CN110028695A - A kind of polypropylene expanded high fondant-strength foaming concentrate and preparation method thereof - Google Patents

A kind of polypropylene expanded high fondant-strength foaming concentrate and preparation method thereof Download PDF

Info

Publication number
CN110028695A
CN110028695A CN201910349795.XA CN201910349795A CN110028695A CN 110028695 A CN110028695 A CN 110028695A CN 201910349795 A CN201910349795 A CN 201910349795A CN 110028695 A CN110028695 A CN 110028695A
Authority
CN
China
Prior art keywords
weight
parts
polypropylene
agent
inorfil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
CN201910349795.XA
Other languages
Chinese (zh)
Inventor
陈庆
昝航
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chengdu New Keli Chemical Science Co Ltd
Original Assignee
Chengdu New Keli Chemical Science Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chengdu New Keli Chemical Science Co Ltd filed Critical Chengdu New Keli Chemical Science Co Ltd
Priority to CN201910349795.XA priority Critical patent/CN110028695A/en
Publication of CN110028695A publication Critical patent/CN110028695A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/22Compounding polymers with additives, e.g. colouring using masterbatch techniques
    • C08J3/226Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
    • 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
    • C08J9/0085Use of fibrous compounding 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
    • C08J9/009Use of pretreated compounding 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
    • C08J9/0095Mixtures of at least two compounding ingredients belonging to different one-dot groups
    • 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
    • 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
    • C08J2203/02CO2-releasing, e.g. NaHCO3 and citric acid
    • 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
    • C08J2403/00Characterised by the use of starch, amylose or amylopectin or of their derivatives or degradation products
    • C08J2403/12Amylose; Amylopectin; Degradation products thereof
    • 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
    • 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
    • C08J2423/10Homopolymers or copolymers of propene
    • C08J2423/12Polypropene

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

The present invention provides a kind of polypropylene expanded high fondant-strength foaming concentrates and preparation method thereof.Active inorganic fiber powder is obtained after inorfil powder with acicular texture is handled using surfactant, then with high amylopectin starch graft reaction, obtain needle-shaped type inorfil/high amylopectin starch composite material, finally high fondant-strength foaming concentrate is used to get polypropylene expanded with chemical foaming agent, nucleating agent, lubricant, dispersing agent, polypropylene mixing extruding pelletization.This method is by obtaining composite material in needle-shaped type inorfil surface grafting high amylopectin starch, and then masterbatch is mixed to prepare with foaming agent, after polypropene blended, the melt strength of expanded polypropylene can be effectively improved, improve foaming quality, and additive amount is small, can effectively realize lightening effect, at low cost, application prospect is good.

