WO2006115138A1 - イソシアネート基末端ウレタンプレポリマーおよびその製造方法、並びに前記ウレタンプレポリマーを含む接着剤 - Google Patents
イソシアネート基末端ウレタンプレポリマーおよびその製造方法、並びに前記ウレタンプレポリマーを含む接着剤 Download PDFInfo
- Publication number
- WO2006115138A1 WO2006115138A1 PCT/JP2006/308182 JP2006308182W WO2006115138A1 WO 2006115138 A1 WO2006115138 A1 WO 2006115138A1 JP 2006308182 W JP2006308182 W JP 2006308182W WO 2006115138 A1 WO2006115138 A1 WO 2006115138A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- adhesive
- urethane prepolymer
- polyol
- terminated urethane
- isocyanate group
- Prior art date
Links
Classifications
-
- 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
- C08G18/08—Processes
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M17/00—Producing multi-layer textile fabrics
- D06M17/04—Producing multi-layer textile fabrics by applying synthetic resins as adhesives
- D06M17/10—Polyurethanes polyurea
-
- 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
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
- C08G18/12—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step using two or more compounds having active hydrogen in the first polymerisation step
-
- 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
-
- 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
- C08G18/4202—Two or more polyesters of different physical or chemical nature
-
- 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
-
- 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
- C08G18/44—Polycarbonates
-
- 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
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
-
- 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
- C09J175/06—Polyurethanes from polyesters
-
- 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
- C08G2170/00—Compositions for adhesives
- C08G2170/20—Compositions for hot melt adhesives
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S528/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S528/905—Polymer prepared from isocyanate reactant has adhesive property
Definitions
- the present invention relates to an isocyanate group-terminated urethane prepolymer, a method for producing the same, and an adhesive containing the urethane prepolymer.
- Reactive hot-melt adhesive a hot-melt type moisture-curing adhesive (hereinafter simply referred to as “reactive hot-melt adhesive”) that is pasty or solid at room temperature and melts when heated.
- Reactive hot-melt adhesive is an initial stage that can fix between substrates when the adhesive is cooled and solidified when applied to substrates using adhesive melted by heating. Adhesive strength is generated, and it is difficult for the substrates to slip even immediately after bonding. After that, the adhesive is moisture-cured, so that strong adhesive strength can be expressed.
- the workability in the process of melting the reactive hot melt adhesive and applying it to the substrate is excellent (for example, reactive hot melt
- the adhesive has a suitable viscosity at the time of melting (melt viscosity), and the initial adhesion can be expressed to such an extent that the strength does not deviate between the base materials), and the adhesive part has resistance to sweat deterioration and hydrolysis resistance.
- Reactive hot melt adhesives are required to be superior and to feel the touch of the bonded textile product, that is, to have a good texture as clothing.
- Polyester diol and urethane isocyanate obtained by reaction of polyisocyanate compound see, for example, Patent Document 1, (a2) hydroxyl value converted average molecular weight 700-2
- Adhesive using urethane prepolymer obtained by reacting polyester diol of 500 and polyester diol having an average molecular weight of about 1000 to 3500 with a polyisocyanate compound for example, see Patent Document 2
- A3 A urethane obtained by reacting a crystalline polyester polyol having a hydroxyl value-converted average molecular weight of 3000 to 10,000 and a crystalline polyester polyol having a hydroxyl value-converted average molecular weight of 1000 to 3000 with a polyisocyanate compound.
- An adhesive using a prepolymer for example, see Patent Document 3
- an isocyanate group-terminated urethane prepolymer obtained by reacting a crystalline polyester diol with a polyisocyanate compound for example, see Patent Document 4.
- An adhesive using a prepolymer obtained by reacting a low molecular diol for example, see Patent Document 4 is known. That.
- a reactive hot-melt adhesive (bl) that also has a combination force of (bl) a polycarbonate-based urethane prepolymer and a saturated polyester resin has been used so far.
- (b2) Degradation resistance to oleic acid (this is sweat resistance and! ⁇ ⁇ ) and hydrolytic resistance to lactic acid aqueous solution.
- Moisture curable adhesives obtained by further reacting isocyanate-terminated urethane prepolymers obtained by using low molecular weight diols and diamines (see, for example, Patent Document 6), (b3) polycarbonate in all polyol components
- a urethane prepolymer having a polyol content of 20% by weight or more, an amine catalyst, and water is known.
- Patent Document 1 Japanese Patent Laid-Open No. 11-256131 (US 5939488)
- Patent Document 2 JP-A 62-181375
- Patent Document 3 Japanese Patent Laid-Open No. 7-118622
- Patent Document 4 JP-A-6-271832
- Patent Document 5 Japanese Patent Publication No. 7-17891
- Patent Document 6 Japanese Unexamined Patent Publication No. 2003-313531
- Patent Document 7 Japanese Patent Laid-Open No. 2003-246830
- the adhesive (al) has a feature that the solidification rate is high, but it cannot be said that the workability is high due to the high melt viscosity.
- the adhesive (a2) described above has flexibility after curing and It is excellent in elasticity and has a good texture and the like obtained when a fabric or the like is adhered. The workability is not sufficiently good because the melt viscosity is high.
- the adhesive (a3) is an adhesive for a soft salt / bulb resin sheet having low heat resistance, and is not necessarily suitable for use as a fiber base material.
- the adhesive (a4) has high adhesive strength at the initial stage of curing, when the isocyanate group-terminated urethane prepolymer is reacted with a low-molecular diol, the urethane prepolymer may solidify and not melt thereafter. In addition, even when it can be melted, it has a drawback that the temperature for melting must be remarkably increased. In addition, reactive hot melt adhesives using these known isocyanate group-terminated polyester urethane prepolymers have insufficient resistance to oleic acid (sweat resistance) and hydrolysis to aqueous lactic acid solutions. .
- the adhesive (bl) is excellent in moisture resistance (hydrolysis resistance) and adhesiveness, it is heated at a high temperature in order to obtain a viscosity that can be easily applied to a substrate. Melting is required and workability is poor.
- the adhesive (b2) above when the isocyanate group-terminated urethane prepolymer is reacted with the low molecular weight diol diamamine, the urethane prepolymer may solidify and then not melt, and if meltable. However, the temperature for melting must be remarkably increased, and workability is poor.
- the adhesive (b3) has drawbacks such as high melt viscosity and poor workability, and the strength of the adhesive may be sufficient for resistance to oleic acid (sweat resistance) depending on the specific polyol content. And that was a lot of work.
- the object of the present invention is that the temperature required for melting is relatively low and the melt viscosity is relatively low, so that the workability as a hot melt adhesive is excellent, and moisture hardening is achieved. After that, it is excellent in sweat deterioration resistance and hydrolysis resistance, and when used for bonding textile products, it has a good texture after curing (for example, feel when touched by hand).
