CN107011542A - A kind of biodegradable expanded material and preparation method thereof - Google Patents

A kind of biodegradable expanded material and preparation method thereof Download PDF

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Publication number
CN107011542A
CN107011542A CN201710396678.XA CN201710396678A CN107011542A CN 107011542 A CN107011542 A CN 107011542A CN 201710396678 A CN201710396678 A CN 201710396678A CN 107011542 A CN107011542 A CN 107011542A
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expanded material
biodegradable expanded
biodegradable
mill
1phr
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陈渠鍫
丁华雄
吴天平
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Three Starr (jiangsu) Environmental Protection Technology Co Ltd
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Three Starr (jiangsu) Environmental Protection Technology Co Ltd
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    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L1/00Compositions of cellulose, modified cellulose or cellulose derivatives
    • C08L1/02Cellulose; Modified cellulose
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C35/00Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
    • B29C35/02Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
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    • 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
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
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    • C08J2203/04N2 releasing, ex azodicarbonamide or nitroso compound
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2301/00Characterised by the use of cellulose, modified cellulose or cellulose derivatives
    • C08J2301/02Cellulose; Modified cellulose
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    • 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
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised 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
    • C08J2423/04Homopolymers or copolymers of ethene
    • C08J2423/06Polyethene
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    • 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
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised 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
    • C08J2423/04Homopolymers or copolymers of ethene
    • C08J2423/08Copolymers of ethene
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    • 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
    • C08J2467/04Polyesters derived from hydroxy carboxylic acids, e.g. lactones
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    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K2003/2296Oxides; Hydroxides of metals of zinc
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
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    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • C08K2003/265Calcium, strontium or barium carbonate
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    • C08L2201/06Biodegradable
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    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C08L2205/025Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
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    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
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    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/06Properties of polyethylene
    • C08L2207/066LDPE (radical process)
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/20Recycled plastic

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Abstract

The invention discloses a kind of biodegradable expanded material and preparation method, by the 15Phr of ethylene-vinyl acetate copolymer EVA 10 as follows by weight, the 15Phr of regeneration low-density high-pressure polyethylene LDPE 10, the 60Phr of biodegradation material 50, the 3Phr of foaming agent 1,0.5~2Phr of zinc oxide, 0.5~2Phr of stearic acid, the 1Phr of peroxide cross-linking agent 0.5, the 20Phr of calcium carbonate 15, colorant 1phr;Biodegradable expanded material is prepared into by the technological process of batch mixing, mill, slice, sulfur foam, cooling and shaping, processing, its various use demand is not only disclosure satisfy that in physical property, also there is excellent elasticity and pliability, have readily biodegradable characteristic concurrently, Environmental Safety, it is nonpoisonous and tasteless, it is harmless, reduce pollution on the environment.

