CN106832887A - A kind of repeatedly foaming TPU composites and preparation method thereof - Google Patents

A kind of repeatedly foaming TPU composites and preparation method thereof Download PDF

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Publication number
CN106832887A
CN106832887A CN201710093503.1A CN201710093503A CN106832887A CN 106832887 A CN106832887 A CN 106832887A CN 201710093503 A CN201710093503 A CN 201710093503A CN 106832887 A CN106832887 A CN 106832887A
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foaming
tpu
weight portions
raw material
preparation
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何建雄
王良
王一良
杨博
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Dongguan Xionglin New Materials Technology Co Ltd
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Dongguan Xionglin New Materials Technology Co Ltd
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L75/00Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • C08L75/04Polyurethanes
    • C08L75/06Polyurethanes from polyesters
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/4009Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
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    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
    • C08G18/66Compounds of groups C08G18/42, C08G18/48, or C08G18/52
    • C08G18/6603Compounds of groups C08G18/42, C08G18/48, or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
    • C08G18/6607Compounds of groups C08G18/42, C08G18/48, or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203
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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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    • 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
    • C08J2375/00Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2375/04Polyurethanes
    • C08J2375/06Polyurethanes from polyesters
    • 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
    • C08J2409/00Characterised by the use of homopolymers or copolymers of conjugated diene hydrocarbons
    • C08J2409/06Copolymers with styrene
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    • 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
    • C08J2425/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Derivatives of such polymers
    • C08J2425/02Homopolymers or copolymers of hydrocarbons
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    • C08J2425/06Polystyrene
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    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/02Flame or fire retardant/resistant
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/14Applications used for foams
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    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • 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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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

The present invention provides a kind of repeatedly foaming TPU composites and preparation method thereof, and the raw material of the foaming TPU composites includes following composition:5 10 weight portion composite foamable agents, 80 95 weight portion TPU particles, 13 parts by weight of flame retardant, 13 weight portion foam stabilisers and 25 weight portion antioxidant.The present invention has obtained multiple expanded material by adding composite foamable agent in TPU particles, the multiple foaming at 40 250 DEG C can be completed, its product surface can't see obvious hole, better appearance, and effect of damping, noise reduction can be played, and product has good mechanical performance, pliability is good, processing characteristics is good, can be prepared as foam films product, has a good application prospect.

Description

A kind of repeatedly foaming TPU composites and preparation method thereof
Technical field
The invention belongs to technical field of polymer materials, it is related to a kind of foaming TPU composites and preparation method thereof, especially relates to And a kind of repeatedly foaming TPU composites and preparation method thereof.
Background technology
Expanded material refer to can material interior evaporation produce bubble make porous mass foaming material, can be with For making foamed plastics, foam rubber, foamed product etc., these expanded materials have well using preceding in multiple fields Scape.
CN103030841A discloses a kind of Novel foam material, and it is equipped with auxiliary agent with pre-gelatinized cornstarch as base-material, It is prepared from by conventional foam process.The expanded material, with pre-gelatinized cornstarch as base-material, the foaming of this pure bio-based Material, can be degradable, does not produce destruction, nonpoisonous and tasteless, safety and environmental protection to environment.
CN104760179A discloses a kind of PU foaming bodies with second time of foaming function, and its raw material is:PU foaming raw materials And the foaming agent of thermal expansion type, foaming agent was uniformly mixed into black material before foaming or white material is interior.Its addition is weight Than 1-10%, PU foaming raw materials include polyurethane, polyalcohol, and polyurethane is black material, and polyalcohol is white material, the expanded material Second time of foaming can be carried out, manufactured goods weight is low and intensity is high.
In order to meet demand of the more areas for expanded material especially multiple expanded material, expect that obtaining one kind can enter The material that row repeatedly foams.
The content of the invention
In view of the shortcomings of the prior art, it is an object of the invention to provide one kind foaming TPU composites and its preparation side Method, is especially to provide a kind of repeatedly foaming TPU composites and preparation method thereof.
It is that, up to this purpose, the present invention uses following technical scheme:
On the one hand, the present invention provides a kind of foaming TPU composites, and the raw material of the foaming TPU composites is included such as Lower composition:
In the present invention system is combined using composite foamable agent with TPU particles and fire retardant, foam stabiliser and antioxidant Standby to obtain the TPU composites that foam, resulting material can repeatedly be foamed, and its product surface can't see hole, relatively more beautiful See, and effect of damping, noise reduction can be played.