- the present invention provides a type adhesive (reactive hot-melt adhesive), an isocyanate group-terminated urethane prepolymer used in the adhesive, and a method for producing the same.
- the process for producing an isocyanate group-terminated urethane prepolymer of the present invention is a process for producing an isocyanate group-terminated urethane prepolymer obtained by reacting a polyol with a polyisocyanate compound, wherein the polyol is 10
- a sebacic acid-based polyester comprising ⁇ 60% by weight of polyester polyol and 90-40% by weight of polycarbonate polyol, and 50 to 100% by weight of the polyester polyol is a polycondensate of sebacic acid and a diol compound
- the average molecular weight in terms of hydroxyl value of the polyester polyol is preferably 1500 to 5000.
- the polycarbonate polyol preferably has an average molecular weight in terms of hydroxyl value of 600 to 1500.
- the polyisocyanate compound is preferably 4,4′-diphenylmethane diisocyanate.
- the isocyanate group-terminated urethane prepolymer obtained by using each of the above production methods preferably has a melting point of 40 ° C to less than 60 ° C and a melt viscosity at 60 ° C of 50000 mPa's or less. .
- the adhesive of the present invention contains, as a main component, the above isocyanate group-terminated urethane prepolymer having a melting point of 40 ° C to less than 60 ° C and a melt viscosity at 60 ° C of 5 OOOOmPa ⁇ s or less.
- the present invention is a moisture curable adhesive containing the isocyanate group-terminated urethane prepolymer as a main component.
- it is a two-component curable adhesive comprising a main component containing the isocyanate group-terminated urethane prepolymer and a curing agent component.
- the adhesive is preferably an adhesive for clothing.
- the isocyanate group-terminated urethane prepolymer produced by the production method of the present invention is used as a reactive hot melt adhesive, an adhesive excellent in sweat resistance and hydrolysis resistance can be obtained. In addition, particularly when used for adhesion of fiber base materials, it has a characteristic of good texture even after curing. Furthermore, in the method for producing an isocyanate group-terminated urethane prepolymer of the present invention, the average molecular weight in terms of hydroxyl value is 1500 to 500.
- polyester polyol and the above-described polycarbonate polyol having a hydroxyl value-converted average molecular weight of 600 to 1500, and 4,4 'diphenylmethane diisocyanate as a polyisocyanate compound The isocyanate group-terminated urethane prepolymer is particularly excellent in sweat resistance and hydrolysis resistance when used as an adhesive, and has a good texture after curing when used for adhesion to a fiber substrate.
- the isocyanate group-terminated urethane pre-bodies obtained by using the method for producing an isocyanate group-terminated urethane prepolymer of the present invention, having a melting point of 40 ° C to less than 60 ° C and a melt viscosity at 60 ° C of 50000 mPa's or less.
- Limer has very good workability when used as a reactive hot-melt adhesive. The adhesive is heated and melted, applied to the substrate, the substrates are bonded together, and then cooled to room temperature. The initial adhesiveness is good, and the adhesive that is difficult to slip between the substrates has a feature that an extremely excellent adhesive force can be obtained after moisture curing.
- the present inventors are obtained by reacting a polyol component containing 50% by mass or more of a sebacic acid-based polyester polyol and a polyol component each containing a specific proportion of a polycarbonate polyol and a polyisocyanate compound. It was found that isocyanate-terminated urethane prepolymers are excellent as reactive hot melt adhesives. That is, when a strong isocyanate group-terminated urethane prepolymer is used as an adhesive, the adhesive can be improved in sweat resistance and hydrolysis resistance after curing, and the melt viscosity of the isocyanate group-terminated urethane prepolymer is further increased.
- the adhesive layer can be made thin when applied to the fiber substrate surface by application, etc., and the adhesive solidifies quickly by cooling after application. The present inventors have found that the texture of the fiber product after curing of the agent is excellent, and have completed the present invention.
- the isocyanate-terminated urethane prepolymer of the present invention is produced by reacting a polyol and a polyisocyanate compound under conditions in which isocyanate groups are excessive.
- a polyol and a polyisocyanate compound used in the present invention will be described.
- the polyol used in the present invention comprises 10 to 60% by mass of polyester polyol and 90 to 40% by mass of polycarbonate polyol. Further, this polyester polyol is composed of a sebacic acid-based polyester polyol which is a polycondensate of 50 to: LOO mass% power sebacic acid and a diol compound.
- the polyester polyol used in the present invention contains 50 to 100% by mass of sebacic acid-based polyester polyol as an essential component.
- the sebacic acid-based polyester polyol used in the present invention is preferably a bifunctional one. Those produced by polycondensation of sebacic acid and a dioli compound are preferred.
- the raw material diol compound used for polycondensation of the above-mentioned sebacic acid-based polyester polyol is not particularly limited, but ethylene glycol, polyethylene glycol, propylene glycol, 1,3 propanediol, 2-methylolene 1,3 butanediol.
- the adhesive containing the isocyanate group-terminated urethane prepolymer of the present invention obtained by using 1,4 butanediol and Z or 1,6 hexanediol, and a polyester polyol obtained by polycondensation of sebacic acid is used after curing. It is preferable because of its excellent resistance to sweat deterioration and hydrolysis. It is particularly preferable to use a polyester polyol obtained by polycondensation of 1,6 hexanediol and sebacic acid. Since sebacic acid-based polyester polyol has moderate crystallinity, and has excellent strength and hydrolysis resistance, it can be used as at least a part of the polyol so that the adhesive of the present invention is cured.
- the texture can be improved, and the hydrolysis resistance and sweat deterioration resistance can be improved.
- the average molecular weight in terms of hydroxyl value of the sebacic acid-based polyester polyol is 1500 to 5000, preferably S, and more preferably 1500 to 4000 S.
- the melt viscosity of the resulting adhesive using the isocyanate group-terminated urethane prepolymer can be set to a moderately low value. For example, it is possible to obtain an adhesive that can be easily applied and has good sweat resistance.
- the hydrolysis resistance of the resulting adhesive can be improved, and the modulus of the adhesive after curing is kept moderately low. Therefore, it is possible to obtain an adhesive with a good texture.
- the average molecular weight in terms of hydroxyl value of a polyol is based on the hydroxyl value (mgKOH / g) of the polyol and the average number of functional groups per molecule of the polyol, as follows:
- Average molecular weight in terms of hydroxyl value (56100Z hydroxyl value) This is a value calculated using the average number of functional groups.
