WO2017067504A1 - Foamed pvc material, preparation method and use thereof - Google Patents

Foamed pvc material, preparation method and use thereof Download PDF

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Publication number
WO2017067504A1
WO2017067504A1 PCT/CN2016/102868 CN2016102868W WO2017067504A1 WO 2017067504 A1 WO2017067504 A1 WO 2017067504A1 CN 2016102868 W CN2016102868 W CN 2016102868W WO 2017067504 A1 WO2017067504 A1 WO 2017067504A1
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foamed pvc
pvc material
mixing
material according
parts
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PCT/CN2016/102868
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French (fr)
Chinese (zh)
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平田隆一
束建强
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大电塑料(上海)有限公司
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Publication of WO2017067504A1 publication Critical patent/WO2017067504A1/en

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    • 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
    • C08K13/00Use of mixtures of ingredients not covered by one single of the preceding main groups, each of these compounds being essential
    • C08K13/02Organic and inorganic ingredients
    • 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
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/08Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing carbon dioxide
    • 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
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/10Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
    • C08J9/102Azo-compounds
    • C08J9/103Azodicarbonamide
    • 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
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/10Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
    • C08J9/104Hydrazines; Hydrazides; Semicarbazides; Semicarbazones; Hydrazones; Derivatives thereof
    • C08J9/105Hydrazines; Hydrazides; Semicarbazides; Semicarbazones; Hydrazones; Derivatives thereof containing sulfur
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • 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
    • 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
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/04N2 releasing, ex azodicarbonamide or nitroso compound
    • 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
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/06CO2, N2 or noble gases
    • 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
    • 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
    • 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
    • C08J2467/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/014Additives containing two or more different additives of the same subgroup in C08K
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/14Applications used for foams

Definitions

  • the invention relates to the field of polymer materials, in particular to a foamed PVC material which can be used for a door sealing material of a refrigerator, a preparation method thereof and a use thereof.
  • the refrigerator door seal is a refrigerator accessory used for sealing between the door body of the refrigerator and the box body, which can ensure the fresh-keeping effect of the refrigerator, and can prolong the service life of the refrigerator, ensure that the door body of the refrigerator can be closed well, and reduce the interior of the refrigerator. Loss of energy. Under normal circumstances, the refrigerator door seal consists of two parts, one is a soft coat and the other is a magnetic strip.
  • the refrigerator door seals (ie, the soft outer jacket portions) used in the existing home appliance industry are generally produced from PVC materials through plastic extruders.
  • PVC is an abbreviation for (Polyvinyl chloride) polyvinyl chloride resin.
  • Polyvinyl chloride homopolymer and polyvinyl chloride copolymer are collectively referred to as polyvinyl chloride resin, which is homopolymerized by vinyl chloride monomer (VCM).
  • VCM vinyl chloride monomer
  • the polyvinyl chloride resin is a white powder or microbeads, which are soft and hard depending on the composition.
  • the PVC material is a material produced by adding a certain proportion of other materials to the polyvinyl chloride resin under certain temperature and pressure.
  • the refrigerator door seal materials used in the home appliance industry are all prepared from unfoamed PVC materials.
  • the seal materials prepared have large thermal conductivity, poor heat insulation effect, high energy consumption, large usage, poor elastic modulus, and the like. problem.
  • a first aspect of the present invention provides a foamed PVC material comprising, by weight, parts by weight of the following components:
  • the polyvinyl chloride has a degree of polymerization of from 800 to 2,500.
  • the polyvinyl chloride has a degree of polymerization of from 1,000 to 1300.
  • the plasticizer is selected from the group consisting of self-identifying diester polyester, trioctyl trimellitate (TOTM), epoxidized soybean oil (ESBO), dioctyl terephthalate (DOTP), and sebacic acid A combination of one or more of octyl (DOS), dioctyl adipate (DOA).
  • TOTM trioctyl trimellitate
  • ESBO epoxidized soybean oil
  • DDP dioctyl terephthalate
  • sebacic acid A combination of one or more of octyl (DOS), dioctyl adipate (DOA).
  • the plasticizer is a combination of an adipic acid polyester and an epoxidized soybean oil, wherein the plasticizer has a weight ratio of adipic acid polyester to epoxidized soybean oil of 1:0.1- 1.5.
  • the preferred viscosity of the oxalic acid polyester is (25 ° C, Mpa ⁇ s) 2400-6000, specific gravity (20/20 ° C) 1.050-1.150, epoxy value of epoxy soybean oil (% ) 6.0 or more, the acid value (KOH mg / g) is 0.5 or less.
  • the filler is calcium carbonate.
  • the processing aid is selected from the group consisting of one or more of an acrylic processing aid and a methyl methacrylate processing aid.
  • the processing aid is selected from the group consisting of acrylic processing aids.
  • the acrylic processing aid is a methyl methacrylate (MMA)/acrylate copolymer having a weight average molecular weight ( ⁇ 10 4 ) of 250 or more.
  • the blowing agent is a chemical blowing agent.
  • the chemical blowing agent is selected from the group consisting of azodicarbonamide, sodium hydrogencarbonate, 4,4'-hydroxybisbenzenesulfonyl hydrazide, preferably a combination of organic chemical foaming Agent.
  • the antioxidant is selected from the group consisting of one or more of antioxidant 1010, antioxidant 168, DLTP.
  • the stabilizer is selected from the group consisting of calcium stearate, zinc stearate, ⁇ -diketone, hydrotalcite, rare earth stabilizer, organotin stabilizer, and antimony zinc stabilizer.
  • the raw material of the foamed PVC material further comprises 0.1-0.5 parts by weight of the anti-mold antibacterial agent.
  • the raw material of the foamed PVC material further comprises, by weight, 3 to 15 parts of a modifier.
  • the modifier is selected from the group consisting of one or more of MBS, nitrile rubber, and acrylate elastomer.
  • a second aspect of the invention provides a method for preparing the foamed PVC material, comprising the steps of:
  • step 5 cooling the material obtained in step 4 to 90-110 ° C, adding a blowing agent and mixing;
  • the material obtained in the step 5 is subjected to internal hardening, and the material obtained by the kneading is extruded and granulated to obtain the foamed PVC material.
  • the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:2-5.
  • the processing aid and the modifier are mixed with the material obtained in the step 3.
  • the specific conditions of the mixing are three-stage mixing, controlled by temperature and rotation speed, respectively, 80-90 ° C / 30-40 rpm, 100-110 ° C / 35-45 rpm, 110-120 °C/30-40rpm.
  • the temperature at the time of extrusion granulation is 90-115 °C.
  • a third aspect of the invention provides the use of the foamed PVC material in the preparation of a PVC door seal.
  • the foamed PVC material is used in the preparation of a PVC door seal for a refrigerator.
  • the foamed PVC material provided by the present invention obtains a suitable foaming rate by controlling the residence time and the processing temperature when being formed by the seal of the extruder, effectively saving social resources, reducing costs, and making the seals
  • the thermal conductivity is significantly reduced, and at the same time, the material obtained by the preparation still has good mechanical properties.
  • the inventor of the present invention adds a specific chemical foaming agent and the like to the PVC formulation, and uses a special processing method to ensure that the chemical foaming agent does not react when the PVC pellets are mixed and granulated, and only passes through the temperature when the door seal is extruded.
  • the extrusion speed is used to ensure a certain foaming rate, so that a large amount of fine bubbles are introduced inside the PVC, and the material properties can be remarkably improved, and the mechanical properties of the PVC material are not lowered.
  • the invention provides a foamed PVC material, the raw material of which comprises the following components in parts by weight:
  • the foamed PVC material provided by the present invention comprises the following components in parts by weight:
  • polyvinyl chloride is used as a base in 100 parts by weight, and the remaining components are used in a certain weight ratio to the polyvinyl chloride.
  • the polyvinyl chloride has a polymerization degree of 800-2500, a preferred degree of polymerization of 1000-1300, and a polyvinyl chloride having a degree of polymerization of 1000-1300 has the best processing property, mechanical properties, and cost performance.
  • the plasticizer is used for reducing the melting temperature and melt viscosity of the PVC material, and the product has good flexibility, elasticity and low temperature resistance.
  • plasticizer is included in parts by weight, preferably 70-85 parts of plasticizer, and those skilled in the art can adjust plasticization according to different processes and environments.
  • the plasticizer is preferably selected from the group consisting of self-identifying diester polyester, trioctyl trimellitate (TOTM), epoxidized soybean oil (ESBO), dioctyl terephthalate (DOTP), dioctyl sebacate. (DOS), a combination of one or more of dioctyl adipate (DOS), more preferably a combination of adipic acid polyester and epoxidized soybean oil, and the diacid polyester can impart superiority to the material.
  • TOTM trioctyl trimellitate
  • ESBO epoxidized soybean oil
  • DDP dioctyl terephthalate
  • DOS dioctyl sebacate
  • DOS dioctyl sebacate
  • DOS dioctyl adipate
  • the ABS/PS resistance, the extraction resistance, the excellent resilience, etc., the epoxy soybean oil can impart the necessary extraction resistance and thermal stability of the material, and the two can be combined to achieve the best use effect.
  • the adipic acid-based polyester is specifically a polymer formed by polycondensation of adipic acid with a diamine or a glycol, and the adipic acid-based polyester includes, but is not limited to, polyethylene adipate.
  • the preferred viscosity of the adipic acid-based polyester is (25 ° C, Mpa ⁇ s) 2400-6000, preferably having a specific gravity of (20/20 ° C) 1.050-1.150 (the ratio of the density of the substance (fully compacted state) to the density of pure H 2 O at 20 ° C under standard atmospheric pressure), in the present invention
  • the adipic acid type polyester is W-2310, and the supplier is a large Japanese ink company; preferably, the epoxy soybean oil has an epoxy value (%) of 6.0 or more, and an acid value (KOH) Mg/
  • a preferred filler is calcium carbonate, and the calcium carbonate may be a light calcium carbonate or a heavy calcium carbonate as long as it does not limit the object of the present invention.
  • the heavy calcium carbonate refers to a sedimentation volume ratio of 1.1-1.9 mL / g of calcium carbonate, light calcium carbonate sedimentation volume ratio of 2.4-2.8 mL / g of calcium carbonate.
  • the model of heavy calcium carbonate is LD-800 and the supplier is Rieter Supermicro Industrial (Suzhou) Co., Ltd.
  • a processing aid preferably 2.4 to 5.5 parts, of a processing aid are included.
  • the processing aid is selected from the group consisting of one or more of an acrylic processing aid and a methyl methacrylate processing aid, preferably an acrylic processing aid.
  • the acrylic processing aid is preferably a methyl methacrylate (MMA) / acrylate copolymer.
  • the weight average molecular weight ( ⁇ 10 4 ) of the methyl methacrylate (MMA)/acrylate copolymer is 250 or more; in an embodiment of the invention, the type of the acrylic processing aid is P- 531A, the supplier is Mitsubishi Rayon (Shanghai) Management Co., Ltd.
  • the foaming agent is preferably a chemical foaming agent, and specific chemical foaming agents may be used, including but not limited to: one of azodicarbonamide, sodium hydrogencarbonate, and 4,4'-hydroxybisbenzenesulfonylhydrazide. Or a combination of multiples. More preferably, it is an organic chemical foaming agent.
  • the organic chemical foaming agent is azodicarbonamide, and is combined with a suitable stabilizer to reduce azodicarbonamide well. The decomposition temperature allows it to be used as a blowing agent in PVC material systems.
  • the antioxidant is used to retard or inhibit the progress of oxidation of the polymer, thereby preventing aging of the polymer and prolonging its service life.
  • the antioxidant may use various antioxidants in the art, and specifically, antioxidants including, but not limited to, antioxidant 1010 (tetrakis [ ⁇ -(3,5-di-tert-butyl-4-hydroxybenzene) One or more of propionic acid] pentaerythritol ester), antioxidant 168 (phenyl (tris(2,4-di-tert-butyl) phosphite), DLTP (dual lauryl thiodipropionate) combination.
  • the antioxidant is an antioxidant 1010.
  • the function of the lubricant in the present invention is to improve the fluidity of the product during processing, to prevent defects due to adhesion in the machine, and to improve the processability of the material.
  • 0.2 to 2.4 parts by weight of the lubricant is included by weight, and those skilled in the art can adjust the amount of the lubricant according to the kind of the lubricant, the process, and the use environment.
