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 PDF

Info

Publication number
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
Authority
CN
China
Prior art keywords
hot melt
polyurethane hot
antioxidant
raw material
variety
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.)
Granted
Application number
CN201811124667.7A
Other languages
Chinese (zh)
Other versions
CN109401719B (en
Inventor
曾作祥
宗泽刚
李健坤
薛为岚
贾成良
王伟
秦平
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.)
SHANGHAI ZHIGUAN HIGH POLYMER MATERIAL Co Ltd
East China University of Science and Technology
Original Assignee
SHANGHAI ZHIGUAN HIGH POLYMER MATERIAL Co Ltd
East China University of Science and Technology
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 SHANGHAI ZHIGUAN HIGH POLYMER MATERIAL Co Ltd, East China University of Science and Technology filed Critical SHANGHAI ZHIGUAN HIGH POLYMER MATERIAL Co Ltd
Priority to CN201811124667.7A priority Critical patent/CN109401719B/en
Publication of CN109401719A publication Critical patent/CN109401719A/en
Application granted granted Critical
Publication of CN109401719B publication Critical patent/CN109401719B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J175/00Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
    • C09J175/04Polyurethanes
    • C09J175/14Polyurethanes having carbon-to-carbon unsaturated bonds
    • 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
    • C08G18/30Low-molecular-weight compounds
    • C08G18/32Polyhydroxy compounds; Polyamines; Hydroxyamines
    • C08G18/3203Polyhydroxy compounds
    • C08G18/3206Polyhydroxy compounds aliphatic
    • 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
    • C08G18/42Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/4236Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups
    • C08G18/4238Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups derived from dicarboxylic acids and dialcohols
    • 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
    • C08G18/48Polyethers
    • C08G18/4854Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group
    • 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
    • C08G18/65Low-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
    • 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
    • C08G18/67Unsaturated compounds having active hydrogen
    • C08G18/671Unsaturated compounds having only one group containing active hydrogen
    • C08G18/672Esters of acrylic or alkyl acrylic acid having only one group containing active hydrogen
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/02Non-macromolecular additives
    • C09J11/04Non-macromolecular additives inorganic

Landscapes

  • 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

A kind of pair of solidification polyurethane hot melt and preparation method thereof and application method
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.
CN201811124667.7A 2018-09-26 2018-09-26 Dual-curing polyurethane hot melt adhesive as well as preparation method and application method thereof Active CN109401719B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811124667.7A CN109401719B (en) 2018-09-26 2018-09-26 Dual-curing polyurethane hot melt adhesive as well as preparation method and application method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811124667.7A CN109401719B (en) 2018-09-26 2018-09-26 Dual-curing polyurethane hot melt adhesive as well as preparation method and application method thereof

Publications (2)

Publication Number Publication Date
CN109401719A true CN109401719A (en) 2019-03-01
CN109401719B CN109401719B (en) 2021-09-10

Family

ID=65465245

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811124667.7A Active CN109401719B (en) 2018-09-26 2018-09-26 Dual-curing polyurethane hot melt adhesive as well as preparation method and application method thereof

Country Status (1)

Country Link
CN (1) CN109401719B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110229644A (en) * 2019-06-05 2019-09-13 格丽泰新材料科技(苏州)有限公司 A kind of reaction type polyurethane hot-melt adhesive and its preparation method and application
CN110452655A (en) * 2019-07-31 2019-11-15 东莞市澳中电子材料有限公司 A kind of light/wet double solidification polyurethane hot melts and preparation method thereof
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
WO2021009565A1 (en) * 2019-07-17 2021-01-21 Arkema France (meth)acrylate-functionalized oligomers and methods of preparing and using such oligomers
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