- the average number of functional groups per molecule of the polyol is 2, for example, in a polyester polyol produced using only dicarboxylic acid and diol as raw materials.
- a component other than a bifunctional component such as triol when used as a part of the raw material, it can take a value other than 2, and the average number of functional groups is based on the number of functional groups and the amount used (mol basis) of each raw material used. Therefore, it can be easily obtained by calculation.
- polyester polyols may be used in combination with the sebacic acid-based polyester polyol as desired, as long as the effects of the present invention are not impaired.
- Other polyester polyols are preferably difunctional, such as succinic acid, dartaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, dodecanedioic acid and other aliphatic dibasic acids; isophthalic acid Aromatic dibasic acids such as acid, terephthalic acid, naphthalene dicarboxylic acid, at least one dibasic acid and diol selected (the diol power listed as the raw material of the above-mentioned sebacic acid polyester polyol can be selected) Polyester polyols obtained by polycondensation; and ⁇ -force prolatatone And poly8-methyl- ⁇ -valerolataton, and other polylatatone diols such as poly- ⁇ -one-
- the average molecular weight in terms of hydroxyl value of the whole polyester polyol is preferably 1500 to 5000, more preferably 1500 to 400000.
- the melt viscosity of the resulting adhesive using the isocyanate group-terminated urethane prepolymer can be reduced to a moderately low value. It is possible to obtain an adhesive that can be easily applied to a cloth and that has good resistance to sweat deterioration.
- the average molecular weight in terms of hydroxyl value of the polyester polyol is set to 1500 or more, the hydrolysis resistance of the obtained adhesive can be improved, and the modulus of the adhesive after curing can be kept moderately low. Therefore, an adhesive with a good texture can be obtained.
- a polycarbonate polyol is used together with the polyester polyol as the polyol used for the production of the isocyanate group-terminated urethane prepolymer.
- the polycarbonate polyol used in the present invention is preferably a polycarbonate polyol.
- Polycarbonate diol can be generally produced from a reaction between a diol compound and phosgene.
- Other methods for producing polycarbonate diols include dialkyl carbonates such as dimethyl carbonate or jetyl carbonate, and diaryl carbonates such as diphenyl carbonate. And a method of polycondensing selected carbonate compounds and diol compounds.
- Diol compounds used in the production of the above polycarbonate polyol include ethylene glycol, 1,2 propanediol, 1,3 propanediol, 2-methyl-1,3 butanediol, 1,4 butanediol, and neopentyl.
- Glycol 1,5-pentanediol, 2-methyl-1,5-pentanediol, 3-methyl-1,5-pentanediol, 1,6 hexanediol, 2, 2, 4 trimethyl-1,6 hexanediol, 3, 3, 5 Trimethyl-1,6 hexanediol, 2,3,5 trimethylpentanediol, 1,9-nonanediol, 2-methyl-1,8 octanediol, decanediol, and dodecanediol.
- a polyol having three or more hydroxyl groups per molecule such as trimethylol ethane, trimethylol propane, hexane triol, and pentaerythritol, can be used together with a dioli compound to obtain a polycarbonate polyol. Can be used together in an amount that does not cause gelling.
- the polycarbonate polyol used for the production of the isocyanate group-terminated urethane prepolymer of the present invention was produced by using 1,6 hexanediol and Z or 1,9 nonanediol as a diol compound, 30 ° It is preferable to use a crystalline polycarbonate polyol having a melting point of C or higher.
- a fiber substrate is bonded using an adhesive containing an isocyanate group-terminated urethane prepolymer of the present invention produced using a crystalline polycarbonate polyol having a melting point of 30 ° C. or higher, a fiber product having a good texture is obtained. Obtainable.
- the polycarbonate polyol can be used alone or in combination of two or more.
- the average molecular weight in terms of hydroxyl value of the polycarbonate polyol used in the present invention is not particularly limited, but is preferably 600 to 1500, and more preferably 800 to 1300.
- an adhesive that can be easily applied (for example, applied) to a substrate having a low melt viscosity can be obtained.
- the modulus of the cured product of the resulting adhesive can be lowered.
- An adhesive having an excellent texture can be obtained.
- the polyester polyol and the polycarbonate polyol are used in combination as the polyol.
- 10 to 60 weight 0/0 of the total polyol, preferably a polyester polyol is 15 to 55 wt%, and 90-40 wt 0/0, preferably in Japanese is 85-45% by weight is polycarbonate polyol
- the polyester polyol and the polycarbonate polyol are used in combination.
- Hydroxyl value conversion average molecular weight and molar fraction of all polyols calculated from the hydroxyl value conversion average molecular weight and molar fraction of the polyol to be used are preferably 1000 to 3500 force ⁇ , more preferably 1000 to 2500 force! / ⁇ .
- the isocyanate group-terminated urethane prepolymer of the present invention can be obtained by reacting the above polyol with a polyisocyanate compound.
- the polyisocyanate compounds used in the present invention include 4,4'-diphenylmethane diisocyanate (MDI), 2,4'-diphenylmethane diisocyanate, 2,4 tolylene diisocyanate.
- Aromatic polyisocyanate compounds such as xylylene diisocyanate and aralkyl polyisocyanate compounds such as tetramethylxylylene diisocyanate; 1, 6 hexamethylenediiso Aliphatic polyisocyanates such as cyanate, 2, 2, 4 trimethylhexamethylene diisocyanate, lysine diisocyanate, and lysine triisocyanate Toy compounds; alicyclic polyisocyanates such as isophorone diisocyanate, 4,4'-dicyclohexylenomethane diisocyanate, and 2,5 and Z or 2,6 norbornane diisocyanate And various modified products of these polyisocyanate compounds.
- polyisocyanate compound only one polyisocyanate compound may be used, or two or more polyisocyanate compounds may be used. The above can also be used together.
- an aromatic polyisocyanate compound is preferable because the cured adhesive obtained has good sweat resistance.
- 4,4′-dimethanemethane diisocyanate, crude MDI, and their modifications are preferred.
- 4,4,1-diphenylmethane diisocyanate is preferred because a light-colored light-colored adhesive can be obtained.
- the viscosity of the isocyanate group-terminated urethane prepolymer obtained can be kept moderately low, and the workability of applying the adhesive of the present invention to the substrate is excellent. It is possible to make the adhesive cured product excellent in sweat resistance and hydrolysis resistance.
- the above isocyanate and the polyisocyanate compound can be reacted to produce the isocyanate group-terminated urethane prepolymer of the present invention, and a known method for producing an isocyanate group-terminated urethane prepolymer can be used. .
- the production conditions of the isocyanate group-terminated urethane prepolymer of the present invention are not particularly limited. Specifically, a method in which a polyol and a polyisocyanate compound are mixed and heated to 40 ° C to 100 ° C with stirring is used. be able to.
