WO2019220806A1 - ポリ乳酸系ホットメルト接着剤の製造方法 - Google Patents
ポリ乳酸系ホットメルト接着剤の製造方法 Download PDFInfo
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- WO2019220806A1 WO2019220806A1 PCT/JP2019/015128 JP2019015128W WO2019220806A1 WO 2019220806 A1 WO2019220806 A1 WO 2019220806A1 JP 2019015128 W JP2019015128 W JP 2019015128W WO 2019220806 A1 WO2019220806 A1 WO 2019220806A1
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J167/00—Adhesives based on polyesters obtained by reactions forming a carboxylic ester link in the main chain; Adhesives based on derivatives of such polymers
- C09J167/04—Polyesters derived from hydroxycarboxylic acids, e.g. lactones
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
- C08K5/0016—Plasticisers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/06—Ethers; Acetals; Ketals; Ortho-esters
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
- C08K5/092—Polycarboxylic acids
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/13—Phenols; Phenolates
- C08K5/134—Phenols containing ester groups
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/36—Sulfur-, selenium-, or tellurium-containing compounds
- C08K5/39—Thiocarbamic acids; Derivatives thereof, e.g. dithiocarbamates
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/49—Phosphorus-containing compounds
- C08K5/51—Phosphorus bound to oxygen
- C08K5/52—Phosphorus bound to oxygen only
- C08K5/524—Esters of phosphorous acids, e.g. of H3PO3
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J11/00—Features of adhesives not provided for in group C09J9/00, e.g. additives
- C09J11/02—Non-macromolecular additives
- C09J11/06—Non-macromolecular additives organic
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J7/00—Adhesives in the form of films or foils
- C09J7/30—Adhesives in the form of films or foils characterised by the adhesive composition
- C09J7/35—Heat-activated
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K15/00—Anti-oxidant compositions; Compositions inhibiting chemical change
- C09K15/04—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds
- C09K15/06—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds containing oxygen
- C09K15/08—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds containing oxygen containing a phenol or quinone moiety
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K15/00—Anti-oxidant compositions; Compositions inhibiting chemical change
- C09K15/04—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds
- C09K15/26—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds containing nitrogen and sulfur
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K15/00—Anti-oxidant compositions; Compositions inhibiting chemical change
- C09K15/04—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds
- C09K15/32—Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds containing two or more of boron, silicon, phosphorus, selenium, tellurium or a metal
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J2467/00—Presence of polyester
Definitions
- the present invention relates to a method for producing a polylactic acid-based hot melt adhesive, and more particularly to a production method including a step of heating polylactic acid in the presence of a dithiocarbamate, a phosphite, and a hindered phenol.
- Hot melt adhesives are melted by heating and applied to objects, then cooled and solidified to adhere objects, and are widely used for packaging, bookbinding, woodworking, etc. .
- Hot melt adhesives generally contain additives such as base polymers, tackifying resins, plasticizers and stabilizers.
- base polymer for example, a thermoplastic resin such as ethylene-vinyl acetate copolymer, a rosin ester, a petroleum resin, or the like as a tackifier resin, a paraffin wax as a plasticizer, and BHT as a heat stabilizer are used.
- polylactic acid Various products containing a copolymer
- a hot melt composition containing a lactic acid homopolymer or lactic acid copolymer and a tackifying resin such as rosin Patent Document 1
- a hot melt adhesive / adhesive containing a lactic acid-based adhesive resin Patent Document 2
- a hot melt adhesive is known in which either or both of a thermoplastic resin and a tackifier resin includes polylactic acid or a lactic acid copolymer resin derived from lactic acid and another hydroxycarboxylic acid (Patent Document 3).
- Patent Document 1 has an initial viscosity of 4,125 cps at 177 ° C. and is 175 cps after 72 hours storage (Patent Document 1, Table 2).
- Patent Document 2 describes a change in viscosity of a hot-melt adhesive at 150 ° C., for example, 15,000 cps after 1 hour of preparation is now 8,500 cps after 4 hours.
- the hot melt adhesive described in Patent Document 3 has a viscosity change within 190% after being left at 190 ° C. for 24 hours, and is said to be thermally stable.