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1153094B1 (en) * 1999-02-16 2004-04-28 PPG Industries Ohio, Inc. Substrate covered by several coating layers
DE60021361D1 (en) * 1999-03-31 2005-08-25 Cray Valley Sa NETWORKED MICROPARTICLES, PROCESS FOR THEIR PRODUCTION AND THEIR USE
CN101372530A (en) * 2008-08-08 2009-02-25 中国工程物理研究院化工材料研究所 Aqueous photo-curing polyurethane resin and preparation thereof
CN101560319A (en) * 2008-04-12 2009-10-21 三菱瓦斯化学株式会社 Acrylic resin composition and molded product using the same
CN101768419A (en) * 2008-12-31 2010-07-07 上海康达化工有限公司 Non-solvent polyurethane laminating adhesive with high initial stick force and preparation method and application thereof
CN103289631A (en) * 2013-06-21 2013-09-11 上海智冠高分子材料有限公司 Preparation method for reactive polyurethane hot melt composition and applications thereof
CN104449533A (en) * 2014-12-31 2015-03-25 广州市白云化工实业有限公司 Reactive polyurethane hot melt adhesive for electronic appliance and preparing method thereof
CN104531045A (en) * 2015-01-06 2015-04-22 烟台德邦科技有限公司 Preparing method for reaction type polyurethane hot melt adhesive with multiple curing modes
CN104769071A (en) * 2012-07-06 2015-07-08 博斯蒂克股份公司 Use of an adhesive composition to provide a bonding in a wet environment
CN104974707A (en) * 2015-07-07 2015-10-14 上海天洋热熔粘接材料股份有限公司 Wet cured polyurethane hot melt adhesive and preparation method thereof
CN106459313A (en) * 2014-04-21 2017-02-22 汉高知识产权控股有限责任公司 Curable adhesive compositions and use thereof
CN107384293A (en) * 2017-06-28 2017-11-24 苏州奥斯汀新材料科技有限公司 A kind of preparation method of thermoplastic polyurethane hot melt adhesive
CN108084952A (en) * 2017-12-30 2018-05-29 烟台泰盛精化科技有限公司 A kind of UV is pressure-sensitive/the double preparation methods for curing polyurethane hot melts of moisture
CN108368221A (en) * 2016-01-06 2018-08-03 株式会社Adeka Optical thin film made of aqueous urethane resin composition and use the composition

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1153094B1 (en) * 1999-02-16 2004-04-28 PPG Industries Ohio, Inc. Substrate covered by several coating layers
DE60021361D1 (en) * 1999-03-31 2005-08-25 Cray Valley Sa NETWORKED MICROPARTICLES, PROCESS FOR THEIR PRODUCTION AND THEIR USE
CN101560319A (en) * 2008-04-12 2009-10-21 三菱瓦斯化学株式会社 Acrylic resin composition and molded product using the same
CN101372530A (en) * 2008-08-08 2009-02-25 中国工程物理研究院化工材料研究所 Aqueous photo-curing polyurethane resin and preparation thereof
CN101768419A (en) * 2008-12-31 2010-07-07 上海康达化工有限公司 Non-solvent polyurethane laminating adhesive with high initial stick force and preparation method and application thereof
CN104769071A (en) * 2012-07-06 2015-07-08 博斯蒂克股份公司 Use of an adhesive composition to provide a bonding in a wet environment
CN103289631A (en) * 2013-06-21 2013-09-11 上海智冠高分子材料有限公司 Preparation method for reactive polyurethane hot melt composition and applications thereof
CN106459313A (en) * 2014-04-21 2017-02-22 汉高知识产权控股有限责任公司 Curable adhesive compositions and use thereof
CN104449533A (en) * 2014-12-31 2015-03-25 广州市白云化工实业有限公司 Reactive polyurethane hot melt adhesive for electronic appliance and preparing method thereof
CN104531045A (en) * 2015-01-06 2015-04-22 烟台德邦科技有限公司 Preparing method for reaction type polyurethane hot melt adhesive with multiple curing modes
CN104974707A (en) * 2015-07-07 2015-10-14 上海天洋热熔粘接材料股份有限公司 Wet cured polyurethane hot melt adhesive and preparation method thereof
CN108368221A (en) * 2016-01-06 2018-08-03 株式会社Adeka Optical thin film made of aqueous urethane resin composition and use the composition
CN107384293A (en) * 2017-06-28 2017-11-24 苏州奥斯汀新材料科技有限公司 A kind of preparation method of thermoplastic polyurethane hot melt adhesive
CN108084952A (en) * 2017-12-30 2018-05-29 烟台泰盛精化科技有限公司 A kind of UV is pressure-sensitive/the double preparation methods for curing polyurethane hot melts of moisture