- a known urethanization catalyst can be used.
- the catalyst include, but are not limited to, organic tin compounds such as dibutyltin dilaurate, and bismuth salts of organic acids such as 2-ethylhexanoic acid and neodecanoic acid.
- organic tin compounds such as dibutyltin dilaurate
- bismuth salts of organic acids such as 2-ethylhexanoic acid and neodecanoic acid.
- a person skilled in the art can appropriately select a preferable amount of catalyst used. [Characteristics of isocyanate group-terminated urethane prepolymers]
- the isocyanate group-terminated urethane prepolymer of the present invention obtained by the reaction of the polyol and the polyisocyanate compound preferably has a melting point of 40 ° C to less than 60 ° C.
- the melting point is also a value obtained from the endothermic peak temperature force measured using a differential scanning calorimeter (DSC), and the measuring method will be described in more detail in Examples.
- DSC differential scanning calorimeter
- the isocyanate terminal urethane prepolymer of the present invention preferably has a melt viscosity of 60,000 mPa's or less at 60 ° C, more preferably 40000 mPa's or less, and more preferably lOOOOmPa's or less. Above is preferred.
- the melt viscosity of the isocyanate group-terminated urethane prepolymer of the present invention is preferably 3000 mPa's or less at 125 ° C, more preferably 2000 mPa's or less, and the squeezing force is preferably 300 mPa's or more.
- the melt viscosity at 60 ° C is a value measured by holding the sample at 60 ° C according to the viscosity measurement method described in JIS K 1603.
- the melt viscosity at 125 ° C is measured using a cone plate viscometer. Details are explained in the examples.
- a urethane prepolymer having the above preferred melt viscosity is usually obtained.
- the isocyanate group-terminated urethane prepolymer obtained at the beginning is preferably slightly deviated from the melt viscosity described above, the molecular weight of each of the polyester polyol and polycarbonate polyol to be used, the use ratio, and the isocyanate group to be reacted are preferred. It is extremely easy for those skilled in the art to produce the above-mentioned preferred isocyanate group-terminated urethane prepolymers by appropriately adjusting the Z hydroxyl group (molar ratio).
- the sweat degradation resistance of the cured product obtained by moisture-curing the isocyanate group-terminated urethane prepolymer of the present invention is that the cured product is maintained in tensile strength after being immersed in oleic acid at 80 ° C for 70 hours.
- the rate is preferably 30% or more.
- the hydrolysis resistance of the cured product is preferably such that the tensile strength retention after immersion in a 132 ° C. aqueous lactic acid solution (concentration of 1% by mass) for 5 hours is 30% or more.
- the adhesive of the present invention essentially contains the above isocyanate group-terminated urethane prepolymer as a main component. More preferably, the adhesive of the present invention consists essentially of the above isocyanate group-terminated urethane prepolymer.
- additives commonly used in the technical field of urethane resin can be added. Examples of additives that can be used include antioxidants, light stabilizers, and anti-aging agents such as ultraviolet absorbers, colorants, flame retardants, and tackifiers. It can be used in combination of more than one species.
- the adhesive of the present invention can be used as a so-called reactive hot-melt adhesive.
- the adhesive of the present invention when the adhesive of the present invention is applied to a substrate such as a textile product, for example, the adhesive is heated and melted at a temperature of 60 to 125 ° C. Applied to the adherend), the substrates are bonded together, and then moisture-cured.
- an applicator for a general hot melt adhesive for example, a roll coater having a heatable adhesive melting tank (gravure tool, reverse) Rolls), curtain coaters, nozzles, and sprays.
- the thickness of the adhesive layer when applied to the substrate is preferably 5 to 45 m.
- the texture of the bonded product can be kept good by setting the thickness of the adhesive layer formed using the present invention to 45 m or less. Since the adhesive of the present invention has a low melt viscosity, it is easy to reduce the thickness of the adhesive layer when applied to a substrate by coating or the like, thereby making the textile product excellent in texture. Can be easily obtained.
- the atmosphere is set to a non-volatile atmosphere such as nitrogen gas. It is preferable to substitute with active gas.
- the adhesive of the present invention is applied to one or both of the substrates to be bonded together, and the substrates are bonded to each other through the adhesive before the adhesive cools and solidifies. Match.
- bonding it is preferable to pressurize the bonded portion.
- pressure it is particularly preferable to apply pressure until the adhesive cools and solidifies, so that the substrates to be bonded are not misaligned.
- the adhesive of the present invention can be cured by using a curing agent in addition to the moisture curing. That is, it can also be used as a two-component curable adhesive.
- Curing agents that can be used include compounds having 2 to 8 active hydrogen-containing functional groups per molecule.
- Preferred hardeners include relatively low molecular weight polyols, alkanolamines, and polyamines, with diols and Z or diamines being particularly preferred.
- the molecular weight of the diol and Z or diamine is preferably 400 or less, more preferably 300 or less, and particularly preferably 200 or less.
- curing agent examples include ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, 1,4 butanediol, neopentyl glycol, 1,5 pentanediol, 3-methyl-1,5 pentanediol, and 1,6.
- Dihydric alcohols such as hexanediol; ethylenediamine, 1,2 propylenediamine, 1,3 propylenediamine, 1,4-tetramethylenediamine, 1,6 hexamethylenediamine, isophorone And polyamines such as 4,4′-cyclohexanediamine; and alkanolamines such as N-methyljetanolamine.
- the above hardener can be used alone or in combination of two or more.
- the amount of curing agent used is 1 mol of isocyanate group of the above isocyanate group-terminated urethane prepolymer of the present invention.
- the amount of the active hydrogen-containing functional group of the curing agent is preferably 0.6 to 1.6 mol, and the amount of the active hydrogen-containing functional group of the curing agent is preferably 0.8 to 1.4 mol. .
- a solvent may be added to the adhesive of the present invention for viscosity adjustment, if desired. It can also be diluted with a solvent and used as a solution-type adhesive.
- the solvent to be used is not particularly limited, and examples thereof include methyl ethyl ketone, toluene, and ethyl acetate, and the solvent may be one kind or a mixture of two or more kinds.
- MDI 4,4, -diphenylmethane diisocyanate (Millionate MT (trade name) manufactured by Nippon Polyurethane Industry Co., Ltd.)
