WO2019144420A1 - Hot-melt adhesive used for out-side membrane transfer printing technology and preparation method thereof - Google Patents

Hot-melt adhesive used for out-side membrane transfer printing technology and preparation method thereof Download PDF

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WO2019144420A1
WO2019144420A1 PCT/CN2018/074581 CN2018074581W WO2019144420A1 WO 2019144420 A1 WO2019144420 A1 WO 2019144420A1 CN 2018074581 W CN2018074581 W CN 2018074581W WO 2019144420 A1 WO2019144420 A1 WO 2019144420A1
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resin
melt adhesive
hot melt
diisocyanate
chloroacetate
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PCT/CN2018/074581
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French (fr)
Chinese (zh)
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宋攀可
张春
白永平
程宝强
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佛山市加恩新材料有限公司
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J175/00Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
    • C09J175/04Polyurethanes
    • C09J175/06Polyurethanes from polyesters
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J167/00Adhesives based on polyesters obtained by reactions forming a carboxylic ester link in the main chain; Adhesives based on derivatives of such polymers
    • C09J167/02Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/4009Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
    • C08G18/4063Mixtures of compounds of group C08G18/62 with other macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/42Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/4205Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups
    • C08G18/4208Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups
    • C08G18/4211Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups derived from aromatic dicarboxylic acids and dialcohols
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/62Polymers of compounds having carbon-to-carbon double bonds
    • C08G18/6275Polymers of halogen containing compounds having carbon-to-carbon double bonds; halogenated polymers of compounds having carbon-to-carbon double bonds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/74Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/76Polyisocyanates or polyisothiocyanates cyclic aromatic
    • C08G18/7657Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
    • C08G18/7664Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
    • C08G18/7671Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups containing only one alkylene bisphenyl group
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/08Macromolecular additives
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J175/00Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
    • C09J175/04Polyurethanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2170/00Compositions for adhesives
    • C08G2170/20Compositions for hot melt adhesives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend

Definitions

  • the invention relates to the field of hot melt adhesives, in particular to a hot melt adhesive for use in an extra-membrane transfer technology and a preparation method thereof.
  • OMD Out-side Model Decoration
  • OMD is a surface decoration technology that uses a high-pressure vacuum transfer to directly coat a graphic onto a plastic or metal surface to form a three-dimensional coating after printing the pattern on a transparent film.
  • the transparent film is the carrier of the graphic.
  • the OMD transfer film is first softened and softened at about 150 °C, and then tightly adsorbed to the surface of the object for about 10 to 15 seconds under the reduced pressure of the vacuum pump. After the bonding is completed, the substrate is peeled off, and the pattern remains on the surface of the object. .
  • OMD transfer film is the core of the external transfer technology. Different functional layers on the transfer film have different functions.
  • the adhesive layer provides the bonding force between the pattern layer and the surface of the object.
  • the properties of the hot melt adhesive used in the adhesive layer determine the pattern layer. Whether it is durable and durable, whether the decorated object can meet the requirements for use.
  • a related patent discloses an adhesive used in thermal transfer.
  • the patent No. CN201210436409.9 discloses a glass-based thermal transfer adhesive prepared by using an epoxy resin as a main component.
  • Patent No. CN201210436137.2 discloses a thermal transfer adhesive prepared by using polyurethane and acrylate as a curing system, a thermal transfer film and a thermal transfer method; Patent No.
  • CN201310194469.9 discloses an epoxy resin And polyurethane composite thermal transfer adhesive and preparation method thereof
  • patent No. CN201310194492.8 discloses an acrylic resin thermal transfer adhesive and a preparation method thereof.
  • the above patents all relate to the adhesive used in thermal transfer, but all of them use a curing agent, which is a thermosetting adhesive. When such an adhesive is used, a curing agent is added to the adhesive and a transfer film is prepared, which causes unstable transfer film performance, short storage period, and poor adaptability. In a high room temperature environment, the activity of the curing agent is enhanced, which tends to cause the adhesive to cure in advance, and the transfer film is scrapped.
  • CN200910099377.6 discloses a polyurethane hot melt adhesive for high-grade lining cloth and a preparation method thereof; and the patent No. CN201310277072.6 discloses a preparation of a composite hot melt adhesive for polyvinyl chloride decorative board.
  • the method of CN201510497729.9 discloses a method for preparing a modified polyester hot melt adhesive and a film thereof.
  • Patent No. CN201710451041.6 discloses a polyester amide hot melt adhesive and a preparation method thereof.
  • the transfer temperature is 120 ⁇ 150 ° C
  • the curing temperature is 60 ⁇ 100 ° C
  • the transfer time is 20 ⁇ 40s
  • the transfer pressure is the air source pressure 8Kg / m 2
  • the above patent belongs to the thermoplastic heat Melt, but the application is different, the thermodynamic index of the hot melt adhesive does not match the OMD process.
  • the materials decorated by the OMD process are various.
  • the polyester hot melt adhesives mentioned in some of the above patents are only suitable for products with rough surface such as cloth and wood, and have insufficient surface bonding strength for low surface energy. Therefore, it is also necessary to develop a hot melt adhesive suitable for the OMD process.
  • the object of the present invention is to provide a hot melt adhesive for film transfer printing technology, which is a thermoplastic adhesive, has wide application range, high peel strength and is suitable for OMD process; the preparation process is simple and easy, and is suitable for Mass production.
  • a hot melt adhesive for use in an off-film transfer technique comprising the following mass fractions:
  • the basic resin is synthesized by a modified chloroacetate resin and a saturated polyester under the action of a diisocyanate.
  • the substance for synthesizing the base resin is a diisocyanate, a modified chloroacetate resin, and a saturated polyester, and the mass fraction ratio of the three is from 1 to 2:2 to 3:5 to 7.
  • the modified chloroacetate resin is obtained by reacting N-2-aminoethyl-2-hydroxypropionamide with a ternary chloroacetate resin;
  • the N-2-aminoethyl-2-hydroxypropionamide is composed of the following mass fraction ratio substances.
  • the diisocyanate is in toluene diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate, dicyclohexylmethane diisocyanate, hexamethylene diisocyanate, lysine diisocyanate One or more.
  • the ternary chloroacetate resin is a terpolymer of vinyl acetate, vinyl chloride, and maleic anhydride; the mass fraction of the three is
  • the saturated polyester is a high molecular polymer obtained by dehydration condensation reaction of a dihydric alcohol and a dibasic acid, and the saturated polyester has a molecular weight of 10,000 to 50,000; One or more of an alcohol, propylene glycol, and butylene glycol; the dibasic acid is one or more of terephthalic acid, isophthalic acid, and phthalic acid.
  • the invention also discloses a method for preparing the above hot melt adhesive, comprising:
  • Step (1) placing the basic resin and the organic solvent in a container with a stirring device, controlling the temperature at 30 to 35 ° C, stirring and dissolving;
  • Step (2) sequentially adding a tackifier, a viscosity modifier and an antioxidant, heating to 60-80 ° C, sealing the container, stirring for 30 to 40 minutes;
  • Step (3) stop heating, keep warm for 30 minutes, let it cool naturally to room temperature.
  • the method of preparing the base resin comprises:
  • Step A the saturated polyester is dissolved in an organic solvent, wherein the mass fraction of the saturated polyester is 40 to 50%, and the mass fraction of the organic solvent is 50 to 60%;
  • Step B adding modified chloroacetate resin and diisocyanate, maintaining the reaction temperature in a four-necked bottle at 60-80 ° C, and reacting for 2 hours.
  • the method for preparing the modified chloroacetate resin comprises:
  • Step a weigh the appropriate amount of lactic acid and ethylenediamine in a reaction vessel, and slowly react for 30 minutes at -5 ° C. When the reactants are converted into a light yellow oily liquid, the reaction is placed in an oven at 60 ° C to dry. , obtaining N-2-aminoethyl-2-hydroxypropionamide;
  • Step b the ternary chloroacetate resin is dissolved in an organic solvent, wherein the mass fraction of the ternary chloroacetate resin is 20-30%, and the mass fraction of the organic solvent is 70-80%;
  • Step c adding N-aminoethyl-2-hydroxypropionamide corresponding to 5% to 8% by mass of the ternary chloroacetate resin in the solution of step b, adding a catalytic amount, and reacting for 1 hour in a four-necked bottle
  • the reaction temperature is 105 to 120 ° C, and the reactant is taken out and dried in an oven to remove the organic solvent for use.
  • the catalyst is from 1 to 3% sodium hypophosphite.
  • the beneficial effects are as follows: 1.
  • the hot melt adhesive is thermoplastic, does not need to add a curing agent, has stable product properties and long storage; 2. high peel strength, suitable for flexible and smooth film of OMD process; 3. simple preparation method Easy to implement, suitable for large-scale production.
  • Figure 1 is a process for synthesizing the modifier N-2-aminoethyl-2-hydroxypropionamide (NHPA) in the present invention.
  • Figure 2 is a schematic diagram of the synthesis of a base resin in the present invention.
  • Fig. 3 is a structural diagram of a molecular chain of a modified chloroacetate resin and a molecular chain of a saturated polyester grafted by a diisocyanate.
  • a represents ethylenediamine and lactic acid to produce EHPA
  • b represents EHPA and lactic acid to produce by-products.
  • a hot melt adhesive for use in an off-film transfer technique comprising the following mass fractions:
  • the basic resin is synthesized by a modified chloroacetate resin and a saturated polyester under the action of a diisocyanate.
  • the tackifier is one or more of rosin, modified rosin, C5 petroleum resin, C9 petroleum resin, and terpene resin for increasing the bonding strength.
  • the viscosity modifier is one or more of paraffin wax, microcrystalline wax, synthetic wax (PE or PP), and fossa wax.
  • the antioxidant is pentaerythritol ester, n-octadecyl propionate, 1,1,3-tris(2-methyl-4-hydroxy-5-tert-butylphenyl)butane, tris(nonylbenzene) Base) phosphite and the like.
  • the organic solvent is one or more of methyl ethyl ketone, cyclohexanone, acetone, toluene, xylene, ethyl acetate, butyl acetate, and isopropyl acetate.
  • the substance for synthesizing the base resin is a diisocyanate, a modified chloroacetate resin, and a saturated polyester, and the mass fraction ratio of the three is from 1 to 2:2 to 3:5 to 7.
  • ester bonds there are a large number of ester bonds in the main chain of saturated polyester.
  • the ester bond is easily hydrolyzed and broken under the acid-base environment and ultraviolet light, resulting in poor acid and alkali resistance of the polyester hot melt adhesive.
  • the modified polyester has chloroacetate resin.
  • the interpenetrating network structure formed by the saturated polyester, the chloroacetic resin has good acid and alkali resistance, and the molecular weight has a wrap-around effect on the ester bond, thereby protecting the prepared hot melt adhesive. Acid and alkali resistance and weather resistance.
  • the modified chloroacetate resin is obtained by reacting N-2-aminoethyl-2-hydroxypropionamide with a ternary chloroacetate resin;
  • the N-2-aminoethyl-2-hydroxypropionamide is composed of the following mass fraction ratio substances.