Description

A kind of polypropylene expanded high fondant-strength foaming concentrate and preparation method thereof
Technical field
The present invention relates to polymeric material fields, and in particular to the preparation of polymer master batch, more particularly to one kind poly- third Alkene foaming high fondant-strength foaming concentrate and preparation method thereof.
Background technique
Expanded polypropylene material, it is a kind of highly crystalline type polymer/gas recombination material of performance brilliance, with its uniqueness And superior performance becomes fastest-rising environment-friendly novel resistance to compression at present and buffers heat-barrier material.Conventional method production polypropylene be A kind of line style semicrystalline polymeric, the seldom branching of strand, molecular weight distribution relative narrower, this leads to its softening point and melts Point very close to.Before temperature reaches fusing point, it is not flowed substantially, and after temperature is more than fusing point, melt strength sharply declines, this Kind melt is difficult to encase gas;In addition, polypropylene, which is changed into crystalline state from molten state, can release a large amount of heat, by melt transform It is longer the time required to for solid;In addition polypropylene air penetrability is high, and foamed gas is easily escaped.Therefore it is suitable for polypropylene expanded humidity province Between it is narrow, foaming process is difficult to control, and easily causes in foaming process that steep that wall rupture, gas escape, abscess collapses and bubble merges.
Polyacrylic melt strength is low, significantly limits its range of work and application field, such as in thermo forming fields, by Low in melt strength of polypropylene, container wall thickness is uneven when causing plastics sucking moulding or rupture;When extrusion coated, plain polypropylene Apparent constriction and melt resonance are shown, thus phenomena such as edge curl, shrink occurs;When extrusion foaming, micro-pore wall is easily sent out It is raw to rupture, expansion ratio is low etc..Therefore, to obtain the PP foam material of high quality, it is crucial for improving its melt strength.
Chinese invention patent application number 201510678792.2 discloses a kind of environment-protective water expanded polypropylene masterbatch, by with The material of lower parts by weight is made: 5 ~ 10 parts of modifying agent, 5 ~ 10 parts of LDPE, micropore absorbs water 30 ~ 60 parts of inorganic foamed material, causes 0.01 ~ 0.2 part of agent, 1 ~ 3 part of surfactant, 0.1 ~ 0.5 part of plastic antioxidants, modifying agent is ethylene-vinyl acetate copolymer, EP rubbers, ethylene-propylene diene copolymer, SBS, one or more of polybutene or POE.
It is female that Chinese invention patent application number 201710728117.5 discloses a kind of foaming for expandable polypropylene resin Material and preparation method thereof, the present invention are used for the foaming concentrate of expandable polypropylene resin, the component comprising following parts by weight: polyethylene 40 parts of resin, 10 ~ 50 parts of sodium bicarbonate, 10 ~ 50 points of sodium citrate, 1 ~ 10 part of talcum powder, 1 ~ 5 part of stearic acid, 1 ~ 5 part of paraffin, 0.1 ~ 3 part of white oil, polyvinyl resin is the polyvinyl resin that its melt index is 40 ~ 50g/10min.The invention is used for polypropylene The preparation method of resin expanded foaming concentrate passes through pelleter by being added to squeeze out in screw extruder by whole components again Pelletizing is prepared.
Chinese invention patent application number 201210101328.3 discloses a kind of polypropylene expanded masterbatch and preparation method thereof, It is to add azodicarbonamide, nano montmorillonite, glycerin monostearate, zinc stearate, poly- two using polyvinyl resin as matrix Foaming concentrate is made in extruding pelletization after methylsiloxane, foam stabilizer mixing.
Chinese invention patent application number 201210086754.4 discloses a kind of microporous foam polypropylene material, material master If being made by containing the following parts by weight: 80 ~ 95 parts of acrylic resin, 1 ~ 10 part of high bath strength acrylic resin, 1 ~ 20 part of masterbatch, 0.5 ~ 8 part of crosslinking agent, 0.8 ~ 10 part of assistant crosslinking agent, 0.1 ~ 1 part of foaming agent, 0.1 ~ 5 part of antioxidant of nucleation. The present invention also discloses the preparation methods of above-mentioned microporous foam polypropylene material.
According to above-mentioned, in existing scheme for polypropylene expanded plastics because material self reason and processing technology not at It is ripe, there are solution intensity is low, the undesirable defect of foaming effect.
Summary of the invention
The defects of there are solution intensity is low, and foaming quality is poor for the wider polypropylene expanded plastics of current application, this hair It is bright to propose a kind of polypropylene expanded high fondant-strength foaming concentrate and preparation method thereof, so as in a small amount of addition preparation foaming Polypropylene effectively improves polyacrylic solution intensity, and foaming quality is high, and lightening effect is good.
Specific technical solution of the present invention is as follows:
A kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, comprising the following steps:
(1) the inorfil powder with acicular texture is added in solvent, is uniformly dispersed and suspension is made, is subsequently added into surface Activating agent carries out microwave treatment, and 3 ~ 8h is then freeze-dried at -10 ~ -30 DEG C, and the active inorganic fiber powder of acicular texture is made Body;
(2) high amylopectin starch, ammonium persulfate/urea are caused system to be scattered in supercritical fluid, is sufficiently swollen, and carried and draw Hair agent fully penetrates into inside starch granules, is subsequently added into active inorganic fiber powder made from step (1), carries out heating and adds Pressure reaction, so that introducing large number of grafted chain on needle-shaped type inorfil surface, is filtered, washed after reaction, dries, Needle-shaped type inorfil/high amylopectin starch composite material is made;
