WO2015016350A1 - Adhesive for crepe and method for manufacturing crepe paper - Google Patents
Adhesive for crepe and method for manufacturing crepe paper Download PDFInfo
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- WO2015016350A1 WO2015016350A1 PCT/JP2014/070356 JP2014070356W WO2015016350A1 WO 2015016350 A1 WO2015016350 A1 WO 2015016350A1 JP 2014070356 W JP2014070356 W JP 2014070356W WO 2015016350 A1 WO2015016350 A1 WO 2015016350A1
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- crepe
- paper
- adhesive
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Classifications
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/146—Crêping adhesives
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/52—Epoxy resins
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
- D21H17/55—Polyamides; Polyaminoamides; Polyester-amides
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
- D21H17/56—Polyamines; Polyimines; Polyester-imides
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
- D21H17/57—Polyureas; Polyurethanes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
- D21H25/005—Mechanical treatment
Definitions
- the present invention relates to an adhesive for crepe used when manufacturing paper such as toilet paper, tissue paper, towel paper, and sanitary paper such as kitchen paper.
- Creping is a process in which a wet fiber web is bonded to a rotary cylinder paper machine dryer known as a Yankee dryer in the drying process, and after drying, the fiber web is scraped off from the dryer surface with a doctor blade, and crepe is applied to the fiber web.
- a crepe adhesive is applied to the dryer surface to form a film.
- the coating on the dryer surface is effective to increase the adhesion of the fiber web to the Yankee dryer and to protect the dryer surface against doctor blade contact.
- thermosetting resins such as polyamide polyamine / epihalohydrin resin and polyamide polyamine polyurea / epihalohydrin resin have been proposed (for example, see Patent Documents 1, 2, and 3).
- plasticizers for crepe adhesives.
- an adhesive prepared by mixing a reaction product of adipic acid and methylbis (aminopropylamine) with a polyamide epichlorohydrin resin obtained by reacting epichlorohydrin and a polyhydric alcohol plasticizer has been proposed (for example, , See Patent Document 4).
- these crepe adhesives are used, there is a problem that the fiber web cannot be uniformly creped because the water resistance of the film formed on the Yankee dryer is weak or the adhesion of the film to the fiber web is weak. It was.
- the object of the present invention is excellent in adhesion between fiber webs when producing paper, and the paper is easy to disaggregate even though there is little elution of the coating film by moisture brought in from wet paper etc. It is an object of the present invention to provide an adhesive for crepe with less wear of a doctor blade because the formed film is soft.
- a crepe adhesive comprising a polyamide polyamine / epihalohydrin resin (A) and / or a polyamide polyamine / polyurea / epihalohydrin resin (B) and a softening agent (C), all of the following conditions (1) to (5):
- a crepe adhesive characterized by filling. (1) 0 to 0.2 mEq of azetidinium group in 1 g of solid content of crepe adhesive (2) The intrinsic viscosity of the crepe adhesive is 0.20 to 0.55 dL / g.
- a method for producing crepe paper comprising a step, ⁇ 4> ⁇ 3> the method for producing a crepe paper according to ⁇ 3>, wherein a softener is used as an internal additive, and the paper is sanitary paper I will provide a.
- the present invention is a crepe adhesive containing at least a polyamide polyamine / epihalohydrin resin (A) and / or a polyamide polyamine / polyurea / epihalohydrin resin (B) and a softening agent (C).
- an adhesive for crepe containing at least a polyamide polyamine / epihalohydrin resin (A) and a softening agent (C) A crepe adhesive containing at least a polyamide polyamine polyurea / epihalohydrin resin (B) and a softener (C);
- a crepe adhesive containing at least a polyamide polyamine / epihalohydrin resin (A), a polyamide polyamine / polyurea / epihalohydrin resin (B) and a softening agent (C) is also included.
- a polyamide polyamine / epihalohydrin resin (e) obtained by reacting a polyalkylene polyamine (a) and a dibasic carboxylic acid (b) with an epihalohydrin (c) to a polyamide polyamine (x) ( A) and softener (C)
- a polyamide polyamine obtained by reacting a polyalkylene polyamine (a), a dibasic carboxylic acid (b) and a urea (d) with a polyamide polyamine polyurea (y) and an epihalohydrin (c)
- Polyamide polyamine which is a crepe adhesive containing at least a polyurea / epihalohydrin resin (B) and a softener (C), and is naturally obtained by reacting a polyalkylene polyamine (a) and a dibasic carboxylic acid (b).
- X is reacted with a polyamidopolyamine / epihalohydrin resin (A) obtained by reacting an epihalohydrin (c) with a polyalkylene polyamine (a), a dibasic carboxylic acid (b) and a urea (d).
- A polyamidopolyamine / epihalohydrin resin obtained by reacting an epihalohydrin (c) with a polyalkylene polyamine (a), a dibasic carboxylic acid (b) and a urea (d).
- Polyamide polyamine polyurea (y) and epihalohydrin (c) obtained Creping adhesive comprising at least obtained by reacting polyamidepolyaminepolyurea-epihalohydrin resin (B) and softening agent (C) also included.
- the polyalkylene polyamine (a) used in the present invention may be any one having at least two alkylene groups and two or more amino groups in the molecule, such as diethylenetriamine, triethylenetetramine, tetraethylene.
- diethylenetriamine, triethylenetetramine, tetraethylene examples include pentamine, pentaethylenehexamine, hexaethyleneheptamine, dipropylenetriamine, tripropylenetetramine, iminobispropylamine, and the like. These may be used alone or in combination of two or more. .
- diethylenetriamine, triethylenetetramine, and tetraethylenepentamine are preferable because of excellent adhesiveness.
- diethylenetriamine is particularly preferable. These may be used alone or in combination of two or more.
- alkylene diamines such as ethylenediamine, propylenediamine or hexamethylenediamine
- aminocarboxylic acids having 1 to 6 carbon atoms such as ⁇ -aminocaproic acid, and 1 to 6 carbon atoms such as ⁇ -caprolactam. Lactams of aminocarboxylic acids can also be used.
- the dibasic carboxylic acids (b) used in the present invention include two dibasic carboxylic acids and / or derivatives thereof in the molecule.
- Examples of the derivatives include mono- or diesters of these dibasic carboxylic acids, or acid anhydrides.
- Examples of the dibasic carboxylic acid include malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, brassic acid, dodecanedioic acid and the like.
- a dibasic carboxylic acid having a number of 5 to 10 is preferred.
- examples of mono- or diesters of dibasic carboxylic acid include lower alcohol (methyl, ethyl, propyl) esters preferably having 1 to 5 carbon atoms, particularly preferably 1 to 3 carbon atoms.
- examples of the acid anhydride include an intramolecular dehydration condensate of a free acid and a condensate of a lower carboxylic acid, preferably a lower carboxylic acid having 1 to 5 carbon atoms.
- Particularly preferred industrially preferred dibasic carboxylic acids (b) include adipic acid, glutaric acid dimethyl ester, and adipic acid dimethyl ester. Said dibasic carboxylic acid (b) can be used 1 type or in combination of 2 or more types.
- carboxylic acids and / or carboxylic acids thereof in the molecule such as citric acid and trimellitic acid, may be used as long as the effects of the present invention are not hindered.
- Acid esters or derivatives having acid anhydrides thereof can also be used.
- ureas (d) used in the present invention include urea, thiourea, guanylurea, phenylurea, methylurea, dimethylurea and the like. Of these, urea is particularly preferred industrially.
- compounds having one or more N unsubstituted amide groups that can undergo an amide exchange reaction with an amino group for example, aliphatic amides such as acetamide and propionamide Or aromatic amides such as benzamide and phenylacetamide can also be used.
- the epihalohydrin (c) used in the present invention includes epichlorohydrin, epibromohydrin and the like, but industrially epichlorohydrin is preferable.
- the polyamide polyamine / epihalohydrin resin (A) in the present invention is obtained by reacting a polyalkylene polyamine (a) and a dibasic carboxylic acid (b) with a polyamido polyamine (x) and an epihalohydrin (c). The resulting resin.
- the polyamide polyamine / epihalohydrin resin (A) of the present invention is preferably a polyalkylene polyamine (a) 38 to 58 mol%, a dibasic carboxylic acid (b) 37 to 55 mol%, and an epihalohydrin (c) 1 to 14 mol. %, A crepe adhesive having excellent film properties can be obtained.
- the polyalkylene polyamine (a) is preferably 43 to 54%
- the dibasic carboxylic acid (b) is 42 to 52 mol%
- the epihalohydrin (c) is preferably 1 to 10 mol%.
- the polyamide polyamine polyurea / epihalohydrin resin (B) in the present invention is a polyamide polyamine polyurea (y) obtained by reacting a polyalkylene polyamine (a), a dibasic carboxylic acid (b), and a urea (d). And epihalohydrin (c).
- the reaction of the polyalkylene polyamine (a), the dibasic carboxylic acid (b) and the urea (d) can be performed in any order or simultaneously.
- the polyalkylene polyamine (a), the dibasic carboxylic acid (b), and the urea (d) can be reacted simultaneously.
- polyalkylene polyamine (a) and ureas (d) are reacted to obtain polyalkylene polyamine polyurea (z), and then the polyalkylene polyamine polyurea (z) is reacted with dibasic carboxylic acids (b). Can be made. Furthermore, the polyalkylene polyamine (a) and the dibasic carboxylic acid (b) can be reacted to obtain a polyamide polyamine (x), and the polyamide polyamine (x) and the urea (d) can be reacted.
- the polyamide polyamine polyurea / epihalohydrin resin (B) of the present invention is preferably a polyalkylene polyamine (a) 28 to 58 mol%, a dibasic carboxylic acid (b) 24 to 55 mol%, and a urea (d) 37
- a polyalkylene polyamine (a) is 33 to 54%
- the dibasic carboxylic acid (b) is 28 to 52 mol%
- the urea (d) is 35 mol% or less
- the epihalohydrin (c) is 1 to 10 mol%. preferable.
- the condensation reaction of the polyalkylene polyamine (a) and the dibasic carboxylic acid (b), or the polyalkylene polyamine (a) and the urea (d), or the polyamide polyamine (x) and the urea (d) Dehydration and / or dealcoholization and / or deammonia reaction is performed.
- the reaction temperature is preferably 110 to 250 ° C. and the reaction time is 1 to 8 hours.