  • the lubricant may use various lubricants in the art, and specifically, lubricants that may be used include, but are not limited to, one or a combination of stearic acid and oxidized polyethylene. In a preferred embodiment of the invention, the lubricant is stearic acid.
  • the stabilizer acts to delay the thermal decomposition thereof, and at the same time cooperates with the foaming agent to reduce the decomposition temperature of the foaming agent.
  • the stabilizer includes a PVC heat stabilizer and an acid acceptor, and preferred PVC heat stabilizers include, but are not limited to, calcium stearate, zinc stearate, ⁇ -diketone (stearoylbenzoylmethane), diphenyl.
  • PVC heat stabilizers include, but are not limited to, calcium stearate, zinc stearate, ⁇ -diketone (stearoylbenzoylmethane), diphenyl.
  • a combination of one or more of formylmethane, preferred acid acceptors include, but are not limited to, hydrotalcite, which is preferably Mg 4 Al 2 (OH) 12 CO 3 .3H 2 O.
  • an antifungal antibacterial agent may also be included.
  • the kind of the anti-mold antibacterial agent is not particularly limited as long as it does not limit the object of the present invention.
  • Specific anti-fungal antibacterial agents that can be used include, but are not limited to, thiabendazole.
  • the modifier may be a combination of one or more of, including but not limited to, MBS, nitrile rubber, acrylate elastomer, and the like.
  • the structural elastomer (rubber), the content of the acrylonitrile monomer in the nitrile rubber may be 23-43%, more specifically 28-38%, the Mooney viscosity ML1+4, 100 ° C may be 37-77, Specifically, it may be 47-67.
  • the nitrile rubber is P-83, and the supplier is French Onofrio Chemical.
  • the acrylate elastomer (acrylate rubber) is An elastomer having a pre-crosslinked structure obtained by copolymerization of an acrylate-based monomer, the acrylate elastomer having a Mooney viscosity ML1+4, 150 ° C may be 15-35, more specifically 20-30, in the present invention In one embodiment, the acrylate elastomer is P-95 and the supplier is French Onofrio Chemical.
  • the invention further provides a preparation method of the foamed PVC material, which performs necessary control on the processing temperature during the preparation process, and the foaming agent does not decompose, specifically comprising the following steps:
  • plasticizer In order to allow the resin powder to absorb the plasticizer well, a small amount of plasticizer is added to allow the resin powder to be absorbed at room temperature (preferably 5-35 ° C), and the remaining plasticization is carried out when the temperature is raised to about 80 ° C. All the agents are added to the mixing pot to allow the resin powder to have sufficient time to absorb and mix.
  • the weight ratio of the plasticizers added in steps 2 and 3 is preferably 1. : 2-5.
  • the processing aid and the modifier may be mixed with the material obtained in the step 3.
  • step 5 cooling the material obtained in step 4 to 90-110 ° C, adding a blowing agent and mixing;
  • the temperature of the material system does not exceed 140 °C.
  • the processing aid is mixed with the material obtained in the step 3. Because of the high-speed mixing of the mixing pot, the material will heat up during the mixing process, and the cooling system (cooling) is adopted when the temperature is raised to 130-140 ° C. Water) The material was cooled to 90-110 ° C, the blowing agent was added and mixed for 3 minutes, and the temperature of the system was maintained at 90-110 ° C during the mixing.
  • the material obtained in the step 5 is subjected to internal hardening, and the material obtained by the kneading is extruded and granulated to obtain the foamed PVC material.
  • the specific conditions of the mixing are three-stage mixing, controlled by temperature and rotation speed, and the three-stage mixing temperature is 80-90 ° C / 30-40 rpm, 100-110 ° C / 35- 45 rpm, 110-120 ° C / 30-40 rpm, the temperature at the time of extrusion granulation is ⁇ 115 ° C, and the preferred temperature is 90-115 ° C.
  • the mixing of the materials is carried out in a high-speed mixing pan.
  • the specific conditions for mixing are as follows:
  • the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:2-5.
  • the processing aid is mixed with the material obtained in the step 3 at 125-135 ° C.
  • the temperature of the system is raised to 130-140 ° C, the material is cooled to 90-110 ° C, the blowing agent is added and mixed for 3 minutes.
  • the invention further provides the use of the foamed PVC material in the preparation of a PVC door seal.
  • the foamed PVC material is used in the preparation of a PVC door seal for a refrigerator.
  • the foamed PVC material provided by the invention is particularly suitable for preparing PVC door sealing material for refrigerators, and the door sealing material introduces a large amount of micro-bubbles inside the PVC by adding a foaming agent, thereby significantly improving the heat insulating performance of the material while ensuring
  • the mechanical properties of the material are suitable for the complex structure and use environment of the refrigerator door seal.
  • the invention further provides a foamed PVC door seal material obtained by preparing the foamed PVC material.
  • azodicarbonamide is not decomposed, and during the preparation process of preparing the foamed PVC door sealant using the foamed PVC material, azodicarbonamide is decomposed and foamed.
  • the foamed PVC door seal can be obtained from the foamed PVC material by various extruders in the art.
  • the processing temperature is preferably from 115 to 170 ° C. In one embodiment of the invention, the processing temperature is from 140 to 158 ° C. In one embodiment of the invention, the processing temperature is from 150 to 168 ° C.
  • Those skilled in the art can adjust the residence time according to different equipment, process and use environment (specifically, different diameters of the extruder, different processing temperatures, etc.) to obtain a suitable foaming rate.
  • the preferred foaming ratio of the sealant is 13-40%.
  • the foamed PVC material provided by the present invention obtains a suitable foaming rate by controlling the residence time and the processing temperature when being formed by the seal of the extruder, effectively saving social resources, reducing costs, and making the seals
  • the thermal conductivity is significantly reduced, and at the same time, the material obtained by the preparation still has good mechanical properties.
  • one or more of the method steps recited in the present invention are not exclusive of other method steps that may be present before or after the combination step, or that other method steps can be inserted between the steps specifically mentioned, unless otherwise It should be understood that the combined connection relationship between one or more devices/devices referred to in the present invention does not exclude that other devices/devices may exist before or after the combined device/device or Other devices/devices can also be inserted between the two devices/devices unless otherwise stated.
  • each method step is merely a convenient means of identifying the various method steps, and is not intended to limit the order of the various method steps or to limit the scope of the invention, the relative In the case where the technical content is not substantially changed, it is considered to be a scope in which the present invention can be implemented.
  • the preparation method of the foamed PVC door sealing material is as follows:
  • step 2 After mixing at a high speed for 60 ⁇ 20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
  • the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
  • the pellet obtained in the step 7 is passed through a ⁇ 20 mm extrusion test machine to prepare a spline of the foamed PVC door sealing material, and the processing temperature is 140 ° C - 158 ° C;
  • the tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
  • the elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
  • the specific gravity is in accordance with JIS K 7112A;
  • the thermal conductivity is calculated according to the formula using thermal diffusivity, constant pressure specific heat capacity, and specific gravity.
  • thermal conductivity thermal diffusivity * constant pressure specific heat capacity * specific gravity
  • Foaming rate specific gravity of unfoamed product / specific gravity of foamed product -1
  • the preparation method of the foamed PVC door sealing material is as follows:
  • step 2 2) mixing a suitable amount of plasticizer with the material obtained in step 1 after mixing at a high speed of ° C for 60 seconds ⁇ 20;
  • the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
  • the pellet obtained in the step 7 is passed through a ⁇ 20 mm extrusion test machine to prepare a spline of the foamed PVC door sealing material, and the processing temperature is 140-158 ° C;
  • the tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
  • the elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
  • the specific gravity is in accordance with JIS K 7112A;
  • the thermal conductivity is calculated according to the formula using thermal diffusivity, constant pressure specific heat capacity, and specific gravity.
  • thermal conductivity thermal diffusivity * constant pressure specific heat capacity * specific gravity
  • Foaming rate specific gravity of unfoamed product / specific gravity of foamed product -1
  • the preparation method of the foamed PVC door sealing material is as follows:
  • step 2 After mixing at a high speed for 60 ⁇ 20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
  • the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:2.
  • the pellet obtained in the step 7 is passed through a ⁇ 20 mm extrusion test machine to prepare a spline of the foamed PVC door sealing material, and the processing temperature is 140-158 ° C;
  • the tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
  • the elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
  • the specific gravity is in accordance with JIS K 7112A;
  • the thermal conductivity is calculated according to the formula using thermal diffusivity, constant pressure specific heat capacity, and specific gravity.
  • thermal conductivity thermal diffusivity * constant pressure specific heat capacity * specific gravity
  • Foaming rate specific gravity of unfoamed product / specific gravity of foamed product -1
  • the preparation method of the foamed PVC door sealing material is as follows:
  • step 2 After mixing at a high speed for 60 ⁇ 20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
  • the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:5.
  • the obtained materials are mixed, and the specific conditions of the mixing are three-stage mixing, controlled by temperature, respectively, at 90 ° C / 40 rpm, 100 ° C / 35 rpm, 110 ° C / 30 rpm, and the materials obtained by the mixing are at 90 Extrusion granulation at -115 ° C;
  • the pellet obtained in the step 7 is passed through a ⁇ 20 mm extrusion test machine to prepare a spline of the foamed PVC door sealing material, and the processing temperature is 140-158 ° C;
  • the tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
  • the elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
  • the specific gravity is in accordance with JIS K 7112A;
  • the thermal conductivity is calculated according to the formula using thermal diffusivity, constant pressure specific heat capacity, and specific gravity.
  • thermal conductivity thermal diffusivity * constant pressure specific heat capacity * specific gravity
  • Foaming rate specific gravity of unfoamed product / specific gravity of foamed product -1
  • the preparation method of the refrigerator door seal is as follows:
  • step 2 After mixing at a high speed for 60 ⁇ 20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
  • the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
  • step 7 The pellet obtained in step 7 is passed through a ⁇ 20 mm extrusion test machine to prepare a spline of the refrigerator door seal, and the processing temperature is 140-158 ° C;
  • the tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
  • the elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
  • the specific gravity is in accordance with JIS K 7112A;
  • thermal conductivity thermal diffusivity * constant pressure specific heat capacity * specific gravity
  • Foaming rate specific gravity of unfoamed product / specific gravity of foamed product -1
  • the preparation method of the refrigerator door seal is as follows:
  • step 2 After mixing at a high speed for 60 ⁇ 20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
  • the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
  • step 7 The pellet obtained in step 7 is passed through a ⁇ 20 mm extrusion test machine to prepare a spline of the refrigerator door seal, and the processing temperature is 140-158 ° C;
  • the tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
  • the elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
  • the specific gravity is in accordance with JIS K 7112A;
  • thermal conductivity thermal diffusivity * constant pressure specific heat capacity * specific gravity
  • Foaming rate specific gravity of unfoamed product / specific gravity of foamed product -1
  • the preparation method of the refrigerator door seal is as follows:
  • step 2 After mixing at a high speed for 60 ⁇ 20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
  • the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
  • the pellet obtained in step 7 is passed through a ⁇ 20 mm extrusion test machine to prepare a spline of the refrigerator door seal, and the processing temperature is 150-168 ° C;
  • the tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
  • the elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
  • the specific gravity is in accordance with JIS K 7112A;
  • thermal conductivity thermal diffusivity * constant pressure specific heat capacity * specific gravity
  • Foaming rate specific gravity of unfoamed product / specific gravity of foamed product -1
  • the present invention effectively overcomes various shortcomings in the prior art and has high industrial utilization value.

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Abstract

The invention relates to the field of macromolecular materials, particularly to a foamed PVC material that is used as a sealant for a refrigerator door, and a preparation method and use thereof. The invention provides a foamed PVC material, the raw materials thereof comprising the following components calculated in parts by weight: 100 parts of a polyvinyl chloride; 60-90 parts of a plasticizer; 25-95 parts of a filling agent; 2.4-12 parts of a processing aid; 1.2-6 parts of a foaming agent; 0.2-0.5 parts of an antioxidant; 0.2-2.4 parts of a lubricant; and 1-8 parts of a stabilizer. The foamed PVC material provided by the invention obtains, when shaping a seal by means of an extruder, suitable foaming rate by means of controlling a dwell time and a processing temperature, efficiently saving social resources and reducing the cost, and reducing the coefficient of heat conductivity significantly. Meanwhile, the material prepared still has good mechanical performances.