  • amidation reaction of a primary amino group in ethylenediamine with a carboxyl group in lactic acid to prepare a N-2-amino group having two different functional groups of an amine group (-NH2) and a hydroxyl group (-OH) is prepared.
  • Ethyl-2-hydroxypropionamide (NHPA) is prepared.
  • the ternary chloroacetate resin has a carboxyl group (-COOH) in its main chain, and the amidation reaction activity is higher than that of the esterification reaction, and the modifier NHPA is reacted with the ternary chloroacetate resin under certain conditions. Its -COOH is converted to -OH.
  • a means ethylenediamine and lactic acid to produce EHPA
  • b means that EHPA reacts with lactic acid to produce by-products. If too many by-products, EHPA is less. Will cause insufficient modification of the chloroacetate resin. Therefore, preferably, when synthesizing NHPA, the mass fraction of ethylenediamine is greater than the mass fraction of lactic acid, which contributes to the reaction in the direction in which NHPA is formed.
  • the diisocyanate is in toluene diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate, dicyclohexylmethane diisocyanate, hexamethylene diisocyanate, lysine diisocyanate One or more.
  • both the modified chloroacetate resin and the saturated polyester have a hydroxyl group (-OH), which can react with the diisocyanate to pass the molecular chain of the chloroacetate resin and the molecular chain of the saturated polyester.
  • the isocyanates are grafted together. This method grafts the polyfunctional chloroacetic resin onto the saturated polyester molecular chain, so that the saturated polyester contains more functional groups, which improves the adaptability of the hot melt adhesive to the bonding material.
  • the ternary chloroacetate resin is a terpolymer of vinyl acetate, vinyl chloride, and maleic anhydride; the mass fraction of the three is
  • Chloroacetate resin has excellent adhesion to metals, especially aluminum, and has excellent adhesion to PVC products, paper, fiber, glass, ceramic tile, sandstone and wood.
  • the saturated polyester is a high molecular polymer obtained by dehydration condensation reaction of a dihydric alcohol and a dibasic acid, the saturated polyester having a molecular weight of 10,000 to 50,000;
  • the glycol is ethylene glycol.
  • the dibasic acid is one or more of terephthalic acid, isophthalic acid and phthalic acid.
  • the dibasic acid of the synthetic polyester has a benzene ring to provide molecular cohesion.
  • the invention also discloses a method for preparing a hot melt adhesive as described above, comprising:
  • Step (1) placing the basic resin and the organic solvent in a container with a stirring device, controlling the temperature at 30 to 35 ° C, stirring and dissolving;
  • Step (2) sequentially adding a tackifier, a viscosity modifier and an antioxidant, heating to 60-80 ° C, sealing the container, stirring for 30 to 40 minutes;
  • Step (3) stop heating, keep warm for 30 minutes, let it cool naturally to room temperature.
  • the method of preparing the base resin comprises:
  • Step A the saturated polyester is dissolved in an organic solvent, wherein the mass fraction of the saturated polyester is 40 to 50%, and the mass fraction of the organic solvent is 50 to 60%;
  • Step B adding modified chloroacetate resin and diisocyanate, maintaining the reaction temperature in a four-necked bottle at 60-80 ° C, and reacting for 2 hours.
  • the four-necked flask also has a condensing unit and a stirring device.
  • the method for preparing the modified chloroacetate resin comprises:
  • Step a weigh the appropriate amount of lactic acid and ethylenediamine in a reaction vessel, and slowly react for 30 minutes at -5 ° C. When the reactants are converted into a light yellow oily liquid, the reaction is placed in an oven at 60 ° C to dry. , obtaining N-2-aminoethyl-2-hydroxypropionamide;
  • Step b the ternary chloroacetate resin is dissolved in an organic solvent, wherein the mass fraction of the ternary chloroacetate resin is 20-30%, and the mass fraction of the organic solvent is 70-80%;
  • Step c adding N-aminoethyl-2-hydroxypropionamide corresponding to 5% to 8% by mass of the ternary chloroacetate resin in the solution of step b, adding a catalytic amount, and reacting for 1 hour in a four-necked bottle
  • the reaction temperature is 105 to 120 ° C, and the reactant is taken out and dried in an oven to remove the organic solvent for use.
  • the reaction of ethylenediamine and lactic acid is very active, a side reaction occurs at normal temperature, so lowering the reaction temperature is advantageous for moving the reaction to the target product.
  • the four-necked flask was provided with a distillation apparatus and a stirring apparatus; it was dried in an oven to remove unreacted ethylenediamine impurities.
  • the catalyst is from 1 to 3% sodium hypophosphite.
  • Sodium hypochlorite is an amidation catalyst and the reaction is an amidation reaction.
  • Step 1 The reactant is weighed according to the mass fraction of 50% lactic acid and 50% ethylenediamine, and placed in a reaction vessel, and slowly reacted in a refrigerator at -5 ° C for 30 minutes. When the reactant is converted into a pale yellow oily liquid, The reaction was dried in an oven at 60 ° C to remove unreacted ethylenediamine to give N-2-aminoethyl-2-hydroxypropanamide (NHPA).
  • NHPA N-2-aminoethyl-2-hydroxypropanamide
  • Anhydride synthesis is prepared by dissolving in an organic solvent to prepare a solution, wherein the ternary chloroacetate resin is 20%, and the solvent is 80%.
  • Step 3 adding NHPA equivalent to 5% by mass of ternary chloroacetate resin to the solution of step 2, adding 1% catalytic amount of sodium hypophosphite, and reacting for 1 hour in a four-necked flask with a distillation device and a stirring device.
  • the reaction temperature was 105 ° C, and the reactant was taken out and dried in an oven to remove the solvent.
  • Step 4 Prepare a solution by dissolving the saturated polyester in an organic solvent, wherein the saturated polyester is 40% and the organic solvent is 60%.
  • the preparation process is as follows:
  • Step (1) the basic resin and the organic solvent are placed in a container equipped with a stirring device according to the above formula, and the temperature is controlled at 35 ° C, and stirred to dissolve.
  • Step (2) adding rosin, modified rosin, paraffin, pentaerythritol ester in turn, heating to 80 ° C, sealing the container, and stirring for 30 minutes.
  • Step (3) terminate the heating device, keep it for 30 minutes, and let it cool to room temperature naturally.
  • Step 1 The reactant is weighed according to the mass fraction of 45% lactic acid and 55% ethylenediamine, and placed in a reaction vessel, and slowly reacted in a refrigerator at -5 ° C for 30 minutes, when the reactant is converted into a pale yellow oily liquid. The reaction was dried in an oven at 60 ° C to remove unreacted ethylenediamine to give N-2-aminoethyl-2-hydroxypropanamide (NHPA).
  • NHPA N-2-aminoethyl-2-hydroxypropanamide
  • Step 3 adding 8% by mass of NHPA equivalent to ternary chloroacetate resin to the solution of step 2, adding 2% catalytic amount of sodium hypophosphite, and reacting for 1 hour in a four-necked flask with a distillation device and a stirring device.
  • the reaction temperature was maintained at 105 ° C, and the reactant was taken out and dried in an oven to remove the solvent.
  • Step 4 Prepare a solution by dissolving a saturated polyester in a solvent, wherein the saturated polyester is 40% and the organic solvent is 60%.
  • the preparation process is as follows:
  • Step (1) the basic resin and the solvent are placed in a container with a stirring device according to the above formula, and the temperature is controlled at 30 ° C, and the mixture is stirred and dissolved.
  • Step (2) sequentially adding C5 petroleum resin, microcrystalline wax, n-stearyl alcohol propionate, heating to 60 ° C, sealing the container, and stirring for 40 minutes.
  • Step (3) terminate the heating device, keep it for 30 minutes, and let it cool to room temperature naturally.
  • Step 1 The reactant is weighed according to the mass fraction of 45% lactic acid and 55% ethylenediamine, and placed in a reaction vessel, and slowly reacted in a refrigerator at -5 ° C for 30 minutes, when the reactant is converted into a pale yellow oily liquid. The reaction was dried in an oven at 60 ° C to remove unreacted ethylenediamine to give N-2-aminoethyl-2-hydroxypropanamide (NHPA).
  • NHPA N-2-aminoethyl-2-hydroxypropanamide
  • Step 3 adding NHPA equivalent to 5% by mass of ternary chloroacetate resin to the solution of step 2, adding 3% catalytic amount of sodium hypophosphite, and reacting for 1 hour in a four-necked flask with a distillation device and a stirring device.
  • the reaction temperature was 120 ° C, and the reactant was taken out and dried in an oven to remove the solvent.
  • Step 4 Prepare a solution by dissolving the saturated polyester in the solvent, wherein the saturated polyester is 50% and the organic solvent is 50%.
  • the apparatus was reacted in a four-necked bottle of the stirring device for 2 hours to obtain a copolymer of a saturated polyester and a chloroacetic resin.
  • the preparation process is as follows:
  • Step (1) the basic resin and the solvent are placed in a container with a stirring device according to the above formula, and the temperature is controlled at 35 ° C, and the mixture is stirred and dissolved.
  • Step (2) sequentially adding C9 petroleum tree, synthetic wax, 1,1,3-tris(2-methyl-4-hydroxy-5-tert-butylphenyl)butane, heating to 60 ° C, sealing the container, stirring 40 minutes.
  • Step (3) terminate the heating device, keep it for 30 minutes, and let it cool to room temperature naturally.
  • Step 1 The reactant is weighed according to the mass fraction of 50% lactic acid and 50% ethylenediamine, and placed in a reaction vessel, and slowly reacted in a refrigerator at -5 ° C for 30 minutes. When the reactant is converted into a pale yellow oily liquid, The reaction was dried in an oven at 60 ° C to remove unreacted ethylenediamine to give N-2-aminoethyl-2-hydroxypropanamide (NHPA).
  • NHPA N-2-aminoethyl-2-hydroxypropanamide
  • Step 3 adding NHPA equivalent to 5% by mass of ternary chloroacetate resin to the solution of step 2, adding 2% catalytic amount of sodium hypophosphite, and reacting for 1 hour in a four-necked flask with a distillation device and a stirring device.
  • the reaction temperature was 115 ° C, and the reactant was taken out and dried in an oven to remove the solvent.
  • Step 4 Prepare a solution by dissolving the saturated polyester in the solvent, wherein the saturated polyester is 45% and the organic solvent is 55%.
  • the preparation process is as follows:
  • Step (1) the basic resin and the solvent are placed in a container with a stirring device according to the above formula, and the temperature is controlled at 30 ° C, and the mixture is stirred and dissolved.
  • Step (2) sequentially adding terpene resin, fossa wax, and tris(nonylphenyl) phosphite, heating to 60 ° C, sealing the container, and stirring for 30 minutes.
  • Step (3) terminate the heating device, keep it for 30 minutes, and let it cool to room temperature naturally.
  • Test method The hot melt adhesive was characterized by DSC and TG, and the results are shown in Table 1.
