WO2012014749A1 - 吸水性樹脂の製造方法 - Google Patents
吸水性樹脂の製造方法 Download PDFInfo
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- WO2012014749A1 WO2012014749A1 PCT/JP2011/066455 JP2011066455W WO2012014749A1 WO 2012014749 A1 WO2012014749 A1 WO 2012014749A1 JP 2011066455 W JP2011066455 W JP 2011066455W WO 2012014749 A1 WO2012014749 A1 WO 2012014749A1
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- WIPO (PCT)
- Prior art keywords
- water
- dispersion medium
- absorbent resin
- aqueous solution
- polymerization
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- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
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- 239000001859 Ethyl hydroxyethyl cellulose Substances 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 1
- 239000004716 Ethylene/acrylic acid copolymer Substances 0.000 description 1
- 229920002581 Glucomannan Polymers 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- 239000004831 Hot glue Substances 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
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- 239000002202 Polyethylene glycol Substances 0.000 description 1
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- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
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- 238000000692 Student's t-test Methods 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- MZVQCMJNVPIDEA-UHFFFAOYSA-N [CH2]CN(CC)CC Chemical group [CH2]CN(CC)CC MZVQCMJNVPIDEA-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000003973 alkyl amines Chemical class 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 235000012501 ammonium carbonate Nutrition 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 229960005070 ascorbic acid Drugs 0.000 description 1
- 235000010323 ascorbic acid Nutrition 0.000 description 1
- 239000011668 ascorbic acid Substances 0.000 description 1
- 230000037396 body weight Effects 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- GYZLOYUZLJXAJU-UHFFFAOYSA-N diglycidyl ether Chemical group C1OC1COCC1CO1 GYZLOYUZLJXAJU-UHFFFAOYSA-N 0.000 description 1
- 125000005442 diisocyanate group Chemical group 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000004815 dispersion polymer Substances 0.000 description 1
- GKIPXFAANLTWBM-UHFFFAOYSA-N epibromohydrin Chemical compound BrCC1CO1 GKIPXFAANLTWBM-UHFFFAOYSA-N 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- CYKDLUMZOVATFT-UHFFFAOYSA-N ethenyl acetate;prop-2-enoic acid Chemical class OC(=O)C=C.CC(=O)OC=C CYKDLUMZOVATFT-UHFFFAOYSA-N 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 235000019326 ethyl hydroxyethyl cellulose Nutrition 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 239000007863 gel particle Substances 0.000 description 1
- 229940046240 glucomannan Drugs 0.000 description 1
- 229930182478 glucoside Natural products 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 125000003055 glycidyl group Chemical group C(C1CO1)* 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 description 1
- 238000003898 horticulture Methods 0.000 description 1
- 229920013819 hydroxyethyl ethylcellulose Polymers 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- TYQCGQRIZGCHNB-JLAZNSOCSA-N l-ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(O)=C(O)C1=O TYQCGQRIZGCHNB-JLAZNSOCSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 125000005641 methacryl group Chemical group 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical compound C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 description 1
- WVFLGSMUPMVNTQ-UHFFFAOYSA-N n-(2-hydroxyethyl)-2-[[1-(2-hydroxyethylamino)-2-methyl-1-oxopropan-2-yl]diazenyl]-2-methylpropanamide Chemical compound OCCNC(=O)C(C)(C)N=NC(C)(C)C(=O)NCCO WVFLGSMUPMVNTQ-UHFFFAOYSA-N 0.000 description 1
- JXTPJDDICSTXJX-UHFFFAOYSA-N n-Triacontane Natural products CCCCCCCCCCCCCCCCCCCCCCCCCCCCCC JXTPJDDICSTXJX-UHFFFAOYSA-N 0.000 description 1
- QYZFTMMPKCOTAN-UHFFFAOYSA-N n-[2-(2-hydroxyethylamino)ethyl]-2-[[1-[2-(2-hydroxyethylamino)ethylamino]-2-methyl-1-oxopropan-2-yl]diazenyl]-2-methylpropanamide Chemical compound OCCNCCNC(=O)C(C)(C)N=NC(C)(C)C(=O)NCCNCCO QYZFTMMPKCOTAN-UHFFFAOYSA-N 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 150000002918 oxazolines Chemical class 0.000 description 1
- 150000002921 oxetanes Chemical class 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- JRKICGRDRMAZLK-UHFFFAOYSA-L persulfate group Chemical group S(=O)(=O)([O-])OOS(=O)(=O)[O-] JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 description 1
- ACVYVLVWPXVTIT-UHFFFAOYSA-N phosphinic acid Chemical compound O[PH2]=O ACVYVLVWPXVTIT-UHFFFAOYSA-N 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920000056 polyoxyethylene ether Polymers 0.000 description 1
- 229940051841 polyoxyethylene ether Drugs 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000007717 redox polymerization reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 150000003333 secondary alcohols Chemical class 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 229940032094 squalane Drugs 0.000 description 1
- 238000010972 statistical evaluation Methods 0.000 description 1
- 150000003462 sulfoxides Chemical class 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 229940104261 taurate Drugs 0.000 description 1
- XOAAWQZATWQOTB-UHFFFAOYSA-N taurine Chemical compound NCCS(O)(=O)=O XOAAWQZATWQOTB-UHFFFAOYSA-N 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- ISIJQEHRDSCQIU-UHFFFAOYSA-N tert-butyl 2,7-diazaspiro[4.5]decane-7-carboxylate Chemical compound C1N(C(=O)OC(C)(C)C)CCCC11CNCC1 ISIJQEHRDSCQIU-UHFFFAOYSA-N 0.000 description 1
- 150000004685 tetrahydrates Chemical class 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 150000003573 thiols Chemical class 0.000 description 1
- DVKJHBMWWAPEIU-UHFFFAOYSA-N toluene 2,4-diisocyanate Chemical compound CC1=CC=C(N=C=O)C=C1N=C=O DVKJHBMWWAPEIU-UHFFFAOYSA-N 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 230000005068 transpiration Effects 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920003169 water-soluble polymer Polymers 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/12—Polymerisation in non-solvents
- C08F2/16—Aqueous medium
- C08F2/18—Suspension polymerisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/32—Polymerisation in water-in-oil emulsions
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/04—Acids, Metal salts or ammonium salts thereof
- C08F20/06—Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/10—Esters
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/52—Amides or imides
- C08F20/54—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
- C08F20/56—Acrylamide; Methacrylamide
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/04—Acids; Metal salts or ammonium salts thereof
- C08F220/06—Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/52—Amides or imides
- C08F220/54—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
- C08F220/56—Acrylamide; Methacrylamide
Definitions
- the present invention relates to a method for producing a water absorbent resin and a water absorbent resin obtained thereby. More specifically, in a method for producing a water-absorbent resin comprising at least two stages of reversed-phase suspension polymerization, a raw material component, in particular, a odor derived from a petroleum hydrocarbon dispersion medium is obtained from a water-absorbent resin obtained by a conventional technique.
- the present invention relates to a method for producing a water-absorbent resin that is further reduced and a water-absorbent resin obtained thereby.
- Water-absorbing resin is widely used in sanitary materials such as disposable diapers and sanitary napkins, daily necessaries such as pet sheets, industrial materials such as water-absorbing sheets for food and water-stopping materials for cables, and water retention agents for greening / agriculture / horticulture. ing.
- Sanitary materials such as disposable diapers and sanitary napkins are generally composed of top sheets, back sheets, hot melt adhesives, stretch materials, water absorbent resins, pulp fibers, etc., and many synthetic resins and modifiers are used. Odor derived from the raw material components may be felt. Since these sanitary materials are worn on the human body, even if they have a slight odor, they give unpleasant feeling to the user, so that no bromide is desired.
- the water-absorbing resin also has a slight odor derived from substances used in its production process, and is likely to be emitted when absorbed, so it is considered desirable to reduce the odor.
- water-absorbing resins used in sanitary materials include polyacrylic acid partial neutralized products, starch-acrylic acid graft polymer neutralized products, starch-acrylonitrile graft polymer hydrolysates, and vinyl acetate-acrylic acid esters.
- a saponified product of a copolymer is known.
- aqueous solution polymerization method As a method for producing such a water absorbent resin, an aqueous solution polymerization method, a reverse phase suspension polymerization method, and the like are known.
- a water-absorbent resin produced by a legal method it is considered that the main cause of the odor is derived from the dispersion medium.
- an internal cross-linking agent for an ⁇ , ⁇ -unsaturated carboxylic acid and an alkali metal salt aqueous solution thereof in a petroleum hydrocarbon solvent using a radical polymerization initiator is used.
- a method for producing a water-absorbing resin characterized by using a sucrose fatty acid ester as a protective colloid agent see Patent Document 1
- a radical polymerization initiator In the case where an aqueous solution of 25% by mass or more of an ⁇ , ⁇ -unsaturated carboxylic acid and an alkali metal salt thereof is polymerized in a hydrocarbon solvent in the presence or absence of an internal crosslinking agent, HLB 2-16 is used as a surfactant.
- Manufacturing methods characterized by the use of polyglycerin fatty acid esters (see Patent Document 2) and the like are known. The odor of the obtained water-absorbent resin was not sufficiently low.
- the present inventors have used a water-soluble ethylenically unsaturated monomer in a petroleum hydrocarbon dispersion medium to which no surfactant is added in the reverse phase suspension polymerization method.
- the aqueous solution of the monomer is dispersed, and a surfactant is added to the obtained dispersion to disperse it further, followed by polymerization (see Patent Document 3), or two or more stages of reversed-phase suspension polymerization.
- a surfactant is added to a dispersion obtained by dispersing a water-soluble ethylenically unsaturated monomer aqueous solution in a petroleum hydrocarbon dispersion medium.
- a surfactant is added to a dispersion obtained by dispersing a water-soluble ethylenically unsaturated monomer aqueous solution in a petroleum hydrocarbon dispersion medium.
- An object of the present invention relates to a method for producing a water-absorbent resin and a water-absorbent resin obtained thereby. More specifically, in a method for producing a water-absorbent resin comprising at least two stages of reversed-phase suspension polymerization, a raw material component, in particular, a odor derived from a petroleum hydrocarbon dispersion medium is obtained from a water-absorbent resin obtained by a conventional technique. In comparison with the above, it is an object of the present invention to provide a method for producing a water-absorbing resin further reduced and a water-absorbing resin obtained thereby.
- a method of producing a water-absorbent resin by at least two-stage reversed-phase suspension polymerization wherein the first-stage polymerization of at least two-stage reversed-phase suspension polymerization comprises: (A) A water-soluble ethylenically unsaturated monomer aqueous solution containing a hydrophilic polymer dispersant is dissolved in a petroleum hydrocarbon dispersion medium in which a hydrophobic polymer dispersant is dissolved or dispersed, and no surfactant is present.
- Hydrophobic polymer dispersant is maleic anhydride modified polyethylene, maleic anhydride modified polypropylene, maleic anhydride modified ethylene / propylene copolymer, maleic anhydride / ethylene copolymer, maleic anhydride / propylene copolymer, It is at least one selected from the group consisting of maleic anhydride / ethylene / propylene copolymer, polyethylene, polypropylene, ethylene / propylene copolymer, oxidized polyethylene, oxidized polypropylene and oxidized ethylene / propylene copolymer.
- Item 4. The method for producing a water-absorbent resin according to any one of Items 1 to 3, wherein Item 5.
- Item 6. Item 1.
- the water-soluble ethylenically unsaturated monomer is at least one selected from the group consisting of acrylic acid and salts thereof, methacrylic acid and salts thereof, and acrylamide.
- the petroleum hydrocarbon dispersion medium is at least one selected from the group consisting of aliphatic hydrocarbons and alicyclic hydrocarbons having 6 to 8 carbon atoms.
- Item 8. Item 8.
- the present invention it is possible to provide a method for producing a water-absorbing resin in which odors derived from raw material components, particularly petroleum-based hydrocarbon dispersion media, are further reduced, and a water-absorbing resin obtained thereby.
- the cause of the odor at the time of water absorption of the water absorbent resin obtained by reverse phase suspension polymerization is mainly the dispersion medium remaining in the water absorbent resin particles.
- the dispersion medium that is the oil phase is incorporated into the droplets of the aqueous monomer solution.
- O / W / O (oil / water / oil) type droplets are generated, and the O / W / O droplets are polymerized while being stabilized, so that the dispersion medium is included.
- the present inventors have found that this is caused by the generation of capsule-like water-absorbing resin particles.
- the method for producing a water-absorbent resin of the present invention comprises a water-soluble ethylenic solvent containing a water-soluble radical polymerization initiator in the absence of a surfactant and in the presence of a hydrophobic polymer-based dispersant when performing reverse phase suspension polymerization.
