WO2022116748A1 - Solvent-free blocked polyurethane resin composition, polyurethane material, and leather product - Google Patents
Solvent-free blocked polyurethane resin composition, polyurethane material, and leather product Download PDFInfo
- Publication number
- WO2022116748A1 WO2022116748A1 PCT/CN2021/126660 CN2021126660W WO2022116748A1 WO 2022116748 A1 WO2022116748 A1 WO 2022116748A1 CN 2021126660 W CN2021126660 W CN 2021126660W WO 2022116748 A1 WO2022116748 A1 WO 2022116748A1
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- WIPO (PCT)
- Prior art keywords
- solvent
- resin composition
- polyurethane resin
- free
- polyol
- Prior art date
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- 229920005749 polyurethane resin Polymers 0.000 title claims abstract description 63
- 239000011342 resin composition Substances 0.000 title claims abstract description 52
- 229920002635 polyurethane Polymers 0.000 title claims abstract description 20
- 239000004814 polyurethane Substances 0.000 title claims abstract description 20
- 239000000463 material Substances 0.000 title claims abstract description 17
- 239000010985 leather Substances 0.000 title claims abstract description 8
- 229920001730 Moisture cure polyurethane Polymers 0.000 claims abstract description 51
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 50
- 239000003054 catalyst Substances 0.000 claims abstract description 42
- 150000001412 amines Chemical class 0.000 claims abstract description 38
- DZIHTWJGPDVSGE-UHFFFAOYSA-N 4-[(4-aminocyclohexyl)methyl]cyclohexan-1-amine Chemical compound C1CC(N)CCC1CC1CCC(N)CC1 DZIHTWJGPDVSGE-UHFFFAOYSA-N 0.000 claims abstract description 4
- RNLHGQLZWXBQNY-UHFFFAOYSA-N 3-(aminomethyl)-3,5,5-trimethylcyclohexan-1-amine Chemical compound CC1(C)CC(N)CC(C)(CN)C1 RNLHGQLZWXBQNY-UHFFFAOYSA-N 0.000 claims abstract 2
- 229920001451 polypropylene glycol Polymers 0.000 claims description 50
- -1 adipate diol Chemical class 0.000 claims description 44
- 229920005862 polyol Polymers 0.000 claims description 34
- 150000003077 polyols Chemical class 0.000 claims description 34
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 27
- 238000002360 preparation method Methods 0.000 claims description 27
- 239000002994 raw material Substances 0.000 claims description 25
- SDXAWLJRERMRKF-UHFFFAOYSA-N 3,5-dimethyl-1h-pyrazole Chemical compound CC=1C=C(C)NN=1 SDXAWLJRERMRKF-UHFFFAOYSA-N 0.000 claims description 19
- 238000006243 chemical reaction Methods 0.000 claims description 15
- 239000002981 blocking agent Substances 0.000 claims description 14
- 150000002009 diols Chemical class 0.000 claims description 14
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 11
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 10
- DVKJHBMWWAPEIU-UHFFFAOYSA-N toluene 2,4-diisocyanate Chemical compound CC1=CC=C(N=C=O)C=C1N=C=O DVKJHBMWWAPEIU-UHFFFAOYSA-N 0.000 claims description 10
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims description 9
- 239000012948 isocyanate Substances 0.000 claims description 9
- 150000002513 isocyanates Chemical class 0.000 claims description 9
- WERYXYBDKMZEQL-UHFFFAOYSA-N 1,4-butanediol Substances OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 claims description 8
- 239000004970 Chain extender Substances 0.000 claims description 7
- 239000003431 cross linking reagent Substances 0.000 claims description 7
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 7
- UPMLOUAZCHDJJD-UHFFFAOYSA-N 4,4'-Diphenylmethane Diisocyanate Chemical compound C1=CC(N=C=O)=CC=C1CC1=CC=C(N=C=O)C=C1 UPMLOUAZCHDJJD-UHFFFAOYSA-N 0.000 claims description 5
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 229920005906 polyester polyol Polymers 0.000 claims description 5
- 229920000570 polyether Polymers 0.000 claims description 5
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 claims description 3
- RUELTTOHQODFPA-UHFFFAOYSA-N toluene 2,6-diisocyanate Chemical compound CC1=C(N=C=O)C=CC=C1N=C=O RUELTTOHQODFPA-UHFFFAOYSA-N 0.000 claims description 3
- WYTZZXDRDKSJID-UHFFFAOYSA-N (3-aminopropyl)triethoxysilane Chemical compound CCO[Si](OCC)(OCC)CCCN WYTZZXDRDKSJID-UHFFFAOYSA-N 0.000 claims description 2
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims description 2
- WTKZEGDFNFYCGP-UHFFFAOYSA-N Pyrazole Chemical compound C=1C=NNC=1 WTKZEGDFNFYCGP-UHFFFAOYSA-N 0.000 claims description 2
- 229910052797 bismuth Inorganic materials 0.000 claims description 2
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 claims description 2
- OWBTYPJTUOEWEK-UHFFFAOYSA-N butane-2,3-diol Chemical compound CC(O)C(C)O OWBTYPJTUOEWEK-UHFFFAOYSA-N 0.000 claims description 2
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 claims description 2
- 229920000921 polyethylene adipate Polymers 0.000 claims description 2
- 150000003217 pyrazoles Chemical class 0.000 claims description 2
- 150000001298 alcohols Chemical class 0.000 claims 1
- 239000003999 initiator Substances 0.000 claims 1
- 230000014759 maintenance of location Effects 0.000 abstract description 16
- 230000007062 hydrolysis Effects 0.000 abstract description 9
- 238000006460 hydrolysis reaction Methods 0.000 abstract description 9
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000001723 curing Methods 0.000 description 66
- 230000000052 comparative effect Effects 0.000 description 23
- GZDFHIJNHHMENY-UHFFFAOYSA-N Dimethyl dicarbonate Chemical compound COC(=O)OC(=O)OC GZDFHIJNHHMENY-UHFFFAOYSA-N 0.000 description 20
- 235000010300 dimethyl dicarbonate Nutrition 0.000 description 20
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical compound ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 9
- 239000002904 solvent Substances 0.000 description 9
- 239000000126 substance Substances 0.000 description 8
- 238000013035 low temperature curing Methods 0.000 description 7
- 239000000853 adhesive Substances 0.000 description 6
- 230000001070 adhesive effect Effects 0.000 description 6
- 239000004744 fabric Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- WNLRTRBMVRJNCN-UHFFFAOYSA-L adipate(2-) Chemical compound [O-]C(=O)CCCCC([O-])=O WNLRTRBMVRJNCN-UHFFFAOYSA-L 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 229920000909 polytetrahydrofuran Polymers 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- LRHSENVDAQAWKP-UHFFFAOYSA-N [C].CC1=CC=CC=C1 Chemical class [C].CC1=CC=CC=C1 LRHSENVDAQAWKP-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- HJOVHMDZYOCNQW-UHFFFAOYSA-N isophorone Chemical compound CC1=CC(=O)CC(C)(C)C1 HJOVHMDZYOCNQW-UHFFFAOYSA-N 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 239000002562 thickening agent Substances 0.000 description 2
- NWYDEWXSKCTWMJ-UHFFFAOYSA-N 2-methylcyclohexane-1,1-diamine Chemical compound CC1CCCCC1(N)N NWYDEWXSKCTWMJ-UHFFFAOYSA-N 0.000 description 1
- 229920001410 Microfiber Polymers 0.000 description 1
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000002238 attenuated effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 239000012975 dibutyltin dilaurate Substances 0.000 description 1
- 239000002612 dispersion medium Substances 0.000 description 1
- 238000009820 dry lamination Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 125000001033 ether group Chemical group 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000011534 incubation Methods 0.000 description 1
- 239000004816 latex Substances 0.000 description 1
- 229920000126 latex Polymers 0.000 description 1
- 239000003658 microfiber Substances 0.000 description 1
- WHIVNJATOVLWBW-UHFFFAOYSA-N n-butan-2-ylidenehydroxylamine Chemical compound CCC(C)=NO WHIVNJATOVLWBW-UHFFFAOYSA-N 0.000 description 1
- 239000011120 plywood Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/80—Masked polyisocyanates
- C08G18/8061—Masked polyisocyanates masked with compounds having only one group containing active hydrogen
- C08G18/807—Masked polyisocyanates masked with compounds having only one group containing active hydrogen with nitrogen containing compounds
-
- 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
- C08G18/30—Low-molecular-weight compounds
- C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
- C08G18/3203—Polyhydroxy compounds
- C08G18/3206—Polyhydroxy compounds aliphatic
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4804—Two or more polyethers of different physical or chemical nature
- C08G18/4812—Mixtures of polyetherdiols with polyetherpolyols having at least three hydroxy groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4825—Polyethers containing two hydroxy groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
- C08G18/66—Compounds of groups C08G18/42, C08G18/48, or C08G18/52
- C08G18/6666—Compounds of group C08G18/48 or C08G18/52
- C08G18/667—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
- C08G18/6674—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203
- C08G18/6677—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203 having at least three hydroxy groups
-
- 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
- C08G18/80—Masked polyisocyanates
- C08G18/8061—Masked polyisocyanates masked with compounds having only one group containing active hydrogen
- C08G18/807—Masked polyisocyanates masked with compounds having only one group containing active hydrogen with nitrogen containing compounds
- C08G18/8077—Oximes
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
- D06N3/12—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. gelatine proteins
- D06N3/14—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. gelatine proteins with polyurethanes
- D06N3/146—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. gelatine proteins with polyurethanes characterised by the macromolecular diols used
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N2211/00—Specially adapted uses
- D06N2211/12—Decorative or sun protection articles
- D06N2211/28—Artificial leather
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
- Y02P70/62—Manufacturing or production processes characterised by the final manufactured product related technologies for production or treatment of textile or flexible materials or products thereof, including footwear
Definitions
- the present application relates to the technical field of polyurethane, and in particular, to a solvent-free sealed polyurethane resin composition, a polyurethane material and a leather product.
- Polyurethane resin is synthesized from polyols, chain extenders, crosslinking agents, isocyanates, etc. as the main raw materials under certain process conditions. It is widely used in aviation, electronic devices, coatings, wood, leather and other industries. It can be divided into four major categories.
- the solvent-based polyurethane resin is baked and cured by replacing the solvent with water or evaporating the solvent at high temperature, which causes pollution to the environment;
- the water-based polyurethane uses water as the dispersion medium to replace the solvent to achieve environmental protection, but the cost Higher, the performance of hydrolysis resistance and weather resistance is worse than that of solvent-based polyurethane resin;
- solvent-free two-component polyurethane resin requires special equipment to meet the application, and the open NCO group makes the product storage requirements strict, and product performance is not good. Stablize.
- the closed polyurethane resin can be stored stably, but most products on the market have a small amount of solvent, and there are also problems of high curing temperature and long curing time in the application process.
- CN101812228A discloses an all-toluene solvent-based polyurethane resin and a preparation method thereof. Based on the weight percentage of the all-toluene solvent-based polyurethane resin, the content of polyurethane is 34%-36%, and the content of toluene is 64%-66%, excluding other Therefore, the activated carbon toluene recovery system can be used to recover toluene, which overcomes the disadvantage that the solvent-based polyurethane resin on the market cannot be used to recover toluene using the activated carbon toluene recovery system because it contains multiple solvent combinations instead of a single solvent, and the economic benefits are improved. And conducive to environmental protection. This scheme can only improve the pollution problem to a certain extent, but cannot completely avoid it. With the attention of all walks of life on the problem of environmental pollution, this scheme can no longer meet the existing requirements.
- CN109266294A discloses a closed-type polyurethane adhesive and a preparation method thereof.
- the preparation method includes: synthesis of closed-type isocyanate and preparation of closed-type polyurethane adhesive.
- Diphenylmethane diisocyanate (MDI) is selected as a raw material to invent a Synthesis of MDI-blocked polyurethane.
- MDI closed polyurethane can be compounded with traditional white latex in proportion to prepare closed polyurethane adhesive.
- the plywood pressed with the adhesive has good bonding strength and no formaldehyde emission. It has the advantages of cost reduction and environmental friendliness, and can be used as an adhesive for interior materials.
- the adhesive has problems of high curing temperature, long curing time and low efficiency during application.
- the present application provides a solvent-free sealed polyurethane resin composition, a polyurethane material and a leather product; wherein, the solvent-free sealed polyurethane resin composition is not only safe and environmentally friendly, but also can be rapidly cured at a lower temperature, making production Increased efficiency and reduced energy consumption, with excellent peel force, peel force retention and hydrolysis resistance.
- the present application provides a solvent-free sealed polyurethane resin composition
- the solvent-free sealed polyurethane resin composition comprises the following components according to parts by weight:
- the amine curing agent includes 3,3-dimethyl-4,4-diaminodicyclohexylmethane (DMDC), 4,4-diaminodicyclohexylmethane (PACM) or isophorone di Any one or a combination of at least two of the amines (IPDA).
