CN109401719A - A kind of pair of solidification polyurethane hot melt and preparation method thereof and application method - Google Patents
A kind of pair of solidification polyurethane hot melt and preparation method thereof and application method Download PDFInfo
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- CN109401719A CN109401719A CN201811124667.7A CN201811124667A CN109401719A CN 109401719 A CN109401719 A CN 109401719A CN 201811124667 A CN201811124667 A CN 201811124667A CN 109401719 A CN109401719 A CN 109401719A
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J175/00—Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
- C09J175/04—Polyurethanes
- C09J175/14—Polyurethanes having carbon-to-carbon unsaturated bonds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/30—Low-molecular-weight compounds
- C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
- C08G18/3203—Polyhydroxy compounds
- C08G18/3206—Polyhydroxy compounds aliphatic
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
- C08G18/4236—Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups
- C08G18/4238—Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups derived from dicarboxylic acids and dialcohols
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4854—Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
- C08G18/66—Compounds of groups C08G18/42, C08G18/48, or C08G18/52
- C08G18/6603—Compounds of groups C08G18/42, C08G18/48, or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
- C08G18/6607—Compounds 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
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/67—Unsaturated compounds having active hydrogen
- C08G18/671—Unsaturated compounds having only one group containing active hydrogen
- C08G18/672—Esters of acrylic or alkyl acrylic acid having only one group containing active hydrogen
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J11/00—Features of adhesives not provided for in group C09J9/00, e.g. additives
- C09J11/02—Non-macromolecular additives
- C09J11/04—Non-macromolecular additives inorganic
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Inorganic Chemistry (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
The present invention discloses a kind of pair of solidification polyurethane hot melt and preparation method thereof and application method, the raw material components of the polyurethane hot melt include major ingredient and auxiliary material;Major ingredient includes following raw material components: polyester polyol, polyether polyol, chemical modifier, isocyanates and chain extender;Auxiliary material includes following raw material components: physical modification agent, catalyst, silane coupling agent, photoinitiator, antioxidant and white carbon black.The shortcomings that technical solution UV light in the application/wet double solidification polyurethane hot melts both have the advantages of moisture-curable polyurethane hot melt adhesive and ultra-violet curing hot melt adhesive, while improving;It uses chemical modifier synthesis UV light/wet pair of solidification polyurethane hot melts and is aided with acrylate diluent blending, improves the compatibility between each component, obtains initial bond strength height, good toughness, weatherability by force and convenient for the polyurethane hot melt product of construction.
Description
Technical field
The present invention relates to a kind of polyurethane hot melts, more particularly to a kind of double solidification polyurethane hot melts and its preparation side
Method and application method.
Background technique
Hot melt adhesive is solid at room temperature, is heated to certain temperature and is just melt into sticky liquid, after being cooled to room temperature again
Become solid, and there is very strong bonding effect.
UV photocuring refers to that under the ultraviolet light of wavelength appropriate and intensity, photoinitiator resolves into rapidly freedom
Base causes the process that unsaturated compounds are cross-linked to form macromolecular.UV curing rate is fast, energy- and time-economizing, and pollution is few, properties of product
It is excellent, but it can be only applied to transparent material, while development and application short period, technology are immature.Moisturecuring refer to-
NCO is the hot melt adhesive of end group, melting coated on after substrate surface ,-NCO and substrate surface micro-moisture or other containing active hydrogen
Compound or moisture in air reaction, form cross-linked network, enhance the process of cohesive force.Moisturecuring is easy to operate, final to be bonded
Intensity is high, environmentally protective, mature production technology, but curing time is long, and initial bonding strength is lower.
Summary of the invention
In view of the foregoing deficiencies of prior art, the purpose of the present invention is to provide a kind of double solidification polyurethane hot melts
And preparation method thereof and application method, for solving the problems of the prior art.
In order to achieve the above objects and other related objects, the present invention obtains by the following technical programs.
The present invention provides a kind of double solidification polyurethane hot melts, and double raw material components for solidifying polyurethane hot melt include
Major ingredient and auxiliary material;
Wherein, major ingredient includes following raw material components: polyester polyol, polyether polyol, chemical modifier, isocyanates and
Chain extender;
Auxiliary material includes following raw material components: physical modification agent, catalyst, silane coupling agent, photoinitiator, antioxidant and white
Carbon black.
