JP2012207317A - Method for producing cationic surface sizing agent and sizing agent obtained by the method - Google Patents
Method for producing cationic surface sizing agent and sizing agent obtained by the method Download PDFInfo
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- JP2012207317A JP2012207317A JP2011071459A JP2011071459A JP2012207317A JP 2012207317 A JP2012207317 A JP 2012207317A JP 2011071459 A JP2011071459 A JP 2011071459A JP 2011071459 A JP2011071459 A JP 2011071459A JP 2012207317 A JP2012207317 A JP 2012207317A
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- sizing agent
- meth
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- 238000004513 sizing Methods 0.000 title claims abstract description 92
- 125000002091 cationic group Chemical group 0.000 title claims abstract description 40
- 238000000034 method Methods 0.000 title claims abstract description 34
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 15
- 229920001577 copolymer Polymers 0.000 claims abstract description 94
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 71
- 239000000123 paper Substances 0.000 claims abstract description 53
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- 125000001302 tertiary amino group Chemical group 0.000 claims abstract description 33
- 239000000203 mixture Substances 0.000 claims abstract description 24
- 239000004094 surface-active agent Substances 0.000 claims abstract description 15
- 239000003999 initiator Substances 0.000 claims abstract description 13
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- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 10
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- 150000003839 salts Chemical class 0.000 claims abstract description 9
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 8
- 150000003254 radicals Chemical class 0.000 claims abstract description 8
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- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical group OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 19
- 125000004432 carbon atom Chemical group C* 0.000 claims description 14
- 239000007864 aqueous solution Substances 0.000 claims description 13
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- 125000004985 dialkyl amino alkyl group Chemical group 0.000 claims description 8
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical group [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims description 8
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims description 8
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- WDQMWEYDKDCEHT-UHFFFAOYSA-N 2-ethylhexyl 2-methylprop-2-enoate Chemical compound CCCCC(CC)COC(=O)C(C)=C WDQMWEYDKDCEHT-UHFFFAOYSA-N 0.000 description 6
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 6
- 239000004372 Polyvinyl alcohol Substances 0.000 description 6
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 6
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- 239000003054 catalyst Substances 0.000 description 3
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 3
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- 230000000379 polymerizing effect Effects 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- YAJYJWXEWKRTPO-UHFFFAOYSA-N 2,3,3,4,4,5-hexamethylhexane-2-thiol Chemical compound CC(C)C(C)(C)C(C)(C)C(C)(C)S YAJYJWXEWKRTPO-UHFFFAOYSA-N 0.000 description 2
- HXVNBWAKAOHACI-UHFFFAOYSA-N 2,4-dimethyl-3-pentanone Chemical compound CC(C)C(=O)C(C)C HXVNBWAKAOHACI-UHFFFAOYSA-N 0.000 description 2
- IUVCFHHAEHNCFT-INIZCTEOSA-N 2-[(1s)-1-[4-amino-3-(3-fluoro-4-propan-2-yloxyphenyl)pyrazolo[3,4-d]pyrimidin-1-yl]ethyl]-6-fluoro-3-(3-fluorophenyl)chromen-4-one Chemical compound C1=C(F)C(OC(C)C)=CC=C1C(C1=C(N)N=CN=C11)=NN1[C@@H](C)C1=C(C=2C=C(F)C=CC=2)C(=O)C2=CC(F)=CC=C2O1 IUVCFHHAEHNCFT-INIZCTEOSA-N 0.000 description 2
- SYBYTAAJFKOIEJ-UHFFFAOYSA-N 3-Methylbutan-2-one Chemical compound CC(C)C(C)=O SYBYTAAJFKOIEJ-UHFFFAOYSA-N 0.000 description 2
- MXLMTQWGSQIYOW-UHFFFAOYSA-N 3-methyl-2-butanol Chemical compound CC(C)C(C)O MXLMTQWGSQIYOW-UHFFFAOYSA-N 0.000 description 2
- 239000004908 Emulsion polymer Substances 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 2
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- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 2
- 229920000881 Modified starch Polymers 0.000 description 2
- 239000004368 Modified starch Substances 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 2
- MZVQCMJNVPIDEA-UHFFFAOYSA-N [CH2]CN(CC)CC Chemical group [CH2]CN(CC)CC MZVQCMJNVPIDEA-UHFFFAOYSA-N 0.000 description 2
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 2
- BTANRVKWQNVYAZ-UHFFFAOYSA-N butan-2-ol Chemical compound CCC(C)O BTANRVKWQNVYAZ-UHFFFAOYSA-N 0.000 description 2
- 229920006317 cationic polymer Polymers 0.000 description 2
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- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- 239000001254 oxidized starch Substances 0.000 description 2
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- XNLICIUVMPYHGG-UHFFFAOYSA-N pentan-2-one Chemical compound CCCC(C)=O XNLICIUVMPYHGG-UHFFFAOYSA-N 0.000 description 2
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- JRKICGRDRMAZLK-UHFFFAOYSA-L peroxydisulfate Chemical compound [O-]S(=O)(=O)OOS([O-])(=O)=O JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 description 2
- 239000002685 polymerization catalyst Substances 0.000 description 2
- HJWLCRVIBGQPNF-UHFFFAOYSA-N prop-2-enylbenzene Chemical compound C=CCC1=CC=CC=C1 HJWLCRVIBGQPNF-UHFFFAOYSA-N 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- CWERGRDVMFNCDR-UHFFFAOYSA-N thioglycolic acid Chemical compound OC(=O)CS CWERGRDVMFNCDR-UHFFFAOYSA-N 0.000 description 2
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- QEQBMZQFDDDTPN-UHFFFAOYSA-N (2-methylpropan-2-yl)oxy benzenecarboperoxoate Chemical compound CC(C)(C)OOOC(=O)C1=CC=CC=C1 QEQBMZQFDDDTPN-UHFFFAOYSA-N 0.000 description 1
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- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 description 1
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- 125000004079 stearyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
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- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- DGVVWUTYPXICAM-UHFFFAOYSA-N β‐Mercaptoethanol Chemical compound OCCS DGVVWUTYPXICAM-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- D21H17/45—Nitrogen-containing groups
- D21H17/455—Nitrogen-containing groups comprising tertiary amine or being at least partially quaternised
-
- 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
- D21H19/00—Coated paper; Coating material
- D21H19/10—Coatings without pigments
- D21H19/14—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
- D21H19/20—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising 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
- 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
- D21H21/16—Sizing or water-repelling agents
-
- 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
- D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
-
- 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/52—Addition to the formed paper by contacting paper with a device carrying the material
- D21H23/56—Rolls
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
- Y10T428/3188—Next to cellulosic
- Y10T428/31895—Paper or wood
- Y10T428/31906—Ester, halide or nitrile of addition polymer
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Paper (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
本発明は、カチオン性表面サイズ剤の製造方法、その方法で得られるサイズ剤、そのサイズ剤を塗工した紙および板紙に関する。 The present invention relates to a method for producing a cationic surface sizing agent, a sizing agent obtained by the method, paper and paperboard coated with the sizing agent.
従来のカチオン性表面サイズ剤は、一般的に、スチレン類および３級アミノ基含有モノマー（すなわち、カチオン性モノマー）を主成分とするモノマー成分を重合させて得られる３級アミノ基を有する共重合体、または３級アミノ基を４級化変成した４級アンモニウム塩基を有する共重合体の水溶液である（特許文献１および２）。これらの共重合体は、以下のような方法で得られる：
（ｉ）有機溶剤または有機溶剤と水との混合溶媒中で、油溶性重合触媒を用いた溶液重合を行う。
（ｉｉ）水主体の水系溶媒中で、水溶性重合触媒を用いた乳化重合を行う。
このような方法で得られたカチオン性表面サイズ剤は、良好なサイズ性を有するものの、適用される環境、特に水の影響（硬度、ｐＨなど）を受けやすく、安定性が不十分という問題がある。
Conventional cationic surface sizing agents generally have a copolymer having a tertiary amino group obtained by polymerizing a monomer component mainly composed of styrenes and a tertiary amino group-containing monomer (that is, a cationic monomer). It is an aqueous solution of a copolymer or a copolymer having a quaternary ammonium base in which a tertiary amino group is quaternized (Patent Documents 1 and 2). These copolymers are obtained in the following way:
(I) Solution polymerization using an oil-soluble polymerization catalyst is performed in an organic solvent or a mixed solvent of an organic solvent and water.
(Ii) Emulsion polymerization using a water-soluble polymerization catalyst is performed in a water-based aqueous solvent.
Although the cationic surface sizing agent obtained by such a method has a good sizing property, it is easily affected by the environment in which it is applied, particularly water (hardness, pH, etc.), and has a problem of insufficient stability. is there.
一方、有機溶剤を用いずに水中で乳化重合して得られるカチオン性表面サイズ剤、あるいは溶液重合によって得られるカチオン性ポリマーと疎水性モノマーとを乳化重合して得られるカチオン性表面サイズ剤は、乳化剤として界面活性剤などを使用する場合が多い（特許文献３〜７）。界面活性剤を使用した乳化重合物は、溶液重合によって得られるカチオン性表面サイズ剤と比較して、使用される環境の影響を受けにくく、安定性の改善が期待できるが、その改善効果は十分ではない。さらに、このような乳化重合物は、界面活性剤を使用しているため、溶液重合によって得られるカチオン性表面サイズ剤と比較して、サイズ性付与効果が劣る。 On the other hand, a cationic surface sizing agent obtained by emulsion polymerization in water without using an organic solvent, or a cationic surface sizing agent obtained by emulsion polymerization of a cationic polymer and a hydrophobic monomer obtained by solution polymerization, A surfactant is often used as an emulsifier (Patent Documents 3 to 7). Compared with cationic surface sizing agents obtained by solution polymerization, emulsion polymers using surfactants are less susceptible to the environment in which they are used and can be expected to improve stability. is not. Furthermore, since such an emulsion polymer uses a surfactant, the effect of imparting sizing properties is inferior to a cationic surface sizing agent obtained by solution polymerization.
また、界面活性剤を用いずに乳化重合を行う製造方法も知られている（特許文献８および９）。界面活性剤を用いずに得られるカチオン性表面サイズ剤は、溶液重合によって得られるカチオン性ポリマー水溶液を分散剤として使用しているため、界面活性剤を使用したサイズ剤と比較して、同等の安定性と優れたサイズ性とを示す。しかし、溶液重合によって得られるカチオン性表面サイズ剤と比較して、サイズ性付与効果が劣る。 Moreover, the manufacturing method which performs emulsion polymerization without using surfactant is also known (patent documents 8 and 9). Since the cationic surface sizing agent obtained without using a surfactant uses an aqueous cationic polymer solution obtained by solution polymerization as a dispersant, it is equivalent to the sizing agent using a surfactant. Shows stability and excellent size. However, compared with the cationic surface sizing agent obtained by solution polymerization, the sizing effect is inferior.