Description

A kind of biodegradable expanded material and preparation method thereof
Technical field
The present invention relates to foam material field, more particularly to a kind of biodegradable expanded material and preparation method thereof.
Background technology
Expanded material has high lightweight, specific strength, excellent insulation performance, buffer capacity notable and high adsorption capacity Advantage, has been widely used in the neck such as auto industry, building industry, packaging industry, agricultural, water process and air filtration Domain.But at present the overwhelming majority commercialization expanded materials be oil based polyalcohol end prod, such as polystyrene (EPS), Polyvinyl chloride (PVC), polyurethane (PUR), polyethylene ((PE) etc., these petroleum base polymer foams due to can high temperature resistant, Acid and alkali-resistance, and with low water absorbable and preferable weatherability, property is stable in natural environment, not degradable, causes serious White pollution, strong influence is caused to soil, water quality and ecoscape.
The drawbacks of not biodegradable of conventional foams and difficult offal treatment, brings very big to environment Threat, while raw material it is non-renewable also limit its application and develop.Therefore develop and develop it is a kind of it is new can Biodegradable expanded material pole is necessary.
The biodegradation material such as starch and lignin is easily by microbial attack, with excellent biodegradability, Therefore, develop biodegradable expanded material and open a new way not only to better profiting from abundant natural resources Footpath, also have found effective settling mode for expanded material welding.
The content of the invention
Goal of the invention:In order to solve the problems of in the prior art, the present invention, which is proposed, a kind of is ensureing excellent It is elastic and it is flexible simultaneously, have excellent biological degradability, the biodegradable expanded material and method of low-carbon environment-friendly concurrently.
Technical scheme:To achieve these objectives, the present invention takes following technical scheme:A kind of biodegradable foaming material Material, including preparing raw material by weight as follows:Ethylene-vinyl acetate copolymer EVA 10-15Phr, regeneration low-density are high Pressure polyethylene LDPE 15-20Phr, biodegradation material 50-60Phr, foaming agent 1-3Phr, 0.5~2Phr of zinc oxide, tristearin 0.5~2Phr of acid, peroxide cross-linking agent 0.5-1Phr, calcium carbonate 15-20Phr, colorant 1phr;
The consumption of various raw materials must strictly strict control coordinates in proportion:
The adding proportion of suitable ethylene-vinyl acetate copolymer can improve the pliability of product, elasticity, be excessively added Cost will be increased.
Regeneration low-density high-pressure polyethylene LDPE suitable addition can improve the cold resistance, heat resistance, wearability of product And chemical resistance, it is excessively added, product surface can be caused coarse, feel is bad, elasticity reduction.
The effect of foaming agent is the density and hardness for adjusting product.
Zinc oxide is blowing promotor, for adjusting expansion rate, coordinates with the amount of foaming agent and is adjusted, too low, is foamed The too small waste of dosage of causing to foam of agent gas forming amount, expansion rate slow down, sulfur foam time lengthening, the increased disadvantage of energy consumption End, crosses at most to foam and causes rate of closed hole to decline soon very much, the problem of product resilience is poor.
Stearic acid is used as helping foaming and lubricant, regulation expansion rate and anti-sticking effect in operating process, foams very little slightly Slack-off, material slightly sticky equipment in operation then foams slightly accelerate too much, heating of being skidded during mixing is slow, and mill process is in mill Upper easy roll release.
Peroxide cross-linking agent, suitable addition can adjust crosslink material density;Very few addition can then cause vulcanization to send out Bubble process middle crosslink density is low, does not live gas so that wrapping so that melt strength is low and forms continuous pore structure or can not foam;Cross Many additions can then cause sulfur foam process middle crosslink density is too high to cause melt strength too high and expansion ratio is small or can not Foaming.
Calcium carbonate, as filler, suitable addition can reduce cost, improve foaming nucleation abscess quality;Excessive Addition can only cause product density height, intensity resilience to be deteriorated, and feel is deteriorated.
It is more highly preferred to, the biodegradation material is thermoplastic starch, polylactic acid PLA and pla-pcl PCL according to 5: 4:1 mass ratio carries out blending extrusion and obtained.
Further, the mesh number of the thermoplastic starch, polylactic acid PLA and pla-pcl PCL is all higher than 200 mesh.
It is more highly preferred to, the foaming agent is azodicarbonamide.
It is more highly preferred to, the peroxide cross-linking agent is in cumyl peroxide, dual-tert-butyl peroxy isopropyl base benzene One kind.
The invention also discloses a kind of above-mentioned preparation method of biodegradable expanded material, comprise the following steps:
(1) batch mixing:Got ready on demand by by required raw material, be placed in banbury and carry out mixing treatment, wherein cooled down in banbury Water temperature is 75-85 DEG C, and compressed air pressure is that 0.7-0.9MPa, material temperature discharge material when being 105-115 DEG C;
(2) mill:The material feeding mill that banbury is discharged carries out mill, and preceding roll temperature is 80-90 DEG C, rear roller temperature Spend for 70-80 DEG C, roll spacing is 0.3-0.7mm, mend refining 3-5 times;
(3) slice:Material feeding film-discharging machine after mill is processed, obtains cooling down after tablet, coolant water temperature≤35 ℃;
(4) sulfur foam:Tablet feeding vulcanizing press after slice is subjected to sulfur foam processing, steam pressure is 0.75-0.8MPa, cure time=mold thickness × 1.1min/mm;
(5) it is cooled and shaped, processes:Cool time >=48 hour, coolant water temperature is 75-85 DEG C, cut, be punched after shaping, Printing, obtains required expanded material.
Be more highly preferred to, the charging sequence of the mixing procedure in step (1) for first by ethylene-vinyl acetate copolymer EVA, Regenerate low-density high-pressure polyethylene LDPE, biodegradation material, calcium carbonate and stearic acid and add mixer mixing once, Deng Dao great Material adds foaming agent, peroxide cross-linking agent, zinc oxide again after uniting, after all materials are mixed uniformly, discharging.