Preferably, polycarbonate polyol in major ingredient, polyether polyol, isocyanates, chemical modifier and chain extender
Molar ratio is 1:(0.1~0.5): (1~10): (0.1~1): (0.1~1).
It is highly preferred that polycarbonate polyol, polyether polyol, isocyanates, chemical modifier and chain extender in major ingredient
Molar ratio are as follows: 1:(0.1~0.5): (2~6): (0.2~0.8): (0.2~0.8).
Preferably, by major ingredient be 100 parts on the basis of count, the dosage of the physical modification agent is 15~40 parts by weight.It is more excellent
Selection of land, the dosage of the physical modification agent are 20~35 parts by weight.
Preferably, by major ingredient be 100 parts on the basis of count, the dosage of the silane coupling agent is no more than 5 parts by weight.More preferably
The dosage on ground, the silane coupling agent is no more than 3 parts by weight.
Preferably, by major ingredient be 100 parts on the basis of count, the dosage of the photoinitiator is no more than 5 parts by weight.More preferably
The dosage on ground, the photoinitiator is no more than 3 parts by weight.
Preferably, by major ingredient be 100 parts on the basis of count, the dosage of the antioxidant is no more than 5 parts by weight.It is highly preferred that
The dosage of the antioxidant is no more than 3 parts by weight.
Preferably, by major ingredient be 100 parts on the basis of count, the dosage of the white carbon black is no more than 5 parts by weight.It is highly preferred that
The dosage of the white carbon black is no more than 3 parts by weight.Preferably, the additional amount of the catalyst is catalytic amount.Preferably, described
The number-average molecular weight of polyester polyol is 2000~5000.It is highly preferred that the polyester polyol is molecular weight 2000 and 3000
Mixture, the mol ratio of the two is n2000:n3000=1:(0.1~0.3).
It is highly preferred that the polyester polyol is polyadipate -1,6- hexylene glycol esterdiol.
Preferably, the polyether polyol is polytetrahydrofuran diol.
Preferably, the number-average molecular weight of the polyether polyol is 1500~3500.
Preferably, the isocyanates is in 4,4' methyl diphenylene diisocyanate and isophorone diisocyanate
It is one or two kinds of.When the isocyanates is the mixture of the two, 4,4' methyl diphenylene diisocyanates and isophorone
The molar ratio of diisocyanate is 1:(0.1~0.5).
Preferably, the chemical modifier is methacrylic acid 2- (4- benzoyl -3- hydroxyphenoxy) ethyl ester.
Preferably, the chain extender is 1,4-butanediol.
Preferably, the physical modification agent is the mixture of tackifying resin and diluting monomer.It is highly preferred that diluting monomer with
The mass ratio of tackifying resin is 1:(0.6~2.0).
Preferably, the diluting monomer is tetrahydrofuran acrylate (referred to as THFA) and ethoxyethoxyethyl third
One or both of olefin(e) acid ester (referred to as EOEOEA).It is highly preferred that the diluting monomer is the mixture of the two.More preferably
The mass ratio of ground, the tetrahydrofuran acrylate and ethoxyethoxyethyl acrylate is 1:(0.6~2.0).
Preferably, the tackifying resin is acrylic resin.It is highly preferred that the number-average molecular weight of the acrylic resin is
2000~4000.
Preferably, the catalyst is organotin catalysts.It is highly preferred that the catalyst is di lauric dibutyl
Tin.
Preferably, the silane coupling agent be selected from γ-methacryloxypropyl trimethoxy silane (KH-550),
γ-glycidyl ether oxygen propyl trimethoxy silicane (KH-560) and γ-methacryloxypropyl trimethoxy silane
One of (KH-570) or it is a variety of.
Preferably, the photoinitiator is benzoin ethyl ether (referred to as BEE), diphenyl (2,4,6- trimethylbenzoyl)
One of phosphine oxide (referred to as TPO) and 1- hydroxycyclohexyl phenyl ketone (referred to as HCPK) are a variety of.It is highly preferred that when being
When a variety of, the usage amount of diphenyl (2,4,6- trimethylbenzoyl) phosphine oxide is no more than the 80% of benzoin ethyl ether;Or 1- hydroxyl
The usage amount of cyclohexyl phenyl ketone is no more than the 80% of benzoin ethyl ether.