- a saturated monomer aqueous solution is primarily dispersed in a petroleum hydrocarbon dispersion medium
- a hydrophilic polymer dispersant is present in the monomer aqueous solution so that O / W / O (oil / water / oil) is present.
- the O / W / O type droplet is an abbreviation of (Oil in Water) in Oil, in which fine droplets of the oil phase are dispersed in the water phase droplets, and the water phase droplets further become the oil phase.
- the state is dispersed. That is, it is formed from the innermost oil phase, the intermediate water phase, and the outermost oil phase.
- the production method of the present application comprises at least two stages of reversed-phase suspension polymerization, and the first-stage polymerization of at least two-stage reversed-phase suspension polymerization comprises the following (A) to (C): Including a process.
- a water-soluble ethylenically unsaturated monomer aqueous solution containing a hydrophilic polymer dispersant is dissolved in a petroleum hydrocarbon dispersion medium in which a hydrophobic polymer dispersant is dissolved or dispersed, and no surfactant is present.
- the “remaining amount of petroleum hydrocarbon dispersion medium” is a value measured by a measurement method described later.
- the present invention is a water-soluble ethylenically unsaturated monomer aqueous solution
- “monomer aqueous solution” refers to “water-soluble ethylenically unsaturated monomer aqueous solution”.
- dispenser medium refers to “petroleum hydrocarbon dispersion medium”
- hydrophilic and hydrophobic polymer dispersion in the absence of a surfactant, and in a hydrophilic and hydrophobic polymer dispersion.
- Primary dispersion which is mixed and dispersed in the presence of an agent, and a “secondary dispersion” in which the surfactant is added in the next step (B) to stabilize the dispersion with the surfactant. It is characterized in that the aqueous solution of the monomer is dispersed and reverse phase suspension polymerization is performed, and the amount of the residual dispersion medium is reduced by suppressing the generation of O / W / O type droplets as compared with the conventional one.
- Examples of the water-soluble ethylenically unsaturated monomer used in the step (A) include (meth) acrylic acid [“(meth) acryl” means “acryl” and “methacryl”. The same shall apply hereinafter), monomers having an acid group such as 2- (meth) acrylamide-2-methylpropanesulfonic acid and maleic acid, and salts thereof; (meth) acrylamide, N, N-dimethyl (meth) acrylamide, 2 Nonionic unsaturated monomers such as hydroxyethyl (meth) acrylate and N-methylol (meth) acrylamide; amino group-containing unsaturated monomers such as diethylaminoethyl (meth) acrylate and diethylaminopropyl (meth) acrylate and the like And the like. These may be used alone or in combination of two or more.
- water-soluble ethylenically unsaturated monomers preferred are (meth) acrylic acid and salts thereof and (meth) acrylamide from the viewpoint of easy industrial availability.
- the acid group may be neutralized and used as a salt.
- the alkaline compound used when neutralizing the monomer having an acid group to form a salt include compounds such as lithium, sodium, potassium, and ammonium. More specifically, sodium hydroxide, potassium hydroxide, lithium hydroxide, sodium carbonate, ammonium carbonate and the like can be mentioned.
- the degree of neutralization is preferably 30 to 90 mol% of the acid group of the water-soluble ethylenically unsaturated monomer.
- the degree of neutralization is lower than 30 mol%, the acid groups are not easily ionized and the water absorption ability may be lowered, which is not preferable.
- the degree of neutralization exceeds 90 mol%, there is a possibility that a safety problem may occur when used as a sanitary material.
- the neutralization timing is generally performed in a monomer state from the viewpoint of uniformity, but the neutralization is performed by adding the alkaline compound to the polymer after the monomer polymerization, so-called post-medium You may use sum together.
- the water-soluble ethylenically unsaturated monomer is used as an aqueous solution.
- the monomer concentration of the water-soluble ethylenically unsaturated monomer aqueous solution is preferably 20% by mass to saturated concentration.
- the water-soluble ethylenically unsaturated monomer aqueous solution may contain a chain transfer agent and the like as necessary.
- chain transfer agent examples include compounds such as thiols, thiolic acids, secondary alcohols, hypophosphorous acid and phosphorous acid. These may be used alone or in combination of two or more.
- Examples of petroleum hydrocarbon dispersion media include n-hexane, n-heptane, 2-methylhexane, 3-methylhexane, 2,3-dimethylpentane, 3-ethylpentane, and n-octane.
- 8 aliphatic hydrocarbons such as cyclohexane, methylcyclohexane, cyclopentane, methylcyclopentane, trans-1,2-dimethylcyclopentane, cis-1,3-dimethylcyclopentane, trans-1,3-dimethylcyclopentane, etc.
- Examples include alicyclic hydrocarbons, aromatic hydrocarbons such as benzene, toluene, and xylene.
- n-hexane, n-heptane, 2-methylhexane, 3-methylhexane, n-octane and the like having 6 to 8 carbon atoms.
- Aliphatic hydrocarbons C6-C8 alicyclic hydrocarbons such as cyclohexane, methylcyclopentane, and methylcyclohexane are more preferably used.
- These hydrocarbon dispersion media may be used independently and may use 2 or more types together.
- the state of W / O type reverse phase suspension in the present invention is good, a suitable particle size is easily obtained, industrial availability is easy, and the quality is stable.
- n-heptane and cyclohexane are preferably used.
- a suitable result can be obtained by using commercially available Exol heptane (manufactured by ExxonMobil Co., Ltd .: containing n-heptane and isomeric hydrocarbons of 75 to 85%). .
- the amount of petroleum hydrocarbon dispersion medium used is usually a water-soluble ethylenically unsaturated monomer aqueous solution from the viewpoint of uniformly dispersing a water-soluble ethylenically unsaturated monomer aqueous solution and facilitating control of the polymerization temperature.
- the amount is preferably 50 to 600 parts by weight, more preferably 50 to 400 parts by weight, and still more preferably 50 to 200 parts by weight with respect to 100 parts by weight.
- step (A) when the water-soluble ethylenically unsaturated monomer aqueous solution is added to the petroleum hydrocarbon dispersion medium for primary dispersion in the absence of the surfactant, the presence of the hydrophobic polymer dispersant is present.
- the residual amount of the petroleum hydrocarbon dispersion medium can be lowered to a lower level.
- the hydrophobic polymer-based dispersant it is preferable to select and use one that dissolves or disperses with respect to the petroleum-based hydrocarbon dispersion medium to be used.
- the viscosity average molecular weight is 20,000 or less, preferably 10,000 or less, more preferably 5,000 or less.
- maleic anhydride modified polyethylene maleic anhydride modified polypropylene, maleic anhydride modified ethylene / propylene copolymer, maleic anhydride / ethylene copolymer, maleic anhydride / propylene copolymer, maleic anhydride / Ethylene / propylene copolymer, polyethylene, polypropylene, ethylene / propylene copolymer, oxidized polyethylene, oxidized polypropylene, oxidized ethylene / propylene copolymer, ethylene / acrylic acid copolymer, ethyl cellulose, ethyl hydroxyethyl cellulose, anhydrous Examples thereof include maleated polybutadiene and anhydrous maleated EPDM (ethylene / propylene / diene terpolymer).
- maleic anhydride modified polyethylene maleic anhydride modified polypropylene, maleic anhydride modified ethylene / propylene copolymer, maleic anhydride / ethylene copolymer, maleic anhydride / propylene copolymer, maleic anhydride / ethylene -At least one selected from the group consisting of propylene copolymer, polyethylene, polypropylene, ethylene / propylene copolymer, oxidized polyethylene, oxidized polypropylene and oxidized ethylene / propylene copolymer is preferable.
- the amount added is preferably 5 parts by mass or less, more preferably 0.01 to 3 parts by mass, based on 100 parts by mass of the water-soluble ethylenically unsaturated monomer aqueous solution. 0.05 to 2 parts by mass is more preferable.
- the amount of the hydrophobic polymer dispersant added is more than 5 parts by mass, it is not economical because it is not economical.
- the dispersion medium After adding the hydrophobic polymer dispersant to the petroleum hydrocarbon dispersion medium, the dispersion medium is once heated to partially dissolve or disperse the hydrophobic polymer dispersant. It is important to add an aqueous monomer solution. After heating, the dispersion medium is cooled, and even if the hydrophobic polymer dispersant is partially or completely precipitated and dispersed in white, the aqueous monomer solution There is no problem to add.
- the water-soluble ethylenically unsaturated monomer aqueous solution is added to the petroleum-based hydrocarbon dispersion medium and dispersed, it is dispersed by stirring, but the stirring conditions vary depending on the desired dispersed droplet size, so they are generally determined. It is not possible.
- the dispersed droplet diameter can be adjusted by the type of the stirring blade, the blade diameter, the rotational speed, and the like.
- stirring blade examples include a propeller blade, a paddle blade, an anchor blade, a turbine blade, a fiddler blade, a ribbon blade, a full zone blade (manufactured by Shinko Pantech Co., Ltd.), and a max blend blade (manufactured by Sumitomo Heavy Industries, Ltd.). Supermix (produced by Satake Chemical Machinery Co., Ltd.) can be used.
- the present application is characterized in that, in the primary dispersion, not only the hydrophobic polymer dispersant is present in the dispersion medium but also the hydrophilic polymer dispersant is present in the monomer aqueous solution.
- the hydrophilic polymer-based dispersant is preferably used in a state of being added and dissolved and mixed in advance in the water-soluble ethylenically unsaturated monomer aqueous solution.
- the monomer aqueous solution containing the hydrophilic polymer-based dispersant is O / W / O type particle generation can be suppressed to a lower level by primary dispersion in a petroleum hydrocarbon dispersion medium in the presence of the above-described hydrophobic polymer dispersant and in the absence of a surfactant. .
- polyvinyl pyrrolidone abbreviation “PVP”
- polyvinyl alcohol abbreviation “PVA”
- polyglycerin abbreviation “CPU”
- polyacrylate or the like
- PVP polyvinyl pyrrolidone
- PVA polyvinyl alcohol
- polyglycerin polyglycerin
- polyacrylate or the like
- PVP polyvinyl pyrrolidone
- PVA polyvinyl alcohol
- polyglycerin polyglycerin
- polyacrylate polyacrylate
- these may be used alone or in combination of two or more.
- polyvinylpyrrolidone and polyvinyl alcohol are particularly preferable because they are easy to handle in terms of solubility in water and the like and are easily effective.
- the preferred amount of the hydrophilic polymer dispersant varies depending on the type and molecular weight of the hydrophilic polymer dispersant to be used. On the other hand, it is preferably 0.1 to 7 parts by mass, more preferably 0.3 to 5 parts by mass, and most preferably 0.5 to 3 parts by mass. If the amount used is less than 0.1 parts by mass, the effect of reducing the amount of the remaining dispersion medium cannot be obtained sufficiently. If it is more than 7.0 parts by mass, the viscosity of the aqueous monomer solution increases, and the target droplets In order to obtain the diameter, it is necessary to greatly increase the stirring speed, which is not preferable because O / W / O type droplets are easily generated.
- the molecular weight and the like of the hydrophilic polymer dispersant are not particularly limited as long as they can be dissolved and added to the monomer aqueous solution.
- K-15 to K-120 can be used as a grade for polyvinylpyrrolidone, but K-30 to K-90 are easy to use, particularly from the viewpoint of the effect of reducing the residual dispersion medium.
- the degree of saponification is not particularly limited, but the degree of saponification is preferably 85% or more from the viewpoint of reducing the amount of residual dispersion medium.
- the polyvinyl alcohol that is suitably used those having a degree of polymerization of about 100 to 3000 are easy to use from the viewpoint of the effect of reducing the residual dispersion medium and from the viewpoint of use after dissolution.
- polyvinylpyrrolidone and polyvinyl alcohol are sometimes used as water-soluble thickeners, but in this application, the effects are different from those of so-called water-soluble polymer thickeners.
- cellulose derivatives such as hydroxyethyl cellulose and ethyl cellulose, guar gum, natural polysaccharides of glucomannan, etc. are not observed to reduce the amount of residual dispersion medium even when added to the monomer aqueous solution.
- the hydrophilic polymer dispersant can protect the droplet surface from the inside (water phase side) of the monomer droplet, It is presumed that the droplets are further stabilized as compared with the techniques of Patent Documents 3 and 4, and not only the inclusion of the dispersion medium but also the dissolution of the dispersion medium into the droplets is prevented.
