CN106167591A - A kind of PVC foam body and manufacture method - Google Patents
A kind of PVC foam body and manufacture method Download PDFInfo
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- CN106167591A CN106167591A CN201610662936.XA CN201610662936A CN106167591A CN 106167591 A CN106167591 A CN 106167591A CN 201610662936 A CN201610662936 A CN 201610662936A CN 106167591 A CN106167591 A CN 106167591A
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- pvc
- foam body
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L27/00—Compositions 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
- C08L27/02—Compositions 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
- C08L27/04—Compositions 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
- C08L27/06—Homopolymers or copolymers of vinyl chloride
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/425—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders using three or more screws
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/435—Sub-screws
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-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
- C08J9/08—Working-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
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-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
- C08J9/10—Working-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
- C08J9/102—Azo-compounds
- C08J9/103—Azodicarbonamide
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/02—CO2-releasing, e.g. NaHCO3 and citric acid
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/04—N2 releasing, ex azodicarbonamide or nitroso compound
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/18—Binary blends of expanding agents
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised 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
- C08J2327/02—Characterised 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
- C08J2327/04—Characterised 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
- C08J2327/06—Homopolymers or copolymers of vinyl chloride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2423/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2423/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2423/04—Homopolymers or copolymers of ethene
- C08J2423/06—Polyethene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2427/00—Characterised 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
- C08J2427/02—Characterised 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
- C08J2427/04—Characterised 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
- C08J2427/06—Homopolymers or copolymers of vinyl chloride
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2203/00—Applications
- C08L2203/14—Applications used for foams
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
- C08L2205/025—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2207/00—Properties characterising the ingredient of the composition
- C08L2207/20—Recycled plastic
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2310/00—Masterbatches
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Molding Of Porous Articles (AREA)
Abstract
The present invention provides a kind of PVC foam body and manufacture method, and the raw material that described PVC foam body uses includes PVC reclaimed materials, foaming agent, stabilizer, lubricant etc., and the quality proportioning of raw material is, PVC reclaimed materials 50 100 parts;Foaming agent 15 parts;Stabilizer 2 10 parts;Lubricant 0.1 1 parts, PVC reclaimed materials is the leftover pieces compound after crushed of PVC foam material.The present invention makes full use of the leftover pieces of PVC foam, cost-effective, reduces and pollutes.Replacing banbury and extruder with planetary extruder, save molding time, energy consumption is low, and yield is high.
Description
Technical field
The present invention relates to a kind of PVC foam body and manufacture method.
Background technology
The leftover pieces of wet type foamed products about 1%-3%, accumulates over a long period, and has large quantities of leftover pieces stocks.PVC wet type relatively
Foaming, PVC dry type foam process is cumbersome, mainly weigh, mix, banburying, extrude, filter, expanding, roll, foam, cold
But, traction etc., spend one technique that the time is most during wherein banburying is whole technique.
Summary of the invention
The technical problem to be solved is to overcome the deficiencies in the prior art, it is provided that a kind of PVC foam body and making
Method.
For solving above technical problem, the present invention adopts the following technical scheme that:
A kind of PVC foam body, the raw material that described PVC foam body uses includes PVC reclaimed materials, foaming agent, stabilizer, lubricant
Deng, the quality proportioning of raw material is
PVC reclaimed materials 50-100 part
Foaming agent 1-5 part
Stabilizer 2-10 part
Lubricant 0.1-1 part,
PVC reclaimed materials is the leftover pieces compound after crushed of PVC foam material.
Preferably, the raw material that described PVC foam body uses also includes PVC powder, plasticizer and colorant, and quality proportioning
For:
PVC powder 0-50 part
Plasticizer 0-50 part.
Preferably, during PVC powder is polyvinyl chloride resin, PVC emulsifying powder, PVC copolymer resin one or more.
Preferably, during plasticizer is DOTP, tributyl 2-acetylcitrate one or both.
Preferably, during foaming agent is azodicarbonamide, sodium bicarbonate one or both.