- sulfonic acids such as sulfuric acid, benzenesulfonic acid, and paratoluenesulfonic acid
- phosphoric acids such as phosphoric acid, phosphonic acid, and hypophosphorous acid
- other known catalysts may be used alone or in combination. These can be used in combination.
- the concentration of the reaction solution is preferably 10 to 80% by mass, and the reaction temperature depends on the reaction concentration. Although adjustment is necessary as appropriate, it is usually preferred to carry out at 5 to 90 ° C.
- the reaction between the polyamide polyamine (x) and / or the polyamide polyamine polyurea (y) and the epihalohydrin (c) is carried out by reacting the resulting polyamide polyamine / epihalohydrin resin (A) and / or polyamide polyamine polyurea / epihalohydrin resin (B).
- the viscosity is within the range of 10 to 350 mPa ⁇ s, preferably 50 to 250 mPa ⁇ s, based on the viscosity at 25 ° C. of an aqueous solution containing 15% by mass of solid content, a resin having excellent adhesive strength can be obtained. Be able to.
- the reaction is stopped by adding water to the reaction liquid and cooling it to obtain an aqueous solution of resin (A) and / or resin (B).
- the aqueous solution of the crepe adhesive of the present invention can be adjusted in pH to improve storage stability and control film formation.
- the pH can be adjusted by adding a pH adjuster.
- the pH adjuster include inorganic acids such as hydrochloric acid, sulfuric acid, nitric acid and phosphoric acid, especially inorganic acids not containing halogen; organic acids such as formic acid and acetic acid; sodium hydroxide, potassium hydroxide, calcium hydroxide, water
- Preferable examples include inorganic bases such as magnesium oxide, sodium carbonate and potassium carbonate; monoamine compounds such as ammonia, diethylamine, triethylamine, propylamine, butylamine, diisobutylamine, hydroxyamine, ethanolamine and diethanolamine.
- the azetidinium group should be 0 to 0.2 mEq, preferably 0 to 0.1 mEq in 1 g of the solid content of the crepe adhesive of the present invention.
- AZR azetidinium group
- a wet paper strength effect is manifested when used as an adhesive for crepes, and water disintegration of toilet paper and the like is achieved. Adversely affect.
- the intrinsic viscosity of the crepe adhesive should be 0.20 to 0.55 dL / g, preferably 0.25 to 0.5 dL / g.
- the intrinsic viscosity is a physical quantity that depends on the molecular weight, shape, and size of the polymer chain that is independently dissolved in the solvent. If it is this range, when using as an adhesive for crepes, it will become easy to form the film
- the softener (C) contained in the crepe adhesive is It must be (i) a boiling point of 150 ° C. or higher and liquid at 80 ° C., and (ii) a water-soluble aliphatic polyol or polyethylene glycol dimethyl ether.
- the softener (C) is preferably ethylene glycol, diethylene glycol, triethylene glycol, polyethylene glycol, propylene glycol, dipropylene glycol, glycerol, 1,3-butanediol, 1,4-butanediol, diethylene glycol dimethyl ether, triethylene.
- Examples thereof include glycol dimethyl ether and tetraethylene glycol dimethyl ether, and polyethylene glycol, diethylene glycol dimethyl ether, and triethylene glycol dimethyl ether are particularly preferable.
- the water resistance required by the following formula (1) needs to be 40 to 100% in the following evaluation of water resistance.
- a tea bag weight W2 (g)
- a petri dish weight W1 (g)
- a uniform film weight of 0.05 g was immersed in water at 50 ° C. for 5 minutes with stirring.
- the petri dish is weighed and measured for each tea bag (weight W3 (g)), and water resistance is calculated from the following equation (1).
- Water resistance (%) 100 ⁇ ⁇ (W1 + W2) ⁇ W3 ⁇ /0.05 ⁇ 100
- the coating film is less likely to be eluted by moisture brought in from wet paper or the like, and the coating film is easily formed on the Yankee dryer.
- the weight average molecular weight of the crepe adhesive of the present invention is preferably from 1 to 5 million, particularly from 1.5 to 4.5 million in order to obtain excellent adhesion.
- the weight average molecular weight in this invention is based on the measurement described in the Example.
- Specific methods for applying the crepe adhesive of the present invention to paper include a method of spraying wet paper in front of a Yankee dryer in a manufacturing process, a method of spraying directly on the surface of a Yankee dryer, and a combination of these methods. There is a way to do it. Spraying directly on the surface of the Yankee dryer is preferable because the effect as an adhesive for crepe is easily obtained.
- the crepe adhesive of the present invention can be used in combination with a crepe release agent in order to control the adhesive force of the fiber web to the surface of the Yankee dryer.
- a crepe release agent examples include silicone oil, hydrocarbon oil, oxidized wax, paraffin wax, polyethylene wax, cationic surfactant, anionic surfactant, and amphoteric surfactant. These can be used alone or in combination of two or more.
- the crepe adhesive of the present invention When the crepe adhesive of the present invention is sprayed directly on the surface of the Yankee dryer, the crepe adhesive is diluted 10 to 1000 times, and the spray amount is 0.01 to 500 mg / m 2 based on the solid content of the resin.
- a content of 0.1 to 300 mg / m 2 is preferable because a uniform coating film suitable for creping is easily obtained. Outside this range, when a sufficient coating film is not formed or dirt is deposited on the coating film, creping becomes difficult in all cases.
- the method of using the crepe adhesive in the present invention is application to paper as described above. However, as another embodiment, it is used by adding (internal addition) to a paper material (pulp slurry), or both internal addition and application. Can also be used.
- the crepe adhesive is added internally, it is usually 0.01 to 1% by mass, preferably 0.01 to 0.5% by mass, based on the solid content of the crepe adhesive, based on the pulp solid content. What is necessary is just to add.
- the basis weight of the paper is 10 to 45 g / m 2 and the density is 0.1 to 0.4 g / cm 3 from the viewpoint of texture.
- the longitudinal dry tear length JIS P 8113
- toilet paper or tissue paper is preferably 0.2 to 0.8 km from the viewpoint of water decomposability.
- the water absorption Japanese Industrial Standards JIS S 3104
- the water absorption is 1 to 10 seconds when two sheets are stacked, from the viewpoint of the wiping effect when used.
- the paper to be creped using the crepe adhesive of the present invention is preferably sanitary paper such as toilet paper, tissue paper, towel paper, kitchen paper, and bleached or unbleached chemicals such as kraft pulp or sulfite pulp as a pulp raw material.
- Waste paper pulp such as bleached or unbleached high yield pulp such as pulp, groundwood pulp, mechanical pulp or thermomechanical pulp, newspaper waste paper, magazine waste paper, corrugated waste paper or deinked waste paper can be contained.
- a softener In producing a paper to be creped using the crepe adhesive of the present invention, a softener, a filler, a sizing agent, a dry paper strength improver, a wet paper strength improver, a yield improver, a bulk enhancer, and a paper thickness improver.
- additives such as an opacifying agent and a freeness improver may be used as necessary in order to develop the physical properties required for each paper type. These may be used alone or in combination of two or more. Among them, it is preferable to add a softener internally or externally because paper having excellent texture can be obtained.
- the softener examples include a fatty acid amide epihalohydrin resin (S1), a quaternary ammonium salt (S2) having an alkyl group and / or an alkenyl group, an alkylene oxide reactant (S3) of a fatty acid and / or an aliphatic alcohol, and the like.
- fatty acid amide epihalohydrin resin (S1) is preferable because of its excellent flexibility effect in the present invention.
- S1 may be used alone or in combination of two or more. Usually, it may be added to the paper in a proportion of 0.01 to 1% by mass, preferably 0.01 to 0.5% by mass, based on the solid content of the pulp.
- Example 1 ⁇ Production of polyamide polyamine (x-1)>
- a four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube 103 g (1 mol) of diethylenetriamine (hereinafter sometimes abbreviated as “DETA”), 0.52 g of 95% sulfuric acid (0 0.005 mol) was added, and while stirring, 146 g (1 mol) of adipic acid was added. Under nitrogen flow, the temperature was raised while removing generated water out of the system, and the reaction was carried out at 175 ° C. for 3 hours. Gradually added to adjust the solid content to 35% to obtain a polyamide polyamine aqueous solution (x-1).
- DETA diethylenetriamine
- Example 2 Epichlorohydrin (12 g, 0.13 mol) was added to the total amount of the polyamide polyamine aqueous solution (x-1) obtained in the same manner as in Example 1, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 470 mPa ⁇ s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-2). Next, 99 g of propylene glycol (30% by mass relative to 100% by mass of resin (A-2) solid content) was added as a softener (C), and the solid content was adjusted to 15% with water. An adhesive was obtained.
- Example 3 ⁇ Production of polyamide polyamine (x-2)> A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 108 g (1.05 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid and stirred with adipine. 146 g (1 mol) of acid was added, the temperature was raised while removing the generated water out of the system under a nitrogen stream, and after reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 35%. A polyamide polyamine aqueous solution (x-2) was obtained.
- Example 4 7.4 g (0.08 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-2) obtained in the same manner as in Example 3, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 20 mPa ⁇ s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-4). Next, 58 g of glycerin as a softening agent (C) (20% by mass with respect to 100% by mass of resin (A-4) solid content) was added, and the solid content was adjusted to 15% with water. Got.
- C softening agent
- Example 5 14.8 g (0.16 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-2) obtained in the same manner as in Example 3, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 510 mPa ⁇ s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-5). Next, 60 g of glycerin as a softening agent (C) was added (so that the resin (A-5) had a solid content of 20% by mass with respect to 100% by mass), and the solid content was adjusted to 15% with water. Got.
- glycerin as a softening agent (C) 60 g of glycerin as a softening agent (C) was added (so that the resin (A-5) had a solid content
- Example 6 Provide of polyamide polyamine polyurea (y-1)> A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 105 g (1.02 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid, and agitated while stirring. 146 g (1 mol) of acid was added, and the temperature was raised while removing the generated water out of the system under a nitrogen stream. After reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 98%. Next, 12 g (0.2 mol) of urea was added and reacted at 125 ° C. for 2 hours, and then water was gradually added to adjust the solid content to 35% to obtain a polyamide polyamine polyurea aqueous solution (y-1).