Preferably, the antioxidant is one or both of antioxidant 1010 and antioxidant 1076.
Preferably, the white carbon black is fumed silica.
Preferably, the water content of raw material components described herein is respectively less than 1g/kg.It can buy and have reached water content
It is required that raw material components, or raw material components are carried out dehydrating by means such as heating, heating in vacuum.
The invention also discloses double preparation methods for solidifying polyurethane hot melt as described above, include the following steps:
1) polyester polyol, polyether polyol, physical modification agent and antioxidant are mixed;
2) isocyanates is added and catalyst is reacted;
3) chemical modifier, chain extender and silane coupling agent is added to be reacted;
4) white carbon black is added, photoinitiator is added when avoiding ultraviolet light, then reacted, then discharges simultaneously
Encapsulation.
Preferably, the method also includes carrying out heat aging step to acquisition product after encapsulation.It is highly preferred that curing
Shi Jia
Hot temperature is 70 DEG C~100 DEG C.It is highly preferred that the curing time is no less than 3h.
Preferably, thermal dehydration processing is carried out to raw material components in step 1).
Preferably, step 2), 3) or/and 4) in, when charging, carries out under inert gas shielding atmosphere.To avoid introducing water
Or vapor.
Preferably, step 2), 3) or/and 4) in, the temperature of reaction is 20~100 DEG C.
Preferably, step 2), 3) or/and 4) in, reaction carries out under vacuum conditions.
Preferably, packaging container or packaging selection ultraviolet light are unable to permeable material in step 4).Such as aluminium foil bag.
Preferably, in step 4), discharging carries out under the conditions of inert gas shielding.
Preferably, in step 4), system temperature is 70~100 DEG C when discharging.
The invention also discloses double application methods for solidifying polyurethane hot melt as described above, are first heated to melting completely
Melt, be then glued and irradiated under ultraviolet, places consolidation to reaching finally viscous intensity.Preferably, heating temperature be 80~
130℃。
Technical solution UV light in the application/wet double solidification polyurethane hot melts have moisture-curable polyurethane hot melt adhesive and ultraviolet
The advantages of solidifying hot-melt adhesive, while the shortcomings that both improve;It selects methacrylic acid 2- (4- benzoyl -3- hydroxy benzenes
Oxygroup) ethyl ester as the double solidification polyurethane hot melts of chemical modifier synthesis UV light/wet and is aided with acrylate diluent and is blended,
The compatibility between each component is improved, obtains initial bond strength height, good toughness, weatherability by force and convenient for the polyurethane of construction heat
Melten gel product.
Specific embodiment
Embodiments of the present invention are illustrated by particular specific embodiment below, those skilled in the art can be by this explanation
Content disclosed by book is understood other advantages and efficacy of the present invention easily.
Before further describing the specific embodiments of the present invention, it should be appreciated that protection scope of the present invention is not limited to down
State specific specific embodiment;It is also understood that term used in the embodiment of the present invention is specific specific in order to describe
Embodiment, rather than limiting the scope of protection of the present invention.The test method of actual conditions is not specified in the following example,
Usually according to normal condition, or according to condition proposed by each manufacturer.
When embodiment provides numberical range, it should be appreciated that except non-present invention is otherwise noted, two ends of each numberical range
Any one numerical value can be selected between point and two endpoints.Unless otherwise defined, the present invention used in all technologies and
Scientific term is identical as the normally understood meaning of those skilled in the art of the present technique.Except specific method, equipment used in embodiment,
Outside material, grasp and record of the invention according to those skilled in the art to the prior art can also be used and this
Any method, equipment and the material of the similar or equivalent prior art of method described in inventive embodiments, equipment, material come real
The existing present invention.
Embodiment 1
(1) 2000 polyhexamethylene adipate glycol 90.00g of molecular weight, 3000 polyadipate hexylene glycol of molecular weight are weighed
Esterdiol 13.50g, 2000 polytetrahydrofuran ether glycol 18.00g of molecular weight, antioxidant 1010 1.70g, acrylic resin
17.00g, tetrahydrofuran acrylate 13.80g and ethoxyethoxyethyl acrylate 8.29g are added to four mouthfuls of 1.0L
In flask, 110~120 DEG C are heated with stirring to, the vacuum dehydration 120min at absolute pressure 80Pa.
