.s.
Crosslinking agent described in the present embodiment step 1 comes for the span of Beijing Yi Taiwei plastic materials Co., Ltd production Amic acid.
Embodiment 4:The preparation method of PVC composite modification materials, is specifically realized by the following steps:
First, weigh:Weigh in parts by weight 60 parts polyvinyl chloride resin, 10 parts of low temperature toughener, 9 parts of impact modifier, 5 parts of processing aid, 1 part of surfactant, 5 parts of compound stabilizer, 5 parts of covering agent, 0.5 part of initiator and 4.5 The crosslinking agent of part;
2nd, premix:By weighed in step 1 60 parts of polyvinyl chloride resin, 5 parts of compound stabilizer and 5 parts of covering agent according to It is secondary to be put into high-speed mixer, 10min is mixed in the case where temperature is 80 DEG C and rotating speed is 10r/min, obtains pre-composition;
3rd, substep is mixed:Weighed in step 1 10 parts of low temperature toughener, 5 parts of processing aid and 9 parts of anti-impact are changed Property agent be sequentially placed into high-speed mixer, high-speed mixer design temperature be 110 DEG C, start high-speed mixer be in rotating speed Mixed under 10r/min, when the mixing temperature of high-speed mixer reaches 80 DEG C, add 1 part of surfactant, continue to mix, Blowing when reaching 110 DEG C to the mixing temperature of high-speed mixer, obtains substep mixture;
4th, it is mixed eventually:The substep mixture that the pre-composition and step 3 that step 2 obtains obtain is sequentially placed into high-speed mixer In, sequentially add 4.5 parts of the crosslinking agent weighed in step 1 and 0.5 part of initiator, high-speed mixer design temperature are 80 DEG C, start high-speed mixer and mixed in the case where rotating speed is 10r/min, stopped when the mixing temperature of high-speed mixer reaches 80 DEG C Mixing, obtain mixed thing eventually;
5th, extruding pelletization:End that step 4 is obtained mixes thing and is transferred in extruder, pass sequentially through extruder shearing, Mixing, kneading and cooling pelletization, obtain PVC composite modification materials;Technological temperature difference of the extrusion from material mouth at mouth mold For:1st area:160~165 DEG C, 2nd area:165~170 DEG C, 3rd area:175~180 DEG C, 4th area:180~185 DEG C, 5th area:185~190 DEG C, 6th area:195~205 DEG C, melt pressure is no more than 10MPa.
Polyvinyl chloride resin described in the present embodiment step 1 is polyvinyl chloride resin of the hardness number 70.
Low temperature toughener described in the present embodiment step 1 is the europeanized powder for learning 's production of Yi Li Nitrile rubber.
Impact modifier described in the present embodiment step 1 is the methyl-prop of the auspicious specialization work Materials Co., Ltd production in Qingdao sea E pioic acid methyl ester-BS.
Processing aid described in the present embodiment step 1 be Zhenjiang Qi Mei industry Chemical Co., Ltd. production acrylonitrile- Styrol copolymer.
Surface compatilizer described in the present embodiment step 1 is the polyoxy base silane of Zhong Jie chemical companies of Changshu City production.
Compound stabilizer described in the present embodiment step 1 is the stable composition of Zhejiang Province Chuanhua Co., Ltd's production Agent.
Covering agent described in the present embodiment step 1 is the rutile of Henan Baililian Chemical Co., Ltd.'s production Type titanium dioxide.
Initiator described in the present embodiment step 1 is the cumyl peroxide of Shanghai Hao Hua Chemical Co., Ltd.s.
Crosslinking agent described in the present embodiment step 1 comes for the span of Beijing Yi Taiwei plastic materials Co., Ltd production Amic acid.
The PVC composite modification materials prepared to existing PVC material and embodiment 1 to 4 detect, the institute of performance indications table 1 Show, by table 1, compared with existing PVC material, the tensile strength of PVC composite modification materials prepared by the present invention, impact are strong Degree, heat distortion temperature and modulus of elasticity all increase significantly.
Table 1
Because polyvinyl chloride resin is because of poor heat resistance, the shortcomings of mechanical strength is not high, his effective way industrially is limited. Therefore the cross-linking modified chemical crosslinking for improving PVC is to improve PVC high temperature tensile strengths, softening temperature and viscoplasticity, dimensionally stable Property, impact flexibility, heat endurance and electrical property reduce thermal deformation, improves product stress concentration, the shortcomings of cracking, improves Rigidity, intensity and ageing-resistant performance, it is stronger to raising PVC performance so as to extend the important method that product uses life, The needs under some specific conditions are met, extend PVC application scenario.