本発明の課題は、使用される環境、特に水の条件（硬度、ｐＨなど）や適用される紙の種類（紙、板紙など）に拘らず、優れた分散安定性を有し、かつ優れたサイズ性を付与するカチオン性表面サイズ剤を提供することである。 The problem of the present invention is that it has excellent dispersion stability regardless of the environment in which it is used, particularly water conditions (hardness, pH, etc.) and the type of paper applied (paper, paperboard, etc.). It is to provide a cationic surface sizing agent that imparts sizing properties.
本発明者らは、上記課題を解決すべく鋭意研究を重ねた結果、
（１）１５〜４５重量％の３級アミノ基含有モノマー（ａ）と、１５〜８５重量％の（メタ）アクリル酸エステル（ｂ）と、０〜７０重量％のスチレン類（ｃ）とを含有するモノマー混合物を、連鎖移動剤の存在下で溶液重合させて共重合体（Ａ）を得る工程であって、前記（メタ）アクリル酸エステル（ｂ）のエステル部分が、４〜１８個の炭素原子を有する鎖状アルキル、４〜１８個の炭素原子を有する環状アルキル、または６〜１８個の炭素原子を有するアリールである第１工程；
前記共重合体（Ａ）と疎水性モノマー（ｄ）とを、界面活性剤の不存在下で、水溶性のフリーラジカル開始剤と重金属塩とを用いる酸化還元系で重合させて共重合体（Ｂ）を得る工程であって、共重合体（Ａ）が共重合体（Ｂ）を構成する成分全体に対して３０〜７０重量％の割合で使用され、かつ前記３級アミノ基含有モノマー（ａ）が、共重合体（Ｂ）を構成する成分全体に対して８〜２０重量％の割合となるように使用される第２工程；および
前記共重合体（Ｂ）に存在する３級アミノ基を４級化し、共重合体（Ｂ）の４級アンモニウム塩を得る第３工程、
を含むことを特徴とする、カチオン性表面サイズ剤の製造方法。
（２）前記水溶性のフリーラジカル開始剤が過酸化水素であり、前記重金属塩が硫酸鉄（ＩＩ）である、（１）に記載の方法。
（３）前記第１工程において、共重合体（Ａ）に存在する３級アミノ基部分を、酸を用いて完全に中和し水溶液の形態にする、（１）または（２）に記載の方法。
（４）前記共重合体（Ａ）が、５０ｎｍ以下の平均粒子径を有する、（１）〜（３）のいずれかの項に記載の方法。
（５）前記共重合体（Ｂ）の４級アンモニウム塩が、１００ｎｍ以上の平均粒子径を有する、（１）〜（４）のいずれかの項に記載の方法。
（６）前記共重合体（Ｂ）に存在する３級アミノ基の５０モル％以上が４級化される、（１）〜（５）のいずれかの項に記載の方法。
（７）前記４級化が、エピクロルヒドリンを用いて行われる、（１）〜（６）のいずれかの項に記載の方法。
（８）前記３級アミノ基含有モノマー（ａ）が、ジアルキルアミノアルキル（メタ）アクリレートおよびジアルキルアミノアルキル（メタ）アクリルアミドからなる群より選択される少なくとも１種である、（１）〜（７）のいずれかの項に記載の方法。
（９）（１）〜（８）のいずれかの項に記載の方法によって製造される、カチオン性表面サイズ剤。
（１０）（９）に記載のカチオン性表面サイズ剤、またはこのサイズ剤と水溶性高分子化合物との混合物を、紙または板紙の表面に塗工する、紙または板紙の表面処理方法。
（１１）（１０）に記載の方法によって得られる、紙または板紙。
（１２）カチオン性表面サイズ剤を塗工する前の紙または板紙が、内添サイズ剤を含まない紙または板紙、ステキヒトサイズ度が２秒以下で且つ紙面ｐＨが６．５〜８．５の中性紙、あるいは２分Ｃｏｂｂ吸水度が１００ｇ／ｍ2以上で且つ紙面ｐＨが６．５〜８．５の中性板紙である、（１１）に記載の紙または板紙。
As a result of intensive studies to solve the above problems, the present inventors,
(1) 15 to 45% by weight of a tertiary amino group-containing monomer (a), 15 to 85% by weight of (meth) acrylic acid ester (b), and 0 to 70% by weight of styrenes (c) The step of obtaining a copolymer (A) by subjecting the monomer mixture to be solution-polymerized in the presence of a chain transfer agent, wherein the (meth) acrylic acid ester (b) has 4 to 18 ester moieties. A first step which is a chain alkyl having carbon atoms, a cyclic alkyl having 4 to 18 carbon atoms, or an aryl having 6 to 18 carbon atoms;
The copolymer (A) and the hydrophobic monomer (d) are polymerized in a redox system using a water-soluble free radical initiator and a heavy metal salt in the absence of a surfactant to obtain a copolymer ( B), wherein the copolymer (A) is used in a proportion of 30 to 70% by weight with respect to the total components constituting the copolymer (B), and the tertiary amino group-containing monomer ( a second step in which a) is used in an amount of 8 to 20% by weight based on the total components constituting the copolymer (B); and a tertiary amino present in the copolymer (B) A third step of quaternizing the group to obtain a quaternary ammonium salt of the copolymer (B);
A method for producing a cationic surface sizing agent, comprising:
(2) The method according to (1), wherein the water-soluble free radical initiator is hydrogen peroxide, and the heavy metal salt is iron (II) sulfate.
(3) In the first step, the tertiary amino group moiety present in the copolymer (A) is completely neutralized with an acid to form an aqueous solution. (1) or (2) Method.
(4) The method according to any one of (1) to (3), wherein the copolymer (A) has an average particle size of 50 nm or less.
(5) The method according to any one of (1) to (4), wherein the quaternary ammonium salt of the copolymer (B) has an average particle diameter of 100 nm or more.
(6) The method according to any one of (1) to (5), wherein 50 mol% or more of the tertiary amino groups present in the copolymer (B) are quaternized.
(7) The method according to any one of (1) to (6), wherein the quaternization is performed using epichlorohydrin.
(8) The tertiary amino group-containing monomer (a) is at least one selected from the group consisting of dialkylaminoalkyl (meth) acrylates and dialkylaminoalkyl (meth) acrylamides (1) to (7) The method according to any one of the items.
(9) A cationic surface sizing agent produced by the method according to any one of (1) to (8).
(10) A surface treatment method for paper or paperboard, wherein the cationic surface sizing agent according to (9) or a mixture of this sizing agent and a water-soluble polymer compound is applied to the surface of paper or paperboard.
(11) Paper or paperboard obtained by the method according to (10).
(12) The paper or paperboard before the application of the cationic surface sizing agent is paper or paperboard containing no internal sizing agent, the Steecht sizing degree is 2 seconds or less, and the paper surface pH is 6.5 to 8.5. The paper or paperboard according to (11), which is a neutral paperboard or a neutral paperboard having a 2-minute Cobb water absorption of 100 g / m 2 or more and a paper surface pH of 6.5 to 8.5.
本発明によれば、使用される環境、特に水の条件（硬度、ｐＨなど）や適用される紙の種類（紙、板紙など）に拘らず、優れた分散安定性を有し、かつ優れたサイズ性を付与するカチオン性表面サイズ剤を提供し得るという効果を奏する。 According to the present invention, regardless of the environment used, particularly the water conditions (hardness, pH, etc.) and the type of paper applied (paper, paperboard, etc.), it has excellent dispersion stability and is excellent. There is an effect that a cationic surface sizing agent that imparts sizing properties can be provided.
すなわち、第１工程および第２工程を経て共重合体（Ｂ）を得ることにより、共重合体（Ａ）と共重合体（Ｂ）の相溶性を向上することができる。また、共重合体（Ｂ）を４級アンモニウム塩の形態とすることにより、使用される水の硬度やｐＨによる影響を受けにくくなり、塗工液濃度まで希釈したときに凝集することなく、均一に分散するなどの効果を有するサイズ剤が得られる。したがって、内添サイズ剤を含まない紙または板紙、ステキヒトサイズ度が２秒以下の中性紙、あるいは２分Ｃｏｂｂ吸水度が１００ｇ／ｍ２以上の中性板紙に、塗工した場合でも表面サイズ剤が紙中全体に凝集分子で分散することなく、紙の表面に分布する量が増加するため、表面サイズ剤の疎水性を紙表面で十分発揮するものと考えられる。 That is, compatibility of the copolymer (A) and the copolymer (B) can be improved by obtaining the copolymer (B) through the first step and the second step. Further, by making the copolymer (B) in the form of a quaternary ammonium salt, it is less affected by the hardness and pH of the water used, and it is uniform without agglomeration when diluted to the coating solution concentration. Thus, a sizing agent having an effect such as being dispersed in an aqueous solution can be obtained. Therefore, even when coated on paper or paperboard that does not contain an internal sizing agent, neutral paper with a Steecht sizing degree of 2 seconds or less, or neutral paperboard with a 2-minute Cobb water absorption of 100 g / m 2 or more, the surface size Since the amount of the agent distributed on the paper surface increases without being dispersed by aggregated molecules throughout the paper, it is considered that the surface sizing agent exhibits the hydrophobicity sufficiently on the paper surface.