- DMDC 3,3-dimethyl-4,4-diaminodicyclohexylmethane
- PAM 4,4-diaminodicyclohexylmethane
- IPDA isophorone di Any one or a combination of at least two of the amines
- the addition amount of the amine curing agent is 4-13 parts, such as 5 parts by weight, 6.2 parts by weight, 6.3 parts by weight, 6.5 parts by weight, 7.1 parts by weight, 8.3 parts by weight, 8.9 parts by weight, etc.; the temperature-sensitive catalyst The added amount is 0.1-10 parts, such as 0.1 parts by weight.
- a specific type of amine curing agent and a temperature-sensitive catalyst are used in the solvent-free closed polyurethane system.
- DMDC, PACM or IPDA have the characteristics of high hardness, strong rigidity, high primary amino activity and high curing strength.
- the temperature-sensitive catalyst is used in combination, and the reactive group can be quickly activated after proper temperature rise, so as to realize the rapid curing of the polyurethane resin at low temperature, and the obtained polyurethane resin has excellent peeling force, peeling force retention rate and hydrolysis resistance.
- the addition amount of amine curing agent must be controlled in the range of 4-13 parts, in order to obtain the above beneficial effects, the addition amount is less than 4 parts, which will lead to low peeling force of the product; the addition amount is more than 13 parts, It will cause the peeling force of the product to be seriously attenuated under high temperature and high humidity.
- the temperature-sensitive catalyst must be controlled within the range of 0.1-10 parts. If the addition amount is less than 0.1 part, the curing efficiency will be reduced; if the addition amount is more than 10 parts, it will lead to abnormal viscosity increase, making it difficult to do normal ingredients, and the product peeling force will be reduced.
- the amine curing agent includes 3,3-dimethyl-4,4-diaminodicyclohexylmethane.
- DMDC is preferred as the curing agent.
- the curing agent has the characteristics of high hardness and good temperature resistance. Compared with IPDA and PACM, the obtained product has high strength after curing and can better maintain peeling under high temperature and high humidity conditions. force.
- a temperature-sensitive catalyst refers to a catalyst that has little catalytic effect at room temperature, and can rapidly catalyze active functional groups at elevated temperature.
- the temperature-sensitive catalyst includes organic bismuth catalyst and/or organic amine catalyst.
- the temperature-sensitive catalyst comprises any one or a combination of at least two of BiCAT Z(M), BiCAT 3228(M), BiCAT 8, BiCAT 8108 or polycat SA8, and the BiCAT Z(M), BiCAT 3228(M), BiCAT 8, BiCAT 8108 are from leading chemical companies in the United States, and the polycat SA8 is from Evonik Specialty Chemicals (Shanghai) Co., Ltd.
- the addition amount of the amine curing agent is 8-12 parts.
- the addition amount of amine curing agent is controlled within this range, which can further improve the comprehensive performance of low temperature curing rate, peel force, peel force retention rate and hydrolysis resistance.
- the temperature-sensitive catalyst is added in an amount of 0.1-2 parts.
- the addition amount of the temperature-sensitive catalyst is controlled within this range, which can further improve the comprehensive performance of low temperature curing rate, peel force, peel force retention rate and hydrolysis resistance.
- the raw materials for preparing the blocked polyurethane prepolymer include a combination of polyol and isocyanate.
- the raw materials for the preparation of the blocked polyurethane prepolymer further include a synergist and/or a blocking agent.
- the synergist includes ⁇ -aminopropyltriethoxysilane (KH550).
- KH550 is used as a synergist, which can be coupled under high temperature and high humidity conditions, resulting in self-crosslinking and improving hydrolysis resistance, especially maintaining high peeling force under high temperature and high humidity, thereby further The high peel strength, peel force retention and hydrolysis resistance of the solvent-free blocked polyurethane resin composition are improved.
- the blocking agent includes pyrazole compounds, preferably 3,5-dimethylpyrazole and/or pyrazole, more preferably 3,5-dimethylpyrazole.
- 3,5-dimethylpyrazole is preferably used as the sealing agent, which not only protects -NCO, can be stored stably, but also further improves the low-temperature curing rate, and the semi-dry lamination operation is controllable Sex is high.
- the raw materials for preparing the closed polyurethane prepolymer further include any one or a combination of at least two of a chain extender, a crosslinking agent or a leveling agent.
- the preparation raw materials of the closed polyurethane prepolymer include the following components according to mass percentage:
- the preparation raw materials of the closed polyurethane prepolymer include the following components according to mass percentage:
- the polyols include polyester polyols and/or polyether polyols.
- the polyester polyol is a polyester structure containing two terminal hydroxyl groups
- the polyether polyol is an ether structure containing two or three terminal hydroxyl groups.
- the molecular weight of the polyol is 250-10000, such as 1000, 2000, 3000, 4000, 6000, 8000 and the like.
- the polyester polyol comprises polyneopentyl adipate diol (PNA), poly-1,4-butanediol adipate diol (PBA), poly-1 adipate diol (PBA) ,6-Hexanediol diol, polyethylene adipate diol, polymethyltrimethylene adipate diol, polydiethylene adipate diol, or polybutylene adipate diol Any one or a combination of at least two of the methyl propylene glycol ester glycols.
- PNA polyneopentyl adipate diol
- PBA poly-1,4-butanediol adipate diol
- PBA poly-1 adipate diol
- 6-Hexanediol diol polyethylene adipate diol
- polymethyltrimethylene adipate diol polydiethylene adipate diol
- the polyether polyol comprises polyoxypropylene glycol (PPG), trifunctional PPG starting with methyl propylene glycol or glycerin, polyoxyethylene glycol (PEG) or polytetramethylene Any one or a combination of at least two of the ether glycols (PTMEG).
- PPG polyoxypropylene glycol
- PEG polyoxyethylene glycol
- PTMEG polytetramethylene Any one or a combination of at least two of the ether glycols
- the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polyoxypropylene glycol with a molecular weight of 2000, and polyoxypropylene glycol with a molecular weight of 1000, and the ratio of the three is 6:2:0.5.
- the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polyoxypropylene triol with a molecular weight of 6000, and polytetrahydrofuran ether glycol with a molecular weight of 2000, and the ratio of the three is 7:7:1.
- the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polyoxypropylene glycol with a molecular weight of 8000, and polyneopentyl adipate glycol with a molecular weight of 2000, and the ratio of the three is 4:4 :1.
- the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polymethyltrimethylene adipate glycol with a molecular weight of 2000, and polyneopentyl adipate glycol with a molecular weight of 4000.
- the ratio is 10:3:4.
- the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polyoxypropylene glycol with a molecular weight of 2000, and polyneopentyl adipate glycol with a molecular weight of 2000, and the ratio of the three is 1:3 :3.
- the polyol is a combination of polyoxypropylene diol with a molecular weight of 2000, polyoxypropylene triol with a molecular weight of 2000, and polyneopentyl adipate diol with a molecular weight of 2000, and the ratio of the three is 4:8 :1.
- the polyol is a combination of polyoxypropylene glycol with a molecular weight of 2000, polyoxypropylene triol with a molecular weight of 6000, and polyneopentyl adipate glycol with a molecular weight of 2000, and the ratio of the three is 4:8 :1.
- the polyol is a combination of polyoxypropylene triol with a molecular weight of 3000, polyoxypropylene diol with a molecular weight of 2000, and polyoxypropylene glycol with a molecular weight of 4000, and the ratio of the three is 8:4:3.
- the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000 and polyoxypropylene glycol with a molecular weight of 1000, and the ratio of the two is 14:1.
- the chain extender comprises any one of ethylene glycol (EG), 1,4-butanediol (BDO), neopentyl glycol (NPG) or 1,6-hexanediol (HDO) or at least two combinations.
- EG ethylene glycol
- BDO 1,4-butanediol
- NPG neopentyl glycol
- HDO 1,6-hexanediol
- the crosslinking agent comprises trimethylolpropane (TMP) and/or glycerol.
- TMP trimethylolpropane
- glycerol trimethylolpropane
- the isocyanate includes any one or a combination of at least two of toluene-2,4-diisocyanate, toluene-2,6-diisocyanate or diphenylmethane diisocyanate.
- the isocyanate may be selected from MDI-50, MDI-100, TDI-65, TDI-80, TDI-100, and the like.
- TDI-65 to TDI-100 refer to the mass ratio of toluene-2,4-diisocyanate to toluene-2,6-diisocyanate from 65:35 to 100:0.
- the leveling agent comprises BYK-9565 and/or BYK-333.
- molecular weight refers to the number average molecular weight.
- the preparation method of the closed polyurethane prepolymer comprises the following steps:
- the total mass of the first part of the polyol and the second part of the polyol is the added amount of the polyol in the formula.
- the preparation method further comprises: mixing a chain extender and/or a crosslinking agent with the first part of the polyol.
- the preparation method further comprises: adding a leveling agent after the adding of the synergist and the blocking agent.
- the specific process of the first reaction is as follows: incubate the reaction at 30-35°C for 1 hour, then react at 65-75°C (preferably 70°C) for 3 hours, and then heat up to 85-90°C and react for 3 hours .
- the second reaction is performed at 70-75° C. for 1 hour.
- the present application provides a polyurethane material, which is formed by curing the solvent-free closed-type polyurethane resin composition described in the first aspect.
- the curing temperature is 60-130°C, such as 60°C, 90°C, 120°C, and the like.
- the curing time is 1-3 minutes.
- the present application provides a leather product, and the raw materials for preparing the leather product include the polyurethane material described in the second aspect.
- a specific type of amine curing agent and a temperature-sensitive catalyst are used in the solvent-free closed polyurethane system, which can realize the rapid curing of the polyurethane resin at low temperature, and the obtained polyurethane resin has excellent peeling force, peeling force retention and hydrolysis resistance.
- the solvent-free blocked polyurethane resin composition provided by this application takes less than 2 minutes and 30 seconds to fully cure at 120°C, the minimum curing temperature can be as low as 60°C, and the time for curing to semi-dry at 90°C does not exceed 1 minute50 Second, the peeling force after complete curing can reach 8-12kg/cm 3 , and the peeling force retention rate can reach 80-95%.
- This embodiment provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 7.1 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
- DMDC amine curing agent
- polycat SA8 a temperature-sensitive catalyst
- the preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
- This embodiment provides a solvent-free sealed polyurethane resin composition, which is composed of 100 g of a sealed polyurethane prepolymer, 5.0 g of an amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
- DMDC amine curing agent
- polycat SA8 a temperature-sensitive catalyst
- the preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
- This embodiment provides a solvent-free sealed polyurethane resin composition, which is composed of 100 g of a sealed polyurethane prepolymer, 5.0 g of an amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
- DMDC amine curing agent
- polycat SA8 a temperature-sensitive catalyst
- the preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
- This embodiment provides a solvent-free sealed polyurethane resin composition, which is composed of 100 g of a sealed polyurethane prepolymer, 6.3 g of an amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
- DMDC amine curing agent
- polycat SA8 a temperature-sensitive catalyst
- the preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
- This embodiment provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 8.9 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
- DMDC amine curing agent
- polycat SA8 a temperature-sensitive catalyst
- the preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
- This example provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 6.5 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
- DMDC amine curing agent
- polycat SA8 a temperature-sensitive catalyst
- the preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
- This embodiment provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 8.3 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
- DMDC amine curing agent
- polycat SA8 a temperature-sensitive catalyst
- the preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
- This embodiment provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 6.2 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
- DMDC amine curing agent
- polycat SA8 a temperature-sensitive catalyst
- the preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
- This embodiment provides a solvent-free sealed polyurethane resin composition, which is composed of 100 g of sealed polyurethane prepolymer (Bayer HS-80) and 10 g of amine curing agent (DMDC);
- the preparation method is as follows:
- Example 1 The only difference from Example 1 is that DMDC is replaced with an equimolar amount of PACM, and the solvent-free blocked polyurethane resin composition is composed of 100 g of blocked polyurethane prepolymer, 6.3 g of amine curing agent (PACM) and 0.1 g of temperature sensitive Catalyst (polycat SA8) composition.
- PAM amine curing agent
- polycat SA8 temperature sensitive Catalyst
- Example 2 The only difference from Example 1 is that the DMDC is replaced with an equimolar amount of IPDA, and the solvent-free blocked polyurethane resin composition is composed of 100 g of blocked polyurethane prepolymer, 5.1 g of amine curing agent (IPDA) and 0.1 g of temperature sensitive. Catalyst (polycat SA8) composition.
- Example 1 The only difference from Example 1 is that KH550 is replaced by an equimolar amount of KH570.
- Example 1 The only difference from Example 1 is that 3,5-dimethylpyrazole is replaced by an equimolar amount of methyl ethyl ketoxime.
- Example 1 The only difference from Example 1 is that the amount of DMDC added is 4 g.
- Example 1 The only difference from Example 1 is that the amount of DMDC added is 13 g.
- Example 2 The difference from Example 1 is that the amount of polycat SA8 added is 10 g.
- Example 1 The difference from Example 1 is that DMDC is replaced by an equimolar amount of methylcyclohexanediamine (HTDA).
- HTDA methylcyclohexanediamine
- Example 1 The only difference from Example 1 is that polycat SA8 is replaced by an equimolar amount of dibutyltin dilaurate (T12).
- Example 1 The only difference from Example 1 is that the amount of DMDC added is 3 g.