It is more highly preferred to, temperature is not higher than 110 DEG C during step (1) charging, prevents foaming agent from decomposing and DCP crosslinkings.
It is more highly preferred to, mould specification is 600mm × 200mm × 12mm in the step (4), and cure time is 16min.
Beneficial effect:A kind of biodegradable expanded material and preparation method that the present invention is provided, will be following with weight The ethylene-vinyl acetate copolymer EVA 10-15Phr of calculating, regeneration low-density high-pressure polyethylene LDPE15-20Phr, biological drop Solve material 50-60Phr, foaming agent 1-3Phr, 0.5~2Phr of zinc oxide, 0.5~2Phr of stearic acid, peroxide cross-linking agent 0.5-1Phr, calcium carbonate 15-20Phr, colorant 1phr;By batch mixing, mill, slice, sulfur foam, cooling and shaping, processing Technological process is prepared into biodegradable expanded material, and its various use demand is not only disclosure satisfy that in physical property, also With excellent elasticity and pliability, readily biodegradable characteristic is had concurrently, Environmental Safety is nonpoisonous and tasteless, harmless, drop Low pollution on the environment.
Embodiment
Embodiment 1:
A kind of biodegradable expanded material, including preparing raw material by weight as follows:Ethene-vinyl acetate is total to Polymers EVA 15Phr, regeneration low-density high-pressure polyethylene LDPE 20Phr, biodegradation material 60Phr, foaming agent 1Phr, oxygen Change zinc 1Phr, stearic acid 1Phr, peroxide cross-linking agent 0.8Phr, calcium carbonate 15Phr, colorant 1phr.
Wherein, the biodegradation material is thermoplastic starch, polylactic acid PLA and pla-pcl PCL according to 5:4:1 matter Amount is obtained than carrying out blending extrusion;And the mesh number of the thermoplastic starch, polylactic acid PLA and pla-pcl PCL is all higher than 200 Mesh;The foaming agent is azodicarbonamide;The peroxide cross-linking agent is dual-tert-butyl peroxy isopropyl base benzene.
Embodiment 2:
A kind of biodegradable expanded material, including preparing raw material by weight as follows:Ethene-vinyl acetate is total to Polymers EVA 10Phr, regeneration low-density high-pressure polyethylene LDPE 15Phr, biodegradation material 60Phr, foaming agent 3Phr, oxygen Change zinc 1Phr, stearic acid 1Phr, peroxide cross-linking agent 0.7Phr, calcium carbonate 15Phr, colorant 1phr.
Wherein, the biodegradation material is thermoplastic starch, polylactic acid PLA and pla-pcl PCL according to 5:4:1 matter Amount is obtained than carrying out blending extrusion;And the mesh number of the thermoplastic starch, polylactic acid PLA and pla-pcl PCL is all higher than 200 Mesh;The foaming agent is azodicarbonamide;The peroxide cross-linking agent is dual-tert-butyl peroxy isopropyl base benzene.
Embodiment 3:
A kind of biodegradable expanded material, including preparing raw material by weight as follows:Ethene-vinyl acetate is total to Polymers EVA 15Phr, regeneration low-density high-pressure polyethylene LDPE 15Phr, biodegradation material 50Phr, foaming agent 2Phr, oxygen Change zinc 1Phr, stearic acid 1Phr, peroxide cross-linking agent 0.7Phr, calcium carbonate 20Phr, colorant 1phr.
Wherein, the biodegradation material is thermoplastic starch, polylactic acid PLA and pla-pcl PCL according to 5:4:1 matter Amount is obtained than carrying out blending extrusion;And the mesh number of the thermoplastic starch, polylactic acid PLA and pla-pcl PCL is all higher than 200 Mesh;The foaming agent is azodicarbonamide;The peroxide cross-linking agent is dual-tert-butyl peroxy isopropyl base benzene.
Take the proportioning of embodiment 1, a kind of above-mentioned preparation method of biodegradable expanded material, including following step Suddenly:
(1) batch mixing:Got ready on demand by by required raw material, be placed in banbury and carry out mixing treatment, wherein cooled down in banbury Water temperature is 75-85 DEG C, and compressed air pressure is that 0.7-0.9MPa, material temperature discharge material when being 105-115 DEG C;Wherein feed process Middle temperature is not higher than 110 DEG C, and charging sequence is first by ethylene-vinyl acetate copolymer EVA, regeneration low-density high-pressure polyethylene LDPE, biodegradation material, calcium carbonate and stearic acid add mixer mixing once, add foaming again after aniseed is united Agent, peroxide cross-linking agent, zinc oxide, after all materials are mixed uniformly, discharging;
(2) mill:The material feeding mill that banbury is discharged carries out mill, and preceding roll temperature is 80-90 DEG C, rear roller temperature Spend for 70-80 DEG C, roll spacing is 0.3-0.7mm, mend refining 3-5 times;
(3) slice:Material feeding film-discharging machine after mill is processed, obtains cooling down after tablet, coolant water temperature≤35 ℃;
(4) sulfur foam:Tablet feeding vulcanizing press after slice is subjected to sulfur foam processing, steam pressure is 0.75-0.8MPa, cure time=mold thickness × 1.1min/mm;Mould specification is 600mm × 200mm × 12mm, during vulcanization Between be 16min;
(5) it is cooled and shaped, processes:Cool time >=48 hour, coolant water temperature is 75-85 DEG C, cut, be punched after shaping, Printing, biodegradable expanded material needed for obtaining.
The biodegradable expanded material for taking the embodiment of the present invention 4 to prepare takes a certain amount of respectively with commercially available common expanded material Material carry out two contrast tests:
(1) biodegradation test of 6 months of laboratory simulation is carried out, condition is tried one's best access expansion condition simulation, respectively In carrying out Mass lost ratio tests to two kinds of materials after 3 months, 6 months.
(2) two kinds of materials are placed in the natural conditions of outdoor test block and carry out biodegradation test, respectively at 6 months, 1 Year, 1 year half and Mass lost ratio tests are carried out to two kinds of materials after 2 years.
Concrete outcome is as shown in table 1:
Table 1 and commercially available common expanded material degraded situation contrast (Mass lost ratio)
Can clearly it find out from the data of table 1, a kind of biodegradable expanded material of the present invention and commercially available common expanded material Compare, its biological degradability is splendid, substantially can be with degradable, environmentally friendly no pressure in 2 years.
It should be pointed out that for those skilled in the art, under the premise without departing from the principles of the invention, Some improvement can also be made, these improvement also should be regarded as protection scope of the present invention.