- PHC1000 Polyhexamethylene polycarbonate polyol, hydroxyl group equivalent average molecular weight 984, average number of hydroxyl groups per molecule 2 (manufactured by Nippon Polyurethane Industry Co., Ltd.-Popporan 981
- PHS3500 Polyester polyol obtained by polycondensation of 1,6-hexanediol and sebacic acid, average molecular weight in terms of hydroxyl value 3215, average number of hydroxyl groups per molecule 2 (URIC SE-3506 manufactured by Ito Oil Co., Ltd. (trade name) ))
- PHS2000 Polyester polyol obtained by polycondensation of 1,6-hexanediol and sebacic acid, average molecular weight in terms of hydroxyl value 2117, average number of hydroxyl groups per molecule 2 (URIC SE-2006, manufactured by Ito Oil Co., Ltd.) ))
- PHA4500 Polyester polyol obtained by polycondensation of 1,6-hexanediol and adipic acid, average molecular weight 4878 in terms of hydroxyl value, average number of hydroxyl groups per molecule 2 (Dai Nippon Ink Chemical Co., Ltd. prototype)
- PNA2000 Polyester polyol obtained by polycondensation of nonanediol and adipic acid, hydroxyl value conversion average molecular weight 2011, average number of hydroxyl groups per molecule 2 (Co., Ltd.) Kuraray N—2010 (trade name))
- PBA3000 Polyester polyol obtained by polycondensation of 1,4-butanediol and adipic acid, average molecular weight in terms of hydroxyl value 3024, average number of hydroxyl groups per molecule
- An isocyanate group-terminated urethane prepolymer was obtained in the same manner as in Example 1 except that the content of PHS3500 in the mixed polyol was changed from 50% by mass to 30% by mass. An evaluation test was conducted using this as an adhesive.
- An isocyanate group-terminated urethane prepolymer was obtained in the same manner as in Example 1 except that the content of PHS3500 in the mixed polyol was changed to 50% by mass and 20% by mass. An evaluation test was conducted using this as an adhesive.
- An isocyanate group-terminated urethane prepolymer was obtained in the same manner as in Example 1 except that PHA4500 was used instead of PHS3500 in the mixed polyol (the content of PHA4500 in the mixed polyol was 50% by mass). An evaluation test was conducted using this as an adhesive.
- An isocyanate group-terminated urethane prepolymer was obtained in the same manner as in Example 1 except that PNA2000 was used instead of PHS3500 in the mixed polyol (the content of PNA2000 in the mixed polyol was 50% by mass). It was. An evaluation test was conducted using this as an adhesive.
- An isocyanate group-terminated urethane prepolymer was obtained in the same manner as in Example 1 except that PBA3000 was used instead of PHS3500 in the above-mentioned mixed polyol (the content of PBA3000 in the mixed polyol was 50% by mass). It was. An evaluation test was conducted using this as an adhesive.
- An isocyanate group-terminated urethane prepolymer was obtained in the same manner as in Example 1 except that only the polycarbonate polyol PHC1000 was used instead of the mixed polyol (the content of the polyester polyol in the mixed polyol was 0%). An evaluation test was conducted using this as an adhesive.
- An isocyanate group-terminated urethane prepolymer was obtained in the same manner as in Example 1 except that only the polyester polyol PHS3500 was used instead of the mixed polyol (the content of the polyester polyol in the mixed polyol was 100%). An evaluation test was performed using this as an adhesive.
- Example 2 The same procedure as in Example 1 was performed except that only the polyester polyol PBA3000 was used instead of the above-described mixed polyol (the content of the polyester polyol in the mixed polyol was 1). An isocyanate group-terminated urethane prepolymer was obtained (which was 00%). An evaluation test was performed using this as an adhesive.
- the isocyanate group content of the isocyanate group-terminated urethane prepolymer was measured according to the method described in JIS K 7301.
- the viscosity of isocyanate group-terminated prepolymers at 60 ° C was measured using a RE80 viscometer manufactured by Toki Sangyo Co., Ltd. according to the method described in JIS K 16 03, and the viscosity at 125 ° C was Research 'Measured using a cone plate viscometer manufactured by Iquipment Corporation.
- the melting point of the isocyanate group-terminated urethane prepolymer was measured by using a differential differential calorimeter (DSC) manufactured by SII NanoTechnology Co., Ltd., with a measurement range of ⁇ 40 ° C to 80 ° C, and a heating rate of 5 °.
- DSC differential differential calorimeter
- the temperature of the endothermic peak that appears when measuring with CZmin was taken as the melting point.
- the temperature of the endothermic peak on the highest temperature side was taken as the melting point.
- a glass plate on which a biaxially stretched polypropylene film (OPP film) was placed was heated from below with a heater set at 80 ° C.
- OPP film biaxially stretched polypropylene film
- the isocyanate group-terminated urethane prepolymer was placed on the heated OPP film and melted, and the melted isocyanate group urethane prepolymer was applied onto the OPP film using an applicator. Since the isocyanate group-terminated urethane prepolymer of Comparative Example 5 had a high viscosity at 60 ° C., the heater was set at 100 ° C. and applied onto the OPP film.
- Example 7 Compare more Since the isocyanate group-terminated urethane prepolymer of Example 7 was fluid at 60 ° C, the heater was set on the OPP film at 140 ° C. Subsequently, this was allowed to stand for 5 days in an atmosphere of 20 ° C. and 60% RH together with the OP P film to obtain a polyurethane film having a thickness of about 100 m. The obtained polyurethane film was evaluated for the following tensile properties, sweat deterioration resistance, and hydrolysis resistance.
- Elongation at break (%) of polyurethane film (“Elongation” in Tables 1 to 3), 100% modulus (hereinafter abbreviated as M100, MPa) and tensile strength (MPa) (“Strength” in Tables 1 to 3) was measured according to JIS K 7311.
- MPa tensile strength
- the polyurethane film was immersed in a 132 ° C lactic acid aqueous solution (1% by mass concentration) for 5 hours, and then the tensile strength (MPa) was measured. The ratio to (MPa) was expressed as strength retention (%).
- ⁇ The touch is soft and preferable. That is, the texture is excellent.
- ⁇ The feel is slightly hard. That is, the texture is slightly inferior.
- Lake-isocyanate group content (W) 6. 3 2. 4 2. 5 6. 4 Base powder viscosity (mPa, s / 60 ° C) 32800) 100000 46400 Flowability viscosity (mPa ⁇ s / 1253 ⁇ 4 ) 1000 4900 3700 1200 Mar R point (.C) Liquid in chamber S 61 51 92 ff Physical properties
- the isocyanate group-terminated urethane prepolymers of Examples 1 to 4 have a relatively low melt viscosity (less than 50000 mPa's at 60 ° C, and 125 It is 3000 mPa's or less at ° C) and workability is good. Furthermore, it had good rust resistance, sweat deterioration resistance and hydrolysis resistance (strength retention, deviation of 30% or more), soft touch, that is, good feeling.