- Example 7 ⁇ Production of polyamide polyamine polyurea (y-2)> A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 105 g (1.02 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid, and agitated while stirring. 146 g (1 mol) of acid was added, and the temperature was raised while removing the generated water out of the system under a nitrogen stream. After reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 98%. Next, 24 g (0.4 mol) of urea was added and reacted at 125 ° C. for 2 hours, and then water was gradually added to adjust the solid content to 35% to obtain a polyamide polyamine polyurea aqueous solution (y-2).
- Example 8 ⁇ Production of polyamide polyamine (x-3)> A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 101 g (0.98 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid, and agitated with stirring. 146 g (1 mol) of acid was added, the temperature was raised while removing the generated water out of the system under a nitrogen stream, and after reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 35%. A polyamide polyamine aqueous solution (x-3) was obtained.
- Example 9 ⁇ Production of polyamide polyamine (x-4)> A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 108 g (1.05 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid and stirred with adipine. 146 g (1 mol) of acid was added, the temperature was raised while removing the generated water out of the system under a nitrogen stream, and after reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 35%. A polyamide polyamine aqueous solution (x-4) was obtained.
- Example 10 11.1 g (0.12 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 80 mPa ⁇ s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-8). Next, 59 g of propylene glycol (20% by mass with respect to 100% by mass of resin (A-8) solid content) was added as a softening agent (C), and the solid content was adjusted to 15% with water. Got.
- Example 11 11.1 g (0.12 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 80 mPa ⁇ s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-9).
- Example 12 11.1 g (0.12 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 80 mPa ⁇ s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-10).
- diethylene glycol dimethyl ether (so as to be 20% by mass with respect to 100% by mass of the resin (A-10) solid content) was added as a softening agent (C), and the solid content was adjusted to 15% with water.
- Example 13 11.1 g (0.12 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 80 mPa ⁇ s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-11). Next, 59 g of triethylene glycol dimethyl ether (20% by mass with respect to 100% by mass of resin (A-11) solid content) was added as a softening agent (C), and the solid content was adjusted to 15% with water. An adhesive was obtained.
- Comparative Example 2 (corresponding to Example 1 of the prior art, Japanese Patent No. 483523) ⁇ Production of polyamide polyamine polyurea (y-3)> A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 105.3 g (1.02 mol) of diethylenetriamine, and 146.1 g (1 mol) of adipic acid was added with stirring. The temperature was raised while removing the generated water out of the system, and the reaction was carried out at 170 ° C. for 3 hours.
- reaction solution was cooled to 130 ° C., 12 g (0.2 mol) of urea was added, and deammonia reaction was performed at the same temperature for 2 hours, and then water was gradually added to polyamide polyamine polyurea having a solid content of 50%. 450 g of an aqueous solution (y-3) was obtained.
- Comparative Example 3 (corresponding to Example 1 of Japanese Patent No. 591046, which is a prior art) A four-necked round bottom flask equipped with a thermometer, a condenser, and a stirrer was charged with 108.2 g (1.05 mol) of diethylenetriamine, 146.1 g (1.00 mol) of adipic acid, and 146.1 g of water. A dehydration reaction was performed at 160 to 170 ° C. for 6 hours to obtain a polyamide polyamine aqueous solution. Water was added thereto to obtain 440 g of a 50% polyamide polyamine aqueous solution (x-5).
- Comparative Example 4 (when the intrinsic viscosity of the crepe adhesive is low and out of range)
- a polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9 3.7 g (0.04 mol) of epichlorohydrin was added, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour.
- water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 45 mPa ⁇ s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-14).
- 57 g of propylene glycol (20% by mass with respect to 100% by mass of resin (A-14) solid content) was added to obtain an adhesive for crepe having a solid content adjusted to 15% with water.
- Comparative Example 5 (when the water resistance evaluation value of the crepe adhesive is out of range) 7.4 g (0.08 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%. After the temperature was raised to 70 ° C., when the viscosity reached 45 mPa ⁇ s, 10.8 g of 98% sulfuric acid was added to terminate the reaction, and the polyamide polyamine / epichlorohydrin resin ( A-15) was obtained. Next, 58 g of propylene glycol (20% by mass with respect to 100% by mass of resin (A-15) solid content) was added, and the pH was adjusted to 15% with 15% sulfuric acid and water, and the solid content was adjusted to 15%. An adhesive was obtained.
- Comparative Example 6 when the intrinsic viscosity of the crepe adhesive is high and out of range 14.8 g (0.16 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%. After the temperature was raised to 70 ° C., when the viscosity reached 640 mPa ⁇ s, 10.8 g of 98% sulfuric acid was added to terminate the reaction, and the polyamide polyamine / epichlorohydrin resin ( A-16) was obtained. Next, 59 g of propylene glycol (20% by mass with respect to 100% by mass of resin (A-16) solid content) was added, and the pH was adjusted to 15% with 15% sulfuric acid and water, and the solid content was adjusted to 15%. An adhesive was obtained.
- Synthesis Example 1 (Production Example of Softening Agent Corresponding to Fatty Acid Amide Epihalohydrin (S1))
- S1 Fatty Acid Amide Epihalohydrin
- the temperature was raised to 180 ° C., and reaction was performed for 3 hours while removing generated water out of the system to obtain an amide compound.
- the amount of residual amino groups of the obtained amide compound was 2 mmol / g.
- 100 g of the amide compound (0.16 mol as an amino group), 5 g of polyoxyethylene (45) stearylamine (the numbers in parentheses indicate the average number of moles added of polyoxyethylene), 100 g of water, and epihalohydrins as epihalohydrins.
- Chlorohydrin (5.9 g, 0.064 mol) was added at 50 ° C., and the mixture was stirred for 30 minutes. Subsequently, after the reaction solution was reacted at 70 ° C.
- reaction solution was cooled and adjusted by adding water so that the solid content was 30% by mass.
- concentration was 30%
- viscosity was 350 mPa ⁇ s
- melting point was obtained at 29 ° C.
- the weight average molecular weight of the crepe adhesive in the present invention is obtained by the GPC-MALS method in which a multi-angle light scattering detector is connected to GPC under the following measurement conditions.
- GPC body LC1100 series manufactured by Agilent Technologies Inc.
- Eluent N / 10 phosphate buffer (pH 3) containing N / 10 sodium nitrate
- Detector 1 Multi-angle light scattering detector DAWN manufactured by Wyatt Technology Detector 2: Suggested refractive index detector RI-101 manufactured by Showa Denko KK
- crepe adhesives of Examples 1 to 13 and Comparative Examples 1 to 6 were 0.3 g / m 2 as a solid content, and the crepe agent CR6154 (manufactured by Seiko PMC Co., Ltd., crepe release agent) as an active ingredient 0.25 g / m 2 and coated on a plate heated to 100 ° C.
- Table 5 shows the Young's modulus of the obtained handmade paper. Young's modulus: Ultrasonic wave propagation velocity V was measured with an orientation measuring instrument SST-2500 manufactured by Nomura Corporation, and the Young's modulus was obtained from the following formula. The lower the number, the more flexible the paper. Relative notation was made assuming that the Young's modulus of the paper without the softener was 100. Young's modulus ⁇ V 2 ( ⁇ : density)
- Softener 1 oleic acid EO (4) PO (12) oleyl ether corresponding to softener (S3).
- EO is ethylene oxide
- PO is propylene oxide
- the numerical value in () indicates the average added molar amount.
- Softener 2 ... Dioleyldimethylammonium chloride equivalent to softener (S2)
- Examples and Comparative Example 1 from Tables 1 to 4 By comparing Examples and Comparative Example 1 from Tables 1 to 4, compared to the case where the amount of AZR of the crepe adhesive is outside the scope of the present invention, the Examples of the present invention have a disaggregation property and adhesive strength. It is clear that the film surface is softer than that of Comparative Example 1. By comparing Examples and Comparative Examples 2 and 3 from Tables 1 to 4, the examples of the present invention have better disaggregation and adhesive strength than the prior art, and the coating surface is softer than the prior art. I understand. By comparing Examples and Comparative Example 4 from Tables 1 to 4, the examples of the present invention have higher disaggregation and adhesive strength than the case where the intrinsic viscosity of the crepe adhesive is low and outside the scope of the present invention. It turns out that it is favorable.
Abstract
Description
<1>
ポリアミドポリアミン・エピハロヒドリン樹脂(A)および/またはポリアミドポリアミンポリ尿素・エピハロヒドリン樹脂(B)並びに軟化剤(C)を含有するクレープ用接着剤であって、下記(1)~(5)の条件を全て満たすことを特徴とするクレープ用接着剤。
(1)クレープ用接着剤の固形分1g中のアゼチジニウム基が0~0.2mEq
(2)クレープ用接着剤の固有粘度が0.20~0.55dL/g
(3)軟化剤(C)が、以下の(i)及び(ii)を満たすものであること
(i)沸点150℃以上でかつ80℃で液体、
(ii)水溶性脂肪族ポリオールまたはポリエチレングリコールジメチルエーテル
(4)質量比で[樹脂(A)および/または樹脂(B)]:[軟化剤(C)]=100:0.5~70
(5)下記の算出方法によって評価される耐水性が40~100%
<耐水性の算出方法>
ティーバッグ(重さW2(g))に、均一な皮膜の重さが0.05gとなるように調製したシャーレ(重さW1(g))を50℃の水中に攪拌下、5分間浸漬し、乾燥させ、前記シャーレの重さをティーバッグごと(重さW3(g))測定し、下式(1)より耐水性を算出する。
式(1) 耐水性(%)=100-{(W1+W2)-W3}/0.05×100
W1(g):皮膜調製した金属シャーレの重さ、W2(g):ティーバッグの重さ、W3(g):浸漬・乾燥後のティーバッグとシャーレの重さ
<2>
クレープ用接着剤の重量平均分子量が100万~500万である前記<1>のクレープ用接着剤、
<3>
クレープ紙の製造方法であって、前記<1>又は<2>のクレープ用接着剤をドライヤー表面に繊維ウェブの面積に対して固形分あたり0.01~500mg/m2になるように塗布する工程を含むクレープ紙の製造方法、
<4>
内添薬品として柔軟剤を用い、紙が衛生用紙である前記<3>のクレープ紙の製造方法、
を提供する。 That is, the present invention
<1>
A crepe adhesive comprising a polyamide polyamine / epihalohydrin resin (A) and / or a polyamide polyamine / polyurea / epihalohydrin resin (B) and a softening agent (C), all of the following conditions (1) to (5): A crepe adhesive characterized by filling.