本発明に係るカチオン性表面サイズ剤の製造方法は、１５〜４５重量％の３級アミノ基含有モノマー（ａ）と、１５〜８５重量％の（メタ）アクリル酸エステル（ｂ）と、０〜７０重量％のスチレン類（ｃ）とを含有するモノマー混合物を、連鎖移動剤の存在下で溶液重合させて共重合体（Ａ）を得る工程であって、前記（メタ）アクリル酸エステル（ｂ）のエステル部分が、４〜１８個の炭素原子を有するアルキルである第１工程；
前記共重合体（Ａ）と疎水性モノマー（ｄ）とを、界面活性剤の不存在下で、水溶性のフリーラジカル開始剤と重金属塩とを用いる酸化還元系で重合させて共重合体（Ｂ）を得る工程であって、共重合体（Ａ）が共重合体（Ｂ）を構成する成分全体に対して３０〜７０重量％の割合で使用され、かつ前記３級アミノ基含有モノマー（ａ）が、共重合体（Ｂ）を構成する成分全体に対して８〜２０重量％の割合となるように使用される第２工程；および
前記共重合体（Ｂ）に存在する３級アミノ基を４級化し、共重合体（Ｂ）の４級アンモニウム塩を得る第３工程、
を含む。以下、本発明について詳細に説明する。
The method for producing a cationic surface sizing agent according to the present invention comprises 15 to 45% by weight of a tertiary amino group-containing monomer (a), 15 to 85% by weight of a (meth) acrylic acid ester (b), 0 to A step of polymerizing a monomer mixture containing 70% by weight of styrenes (c) in the presence of a chain transfer agent to obtain a copolymer (A), wherein the (meth) acrylic acid ester (b) A first step wherein the ester moiety is an alkyl having from 4 to 18 carbon atoms;
The copolymer (A) and the hydrophobic monomer (d) are polymerized in a redox system using a water-soluble free radical initiator and a heavy metal salt in the absence of a surfactant to obtain a copolymer ( B), wherein the copolymer (A) is used in a proportion of 30 to 70% by weight with respect to the total components constituting the copolymer (B), and the tertiary amino group-containing monomer ( a second step in which a) is used in an amount of 8 to 20% by weight based on the total components constituting the copolymer (B); and a tertiary amino present in the copolymer (B) A third step of quaternizing the group to obtain a quaternary ammonium salt of the copolymer (B);
including. Hereinafter, the present invention will be described in detail.
（カチオン性表面サイズ剤の製造方法）
（第１工程）
第１工程は、３級アミノ基含有モノマー（ａ）（以下、単に「ａ成分」と記載する場合がある）と、特定の（メタ）アクリル酸エステル（ｂ）（以下、単に「ｂ成分」と記載する場合がある）と、スチレン類（ｃ）（以下、単に「ｃ成分」と記載する場合がある）とを特定の割合で含有するモノマー混合物を、連鎖移動剤の存在下で溶液重合させて共重合体（Ａ）を得る工程である。
(Method for producing cationic surface sizing agent)
(First step)
The first step includes a tertiary amino group-containing monomer (a) (hereinafter sometimes simply referred to as “component a”) and a specific (meth) acrylic acid ester (b) (hereinafter simply referred to as “component b”). And a monomer mixture containing styrenes (c) (hereinafter sometimes simply referred to as “component c”) at a specific ratio in the presence of a chain transfer agent. In this step, the copolymer (A) is obtained.
本発明の製造方法に用いられる３級アミノ基含有モノマー（ａ成分）は、分子内に３級アミノ基を有し、後述の（メタ）アクリル酸エステル（ｂ）およびスチレン類（ｃ）と共重合可能なモノマーであれば、特に限定されない。このようなａ成分としては、例えば、ジアルキルアミノアルキル（メタ）アクリレート、ジアルキルアミノアルキル（メタ）アクリルアミドなどが挙げられる。 The tertiary amino group-containing monomer (component a) used in the production method of the present invention has a tertiary amino group in the molecule, and is combined with (meth) acrylic acid ester (b) and styrenes (c) described later. If it is a monomer which can superpose | polymerize, it will not specifically limit. Examples of such a component include dialkylaminoalkyl (meth) acrylate and dialkylaminoalkyl (meth) acrylamide.
ジアルキルアミノアルキル（メタ）アクリレートとしては、例えば、ジメチルアミノエチル（メタ）アクリレート、ジメチルアミノプロピル（メタ）アクリレート、ジエチルアミノエチル（メタ）アクリレート、ジメチルアミノプロピル（メタ）アクリレート、ジエチルアミノプロピル（メタ）アクリレートなどが挙げられる。 Examples of the dialkylaminoalkyl (meth) acrylate include dimethylaminoethyl (meth) acrylate, dimethylaminopropyl (meth) acrylate, diethylaminoethyl (meth) acrylate, dimethylaminopropyl (meth) acrylate, and diethylaminopropyl (meth) acrylate. Is mentioned.
ジアルキルアミノアルキル（メタ）アクリルアミドとしては、例えば、ジメチルアミノエチル（メタ）アクリルアミド、ジエチルアミノエチル（メタ）アクリルアミド、ジメチルアミノプロピル（メタ）アクリルアミド、ジエチルアミノプロピル（メタ）アクリルアミドなどが挙げられる。 Examples of the dialkylaminoalkyl (meth) acrylamide include dimethylaminoethyl (meth) acrylamide, diethylaminoethyl (meth) acrylamide, dimethylaminopropyl (meth) acrylamide, and diethylaminopropyl (meth) acrylamide.
これらａ成分の中でも、ジメチルアミノエチル（メタ）アクリレートあるいはジメチルアミノプロピル（メタ）アクリルアミドが好ましい。 Among these a components, dimethylaminoethyl (meth) acrylate or dimethylaminopropyl (meth) acrylamide is preferable.
ａ成分は、共重合体（Ａ）を構成するモノマー混合物中に、１５〜４５重量％の割合で含有される。ａ成分の割合が１５重量％未満の場合、共重合体（Ａ）の親水性が低下し、水中で均一に分散できなくなる。一方、ａ成分の割合が４５重量％を超える場合、共重合体（Ａ）の疎水性が低下し、得られるサイズ剤のサイズ性が低下する。ａ成分は、好ましくは１８〜４０重量％、より好ましくは２０〜３５量％の割合で含有される。 a component is contained in the monomer mixture which comprises a copolymer (A) in the ratio of 15 to 45 weight%. When the proportion of the component a is less than 15% by weight, the hydrophilicity of the copolymer (A) is lowered and cannot be uniformly dispersed in water. On the other hand, when the proportion of the component a exceeds 45% by weight, the hydrophobicity of the copolymer (A) is lowered, and the sizing property of the resulting sizing agent is lowered. The component a is preferably contained in a proportion of 18 to 40% by weight, more preferably 20 to 35% by weight.
ａ成分は、単独で用いてもよく、２種以上を併用してもよい。なお、２種以上を併用する場合、含有量は合計で上記範囲を満たすようにする。 A component may be used independently and may use 2 or more types together. In addition, when using 2 or more types together, content shall satisfy the said range in total.
本発明の製造方法に用いられる特定の（メタ）アクリル酸エステル（ｂ成分）は、（メタ）アクリル酸エステルのエステル部分が４〜１８個の炭素原子を有する鎖状アルキル、４〜１８個の炭素原子を有する環状アルキル、または６〜１８個の炭素原子を有するアリールであるもの、すなわち、ＣＨ2＝ＣＨ−ＣＯＯＲまたはＣＨ2＝Ｃ（ＣＨ3）−ＣＯＯＲのＲが、４〜１８個の炭素原子を有するアルキル基、４〜１８個の炭素原子を有する環状アルキル基、または６〜１８個の炭素原子を有するアリール基であるものである。 The specific (meth) acrylic acid ester (component b) used in the production method of the present invention is a chain alkyl having 4 to 18 carbon atoms in the ester portion of the (meth) acrylic acid ester, 4 to 18 Are cyclic alkyl having carbon atoms, or aryl having 6 to 18 carbon atoms, that is, CH 2 ═CH—COOR or CH 2 ═C (CH 3 ) —COOR R is 4 to 18 An alkyl group having a carbon atom, a cyclic alkyl group having 4 to 18 carbon atoms, or an aryl group having 6 to 18 carbon atoms.
このようなｂ成分としては、イソブチル（メタ）アクリレート、ｎ−ブチル（メタ）アクリレート、エチルヘキシル（メタ）アクリレート、ラウリル（メタ）アクリレート、セチル（メタ）アクリレート、ステアリル（メタ）アクリレート、シクロヘキシル（メタ）アクリレート、ベンジル（メタ）アクリレートなどが挙げられる。これらの中でも、イソブチル（メタ）アクリレート、ｎ−ブチル（メタ）アクリレートあるいはエチルヘキシル（メタ）アクリレートが好ましい。 As such b component, isobutyl (meth) acrylate, n-butyl (meth) acrylate, ethylhexyl (meth) acrylate, lauryl (meth) acrylate, cetyl (meth) acrylate, stearyl (meth) acrylate, cyclohexyl (meth) Examples thereof include acrylate and benzyl (meth) acrylate. Among these, isobutyl (meth) acrylate, n-butyl (meth) acrylate or ethylhexyl (meth) acrylate is preferable.
ｂ成分は、共重合体（Ａ）を構成するモノマー混合物中に、１５〜８５重量％の割合で含有される。ｂ成分の割合が１５重量％未満の場合、得られるサイズ剤のサイズ性が低下する。一方、ｂ成分の割合が８５重量％を超える場合、共重合体（Ａ）の親水性が低下し、水中で均一に分散できなくなる。ｂ成分は、好ましくは２０〜８０重量％、より好ましくは４０〜８０重量％の割合で含有される。 The component b is contained in a proportion of 15 to 85% by weight in the monomer mixture constituting the copolymer (A). When the ratio of b component is less than 15 weight%, the size property of the sizing agent obtained will fall. On the other hand, when the proportion of the component b exceeds 85% by weight, the hydrophilicity of the copolymer (A) is lowered and cannot be uniformly dispersed in water. The component b is preferably contained in a proportion of 20 to 80% by weight, more preferably 40 to 80% by weight.
ｂ成分は、単独で用いてもよく、２種以上を併用してもよい。なお、２種以上を併用する場合、含有量は合計で上記範囲を満たすようにする。 b component may be used independently and may use 2 or more types together. In addition, when using 2 or more types together, content shall satisfy the said range in total.
本発明の製造方法に用いられるスチレン類（ｃ成分）は、上記ａ成分およびｂ成分と共重合可能なものであれば、特に限定されない。ｃ成分としては、例えば、スチレン、α−メチルスチレン、ビニルトルエン、エチルビニルトルエン、クロルメチルスチレンなどが挙げられる。これらの中でも、スチレン、α−メチルスチレンあるいはビニルトルエンが好ましい。 The styrenes (component c) used in the production method of the present invention are not particularly limited as long as they can be copolymerized with the components a and b. Examples of the component c include styrene, α-methylstyrene, vinyl toluene, ethyl vinyl toluene, chloromethyl styrene, and the like. Among these, styrene, α-methylstyrene, or vinyl toluene is preferable.
ｃ成分は、共重合体（Ａ）を構成するモノマー混合物中に、０〜７０重量％の割合で含有される。ｃ成分の割合が７０重量％を超える場合、溶液重合に際して共重合性が悪くなる。共重合性が低下すると、表面サイズ剤の有効成分が凝集したミクロ粒子状となって紙表面に点在し、不均一な被覆しかできないため、サイズ効果が低減してしまう。ｃ成分は、好ましくは０〜５０重量％、より好ましくは０〜４０重量％の割合で含有される。 c component is contained in the monomer mixture which comprises a copolymer (A) in the ratio of 0 to 70 weight%. When the proportion of component c exceeds 70% by weight, the copolymerizability deteriorates during solution polymerization. When the copolymerizability is lowered, the active ingredient of the surface sizing agent is agglomerated microparticles and scattered on the paper surface, and only a non-uniform coating can be achieved, so the size effect is reduced. The component c is preferably contained in a proportion of 0 to 50% by weight, more preferably 0 to 40% by weight.