- Example 1 The only difference from Example 1 is that the amount of DMDC added is 15 g.
- Example 1 The only difference from Example 1 is that the amount of polycat SA8 added is 0.05g.
- Example 1 The only difference from Example 1 is that the amount of polycat SA8 added is 11 g.
- Example 12 120°C 2 minutes
- Example 13 160°C 4 minutes
- Example 14 120°C 1 minute 40 seconds
- Example 15 120°C 2 minutes 30 seconds
- Example 16 120°C 40 seconds Comparative Example 1 120°C 5 minutes Comparative Example 2 120°C 5 minutes 10 seconds Comparative Example 3 120°C 2 minutes 50 seconds Comparative Example 4 120°C 3 minutes 30 seconds Comparative Example 5 120°C 3 minutes 50 seconds Comparative Example 6 120°C 30 seconds
- the present application can effectively improve the curing rate of the solvent-free blocked polyurethane resin composition by adding a specific amine curing agent and a temperature-sensitive catalyst.
- Comparative example 1 uses other kinds of room temperature curing agent, and comparative example 2 uses non-temperature-sensitive catalyst, and its curing rate is significantly lower than that of Example 1; the addition amount of curing agent in Comparative Examples 3 and 4 is not within the scope of this application , the curing rate is also reduced; in Comparative Example 5, the addition amount of temperature-sensitive catalyst is less, and the curing rate is significantly reduced. ingredients, which will result in a decrease in the peel force of the product.
- Example 9 Using the prepolymer of Bayer HS-80, compared with the prepolymer prepared with 3,5-dimethylpyrazole as the blocking agent and KH550 as the synergist, the curing rate of the polyurethane resin composition was significantly reduced , with higher cure times at higher temperatures.
- Example 13 By comparing Example 1 and Example 13, it can be seen that the curing rate can be further improved by selecting 3,5-dimethylpyrazole as the blocking agent (Example 1).
- the preparation method of the above-mentioned fabric film is: 100 parts of Huafeng JF-PDY-821H resin, 1 part of dynol 604 wetting and leveling agent (purchased from Evonik Specialty Chemicals (Shanghai) Co., Ltd.), dark blue water-based black pulp BLPE 517 (purchased from Evonik). 2 parts from Zhejiang Shenlan New Material Technology Co., Ltd.
- TEGO ViscoPlus 3030 thickener purchased from Evonik Specialty Chemicals (Shanghai) Co., Ltd.
- dispersed for 30 minutes filtered and deaerated for 30 minutes, and scraped for 10 seconds Bake at 90°C/110°C/130°C for 3 minutes each, then scrape for 15 seconds for the second time, and bake at 90°C/110°C/130°C for 3 minutes each to obtain a fabric film;
- the semi-dry described in this application means that the solvent-free blocked polyurethane resin composition has a certain viscosity, but is not completely cured.
- the solvent-free sealed polyurethane resin composition provided by the present application can be rapidly cured at a lower temperature, and after complete curing, it has a relatively high peel force and a peel force retention rate under high temperature and high humidity conditions.
- Comparative Example 1 uses other kinds of normal temperature curing agents, and Comparative Example 2 uses a non-temperature-sensitive catalyst, and the low-temperature curing rate is not as good as that of Example 1, and the peel force and peel force retention rate are also worse;
- Example 3 the amount of curing agent added is less, the curing rate is reduced, and the peel force of the product is significantly reduced.
- Comparative Example 4 the amount of curing agent added is too large, and the peel force retention rate of the product is significantly reduced; If the amount is less, the low-temperature curing rate is obviously reduced, and the addition amount of the temperature-sensitive catalyst in Comparative Example 6 is too large, and the peeling force and the peeling force retention rate are obviously deteriorated.
- DMDC is selected as the curing agent (Example 1), which is more conducive to improving peel force and peel force retention than PACM (Example 10) and IPDA (Example 11). .
- Example 13 By comparing Example 1 and Example 13, it can be seen that the use of dimethylpyrazole as the blocking agent (Example 1) can further promote low-temperature curing performance compared with other types of blocking agents (Example 13).
- Example 9 Using the prepolymer of Bayer HS-80, compared with the prepolymer prepared with 3,5-dimethylpyrazole as the blocking agent and KH550 as the synergist, it could not be cured at 90°C, It is proved that the selection of specific blocking agent and synergist in this application is beneficial to improve the low temperature curing performance of polyurethane.
- the present application illustrates the detailed method of the present application through the above-mentioned embodiments, but the present application is not limited to the above-mentioned detailed method, that is, it does not mean that the present application must rely on the above-mentioned detailed method for implementation.
- Those skilled in the art should understand that any improvement to the application, the equivalent replacement of each raw material of the product of the application, the addition of auxiliary components, the selection of specific methods, etc., all fall within the scope of protection and disclosure of the application.
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Abstract
The present application relates to a solvent-free blocked polyurethane resin composition, a polyurethane material, and a leather product. The solvent-free blocked polyurethane resin composition comprises the following components in parts by weight: 100 parts of a blocked polyurethane prepolymer, 4-13 parts of an amine curing agent, and 0.1-10 parts of a temperature-sensitive catalyst. The amine curing agent comprises any one or a combination of at least two of 3,3-dimethyl-4,4-diaminodicyclohexylmethane, 4,4-diaminodicyclohexylmethane, or isophorone diamine. The solvent-free blocked polyurethane resin composition provided by the present application is safe and environment-friendly, and can be quickly cured at relatively low temperature, thereby improving the production efficiency, and reducing the energy consumption; moreover, the solvent-free blocked polyurethane resin composition has excellent peel force, peel force retention rate and hydrolysis resistance.
Description
本申请涉及聚氨酯技术领域,尤其涉及一种无溶剂封闭型聚氨酯树脂组合物、聚氨酯材料和皮革产品。The present application relates to the technical field of polyurethane, and in particular, to a solvent-free sealed polyurethane resin composition, a polyurethane material and a leather product.
聚氨酯树脂是将多元醇、扩链剂、交联剂、异氰酸酯等为主要原料在某种工艺条件下合成得到,广泛应用于航空、电子器件、涂料、木材、皮革等行业,可分为四大类,其一,溶剂型聚氨酯树脂通过溶剂与水的置换或者高温蒸发溶剂从而烘烤固化,这种工艺对环境造成污染;其二,水性聚氨酯以水为分散介质替代溶剂实现了环保,但成本较高,耐水解、耐候性方面的性能差于溶剂型聚氨酯树脂;其三,无溶剂双组份聚氨酯树脂需要特殊设备才能满足应用,开放式的NCO基团使得产品储存要求严格,产品性能不稳定。其四,封闭型聚氨酯树脂可以稳定存放,但市面上绝大多数产品存在少量的溶剂,以及在应用过程中也存在固化温度高及固化时间长效率低的问题。Polyurethane resin is synthesized from polyols, chain extenders, crosslinking agents, isocyanates, etc. as the main raw materials under certain process conditions. It is widely used in aviation, electronic devices, coatings, wood, leather and other industries. It can be divided into four major categories. First, the solvent-based polyurethane resin is baked and cured by replacing the solvent with water or evaporating the solvent at high temperature, which causes pollution to the environment; second, the water-based polyurethane uses water as the dispersion medium to replace the solvent to achieve environmental protection, but the cost Higher, the performance of hydrolysis resistance and weather resistance is worse than that of solvent-based polyurethane resin; thirdly, solvent-free two-component polyurethane resin requires special equipment to meet the application, and the open NCO group makes the product storage requirements strict, and product performance is not good. Stablize. Fourth, the closed polyurethane resin can be stored stably, but most products on the market have a small amount of solvent, and there are also problems of high curing temperature and long curing time in the application process.
CN101812228A公开了一种全甲苯溶剂型聚氨酯树脂及其制备方法,以全甲苯溶剂型聚氨酯树脂重量百分比计,聚氨酯的含量为34%-36%,甲苯的含量为64%-66%,不含其他成分,因此可以用活性碳甲苯回收系统回收甲苯,克服了目前市场上溶剂型聚氨酯树脂因含多种溶剂组合而非单一溶剂,无法使用活性碳甲苯回收系统回收甲苯的弊端,提高了经济效益,且利于环保。该方案只能在一定程度上改善污染问题,无法完全避免该问题,随着社会各界对于环境污染问题的关注,该方案已不能满足现有要求。CN101812228A discloses an all-toluene solvent-based polyurethane resin and a preparation method thereof. Based on the weight percentage of the all-toluene solvent-based polyurethane resin, the content of polyurethane is 34%-36%, and the content of toluene is 64%-66%, excluding other Therefore, the activated carbon toluene recovery system can be used to recover toluene, which overcomes the disadvantage that the solvent-based polyurethane resin on the market cannot be used to recover toluene using the activated carbon toluene recovery system because it contains multiple solvent combinations instead of a single solvent, and the economic benefits are improved. And conducive to environmental protection. This scheme can only improve the pollution problem to a certain extent, but cannot completely avoid it. With the attention of all walks of life on the problem of environmental pollution, this scheme can no longer meet the existing requirements.
CN109266294A公开了一种封闭型聚氨酯胶黏剂及其制备方法,该制备方法包括:封闭型异氰酸酯合成以及封闭型聚氨酯胶黏剂制备,选用二苯基甲烷二异氰酸酯(MDI)为原料,发明一种MDI封闭型聚氨酯的合成方法。MDI封闭型聚氨酯可以与传统白乳胶按比例复配,制备封闭型聚氨酯胶黏剂。利用该胶黏剂压制的胶合板具有良好的胶合强度,没有甲醛释放。具有降低成本和环境友好等优点,可以作为室内材料的胶黏剂使用。但是,该胶黏剂在应用过程中存在固化温度高及固化时间长、效率低的问题。CN109266294A discloses a closed-type polyurethane adhesive and a preparation method thereof. The preparation method includes: synthesis of closed-type isocyanate and preparation of closed-type polyurethane adhesive. Diphenylmethane diisocyanate (MDI) is selected as a raw material to invent a Synthesis of MDI-blocked polyurethane. MDI closed polyurethane can be compounded with traditional white latex in proportion to prepare closed polyurethane adhesive. The plywood pressed with the adhesive has good bonding strength and no formaldehyde emission. It has the advantages of cost reduction and environmental friendliness, and can be used as an adhesive for interior materials. However, the adhesive has problems of high curing temperature, long curing time and low efficiency during application.
因此开发一种可以快速固化且无溶剂的封闭型聚氨酯树脂极为重要,不仅安全环保,而且能够在较低的温度下快速固化,使生产效率提升,能耗降低,同时具有优异的剥离强度、耐水解和耐候性。Therefore, it is extremely important to develop a fast-curing and solvent-free closed-type polyurethane resin, which is not only safe and environmentally friendly, but also can be quickly cured at a lower temperature, which can improve production efficiency and reduce energy consumption. It also has excellent peel strength and water resistance. solution and weatherability.
发明内容SUMMARY OF THE INVENTION
本申请提供了一种无溶剂封闭型聚氨酯树脂组合物、聚氨酯材料和皮革产品;其中,所述无溶剂封闭型聚氨酯树脂组合物不仅安全环保,而且能够在较低的温度下快速固化,使生产效率提升,能耗降低,同时具有优异的剥离力、剥离力保持率和耐水解性。The present application provides a solvent-free sealed polyurethane resin composition, a polyurethane material and a leather product; wherein, the solvent-free sealed polyurethane resin composition is not only safe and environmentally friendly, but also can be rapidly cured at a lower temperature, making production Increased efficiency and reduced energy consumption, with excellent peel force, peel force retention and hydrolysis resistance.
第一方面,本申请提供了一种无溶剂封闭型聚氨酯树脂组合物,所述无溶剂封闭型聚氨酯树脂组合物按照重量份数包括如下组分:In a first aspect, the present application provides a solvent-free sealed polyurethane resin composition, the solvent-free sealed polyurethane resin composition comprises the following components according to parts by weight:
封闭型聚氨酯预聚体 100份;100 copies of closed polyurethane prepolymer;
胺类固化剂 4-13份;和4-13 parts of amine curing agent; and
温敏催化剂 0.1-10份;0.1-10 copies of temperature-sensitive catalyst;
其中,所述胺类固化剂包括3,3-二甲基-4,4-二氨基二环己基甲烷(DMDC)、4,4-二氨基二环己基甲烷(PACM)或异氟尔酮二胺(IPDA)中的任意一种或至少两种组合。Wherein, the amine curing agent includes 3,3-dimethyl-4,4-diaminodicyclohexylmethane (DMDC), 4,4-diaminodicyclohexylmethane (PACM) or isophorone di Any one or a combination of at least two of the amines (IPDA).
所述胺类固化剂的添加量为4-13份,例如5重量份、6.2重量份、6.3重量份、6.5重量份、7.1重量份、8.3重量份、8.9重量份等;所述温敏催化剂的添加量为0.1-10份,例如0.1重量份等。The addition amount of the amine curing agent is 4-13 parts, such as 5 parts by weight, 6.2 parts by weight, 6.3 parts by weight, 6.5 parts by weight, 7.1 parts by weight, 8.3 parts by weight, 8.9 parts by weight, etc.; the temperature-sensitive catalyst The added amount is 0.1-10 parts, such as 0.1 parts by weight.
