WO2004020736A1 - 紙質向上剤 - Google Patents
紙質向上剤 Download PDFInfo
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- WO2004020736A1 WO2004020736A1 PCT/JP2003/010867 JP0310867W WO2004020736A1 WO 2004020736 A1 WO2004020736 A1 WO 2004020736A1 JP 0310867 W JP0310867 W JP 0310867W WO 2004020736 A1 WO2004020736 A1 WO 2004020736A1
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- paper quality
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- pulp
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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
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/71—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes
- D21H17/72—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes of organic material
-
- 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
- D21H21/22—Agents rendering paper porous, absorbent or bulky
-
- 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
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/28—Starch
- D21H17/29—Starch cationic
-
- 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
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
-
- 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
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
- D21H17/44—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups cationic
Definitions
- the present invention relates to an additive for internal addition useful for improving the paper quality of a pulp sheet.
- the thickness of paper has been reduced due to the reduction of paper weight, the speed of papermaking, and the increased blending of deinked pulp for the purpose of reducing the burden on the environment and reducing transportation costs. While bulky paper is desired, the stiffness of paper is proportional to the cube of its thickness, so a decrease in paper thickness causes a decrease in stiffness.
- the stiffness of paper greatly affects the sense of quality, the operability during papermaking and printing, and the durability of boxes and the like, and the decrease in stiffness gives a low-grade feeling, paper jams during operation and swelling of boxes and the like. cause.
- Techniques for improving stiffness include (1) increasing the unit pulp weight (basis weight), (2) using a paper strength agent, etc., but the required pulp amount increases in (1). (2) is that the paper strength (the resistance to paper tear) is improved and the stiffness is improved to some extent, but it does not reach a satisfactory level.
- Japanese Patent Application Laid-Open No. 8-170296 discloses a paper for a paper comprising polymer particles of a vinyl monomer or a gen-based monomer using a cationic polyvinyl alcohol having a mercapto group as a dispersant as an internal additive for paper.
- JP-A-11-309292 discloses a starch particle form without gelatinizing starch.
- Patent Document 1 discloses a papermaking additive mainly containing a grafted starch obtained by graft copolymerizing a monomer containing (meth) acrylamide while maintaining the stiffness. Although the improvement was to some degree, it was still insufficient.
- 2971-4747 discloses an ester compound of a polyhydric alcohol and a fatty acid
- Patent No. 32833248 discloses a water separation degree. Paper quality improvers have been disclosed that improve the bulk, whiteness, and opacity by at least 4%, but improvement in rigidity is also desired.
- An object of the present invention is to provide an internally-added paper quality improver that improves the stiffness, bulk, and the like of a pulp sheet.
- it is to provide an internally added paper quality improver useful as a stiffness improver.
- the present invention relates to an internal paper quality improver comprising a polymer emulsion containing a natural cationic polymer (A) and a polymer particle (B) containing at least a structural unit derived from a vinyl monomer.
- the present invention also relates to a pulp sheet in which the above-mentioned paper quality improver for internal addition of the present invention is present on the surface and / or inside of the pulp sheet.
- the present invention also relates to a method for improving the paper quality of a pulp sheet, wherein the pulp is brought into contact with the internal paper quality improving agent of the present invention.
- the present invention provides a method for improving the paper quality of a pulp sheet, which comprises adding the above-mentioned internally added paper quality improving agent to the pulp slurry during papermaking. Further, the present invention also provides use of the above-mentioned internal paper quality improver as a stiffness improver.
- the present invention relates to a synthetic cationic polymer ( ⁇ ′) having an aqueous solution (7% by weight) having a viscosity of 20 mPa * s (50 ° C.) or more and a nitrogen content of 1.0% by weight or less, and a vinyl monomer.
- the present invention relates to an internally-added paper quality improver comprising a polymer emulsion containing polymer particles (B) having a glass transition temperature (Tg) of 90 ° C. or less having structural units of one origin.
- the present invention contains a natural cationic polymer (A) or a synthetic cationic polymer ( ⁇ ′) and at least a constituent unit derived from a vinyl monomer, and has a glass transition temperature (Tg) of 90 ° C. or less.
- the present invention relates to an internally added paper quality improver comprising a polymer emulsion containing polymer particles (B).
- the synthetic cationic polymer ( ⁇ ′) includes a synthetic cationic polymer having an aqueous solution (7% by weight) viscosity of 20 mPa ′ s (50 ° C.) or more and a nitrogen content of 1.0% by weight or less.
- the internally added paper quality improver of the present invention comprises an emulsion containing a natural cationic polymer (A) and polymer fine particles (B) containing at least a constitutional unit derived from a vinyl monomer.
- A natural cationic polymer
- B polymer fine particles
- the internally added paper quality improver of the present invention has the effect of improving rigidity. Is remarkable, it is preferable to use it for the purpose of improving rigidity.
- the internally added paper quality improver of the present invention is a synthetic cation having an aqueous solution (7% by weight) viscosity of 20 mPa's (50 ° C.) or more and a nitrogen content of 1.0% by weight or less.
- Internal paper quality improvement consisting of a polymer emulsion containing a conductive polymer ( ⁇ ') and polymer particles having a structural unit derived from a vinyl monomer and having a glass transition temperature ( ⁇ g) of 90 ° C or less. Consisting of agents. Even if it is a synthetic polymer, if it has a specific substance value, it is considered to have a strong affinity with pulp.
- the natural cationic polymer (A) used in the present invention is a polymer obtained by extracting or purifying natural products from a natural product and a polymer obtained by chemically modifying the polymer. Those having a glucose residue in the polymer skeleton (starch residue, cellulose residue, etc.) are preferred. For example, cationic starch or cationic cellulose (particularly those which are water-soluble and whose cationic group is a quaternary ammonium cationic group) And the like. One or more may be used alone, or a mixture of two or more may be used.