ｃ成分は、単独で用いてもよく、２種以上を併用してもよい。なお、２種以上を併用する場合、含有量は合計で上記範囲を満たすようにする。 c component may be used independently and may use 2 or more types together. In addition, when using 2 or more types together, content shall satisfy the said range in total.
さらに、モノマー混合物は、本発明の効果を阻害しない範囲で、ａ成分〜ｃ成分以外のモノマーを含んでいてもよい。このようなモノマーとしては、例えば、メチル（メタ）アクリレート、エチル（メタ）アクリレート、ｎ−プロピル（メタ）アクリレート、イソプロピル（メタ）アクリレートなどの短鎖アルキル（メタ）アクリレート；ヒドロキシプロピル（メタ）アクリレート、２−ヒドロキシエチル（メタ）アクリレートなどの水酸基含有（メタ）アクリレート；（メタ）アクリルアミド；アクリロニトリルなどのようなビニル基やアリル基を有する化合物が挙げられる。 Furthermore, the monomer mixture may contain monomers other than the components a to c as long as the effects of the present invention are not impaired. Examples of such monomers include short-chain alkyl (meth) acrylates such as methyl (meth) acrylate, ethyl (meth) acrylate, n-propyl (meth) acrylate, and isopropyl (meth) acrylate; hydroxypropyl (meth) acrylate , 2-hydroxyethyl (meth) acrylate and other hydroxyl group-containing (meth) acrylates; (meth) acrylamides; compounds having a vinyl group or an allyl group such as acrylonitrile.
共重合体（Ａ）は、上記ａ成分〜ｃ成分を含有するモノマー混合物を、連鎖移動剤の存在下で溶液重合させて得られる。モノマー混合物の溶液重合は特に限定されず、例えば、一般的なラジカル重合によって行われる。 The copolymer (A) is obtained by subjecting a monomer mixture containing the components a to c to solution polymerization in the presence of a chain transfer agent. The solution polymerization of the monomer mixture is not particularly limited, and is performed, for example, by general radical polymerization.
溶液重合の際に用いられる溶剤は、モノマー混合物の組成によって適宜選択され得、例えば、イソプロピルアルコール、ｎ−ブタノール、イソブタノール、ｔ−ブタノール、ｓｅｃ−ブタノール、アセトン、メチルエチルケトン、メチル−ｎ−プロピルケトン、３−メチル−２−ブタノール、ジエチルケトン、メチルイソプロピルケトン、メチルイソブチルケトン、ジイソプロピルケトン、エチルベンゼン、トルエンなどが挙げられる。これらの中でも、好ましくはイソプロピルアルコール、メチルイソブチルケトンあるいはトルエンが用いられる。 The solvent used in the solution polymerization can be appropriately selected depending on the composition of the monomer mixture, such as isopropyl alcohol, n-butanol, isobutanol, t-butanol, sec-butanol, acetone, methyl ethyl ketone, methyl-n-propyl ketone. , 3-methyl-2-butanol, diethyl ketone, methyl isopropyl ketone, methyl isobutyl ketone, diisopropyl ketone, ethylbenzene, toluene and the like. Of these, isopropyl alcohol, methyl isobutyl ketone or toluene is preferably used.
連鎖移動剤は、共重合体（Ａ）の重量平均分子量を制御するために用いられる。連鎖移動剤としては、油溶性連鎖移動剤（例えば、ｔ−ドデシルメルカプタン、ｎ−ドデシルメルカプタン、ｎ−オクチルメルカプタン、メルカプトプロピオン酸ドデシルエステルなどのメルカプタン類、クメン、四塩化炭素、α−メチルスチレンダイマー、ターピノーレンなど）、水溶性連鎖移動剤（例えば、メルカプトエタノール、チオグリコール酸およびその塩など）などが挙げられる。連鎖移動剤は、溶剤やモノマー混合物の組成によって適宜選択され得、その使用量は、所望の重量平均分子量を有する共重合体（Ａ）が得られるように、適宜決定され得る。 A chain transfer agent is used in order to control the weight average molecular weight of a copolymer (A). Examples of chain transfer agents include oil-soluble chain transfer agents (for example, mercaptans such as t-dodecyl mercaptan, n-dodecyl mercaptan, n-octyl mercaptan, mercaptopropionic acid dodecyl ester, cumene, carbon tetrachloride, α-methylstyrene dimer). And water-soluble chain transfer agents (for example, mercaptoethanol, thioglycolic acid and salts thereof), and the like. The chain transfer agent can be appropriately selected depending on the composition of the solvent and the monomer mixture, and the amount used can be appropriately determined so as to obtain a copolymer (A) having a desired weight average molecular weight.
重合開始剤としては、特に限定されず、アゾ系開始剤（例えば、アゾビスメチルブチロニトリル、ジメチルアゾビスイソブチレート、アゾビスジメチルバレロニトリル、アゾビスイソブチロニトリルなど）、過酸化物系重合開始剤（例えば、過酸化水素、過硫酸ベンゾイル、ｔ−ブチルパーオキシベンゾエート、ｔ−ブチルパーオキシイソプロピルモノカーボネート、ｔ−ブチルパーオキシ−２−エチルヘキサノエート、クメンヒドロペルオキシドなど）などが挙げられる。重合開始剤の使用量は、特に限定されず、モノマー混合物の組成によって適宜決定され得る。 The polymerization initiator is not particularly limited, and an azo initiator (for example, azobismethylbutyronitrile, dimethylazobisisobutyrate, azobisdimethylvaleronitrile, azobisisobutyronitrile, etc.), peroxide Polymerization initiators (for example, hydrogen peroxide, benzoyl persulfate, t-butyl peroxybenzoate, t-butyl peroxyisopropyl monocarbonate, t-butyl peroxy-2-ethylhexanoate, cumene hydroperoxide, etc.) Is mentioned. The usage-amount of a polymerization initiator is not specifically limited, It can determine suitably with the composition of a monomer mixture.
重合反応の温度や時間は、特に限定されず、溶剤、モノマー混合物の組成、用いる重合開始剤などによって、適宜設定され得る。重合反応は、通常８０〜１２０℃、好ましくは８５〜１１５℃で行われる。また、反応時間は、通常２〜６時間、好ましくは３〜５時間である。 The temperature and time of the polymerization reaction are not particularly limited, and can be appropriately set depending on the solvent, the composition of the monomer mixture, the polymerization initiator used, and the like. The polymerization reaction is usually performed at 80 to 120 ° C, preferably 85 to 115 ° C. Moreover, reaction time is 2 to 6 hours normally, Preferably it is 3 to 5 hours.
このようにして得られた共重合体（Ａ）は、次の工程に供するに際し、水に可溶化させることが好ましい。例えば、共重合体（Ａ）に存在する３級アミノ基部分を、塩酸、硫酸、酢酸などの酸を用いて完全に中和し、水溶液の形態にするのが好ましい。さらに、共重合体（Ａ）は、好ましくは５０ｎｍ以下、より好ましくは３０ｎｍ以下の平均粒子径を有する。 The copolymer (A) thus obtained is preferably solubilized in water when subjected to the next step. For example, the tertiary amino group moiety present in the copolymer (A) is preferably completely neutralized with an acid such as hydrochloric acid, sulfuric acid or acetic acid to form an aqueous solution. Furthermore, the copolymer (A) preferably has an average particle size of 50 nm or less, more preferably 30 nm or less.
（第２工程）
第２工程は、上記共重合体（Ａ）と疎水性モノマー（ｄ）（以下、単に「ｄ成分」と記載する場合がある）とを、界面活性剤を用いずに、特定の条件下で重合させて共重合体（Ｂ）を得る工程である。
(Second step)
In the second step, the copolymer (A) and the hydrophobic monomer (d) (hereinafter sometimes simply referred to as “d component”) are used under specific conditions without using a surfactant. This is a step of polymerizing to obtain a copolymer (B).
本発明の製造方法に用いられる疎水性モノマー（ｄ成分）は、共重合体（Ａ）と共重合可能なものであれば、特に限定されない。ｄ成分としては、例えば、スチレン、２−エチルヘキシル（メタ）アクリレート、メチル（メタ）アクリレート、ｎ−ブチル（メタ）アクリレート、イソブチル（メタ）アクリレート、ｔ−ブチル（メタ）アクリレートなどが挙げられる。 The hydrophobic monomer (d component) used in the production method of the present invention is not particularly limited as long as it is copolymerizable with the copolymer (A). Examples of the d component include styrene, 2-ethylhexyl (meth) acrylate, methyl (meth) acrylate, n-butyl (meth) acrylate, isobutyl (meth) acrylate, t-butyl (meth) acrylate, and the like.
第２工程において、共重合体（Ａ）は、共重合体（Ｂ）を構成する成分全体に対して３０〜７０重量％の割合で使用され、かつａ成分が共重合体（Ｂ）を構成する成分全体に対して８〜２０重量％の割合となるように使用される。共重合体（Ａ）およびａ成分を、特定の割合となるように使用することにより、良好なサイズ性および分散性を得ることができる。
共重合体（Ａ）は、共重合体（Ｂ）を構成する成分全体に対して好ましくは４０〜７０重量％の割合で使用され、かつａ成分が共重合体（Ｂ）を構成する成分全体に対して好ましくは８〜１８重量％の割合となるように使用される。
In the second step, the copolymer (A) is used in a proportion of 30 to 70% by weight with respect to the entire components constituting the copolymer (B), and the component a constitutes the copolymer (B). It is used so that it may become a ratio of 8-20 weight% with respect to the whole component to do. By using the copolymer (A) and the component a so as to have a specific ratio, good size and dispersibility can be obtained.
The copolymer (A) is preferably used in a proportion of 40 to 70% by weight with respect to the total components constituting the copolymer (B), and the a component is the total components constituting the copolymer (B). Preferably it is used so that it may become a ratio of 8-18 weight%.