(1) 0 to 0.2 mEq of azetidinium group in 1 g of solid content of crepe adhesive
(2) The intrinsic viscosity of the crepe adhesive is 0.20 to 0.55 dL / g.
(3) The softener (C) satisfies the following (i) and (ii): (i) a liquid having a boiling point of 150 ° C or higher and 80 ° C;
(Ii) Water-soluble aliphatic polyol or polyethylene glycol dimethyl ether (4) [resin (A) and / or resin (B)]: [softener (C)] = 100: 0.5 to 70 in mass ratio
(5) Water resistance evaluated by the following calculation method is 40 to 100%
<Calculation method of water resistance>
In a tea bag (weight W2 (g)), a petri dish (weight W1 (g)) prepared so as to have a uniform film weight of 0.05 g was immersed in water at 50 ° C. for 5 minutes with stirring. Then, the petri dish is weighed and measured for each tea bag (weight W3 (g)), and water resistance is calculated from the following equation (1).
Formula (1) Water resistance (%) = 100 − {(W1 + W2) −W3} /0.05×100
W1 (g): Weight of the metal petri dish prepared as a film, W2 (g): Weight of the tea bag, W3 (g): Weight of the tea bag and the petri dish after dipping and drying <2>
The crepe adhesive according to the above <1>, wherein the crepe adhesive has a weight average molecular weight of 1,000,000 to 5,000,000;
<3>
A method for producing crepe paper, wherein the crepe adhesive according to <1> or <2> is applied to a dryer surface so as to be 0.01 to 500 mg / m 2 per solid content with respect to the area of the fiber web. A method for producing crepe paper comprising a step,
<4>
<3> the method for producing a crepe paper according to <3>, wherein a softener is used as an internal additive, and the paper is sanitary paper
I will provide a.
すなわち、ポリアミドポリアミン・エピハロヒドリン樹脂(A)および軟化剤(C)を少なくとも含有するクレープ用接着剤、
ポリアミドポリアミンポリ尿素・エピハロヒドリン樹脂(B)及び軟化剤(C)を少なくとも含有するクレープ用接着剤、
という態様であり、当然に
ポリアミドポリアミン・エピハロヒドリン樹脂(A)、ポリアミドポリアミンポリ尿素・エピハロヒドリン樹脂(B)及び軟化剤(C)を少なくとも含有するクレープ用接着剤という態様も含まれる。 The present invention is a crepe adhesive containing at least a polyamide polyamine / epihalohydrin resin (A) and / or a polyamide polyamine / polyurea / epihalohydrin resin (B) and a softening agent (C).
That is, an adhesive for crepe containing at least a polyamide polyamine / epihalohydrin resin (A) and a softening agent (C),
A crepe adhesive containing at least a polyamide polyamine polyurea / epihalohydrin resin (B) and a softener (C);
Naturally, an embodiment of a crepe adhesive containing at least a polyamide polyamine / epihalohydrin resin (A), a polyamide polyamine / polyurea / epihalohydrin resin (B) and a softening agent (C) is also included.
または、ポリアルキレンポリアミン(a)、二塩基性カルボン酸類(b)および尿素類(d)を反応させて得られるポリアミドポリアミンポリ尿素(y)とエピハロヒドリン(c)とを反応させて得られるポリアミドポリアミンポリ尿素・エピハロヒドリン樹脂(B)と軟化剤(C)を少なくとも含有するクレープ用接着剤であり、当然に
ポリアルキレンポリアミン(a)および二塩基性カルボン酸類(b)を反応させて得られるポリアミドポリアミン(x)に対し、エピハロヒドリン(c)を反応させて得られるポリアミドポリアミン・エピハロヒドリン樹脂(A)とポリアルキレンポリアミン(a)、二塩基性カルボン酸類(b)および尿素類(d)を反応させて得られるポリアミドポリアミンポリ尿素(y)とエピハロヒドリン(c)とを反応させて得られるポリアミドポリアミンポリ尿素・エピハロヒドリン樹脂(B)と軟化剤(C)を少なくとも含有するクレープ用接着剤も含まれる。 Specifically, a polyamide polyamine / epihalohydrin resin (e) obtained by reacting a polyalkylene polyamine (a) and a dibasic carboxylic acid (b) with an epihalohydrin (c) to a polyamide polyamine (x) ( A) and softener (C),
Alternatively, a polyamide polyamine obtained by reacting a polyalkylene polyamine (a), a dibasic carboxylic acid (b) and a urea (d) with a polyamide polyamine polyurea (y) and an epihalohydrin (c) Polyamide polyamine which is a crepe adhesive containing at least a polyurea / epihalohydrin resin (B) and a softener (C), and is naturally obtained by reacting a polyalkylene polyamine (a) and a dibasic carboxylic acid (b). (X) is reacted with a polyamidopolyamine / epihalohydrin resin (A) obtained by reacting an epihalohydrin (c) with a polyalkylene polyamine (a), a dibasic carboxylic acid (b) and a urea (d). Polyamide polyamine polyurea (y) and epihalohydrin (c) obtained Creping adhesive comprising at least obtained by reacting polyamidepolyaminepolyurea-epihalohydrin resin (B) and softening agent (C) also included.
(i)沸点150℃以上でかつ80℃で液体、かつ
(ii)水溶性脂肪族ポリオールまたはポリエチレングリコールジメチルエーテル
である必要がある。 The softener (C) contained in the crepe adhesive is
It must be (i) a boiling point of 150 ° C. or higher and liquid at 80 ° C., and (ii) a water-soluble aliphatic polyol or polyethylene glycol dimethyl ether.
ティーバッグ(重さW2(g))に、均一な皮膜の重さが0.05gとなるように調製したシャーレ(重さW1(g))を50℃の水中に攪拌下、5分間浸漬し、乾燥させ、前記シャーレの重さをティーバッグごと(重さW3(g))測定し、下式(1)より耐水性を算出する。
式(1) 耐水性(%)=100-{(W1+W2)-W3}/0.05×100
W1(g):皮膜調製した金属シャーレの重さ、W2(g):ティーバッグの重さ、W3(g):浸漬・乾燥後のティーバッグとシャーレの重さ
耐水性が上記範囲であれば、湿紙などから持ち込まれる水分によるコーティング皮膜の溶出が少なく、ヤンキードライヤー上にコーティング皮膜が形成し易くなる。 In the crepe adhesive of the present invention, the water resistance required by the following formula (1) needs to be 40 to 100% in the following evaluation of water resistance.
In a tea bag (weight W2 (g)), a petri dish (weight W1 (g)) prepared so as to have a uniform film weight of 0.05 g was immersed in water at 50 ° C. for 5 minutes with stirring. Then, the petri dish is weighed and measured for each tea bag (weight W3 (g)), and water resistance is calculated from the following equation (1).
Formula (1) Water resistance (%) = 100 − {(W1 + W2) −W3} /0.05×100
W1 (g): Weight of metal petri dish with coating prepared, W2 (g): Weight of tea bag, W3 (g): Weight of tea bag and petri dish after immersion / drying If water resistance is in the above range The coating film is less likely to be eluted by moisture brought in from wet paper or the like, and the coating film is easily formed on the Yankee dryer.
<ポリアミドポリアミン(x-1)の製造>
温度計、還流冷却器、攪拌機、窒素導入管を備えた四つ口丸底フラスコに、ジエチレントリアミン(以下、「DETA」と略することがある)103g(1mol)、95%硫酸0.52g(0.005 mol)を仕込み、攪拌しながら、アジピン酸146g(1mol)を加え、窒素気流下、生成する水を系外に除去しながら昇温し、175℃で3時間反応させた後、水を徐々に加えて固形分35%に調整し、ポリアミドポリアミン水溶液(x-1)を得た。 Example 1
<Production of polyamide polyamine (x-1)>
In a four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube, 103 g (1 mol) of diethylenetriamine (hereinafter sometimes abbreviated as “DETA”), 0.52 g of 95% sulfuric acid (0 0.005 mol) was added, and while stirring, 146 g (1 mol) of adipic acid was added. Under nitrogen flow, the temperature was raised while removing generated water out of the system, and the reaction was carried out at 175 ° C. for 3 hours. Gradually added to adjust the solid content to 35% to obtain a polyamide polyamine aqueous solution (x-1).
上記で得られたポリアミドポリアミン水溶液(x-1)全量にエピクロロヒドリン7.4g(0.08mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度45mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-1)を得た。次いで軟化剤(C)として、プロピレングリコールを12g(樹脂(A-1)固形分100質量%に対して5質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 <Manufacture of crepe adhesive>
7.4 g (0.08 mol) of epichlorohydrin was added to the total amount of the polyamidepolyamine aqueous solution (x-1) obtained above, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 45 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-1). Next, 12 g of propylene glycol (5% by mass relative to 100% by mass of the resin (A-1) solid content) was added as a softening agent (C), and the solid content was adjusted to 15% with water. An adhesive was obtained.
実施例1と同様にして得たポリアミドポリアミン水溶液(x-1)全量にエピクロロヒドリン12g(0.13mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度470mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-2)を得た。次いで軟化剤(C)として、プロピレングリコールを99g(樹脂(A-2)固形分100質量%に対して30質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 Example 2
Epichlorohydrin (12 g, 0.13 mol) was added to the total amount of the polyamide polyamine aqueous solution (x-1) obtained in the same manner as in Example 1, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 470 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-2). Next, 99 g of propylene glycol (30% by mass relative to 100% by mass of resin (A-2) solid content) was added as a softener (C), and the solid content was adjusted to 15% with water. An adhesive was obtained.
<ポリアミドポリアミン(x-2)の製造>
温度計、還流冷却器、攪拌機、窒素導入管を備えた四つ口丸底フラスコに、ジエチレントリアミン108g(1.05mol)、95%硫酸0.52g(0.005mol)を仕込み、攪拌しながら、アジピン酸146g(1mol)を加え、窒素気流下、生成する水を系外に除去しながら昇温し、175℃で6時間反応させた後、水を徐々に加えて固形分35%に調整し、ポリアミドポリアミン水溶液(x-2)を得た。 Example 3
<Production of polyamide polyamine (x-2)>
A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 108 g (1.05 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid and stirred with adipine. 146 g (1 mol) of acid was added, the temperature was raised while removing the generated water out of the system under a nitrogen stream, and after reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 35%. A polyamide polyamine aqueous solution (x-2) was obtained.