- the cationic groups include those in which an ammonium group or an amino group is neutralized with an acid.
- it includes those neutralized with hydrochloric acid, sulfuric acid, nitric acid, acetic acid, formic acid, maleic acid, fumaric acid, citric acid, tartaric acid, adipic acid, lactic acid and the like.
- cationic starch or the cationic cellulose for example, those represented by the following formula (1) are preferable.
- A starch residue or cellulose residue
- R an alkylene group or a hydroxyalkylene group
- RR 2 and R 3 may be the same or different and may form a heterocyclic ring containing an alkyl group, an aryl group, an aralkyl group or a nitrogen atom in the formula.
- X— Indicates a counter ion of ammonium salt.
- starch residue or cellulose residue those obtained by removing i hydroxyl groups from starch or cellulose are preferable.
- R is preferably an alkylene group or hydroxyalkylene group having 1 to 12 carbon atoms, more preferably 1 to 3 carbon atoms, and particularly preferably a hydroxypropylene group.
- RR 2 and R 3 are preferably an alkyl group having 1 to 12 carbon atoms, more preferably an alkyl group having 1 to 3 carbon atoms, such as a methyl group, an ethyl group, an i-propyl group, and an n-propyl group.
- ⁇ - include halogen ions such as chlorine, iodine, and bromine, and organic anions such as sulfuric acid, sulfonic acid, methylsulfuric acid, phosphoric acid, and nitric acid.
- i is determined according to the aforementioned degree of cation substitution.
- the natural cationic polymer is produced by a known method.
- a cationizing agent corn starch or the like is cationized with a water-alcohol system, then neutralized with acetic acid, washed with water, and dried.
- the molecular weight is easily adjusted by adding a strong acid such as hydrochloric acid to the thiolated slurry and heating.
- Cationic starch can be used, for example, under alkaline conditions, such as corn, potato, evening pio, raw starch from wheat, rice, etc. It can be obtained by reacting muchloride. It can also be obtained by quaternizing dimethylaminoethylated starch. Furthermore, it can be obtained by reacting starch with 41-chlorobutenetrimethylammonium chloride.
- the cationic cellulose can be obtained, for example, by performing the above-mentioned reaction on hydroxyethyl cellulose.
- the nitrogen content of the natural cationic polymer is preferably 0.05 to 1% by weight from the viewpoint of improving rigidity. 0.07-0.9% by weight is particularly preferred.
- the nitrogen weight% (hereinafter referred to as N%) is preferably at least 0.5% by weight, and from the viewpoint of the rigidity improving effect, it is preferably at most 1% by weight. N% is analyzed by the Kjeldahl method (JISK 8001).
- the natural cationic polymer should have a low molecular weight within a range that does not impair the effects of the present invention, since high solid differentiation of the emulsion is desired in consideration of productivity, in addition to handling convenience and handling properties. Can be.
- the molecular weight of the natural cationic polymer is expressed in terms of the viscosity of an aqueous solution, the viscosity is as follows: 50 ° C, 7% by weight aqueous solution viscosity (B-type viscometer, rotor No. 2, 60 rpm) 40 to: L 0,000 mPa ⁇ s is preferred, and 50 to 8,000 OmPa ⁇ s is more preferred.
- a functional group such as an ester group such as an ether group such as a hydroxyalkyl group or a acetyl group may be introduced into the natural cationic polymer to prevent aging.
- a natural cationic polymer in order to improve polymerization stability and mechanical stability, is used in combination with a natural cationic polymer, such as a synthetic cationic polymer or a nonionic polymer.
- Synthetic cationic polymers include cationic polyvinyl alcohol; nonionic polymers include semisynthetic water-soluble polymers such as methylcellulose, hydroxyethylcellulose, and soluble starch; and synthetic water-soluble polymers such as polyvinylalcohol. preferable.
- the amount of the polymer other than the natural cationic polymer is preferably 0 to 100 parts by weight based on 100 parts by weight of the vinyl monomer constituting the polymer particles (B). It is more preferable to use 0 to 50 parts by weight.
- the synthetic cationic polymer used in the present invention has a nitrogen content ( ⁇ %: analyzed by a Kjeldahl method) of preferably 0.05% by weight or more, more preferably 0.07% by weight or more. It is particularly preferably at least 1% by weight, more preferably at most 1.0% by weight, further preferably at most 0.9% by weight, particularly preferably at most 0.7% by weight. It is preferred that the polymer has a cationic group so that the nitrogen content is in this range.
- the cationic group may be introduced by polymerizing a cationic monomer, or by introducing a cationic group into the polymer by a reaction or the like. With the nitrogen content in this range, the effect of improving paper quality such as rigidity and bulk of the present invention can be sufficiently obtained.
- an ammonium group or an amino group is used for hydrochloric acid, sulfuric acid, nitric acid, and vinegar. It may be neutralized with acid, formic acid, maleic acid, fumaric acid, citric acid, tartaric acid, acid, lactic acid and the like.
- % Aqueous solution viscosity is preferably 2 OmPa ⁇ s or more, more preferably 40 mPa's or more, and still more preferably 65 mPa ⁇ s or more, and the upper limit is preferably 10,000 mPa ⁇ s or less, and 8.0 OmPa ⁇ s or less. ⁇ S or less is more preferable, and 5,000 mPa-s or less is particularly preferable. Within this range, the cationic polymer is easy to handle, the emulsion can be highly solidified, and the paper quality such as the rigidity and bulk of the pulp sheet can be improved.