Preferably, one during stabilizer is solid calcium zinc composite stabilizer, Liquid K zinc composite stabilizer, epoxy soybean oil
Or it is several.
Preferably, one or more during lubricant is Tissuemat E, glyceryl monostearate, stearic acid.
The present invention also provides for the manufacture method of a kind of PVC foam body, and described manufacture method comprises the following steps,
(1) by proportioning, raw material is mixed;(2) planetary extruder plasticizing is used;(3) filter;(4) expanding;(5) calendering;(6) send out
Bubble;(7) cooling and shaping.
Preferably, step (6) is carried out in foaming furnace, and the temperature of foaming furnace is at 180 ~ 220 DEG C.
Preferably, in step (7) a metallic, cooling medium be water or/and gas, the temperature of cooling medium is 20-40 DEG C.
Due to the employing of above technical scheme, the present invention compared with prior art has the advantage that
The present invention makes full use of the leftover pieces of PVC foam, cost-effective, reduces and pollutes.With planetary extruder replace banbury and
Extruder, saves molding time, and energy consumption is low, and yield is high.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention is described in further details.Should be understood that these embodiments are for saying
The ultimate principle of the bright present invention, principal character and advantage, and the present invention is not limited by the scope of following example.Embodiment is adopted
Implementation condition can do further adjustment according to specific requirement, not marked implementation condition is usually the bar in normal experiment
Part.
Below in conjunction with concrete case, patent of the present invention is further described in detail.
Embodiment 1
The quality proportioning of raw material is:
PVC reclaimed materials 100 parts;Azodicarbonamide 4 parts;Calcium-zinc composite stabilizing agent 5 parts;Stearic acid 0.2 part;Tissuemat E 0.2
Part;SG5 type PVC powder 5 parts;DOTP(DOTP) 5 parts;Black masterbatch 2 parts.
Embodiment 2
The quality proportioning of raw material is:
PVC reclaimed materials 100 parts;Azodicarbonamide 3 parts;Sodium bicarbonate 2 parts;Calcium-zinc composite stabilizing agent 4 parts;Glyceryl monostearate
0.3 part;Tissuemat E 0.2 part;Black masterbatch 2 parts.
Embodiment 3
The quality proportioning of raw material is:
PVC reclaimed materials 100 parts;Foaming agent 5 parts;Stabilizer 10 parts;Lubricant 1 part, PVC powder 50 parts;Plasticizer 50 parts.
Embodiment 4
The quality proportioning of raw material is:
PVC reclaimed materials 50 parts;Foaming agent 1 part;Stabilizer 2 parts;Lubricant 0.1 part.
In above-described embodiment, PVC reclaimed materials is the leftover pieces compound after crushed of PVC foam material.
The manufacture method of foaming body, (1) mixes in raw material putting into high-speed mixer by proportioning;(2) by step (1)
The material of gained puts into planetary extruder and plastifies, and uses planetary extruder to plastify.Due to the PVC feed back density used
Low, the charging system of planetary extruder is to force feeding device, can have sufficiently large charging rate, can prevent appearance in hopper
Arch formation, and force to have bottom feeding device chiller, PVC feed back can be avoided to be burnt decomposition in feeding device;
Material is in plasticizing process, and the center bolt of rotation drives planetary-screw rotation, makes material melts plastify, and screw rod and machine barrel
Gap between internal tooth, at 0.2-0.4mm, makes material dispersion evenly, and plasticizing efficiency is high.During plasticizing, each district of planetary extruder
Temperature is at 140-160 DEG C, and extrusion rotating speed 30-50 turns/min.Preferably, the rotating speed 35r/min of planetary extruder, extrusion temperature
155 DEG C, feeding section has adsorbent equipment, the metallics in absorption batch mixing.(3) material of step (2) gained is put into filter
Filter;(4) material of step (3) gained is put into expanding mould and carry out expanding;(5) material of step (4) gained is thrown
Rolling in entering calender, control thickness 2mm, calender is two-roll calendar or tri-roll press machine;(6) by step (5) institute
Material put into dry type stove of firing and foam, foaming furnace each district temperature is at 180-220 DEG C, and hauling speed is 1-15m/min,
Preferably, blowing temperature 190 DEG C, hauling speed 5m/min, stove of firing is open stove of firing;(7) by the thing of step (6) gained
Material puts into cooling chamber and carries out cooling and shaping, the product thickness obtained about 10mm, hardness about 30HD, and density about 0.35 g/cm3 makes
Cooling medium be in water, gas one or both combination, it is ensured that cooling and shaping temperature is at 20-40 DEG C, it is preferable that cooling be situated between
Matter is the air of 25-30 DEG C;(8) material of step (7) gained is carried out rolling according to specification.