  • Example 1 38.3 122.6 376.3
  • Example 2 40.5 125.4 384.5
  • Example 3 39.6 120.7 379.6
  • Example 4 37.2 118.7 374.2
  • the comparative example 0 is an unmodified saturated resin. From the data point of view, the glass transition temperature of the unmodified saturated resin is low, the performance of the prepared transfer film is unstable, and it may be softened in advance in a high temperature working environment. , affecting the process. It can be seen from the data of Examples 1 to 4 that, after the above modified resin, the glass transition temperature is increased to 37 to 40 ° C, the stability of the transfer film is improved, and the softening temperature is increased to 118 to 122 ° C, which is consistent with this temperature. The operating temperature of the external transfer, and the decomposition temperature is increased from 334 ° C to 374 ⁇ 384 ° C, improving the heat resistance of the hot melt adhesive.
  • Test method The hot melt adhesive was tested according to the 180° peel strength test standard ISO 8510-2-2006, and the results are shown in the table.
  • V0 represents Comparative Example 0
  • V1 represents Embodiment 1
  • V2 represents Embodiment 2
  • V3 represents Embodiment 3
  • V4 represents Embodiment 4.
  • the comparative example 0 is an unmodified saturated polyester. From the peeling strength test results, the peel strength of the modified saturated polyester is increased from 1.56 KN/m to 2.55 to 3.03 KN/m, and the hot melt adhesive is adhered. The quality of the joint is improved, the adhesion of the layer in the transfer film to the surface of the object to be decorated is improved, and the quality of the decoration is optimized.
  • Test method Bonding hot melt adhesive to different materials, including PET plastic, ABS plastic, PC plastic, glass, aluminum, copper. The test was then carried out in accordance with the 180° peel strength test standard ISO 8510-2-2006. The results are shown in Table 3.
  • the comparative example 0 is unmodified saturated polyester.
  • One of the requirements of OMD transfer technology for hot melt adhesive is 180° peel strength greater than 2.0KN/m. It can be seen from the data in the table that unmodified saturated polyester Only the peel strength to PET was greater than 2.0 KN/m, and sample examples 1-4 increased the peel strength of the material to the standard. For example, the peel strength of PET, PC, aluminum, and copper in Example 1 reached the standard. Therefore, the modified polyester has increased the adaptability of the material, expanding the decorative range of the OMD technology.
  • Test method The hot-melt adhesive is bonded to the aluminum sheet to prepare the bonded test piece, and the bonded test piece is separately placed in the outdoor, artificial sweat, hydrochloric acid solution (0.1 mol/L), sodium hydroxide solution (0.1 mol/L). In the middle, the peel strength was tested on the first day, the third day, and the seventh day, respectively. The test results are shown in Table 4.
  • the comparative example has a large loss of peel strength after soaking in the test liquid, because the saturated polyester has a large number of ester bonds in its main chain, and the ester bond is easily hydrolyzed and broken in an acid-base environment and ultraviolet light. , causing the phenomenon that the polyester hot melt adhesive is poor in acid and alkali resistance.
  • the polyester modified as described above exhibits good resistance in the test liquid.
  • the peel strengths of the sample of Example 1 after immersion in HCl for one day, three days, and seven days are respectively 2.43, 2.23, and 1.67 KN/m, and the peeling is performed. The strength loss was 0.76 KN/m, while the sample comparative loss lost 1.23 KN/m after seven days.
  • the chloroacetic resin has good acid and alkali resistance, and its molecular weight has a wrap-around effect on the ester bond. It has a protective effect, thus improving its acid and alkali resistance and weather resistance.
  • the hot-melt adhesive has improved acid and alkali resistance and weather resistance, which optimizes the weather resistance of the decorative coating and prolongs its service life.

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Abstract

A hot-melt adhesive used for out-side membrane transfer technology, comprising the following substances in mass fraction: a basic resin 30-40%; a tackifier 30-40%; a viscosity modifier 5-10%; an antioxidant 5-10%; and an organic solvent 25-50%; the basic resin is synthesized from a modified chloroacetate resin and saturated polyester under the action of a diisocyanate. The hot-melt adhesive in the present invention is thermoplastic, while a curing agent does not need to be added, a finished product has stable properties, storage period is long, and peel strength is high, thus being suitable for flexible and smooth membranes in an out-side model decoration (OMD) process; the preparation method is simple and easy, and is suitable for mass production.

Description

[根据细则26改正02.04.2018] 一种用于膜外转印技术的热熔胶及其制备方法[Correction according to Rule 26 02.04.2018] Hot melt adhesive for film transfer technology and preparation method thereof 技术领域Technical field
本发明涉及热熔胶领域,尤其涉及一种用于膜外转印技术的的热熔胶及其制备方法。The invention relates to the field of hot melt adhesives, in particular to a hot melt adhesive for use in an extra-membrane transfer technology and a preparation method thereof.
背景技术Background technique
OMD(Out-side Model Decoration)模外装饰技术是将图案文字印刷于透明薄膜后,采用高压真空转印直接将图文披覆在塑料或金属表面形成立体涂装的一种表面装饰技术,其中的透明薄膜是图文的载体。OMD转印膜转印图案时首先在150℃左右受热软化,然后在真空泵的减压下紧紧吸附到物体表面10~15s左右,贴合完成后撕下基材,图案就留在了物体表面。OMD (Out-side Model Decoration) is a surface decoration technology that uses a high-pressure vacuum transfer to directly coat a graphic onto a plastic or metal surface to form a three-dimensional coating after printing the pattern on a transparent film. The transparent film is the carrier of the graphic. When transferring the pattern, the OMD transfer film is first softened and softened at about 150 °C, and then tightly adsorbed to the surface of the object for about 10 to 15 seconds under the reduced pressure of the vacuum pump. After the bonding is completed, the substrate is peeled off, and the pattern remains on the surface of the object. .
OMD转印膜是模外转印技术的核心,转印膜上不同功能层具有不同的作用,其中胶层提供图案层和物体表面的结合力,胶层所用热熔胶的性能决定了图案层是否持久耐劳,被装饰物体是否能达到使用要求。有相关专利公开了涉及热转印所使用的胶黏剂,如专利号为:CN201210436409.9的专利公开了一种使用环氧树脂为主要成分制备的用于玻璃基的热转印胶黏剂;专利号CN201210436137.2的专利公开了一种以聚氨酯和丙烯酸酯为固化体系制备的热转印胶粘剂、热转印膜和热转印方法;专利号为CN201310194469.9公开了一种环氧树脂与聚氨酯复合热转印胶及其制备方法;专利号为CN201310194492.8的专利公开了一种丙烯酸树脂热转印胶及其制备方法。以上专利都涉及热转印所用的胶黏剂,但其中都用到了固化剂,属于热固性胶黏剂。此类胶黏剂在使用时要将固化剂加入胶黏剂中然后制备转印膜,这样会造成转印膜性能不稳定、储存期短、适应性差。在室温较高的环境下,固化剂活性增强,容易导致胶黏剂提前固化,令转印膜报废。另外,专利号为CN200910099377.6的专利公开了一种高档衬布用聚氨酯热熔胶及其制备方法;专利号为CN201310277072.6的专利公开了一种聚氯乙烯装饰板专用复合热熔胶的制备方法;CN201510497729.9的专利公开了一种改性聚酯热熔胶及其胶膜的制备方法。专利号为CN201710451041.6的专利公开了一种聚酯酰胺热熔胶及其制备方法。OMD有特定的工艺参数,其转印温度为120~150℃,熟化温度 为60~100℃,转印时间20~40s,转印压力为气源压力8Kg/m 2,以上的专利属于热塑性热熔胶,但应用场合各异,所涉及热熔胶的热力学指标与OMD工艺不相符。而且,OMD工艺所装饰的材料是多种多样的,上述部分专利所涉及到的聚酯热熔胶只适用于布料、木材等表面粗糙的产品,对于表面能低的表面粘接强度不够。因此,还需要研发一种适用于OMD工艺的热熔胶。 OMD transfer film is the core of the external transfer technology. Different functional layers on the transfer film have different functions. The adhesive layer provides the bonding force between the pattern layer and the surface of the object. The properties of the hot melt adhesive used in the adhesive layer determine the pattern layer. Whether it is durable and durable, whether the decorated object can meet the requirements for use. A related patent discloses an adhesive used in thermal transfer. For example, the patent No. CN201210436409.9 discloses a glass-based thermal transfer adhesive prepared by using an epoxy resin as a main component. Patent No. CN201210436137.2 discloses a thermal transfer adhesive prepared by using polyurethane and acrylate as a curing system, a thermal transfer film and a thermal transfer method; Patent No. CN201310194469.9 discloses an epoxy resin And polyurethane composite thermal transfer adhesive and preparation method thereof; patent No. CN201310194492.8 discloses an acrylic resin thermal transfer adhesive and a preparation method thereof. The above patents all relate to the adhesive used in thermal transfer, but all of them use a curing agent, which is a thermosetting adhesive. When such an adhesive is used, a curing agent is added to the adhesive and a transfer film is prepared, which causes unstable transfer film performance, short storage period, and poor adaptability. In a high room temperature environment, the activity of the curing agent is enhanced, which tends to cause the adhesive to cure in advance, and the transfer film is scrapped. In addition, the patent No. CN200910099377.6 discloses a polyurethane hot melt adhesive for high-grade lining cloth and a preparation method thereof; and the patent No. CN201310277072.6 discloses a preparation of a composite hot melt adhesive for polyvinyl chloride decorative board. The method of CN201510497729.9 discloses a method for preparing a modified polyester hot melt adhesive and a film thereof. Patent No. CN201710451041.6 discloses a polyester amide hot melt adhesive and a preparation method thereof. OMD has specific process parameters, the transfer temperature is 120 ~ 150 ° C, the curing temperature is 60 ~ 100 ° C, the transfer time is 20 ~ 40s, the transfer pressure is the air source pressure 8Kg / m 2 , the above patent belongs to the thermoplastic heat Melt, but the application is different, the thermodynamic index of the hot melt adhesive does not match the OMD process. Moreover, the materials decorated by the OMD process are various. The polyester hot melt adhesives mentioned in some of the above patents are only suitable for products with rough surface such as cloth and wood, and have insufficient surface bonding strength for low surface energy. Therefore, it is also necessary to develop a hot melt adhesive suitable for the OMD process.
发明内容Summary of the invention
本发明的目的在于提出一种用于膜外转印技术的的热熔胶,其是热塑性胶黏剂,适用范围广、剥离强度高、适用于OMD工艺;其制备工艺简单易行,适用于大规模生产。The object of the present invention is to provide a hot melt adhesive for film transfer printing technology, which is a thermoplastic adhesive, has wide application range, high peel strength and is suitable for OMD process; the preparation process is simple and easy, and is suitable for Mass production.