- Examples of the synthetic cationic polymer include a cationic polymerizable unit derived from a monomer having a polymerizable unsaturated group (for example, a vinyl group, a vinylene group, a vinylidene group, an aryl group, etc.), preferably a compound represented by the general formula (1 ′): Cationic polymers having (meth) acrylic acid-based, styrene-based, vinylpyridine-based, vinylimidazoline-based, and diarylamine-based polymer units represented by (2) to (5).
- R ! hydrogen atom or methyl group
- RK RK R 4 same or different, hydrogen atom, alkyl group having 1 to 22 carbon atoms or substituted alkyl group
- Z is preferably an alkylene group having 2 to 6 carbon atoms, more preferably 1 to 3, or a hydroxyalkylene group, and particularly preferably a hydroxypropylene group.
- RK R ⁇ R 4 is preferably the number 1 to 1 2 carbon atoms, more preferably an alkyl group having 1 to 3 carbon atoms, a methyl group, Echiru group, i one propyl and n- propyl group.
- ⁇ - include halogen ions such as chlorine, iodine, and bromine; and organic anions such as sulfuric acid, sulfonic acid, methylsulfuric acid, phosphoric acid, and nitric acid.
- R 5 hydrogen atom or methyl group
- R 6 an alkylene group having 1 to 3 carbon atoms
- R 7 , R s , R 9 same or different, a hydrogen atom or an alkyl group having 1 to 22 carbon atoms which may have a substituent
- R 6 is preferably a methylene group.
- R 7 , R 8 and R 9 are preferably an alkyl group having 1 to 12 carbon atoms, more preferably an alkyl group having 1 to 3 carbon atoms, such as a methyl group, an ethyl group, an i-propyl group, an n- And a propyl group.
- the substituent include a hydroxyl group and a halogen atom.
- Specific examples of X— include those described above.
- the styrenic polymerization unit preferably has a substituent at the para position.
- R 10 hydrogen atom or methyl group
- R " a hydrogen atom or an alkyl group having 1 to 22 carbon atoms
- R 11 is preferably an alkyl group having 1 to 12 carbon atoms, more preferably 1 to 3 carbon atoms. And a methyl group, such as a methyl group, an ethyl group, an i-propyl group, or an n-propyl group, and particularly preferably a methyl group.
- X— include those described above.
- R 12 hydrogen atom or methyl group
- R 13 a hydrogen atom or an alkyl group having 1 to 3 carbon atoms
- R 14 hydrogen atom or alkyl group having 1 to 22 carbon atoms
- R 13 is preferably a hydrogen atom or a methyl group, and more preferably a hydrogen atom.
- R 14 is preferably an alkyl group having 1 to 12 carbon atoms, more preferably an alkyl group having 1 to 3 carbon atoms, and includes a methyl group, an ethyl group, an i-propyl group, an n-propyl group, and the like. Is a methyl group.
- X- is, c which include those previously described
- R 15 and R 16 are the same or different and represent a hydrogen atom or an alkyl group having 1 to 3 carbon atoms (X: has the same meaning as described above).
- R 15 and R 16 are preferably the same or different and include a hydrogen atom, a methyl group, an ethyl group, an i-propyl group, an n-propyl group and the like. Specific examples of X- include those described above.
- the synthetic cationic polymer of the present invention is preferably a copolymer containing a nonionic polymerized unit.
- the nonionic polymerized unit is more preferably a hydrophilic nonionic polymerized unit.
- the term “polymeric units are hydrophilic” is the basis from which polymerized units can be obtained in the Organic Conceptual Diagram Basics and Applications 1 (by Yoshio Koda, Sankyo Publishing Co., Ltd., published on May 10, 1984). Ratio of inorganic (I) and organic (0) monomers
- [I / O] means 0.60 or more, preferably 1.00 or more, and more preferably 1.30 or more.
- the nonionic polymerized unit can be obtained by copolymerizing with a nonionic monomer.
- non-ionic monomers include vinyl alcohol; hydroxypropyl (meth) acrylamide, hydroxyethyl (meth) ac (Meth) acrylate or (meth) acrylamide having a hydroxyalkyl (C1-8) group such as N-hydroxypropyl (meth) acrylamide; polyethylene glycol (meth) atalylate ( (Meth) acrylic acid esters of polyhydric alcohols such as ethylene glycol polymerization degree 1-30); (meth) acrylamide; N-methyl (meth) acrylamide; N-n-propyl (me) Acrylamide, N-isopropyl (meth) acrylamide, N-t-butyl (meth) acrylamide, N-isobutyl (meth) acrylamide, etc.
- the synthetic cationic polymer can be synthesized by the following known synthesis method 1 or 2, respectively.
- Synthesis method 1 After polymerizing monomers represented by the following general formulas (6), (7), (8), (9), and (10), neutralize the reaction product with an acid or A quaternization method using a grading agent.
- Synthesis method 2 Represented by the following general formulas (6), (7), (8), (9), and (10) Method of polymerizing the monomer after neutralization with an acid or quaternization with a quaternizing agent:
- R 5 , R 6 , R 7 , and R 8 have the same meanings as described above.
- the monomer can be produced by a known radical polymerization method, for example, a solution polymerization method.
- polymerization initiator examples include peroxides such as sodium peroxide and the like, and azo compounds such as 2,2 ′ azobis (2-amidinopropane) hydride and the like.
- solvent water; alcohols such as methanol, ethanol, and isopropanol are preferable.
- reaction temperature and reaction time are appropriately determined depending on the monomer, but it is preferable to carry out the reaction at 50 to 100 ° C. for 3 to 15 hours.
- the molecular weight can be controlled by appropriately selecting polymerization conditions such as polymerization temperature, type and amount of polymerization initiator, and monomer concentration. It is preferable that the synthetic cationic polymer used in the present invention is obtained by copolymerizing the above-mentioned nonionic monomer so as to have the above-mentioned nitrogen content.