- Comparative Examples 1 to 3 the force when the adipic acid-based polyester polyol was used as a polyol component was slightly hard, that is, the texture was slightly inferior, and as a fiber substrate adhesive, Somewhat dissatisfied. Further, in Comparative Example 4 in which only the polycarbonate polyol is used as the polyol component, the feel is very hard, that is, the texture is inferior. As for Comparative Examples 5 and 6 using only polyester polyol as the polyol component, Comparative Example 5 is inferior in sweat resistance and Comparative Example 6 is inferior in hydrolysis resistance as compared with Examples 1 to 4. On the other hand, the isocyanate group-terminated urethane prepolymer of Comparative Example 7 chain-extended with a low molecular weight diol is inferior in workability to a substrate having a very high viscosity.
- the isocyanate group-terminated urethane prepolymer of the present invention can be melted at a relatively low temperature, and the melt viscosity is low, and it can be applied thinly on a substrate, has good workability and is hardened. It can be seen that the later adhesive is excellent in sweat resistance and hydrolysis resistance. Furthermore, when the isocyanate group-terminated urethane prepolymer of the present invention is used as an adhesive for a fiber substrate, it can be seen that the texture of the bonded portion after curing of the adhesive is good.
- the isocyanate group-terminated urethane prepolymer of the present invention is a porous material such as a fabric, a porous plastic film, a porous plastic film sheet, and a porous plastic foam.
- Adhesive that has a soft and good texture and is also excellent in hydrolysis resistance and sweat deterioration resistance.
- Can be used as The adhesive of the present invention is suitable as an adhesive for textile substrates in clothing, sports equipment, shoes, and other applications where durability is required.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2006800135604A CN101163728B (zh) | 2005-04-22 | 2006-04-19 | 异氰酸酯基封端的氨基甲酸酯预聚物、其制备方法和包括该氨基甲酸酯预聚物的粘合剂 |
EP06732089A EP1873177B1 (en) | 2005-04-22 | 2006-04-19 | Isocyanate-terminated urethane prepolymer, process for producing the same, and adhesive comprising the urethane prepolymer |
KR1020077024193A KR101252883B1 (ko) | 2005-04-22 | 2006-04-19 | 이소시아네이트기 말단 우레탄 예비중합체 및 그의 제조방법, 및 상기 우레탄 예비중합체를 포함하는 접착제 |
JP2007514621A JP5176544B2 (ja) | 2005-04-22 | 2006-04-19 | ホットメルト型の湿気硬化型接着剤およびこれを用いた接着方法 |
DE602006017677T DE602006017677D1 (de) | 2005-04-22 | 2006-04-19 | Isocyanatterminiertes urethanprepolymer, herstellungsverfahren dafür und klebstoff, der das urethanprepolymer enthält |
US11/876,200 US7906607B2 (en) | 2005-04-22 | 2007-10-22 | Isocyanate group-terminated urethane prepolymer, process for producing the same, and adhesive comprising the urethane prepolymer |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2005125131 | 2005-04-22 | ||
JP2005-125131 | 2005-04-22 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/876,200 Continuation US7906607B2 (en) | 2005-04-22 | 2007-10-22 | Isocyanate group-terminated urethane prepolymer, process for producing the same, and adhesive comprising the urethane prepolymer |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2006115138A1 true WO2006115138A1 (ja) | 2006-11-02 |
Family
ID=37214757
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2006/308182 WO2006115138A1 (ja) | 2005-04-22 | 2006-04-19 | イソシアネート基末端ウレタンプレポリマーおよびその製造方法、並びに前記ウレタンプレポリマーを含む接着剤 |
Country Status (7)
Country | Link |
---|---|
US (1) | US7906607B2 (ja) |
EP (1) | EP1873177B1 (ja) |
JP (1) | JP5176544B2 (ja) |
KR (1) | KR101252883B1 (ja) |
CN (1) | CN101163728B (ja) |
DE (1) | DE602006017677D1 (ja) |
WO (1) | WO2006115138A1 (ja) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2018104487A (ja) * | 2016-12-22 | 2018-07-05 | Dic株式会社 | 湿気硬化型ポリウレタンホットメルト組成物 |
WO2018173768A1 (ja) * | 2017-03-24 | 2018-09-27 | Dic株式会社 | 湿気硬化型ポリウレタンホットメルト樹脂組成物、及び、積層体 |
CN108728035A (zh) * | 2018-06-14 | 2018-11-02 | 汕头市鲁汕化工原料有限公司 | 一种自催化型聚氨酯热熔胶及其制备方法 |
JP2019044004A (ja) * | 2017-08-30 | 2019-03-22 | Dic株式会社 | 湿気硬化型ホットメルト樹脂組成物及び積層体又は成形体 |
WO2020067534A1 (ja) * | 2018-09-28 | 2020-04-02 | 横浜ゴム株式会社 | 2液硬化型接着剤組成物 |
WO2021039338A1 (ja) * | 2019-08-26 | 2021-03-04 | Dic株式会社 | 2液型接着剤、積層体、成型体、包装材 |
CN115558455A (zh) * | 2022-09-27 | 2023-01-03 | 南通高盟新材料有限公司 | 一种符合eu10法规的铝箔高温蒸煮胶及其制备方法 |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8044234B2 (en) * | 2005-05-05 | 2011-10-25 | Tyco Healthcare Group Lp | Bioabsorbable surgical composition |