In the present invention, the consumption of the composite foamable agent can be 5 weight portions, 5.5 weight portions, 6 weight portions, 6.5 weights Amount part, 7 weight portions, 7.5 weight portions, 8 weight portions, 8.5 weight portions, 9 weight portions, 9.5 weight portions or 10 weight portions, its consumption mistake I haven't seen you for ages causes that foaming effect is deteriorated, and consumption is crossed and can at most cause the larger hole of product surface producing ratio, is caused unsightly.
In the present invention, the consumption of the TPU particles can be 80 weight portions, 82 weight portions, 84 weight portions, 86 weight Part, 88 weight portions, 90 weight portions, 92 weight portions, 94 weight portions or 95 weight portions.
In the present invention, the consumption of the fire retardant can be 1.3 weight portions, 1.5 weight portions, 1.8 weight portions, 2 weight Part, 2.3 weight portions, 2.5 weight portions or 2.8 weight portions.
Preferably, the fire retardant is any one in antimony oxide, aluminium hydroxide, magnesium hydroxide or APP Or at least two combination.
In the present invention, the consumption of the foam stabiliser can be 1.3 weight portions, 1.5 weight portions, 1.8 weight portions, 2 Weight portion, 2.3 weight portions, 2.5 weight portions or 2.8 weight portions.
In the present invention, the consumption of the antioxidant can be 2.3 weight portions, 2.5 weight portions, 2.8 weight portions, 3 weight Part, 3.3 weight portions, 3.5 weight portions, 3.8 weight portions, 4 weight portions, 4.3 weight portions, 4.5 weight portions or 4.8 weight portions.
Preferably, the composite foamable agent includes the component of following mass percent:
In the present invention, the composite foamable agent can be realized being foamed under condition of different temperatures, by setting not Same blowing temperature realizes the multiple foaming of material.
In the present invention, in the composite foamable agent expandable polystyrene (EPS) content can for 40%, 41%, 42%, 43%th, 44%, 45%, 46%, 47%, 48%, 49% or 50%.
In the present invention, in the composite foamable agent EVA resin content can for 20%, 21%, 22%, 23%, 24%th, 25%, 26%, 27%, 28%, 29% or 30%.
Preferably, in the EVA resin ethylene contents be 18-25%, such as 18%, 19%, 20%, 21%, 22%, 23%th, 24% or 25%.
In the present invention, in the composite foamable agent dimethyl ether consumption can for 5%, 6%, 7%, 8%, 9% or 10%.The blowing temperature of dimethyl ether is relatively low, can at a lower temperature realize foaming.
In the present invention, in the composite foamable agent blowing agent AC -3000H content can for 10%, 11%, 12%, 13%th, 14%, 15%, 16%, 17%, 18%, 19% or 20%.
In the present invention, in the composite foamable agent foaming agent AD-300 content can for 5%, 5.5%, 6%, 6.5%th, 7%, 7.5%, 8%, 8.5%, 9%, 9.5% or 10%.
Preferably, the raw material of the TPU particles includes following component:
Prepared by adding Graphene, polystyrene, butadiene-styrene rubber in the raw material of TPU particles in the present invention Obtain TPU particles, polystyrene, the intensity and toughness of the addition enhancing TPU materials of butadiene-styrene rubber.
In the present invention, the consumption of the diisocyanate can be 50 weight portions, 51 weight portions, 52 weight portions, 53 weights Amount part, 54 weight portions, 55 weight portions, 56 weight portions, 57 weight portions, 58 weight portions, 59 weight portions or 60 weight portions.
In the present invention, the consumption of the polyalcohol can for 35 weight portions, 37 weight portions, 39 weight portions, 40 weight portions, 43 weight portions, 45 weight portions, 48 weight portions or 50 weight portions.
In the present invention, the consumption of the Graphene can for 1 weight portion, 1.5 weight portions, 2 weight portions, 2.5 weight portions, 3 weight portions, 3.5 weight portions, 4 weight portions, 4.5 weight portions or 5 weight portions.Graphene can be with the damping of reinforcing material, noise reduction work( Effect.
In the present invention, the consumption of the polystyrene can be 6 weight portions, 7 weight portions, 8 weight portions, 9 weight portions, 10 Weight portion, 11 weight portions, 12 weight portions, 13 weight portions, 14 weight portions or 15 weight portions.
In the present invention, the consumption of the butadiene-styrene rubber can be 5 weight portions, 6 weight portions, 7 weight portions, 8 weight portions, 9 Weight portion or 10 weight portions.