- the surfactant is added to the primary dispersion obtained in the step (A), and the aqueous water-soluble ethylenically unsaturated monomer aqueous solution is further secondary dispersed in the petroleum hydrocarbon dispersion medium. (Process (B))
- Examples of the surfactant used in the step (B) include sorbitan fatty acid ester, polyoxyethylene sorbitan fatty acid ester, polyglycerin fatty acid ester, polyoxyethylene glycerin fatty acid ester, sucrose fatty acid ester, sorbitol fatty acid ester, polyoxyethylene.
- Sorbitol fatty acid ester polyoxyethylene alkyl ether, polyoxyethylene alkyl phenyl ether, polyoxyethylene castor oil, polyoxyethylene hydrogenated castor oil, alkylallyl formaldehyde condensed polyoxyethylene ether, polyoxyethylene polyoxypropyl alkyl ether, polyethylene glycol Fatty acid esters, alkyl glucosides, N-alkyl gluconamides, polyoxyethylene fatty acid amides, And nonionic surfactants such as polyoxyethylene alkylamine, fatty acid salt, alkylbenzene sulfonate, alkylmethyl taurate, polyoxyethylene alkylphenyl ether sulfate, polyoxyethylene alkyl ether sulfate, polyoxyethylene Anionic surfactants such as alkyl ether sulfonic acid and its salt, polyoxyethylene alkyl phenyl ether phosphoric acid and its salt, polyoxyethylene alkyl ether phosphoric acid and its
- At least one selected from the group consisting of polyglycerin fatty acid ester, sucrose fatty acid ester and sorbitan fatty acid ester is used from the viewpoint of dispersion stability of the water-soluble ethylenically unsaturated monomer aqueous solution. preferable.
- the addition amount of the surfactant used in the step (B) is preferably 0.01 to 5 parts by mass, and 0.05 to 3 parts by mass with respect to 100 parts by mass of the water-soluble ethylenically unsaturated monomer aqueous solution. More preferred. When the addition amount of the surfactant is less than 0.01 parts by mass, the dispersion stability of the aqueous monomer solution is lowered, and this is not preferable.
- the form of the surfactant added in the step (B) is not particularly limited, but a method of diluting or dissolving the surfactant in a small amount of a dispersion medium in advance is preferable because the dispersion can be stabilized in a short time.
- the stirring rotation speed of a stirring blade can be increased.
- the final dispersed droplet diameter is determined by the stirring rotation speed after the speed increase, and the particle size in the first stage polymerization stage is determined.
- the dispersion obtained in the step (B) is subjected to radical polymerization to obtain water-containing water-absorbent resin particles in a hydrogel state dispersed in a petroleum hydrocarbon dispersion medium. (Process (C))
- water-soluble radical polymerization initiator examples include persulfates such as potassium persulfate, ammonium persulfate and sodium persulfate; peroxides such as hydrogen peroxide; 2,2′-azobis (2-amidinopropane) dihydrochloride Salt, 2,2′-azobis [N- (2-carboxyethyl) -2-methylpropiondiamine] tetrahydrate, 2,2′-azobis (1-imino-1-pyrrolidino-2-methylpropane) dihydrochloride And azo compounds such as 2,2′-azobis [2-methyl-N- (2-hydroxyethyl) -propionamide] and the like.
- persulfates such as potassium persulfate, ammonium persulfate and sodium persulfate
- peroxides such as hydrogen peroxide
- 2,2′-azobis (2-amidinopropane) dihydrochloride Salt 2,2′-azobis [N- (2-carbox
- the water-soluble radical polymerization initiator may be used as a redox polymerization initiator in combination with a reducing agent such as sulfite or ascorbic acid.
- the amount of the water-soluble radical polymerization initiator used is usually 0.01 to 1 part by mass per 100 parts by mass of the water-soluble ethylenically unsaturated monomer. When the amount is less than 0.01 parts by mass, the polymerization rate is low. When the amount is more than 1 part by mass, a rapid polymerization reaction occurs, which is not preferable.
- the addition timing of the water-soluble radical polymerization initiator is not particularly limited, but it is preferably added in advance to the water-soluble ethylenically unsaturated monomer aqueous solution from the viewpoint of uniformity.
- an internal crosslinking agent may be added to the aqueous monomer solution during the polymerization.
- (poly) ethylene glycol ““(poly)” means with or without the prefix “poly”. The same shall apply hereinafter), polyols such as 1,4-butanediol, glycerin, trimethylolpropane, etc., and a polymer having two or more vinyl groups obtained by reacting a polyol with an unsaturated acid such as acrylic acid or methacrylic acid.
- Unsaturated esters bisacrylamides such as N, N'-methylenebisacrylamide, (poly) ethylene glycol diglycidyl ether, (poly) ethylene glycol triglycidyl ether, (poly) glycerin diglycidyl ether, (poly) glycerin tri Examples thereof include polyglycidyl compounds containing two or more glycidyl groups such as glycidyl ether, (poly) propylene glycol polyglycidyl ether, and (poly) glycerol polyglycidyl ether. These may be used alone or in combination of two or more.
- the amount added is preferably 3 parts by mass or less, more preferably 1 part by mass or less, and more preferably 0.001 to 0.1 parts per 100 parts by mass of the water-soluble ethylenically unsaturated monomer. Part by mass is more preferable. When the addition amount exceeds 3 parts by mass, the crosslinking becomes excessive and the water absorption performance becomes too low, which is not preferable.
- the internal cross-linking agent is preferably added in advance to the water-soluble ethylenically unsaturated monomer aqueous solution.
- the reaction temperature in the reverse phase suspension polymerization in the present invention varies depending on the kind and amount of the polymerization initiator used, and thus cannot be determined unconditionally, but is preferably 20 to 100 ° C., more preferably 40 to 90. ° C.
- the reaction temperature is lower than 20 ° C, the polymerization rate may be lowered, and when the reaction temperature is higher than 100 ° C, a rapid polymerization reaction occurs, which is not preferable.
- particles in a hydrogel state that can be a water-absorbing resin with a small amount of residual dispersion medium are obtained.
- the obtained water-containing gel particles may be dehydrated, dried and post-crosslinked to obtain water-absorbent resin particles.
- This polymerization is the first stage polymerization, and the dispersion containing the water-containing gel obtained by the polymerization is used.
- the addition of an aqueous monomer solution to the slurry of the medium to carry out the second and subsequent polymerizations increases the effect of reducing the residual dispersion medium, and the size of the resulting water-absorbent resin particle size. Is advantageous in that it is suitable for hygiene applications.
- the size of the particles after the first stage polymerization obtained by the polymerization of the water-soluble ethylenically unsaturated monomer is such that the median particle diameter is 20 from the viewpoint of obtaining an appropriate aggregate particle diameter in the multistage polymerization. Is preferably from 200 to 200 ⁇ m, more preferably from 30 to 150 ⁇ m, still more preferably from 40 to 100 ⁇ m.
- the median particle diameter of the first-stage polymer particles is a value measured according to the measurement method described below for particles obtained by dehydration and drying after the completion of the first-stage polymerization.
- the water-soluble ethylenically unsaturated monomer aqueous solution of the second stage polymerization is added to the polymerization slurry that has completed the step (C), and then the second stage reverse phase suspension polymerization is carried out.
- the procedure starts by first depositing at least part of the surfactant after the completion of the first stage polymerization.
- Surfactant when deposited, has the ability to stabilize water phase droplets in the oil phase inherent in the surfactant (or the ability to stabilize oil phase droplets in the opposite water phase). lose.
- the precipitation method is not particularly limited, and examples thereof include a method of reducing the temperature of the slurry after polymerization by cooling. Before adding the water-soluble ethylenically unsaturated monomer aqueous solution in the second-stage polymerization, at least part of the surfactant is allowed to precipitate, so that the monomer aqueous solution in the added second-stage polymerization is reduced.
- the droplets are not stabilized in the dispersion medium and are absorbed by the gel-like primary particles, whereby the primary particles are aggregated to obtain a particle size suitable for hygiene materials.
- the precipitation of the surfactant suppresses the generation of new O / W / O type droplets upon addition of the monomer aqueous solution in the second stage polymerization, and increases the amount of residual dispersion medium. It will be suppressed. Therefore, by performing the second stage polymerization with almost no increase in the amount of residual dispersion medium, the amount of water-absorbing resin obtained is substantially increased with respect to the residual dispersion medium taken in by the first stage polymerization, so that the water absorption obtained The amount of residual dispersion medium of the resin becomes smaller.
- the hydrophobic polymer-based dispersant dissolved with the surfactant cannot be dissolved in the dispersion medium when cooled, and precipitates in the dispersion medium when the second monomer aqueous solution is added. In some cases.
- a water-soluble ethylenically unsaturated monomer aqueous solution of the second-stage polymerization containing a water-soluble radical polymerization initiator is stirred and mixed and absorbed in the first-stage polymerization gel. -Aggregate.
- the water-soluble ethylenically unsaturated monomer for the second stage polymerization those similar to those exemplified as the water-soluble ethylenically unsaturated monomer for the first stage polymerization can be used.
- the degree of neutralization, neutralized salt and monomer aqueous solution concentration may be the same as or different from the water-soluble ethylenically unsaturated monomer of the first stage polymerization.
- the polymerization initiator added to the water-soluble ethylenically unsaturated monomer aqueous solution in the second stage polymerization can also be appropriately selected from those exemplified as the polymerization initiator used in the first stage polymerization. .
- an internal cross-linking agent, a chain transfer agent, etc. may be added to the water-soluble ethylenically unsaturated monomer aqueous solution of the second stage polymerization, if necessary, and exemplified in the case of the first stage polymerization.
- the addition amount of the water-soluble ethylenically unsaturated monomer in the second stage polymerization is determined from the viewpoint of obtaining appropriate aggregated particles and the reduction in the amount of residual dispersion medium. It is preferably 1.0 to 2.0 times, more preferably 1.1 to 1.8 times the body weight. If it is less than 1.0 times, the obtained amount is reduced, and the effect of reducing the amount of the remaining dispersion medium is thin and undesirable. On the other hand, if the ratio is more than 2.0 times, the first-stage polymer particles cannot absorb the monomer aqueous solution of the second-stage polymerization, and fine powder is generated, so that agglomerated particles having an appropriate medium particle size cannot be obtained. Not good
- the stirring in the reverse phase suspension polymerization of the second stage polymerization may be performed as long as the whole is uniformly mixed.
- the median particle size of the agglomerated particles can be controlled according to the precipitation state of the surfactant and the amount of the ethylenically unsaturated monomer in the second stage polymerization relative to the ethylenically unsaturated monomer in the first stage polymerization. it can.
- the median particle size of the aggregated particles suitable for hygiene materials is preferably 200 to 600 ⁇ m, more preferably 250 to 500 ⁇ m, and even more preferably 300 to 450 ⁇ m.
- the mixture After adding the monomer aqueous solution of the second stage polymerization, the mixture is heated and polymerized by radical polymerization.
- the reaction temperature in the reverse phase suspension polymerization of the second stage polymerization also varies depending on the type and amount of the polymerization initiator and cannot be determined unconditionally, but is preferably 20 to 100 ° C., more preferably 40 to 90 ° C. It is.
- the dispersion medium may be used after the first stage polymerization is completed. It may be preferable to add to the polymerization system.
- the amount of the petroleum hydrocarbon dispersion medium used for the reverse phase suspension polymerization is less than 50 parts by weight with respect to 100 parts by weight of the water-soluble ethylenically unsaturated monomer aqueous solution, uniform dispersion and temperature control are possible. Therefore, if this balance is lost by adding the aqueous monomer solution for the second stage polymerization, it is preferable to add the dispersion medium in advance after the completion of the first stage polymerization.
- the total amount of the monomer aqueous solution (the monomer aqueous solution for the first-stage polymerization). It is preferable to add the dispersion medium so that the W / O ratio obtained by dividing (amount + amount of monomer aqueous solution of the second stage polymerization) by the amount of the dispersion medium is less than 1.7, more preferably less than 1.4.
- aggregation of particles in the second stage polymerization tends to occur excessively, so that the median particle size increases and a water absorbent resin having an optimum particle size may not be obtained.
- the mechanism is not clear, but if the amount of the dispersion medium is not sufficient, it is presumed that the aggregation of particles is promoted by the adhesiveness of polyvinyl alcohol and polyglycerin existing on the particle surface. .
- the timing of adding the dispersion medium is not particularly limited, but it is preferable to add a low temperature dispersion medium after the completion of the first stage polymerization in order to achieve a cooling effect.
- a multistage reverse phase suspension polymerization may be carried out by carrying out the polymerization reaction of the third and subsequent stages in the same manner as the second stage reverse phase suspension polymerization as described above.