- dehydration condensation polymerization of lactic acid including a resin having a weight average molecular weight of more than 10,000 and a tackifying resin having a weight average molecular weight of less than 10,000, it is not easy to prepare both. It takes time (Patent Document 3, Example 1).
- hot melt adhesives based on polylactic acid have not been put into practical use.
- an object of the present invention is to provide a production method capable of easily preparing a polylactic acid-based hot melt adhesive having thermal stability that can withstand practical use.
- the present inventors have succeeded in imparting tackiness to the polylactic acid by a controlled method, thereby completing the present invention. That is, the present invention is as follows.
- a method for producing a polylactic acid-based hot melt adhesive (1) At a temperature of 180 to 280 ° C., 100 parts by weight of a first polylactic acid having a relative viscosity of 2.5 to 4.0 measured according to ASTM D5225 is added to a mixture of dithiocarbamate and a plasticizer. Adding and melt-mixing, and then adding a phosphite and a hindered phenol to prepare a first polylactic acid composition, wherein the plasticizer is 10 to 100 parts per 100 parts by weight.
- the viscosity of the composition measured at 180-220 ° C. is 70-700 mPa ⁇ s
- a second polylactic acid having a relative viscosity of 2.5 to 4.0 measured according to ASTM D5225 at a temperature of 180 to 280 ° C. is added to the first polylactic acid composition. / Mixing the second polylactic acid in an amount of 2/8 to 8/2 by weight, Including methods.
- the method of the present invention uses a combination of dithiocarbamate, phosphite, and hindered phenol, so that polylactic acid-based hot water can be obtained in a simpler and shorter time than the conventional reaction in which a lactic acid monomer is polymerized to obtain a tackifying resin.
- a melt adhesive can be obtained.
- the obtained adhesive can achieve an adhesive strength equal to or higher than that of an ethylene vinyl acetate (EVA) -based hot melt adhesive that is currently widely used.
- EVA ethylene vinyl acetate
- FIG. 1 is a photograph showing how the adhesive strength is examined in a heat resistant adhesive test, a cold resistant adhesive test, and an accelerated aging test in Examples.
- adheresive means both an adhesive and an adhesive.
- Adhesives differ from adhesives in that they are temporarily attached under pressure and can be peeled off at the interface with the object, but they contain more plasticizer than adhesives, etc. Although there is a difference, it can be obtained by the same method as the adhesive.
- a phosphite and a hindered phenol are added to the first polylactic acid in a predetermined viscosity range. It is a process of preparing a composition. It is known that the molecular weight of polylactic acid in the molten state is reduced mainly by thermal decomposition. The mechanism is diverse, and it is known that recombination of decomposition products occurs in addition to decomposition mechanisms such as random decomposition reaction and intramolecular transesterification reaction, and is very complicated. Phosphites and hindered phenols are known as stabilizers that suppress the degradation of polylactic acid.
- Dithiocarbamate is a rubber crosslinking agent and is used as a stabilizer for rubber-based hot melt adhesives. Surprisingly, however, it was found that dithiocarbamate acts as a degrading agent for polylactic acid, but does not inhibit the stabilizing action of phosphite esters and hindered phenols on polylactic acid. By adding these combinations to polylactic acid, we succeeded in reducing the molecular weight of the target polylactic acid. The phosphite and hindered phenol may be added from the beginning, but it is preferable to add them after the decomposition reaction of the first polylactic acid has proceeded to some extent.
- Dithiocarbamate is represented by the following general formula.
- R 1 and R 2 are each independently a C1-6 alkyl group or a C6-12 aromatic group
- M is a Group 1, 12, or 16 metal atom
- n is an integer of 1 to 3.
- alkyl group include a methyl group, an ethyl group, and a butyl group, and may have a branch.
- aromatic group include a phenyl group, a methylphenyl group, and an ethylphenyl group.
- R 1 and R 2 are independently selected from methyl, ethyl, butyl and ethylphenyl groups, and M is selected from sodium, copper, iron, zinc, selenium and tellurium. Most preferably, R 1 and R 2 are n-butyl, M is zinc and n is 2.