(2) 80 DEG C are cooled to, nitrogen is passed through and releases vacuum, 4,4 '-methyl diphenylene diisocyanates (MDI) are added
37.80g, isophorone diisocyanate (IPDI) 3.73g, catalyst dibutyltin dilaurylate 1.70g are then shut off nitrogen
And at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(3) it is passed through nitrogen and releases vacuum, methacrylic acid 2- (4- benzoyl -3- hydroxyphenoxy) ethyl ester is added
5.50g, chain extender 1,4-butanediol 1.42g, silane coupling agent KH-560 1.50g, KH-570 1.05g, is then shut off nitrogen
And at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(4) it is passed through nitrogen and releases vacuum, fumed silica 1.70g and benzoin ethyl ether 3.91g is added, is then shut off nitrogen
Gas and at 85~95 DEG C, absolute pressure continues to stir 30min under the conditions of being less than 100Pa, quickly discharging and seals under nitrogen protection
Loaded in aluminium foil bag.
(5) 6h is cured after packaging in 80-85 DEG C of baking oven, products obtained therefrom is labeled as A.
Embodiment 2
(1) 2000 polyhexamethylene adipate glycol 90.00g of molecular weight, 3000 polyadipate hexylene glycol of molecular weight are weighed
Esterdiol 20.25g, 2000 polytetrahydrofuran ether glycol 9.00g of molecular weight, antioxidant 1010 1.72g, acrylic resin
25.72g, tetrahydrofuran acrylate 10.97g, ethoxyethoxyethyl acrylate 16.45g are added to four mouthfuls of 1.0L
In flask, 110~120 DEG C are heated with stirring to, the vacuum dehydration 120min at absolute pressure 80Pa.
(2) 80 DEG C are cooled to, nitrogen is passed through and releases vacuum, 4,4 '-methyl diphenylene diisocyanates (MDI) are added
33.36g, isophorone diisocyanate (IPDI) 9.88g, catalyst dibutyltin dilaurylate 1.72g is then shut off nitrogen
And at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(3) it is passed through nitrogen and releases vacuum, methacrylic acid 2- (4- benzoyl -3- hydroxyphenoxy) ethyl ester is added
7.71g, chain extender 1,4-butanediol 1.22g, silane coupling agent KH-560 0.92g, KH-570 0.80g, is then shut off nitrogen
And at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(4) be passed through nitrogen and release vacuum, be added fumed silica 1.72g, benzoin ethyl ether 3.20g and diphenyl (2,
4,6- trimethylbenzoyls) phosphine oxide 1.95g, be then shut off nitrogen and at 85~95 DEG C, absolute pressure be less than under the conditions of 100Pa after
Continuous stirring 30min quickly discharging and is packaged in aluminium foil bag under nitrogen protection;
(5) 8h is cured after packaging in 80-85 DEG C of baking oven, products obtained therefrom is labeled as B.
Embodiment 3
(1) 2000 polyhexamethylene adipate glycol 90.00g of molecular weight, 3000 polyadipate hexylene glycol of molecular weight are weighed
Esterdiol 27.0g, 2000 polytetrahydrofuran ether glycol 27.0g of molecular weight, antioxidant 1010 2.00g, acrylic resin
24.0g, tetrahydrofuran acrylate 20.00g and ethoxyethoxyethyl acrylate 19.99g are added to four mouthfuls of 1.0L
In flask, 110~120 DEG C are heated with stirring to, the vacuum dehydration 120min at absolute pressure 80Pa.
(2) 80 DEG C are cooled to, nitrogen is passed through and releases vacuum, 4,4 '-methyl diphenylene diisocyanates (MDI) are added
41.34g, isophorone diisocyanate (IPDI) 9.18g and catalyst dibutyltin dilaurylate 2.00g, are then shut off nitrogen
Gas and at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(3) it is passed through nitrogen and releases vacuum, methacrylic acid 2- (4- benzoyl -3- hydroxyphenoxy) ethyl ester is added
4.41g, chain extender 1,4-butanediol 1.01g, silane coupling agent KH-560 0.60g and KH-570 0.40g, are then shut off nitrogen
And at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(4) it is passed through nitrogen and releases vacuum, fumed silica 2.00g, benzoin ethyl ether 2.50g and 1- hydroxy cyclohexylphenyl is added
Base phenyl ketone 1.10g, is then shut off nitrogen and at 85~95 DEG C, and absolute pressure continues to stir under the conditions of being less than 100Pa
30min quickly discharging and is packaged in aluminium foil bag under nitrogen protection.