In the present invention, the consumption of the chain extender can be 2 weight portions, 2.5 weight portions, 3 weight portions, 4 weight portions, 5 Weight portion, 6 weight portions, 7 weight portions or 8 weight portions.
In the present invention, the consumption of the catalyst can be 1.3 weight portions, 1.5 weight portions, 1.8 weight portions, 2 weight Part, 2.3 weight portions, 2.5 weight portions or 2.8 weight portions.
Preferably, the raw material of the TPU particles includes following component:
Preferably, the diisocyanate is the mixture of toluene di-isocyanate(TDI) and hexamethylene diisocyanate, described polynary Alcohol is PEPA and PPG.
Two kinds of specific diisocyanate, both diisocyanate and two kinds of polyalcohol phase interworkings are selected in the present invention Close, be easier to control the soft section and hard section ratio of polyurethane than a kind of diisocyanate or a kind of polyalcohol is used alone, the two Mechanical property, elasticity and flexibility in enhancing polyurethane have synergy.
Preferably, the mass ratio of the toluene di-isocyanate(TDI) and hexamethylene diisocyanate is (2-5):1, such as 2:1、.3: 1、4:1 or 5:1, two kinds of specific diisocyanate are used in conjunction with each other, and can preferably adjust the wearability of polyurethane material And pliability.
Preferably, the mass ratio of PEPA and PPG is (1-4) in the polyalcohol:1, such as 1:1、 1.5:1、2:1、2.5:1、3:1、3.5:1 or 4:1.
Preferably, the weight average molecular weight of the polyalcohol be 500-3500, such as 500,1000,1500,2000,3000 or 3500, preferably 1000-2000.
Preferably, the weight average molecular weight of the polystyrene be 5000-10000, such as 5000,6000,7000,8000, 9000 or 10000.
Preferably, the chain extender is in ethylene glycol, ethylenediamine, 1,3-PD, BDO or 1,5-PD Any one or at least two combination.
Preferably, the catalyst is any in stannous octoate, two sad dibutyl tins or dibutyl tin laurate It is a kind of or at least two combination.
On the other hand, the invention provides the preparation method of foaming TPU composites as described above, methods described includes Following steps:
(1) expandable polystyrene (EPS), EVA resin, dimethyl ether, blowing agent AC -3000H, foaming agent AD-300 are mixed equal It is even, obtain composite foamable agent;
(2) diisocyanate is added in A storage tanks, polyalcohol is added in B storage tanks, chain extender and catalyst add Enter in C storage tanks, under agitation, vacuum dehydration;
(3) by the raw material pumping in step (2) to double screw extruder, while adding Graphene, polystyrene, butylbenzene Rubber, using double screw extruder reaction, granulation, obtains the TPU particles;
(4) TPU particles and fire retardant, foam stabiliser that the composite foamable agent that obtains step (1), step (3) are obtained And antioxidant is well mixed, it is cast using single screw extrusion machine, obtains described foaming TPU composites.
Preferably, temperature during step (2) described vacuum dehydration be 60-80 DEG C, such as 60 DEG C, 63 DEG C, 65 DEG C, 68 DEG C, 70 DEG C, 72 DEG C, 75 DEG C, 78 DEG C or 80 DEG C.
Preferably, the speed of step (2) described stirring be 300-1000r/min, such as 300r/min, 400r/min, 500r/min, 600r/min, 800r/min or 1000r/min.
Preferably, pressure during step (2) described vacuum dehydration be -0.3~-0.1kPa, such as -0.3kPa, - 0.28kPa, -0.25kPa, -0.23kPa, -0.2kPa, -0.18kPa, -0.15kPa, -0.13kPa or -0.1kPa.
Preferably, the feeding section temperature of step (3) described double screw extruder is 110-120 DEG C, such as 112 DEG C, 115 DEG C, 118 DEG C or 120 DEG C, mixing section temperature be 130-150 DEG C, such as 132 DEG C, 135 DEG C, 138 DEG C, 140 DEG C, 143 DEG C, 145 DEG C Or 148 DEG C, extruding zone temperature is 170-180 DEG C, such as 172 DEG C, 175 DEG C, 178 DEG C or 180 DEG C, and head temperature is 150-160 DEG C, such as 153 DEG C, 155 DEG C, 158 DEG C or 160 DEG C.