- Dithiocarbamate can control the degree of decomposition or molecular weight of the first polylactic acid depending on the amount of dithiocarbamate. It is used in an amount of 0.02 to 0.3 parts by weight, preferably 0.04 to 0.2 parts by weight, based on 100 parts by weight of the first polylactic acid. If the amount of dithiocarbamate is less than the lower limit, the effect of promoting the decrease in molecular weight of the first polylactic acid is not sufficient, and if the amount exceeds the upper limit, control of the molecular weight becomes difficult.
- the first polylactic acid may be either an amorphous polymer, a semicrystalline with a melting point of 130 to 180 ° C., or a highly crystalline polymer, depending on the content and arrangement of D-lactic acid and L-lactic acid. Good. From the viewpoint of adhesiveness, an amorphous polymer is preferable, and from the viewpoint of low blocking of the hot melt adhesive, a crystalline polymer is preferable, and these can be used by appropriately mixing them.
- the polylactic acid may be produced by either a method obtained by dehydration condensation polymerization of a lactic acid monomer or a method of preparing a ring lactide of a lactic acid dimer and ring-opening polymerization.
- polylactic acid produced by the latter method is used.
- the first polylactic acid may be a copolymer of lactic acid and another monomer, or may be a mixture of polylactic acid and the copolymer.
- examples of other monomers include glycolic acid, hydroxycarboxylic acids such as hydroxybutyric acid, and lactones such as ⁇ -caprolactone.
- the first polylactic acid has a relative viscosity of 2.5 to 4.1 measured according to ASTM D5225.
- ASTM D5225 is a method of measuring the viscosity of a solution obtained by dissolving a polymer in a solvent using a differential viscometer.
- the viscosity at 30 ° C. of a solution in which chloroform is used as a solvent and the concentration of polylactic acid is 1.0 g / 100 mL.
- polylactic acid having a relative viscosity of 3.2 to 4.1 is used.
- plasticizer may be used as long as it is used for polylactic acid.
- polyhydric alcohols such as propylene glycol and polyglycerol, glycerol esters, glycerol ester monoglycerides, polyglycerol fatty acid esters and the like
- Polyhydric carboxylic acid esters such as monohydric alcohol esters and dialkyl adipates, phthalic acid esters, epoxidized vegetable oils and the like can be used.
- glycerin triacetate, butylbenzyl phthalate, epoxidized soybean oil, tall oil, adipic acid ester, polyglycerin fatty acid ester, and mixtures thereof are preferred.
- the plasticizer is used in an amount of 10 to 100 parts by weight, preferably 20 to 80 parts by weight, based on 100 parts by weight of the first polylactic acid.
- the amount of plasticizer is 20 to 50% of the total weight of the first polylactic acid, second polylactic acid and plasticizer %, More preferably 20 to 40% by weight.
- a hot melt adhesive it is preferably 5 to 20% by weight, more preferably 8 to 15% by weight of the total weight.
- the heating temperature is 180 to 280 ° C, preferably 200 to 250 ° C, more preferably 210 to 220 ° C.
- the temperature is less than the lower limit value, the molecular weight decreases slowly, and when the temperature exceeds the upper limit value, the decrease rate is high and control becomes difficult.
- adding the first polylactic acid it is preferable to add it in a plurality of times, for example, 2 to 4 times, so that the temperature does not deviate from the above range.
- Examples of the phosphite include monophosphite, diphosphite, and pentaerythritol phosphite represented by the following formula.
- the monophosphite ester is represented by the following formula.
- R 3 to R 5 are each independently a C6-16 alkyl group or a C6-18 aromatic group, and two adjacent groups are bonded by a C1-3 alkylene group to form a cyclic structure. It may be formed.
- R 3 to R 5 are each independently a C8-10 alkyl group, phenyl group, di-t-butylphenyl group, or nonylphenyl group, more preferably 2 of R 3 to R 5.
- One is a di-t-butylphenyl group, which are bonded with a methylene group to form a cyclic structure.
- the diphosphite ester is represented by the following formula.
- R 6 to R 9 are each independently a C10-18 alkyl group, and R 10 is a C2-4 alkyleneoxyalkylene group or a 4,4′-isopropylidene-diphenylene group.
- Pentaerythritol phosphite is represented by the following formula.
- R 11 and R 12 are each independently a C16-20 alkyl group or a C6-20 aromatic group.