Description

一种发泡PVC材料及其制备方法和用途Foamed PVC material, preparation method and use thereof 技术领域Technical field
本发明涉及高分子材料领域,特别是涉及一种可用于电冰箱门封料的发泡PVC材料及其制备方法和用途。The invention relates to the field of polymer materials, in particular to a foamed PVC material which can be used for a door sealing material of a refrigerator, a preparation method thereof and a use thereof.
背景技术Background technique
冰箱门封条是用在冰箱门体和箱体之间用来密封的一种冰箱配件,能够保证冰箱保鲜效果,并且能延长冰箱的使用寿命,保证冰箱门体能够很好的闭合,减少冰箱内部能量的损失。一般情况下,冰箱门封条由两部分组成,一部分是软质外套,另一部分是磁性胶条。The refrigerator door seal is a refrigerator accessory used for sealing between the door body of the refrigerator and the box body, which can ensure the fresh-keeping effect of the refrigerator, and can prolong the service life of the refrigerator, ensure that the door body of the refrigerator can be closed well, and reduce the interior of the refrigerator. Loss of energy. Under normal circumstances, the refrigerator door seal consists of two parts, one is a soft coat and the other is a magnetic strip.
现有的家电行业中所使用的冰箱门封条料(即软质外套部分)一般是由PVC材料通过塑料挤出机生产的。PVC是(Polyvinyl chloride)聚氯乙烯树脂的缩写,聚氯乙烯均聚物和聚氯乙烯共聚物统称为聚氯乙烯树脂,其是由氯乙烯单体(vinyl chloride monomer,简称VCM)经过均聚或由氯乙烯单体与其他单体共聚而成,聚氯乙烯树脂是一种白色粉末或微珠粒,根据组成不同有软硬之分。而PVC材料是聚氯乙烯树脂加入一定比例的其他材料,在一定的温度和压力作用下而产生的材料。The refrigerator door seals (ie, the soft outer jacket portions) used in the existing home appliance industry are generally produced from PVC materials through plastic extruders. PVC is an abbreviation for (Polyvinyl chloride) polyvinyl chloride resin. Polyvinyl chloride homopolymer and polyvinyl chloride copolymer are collectively referred to as polyvinyl chloride resin, which is homopolymerized by vinyl chloride monomer (VCM). Or a vinyl chloride monomer copolymerized with other monomers, the polyvinyl chloride resin is a white powder or microbeads, which are soft and hard depending on the composition. The PVC material is a material produced by adding a certain proportion of other materials to the polyvinyl chloride resin under certain temperature and pressure.
对于现在家电行业使用的冰箱门封条料均是由未发泡的PVC材料制备获得,所制备的封条料存在导热系数大、隔热效果差、能耗大、使用量大、弹性率差等诸多问题。The refrigerator door seal materials used in the home appliance industry are all prepared from unfoamed PVC materials. The seal materials prepared have large thermal conductivity, poor heat insulation effect, high energy consumption, large usage, poor elastic modulus, and the like. problem.
发明内容Summary of the invention
鉴于以上所述现有技术的缺点,本发明的目的在于提供一种可用于电冰箱门封料的发泡PVC材料及其制备方法和用途,用于解决现有技术中的问题。In view of the above-mentioned shortcomings of the prior art, it is an object of the present invention to provide a foamed PVC material which can be used for a refrigerator door seal and a preparation method and use thereof for solving the problems in the prior art.
为实现上述目的及其他相关目的,本发明第一方面提供一种发泡PVC材料,其原料按重量份计,包括如下组分:In order to achieve the above object and other related objects, a first aspect of the present invention provides a foamed PVC material comprising, by weight, parts by weight of the following components:
Figure PCTCN2016102868-appb-000001
Figure PCTCN2016102868-appb-000001
Figure PCTCN2016102868-appb-000002
Figure PCTCN2016102868-appb-000002
优选的,所述聚氯乙烯的聚合度为800-2500。Preferably, the polyvinyl chloride has a degree of polymerization of from 800 to 2,500.
更优选的,所述聚氯乙烯的聚合度为1000-1300。More preferably, the polyvinyl chloride has a degree of polymerization of from 1,000 to 1300.
优选的,所述增塑剂选自己二酸类聚酯、偏苯三酸三辛酯(TOTM)、环氧大豆油(ESBO)、对苯二甲酸二辛酯(DOTP)、癸二酸二辛酯(DOS)、己二酸二辛酯(DOA)中的一种或多种的组合。Preferably, the plasticizer is selected from the group consisting of self-identifying diester polyester, trioctyl trimellitate (TOTM), epoxidized soybean oil (ESBO), dioctyl terephthalate (DOTP), and sebacic acid A combination of one or more of octyl (DOS), dioctyl adipate (DOA).
更优选的,所述增塑剂为己二酸类聚酯和环氧大豆油的组合,所述增塑剂中,己二酸类聚酯和环氧大豆油的重量比为1:0.1-1.5。More preferably, the plasticizer is a combination of an adipic acid polyester and an epoxidized soybean oil, wherein the plasticizer has a weight ratio of adipic acid polyester to epoxidized soybean oil of 1:0.1- 1.5.
进一步优选的,所述乙二酸类聚酯的优选粘度为(25℃,Mpa·s)2400-6000,比重为(20/20℃)1.050-1.150,环氧大豆油的环氧值(%)6.0以上,酸值(KOH mg/g)0.5以下。Further preferably, the preferred viscosity of the oxalic acid polyester is (25 ° C, Mpa·s) 2400-6000, specific gravity (20/20 ° C) 1.050-1.150, epoxy value of epoxy soybean oil (% ) 6.0 or more, the acid value (KOH mg / g) is 0.5 or less.
优选的,所述填充剂为碳酸钙。Preferably, the filler is calcium carbonate.
优选的,所述加工助剂选自丙烯酸类加工助剂和甲基丙烯酸甲酯类加工助剂中的一种或多种的组合。Preferably, the processing aid is selected from the group consisting of one or more of an acrylic processing aid and a methyl methacrylate processing aid.
更优选的,所述加工助剂选自丙烯酸类加工助剂。More preferably, the processing aid is selected from the group consisting of acrylic processing aids.
进一步优选的,所述丙烯酸类加工助剂为甲基丙烯酸甲酯(MMA)/丙烯酸酯共聚物,其重量平均分子量(×104)250以上。Further preferably, the acrylic processing aid is a methyl methacrylate (MMA)/acrylate copolymer having a weight average molecular weight (×10 4 ) of 250 or more.
优选的,所述发泡剂为化学发泡剂。Preferably, the blowing agent is a chemical blowing agent.
更有选的,所述化学发泡剂选自偶氮二甲酰胺、碳酸氢钠、4,4'-羟基双苯磺酰肼中的一种或多种的组合,优选为有机化学发泡剂。More preferably, the chemical blowing agent is selected from the group consisting of azodicarbonamide, sodium hydrogencarbonate, 4,4'-hydroxybisbenzenesulfonyl hydrazide, preferably a combination of organic chemical foaming Agent.
优选的,所述抗氧剂选自抗氧剂1010、抗氧剂168、DLTP中的一种或多种的组合。Preferably, the antioxidant is selected from the group consisting of one or more of antioxidant 1010, antioxidant 168, DLTP.
优选的,所述稳定剂选自硬脂酸钙、硬脂酸锌、β-二酮、水滑石、稀土稳定剂、有机锡稳定剂、钡锌稳定剂中的一种或多种的组合。Preferably, the stabilizer is selected from the group consisting of calcium stearate, zinc stearate, β-diketone, hydrotalcite, rare earth stabilizer, organotin stabilizer, and antimony zinc stabilizer.
更优选的,所述稳定剂包括硬脂酸钙、硬脂酸锌、β-二酮和水滑石,各组分的重量份之比为:硬脂酸钙、硬脂酸锌、β-二酮和水滑石=1-10:1-10:1-10:1-10。More preferably, the stabilizer comprises calcium stearate, zinc stearate, β-diketone and hydrotalcite, and the ratio by weight of each component is: calcium stearate, zinc stearate, β-di Ketone and hydrotalcite = 1-10:1-10:1-10:1-10.
优选的,所述发泡PVC材料的原料按重量份计,还包括如防霉抗菌剂0.1-0.5份。Preferably, the raw material of the foamed PVC material further comprises 0.1-0.5 parts by weight of the anti-mold antibacterial agent.
优选的,所述发泡PVC材料的原料按重量份计,还包括3-15份改性剂。Preferably, the raw material of the foamed PVC material further comprises, by weight, 3 to 15 parts of a modifier.
更优选的,所述改性剂选自MBS、丁腈橡胶、丙烯酸酯弹性体中的一种或多种的组合。More preferably, the modifier is selected from the group consisting of one or more of MBS, nitrile rubber, and acrylate elastomer.
本发明第二方面提供所述发泡PVC材料的制备方法,包括如下步骤:A second aspect of the invention provides a method for preparing the foamed PVC material, comprising the steps of:
1)将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂进行混合;1) mixing polyvinyl chloride, a filler, an antioxidant, a lubricant, and a stabilizer;
2)在室温下将适量增塑剂与步骤1所得物料进行混合;2) mixing an appropriate amount of plasticizer with the material obtained in step 1 at room temperature;
3)在70-90℃下将剩余增塑剂与步骤2所得物料进行混合; 3) mixing the remaining plasticizer with the material obtained in step 2 at 70-90 ° C;
4)在125-135℃下将加工助剂与步骤3所得物料进行混合;4) mixing the processing aid with the material obtained in step 3 at 125-135 ° C;
5)将步骤4所得物料冷却至90-110℃,加入发泡剂并混合;5) cooling the material obtained in step 4 to 90-110 ° C, adding a blowing agent and mixing;
6)将步骤5所得物料进行密炼,并将密炼所得的物料挤出造粒,即得所述发泡PVC材料。6) The material obtained in the step 5 is subjected to internal hardening, and the material obtained by the kneading is extruded and granulated to obtain the foamed PVC material.
优选的,所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:2-5。Preferably, the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:2-5.
优选的,所述步骤4中,将加工助剂和改性剂与步骤3所得物料进行混合。Preferably, in the step 4, the processing aid and the modifier are mixed with the material obtained in the step 3.
优选的,所述步骤6中,密炼的具体条件为三段密炼,以温度和转速进行控制,分别为80-90℃/30-40rpm、100-110℃/35-45rpm、110-120℃/30-40rpm。Preferably, in the step 6, the specific conditions of the mixing are three-stage mixing, controlled by temperature and rotation speed, respectively, 80-90 ° C / 30-40 rpm, 100-110 ° C / 35-45 rpm, 110-120 °C/30-40rpm.
优选的,所述步骤6中,挤出造粒时的温度为90-115℃。Preferably, in the step 6, the temperature at the time of extrusion granulation is 90-115 °C.
本发明第三方面提供所述发泡PVC材料在制备PVC门封料中的用途。A third aspect of the invention provides the use of the foamed PVC material in the preparation of a PVC door seal.
优选的,所述发泡PVC材料在制备冰箱用PVC门封料中的用途。Preferably, the foamed PVC material is used in the preparation of a PVC door seal for a refrigerator.
如上所述,本发明所提供的发泡PVC材料,在经押出机封条成型时,通过停留时间和加工温度控制获得了合适的发泡率,有效的节约社会资源、减少成本,并使封条的导热系数明显下降,同时,制备所获得材料依然具有良好的力学性能。As described above, the foamed PVC material provided by the present invention obtains a suitable foaming rate by controlling the residence time and the processing temperature when being formed by the seal of the extruder, effectively saving social resources, reducing costs, and making the seals The thermal conductivity is significantly reduced, and at the same time, the material obtained by the preparation still has good mechanical properties.
具体实施方式detailed description
本发明发明人在PVC配方中添加特定的化学发泡剂等辅助材料,使用特殊的加工方式,保证在PVC粒料混合造粒时化学发泡剂未反应,只在门封条押出时通过温度和押出速度来保证一定的发泡率,从而在PVC内部引入大量的微细气泡的同时,能够显著提高材料特性,并保证PVC材料力学性能不下降。The inventor of the present invention adds a specific chemical foaming agent and the like to the PVC formulation, and uses a special processing method to ensure that the chemical foaming agent does not react when the PVC pellets are mixed and granulated, and only passes through the temperature when the door seal is extruded. The extrusion speed is used to ensure a certain foaming rate, so that a large amount of fine bubbles are introduced inside the PVC, and the material properties can be remarkably improved, and the mechanical properties of the PVC material are not lowered.