The foaming TPU composites that the present invention is prepared can repeatedly be foamed, and it can be in 40-250 DEG C of foaming Repeatedly foaming is completed in temperature range;Can carry out first time foaming at 40-60 DEG C, foamed time be 10s-30s (such as 10s, 13s, 15s, 18s, 20s, 23s, 25s, 28s or 30s), now made mainly due to the volatilization of the dimethyl ether in composite foamable agent Into foaming materials, second time of foaming can be carried out at 90-140 DEG C, now a part of expandable polystyrene (EPS) and foaming agent AD-300 Etc. can produce foaming, foamed time be 5-20min (such as 5min, 8min, 10min, 13min, 15min, 18min or 20min);Three foaming can be carried out for 150-200 DEG C in temperature, now blowing agent AC -3000H and can in composite foamable agent Expanded polystyrene (EPS) and TPU particles etc. can cause foaming, foamed time be 10-30min (such as 10min, 13min, 15min, 18min, 20min, 23min, 25min or 28min), the 4th foaming can be carried out at 220-250 DEG C, now composite foamable agent Middle blowing agent AC -3000H and EVA resin and TPU particles can cause foaming, foamed time be 1-8min (such as 2min, 3min, 4min, 5min, 6min, 7min or 8min).
Mould of different shapes such as hemispherical can be used during material of the invention is foamed, is sent out Bubble, so as to obtain product of different shapes.
In the present invention, the proportion after the foaming TPU composite one step foamings is 40-200 g/l, one step foaming times Rate is 60-95% (such as 60%, 65%, 70%, 75%, 80%, 85%, 90% or 95%);Second time of foaming multiplying power is 5- 40% (such as 5%, 8%, 10%, 15%, 18%, 20%, 25%, 30%, 35% or 40%), preferably 7-27%, three hairs Bubble rate is 10-20% (such as 10%, 13%, 15%, 18% or 20%), four expansion ratios be 5-15% (such as 5%, 7%th, 9%, 11%, 13% or 15%).
On the other hand, the present invention provides a kind of foam films, and the foam films are by the TPU composite shapes that foam as described above Into.
Foam films of the invention can be used for preparing has sandwich construction and with the product of secondary or multiple foam performance.
Relative to prior art, the invention has the advantages that:
The present invention has obtained multiple expanded material by adding composite foamable agent in TPU particles, can complete in 40- Multiple foaming at 250 DEG C, its product surface can't see obvious hole, better appearance, and can play the work(of damping, noise reduction Effect, and product has good mechanical performance, and pliability is good, and processing characteristics is good, can be prepared as foam films product, has There is good application prospect.
Specific embodiment
Technical scheme is further illustrated below by specific embodiment.Those skilled in the art should be bright , the embodiment be only to aid in understand the present invention, be not construed as to concrete restriction of the invention.
Embodiment 1
In the present embodiment, foaming TPU composites are prepared by following material composition:
The composite foamable agent includes the component of following mass percent:
The raw material of the TPU particles includes following component:
Wherein diisocyanate is the mixture of toluene di-isocyanate(TDI) and hexamethylene diisocyanate, toluene di-isocyanate(TDI) and The mass ratio of hexamethylene diisocyanate is 3:1, the polyalcohol be PEPA and PPG, wherein PEPA and The mass ratio of PPG is 2:1, the weight average molecular weight of the polyalcohol is 1500, the weight average molecular weight of the polystyrene It is 5000, chain extender is ethylene glycol, catalyst is stannous octoate.
The preparation method of the foaming TPU composites is as follows:
(1) expandable polystyrene (EPS), EVA resin, dimethyl ether, blowing agent AC -3000H, foaming agent AD-300 are mixed equal It is even, obtain composite foamable agent;
(2) diisocyanate is added in A storage tanks, polyalcohol is added in B storage tanks, chain extender and catalyst add Enter in C storage tanks, 500r/min rotating speeds stirring under, under -0.3kPa pressure in 70 DEG C of vacuum dehydrations;
(3) by the raw material pumping in step (2) to double screw extruder, while adding Graphene, polystyrene, butylbenzene Rubber, using double screw extruder reaction, granulation, obtains the TPU particles, and the feeding section temperature of double screw extruder is 110 DEG C, mixing section temperature is 130 DEG C, and it is 170 DEG C to go out section temperature, and head temperature is 150 DEG C;
(4) TPU particles and fire retardant, foam stabiliser that the composite foamable agent that obtains step (1), step (3) are obtained And antioxidant is well mixed, it is cast using single screw extrusion machine, obtains described foaming TPU composites, single screw rod temperature It it is 210 DEG C, die head temperature is 200 DEG C.