- a crosslinking agent containing two or more functional groups having reactivity with the functional group derived from the water-soluble ethylenically unsaturated monomer after the reverse phase suspension polymerization.
- a cross-linking agent and reacting after polymerization By adding a cross-linking agent and reacting after polymerization, the cross-linking density of the surface layer of the water-absorbent resin particles can be increased, and various performances such as water absorption capacity under pressure, water absorption speed, gel strength, etc. can be improved. Performance is added.
- the post-crosslinking agent used for the crosslinking reaction is not particularly limited as long as it can react with the functional group derived from the water-soluble ethylenically unsaturated monomer used for the polymerization.
- the post-crosslinking agent used include, for example, polyols such as ethylene glycol, propylene glycol, 1,4-butanediol, trimethylolpropane, glycerin, polyoxyethylene glycol, polyoxypropylene glycol, and polyglycerin; (poly) Polyethylene such as ethylene glycol diglycidyl ether, (poly) ethylene glycol triglycidyl ether, (poly) glycerin diglycidyl ether, (poly) glycerin triglycidyl ether, (poly) propylene glycol polyglycidyl ether, (poly) glycerol polyglycidyl ether Glycidyl compounds; haloepoxy
- the post-crosslinking agent is added in an amount of preferably 0.01 to 5 parts by mass, more preferably 0.02 to 3 parts per 100 parts by mass of the total amount of water-soluble ethylenically unsaturated monomers subjected to polymerization. Part by mass.
- the addition amount of the post-crosslinking agent is less than 0.01 parts by mass, it is not possible to improve various performances such as water absorption capacity under pressure, water absorption rate, gel strength, etc. of the resulting water absorbent resin. This is not preferable because the water absorption capacity is too low.
- the post-crosslinking agent may be added as it is or as an aqueous solution, but if necessary, it may be added as a solution using a hydrophilic organic solvent as a solvent.
- a hydrophilic organic solvent include lower alcohols such as methyl alcohol, ethyl alcohol, n-propyl alcohol, isopropyl alcohol and propylene glycol, ketones such as acetone and methyl ethyl ketone, and ethers such as diethyl ether, dioxane and tetrahydrofuran. Amides such as N, N-dimethylformamide, and sulfoxides such as dimethyl sulfoxide. These hydrophilic organic solvents may be used alone or in combination of two or more or as a mixed solvent with water.
- the timing for adding the post-crosslinking agent is not particularly limited as long as it is after the completion of polymerization.
- the post-crosslinking reaction is preferably carried out in the presence of water in the range of 1 to 200 parts by weight with respect to 100 parts by weight of the water-absorbent resin in the dehydration / drying step after polymerization. More preferably, it is carried out in the presence of 10 to 50 parts by weight of water.
- water content when the post-crosslinking agent is added post-crosslinking in the particle surface layer of the water-absorbent resin can be more suitably performed, and excellent water absorption performance can be exhibited.
- the temperature in the post-crosslinking reaction is preferably 50 to 250 ° C, more preferably 60 to 180 ° C, still more preferably 60 to 140 ° C, and still more preferably 70 to 120 ° C.
- the drying step may be performed under normal pressure or under reduced pressure, and may be performed under an air stream such as nitrogen in order to increase drying efficiency.
- the drying temperature is preferably 70 to 250 ° C, more preferably 80 to 180 ° C, further preferably 80 to 140 ° C, and still more preferably 90 to 130 ° C.
- the drying temperature is preferably 60 to 100 ° C, more preferably 70 to 90 ° C.
- the water content of the water-absorbent resin after drying is 20% by mass or less, and preferably 10% by mass or less from the viewpoint of imparting fluidity.
- an inorganic active agent such as amorphous silica powder may be added.
- the median particle diameter, moisture content, and amount of residual dispersion medium (amount of petroleum hydrocarbon dispersion medium remaining inside the water absorbent resin particles) of the water absorbent resins obtained in each Example and Comparative Example are shown below.
- the method was evaluated. Note that the amount of the residual dispersion medium described in Patent Document 4 is sometimes measured because the absolute value of the residual dispersion medium amount has decreased to 500 ppm or less, and extraction from the water-absorbent resin is more sufficiently performed. Improved method.
- Median particle diameter 50 g of a water-absorbing resin is passed through a JIS standard sieve with a sieve opening of 250 ⁇ m, and when the amount remaining on the sieve is 50% by mass or more, a combination of ⁇ > sieves In the case of less than 50% by mass, the median particle diameter was measured using a combination of ⁇ > sieves.
- the mass of the water-absorbent resin remaining on each sieve is calculated as a percentage by mass with respect to the total amount, and the mass of the water-absorbent resin remaining on the sieve opening and the sieve is calculated by integrating in order from the larger particle size.
- the relationship between percentage and integrated value was plotted on a logarithmic probability paper. By connecting the plots on the probability paper with a straight line, the particle diameter corresponding to an integrated mass percentage of 50 mass% was defined as the median particle diameter.
- Residual Dispersion Medium Amount The residual dispersion medium from the water-absorbing resin charged in the sample bottle is compared with the conventional measurement method of Patent Document 4 so that the residual dispersion medium amount can be measured at a lower level. In order to extract the amount more fully, the swelling ratio was increased, and phosphoric acid was added to improve the swelling gel so that the swollen gel was easily dissolved.
- 0.2 g of the above dispersion medium was precisely weighed into a 50 ml screw bottle, and the above cooled DMF was added thereto to make a total of 20 g, which was precisely weighed and stirred with a stirrer chip to obtain a standard sample solution 1.
- This standard sample solution 1 was also cooled by an ice water bath.
- 0.2 g of the above standard sample solution 1 was precisely weighed into a 50 ml screw bottle, and the above cooled DMF was added thereto to make a total of 20 g, precisely weighed, and stirred with a stirrer chip to obtain standard sample solution 2.
- This standard sample solution 2 was also cooled by an ice water bath. From the standard sample solution 2, 0.02, 0.05, 0.1, and 0.5 g and 0.02 g from the standard sample solution 1 were purified in a 20 ml vial (No. 5, manufactured by Marmu). The cooled DMF was added thereto, and the total volume of each vial was adjusted to 3.8 g (4 mL). Further, 5 mL of the 25% by mass phosphoric acid aqueous solution was added to each vial, and it was capped with a septum rubber and an aluminum cap, and then the bottle was shaken and stirred.
- both reagents should be sufficiently cooled, sealed with an aluminum cap or the like, and then mixed thoroughly. Also noted.
- the vial was heated at 110 ° C. for 2 hours, and 1 ml of the gas phase was sampled so as not to cool and injected into a gas chromatograph to obtain a chromatogram. (Uses a headspace autosampler) Based on the charged amount, the concentration of the standard sample solution was determined, the charged amount of the dispersion medium in each vial was calculated, and a calibration curve was created from the charged amount and the peak area of the chromatogram. (Note that when a mixture of petroleum hydrocarbons was used as the dispersion medium, a plurality of peaks appeared, so a calibration curve was created using the total area value and the charged amount.)
- the vial was heated at 110 ° C. for 2 hours, and 1 ml of the gas phase was sampled so as not to cool and injected into a gas chromatograph to obtain a chromatogram. (Uses a headspace autosampler) Based on the peak area of the obtained chromatogram, the amount of dispersion medium contained in the charged sample amount (actually measured value of 0.10 g) is calculated from the calibration curve created earlier, and the amount of dispersion medium contained per gram of sample is calculated. Converted to [ppm].
- the conditions of the gas chromatograph used for the measurement of the residual dispersion medium amount in the present invention are as follows. Model: GC-14A + HSS2B (headspace autosampler) manufactured by Shimadzu Corporation Filler: Squalane 25% Shimalite (NAW) (101) 80-100 mesh Column: 3.2mm ⁇ ⁇ 2.1m Column temperature: 80 ° C Inlet temperature: 180 ° C Detector temperature: 180 ° C Detector: FID Gas carrier: Nitrogen gas Vial heating temperature: 110 ° C Syringe set temperature: 110 ° C
- each of the examples and comparative examples was carried out three times, and the amount of residual dispersion medium in each group was shown as an average ⁇ standard deviation.
- Statistical evaluation of differences between individual groups was performed using Student's t-test ( * indicates p ⁇ 0.05).
- Ion exchange water 21.9g was added to this, and water-soluble ethylenically unsaturated monomer aqueous solution was prepared. (75 mol% neutralization, 38% by weight acrylic acid neutralization solution) 2) Petroleum hydrocarbon dispersion in a 2 L 5-neck cylindrical round bottom separable flask (hereinafter “round bottom flask”) equipped with a stirrer equipped with two stages of 50 mm ⁇ inclined paddle blades, a thermometer and a cooling tube As a medium, 171 g of n-heptane was weighed. 3) The aforementioned round bottom flask was immersed in a hot water bath, and n-heptane was stirred at 500 rpm to keep the internal temperature at 40 ⁇ 1 ° C.
- Example 8 of WO2009 / 025235 was carried out as Comparative Example 1.
- This example is an example having the lowest residual dispersion medium amount in Patent Document 4.
- a 500 mL Erlenmeyer flask was charged with 92.0 g of an 80% by mass aqueous acrylic acid solution, and neutralized by dropwise addition of 102.2 g of 30% by mass sodium hydroxide while cooling the flask from the outside.
- 0.11 g of potassium persulfate, 8.3 mg of ethylene glycol diglycidyl ether and 43.6 g of ion-exchanged water were added to prepare an aqueous monomer solution.
- round bottom flask A 2 L five-necked cylindrical round bottom separable flask (hereinafter “round bottom flask”) equipped with a stirrer, thermometer, reflux condenser and nitrogen gas inlet tube equipped with a two-stage 50 mm ⁇ tilted paddle blade 334 g of heptane was weighed as a system hydrocarbon dispersion medium.
- the monomer aqueous solution was charged all at once into the heptane stirred at 300 rpm. After addition of the aqueous monomer solution, the mixture was stirred for 10 minutes at an internal temperature of 40 ° C. to be primarily dispersed.
- a surfactant 0.92 g of sucrose fatty acid ester (Mitsubishi Chemical Foods Co., Ltd., trade name: S-370) was separately heated and dissolved in 8.28 g of heptane at 60 ° C. or higher.
- the mixture was added to the bottom flask using a funnel, and then the stirring speed was increased to 500 rpm, and the aqueous monomer solution was secondarily dispersed.
- the system was sufficiently purged with nitrogen while maintaining the internal temperature of the round bottom flask containing the dispersion at 40 ° C., and then heated for 1 hour using a 70 ° C. hot water bath to perform radical polymerization reaction.
- the stirring speed was increased to 1000 rpm, the internal temperature was cooled to near room temperature, and at least a part of the surfactant was precipitated.
- the second-stage polymerization monomer aqueous solution was added to the cooled above-mentioned polymerization slurry with a dropping funnel, stirred and mixed for a while, dispersed and absorbed in the first-stage polymerization gel, and the hydrogel particles were aggregated.
- the system was sufficiently purged with nitrogen while maintaining the internal temperature of the round bottom flask at about room temperature, and then heated for 1 hour using a 70 ° C. hot water bath to perform radical polymerization reaction.
- the dehydrated polymer dispersed in heptane was heated by using an oil bath at 120 ° C., and 260 g of water was removed out of the system by refluxing heptane to the flask by azeotropic distillation. Got.
- 8.2 g of a 2% ethylene glycol diglycidyl ether aqueous solution was added as a post-crosslinking agent, and a post-crosslinking reaction was performed at 83 ° C. for 2 hours.
- the mixture was heated using an oil bath at 120 ° C., heptane and water were removed from the system by distillation, dried under a nitrogen stream, passed through a 850 ⁇ m sieve, and 235 g of a water-absorbing resin in which spherical particles were aggregated.
- the median particle diameter of this water absorbent resin was 356 ⁇ m, and the moisture content was 4.5%.
- Example 7 of WO2009 / 025235 was carried out as Comparative Example 2.
- Comparative Example 1 0.46 g of an oxidized ethylene / propylene copolymer (Mitsui Chemicals, trade name: High Wax 4052E) and a maleic anhydride modified ethylene / propylene as a hydrophobic polymer dispersant added to the dispersion medium Instead of 0.46 g of copolymer (Mitsui Chemicals, trade name: High Wax 1105A), 0.92 g of maleic anhydride-modified ethylene / propylene copolymer (Mitsui Chemicals, trade name: High Wax 1105A)
- 237 g of a water-absorbing resin in the form of aggregated spherical particles was obtained in the same manner as in Comparative Example 1 except that the solution was dissolved and dispersed in a dispersion medium and heated to 75 to 80 ° C. in a 85 ° C.