上記で得られたポリアミドポリアミン水溶液(x-2)全量にエピクロロヒドリン18.5g(0.2mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度50mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-3)を得た。次いで軟化剤(C)として、グリセリン61g(樹脂(A-3)固形分100質量%に対して20質量%となるように)加えて、15%硫酸と水でpH5、固形分を15%に調整したクレープ用接着剤を得た。 <Manufacture of crepe adhesive>
18.5 g (0.2 mol) of epichlorohydrin was added to the total amount of the polyamidepolyamine aqueous solution (x-2) obtained above, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 50 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-3). Next, 61 g of glycerin (so that it becomes 20% by mass with respect to 100% by mass of the resin (A-3) solid content) is added as a softener (C), and the pH is 5 with 15% sulfuric acid and water, and the solid content is 15%. An adjusted crepe adhesive was obtained.
実施例3と同様にして得たポリアミドポリアミン水溶液(x-2)全量にエピクロロヒドリン7.4g(0.08mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度20mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-4)を得た。次いで軟化剤(C)としてグリセリンを58g(樹脂(A-4)固形分100質量%に対して20質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 Example 4
7.4 g (0.08 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-2) obtained in the same manner as in Example 3, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 20 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-4). Next, 58 g of glycerin as a softening agent (C) (20% by mass with respect to 100% by mass of resin (A-4) solid content) was added, and the solid content was adjusted to 15% with water. Got.
実施例3と同様にして得たポリアミドポリアミン水溶液(x-2)全量にエピクロロヒドリン14.8g(0.16mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度510mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-5)を得た。次いで軟化剤(C)としてグリセリンを60g(樹脂(A-5)固形分100質量%に対して20質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 Example 5
14.8 g (0.16 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-2) obtained in the same manner as in Example 3, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 510 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-5). Next, 60 g of glycerin as a softening agent (C) was added (so that the resin (A-5) had a solid content of 20% by mass with respect to 100% by mass), and the solid content was adjusted to 15% with water. Got.
<ポリアミドポリアミンポリ尿素(y-1)の製造>
温度計、還流冷却器、攪拌機、窒素導入管を備えた四つ口丸底フラスコに、ジエチレントリアミン105g(1.02mol)、95%硫酸0.52g(0.005mol)を仕込み、攪拌しながら、アジピン酸146g(1mol)を加え、窒素気流下、生成する水を系外に除去しながら昇温し、175℃で6時間反応させた後、水を徐々に加えて固形分98%に調整した。次いで尿素12g(0.2mol)を加えて125℃で2時間反応させた後、水を徐々に加えて固形分35%に調整し、ポリアミドポリアミンポリ尿素水溶液(y-1)を得た。 Example 6
<Production of polyamide polyamine polyurea (y-1)>
A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 105 g (1.02 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid, and agitated while stirring. 146 g (1 mol) of acid was added, and the temperature was raised while removing the generated water out of the system under a nitrogen stream. After reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 98%. Next, 12 g (0.2 mol) of urea was added and reacted at 125 ° C. for 2 hours, and then water was gradually added to adjust the solid content to 35% to obtain a polyamide polyamine polyurea aqueous solution (y-1).
上記で得られたポリアミドポリアミンポリ尿素水溶液(y-1)全量にエピクロロヒドリン8.3g(0.09mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度95mPa・sに達したところで反応を終了させポリアミドポリアミンポリ尿素・エピクロロヒドリン樹脂(B-1)を得た。次いで軟化剤(C)として、グリセリン59g(樹脂(B-1)固形分100質量%に対して20質量%となるように)を加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 <Manufacture of crepe adhesive>
8.3 g (0.09 mol) of epichlorohydrin was added to the total amount of the polyamidepolyaminepolyurea aqueous solution (y-1) obtained above, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 95 mPa · s, the reaction was terminated to obtain a polyamide polyamine polyurea / epichlorohydrin resin (B-1). . Next, 59 g of glycerin (so that it becomes 20% by mass with respect to 100% by mass of the resin (B-1) solid content) was added as a softening agent (C), and the solid content was adjusted to 15% with water. An agent was obtained.
<ポリアミドポリアミンポリ尿素(y-2)の製造>
温度計、還流冷却器、攪拌機、窒素導入管を備えた四つ口丸底フラスコに、ジエチレントリアミン105g(1.02mol)、95%硫酸0.52g(0.005mol)を仕込み、攪拌しながら、アジピン酸146g(1mol)を加え、窒素気流下、生成する水を系外に除去しながら昇温し、175℃で6時間反応させた後、水を徐々に加えて固形分98%に調整した。次いで尿素24g(0.4mol)を加えて125℃で2時間反応させた後、水を徐々に加えて固形分35%に調整し、ポリアミドポリアミンポリ尿素水溶液(y-2)を得た。 Example 7
<Production of polyamide polyamine polyurea (y-2)>
A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 105 g (1.02 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid, and agitated while stirring. 146 g (1 mol) of acid was added, and the temperature was raised while removing the generated water out of the system under a nitrogen stream. After reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 98%. Next, 24 g (0.4 mol) of urea was added and reacted at 125 ° C. for 2 hours, and then water was gradually added to adjust the solid content to 35% to obtain a polyamide polyamine polyurea aqueous solution (y-2).
上記で得られたポリアミドポリアミンポリ尿素水溶液(y-2)全量にエピクロロヒドリン8.3g(0.09mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度65mPa・sに達したところで反応を終了させポリアミドポリアミンポリ尿素・エピクロロヒドリン樹脂(B-2)を得た。次いでグリセリン60g(樹脂(B-2)固形分100質量%に対して20質量%となるように)を加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 <Manufacture of crepe adhesive>
8.3 g (0.09 mol) of epichlorohydrin was added to the total amount of the polyamidepolyaminepolyurea aqueous solution (y-2) obtained above, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 65 mPa · s, the reaction was terminated to obtain a polyamide polyamine polyurea / epichlorohydrin resin (B-2). . Next, 60 g of glycerin (20% by mass with respect to 100% by mass of resin (B-2) solid content) was added to obtain an adhesive for crepes having a solid content adjusted to 15% with water.
<ポリアミドポリアミン(x-3)の製造>
温度計、還流冷却器、攪拌機、窒素導入管を備えた四つ口丸底フラスコに、ジエチレントリアミン101g(0.98mol)、95%硫酸0.52g(0.005mol)を仕込み、攪拌しながら、アジピン酸146g(1mol)を加え、窒素気流下、生成する水を系外に除去しながら昇温し、175℃で6時間反応させた後、水を徐々に加えて固形分35%に調整し、ポリアミドポリアミン水溶液(x-3)を得た。 Example 8
<Production of polyamide polyamine (x-3)>
A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 101 g (0.98 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid, and agitated with stirring. 146 g (1 mol) of acid was added, the temperature was raised while removing the generated water out of the system under a nitrogen stream, and after reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 35%. A polyamide polyamine aqueous solution (x-3) was obtained.
上記で得られたポリアミドポリアミン水溶液(x-3)全量にエピクロロヒドリン5.6g(0.06mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度60mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-6)を得た。次いでグリセリン56g(樹脂(A-6)固形分100質量%に対して20質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 <Manufacture of crepe adhesive>
5.6 g (0.06 mol) of epichlorohydrin was added to the total amount of the polyamidepolyamine aqueous solution (x-3) obtained above, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 60 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-6). Next, 56 g of glycerin (20% by mass with respect to 100% by mass of the resin (A-6) solid content) was added to obtain an adhesive for crepes having a solid content adjusted to 15% with water.
<ポリアミドポリアミン(x-4)の製造>
温度計、還流冷却器、攪拌機、窒素導入管を備えた四つ口丸底フラスコに、ジエチレントリアミン108g(1.05mol)、95%硫酸0.52g(0.005mol)を仕込み、攪拌しながら、アジピン酸146g(1mol)を加え、窒素気流下、生成する水を系外に除去しながら昇温し、175℃で6時間反応させた後、水を徐々に加えて固形分35%に調整し、ポリアミドポリアミン水溶液(x-4)を得た。 Example 9
<Production of polyamide polyamine (x-4)>
A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 108 g (1.05 mol) of diethylenetriamine and 0.52 g (0.005 mol) of 95% sulfuric acid and stirred with adipine. 146 g (1 mol) of acid was added, the temperature was raised while removing the generated water out of the system under a nitrogen stream, and after reacting at 175 ° C. for 6 hours, water was gradually added to adjust the solid content to 35%. A polyamide polyamine aqueous solution (x-4) was obtained.
上記で得られたポリアミドポリアミン水溶液(x-4)全量にエピクロロヒドリン11.1g(0.12mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度60mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-7)を得た。次いで軟化剤(C)としてグリセリン59g(樹脂(A-7)固形分100質量%に対して20質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 <Manufacture of crepe adhesive>
Epichlorohydrin 11.1 g (0.12 mol) was added to the total amount of the polyamidepolyamine aqueous solution (x-4) obtained above, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 60 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-7). Next, 59 g of glycerin (so that the resin (A-7) solid content is 20% by mass) is added as a softening agent (C), and a crepe adhesive whose solid content is adjusted to 15% with water is added. Obtained.
実施例9と同様にして得たポリアミドポリアミン水溶液(x-4)全量にエピクロロヒドリン11.1g(0.12mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度80mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-8)を得た。次いで軟化剤(C)としてプロピレングリコール59g(樹脂(A-8)固形分100質量%に対して20質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 Example 10
11.1 g (0.12 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 80 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-8). Next, 59 g of propylene glycol (20% by mass with respect to 100% by mass of resin (A-8) solid content) was added as a softening agent (C), and the solid content was adjusted to 15% with water. Got.
実施例9と同様にして得たポリアミドポリアミン水溶液(x-4)全量にエピクロロヒドリン11.1g(0.12mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度80mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-9)を得た。次いで軟化剤(C)として、ポリエチレングリコール(重合度200)59g(樹脂(A-9)固形分100質量%に対して20質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 Example 11
11.1 g (0.12 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 80 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-9). Next, 59 g of polyethylene glycol (degree of polymerization: 200) is added as a softening agent (C) (20% by mass with respect to 100% by mass of resin (A-9) solid content), and the solid content is made 15% with water. An adjusted crepe adhesive was obtained.