The present invention makes full use of the leftover pieces of PVC foam, cost-effective, reduces and pollutes.Banburying is replaced with planetary extruder
Machine and extruder, save molding time, and energy consumption is low, and yield is high.
Above the present invention is described in detail, the explanation of embodiment be only intended to help to understand the method for the present invention and
Its core concept, its object is to allow the personage being familiar with this art will appreciate that present disclosure and to implement according to this, and
Can not limit the scope of the invention with this.All equivalence changes made according to spirit of the invention or modification, all should contain
Cover within protection scope of the present invention.
Claims (10)
1. a PVC foam body, it is characterised in that: the raw material that described PVC foam body uses include PVC reclaimed materials, foaming agent,
Stabilizer, lubricant etc., the quality proportioning of raw material is
PVC reclaimed materials 50-100 part
Foaming agent 1-5 part
Stabilizer 2-10 part
Lubricant 0.1-1 part,
PVC reclaimed materials is the leftover pieces compound after crushed of PVC foam material.
A kind of PVC foam body the most according to claim 1, it is characterised in that: the raw material that described PVC foam body uses is also
Including PVC powder, plasticizer and colorant, and quality proportioning is:
PVC powder 0-50 part
Plasticizer 0-50 part.
PVC foam body the most according to claim 1, it is characterised in that: PVC powder is that polyvinyl chloride resin, PVC emulsifying powder, PVC are common
In poly resin one or more.
PVC foam body the most according to claim 2, it is characterised in that: plasticizer is DOTP, acetyl lemon
In lemon acid tributyl one or both.
PVC foam body the most according to claim 2, it is characterised in that: foaming agent is in azodicarbonamide, sodium bicarbonate one
Plant or two kinds.
PVC foam body the most according to claim 1, it is characterised in that: stabilizer is powder body calcium-zinc composite stabilizing agent, liquid
In potassium zinc composite stabilizer, epoxy soybean oil one or more.
PVC foam body the most according to claim 1, it is characterised in that: lubricant is Tissuemat E, glycerol monostearate
One or more in fat, stearic acid.
8. according to the manufacture method of the PVC foam body described in any one of claim 1 ~ 7, it is characterised in that: described making side
Method comprises the following steps,
(1) by proportioning, raw material is mixed;(2) planetary extruder plasticizing is used;(3) filter;(4) expanding;(5) calendering;(6) send out
Bubble;(7) cooling and shaping.
The manufacture method of PVC foam body the most according to claim 8, it is characterised in that: step (6) is entered in foaming furnace
OK, the temperature of foaming furnace is at 180 ~ 220 DEG C.
The manufacture method of PVC foam body the most according to claim 8, it is characterised in that: in step (7) a metallic, cooling medium
For water or/and gas, the temperature of cooling medium is 20-40 DEG C.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2019000590A1 (en) * | 2017-06-29 | 2019-01-03 | 顾崧 | Regenerated material produced on the basis of pvc recycled material |
GB2601454A (en) * | 2017-12-21 | 2022-06-01 | Altro Ltd | Improvements in or relating to plasticiser formulations |
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CN104893156A (en) * | 2015-06-08 | 2015-09-09 | 山东汇丰木塑型材股份有限公司 | 6-17mm-thick polyvinyl chloride foamed poster board and preparation method thereof |
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2016
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