Claims (9)

1. a kind of biodegradable expanded material, it is characterised in that including preparing raw material as follows by weight:Ethene-vinegar Sour ethylene copolymer EVA 10-15Phr, regeneration low-density high-pressure polyethylene LDPE 15-20Phr, biodegradation material 50- 60Phr, foaming agent 1-3Phr, 0.5~2Phr of zinc oxide, 0.5~2Phr of stearic acid, peroxide cross-linking agent 0.5-1Phr, carbon Sour calcium 15-20Phr, colorant 1phr.
2. biodegradable expanded material according to claim 1, it is characterised in that:The biodegradation material is heat Plastic starch, polylactic acid PLA and pla-pcl PCL are according to 5:4:1 mass ratio carries out blending extrusion and obtained.
3. biodegradable expanded material according to claim 2, it is characterised in that:The thermoplastic starch, poly- breast Sour PLA and pla-pcl PCL mesh number is all higher than 200 mesh.
4. biodegradable expanded material according to claim 1, it is characterised in that:The foaming agent is azo diformazan Acid amides.
5. biodegradable expanded material according to claim 1, it is characterised in that:The peroxide cross-linking agent is One kind in cumyl peroxide, dual-tert-butyl peroxy isopropyl base benzene.
6. the preparation method of biodegradable expanded material as claimed in claim 1, it is characterised in that comprise the following steps:
(1) batch mixing:Got ready on demand by by required raw material, be placed in banbury and carry out mixing treatment, wherein coolant water temperature in banbury For 75-85 DEG C, compressed air pressure is that 0.7-0.9MPa, material temperature discharge material when being 105-115 DEG C;
(2) mill:The material feeding mill that banbury is discharged carries out mill, and preceding roll temperature is 80-90 DEG C, and rear roll temperature is 70-80 DEG C, roll spacing is 0.3-0.7mm, mends refining 3-5 times;
(3) slice:Material feeding film-discharging machine after mill is processed, obtains cooling down after tablet, coolant water temperature≤35 DEG C;
(4) sulfur foam:Tablet feeding vulcanizing press after slice is subjected to sulfur foam processing, steam pressure is 0.75- 0.8MPa, cure time=mold thickness × 1.1min/mm;
(5) it is cooled and shaped, processes:Cool time >=48 hour, coolant water temperature is 75-85 DEG C, cuts, is punched, prints after shaping, Obtain required expanded material.
7. the preparation method of biodegradable expanded material according to claim 6, it is characterised in that:In step (1) Mixing procedure charging sequence for first by ethylene-vinyl acetate copolymer EVA, regeneration low-density high-pressure polyethylene LDPE, life Thing degradable material, calcium carbonate and stearic acid add mixer mixing once, add foaming agent, peroxidating again after aniseed is united Thing crosslinking agent, zinc oxide, after all materials are mixed uniformly, discharging.
8. the preparation method of biodegradable expanded material according to claim 7, it is characterised in that:Step (1) adds Temperature is not higher than 110 DEG C during material.
9. the preparation method of biodegradable expanded material according to claim 7, it is characterised in that:The step (4) mould specification is 600mm × 200mm × 12mm in, and cure time is 16min.
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Cited By (8)