本申请在无溶剂封闭型聚氨酯体系中,采用特定类型的胺类固化剂与温敏催化剂复配,DMDC、PACM或IPDA具有硬度大、刚性强、伯氨基活性高、固化强度高的特性,与温敏催化剂搭配使用,适当升温后可快速活化反应基团,从而实现聚氨酯树脂在低温下的快速固化,并且,得到的聚氨酯树脂具有优异的剥离力、剥离力保持率和耐水解性。In this application, a specific type of amine curing agent and a temperature-sensitive catalyst are used in the solvent-free closed polyurethane system. DMDC, PACM or IPDA have the characteristics of high hardness, strong rigidity, high primary amino activity and high curing strength. The temperature-sensitive catalyst is used in combination, and the reactive group can be quickly activated after proper temperature rise, so as to realize the rapid curing of the polyurethane resin at low temperature, and the obtained polyurethane resin has excellent peeling force, peeling force retention rate and hydrolysis resistance.
此外,申请人在研究中发现,胺类固化剂的添加量必须控制在4-13份范围,才能获得上述有益效果,添加量小于4份,会导致产品剥离力低;添加量大于13份,会导致产品在高温高湿下剥离力衰减严重。同样的,温敏催化剂必须控制在0.1-10份范围内,添加量小于0.1份,会降低固化效率;添加量大于10份,会导致异常增粘,难以正常配料,并且产品剥离力降低。In addition, the applicant found in research that the addition amount of amine curing agent must be controlled in the range of 4-13 parts, in order to obtain the above beneficial effects, the addition amount is less than 4 parts, which will lead to low peeling force of the product; the addition amount is more than 13 parts, It will cause the peeling force of the product to be seriously attenuated under high temperature and high humidity. Similarly, the temperature-sensitive catalyst must be controlled within the range of 0.1-10 parts. If the addition amount is less than 0.1 part, the curing efficiency will be reduced; if the addition amount is more than 10 parts, it will lead to abnormal viscosity increase, making it difficult to do normal ingredients, and the product peeling force will be reduced.
优选地,所述胺类固化剂包括3,3-二甲基-4,4-二氨基二环己基甲烷。Preferably, the amine curing agent includes 3,3-dimethyl-4,4-diaminodicyclohexylmethane.
本申请优选DMDC作为固化剂,该固化剂具有高硬度、耐温性好的特点,相较于IPDA和PACM,制得的产品固化后强度高且能够在高温高湿条件下更好的保持剥离力。In this application, DMDC is preferred as the curing agent. The curing agent has the characteristics of high hardness and good temperature resistance. Compared with IPDA and PACM, the obtained product has high strength after curing and can better maintain peeling under high temperature and high humidity conditions. force.
本申请中,温敏催化剂指的是在室温下几乎不起催化效果,升温能够快速催化活性官能团的催化剂。In this application, a temperature-sensitive catalyst refers to a catalyst that has little catalytic effect at room temperature, and can rapidly catalyze active functional groups at elevated temperature.
优选地,所述温敏催化剂包括有机铋催化和/或有机胺催化剂。Preferably, the temperature-sensitive catalyst includes organic bismuth catalyst and/or organic amine catalyst.
优选地,所述温敏催化剂包括BiCAT Z(M)、BiCAT 3228(M)、BiCAT 8、BiCAT 8108或polycat SA8中的任意一种或至少两种组合,所述的BiCAT Z(M)、BiCAT 3228(M)、BiCAT 8、BiCAT 8108来源于美国领先化学品公司,所述的polycat SA8来源于赢创特种化学(上海)有限公司。Preferably, the temperature-sensitive catalyst comprises any one or a combination of at least two of BiCAT Z(M), BiCAT 3228(M), BiCAT 8, BiCAT 8108 or polycat SA8, and the BiCAT Z(M), BiCAT 3228(M), BiCAT 8, BiCAT 8108 are from leading chemical companies in the United States, and the polycat SA8 is from Evonik Specialty Chemicals (Shanghai) Co., Ltd.
优选地,所述胺类固化剂的添加量为8-12份。胺类固化剂的添加量控制在该范围内,能够进一步提高低温固化速率、剥离力、剥离力保持率和耐水解性综合性能。Preferably, the addition amount of the amine curing agent is 8-12 parts. The addition amount of amine curing agent is controlled within this range, which can further improve the comprehensive performance of low temperature curing rate, peel force, peel force retention rate and hydrolysis resistance.
优选地,所述温敏催化剂的添加量为0.1-2份。温敏催化剂的添加量控制在该范围内,能够进一步提高低温固化速率、剥离力、剥离力保持率和耐水解性综合性能。Preferably, the temperature-sensitive catalyst is added in an amount of 0.1-2 parts. The addition amount of the temperature-sensitive catalyst is controlled within this range, which can further improve the comprehensive performance of low temperature curing rate, peel force, peel force retention rate and hydrolysis resistance.
优选地,所述封闭型聚氨酯预聚体的制备原料包括多元醇和异氰酸酯的组合。Preferably, the raw materials for preparing the blocked polyurethane prepolymer include a combination of polyol and isocyanate.
优选地,所述封闭型聚氨酯预聚体的制备原料还包括协同剂和/或封闭剂。Preferably, the raw materials for the preparation of the blocked polyurethane prepolymer further include a synergist and/or a blocking agent.
优选地,所述协同剂包括γ-氨丙基三乙氧基硅烷(KH550)。Preferably, the synergist includes γ-aminopropyltriethoxysilane (KH550).
在本申请的优选技术方案中,采用KH550作为协同剂,其能够在高温高湿条件下进行偶联,产生自交联提高耐水解性,尤其是维持高温高湿下的高剥离力,从而进一步提高无溶剂封闭型聚氨酯树脂组合物的剥离强度高、剥离力保持率以及耐水解性能。In the preferred technical solution of the present application, KH550 is used as a synergist, which can be coupled under high temperature and high humidity conditions, resulting in self-crosslinking and improving hydrolysis resistance, especially maintaining high peeling force under high temperature and high humidity, thereby further The high peel strength, peel force retention and hydrolysis resistance of the solvent-free blocked polyurethane resin composition are improved.
优选地,所述封闭剂包括吡唑类化合物,优选3,5-二甲基吡唑和/或吡唑,进一步优选3,5-二甲基吡唑。Preferably, the blocking agent includes pyrazole compounds, preferably 3,5-dimethylpyrazole and/or pyrazole, more preferably 3,5-dimethylpyrazole.
在本申请的又一优选技术方案中,优选3,5-二甲基吡唑作为封闭剂,既保护了-NCO,可稳定储存,又能进一步提高低温固化速率,半干贴合操作可控性高。In another preferred technical solution of the present application, 3,5-dimethylpyrazole is preferably used as the sealing agent, which not only protects -NCO, can be stored stably, but also further improves the low-temperature curing rate, and the semi-dry lamination operation is controllable Sex is high.
优选地,所述封闭型聚氨酯预聚体的制备原料还包括扩链剂、交联剂或流 平剂中的任意一种或至少两种组合。Preferably, the raw materials for preparing the closed polyurethane prepolymer further include any one or a combination of at least two of a chain extender, a crosslinking agent or a leveling agent.
优选地,所述封闭型聚氨酯预聚体的制备原料按照质量百分比包括如下组分:Preferably, the preparation raw materials of the closed polyurethane prepolymer include the following components according to mass percentage:
优选地,所述封闭型聚氨酯预聚体的制备原料按照质量百分比包括如下组分:Preferably, the preparation raw materials of the closed polyurethane prepolymer include the following components according to mass percentage:
优选地,所述多元醇包括聚酯多元醇和/或聚醚多元醇。Preferably, the polyols include polyester polyols and/or polyether polyols.
所述聚酯多元醇为含2个端羟基含聚酯结构,所述聚醚多元醇为含2个或3个端羟基含醚结构。The polyester polyol is a polyester structure containing two terminal hydroxyl groups, and the polyether polyol is an ether structure containing two or three terminal hydroxyl groups.
优选地,所述多元醇的分子量为250-10000,例如1000、2000、3000、4000、6000、8000等。Preferably, the molecular weight of the polyol is 250-10000, such as 1000, 2000, 3000, 4000, 6000, 8000 and the like.
优选地,所述聚酯多元醇包括聚己二酸新戊二醇酯二醇(PNA)、聚己二酸-1,4-丁二醇酯二醇(PBA)、聚己二酸-1,6-己二醇酯二醇、聚己二酸乙二醇酯二醇、聚己二酸甲基丙二醇酯二醇、聚己二酸二甘醇酯二醇或聚己二酸丁二醇甲基丙二醇酯二醇中的任意一种或至少两种组合。Preferably, the polyester polyol comprises polyneopentyl adipate diol (PNA), poly-1,4-butanediol adipate diol (PBA), poly-1 adipate diol (PBA) ,6-Hexanediol diol, polyethylene adipate diol, polymethyltrimethylene adipate diol, polydiethylene adipate diol, or polybutylene adipate diol Any one or a combination of at least two of the methyl propylene glycol ester glycols.
优选地,所述聚醚多元醇包括聚氧化丙烯二醇(PPG)、以甲基丙二醇或甘油为起始剂的三官能度PPG、聚氧化乙烯二元醇(PEG)或聚四亚甲基醚二醇 (PTMEG)中的任意一种或至少两种组合。Preferably, the polyether polyol comprises polyoxypropylene glycol (PPG), trifunctional PPG starting with methyl propylene glycol or glycerin, polyoxyethylene glycol (PEG) or polytetramethylene Any one or a combination of at least two of the ether glycols (PTMEG).
优选地,所述多元醇为分子量4000的聚氧化丙烯二醇、分子量2000的聚氧化丙烯二醇、分子量1000的聚氧化丙烯二醇的组合,三者比例为6:2:0.5。Preferably, the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polyoxypropylene glycol with a molecular weight of 2000, and polyoxypropylene glycol with a molecular weight of 1000, and the ratio of the three is 6:2:0.5.
优选地,所述多元醇为分子量4000的聚氧化丙烯二醇、分子量6000的聚氧化丙烯三醇、分子量2000的聚四氢呋喃醚二醇的组合,三者比例为7:7:1。Preferably, the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polyoxypropylene triol with a molecular weight of 6000, and polytetrahydrofuran ether glycol with a molecular weight of 2000, and the ratio of the three is 7:7:1.
优选地,所述多元醇为分子量4000的聚氧化丙烯二醇、分子量8000的聚氧化丙烯二醇、分子量2000的聚己二酸新戊二醇酯二醇的组合,三者比例为4:4:1。Preferably, the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polyoxypropylene glycol with a molecular weight of 8000, and polyneopentyl adipate glycol with a molecular weight of 2000, and the ratio of the three is 4:4 :1.
优选地,所述多元醇为分子量4000的聚氧化丙烯二醇、分子量2000的聚己二酸甲基丙二醇酯二醇、分子量4000的聚己二酸新戊二醇酯二醇的组合,三者比例为10:3:4。Preferably, the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polymethyltrimethylene adipate glycol with a molecular weight of 2000, and polyneopentyl adipate glycol with a molecular weight of 4000. The ratio is 10:3:4.
优选地,所述多元醇为分子量4000的聚氧化丙烯二醇、分子量2000的聚氧化丙烯二醇、分子量2000的聚己二酸新戊二醇酯二醇的组合,三者比例为1:3:3。Preferably, the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000, polyoxypropylene glycol with a molecular weight of 2000, and polyneopentyl adipate glycol with a molecular weight of 2000, and the ratio of the three is 1:3 :3.
优选地,所述多元醇为分子量2000的聚氧化丙烯二醇、分子量2000的聚氧化丙烯三醇、分子量2000的聚己二酸新戊二醇酯二醇的组合,三者比例为4:8:1。Preferably, the polyol is a combination of polyoxypropylene diol with a molecular weight of 2000, polyoxypropylene triol with a molecular weight of 2000, and polyneopentyl adipate diol with a molecular weight of 2000, and the ratio of the three is 4:8 :1.
优选地,所述多元醇为分子量2000的聚氧化丙烯二醇、分子量6000的聚氧化丙烯三醇、分子量2000的聚己二酸新戊二醇酯二醇的组合,三者比例为4:8:1。Preferably, the polyol is a combination of polyoxypropylene glycol with a molecular weight of 2000, polyoxypropylene triol with a molecular weight of 6000, and polyneopentyl adipate glycol with a molecular weight of 2000, and the ratio of the three is 4:8 :1.
优选地,所述多元醇为分子量3000的聚氧化丙烯三醇、分子量2000的聚氧化丙烯二醇、分子量4000的聚氧化丙烯二醇的组合,三者比例为8:4:3。Preferably, the polyol is a combination of polyoxypropylene triol with a molecular weight of 3000, polyoxypropylene diol with a molecular weight of 2000, and polyoxypropylene glycol with a molecular weight of 4000, and the ratio of the three is 8:4:3.
优选地,所述多元醇为分子量4000的聚氧化丙烯二醇和分子量1000的聚氧化丙烯二醇的组合,二者比例为14:1。Preferably, the polyol is a combination of polyoxypropylene glycol with a molecular weight of 4000 and polyoxypropylene glycol with a molecular weight of 1000, and the ratio of the two is 14:1.