- Preferred acids for obtaining the acid neutralized product include hydrochloric acid, sulfuric acid, nitric acid, acetic acid, formic acid, maleic acid, fumaric acid, citric acid, tartaric acid, adipic acid, sulfamic acid, toluenesulfonic acid, lactic acid, and pyrrolidone.
- Preferred examples of the quaternizing agent for obtaining the quaternary ammonium salt include alkyl halides such as methyl chloride, chlorinated methyl chloride, methyl bromide, and methyl iodide.
- Nonionic polymers include semi-synthetic water-soluble polymers such as methylcellulose, hydroxyethylcellulose, and soluble starch; synthetic water-soluble polymers obtained by polymerizing the above-mentioned nonionic monomers, such as polyvinyl alcohol. Is preferred.
- the amount of the nonionic polymer to be used is preferably from 0 to 100 parts by weight, more preferably from 0 to 50 parts by weight, based on 100 parts by weight of the total vinyl monomer.
- the glass transition temperature (Tg) of the polymer particles (B) used in the present invention is preferably 90 ° C. or lower, more preferably 80 ° C. or lower.
- Tg of the polymer is 90 ° C. or less, a part or all of the internally added paper quality improver contained in the paper is melted in the paper manufacturing process, which is preferable from the viewpoint of the stiffness improving performance.
- the lower limit is not particularly limited, but is preferably at least 10 ° C.
- the Tg is preferably 90 ° C or less.
- the Tg of the copolymer can be calculated based on “2.4 Glass transition equation of copolymer” in “Mechanical properties of polymer” (Chemical Doujinshi 1969). For Tg, a numerical value described in rpOLYMER HANDBOOK Fourth Edition 1999 by John Wiley & Sons, Inc. J was used.
- T gn glass transition temperature of homopolymer
- the polymer particles used in the present invention contain a structural unit derived from a vinyl monomer.
- the content of the constituting vinyl monomer in the polymer particles is not particularly limited, but is preferably 50 to 100 mol%, particularly preferably 80 to 100 mol%.
- Examples of the biel monomer include a vinyl compound, a vinylene compound, a vinylidene compound, and a cyclic olefin, and the following compounds are preferred.
- Methyl (meth) acrylate ((meth) acrylic refers to acryl, methacrylic or a mixture thereof; the same applies hereinafter.), (Meth) ethyl acrylate, (meth) isopropyl acrylate, (meth) acrylic (Meth) acrylic acid having an alkyl group having preferably 1 to 12 carbon atoms, more preferably 1 to 4 carbon atoms, such as butyl acid acid, isoptyl (meth) acrylate, and t-butyl (meth) acrylate. Alkyl esters;
- a fatty acid comprising an ester of a vinyl alcohol with a linear or branched fatty acid having 1 to 18 carbon atoms, preferably 1 to 6 carbon atoms, such as vinyl acetate, vinyl propionate, vinyl butyrate and vinyl vivalate.
- salt examples include an alkali metal salt (sodium salt, potassium salt, lithium salt, etc.), an alkaline earth metal salt (calcium salt, magnesium salt, Barium salts), and ammonium salts (quaternary ammonium salts, quaternary alkyl ammonium salts, etc.).
- alkali metal salt sodium salt, potassium salt, lithium salt, etc.
- alkaline earth metal salt calcium salt, magnesium salt, Barium salts
- ammonium salts quaternary ammonium salts, quaternary alkyl ammonium salts, etc.
- sodium salt is the cheapest and preferred.
- Specific examples thereof include an amino group-containing monomer having a polymerizable unsaturated group such as acrylamide and the like, or an acid neutralized product or a quaternized product thereof.
- Preferred acids for obtaining the acid neutralized product include hydrochloric acid, sulfuric acid, nitric acid, acetic acid, formic acid, maleic acid, fumaric acid, citric acid, tartaric acid, adipic acid, lactic acid and the like.
- alkylating agents such as alkyl halides such as methyl chloride, ethyl chloride, methyl bromide and methyl iodide, dimethyl sulfate, getyl sulfate and di-n-propyl sulfate are exemplified.
- Method for producing polymer particles used in the present invention Can be obtained by emulsion polymerization, suspension polymerization or dispersion polymerization.
- the above-mentioned polymer particles (B) are preferably added to the emulsion at a solid content concentration of preferably 5 to 60% by weight or 10 to 60% by weight, more preferably 15 to 60% by weight, from the viewpoint of easy handling. Contains 55% by weight.
- the average particle size of the polymer particles (B) is preferably from 0.01 to 50 im, more preferably from 0.1 to 30 m, particularly preferably from 0.1 to 30 m, from the viewpoint of the stability of the emulsion and the adsorptivity to pulp. 2-20 m is preferred.
- the solid content concentration is measured by the method described in the examples.
- the ratio of the natural cationic polymer (A) or the synthetic cationic polymer ( ⁇ ') is 5 to 200 parts by weight, and further 5 to 1 part by weight per 100 parts by weight of the polymer particles ( ⁇ ). It is preferably 50, parts by weight, particularly preferably 7 to 120 parts by weight. In this ratio, the weight of the polymer particles (II) is the total weight of all monomers constituting the polymer.
- the natural cationic polymer In order to effectively adsorb the polymer particles ( ⁇ ) to the pulp and obtain the auxiliary effect of improving rigidity by the natural cationic polymer ( ⁇ ) or the synthetic cationic polymer ( ⁇ '), the natural cationic polymer
- the ratio of ( ⁇ ) or the synthetic cationic polymer ( ⁇ ') is 5 to 500 parts by weight, more preferably 7 to 500 parts by weight, especially 10 to 5 parts by weight, per 100 parts by weight of the polymer particles ( ⁇ ). It is preferably 00 parts by weight.