実施例9と同様にして得たポリアミドポリアミン水溶液(x-4)全量にエピクロロヒドリン11.1g(0.12mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度80mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-10)を得た。次いで軟化剤(C)としてジエチレングリコールジメチルエーテル59g(樹脂(A-10)固形分100質量%に対して20質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 Example 12
11.1 g (0.12 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 80 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-10). Next, 59 g of diethylene glycol dimethyl ether (so as to be 20% by mass with respect to 100% by mass of the resin (A-10) solid content) was added as a softening agent (C), and the solid content was adjusted to 15% with water. Got.
実施例9と同様にして得たポリアミドポリアミン水溶液(x-4)全量にエピクロロヒドリン11.1g(0.12mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度80mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-11)を得た。次いで軟化剤(C)としてトリエチレングリコールジメチルエーテル59g(樹脂(A-11)固形分100質量%に対して20質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 Example 13
11.1 g (0.12 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 80 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-11). Next, 59 g of triethylene glycol dimethyl ether (20% by mass with respect to 100% by mass of resin (A-11) solid content) was added as a softening agent (C), and the solid content was adjusted to 15% with water. An adhesive was obtained.
実施例1と同様にして得たポリアミドポリアミン水溶液(x-1)全量にエピクロロヒドリン37g(0.4mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度100mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-12)を得た。次いで軟化剤(C)として、プロピレングリコール64g(樹脂(A-12)固形分100質量%に対して20質量%となるように)加えて、15%硫酸と水を加えてpHを3.2、固形分を15%に調整したクレープ用接着剤を得た。 Comparative Example 1 (when the amount of AZR in the crepe adhesive is too large and out of range)
Epichlorohydrin (37 g, 0.4 mol) was added to the total amount of the polyamide polyamine aqueous solution (x-1) obtained in the same manner as in Example 1, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 100 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-12). Next, as a softener (C), 64 g of propylene glycol (20% by mass with respect to 100% by mass of resin (A-12) solid content) was added, and 15% sulfuric acid and water were added to adjust the pH to 3.2. A crepe adhesive having a solid content adjusted to 15% was obtained.
<ポリアミドポリアミンポリ尿素(y-3)の製造>
温度計、還流冷却器、攪拌機、窒素導入管を備えた四つ口丸底フラスコに、ジエチレントリアミン105.3g(1.02モル)を仕込み、攪拌しながらアジピン酸146.1g(1モル)を加え、生成する水を系外に除去しながら昇温し、170℃で3時間反応を行った。次いで、反応液を130℃まで冷却し、尿素12g(0.2モル)を加えて同温度で2時間脱アンモニア反応を行った後、水を徐々に加えて固形分50%のポリアミドポリアミンポリ尿素水溶液(y―3)を450g得た。 Comparative Example 2 (corresponding to Example 1 of the prior art, Japanese Patent No. 483523)
<Production of polyamide polyamine polyurea (y-3)>
A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and nitrogen inlet tube was charged with 105.3 g (1.02 mol) of diethylenetriamine, and 146.1 g (1 mol) of adipic acid was added with stirring. The temperature was raised while removing the generated water out of the system, and the reaction was carried out at 170 ° C. for 3 hours. Next, the reaction solution was cooled to 130 ° C., 12 g (0.2 mol) of urea was added, and deammonia reaction was performed at the same temperature for 2 hours, and then water was gradually added to polyamide polyamine polyurea having a solid content of 50%. 450 g of an aqueous solution (y-3) was obtained.
温度計、還流冷却器、撹拌機及び滴下ロートを備えた四つ口丸底フラスコに、ポリアミドポリアミンポリ尿素水溶液(y-3)200gを仕込み、20℃でエピクロロヒドリン5.5g(樹脂Bの組成比としてアジピン酸1モルに対して0.13モルのエピクロロヒドリンに相当)を加えた後、30℃に加熱して10分間同温度で保持しポリアミドポリアミンポリ尿素・エピクロロヒドリン樹脂(B-3)を得た。次いで、水122gを加えて、50℃まで加熱して粘度が200mPa・s(25℃)に到達するまで同温度で保持した後、30%硫酸と水を加えてpHを6、固形分を15%に調整したクレープ用接着剤を得た。 <Manufacture of crepe adhesive>
A four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer and dropping funnel was charged with 200 g of polyamide polyamine polyurea aqueous solution (y-3), and 5.5 g of epichlorohydrin (resin B) at 20 ° C. The composition ratio of 0.13 mol of epichlorohydrin to 1 mol of adipic acid was added, and then heated to 30 ° C. and kept at the same temperature for 10 minutes. Polyamide polyamine polyurea / epichlorohydrin Resin (B-3) was obtained. Next, 122 g of water was added and heated to 50 ° C. and maintained at the same temperature until the viscosity reached 200 mPa · s (25 ° C.), then 30% sulfuric acid and water were added to adjust the pH to 6 and the solid content to 15 % Of crepe adhesive was obtained.
温度計、冷却器、撹拌機を備えた四つ口丸底フラスコに、ジエチレントリアミンを108.2g(1.05モル)、アジピン酸146.1g(1.00モル)、水146.1gを仕込み、160~170℃にて脱水反応を6時間行い、ポリアミドポリアミン水溶液を得た。これに水を加えて50%ポリアミドポリアミン水溶液(x-5)を440g得た。次に、温度計、冷却器、撹拌機を備えた四つ口フラスコに、上記ポリアミドポリアミン水溶液(x-5)を112.5gと水241.0gを仕込み、さらに、エピクロルヒドリン10.5g(樹脂Aの組成比としてアジピン酸1モルに対して0.44モルのエピクロロヒドリンに相当)を投入した。その後、50℃に昇温し、12時間保持しポリアミドポリアミン・エピクロロヒドリン樹脂(A-13)を得た。次いで同温で98%硫酸1.0g(0.01モル)を加え、水で固形分を15%に調整したクレープ用接着剤を得た。 Comparative Example 3 (corresponding to Example 1 of Japanese Patent No. 591046, which is a prior art)
A four-necked round bottom flask equipped with a thermometer, a condenser, and a stirrer was charged with 108.2 g (1.05 mol) of diethylenetriamine, 146.1 g (1.00 mol) of adipic acid, and 146.1 g of water. A dehydration reaction was performed at 160 to 170 ° C. for 6 hours to obtain a polyamide polyamine aqueous solution. Water was added thereto to obtain 440 g of a 50% polyamide polyamine aqueous solution (x-5). Next, 112.5 g of the polyamide polyamine aqueous solution (x-5) and 241.0 g of water were charged into a four-necked flask equipped with a thermometer, a cooler, and a stirrer, and 10.5 g of epichlorohydrin (resin A The composition ratio was 0.44 mol of epichlorohydrin per mol of adipic acid). Thereafter, the temperature was raised to 50 ° C. and maintained for 12 hours to obtain a polyamide polyamine / epichlorohydrin resin (A-13). Next, 1.0 g (0.01 mol) of 98% sulfuric acid was added at the same temperature to obtain a crepe adhesive whose solid content was adjusted to 15% with water.
実施例9と同様にして得たポリアミドポリアミン水溶液(x-4)全量にエピクロロヒドリン3.7g(0.04mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度45mPa・sに達したところで反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-14)を得た。次いで、プロピレングリコールを57g(樹脂(A-14)固形分100質量%に対して20質量%となるように)加えて、水で固形分を15%に調整したクレープ用接着剤を得た。 Comparative Example 4 (when the intrinsic viscosity of the crepe adhesive is low and out of range)
To the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, 3.7 g (0.04 mol) of epichlorohydrin was added, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%, the temperature was raised to 70 ° C., and when the viscosity reached 45 mPa · s, the reaction was terminated to obtain a polyamide polyamine / epichlorohydrin resin (A-14). Next, 57 g of propylene glycol (20% by mass with respect to 100% by mass of resin (A-14) solid content) was added to obtain an adhesive for crepe having a solid content adjusted to 15% with water.
実施例9と同様にして得たポリアミドポリアミン水溶液(x-4)全量にエピクロロヒドリン7.4g(0.08mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度45mPa・sに達したところで98%硫酸10.8gを加えて反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-15)を得た。次いで、プロピレングリコールを58g(樹脂(A-15)固形分100質量%に対して20質量%となるように)加えて、15%硫酸と水でpH5、固形分を15%に調整したクレープ用接着剤を得た。 Comparative Example 5 (when the water resistance evaluation value of the crepe adhesive is out of range)
7.4 g (0.08 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%. After the temperature was raised to 70 ° C., when the viscosity reached 45 mPa · s, 10.8 g of 98% sulfuric acid was added to terminate the reaction, and the polyamide polyamine / epichlorohydrin resin ( A-15) was obtained. Next, 58 g of propylene glycol (20% by mass with respect to 100% by mass of resin (A-15) solid content) was added, and the pH was adjusted to 15% with 15% sulfuric acid and water, and the solid content was adjusted to 15%. An adhesive was obtained.
実施例9と同様にして得たポリアミドポリアミン水溶液(x-4)全量にエピクロロヒドリン14.8g(0.16mol)を加え、30℃に昇温して1時間同温度で保温した。次いで、水を加えて固形分を15%とし、70℃に昇温後、粘度640mPa・sに達したところで98%硫酸10.8gを加えて反応を終了させポリアミドポリアミン・エピクロロヒドリン樹脂(A-16)を得た。
次いで、プロピレングリコールを59g(樹脂(A-16)固形分100質量%に対して20質量%となるように)加えて、15%硫酸と水でpH5、固形分を15%に調整したクレープ用接着剤を得た。 Comparative Example 6 (when the intrinsic viscosity of the crepe adhesive is high and out of range)
14.8 g (0.16 mol) of epichlorohydrin was added to the total amount of the polyamide polyamine aqueous solution (x-4) obtained in the same manner as in Example 9, and the temperature was raised to 30 ° C. and kept at the same temperature for 1 hour. Next, water was added to adjust the solid content to 15%. After the temperature was raised to 70 ° C., when the viscosity reached 640 mPa · s, 10.8 g of 98% sulfuric acid was added to terminate the reaction, and the polyamide polyamine / epichlorohydrin resin ( A-16) was obtained.