- Example 1 For Comparative Example 1 (Patent Document 4, Example 8), polyvinyl pyrrolidone (hereinafter referred to as “PVP”) as a hydrophilic polymer dispersing agent was added to the monomer aqueous solution for the first stage polymerization, and the monomer mass was adjusted. 1.0 mass% was added with respect to it. Prior to the preparation of the monomer aqueous solution, 50 g of a 5% by mass aqueous solution of PVP (IS Japan Co., Ltd .: K-90) was prepared.
- PVP polyvinyl pyrrolidone
- the monomer aqueous solution was charged all at once into the heptane stirred at 300 rpm. After addition of the aqueous monomer solution, the mixture was stirred for 10 minutes at an internal temperature of 40 ° C. to be primarily dispersed.
- a surfactant a solution obtained by separately heating and dissolving 0.92 g of sucrose fatty acid ester (Mitsubishi Chemical Foods Co., Ltd., trade name: S-370) in 8.28 g of n-heptane at 60 ° C.
- the mixture was added to the round bottom flask using a funnel, and then the stirring speed was increased to 500 rpm, and the monomer aqueous solution was secondarily dispersed.
- the system was sufficiently purged with nitrogen while maintaining the internal temperature of the round bottom flask containing the dispersion at 40 ° C., and then heated for 1 hour using a 70 ° C. hot water bath to perform radical polymerization reaction.
- the stirring speed was increased to 1000 rpm, the internal temperature was cooled to 30 ° C. or lower, and at least a part of the surfactant was precipitated.
- the second-stage polymerization monomer aqueous solution was added to the cooled above-mentioned polymerization slurry with a dropping funnel, stirred and mixed for a while, dispersed and absorbed in the first-stage polymerization gel, and the hydrogel particles were aggregated. .
- the inside of the system was sufficiently purged with nitrogen while maintaining the internal temperature of the round bottom flask, and then heated for 1 hour using a 70 ° C. hot water bath to perform a radical polymerization reaction.
- the dehydrated polymer dispersed in heptane was heated by using an oil bath at 120 ° C., and 260 g of water was removed out of the system by refluxing heptane to the flask by azeotropic distillation. Got.
- 8.2 g of a 2% ethylene glycol diglycidyl ether aqueous solution was added as a post-crosslinking agent, and a post-crosslinking reaction was performed at 83 ° C. for 2 hours.
- the mixture was heated using an oil bath at 120 ° C., heptane and water were removed from the system by distillation, dried under a nitrogen stream, passed through a 850 ⁇ m sieve, and 228 g of a water-absorbent resin in which spherical particles were aggregated. Got.
- the median particle diameter of this water-absorbent resin was 387 ⁇ m, and the moisture content was 5.1%.
- Example 2 For Example 1, 2.0% by mass of PVP as a hydrophilic polymer dispersant was added to the monomer aqueous solution of the first stage polymerization with respect to the monomer mass. Prior to the preparation of the monomer aqueous solution, 50 g of a 5% by mass aqueous solution of PVP (IS Japan Co., Ltd .: K-90) was prepared. Next, 92.0 g of an 80% by mass acrylic acid aqueous solution was charged into a 500 mL Erlenmeyer flask, and neutralized by dropwise addition of 102.2 g of 30% by mass sodium hydroxide while cooling the flask from outside.
- PVP as a hydrophilic polymer dispersant
- the monomer aqueous solution was charged all at once into the heptane stirred at 300 rpm. After addition of the aqueous monomer solution, the mixture was stirred for 10 minutes at an internal temperature of 40 ° C. to be primarily dispersed.
- a surfactant a solution obtained by separately heating and dissolving 0.92 g of sucrose fatty acid ester (Mitsubishi Chemical Foods Co., Ltd., trade name: S-370) in 8.28 g of n-heptane at 60 ° C.
- Example 2 The solution was added to the round bottom flask using a funnel, and then the stirring speed was increased to 700 rpm, and the monomer aqueous solution was secondarily dispersed. Thereafter, in the same manner as in Example 1, 225 g of a water-absorbing resin having a shape in which spherical particles were aggregated was obtained. The median particle diameter of this water absorbent resin was 420 ⁇ m, and the water content was 4.5%.
- PVA Polyvinyl alcohol
- Gohsenol GH-20 Polyvinyl alcohol
- 275 g of heptane as a petroleum hydrocarbon dispersion medium was weighed into a 2 L five-necked round bottom flask equipped with a stirrer equipped with two stages of 50 mm ⁇ inclined paddle blades, a thermometer, a reflux condenser and a nitrogen gas introduction tube.
- 0.74 g of maleic anhydride-modified ethylene / propylene copolymer (Mitsui Chemicals, trade name: High Wax 1105A) was added as a hydrophobic polymer dispersant, and 85 ° C. hot water at 300 rpm with stirring. The mixture was heated to 75-80 ° C.
- aqueous solution was charged all at once into the heptane stirred at 300 rpm. After addition of the aqueous monomer solution, the mixture was stirred for 10 minutes at an internal temperature of 40 ° C. to be primarily dispersed.
- a surfactant a solution obtained by separately heating and dissolving 0.74 g of sucrose fatty acid ester (Mitsubishi Chemical Foods, Inc., trade name: S-370) in 6.6 g of n-heptane at 60 ° C.
- the solution was added to the round bottom flask using a funnel, and then the stirring speed was increased to 500 rpm, and the aqueous monomer solution was secondarily dispersed.
- the system was sufficiently purged with nitrogen while maintaining the internal temperature of the round bottom flask containing the dispersion at 40 ° C., and then heated for 1 hour using a 70 ° C. hot water bath to perform radical polymerization reaction.
- the stirring speed was increased to 1000 rpm, the internal temperature was cooled to around 30 ° C., and at least a part of the surfactant was precipitated.
- the second-stage polymerization monomer aqueous solution was added to the cooled above-mentioned polymerization slurry with a dropping funnel, stirred and mixed for a while, dispersed and absorbed in the first-stage polymerization gel, and the hydrogel particles were aggregated.
- the system was sufficiently purged with nitrogen while maintaining the internal temperature of the round bottom flask at about room temperature, and then heated for 1 hour using a 70 ° C. hot water bath to perform radical polymerization reaction.
- the mixture was heated using an oil bath at 120 ° C., heptane and water were removed from the system by distillation, dried under a nitrogen stream, passed through a 850 ⁇ m sieve, and 185 g of a water-absorbing resin in which spherical particles were aggregated.
- the median particle diameter of this water-absorbent resin was 355 ⁇ m, and the moisture content was 6.2%.
- Example 4 A 500 mL Erlenmeyer flask using polyvinyl alcohol (hereinafter abbreviated as “PVA”) as a hydrophilic polymer-based dispersant in the first stage polymerization monomer aqueous solution in an amount of 0.8 mass% based on the monomer mass. Then, 92.0 g of 80 mass% acrylic acid aqueous solution was charged, and neutralized by dropping 102.2 g of 30 mass% sodium hydroxide with stirring while cooling the flask from the outside.
- PVA polyvinyl alcohol
- aqueous monomer solution After addition of the aqueous monomer solution, the mixture was stirred for 10 minutes at an internal temperature of 40 ° C. to be primarily dispersed.
- a surfactant a solution obtained by separately heating and dissolving 0.74 g of sucrose fatty acid ester (Mitsubishi Chemical Foods, Inc., trade name: S-370) in 6.6 g of n-heptane at 60 ° C. or more, The solution was added to the round bottom flask using a funnel, and then the stirring speed was increased to 700 rpm, and the aqueous monomer solution was secondarily dispersed.
- the system was sufficiently purged with nitrogen while maintaining the internal temperature of the round bottom flask containing the dispersion at 40 ° C., and then heated for 1 hour using a 70 ° C. hot water bath to perform radical polymerization reaction. After completion of the first stage polymerization, 141 g of heptane was added, the stirring speed was increased to 1000 rpm, the internal temperature was cooled to around 30 ° C., and at least a part of the surfactant was precipitated.
- the second-stage polymerization monomer aqueous solution was added to the cooled above-mentioned polymerization slurry with a dropping funnel, stirred and mixed for a while, dispersed and absorbed in the first-stage polymerization gel, and the hydrogel particles were aggregated. .
- the system was sufficiently purged with nitrogen while maintaining the internal temperature of the round bottom flask at about room temperature, and then heated for 1 hour using a 70 ° C. hot water bath to perform radical polymerization reaction.
- dehydrated polymer dispersed in heptane by heating using an oil bath at 120 ° C.
- Comparative Example 3 In Example 1, the case where the two-stage dispersion (primary dispersion and secondary dispersion) of the monomer aqueous solution of the first stage polymerization, which is the feature of the present application, was not performed, was referred to as Comparative Example 3. Specifically, after preparing a first-stage polymerization monomer aqueous solution in the same manner as in Example 1, a stirrer equipped with two stages of 50 mm ⁇ inclined paddle blades, a thermometer, a reflux condenser, and a nitrogen gas introduction pipe were provided. In addition, 342 g of n-heptane was weighed as a petroleum hydrocarbon dispersion medium into a 2 L 6-neck round bottom flask.
- sucrose fatty acid ester (Mitsubishi Chemical Foods Co., Ltd., trade name: S-370) as a surfactant in a round bottom flask and an oxidized ethylene / propylene copolymer (Mitsui Chemicals) as a polymeric dispersant Company, brand name: High Wax 4052E) 0.46 g and maleic anhydride modified ethylene / propylene copolymer (Mitsui Chemicals, trade name: High Wax 1105A) 0.46 g were added and hot water at 90 ° C. with stirring at 300 rpm. After heating to 83-86 ° C.
- the stirring speed was increased to 300 rpm and the internal temperature was cooled to 61 ° C. by air.
- the monomer aqueous solution was dispersed while maintaining 300 rpm after addition of the monomer aqueous solution.
- the mixture was stirred at 300 rpm for 10 minutes in the same manner as in Example 1 except that the surfactant was not added, and then increased to 500 rpm.
- the system was sufficiently purged with nitrogen while maintaining the internal temperature of the round bottom flask at 40 ° C., and then heated for 1 hour using a 70 ° C. hot water bath to carry out radical polymerization reaction.
- Example 2 Thereafter, the same procedure as in Example 1 was performed to obtain 225 g of a water-absorbing resin in a shape in which spherical particles were aggregated.
- the median particle diameter of this water absorbent resin was 389 ⁇ m, and the water content was 4.8%.
- HEC hydroxyethyl cellulose
- aqueous monomer solution for the first stage polymerization in an amount of 0.3 mass% based on the monomer mass.
- a 500 mL Erlenmeyer flask was charged with 92.0 g of an 80% by mass aqueous acrylic acid solution, and neutralized by dropwise addition of 102.2 g of 30% by mass sodium hydroxide while cooling the flask from the outside.
- 0.27 g of HEC (Sumitomo Seika Co., Ltd .: AW-15F) was added and sufficiently stirred to dissolve.
- Example 2 To this, 0.11 g of potassium persulfate, 8.3 mg of ethylene glycol diglycidyl ether, and 43.3 g of ion-exchanged water were added to prepare an aqueous monomer solution. Thereafter, an experiment was conducted in the same manner as in Example 1 to obtain 226 g of a water-absorbent resin having a shape in which spherical particles were aggregated. The median particle diameter of this water-absorbent resin was 378 ⁇ m, and the moisture content was 5.2%.
- Comparative Example 5 In Comparative Example 4, the experiment was performed in the same manner as in Comparative Example 4 except that the amount of HEC added was changed to 0.91 g corresponding to 1.0% by mass and the amount of ion-exchanged water to be added was changed to 42.7 g. .
- the obtained particles had about 70% of particles having a size of 850 ⁇ m or more, 68 g of particles having a size of 850 ⁇ m or less, and a moisture content of 6.2%.
- the amount of residual dispersion medium was measured with the particles of 850 ⁇ m or less.
- the water-absorbent resin in which the residual amount of the petroleum-based hydrocarbon dispersion medium used in the reverse-phase suspension polymerization contained in the water-absorbent resin is small, and the odor derived from the petroleum-based hydrocarbon dispersion medium is further reduced. And a water-absorbent resin obtained thereby.