本发明提供一种发泡PVC材料,其原料按重量份计,包括如下组分:The invention provides a foamed PVC material, the raw material of which comprises the following components in parts by weight:
Figure PCTCN2016102868-appb-000003
Figure PCTCN2016102868-appb-000003
优选的,本发明所提供的发泡PVC材料,其原料按重量份计,包括如下组分:Preferably, the foamed PVC material provided by the present invention comprises the following components in parts by weight:
Figure PCTCN2016102868-appb-000004
Figure PCTCN2016102868-appb-000004
Figure PCTCN2016102868-appb-000005
Figure PCTCN2016102868-appb-000005
下面对各组分进行详细说明:The components are described in detail below:
聚氯乙烯Polyvinyl chloride
在本发明所提供的发泡PVC材料的配方中,聚氯乙烯以100重量份份作为基数,其余组分的使用量均与聚氯乙烯形成一定重量比。所述聚氯乙烯的聚合度为800-2500,优选的聚合度为1000-1300,聚合度为1000-1300范围内的聚氯乙烯其加工性能、力学性能、性价比最佳。In the formulation of the foamed PVC material provided by the present invention, polyvinyl chloride is used as a base in 100 parts by weight, and the remaining components are used in a certain weight ratio to the polyvinyl chloride. The polyvinyl chloride has a polymerization degree of 800-2500, a preferred degree of polymerization of 1000-1300, and a polyvinyl chloride having a degree of polymerization of 1000-1300 has the best processing property, mechanical properties, and cost performance.
增塑剂Plasticizer
本发明中增塑剂用于降低PVC材料熔融温度及熔体粘度,并使产品具有良好的柔软性、弹性及耐低温性能。In the invention, the plasticizer is used for reducing the melting temperature and melt viscosity of the PVC material, and the product has good flexibility, elasticity and low temperature resistance.
在本发明所提供的发泡PVC材料中,按重量份计包括60-90份增塑剂,优选包括70-85份增塑剂,本领域技术人员可根据工艺和使用环境的不同调整增塑剂的用量。所述增塑剂优选选自己二酸类聚酯、偏苯三酸三辛酯(TOTM)、环氧大豆油(ESBO)、对苯二甲酸二辛酯(DOTP)、癸二酸二辛酯(DOS)、己二酸二辛酯(DOS)中的一种或多种的组合,更优选为己二酸类聚酯和环氧大豆油的组合,已二酸类聚酯可以赋予材料优越的耐ABS/PS迁移性、耐抽出性、优良的回弹性等,环氧大豆油可以赋予材料必要的耐抽出性和热稳定性,两者组合在一起可以达到最佳的使用效果。在增塑剂中己二酸类聚酯和环氧大豆油两者的重量比优选为己二酸类聚酯:环氧大豆油=1:0.1-1.5,更优选为1:0.3-1.2。所述己二酸类聚酯具体为己二酸与二元胺或二元醇缩聚所形成的高分子聚合物,所述己二酸类聚酯包括但不限于聚己二酸乙二醇酯、聚己二酸-1,2-丙二醇酯、聚己二酸-1,3-丁二醇酯、聚己二酸-1,4-丁二醇酯、聚己二酸新戊醇酯、聚己二酸-1,6-己二醇酯、聚己二酸己二胺等中的一种或多种的组合,所述己二酸类聚酯的优选粘度为(25℃,Mpa·s)2400-6000,优选比重为(20/20℃)1.050-1.150(在标准大气压下、20℃时,物质(完全密实状态)的密度与纯H2O的密度的比值),在本发明一实施例中,所述己二酸类聚酯型号为W-2310,供应商为大日本油墨公司;优选的,所述环氧大豆油的环氧值(%)6.0以上,酸值(KOH mg/g)0.5以下,在本发明一实施例中,所述环氧大豆油为型号为E-20,供应商为广州新锦龙塑料助剂有限公司。 In the foamed PVC material provided by the present invention, 60-90 parts of plasticizer is included in parts by weight, preferably 70-85 parts of plasticizer, and those skilled in the art can adjust plasticization according to different processes and environments. The amount of the agent. The plasticizer is preferably selected from the group consisting of self-identifying diester polyester, trioctyl trimellitate (TOTM), epoxidized soybean oil (ESBO), dioctyl terephthalate (DOTP), dioctyl sebacate. (DOS), a combination of one or more of dioctyl adipate (DOS), more preferably a combination of adipic acid polyester and epoxidized soybean oil, and the diacid polyester can impart superiority to the material. The ABS/PS resistance, the extraction resistance, the excellent resilience, etc., the epoxy soybean oil can impart the necessary extraction resistance and thermal stability of the material, and the two can be combined to achieve the best use effect. The weight ratio of both the adipic acid polyester and the epoxidized soybean oil in the plasticizer is preferably adipic acid polyester: epoxidized soybean oil = 1: 0.1 to 1.5, more preferably 1: 0.3 to 1.2. The adipic acid-based polyester is specifically a polymer formed by polycondensation of adipic acid with a diamine or a glycol, and the adipic acid-based polyester includes, but is not limited to, polyethylene adipate. , polyadipate-1,2-propanediol ester, polyadipate-1,3-butylene glycol ester, polyadipate-1,4-butanediol ester, polyadipylate adipate, a combination of one or more of polyadipate-1,6-hexanediol ester, polyhexamethylene adipate, etc., the preferred viscosity of the adipic acid-based polyester is (25 ° C, Mpa· s) 2400-6000, preferably having a specific gravity of (20/20 ° C) 1.050-1.150 (the ratio of the density of the substance (fully compacted state) to the density of pure H 2 O at 20 ° C under standard atmospheric pressure), in the present invention In one embodiment, the adipic acid type polyester is W-2310, and the supplier is a large Japanese ink company; preferably, the epoxy soybean oil has an epoxy value (%) of 6.0 or more, and an acid value (KOH) Mg/g) 0.5 or less, in an embodiment of the invention, the epoxidized soybean oil is model E-20, and the supplier is Guangzhou Xinjinlong Plastic Additive Co., Ltd.
填充剂Filler
在本发明所提供的发泡PVC材料中,按重量份计包括25-95份填充剂,优选包括40-80份填充剂。优选的填充剂为碳酸钙,所述碳酸钙可使用轻质碳酸钙,也可使用重质碳酸钙,只要不对本发明的发明目的产生限制即可,所述重质碳酸钙指沉降体积比为1.1-1.9mL/g的碳酸钙,轻质碳酸钙酯沉降体积比为2.4-2.8mL/g的碳酸钙。在本发明一优选实施例中,所使用的是重质碳酸钙的型号为LD-800,供应商为立达超微工业(苏州)有限公司。In the foamed PVC material provided by the present invention, 25 to 95 parts by weight, preferably 40 to 80 parts, of filler are included in parts by weight. A preferred filler is calcium carbonate, and the calcium carbonate may be a light calcium carbonate or a heavy calcium carbonate as long as it does not limit the object of the present invention. The heavy calcium carbonate refers to a sedimentation volume ratio of 1.1-1.9 mL / g of calcium carbonate, light calcium carbonate sedimentation volume ratio of 2.4-2.8 mL / g of calcium carbonate. In a preferred embodiment of the invention, the model of heavy calcium carbonate is LD-800 and the supplier is Rieter Supermicro Industrial (Suzhou) Co., Ltd.
加工助剂Processing aids
因为PVC材料发泡后气孔分布及大小存在明显的不均一,在拉伸试验时出现应力集中在薄面部分,容易破裂,所以需要选择适当的加工助剂和添加量,来保证气孔分布和大小的均一,从而提高拉伸强度。Because the distribution and size of the pores of PVC materials are obviously uneven, the stress is concentrated on the thin surface during the tensile test, which is easy to break. Therefore, it is necessary to select appropriate processing aids and addition amount to ensure the distribution and size of the pores. Uniform, thereby increasing tensile strength.
在本发明所提供的发泡PVC材料中,按重量份计包括2.4-12份加工助剂,优选包括2.4-5.5份加工助剂。所述加工助剂选自丙烯酸类加工助剂和甲基丙烯酸甲酯类加工助剂中的一种或多种的组合,优选为丙烯酸类加工助剂。进一步的,所述丙烯酸类加工助剂优选为甲基丙烯酸甲酯(MMA)/丙烯酸酯共聚物。优选的,所述甲基丙烯酸甲酯(MMA)/丙烯酸酯共聚物的重量平均分子量(×104)250以上;在本发明一实施例中,所述丙烯酸类加工助剂的型号为P-531A,供应商为三菱丽阳(上海)管理有限公司。In the foamed PVC material provided by the present invention, 2.4 to 12 parts by weight of a processing aid, preferably 2.4 to 5.5 parts, of a processing aid are included. The processing aid is selected from the group consisting of one or more of an acrylic processing aid and a methyl methacrylate processing aid, preferably an acrylic processing aid. Further, the acrylic processing aid is preferably a methyl methacrylate (MMA) / acrylate copolymer. Preferably, the weight average molecular weight (×10 4 ) of the methyl methacrylate (MMA)/acrylate copolymer is 250 or more; in an embodiment of the invention, the type of the acrylic processing aid is P- 531A, the supplier is Mitsubishi Rayon (Shanghai) Management Co., Ltd.
发泡剂Foaming agent
在本发明所提供的发泡PVC材料中,按重量份计包括1.2-6份发泡剂,优选包括1.5-3份发泡剂。所述发泡剂优选为化学发泡剂,具体可使用的化学发泡剂包括但不限于:偶氮二甲酰胺、碳酸氢钠、4,4'-羟基双苯磺酰肼中的一种或多种的组合。更优选为有机化学发泡剂,在本发明一优选实施例中,所述有机化学发泡剂为偶氮二甲酰胺,并与合适的稳定剂配合,很好地降低了偶氮二甲酰胺的分解温度,使其能在PVC材料体系中作为发泡剂使用。In the foamed PVC material provided by the present invention, 1.2 to 6 parts by weight of the foaming agent is contained, preferably 1.5 to 3 parts by weight of the foaming agent. The foaming agent is preferably a chemical foaming agent, and specific chemical foaming agents may be used, including but not limited to: one of azodicarbonamide, sodium hydrogencarbonate, and 4,4'-hydroxybisbenzenesulfonylhydrazide. Or a combination of multiples. More preferably, it is an organic chemical foaming agent. In a preferred embodiment of the present invention, the organic chemical foaming agent is azodicarbonamide, and is combined with a suitable stabilizer to reduce azodicarbonamide well. The decomposition temperature allows it to be used as a blowing agent in PVC material systems.
抗氧剂Antioxidant
本发明所提供的发泡PVC材料中,抗氧剂用于延缓或抑制聚合物氧化的进程,从而阻止聚合物的老化并延长其使用寿命。In the foamed PVC material provided by the present invention, the antioxidant is used to retard or inhibit the progress of oxidation of the polymer, thereby preventing aging of the polymer and prolonging its service life.
在本发明所提供的发泡PVC材料中,按重量份计包括0.2-0.5份抗氧剂,优选包括0.2-0.3份抗氧剂。所述抗氧剂可使用本领域各种抗氧剂,具体可使用的抗氧剂包括但不限于:抗氧剂1010(四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯)、抗氧剂168(三(2,4-二叔丁基)亚磷酸苯酯)、DLTP(硫代二丙酸双月桂酯)中的一种或多种的组合。在本发明一优选实施例中,所述抗氧剂为抗氧剂1010。In the foamed PVC material provided by the present invention, 0.2 to 0.5 parts by weight of the antioxidant, preferably 0.2 to 0.3 parts by weight of the antioxidant are included in parts by weight. The antioxidant may use various antioxidants in the art, and specifically, antioxidants including, but not limited to, antioxidant 1010 (tetrakis [β-(3,5-di-tert-butyl-4-hydroxybenzene) One or more of propionic acid] pentaerythritol ester), antioxidant 168 (phenyl (tris(2,4-di-tert-butyl) phosphite), DLTP (dual lauryl thiodipropionate) combination. In a preferred embodiment of the invention, the antioxidant is an antioxidant 1010.
润滑剂 Lubricant
本发明中润滑剂的作用是在加工过程中改善产品的流动性,防止在机内内因粘着而产生缺陷,并能够改善材料的可加工性能。The function of the lubricant in the present invention is to improve the fluidity of the product during processing, to prevent defects due to adhesion in the machine, and to improve the processability of the material.