Embodiment 2
In the present embodiment, foaming TPU composites are prepared by following material composition:
The composite foamable agent includes the component of following mass percent:
The raw material of the TPU particles includes following component:
Wherein diisocyanate is the mixture of toluene di-isocyanate(TDI) and hexamethylene diisocyanate, toluene di-isocyanate(TDI) and The mass ratio of hexamethylene diisocyanate is 4:1, the polyalcohol be PEPA and PPG, wherein PEPA and The mass ratio of PPG is 3:1, the number-average molecular weight of the polyalcohol is 1000, the weight average molecular weight of the polystyrene It is 10000, chain extender is ethylenediamine, catalyst is the fourth tin of moon silicic acid two.
The preparation method of the foaming TPU composites is as follows:
(1) expandable polystyrene (EPS), EVA resin, dimethyl ether, blowing agent AC -3000H, foaming agent AD-300 are mixed equal It is even, obtain composite foamable agent;
(2) diisocyanate is added in A storage tanks, polyalcohol is added in B storage tanks, chain extender and catalyst add Enter in C storage tanks, 600r/min rotating speeds stirring under, under -0.2kPa pressure in 80 DEG C of vacuum dehydrations;
(3) by the raw material pumping in step (2) to double screw extruder, while adding Graphene, polystyrene, butylbenzene Rubber, using double screw extruder reaction, granulation, obtains the TPU particles, and the feeding section temperature of double screw extruder is 120 DEG C, mixing section temperature is 150 DEG C, and it is 180 DEG C to go out section temperature, and head temperature is 160 DEG C;
(4) TPU particles and fire retardant, foam stabiliser that the composite foamable agent that obtains step (1), step (3) are obtained And antioxidant is well mixed, it is cast using single screw extrusion machine, obtains described foaming TPU composites, single screw rod temperature It it is 208 DEG C, die head temperature is 198 DEG C.
Embodiment 3
In the present embodiment, foaming TPU composites are prepared by following material composition:
The composite foamable agent includes the component of following mass percent:
The raw material of the TPU particles includes following component:
Wherein diisocyanate is the mixture of toluene di-isocyanate(TDI) and hexamethylene diisocyanate, toluene di-isocyanate(TDI) and The mass ratio of hexamethylene diisocyanate is 5:1, the polyalcohol be PEPA and PPG, wherein PEPA and The mass ratio of PPG is 4:The number-average molecular weight of polyalcohol described in 1 is 1500, the weight average molecular weight of the polystyrene It is 5000, chain extender is BDO, catalyst is two sad two fourths tin.
The preparation method of the foaming TPU composites is as follows:
(1) expandable polystyrene (EPS), EVA resin, dimethyl ether, blowing agent AC -3000H, foaming agent AD-300 are mixed equal It is even, obtain composite foamable agent;
(2) diisocyanate is added in A storage tanks, polyalcohol is added in B storage tanks, chain extender and catalyst add Enter in C storage tanks, 500r/min rotating speeds stirring under, under -0.1kPa pressure in 70 DEG C of vacuum dehydrations;
(3) by the raw material pumping in step (2) to double screw extruder, while adding Graphene, polystyrene, butylbenzene Rubber, using double screw extruder reaction, granulation, obtains the TPU particles, and the feeding section temperature of double screw extruder is 120 DEG C, mixing section temperature is 140 DEG C, and it is 175 DEG C to go out section temperature, and head temperature is 155 DEG C;
(4) TPU particles and fire retardant, foam stabiliser that the composite foamable agent that obtains step (1), step (3) are obtained And antioxidant is well mixed, it is cast using single screw extrusion machine, obtains described foaming TPU composites, single screw rod temperature It it is 205 DEG C, die head temperature is 195 DEG C.
Embodiment 4
In the present embodiment, foaming TPU composites are prepared by following material composition:
The composite foamable agent includes the component of following mass percent:
The raw material of the TPU particles includes following component:
Wherein diisocyanate is the mixture of toluene di-isocyanate(TDI) and hexamethylene diisocyanate, toluene di-isocyanate(TDI) and The mass ratio of hexamethylene diisocyanate is 2:1, the polyalcohol be PEPA and PPG, wherein PEPA and The mass ratio of PPG is 1:The number-average molecular weight of polyalcohol described in 1 is 1500, the weight average molecular weight of the polystyrene It is 5000, chain extender is BDO, catalyst is stannous octoate.