Next, 59 g of propylene glycol (20% by mass with respect to 100% by mass of resin (A-16) solid content) was added, and the pH was adjusted to 15% with 15% sulfuric acid and water, and the solid content was adjusted to 15%. An adhesive was obtained.
温度計、還流冷却器、攪拌機、滴下ロートを備えた3L四つ口丸底フラスコに、ポリアルキレンポリアミン類としてジエチレントリアミン103g(1mol)、炭素数6~24のモノカルボン酸類としてヤシ油オレイン酸{オレイン酸/リノール酸/パルミチン酸(混合質量比70/20/10)}559g(2mol)を徐々に加えた。180℃まで昇温し、生成する水を系外に除去しながら3時間反応させてアミド化合物を得た。得られたアミド化合物の残存アミノ基量は2mmol/gであった。
次いで、上記アミド化合物100g(アミノ基として0.16mol)とポリオキシエチレン(45)ステアリルアミン(カッコ内の数値はポリオキシエチレンの平均付加モル数を示す。)5gと水100gとエピハロヒドリン類としてエピクロロヒドリン5.9g(0.064mol)を50℃で加えて30分間撹拌した。続いて反応液を70℃にして1時間反応させた後、反応液を冷却しながら、固形分が30質量%になるように水を加えて調整し、濃度30%、粘度350mPa・s、融点29℃、粒子径4μmの紙用柔軟剤を得た。 Synthesis Example 1 (Production Example of Softening Agent Corresponding to Fatty Acid Amide Epihalohydrin (S1))
In a 3 L four-necked round bottom flask equipped with a thermometer, reflux condenser, stirrer, and dropping funnel, 103 g (1 mol) of diethylenetriamine as a polyalkylene polyamine, and coconut oil oleic acid {olein as a monocarboxylic acid having 6 to 24 carbon atoms 559 g (2 mol) of acid / linoleic acid / palmitic acid (mixing mass ratio 70/20/10)} was gradually added. The temperature was raised to 180 ° C., and reaction was performed for 3 hours while removing generated water out of the system to obtain an amide compound. The amount of residual amino groups of the obtained amide compound was 2 mmol / g.
Next, 100 g of the amide compound (0.16 mol as an amino group), 5 g of polyoxyethylene (45) stearylamine (the numbers in parentheses indicate the average number of moles added of polyoxyethylene), 100 g of water, and epihalohydrins as epihalohydrins. Chlorohydrin (5.9 g, 0.064 mol) was added at 50 ° C., and the mixture was stirred for 30 minutes. Subsequently, after the reaction solution was reacted at 70 ° C. for 1 hour, the reaction solution was cooled and adjusted by adding water so that the solid content was 30% by mass. The concentration was 30%, the viscosity was 350 mPa · s, the melting point. A paper softening agent having a particle size of 4 μm was obtained at 29 ° C.
本発明におけるクレープ用接着剤の重量平均分子量は、GPCに多角度光散乱検出器を接続したGPC-MALS法により以下の測定条件によって得られたものである。
GPC本体:アジレント・テクノロジー社製
LC1100シリーズカラム:昭和電工(株)製 SHODEX SB806M HQ
溶離液:N/10硝酸ナトリウムを含むN/15リン酸緩衝液 (pH3)
検出器1:ワイアットテクノロジー社製多角度光散乱検出器DAWN
検出器2:昭和電工(株)製示唆屈折率検出器RI-101 <Measurement of molecular weight>
The weight average molecular weight of the crepe adhesive in the present invention is obtained by the GPC-MALS method in which a multi-angle light scattering detector is connected to GPC under the following measurement conditions.
GPC body: LC1100 series manufactured by Agilent Technologies Inc. Column: SHODEX SB806M HQ manufactured by Showa Denko KK
Eluent: N / 10 phosphate buffer (pH 3) containing N / 10 sodium nitrate
Detector 1: Multi-angle light scattering detector DAWN manufactured by Wyatt Technology
Detector 2: Suggested refractive index detector RI-101 manufactured by Showa Denko KK
実施例におけるクレープ用接着剤の固形分濃度1%、0.5%、0.2%の1N塩化アンモニウム水溶液についてウベローデ粘度計を使用し、測定温度25℃での還元比粘度ηsp/Cを求め、固有粘度[η]を求めた。
ηsp/C=[η]+k’[η]2×C
ここでC は濃度,[η]は固有粘度,k’ はハギンス定数 <Measurement of intrinsic viscosity>
The reduced specific viscosity η sp / C at a measurement temperature of 25 ° C. was measured using an Ubbelohde viscometer for 1N ammonium chloride aqueous solutions having a solid content concentration of 1%, 0.5%, and 0.2% of the adhesive for crepe in the examples. The intrinsic viscosity [η] was determined.
η sp / C = [η] + k ′ [η] 2 × C
Where C is the concentration, [η] is the intrinsic viscosity, and k ′ is the Huggins constant.
クレープ用接着剤に既知量のメタノールを加えた試料の1HNMRを測定し、メタノールとAZRのプロトン比からAZR量を求めた。なおクレープ用接着剤の固形分1gに対しメタノールを0.01g加えたものを試料とした。 <Measurement of AZR content>
1 HNMR of a sample obtained by adding a known amount of methanol to the crepe adhesive was measured, and the AZR amount was determined from the proton ratio of methanol and AZR. A sample obtained by adding 0.01 g of methanol to 1 g of the solid content of the crepe adhesive was used.
ティーバッグ(重さW2(g))に、均一な皮膜の重さが0.05gとなるように調製したシャーレ(重さW1(g))を50℃の水中に攪拌下、5分間浸漬し、乾燥させ、前記シャーレの重さをティーバッグごと(重さW3(g))に測定し、下式(1)より耐水性を算出する。
式(1) 耐水性(%)=100-{(W1+W2)-W3}/0.05×100
W1(g):皮膜調製した金属シャーレの重さ、W2(g):ティーバッグの重さ、W3(g):浸漬・乾燥後のティーバッグとシャーレの重さ <Water resistance>
In a tea bag (weight W2 (g)), a petri dish (weight W1 (g)) prepared so as to have a uniform film weight of 0.05 g was immersed in water at 50 ° C. for 5 minutes with stirring. Then, the petri dish is dried, the weight of the petri dish is measured for each tea bag (weight W3 (g)), and water resistance is calculated from the following formula (1).
Formula (1) Water resistance (%) = 100 − {(W1 + W2) −W3} /0.05×100
W1 (g): Weight of the metal petri dish prepared as a film, W2 (g): Weight of the tea bag, W3 (g): Weight of the tea bag and the petri dish after soaking and drying
実施例1~13、比較例1~6のクレープ用接着剤を固形分として0.3g/m2、クレープ剤CR6154(星光PMC株式会社製・クレープ用剥離剤)を有効成分0.25g/m2となるように、100℃に加熱したプレート(面積0.2cm2)に塗布し1分間乾燥後、塗布面を300gf/cm2となるようにプレートと2μLの水を滴下した半紙(坪量30g/m2、厚さ0.07mm、5μLドロップサイズ12秒)に押し付け、引き剥がす際に必要な荷重をプローブタック試験機で評価した。評価結果を表1、2に示す。
なお、接着強度は数値が高いほど好ましい。また、本試験は、クレープ用接着剤をドライヤーに塗布した場合と同様の傾向を得ることが簡易でできるため採用している。 <Evaluation test of adhesive strength>
The crepe adhesives of Examples 1 to 13 and Comparative Examples 1 to 6 were 0.3 g / m 2 as a solid content, and the crepe agent CR6154 (manufactured by Seiko PMC Co., Ltd., crepe release agent) as an active ingredient 0.25 g / m 2 and coated on a plate heated to 100 ° C. (area 0.2 cm 2 ), dried for 1 minute, and then a half paper (basis weight) on which 2 μL of water was dropped to the plate so that the coated surface was 300 gf / cm 2 30 g / m 2 , thickness 0.07 mm, 5 μL drop size 12 seconds), and the load required for peeling was evaluated with a probe tack tester. The evaluation results are shown in Tables 1 and 2.
In addition, it is preferable that the adhesive strength is higher. This test is adopted because it is easy to obtain the same tendency as when the crepe adhesive is applied to a dryer.
実施例1~13、比較例1~6のクレープ用接着剤固形分0.13g分を内径6.5cmの金属シャーレに取り、加熱乾燥(110℃、2時間)させてクレープ用接着剤の皮膜を調製した。鉛筆は芯の硬い6H、5H、4H、3H、2H、H、F、HB、B、2B、3B、4B、5B、6Bの順で調製した皮膜を引掻き、傷跡がつかない鉛筆の硬度を評価した。6Hで傷つかないものを15とし、順に芯の軟らかい鉛筆で引掻いて6Bで傷つかないものを2とし、6Bで傷がつくものを1とした。数値が低いほうが「やわらかい」とし、15段階で評価した。評価結果を表1、2に示す。
<軟らかい> 1 ← 2(6B) ← 7(B) → 15(6H)<硬い>
( )内は数値の対象となる傷跡がつかない鉛筆の硬度を示す
なお、数値が低いほうがブレードの摩耗が少なく好ましく、6以下が好適である。
また、本試験は、クレープ用接着剤をドライヤーに塗布した場合と同様の傾向を得ることが簡易でできるため採用している。 <Method for evaluating film hardness>
The solid content of 0.13 g of the crepe adhesive in Examples 1 to 13 and Comparative Examples 1 to 6 was placed in a metal petri dish having an inner diameter of 6.5 cm and dried by heating (110 ° C., 2 hours) to form a crepe adhesive film. Was prepared. The pencil is scratched with a hard core 6H, 5H, 4H, 3H, 2H, H, F, HB, B, 2B, 3B, 4B, 5B, 6B in order, and the hardness of the pencil with no scars is evaluated. did. Those that were not damaged by 6H were set to 15, those that were not damaged by 6B by scratching with a soft pencil in order were set to 2, and those that were damaged by 6B were set to 1. The lower the numerical value, the softer it was, and it was rated on a 15-point scale. The evaluation results are shown in Tables 1 and 2.