在本发明所提供的发泡PVC材料中,按重量份计包括0.2-2.4份润滑剂,本领域技术人员可根据润滑剂的种类、工艺和使用环境的不同调整润滑剂的用量。所述润滑剂可使用本领域各种润滑剂,具体可使用的润滑剂包括但不限于:硬脂酸、氧化聚乙烯中的一种或多种的组合。在本发明一优选实施例中,润滑剂为硬脂酸。In the foamed PVC material provided by the present invention, 0.2 to 2.4 parts by weight of the lubricant is included by weight, and those skilled in the art can adjust the amount of the lubricant according to the kind of the lubricant, the process, and the use environment. The lubricant may use various lubricants in the art, and specifically, lubricants that may be used include, but are not limited to, one or a combination of stearic acid and oxidized polyethylene. In a preferred embodiment of the invention, the lubricant is stearic acid.
稳定剂stabilizer
本发明所提供的发泡PVC材料中,稳定剂起到延缓其热分解的作用,并同时与发泡剂相配合,起到降低发泡剂分解温度的作用。In the foamed PVC material provided by the invention, the stabilizer acts to delay the thermal decomposition thereof, and at the same time cooperates with the foaming agent to reduce the decomposition temperature of the foaming agent.
在本发明所提供的发泡PVC材料中,按重量份计包括1-8份稳定剂,优选包括1-6份稳定剂,本领域技术人员可根据工艺和使用环境的不同调整增塑剂的用量。所述稳定剂包括PVC热稳定剂和吸酸剂,优选的PVC热稳定剂包括但不限于硬脂酸钙、硬脂酸锌、β-二酮(硬脂酰苯甲酰甲烷)、二苯甲酰甲烷中的一种或多种的组合,优选的吸酸剂包括但不限于水滑石,所述水滑石优选为Mg4Al2(OH)12CO3·3H2O。在本发明一优选实施例中,所述稳定剂包括硬脂酸钙、硬脂酸锌、β-二酮和水滑石,各组分的重量份之比为:硬脂酸钙、硬脂酸锌、β-二酮和水滑石=0.1-10:0.1-10:0.1-10:0.1-10,优选为硬脂酸钙、硬脂酸锌、β-二酮和水滑石=0.4-0.8:0.4-0.8:0.1-0.5:0.5-4,所述水滑石为的型号为HT-1,供应商为日本堺化学株式会社。In the foamed PVC material provided by the present invention, 1-8 parts by weight, preferably 1-6 parts of stabilizer, are included in parts by weight, and those skilled in the art can adjust the plasticizer according to the process and the use environment. Dosage. The stabilizer includes a PVC heat stabilizer and an acid acceptor, and preferred PVC heat stabilizers include, but are not limited to, calcium stearate, zinc stearate, β-diketone (stearoylbenzoylmethane), diphenyl. A combination of one or more of formylmethane, preferred acid acceptors include, but are not limited to, hydrotalcite, which is preferably Mg 4 Al 2 (OH) 12 CO 3 .3H 2 O. In a preferred embodiment of the present invention, the stabilizer comprises calcium stearate, zinc stearate, β-diketone and hydrotalcite, and the ratio by weight of each component is: calcium stearate, stearic acid Zinc, β-diketone and hydrotalcite = 0.10-1: 0.1-10: 0.1-10: 0.1-10, preferably calcium stearate, zinc stearate, β-diketone and hydrotalcite = 0.4-0.8: 0.4-0.8: 0.1-0.5: 0.5-4, the hydrotalcite is of the type HT-1, and the supplier is Nippon Chemical Co., Ltd.
防霉抗菌剂Anti-mold antibacterial agent
在本发明所提供的发泡PVC材料中,还可包括如防霉抗菌剂0.1-0.5份。所述防霉抗菌剂的种类没有特殊限制,只要不对本发明的发明目的产生限制即可。具体可使用的防霉抗菌剂包括但不限于噻苯咪唑。In the foamed PVC material provided by the present invention, 0.1 to 0.5 parts of an antifungal antibacterial agent may also be included. The kind of the anti-mold antibacterial agent is not particularly limited as long as it does not limit the object of the present invention. Specific anti-fungal antibacterial agents that can be used include, but are not limited to, thiabendazole.
改性剂Modifier
在本发明所提供的发泡PVC材料中,按重量份计,还可以包括改性剂3-15份,优选可以包括改性剂5-15份。所述改性剂可以是包括但不限于MBS、丁腈橡胶、丙烯酸酯弹性体等中的一种或多种的组合。所述MBS为甲基丙烯酸甲酯(M)、丁二烯(B)及苯乙烯(S)的三元共聚物,所述MBS中单体的比例可以为B:S=50-70:30-50,更具体可以为M:B:S=20-40:35-55:20-40;所述丁腈橡胶(丁腈弹性体)为丁二烯和丙烯腈共聚合制得预交联结构的弹性体(橡胶),所述丁腈橡胶中丙烯腈单体的含量可以为23-43%,更具体可以为28-38%,门尼粘度ML1+4,100℃可以为37-77,更具体可以为47-67,在本发明一实施例中,所述丁腈橡胶为P-83,供应商为法国欧诺法化学。所述丙烯酸酯弹性体(丙烯酸酯橡胶)为 以丙烯酸酯为主单体经共聚而得预交联结构的弹性体,所述丙烯酸酯弹性体为门尼粘度ML1+4,150℃可以为15-35,更具体可以为20-30,在本发明一实施例中,所述丙烯酸酯弹性体为P-95,供应商为法国欧诺法化学。In the foamed PVC material provided by the present invention, 3 to 15 parts by weight of the modifier may be further included, and preferably 5 to 15 parts of the modifier may be included. The modifier may be a combination of one or more of, including but not limited to, MBS, nitrile rubber, acrylate elastomer, and the like. The MBS is a terpolymer of methyl methacrylate (M), butadiene (B) and styrene (S), and the ratio of the monomers in the MBS may be B: S=50-70:30 -50, more specifically M: B: S = 20-40: 35-55: 20-40; the nitrile rubber (butyronitrile elastomer) is pre-crosslinked by copolymerization of butadiene and acrylonitrile The structural elastomer (rubber), the content of the acrylonitrile monomer in the nitrile rubber may be 23-43%, more specifically 28-38%, the Mooney viscosity ML1+4, 100 ° C may be 37-77, Specifically, it may be 47-67. In an embodiment of the invention, the nitrile rubber is P-83, and the supplier is French Onofrio Chemical. The acrylate elastomer (acrylate rubber) is An elastomer having a pre-crosslinked structure obtained by copolymerization of an acrylate-based monomer, the acrylate elastomer having a Mooney viscosity ML1+4, 150 ° C may be 15-35, more specifically 20-30, in the present invention In one embodiment, the acrylate elastomer is P-95 and the supplier is French Onofrio Chemical.
本发明进一步提供所述发泡PVC材料的制备方法,在制备过程中对加工温度进行必要的控制,发泡剂是不会分解的,具体包括如下步骤:The invention further provides a preparation method of the foamed PVC material, which performs necessary control on the processing temperature during the preparation process, and the foaming agent does not decompose, specifically comprising the following steps:
1)将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂进行混合;1) mixing polyvinyl chloride, a filler, an antioxidant, a lubricant, and a stabilizer;
2)在室温下将适量增塑剂与步骤1所得物料进行混合;2) mixing an appropriate amount of plasticizer with the material obtained in step 1 at room temperature;
3)在70-90℃下将剩余增塑剂与步骤2所得物料进行混合;3) mixing the remaining plasticizer with the material obtained in step 2 at 70-90 ° C;
为了让树脂粉很好的吸收增塑剂,所以在刚开机室温(优选为5-35℃)状态下少量加入增塑剂让树脂粉吸收,当温度提升到80℃左右时将剩余的增塑剂全部加入混料锅中让树脂粉有充足的时间吸收混合。In order to allow the resin powder to absorb the plasticizer well, a small amount of plasticizer is added to allow the resin powder to be absorbed at room temperature (preferably 5-35 ° C), and the remaining plasticization is carried out when the temperature is raised to about 80 ° C. All the agents are added to the mixing pot to allow the resin powder to have sufficient time to absorb and mix.
本领域技术人员可根据实际应用情况调整步骤2和步骤3中分批加入的增塑剂的重量比,优选的,所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:2-5。A person skilled in the art can adjust the weight ratio of the plasticizers added in steps 2 and 3 according to the actual application. Preferably, the weight ratio of the plasticizer added in the steps 2 and 3 is preferably 1. : 2-5.
4)在125-135℃下将加工助剂与步骤3所得物料进行混合;4) mixing the processing aid with the material obtained in step 3 at 125-135 ° C;
当发泡PVC材料中还包括改性剂时,所述步骤4中,可以将加工助剂和改性剂与步骤3所得物料进行混合。When the modifier is further included in the foamed PVC material, in the step 4, the processing aid and the modifier may be mixed with the material obtained in the step 3.
5)将步骤4所得物料冷却至90-110℃,加入发泡剂并混合;5) cooling the material obtained in step 4 to 90-110 ° C, adding a blowing agent and mixing;
整个物料混合过程中,物料体系的温度不超过140℃。During the entire material mixing process, the temperature of the material system does not exceed 140 °C.
所述步骤4和5中,将加工助剂与步骤3所得物料进行混合,由于混料锅的高速混合,混合过程中物料会升温,待温度升至130-140℃时,通过冷却体系(冷却水)将物料冷却至90-110℃,加入发泡剂并混合3分钟,混合过程中保持体系温度在90-110℃。In the steps 4 and 5, the processing aid is mixed with the material obtained in the step 3. Because of the high-speed mixing of the mixing pot, the material will heat up during the mixing process, and the cooling system (cooling) is adopted when the temperature is raised to 130-140 ° C. Water) The material was cooled to 90-110 ° C, the blowing agent was added and mixed for 3 minutes, and the temperature of the system was maintained at 90-110 ° C during the mixing.
6)将步骤5所得物料进行密炼,并将密炼所得的物料挤出造粒,即得所述发泡PVC材料。6) The material obtained in the step 5 is subjected to internal hardening, and the material obtained by the kneading is extruded and granulated to obtain the foamed PVC material.
在本发明一实施例中,密炼的具体条件为三段密炼,以温度和转速进行控制,三段密炼的温度分别为80-90℃/30-40rpm、100-110℃/35-45rpm、110-120℃/30-40rpm,挤出造粒时温度≤115℃,优选的温度为90-115℃。In an embodiment of the present invention, the specific conditions of the mixing are three-stage mixing, controlled by temperature and rotation speed, and the three-stage mixing temperature is 80-90 ° C / 30-40 rpm, 100-110 ° C / 35- 45 rpm, 110-120 ° C / 30-40 rpm, the temperature at the time of extrusion granulation is ≤ 115 ° C, and the preferred temperature is 90-115 ° C.
在本发明一实施例中,各物料的混合在高速混料锅中进行,各步骤中,混合时的具体条件分别为:In an embodiment of the present invention, the mixing of the materials is carried out in a high-speed mixing pan. In each step, the specific conditions for mixing are as follows:
1)将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂进行混合;1) mixing polyvinyl chloride, a filler, an antioxidant, a lubricant, and a stabilizer;
2)在5-35℃下将适量增塑剂与步骤1所得物料进行混合;2) mixing an appropriate amount of plasticizer with the material obtained in step 1 at 5-35 ° C;
3)在70-90℃下将剩余增塑剂与步骤2所得物料进行混合; 3) mixing the remaining plasticizer with the material obtained in step 2 at 70-90 ° C;
4)所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:2-5。4) The weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:2-5.
5)在125-135℃下将加工助剂与步骤3所得物料进行混合,当体系温度升至130-140℃时,将物料冷却至90-110℃,加入发泡剂并混合3分钟。5) The processing aid is mixed with the material obtained in the step 3 at 125-135 ° C. When the temperature of the system is raised to 130-140 ° C, the material is cooled to 90-110 ° C, the blowing agent is added and mixed for 3 minutes.
本发明进一步提供所述发泡PVC材料在制备PVC门封料中的用途。The invention further provides the use of the foamed PVC material in the preparation of a PVC door seal.