一种用于膜外转印技术的的热熔胶,包括如下质量分数的物质:A hot melt adhesive for use in an off-film transfer technique, comprising the following mass fractions:
Figure PCTCN2018074581-appb-000001
Figure PCTCN2018074581-appb-000001
其中,所述基本树脂由改性氯醋树脂和饱和聚酯在二异氰酸酯的作用下合成。Wherein, the basic resin is synthesized by a modified chloroacetate resin and a saturated polyester under the action of a diisocyanate.
在一些实施例中,合成所述基本树脂的物质为二异氰酸酯、改性氯醋树脂和饱和聚酯,三者的质量分数比为1~2:2~3:5~7。In some embodiments, the substance for synthesizing the base resin is a diisocyanate, a modified chloroacetate resin, and a saturated polyester, and the mass fraction ratio of the three is from 1 to 2:2 to 3:5 to 7.
在一些实施例中,所述改性氯醋树脂由N-2-氨基乙基-2-羟基丙酰胺和三元氯醋树脂反应所得;In some embodiments, the modified chloroacetate resin is obtained by reacting N-2-aminoethyl-2-hydroxypropionamide with a ternary chloroacetate resin;
所述N-2-氨基乙基-2-羟基丙酰胺由如下质量分数比的物质组成,The N-2-aminoethyl-2-hydroxypropionamide is composed of the following mass fraction ratio substances.
乳酸                 45~50%;Lactic acid 45 to 50%;
乙二胺               50~55%。Ethylenediamine 50 to 55%.
在一些实施例中,所述二异氰酸酯是甲苯二异氰酸酯、异佛尔酮二异氰酸酯、二苯基甲烷二异氰酸酯、二环己基甲烷二异氰酸酯、六亚甲基二异氰酸酯、赖氨酸二异氰酸酯中的一种或多种。In some embodiments, the diisocyanate is in toluene diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate, dicyclohexylmethane diisocyanate, hexamethylene diisocyanate, lysine diisocyanate One or more.
在一些实施例中,所述三元氯醋树脂是醋酸乙烯酯、氯乙烯和马来酸酐的三元聚合物;三者的质量分数是In some embodiments, the ternary chloroacetate resin is a terpolymer of vinyl acetate, vinyl chloride, and maleic anhydride; the mass fraction of the three is
醋酸乙烯酯    13~15%;Vinyl acetate 13-15%;
氯乙烯        81~84%Vinyl chloride 81~84%
马来酸酐      1~6%。Maleic anhydride 1 to 6%.
在一些实施例中,:所述饱和聚酯是二元醇和二元酸经脱水缩合反应得到的高分子聚合物,所述饱和聚酯的分子量为10000~50000;所述二元醇是乙二醇、丙二醇和丁二醇中的一种或多种;所述二元酸是对苯二甲酸、间苯二甲酸和邻苯二甲酸中的一种或多种。In some embodiments, the saturated polyester is a high molecular polymer obtained by dehydration condensation reaction of a dihydric alcohol and a dibasic acid, and the saturated polyester has a molecular weight of 10,000 to 50,000; One or more of an alcohol, propylene glycol, and butylene glycol; the dibasic acid is one or more of terephthalic acid, isophthalic acid, and phthalic acid.
本发明还公开了一种制备上述热熔胶的方法,包括:The invention also discloses a method for preparing the above hot melt adhesive, comprising:
步骤(一)、将基本树脂和有机溶剂置入带有搅拌装置的容器中,控制温度在30~35℃,搅拌溶解;Step (1), placing the basic resin and the organic solvent in a container with a stirring device, controlling the temperature at 30 to 35 ° C, stirring and dissolving;
步骤(二)、依次加入增粘剂、黏度调节剂和抗氧剂,升温至60~80℃,密封容器,搅拌30~40分钟;Step (2), sequentially adding a tackifier, a viscosity modifier and an antioxidant, heating to 60-80 ° C, sealing the container, stirring for 30 to 40 minutes;
步骤(三)、停止加热,保温30分钟,使其自然冷却至室温即可。Step (3), stop heating, keep warm for 30 minutes, let it cool naturally to room temperature.
在一些实施例中,所述基本树脂的制备方法包括:In some embodiments, the method of preparing the base resin comprises:
步骤A、将饱和聚酯溶于有机溶剂中,其中饱和聚酯的质量分数为40~50%,有机溶剂的质量分数为50~60%;Step A, the saturated polyester is dissolved in an organic solvent, wherein the mass fraction of the saturated polyester is 40 to 50%, and the mass fraction of the organic solvent is 50 to 60%;
步骤B、加入改性氯醋树脂和二异氰酸酯,在四口瓶中保持反应温度为60~80℃,反应2h即可。Step B, adding modified chloroacetate resin and diisocyanate, maintaining the reaction temperature in a four-necked bottle at 60-80 ° C, and reacting for 2 hours.
在一些实施例中,所述改性氯醋树脂的制备方法包括:In some embodiments, the method for preparing the modified chloroacetate resin comprises:
步骤a、称取适量乳酸和乙二胺置于反应容器中,在-5℃的环境下缓慢反应30分钟,待反应物转化为淡黄色油状液体时,将反应物置于60℃的烘箱中干燥,得到N-2-氨基乙基-2-羟基丙酰胺;Step a, weigh the appropriate amount of lactic acid and ethylenediamine in a reaction vessel, and slowly react for 30 minutes at -5 ° C. When the reactants are converted into a light yellow oily liquid, the reaction is placed in an oven at 60 ° C to dry. , obtaining N-2-aminoethyl-2-hydroxypropionamide;
步骤b、将三元氯醋树脂溶于有机溶剂中,其中三元氯醋树脂的质量分数为20~30%,有机溶剂的质量分数为70~80%;Step b, the ternary chloroacetate resin is dissolved in an organic solvent, wherein the mass fraction of the ternary chloroacetate resin is 20-30%, and the mass fraction of the organic solvent is 70-80%;
步骤c、在步骤b的溶液中加入相当于三元氯醋树脂5%~8%质量分数的N-2-氨基乙基-2-羟基丙酰胺,加入催化量,在四口瓶中反应1h,反应温度105~120℃,取出反应物于烘箱中干燥,除去有机溶剂备用。Step c, adding N-aminoethyl-2-hydroxypropionamide corresponding to 5% to 8% by mass of the ternary chloroacetate resin in the solution of step b, adding a catalytic amount, and reacting for 1 hour in a four-necked bottle The reaction temperature is 105 to 120 ° C, and the reactant is taken out and dried in an oven to remove the organic solvent for use.
在一些实施例中,所述催化剂是1~3%的次磷酸钠。In some embodiments, the catalyst is from 1 to 3% sodium hypophosphite.
其有益效果在于:1、此热熔胶是热塑性的,不需要添加固化剂,成品性质 稳定、储存器长;2、剥离强度高,适用于OMD工艺的柔性光滑的薄膜;3、制备方法简单易行,适用于大规模生产。The beneficial effects are as follows: 1. The hot melt adhesive is thermoplastic, does not need to add a curing agent, has stable product properties and long storage; 2. high peel strength, suitable for flexible and smooth film of OMD process; 3. simple preparation method Easy to implement, suitable for large-scale production.
附图说明DRAWINGS
图1是本发明中合成改性剂N-2-氨基乙基-2-羟基丙酰胺(NHPA)的过程。BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a process for synthesizing the modifier N-2-aminoethyl-2-hydroxypropionamide (NHPA) in the present invention.
图2是本发明中合成基本树脂的原理图。Figure 2 is a schematic diagram of the synthesis of a base resin in the present invention.
图3是改性氯醋树脂的分子链和饱和聚酯的分子链通过二异氰酸酯接枝的结构图。Fig. 3 is a structural diagram of a molecular chain of a modified chloroacetate resin and a molecular chain of a saturated polyester grafted by a diisocyanate.
其中,a表示乙二胺和乳酸生产EHPA,b表示EHPA与乳酸反应生产副产物。Among them, a represents ethylenediamine and lactic acid to produce EHPA, and b represents EHPA and lactic acid to produce by-products.
具体实施方式Detailed ways
下面结合附图来说明本发明的技术方案。The technical solution of the present invention will be described below with reference to the accompanying drawings.
一种用于膜外转印技术的的热熔胶,包括如下质量分数的物质:A hot melt adhesive for use in an off-film transfer technique, comprising the following mass fractions:
Figure PCTCN2018074581-appb-000002
Figure PCTCN2018074581-appb-000002
其中,所述基本树脂由改性氯醋树脂和饱和聚酯在二异氰酸酯的作用下合成。Wherein, the basic resin is synthesized by a modified chloroacetate resin and a saturated polyester under the action of a diisocyanate.
所述增粘剂为松香、改性松香、C5石油树脂、C9石油树脂、萜烯树脂中的一种或几种,用于增加粘接强度。The tackifier is one or more of rosin, modified rosin, C5 petroleum resin, C9 petroleum resin, and terpene resin for increasing the bonding strength.
所述粘度调节剂为石蜡、微晶蜡、合成蜡(PE或PP)、佛托蜡中的一种或几种。The viscosity modifier is one or more of paraffin wax, microcrystalline wax, synthetic wax (PE or PP), and fossa wax.
所述抗氧剂为季戊四醇酯、丙酸正十八碳醇酯、1,1,3-三(2-甲基-4-羟基-5-叔丁苯基)丁烷、三(壬基苯基)亚磷酸酯等。The antioxidant is pentaerythritol ester, n-octadecyl propionate, 1,1,3-tris(2-methyl-4-hydroxy-5-tert-butylphenyl)butane, tris(nonylbenzene) Base) phosphite and the like.
所述有机溶剂为丁酮、环己酮、丙酮、甲苯、二甲苯、醋酸乙酯、醋酸丁酯、醋酸异丙酯的一种或多种。The organic solvent is one or more of methyl ethyl ketone, cyclohexanone, acetone, toluene, xylene, ethyl acetate, butyl acetate, and isopropyl acetate.
在一些实施例中,合成所述基本树脂的物质为二异氰酸酯、改性氯醋树脂和饱和聚酯,三者的质量分数比为1~2:2~3:5~7。In some embodiments, the substance for synthesizing the base resin is a diisocyanate, a modified chloroacetate resin, and a saturated polyester, and the mass fraction ratio of the three is from 1 to 2:2 to 3:5 to 7.
饱和聚酯的主链中有大量酯键,酯键在酸碱环境及紫外光下容易水解、断裂,造成聚酯热熔胶耐酸碱性差,经过改性后的聚酯具有由氯醋树脂和饱和聚酯形成的互穿网络结构,氯醋树脂有很好的耐酸碱性,其分子量对酯键具有缠绕包裹的作用,对其起到了保护效果,因此提高了制成的热熔胶的耐酸碱及耐候性。There are a large number of ester bonds in the main chain of saturated polyester. The ester bond is easily hydrolyzed and broken under the acid-base environment and ultraviolet light, resulting in poor acid and alkali resistance of the polyester hot melt adhesive. The modified polyester has chloroacetate resin. The interpenetrating network structure formed by the saturated polyester, the chloroacetic resin has good acid and alkali resistance, and the molecular weight has a wrap-around effect on the ester bond, thereby protecting the prepared hot melt adhesive. Acid and alkali resistance and weather resistance.