共重合体（Ａ）とｄ成分との重合反応は、界面活性剤を用いずに、水溶性のフリーラジカル開始剤と重金属塩とを用いる酸化還元系、すなわちレドックス触媒を用いて行われる。共重合体（Ａ）とｄ成分との重合反応を、酸化還元系、すなわちレドックス触媒を用いて行うことにより、ｄ成分の単独重合体が合成されにくく、本発明において目的とする共重合体（Ａ）とｄ成分とのグラフト共重合体（共重合体（Ｂ））が合成されやすくなる。その結果、優れた分散性を有し、優れたサイズ性を付与し得るサイズ剤を得ることができる。また、界面活性剤を用いないことにより、界面活性剤によって分散されたｄ成分のみの重合体が合成されにくく、最終的に得られるサイズ剤にも界面活性剤が含まれないため、さらなるサイズ性付与効果の向上が期待できる。 The polymerization reaction of the copolymer (A) and the component d is carried out using a redox catalyst using a water-soluble free radical initiator and a heavy metal salt, that is, a redox catalyst, without using a surfactant. By carrying out the polymerization reaction of the copolymer (A) and the d component using a redox system, that is, a redox catalyst, it is difficult to synthesize the homopolymer of the d component, and the target copolymer ( A graft copolymer (copolymer (B)) of A) and d component is easily synthesized. As a result, a sizing agent having excellent dispersibility and capable of imparting excellent sizing properties can be obtained. Further, by not using a surfactant, it is difficult to synthesize a polymer containing only the d component dispersed by the surfactant, and the final sizing agent does not contain a surfactant, so that further sizing properties are achieved. Improvement of the grant effect can be expected.
水溶性のフリーラジカル開始剤としては、パーオキソ化合物、アゾ化合物、過酸化水素、過硫酸塩などが挙げられ、重金属塩としては、セリウム、マンガン、鉄（ＩＩ）などが挙げられる。これらの中でも、過酸化水素と硫酸鉄（ＩＩ）との組み合わせが好ましい。 Examples of water-soluble free radical initiators include peroxo compounds, azo compounds, hydrogen peroxide, persulfates, and examples of heavy metal salts include cerium, manganese, iron (II), and the like. Among these, a combination of hydrogen peroxide and iron (II) sulfate is preferable.
第２工程における重合反応の反応温度および反応時間は、特に限定されず、適宜設定され得る。重合反応は、通常７０〜９０℃、好ましくは７５〜９０℃で行われる。また、反応時間は、通常１〜５時間、好ましくは２〜４時間である。 The reaction temperature and reaction time of the polymerization reaction in the second step are not particularly limited and can be set as appropriate. The polymerization reaction is usually performed at 70 to 90 ° C, preferably 75 to 90 ° C. Moreover, reaction time is 1 to 5 hours normally, Preferably it is 2 to 4 hours.
（第３工程）
第３工程は、上記共重合体（Ｂ）に存在する３級アミノ基を４級化し、共重合体（Ｂ）の４級アンモニウム塩を得る工程である。
(Third step)
The third step is a step of quaternizing the tertiary amino group present in the copolymer (B) to obtain a quaternary ammonium salt of the copolymer (B).
共重合体（Ｂ）に存在する３級アミノ基のうち、４級化される割合は特に限定されないが、好ましくは５０モル％以上、より好ましくは６０モル％以上の３級アミノ基が４級化される。 The ratio of quaternization among the tertiary amino groups present in the copolymer (B) is not particularly limited, but preferably 50 mol% or more, more preferably 60 mol% or more of the tertiary amino groups are quaternary. It becomes.
４級化は、通常、エピクロルヒドリンやエピブロモヒドリンといったエピハロヒドリンなどの４級化剤を用いて行う。 Quaternization is usually performed using a quaternizing agent such as epihalohydrin such as epichlorohydrin or epibromohydrin.
このようにして得られた共重合体（Ｂ）の４級アンモニウム塩は、好ましくは１００ｎｍ以上、より好ましくは１００〜３００ｎｍの平均粒子径を有する。 The quaternary ammonium salt of the copolymer (B) thus obtained preferably has an average particle diameter of 100 nm or more, more preferably 100 to 300 nm.
＜カチオン性表面サイズ剤＞
本発明のカチオン性表面サイズ剤は、上述の第１工程〜第４工程を経て得られる。このようにして得られるカチオン性表面サイズ剤は、紙や板紙に塗工する際の環境、特に水の硬度やｐＨなどの影響を受けずに優れた分散安定性を有するため、凝集することなく紙表面に均一に塗布され得る。したがって、本発明のカチオン性表面サイズ剤は、紙や板紙に優れたサイズ性を付与することができる。
<Cationic surface sizing agent>
The cationic surface sizing agent of the present invention is obtained through the first to fourth steps described above. The cationic surface sizing agent obtained in this way has excellent dispersion stability without being affected by the environment when applied to paper or paperboard, in particular, the hardness or pH of water, so that it does not aggregate. It can be uniformly applied to the paper surface. Therefore, the cationic surface sizing agent of the present invention can impart excellent sizing properties to paper and paperboard.
本発明のカチオン性表面サイズ剤は、紙や板紙の表面に塗工する場合、単独で使用してもよく、水溶性高分子化合物と併用してもよい。併用する場合、好ましくは水溶性高分子化合物と本発明のカチオン性表面サイズ剤とが、重量比で５００：１〜１：１、より好ましくは１００：１〜５：１の割合で混合される。水溶性高分子化合物としては、例えば、澱粉、酵素変性澱粉、熱化学変性澱粉、酸化澱粉、エステル化澱粉、エーテル化澱粉（例えば、ヒドロキシエチル化澱粉など）、カチオン化澱粉などの澱粉類；ポリビニルアルコール、完全ケン化ポリビニルアルコール、部分ケン化ポリビニルアルコール、カルポキシル変性ポリビニルアルコール、シラノール変性ポリビニルアルコール、カチオン変性ポリビニルアルコール、末端アルキル変性ポリビニルアルコールなどのポリビニルアルコール類；ポリアクリルアミド、カチオン性ポリアクリルアミド、アニオン性ポリアクリルアミド、両性ポリアクリルアミドなどのポリアクリルアミド類；カルポキシメチルセルロース、ヒドロキシエチルセルロース、メチルセルロースなどのセルロース誘導体などが挙げられる。 The cationic surface sizing agent of the present invention may be used alone or in combination with a water-soluble polymer compound when applied to the surface of paper or paperboard. When used in combination, the water-soluble polymer compound and the cationic surface sizing agent of the present invention are preferably mixed at a weight ratio of 500: 1 to 1: 1, more preferably 100: 1 to 5: 1. . Examples of the water-soluble polymer compound include starches such as starch, enzyme-modified starch, thermochemically-modified starch, oxidized starch, esterified starch, etherified starch (for example, hydroxyethylated starch), cationized starch and the like; polyvinyl Polyvinyl alcohols such as alcohol, fully saponified polyvinyl alcohol, partially saponified polyvinyl alcohol, carboxy-modified polyvinyl alcohol, silanol-modified polyvinyl alcohol, cation-modified polyvinyl alcohol, and terminal alkyl-modified polyvinyl alcohol; polyacrylamide, cationic polyacrylamide, anionic Polyacrylamides such as polyacrylamide and amphoteric polyacrylamide; cellulose derivatives such as carboxymethylcellulose, hydroxyethylcellulose, and methylcellulose And the like.
本発明のカチオン性表面サイズ剤を塗工する紙や板紙は特に限定されず、任意の紙および板紙に塗工することができる。本発明のカチオン性表面サイズ剤は、好ましくは内添サイズ剤を含まない紙または板紙、ステキヒトサイズ度が２秒以下で且つ紙面ｐＨが６．５〜８．５の中性紙、２分Ｃｏｂｂ吸水度が１００ｇ／ｍ2以上で且つ紙面ｐＨが６．５〜８．５の中性板紙などの表面に塗工される。 The paper or paperboard on which the cationic surface sizing agent of the present invention is applied is not particularly limited, and can be applied to any paper and paperboard. The cationic surface sizing agent of the present invention is preferably a paper or paperboard containing no internal sizing agent, a neutral paper having a Steecht sizing degree of 2 seconds or less and a paper surface pH of 6.5 to 8.5, 2 minutes Cobb water absorption is 100 g / m 2 or more and paper surface pH is applied to the surface of neutral paperboard of 6.5 to 8.5.
本発明のカチオン性表面サイズ剤は、水の硬度やｐＨに影響されずに塗工できるため、非常に有用である。さらに、本発明のカチオン性表面サイズ剤が塗工された紙および板紙は、優れたサイズ性を有し、各種分野で使用される。 The cationic surface sizing agent of the present invention is very useful because it can be applied without being affected by the hardness and pH of water. Furthermore, the paper and paperboard coated with the cationic surface sizing agent of the present invention have excellent sizing properties and are used in various fields.
以下、実施例および比較例を挙げて本発明を具体的に説明するが、本発明はこれらの実施例に限定されるものではない。 EXAMPLES Hereinafter, although an Example and a comparative example are given and this invention is demonstrated concretely, this invention is not limited to these Examples.
実施例、比較例および表に記載された略号は、以下の化合物を示す。
ＤＭ：ジメチルアミノエチルメタクリレート
ＤＭＡＰＡＡ：ジメチルアミノプロピルアクリルアミド
Ｓｔ：スチレン
２ＥＨＡ：２−エチルヘキシルアクリレート
２ＥＨＭＡ：２−エチルヘキシルメタクリレート
ＭＭＡ：メチルメタクリレート
ＬＭＡ：ラウリルメタクリレート
ｎＢＡ：ｎ−ブチルアクリレート
ｎＢＭＡ：ｎ−ブチルメタクリレート
ｉＢＡ：ｉ−ブチルアクリレート
ｉＢＭＡ：ｉ−ブチルメタクリレート
ｔＢＭＡ：ｔ−ブチルメタクリレート
ＣＨＭＡ：シクロヘキシルメタクリレート
２ＨＥＡ：２−ヒドロキシエチルアクリレート
The abbreviations described in Examples, Comparative Examples and Tables indicate the following compounds.