- the emulsion of the present invention preferably contains 40 to 90% by weight of a dispersion medium, more preferably Or 45 to 85% by weight.
- the dispersion medium is preferably water, but may contain a lower alcohol having 1 to 4 carbon atoms. Examples of the lower alcohol include methyl, ethyl, and isopropyl alcohols having 1 to 3 carbon atoms.
- the natural cationic polymer ( ⁇ ) or the composite cationic polymer ( ⁇ ') Is preferably 5 to 500 parts by weight, more preferably 7 to 500 parts by weight, and particularly preferably 30 to 500 parts by weight, based on 100 parts by weight of the polymer particles ( ⁇ ).
- fillers such as calcium carbonate, talc, white cellulose, pigments and the like may be contained as additives.
- the emulsion (suspension, water dispersion) of polymer particles ( ⁇ ) obtained by polymerizing the above-mentioned vinyl monomer is used as the internal paper quality improver of the present invention.
- the polymerization method of the polymer particles ( ⁇ ) may be a general anionic, cationic, nonionic or amphoteric surfactant, a natural, semi-synthetic or synthetic anionic, nonionic, or a dispersant or emulsion stabilizer.
- Emulsion polymerization, suspension polymerization, or dispersion polymerization using the above-described cationic polymer or the like is preferable.
- anionic surfactants such as sodium polyoxyethylene dodecyl ether sulfate and sodium dodecyl ether sulfate; trimethyl stearyl ammonium chloride and carboxymethyl dimethyl cetyl ammonium; Cationic and amphoteric surfactants; sucrose fatty acid esters such as sucrose monostearate and sucrose diureate; sorbitan such as sorbitan monostearate
- Nonionic surfactants such as polyoxyalkylene adducts of sorbitan esters such as polyesters, polyoxyethylene sorbitan monostearate, and polyoxyalkylene adducts of aliphatic alcohols; starch and derivatives thereof, ethylcellulose, etc.
- natural and semi-synthetic polymers such as cellulose ethers, cellulose acetates and other cellulose esters, and cellulose derivatives; polyvinyl alcohol and derivatives thereof, and synthetic polymers such as maleated polybutadiene.
- the emulsion polymerization, suspension polymerization, or dispersion polymerization method for polymerizing vinyl monomers in the presence of the above-mentioned natural cationic polymer (A) or synthetic cationic polymer (A,) is used.
- the one produced is preferred, and the emulsion polymerization method is particularly preferred.
- the vinyl monomer is preferably used in an amount of 1 to 70 parts by weight, more preferably 1.5 to 60 parts by weight, particularly preferably 8 to 57 parts by weight, based on 100 parts by weight of the reaction solvent.
- Preferred examples of the reaction solvent include water and lower alcohols.
- a peroxide, an organic or inorganic peracid or a salt thereof, a redox-based azobis compound alone or in combination with a reducing agent, which is uniformly dissolved in a solvent is used.
- Representative examples of the compound are, for example, t-butyl peroxide, t-amyl peroxide, cumyl peroxide, acetyl-peroxide, propionyl-peroxide, benzoyl-peroxide, benzoyl-isobutyryl-peroxide.
- the reaction temperature is preferably 30 to 90 ° C, and the reaction time is preferably about 30 minutes to 10 hours.
- the emulsion after the completion of the reaction can be used as it is as an internally added paper quality improver.
- the natural cationic polymer ( ⁇ ) or synthetic form is added to the emulsion.
- the cationic polymer ( ⁇ ') is added and mixed, preferably at room temperature. Even when a natural cationic polymer ( ⁇ ) or a synthetic cationic polymer ( ⁇ ') is used as a dispersing agent or an emulsion stabilizer, after the polymerization, the natural cationic polymer ( ⁇ ) or A synthetic cationic polymer ( ⁇ ′) may be added.
- an additive such as a ⁇ adjuster may be used at the time of polymerization.
- a ⁇ adjuster acids such as phosphoric acid and tartaric acid and aqueous alkali solutions such as sodium hydroxide and potassium hydroxide are polymerized. Is added to
- the above-mentioned emulsion is mixed with pulp, preferably at room temperature, and the paper is made to obtain a pulp sheet containing an internally added paper quality improver on the surface and / or inside of the pulp sheet.
- the paper quality improver according to the present invention can also be obtained by separately adding to the pulp the emulsion containing the polymer particles (B) and the natural cationic polymer (A) or the synthetic cationic polymer ( ⁇ ′). Is obtained on the surface and inside or inside of the pulp sheet.
- the addition amount of the internally added paper quality improver is preferably from 0.05 to 20 parts by weight, more preferably from 0.1 to 10 parts by weight, based on 100 parts by weight of pulp in terms of solid content.
- the internal addition amount is preferably at least 0.05 part by weight from the viewpoint of rigidity and bulk improving performance, and is preferably at most 20 parts by weight from the viewpoint of the inherent performance of the pulp sheet.
- the stiffness improvement rate is determined by comparing the pulp sheet without the paper stiffness improver to the pulp sheet with 0.5 to 1.0 parts by weight of the internally added paper quality improver per 100 parts by weight of the pulp.
- the stiffness is preferably improved by at least 1%, more preferably by at least 2.5%.
- the internal addition in the present invention means that it is used as an agent to be added to the pulp slurry during the process of producing the pulp sheet, that is, at the time of papermaking.
- the place of addition is before the papermaking process, in which the dilute pulp raw material is drained while traveling on the wire mesh to form a paper layer, such as a disintegrator such as pulp and refiner, a beater, a machine chest, and the like. It may be added to tanks such as head boxes and white water tanks, or to piping connected to these facilities, but it is added in refiners, machine chests, and head boxes. It is desirable to have a place where the pulp material can be blended uniformly.