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Abstract
Description
しかしながら、これらの従来技術の方法では、多量の吸水性樹脂を用いた場合、吸水時に分散媒由来の臭気が感知されることがあり、さらなる臭気の低減が求められていた。
項1.少なくとも2段の逆相懸濁重合により吸水性樹脂を製造する方法であって、少なくとも2段の逆相懸濁重合の第1段の重合が、
(A)親水性高分子系分散剤を含む水溶性エチレン性不飽和単量体水溶液を、疎水性高分子系分散剤を溶解または分散させた石油系炭化水素分散媒に、界面活性剤非存在下で攪拌混合し一次分散させ、
(B)得られた分散液に界面活性剤を添加して更に二次分散させ、次いで、
(C)水溶性ラジカル重合開始剤を用いて重合を行い、前記石油系炭化水素分散媒に分散する含水ゲル状態の粒子として吸水性樹脂を得る
工程を含むことを特徴とする吸水性樹脂の製造方法。
項2.第1段の逆相懸濁重合後に、前記工程(C)により得られた、含水ゲル状態の粒子を含む前記分散媒のスラリー中の界面活性剤の少なくとも一部を析出させ、次いで、水溶性エチレン性不飽和単量体水溶液を添加して、2段または3段の逆相懸濁重合をさらに行うことを特徴とする項1記載の吸水性樹脂の製造方法。
項3.親水性高分子系分散剤が、ポリビニルピロリドンおよびポリビニルアルコールからなる群より選ばれた少なくとも1種であることを特徴とする項1または2記載の吸水性樹脂の製造方法。
項4.疎水性高分子系分散剤が、無水マレイン酸変性ポリエチレン、無水マレイン酸変性ポリプロピレン、無水マレイン酸変性エチレン・プロピレン共重合体、無水マレイン酸・エチレン共重合体、無水マレイン酸・プロピレン共重合体、無水マレイン酸・エチレン・プロピレン共重合体、ポリエチレン、ポリプロピレン、エチレン・プロピレン共重合体、酸化型ポリエチレン、酸化型ポリプロピレンおよび酸化型エチレン・プロピレン共重合体からなる群より選ばれた少なくとも1種であることを特徴とする項1~3のいずれか1項に記載の吸水性樹脂の製造方法。
項5.界面活性剤が、ポリグリセリン脂肪酸エステル、ショ糖脂肪酸エステルおよびソルビタン脂肪酸エステルからなる群より選ばれた少なくとも1種であることを特徴とする項1~4のいずれか1項に記載の吸水性樹脂の製造方法。
項6.水溶性エチレン性不飽和単量体が、アクリル酸およびその塩、メタクリル酸およびその塩、ならびにアクリルアミドからなる群より選ばれた少なくとも1種であることを特徴とする項1~5のいずれか1項に記載の吸水性樹脂の製造方法。
項7.石油系炭化水素分散媒が、炭素数6~8の脂肪族炭化水素および脂環族炭化水素からなる群より選ばれた少なくとも1種であることを特徴とする項1~6のいずれか1項に記載の吸水性樹脂の製造方法。
項8.項1~7のいずれかに記載の製造方法により得られる吸水性樹脂。
本発明の吸水性樹脂の製造方法は、逆相懸濁重合を行うに際し、界面活性剤非存在かつ疎水性高分子系分散剤存在下に、水溶性ラジカル重合開始剤を含む水溶性エチレン性不飽和単量体水溶液を石油系炭化水素分散媒に一次分散させる際、その単量体水溶液中に親水性高分子系分散剤を存在させることで、O/W/O(油/水/油)型液滴の発生を従来よりも抑制させ、次いで界面活性剤を添加し更に二次分散させた後、水溶性ラジカル重合開始剤を用いて重合させることをひとつの特徴とする。O/W/O型液滴とは、(Oil in Water) in Oilの略記であり、油相の微細液滴が水相液滴中に分散しており、その水相液滴が更に油相に分散している状態をいう。つまり、最内油相、中間水相、最外油相より形成されており、本願では、分散媒中(油相)に存在する、単量体水溶液(水相)の液滴の中に、更に小さな分散媒(油相)の液滴が含まれている状態を示している。
(A)親水性高分子系分散剤を含む水溶性エチレン性不飽和単量体水溶液を、疎水性高分子系分散剤を溶解または分散させた石油系炭化水素分散媒に、界面活性剤非存在下で攪拌混合し一次分散させ、
(B)得られた分散液に界面活性剤を添加して更に二次分散させ、次いで
(C)水溶性ラジカル重合開始剤を用いて重合を行い、前記石油系炭化水素分散媒に分散する含水ゲル状態の粒子として吸水性樹脂を得る。
水溶性エチレン性不飽和単量体が酸基を有する場合、酸基を中和して塩として用いてもよい。
酸基を有する単量体を中和して塩とする場合に用いられるアルカリ性化合物としては、リチウム、ナトリウム、カリウム、アンモニウム等の化合物が挙げられる。より詳しくは、水酸化ナトリウム、水酸化カリウム、水酸化リチウム、炭酸ナトリウム、炭酸アンモニウム等が挙げられる。
酸基を有する単量体を中和する場合、その中和度は、水溶性エチレン性不飽和単量体の酸基の30~90モル%であることが好ましい。中和度が30モル%より低い場合、酸基がイオン化されにくく、吸水能が低くなる可能性があるため好ましくない。中和度が90モル%を超えると、衛生材料として使用される場合、安全性等に問題が生ずる可能性があるため好ましくない。また、中和のタイミングは単量体状態で行うことが均一度の観点から一般的であるが、単量体重合後のポリマーに、上記アルカリ性化合物を添加して中和を行う、いわゆる後中和を併用しても構わない。
さらに、これらの炭化水素分散媒のなかでも、本発明におけるW/O型逆相懸濁の状態が良好で、好適な粒子径が得られやすく、工業的に入手が容易かつ品質が安定している観点から、n-ヘプタン、シクロヘキサンが好適に用いられる。また、上記炭化水素の混合物の例として、市販されているエクソールヘプタン(エクソンモービル社製:n-ヘプタンおよび異性体の炭化水素75~85%含有)などを用いても好適な結果が得られる。
これらの中では無水マレイン酸変性ポリエチレン、無水マレイン酸変性ポリプロピレン、無水マレイン酸変性エチレン・プロピレン共重合体、無水マレイン酸・エチレン共重合体、無水マレイン酸・プロピレン共重合体、無水マレイン酸・エチレン・プロピレン共重合体、ポリエチレン、ポリプロピレン、エチレン・プロピレン共重合体、酸化型ポリエチレン、酸化型ポリプロピレンおよび酸化型エチレン・プロピレン共重合体からなる群より選ばれた少なくとも1種が好ましい。
分散液滴径は、攪拌翼の種類、翼径、回転数等により調節することができる。
また、ポリビニルアルコールであれば、けん化度等は特に限定はされないが、残存分散媒量低減の観点から、けん化度は85%以上であることが好ましい。さらに、好適に用いられるポリビニルアルコールとしては、残存分散媒の低減効果の観点および溶解させて用いる観点から、重合度が100~3000程度のものが使いやすい。
工程(B)で添加される界面活性剤の形態は特に限定されないが、界面活性剤を予め少量の分散媒に希釈もしくは溶解して使用する方法が、短時間で分散安定化できるので好ましい。なお、工程(B)にて界面活性剤を添加した後、攪拌翼の攪拌回転数を増速することができる。増速後の攪拌回転数により、最終的な分散液滴径が決定され、1段目の重合段階での粒子の大きさが決定される。工程(A)の一次分散の攪拌回転数を工程(B)での二次分散の攪拌回転数よりある程度低く設定することで、分散媒が単量体水溶液液滴に内包されるのを抑制することができ、結果として吸水性樹脂の残存分散媒量をより低減することができる。
なお、水溶性ラジカル重合開始剤は、亜硫酸塩、アスコルビン酸等の還元剤と併用してレドックス重合開始剤として用いてもよい。
水溶性ラジカル重合開始剤の添加時期は特に制限されないが、均一性の観点からあらかじめ水溶性エチレン性不飽和単量体水溶液に添加しておくのが好ましい。
内部架橋剤は、あらかじめ水溶性エチレン性不飽和単量体水溶液に添加しておくのが好ましい。
2段目重合の水溶性エチレン性不飽和単量体としては、1段目重合の水溶性エチレン性不飽和単量体として例示したものと同様なものが使用できるが、単量体の種類、中和度、中和塩および単量体水溶液濃度は、1段目重合の水溶性エチレン性不飽和単量体と同じであっても異なっていてもよい。
2段目重合の水溶性エチレン性不飽和単量体水溶液に添加される重合開始剤についても、1段目の重合に用いられる重合開始剤として例示したものから適宜選択して使用することができる。
また、2段目重合の水溶性エチレン性不飽和単量体水溶液にも、必要に応じて、内部架橋剤、連鎖移動剤等を添加してもよく、1段目の重合の際に例示したものから選択して使用することができる。
2段目重合の水溶性エチレン性不飽和単量体の添加量は、適度な凝集粒子を得る観点及び、残存分散媒量低減の観点から、1段目重合の水溶性エチレン性不飽和単量体量に対して、1.0~2.0倍が好ましく、1.1~1.8倍がより好ましい。1.0倍未満であると、取得量が減るため残存分散媒量の低減効果が薄く好ましくない。また2.0倍より多いと、1段目の重合粒子が2段目重合の単量体水溶液を吸収しきれず、微粉が発生し、適正な中位粒径を持つ凝集粒子が得られなくなるので好ましくない
なお、衛生材料用途に好適な凝集粒子の中位粒子径としては、200~600μmが好ましく、250~500μmがより好ましく、300~450μmがさらに好ましい。
分散媒の追加の時期については特に限定されないが、冷却効果をかねて1段目重合終了後に低い温度の分散媒を追加することが好ましい。
使用される後架橋剤としては、例えば、エチレングリコール、プロピレングリコール、1,4-ブタンジオール、トリメチロールプロパン、グリセリン、ポリオキシエチレングリコール、ポリオキシプロピレングリコール、ポリグリセリン等のポリオール類;(ポリ)エチレングリコールジグリシジルエーテル、(ポリ)エチレングリコールトリグリシジルエーテル、(ポリ)グリセリンジグリシジルエーテル、(ポリ)グリセリントリグリシジルエーテル、(ポリ)プロピレングリコールポリグリシジルエーテル、(ポリ)グリセロールポリグリシジルエーテル等のポリグリシジル化合物;エピクロルヒドリン、エピブロムヒドリン、α-メチルエピクロルヒドリン等のハロエポキシ化合物;2,4-トリレンジイソシアネート、ヘキサメチレンジイソシアネート等のイソシアネート化合物等の反応性官能基を2個以上有する化合物;3-メチル-3-オキセタンメタノール、3-エチル-3-オキセタンメタノール、3-ブチル-3-オキセタンメタノール、3-メチル-3-オキセタンエタノール、3-エチル-3-オキセタンエタノール、3-ブチル-3-オキセタンエタノール等のオキセタン化合物、1,2-エチレンビスオキサゾリン等のオキサゾリン化合物、エチレンカーボネート等のカーボネート化合物等が挙げられる。これらは、それぞれ単独で用いてもよく、2種以上を混合して用いてもよい。
なお、特許文献4に記載されている残存分散媒量については、残存分散媒量の絶対値が500ppm以下まで下がってきたこともあり、より充分に吸水性樹脂からの抽出を行うため、その測定方法の改良を行った。
吸水性樹脂50gを、JIS標準篩の目開き250μmの篩を用いて通過させ、篩上に残る量がその50質量%以上の場合には<α>の篩の組み合わせを、50質量%未満の場合には<β>の篩の組み合わせを、用いて中位粒子径を測定した。
<α>JIS標準篩を上から、目開き850μmの篩、目開き600μmの篩、目開き500μmの篩、目開き425μmの篩、目開き300μmの篩、目開き250μmの篩、目開き150μmの篩および受け皿の順に組み合わせた。
<β>JIS標準篩を上から、目開き425μmの篩、目開き250μmの篩、目開き180μmの篩、目開き150μmの篩、目開き106μmの篩、目開き75μmの篩、目開き45μmの篩および受け皿の順に組み合わせた。
組み合わせた最上の篩に、前記吸水性樹脂約50gを入れ、ロータップ式振とう器を用いて20分間振とうさせて分級した。
分級後、各篩上に残った吸水性樹脂の質量を全量に対する質量百分率として計算し、粒子径の大きい方から順に積算することにより、篩の目開きと篩上に残った吸水性樹脂の質量百分率の積算値との関係を対数確率紙にプロットした。確率紙上のプロットを直線で結ぶことにより、積算質量百分率50質量%に相当する粒子径を中位粒子径とした。
吸水性樹脂約2.5gをアルミカップに精秤し(Xg)、105℃の熱風乾燥機を用いて2時間乾燥後、乾燥した吸水性樹脂の質量(Yg)を測定して、下記式より水分率を算出した。なお、アルミカップの乾燥前後の風袋質量は一定とした。