优选的,所述发泡PVC材料在制备冰箱用PVC门封料中的用途。本发明所提供的发泡PVC材料尤其适合制备冰箱用PVC门封料,所述门封料通过添加发泡剂在PVC内部引入大量的微气泡,在显著提升材料隔热性能的同时,还保证了材料的各项力学性能,适用于冰箱门封料的复杂结构和使用环境。Preferably, the foamed PVC material is used in the preparation of a PVC door seal for a refrigerator. The foamed PVC material provided by the invention is particularly suitable for preparing PVC door sealing material for refrigerators, and the door sealing material introduces a large amount of micro-bubbles inside the PVC by adding a foaming agent, thereby significantly improving the heat insulating performance of the material while ensuring The mechanical properties of the material are suitable for the complex structure and use environment of the refrigerator door seal.
本发明进一步提供一种发泡PVC门封料,由所述发泡PVC材料制备获得。The invention further provides a foamed PVC door seal material obtained by preparing the foamed PVC material.
所述发泡PVC材料中,偶氮二甲酰胺没有分解,在使用所述发泡PVC材料制备发泡PVC门封料的制备过程中,偶氮二甲酰胺分解发泡。In the foamed PVC material, azodicarbonamide is not decomposed, and during the preparation process of preparing the foamed PVC door sealant using the foamed PVC material, azodicarbonamide is decomposed and foamed.
本发明中,所述发泡PVC门封料可通过本领域各种押出机,由所述发泡PVC材料制备获得。加工过程中,加工温度优选为115-170℃,在本发明一实施例中,加工温度为140-158℃,在本发明一实施例中,加工温度为150-168℃。本领域技术人员可根据设备、工艺和使用环境的不同(具体如押出机的不同直径、不同的加工温度等),对停留时间进行调整,以获得合适的发泡率,所述发泡PVC门封料优选的发泡率为13-40%。In the present invention, the foamed PVC door seal can be obtained from the foamed PVC material by various extruders in the art. During processing, the processing temperature is preferably from 115 to 170 ° C. In one embodiment of the invention, the processing temperature is from 140 to 158 ° C. In one embodiment of the invention, the processing temperature is from 150 to 168 ° C. Those skilled in the art can adjust the residence time according to different equipment, process and use environment (specifically, different diameters of the extruder, different processing temperatures, etc.) to obtain a suitable foaming rate. The preferred foaming ratio of the sealant is 13-40%.
如上所述,本发明所提供的发泡PVC材料,在经押出机封条成型时,通过停留时间和加工温度控制获得了合适的发泡率,有效的节约社会资源、减少成本,并使封条的导热系数明显下降,同时,制备所获得材料依然具有良好的力学性能。As described above, the foamed PVC material provided by the present invention obtains a suitable foaming rate by controlling the residence time and the processing temperature when being formed by the seal of the extruder, effectively saving social resources, reducing costs, and making the seals The thermal conductivity is significantly reduced, and at the same time, the material obtained by the preparation still has good mechanical properties.
以下通过特定的具体实例说明本发明的实施方式,本领域技术人员可由本说明书所揭露的内容轻易地了解本发明的其他优点与功效。本发明还可以通过另外不同的具体实施方式加以实施或应用,本说明书中的各项细节也可以基于不同观点与应用,在没有背离本发明的精神下进行各种修饰或改变。The embodiments of the present invention are described below by way of specific examples, and those skilled in the art can readily understand other advantages and effects of the present invention from the disclosure of the present disclosure. The present invention may be embodied or applied in various other specific embodiments, and various modifications and changes can be made without departing from the spirit and scope of the invention.
须知,下列实施例中未具体注明的工艺设备或装置均采用本领域内的常规设备或装置。It should be noted that the process equipment or apparatus not specifically noted in the following examples employ conventional equipment or apparatus in the art.
此外应理解,本发明中提到的一个或多个方法步骤并不排斥在所述组合步骤前后还可以存在其他方法步骤或在这些明确提到的步骤之间还可以插入其他方法步骤,除非另有说明;还应理解,本发明中提到的一个或多个设备/装置之间的组合连接关系并不排斥在所述组合设备/装置前后还可以存在其他设备/装置或在这些明确提到的两个设备/装置之间还可以插入其他设备/装置,除非另有说明。而且,除非另有说明,各方法步骤的编号仅为鉴别各方法步骤的便利工具,而非为限制各方法步骤的排列次序或限定本发明可实施的范围,其相对关系的改变或调整,在无实质变更技术内容的情况下,当亦视为本发明可实施的范畴。 In addition, it should be understood that one or more of the method steps recited in the present invention are not exclusive of other method steps that may be present before or after the combination step, or that other method steps can be inserted between the steps specifically mentioned, unless otherwise It should be understood that the combined connection relationship between one or more devices/devices referred to in the present invention does not exclude that other devices/devices may exist before or after the combined device/device or Other devices/devices can also be inserted between the two devices/devices unless otherwise stated. Moreover, unless otherwise indicated, the numbering of each method step is merely a convenient means of identifying the various method steps, and is not intended to limit the order of the various method steps or to limit the scope of the invention, the relative In the case where the technical content is not substantially changed, it is considered to be a scope in which the present invention can be implemented.
具体实例中所使用的产品信息如下:The product information used in the specific examples is as follows:
Figure PCTCN2016102868-appb-000006
Figure PCTCN2016102868-appb-000006
实施例1Example 1
发泡PVC门封料的制备方法如下:The preparation method of the foamed PVC door sealing material is as follows:
1)按表1中的配方,将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂加入高速混料锅中进行混合;1) According to the formula in Table 1, the polyvinyl chloride, the filler, the antioxidant, the lubricant and the stabilizer are added to the high-speed mixing pot for mixing;
2)在高速混合60±20秒后将适量增塑剂与步骤1所得物料进行混合,混合温度为室温;2) After mixing at a high speed for 60±20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
3)在80℃下将剩余增塑剂与步骤2所得物料进行混合;3) mixing the remaining plasticizer with the material obtained in step 2 at 80 ° C;
所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:4。The weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
4)在130℃下将加工助剂与步骤3所得物料进行混合;4) mixing the processing aid with the material obtained in step 3 at 130 ° C;
5)在135℃停机;5) Stop at 135 ° C;
6)开冷却水进行冷却,将物料冷却至90-110℃,加入发泡剂并混合3分钟;(未发泡品无此步骤)6) Cooling water is cooled, the material is cooled to 90-110 ° C, foaming agent is added and mixed for 3 minutes; (unexpanded product does not have this step)
7)将所得物料进行密炼,密炼的具体条件为三段密炼,以温度进行控制,分别为85℃/35rpm、105℃/40rpm、115℃/35rpm,将密炼所得的物料在90-115℃下挤出造粒;7) The obtained materials are mixed, and the specific conditions of the mixing are three-stage mixing and controlled by temperature, which are 85 ° C / 35 rpm, 105 ° C / 40 rpm, 115 ° C / 35 rpm, and the materials obtained by the mixing are at 90. Extrusion granulation at -115 ° C;
将步骤7所得粒料通过φ20mm押出试验机制备发泡PVC门封料的样条,加工温度为140℃-158℃;The pellet obtained in the step 7 is passed through a φ20 mm extrusion test machine to prepare a spline of the foamed PVC door sealing material, and the processing temperature is 140 ° C - 158 ° C;
押出机转速:30rpm、停留时间:2min。Extruder speed: 30 rpm, residence time: 2 min.
表1Table 1
Figure PCTCN2016102868-appb-000007
Figure PCTCN2016102868-appb-000007
Figure PCTCN2016102868-appb-000008
Figure PCTCN2016102868-appb-000008
将上述制备获得的样条进行性能测试,具体结果如表2所示:The splines obtained in the above preparation were tested for performance. The specific results are shown in Table 2:
拉伸强度按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
断裂伸长率按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
比重按照JIS K 7112A规定进行;The specific gravity is in accordance with JIS K 7112A;
导热系数按照公式用热扩散系数、定压比热容、比重参与计算所得。The thermal conductivity is calculated according to the formula using thermal diffusivity, constant pressure specific heat capacity, and specific gravity.
表2Table 2
Figure PCTCN2016102868-appb-000009
Figure PCTCN2016102868-appb-000009
相关公式:导热系数=热扩散系数*定压比热容*比重 Related formula: thermal conductivity = thermal diffusivity * constant pressure specific heat capacity * specific gravity
发泡率=未发泡品比重/发泡品比重-1Foaming rate = specific gravity of unfoamed product / specific gravity of foamed product -1
实施例2Example 2
发泡PVC门封料的制备方法如下:The preparation method of the foamed PVC door sealing material is as follows:
1)按表3中的配方,将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂加入高速混料锅中进行混合;1) According to the formula in Table 3, the polyvinyl chloride, the filler, the antioxidant, the lubricant and the stabilizer are added to the high-speed mixing pot for mixing;
2)在℃高速混合60秒±20后将适量增塑剂与步骤1所得物料进行混合;2) mixing a suitable amount of plasticizer with the material obtained in step 1 after mixing at a high speed of ° C for 60 seconds ± 20;
3)在80℃下将剩余增塑剂与步骤2所得物料进行混合;3) mixing the remaining plasticizer with the material obtained in step 2 at 80 ° C;
所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:4。The weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
4)在130℃下将加工助剂与步骤3所得物料进行混合;4) mixing the processing aid with the material obtained in step 3 at 130 ° C;
5)在135℃停机;5) Stop at 135 ° C;
6)开冷却水进行冷却,将物料冷却至90-110℃,加入发泡剂并混合3分钟;(未发泡品无此步骤)6) Cooling water is cooled, the material is cooled to 90-110 ° C, foaming agent is added and mixed for 3 minutes; (unexpanded product does not have this step)
7)将所得物料进行密炼,密炼的具体条件为三段密炼,以温度进行控制,分别为85℃/35rpm、105℃/40rpm、115℃/35rpm,将密炼所得的物料在90-115℃下挤出造粒;7) The obtained materials are mixed, and the specific conditions of the mixing are three-stage mixing and controlled by temperature, which are 85 ° C / 35 rpm, 105 ° C / 40 rpm, 115 ° C / 35 rpm, and the materials obtained by the mixing are at 90. Extrusion granulation at -115 ° C;
将步骤7所得粒料通过φ20mm押出试验机制备发泡PVC门封料的样条,加工温度为140-158℃;The pellet obtained in the step 7 is passed through a φ20 mm extrusion test machine to prepare a spline of the foamed PVC door sealing material, and the processing temperature is 140-158 ° C;
押出机转速:30rpm、停留时间:2min。Extruder speed: 30 rpm, residence time: 2 min.
表3table 3
Figure PCTCN2016102868-appb-000010
Figure PCTCN2016102868-appb-000010
Figure PCTCN2016102868-appb-000011
Figure PCTCN2016102868-appb-000011
将上述制备获得的样条进行性能测试,具体结果如表4所示:The splines obtained in the above preparation were tested for performance. The specific results are shown in Table 4:
拉伸强度按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
断裂伸长率按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
比重按照JIS K 7112A规定进行;The specific gravity is in accordance with JIS K 7112A;
导热系数按照公式用热扩散系数、定压比热容、比重参与计算所得。The thermal conductivity is calculated according to the formula using thermal diffusivity, constant pressure specific heat capacity, and specific gravity.
表4Table 4
Figure PCTCN2016102868-appb-000012
Figure PCTCN2016102868-appb-000012
相关公式:导热系数=热扩散系数*定压比热容*比重Related formula: thermal conductivity = thermal diffusivity * constant pressure specific heat capacity * specific gravity
发泡率=未发泡品比重/发泡品比重-1Foaming rate = specific gravity of unfoamed product / specific gravity of foamed product -1
实施例3Example 3
发泡PVC门封料的制备方法如下:The preparation method of the foamed PVC door sealing material is as follows:
1)按表5中的配方,将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂加入高速混料锅中进行混合;1) according to the formula in Table 5, the polyvinyl chloride, filler, antioxidant, lubricant, stabilizer is added to the high-speed mixing pot for mixing;
2)在高速混合60±20秒后将适量增塑剂与步骤1所得物料进行混合,混合温度为室温;2) After mixing at a high speed for 60±20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
3)在70℃下将剩余增塑剂与步骤2所得物料进行混合;3) mixing the remaining plasticizer with the material obtained in step 2 at 70 ° C;
所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:2。 The weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:2.