DM: dimethylaminoethyl methacrylate DMAPAA: dimethylaminopropyl acrylamide St: styrene 2EHA: 2-ethylhexyl acrylate 2EHMA: 2-ethylhexyl methacrylate MMA: methyl methacrylate LMA: lauryl methacrylate nBA: n-butyl acrylate nBMA: n-butyl methacrylate iBA: i -Butyl acrylate iBMA: i-butyl methacrylate tBMA: t-butyl methacrylate CHMA: cyclohexyl methacrylate 2HEA: 2-hydroxyethyl acrylate
＜共重合体（Ａ）の合成＞
（合成例Ａ１）
２０重量部のジメチルアミノエチルメタクリレート（ＤＭ）、２０重量部の２−エチルヘキシルアクリレート（２ＥＨＡ）、６０重量部のスチレン（Ｓｔ）、連鎖移動剤として０．７重量部のｎ−ドデシルメルカプタン、および溶剤として３２重量部のトルエンを４つ口フラスコに投入して撹拌した。次いで、約１０５℃まで加熱し、開始剤として１重量部のｔ−ブチルパーオキシイソプロピルモノカーボネートを添加し約１１０℃で３時間反応を行った。次いで、得られた共重合体の３級アミノ基部分および残存する微量のＤＭを中和するため、８．５重量部の９０重量％酢酸および３００重量部の水を４つ口フラスコに投入した。次いで、加熱蒸留によりトルエンを留去した後、固形分濃度が２５重量％となるように水で希釈し、共重合体（Ａ１）を得た。
<Synthesis of copolymer (A)>
(Synthesis Example A1)
20 parts by weight dimethylaminoethyl methacrylate (DM), 20 parts by weight 2-ethylhexyl acrylate (2EHA), 60 parts by weight styrene (St), 0.7 parts by weight n-dodecyl mercaptan as chain transfer agent, and solvent 32 parts by weight of toluene was added to a four-necked flask and stirred. Subsequently, it heated to about 105 degreeC, 1 weight part t-butyl peroxy isopropyl monocarbonate was added as an initiator, and reaction was performed at about 110 degreeC for 3 hours. Subsequently, in order to neutralize the tertiary amino group portion and the remaining trace amount of DM of the obtained copolymer, 8.5 parts by weight of 90% by weight acetic acid and 300 parts by weight of water were charged into a four-necked flask. . Subsequently, toluene was distilled off by heating distillation, and then diluted with water so that the solid content concentration was 25% by weight to obtain a copolymer (A1).
（合成例Ａ２）
３０重量部のジメチルアミノエチルメタクリレート（ＤＭ）、３０重量部のｎ−ブチルメタクリレート（ｎＢＭＡ）、４０重量部のスチレン（Ｓｔ）、連鎖移動剤として０．５重量部のｔ−ドデシルメルカプタン、および溶剤として３２重量部のイソプロピルアルコールを４つ口フラスコに投入して撹拌した。次いで、約８５℃まで加熱し、開始剤として１重量部の２，２'−アゾビスイソブチロニトリルを添加し約９０℃で３時間反応を行った。次いで、得られた共重合体の３級アミノ基部分および残存する微量のＤＭを中和するため、１２．７重量部の９０重量％酢酸および３００重量部の水を４つ口フラスコに投入した。次いで、加熱蒸留によりイソプロピルアルコールを留去した後、固形分濃度が２５重量％となるように水で希釈し、共重合体（Ａ２）を得た。
(Synthesis Example A2)
30 parts by weight dimethylaminoethyl methacrylate (DM), 30 parts by weight n-butyl methacrylate (nBMA), 40 parts by weight styrene (St), 0.5 parts by weight t-dodecyl mercaptan as chain transfer agent, and solvent As 32 parts by weight of isopropyl alcohol was added to a four-necked flask and stirred. Subsequently, it heated to about 85 degreeC, 1 weight part 2,2'- azobisisobutyronitrile was added as an initiator, and reaction was performed at about 90 degreeC for 3 hours. Subsequently, in order to neutralize the tertiary amino group portion of the obtained copolymer and the remaining trace amount of DM, 12.7 parts by weight of 90% by weight acetic acid and 300 parts by weight of water were put into a four-necked flask. . Subsequently, after isopropyl alcohol was distilled off by heating distillation, it was diluted with water so that the solid content concentration was 25% by weight to obtain a copolymer (A2).
（合成例Ａ３〜Ａ８）
表１に記載の各成分を表１に記載の割合で用いたこと以外は、合成例Ａ２と同様の手順で共重合体（Ａ３）〜（Ａ８）を得た。なお、以下の表に記載の「ＤＭ中和率」は、得られた共重合体の３級アミノ基部分および残存する微量のＤＭを、どの程度中和したかを示す。例えば、ＤＭ中和率が１００ｍｏｌ％の場合、完全に中和されていることを示す。
(Synthesis Examples A3 to A8)
Copolymers (A3) to (A8) were obtained in the same procedure as in Synthesis Example A2, except that the components shown in Table 1 were used in the proportions shown in Table 1. The “DM neutralization rate” described in the following table indicates how much the tertiary amino group portion of the obtained copolymer and the remaining trace amount of DM were neutralized. For example, when the DM neutralization rate is 100 mol%, it indicates that the DM is completely neutralized.
（合成例Ａ９）
２０重量部のジメチルアミノエチルメタクリレート（ＤＭ）、８０重量部のスチレン（Ｓｔ）、連鎖移動剤として１．５重量部のｎ−ドデシルメルカプタン、および溶剤として３２重量部のイソプロピルアルコールを４つ口フラスコに投入して撹拌した。次いで、約８５℃まで加熱し、開始剤として１．５重量部の２，２'−アゾビスイソブチロニトリルを添加し約９０℃で３時間反応を行った。次いで、得られた共重合体の３級アミノ基部分および残存する微量のＤＭを中和するため、８．５重量部の９０重量％酢酸および３００重量部の水を４つ口フラスコに投入した。次いで、加熱蒸留によりイソプロピルアルコールを留去した後、固形分濃度が２５重量％となるように水で希釈し、共重合体（Ａ９）を得た。
(Synthesis Example A9)
4-neck flask with 20 parts by weight dimethylaminoethyl methacrylate (DM), 80 parts by weight styrene (St), 1.5 parts by weight n-dodecyl mercaptan as chain transfer agent, and 32 parts by weight isopropyl alcohol as solvent And stirred. Subsequently, it heated to about 85 degreeC, 1.5 weight part 2,2'- azobisisobutyronitrile was added as an initiator, and reaction was performed at about 90 degreeC for 3 hours. Subsequently, in order to neutralize the tertiary amino group portion and the remaining trace amount of DM of the obtained copolymer, 8.5 parts by weight of 90% by weight acetic acid and 300 parts by weight of water were charged into a four-necked flask. . Subsequently, after isopropyl alcohol was distilled off by heating distillation, it was diluted with water so that the solid content concentration was 25% by weight to obtain a copolymer (A9).
（合成例Ａ１０〜Ａ１８）
表１に記載の各成分を表１に記載の割合で用いたこと以外は、合成例Ａ９と同様の手順で共重合体（Ａ１０）〜（Ａ１８）を得た。
(Synthesis Examples A10 to A18)
Copolymers (A10) to (A18) were obtained in the same procedure as in Synthesis Example A9, except that the components shown in Table 1 were used in the proportions shown in Table 1.
＜カチオン性表面サイズ剤の合成＞
（実施例１）
合成例Ａ１で得られた４００重量部の共重合体（Ａ１）の水溶液（固形分濃度２５重量％）、２５重量部の水、および７．９重量部の９０重量％酢酸を４つ口フラスコに投入して約８５℃まで昇温した。次いで、２．２重量部の硫酸鉄(ＩＩ)水溶液（濃度１重量％）および１．８重量部のアスコルビン酸水溶液（濃度１重量％）を添加し、疎水性モノマーとして、１１重量部のメチルメタクリレート（ＭＭＡ）、６重量部のｎ−ブチルメタクリレート（ｎＢＭＡ）、６重量部の２−エチルヘキシルアクリレート（２ＥＨＡ）および２０重量部のスチレン（Ｓｔ）、１６重量部の過酸化水素水（濃度８重量％）を４つ口フラスコに投入し、約８５℃で３時間を行った。反応後、７．１重量部のエピクロルヒドリンを４つ口フラスコに添加し、約８５℃で３時間反応を行い、固形分濃度が３０重量％となるように水で希釈し、サイズ剤を得た。
<Synthesis of cationic surface sizing agent>
Example 1
Four-necked flask containing 400 parts by weight of the copolymer (A1) obtained in Synthesis Example A1 (solid content concentration 25% by weight), 25 parts by weight of water, and 7.9 parts by weight of 90% by weight acetic acid The temperature was raised to about 85 ° C. Next, 2.2 parts by weight of iron (II) sulfate aqueous solution (concentration 1% by weight) and 1.8 parts by weight of ascorbic acid aqueous solution (concentration 1% by weight) were added, and 11 parts by weight of methyl as a hydrophobic monomer was added. Methacrylate (MMA), 6 parts by weight n-butyl methacrylate (nBMA), 6 parts by weight 2-ethylhexyl acrylate (2EHA) and 20 parts by weight styrene (St), 16 parts by weight hydrogen peroxide (concentration 8 weights) %) Was put into a four-necked flask and carried out at about 85 ° C. for 3 hours. After the reaction, 7.1 parts by weight of epichlorohydrin was added to a four-necked flask, reacted at about 85 ° C. for 3 hours, and diluted with water to a solid content concentration of 30% by weight to obtain a sizing agent. .
（実施例２）
合成例Ａ２で得られた４００重量部の共重合体（Ａ２）の水溶液（固形分濃度２５重量％）および１５０重量部の水を４つ口フラスコに投入して約８５℃まで昇温した。次いで、５．２重量部の硫酸鉄(ＩＩ)水溶液（濃度１重量％）を添加し、疎水性モノマーとして、３６重量部のｎ−ブチルメタクリレート（ｎＢＭＡ）、３２重量部のｎ−ブチルアクリレート（ｎＢＡ）および３２重量部のスチレン（Ｓｔ）、３８重量部の過酸化水素水（濃度８重量％）を４つ口フラスコに投入し、約８５℃で３時間を行った。反応後、２１．４重量部のエピクロルヒドリンを４つ口フラスコに添加し、約８５℃で３時間反応を行い、固形分濃度が３０重量％となるように水で希釈し、サイズ剤を得た。
(Example 2)
400 parts by weight of the aqueous solution of copolymer (A2) obtained in Synthesis Example A2 (solid content concentration: 25% by weight) and 150 parts by weight of water were charged into a four-necked flask and heated to about 85 ° C. Next, 5.2 parts by weight of an aqueous iron (II) sulfate solution (concentration 1% by weight) was added, and 36 parts by weight of n-butyl methacrylate (nBMA), 32 parts by weight of n-butyl acrylate (n nBA), 32 parts by weight of styrene (St), and 38 parts by weight of hydrogen peroxide (concentration: 8% by weight) were charged into a four-necked flask, and the reaction was performed at about 85 ° C. for 3 hours. After the reaction, 21.4 parts by weight of epichlorohydrin was added to the four-necked flask, reacted at about 85 ° C. for 3 hours, and diluted with water so that the solid content concentration was 30% by weight to obtain a sizing agent. .