<Soft> 1 ← 2 (6B) ← 7 (B) → 15 (6H) <Hard>
Figures in parentheses indicate the hardness of pencils that do not have scars that are subject to numerical values.
A lower numerical value is preferable because there is less abrasion of the blade, and 6 or less is preferable.
This test is adopted because it is easy to obtain the same tendency as when the crepe adhesive is applied to a dryer.
クレープ用接着剤を内添した手抄き紙の湿潤裂断長を測定することで、クレープ用接着剤の水解性を簡便に評価することができる。晒クラフトパルプ(広葉樹/針葉樹=9/1)を叩解度(CSF)400に調整した濃度2.4質量%の紙料に、実施例1~13、比較例1~6で調製したクレープ用接着剤を対パルプ固形分当たり0.1質量%になるように添加した。撹拌の後、角型シートマシンにて抄紙して、坪量65g/m2の手抄き紙を得た。得られた手抄き紙の湿潤裂断長を表3、4に示す。湿潤裂断長の数値が大きいほど、水解性が悪くなるため、数値が小さいほど好ましい。なお、本評価を離解性という。
湿潤裂断長: JIS P8135に準拠 <Preparation of handmade paper and evaluation results of paper quality>
By measuring the wet tear length of the handmade paper internally added with the crepe adhesive, the water disintegrability of the crepe adhesive can be easily evaluated. Adhesion for crepes prepared in Examples 1 to 13 and Comparative Examples 1 to 6 on a paper stock having a concentration of 2.4% by mass adjusted to a beating degree (CSF) of bleached kraft pulp (hardwood / conifer = 9/1) The agent was added so that it might become 0.1 mass% with respect to pulp solid content. After stirring, the paper was made with a square sheet machine to obtain handmade paper with a basis weight of 65 g / m 2 . The wet tear lengths of the obtained handmade paper are shown in Tables 3 and 4. The larger the value of the wet tear length, the worse the water disintegrability, so the smaller the value, the better. This evaluation is called disaggregation.
Wet tear length: according to JIS P8135
ヤング率:野村商事製 配向性測定器SST-2500により超音波伝播速度 Vを測定し、下記式よりヤング率を求めた。数値が低いほど紙が柔軟になったことを示す。柔軟剤無添加の紙のヤング率を100として相対表記した。
ヤング率∝ρV2 (ρ:密度) After adding 0.1% by mass of the crepe adhesive described in Table 5 to the solid content of pulp, 0.3% by mass of the various softening agents described in Table 5 were added to the above handmade paper. In the same manner, hand-made paper was obtained. Table 5 shows the Young's modulus of the obtained handmade paper.
Young's modulus: Ultrasonic wave propagation velocity V was measured with an orientation measuring instrument SST-2500 manufactured by Nomura Corporation, and the Young's modulus was obtained from the following formula. The lower the number, the more flexible the paper. Relative notation was made assuming that the Young's modulus of the paper without the softener was 100.
Young's modulus ∝ρV 2 (ρ: density)
柔軟剤2・・・柔軟剤(S2)に相当するジオレイルジメチルアンモニウムクロライド
Softener 2 ... Dioleyldimethylammonium chloride equivalent to softener (S2)
表1~4から実施例と比較例2及び3を対比することで先行技術に比べ、本願発明の実施例は、離解性及び接着強度が良好であり、更に先行技術よりも皮膜表面が柔らかいことがわかる。
表1~4から実施例と比較例4を対比することで、クレープ用接着剤の固有粘度が低く本発明の範囲外である場合に比べ、本願発明の実施例は、離解性及び接着強度が良好であることがわかる。
表1~4から実施例と比較例5を対比することで、クレープ用接着剤の耐水性評価値が本発明の範囲外である場合に比べ、本願発明の実施例は、離解性及び接着強度が良好であり、更に比較例5よりも皮膜表面がやわらかいことがわかる。
表1~4から実施例と比較例6を対比することでクレープ用接着剤の固有粘度が高く、本発明の範囲外である場合に比べ、本願発明の実施例は離解性及び接着強度が良好であり、更に比較例6よりも皮膜表面がやわらかいことがわかる。
表1~4から実施例1と実施例2以外の実施例を対比することで分子量が100万~500万であることが、接着強度が良好であり、好ましいことがわかる。
By comparing Examples and Comparative Example 1 from Tables 1 to 4, compared to the case where the amount of AZR of the crepe adhesive is outside the scope of the present invention, the Examples of the present invention have a disaggregation property and adhesive strength. It is clear that the film surface is softer than that of Comparative Example 1.
By comparing Examples and Comparative Examples 2 and 3 from Tables 1 to 4, the examples of the present invention have better disaggregation and adhesive strength than the prior art, and the coating surface is softer than the prior art. I understand.
By comparing Examples and Comparative Example 4 from Tables 1 to 4, the examples of the present invention have higher disaggregation and adhesive strength than the case where the intrinsic viscosity of the crepe adhesive is low and outside the scope of the present invention. It turns out that it is favorable.
By comparing Examples and Comparative Example 5 from Tables 1 to 4, compared to the case where the water resistance evaluation value of the crepe adhesive is out of the range of the present invention, the examples of the present invention have a disaggregation property and an adhesive strength. It can be seen that the film surface is softer than that of Comparative Example 5.
By comparing Examples and Comparative Example 6 from Tables 1 to 4, the inherent viscosity of the crepe adhesive is high, and the examples of the present invention have better disaggregation and adhesive strength than those outside the scope of the present invention. Further, it can be seen that the surface of the film is softer than Comparative Example 6.
From Tables 1 to 4, it can be seen that a molecular weight of 1,000,000 to 5,000,000 is good and preferable by comparing Examples 1 and 2 other than Example 2.
Claims (4)
- ポリアミドポリアミン・エピハロヒドリン樹脂(A)および/またはポリアミドポリアミンポリ尿素・エピハロヒドリン樹脂(B)並びに軟化剤(C)を含有するクレープ用接着剤であって、下記(1)~(5)の条件を全て満たすことを特徴とするクレープ用接着剤。
(1)クレープ用接着剤の固形分1g中のアゼチジニウム基の含有量が0~0.2mEq
(2)クレープ用接着剤の固有粘度が0.20~0.55dL/g
(3)軟化剤(C)が、以下の(i)及び(ii)を満たすものであること
(i)沸点150℃以上でかつ80℃で液体、
(ii)水溶性脂肪族ポリオールまたはポリエチレングリコールジメチルエーテル
(4)質量比で[樹脂(A)および/または樹脂(B)]:[軟化剤(C)]=100:0.5~70
(5)下記の算出方法によって評価される耐水性が40~100%
<耐水性の算出方法>
ティーバッグ(重さW2(g))に、均一な皮膜の重さが0.05gとなるように調製したシャーレ(重さW1(g))を50℃の水中に攪拌下、5分間浸漬し、乾燥させ、前記シャーレの重さをティーバッグごと(重さW3(g))測定し、下式(1)より耐水性を算出する。
式(1) 耐水性(%)=100-{(W1+W2)-W3}/0.05×100
W1(g):皮膜調製した金属シャーレの重さ、W2(g):ティーバッグの重さ、W3(g):浸漬・乾燥後のティーバッグとシャーレの重さ A crepe adhesive comprising a polyamide polyamine / epihalohydrin resin (A) and / or a polyamide polyamine / polyurea / epihalohydrin resin (B) and a softening agent (C), all of the following conditions (1) to (5): A crepe adhesive characterized by filling.
(1) Content of azetidinium group in 1 g of solid content of crepe adhesive is 0 to 0.2 mEq
(2) The intrinsic viscosity of the crepe adhesive is 0.20 to 0.55 dL / g.
(3) The softener (C) satisfies the following (i) and (ii): (i) a liquid having a boiling point of 150 ° C or higher and 80 ° C;
(Ii) Water-soluble aliphatic polyol or polyethylene glycol dimethyl ether (4) [resin (A) and / or resin (B)]: [softener (C)] = 100: 0.5 to 70 in mass ratio
(5) Water resistance evaluated by the following calculation method is 40 to 100%
<Calculation method of water resistance>
In a tea bag (weight W2 (g)), a petri dish (weight W1 (g)) prepared so as to have a uniform film weight of 0.05 g was immersed in water at 50 ° C. for 5 minutes with stirring. Then, the petri dish is weighed and measured for each tea bag (weight W3 (g)), and water resistance is calculated from the following equation (1).
Formula (1) Water resistance (%) = 100 − {(W1 + W2) −W3} /0.05×100
W1 (g): Weight of the metal petri dish prepared as a film, W2 (g): Weight of the tea bag, W3 (g): Weight of the tea bag and the petri dish after soaking and drying - クレープ用接着剤の重量平均分子量が100万~500万であることを特徴とする請求項1に記載のクレープ用接着剤。 The crepe adhesive according to claim 1, wherein the crepe adhesive has a weight average molecular weight of 1,000,000 to 5,000,000.
- クレープ紙の製造方法であって、前記請求項1又は2に記載されたクレープ用接着剤をドライヤー表面に、繊維ウェブの面積に対して固形分あたり0.01~500mg/m2になるように塗布する工程を含む、クレープ紙の製造方法。 A method for producing a crepe paper, wherein the crepe adhesive according to claim 1 or 2 is applied to a dryer surface such that the amount of the crepe adhesive is 0.01 to 500 mg / m 2 per solid content relative to the area of the fiber web. A method for producing crepe paper, comprising a step of applying.
- 内添薬品として柔軟剤を用い、紙が衛生用紙であることを特徴とする請求項3に記載のクレープ紙の製造方法。
4. The method for producing crepe paper according to claim 3, wherein a softener is used as the internal chemical and the paper is sanitary paper.
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JP2018528279A (en) * | 2015-06-25 | 2018-09-27 | エコラブ ユーエスエイ インク | Crepe processing adhesive containing functional cross-linked resin |
CN108859503A (en) * | 2018-08-10 | 2018-11-23 | 青岛理工大学 | Waste paper recycling pencil process units |
JP2020033672A (en) * | 2018-08-30 | 2020-03-05 | 星光Pmc株式会社 | Manufacturing method of adhesive for crepe and crepe paper |
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JP7172292B2 (en) | 2018-08-30 | 2022-11-16 | 星光Pmc株式会社 | Crepe adhesive and method for producing crepe paper |
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JPWO2015016350A1 (en) | 2017-03-02 |
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