- the pulp sheet obtained using the internal paper quality improver of the present invention is suitable for newsprint, uncoated printing paper, finely coated printing paper, coated printing paper, information paper, corrugated paper, and white paperboard. Used for
- emalgen 150 nonionic surfactant, 20% aqueous solution, manufactured by Kao Corporation
- 75% phosphoric acid aqueous solution in 17.2 g of ion-exchanged water in advance
- vinyl acetate Manufactured by Shin-Etsu Vinyl Acetate Co., Ltd.
- Initiator V-50, azo-based initiator, manufactured by Wako Pure Chemical Industries, Ltd.
- cationic starch ACN% 0.6%, 7% aqueous solution viscosity 26 OmPas (50 ° C, B-type viscometer, rotor No. 2, 60 rpm)] 48.2 g, polyvinyl alcohol (GL-05, degree of polymerization 500, degree of degradation 88 mo 1%, manufactured by Nippon Synthetic Chemical Co., Ltd.) 8.1 g, ion-exchanged water 585.2 g was charged and dissolved by heating to 90 ° C.
- emalgen 150 nonionic surfactant, 20% aqueous solution, manufactured by Kao Corporation
- 17.2 g of ion-exchanged water in advance were added to a 75% aqueous solution of phosphoric acid 1.
- an aqueous solution obtained by mixing 9 g and 45.0 g of 4% sodium glacial oxide the mixture was stirred at 120 rpm, heated to 60 ° C. while blowing nitrogen, and held for 30 minutes. .
- 20.4 g of vinyl acetate manufactured by Shin-Etsu Vinyl Acetate Co., Ltd.
- initiator V-50, azo-based initiator, manufactured by Wako Pure Chemical Industries, Ltd.
- Ig was replaced with 29.6 g of ion-exchanged water Was added and kept for 15 minutes. Then, after raising the temperature to 77, vinyl acetate 205. 5.5 g of tacrylic acid (manufactured by Mitsubishi Rayon Co., Ltd.), 6.6 g of dimethylacrylamide (reagent, manufactured by Wako Pure Chemical Industries, Ltd.), and 0.35 g of initiator (V-50) 0.35 g A solution dissolved in 101 g of exchanged water was dropped from each dropping funnel for 3 hours to carry out polymerization. Next, the temperature was increased to 82 ° C, aged for 1 hour, cooled, and taken out.
- a cationic emulsion II having a solid content of 23.5% and an average particle size of 0.52 m was obtained.
- the monomers of the cationic polymer and the polymer particles ( ⁇ ) were changed as shown in Tables 1 and 2 and each was synthesized (note that polyvinyl alcohol was used in 100 parts by weight of the cationic polymer based on 100 parts by weight). 16.8 parts by weight The amount of ion-exchanged water was changed appropriately).
- Emalgen 15 0 Non-ionic surfactant, 20% aqueous solution, manufactured by Kao Corporation 21.3 g and 75% phosphoric acid aqueous solution in 0.2 g of ion-exchanged water in advance 1.lg and 4 After adding an aqueous solution mixed with 26.6 g of sodium hydroxide, the mixture was stirred at 120 rpm, heated to 60 C while blowing nitrogen, and kept for 30 minutes. Then, 10.7 g of vinyl acetate (manufactured by Shin-Etsu Vinyl Acetate Co., Ltd.), initiator (V-50, azo-based initiator, manufactured by Wako Pure Chemical Industries, Ltd.) 1. Og was replaced with ion-exchanged water 9 .0 g was added and kept for 15 minutes. Subsequently, the temperature was raised to 77 ° C., aged for 1 hour, cooled, and taken out.
- V-50 azo-based initiator
- a cationic emulsion XVIII having a solid content of 7.9% and an average particle size of 0.20 xm was obtained.
- N% 0.6%, 7% aqueous solution viscosity 26 OmPas (50 ° C, B-type viscometer, Yuichi No. 2, 60 rpm)] 28.9 g
- emulgen 150 nonionic surfactant, 20% aqueous solution, manufactured by Kao Corporation
- phosphoric acid in 10.2 g of ion-exchanged water in advance
- an aqueous solution of 1.lg and an aqueous solution obtained by mixing 46.6 g of 4% sodium hydroxide the mixture was stirred at 120 rpm and heated to 60 ° C. while blowing nitrogen. Hold for 30 minutes.
- 10.7 g of vinyl acetate manufactured by Shin-Etsu Vinyl Acetate Co., Ltd.
- initiator V-50, azo-based initiator, manufactured by Wako Pure Chemical Industries, Ltd.
- Og was replaced with ion-exchanged water 9
- a mixture prepared by dissolving 9 g of the mixture and 0.85 g of the initiator (V-50) in 130 g of ion-exchanged water was dropped from each dropping funnel over 3 hours, and polymerization was carried out.
- a cationic emulsion XIX having a solid content of 13.1% and an average particle diameter of 0.43 / im was obtained.
- Emulgen 150 nonionic surfactant, 20% aqueous solution, manufactured by Kao Corporation
- 11.4 g of 4% tartaric acid reagent, manufactured by Wako Pure Chemical Industries, Ltd.
- a cationic emulsion II-I having a solid content of 36.3% and an average particle size of 5.68 / im was obtained.
- Emulsion II-III had a solid concentration of 32% and an average particle size of 5.52 im.
- Emulsion XVIII The synthesis was carried out in accordance with the polymerization method and monomer composition of Emulsion XVIII, except that 468.0 g of ion-exchanged water and 175.8 g of Emulgen 150 were used. An emulsion ⁇ ⁇ — ⁇ having a solid content of 19.5% and an average particle size of 0.22 m was obtained.