在一些实施例中,所述改性氯醋树脂由N-2-氨基乙基-2-羟基丙酰胺和三元氯醋树脂反应所得;In some embodiments, the modified chloroacetate resin is obtained by reacting N-2-aminoethyl-2-hydroxypropionamide with a ternary chloroacetate resin;
所述N-2-氨基乙基-2-羟基丙酰胺由如下质量分数比的物质组成,The N-2-aminoethyl-2-hydroxypropionamide is composed of the following mass fraction ratio substances.
乳酸                45~50%;Lactic acid 45 to 50%;
乙二胺              50~55%。Ethylenediamine 50 to 55%.
如图1所示,利用乙二胺中伯胺基与乳酸中羧基进行酰胺化反应制备出具有胺基(-NH2)和羟基(-OH)两个不同官能团的改性剂N-2-氨基乙基-2-羟基丙酰胺(NHPA)。同时,三元氯醋树脂的主链上具有羧基(-COOH),利用酰胺化的反应活性比酯化反应高的特性,在一定条件下使改性剂NHPA与三元氯醋树脂反应,将其-COOH转化为-OH。在乙二胺和乳酸的化学反应中,有两条反应路线,其中a是指乙二胺和乳酸生产EHPA,b是指EHPA又与乳酸反应生产副产物,副产物过多的话,EHPA就少,会引起氯醋树脂改性不充分。因此,优选的,合成NHPA时,乙二胺的质量分数大于乳酸的质量分数,有助于反应向生成NHPA的方向进行。As shown in Fig. 1, amidation reaction of a primary amino group in ethylenediamine with a carboxyl group in lactic acid to prepare a N-2-amino group having two different functional groups of an amine group (-NH2) and a hydroxyl group (-OH) is prepared. Ethyl-2-hydroxypropionamide (NHPA). At the same time, the ternary chloroacetate resin has a carboxyl group (-COOH) in its main chain, and the amidation reaction activity is higher than that of the esterification reaction, and the modifier NHPA is reacted with the ternary chloroacetate resin under certain conditions. Its -COOH is converted to -OH. In the chemical reaction of ethylenediamine and lactic acid, there are two reaction routes, wherein a means ethylenediamine and lactic acid to produce EHPA, and b means that EHPA reacts with lactic acid to produce by-products. If too many by-products, EHPA is less. Will cause insufficient modification of the chloroacetate resin. Therefore, preferably, when synthesizing NHPA, the mass fraction of ethylenediamine is greater than the mass fraction of lactic acid, which contributes to the reaction in the direction in which NHPA is formed.
在一些实施例中,所述二异氰酸酯是甲苯二异氰酸酯、异佛尔酮二异氰酸酯、二苯基甲烷二异氰酸酯、二环己基甲烷二异氰酸酯、六亚甲基二异氰酸酯、赖氨酸二异氰酸酯中的一种或多种。In some embodiments, the diisocyanate is in toluene diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate, dicyclohexylmethane diisocyanate, hexamethylene diisocyanate, lysine diisocyanate One or more.
如图2和图3所示,改性氯醋树脂和饱和聚酯都带有羟基(-OH),能与二异氰酸酯发生反应,使氯醋树脂的分子链和饱和聚酯的分子链通过二异氰酸酯接枝在一起。这种方法将多官能团的氯醋树脂接枝在饱和聚酯分子链上,使饱和聚酯含有更多的官能团,提高了热熔胶对粘接材料的适应性。As shown in Fig. 2 and Fig. 3, both the modified chloroacetate resin and the saturated polyester have a hydroxyl group (-OH), which can react with the diisocyanate to pass the molecular chain of the chloroacetate resin and the molecular chain of the saturated polyester. The isocyanates are grafted together. This method grafts the polyfunctional chloroacetic resin onto the saturated polyester molecular chain, so that the saturated polyester contains more functional groups, which improves the adaptability of the hot melt adhesive to the bonding material.
在一些实施例中,所述三元氯醋树脂是醋酸乙烯酯、氯乙烯和马来酸酐的三元聚合物;三者的质量分数是In some embodiments, the ternary chloroacetate resin is a terpolymer of vinyl acetate, vinyl chloride, and maleic anhydride; the mass fraction of the three is
醋酸乙烯酯   13~15%;Vinyl acetate 13-15%;
氯乙烯       81~84%Vinyl chloride 81~84%
马来酸酐     1~6%。Maleic anhydride 1 to 6%.
氯醋树脂对金属尤其是铝有优越的粘着性,对PVC制品、纸、纤维、玻璃、瓷砖、沙石、木材也有优良的粘着性。Chloroacetate resin has excellent adhesion to metals, especially aluminum, and has excellent adhesion to PVC products, paper, fiber, glass, ceramic tile, sandstone and wood.
在一些实施例中,所述饱和聚酯是二元醇和二元酸经脱水缩合反应得到的高分子聚合物,所述饱和聚酯的分子量为10000~50000;所述二元醇是乙二醇、丙二醇和丁二醇中的一种或多种;所述二元酸是对苯二甲酸、间苯二甲酸和邻苯二甲酸中的一种或多种。In some embodiments, the saturated polyester is a high molecular polymer obtained by dehydration condensation reaction of a dihydric alcohol and a dibasic acid, the saturated polyester having a molecular weight of 10,000 to 50,000; the glycol is ethylene glycol. One or more of propylene glycol and butylene glycol; the dibasic acid is one or more of terephthalic acid, isophthalic acid and phthalic acid.
合成聚酯的二元酸中带有苯环,可以提供分子内聚力。The dibasic acid of the synthetic polyester has a benzene ring to provide molecular cohesion.
本发明还公开了一种制备如上所述的热熔胶的方法,包括:The invention also discloses a method for preparing a hot melt adhesive as described above, comprising:
步骤(一)、将基本树脂和有机溶剂置入带有搅拌装置的容器中,控制温度在30~35℃,搅拌溶解;Step (1), placing the basic resin and the organic solvent in a container with a stirring device, controlling the temperature at 30 to 35 ° C, stirring and dissolving;
步骤(二)、依次加入增粘剂、黏度调节剂和抗氧剂,升温至60~80℃,密封容器,搅拌30~40分钟;Step (2), sequentially adding a tackifier, a viscosity modifier and an antioxidant, heating to 60-80 ° C, sealing the container, stirring for 30 to 40 minutes;
步骤(三)、停止加热,保温30分钟,使其自然冷却至室温即可。Step (3), stop heating, keep warm for 30 minutes, let it cool naturally to room temperature.
在一些实施例中,所述基本树脂的制备方法包括:In some embodiments, the method of preparing the base resin comprises:
步骤A、将饱和聚酯溶于有机溶剂中,其中饱和聚酯的质量分数为40~50%,有机溶剂的质量分数为50~60%;Step A, the saturated polyester is dissolved in an organic solvent, wherein the mass fraction of the saturated polyester is 40 to 50%, and the mass fraction of the organic solvent is 50 to 60%;
步骤B、加入改性氯醋树脂和二异氰酸酯,在四口瓶中保持反应温度为60~80℃,反应2h即可。Step B, adding modified chloroacetate resin and diisocyanate, maintaining the reaction temperature in a four-necked bottle at 60-80 ° C, and reacting for 2 hours.
四口烧瓶中还带有冷凝装置和搅拌装置。The four-necked flask also has a condensing unit and a stirring device.
在一些实施例中,所述改性氯醋树脂的制备方法包括:In some embodiments, the method for preparing the modified chloroacetate resin comprises:
步骤a、称取适量乳酸和乙二胺置于反应容器中,在-5℃的环境下缓慢反应30分钟,待反应物转化为淡黄色油状液体时,将反应物置于60℃的烘箱中干燥,得到N-2-氨基乙基-2-羟基丙酰胺;Step a, weigh the appropriate amount of lactic acid and ethylenediamine in a reaction vessel, and slowly react for 30 minutes at -5 ° C. When the reactants are converted into a light yellow oily liquid, the reaction is placed in an oven at 60 ° C to dry. , obtaining N-2-aminoethyl-2-hydroxypropionamide;
步骤b、将三元氯醋树脂溶于有机溶剂中,其中三元氯醋树脂的质量分数为20~30%,有机溶剂的质量分数为70~80%;Step b, the ternary chloroacetate resin is dissolved in an organic solvent, wherein the mass fraction of the ternary chloroacetate resin is 20-30%, and the mass fraction of the organic solvent is 70-80%;
步骤c、在步骤b的溶液中加入相当于三元氯醋树脂5%~8%质量分数的N-2-氨基乙基-2-羟基丙酰胺,加入催化量,在四口瓶中反应1h,反应温度 105~120℃,取出反应物于烘箱中干燥,除去有机溶剂备用。Step c, adding N-aminoethyl-2-hydroxypropionamide corresponding to 5% to 8% by mass of the ternary chloroacetate resin in the solution of step b, adding a catalytic amount, and reacting for 1 hour in a four-necked bottle The reaction temperature is 105 to 120 ° C, and the reactant is taken out and dried in an oven to remove the organic solvent for use.
步骤a中,由于乙二胺和乳酸的反应非常活泼,常温下会发生副反应,因此降低反应温度有利于使反应向目标生成物移动。步骤c中,四口烧瓶带有蒸馏装置和搅拌装置;在烘箱中干燥是为了除去未反应的乙二胺杂质。In the step a, since the reaction of ethylenediamine and lactic acid is very active, a side reaction occurs at normal temperature, so lowering the reaction temperature is advantageous for moving the reaction to the target product. In the step c, the four-necked flask was provided with a distillation apparatus and a stirring apparatus; it was dried in an oven to remove unreacted ethylenediamine impurities.
在一些实施例中,:所述催化剂是1~3%的次磷酸钠。In some embodiments, the catalyst is from 1 to 3% sodium hypophosphite.
次氯酸钠是酰胺化催化剂,所述反应是酰胺化反应。Sodium hypochlorite is an amidation catalyst and the reaction is an amidation reaction.
以下通过具体实施例来进一步说明本发明的技术方案。The technical solution of the present invention will be further described below by way of specific examples.
实施例1Example 1
一、按照如下步骤制备基本树脂:1. Prepare the basic resin as follows:
步骤1、按照质量分数比乳酸50%,乙二胺50%称量反应物并置于反应容器中,在-5℃的冰箱里缓慢反应30分钟,待反应物转化为淡黄色油状液体时,将反应物至于60℃的烘箱中干燥,除去未反应的乙二胺,得到N-2-氨基乙基-2-羟基丙酰胺(NHPA)。Step 1. The reactant is weighed according to the mass fraction of 50% lactic acid and 50% ethylenediamine, and placed in a reaction vessel, and slowly reacted in a refrigerator at -5 ° C for 30 minutes. When the reactant is converted into a pale yellow oily liquid, The reaction was dried in an oven at 60 ° C to remove unreacted ethylenediamine to give N-2-aminoethyl-2-hydroxypropanamide (NHPA).