(5) 8h is cured after packaging in 80-85 DEG C of baking oven, products obtained therefrom is labeled as C.
Embodiment 4
(1) 2000 polyhexamethylene adipate glycol 90.00g of molecular weight, 3000 polyadipate hexylene glycol of molecular weight are weighed
Esterdiol 33.75g, 2000 polytetrahydrofuran ether glycol 22.5g of molecular weight, antioxidant 1010 2.04g, acrylic resin
28.46g, tetrahydrofuran acrylate 12.29g, ethoxyethoxyethyl acrylate 8.03g are added to four mouthfuls of burnings of 1.0L
In bottle, 110~120 DEG C are heated with stirring to, the vacuum dehydration 120min at absolute pressure 80Pa.
(2) 80 DEG C are cooled to, nitrogen is passed through and releases vacuum, 4,4 '-methyl diphenylene diisocyanates (MDI) are added
40.85g, isophorone diisocyanate (IPDI) 6.43g, catalyst dibutyltin dilaurylate 2.04g are then shut off nitrogen
And at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(3) it is passed through nitrogen and releases vacuum, methacrylic acid 2- (4- benzoyl -3- hydroxyphenoxy) ethyl ester is added
8.82g, chain extender 1,4-butanediol 0.81g, silane coupling agent KH-560 0.52g and KH-570 0.50g, are then shut off nitrogen
And at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(4) it is passed through nitrogen and releases vacuum, fumed silica 2.04g, benzoin ethyl ether 2.5g and 1- hydroxy cyclohexylphenyl is added
Base phenyl ketone 0.75g, is then shut off nitrogen and at 85~95 DEG C, and absolute pressure continues to stir under the conditions of being less than 100Pa
30min quickly discharging and is packaged in aluminium foil bag under nitrogen protection.
(5) 7h is cured after packaging in 85 DEG C of baking oven, products obtained therefrom is labeled as D.
Embodiment 5
(1) 2000 polyhexamethylene adipate glycol 90.00g of molecular weight, 3000 polyadipate hexylene glycol of molecular weight are weighed
Esterdiol 40.5g, 2000 polytetrahydrofuran ether glycol 13.5g of molecular weight, antioxidant 1010 2.07g, acrylic resin
26.84g, tetrahydrofuran acrylate 16.89g, ethoxyethoxyethyl acrylate 20.27g are added to four mouthfuls of 1.0L
In flask, 110~120 DEG C are heated with stirring to, the vacuum dehydration 120min at absolute pressure 80Pa.
(2) 80 DEG C are cooled to, nitrogen is passed through and releases vacuum, 4,4 '-methyl diphenylene diisocyanates (MDI) are added
39.26g, isophorone diisocyanate (IPDI) 14.94g, catalyst dibutyltin dilaurylate 2.07g are then shut off nitrogen
Gas and at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(3) it is passed through nitrogen and releases vacuum, methacrylic acid 2- (4- benzoyl -3- hydroxyphenoxy) ethyl ester is added
6.60g, chain extender 1,4-butanediol 1.63g, silane coupling agent KH-560 1.2g and KH-570 0.86g, are then shut off nitrogen
And at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(4) be passed through nitrogen and release vacuum, be added fumed silica 2.07g, benzoin ethyl ether 2.3g and diphenyl (2,4,
6- trimethylbenzoyl) phosphine oxide 1.83g, it is then shut off nitrogen and at 85~95 DEG C, absolute pressure continues under the conditions of being less than 100Pa
30min is stirred, quickly discharging and is packaged in aluminium foil bag under nitrogen protection.
(5) 7h is cured after packaging in 85 DEG C of baking oven, products obtained therefrom is labeled as E.