4)在125℃下将加工助剂与步骤3所得物料进行混合;4) mixing the processing aid with the material obtained in step 3 at 125 ° C;
5)在135℃停机;5) Stop at 135 ° C;
6)开冷却水进行冷却,将物料冷却至90-110℃,加入发泡剂并混合3分钟;(未发泡品无此步骤)6) Cooling water is cooled, the material is cooled to 90-110 ° C, foaming agent is added and mixed for 3 minutes; (unexpanded product does not have this step)
7)将所得物料进行密炼,密炼的具体条件为三段密炼,以温度进行控制,分别为80℃/30rpm、110℃/45rpm、120℃/40rpm,将密炼所得的物料在90-115℃下挤出造粒;7) The obtained materials are mixed, and the specific conditions of the mixing are three-stage mixing and controlled by temperature, which are 80 ° C / 30 rpm, 110 ° C / 45 rpm, 120 ° C / 40 rpm, and the materials obtained by the mixing are 90. Extrusion granulation at -115 ° C;
将步骤7所得粒料通过φ20mm押出试验机制备发泡PVC门封料的样条,加工温度为140-158℃;The pellet obtained in the step 7 is passed through a φ20 mm extrusion test machine to prepare a spline of the foamed PVC door sealing material, and the processing temperature is 140-158 ° C;
押出机转速:30rpm、停留时间:2min。Extruder speed: 30 rpm, residence time: 2 min.
表5table 5
Figure PCTCN2016102868-appb-000013
Figure PCTCN2016102868-appb-000013
将上述制备获得的样条进行性能测试,具体结果如表6所示:The splines obtained in the above preparation were tested for performance. The specific results are shown in Table 6:
拉伸强度按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
断裂伸长率按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
比重按照JIS K 7112A规定进行;The specific gravity is in accordance with JIS K 7112A;
导热系数按照公式用热扩散系数、定压比热容、比重参与计算所得。 The thermal conductivity is calculated according to the formula using thermal diffusivity, constant pressure specific heat capacity, and specific gravity.
表6Table 6
Figure PCTCN2016102868-appb-000014
Figure PCTCN2016102868-appb-000014
相关公式:导热系数=热扩散系数*定压比热容*比重Related formula: thermal conductivity = thermal diffusivity * constant pressure specific heat capacity * specific gravity
发泡率=未发泡品比重/发泡品比重-1Foaming rate = specific gravity of unfoamed product / specific gravity of foamed product -1
实施例4Example 4
发泡PVC门封料的制备方法如下:The preparation method of the foamed PVC door sealing material is as follows:
1)按表7中的配方,将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂加入高速混料锅中进行混合;1) According to the formula in Table 7, the polyvinyl chloride, the filler, the antioxidant, the lubricant and the stabilizer are added to the high-speed mixing pot for mixing;
2)在高速混合60±20秒后将适量增塑剂与步骤1所得物料进行混合,混合温度为室温;2) After mixing at a high speed for 60±20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
3)在90℃下将剩余增塑剂与步骤2所得物料进行混合;3) mixing the remaining plasticizer with the material obtained in step 2 at 90 ° C;
所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:5。The weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:5.
4)在135℃下将加工助剂与步骤3所得物料进行混合;4) mixing the processing aid with the material obtained in step 3 at 135 ° C;
5)在140℃停机;5) Stop at 140 °C;
6)开冷却水进行冷却,将物料冷却至90-110℃,加入发泡剂并混合3分钟;(未发泡品无此步骤)6) Cooling water is cooled, the material is cooled to 90-110 ° C, foaming agent is added and mixed for 3 minutes; (unexpanded product does not have this step)
7)将所得物料进行密炼,密炼的具体条件为三段密炼,以温度进行控制,分别为90℃/40rpm、100℃/35rpm、110℃/30rpm,将密炼所得的物料在90-115℃下挤出造粒;7) The obtained materials are mixed, and the specific conditions of the mixing are three-stage mixing, controlled by temperature, respectively, at 90 ° C / 40 rpm, 100 ° C / 35 rpm, 110 ° C / 30 rpm, and the materials obtained by the mixing are at 90 Extrusion granulation at -115 ° C;
将步骤7所得粒料通过φ20mm押出试验机制备发泡PVC门封料的样条,加工温度为140-158℃;The pellet obtained in the step 7 is passed through a φ20 mm extrusion test machine to prepare a spline of the foamed PVC door sealing material, and the processing temperature is 140-158 ° C;
押出机转速:30rpm、停留时间:2min。Extruder speed: 30 rpm, residence time: 2 min.
表7 Table 7
Figure PCTCN2016102868-appb-000015
Figure PCTCN2016102868-appb-000015
将上述制备获得的样条进行性能测试,具体结果如表8所示:The splines obtained in the above preparation were tested for performance. The specific results are shown in Table 8:
拉伸强度按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
断裂伸长率按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
比重按照JIS K 7112A规定进行;The specific gravity is in accordance with JIS K 7112A;
导热系数按照公式用热扩散系数、定压比热容、比重参与计算所得。The thermal conductivity is calculated according to the formula using thermal diffusivity, constant pressure specific heat capacity, and specific gravity.
表8Table 8
Figure PCTCN2016102868-appb-000016
Figure PCTCN2016102868-appb-000016
Figure PCTCN2016102868-appb-000017
Figure PCTCN2016102868-appb-000017
相关公式:导热系数=热扩散系数*定压比热容*比重Related formula: thermal conductivity = thermal diffusivity * constant pressure specific heat capacity * specific gravity
发泡率=未发泡品比重/发泡品比重-1Foaming rate = specific gravity of unfoamed product / specific gravity of foamed product -1
实施例5Example 5
冰箱门封的制备方法如下:The preparation method of the refrigerator door seal is as follows:
1)按表9中的配方,将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂加入高速混料锅中进行混合;1) According to the formula in Table 9, the polyvinyl chloride, the filler, the antioxidant, the lubricant and the stabilizer are added to the high-speed mixing pot for mixing;
2)在高速混合60±20秒后将适量增塑剂与步骤1所得物料进行混合,混合温度为室温;2) After mixing at a high speed for 60±20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
3)在80℃下将剩余增塑剂与步骤2所得物料进行混合;3) mixing the remaining plasticizer with the material obtained in step 2 at 80 ° C;
所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:4。The weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
4)在130℃下将加工助剂和改性剂与步骤3所得物料进行混合;4) mixing the processing aid and the modifier with the material obtained in step 3 at 130 ° C;
5)在135℃停机;5) Stop at 135 ° C;
6)开冷却水进行冷却,将物料冷却至90-110℃,加入发泡剂并混合3分钟;(未发泡品无此步骤)6) Cooling water is cooled, the material is cooled to 90-110 ° C, foaming agent is added and mixed for 3 minutes; (unexpanded product does not have this step)
7)将所得物料进行密炼,密炼的具体条件为三段密炼,以温度进行控制,分别为85℃/35rpm、105℃/40rpm、115℃/35rpm,将密炼所得的物料在90-115℃下挤出造粒;7) The obtained materials are mixed, and the specific conditions of the mixing are three-stage mixing and controlled by temperature, which are 85 ° C / 35 rpm, 105 ° C / 40 rpm, 115 ° C / 35 rpm, and the materials obtained by the mixing are at 90. Extrusion granulation at -115 ° C;
将步骤7所得粒料通过φ20mm押出试验机制备冰箱门封的样条,加工温度为140-158℃;The pellet obtained in step 7 is passed through a φ20 mm extrusion test machine to prepare a spline of the refrigerator door seal, and the processing temperature is 140-158 ° C;
押出机转速:30rpm、停留时间:2min。Extruder speed: 30 rpm, residence time: 2 min.
表9Table 9
Figure PCTCN2016102868-appb-000018
Figure PCTCN2016102868-appb-000018
Figure PCTCN2016102868-appb-000019
Figure PCTCN2016102868-appb-000019
将上述制备获得的样条进行性能测试,具体结果如表10所示:The splines obtained in the above preparation were tested for performance. The specific results are shown in Table 10:
拉伸强度按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
断裂伸长率按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
比重按照JIS K 7112A规定进行;The specific gravity is in accordance with JIS K 7112A;
表10Table 10
Figure PCTCN2016102868-appb-000020
Figure PCTCN2016102868-appb-000020
相关公式:导热系数=热扩散系数*定压比热容*比重Related formula: thermal conductivity = thermal diffusivity * constant pressure specific heat capacity * specific gravity
发泡率=未发泡品比重/发泡品比重-1Foaming rate = specific gravity of unfoamed product / specific gravity of foamed product -1
实施例6Example 6
冰箱门封的制备方法如下: The preparation method of the refrigerator door seal is as follows:
1)按表11中的配方,将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂加入高速混料锅中进行混合;1) According to the formula in Table 11, the polyvinyl chloride, the filler, the antioxidant, the lubricant and the stabilizer are added to the high-speed mixing pot for mixing;
2)在高速混合60±20秒后将适量增塑剂与步骤1所得物料进行混合,混合温度为室温;2) After mixing at a high speed for 60±20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
3)在80℃下将剩余增塑剂与步骤2所得物料进行混合;3) mixing the remaining plasticizer with the material obtained in step 2 at 80 ° C;
所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:4。The weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
4)在130℃下将加工助剂和改性剂与步骤3所得物料进行混合;4) mixing the processing aid and the modifier with the material obtained in step 3 at 130 ° C;
5)在135℃停机;5) Stop at 135 ° C;
6)开冷却水进行冷却,将物料冷却至90-110℃,加入发泡剂并混合3分钟;(未发泡品无此步骤)6) Cooling water is cooled, the material is cooled to 90-110 ° C, foaming agent is added and mixed for 3 minutes; (unexpanded product does not have this step)
7)将所得物料进行密炼,密炼的具体条件为三段密炼,以温度进行控制,分别为85℃/35rpm、105℃/40rpm、115℃/35rpm,将密炼所得的物料在90-115℃下挤出造粒;7) The obtained materials are mixed, and the specific conditions of the mixing are three-stage mixing and controlled by temperature, which are 85 ° C / 35 rpm, 105 ° C / 40 rpm, 115 ° C / 35 rpm, and the materials obtained by the mixing are at 90. Extrusion granulation at -115 ° C;
将步骤7所得粒料通过φ20mm押出试验机制备冰箱门封的样条,加工温度为140-158℃;The pellet obtained in step 7 is passed through a φ20 mm extrusion test machine to prepare a spline of the refrigerator door seal, and the processing temperature is 140-158 ° C;
押出机转速:30rpm、停留时间:2min。Extruder speed: 30 rpm, residence time: 2 min.
表11Table 11
Figure PCTCN2016102868-appb-000021
Figure PCTCN2016102868-appb-000021
Figure PCTCN2016102868-appb-000022
Figure PCTCN2016102868-appb-000022
将上述制备获得的样条进行性能测试,具体结果如表12所示:The splines obtained in the above preparation were tested for performance. The specific results are shown in Table 12:
拉伸强度按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
断裂伸长率按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
比重按照JIS K 7112A规定进行;The specific gravity is in accordance with JIS K 7112A;
表12Table 12
Figure PCTCN2016102868-appb-000023
Figure PCTCN2016102868-appb-000023
相关公式:导热系数=热扩散系数*定压比热容*比重Related formula: thermal conductivity = thermal diffusivity * constant pressure specific heat capacity * specific gravity
发泡率=未发泡品比重/发泡品比重-1Foaming rate = specific gravity of unfoamed product / specific gravity of foamed product -1
实施例7Example 7
冰箱门封的制备方法如下:The preparation method of the refrigerator door seal is as follows:
1)按表13中的配方,将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂加入高速混料锅中进行混合;1) According to the formula in Table 13, the polyvinyl chloride, the filler, the antioxidant, the lubricant and the stabilizer are added to the high-speed mixing pot for mixing;
2)在高速混合60±20秒后将适量增塑剂与步骤1所得物料进行混合,混合温度为室温;2) After mixing at a high speed for 60±20 seconds, an appropriate amount of plasticizer is mixed with the material obtained in step 1, and the mixing temperature is room temperature;
3)在80℃下将剩余增塑剂与步骤2所得物料进行混合;3) mixing the remaining plasticizer with the material obtained in step 2 at 80 ° C;
所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:4。 The weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:4.