步骤2、以质量分数比丁酮:甲苯=1:1的比例配制有机溶剂,将三元氯醋树脂(由质量分数为13%的醋酸乙烯酯、81%的氯乙烯和6%的马来酸酐合成)溶于所配有机溶剂中制备溶液,其中三元氯醋树脂20%,溶剂80%,Step 2: Prepare an organic solvent with a mass fraction of methyl butanone: toluene = 1:1, and use a ternary chloroacetate resin (from 13% by mass of vinyl acetate, 81% of vinyl chloride, and 6% of Malay). Anhydride synthesis) is prepared by dissolving in an organic solvent to prepare a solution, wherein the ternary chloroacetate resin is 20%, and the solvent is 80%.
步骤3、在步骤2的溶液中加入相当于三元氯醋树脂5%质量分数的NHPA,加入1%催化量的次磷酸钠,在带有蒸馏装置和搅拌装置的四口瓶中反应1h,反应温度105℃,取出反应物与烘箱中干燥,除去溶剂备用。Step 3, adding NHPA equivalent to 5% by mass of ternary chloroacetate resin to the solution of step 2, adding 1% catalytic amount of sodium hypophosphite, and reacting for 1 hour in a four-necked flask with a distillation device and a stirring device. The reaction temperature was 105 ° C, and the reactant was taken out and dried in an oven to remove the solvent.
步骤4、将饱和聚酯溶于所配有机溶剂中制备溶液,其中饱和聚酯40%,有机溶剂为60%。Step 4. Prepare a solution by dissolving the saturated polyester in an organic solvent, wherein the saturated polyester is 40% and the organic solvent is 60%.
步骤5、加入上述改性氯醋树脂和二异氰酸酯,其质量分数比为二异氰酸酯:改性氯醋树脂:饱和聚酯=1:3:6,控制反应温度为80℃,在带有冷凝装置和搅拌装置的四口瓶中反应2h得到饱和聚酯和氯醋树脂的共聚物。Step 5, adding the above modified chloroacetate resin and diisocyanate, the mass fraction ratio is diisocyanate: modified chloroacetate resin: saturated polyester = 1:3:6, controlled reaction temperature is 80 ° C, with a condensing device The reaction was carried out for 2 hours in a four-necked flask with a stirring device to obtain a copolymer of a saturated polyester and a chloroacetic resin.
二、按照以下配方制备热熔胶:2. Prepare hot melt adhesive according to the following formula:
Figure PCTCN2018074581-appb-000003
Figure PCTCN2018074581-appb-000003
Figure PCTCN2018074581-appb-000004
Figure PCTCN2018074581-appb-000004
制备过程如下:The preparation process is as follows:
步骤(一)、按照上述配方将基本树脂和有机溶剂置入带有搅拌装置的容器中,控制温度在35℃,搅拌溶解。Step (1), the basic resin and the organic solvent are placed in a container equipped with a stirring device according to the above formula, and the temperature is controlled at 35 ° C, and stirred to dissolve.
步骤(二)、依次加入松香、改性松香、石蜡、季戊四醇酯,升温至80℃,密封容器,搅拌30分钟。Step (2), adding rosin, modified rosin, paraffin, pentaerythritol ester in turn, heating to 80 ° C, sealing the container, and stirring for 30 minutes.
步骤(三)、终止加热装置,保温30分钟,使其自然冷却至室温即可。Step (3), terminate the heating device, keep it for 30 minutes, and let it cool to room temperature naturally.
实施例2Example 2
一、按照如下步骤制备基本树脂:1. Prepare the basic resin as follows:
步骤1、按照质量分数比乳酸45%,乙二胺55%称量反应物并置于反应容器中,在-5℃的冰箱里缓慢反应30分钟,待反应物转化为淡黄色油状液体时,将反应物至于60℃的烘箱中干燥,除去未反应的乙二胺,得到N-2-氨基乙基-2-羟基丙酰胺(NHPA)。Step 1. The reactant is weighed according to the mass fraction of 45% lactic acid and 55% ethylenediamine, and placed in a reaction vessel, and slowly reacted in a refrigerator at -5 ° C for 30 minutes, when the reactant is converted into a pale yellow oily liquid. The reaction was dried in an oven at 60 ° C to remove unreacted ethylenediamine to give N-2-aminoethyl-2-hydroxypropanamide (NHPA).
步骤2、以质量分数比环己酮:丙酮=1:1配制溶剂,将三元氯醋树脂(由质量分数为15%的醋酸乙烯酯、84%的氯乙烯和1%的马来酸酐合成)溶于所配溶剂中制备溶液,其中三元氯醋树脂30%,溶剂70%,Step 2: Prepare the solvent with a mass fraction of cyclohexanone:acetone=1:1, and synthesize the ternary chloroacetate resin (combined by 15% by mass of vinyl acetate, 84% of vinyl chloride and 1% of maleic anhydride). Preparing a solution in a solvent, wherein the ternary chloroacetate resin is 30% and the solvent is 70%.
步骤3、在步骤2的溶液中加入相当于三元氯醋树脂8%质量分数的NHPA,加入2%催化量的次磷酸钠,在带有蒸馏装置和搅拌装置的四口瓶中反应1h,保持反应温度为105℃,取出反应物与烘箱中干燥,除去溶剂备用。Step 3, adding 8% by mass of NHPA equivalent to ternary chloroacetate resin to the solution of step 2, adding 2% catalytic amount of sodium hypophosphite, and reacting for 1 hour in a four-necked flask with a distillation device and a stirring device. The reaction temperature was maintained at 105 ° C, and the reactant was taken out and dried in an oven to remove the solvent.
步骤4、将饱和聚酯溶于所配溶剂中制备溶液,其中饱和聚酯40%,有机溶剂为60%。Step 4. Prepare a solution by dissolving a saturated polyester in a solvent, wherein the saturated polyester is 40% and the organic solvent is 60%.
步骤5、加入上述改性氯醋树脂和二异氰酸酯,其质量分数比为二异氰酸酯:改性氯醋树脂:饱和聚酯=2:3:5,控制反应温度为60℃,在带有冷凝装置和搅拌装置的四口瓶中反应2h得到饱和聚酯和氯醋树脂的共聚物。Step 5, adding the above modified chloroacetate resin and diisocyanate, the mass fraction ratio is diisocyanate: modified chloroacetate resin: saturated polyester = 2:3:5, controlled reaction temperature is 60 ° C, with a condensing device The reaction was carried out for 2 hours in a four-necked flask with a stirring device to obtain a copolymer of a saturated polyester and a chloroacetic resin.
二、按照以下配方制备热熔胶:2. Prepare hot melt adhesive according to the following formula:
Figure PCTCN2018074581-appb-000005
Figure PCTCN2018074581-appb-000005
Figure PCTCN2018074581-appb-000006
Figure PCTCN2018074581-appb-000006
制备过程如下:The preparation process is as follows:
步骤(一)、按照上述配方将基本树脂和溶剂置入带有搅拌装置的容器中,控制温度在30℃,搅拌溶解。Step (1), the basic resin and the solvent are placed in a container with a stirring device according to the above formula, and the temperature is controlled at 30 ° C, and the mixture is stirred and dissolved.
步骤(二)、依次加入C5石油树脂、微晶蜡、丙酸正十八碳醇酯,升温至60℃,密封容器,搅拌40分钟。Step (2), sequentially adding C5 petroleum resin, microcrystalline wax, n-stearyl alcohol propionate, heating to 60 ° C, sealing the container, and stirring for 40 minutes.
步骤(三)、终止加热装置,保温30分钟,使其自然冷却至室温即可。Step (3), terminate the heating device, keep it for 30 minutes, and let it cool to room temperature naturally.
实施例3Example 3
一、按照如下步骤制备基本树脂:1. Prepare the basic resin as follows:
步骤1、按照质量分数比乳酸45%,乙二胺55%称量反应物并置于反应容器中,在-5℃的冰箱里缓慢反应30分钟,待反应物转化为淡黄色油状液体时,将反应物至于60℃的烘箱中干燥,除去未反应的乙二胺,得到N-2-氨基乙基-2-羟基丙酰胺(NHPA)。Step 1. The reactant is weighed according to the mass fraction of 45% lactic acid and 55% ethylenediamine, and placed in a reaction vessel, and slowly reacted in a refrigerator at -5 ° C for 30 minutes, when the reactant is converted into a pale yellow oily liquid. The reaction was dried in an oven at 60 ° C to remove unreacted ethylenediamine to give N-2-aminoethyl-2-hydroxypropanamide (NHPA).
步骤2、以质量比二甲苯、醋酸乙酯=1:1.5配制溶剂,将三元氯醋树脂(由质量分数为14%的醋酸乙烯酯、83%的氯乙烯和3%的马来酸酐合成)溶于所配溶剂中制备溶液,其中三元氯醋树脂20%,溶剂80%,Step 2: The solvent is prepared by mass ratio of xylene and ethyl acetate = 1:1.5, and the ternary chloroacetate resin (combined by 14% by mass of vinyl acetate, 83% of vinyl chloride and 3% of maleic anhydride) Preparing a solution in a solvent, wherein the ternary chloroacetate resin is 20% and the solvent is 80%.
步骤3、在步骤2的溶液中加入相当于三元氯醋树脂5%质量分数的NHPA,加入3%催化量的次磷酸钠,在带有蒸馏装置和搅拌装置的四口瓶中反应1h,反应温度120℃,取出反应物与烘箱中干燥,除去溶剂备用。Step 3, adding NHPA equivalent to 5% by mass of ternary chloroacetate resin to the solution of step 2, adding 3% catalytic amount of sodium hypophosphite, and reacting for 1 hour in a four-necked flask with a distillation device and a stirring device. The reaction temperature was 120 ° C, and the reactant was taken out and dried in an oven to remove the solvent.
步骤4、将饱和聚酯溶于所配溶剂中制备溶液,其中饱和聚酯50%,有机溶剂为50%。Step 4. Prepare a solution by dissolving the saturated polyester in the solvent, wherein the saturated polyester is 50% and the organic solvent is 50%.
步骤5、加入上述改性三元氯醋树脂和二异氰酸酯,其质量比为二异氰酸酯:改性氯醋树脂:饱和聚酯=1:2:7,控制反应温度为80℃,在带有冷凝装置和搅拌装置的四口瓶中反应2h得到饱和聚酯和氯醋树脂的共聚物。Step 5, adding the above modified ternary chloroacetate resin and diisocyanate, the mass ratio of which is diisocyanate: modified chloroacetate resin: saturated polyester = 1:2:7, controlled reaction temperature is 80 ° C, with condensation The apparatus was reacted in a four-necked bottle of the stirring device for 2 hours to obtain a copolymer of a saturated polyester and a chloroacetic resin.