优选地,所述扩链剂包括乙二醇(EG)、1,4-丁二醇(BDO)、新戊二醇(NPG)或1,6-己二醇(HDO)的任意一种或至少两种组合。Preferably, the chain extender comprises any one of ethylene glycol (EG), 1,4-butanediol (BDO), neopentyl glycol (NPG) or 1,6-hexanediol (HDO) or at least two combinations.
优选地,所述交联剂包括三羟甲基丙烷(TMP)和/或甘油。Preferably, the crosslinking agent comprises trimethylolpropane (TMP) and/or glycerol.
优选地,所述异氰酸酯包括甲苯-2,4-二异氰酸酯、甲苯-2,6-二异氰酸酯或二苯基甲烷二异氰酸酯中的任意一种或至少两种组合。Preferably, the isocyanate includes any one or a combination of at least two of toluene-2,4-diisocyanate, toluene-2,6-diisocyanate or diphenylmethane diisocyanate.
示例性地,异氰酸酯可以选自MDI-50、MDI-100、TDI-65、TDI-80、TDI-100 等。TDI-65至TDI-100,指甲苯-2,4-二异氰酸酯与甲苯-2,6-二异氰酸酯的质量比从65:35至100:0。Illustratively, the isocyanate may be selected from MDI-50, MDI-100, TDI-65, TDI-80, TDI-100, and the like. TDI-65 to TDI-100 refer to the mass ratio of toluene-2,4-diisocyanate to toluene-2,6-diisocyanate from 65:35 to 100:0.
优选地,所述流平剂包括BYK-9565和/或BYK-333。Preferably, the leveling agent comprises BYK-9565 and/or BYK-333.
本申请中,“分子量”指的是数均分子量。In this application, "molecular weight" refers to the number average molecular weight.
优选地,所述封闭型聚氨酯预聚体的制备方法包括如下步骤:Preferably, the preparation method of the closed polyurethane prepolymer comprises the following steps:
将第一部分多元醇和异氰酸酯混合,进行第一次反应,再加入第二部分多元醇,反应至异氰酸酯基(-NCO)低于理论值,停止反应,加入协同剂和封闭剂,进行第二次反应,反应至体系中无异氰酸酯基,得到所述封闭型聚氨酯预聚体;Mix the first part of polyol and isocyanate to carry out the first reaction, then add the second part of polyol, react until the isocyanate group (-NCO) is lower than the theoretical value, stop the reaction, add synergist and blocking agent, and carry out the second reaction , react until there is no isocyanate group in the system to obtain the closed polyurethane prepolymer;
其中,所述第一部分多元醇和所述第二部分多元醇的总质量为配方中多元醇的添加量。Wherein, the total mass of the first part of the polyol and the second part of the polyol is the added amount of the polyol in the formula.
优选地,所述制备方法还包括:将扩链剂和/或交联剂与所述第一部分多元醇混合。Preferably, the preparation method further comprises: mixing a chain extender and/or a crosslinking agent with the first part of the polyol.
优选地,所述制备方法还包括:在所述加入协同剂和封闭剂之后加入流平剂。Preferably, the preparation method further comprises: adding a leveling agent after the adding of the synergist and the blocking agent.
优选地,所述第一次反应的具体过程为:先于30-35℃保温反应1小时,再于65-75℃(优选70℃)反应3小时,后升温至85-90℃反应3小时。Preferably, the specific process of the first reaction is as follows: incubate the reaction at 30-35°C for 1 hour, then react at 65-75°C (preferably 70°C) for 3 hours, and then heat up to 85-90°C and react for 3 hours .
优选地,所述第二次反应具体为在70-75℃反应1小时。Preferably, the second reaction is performed at 70-75° C. for 1 hour.
第二方面,本申请提供了一种聚氨酯材料,所述聚氨酯材料由第一方面所述的无溶剂封闭型聚氨酯树脂组合物固化而成。In a second aspect, the present application provides a polyurethane material, which is formed by curing the solvent-free closed-type polyurethane resin composition described in the first aspect.
优选地,所述固化的温度为60-130℃,例如60℃、90℃、120℃等。Preferably, the curing temperature is 60-130°C, such as 60°C, 90°C, 120°C, and the like.
优选地,所述固化的时间为1-3分钟。Preferably, the curing time is 1-3 minutes.
第三方面,本申请提供了一种皮革产品,所述皮革产品的制备原料包括第二方面所述的聚氨酯材料。In a third aspect, the present application provides a leather product, and the raw materials for preparing the leather product include the polyurethane material described in the second aspect.
相对于现有技术,本申请具有以下有益效果:Compared with the prior art, the present application has the following beneficial effects:
本申请在无溶剂封闭型聚氨酯体系中,采用特定类型的胺类固化剂与温敏催化剂复配,能够实现聚氨酯树脂在低温下的快速固化,并且,得到的聚氨酯树脂具有优异的剥离力、剥离力保持率和耐水解性。In the present application, a specific type of amine curing agent and a temperature-sensitive catalyst are used in the solvent-free closed polyurethane system, which can realize the rapid curing of the polyurethane resin at low temperature, and the obtained polyurethane resin has excellent peeling force, peeling force retention and hydrolysis resistance.
本申请提供的无溶剂封闭型聚氨酯树脂组合物在120℃完全固化的时间在2分钟30秒以下,最低固化温度可低至60℃,在90℃条件固化至半干的时间不 超过1分钟50秒,完全固化后的剥离力可达8-12kg/cm
3,剥离力保持率可达80-95%。
The solvent-free blocked polyurethane resin composition provided by this application takes less than 2 minutes and 30 seconds to fully cure at 120°C, the minimum curing temperature can be as low as 60°C, and the time for curing to semi-dry at 90°C does not exceed 1 minute50 Second, the peeling force after complete curing can reach 8-12kg/cm 3 , and the peeling force retention rate can reach 80-95%.
下面通过具体实施方式来进一步说明本申请的技术方案。本领域技术人员应该明了,所述实施例仅仅是帮助理解本申请,不应视为对本申请的具体限制。The technical solutions of the present application are further described below through specific embodiments. It should be understood by those skilled in the art that the embodiments are only for helping the understanding of the present application, and should not be regarded as a specific limitation of the present application.
以下实施例和对比例中所使用的原料的详细信息如下:Details of the raw materials used in the following examples and comparative examples are as follows:
原料raw material | 购买厂家buy manufacturers |
聚氧化丙烯二醇,分子量1000Polyoxypropylene glycol, molecular weight 1000 | 陶氏化学(中国)有限公司Dow Chemical (China) Co., Ltd. |
聚氧化丙烯二醇,分子量2000Polyoxypropylene glycol, molecular weight 2000 | 陶氏化学(中国)有限公司Dow Chemical (China) Co., Ltd. |
聚氧化丙烯三醇,分子量3000Polyoxypropylene triol, molecular weight 3000 | 佳化化学股份有限公司jia hua chemical co., ltd. |
聚氧化丙烯二醇,分子量4000Polyoxypropylene glycol, molecular weight 4000 | 佳化化学股份有限公司jia hua chemical co., ltd. |
聚氧化丙烯三醇,分子量6000Polyoxypropylene triol, molecular weight 6000 | 可利亚多元醇(南京)有限公司Kelia Polyol (Nanjing) Co., Ltd. |
聚氧化丙烯二醇,分子量8000Polyoxypropylene glycol, molecular weight 8000 | 佳化化学股份有限公司jia hua chemical co., ltd. |
聚四氢呋喃醚二醇,分子量2000Polytetrahydrofuran ether glycol, molecular weight 2000 | 巴斯夫(中国)有限公司BASF (China) Co., Ltd. |
三羟甲基丙烷(TMP)Trimethylolpropane (TMP) | 山东顺欣隆新材料科技有限公司Shandong Shunxinlong New Material Technology Co., Ltd. |
MDI-50MDI-50 | 万华化学集团股份有限公司Wanhua Chemical Group Co., Ltd. |
MDI-100MDI-100 | 万华化学集团股份有限公司Wanhua Chemical Group Co., Ltd. |
TDI-65TDI-65 | 优麦化学有限公司Umay Chemical Co., Ltd. |
TDI-80TDI-80 | 优麦化学有限公司Umay Chemical Co., Ltd. |
TDI-100TDI-100 | 拜耳(中国)有限公司Bayer (China) Co., Ltd. |
KH550KH550 | 南京辰工有机硅材料有限公司Nanjing Chengong Silicone Materials Co., Ltd. |
BYK-9565BYK-9565 | 德国毕克化学公司BYK chemical company |
3,5-二甲基吡唑3,5-Dimethylpyrazole | 武汉远成赛创科技有限责任公司Wuhan Yuancheng Saichuang Technology Co., Ltd. |
polycat SA8polycat SA8 | 赢创特种化学有限公司Evonik Specialty Chemicals Ltd. |
实施例1Example 1
本实施例提供一种无溶剂封闭型聚氨酯树脂组合物,由100g封闭型聚氨酯预聚物、7.1g胺类固化剂(DMDC)和0.1g温敏催化剂(polycat SA8)组成。This embodiment provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 7.1 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
上述封闭型聚氨酯预聚物的制备原料如下:The preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
(1)将600g聚氧化丙烯二醇(PPG-4000)和1g三羟甲基丙烷混合后,一次性加入TDI-80于33℃下搅拌反应30分钟,升温至85℃反应4小时,再投入200g聚氧化丙烯二醇(PPG-2000)和50g聚氧化丙烯二醇(PPG-1000)于80℃保温反应4小时,测试-NCO值为2.69%,降温至60℃滴加2g KH550(协同剂)和62g缓慢加入3,5-二甲基吡唑,随后一次性加入5g BYK-9565继续保温1小时,-NCO测试为零后出料,得到封闭型聚氨酯预聚体,25℃粘度为23000cps。(1) After mixing 600g of polyoxypropylene glycol (PPG-4000) and 1g of trimethylolpropane, add TDI-80 at one time, stir and react at 33°C for 30 minutes, heat up to 85°C and react for 4 hours, then put in 200g of polyoxypropylene glycol (PPG-2000) and 50g of polyoxypropylene glycol (PPG-1000) were incubated at 80°C for 4 hours, the test-NCO value was 2.69%, cooled to 60°C, and 2g KH550 (synergist) was added dropwise. ) and 62g slowly add 3,5-dimethylpyrazole, then add 5g BYK-9565 at one time and continue to keep the temperature for 1 hour, after the -NCO test is zero, the material is discharged to obtain a closed polyurethane prepolymer with a viscosity of 23000cps at 25°C .
(2)在所述封闭型聚氨酯预聚体中添加配方量的胺类固化剂和温敏催化剂,300rpm分散10分钟,得到无溶剂封闭型聚氨酯树脂组合物。(2) Adding formula amounts of amine curing agent and temperature-sensitive catalyst to the blocked polyurethane prepolymer, and dispersing at 300 rpm for 10 minutes to obtain a solvent-free blocked polyurethane resin composition.
实施例2Example 2
本实施例提供一种无溶剂封闭型聚氨酯树脂组合物,由100g封闭型聚氨酯预聚物、5.0g胺类固化剂(DMDC)和0.1g温敏催化剂(polycat SA8)组成。This embodiment provides a solvent-free sealed polyurethane resin composition, which is composed of 100 g of a sealed polyurethane prepolymer, 5.0 g of an amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
上述封闭型聚氨酯预聚物的制备原料如下:The preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
(1)将81.1g TDI-80和50g MDI-50搅拌混合15分钟,加入350g聚氧化丙烯二醇(PPG-4000)和350g聚氧化丙烯三醇(PPG-6000)先于65℃反应2小时,再升温至80℃反应5小时以上,降温至60℃再加入50g聚四氢呋喃醚二醇(PTMEG-2000)缓慢升温至80℃,保温3小时,测试-NCO值1.9%以下,降温至60℃,滴加KH550和缓慢加入3,5-二甲基吡唑,随后一次性加入5g BYK-9565继续保温1小时,-NCO测试为零后出料,得到封闭型聚氨酯预聚体,25℃粘度为28000cps。(1) Stir and mix 81.1g TDI-80 and 50g MDI-50 for 15 minutes, add 350g polyoxypropylene diol (PPG-4000) and 350g polyoxypropylene triol (PPG-6000) and react at 65°C for 2 hours , then heat up to 80°C for more than 5 hours, cool down to 60°C and add 50g polytetrahydrofuran ether diol (PTMEG-2000) and slowly heat up to 80°C, keep for 3 hours, test-NCO value below 1.9%, cool down to 60°C , dropwise add KH550 and slowly add 3,5-dimethylpyrazole, then add 5g BYK-9565 at one time and continue to keep warm for 1 hour, after the -NCO test is zero, the material is discharged to obtain a closed polyurethane prepolymer with a viscosity of 25°C is 28000cps.
(2)在所述封闭型聚氨酯预聚体中添加配方量的胺类固化剂和温敏催化剂,300rpm分散10分钟,得到无溶剂封闭型聚氨酯树脂组合物。(2) Adding formula amounts of amine curing agent and temperature-sensitive catalyst to the blocked polyurethane prepolymer, and dispersing at 300 rpm for 10 minutes to obtain a solvent-free blocked polyurethane resin composition.