（実施例３〜８）
表２に記載の各成分を表２に記載の割合で用いたこと以外は、実施例１と同様の手順でサイズ剤を得た。なお、以下の表に記載の重合開始剤は、以下の通りである。
Ｉ１：過酸化水素水（濃度８重量％）
Ｉ２：硫酸鉄(ＩＩ)水溶液（濃度１重量％）
Ｉ３：アスコルビン酸水溶液（濃度１重量％）
Ｉ４：２，２’−アゾビス（２−メチルプロピオンジアミン）ジヒドロクロライド
(Examples 3 to 8)
A sizing agent was obtained in the same procedure as in Example 1 except that each component shown in Table 2 was used in the ratio shown in Table 2. In addition, the polymerization initiators described in the following table are as follows.
I1: Hydrogen peroxide solution (concentration 8% by weight)
I2: Iron (II) sulfate aqueous solution (concentration 1% by weight)
I3: Ascorbic acid aqueous solution (concentration 1% by weight)
I4: 2,2′-azobis (2-methylpropiondiamine) dihydrochloride
（比較例１）
合成例Ａ９で得られた４００重量部の共重合体（Ａ９）の水溶液（固形分濃度２５重量％）、３００重量部の水、および７．９重量部の９０重量％酢酸を４つ口フラスコに投入して約８５℃まで昇温した。次いで、７．１重量部のエピクロルヒドリンを４つ口フラスコに添加し、約８５℃で３時間反応を行った。次いで、７．９重量部の硫酸鉄(ＩＩ)水溶液（濃度１重量％）および６．２重量部のアスコルビン酸水溶液（濃度１重量％）を添加し、疎水性モノマーとして、４０重量部のメチルメタクリレート（ＭＭＡ）、７０重量部のｎ−ブチルメタクリレート（ｎＢＭＡ）、４０重量部の２−エチルヘキシルメタクリレート（２ＥＨＭＡ）、および５６重量部の過酸化水素水（濃度８重量％）を４つ口フラスコに投入し、約８５℃で３時間を行った。反応後、冷却して固形分濃度が３０重量％となるように水で希釈し、サイズ剤を得た。
(Comparative Example 1)
Four-neck flask containing 400 parts by weight of the copolymer (A9) obtained in Synthesis Example A9 (solid content concentration 25% by weight), 300 parts by weight of water, and 7.9 parts by weight of 90% by weight acetic acid The temperature was raised to about 85 ° C. Next, 7.1 parts by weight of epichlorohydrin was added to the four-necked flask and reacted at about 85 ° C. for 3 hours. Then, 7.9 parts by weight of an iron (II) sulfate aqueous solution (concentration 1% by weight) and 6.2 parts by weight of an ascorbic acid aqueous solution (concentration 1% by weight) were added, and 40 parts by weight of methyl as a hydrophobic monomer was added. Methacrylate (MMA), 70 parts by weight of n-butyl methacrylate (nBMA), 40 parts by weight of 2-ethylhexyl methacrylate (2EHMA), and 56 parts by weight of hydrogen peroxide (concentration 8% by weight) in a four-necked flask The mixture was charged at a temperature of about 85 ° C for 3 hours. After the reaction, the mixture was cooled and diluted with water so that the solid concentration was 30% by weight to obtain a sizing agent.
（比較例２）
合成例Ａ１０で得られた４００重量部の共重合体（Ａ１０）の水溶液（固形分濃度２５重量％）および５０重量部の水を４つ口フラスコに投入して約８５℃まで昇温した。次いで、２．８重量部の硫酸鉄(ＩＩ)水溶液（濃度１重量％）を添加し、疎水性モノマーとして、１８重量部のメチルメタクリレート（ＭＭＡ）、１７重量部のｎ−ブチルメタクリレート（ｎＢＭＡ）、１８重量部のｎ−ブチルアクリレート（ｎＢＡ）、および２０重量部の過酸化水素水（濃度８重量％）を４つ口フラスコに投入し、約８５℃で３時間を行った。反応後、８．９重量部のエピクロルヒドリンを４つ口フラスコに添加し、約８５℃で３時間反応を行い、固形分濃度が３０重量％となるように水で希釈し、サイズ剤を得た。
(Comparative Example 2)
400 parts by weight of the aqueous solution of copolymer (A10) obtained in Synthesis Example A10 (solid content concentration: 25% by weight) and 50 parts by weight of water were charged into a four-necked flask and heated to about 85 ° C. Next, 2.8 parts by weight of an aqueous iron (II) sulfate solution (concentration 1% by weight) was added, and 18 parts by weight of methyl methacrylate (MMA) and 17 parts by weight of n-butyl methacrylate (nBMA) were used as hydrophobic monomers. 18 parts by weight of n-butyl acrylate (nBA) and 20 parts by weight of hydrogen peroxide (concentration: 8% by weight) were charged into a four-necked flask, and the reaction was performed at about 85 ° C. for 3 hours. After the reaction, 8.9 parts by weight of epichlorohydrin was added to the four-necked flask, reacted at about 85 ° C. for 3 hours, and diluted with water so that the solid content concentration became 30% by weight to obtain a sizing agent. .
（比較例３〜１０）
表３に記載の各成分を表３に記載の割合で用いたこと以外は、比較例２と同様の手順でサイズ剤を得た。
(Comparative Examples 3 to 10)
A sizing agent was obtained in the same procedure as in Comparative Example 2 except that the components shown in Table 3 were used in the proportions shown in Table 3.
（比較例１１）
２５重量部のジメチルアミノエチルメタクリレート（ＤＭ）、１５重量部の２−エチルヘキシルメタクリレート（２ＥＨＭＡ）、６０重量部のスチレン（Ｓｔ）、連鎖移動剤として１．５重量部のｎ−ドデシルメルカプタン、および溶剤として３２重量部のイソプロピルアルコールを４つ口フラスコに投入して撹拌した。次いで、約８５℃まで加熱し、開始剤として１．５重量部の２，２'−アゾビスイソブチロニトリルを添加し約９０℃で３時間反応を行った。次いで、得られた共重合体の３級アミノ基部分および残存する微量のＤＭを中和するため、１０．６重量部の９０重量％酢酸および３００重量部の水を４つ口フラスコに投入した。次いで、加熱蒸留によりイソプロピルアルコールを留去した。イソプロピルアルコールを留去後、１１．９重量部のエピクロルヒドリンを添加して、８５℃で３時間反応を行った。次いで、冷却して固形分濃度が２５重量％となるように水で希釈し、サイズ剤を得た。なお、共重合体の３級アミノ基部分および残存する微量のＤＭの中和率は１００ｍｏｌ％であり、得られたサイズ剤（共重合体）の４級化率は８０ｍｏｌ％、平均粒子径は３０ｎｍ以下であった。
(Comparative Example 11)
25 parts by weight dimethylaminoethyl methacrylate (DM), 15 parts by weight 2-ethylhexyl methacrylate (2EHMA), 60 parts by weight styrene (St), 1.5 parts by weight n-dodecyl mercaptan as chain transfer agent, and solvent As 32 parts by weight of isopropyl alcohol was added to a four-necked flask and stirred. Subsequently, it heated to about 85 degreeC, 1.5 weight part 2,2'- azobisisobutyronitrile was added as an initiator, and reaction was performed at about 90 degreeC for 3 hours. Subsequently, in order to neutralize the tertiary amino group part and the remaining trace amount of DM of the obtained copolymer, 10.6 parts by weight of 90% by weight acetic acid and 300 parts by weight of water were put into a four-necked flask. . Subsequently, isopropyl alcohol was distilled off by heating distillation. After isopropyl alcohol was distilled off, 11.9 parts by weight of epichlorohydrin was added and the reaction was carried out at 85 ° C. for 3 hours. Subsequently, it cooled and diluted with water so that solid content concentration might be 25 weight%, and the sizing agent was obtained. The neutralization rate of the tertiary amino group portion of the copolymer and the remaining trace amount of DM is 100 mol%, the quaternization rate of the obtained sizing agent (copolymer) is 80 mol%, and the average particle size is It was 30 nm or less.
上記実施例および比較例で得られたサイズ剤について、サイズ性（ステキヒトサイズ度および２分Ｃｏｂｂ吸水度）および発泡性を、以下の方法で評価した。結果を表４に示す。 With respect to the sizing agents obtained in the above Examples and Comparative Examples, the sizing properties (Stechht sizing degree and 2-minute Cobb water absorption) and foaming properties were evaluated by the following methods. The results are shown in Table 4.
＜ステキヒトサイズ度＞
実施例および比較例で得られたサイズ剤が０．４重量％、酸化澱粉が５．０重量％および硬度６０ｐｐｍ（ＣａＣＯ3として）の水道水が９４．６重量％となるように混合して、それぞれ塗工液を調製した。次いで、内添サイズ剤が添加されていない中性上質原紙（坪量７０ｇ／ｍ2、ステキヒトサイズ度０秒、紙面ｐＨ７．６）の両面に、それぞれ得られた塗工液を、両面吸液量が３０ｇ／ｍ2となるように塗工した。次いで、回転式ドラムドライヤー（熊谷理機工業（株）製、ＫＲＫ回転型乾燥機）を用いて、９０℃で９０秒間乾燥して、塗工紙を得た。
これとは別に、上記塗工液それぞれを調整する際に、硬度２０００ｐｐｍ（ＣａＣＯ3として）の合成硬水を、塗工液の硬度が５００ｐｐｍとなるように添加して、高硬度塗工液を得た。この高硬度塗工液を、上記と同様の手順で中性上質原紙に塗工して塗工紙を得た。
得られた各塗工紙のステキヒトサイズ度を、ＪＩＳ Ｐ８１２２に準拠して測定した。
<Stick human sizing degree>
Mix so that the sizing agent obtained in Examples and Comparative Examples was 0.4% by weight, oxidized starch was 5.0% by weight, and tap water having a hardness of 60 ppm (as CaCO 3 ) was 94.6% by weight. A coating solution was prepared for each. Next, the obtained coating liquid was applied to both sides of a neutral high-quality base paper (basis weight 70 g / m 2 , Steecht size degree 0 second, paper surface pH 7.6) to which no internal sizing agent was added. Coating was performed so that the liquid amount was 30 g / m 2 . Subsequently, it was dried at 90 ° C. for 90 seconds using a rotary drum dryer (manufactured by Kumagai Riki Kogyo Co., Ltd., KRK rotary dryer) to obtain a coated paper.
Separately, when adjusting each of the above coating liquids, synthetic hard water having a hardness of 2000 ppm (as CaCO 3 ) is added so that the hardness of the coating liquid is 500 ppm to obtain a high hardness coating liquid. It was. This high-hardness coating solution was applied to neutral high-quality base paper in the same procedure as described above to obtain a coated paper.