4)在130℃下将加工助剂和改性剂与步骤3所得物料进行混合;4) mixing the processing aid and the modifier with the material obtained in step 3 at 130 ° C;
5)在135℃停机;5) Stop at 135 ° C;
6)开冷却水进行冷却,将物料冷却至90-110℃,加入发泡剂并混合3分钟;(未发泡品无此步骤)6) Cooling water is cooled, the material is cooled to 90-110 ° C, foaming agent is added and mixed for 3 minutes; (unexpanded product does not have this step)
7)将所得物料进行密炼,密炼的具体条件为三段密炼,以温度进行控制,分别为85℃/35rpm、105℃/40rpm、115℃/35rpm,将密炼所得的物料在90-115℃下挤出造粒;7) The obtained materials are mixed, and the specific conditions of the mixing are three-stage mixing and controlled by temperature, which are 85 ° C / 35 rpm, 105 ° C / 40 rpm, 115 ° C / 35 rpm, and the materials obtained by the mixing are at 90. Extrusion granulation at -115 ° C;
将步骤7所得粒料通过φ20mm押出试验机制备冰箱门封的样条,加工温度为150-168℃;The pellet obtained in step 7 is passed through a φ20 mm extrusion test machine to prepare a spline of the refrigerator door seal, and the processing temperature is 150-168 ° C;
押出机转速:30rpm、停留时间:2min。Extruder speed: 30 rpm, residence time: 2 min.
表13Table 13
Figure PCTCN2016102868-appb-000024
Figure PCTCN2016102868-appb-000024
将上述制备获得的样条进行性能测试,具体结果如表14所示:The splines obtained in the above preparation were tested for performance. The specific results are shown in Table 14:
拉伸强度按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The tensile strength is in accordance with JIS K 6723 6.3, and the tensile speed is 200 mm/min;
断裂伸长率按照JIS K 6723 6.3规定进行,拉伸速度200mm/min;The elongation at break is carried out in accordance with JIS K 6723 6.3, and the drawing speed is 200 mm/min;
比重按照JIS K 7112A规定进行; The specific gravity is in accordance with JIS K 7112A;
表14Table 14
Figure PCTCN2016102868-appb-000025
Figure PCTCN2016102868-appb-000025
相关公式:导热系数=热扩散系数*定压比热容*比重Related formula: thermal conductivity = thermal diffusivity * constant pressure specific heat capacity * specific gravity
发泡率=未发泡品比重/发泡品比重-1Foaming rate = specific gravity of unfoamed product / specific gravity of foamed product -1
综上所述,本发明有效克服了现有技术中的种种缺点而具高度产业利用价值。In summary, the present invention effectively overcomes various shortcomings in the prior art and has high industrial utilization value.
上述实施例仅例示性说明本发明的原理及其功效,而非用于限制本发明。任何熟悉此技术的人士皆可在不违背本发明的精神及范畴下,对上述实施例进行修饰或改变。因此,举凡所属技术领域中具有通常知识者在未脱离本发明所揭示的精神与技术思想下所完成的一切等效修饰或改变,仍应由本发明的权利要求所涵盖。 The above-described embodiments are merely illustrative of the principles of the invention and its effects, and are not intended to limit the invention. Modifications or variations of the above-described embodiments may be made by those skilled in the art without departing from the spirit and scope of the invention. Therefore, all equivalent modifications or changes made by those skilled in the art without departing from the spirit and scope of the invention will be covered by the appended claims.

Claims (23)

  1. 一种发泡PVC材料,其原料按重量份计,包括如下组分:A foamed PVC material, the raw materials of which include the following components by weight:
    Figure PCTCN2016102868-appb-100001
    Figure PCTCN2016102868-appb-100001
  2. 如权利要求1所述的一种发泡PVC材料,其特征在于,所述聚氯乙烯的聚合度为800-2500,优选为1000-1300。A foamed PVC material according to claim 1, wherein said polyvinyl chloride has a degree of polymerization of from 800 to 2,500, preferably from 1,000 to 1,300.
  3. 如权利要求1所述的一种发泡PVC材料,其特征在于,所述增塑剂选自己二酸类聚酯、偏苯三酸三辛酯、环氧大豆油、对苯二甲酸二辛酯、癸二酸二辛酯、己二酸二辛酯中的一种或多种的组合。A foamed PVC material according to claim 1, wherein said plasticizer is selected from the group consisting of self-acidic polyester, trioctyl trimellitate, epoxidized soybean oil, and dioctyl terephthalate. A combination of one or more of an ester, dioctyl sebacate, and dioctyl adipate.
  4. 如权利要求3所述的一种发泡PVC材料,其特征在于,所述增塑剂为己二酸类聚酯和环氧大豆油的组合,所述增塑剂中,己二酸类聚酯和环氧大豆油的重量比为1:0.1-1.5。A foamed PVC material according to claim 3, wherein said plasticizer is a combination of adipic acid polyester and epoxidized soybean oil, wherein said plasticizer is adipic acid. The weight ratio of ester to epoxidized soybean oil is from 1:0.1 to 1.5.
  5. 如权利要求3所述的一种发泡PVC材料,其特征在于,所述乙二酸类聚酯的粘度为(25℃,Mpa·s)2400-6000,比重为(20/20℃)1.050-1.150,环氧大豆油的环氧值(%)6.0以上,酸值(KOH mg/g)0.5以下。A foamed PVC material according to claim 3, wherein the viscosity of the oxalic acid polyester is (25 ° C, Mpa·s) 2400-6000, and the specific gravity is (20/20 ° C) 1.050. -1.150, the epoxy value (%) of the epoxidized soybean oil is 6.0 or more, and the acid value (KOH mg/g) is 0.5 or less.
  6. 如权利要求1所述的一种发泡PVC材料,其特征在于,所述填充剂为碳酸钙。A foamed PVC material according to claim 1 wherein said filler is calcium carbonate.
  7. 如权利要求1所述的一种发泡PVC材料,其特征在于,所述加工助剂选自丙烯酸类加工助剂和甲基丙烯酸甲酯类加工助剂中的一种或多种的组合。A foamed PVC material according to claim 1 wherein said processing aid is selected from the group consisting of one or more of an acrylic processing aid and a methyl methacrylate processing aid.
  8. 如权利要求7所述的一种发泡PVC材料,其特征在于,所述丙烯酸类加工助剂为甲基丙烯酸甲酯(MMA)/丙烯酸酯共聚物,其重量平均分子量(×104)250以上。A foamed PVC material according to claim 7, wherein said acrylic processing aid is a methyl methacrylate (MMA) / acrylate copolymer having a weight average molecular weight (×10 4 ) of 250 the above.
  9. 如权利要求1所述的一种发泡PVC材料,其特征在于,所述化学发泡剂为有机化学发泡剂。A foamed PVC material according to claim 1 wherein said chemical blowing agent is an organic chemical blowing agent.
  10. 如权利要求9所述的一种发泡PVC材料,其特征在于,所述化学发泡剂选自偶氮二甲酰胺、碳酸氢钠、4,4'-羟基双苯磺酰肼中的一种或多种的组合。A foamed PVC material according to claim 9, wherein said chemical foaming agent is selected from the group consisting of azodicarbonamide, sodium hydrogencarbonate, and 4,4'-hydroxybisbenzenesulfonylhydrazide. Combination of species or multiples.
  11. 如权利要求1所述的一种发泡PVC材料,其特征在于,所述抗氧剂选自抗氧剂1010、抗氧剂168、DLTP中的一种或多种的组合。 A foamed PVC material according to claim 1 wherein said antioxidant is selected from the group consisting of one or more of antioxidant 1010, antioxidant 168, DLTP.
  12. 如权利要求1所述的一种发泡PVC材料,其特征在于,所述稳定剂选自硬脂酸钙、硬脂酸锌、β-二酮、水滑石、稀土稳定剂、有机锡稳定剂、钡锌稳定剂中的一种或多种的组合。A foamed PVC material according to claim 1, wherein said stabilizer is selected from the group consisting of calcium stearate, zinc stearate, beta-diketone, hydrotalcite, rare earth stabilizer, and organotin stabilizer. a combination of one or more of zinc antimony stabilizers.
  13. 如权利要求12所述的一种发泡PVC材料,其特征在于,所述稳定剂包括硬脂酸钙、硬脂酸锌、β-二酮和水滑石,各组分的重量份之比为:硬脂酸钙、硬脂酸锌、β-二酮和水滑石=1-10:1-10:1-10:1-10。A foamed PVC material according to claim 12, wherein said stabilizer comprises calcium stearate, zinc stearate, ?-diketone and hydrotalcite, and the ratio by weight of each component is : calcium stearate, zinc stearate, β-diketone and hydrotalcite = 1-10:1-10:1-10:1-10.
  14. 如权利要求1所述的一种发泡PVC材料,其特征在于,所述发泡PVC材料的原料按重量份计,还包括如防霉抗菌剂0.1-0.5份。A foamed PVC material according to claim 1, wherein the raw material of the foamed PVC material further comprises, for example, 0.1 to 0.5 parts by weight of the antibacterial agent.
  15. 如权利要求1所述的一种发泡PVC材料,其特征在于,所述发泡PVC材料的原料按重量份计,还包括3-15份改性剂。A foamed PVC material according to claim 1, wherein the raw material of the foamed PVC material further comprises, by weight, 3 to 15 parts of a modifier.
  16. 如权利要求15所述的一种发泡PVC材料,其特征在于,所述改性剂选自MBS、丁腈橡胶、丙烯酸酯弹性体中的一种或多种的组合。A foamed PVC material according to claim 15 wherein said modifier is selected from the group consisting of one or more of MBS, nitrile rubber, and acrylate elastomer.
  17. 如权利要求1-16任一权利要求所述的发泡PVC材料的制备方法,包括如下步骤:The method for preparing a foamed PVC material according to any one of claims 1 to 16, comprising the steps of:
    1)将聚氯乙烯、填充剂、抗氧剂、润滑剂、稳定剂进行混合;1) mixing polyvinyl chloride, a filler, an antioxidant, a lubricant, and a stabilizer;
    2)在室温下将适量增塑剂与步骤1所得物料进行混合;2) mixing an appropriate amount of plasticizer with the material obtained in step 1 at room temperature;
    3)在70-90℃下将剩余增塑剂与步骤2所得物料进行混合;3) mixing the remaining plasticizer with the material obtained in step 2 at 70-90 ° C;
    4)在125-135℃下将加工助剂与步骤3所得物料进行混合;4) mixing the processing aid with the material obtained in step 3 at 125-135 ° C;
    5)将步骤4所得物料冷却至90-110℃,加入发泡剂并混合;5) cooling the material obtained in step 4 to 90-110 ° C, adding a blowing agent and mixing;
    6)将步骤5所得物料进行密炼,并将密炼所得的物料挤出造粒,即得所述发泡PVC材料。6) The material obtained in the step 5 is subjected to internal hardening, and the material obtained by the kneading is extruded and granulated to obtain the foamed PVC material.
  18. 如权利要求17所述的制备方法,其特征在于,所述步骤2和步骤3中所加入的增塑剂的重量比优选为1:2-5。The preparation method according to claim 17, wherein the weight ratio of the plasticizer added in the step 2 and the step 3 is preferably 1:2 to 5.
  19. 如权利要求17所述的制备方法,其特征在于,所述步骤4中,将加工助剂和改性剂与步骤3所得物料进行混合。The preparation method according to claim 17, wherein in the step 4, the processing aid and the modifier are mixed with the material obtained in the step 3.
  20. 如权利要求17所述的制备方法,其特征在于,所述步骤6中,密炼的具体条件为三段密炼,以温度和转速进行控制,分别为80-90℃/30-40rpm、100-110℃/35-45rpm、110-120℃/30-40rpm。The preparation method according to claim 17, wherein in the step 6, the specific conditions of the mixing are three-stage mixing, and the temperature and the rotation speed are controlled, respectively, 80-90 ° C / 30-40 rpm, 100. -110 ° C / 35-45 rpm, 110-120 ° C / 30-40 rpm.
  21. 如权利要求17所述的制备方法,其特征在于,所述步骤6中,挤出造粒时的温度为90-115℃。The production method according to claim 17, wherein in the step 6, the temperature at the time of extrusion granulation is from 90 to 115 °C.
  22. 如权利要求1-16任一权利要求所述的发泡PVC材料在制备PVC门封料中的用途。Use of a foamed PVC material according to any of claims 1-16 in the preparation of a PVC door seal.
  23. 如权利要求22所述的用途,其特征在于,所述PVC门封料为冰箱用PVC门封料。 The use according to claim 22, wherein the PVC door seal is a PVC door seal for a refrigerator.
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