实施例3Example 3
本实施例提供一种无溶剂封闭型聚氨酯树脂组合物,由100g封闭型聚氨酯预聚物、5.0g胺类固化剂(DMDC)和0.1g温敏催化剂(polycat SA8)组成。This embodiment provides a solvent-free sealed polyurethane resin composition, which is composed of 100 g of a sealed polyurethane prepolymer, 5.0 g of an amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
上述封闭型聚氨酯预聚物的制备原料如下:The preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
(1)将400g聚氧化丙烯二醇(PPG-4000)、400g聚氧化丙烯二醇(PPG-8000) 和2g三羟甲基丙烷于65℃搅拌混合30分钟,降温至40℃一次性加入77.5g TDI-100,搅拌30分钟后升温至90℃反应6小时以上,降温至50℃再加入100g聚己二酸新戊二醇酯二醇(PNA,分子量2000),缓慢升温至90℃继续保温反应3小时,测试-NCO值2.0%以下,降温至60℃,滴加KH550和缓慢加入3,5-二甲基吡唑,随后一次性加入5g BYK-9565继续保温1小时,-NCO测试为零后出料,得到封闭型聚氨酯预聚体,25℃粘度为22000cps。(1) 400 g of polyoxypropylene glycol (PPG-4000), 400 g of polyoxypropylene glycol (PPG-8000) and 2 g of trimethylolpropane were stirred and mixed at 65°C for 30 minutes, cooled to 40°C, and 77.5 g TDI-100, stir for 30 minutes and then heat up to 90°C for more than 6 hours, cool down to 50°C and add 100g polyneopentyl adipate diol (PNA, molecular weight 2000), slowly heat up to 90°C and continue to keep warm React for 3 hours, test the -NCO value below 2.0%, cool down to 60°C, add KH550 dropwise and slowly add 3,5-dimethylpyrazole, then add 5g BYK-9565 at one time and continue to hold for 1 hour, the -NCO test is After zero discharge, a closed polyurethane prepolymer is obtained, and the viscosity at 25°C is 22000cps.
(2)在所述封闭型聚氨酯预聚体中添加配方量的胺类固化剂和温敏催化剂,300rpm分散10分钟,得到无溶剂封闭型聚氨酯树脂组合物。(2) Adding formula amounts of amine curing agent and temperature-sensitive catalyst to the blocked polyurethane prepolymer, and dispersing at 300 rpm for 10 minutes to obtain a solvent-free blocked polyurethane resin composition.
实施例4Example 4
本实施例提供一种无溶剂封闭型聚氨酯树脂组合物,由100g封闭型聚氨酯预聚物、6.3g胺类固化剂(DMDC)和0.1g温敏催化剂(polycat SA8)组成。This embodiment provides a solvent-free sealed polyurethane resin composition, which is composed of 100 g of a sealed polyurethane prepolymer, 6.3 g of an amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
上述封闭型聚氨酯预聚物的制备原料如下:The preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
(1)将2.0g三羟甲基丙烷和500g聚氧化丙烯二醇(PPG-4000)于65℃下搅拌20分钟,降温至40度一次性加入95.0g TDI-65,升温至90℃反应5小时后,降温至70℃后加入150g聚己二酸甲基丙二醇酯二醇(分子量2000)及200g聚己二酸新戊二醇酯二醇(分子量4000),缓慢升温至80℃,继续保温反应6小时,测试-NCO值2.4%以下,降温至60℃,滴加KH550和缓慢加入3,5-二甲基吡唑,随后一次性加入7g BYK-9565继续保温1小时,-NCO测试为零 后出料,得到封闭型聚氨酯预聚体,25℃粘度为45000cps。(1) 2.0g trimethylolpropane and 500g polyoxypropylene glycol (PPG-4000) were stirred at 65°C for 20 minutes, cooled to 40°C, and 95.0g TDI-65 was added at one time, and the temperature was raised to 90°C for reaction 5 After one hour, the temperature was lowered to 70°C, and 150g of poly(methyltrimethylene adipate) diol (molecular weight 2000) and 200g of poly(neopentyl adipate) diol (molecular weight 4000) were added, and the temperature was slowly raised to 80°C, and the temperature was continued. React for 6 hours, test the -NCO value below 2.4%, cool down to 60°C, add KH550 dropwise and slowly add 3,5-dimethylpyrazole, then add 7g BYK-9565 at one time and continue to hold for 1 hour, the -NCO test is After zero discharge, a closed polyurethane prepolymer is obtained, and the viscosity at 25°C is 45000cps.
(2)在所述封闭型聚氨酯预聚体中添加配方量的胺类固化剂和温敏催化剂,300rpm分散10分钟,得到无溶剂封闭型聚氨酯树脂组合物。(2) Adding formula amounts of amine curing agent and temperature-sensitive catalyst to the blocked polyurethane prepolymer, and dispersing at 300 rpm for 10 minutes to obtain a solvent-free blocked polyurethane resin composition.
实施例5Example 5
本实施例提供一种无溶剂封闭型聚氨酯树脂组合物,由100g封闭型聚氨酯预聚物、8.9g胺类固化剂(DMDC)和0.1g温敏催化剂(polycat SA8)组成。This embodiment provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 8.9 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
上述封闭型聚氨酯预聚物的制备原料如下:The preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
(1)将2.0g三羟甲基丙烷和100g聚氧化丙烯二醇(PPG-4000)、300g聚氧化丙烯二醇(PPG-2000)和1.5g三羟甲基丙烷于65℃下搅拌20分钟,降温至40度一次性加入119g TDI-80,升温至80℃反应4小时,降温至70℃后加入300g聚己二酸新戊二醇酯二醇(分子量2000),缓慢升温至80℃,继续保温反应6小时,测试-NCO值3.5%以下,降温至60℃,滴加KH550和缓慢加入3,5-二甲基吡唑,随后一次性加入7g BYK-9565继续保温1小时,-NCO测试为零后出料,得到封闭型聚氨酯预聚体,25℃粘度为38000cps。(1) 2.0 g of trimethylolpropane, 100 g of polyoxypropylene glycol (PPG-4000), 300 g of polyoxypropylene glycol (PPG-2000) and 1.5 g of trimethylolpropane were stirred at 65° C. for 20 minutes , cooled to 40 degrees and added 119g TDI-80 at one time, heated to 80°C for 4 hours, cooled to 70°C and added 300g polyneopentyl adipate diol (molecular weight 2000), slowly heated to 80°C, Continue the incubation reaction for 6 hours, test the -NCO value below 3.5%, cool down to 60 ° C, add KH550 dropwise and slowly add 3,5-dimethylpyrazole, then add 7g BYK-9565 at one time and continue to incubate for 1 hour, -NCO After the test is zero, the material is discharged to obtain a closed polyurethane prepolymer with a viscosity of 38000cps at 25°C.
(2)在所述封闭型聚氨酯预聚体中添加配方量的胺类固化剂和温敏催化剂,300rpm分散10分钟,得到无溶剂封闭型聚氨酯树脂组合物。(2) Adding formula amounts of amine curing agent and temperature-sensitive catalyst to the blocked polyurethane prepolymer, and dispersing at 300 rpm for 10 minutes to obtain a solvent-free blocked polyurethane resin composition.
实施例6Example 6
本实施例提供一种无溶剂封闭型聚氨酯树脂组合物,由100g封闭型聚氨酯 预聚物、6.5g胺类固化剂(DMDC)和0.1g温敏催化剂(polycat SA8)组成。This example provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 6.5 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
上述封闭型聚氨酯预聚物的制备原料如下:The preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
(1)将200.0g聚氧化丙烯二醇(PPG-2000)和400g聚氧化丙烯三醇(PPG-6000)、40℃下搅拌20分钟,一次性加入84.5g MDI-50和19.6g TDI-80,升温至70℃反应2.5小时,降温至60℃后加入50g聚己二酸新戊二醇酯二醇(分子量2000),缓慢升温至75℃,继续保温反应4小时,测试-NCO值2.5%以下,降温至60℃,滴加KH550和缓慢加入3,5-二甲基吡唑,随后一次性加入6g BYK-9565继续保温1小时,-NCO测试为零后出料,得到封闭型聚氨酯预聚体,25℃粘度为29000cps。(1) 200.0 g of polyoxypropylene diol (PPG-2000) and 400 g of polyoxypropylene triol (PPG-6000) were stirred at 40°C for 20 minutes, and 84.5 g of MDI-50 and 19.6 g of TDI-80 were added at one time. , heat up to 70 ℃ and react for 2.5 hours, cool down to 60 ℃, add 50g polyneopentyl adipate diol (molecular weight 2000), slowly heat up to 75 ℃, continue to hold the reaction for 4 hours, test-NCO value 2.5% Below, the temperature was lowered to 60°C, KH550 was added dropwise and 3,5-dimethylpyrazole was slowly added, and then 6g of BYK-9565 was added at one time to keep the temperature for 1 hour. After the -NCO test was zero, the material was discharged to obtain a closed polyurethane Polymer, the viscosity at 25°C is 29000cps.
(2)在所述封闭型聚氨酯预聚体中添加配方量的胺类固化剂和温敏催化剂,300rpm分散10分钟,得到无溶剂封闭型聚氨酯树脂组合物。(2) Adding formula amounts of amine curing agent and temperature-sensitive catalyst to the blocked polyurethane prepolymer, and dispersing at 300 rpm for 10 minutes to obtain a solvent-free blocked polyurethane resin composition.
实施例7Example 7
本实施例提供一种无溶剂封闭型聚氨酯树脂组合物,由100g封闭型聚氨酯预聚物、8.3g胺类固化剂(DMDC)和0.1g温敏催化剂(polycat SA8)组成。This embodiment provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 8.3 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
上述封闭型聚氨酯预聚物的制备原料如下:The preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
(1)将400.0g聚氧化丙烯三醇(PPG-3000)和200g聚氧化丙烯二醇(PPG-2000)及150g聚氧化丙烯二醇(PPG-4000)40℃下搅拌20分钟,一次性加入88.2g TDI-80和42.2g MDI-100,升温至70℃反应6小时,测试-NCO值3.2%以下,降温至60℃,滴加KH550和缓慢加入3,5-二甲基吡唑,随后一次性加入6g BYK-9565继续保温1小时,-NCO测试为零后出料,得到封闭型聚氨酯预聚体,25℃粘度为42000cps。(1) 400.0 g of polyoxypropylene triol (PPG-3000), 200 g of polyoxypropylene diol (PPG-2000) and 150 g of polyoxypropylene diol (PPG-4000) were stirred at 40°C for 20 minutes, and added at one time. 88.2g TDI-80 and 42.2g MDI-100 were heated to 70°C for 6 hours, the test-NCO value was below 3.2%, cooled to 60°C, KH550 was added dropwise and 3,5-dimethylpyrazole was slowly added, followed by Add 6g of BYK-9565 at one time and continue to keep the temperature for 1 hour. After the -NCO test is zero, the material is discharged to obtain a closed polyurethane prepolymer with a viscosity of 42000cps at 25°C.
(2)在所述封闭型聚氨酯预聚体中添加配方量的胺类固化剂和温敏催化剂,300rpm分散10分钟,得到无溶剂封闭型聚氨酯树脂组合物。(2) Adding formula amounts of amine curing agent and temperature-sensitive catalyst to the blocked polyurethane prepolymer, and dispersing at 300 rpm for 10 minutes to obtain a solvent-free blocked polyurethane resin composition.
实施例8Example 8
本实施例提供一种无溶剂封闭型聚氨酯树脂组合物,由100g封闭型聚氨酯预聚物、6.2g胺类固化剂(DMDC)和0.1g温敏催化剂(polycat SA8)组成。This embodiment provides a solvent-free blocked polyurethane resin composition, which is composed of 100 g of blocked polyurethane prepolymer, 6.2 g of amine curing agent (DMDC) and 0.1 g of a temperature-sensitive catalyst (polycat SA8).
上述封闭型聚氨酯预聚物的制备原料如下:The preparation raw material of above-mentioned closed type polyurethane prepolymer is as follows:
(1)将2.0g TMP、700.0g聚氧化丙烯二醇(PPG-4000)和50g聚氧化丙烯二醇(PPG-1000)于40℃下搅拌20分钟,一次性加入123.8g MDI-50,升温至70℃反应6小时,测试-NCO值2.4%以下,降温至60℃,滴加KH550和缓慢加入3,5-二甲基吡唑,随后一次性加入5g BYK-9565继续保温1小时,-NCO测试为零后出料,得到封闭型聚氨酯预聚体,25℃粘度为22000cps。(1) 2.0g TMP, 700.0g polyoxypropylene glycol (PPG-4000) and 50g polyoxypropylene glycol (PPG-1000) were stirred at 40°C for 20 minutes, 123.8g MDI-50 was added at one time, and the temperature was increased. React at 70°C for 6 hours, test-NCO value below 2.4%, cool down to 60°C, dropwise add KH550 and slowly add 3,5-dimethylpyrazole, then add 5g BYK-9565 at one time and continue to hold for 1 hour,- After the NCO test is zero, the material is discharged to obtain a closed polyurethane prepolymer with a viscosity of 22000cps at 25°C.