水分率(%)=(X-Y)÷X×100
より低レベルでの残存分散媒量の測定を可能とするように、特許文献4の従来の測定方法に対し、サンプル瓶内に仕込んだ吸水性樹脂からの残存分散媒量をより充分に抽出するため、膨潤倍率を上げ、更にリン酸を加え膨潤ゲルが溶解しやすいように下記のように改良を行った。
残存分散媒を測定するサンプルの重合に使用した石油系炭化水素系分散媒(以後「分散媒」と表記)を10g程度スクリュー瓶等に入れ、氷水浴にて冷却した。同様に測定に使用するDMF(ジメチルフォルムアミド)60gと25質量%リン酸水溶液60gも氷水浴で冷却した。(仕込中の分散媒の蒸散抑制のため、充分冷却の後に仕込を行う。)
50ml容スクリュー瓶に上記分散媒を0.2g精秤し、そこに上記冷却DMFを加え、合計20gにして精秤し、スターラチップで撹拌して標準試料液1とした。この標準試料液1も氷水浴により冷却をした。
次いで50ml容スクリュー瓶に上記標準試料液1を0.2g精秤し、そこに上記冷却DMFを加え、合計20gにして精秤し、スターラチップで撹拌して標準試料液2とした。この標準試料液2も氷水浴により冷却をしておいた。
20ml容のバイアル瓶(マルエム社製、No.5)に上記標準試料液2より、0.02、0.05、0.1、0.5gおよび上記標準試料液1より0.02gをそれぞれ精秤し、そこに上記冷却DMFを加え、各バイアル瓶の内容量を計3.8g(4mL)とした。更に各バイアルに上記25質量%リン酸水溶液5mLを加え、セプタムゴム、アルミキャップで栓をして締め付けた後、瓶を振って攪拌した。
なお、20ml容のバイアルへの試料の仕込から栓の締め付けまではすばやく行い、分散媒がバイアルから蒸散するのを極力防ぐように留意した。また、DMFと25質量%リン酸水溶液の混合時の発熱で分散媒が蒸散しないように、両試薬の冷却を充分行っておき、アルミキャップ等で密栓状態にしてから、充分混合を行うようにも留意した。
仕込量を基に上記標準試料液の濃度を求め、各バイアル瓶中の分散媒の仕込量を算出し、その仕込量とクロマトグラムのピーク面積より、検量線を作成した。(なお、分散媒として石油系炭化水素の混合物を用いた場合、複数のピークが表れるため、その面積の総和値と仕込量で検量線を作成した。)
測定する吸水性樹脂のサンプル約2gをアルミカップに入れ、105℃の熱風乾燥機にて2時間乾燥させ、含有する水分量を調整した。
測定に使用するDMFと25質量%リン酸水溶液も必要量スクリュー瓶に入れ氷水浴で冷却した。
20ml容のバイアル瓶(マルエム社製、No.5)に上記サンプルを0.10g精秤し、仮のゴムキャップをつけた後、バイアル瓶底部を氷浴に漬け、バイアル瓶と吸水性樹脂を冷却した。このバイアル瓶内に、前述の冷却DMFを4mL加え、更に前述の25質量%リン酸水溶液5mLを加え、セプタムゴム、アルミキャップで栓をしてすばやく締め付けた後、軽くバイアル瓶を振り混合した。10分静置後、中の吸水性樹脂が膨潤していることを確認し、同バイアル瓶を激しく振り混ぜ内部を強撹拌した。このバイアル瓶を110℃で2時間予備加熱し、加熱後再度強攪拌を行った。
なお、20ml容のバイアルへの仕込から栓の締め付けまでは、すばやく行い、分散媒がバイアルから蒸散するのを極力防ぐように留意した。
得られたクロマトグラムのピーク面積を基に、先に作成した検量線から、仕込サンプル量(0.10gの実測値)に含まれる分散媒量を算出し、サンプル1gあたりに含まれる分散媒量[ppm]に換算した。
機種:島津製作所製 GC-14A+HSS2B(ヘッドスペースオートサンプラ)
充填剤:Squalane 25% Shimalite(NAW)(101)
80-100mesh
カラム:3.2mmφ×2.1m
カラム温度:80℃
注入口温度:180℃
検出器温度:180℃
検出器:FID
ガスキャリア:窒素ガス
バイアル瓶加熱温度:110℃
シリンジ設定温度:110℃
同一サンプルにつき残存分散媒量を測定した結果、本願の前記測定方法は、特許文献4の従来方法に比較してより高感度で残存分散媒量を測定できた。例えば、本願の比較例1につき、本願の測定方法では100ppmであるのに対し、従来方法では80ppmの残存分散媒量しか示さなかった。
界面活性剤等非存在下での単量体水溶液中に溶解する分散媒量を調べる目的で、下記の実験を行った。
[参考実験例]
単量体水溶液への分散媒の溶解量測定を下記の手順にて行った。
1)500mL容の三角フラスコに、80質量%アクリル酸水溶液46.0gを仕込み、フラスコを外部から冷却しつつ、攪拌しながら30質量%水酸化ナトリウム51.1gを滴下して中和を行なった。これにイオン交換水21.9gを加え、水溶性エチレン性不飽和単量体水溶液を調製した。(75mol%中和、38質量%濃度のアクリル酸中和液)
2)2段の50mmφ傾斜パドル翼を備えた攪拌機、温度計および冷却管を備えた2L容の五ツ口円筒形丸底セパラブルフラスコ(以後「丸底フラスコ」)に、石油系炭化水素分散媒としてn-ヘプタン171gを計量した。
3)湯浴に前述の丸底フラスコを浸し、500rpmでn-ヘプタンを攪拌し内温40±1℃に保温した。
4)手順1)で調整したアクリル酸中和液を投入し、30分間500rpmで攪拌しながら内温40±1℃になるように湯浴の温度を調整して保温した。
5)30分間の攪拌後、攪拌機を停止し同じ湯浴温度にしたまま30分間静置した。
6)2層分離を混合しないように静かに下層の中和液層のみを回収した。
7)残存分散媒量の測定方法に準じ、20mL容バイアル瓶に回収した中和液約0.26gを精秤し(単量体量で約0.1g相当)、冷却したDMFとリン酸水溶液を加えた。
8)バイアルキャップを封鎖後、攪拌した後110℃で2時間予備加熱した上で、残存分散媒量の測定方法に準じて中和液中のn-ヘプタン量を測定した。
WO2009/025235(特許文献4)の実施例8を比較例1として実施した。なお、同例は、特許文献4の中で残存分散媒量が最も低い実施例である。
500mL容の三角フラスコに、80質量%アクリル酸水溶液92.0gを仕込み、フラスコを外部から冷却しつつ、攪拌しながら30質量%水酸化ナトリウム102.2gを滴下して中和を行なった。これに過硫酸カリウム0.11gとエチレングリコールジグリシジルエーテル8.3mg、イオン交換水43.6gを加え、単量体水溶液を調製した。
2段の50mmφ傾斜パドル翼を備えた攪拌機、温度計、還流冷却器および窒素ガス導入管を備えた2L容の五ツ口円筒形丸底セパラブルフラスコ(以後「丸底フラスコ」)に、石油系炭化水素分散媒としてヘプタン334gを計量した。丸底フラスコ内に疎水性高分子系分散剤として酸化型エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス4052E)0.46gと無水マレイン酸変性エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス1105A)0.46gを加えて300rpmの攪拌下90℃の湯浴で83~86℃に加温し溶解・分散させた後、内温61℃まで空冷した。先端の開口部が内径8mmφのSUS製ロートを用いて、300rpmで攪拌している上記ヘプタン中に、上記単量体水溶液を一括で投入した。単量体水溶液添加後、内温40℃にて10分間攪拌し一次分散させた。
次に、界面活性剤として、ショ糖脂肪酸エステル(三菱化学フーズ株式会社、商品名:S-370)0.92gをヘプタン8.28gに60℃以上で別途加温溶解させた液を、前記丸底フラスコ内に漏斗を用いて添加し、次いで攪拌速度を500rpmまで増速し、単量体水溶液を二次分散させた。
前記分散液を含む丸底フラスコの内温を40℃に保持しながら系内を充分に窒素置換した後、70℃の湯浴を用いて1時間加温し、ラジカル重合反応を行なった。
1段目重合終了後、撹拌速度を1000rpmに増速し、内温を室温付近まで冷却し、界面活性剤を少なくとも一部析出させた。
2段目の重合反応後、120℃の油浴を用いて加熱し、共沸蒸留により、ヘプタンをフラスコに還流しながら260gの水を系外に除去することによりヘプタンに分散された脱水重合体を得た。得られたヘプタン分散脱水重合体に、後架橋剤として2%エチレングリコールジグリシジルエーテル水溶液8.2gを添加し、83℃で2時間、後架橋反応を行なった。
その後、120℃の油浴を用いて加熱し、ヘプタンと水を蒸留により系外へ除去後、窒素気流下で乾燥し、850μmの篩を通過させ、球状粒子が凝集した形状の吸水性樹脂235gを得た。この吸水性樹脂の中位粒子径は356μmで、水分率は4.5%であった。
WO2009/025235(特許文献4)の実施例7を比較例2として実施した。
比較例1において、分散媒に添加する疎水性高分子系分散剤として酸化型エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス4052E)0.46g及び無水マレイン酸変性エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス1105A)0.46gに代えて、無水マレイン酸変性エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス1105A)0.92gを加えて、その分散媒への溶解・分散に85℃の湯浴で75~80℃に加温した以外は、比較例1と同様にし、球状粒子が凝集した形状の吸水性樹脂237gを得た。この吸水性樹脂の中位粒子径は372μmで、水分率は4.8%であった。
比較例1(特許文献4、実施例8)に対し、親水性高分子系分散剤としてポリビニルピロリドン(以下「PVP」と記す)を1段目重合の単量体水溶液に、単量体質量に対し1.0質量%を添加した。
単量体水溶液の調整に先立ちPVP(アイエスピー・ジャパン株式会社:K-90)の5質量%水溶液を50g作製した。次いで500mL容の三角フラスコに、80質量%アクリル酸水溶液92.0gを仕込み、フラスコを外部から冷却しつつ、攪拌しながら30質量%水酸化ナトリウム102.2gを滴下して中和を行なった。これに過硫酸カリウム0.11gとエチレングリコールジグリシジルエーテル8.3mg、前述の5質量%PVP水溶液を18.1g及びイオン交換水25.5gを加え、単量体水溶液を調製・攪拌混合した。
2段の50mmφ傾斜パドル翼を備えた攪拌機、温度計、還流冷却器および窒素ガス導入管を備えた2L容の五ツ口丸底フラスコに、石油系炭化水素分散媒としてヘプタン334gを計量した。丸底フラスコ内に疎水性高分子系分散剤として酸化型エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス4052E)0.46gと無水マレイン酸変性エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス1105A)0.46gを加えて300rpmの攪拌下90℃の湯浴で83~86℃に加温し溶解・分散させた後、内温61℃まで空冷した。先端の開口部が内径8mmφのSUS製ロートを用いて、300rpmで攪拌している上記ヘプタン中に、上記単量体水溶液を一括で投入した。単量体水溶液添加後、内温40℃にて10分間攪拌し一次分散させた。
次に、界面活性剤として、ショ糖脂肪酸エステル(三菱化学フーズ株式会社、商品名:S-370)0.92gをn-ヘプタン8.28gに60℃以上で別途加温溶解させた液を、前記丸底フラスコ内に漏斗を用いて添加し、次いで、攪拌速度を500rpmまで増速し、単量体水溶液を二次分散させた。
前記分散液を含む丸底フラスコの内温を40℃に保持しながら系内を充分に窒素置換した後、70℃の湯浴を用いて1時間加温し、ラジカル重合反応を行なった。
1段目重合終了後、撹拌速度を1000rpmに増速し、内温を30℃以下まで冷却し、界面活性剤を少なくとも一部析出させた。
2段目の重合反応後、120℃の油浴を用いて加熱し、共沸蒸留により、ヘプタンをフラスコに還流しながら260gの水を系外に除去することによりヘプタンに分散された脱水重合体を得た。得られたヘプタン分散脱水重合体に、後架橋剤として2%エチレングリコールジグリシジルエーテル水溶液8.2gを添加し、83℃で2時間、後架橋反応を行なった。
その後、120℃の油浴を用いて加熱し、ヘプタンと水を蒸留により系外へ除去後、窒素気流下で乾燥し、850μmの篩を通過させ、球状粒子が凝集した形状の吸水性樹脂228gを得た。この吸水性樹脂の中位粒子径は387μmで、水分率は5.1%であった。