DE102006053741A1 (de) * | 2006-11-15 | 2008-05-21 | Bayer Materialscience Ag | Beschichtungsmittel |
CN101679593A (zh) * | 2007-06-07 | 2010-03-24 | 旭硝子株式会社 | 含热塑性聚氨酯的树脂组合物及热熔性粘合剂 |
KR101502194B1 (ko) * | 2007-10-05 | 2015-03-12 | 도레이 카부시키가이샤 | 식물 유래 성분으로 이루어진 방수 가공 포백 |
JP4875179B2 (ja) * | 2009-03-31 | 2012-02-15 | 本田技研工業株式会社 | 車両内装材用合成皮革及びその製造方法 |
EP2540908B1 (en) * | 2010-02-23 | 2017-04-26 | Seiren Co., Ltd. | Moisture-permeable water-proof fabric |
CN107075336B (zh) * | 2014-10-20 | 2020-10-27 | Dic株式会社 | 粘合剂组合物及粘合片 |
CN109749687A (zh) * | 2018-12-03 | 2019-05-14 | 上海康达化工新材料股份有限公司 | 一种湿固化反应型聚氨酯热熔胶及其制备方法 |
CN111040712A (zh) * | 2019-12-20 | 2020-04-21 | 烟台德邦科技有限公司 | 一种高强度耐汗液聚氨酯热熔胶的制备方法 |
EP4103656A4 (en) * | 2020-02-13 | 2023-09-27 | Henkel AG & Co. KGaA | REACTIVE HOT HOT ADHESIVE COMPOSITION AND USE THEREOF |
CN111269684B (zh) * | 2020-03-31 | 2022-02-15 | 扬州工业职业技术学院 | 双层超纤毛巾布用pu黏合剂及其制备方法 |
CN114716964B (zh) * | 2021-12-30 | 2023-11-28 | 无锡市万力粘合材料股份有限公司 | 一种太阳能背板材料粘结用uv固化胶水及其制备方法 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0216180A (ja) * | 1988-05-06 | 1990-01-19 | Emhart Ind Inc | ホットメルトポリウレタン接着性組成物 |
JPH10259369A (ja) * | 1997-01-20 | 1998-09-29 | Sanyo Chem Ind Ltd | ホットメルト接着剤 |
JP2003277717A (ja) * | 2002-03-25 | 2003-10-02 | Dainippon Ink & Chem Inc | 反応性ホットメルト接着剤 |
JP2003327647A (ja) * | 2002-05-15 | 2003-11-19 | Sekisui Chem Co Ltd | 1液湿気硬化型ポリウレタン樹脂組成物 |
WO2004031296A1 (ja) * | 2002-10-01 | 2004-04-15 | Ube Industries, Ltd. | ポリオール混合物および該混合物より得られる反応性ホットメルト組成物ならびに該組成物を使用して得られる成形品 |
JP2005023181A (ja) * | 2003-07-01 | 2005-01-27 | Ube Ind Ltd | ポリオール混合物、該混合物より得られる反応性ホットメルト組成物、並びに該組成物より得られる成型品 |
Family Cites Families (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62181375A (ja) | 1985-10-15 | 1987-08-08 | Asahi Glass Co Ltd | ポリウレタン系接着剤 |
IT1227361B (it) * | 1988-11-18 | 1991-04-08 | Enichem Sintesi | Composizione di hot melt reattivo. |
DE3931844A1 (de) * | 1989-09-23 | 1991-04-04 | Bayer Ag | Lagerstabile polyurethanklebstoffe |
JP3482609B2 (ja) * | 1991-08-22 | 2003-12-22 | 大日本インキ化学工業株式会社 | ホットメルト接着剤 |
US5175228A (en) * | 1991-12-09 | 1992-12-29 | Gencorp Inc. | Two-component primerless urethane-isocyanurate adhesive compositions having high temperature resistance |
JPH06271832A (ja) | 1993-03-18 | 1994-09-27 | Sekisui Chem Co Ltd | 反応性ホットメルト型接着剤 |
JPH0717891A (ja) | 1993-07-02 | 1995-01-20 | Nippon Zeon Co Ltd | カルボニル化合物の製造法 |
JPH07118622A (ja) | 1993-10-27 | 1995-05-09 | Sekisui Chem Co Ltd | ホットメルト接着剤組成物 |
EP0781792B1 (en) * | 1995-12-28 | 2002-02-06 | Asahi Glass Company Ltd. | Cross-linked polyurethane resin sheet and laminated product employing it |
US5939488A (en) | 1997-10-15 | 1999-08-17 | National Starch And Chemical Investment Holding Corporation | Fast setting polyurethane hot melt adhesive composition comprising low hydroxyl number/high molecular weight polyester diols |
EP0915112B1 (en) | 1997-11-05 | 2004-02-18 | Asahi Glass Company Ltd. | Reactive hot melt adhesive and adhesive composite sheet material |
JP4788020B2 (ja) | 2000-06-12 | 2011-10-05 | 旭硝子株式会社 | コーティング剤組成物 |
US6423810B1 (en) * | 2001-02-05 | 2002-07-23 | Lord Corporation | High strength, long-open time structural polyurethane adhesive and method of use thereof |
DE10131463A1 (de) * | 2001-06-29 | 2003-01-09 | Bayer Ag | Hitzehärtbare Zwei-Komponenten-Beschichtungssysteme |
JP4029667B2 (ja) * | 2001-11-09 | 2008-01-09 | 大日本インキ化学工業株式会社 | 無溶剤型湿気硬化性ホットメルトウレタン樹脂組成物、発泡体及びそれを用いたシート構造体 |
JP4038608B2 (ja) | 2002-02-25 | 2008-01-30 | 大日本インキ化学工業株式会社 | 耐久性に優れた無溶剤型湿気硬化性ホットメルトウレタン樹脂組成物、発泡体、及びそれを用いたシート構造体 |
JP4144245B2 (ja) | 2002-04-22 | 2008-09-03 | 旭硝子株式会社 | 湿気硬化型接着剤 |
JP4107032B2 (ja) * | 2002-09-27 | 2008-06-25 | Dic株式会社 | 無溶剤型湿気硬化性ホットメルトウレタン樹脂組成物、発泡体、及びそれを用いたシート構造体 |
WO2005116102A1 (ja) | 2004-05-31 | 2005-12-08 | Asahi Glass Company, Limited | ポリウレタンエラストマーおよびその製造方法 |
JP4905132B2 (ja) | 2004-10-20 | 2012-03-28 | 旭硝子株式会社 | ウレタン樹脂溶液、その製造方法及びウレタン樹脂の製造方法 |
JP4539656B2 (ja) | 2004-10-21 | 2010-09-08 | 旭硝子株式会社 | ポリウレタン樹脂およびポリウレタン樹脂溶液の製造方法 |
-
2006
- 2006-04-19 JP JP2007514621A patent/JP5176544B2/ja not_active Expired - Fee Related
- 2006-04-19 EP EP06732089A patent/EP1873177B1/en not_active Not-in-force
- 2006-04-19 CN CN2006800135604A patent/CN101163728B/zh not_active Expired - Fee Related
- 2006-04-19 DE DE602006017677T patent/DE602006017677D1/de active Active