- monophosphite is used, more preferably 2,2-methylenebis (4,6-di-t-butylphenyl) 2-ethylhexyl phosphite or 2-ethylhexyl diphenyl phosphite.
- the phosphite is used in an amount of 1 to 10 parts by weight, preferably 2 to 6 parts by weight, based on 100 parts by weight of the first polylactic acid.
- the hindered phenol is a phenol in which at least one group adjacent to the phenolic hydroxyl group is a sterically bulky substituent such as a tert-butyl group.
- a tert-butyl group For example, 1,1,3-tris (2-methyl -4-hydroxy-5-tert-butylphenyl) butane, 4,4'-butylidenebis (6-tert-butyl-3-methylphenol), 3- (1,1-dimethylethyl) -4-hydroxy-5 Methylbenzenepropionic acid 2,4,8,10-tetraoxaspiro [5.5] undecane-3,9-diylbis (2,2-dimethyl-2,1-ethanediyl) ester, 2,6-di-tert- Butylphenol, 1,3,5-tris (di-tert-butyl-4-hydroxyphenylmethyl) -2,4,6-trimethylbenzene, 1,3 5-trimethyl-2,4,
- a phenolic hydroxyl group having a tert-butyl group at the ortho position and a methyl group at the meta position such as 1,1,3-tris (2-methyl-4-hydroxy-5-tert-butylphenyl) butane, 4,4′-butylidenebis (6-tert-butyl-3-methylphenol) is used, more preferably 1,1,3-tris (2-methyl-4-hydroxy-5-tert-butylphenyl) butane. used.
- the hindered phenol is used in an amount of 1 to 10 parts by weight, preferably 2 to 6 parts by weight, based on 100 parts by weight of the first polylactic acid.
- a rosin ester, a tackifying resin such as a terpene phenol resin, or a wax such as carnauba wax, polyester wax, or ester amide wax may be added.
- the addition amount is about 40% by weight or less with respect to the total of 100% by weight of the first polylactic acid, the plasticizer, and the second polylactic acid.
- the viscosity of the reaction mixture is set at 180-220 ° C. using a viscometer, such as a Brookfield rotational viscometer, 70-700 mPa ⁇ s.
- the first polylactic acid composition is obtained by stirring while maintaining the temperature until preferably 90 to 550 mPa ⁇ s.
- the time required for step (1) may vary depending on the reaction vessel, the amount charged, etc., but is about 40 minutes to about 80 minutes. This is significantly shorter than the method of polymerizing tackifying resins.
- Step (2) is a step of obtaining a hot melt adhesive by mixing the second polylactic acid with the first polylactic acid composition obtained in the step (1).
- Step (2) may be performed as a continuous step of step (1), or may be performed after storing the first polylactic acid composition for a certain time after step (1).
- steps (1) and (2) are performed continuously.
- the second polylactic acid may be the same as or different from the first polylactic acid.
- the same polylactic acid as the first polylactic acid is used.
- Mixing ratio of the first and second polylactic acid that is, an amount such that the weight ratio (first polylactic acid / second polylactic acid) is 2/8 to 8/2, preferably 3/7 to 7/3 It is.
- the temperature in the second step is set to 180 to 280 ° C., preferably 200 to 250 ° C., more preferably 210 to 220 ° C.
- the time required for the step (2) may vary depending on the reaction vessel, the charged amount, etc., but is 40 to 90 minutes.
- the viscosity of the resulting hot melt adhesive composition is 1,000 to 10,000 mPa ⁇ s, preferably 1,000 to 5,000 mPa ⁇ s, using a Brookfield rotational viscometer set at 180 ° C. .
- the viscosity is a viscosity measured after standing at room temperature for 24 hours after completion of the production process and further re-dissolving.
- the hot melt adhesive is poured in a molten state onto a silicone resin mold or a cooled steel belt, cooled, and solidified into a pellet, strip, drop, block, stick, flake, powder, film or the like.
- a moisture-proof aluminum laminate bag or a sealed container In order to prevent moisture absorption, it is preferably provided in a moisture-proof aluminum laminate bag or a sealed container.