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
YUKIHIRO NOMURA: "Synthesis of Novel Moisture-Curable Polyurethanes", 《INTERSCIENCE》 *
宋彩雨: "活性稀释剂对紫外光固化树脂性能的影响", 《化学与黏合》 *
李红强: "《胶粘原理、技术及应用》", 30 January 2014, 华南理工大学出版社 *
邓舜扬: "《新型塑料材料·工艺·配方》", 30 January 2000, 中国轻工业出版社 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110229644A (en) * 2019-06-05 2019-09-13 格丽泰新材料科技(苏州)有限公司 A kind of reaction type polyurethane hot-melt adhesive and its preparation method and application
CN110229644B (en) * 2019-06-05 2021-09-03 格丽泰新材料科技(苏州)有限公司 Reactive polyurethane hot melt adhesive and preparation method and application thereof
WO2021009565A1 (en) * 2019-07-17 2021-01-21 Arkema France (meth)acrylate-functionalized oligomers and methods of preparing and using such oligomers
CN110452655A (en) * 2019-07-31 2019-11-15 东莞市澳中电子材料有限公司 A kind of light/wet double solidification polyurethane hot melts and preparation method thereof
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
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

Also Published As

Publication number Publication date
CN109401719B (en) 2021-09-10

Similar Documents

Publication Publication Date Title
CN109401719A (en) A kind of pair of solidification polyurethane hot melt and preparation method thereof and application method
CN109370503A (en) A kind of polycarbonate type is double to solidify polyurethane hot melts and preparation method thereof
US11891550B2 (en) Curable and optically clear pressure sensitive adhesives and uses thereof
US7189781B2 (en) Moisture curable, radiation curable sealant composition
CN109370507A (en) A kind of three proofings adhesive and preparation method thereof of low viscosity environmental protection UV/ moisture dual cure
EP2944662B1 (en) Thermoplastic polyurethane hot melt adhesive
CN103305174B (en) Preparation method of light/humidity dual-curing polyurethane hot melt adhesive
CN110172327B (en) Photocuring composite adhesive and production process thereof
CN105916899B (en) Optics of liquids adhesive composition
CN104271163A (en) Breathable self-adhesive articles
CN102464952A (en) UV-curable optical resin adhesive composition
CN107163898A (en) A kind of preparation method of high temperature resistant type damp solidifying polyurethane PUR
WO2022227445A1 (en) Organosilicon-modified acrylate, silane-modified polyether adhesive, and preparation method therefor
CN115386329B (en) UV moisture dual-curing adhesive for electronic components
CN110204685A (en) A kind of three-functionality-degree polyurethane acrylate resin and its preparation method and application
CN109575871A (en) A kind of ultraviolet radioactive and the adhesive composition of moisture dual cure and application thereof
CN113462341B (en) Double-component solvent-free reaction type polyurethane hot melt adhesive
CN104974709A (en) UV moisture dual-curing type acrylate pressure-sensitive adhesive and preparation method thereof
CN115433537B (en) High-cohesiveness ultraviolet light curing adhesive and preparation method and application thereof
CN110343497A (en) A kind of photovoltaic back solvent-free polyurethane adhesive, preparation method and photovoltaic back
WO2023123747A1 (en) Hydrogen abstraction photoinitiator, preparation method therefor, and use thereof
CN102102007A (en) Radiation cured adhesive for indium tin oxide (ITO) circuit and module protection
CN113604187A (en) Biodegradable dual-curing reaction type polyurethane hot melt adhesive
CN108368212A (en) Solidification compound, adhesive linkage, transparent facestock, laminated body and image display device
CN113667429B (en) Ultraviolet-curing heat-conducting adhesive tape 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
GR01 Patent grant
GR01 Patent grant