The degree of sticky sizing of each coated paper obtained was measured according to JIS P8122.
＜２分Ｃｏｂｂ吸水度＞
実施例および比較例で得られたサイズ剤が０．２重量％および硬度６０ｐｐｍ（ＣａＣＯ3として）の水道水が９９．８重量％となるように混合して、それぞれ塗工液を調製した。次いで、内添サイズ剤が添加されたライナー用原紙（坪量１８０ｇ／ｍ2、２分Ｃｏｂｂ吸水度２１０ｇ／ｍ2、紙面ｐＨ７．２）の片面に、それぞれ得られた塗工液を、片面吸液量が１５ｇ／ｍ2となるように塗工した。次いで、上記回転式ドラムドライヤーを用いて、９０℃で９０秒間乾燥して、塗工紙を得た。
これとは別に、上記塗工液それぞれを調整する際に、硬度２０００ｐｐｍ（ＣａＣＯ3として）の合成硬水を、塗工液の硬度が５００ｐｐｍとなるように添加して、高硬度塗工液を得た。この高硬度塗工液を、上記と同様の手順で中性上質原紙に塗工して塗工紙を得た。
得られた各塗工紙の２分Ｃｏｂｂ吸水度を、ＪＩＳ Ｐ８１４０に準拠して測定した。
<2 minutes Cobb water absorption>
The sizing agents obtained in Examples and Comparative Examples were mixed so that the amount of tap water with 0.2 wt% and hardness of 60 ppm (as CaCO 3 ) would be 99.8 wt% to prepare coating solutions. Next, the obtained coating liquid was applied to one side of a liner base paper (basis weight 180 g / m 2 , 2 minutes Cobb water absorption 210 g / m 2 , paper surface pH 7.2) to which an internal sizing agent was added. Coating was performed so that the liquid absorption amount was 15 g / m 2 . Subsequently, it dried for 90 seconds at 90 degreeC using the said rotary drum dryer, and the coated paper was obtained.
Separately, when adjusting each of the above coating liquids, synthetic hard water having a hardness of 2000 ppm (as CaCO 3 ) is added so that the hardness of the coating liquid is 500 ppm to obtain a high hardness coating liquid. It was. This high-hardness coating solution was applied to neutral high-quality base paper in the same procedure as described above to obtain a coated paper.
The 2-minute Cobb water absorption of each coated paper obtained was measured in accordance with JIS P8140.
＜発泡性＞
上記ステキヒトサイズ度の評価で使用した塗工液および高硬度塗工液を、家庭用ミキサー（松下電器産業（株）製、ファイバーミキサー）に入れて、３分間撹拌した。撹拌を停止してから３分後の泡の高さを測定した。
<Foaming properties>
The coating liquid and the high-hardness coating liquid used in the evaluation of the above-mentioned Steecht sizing degree were placed in a household mixer (manufactured by Matsushita Electric Industrial Co., Ltd., fiber mixer) and stirred for 3 minutes. The height of the foam 3 minutes after the stirring was stopped was measured.
＜安定性試験＞
上記発泡性の評価に使用した水道水を用いた塗工液および合成硬水を用いた塗工液について、発泡性試験の後、２００メッシュの金網にて濾過し、残渣の重量から安定性を評価した。残渣が少ないほど、凝集物などが少なく分散安定性に優れている。
<Stability test>
About the coating liquid using the tap water used for the said foamability evaluation and the coating liquid using the synthetic hard water, after a foamability test, it filters with a 200 mesh metal-mesh, and evaluates stability from the weight of a residue. did. The smaller the residue, the less aggregates and the better the dispersion stability.
表４に示すように、本発明の製造方法によって得られたカチオン性表面サイズ剤が塗工された紙は、合成硬水を用いた場合でも、水道水を用いた場合とほとんど遜色のない優れたサイズ性を有し、２分Ｃｏｂｂ吸水度も低く水が吸収されにくいことがわかる。さらに、本発明の製造方法によって得られたカチオン性表面サイズ剤は、水道水および合成硬水のいずれを用いた場合も発泡性が低く、塗工作業性にも優れていることがわかる。また、水道水および合成硬水のいずれを用いた場合も濾過残渣量が少なく、塗工液中での安定性（分散安定性）に優れることがわかる。 As shown in Table 4, the paper coated with the cationic surface sizing agent obtained by the production method of the present invention was superior to the case of using tap water even when using synthetic hard water. It can be seen that it has sizing properties and the 2-minute Cobb water absorption is low, making it difficult for water to be absorbed. Furthermore, it can be seen that the cationic surface sizing agent obtained by the production method of the present invention has low foaming properties and excellent coating workability when either tap water or synthetic hard water is used. Moreover, it can be seen that the amount of filtration residue is small when either tap water or synthetic hard water is used, and the stability (dispersion stability) in the coating solution is excellent.
一方、本発明の製造方法以外の方法によって得られたカチオン性表面サイズ剤が塗工された紙は、相対的にサイズ度が低いことがわかる。また、比較的良好なサイズ度を有する場合でも（比較例２および７）、合成硬水を用いた場合には、サイズ度が半分程度まで低下することがわかる。また、２分Ｃｏｂｂ吸水度についても相対的に高く、特に、合成硬水を用いた場合には、非常に水が吸収されやすいことがわかる。さらに、発泡性についても、合成硬水を用いた場合には、非常に発泡しやすいことがわかる。また、水道水および合成硬水のいずれを用いた場合も濾過残渣量が多く、塗工液中での安定性（分散安定性）に劣ることがわかる。 On the other hand, it can be seen that the paper coated with the cationic surface sizing agent obtained by a method other than the production method of the present invention has a relatively low sizing degree. Moreover, even when it has a comparatively favorable sizing degree (comparative examples 2 and 7), when synthetic hard water is used, it turns out that a sizing degree falls to about a half. Further, the 2-minute Cobb water absorption is also relatively high, and it can be seen that water is very easily absorbed particularly when synthetic hard water is used. Furthermore, it can be seen that foaming is very easy to foam when synthetic hard water is used. In addition, it can be seen that when either tap water or synthetic hard water is used, the amount of filtration residue is large and the stability (dispersion stability) in the coating solution is poor.
Claims (12)
前記共重合体（Ａ）と疎水性モノマー（ｄ）とを、界面活性剤の不存在下で、水溶性のフリーラジカル開始剤と重金属塩とを用いる酸化還元系で重合させて共重合体（Ｂ）を得る工程であって、共重合体（Ａ）が共重合体（Ｂ）を構成する成分全体に対して３０〜７０重量％の割合で使用され、かつ前記３級アミノ基含有モノマー（ａ）が、共重合体（Ｂ）を構成する成分全体に対して８〜２０重量％の割合となるように使用される第２工程；および
前記共重合体（Ｂ）に存在する３級アミノ基を４級化し、共重合体（Ｂ）の４級アンモニウム塩を得る第３工程、
を含むことを特徴とする、カチオン性表面サイズ剤の製造方法。 Monomer containing 15 to 45% by weight of tertiary amino group-containing monomer (a), 15 to 85% by weight of (meth) acrylic acid ester (b), and 0 to 70% by weight of styrenes (c) The mixture is subjected to solution polymerization in the presence of a chain transfer agent to obtain a copolymer (A), wherein the ester portion of the (meth) acrylic acid ester (b) has 4 to 18 carbon atoms. A first step which is a chain alkyl having 4 to 18 carbon atoms, a cyclic alkyl having 6 to 18 carbon atoms, or an aryl having 6 to 18 carbon atoms;
The copolymer (A) and the hydrophobic monomer (d) are polymerized in a redox system using a water-soluble free radical initiator and a heavy metal salt in the absence of a surfactant to obtain a copolymer ( B), wherein the copolymer (A) is used in a proportion of 30 to 70% by weight with respect to the total components constituting the copolymer (B), and the tertiary amino group-containing monomer ( a second step in which a) is used in an amount of 8 to 20% by weight based on the total components constituting the copolymer (B); and a tertiary amino present in the copolymer (B) A third step of quaternizing the group to obtain a quaternary ammonium salt of the copolymer (B);
A method for producing a cationic surface sizing agent, comprising:
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| US14/007,902 US20140023872A1 (en) | 2011-03-29 | 2011-08-18 | Method for producing cationic surface sizing agent, and sizing agent obtained by method |
| PCT/JP2011/068672 WO2012132045A1 (en) | 2011-03-29 | 2011-08-18 | Method for producing cationic surface sizing agent, and sizing agent obtained by method |
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| JP2016017170A (en) * | 2014-07-11 | 2016-02-01 | 東亞合成株式会社 | Additive for lubricating oil and lubricating oil composition |
| JP2019011540A (en) * | 2017-06-29 | 2019-01-24 | ハリマ化成株式会社 | Manufacturing method of cationic surface size agent and cationic surface size agent |
| JP2019123968A (en) * | 2018-01-18 | 2019-07-25 | 星光Pmc株式会社 | Surface size agent for paper manufacturing and paper having coating layer containing same |
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| DE102016224415A1 (en) * | 2016-12-08 | 2018-06-14 | Leoni Kabel Gmbh | Line and method for producing such |
| CN109208379B (en) * | 2017-06-29 | 2022-08-26 | 哈利玛化成株式会社 | Method for producing cationic surface sizing agent and cationic surface sizing agent |
| JP6760344B2 (en) * | 2018-09-18 | 2020-09-23 | 栗田工業株式会社 | Surface sizing agent for papermaking |
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| JP4864418B2 (en) * | 2005-10-27 | 2012-02-01 | ハリマ化成株式会社 | Method for producing newsprint for offset printing and method for preventing plate smear in offset printing |
| US7988826B2 (en) * | 2006-03-30 | 2011-08-02 | Harima Chemicals, Inc. | Cationic surface sizing agent and paper coated with the same |
| JP5879041B2 (en) * | 2011-03-29 | 2016-03-08 | ハリマ化成株式会社 | Method for producing cationic surface sizing agent and sizing agent obtained by the method |
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| JP2019011540A (en) * | 2017-06-29 | 2019-01-24 | ハリマ化成株式会社 | Manufacturing method of cationic surface size agent and cationic surface size agent |
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| JP2019123968A (en) * | 2018-01-18 | 2019-07-25 | 星光Pmc株式会社 | Surface size agent for paper manufacturing and paper having coating layer containing same |
| JP6991460B2 (en) | 2018-01-18 | 2022-01-12 | 星光Pmc株式会社 | Paper with a surface sizing agent for papermaking and a coating layer containing it |
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| CN103459717A (en) | 2013-12-18 |
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