二、按照以下配方制备热熔胶:2. Prepare hot melt adhesive according to the following formula:
Figure PCTCN2018074581-appb-000007
Figure PCTCN2018074581-appb-000007
Figure PCTCN2018074581-appb-000008
Figure PCTCN2018074581-appb-000008
制备过程如下:The preparation process is as follows:
步骤(一)、按照上述配方将基本树脂和溶剂置入带有搅拌装置的容器中,控制温度在35℃,搅拌溶解。Step (1), the basic resin and the solvent are placed in a container with a stirring device according to the above formula, and the temperature is controlled at 35 ° C, and the mixture is stirred and dissolved.
步骤(二)、依次加入C9石油树、合成蜡、1,1,3-三(2-甲基-4-羟基-5-叔丁苯基)丁烷,升温至60℃,密封容器,搅拌40分钟。Step (2), sequentially adding C9 petroleum tree, synthetic wax, 1,1,3-tris(2-methyl-4-hydroxy-5-tert-butylphenyl)butane, heating to 60 ° C, sealing the container, stirring 40 minutes.
步骤(三)、终止加热装置,保温30分钟,使其自然冷却至室温即可。Step (3), terminate the heating device, keep it for 30 minutes, and let it cool to room temperature naturally.
实施例4Example 4
一、按照如下步骤制备基本树脂:1. Prepare the basic resin as follows:
步骤1、按照质量分数比乳酸50%,乙二胺50%称量反应物并置于反应容器中,在-5℃的冰箱里缓慢反应30分钟,待反应物转化为淡黄色油状液体时,将反应物至于60℃的烘箱中干燥,除去未反应的乙二胺,得到N-2-氨基乙基-2-羟基丙酰胺(NHPA)。Step 1. The reactant is weighed according to the mass fraction of 50% lactic acid and 50% ethylenediamine, and placed in a reaction vessel, and slowly reacted in a refrigerator at -5 ° C for 30 minutes. When the reactant is converted into a pale yellow oily liquid, The reaction was dried in an oven at 60 ° C to remove unreacted ethylenediamine to give N-2-aminoethyl-2-hydroxypropanamide (NHPA).
步骤2、以质量比醋酸丁酯、醋酸异丙酯=1:2配制溶剂,将三元氯醋树脂(由质量分数为14%的醋酸乙烯酯、82%的氯乙烯和4%的马来酸酐合成)溶于所配溶剂中制备溶液,其中三元氯醋树脂25%,溶剂75%。Step 2. Prepare the solvent by mass ratio of butyl acetate and isopropyl acetate = 1:2, and ternary chloroacetate resin (from 14% by mass of vinyl acetate, 82% of vinyl chloride and 4% of Malay) Anhydride synthesis) is prepared by dissolving in a solvent to prepare a solution, wherein the ternary chloroacetate resin is 25% and the solvent is 75%.
步骤3、在步骤2的溶液中加入相当于三元氯醋树脂5%质量分数的NHPA,加入2%催化量的次磷酸钠,在带有蒸馏装置和搅拌装置的四口瓶中反应1h,反应温度115℃,取出反应物与烘箱中干燥,除去溶剂备用。Step 3, adding NHPA equivalent to 5% by mass of ternary chloroacetate resin to the solution of step 2, adding 2% catalytic amount of sodium hypophosphite, and reacting for 1 hour in a four-necked flask with a distillation device and a stirring device. The reaction temperature was 115 ° C, and the reactant was taken out and dried in an oven to remove the solvent.
步骤4、将饱和聚酯溶于所配溶剂中制备溶液,其中饱和聚酯45%,有机溶剂为55%。Step 4. Prepare a solution by dissolving the saturated polyester in the solvent, wherein the saturated polyester is 45% and the organic solvent is 55%.
步骤5、加入上述改性氯醋树脂和二异氰酸酯,其质量比为二异氰酸酯:改性氯醋树脂:饱和聚酯=1:3:6,控制反应温度为80℃,在带有冷凝装置和搅拌装置的四口瓶中反应2h得到饱和聚酯和氯醋树脂的共聚物。Step 5, adding the above modified chloroacetate resin and diisocyanate, the mass ratio of which is diisocyanate: modified chloroacetate resin: saturated polyester = 1:3:6, controlled reaction temperature is 80 ° C, with a condensation device and The reaction was carried out for 2 hours in a four-necked bottle of a stirring device to obtain a copolymer of a saturated polyester and a chloroacetic resin.
二、按照以下配方制备热熔胶:2. Prepare hot melt adhesive according to the following formula:
Figure PCTCN2018074581-appb-000009
Figure PCTCN2018074581-appb-000009
Figure PCTCN2018074581-appb-000010
Figure PCTCN2018074581-appb-000010
制备过程如下:The preparation process is as follows:
步骤(一)、按照上述配方将基本树脂和溶剂置入带有搅拌装置的容器中,控制温度在30℃,搅拌溶解。Step (1), the basic resin and the solvent are placed in a container with a stirring device according to the above formula, and the temperature is controlled at 30 ° C, and the mixture is stirred and dissolved.
步骤(二)、依次加入萜烯树脂、佛托蜡、三(壬基苯基)亚磷酸酯,升温至60℃,密封容器,搅拌30分钟。Step (2), sequentially adding terpene resin, fossa wax, and tris(nonylphenyl) phosphite, heating to 60 ° C, sealing the container, and stirring for 30 minutes.
步骤(三)、终止加热装置,保温30分钟,使其自然冷却至室温即可。Step (3), terminate the heating device, keep it for 30 minutes, and let it cool to room temperature naturally.
性能测试实验数据Performance test experimental data
1、热熔胶热力学性能测试1, hot melt adhesive thermodynamic performance test
测试方法:使用DSC和TG对热熔胶进行表征,结果如表1。Test method: The hot melt adhesive was characterized by DSC and TG, and the results are shown in Table 1.
表1 热熔胶热力学性能测试结果Table 1 Thermowell performance test results of hot melt adhesive
实施例Example 玻璃化温度(℃)Glass transition temperature (°C) 软化温度(℃)Softening temperature (°C) 分解温度(℃)Decomposition temperature (°C)
对比例0 Comparative ratio 0 15.515.5 80.280.2 334.0334.0
实施例1Example 1 38.338.3 122.6122.6 376.3376.3
实施例2Example 2 40.540.5 125.4125.4 384.5384.5
实施例3Example 3 39.639.6 120.7120.7 379.6379.6
实施例4Example 4 37.237.2 118.7118.7 374.2374.2
其中对比例0为未改性的饱和树脂,从数据上看,未改性饱和树脂的玻璃化温度偏低,所制备的转印膜性能不稳定,在温度较高的工作环境中可能提前软化,影响工艺。从实施例1~4的数据可以看出,经过上述改性的树脂,玻璃化温度提高至37~40℃,提高了转印膜稳定性,同时软化温度提高至118~122℃,此温度符合模外转印的工作温度,另外分解温度从334℃提升至374~384℃,提高了热熔胶的耐热性。The comparative example 0 is an unmodified saturated resin. From the data point of view, the glass transition temperature of the unmodified saturated resin is low, the performance of the prepared transfer film is unstable, and it may be softened in advance in a high temperature working environment. , affecting the process. It can be seen from the data of Examples 1 to 4 that, after the above modified resin, the glass transition temperature is increased to 37 to 40 ° C, the stability of the transfer film is improved, and the softening temperature is increased to 118 to 122 ° C, which is consistent with this temperature. The operating temperature of the external transfer, and the decomposition temperature is increased from 334 ° C to 374 ~ 384 ° C, improving the heat resistance of the hot melt adhesive.
2、剥离强度测试2, peel strength test
测试方法:根据180°剥离强度测试标准ISO 8510-2-2006对热熔胶进行测试,结果如表。Test method: The hot melt adhesive was tested according to the 180° peel strength test standard ISO 8510-2-2006, and the results are shown in the table.
表2 热熔胶玻璃强度测试结果Table 2 Hot melt adhesive glass strength test results
Figure PCTCN2018074581-appb-000011
Figure PCTCN2018074581-appb-000011
(V0代表对比例0,V1代表实施例1,V2代表实施例2,V3代表实施例3,V4代表实施例4。)(V0 represents Comparative Example 0, V1 represents Embodiment 1, V2 represents Embodiment 2, V3 represents Embodiment 3, and V4 represents Embodiment 4.)
其中对比例0为未改性饱和聚酯,由剥离强度实验结果看,经上述改性过的饱和聚酯的剥离强度从1.56KN/m提升至2.55~3.03KN/m,热熔胶的粘接质量得到提升,提高了转印膜中图层附着在被装饰物体表面的附着力,优化了装饰质量。The comparative example 0 is an unmodified saturated polyester. From the peeling strength test results, the peel strength of the modified saturated polyester is increased from 1.56 KN/m to 2.55 to 3.03 KN/m, and the hot melt adhesive is adhered. The quality of the joint is improved, the adhesion of the layer in the transfer film to the surface of the object to be decorated is improved, and the quality of the decoration is optimized.
3、热熔胶材料适应性测试3, hot melt adhesive material adaptability test
测试方法:将热熔胶粘接在不同材料表面,包括PET塑料、ABS塑料、PC塑料、玻璃片、铝片、铜片。然后按照180°剥离强度测试标准ISO 8510-2-2006进行测试。结果如表3。Test method: Bonding hot melt adhesive to different materials, including PET plastic, ABS plastic, PC plastic, glass, aluminum, copper. The test was then carried out in accordance with the 180° peel strength test standard ISO 8510-2-2006. The results are shown in Table 3.
表3 热熔胶材料适应性测试结果Table 3 Hot melt adhesive material adaptability test results
强度(KN/m)Strength (KN/m) PET塑料PET plastic ABS塑料ABS plastic PC塑料PC plastic 玻璃片Glass piece 铝片Aluminum sheet 铜片Copper sheet
对比例Comparative example 2.012.01 1.731.73 1.651.65 1.221.22 1.561.56 1.021.02
实施例1Example 1 2.682.68 1.891.89 2.742.74 1.761.76 2.552.55 2.282.28
实施例2Example 2 2.902.90 2.342.34 2.902.90 1.981.98 3.033.03 2.342.34
实施例3Example 3 2.852.85 2.672.67 2.342.34 2.312.31 2.862.86 2.512.51
实施例4Example 4 2.792.79 2.562.56 2.122.12 2.242.24 2.732.73 2.452.45
其中对比例0为未改性饱和聚酯,OMD转印技术对热熔胶的要求之一是180°剥离强度大于2.0KN/m,通过表中数据可以看出,未改性的饱和聚酯只有对PET的剥离强度大于2.0KN/m,而样品实施例1~4对材料的剥离强度到达标准的数量都有所增加。例如实施例1对PET、PC、铝、铜的剥离强度均达到标准。因此,经过改性的聚酯对材料的适应性有所增加,扩大了OMD技术的装饰范围。The comparative example 0 is unmodified saturated polyester. One of the requirements of OMD transfer technology for hot melt adhesive is 180° peel strength greater than 2.0KN/m. It can be seen from the data in the table that unmodified saturated polyester Only the peel strength to PET was greater than 2.0 KN/m, and sample examples 1-4 increased the peel strength of the material to the standard. For example, the peel strength of PET, PC, aluminum, and copper in Example 1 reached the standard. Therefore, the modified polyester has increased the adaptability of the material, expanding the decorative range of the OMD technology.