(3) by needle-shaped type inorfil/high amylopectin starch composite material made from step (2) and chemical foaming agent, nucleating agent, profit Lubrication prescription, dispersing agent, polypropylene are added in high-speed mixer and are uniformly mixed, and are then transferred in Dual inoculation squeeze out and make Grain, extrusion temperature are 80 ~ 100 DEG C and use high fondant-strength foaming concentrate to get polypropylene expanded.
The present invention is by the way that under the swelling action of supercritical fluid, high amylopectin starch successfully grafts on needle-shaped type inorfil Surface introduces large number of grafted chain, by the masterbatch with it is polypropene blended, utilize numerous the connecing on needle-shaped type inorfil surface Branch chain and polypropylene macromolecular chain carry out abundant physical entanglement, improve polyacrylic melt strength, greatly improvement foaming quality.
Preferably, step (1) the inorfil powder with acicular texture is calcium carbonate crystal whisker, wollastonite, Hai Pao At least one of stone, shepardite, glass fibre, pyrophillite, nepheline.
Preferably, step (1) solvent is one of deionized water, dehydrated alcohol.
Preferably, step (1) surfactant is cetyl trimethylammonium bromide.
Preferably, the microwave power of step (1) described microwave treatment is 680 ~ 720W, and treatment temperature is 60 ~ 80 DEG C, processing 5 ~ 6min of time.
Preferably, in step (1), 20 ~ 40 parts by weight of inorfil powder, 56 ~ 78 weight of solvent with acicular texture Part, 2 ~ 4 parts by weight of surfactant.
Preferably, step (2) supercritical fluid is supercritical water, supercritical carbon dioxide, supercritical nitrogen, surpasses and face One of boundary's ethyl alcohol.
Preferably, step (2) it is described heating compressive reaction temperature be 60 ~ 70 DEG C, pressure be 20 ~ 25MPa, the time be 3 ~ 5h。
Preferably, in step (2), 14 ~ 18 parts by weight of high amylopectin starch, 2 ~ 4 parts by weight of ammonium persulfate, 2 ~ 4 weight of urea Part, 44 ~ 57 parts by weight of supercritical fluid, 25 ~ 30 parts by weight of active inorganic fiber powder.
Preferably, step (3) chemical foaming agent is sodium bicarbonate, ammonium hydrogen carbonate, 2,2'- azodiisobutyronitrile, idol One of nitrogen dioctyl phthalate diisopropyl ester.
Preferably, step (3) nucleating agent be talcum powder, calcium carbonate, silica, calcium oxide, magnesia, carbon black, At least one of mica.
Preferably, step (3) lubricant is stearic acid, in butyl stearate, oleamide, ethylene bis stearamide It is at least one.
Preferably, step (3) dispersing agent is barium stearate, zinc stearate, calcium stearate, cadmium stearate, stearic acid At least one of magnesium, copper stearate.
Preferably, in step (3), needle-shaped type inorfil/61 ~ 73 parts by weight of high amylopectin starch composite material, chemistry hair 15 ~ 20 parts by weight of infusion, 5 ~ 8 parts by weight of nucleating agent, 4 ~ 6 parts by weight of lubricant, 3 ~ 5 parts by weight of dispersing agent, polypropylene 10-20 weight Measure part.
The present invention also provides the polypropylene expanded use high fondant-strength foaming concentrates that a kind of above-mentioned preparation method is prepared. The inorfil powder with acicular texture is selected, is dispersed in solvent and suspension is made, surfactant 16 is added Alkyl trimethyl ammonium bromide carries out microwave treatment, and the active inorganic fiber powder of acicular texture is obtained after freeze-drying;Height is propped up Chain starch, ammonium persulfate/urea initiation system are dispersed in supercritical fluid and are sufficiently swollen, and carries initiator and fully permeate Into inside starch granules, gained active inorganic fiber powder is added, heat up compressive reaction, draws on needle-shaped type inorfil surface Enter large number of grafted chain, obtains needle-shaped type inorfil/high amylopectin starch composite material;By needle-shaped type inorfil/height Amylopectin composite material mixes in a high speed mixer with auxiliary agents such as chemical foaming agent, nucleating agent, lubricant, dispersing agents It is even, it is then added to extruding pelletization in Dual inoculation, obtains product.
The present invention provides a kind of polypropylene expanded high fondant-strength foaming concentrates and preparation method thereof, with the prior art It compares, the feature and excellent effect protruded is:
1, propose to be grafted with high amylopectin starch needle-shaped type inorfil prepare it is polypropylene expanded with high fondant-strength foaming concentrate Method.
2, it by obtaining composite material in needle-shaped type inorfil surface grafting high amylopectin starch, and then is mixed with foaming agent Masterbatch is made, after polypropene blended, the melt strength of expanded polypropylene can be effectively improved, improve foaming quality.
3, the additive amount of foaming concentrate produced by the present invention is small, and modified effect is good, can effectively realize lightening effect, cost Low, application prospect is good.
Specific embodiment
In the following, the present invention will be further described in detail by way of specific embodiments, but this should not be interpreted as to the present invention Range be only limitted to example below.Without departing from the idea of the above method of the present invention, according to ordinary skill The various replacements or change that knowledge and customary means are made, should be included in the scope of the present invention.
Embodiment 1
Preparation process are as follows:
(1) the inorfil powder with acicular texture is added in solvent, is uniformly dispersed and suspension is made, is subsequently added into surface Activating agent carries out microwave treatment, is then freeze-dried 5h at -20 DEG C, and the active inorganic fiber powder of acicular texture is made;Tool The inorfil powder for having acicular texture is calcium carbonate crystal whisker;Solvent is deionized water;Surfactant is cetyl front three Base ammonium bromide;The microwave power of microwave treatment is 690W, and treatment temperature is 68 DEG C, handles time 6min;Wherein, there is needle-shaped knot 28 parts by weight of inorfil powder, 69 parts by weight of solvent, 3 parts by weight of surfactant of structure;
(2) high amylopectin starch, ammonium persulfate/urea are caused system to be scattered in supercritical fluid, is sufficiently swollen, and carried and draw Hair agent fully penetrates into inside starch granules, is subsequently added into active inorganic fiber powder made from step (1), carries out heating and adds Pressure reaction, is filtered, washed after reaction, dries, needle-shaped type inorfil/high amylopectin starch composite material is made;It is overcritical Fluid is supercritical water;The temperature of heating compressive reaction is 66 DEG C, pressure 23MPa, time 4h;Wherein, high amylopectin starch 15 parts by weight, 3 parts by weight of ammonium persulfate, 3 parts by weight of urea, 52 parts by weight of supercritical fluid, 27 weight of active inorganic fiber powder Measure part;
(3) by needle-shaped type inorfil/high amylopectin starch composite material made from step (2) and chemical foaming agent, nucleating agent, profit Lubrication prescription, dispersing agent, polypropylene are added in high-speed mixer and are uniformly mixed, and are then transferred in Dual inoculation squeeze out and make Grain, extrusion temperature are 80 DEG C and use high fondant-strength foaming concentrate to get polypropylene expanded;Chemical foaming agent is sodium bicarbonate;At Core agent is talcum powder;Lubricant is stearic acid;Dispersing agent is barium stearate;Wherein, needle-shaped type inorfil/high amylopectin starch is multiple 67 parts by weight of condensation material, 17 parts by weight of chemical foaming agent, 7 parts by weight of nucleating agent, 5 parts by weight of lubricant, 4 parts by weight of dispersing agent, 10 parts by weight of polypropylene.
Test method are as follows:
Expanded polypropylene melt strength: being added polypropylene matrix according to mass ratio 10% for foaming concentrate made from embodiment 1, Mixing, which squeezes out, is made expanded polypropylene sample, measures foaming poly- third using German Rheotens71.97 type solution strength tester The melt strength of alkene sample;
Expanded polypropylene density: polypropylene matrix, mixing is added according to mass ratio 10% in foaming concentrate made from embodiment 1 It squeezes out and expanded polypropylene sample is made, the density of expanded polypropylene sample is measured using density tester.
The melt strength of expanded polypropylene made from the foaming concentrate addition of the embodiment 1 measured as the above method and close Degree is as shown in table 1.
Embodiment 2
Preparation process are as follows:
(1) the inorfil powder with acicular texture is added in solvent, is uniformly dispersed and suspension is made, is subsequently added into surface Activating agent carries out microwave treatment, is then freeze-dried 8h at -10 DEG C, and the active inorganic fiber powder of acicular texture is made;Tool The inorfil powder for having acicular texture is wollastonite;Solvent is dehydrated alcohol;Surfactant is cetyl trimethyl bromine Change ammonium;The microwave power of microwave treatment is 690W, and treatment temperature is 65 DEG C, handles time 6min;Wherein, with acicular texture 25 parts by weight of inorfil powder, 73 parts by weight of solvent, 2 parts by weight of surfactant;
(2) high amylopectin starch, ammonium persulfate/urea are caused system to be scattered in supercritical fluid, is sufficiently swollen, and carried and draw Hair agent fully penetrates into inside starch granules, is subsequently added into active inorganic fiber powder made from step (1), carries out heating and adds Pressure reaction, is filtered, washed after reaction, dries, needle-shaped type inorfil/high amylopectin starch composite material is made;It is overcritical Fluid is supercritical carbon dioxide;The temperature of heating compressive reaction is 62 DEG C, pressure 21MPa, time 4.5h;Wherein, high 15 parts by weight of amylopectin, 2 parts by weight of ammonium persulfate, 3 parts by weight of urea, 55 parts by weight of supercritical fluid, active inorganic fiber 26 parts by weight of powder;
(3) by needle-shaped type inorfil/high amylopectin starch composite material made from step (2) and chemical foaming agent, nucleating agent, profit Lubrication prescription, dispersing agent, polypropylene are added in high-speed mixer and are uniformly mixed, and are then transferred in Dual inoculation squeeze out and make Grain, extrusion temperature are 100 DEG C and use high fondant-strength foaming concentrate to get polypropylene expanded;Chemical foaming agent is ammonium hydrogen carbonate;At Core agent is calcium carbonate;Lubricant is butyl stearate;Dispersing agent is zinc stearate;Wherein, needle-shaped type inorfil/high branch forms sediment 70 parts by weight of powder composite material, 16 parts by weight of chemical foaming agent, 6 parts by weight of nucleating agent, 5 parts by weight of lubricant, 3 weight of dispersing agent Part, 15 parts by weight of polypropylene.
Test method are as follows:
Expanded polypropylene melt strength: being added polypropylene matrix according to mass ratio 10% for foaming concentrate made from embodiment 2, Mixing, which squeezes out, is made expanded polypropylene sample, measures foaming poly- third using German Rheotens71.97 type solution strength tester The melt strength of alkene sample;
Expanded polypropylene density: polypropylene matrix, mixing is added according to mass ratio 10% in foaming concentrate made from embodiment 2 It squeezes out and expanded polypropylene sample is made, the density of expanded polypropylene sample is measured using density tester.