- Hot melt adhesive is re-melted at 150-200 ° C, and with an applicator, for corrugated cardboard box making, small paper box box making, bag making cylinder pasting, bookbinding backing, woodworking edge pasting, woodworking plywood core It is applied and bonded to parts, parts, etc., and is used for aluminum cap seals, cut tapes, thermal labels, etc. by a coater.
- a hot melt adhesive was prepared by the following method. (1) A 500 ml separable flask equipped with a stirrer was charged with 16 g of epoxidized soybean oil, 28 g of adipic acid ester, and 0.28 g of zinc di-n-butyldithiocarbamate (Accel BZ, manufactured by Kawaguchi Chemical Co., Ltd.) After heating to 270 ° C. with a mantle heater and stirring for 15 minutes, 200 g of first polylactic acid (Ingeo 4060D, manufactured by Nature Works) was put into a separable flask, and stirring and mixing were continued for 40 minutes. After the mantle heater was set at 240 ° C.
- the first polylactic acid composition was obtained by mixing.
- the viscosity of the composition was 400 to 500 mPa ⁇ s using a Brookfield rotational viscometer set at 180 ° C.
- Thermal stability test The initial melt viscosity at 180 ° C. and the melt viscosity after 24 hours of the hot melt adhesives obtained in the examples were measured with a Brookfield viscometer, and the thermal stability was examined.
- Initial viscosity 1,085 mPa ⁇ s, after 4 hours 1,037 mPa ⁇ s (viscosity change rate 4.4%), after 8 hours 1,017 mPa ⁇ s (viscosity change rate 6.3%), after 12 hours 1,007 mPa ⁇ s S (viscosity change rate 7.2%), and after 24 hours, 992 mPa ⁇ s (viscosity change rate 8.6%).
- the initial viscosity is a viscosity measured after being left at room temperature for 24 hours after completion of the production process and then re-dissolved.
- Test piece front liner K170 / core S115 / back liner K170 AF Test piece preparation conditions: A hot melt agent melted at 180 ° C. was applied to a test piece (100 ⁇ 50 mm) at a coating amount of about 3 g / m, and another test piece (50 ⁇ 50 mm) was pressure-bonded thereon with a pressing load of 2 kg. After fixing with a set time of 2 seconds or with an open time of 2 seconds, the adhesive strength is measured using a hot melt tester (ASM-15 adhesive evaluation machine, manufactured by JT Toshi Co., Ltd.). The condition of destruction was visually observed.
- ASM-15 adhesive evaluation machine manufactured by JT Toshi Co., Ltd.
- an EVA hot melt agent (Nitite HC-225SS, manufactured by Nitta Gelatin Co., Ltd.) was used. In Test 1, the measurement was performed at an open time of 5, 10, 15 seconds, and in Test 2, the set time was 0. Measurements were taken in 5, 1, 5 seconds. The results are shown in Tables 1 and 2, respectively. In the table, “material breakage” indicates failure of the specimen. “Interface peeling” means peeling at the interface between the test piece and the adhesive layer, and “cohesive failure” means breaking of the adhesive layer.
- Test piece front liner K170 / core S115 / back liner K170 AF
- Test piece preparation conditions On one side of a test piece (100 ⁇ 50 mm), the hot melt agent obtained in the example was melted at 180 ° C. and applied at a coating amount of about 3 g / m, and another test piece (50 ⁇ 50 mm) was applied thereon. ) With a pressing load of 2 kg. After leaving the test pieces obtained by bonding with an open time of 2 seconds and a set time of 2 seconds in each of the following environments, as shown in FIG.
- the condition of the test piece was visually observed while grasping the jig by hand and pulling it up vertically.
- ⁇ Heat resistant bonding> After 5 samples of the test piece were left at 60 ° C. for 5 days, the adhesive strength was measured. The result was material failure of the specimens in all 5 samples.
- ⁇ Cold-resistant adhesion> After 5 samples of the test piece were allowed to stand at ⁇ 18 ° C. for 3 days, the adhesive strength was measured. The result was material failure of the specimens in all 5 samples.
- ⁇ Accelerated aging test> Fifteen test specimens were allowed to stand at 40 ° C. and 90% RH for 96 hours, and then left at 23 ° C. and 50% RH for 72 hours to measure the adhesive strength. The result was material failure of the specimens in all 15 samples.