(2)在所述封闭型聚氨酯预聚体中添加配方量的胺类固化剂和温敏催化剂,300rpm分散10分钟,得到无溶剂封闭型聚氨酯树脂组合物。(2) Adding formula amounts of amine curing agent and temperature-sensitive catalyst to the blocked polyurethane prepolymer, and dispersing at 300 rpm for 10 minutes to obtain a solvent-free blocked polyurethane resin composition.
实施例9Example 9
本实施例提供一种无溶剂封闭型聚氨酯树脂组合物,由100g封闭型聚氨酯预聚物(拜耳HS-80)和10g胺类固化剂(DMDC)组成;This embodiment provides a solvent-free sealed polyurethane resin composition, which is composed of 100 g of sealed polyurethane prepolymer (Bayer HS-80) and 10 g of amine curing agent (DMDC);
制备方法如下:The preparation method is as follows:
在所述拜耳HS-80中添加10g胺类固化剂,300rpm分散10分钟,得到无溶剂封闭型聚氨酯树脂组合物。10 g of an amine curing agent was added to the Bayer HS-80, and dispersed at 300 rpm for 10 minutes to obtain a solvent-free sealed polyurethane resin composition.
实施例10Example 10
与实施例1的区别仅在于,将DMDC替换为等摩尔量的PACM,无溶剂封闭型聚氨酯树脂组合物由100g封闭型聚氨酯预聚物、6.3g胺类固化剂(PACM)和0.1g温敏催化剂(polycat SA8)组成。The only difference from Example 1 is that DMDC is replaced with an equimolar amount of PACM, and the solvent-free blocked polyurethane resin composition is composed of 100 g of blocked polyurethane prepolymer, 6.3 g of amine curing agent (PACM) and 0.1 g of temperature sensitive Catalyst (polycat SA8) composition.
实施例11Example 11
与实施例1的区别仅在于,将DMDC替换为等摩尔量的IPDA,无溶剂封闭型聚氨酯树脂组合物由100g封闭型聚氨酯预聚物、5.1g胺类固化剂(IPDA)和0.1g温敏催化剂(polycat SA8)组成。The only difference from Example 1 is that the DMDC is replaced with an equimolar amount of IPDA, and the solvent-free blocked polyurethane resin composition is composed of 100 g of blocked polyurethane prepolymer, 5.1 g of amine curing agent (IPDA) and 0.1 g of temperature sensitive. Catalyst (polycat SA8) composition.
实施例12Example 12
与实施例1的区别仅在于,将KH550替换为等摩尔量的KH570。The only difference from Example 1 is that KH550 is replaced by an equimolar amount of KH570.
实施例13Example 13
与实施例1的区别仅在于,将3,5-二甲基吡唑替换为等摩尔量的甲乙酮肟。The only difference from Example 1 is that 3,5-dimethylpyrazole is replaced by an equimolar amount of methyl ethyl ketoxime.
实施例14Example 14
与实施例1的区别仅在于,DMDC的添加量为4g。The only difference from Example 1 is that the amount of DMDC added is 4 g.
实施例15Example 15
与实施例1的区别仅在于,DMDC的添加量为13g。The only difference from Example 1 is that the amount of DMDC added is 13 g.
实施例16Example 16
与实施例1的区别在于,polycat SA8的添加量为10g。The difference from Example 1 is that the amount of polycat SA8 added is 10 g.
对比例1Comparative Example 1
与实施例1的区别在于,将DMDC替换为等摩尔量的甲基环己二胺(HTDA)。The difference from Example 1 is that DMDC is replaced by an equimolar amount of methylcyclohexanediamine (HTDA).
对比例2Comparative Example 2
与实施例1的区别仅在于,将polycat SA8替换为等摩尔量的二月桂酸二丁基锡(T12)。The only difference from Example 1 is that polycat SA8 is replaced by an equimolar amount of dibutyltin dilaurate (T12).
对比例3Comparative Example 3
与实施例1的区别仅在于,DMDC的添加量为3g。The only difference from Example 1 is that the amount of DMDC added is 3 g.
对比例4Comparative Example 4
与实施例1的区别仅在于,DMDC的添加量为15g。The only difference from Example 1 is that the amount of DMDC added is 15 g.
对比例5Comparative Example 5
与实施例1的区别仅在于,polycat SA8的添加量为0.05g。The only difference from Example 1 is that the amount of polycat SA8 added is 0.05g.
对比例6Comparative Example 6
与实施例1的区别仅在于,polycat SA8的添加量为11g。The only difference from Example 1 is that the amount of polycat SA8 added is 11 g.
性能测试1performance test 1
测试上述实施例和对比例提供的无溶剂封闭型聚氨酯树脂组合物在一定固化温度下完全固化所需的时间,测试结果如下表所示:The time required for complete curing of the solvent-free blocked polyurethane resin compositions provided by the above examples and comparative examples is tested at a certain curing temperature, and the test results are shown in the following table:
固化温度curing temperature | 固化时间curing time | |
实施例1Example 1 | 120℃120℃ | 2分钟2 minutes |
实施例2Example 2 | 120℃120℃ | 2分钟2 minutes |
实施例3Example 3 | 120℃120℃ | 2分钟2 minutes |
实施例4Example 4 | 120℃120℃ | 2分钟2 minutes |
实施例5Example 5 | 120℃120℃ | 2分钟2 minutes |
实施例6Example 6 | 120℃120℃ | 2分钟2 minutes |
实施例7Example 7 | 120℃120℃ | 2分钟2 minutes |
实施例8Example 8 | 120℃120℃ | 2分钟2 minutes |
实施例9Example 9 | 160℃160℃ | 4分钟4 minutes |
实施例10Example 10 | 120℃120℃ | 2分钟2 minutes |
实施例11Example 11 | 120℃120℃ | 2分30秒2 minutes 30 seconds |
实施例12Example 12 | 120℃120℃ | 2分钟2 minutes |
实施例13Example 13 | 160℃160℃ | 4分钟4 minutes |
实施例14Example 14 | 120℃120℃ | 1分40秒1 minute 40 seconds |
实施例15Example 15 | 120℃120℃ | 2分30秒2 minutes 30 seconds |
实施例16Example 16 | 120℃120℃ | 40秒40 seconds |
对比例1Comparative Example 1 | 120℃120℃ | 5分钟5 minutes |
对比例2Comparative Example 2 | 120℃120℃ | 5分10秒5 minutes 10 seconds |
对比例3Comparative Example 3 | 120℃120℃ | 2分50秒2 minutes 50 seconds |
对比例4Comparative Example 4 | 120℃120℃ | 3分30秒3 minutes 30 seconds |
对比例5Comparative Example 5 | 120℃120℃ | 3分50秒3 minutes 50 seconds |
对比例6Comparative Example 6 | 120℃120℃ | 30秒30 seconds |
由上表可知,本申请通过添加特定的胺类固化剂和温敏催化剂,能够有效提高无溶剂封闭型聚氨酯树脂组合物的固化速率。It can be seen from the above table that the present application can effectively improve the curing rate of the solvent-free blocked polyurethane resin composition by adding a specific amine curing agent and a temperature-sensitive catalyst.
对比例1使用其他种类的常温固化剂,对比例2使用非温敏型催化剂,其固化速率相较于实施例1明显降低;对比例3和4中固化剂的添加量不在本申请范围之内,其固化速率也有所降低;对比例5中温敏催化剂的添加量较少,固化速率明显降低,对比例6中温敏催化剂的添加量较多,虽然固化较快,但是产品异常增粘,难以正常配料,会导致产品剥离力降低。Comparative example 1 uses other kinds of room temperature curing agent, and comparative example 2 uses non-temperature-sensitive catalyst, and its curing rate is significantly lower than that of Example 1; the addition amount of curing agent in Comparative Examples 3 and 4 is not within the scope of this application , the curing rate is also reduced; in Comparative Example 5, the addition amount of temperature-sensitive catalyst is less, and the curing rate is significantly reduced. ingredients, which will result in a decrease in the peel force of the product.
实施例9采用拜耳HS-80的预聚物,与以3,5-二甲基吡唑为封闭剂、KH550为协同剂制备得到的预聚物相比,聚氨酯树脂组合物的固化速率明显降低,在更高的温度下具有更高的固化时间。Example 9 Using the prepolymer of Bayer HS-80, compared with the prepolymer prepared with 3,5-dimethylpyrazole as the blocking agent and KH550 as the synergist, the curing rate of the polyurethane resin composition was significantly reduced , with higher cure times at higher temperatures.
通过对比实施例1和实施例13可知,选用3,5-二甲基吡唑作为封闭剂(实施例1),能够进一步提高固化速率。By comparing Example 1 and Example 13, it can be seen that the curing rate can be further improved by selecting 3,5-dimethylpyrazole as the blocking agent (Example 1).
性能测试2performance test 2
针对上述实施例和对比例提供的无溶剂封闭型聚氨酯树脂组合物进行如下测试:The following tests are carried out for the solvent-free blocked polyurethane resin compositions provided by the above examples and comparative examples:
(1)用300微米涂布棒刮涂于面料膜上,一定温度烘烤固化至半干,记录半干时间;(1) Scrape on the fabric film with a 300-micron coating rod, bake and solidify at a certain temperature to semi-dry, and record the semi-dry time;
上述面料膜的制备方法为:华峰JF-PDY-821H树脂100份,dynol 604润湿流平剂(购自赢创特种化学(上海)有限公司)1份,深蓝水性黑色浆BLPE 517 (购自浙江深蓝新材料科技股份有限公司)2份及TEGO ViscoPlus 3030增稠剂(购自赢创特种化学(上海)有限公司)0.8份,分散30分钟,再过滤脱泡30分钟,刮涂10秒于90℃/110℃/130℃各烘烤3分钟,随后二次刮涂15秒,于90℃/110℃/130℃各烘烤3分钟,得到面料膜;The preparation method of the above-mentioned fabric film is: 100 parts of Huafeng JF-PDY-821H resin, 1 part of dynol 604 wetting and leveling agent (purchased from Evonik Specialty Chemicals (Shanghai) Co., Ltd.), dark blue water-based black pulp BLPE 517 (purchased from Evonik). 2 parts from Zhejiang Shenlan New Material Technology Co., Ltd. and 0.8 part of TEGO ViscoPlus 3030 thickener (purchased from Evonik Specialty Chemicals (Shanghai) Co., Ltd.), dispersed for 30 minutes, filtered and deaerated for 30 minutes, and scraped for 10 seconds Bake at 90°C/110°C/130°C for 3 minutes each, then scrape for 15 seconds for the second time, and bake at 90°C/110°C/130°C for 3 minutes each to obtain a fabric film;
(2)半干后立即贴布,再用10kg的压辊进行重压贴合,继续烘烤至完全固化,按照QB/T2888-2007标准测试固化膜的剥离力,随后在70℃/95%湿度下放置5周后再次测试剥离力,按照(5周后剥离力/初始剥离力)×100%计算得到剥离力保持率。(2) Immediately apply the cloth after semi-drying, and then use a 10kg pressure roller for heavy pressure bonding, continue to bake until fully cured, and test the peeling force of the cured film according to the QB/T2888-2007 standard, then at 70 ° C/95% The peeling force was tested again after being placed under humidity for 5 weeks, and the peeling force retention rate was calculated according to (peeling force after 5 weeks/initial peeling force)×100%.
(3)针对无法在90℃半干贴的树脂组合物(实施例9和13)进行如下剥离力测试:华峰JF-PDY-511H树脂100份,BYK425增稠剂(购自德国毕克化学公司)2份增粘至15000cp左右,刮涂无法固化的树脂组合物在烘干后的JF-PDY-821H面料上,于160℃烘4分钟,再刮涂511H 15秒,5kg压辊贴合超纤1.0mm贝斯,90℃/110℃/130℃各烘烤3分钟,按照(2)的方式进行剥离力和剥离力保持率的测试。(3) The following peel force test was carried out for the resin compositions (Examples 9 and 13) that could not be semi-dry at 90°C: 100 parts of Huafeng JF-PDY-511H resin, BYK425 thickener (purchased from BYK, Germany) Company) 2 parts to increase the viscosity to about 15000cp, scrape the uncurable resin composition on the dried JF-PDY-821H fabric, bake at 160 ℃ for 4 minutes, and then scrape 511H for 15 seconds, 5kg pressure roller to fit The microfiber 1.0mm bass was baked at 90°C/110°C/130°C for 3 minutes each, and the peel force and peel force retention rate were tested according to the method (2).
上述测试结果如下表所示:The above test results are shown in the following table:
本申请所述的半干指无溶剂封闭型聚氨酯树脂组合物具有一定的粘性,但未彻底固化。The semi-dry described in this application means that the solvent-free blocked polyurethane resin composition has a certain viscosity, but is not completely cured.
由上表可知,本申请提供的无溶剂封闭型聚氨酯树脂组合物能够在较低温度下快速固化,且完全固化之后具有较高的剥离力以及高温高湿条件下的剥离力保持率。It can be seen from the above table that the solvent-free sealed polyurethane resin composition provided by the present application can be rapidly cured at a lower temperature, and after complete curing, it has a relatively high peel force and a peel force retention rate under high temperature and high humidity conditions.