The melt strength of expanded polypropylene made from the foaming concentrate addition of the embodiment 2 measured as the above method and close Degree is as shown in table 1.
Embodiment 3
Preparation process are as follows:
(1) the inorfil powder with acicular texture is added in solvent, is uniformly dispersed and suspension is made, is subsequently added into surface Activating agent carries out microwave treatment, is then freeze-dried 3h at -30 DEG C, and the active inorganic fiber powder of acicular texture is made;Tool The inorfil powder for having acicular texture is sepiolite;Solvent is deionized water;Surfactant is cetyl trimethyl bromine Change ammonium;The microwave power of microwave treatment is 710W, and treatment temperature is 68 DEG C, handles time 5min;Wherein, with acicular texture 35 parts by weight of inorfil powder, 71 parts by weight of solvent, 4 parts by weight of surfactant;
(2) high amylopectin starch, ammonium persulfate/urea are caused system to be scattered in supercritical fluid, is sufficiently swollen, and carried and draw Hair agent fully penetrates into inside starch granules, is subsequently added into active inorganic fiber powder made from step (1), carries out heating and adds Pressure reaction, is filtered, washed after reaction, dries, needle-shaped type inorfil/high amylopectin starch composite material is made;It is overcritical Fluid is supercritical nitrogen;The temperature of heating compressive reaction is 68 DEG C, pressure 24MPa, time 3.5h;Wherein, Gao Zhilian 17 parts by weight of starch, 4 parts by weight of ammonium persulfate, 3 parts by weight of urea, 47 parts by weight of supercritical fluid, active inorganic fiber powder 29 parts by weight;
(3) by needle-shaped type inorfil/high amylopectin starch composite material made from step (2) and chemical foaming agent, nucleating agent, profit Lubrication prescription, dispersing agent, polypropylene are added in high-speed mixer and are uniformly mixed, and are then transferred in Dual inoculation squeeze out and make Grain, extrusion temperature are 80 DEG C and use high fondant-strength foaming concentrate to get polypropylene expanded;Chemical foaming agent is 2,2'- azo two Isobutyronitrile;Nucleating agent is silica;Lubricant is oleamide;Dispersing agent is calcium stearate;Wherein, needle-shaped type inorfil/ 64 parts by weight of high amylopectin starch composite material, 7 parts by weight of nucleating agent, 6 parts by weight of lubricant, are divided at 19 parts by weight of chemical foaming agent 4 parts by weight of powder, 15 parts by weight of polypropylene.
Test method are as follows:
Expanded polypropylene melt strength: being added polypropylene matrix according to mass ratio 10% for foaming concentrate made from embodiment 3, Mixing, which squeezes out, is made expanded polypropylene sample, measures foaming poly- third using German Rheotens71.97 type solution strength tester The melt strength of alkene sample;
Expanded polypropylene density: polypropylene matrix, mixing is added according to mass ratio 10% in foaming concentrate made from embodiment 3 It squeezes out and expanded polypropylene sample is made, the density of expanded polypropylene sample is measured using density tester.
The melt strength of expanded polypropylene made from the foaming concentrate addition of the embodiment 3 measured as the above method and close Degree is as shown in table 1.
Embodiment 4
Preparation process are as follows:
(1) the inorfil powder with acicular texture is added in solvent, is uniformly dispersed and suspension is made, is subsequently added into surface Activating agent carries out microwave treatment, is then freeze-dried 6h at -15 DEG C, and the active inorganic fiber powder of acicular texture is made;Tool The inorfil powder for having acicular texture is shepardite;Solvent is dehydrated alcohol;Surfactant is cetyl trimethyl bromine Change ammonium;The microwave power of microwave treatment is 680W, and treatment temperature is 60 DEG C, handles time 6min;Wherein, with acicular texture 20 parts by weight of inorfil powder, 78 parts by weight of solvent, 2 parts by weight of surfactant;
(2) high amylopectin starch, ammonium persulfate/urea are caused system to be scattered in supercritical fluid, is sufficiently swollen, and carried and draw Hair agent fully penetrates into inside starch granules, is subsequently added into active inorganic fiber powder made from step (1), carries out heating and adds Pressure reaction, is filtered, washed after reaction, dries, needle-shaped type inorfil/high amylopectin starch composite material is made;It is overcritical Fluid is Supercritical Ethanol;The temperature of heating compressive reaction is 60 DEG C, pressure 20MPa, time 5h;Wherein, high branch forms sediment 14 parts by weight of powder, 2 parts by weight of ammonium persulfate, 2 parts by weight of urea, 57 parts by weight of supercritical fluid, active inorganic fiber powder 25 Parts by weight;
(3) by needle-shaped type inorfil/high amylopectin starch composite material made from step (2) and chemical foaming agent, nucleating agent, profit Lubrication prescription, dispersing agent, polypropylene are added in high-speed mixer and are uniformly mixed, and are then transferred in Dual inoculation squeeze out and make Grain, extrusion temperature are 100 DEG C and use high fondant-strength foaming concentrate to get polypropylene expanded;Chemical foaming agent is azoformic acid Diisopropyl ester;Nucleating agent is calcium oxide;Lubricant is ethylene bis stearamide;Dispersing agent is cadmium stearate;Wherein, needle-shaped type without Machine fiber/73 parts by weight of high amylopectin starch composite material, 15 parts by weight of chemical foaming agent, 5 parts by weight of nucleating agent, 4 weight of lubricant Measure part, 3 parts by weight of dispersing agent, 15 parts by weight of polypropylene.
Test method are as follows:
Expanded polypropylene melt strength: being added polypropylene matrix according to mass ratio 10% for foaming concentrate made from embodiment 4, Mixing, which squeezes out, is made expanded polypropylene sample, measures foaming poly- third using German Rheotens71.97 type solution strength tester The melt strength of alkene sample;