- the solid content concentration in the emulsion was measured by heating 1 g of the sample with an infrared moisture meter (Kett, Infrared Moisture Determination Balance ⁇ FD-240) at 150 ° C for 20 minutes.
- the average particle size of the dispersed particles in the emulsion was measured with a laser diffraction / scattering type particle size distribution analyzer LA-910 (manufactured by Horiba, Ltd.). The median diameter was used as the average particle diameter. However, in this measurement method, particles less than 0.4 im were measured with a dynamic light scattering particle size distribution analyzer N4Plus (Beckman Coulter, Inc.) in terms of measurement accuracy. In this case, the average particle diameter was determined by the unimodal method (kiwland method).
- the nitrogen content of the cationic polymer was determined.
- the viscosity (7% by weight) of the cationic polymer was measured using a B-type viscometer (60 rpm, 50 ° C). The mouth was selected appropriately according to the measured viscosity.
- LBKP hardwood bleached pulp
- JISP8121 Canadian standard freeness
- the crack stiffness (according to the JISP 8143 method) is calculated for the paper with and without the paper quality improver, and calculated by the following formula.
- the results are shown in Tables 1 and 2.
- the rigidity was improved by 7.6% or more at the internal addition amount of 5%, and the rigidity was improved by 2.6% or more at the internal addition amount of 0.5%.
- the improvement in rigidity was 4.8% at the internal addition amount of 5%.
- the improvement in stiffness is less than 1.6% at 0.5% internal addition.
- Stiffness improvement rate (%) (Clark stiffness of paper with agent added) Clark stiffness of paper without Z agent 1) X 100
- the tension (according to JISP 8118) is calculated for the paper with the paper quality improver internally added and the paper without the paper quality improver, and calculated by the following formula.
- Example 11 Cationized starch A 0.6 260 VAc 94.66 MAA 1.21 DMAAm 1.45-34 X 10 39.0 0.94 5.0 26.0 5.46
- Example 25 Cationized starch A 0.6 260 VAc 98.55 DMAAm 1.45-33 X E 10 29.5 0.43 0.5 7.6 5.20
- Each cationic polymer is as follows.
- PVA-1 Mercapto-modified polyvinyl alcohol (M-115, degree of polymerization 1500, manufactured by Kuraray Co., Ltd.)
- PVA-2 Cationized polyvinyl alcohol (C-506, degree of polymerization 600, manufactured by Kuraray Co., Ltd.)
- the amount of (A) added depends on the monomer composition of the polymer particles (B). % By weight based on weight.
- the stiffness and bulkiness of paper made from the following pulp raw materials were evaluated using the paper quality improvers shown in Table 3 in the same manner as in Example 1. Table 3 shows the results.
- the paper quality improving agent of the present invention can obtain a paper quality improving effect even with a relatively small amount of the cationic polymer used.
- Type 3 ri Monomer composition 1 o.
- DMAAm is dimethyl acrylamide
- GMAC is hydroxypropylmethylammonium chloride.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Paper (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002496638A CA2496638A1 (en) | 2002-08-27 | 2003-08-27 | Paper quality improver |
US10/525,458 US7744725B2 (en) | 2002-08-27 | 2003-08-27 | Paper quality improver |
EP03791345A EP1550770B1 (en) | 2002-08-27 | 2003-08-27 | method of improving paper stiffness |
AU2003261765A AU2003261765A1 (en) | 2002-08-27 | 2003-08-27 | Paper quality improver |
DE60328211T DE60328211D1 (de) | 2002-08-27 | 2003-08-27 | Verfahren zum Verbessern von Papiersteifigkeit |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002-247754 | 2002-08-27 | ||
JP2002247754 | 2002-08-27 | ||
JP2002-252659 | 2002-08-30 | ||
JP2002252659A JP3976136B2 (ja) | 2002-08-30 | 2002-08-30 | 紙質向上剤 |
Publications (1)
Publication Number | Publication Date |
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WO2004020736A1 true WO2004020736A1 (ja) | 2004-03-11 |
Family
ID=31980489
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2003/010867 WO2004020736A1 (ja) | 2002-08-27 | 2003-08-27 | 紙質向上剤 |
Country Status (8)
Country | Link |
---|---|
US (1) | US7744725B2 (ja) |
EP (1) | EP1550770B1 (ja) |
KR (1) | KR100989538B1 (ja) |
CN (1) | CN1316123C (ja) |
AU (1) | AU2003261765A1 (ja) |
CA (1) | CA2496638A1 (ja) |
DE (1) | DE60328211D1 (ja) |
WO (1) | WO2004020736A1 (ja) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
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EP3077212A1 (en) | 2013-12-06 | 2016-10-12 | Hewlett-Packard Development Company, L.P. | Cationic latex fixative for ink applications |
JP6795790B2 (ja) * | 2016-06-23 | 2020-12-02 | 荒川化学工業株式会社 | 抄き合わせ紙の製造方法 |
US11242423B2 (en) * | 2017-03-30 | 2022-02-08 | Kemira Oyj | Surface sizing composition, method of production, and use thereof |
Citations (6)
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US4124439A (en) * | 1973-06-25 | 1978-11-07 | Feldmuhle Aktiengesellschaft | High bulk paper of great stiffness |