Comparative example 1
(1) 2000 polyhexamethylene adipate glycol 90.00g of molecular weight, 3000 polyadipate hexylene glycol of molecular weight are weighed
Esterdiol 27.0g, 2000 polytetrahydrofuran ether glycol 9.0g of molecular weight, antioxidant 1010 1.72g, acrylic resin
25.50g, tetrahydrofuran acrylate 14.51g, ethoxyethoxyethyl acrylate 11.0g are added to four mouthfuls of burnings of 1.0L
In bottle, 110~120 DEG C are heated with stirring to, the vacuum dehydration 120min at absolute pressure 80Pa.
(2) 80 DEG C are cooled to, nitrogen is passed through and releases vacuum, 4,4 '-methyl diphenylene diisocyanates (MDI) are added
30.88g, isophorone diisocyanate (IPDI) 11.49g, catalyst dibutyltin dilaurylate 1.7g are then shut off nitrogen
And at 85~95 DEG C, absolute pressure reacts 60min under the conditions of being less than 100Pa;
(3) be passed through nitrogen release vacuum, be added chain extender 1,4-butanediol 1.63g, silane coupling agent KH-560 1.0g and
KH-570 0.70g, is then shut off nitrogen and at 85~95 DEG C, and absolute pressure reacts 60min under the conditions of being less than 100Pa;
(4) it is passed through nitrogen and releases vacuum, fumed silica 1.7g is added, is then shut off nitrogen and at 85~95 DEG C, absolutely
Pressure is less than and continues to stir 30min under the conditions of 100Pa, quickly discharging and is packaged in aluminium foil bag under nitrogen protection.
(5) 7h is cured after packaging in 85 DEG C of baking oven, products obtained therefrom is labeled as F.
Embodiment 6
Polycarbonate polyol, polyether polyol, isocyanates, chemical modifier and chain extender in major ingredient in the present embodiment
Molar ratio be 1:0.2:2:0.2:0.5.
In the present embodiment auxiliary material, by major ingredient be 100 parts on the basis of count, physical modification agent be 20 parts by weight;Silane coupling agent
For 5 parts by weight;Photoinitiator is 3 parts by weight;Antioxidant is 3 parts by weight;White carbon black is 3 parts by weight;The dosage of catalyst is to urge
Agent amount.
In the present embodiment the step of the preparation method of hot melt adhesive and parameter is same as Example 1.
Embodiment 7
Polycarbonate polyol, polyether polyol, isocyanates, chemical modifier and chain extender in major ingredient in the present embodiment
Molar ratio be 1:0.5:6:0.5:0.2.
In the present embodiment auxiliary material, by major ingredient be 100 parts on the basis of count, physical modification agent be 35 parts by weight;Silane coupling agent
For 3 parts by weight;Photoinitiator is 2 parts by weight;Antioxidant is 2 parts by weight;White carbon black is 4 parts by weight;The dosage of catalyst is to urge
Agent amount.
In the present embodiment the step of the preparation method of hot melt adhesive and parameter is same as Example 1
Embodiment 8
Polycarbonate polyol, polyether polyol, isocyanates, chemical modifier and chain extender in major ingredient in the present embodiment
Molar ratio be 1:0.4:6:0.3:0.8.
In the present embodiment auxiliary material, by major ingredient be 100 parts on the basis of count, physical modification agent be 25 parts by weight;Silane coupling agent
For 2 parts by weight;Photoinitiator is 3 parts by weight;Antioxidant is 4 parts by weight;White carbon black is 3 parts by weight;The dosage of catalyst is to urge
Agent amount.
In the present embodiment the step of the preparation method of hot melt adhesive and parameter is same as Example 1.
Embodiment 9
Polycarbonate polyol, polyether polyol, isocyanates, chemical modifier and chain extender in major ingredient in the present embodiment
Molar ratio be 1:0.5:2:0.8:0.6.
In the present embodiment auxiliary material, by major ingredient be 100 parts on the basis of count, physical modification agent be 30 parts by weight;Silane coupling agent
For 4 parts by weight;Photoinitiator is 2 parts by weight;Antioxidant is 2 parts by weight;White carbon black is 3 parts by weight;The dosage of catalyst is to urge
Agent amount.
In the present embodiment the step of the preparation method of hot melt adhesive and parameter is same as Example 1.