Expanded polypropylene density: polypropylene matrix, mixing is added according to mass ratio 10% in foaming concentrate made from embodiment 4 It squeezes out and expanded polypropylene sample is made, the density of expanded polypropylene sample is measured using density tester.
The melt strength of expanded polypropylene made from the foaming concentrate addition of the embodiment 4 measured as the above method and close Degree is as shown in table 1.
Embodiment 5
Preparation process are as follows:
(1) the inorfil powder with acicular texture is added in solvent, is uniformly dispersed and suspension is made, is subsequently added into surface Activating agent carries out microwave treatment, is then freeze-dried 7h at -18 DEG C, and the active inorganic fiber powder of acicular texture is made;Tool The inorfil powder for having acicular texture is glass fibre;Solvent is deionized water;Surfactant is cetyl trimethyl Ammonium bromide;The microwave power of microwave treatment is 720W, and treatment temperature is 80 DEG C, handles time 5min;Wherein, there is acicular texture 40 parts by weight of inorfil powder, 56 parts by weight of solvent, 4 parts by weight of surfactant;
(2) high amylopectin starch, ammonium persulfate/urea are caused system to be scattered in supercritical fluid, is sufficiently swollen, and carried and draw Hair agent fully penetrates into inside starch granules, is subsequently added into active inorganic fiber powder made from step (1), carries out heating and adds Pressure reaction, is filtered, washed after reaction, dries, needle-shaped type inorfil/high amylopectin starch composite material is made;It is overcritical Fluid is supercritical water;The temperature of heating compressive reaction is 70 DEG C, pressure 25MPa, time 3h;Wherein, high amylopectin starch 18 parts by weight, 4 parts by weight of ammonium persulfate, 4 parts by weight of urea, 44 parts by weight of supercritical fluid, 30 weight of active inorganic fiber powder Measure part;
(3) by needle-shaped type inorfil/high amylopectin starch composite material made from step (2) and chemical foaming agent, nucleating agent, profit Lubrication prescription, dispersing agent, polypropylene are added in high-speed mixer and are uniformly mixed, and are then transferred in Dual inoculation squeeze out and make Grain, extrusion temperature are 90 DEG C and use high fondant-strength foaming concentrate to get polypropylene expanded;Chemical foaming agent is sodium bicarbonate;At Core agent is carbon black;Lubricant is stearic acid;Dispersing agent is magnesium stearate;Wherein, needle-shaped type inorfil/high amylopectin starch is compound 61 parts by weight of material, 8 parts by weight of nucleating agent, 6 parts by weight of lubricant, 5 parts by weight of dispersing agent, are gathered at 20 parts by weight of chemical foaming agent 18 parts by weight of propylene.
Test method are as follows:
Expanded polypropylene melt strength: being added polypropylene matrix according to mass ratio 10% for foaming concentrate made from embodiment 5, Mixing, which squeezes out, is made expanded polypropylene sample, measures foaming poly- third using German Rheotens71.97 type solution strength tester The melt strength of alkene sample;
Expanded polypropylene density: polypropylene matrix, mixing is added according to mass ratio 10% in foaming concentrate made from embodiment 5 It squeezes out and expanded polypropylene sample is made, the density of expanded polypropylene sample is measured using density tester.
The melt strength of expanded polypropylene made from the foaming concentrate addition of the embodiment 5 measured as the above method and close Degree is as shown in table 1.
Comparative example 1
Preparation process are as follows:
(1) the inorfil powder with acicular texture is added in solvent, is uniformly dispersed and suspension is made, is subsequently added into surface Activating agent carries out microwave treatment, is then freeze-dried 5h at -20 DEG C, and the active inorganic fiber powder of acicular texture is made;Tool The inorfil powder for having acicular texture is nepheline;Solvent is dehydrated alcohol;Surfactant is cetyl trimethyl bromination Ammonium;The microwave power of microwave treatment is 700W, and treatment temperature is 70 DEG C, handles time 5.5min;Wherein, with acicular texture 30 parts by weight of inorfil powder, 67 parts by weight of solvent, 3 parts by weight of surfactant;
(2) by the active inorganic fiber powder of acicular texture made from step (1) and chemical foaming agent, nucleating agent, lubricant, point Powder, polypropylene are added in high-speed mixer and are uniformly mixed, and are then transferred in Dual inoculation and carry out extruding pelletization, squeeze out temperature Degree is for 100 DEG C to get foaming concentrate;Chemical foaming agent is diisopropyl azodiformate;Nucleating agent is mica;Lubricant is hard Resin acid butyl ester;Dispersing agent is copper stearate;Wherein, 67 parts by weight of active inorganic fiber powder, the chemical foaming agent of acicular texture 18 parts by weight, 6 parts by weight of nucleating agent, 5 parts by weight of lubricant, 4 parts by weight of dispersing agent, 15 parts by weight of polypropylene.
Test method are as follows:
Expanded polypropylene melt strength: being added polypropylene matrix according to mass ratio 10% for foaming concentrate made from comparative example 1, Mixing, which squeezes out, is made expanded polypropylene sample, measures foaming poly- third using German Rheotens71.97 type solution strength tester The melt strength of alkene sample;
Expanded polypropylene density: polypropylene matrix, mixing is added according to mass ratio 10% in foaming concentrate made from comparative example 1 It squeezes out and expanded polypropylene sample is made, the density of expanded polypropylene sample is measured using density tester.
The melt strength of expanded polypropylene made from the foaming concentrate addition of the comparative example 1 measured as the above method and close Degree is as shown in table 1.
Table 1:

Claims (10)

1. a kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, which comprises the following steps:
(1) the inorfil powder with acicular texture is added in solvent, is uniformly dispersed and suspension is made, is subsequently added into surface Activating agent carries out microwave treatment, and 3 ~ 8h is then freeze-dried at -10 ~ -30 DEG C, and the active inorganic fiber powder of acicular texture is made Body;
(2) high amylopectin starch, ammonium persulfate/urea are caused system to be scattered in supercritical fluid, is sufficiently swollen, and carried and draw Hair agent fully penetrates into inside starch granules, is subsequently added into active inorganic fiber powder made from step (1), carries out heating and adds Pressure reaction, so that introducing large number of grafted chain on needle-shaped type inorfil surface, is filtered, washed after reaction, dries, Needle-shaped type inorfil/high amylopectin starch composite material is made;
(3) by needle-shaped type inorfil/high amylopectin starch composite material made from step (2) and chemical foaming agent, nucleating agent, profit Lubrication prescription, dispersing agent, polypropylene are added in high-speed mixer and are uniformly mixed, and are then transferred in Dual inoculation squeeze out and make Grain, extrusion temperature are 80-100 DEG C and use high fondant-strength foaming concentrate to get polypropylene expanded.
2. a kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, feature exist according to claim 1 In: step (1) the inorfil powder with acicular texture is calcium carbonate crystal whisker, wollastonite, sepiolite, shepardite, glass At least one of glass fiber, pyrophillite, nepheline, the solvent are one of deionized water, dehydrated alcohol, and the surface is living Property agent be cetyl trimethylammonium bromide.
3. a kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, feature exist according to claim 1 In: the microwave power of step (1) described microwave treatment is 680 ~ 720W, and treatment temperature is 60 ~ 80 DEG C, handles 5 ~ 6min of time.
4. a kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, feature exist according to claim 1 In: in step (1), 20 ~ 40 parts by weight of inorfil powder, 56 ~ 78 parts by weight of solvent, surfactant with acicular texture 2 ~ 4 parts by weight.
5. a kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, feature exist according to claim 1 In: step (2) supercritical fluid be supercritical water, supercritical carbon dioxide, supercritical nitrogen, one in Supercritical Ethanol Kind.
6. a kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, feature exist according to claim 1 In: the temperature of step (2) the heating compressive reaction is 60 ~ 70 DEG C, and pressure is 20 ~ 25MPa, and the time is 3 ~ 5h.
7. a kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, feature exist according to claim 1 In: in step (2), 14 ~ 18 parts by weight of high amylopectin starch, 2 ~ 4 parts by weight of ammonium persulfate, 2 ~ 4 parts by weight of urea, supercritical fluid 44 ~ 57 parts by weight, 25 ~ 30 parts by weight of active inorganic fiber powder.
8. a kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, feature exist according to claim 1 It is that sodium bicarbonate, ammonium hydrogen carbonate, 2,2'- azodiisobutyronitrile, azoformic acid two are different in: step (3) chemical foaming agent One of propyl ester, the nucleating agent be talcum powder, calcium carbonate, silica, calcium oxide, magnesia, carbon black, in mica extremely Few one kind, the lubricant are at least one of stearic acid, butyl stearate, oleamide, ethylene bis stearamide, described point Powder is at least one of barium stearate, zinc stearate, calcium stearate, cadmium stearate, magnesium stearate, copper stearate.
9. a kind of polypropylene expanded preparation method with high fondant-strength foaming concentrate, feature exist according to claim 1 In: in step (3), needle-shaped type inorfil/61 ~ 73 parts by weight of high amylopectin starch composite material, 15 ~ 20 weight of chemical foaming agent Part, 5 ~ 8 parts by weight of nucleating agent, 4 ~ 6 parts by weight of lubricant, 3 ~ 5 parts by weight of dispersing agent, polypropylene 10-20 parts by weight.
It is foamed 10. one kind that any one of claim 1 ~ 9 preparation method is prepared is polypropylene expanded with high fondant-strength Masterbatch.
CN201910349795.XA 2019-04-28 2019-04-28 A kind of polypropylene expanded high fondant-strength foaming concentrate and preparation method thereof Withdrawn CN110028695A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910349795.XA CN110028695A (en) 2019-04-28 2019-04-28 A kind of polypropylene expanded high fondant-strength foaming concentrate and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910349795.XA CN110028695A (en) 2019-04-28 2019-04-28 A kind of polypropylene expanded high fondant-strength foaming concentrate and preparation method thereof