JPS5434409A (en) * | 1977-08-23 | 1979-03-13 | Sanyo Chemical Ind Ltd | Internally adding and treating agent for paper making |
JPH03227489A (ja) * | 1990-01-31 | 1991-10-08 | Mitsui Toatsu Chem Inc | 製紙用添加剤 |
WO2000046264A1 (en) * | 1999-02-05 | 2000-08-10 | Raisio Chemicals Ltd | Polymer dispersion and method to produce the same |
JP2000265389A (ja) * | 1999-03-12 | 2000-09-26 | Nippon Mitsubishi Oil Corp | 紙のサイジング方法 |
JP2002115197A (ja) * | 2000-08-03 | 2002-04-19 | Hymo Corp | 中質紙の抄紙方法 |
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US3632535A (en) * | 1967-09-20 | 1972-01-04 | Cpc International Inc | Emulsion polymerization method and resultant aqueous latex |
DE3534273A1 (de) * | 1985-09-26 | 1987-04-02 | Basf Ag | Verfahren zur herstellung von vinylamin-einheiten enthaltenden wasserloeslichen copolymerisaten und deren verwendung als nass- und trockenverfestigungsmittel fuer papier |
DE3730887A1 (de) * | 1987-09-15 | 1989-03-23 | Basf Ag | Verfahren zur verbesserung der bedruckbarkeit von papier |
US4940741A (en) * | 1988-06-17 | 1990-07-10 | National Starch And Chemical Investment Holding Corporation | Process for the production of hardboard |
US5349089A (en) * | 1989-07-07 | 1994-09-20 | National Starch And Chemical Investment Holding Corporation | Reagent for preparing polycationic polysaccharides |
US5274055A (en) * | 1990-06-11 | 1993-12-28 | American Cyanamid Company | Charged organic polymer microbeads in paper-making process |
US5167766A (en) * | 1990-06-18 | 1992-12-01 | American Cyanamid Company | Charged organic polymer microbeads in paper making process |
CA2116020C (en) * | 1992-06-19 | 2000-08-08 | Charles C. Nguyen | Cationic starch/vinyl acetate containing board coating binders |
US5431783A (en) * | 1993-07-19 | 1995-07-11 | Cytec Technology Corp. | Compositions and methods for improving performance during separation of solids from liquid particulate dispersions |
JP3434055B2 (ja) | 1994-12-14 | 2003-08-04 | 株式会社クラレ | 紙用の内添剤 |
ES2146920T5 (es) * | 1995-12-25 | 2007-02-01 | Hymo Corporation | Proceso de fabricacion de papel. |
US6146494A (en) * | 1997-06-12 | 2000-11-14 | The Procter & Gamble Company | Modified cellulosic fibers and fibrous webs containing these fibers |
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JP2971447B1 (ja) | 1998-06-02 | 1999-11-08 | 花王株式会社 | 紙用嵩高剤 |
FI107173B (fi) | 1998-07-10 | 2001-06-15 | Raisio Chem Oy | Paperinvalmistuksen lisäaine |
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JP3283248B2 (ja) | 1998-12-28 | 2002-05-20 | 花王株式会社 | 抄紙用紙質向上剤 |
EP1232189B1 (de) * | 1999-10-19 | 2003-12-03 | Südzucker Aktiengesellschaft Mannheim/Ochsenfurt | Emulsionspolymerisationsverfahren |
PL366291A1 (en) * | 1999-12-06 | 2005-01-24 | Hercules Incorporated | Method for using hydrophobically associative polymers in preparing cellulosic fiber compositions, and cellulosic fiber compositions incorporating the hydrophobically associative polymers |
MY140287A (en) * | 2000-10-16 | 2009-12-31 | Ciba Spec Chem Water Treat Ltd | Manufacture of paper and paperboard |
-
2003
- 2003-08-27 CA CA002496638A patent/CA2496638A1/en not_active Abandoned
- 2003-08-27 AU AU2003261765A patent/AU2003261765A1/en not_active Abandoned
- 2003-08-27 DE DE60328211T patent/DE60328211D1/de not_active Expired - Lifetime
- 2003-08-27 WO PCT/JP2003/010867 patent/WO2004020736A1/ja active Application Filing
- 2003-08-27 EP EP03791345A patent/EP1550770B1/en not_active Expired - Fee Related
- 2003-08-27 CN CNB038202808A patent/CN1316123C/zh not_active Expired - Fee Related
- 2003-08-27 US US10/525,458 patent/US7744725B2/en not_active Expired - Fee Related
- 2003-08-27 KR KR1020057003162A patent/KR100989538B1/ko not_active IP Right Cessation
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US4124439A (en) * | 1973-06-25 | 1978-11-07 | Feldmuhle Aktiengesellschaft | High bulk paper of great stiffness |
JPS5434409A (en) * | 1977-08-23 | 1979-03-13 | Sanyo Chemical Ind Ltd | Internally adding and treating agent for paper making |
JPH03227489A (ja) * | 1990-01-31 | 1991-10-08 | Mitsui Toatsu Chem Inc | 製紙用添加剤 |
WO2000046264A1 (en) * | 1999-02-05 | 2000-08-10 | Raisio Chemicals Ltd | Polymer dispersion and method to produce the same |
JP2000265389A (ja) * | 1999-03-12 | 2000-09-26 | Nippon Mitsubishi Oil Corp | 紙のサイジング方法 |
JP2002115197A (ja) * | 2000-08-03 | 2002-04-19 | Hymo Corp | 中質紙の抄紙方法 |
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Also Published As
Publication number | Publication date |
---|---|
US7744725B2 (en) | 2010-06-29 |
DE60328211D1 (de) | 2009-08-13 |
CA2496638A1 (en) | 2004-03-11 |
AU2003261765A1 (en) | 2004-03-19 |
EP1550770B1 (en) | 2009-07-01 |
KR20050058513A (ko) | 2005-06-16 |
US20060106137A1 (en) | 2006-05-18 |
EP1550770A4 (en) | 2006-08-23 |
EP1550770A1 (en) | 2005-07-06 |
CN1678793A (zh) | 2005-10-05 |
CN1316123C (zh) | 2007-05-16 |
KR100989538B1 (ko) | 2010-10-25 |
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