Sample test
(1) melt viscosity:
It is measured at 120 DEG C, reference standard HG/T3660-1999, intact polyurethane hot melt will be sealed and be put in 110 DEG C
30min is kept in the syringe heater of HL-YR123.Hot melt adhesive pours into rapidly DV-II+pro at molten fluid at this time
In sleeve in Viscometer viscosimeter viscosity apparatus, 10.0 ± 0.2g is weighed, temperature is set at 120 DEG C and is kept for 20 minutes,
So that hot melt adhesive internal temperature uniformly and deaeration.At a temperature of 120 DEG C, the constant temperature melt viscosity of hot melt adhesive is measured.
(2) adhesive strength:
Be 25mm wide in specification, on the glass plate of 100mm long, 5mm thickness, on the direction grown along glass plate, and away from
Uniformly coating width is 1mm at two edge 6mm, long to be greater than 25mm, with a thickness of 2 above-mentioned hot melt adhesive adhesive tape of 0.3mm.Use 0.15mm
The steel wire of diameter controls the thickness of adhesive tape, at once with the glass plate of second piece of same specification with the direction of vertical first piece of glass plate
Two pieces of glass plates are glued together, and with 1.5 Kgfs pressing weld 15 seconds, with the high voltage mercury lamp radiation 10s of 1000W, so
It is placed on the adhesive strength tested respectively after 15min and 72h in climatic chamber, the respectively initial adhesive strength of the sample and end
Viscous intensity.
(3) tensile strength and elongation at break:
Reference standard ASTM D638 sample preparation, glue sample are made into the wide 6mm of sheet type, thick 0.5mm, dumbbell shaped.Sample is existed
(humidity 60%, 25 DEG C of temperature) places 72h in climatic chamber, carries out further according to ASTM D638 standard the method to glue sample
Tensile strength and elongation at break test, tensile speed 100mm/min, test temperature are 25 DEG C.Gained tensile strength and disconnected
It splits elongation and is denoted as TS respectively0And EL0。
(4) weatherability is tested: reference standard ASTM D638 sample preparation, glue sample are made into the wide 6mm of sheet type, thick 0.5mm,
Dumbbell shaped.By sample, (humidity 60%, 25 DEG C of temperature) places 72h in climatic chamber, is then placed in high/low temperature hydrothermal aging
Atmospheric exposure test 240h is carried out in case, which is carried out automatically by ageing oven, and the specific steps are elder generations in 80 DEG C of temperature, humidity
10h is tested under the conditions of 80%, then tests 10h under conditions of -40 DEG C, humidity 80%, is then alternately gone down until total examination
Testing the time is 240h.Carry out tensile strength and elongation at break test again after the test, tensile speed 100mm/min is surveyed
Trying temperature is 25 DEG C.Gained tensile strength and elongation at break are denoted as TS respectively1And EL1.The weatherability of each sample is stretched strong by it
Change rate (α) and elongation at break change rate (β) are spent to characterize, and calculation formula is as follows:
1 embodiment and comparative example properties of product test value of table
As can be seen from Table 1, the initial adhesive strength of product and viscous eventually in the embodiment of the present invention 1~5 and embodiment 6~9
Intensity is higher by 424%~581% and 8.6%~36.7% than comparative example product F respectively, shows that Light Curing can significantly improve
Its initial adhesive strength, and the addition of chemical modifier also has certain good effect to its raising for gluing intensity eventually.On the other hand, originally
The tensile strength of product and elongation at break are higher by than comparative example product (F) respectively in inventive embodiments 1~5 and embodiment 6~9
4.7% and 21.5% or more, especially product A~E test post-tensioning intensity and elongation at break through high/low temperature hydrothermal aging
Change rate is also more much smaller than product F, shows that the toughness of product and weather-proof also can be improved by the way that chemical modifier is added in the present invention
Property.
The above-described embodiments merely illustrate the principles and effects of the present invention, and is not intended to limit the present invention.It is any ripe
The personage for knowing this technology all without departing from the spirit and scope of the present invention, carries out modifications and changes to above-described embodiment.Cause
This, institute is complete without departing from the spirit and technical ideas disclosed in the present invention by those of ordinary skill in the art such as
At all equivalent modifications or change, should be covered by the claims of the present invention.