Publications (1)

Publication Number Publication Date
CN110028695A true CN110028695A (en) 2019-07-19

Family

ID=67240683

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910349795.XA Withdrawn CN110028695A (en) 2019-04-28 2019-04-28 A kind of polypropylene expanded high fondant-strength foaming concentrate and preparation method thereof

Country Status (1)

Country Link
CN (1) CN110028695A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102604223A (en) * 2012-03-16 2012-07-25 武汉富蒂亚新型材料有限公司 Polypropylene resin foam concentrate and preparation method thereof
CN105566831A (en) * 2016-03-07 2016-05-11 惠州市环美盛新材料有限公司 Water-foamed, antibacterial and air-permeable microporous film masterbatch, film and preparation method thereof
CN106432897A (en) * 2015-08-07 2017-02-22 现代自动车株式会社 Foamable masterbatch and polyolefin resin composition with excellent expandability and direct metallizing property
US20180002505A1 (en) * 2016-07-04 2018-01-04 Hyundai Motor Company Polypropylene resin composition with improved foaming capability

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102604223A (en) * 2012-03-16 2012-07-25 武汉富蒂亚新型材料有限公司 Polypropylene resin foam concentrate and preparation method thereof
CN106432897A (en) * 2015-08-07 2017-02-22 现代自动车株式会社 Foamable masterbatch and polyolefin resin composition with excellent expandability and direct metallizing property
CN105566831A (en) * 2016-03-07 2016-05-11 惠州市环美盛新材料有限公司 Water-foamed, antibacterial and air-permeable microporous film masterbatch, film and preparation method thereof
US20180002505A1 (en) * 2016-07-04 2018-01-04 Hyundai Motor Company Polypropylene resin composition with improved foaming capability

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
施悦 等: "《环境氧化还原处理技术原理与应用》", 31 August 2013, 哈尔滨工业大学出版社 *

Similar Documents

Publication Publication Date Title
CN111138755A (en) Low-density low-dielectric polypropylene composite material and preparation method thereof
CN110655702A (en) Preparation method of polyethylene foam material and polyethylene foam material prepared by same
CN103030875A (en) Modified PP (polypropylene) foaming material and forming method thereof
CN109705465B (en) Hollow polyolefin foam material and preparation method thereof
CN107987387B (en) High-modulus polypropylene/cage-type silsesquioxane micro-foaming composite material and preparation method thereof
CN104204071A (en) Polypropylene composition for foaming
CN108530752B (en) Micro-foaming continuous long glass fiber reinforced polypropylene composite material and preparation method and application thereof
CN110229372A (en) Low molding energy consumption polypropylene foamed particles of one kind and preparation method thereof
CN104629176A (en) Open-celled polypropylene microcellular foaming sheet and production method thereof
CN106750998A (en) A kind of novel flame-retardant PP foam material and preparation method thereof
CN111393812A (en) P L A/EVA supercritical foaming composite material and preparation method thereof
CN106432887B (en) The composition and preparation method and purposes of a kind of polyalkene foaming master batch
CN107446154B (en) High-performance micro-foaming master batch and preparation method and application thereof
CN106883446A (en) Fretting map functional agglomerate composition and preparation method thereof and refrigerator foaming plate
CN106117741A (en) A kind of polyethylene composite foam material and preparation method thereof
CN114230916B (en) Polypropylene composite material and preparation method and application thereof
CN110128741B (en) Polyolefin foam material and preparation method thereof
CN103951866A (en) Foamed polyolefin composition and polyolefin foamed material, preparation method of foamed polyolefin composition as well as product prepared by adopting foamed polyolefin composition
CN104004259A (en) Foamed polyolefin composition, polyolefin foamed material, preparation method thereof and product prepared from composition
CN107383636A (en) A kind of low thermal conductivity expanded particle and preparation method thereof
CN110028695A (en) A kind of polypropylene expanded high fondant-strength foaming concentrate and preparation method thereof
WO2024066971A1 (en) Polypropylene micro-foaming material, and preparation method therefor and use thereof
CN109265825B (en) Polypropylene or polypropylene compound foamed product and preparation method thereof
CN104479165B (en) A kind of method for preparing polypropylene low temperature solid phase expanded bead
CN111777817A (en) Phase-change energy storage material and preparation method and application thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WW01 Invention patent application withdrawn after publication

Application publication date: 20190719

WW01 Invention patent application withdrawn after publication