Claims (10)

1.PVC composite modification materials, it is characterised in that PVC composite modification materials in parts by weight by 60~85 parts of polyvinyl chloride resin, 3.5~10 parts of low temperature toughener, 4~9 parts of impact modifier, 2~5 parts of processing aid, 0.5~1 part of surface-active Agent, 2~5 parts of compound stabilizer, 2~5 parts of covering agent, 0.1~0.5 part of initiator and 0.5~4.5 part of crosslinking agent system It is standby to form.
2. PVC composite modification materials according to claim 1, it is characterised in that described polyvinyl chloride resin is hardness number 70 Polyvinyl chloride resin.
3. PVC composite modification materials according to claim 1, it is characterised in that described covering agent is rutile-type dioxy Change titanium.
4. PVC composite modification materials according to claim 1, it is characterised in that described low temperature toughener is powdered nitrile rubber Rubber;Described impact modifier is MBS;Described processing aid is third Alkene nitrile-styrol copolymer;Described surfactant is polyoxy base silane.
5. PVC composite modification materials according to claim 1, it is characterised in that described initiator is peroxidating diisopropyl Benzene;Described crosslinking agent is double maleamic acids.
6. the preparation method of PVC composite modification materials as claimed in claim 1, it is characterised in that it is to complete according to the following steps 's:
First, weigh:60~85 parts of polyvinyl chloride resin, 3.5~10 parts of low temperature toughener, 4~9 parts anti-is weighed in parts by weight Impact modifier, 2~5 parts of processing aid, 0.5~1 part of surfactant, 2~5 parts of compound stabilizer, 2~5 parts of screening Lid agent, 0.1~0.5 part of initiator and 0.5~4.5 part of crosslinking agent;
2nd, premix:By weighed in step 1 60~85 parts of polyvinyl chloride resin, 2~5 parts of compound stabilizer and 2~5 parts of screening Lid agent is sequentially placed into high-speed mixer, and 5min is mixed in the case where temperature is 70 DEG C~80 DEG C and rotating speed is 10r/min~15r/min ~15min, obtains pre-composition;
3rd, substep is mixed:By weighed in step 1 3.5~10 parts of low temperature toughener, 2~5 parts of processing aid and 4~9 parts Impact modifier be sequentially placed into high-speed mixer, high-speed mixer design temperature be 110 DEG C, start high-speed mixer turn Speed is to be mixed under 10r/min~15r/min, when the mixing temperature of high-speed mixer reaches 70~80 DEG C, adds 0.5~1 part Surfactant, continue to mix, blowing when reaching 110 DEG C to the mixing temperature of high-speed mixer, obtain substep mixture;
4th, it is mixed eventually:The substep mixture that the pre-composition and step 3 that step 2 obtains obtain is sequentially placed into high-speed mixer, then Sequentially add 0.5~4.5 part of the crosslinking agent and 0.1~0.5 part of initiator weighed in step 1, high-speed mixer setting temperature Spend for 70~80 DEG C, start high-speed mixer and mixed in the case where rotating speed is 10r/min~15r/min, when the mixing of high-speed mixer Temperature stops mixing when reaching 70~80 DEG C, obtains mixed thing eventually;
5th, extruding pelletization:End that step 4 is obtained mixes thing and is transferred in extruder, pass sequentially through the shearing of extruder, mixing, Kneading and cooling pelletization, obtain PVC composite modification materials;Technological temperature of the extrusion from material mouth at mouth mold be respectively:1 Area:160~165 DEG C, 2nd area:165~170 DEG C, 3rd area:175~180 DEG C, 4th area:180~185 DEG C, 5th area:185~190 DEG C, 6 Area:195~205 DEG C, melt pressure is no more than 10MPa.
7. the preparation method of PVC composite modification materials according to claim 1, it is characterised in that described in step 1 Polyvinyl chloride resin is polyvinyl chloride resin of the hardness number 70.
8. the preparation method of PVC composite modification materials according to claim 1, it is characterised in that the screening described in step 1 Lid agent is rutile titanium dioxide.
9. the preparation method of PVC composite modification materials according to claim 1, it is characterised in that low described in step 1 Warm toughener is PNBR;Impact modifier described in step 1 is MBS Copolymer;Processing aid described in step 1 is acrylonitritrile-styrene resin;Surfactant described in step 1 is Polyoxy base silane.
10. the preparation method of PVC composite modification materials according to claim 1, it is characterised in that described in step 1 Initiator is cumyl peroxide;Crosslinking agent described in step 1 is double maleamic acids.
CN201710695883.6A 2017-08-01 2017-08-01 PVC composite modification materials and preparation method thereof Pending CN107474428A (en)

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CN115093653A (en) * 2022-06-21 2022-09-23 广东裕泰实业有限公司 Ultraviolet-proof PVC (polyvinyl chloride) film and preparation method thereof

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