The preparation method of the foaming TPU composites is as follows:
(1) expandable polystyrene (EPS), EVA resin, dimethyl ether, blowing agent AC -3000H, foaming agent AD-300 are mixed equal It is even, obtain composite foamable agent;
(2) diisocyanate is added in A storage tanks, polyalcohol is added in B storage tanks, chain extender and catalyst add Enter in C storage tanks, 600r/min rotating speeds stirring under, under -0.3kPa pressure in 70 DEG C of vacuum dehydrations;
(3) by the raw material pumping in step (2) to double screw extruder, while adding Graphene, polystyrene, butylbenzene Rubber, using double screw extruder reaction, granulation, obtains the TPU particles, and the feeding section temperature of double screw extruder is 110 DEG C, mixing section temperature is 130 DEG C, and it is 170 DEG C to go out section temperature, and head temperature is 150 DEG C;
(4) TPU particles and fire retardant, foam stabiliser that the composite foamable agent that obtains step (1), step (3) are obtained And antioxidant is well mixed, it is cast using single screw extrusion machine, obtains described foaming TPU composites, single screw rod temperature It it is 205 DEG C, die head temperature is 195 DEG C.
Comparative example 1
The comparative example be the difference is that only with embodiment 1, and composite foamable agent is not used in foaming TPU composites, Remaining raw material is same as Example 1 with raw material dosage and preparation method.
Comparative example 2
The comparative example the difference is that only that the consumption of composite foamable agent is in foaming TPU composites with embodiment 1 3 weight portions, remaining raw material is same as Example 1 with raw material dosage and preparation method.
Comparative example 3
The comparative example the difference is that only that the consumption of composite foamable agent is in foaming TPU composites with embodiment 1 12 weight portions, remaining raw material is same as Example 1 with raw material dosage and preparation method.
Comparative example 4
The comparative example be the difference is that only with embodiment 1, and polystyrene and butylbenzene are added without in the raw material of TPU particles Rubber, remaining raw material is same as Example 1 with raw material dosage and preparation method.
Comparative example 5
The comparative example the difference is that only that diisocyanate is single toluene di-isocyanate(TDI) with embodiment 1, its Remaining raw material and raw material dosage and preparation method and condition are same as Example 1.
Comparative example 6
The comparative example the difference is that only that diisocyanate is single hexamethylene diisocyanate with embodiment 1, remaining Raw material and raw material dosage and preparation method and condition are same as Example 1.
Comparative example 7
The comparative example the difference is that only with embodiment 1, the quality of toluene di-isocyanate(TDI) and hexamethylene diisocyanate Than being 1:2, remaining raw material and raw material dosage and preparation method and condition are same as Example 1.
Comparative example 8
The comparative example the difference is that only with embodiment 1, the quality of toluene di-isocyanate(TDI) and hexamethylene diisocyanate Than being 1:1, remaining raw material and raw material dosage and preparation method and condition are same as Example 1.
Comparative example 9
The comparative example the difference is that only that the polyalcohol is single PPG with embodiment 1, and remaining is former Material and raw material dosage and preparation method and condition are same as Example 1.
Comparative example 10
The comparative example the difference is that only that the polyalcohol is single PEPA with embodiment 1, and remaining is former Material and raw material dosage and preparation method and condition are same as Example 1.
Comparative example 11
The comparative example the difference is that only that the mass ratio of PEPA and PPG is 1 with embodiment 1: 2, remaining raw material and raw material dosage and preparation method and condition are same as Example 1.
Comparative example 12
The comparative example the difference is that only that the mass ratio of PEPA and PPG is 6 with embodiment 1: 1, remaining raw material and raw material dosage and preparation method and condition are same as Example 1.
Comparative example 13
The comparative example the difference is that only that the weight average molecular weight of the polyalcohol is 400, and remaining is former with embodiment 1 Material and raw material dosage and preparation method and condition are same as Example 1.
Comparative example 14
The comparative example the difference is that only that the weight average molecular weight of the polyalcohol is 4000, and remaining is former with embodiment 1 Material and raw material dosage and preparation method and condition are same as Example 1.
The tensile strength of the TPU composites prepared to embodiment 1-5 and comparative example 1-14, elongation at break with And foam performance is tested, its test result is as shown in table 1.
Table 1
It refers to that can carry out first time foaming at 40-60 DEG C to be capable of achieving four foaming at 40-250 DEG C described in table 1, during foaming Between be 10s-30s;Second time of foaming can be carried out at 90-140 DEG C, foamed time is 5-20min, three can be carried out at 150-200 DEG C Secondary foaming, foamed time is 10-30min;The 4th foaming can be carried out at 220-250 DEG C, foamed time is 1-8min.
As can be seen from Table 1, the present invention has obtained multiple foaming material by adding composite foamable agent in TPU particles Material, can complete the multiple foaming at 40-250 DEG C, and its product surface can't see obvious hole, better appearance, and can be with Effect of damping, noise reduction is played, and product has good mechanical performance, and pliability is good, and processing characteristics is good, can make Standby is foam films product, is had a good application prospect.