- 2006-04-19 WO PCT/JP2006/308182 patent/WO2006115138A1/ja active Application Filing
- 2006-04-19 KR KR1020077024193A patent/KR101252883B1/ko not_active IP Right Cessation
-
2007
- 2007-10-22 US US11/876,200 patent/US7906607B2/en not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0216180A (ja) * | 1988-05-06 | 1990-01-19 | Emhart Ind Inc | ホットメルトポリウレタン接着性組成物 |
JPH10259369A (ja) * | 1997-01-20 | 1998-09-29 | Sanyo Chem Ind Ltd | ホットメルト接着剤 |
JP2003277717A (ja) * | 2002-03-25 | 2003-10-02 | Dainippon Ink & Chem Inc | 反応性ホットメルト接着剤 |
JP2003327647A (ja) * | 2002-05-15 | 2003-11-19 | Sekisui Chem Co Ltd | 1液湿気硬化型ポリウレタン樹脂組成物 |
WO2004031296A1 (ja) * | 2002-10-01 | 2004-04-15 | Ube Industries, Ltd. | ポリオール混合物および該混合物より得られる反応性ホットメルト組成物ならびに該組成物を使用して得られる成形品 |
JP2005023181A (ja) * | 2003-07-01 | 2005-01-27 | Ube Ind Ltd | ポリオール混合物、該混合物より得られる反応性ホットメルト組成物、並びに該組成物より得られる成型品 |
Non-Patent Citations (1)
Title |
---|
See also references of EP1873177A4 * |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2018104487A (ja) * | 2016-12-22 | 2018-07-05 | Dic株式会社 | 湿気硬化型ポリウレタンホットメルト組成物 |
WO2018173768A1 (ja) * | 2017-03-24 | 2018-09-27 | Dic株式会社 | 湿気硬化型ポリウレタンホットメルト樹脂組成物、及び、積層体 |
JP6481801B2 (ja) * | 2017-03-24 | 2019-03-13 | Dic株式会社 | 湿気硬化型ポリウレタンホットメルト樹脂組成物、及び、積層体 |
JPWO2018173768A1 (ja) * | 2017-03-24 | 2019-03-28 | Dic株式会社 | 湿気硬化型ポリウレタンホットメルト樹脂組成物、及び、積層体 |
JP7451071B2 (ja) | 2017-08-30 | 2024-03-18 | Dic株式会社 | 湿気硬化型ホットメルト樹脂組成物及び積層体又は成形体 |
JP2019044004A (ja) * | 2017-08-30 | 2019-03-22 | Dic株式会社 | 湿気硬化型ホットメルト樹脂組成物及び積層体又は成形体 |
CN108728035A (zh) * | 2018-06-14 | 2018-11-02 | 汕头市鲁汕化工原料有限公司 | 一种自催化型聚氨酯热熔胶及其制备方法 |
WO2020067534A1 (ja) * | 2018-09-28 | 2020-04-02 | 横浜ゴム株式会社 | 2液硬化型接着剤組成物 |
JPWO2020067534A1 (ja) * | 2018-09-28 | 2021-08-30 | 横浜ゴム株式会社 | 2液硬化型接着剤組成物 |
JP7469672B2 (ja) | 2018-09-28 | 2024-04-17 | 横浜ゴム株式会社 | 2液硬化型接着剤組成物 |
JP6892036B1 (ja) * | 2019-08-26 | 2021-06-18 | Dic株式会社 | 2液型接着剤、積層体、成型体、包装材 |
WO2021039338A1 (ja) * | 2019-08-26 | 2021-03-04 | Dic株式会社 | 2液型接着剤、積層体、成型体、包装材 |
CN115558455A (zh) * | 2022-09-27 | 2023-01-03 | 南通高盟新材料有限公司 | 一种符合eu10法规的铝箔高温蒸煮胶及其制备方法 |
Also Published As
Publication number | Publication date |
---|---|
EP1873177B1 (en) | 2010-10-20 |
EP1873177A1 (en) | 2008-01-02 |
US20080210132A1 (en) | 2008-09-04 |
CN101163728B (zh) | 2010-11-24 |
EP1873177A4 (en) | 2009-07-22 |
CN101163728A (zh) | 2008-04-16 |
DE602006017677D1 (de) | 2010-12-02 |
US7906607B2 (en) | 2011-03-15 |
KR20080009089A (ko) | 2008-01-24 |
KR101252883B1 (ko) | 2013-04-09 |
JPWO2006115138A1 (ja) | 2008-12-18 |
JP5176544B2 (ja) | 2013-04-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2006115138A1 (ja) | イソシアネート基末端ウレタンプレポリマーおよびその製造方法、並びに前記ウレタンプレポリマーを含む接着剤 | |
JP5872475B2 (ja) | 結晶質または半結晶質ポリウレタンポリマーに基づく水性処方物 | |
JP5889887B2 (ja) | Tpu貼合せ用接着剤 | |
US6660376B1 (en) | Method of bonding permeable substrates with hot melt moisture cure adhesive having low viscosity and high green strength | |
KR101522056B1 (ko) | 무용매 접착제에 유용한 액체 폴리우레탄 예비중합체 | |
TW200418895A (en) | Polyurethane dispersion and articles prepared therefrom | |
JP2007063510A (ja) | 湿気硬化性ポリウレタンホットメルト組成物 | |
CN109476812B (zh) | 低硬度聚氨酯分散体 | |
TW202003614A (zh) | 聚胺酯預聚物、接著劑、及合成人造皮 | |
WO2023002992A1 (ja) | 湿気硬化型ポリウレタンホットメルト接着剤 | |
WO2005030873A1 (ja) | ポリウレタン樹脂水性分散体、それを含有してなる水性接着剤、及び水性プライマーコート剤 | |
JP4144245B2 (ja) | 湿気硬化型接着剤 | |
JPH0346515B2 (ja) | ||
JP3944782B2 (ja) | ポリウレタン樹脂水性分散体、それを含有してなる水性接着剤、及び水性プライマーコート剤 | |
TW201840797A (zh) | 含有聚酯-聚胺基甲酸酯之反應性熱熔黏著劑組成物 | |
JP2008248201A (ja) | 湿気硬化型反応性ホットメルト接着剤 | |
JP2022114079A (ja) | 湿気硬化型ポリウレタンホットメルト樹脂組成物、湿気硬化型ポリウレタンホットメルト接着剤、硬化物及び積層体 | |
WO2022133635A1 (en) | Oil resistant adhesive composition | |
JP2011147859A (ja) | ウレタン塗膜形成方法 | |
KR100592913B1 (ko) | 핫멜트 폴리우레탄계 접착제의 제조방법 | |
WO2023080134A1 (ja) | ポリエステルポリカーボネートポリオール | |
JP7228231B2 (ja) | 多液型接着剤組成物 | |
JP2021161140A (ja) | 耐破壊特性材料用の水性ポリウレタン樹脂分散体 | |
KR100297075B1 (ko) | 반응성고온용융접착제 | |
JP2024020871A (ja) | 湿気硬化型ポリウレタンホットメルト接着剤 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 200680013560.4 Country of ref document: CN |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2007514621 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2006732089 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1020077024193 Country of ref document: KR |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
NENP | Non-entry into the national phase |
Ref country code: RU |
|
WWP | Wipo information: published in national office |
Ref document number: 2006732089 Country of ref document: EP |