- the production method of the present invention is very useful for easily preparing a polylactic acid-based hot melt adhesive composition having heat stability that can be practically used.
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Abstract
Description
ポリ乳酸系ホットメルト接着剤の製造方法であって,
(1)180~280℃の温度で,ジチオカルバミン酸塩と可塑剤の混合液に,ASTM D5225に準拠して測定される相対粘度が2.5~4.0の第1ポリ乳酸100重量部を添加して溶融混合した後,亜リン酸エステルとヒンダードフェノールを添加して,第1ポリ乳酸組成物を調製する工程であって,該100重量部に対して,該可塑剤は10~100重量部,該ジチオカルバミン酸塩は0.02~0.3重量部,該亜リン酸エステルは1~10重量部,及び該ヒンダードフェノールは1~10重量部で添加され,該第1ポリ乳酸組成物の180~220℃で測定される粘度が70~700mPa・sである,工程,
(2)該第1ポリ乳酸組成物に,180~280℃の温度で,ASTM D5225に準拠して測定される相対粘度が2.5~4.0の第2ポリ乳酸を,第1ポリ乳酸/第2ポリ乳酸が重量比2/8~8/2となる量で混合する工程,
を含む方法。
R6~R9は,互いに独立に,C10~18のアルキル基であり,R10はC2~4のアルキレンオキシアルキレン基,又は4,4’-イソプロピリデン-ジフェニレン基である。
(1)撹拌装置を備えた500mlセパラブルフラスコに,エポキシ化大豆油16g,アジピン酸エステル28g,及びジ-n-ブチルジチオカルバミン酸亜鉛(アクセルBZ,川口化学社製)0.28gを投入し,マントルヒーターにより270℃に加熱し,15分間撹拌した後,第1ポリ乳酸(Ingeo 4060D,ネイチャーワークス社製)200gをセパラブルフラスコに投入し40分撹拌混合を続けた。マントルヒーターの設定温度を240℃にして15分間撹拌混合した後,亜リン酸エステル(アデカスタブHP10,2,2-メチレンビス(4,6-ジ-t-ブチルフェニル)2-エチルヘキシルホスファイト,アデカ社製),ヒンダードフェノール(アデカスタブAO-30,1,1,3-トリス(2-メチル-4-ヒドロキシ-5-tert-ブチルフェニル)ブタン,アデカ社製)各4gを投入し,5分間撹拌混合して,第1ポリ乳酸組成物を得た。該組成物の粘度は,180℃に設定されたブルックフィールド回転粘度計を用いて,400~500mPa・sであった。
(2)次いで,マントルヒーターの温度を270℃にし,第2ポリ乳酸(Ingeo 4060D)156gを投入し,40分撹拌混合した後,徐々に温度を190℃に下げながら,50分撹拌混合を続けた。
得られた溶融ホットメルト接着剤を2cm×1cm×0.2cm×300個のシリコーン製成型シートに流し入れて,自然冷却し,短冊状のホットメルト接着剤組成物を得た。
実施例で得られたホットメルト接着剤の,180℃での初期溶融粘度と24時間後の溶融粘度をブルックフィールド粘度計により測定し,熱安定性を調べた。初期粘度1,085mPa・s,4時間後1,037mPa・s(粘度変化率4.4%),8時間後1,017mPa・s(粘度変化率6.3%),12時間後1,007mPa・s(粘度変化率7.2%),24時間後992mPa・s(粘度変化率8.6%)となった。該初期粘度は,上述のとおり,製造工程終了後,24時間室温で放置後,再溶解させて測定した粘度である。
室温にて,オープンタイム(試験1)とセットタイム(試験2)を測定した。試験条件は以下のとおりである。
試験片:表ライナーK170/中芯S115/裏ライナーK170 AF
試験片作成条件:試験片(100x50mm)に180℃で溶融したホットメルト剤を塗布量約3g/mで塗布し,その上から他の試験片(50x50mm)を圧締荷重2kgで圧着した。セットタイムを2秒に固定し,又はオープンタイムを2秒に固定して接着した後,接着強度をホットメルト試験機(ASM-15接着性評価機,JTトーシ(株)製)を用いて測定し,破壊の状況を目視した。比較試料として,EVA系ホットメルト剤(ニッタイトHC-225SS,新田ゼラチン(株)製)を用い,試験1ではオープンタイム5,10,15秒での測定を,試験2においては,セットタイム0.5,1,5秒で測定を行った。結果を夫々表1,2に示す。表中,「材破」は試験片の破壊を示す。「界面剥離」は試験片と接着層との界面での剥離を意味し,「凝集破壊」は接着層の破壊を意味する。