Applicant state, the present invention illustrated by above-described embodiment multiple foaming TPU composites of the invention and its Preparation method, but the invention is not limited in above-described embodiment, that is, do not mean that the present invention has to rely on above-described embodiment ability Implement.Person of ordinary skill in the field it will be clearly understood that any improvement in the present invention, to each raw material of product of the present invention etc. Effect replacement and addition, selection of concrete mode of auxiliary element etc., within the scope of all falling within protection scope of the present invention and disclosing.

Claims (10)

1. a kind of foaming TPU composites, it is characterised in that the raw material of the foaming TPU composites includes following composition:
2. foaming TPU composites according to claim 1, it is characterised in that the composite foamable agent includes following matter Measure the component of percentage:
3. foaming TPU composites according to claim 2, it is characterised in that ethylene contents are in the EVA resin 18-25%.
4. foaming TPU composites according to any one of claim 1-3, it is characterised in that the original of the TPU particles Material includes following component:
5. foaming TPU composites according to claim 4, it is characterised in that the raw material of the TPU particles includes following Composition:
Preferably, the diisocyanate is the mixture of toluene di-isocyanate(TDI) and hexamethylene diisocyanate, and the polyalcohol is PEPA and PPG;
Preferably, the mass ratio of the toluene di-isocyanate(TDI) and hexamethylene diisocyanate is (2-5):1;
Preferably, the mass ratio of PEPA and PPG is (1-4) in the polyalcohol:1;
Preferably, the weight average molecular weight of the polyalcohol is 500-3500, preferably 1000-2000;
Preferably, the weight average molecular weight of the polystyrene is 5000-10000;
Preferably, the chain extender is appointing in ethylene glycol, ethylenediamine, 1,3-PD, BDO or 1,5-PD Meaning it is a kind of or at least two combinations;
Preferably, the catalyst is any one in stannous octoate, two sad dibutyl tins or dibutyl tin laurate Or at least two combination.
6. foaming TPU composites according to any one of claim 1-5, it is characterised in that the fire retardant is three Aoxidize in two antimony, aluminium hydroxide, magnesium hydroxide or APP any one or at least two combination.
7. the preparation method of the foaming TPU composites according to any one of claim 1-6, it is characterised in that described Method is comprised the following steps:
(1) expandable polystyrene (EPS), EVA resin, dimethyl ether, blowing agent AC -3000H, foaming agent AD-300 are well mixed, are obtained To composite foamable agent;
(2) diisocyanate is added in A storage tanks, polyalcohol is added in B storage tanks, chain extender and catalyst are added to In C storage tanks, under agitation, vacuum dehydration;
(3) by the raw material pumping in step (2) to double screw extruder, while adding Graphene, polystyrene, butylbenzene rubber Glue, using double screw extruder reaction, granulation, obtains the TPU particles;
(4) TPU particles that the composite foamable agent that obtains step (1), step (3) are obtained and fire retardant, foam stabiliser and Antioxidant is well mixed, and described foaming TPU composites are obtained using single screw extrusion machine curtain coating.
8. preparation method according to claim 7, it is characterised in that temperature during step (2) described vacuum dehydration is 60- 80℃;
Preferably, the speed of step (2) described stirring is 300-1000r/min;
Preferably, pressure during step (2) described vacuum dehydration is -0.3~-0.1kPa.
9. the preparation method according to claim 7 or 8, it is characterised in that the feeding of step (3) described double screw extruder Duan Wendu is 110-120 DEG C, and mixing section temperature is 130-150 DEG C, and extruding zone temperature is 170-180 DEG C, and head temperature is 150- 160℃;The extruder temperature of the single screw extrusion machine described in step (4) is 190-220 DEG C, and die head temperature is 180-200 DEG C.
10. a kind of foam films, it is characterised in that the foam films are answered as the foaming TPU as any one of claim 1-6 Condensation material is formed.