与实施例1相比,对比例1使用其他种类的常温固化剂,对比例2使用非温敏型催化剂,低温固化速率均不及实施例1,且剥离力和剥离力保持率也变差;对比例3中固化剂的添加量较少,固化速率降低,且产品剥离力明显降低,对比例4中固化剂添加量过多,产品的剥离力保持率明显降低;对比例5中温敏催化剂的添加量较少,低温固化速率明显降低,对比例6中温敏催化剂的添加量过多,剥离力以及剥离力保持率均明显变差。Compared with Example 1, Comparative Example 1 uses other kinds of normal temperature curing agents, and Comparative Example 2 uses a non-temperature-sensitive catalyst, and the low-temperature curing rate is not as good as that of Example 1, and the peel force and peel force retention rate are also worse; In Example 3, the amount of curing agent added is less, the curing rate is reduced, and the peel force of the product is significantly reduced. In Comparative Example 4, the amount of curing agent added is too large, and the peel force retention rate of the product is significantly reduced; If the amount is less, the low-temperature curing rate is obviously reduced, and the addition amount of the temperature-sensitive catalyst in Comparative Example 6 is too large, and the peeling force and the peeling force retention rate are obviously deteriorated.
通过对比实施例1、10和11可知,选用DMDC作为固化剂(实施例1),相较于PACM(实施例10)和IPDA(实施例11),更有利于提高剥离力和剥离力保持率。By comparing Examples 1, 10 and 11, it can be seen that DMDC is selected as the curing agent (Example 1), which is more conducive to improving peel force and peel force retention than PACM (Example 10) and IPDA (Example 11). .
通过对比实施例1和12可知,采用KH550作为协同剂(实施例1),相较于其他类型的协同剂(实施例12),更有利于提高剥离力保持率。By comparing Examples 1 and 12, it can be seen that using KH550 as a synergist (Example 1) is more conducive to improving the peel force retention rate than other types of synergists (Example 12).
通过对比实施例1和实施例13可知,采用二甲基吡唑作为封闭剂(实施例1),相较于其他类型的封闭剂(实施例13),能够进一步促进低温固化性能。By comparing Example 1 and Example 13, it can be seen that the use of dimethylpyrazole as the blocking agent (Example 1) can further promote low-temperature curing performance compared with other types of blocking agents (Example 13).
实施例9采用拜耳HS-80的预聚物,与以3,5-二甲基吡唑为封闭剂、KH550为协同剂制备得到的预聚物相比,其在90℃条件下无法固化,证明本申请对于特定封闭剂和协同剂的选择有利于提高聚氨酯的低温固化性能。Example 9 Using the prepolymer of Bayer HS-80, compared with the prepolymer prepared with 3,5-dimethylpyrazole as the blocking agent and KH550 as the synergist, it could not be cured at 90°C, It is proved that the selection of specific blocking agent and synergist in this application is beneficial to improve the low temperature curing performance of polyurethane.
本申请通过上述实施例来说明本申请的详细方法,但本申请并不局限于上述详细方法,即不意味着本申请必须依赖上述详细方法才能实施。所属技术领域的技术人员应该明了,对本申请的任何改进,对本申请产品各原料的等效替换及辅助成分的添加、具体方式的选择等,均落在本申请的保护范围和公开范围之内。The present application illustrates the detailed method of the present application through the above-mentioned embodiments, but the present application is not limited to the above-mentioned detailed method, that is, it does not mean that the present application must rely on the above-mentioned detailed method for implementation. Those skilled in the art should understand that any improvement to the application, the equivalent replacement of each raw material of the product of the application, the addition of auxiliary components, the selection of specific methods, etc., all fall within the scope of protection and disclosure of the application.
Claims (12)
- 一种无溶剂封闭型聚氨酯树脂组合物,其按照重量份数包括如下组分:A solvent-free closed type polyurethane resin composition, which comprises the following components according to parts by weight:封闭型聚氨酯预聚体 100份;100 copies of closed polyurethane prepolymer;胺类固化剂 4-13份;和4-13 parts of amine curing agent; and温敏催化剂 0.1-10份;0.1-10 copies of temperature-sensitive catalyst;其中,所述胺类固化剂包括3,3-二甲基-4,4-二氨基二环己基甲烷、4,4-二氨基二环己基甲烷或异氟尔酮二胺中的任意一种或至少两种组合。Wherein, the amine curing agent includes any one of 3,3-dimethyl-4,4-diaminodicyclohexylmethane, 4,4-diaminodicyclohexylmethane or isophorone diamine or at least two combinations.
- 根据权利要求1所述的无溶剂封闭型聚氨酯树脂组合物,其中,所述胺类固化剂包括3,3-二甲基-4,4-二氨基二环己基甲烷。The solvent-free blocked polyurethane resin composition according to claim 1, wherein the amine curing agent comprises 3,3-dimethyl-4,4-diaminodicyclohexylmethane.
- 根据权利要求1或2所述的无溶剂封闭型聚氨酯树脂组合物,其中,所述温敏催化剂包括有机铋催化剂和/或有机胺催化剂。The solvent-free blocked polyurethane resin composition according to claim 1 or 2, wherein the temperature-sensitive catalyst comprises an organic bismuth catalyst and/or an organic amine catalyst.
- 根据权利要求1-3中任一项所述的无溶剂封闭型聚氨酯树脂组合物,其中,所述封闭型聚氨酯预聚体的制备原料包括多元醇和异氰酸酯的组合。The solvent-free blocked polyurethane resin composition according to any one of claims 1-3, wherein the raw materials for preparing the blocked polyurethane prepolymer include a combination of polyol and isocyanate.
- 根据权利要求1-4中任一项所述的无溶剂封闭型聚氨酯树脂组合物,其中,所述封闭型聚氨酯预聚体的制备原料还包括协同剂和/或封闭剂;The solvent-free blocked polyurethane resin composition according to any one of claims 1-4, wherein the preparation raw materials of the blocked polyurethane prepolymer further include a synergist and/or a blocking agent;优选地,所述协同剂包括γ―氨丙基三乙氧基硅烷;Preferably, the synergist comprises γ-aminopropyltriethoxysilane;优选地,所述封闭剂包括吡唑类化合物,优选3,5-二甲基吡唑和/或吡唑,进一步优选3,5-二甲基吡唑;Preferably, the blocking agent includes pyrazole compounds, preferably 3,5-dimethylpyrazole and/or pyrazole, more preferably 3,5-dimethylpyrazole;优选地,所述封闭型聚氨酯预聚体的制备原料还包括扩链剂、交联剂或流平剂中的任意一种或至少两种组合。Preferably, the raw materials for preparing the closed polyurethane prepolymer further include any one or a combination of at least two of a chain extender, a crosslinking agent or a leveling agent.
- 根据权利要求1-5中任一项所述的无溶剂封闭型聚氨酯树脂组合物,其中,所述封闭型聚氨酯预聚体的制备原料按照质量百分比包括如下组分:The solvent-free closed-type polyurethane resin composition according to any one of claims 1-5, wherein the preparation raw materials of the closed-type polyurethane prepolymer include the following components according to mass percentage:
- 根据权利要求1-6中任一项所述的无溶剂封闭型聚氨酯树脂组合物,其中,所述封闭型聚氨酯预聚体的制备原料按照质量百分比包括如下组分:The solvent-free closed-type polyurethane resin composition according to any one of claims 1-6, wherein the preparation raw materials of the closed-type polyurethane prepolymer include the following components according to mass percentage:
- 根据权利要求4-7中任一项所述的无溶剂封闭型聚氨酯树脂组合物,其中,所述多元醇包括聚酯多元醇和/或聚醚多元醇;The solvent-free blocked polyurethane resin composition according to any one of claims 4-7, wherein the polyol comprises polyester polyol and/or polyether polyol;优选地,所述多元醇的分子量为250-10000;Preferably, the molecular weight of the polyol is 250-10000;优选地,所述聚酯多元醇包括聚己二酸新戊二醇酯二醇、聚己二酸-1,4-丁二醇酯二醇、聚己二酸-1,6-己二醇酯二醇、聚己二酸乙二醇酯二醇、聚己二酸甲基丙二醇酯二醇、聚己二酸二甘醇酯二醇或聚己二酸丁二醇甲基丙二醇酯二醇中的任意一种或至少两种组合;Preferably, the polyester polyol comprises polyneopentyl adipate diol, poly-1,4-butanediol adipate diol, poly-1,6-hexanediol adipate Ester diol, polyethylene adipate diol, polymethyltrimethylene adipate diol, polydiethylene adipate diol, or polybutylene methyltrimethylene adipate diol any one or a combination of at least two;优选地,所述聚醚多元醇包括聚氧化丙烯二醇、以甲基丙二醇或甘油为起始剂的三官能度聚氧化丙烯二醇、聚氧化乙烯二元醇或聚四亚甲基醚二醇中的任意一种或至少两种组合。Preferably, the polyether polyol includes polyoxypropylene glycol, trifunctional polyoxypropylene glycol with methyl propylene glycol or glycerol as the initiator, polyoxyethylene glycol or polytetramethylene ether diol Any one or a combination of at least two of the alcohols.
- 根据权利要求4-8中任一项所述的无溶剂封闭型聚氨酯树脂组合物,其中,所述扩链剂包括乙二醇、1,4-丁二醇(BDO)、新戊二醇或1,6-己二醇的任意一种或至少两种组合;The solvent-free blocked polyurethane resin composition according to any one of claims 4-8, wherein the chain extender comprises ethylene glycol, 1,4-butanediol (BDO), neopentyl glycol or Any one or at least two combinations of 1,6-hexanediol;优选地,所述交联剂包括三羟甲基丙烷和/或甘油;Preferably, the cross-linking agent comprises trimethylolpropane and/or glycerol;优选地,所述异氰酸酯包括甲苯-2,4-二异氰酸酯、甲苯-2,6-二异氰酸酯或二苯基甲烷二异氰酸酯中的任意一种或至少两种组合。Preferably, the isocyanate includes any one or a combination of at least two of toluene-2,4-diisocyanate, toluene-2,6-diisocyanate or diphenylmethane diisocyanate.
- 根据权利要求6-8中任一项所述的无溶剂封闭型聚氨酯树脂组合物,其中,所述封闭型聚氨酯预聚体的制备方法包括如下步骤:The solvent-free closed-type polyurethane resin composition according to any one of claims 6-8, wherein the preparation method of the closed-type polyurethane prepolymer comprises the following steps:将第一部分多元醇和异氰酸酯混合,进行第一次反应,再加入第二部分多元醇,反应至异氰酸酯基低于理论值,停止反应,加入协同剂和封闭剂,进行第二次反应,反应至体系中无异氰酸酯基,得到所述封闭型聚氨酯预聚体;Mix the first part of polyol and isocyanate, carry out the first reaction, then add the second part of polyol, react until the isocyanate group is lower than the theoretical value, stop the reaction, add synergist and blocking agent, carry out the second reaction, and react to the system There is no isocyanate group in it to obtain the closed polyurethane prepolymer;其中,所述第一部分多元醇和所述第二部分多元醇的总质量为配方中多元醇的添加量;Wherein, the total mass of the first part of the polyol and the second part of the polyol is the added amount of the polyol in the formula;优选地,所述制备方法还包括:将扩链剂和/或交联剂与所述第一部分多元醇混合;Preferably, the preparation method further comprises: mixing a chain extender and/or a cross-linking agent with the first part of the polyol;优选地,所述制备方法还包括:在所述加入协同剂和封闭剂之后加入流平剂;Preferably, the preparation method further comprises: adding a leveling agent after the adding of the synergist and the blocking agent;优选地,所述第一次反应的具体过程为:先于30-35℃保温反应1小时,再于65-75℃反应3小时,后升温至85-90℃反应3小时;Preferably, the specific process of the first reaction is as follows: firstly, the temperature is kept at 30-35°C for 1 hour, then the reaction is performed at 65-75°C for 3 hours, and then the temperature is raised to 85-90°C for 3 hours;优选地,所述第二次反应具体为在70-75℃反应1小时。Preferably, the second reaction is performed at 70-75° C. for 1 hour.
- 一种聚氨酯材料,其由权利要求1-10中任一项所述的无溶剂封闭型聚氨酯树脂组合物固化而成;A polyurethane material, which is formed by curing the solvent-free closed-type polyurethane resin composition according to any one of claims 1-10;优选地,所述固化的温度为60-130℃;Preferably, the curing temperature is 60-130°C;优选地,所述固化的时间为1-3分钟。Preferably, the curing time is 1-3 minutes.
- 一种皮革产品,其制备原料包括权利要求11所述的聚氨酯材料。A leather product, the preparation raw material of which comprises the polyurethane material of claim 11 .
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CN114133529B (en) * | 2021-12-14 | 2023-07-14 | 上海华峰新材料研发科技有限公司 | Aromatic polyurethane resin and preparation method and application thereof |
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CN115010895B (en) * | 2022-07-05 | 2023-11-07 | 上海华峰新材料研发科技有限公司 | Enclosed polyurethane resin composition and preparation method and application thereof |
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