試験片:表ライナーK170/中芯S115/裏ライナーK170 AF
試験片作成条件:試験片(100x50mm)の一面に実施例で得られたホットメルト剤を180℃で溶融して,約3g/mの塗布量で塗布し,その上から他の試験片(50x50mm)を圧締荷重2kgで圧着した。オープンタイム2秒,セットタイム2秒で接着して得られた試験片を,下記それぞれの環境に放置した後,図1のaに示すように接着面の両端から治具を夫々挿入し,図1bに示すように該治具を手でつかんで垂直上方向に引き上げながら,試験片の破壊の状況を目視にて観察した。
<耐熱接着>
試験片5サンプルを60℃5日間放置後,接着強度を測定した。結果は,5サンプルすべてで試験片の材質破壊であった。
<耐寒接着>
試験片5サンプルを-18℃3日間放置後,接着強度を測定した。結果は,5サンプルすべてで試験片の材質破壊であった。
<促進老化テスト>
試験片15サンプルを40℃90%RHで96時間放置後,23℃50%RHで72時間放置して,接着強度を測定した。結果は,15サンプルすべてで試験片の材質破壊であった。
Claims (5)
- ポリ乳酸系ホットメルト接着剤の製造方法であって,
(1)180~280℃の温度で,ジチオカルバミン酸塩と可塑剤の混合液に,ASTM D5225に準拠して測定される相対粘度が2.5~4.0の第1ポリ乳酸100重量部を添加して溶融混合した後,亜リン酸エステルとヒンダードフェノールを添加して,第1ポリ乳酸組成物を調製する工程であって,該100重量部に対して,該可塑剤は10~100重量部,該ジチオカルバミン酸塩は0.02~0.3重量部,該亜リン酸エステルは1~10重量部,及び該ヒンダードフェノールは1~10重量部で添加され,該第1ポリ乳酸組成物の180~220℃で測定される粘度が70~700mPa・sである,工程,
(2)該第1ポリ乳酸組成物に,180~280℃の温度で,ASTM D5225に準拠して測定される相対粘度が2.5~4.0の第2ポリ乳酸を,第1ポリ乳酸/第2ポリ乳酸が重量比2/8~8/2となる量で混合する工程,
を含む方法。 - 該可塑剤が,グリセリントリアセテート,フタル酸ブチルベンジル,エポキシ化大豆油,トール油,アジピン酸エステル,及びポリグリセリン脂肪酸エステルからなる群より選ばれる少なくとも一種である,請求項1又は2記載の方法。
- 該ヒンダードフェノールが,1,1,3-トリス(2-メチル-4-ヒドロキシ-5-tert-ブチルフェニル)ブタン,又は4,4’-ブチリデンビス(6-tert-ブチル-3-メチルフェノール)である,請求項1~4のいずれか1項記載の方法。
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US17/042,126 US11802225B2 (en) | 2018-05-18 | 2019-04-05 | Method for producing polylactic acid-based hot melt adhesive |
EP19804429.9A EP3795651A4 (en) | 2018-05-18 | 2019-04-05 | METHOD FOR PRODUCTION OF POLY(LACTIC ACID) HOT MELTING ADHESIVE |
CN201980006538.4A CN111492028B (zh) | 2018-05-18 | 2019-04-05 | 聚乳酸类热熔胶接着剂的制造方法 |
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JPH01213381A (ja) * | 1988-02-22 | 1989-08-28 | Nippon Zeon Co Ltd | ホットメルト型粘着剤用組成物およびホットメルト型粘着剤 |
JPH05339557A (ja) | 1992-06-11 | 1993-12-21 | Mitsui Toatsu Chem Inc | ホットメルト接着剤組成物 |
US5252646A (en) | 1992-10-29 | 1993-10-12 | National Starch And Chemical Investment Holding Corporation | Polylactide containing hot melt adhesive |
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