CN201710093503.1A 2017-02-21 2017-02-21 A kind of repeatedly foaming TPU composites and preparation method thereof Pending CN106832887A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107383854A (en) * 2017-08-04 2017-11-24 南通德亿新材料有限公司 A kind of preparation method of the micro- air bag elastomeric material of thermoplastic polyurethane
CN107599338A (en) * 2017-10-23 2018-01-19 广东富盛新材料股份有限公司 A kind of preparation method of light composite material
CN108503946A (en) * 2018-05-03 2018-09-07 东莞市雄林新材料科技股份有限公司 A kind of bladders expanded material and preparation method thereof
CN108559057A (en) * 2018-05-03 2018-09-21 东莞市雄林新材料科技股份有限公司 A kind of NEW TYPE OF COMPOSITE expanded material and preparation method thereof
CN109135258A (en) * 2018-08-23 2019-01-04 惠州市顺利包装制品有限公司 A kind of environment-friendly type foamed plastics and processing method
WO2021135378A1 (en) * 2019-12-31 2021-07-08 苏州桐力光电股份有限公司 Graphene-based polyurethane porous nanometer material and preparation method therefor

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101624452A (en) * 2009-08-13 2010-01-13 陈雅君 Method for producing thermoplastic urethane foam
CN102276785A (en) * 2011-07-12 2011-12-14 山东奥邦聚氨酯有限公司 Low-density foamed thermoplastic polyurethane elastic body and preparation process thereof
CN103642200A (en) * 2013-12-20 2014-03-19 烟台开发区新龙华包装材料有限公司 Foaming thermoplastic polyurethane bead and preparation method thereof
CN105348665A (en) * 2015-12-11 2016-02-24 绍兴文理学院元培学院 Composite TPU and EPS expandable resin and preparing method thereof
CN105884998A (en) * 2016-04-14 2016-08-24 美瑞新材料股份有限公司 Foamed type TPU (thermoplastic polyurethane elastomer) material and preparation method thereof
CN106243681A (en) * 2016-08-02 2016-12-21 陕西理工大学 A kind of preparation method of Boehmeria crystallite/graphene nanometer sheet modified TPU microperforated sheet

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101624452A (en) * 2009-08-13 2010-01-13 陈雅君 Method for producing thermoplastic urethane foam
CN102276785A (en) * 2011-07-12 2011-12-14 山东奥邦聚氨酯有限公司 Low-density foamed thermoplastic polyurethane elastic body and preparation process thereof
CN103642200A (en) * 2013-12-20 2014-03-19 烟台开发区新龙华包装材料有限公司 Foaming thermoplastic polyurethane bead and preparation method thereof
CN105348665A (en) * 2015-12-11 2016-02-24 绍兴文理学院元培学院 Composite TPU and EPS expandable resin and preparing method thereof
CN105884998A (en) * 2016-04-14 2016-08-24 美瑞新材料股份有限公司 Foamed type TPU (thermoplastic polyurethane elastomer) material and preparation method thereof
CN106243681A (en) * 2016-08-02 2016-12-21 陕西理工大学 A kind of preparation method of Boehmeria crystallite/graphene nanometer sheet modified TPU microperforated sheet

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107383854A (en) * 2017-08-04 2017-11-24 南通德亿新材料有限公司 A kind of preparation method of the micro- air bag elastomeric material of thermoplastic polyurethane
WO2019024589A1 (en) * 2017-08-04 2019-02-07 南通德亿新材料有限公司 Preparation method for thermoplastic polyurethane micro air bag elastomer material
US11472084B2 (en) 2017-08-04 2022-10-18 Nantong De New Material Co., Ltd. Preparation method for thermoplastic polyurethane micro air bag elastomer material
CN107599338A (en) * 2017-10-23 2018-01-19 广东富盛新材料股份有限公司 A kind of preparation method of light composite material
CN107599338B (en) * 2017-10-23 2019-06-28 广东富盛新材料股份有限公司 A kind of preparation method of light composite material
CN108503946A (en) * 2018-05-03 2018-09-07 东莞市雄林新材料科技股份有限公司 A kind of bladders expanded material and preparation method thereof
CN108559057A (en) * 2018-05-03 2018-09-21 东莞市雄林新材料科技股份有限公司 A kind of NEW TYPE OF COMPOSITE expanded material and preparation method thereof
CN108559057B (en) * 2018-05-03 2021-02-12 东莞市雄林新材料科技股份有限公司 Novel composite foam material and preparation method thereof
CN108503946B (en) * 2018-05-03 2021-04-02 东莞市雄林新材料科技股份有限公司 Foaming material for bladder and preparation method thereof
CN109135258A (en) * 2018-08-23 2019-01-04 惠州市顺利包装制品有限公司 A kind of environment-friendly type foamed plastics and processing method
WO2021135378A1 (en) * 2019-12-31 2021-07-08 苏州桐力光电股份有限公司 Graphene-based polyurethane porous nanometer material and preparation method therefor

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Application publication date: 20170613