* Cited by examiner, † Cited by third party
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CN107722581A (en) * 2017-10-27 2018-02-23 北京工商大学 A kind of polylactic acid alloy expanded material of high foamability and preparation method thereof
CN108659486A (en) * 2018-04-09 2018-10-16 广东国立科技股份有限公司 A kind of degradable EVA foam shoe material and preparation method thereof
CN109401030A (en) * 2018-09-28 2019-03-01 晋江市新奇美鞋材发展有限公司 A kind of light wear-resistant EVA shoe bottom material and preparation method thereof
CN110591309A (en) * 2019-08-31 2019-12-20 佛山碧嘉高新材料科技有限公司 Biodegradable foamed plastic composite material and preparation method and application thereof
CN110591310A (en) * 2019-09-04 2019-12-20 常州大学 Modified polylactic acid foaming material and forming method thereof
CN111253722A (en) * 2019-03-11 2020-06-09 汕头市三马塑胶制品有限公司 Foaming-grade modified polylactic acid and preparation method thereof
CN113583333A (en) * 2021-09-06 2021-11-02 东莞兆阳兴业塑胶制品有限公司 Preparation method of degradable foamed shoe material
CN115636987A (en) * 2022-11-15 2023-01-24 深圳辰梦源科技有限公司 Bio-based foaming material and preparation method thereof

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CN107722581A (en) * 2017-10-27 2018-02-23 北京工商大学 A kind of polylactic acid alloy expanded material of high foamability and preparation method thereof
CN108659486A (en) * 2018-04-09 2018-10-16 广东国立科技股份有限公司 A kind of degradable EVA foam shoe material and preparation method thereof
CN109401030A (en) * 2018-09-28 2019-03-01 晋江市新奇美鞋材发展有限公司 A kind of light wear-resistant EVA shoe bottom material and preparation method thereof
CN111253722A (en) * 2019-03-11 2020-06-09 汕头市三马塑胶制品有限公司 Foaming-grade modified polylactic acid and preparation method thereof
CN111253722B (en) * 2019-03-11 2022-10-04 汕头市三马塑胶制品有限公司 Foaming-grade modified polylactic acid and preparation method thereof
CN110591309A (en) * 2019-08-31 2019-12-20 佛山碧嘉高新材料科技有限公司 Biodegradable foamed plastic composite material and preparation method and application thereof
CN110591310A (en) * 2019-09-04 2019-12-20 常州大学 Modified polylactic acid foaming material and forming method thereof
CN110591310B (en) * 2019-09-04 2021-07-30 常州大学 Modified polylactic acid foaming material and forming method thereof
CN113583333A (en) * 2021-09-06 2021-11-02 东莞兆阳兴业塑胶制品有限公司 Preparation method of degradable foamed shoe material
CN115636987A (en) * 2022-11-15 2023-01-24 深圳辰梦源科技有限公司 Bio-based foaming material and preparation method thereof

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