Claims (10)
1. a kind of double solidification polyurethane hot melts, which is characterized in that the raw material components of the polyurethane hot melt include major ingredient and
Auxiliary material;
Wherein, major ingredient includes following raw material components: polyester polyol, polyether polyol, chemical modifier, isocyanates and chain extension
Agent;
Auxiliary material includes following raw material components: physical modification agent, catalyst, silane coupling agent, photoinitiator, antioxidant and hard charcoal
It is black.
2. double solidification polyurethane hot melt according to claim 1, which is characterized in that including one of following feature or
It is a variety of:
The number-average molecular weight of the polyester polyol is 2000~5000;
The polyester polyol is polyadipate -1,6-HD esterdiol;
The polyether polyol is polytetrahydrofuran diol;
The number-average molecular weight of the polyether polyol is 1500~3500;
The isocyanates is one or both of 4,4' methyl diphenylene diisocyanate and isophorone diisocyanate;
The chemical modifier is methacrylic acid 2- (4- benzoyl -3- hydroxyphenoxy) ethyl ester;
The chain extender is 1,4- butanediol.
3. double solidification polyurethane hot melt according to claim 1, which is characterized in that including one of following feature or
It is a variety of:
The physical modification agent is the mixture of tackifying resin and diluting monomer;
The mass ratio of diluting monomer and tackifying resin is 1:(0.6~2.0);
The diluting monomer is one or both of tetrahydrofuran acrylate and ethoxyethoxyethyl acrylate;
The tackifying resin is acrylic resin;
The catalyst is organotin catalysts;
The silane coupling agent is selected from γ-methacryloxypropyl trimethoxy silane, γ-glycidyl ether oxygen propyl three
One of methoxy silane and γ-methacryloxypropyl trimethoxy silane are a variety of;
The photoinitiator is benzoin ethyl ether, diphenyl (2,4,6- trimethylbenzoyl) phosphine oxide and 1- hydroxycyclohexylphenyl
One of ketone is a variety of;
The antioxidant is one or both of antioxidant 1010 and antioxidant 1076;
The white carbon black is fumed silica;
The water content of the raw material components is respectively less than 1g/kg.
4. a kind of prepare double methods for solidifying polyurethane hot melt as described in any one of claims 1 to 3, include the following steps:
1) polyester polyol, polyether polyol, physical modification agent and antioxidant are mixed;
2) isocyanates is added and catalyst is reacted;
3) chemical modifier, chain extender and silane coupling agent is added to be reacted;
4) white carbon black is added, photoinitiator is added when avoiding ultraviolet light, then reacted, then discharged and sealed
Dress.
5. according to the method described in claim 4, it is characterized in that, the method also includes the product progress to obtaining after encapsulation
Heat aging step.
6. according to the method described in claim 5, it is characterised in that it includes one of following feature or a variety of:
Heating temperature is 70 DEG C~100 DEG C when curing;
Curing time is no less than 3h.
7. according to the method described in claim 4, it is characterised in that it includes one of following feature or a variety of:
Step 2), 3) or/and 4) in, when charging, carries out under inert gas shielding atmosphere;
Step 2), 3) or/and 4) in, the temperature of reaction is 20~100 DEG C;
Step 2), 3) or/and 4) in, reaction carries out under vacuum conditions.
8. according to the method described in claim 4, it is characterised in that it includes one of following feature or a variety of:
In step 4), packaging container or packaging selection ultraviolet light are unable to permeable material;
In step 4), discharging carries out under the conditions of inert gas shielding;
In step 4), system temperature is 70 DEG C~100 DEG C when discharging.
9. a kind of double application methods for solidifying polyurethane hot melt as claimed in any one of claims 1 to 3, are first heated to completely
Then melting is glued and irradiates under ultraviolet, place consolidation to reaching finally viscous intensity.
10. double application method for solidifying polyurethane hot melt according to claim 9, which is characterized in that heating temperature is
80~130 DEG C.
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WO2021212358A1 (en) * | 2020-04-22 | 2021-10-28 | 北京理工大学 | Hot-melt reaction type polyurethane material, preparation method therefor and use thereof |
WO2023196484A1 (en) * | 2022-04-07 | 2023-10-12 | Basf Se | Dual curable pressure sensitive adhesive |
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CN111154067A (en) * | 2020-01-21 | 2020-05-15 | 江苏景宏新材料科技有限公司 | Low-viscosity high-peel-strength UV (ultraviolet) curing composite adhesive and preparation method thereof |
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