4、热熔胶的耐酸碱及耐候性测试4. Acid and alkali resistance and weather resistance test of hot melt adhesive
测试方法:将热熔胶粘接铝片上制备出粘接试件,将粘接试件分别置于室外、人工汗液、盐酸溶液(0.1mol/L)、氢氧化钠溶液(0.1mol/L)中,分别在第一天、第三天、第七天测试其剥离强度。测试结果见表4。Test method: The hot-melt adhesive is bonded to the aluminum sheet to prepare the bonded test piece, and the bonded test piece is separately placed in the outdoor, artificial sweat, hydrochloric acid solution (0.1 mol/L), sodium hydroxide solution (0.1 mol/L). In the middle, the peel strength was tested on the first day, the third day, and the seventh day, respectively. The test results are shown in Table 4.
表4 热熔胶耐酸碱即耐候性测试结果Table 4 Hot melt adhesive acid and alkali resistance, weather resistance test results
Figure PCTCN2018074581-appb-000012
Figure PCTCN2018074581-appb-000012
从表中可以看出,对比例经测试液浸泡后剥离强度有较大损失,这是因为饱和聚酯的主链中有大量酯键,酯键在酸碱环境及紫外光下容易水解、断裂,造成聚酯热熔胶耐酸碱性差的现象。经上述改性的聚酯在测试液中表现出较好的抵抗力,例如样品实施例1在HCl浸泡一天、三天、七天后的剥离强度分别为2.43、2.23、1.67KN/m,其剥离强度损失了0.76KN/m,而样品对比例在七天后损失了1.23KN/m。这由于改性后的聚酯一种由氯醋树脂和饱和聚酯形成的互穿网络结构,氯醋树脂有很好的耐酸碱性,其分子量对酯键具有缠绕包裹的作用,对其起到了保护作用,因此提高了其耐酸碱及耐候性。热熔胶耐酸碱及耐候性的提高,优化了装饰涂层的耐候性,延长了其使用寿命。It can be seen from the table that the comparative example has a large loss of peel strength after soaking in the test liquid, because the saturated polyester has a large number of ester bonds in its main chain, and the ester bond is easily hydrolyzed and broken in an acid-base environment and ultraviolet light. , causing the phenomenon that the polyester hot melt adhesive is poor in acid and alkali resistance. The polyester modified as described above exhibits good resistance in the test liquid. For example, the peel strengths of the sample of Example 1 after immersion in HCl for one day, three days, and seven days are respectively 2.43, 2.23, and 1.67 KN/m, and the peeling is performed. The strength loss was 0.76 KN/m, while the sample comparative loss lost 1.23 KN/m after seven days. This is due to the modified interpenetrating network structure formed by chloroacetic resin and saturated polyester. The chloroacetic resin has good acid and alkali resistance, and its molecular weight has a wrap-around effect on the ester bond. It has a protective effect, thus improving its acid and alkali resistance and weather resistance. The hot-melt adhesive has improved acid and alkali resistance and weather resistance, which optimizes the weather resistance of the decorative coating and prolongs its service life.
以上内容仅为本发明的较佳实施例,对于本领域的普通技术人员,依据本发明的思想,在具体实施方式及应用范围上均会有改变之处,本说明书内容不 应理解为对本发明的限制,因此本发明的保护范围以权利要求界定的范围为准。The above content is only a preferred embodiment of the present invention, and those skilled in the art will have a change in the specific embodiment and application scope according to the idea of the present invention. The content of the present specification should not be construed as the present invention. The scope of the invention is therefore defined by the scope of the claims.

Claims (10)

  1. 一种用于膜外转印技术的的热熔胶,其特征在于,包括如下质量分数的物质:A hot melt adhesive for use in an off-film transfer technique, comprising: a mass fraction of:
    Figure PCTCN2018074581-appb-100001
    Figure PCTCN2018074581-appb-100001
    其中,所述基本树脂由改性氯醋树脂和饱和聚酯在二异氰酸酯的作用下合成。Wherein, the basic resin is synthesized by a modified chloroacetate resin and a saturated polyester under the action of a diisocyanate.
  2. 如权利要求1所述的热熔胶,其特征在于,合成所述基本树脂的物质为二异氰酸酯、改性氯醋树脂和饱和聚酯,三者的质量分数比为1~2:2~3:5~7。The hot melt adhesive according to claim 1, wherein the substance for synthesizing the base resin is diisocyanate, modified chloroacetate resin and saturated polyester, and the mass fraction ratio of the three is 1 to 2:2 to 3 : 5 to 7.
  3. 如权利要求2所述的热熔胶,其特征在于:所述改性氯醋树脂由N-2-氨基乙基-2-羟基丙酰胺和三元氯醋树脂反应所得;The hot melt adhesive according to claim 2, wherein the modified chloroacetate resin is obtained by reacting N-2-aminoethyl-2-hydroxypropionamide with a ternary chloroacetate resin;
    所述N-2-氨基乙基-2-羟基丙酰胺由如下质量分数比的物质组成,The N-2-aminoethyl-2-hydroxypropionamide is composed of the following mass fraction ratio substances.
    乳酸        45~50%;Lactic acid 45 to 50%;
    乙二胺      50~55%。Ethylenediamine 50 to 55%.
  4. 如权利要求2所述的热熔胶,其特征在于:所述二异氰酸酯是甲苯二异氰酸酯、异佛尔酮二异氰酸酯、二苯基甲烷二异氰酸酯、二环己基甲烷二异氰酸酯、六亚甲基二异氰酸酯、赖氨酸二异氰酸酯中的一种或多种。The hot melt adhesive according to claim 2, wherein the diisocyanate is toluene diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate, dicyclohexylmethane diisocyanate, hexamethylene diene. One or more of isocyanate and lysine diisocyanate.
  5. 如权利要求3所述的热熔胶的基本树脂,其特征在于:所述三元氯醋树脂是醋酸乙烯酯、氯乙烯和马来酸酐的三元聚合物;三者的质量分数是The base resin of the hot melt adhesive according to claim 3, wherein the ternary chloroacetate resin is a terpolymer of vinyl acetate, vinyl chloride and maleic anhydride; the mass fraction of the three is
    醋酸乙烯酯  13~15%;Vinyl acetate 13-15%;
    氯乙烯      81~84%Vinyl chloride 81~84%
    马来酸酐    1~6%。Maleic anhydride 1 to 6%.
  6. 如权利要求3所述的热熔胶的基本树脂,其特征在于:所述饱和聚酯是二元醇和二元酸经脱水缩合反应得到的高分子聚合物,所述饱和聚酯的分子量为10000~50000;所述二元醇是乙二醇、丙二醇和丁二醇中的一种或多种;所述二元酸是对苯二甲酸、间苯二甲酸和邻苯二甲酸中的一种或多种。The base resin of a hot melt adhesive according to claim 3, wherein the saturated polyester is a high molecular polymer obtained by dehydration condensation reaction of a dihydric alcohol and a dibasic acid, and the molecular weight of the saturated polyester is 10,000. ~50000; the diol is one or more of ethylene glycol, propylene glycol and butylene glycol; the dibasic acid is one of terephthalic acid, isophthalic acid and phthalic acid Or a variety.
  7. 制备如权利要求1所述的热熔胶的方法,其特征在于,包括:A method of preparing a hot melt adhesive according to claim 1, comprising:
    步骤(一)、将基本树脂和有机溶剂置入带有搅拌装置的容器中,控制温度在30~35℃,搅拌溶解;Step (1), placing the basic resin and the organic solvent in a container with a stirring device, controlling the temperature at 30 to 35 ° C, stirring and dissolving;
    步骤(二)、依次加入增粘剂、黏度调节剂和抗氧剂,升温至60~80℃,密封容器,搅拌30~40分钟;Step (2), sequentially adding a tackifier, a viscosity modifier and an antioxidant, heating to 60-80 ° C, sealing the container, stirring for 30 to 40 minutes;
    步骤(三)、停止加热,保温30分钟,使其自然冷却至室温即可。Step (3), stop heating, keep warm for 30 minutes, let it cool naturally to room temperature.
  8. 如权利要求7的热熔胶的制备方法,其特征在于,所述基本树脂的制备方法包括:A method of preparing a hot melt adhesive according to claim 7, wherein the method for preparing the base resin comprises:
    步骤A、将饱和聚酯溶于有机溶剂中,其中饱和聚酯的质量分数为40~50%,有机溶剂的质量分数为50~60%;Step A, the saturated polyester is dissolved in an organic solvent, wherein the mass fraction of the saturated polyester is 40 to 50%, and the mass fraction of the organic solvent is 50 to 60%;
    步骤B、加入改性氯醋树脂和二异氰酸酯,在四口瓶中保持反应温度为60~80℃,反应2h即可。Step B, adding modified chloroacetate resin and diisocyanate, maintaining the reaction temperature in a four-necked bottle at 60-80 ° C, and reacting for 2 hours.
  9. 如权利要求8的热熔胶的制备方法,其特征在于,所述改性氯醋树脂的制备方法包括:The method for preparing a hot melt adhesive according to claim 8, wherein the method for preparing the modified chloroacetate resin comprises:
    步骤a、称取适量乳酸和乙二胺置于反应容器中,在-5℃的环境下缓慢反应30分钟,待反应物转化为淡黄色油状液体时,将反应物置于60℃的烘箱中干燥,得到N-2-氨基乙基-2-羟基丙酰胺;Step a, weigh the appropriate amount of lactic acid and ethylenediamine in a reaction vessel, and slowly react for 30 minutes at -5 ° C. When the reactants are converted into a light yellow oily liquid, the reaction is placed in an oven at 60 ° C to dry. , obtaining N-2-aminoethyl-2-hydroxypropionamide;
    步骤b、将三元氯醋树脂溶于有机溶剂中,其中三元氯醋树脂的质量分数为20~30%,有机溶剂的质量分数为70~80%;Step b, the ternary chloroacetate resin is dissolved in an organic solvent, wherein the mass fraction of the ternary chloroacetate resin is 20-30%, and the mass fraction of the organic solvent is 70-80%;
    步骤c、在步骤b的溶液中加入相当于三元氯醋树脂5%~8%质量分数的N-2-氨基乙基-2-羟基丙酰胺,加入催化量,在四口瓶中反应1h,反应温度105~120℃,取出反应物于烘箱中干燥,除去有机溶剂备用。Step c, adding N-aminoethyl-2-hydroxypropionamide corresponding to 5% to 8% by mass of the ternary chloroacetate resin in the solution of step b, adding a catalytic amount, and reacting for 1 hour in a four-necked bottle The reaction temperature is 105 to 120 ° C, and the reactant is taken out and dried in an oven to remove the organic solvent for use.
  10. 如权利要求9的热熔胶的制备方法,其特征在于:所述催化剂是1~3%的次磷酸钠。A method of producing a hot melt adhesive according to claim 9, wherein said catalyst is from 1 to 3% of sodium hypophosphite.
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