実施例1に対し、親水性高分子系分散剤としてPVPを1段目重合の単量体水溶液に、単量体質量に対し2.0質量%を添加した。
単量体水溶液の調整に先立ちPVP(アイエスピー・ジャパン株式会社:K-90)の5質量%水溶液を50g作製した。次いで500mL容の三角フラスコに、80質量%アクリル酸水溶液92.0gを仕込み、フラスコを外部から冷却しつつ、攪拌しながら30質量%水酸化ナトリウム102.2gを滴下して中和を行なった。これに過硫酸カリウム0.11gとエチレングリコールジグリシジルエーテル8.3mg、前述の5質量%PVP水溶液を36.2g及びイオン交換水7.4gを加え、単量体水溶液を調製・攪拌混合した。
2段の50mmφ傾斜パドル翼を備えた攪拌機、温度計、還流冷却器および窒素ガス導入管を備えた2L容の五ツ口丸底フラスコに、石油系炭化水素分散媒としてヘプタン334gを計量した。丸底フラスコ内に疎水性高分子系分散剤として酸化型エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス4052E)0.46gと無水マレイン酸変性エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス1105A)0.46gを加えて300rpmの攪拌下85℃の湯浴で75~80℃に加温し溶解・分散させた後、内温61℃まで空冷した。先端の開口部が内径8mmφのSUS製ロートを用いて、300rpmで攪拌している上記ヘプタン中に、上記単量体水溶液を一括で投入した。単量体水溶液添加後、内温40℃にて10分間攪拌し一次分散させた。
次に、界面活性剤として、ショ糖脂肪酸エステル(三菱化学フーズ株式会社、商品名:S-370)0.92gをn-ヘプタン8.28gに60℃以上で別途加温溶解させた液を、前記丸底フラスコ内に漏斗を用いて添加し、次いで、攪拌速度を700rpmまで増速し、単量体水溶液を二次分散させた。
以降は実施例1と同様にし、球状粒子が凝集した形状の吸水性樹脂225gを得た。この吸水性樹脂の中位粒子径は420μmで、水分率は4.5%であった。
親水性高分子系分散剤としてポリビニールアルコール(以降「PVA」と略記)を1段目重合の単量体水溶液に、単量体質量に対し0.7質量%を使用した
単量体水溶液の調整に先立ちPVA(日本合成化学工業株式会社:ゴーセノールGH-20)の20gを380gの蒸留水に加温攪拌溶解後、室温まで放冷した5質量%水溶液400gを作製した。次いで500mL容の三角フラスコに、80質量%アクリル酸水溶液92.0gを仕込み、フラスコを外部から冷却しつつ、攪拌しながら30質量%水酸化ナトリウム102.2gを滴下して中和を行なった。これに過硫酸カリウム0.07gとエチレングリコールジグリシジルエーテル10.1mg、親水性高分子系分散剤として前述の5質量%PVA水溶液を12.7g及びイオン交換水30.9gを加え、単量体水溶液を調製・攪拌混合した。
2段の50mmφ傾斜パドル翼を備えた攪拌機、温度計、還流冷却器および窒素ガス導入管を備えた2L容の五ツ口丸底フラスコに、石油系炭化水素分散媒としてヘプタン275gを計量した。丸底フラスコ内に疎水性高分子系分散剤として無水マレイン酸変性エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス1105A)0.74gを加えて300rpmの攪拌下85℃の湯浴で75~80℃に加温し溶解・分散させた後、内温65℃まで空冷した。先端の開口部が内径8mmφのSUS製ロートを用いて、300rpmで攪拌している上記ヘプタン中に、上記単量体水溶液を一括で投入した。単量体水溶液添加後、内温40℃にて10分間攪拌し一次分散させた。
次に、界面活性剤として、ショ糖脂肪酸エステル(三菱化学フーズ株式会社、商品名:S-370)0.74gをn-ヘプタン6.6gに60℃以上で別途加温溶解させた液を、前記丸底フラスコ内に漏斗を用いて添加し、次いで攪拌速度を500rpmまで増速し、単量体水溶液を二次分散させた。
前記分散液を含む丸底フラスコの内温を40℃に保持しながら系内を充分に窒素置換した後、70℃の湯浴を用いて1時間加温し、ラジカル重合反応を行なった。
1段目重合終了後、攪拌速度を1000rpmに増速し、内温を30℃付近まで冷却し、界面活性剤を少なくとも一部析出させた。
2段目の重合反応後、ヘプタン100gを追加した後、120℃の油浴を用いて加熱し、共沸蒸留により、ヘプタンをフラスコに還流しながら220gの水を系外に除去することによりヘプタンに分散された脱水重合体を得た。得られたヘプタン分散脱水重合体に、後架橋剤として2%エチレングリコールジグリシジルエーテル水溶液3.9gを添加し、83℃で2時間、後架橋反応を行なった。
その後、120℃の油浴を用いて加熱し、ヘプタンと水を蒸留により系外へ除去後、窒素気流下で乾燥し、850μmの篩を通過させ、球状粒子が凝集した形状の吸水性樹脂185gを得た。この吸水性樹脂の中位粒子径は355μmで、水分率は6.2%であった。
親水性高分子系分散剤としてポリビニールアルコール(以降「PVA」と略記)を1段目重合の単量体水溶液に、単量体質量に対し0.8質量%を使用した
500mL容の三角フラスコに、80質量%アクリル酸水溶液92.0gを仕込み、フラスコを外部から冷却しつつ、攪拌しながら30質量%水酸化ナトリウム102.2gを滴下して中和を行なった。これに過硫酸カリウム0.07gとエチレングリコールジグリシジルエーテル10.1mg、実施例3と同じの5質量%PVA水溶液を14.7g及びイオン交換水28.9gを加え、単量体水溶液を調製・攪拌混合した。
2段の50mmφ傾斜パドル翼を備えた攪拌機、温度計、還流冷却器および窒素ガス導入管を備えた2L容の五ツ口丸底フラスコに、石油系炭化水素分散媒としてヘプタン275gを計量した。丸底フラスコ内に疎水性高分子系分散剤として無水マレイン酸変性エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス1105A)0.74gを加えて300rpmの攪拌下85℃の湯浴で75~80℃に加温し溶解・分散させた後、内温65℃まで空冷した。先端の開口部が内径8mmφのSUS製ロートを用いて、300rpmで攪拌している上記ヘプタン中に、上記単量体水溶液を一括で投入した。単量体水溶液添加後、内温40℃にて10分間攪拌し一次分散させた。
次に、界面活性剤として、ショ糖脂肪酸エステル(三菱化学フーズ株式会社、商品名:S-370)0.74gをn-ヘプタン6.6gに60℃以上で別途加温溶解させた液を、前記丸底フラスコ内に漏斗を用いて添加し、次いで攪拌速度を700rpmまで増速し、単量体水溶液を二次分散させた。
前記分散液を含む丸底フラスコの内温を40℃に保持しながら系内を充分に窒素置換した後、70℃の湯浴を用いて1時間加温し、ラジカル重合反応を行なった。
1段目重合終了後、ヘプタン141gを追加した後、撹拌速度を1000rpmに増速し、内温を30℃付近まで冷却し、界面活性剤を少なくとも一部析出させた。
2段目の重合反応後、120℃の油浴を用いて加熱し、共沸蒸留により、ヘプタンをフラスコに還流しながら250gの水を系外に除去することによりヘプタンに分散された脱水重合体を得た。得られたヘプタン分散脱水重合体に、後架橋剤として2%エチレングリコールジグリシジルエーテル水溶液4.4gを添加し、83℃で2時間、後架橋反応を行なった。
その後、120℃の油浴を用いて加熱し、ヘプタンと水を蒸留により系外へ除去後、窒素気流下で乾燥し、850μmの篩を通過させ、球状粒子が凝集した形状の吸水性樹脂223gを得た。この吸水性樹脂の中位粒子径は378μmで、水分率は5.9%であった。
実施例1において、本願の特徴の1段目重合の単量体水溶液の2段階分散(一次分散及び二次分散)を行わなかった場合を比較例3とした。
具体的には、実施例1と同様に1段目重合の単量体水溶液を調整した後、2段の50mmφ傾斜パドル翼を備えた攪拌機、温度計、還流冷却器および窒素ガス導入管を備えた2L容の六ツ口丸底フラスコに、石油系炭化水素分散媒としてn-ヘプタン342gを計量した。丸底フラスコ内に界面活性剤として、ショ糖脂肪酸エステル(三菱化学フーズ株式会社、商品名:S-370)0.92gと高分子系分散剤として酸化型エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス4052E)0.46gと無水マレイン酸変性エチレン・プロピレン共重合体(三井化学株式会社、商品名:ハイワックス1105A)0.46gを加えて300rpmの攪拌下90℃の湯浴で83~86℃に加温し溶解・分散させた後、攪拌速度を300rpmに増速し、内温61℃まで空冷した。先端の開口部が内径8mmφのSUS製ロートを用いて、単量体水溶液添加後、300rpmのまま単量体水溶液を分散させた。界面活性剤を添加しない以外は実施例1と同様に10分間300rpmで攪拌した後、500rpmに増速した。そのまま丸底フラスコの内温を40℃に保持しながら系内を充分に窒素置換した後、70℃の湯浴を用いて1時間加温し、ラジカル重合反応を行なった。
以降、実施例1と同様に実施し、球状粒子が凝集した形状の吸水性樹脂225gを得た。この吸水性樹脂の中位粒子径は389μmで、水分率は4.8%であった。
比較例2において、増粘剤としてヒドロキシエチルセルロース(以後「HEC」と略記)を1段目重合の単量体水溶液に、単量体質量に対し0.3質量%添加した。
500mL容の三角フラスコに、80質量%アクリル酸水溶液92.0gを仕込み、フラスコを外部から冷却しつつ、攪拌しながら30質量%水酸化ナトリウム102.2gを滴下して中和を行なった。この中和液にHEC(住友精化株式会社:AW-15F)を0.27g添加し充分に攪拌して、溶解させた。これに過硫酸カリウム0.11gとエチレングリコールジグリシジルエーテル8.3mg、及びイオン交換水43.3gを加え、単量体水溶液を調製した。
以後、実施例1と同様に実験を行い、球状粒子が凝集した形状の吸水性樹脂226gを得た。この吸水性樹脂の中位粒子径は378μmで、水分率は5.2%であった。
比較例4において、HECの添加量を1.0質量%に相当する0.91gに変更し、添加するイオン交換水量を42.7gに変更した以外は、比較例4と同様に実験を行った。得られた粒子は850μm以上の粒子が全体の7割程あり、850μm以下の状粒子は68gで、水分率は6.2%であった。この850μm以下の粒子で残存分散媒量を測定した。
Claims (8)
- 少なくとも2段の逆相懸濁重合により吸水性樹脂を製造する方法であって、少なくとも2段の逆相懸濁重合の第1段の重合が、
(A)親水性高分子系分散剤を含む水溶性エチレン性不飽和単量体水溶液を、疎水性高分子系分散剤を溶解または分散させた石油系炭化水素分散媒に、界面活性剤非存在下で攪拌混合し一次分散させ、
(B)得られた分散液に界面活性剤を添加して更に二次分散させ、次いで、
(C)水溶性ラジカル重合開始剤を用いて重合を行い、前記石油系炭化水素分散媒に分散する含水ゲル状態の粒子として吸水性樹脂を得る
工程を含むことを特徴とする吸水性樹脂の製造方法。 - 第1段の逆相懸濁重合後に、前記工程(C)により得られた、含水ゲル状態の粒子を含む前記分散媒のスラリー中の界面活性剤の少なくとも一部を析出させ、次いで、水溶性エチレン性不飽和単量体水溶液を添加して、2段または3段の逆相懸濁重合をさらに行うことを特徴とする請求項1記載の吸水性樹脂の製造方法。
- 親水性高分子系分散剤が、ポリビニルピロリドンおよびポリビニルアルコールからなる群より選ばれた少なくとも1種であることを特徴とする請求項1または2記載の吸水性樹脂の製造方法。
- 疎水性高分子系分散剤が、無水マレイン酸変性ポリエチレン、無水マレイン酸変性ポリプロピレン、無水マレイン酸変性エチレン・プロピレン共重合体、無水マレイン酸・エチレン共重合体、無水マレイン酸・プロピレン共重合体、無水マレイン酸・エチレン・プロピレン共重合体、ポリエチレン、ポリプロピレン、エチレン・プロピレン共重合体、酸化型ポリエチレン、酸化型ポリプロピレンおよび酸化型エチレン・プロピレン共重合体からなる群より選ばれた少なくとも1種であることを特徴とする請求項1~3のいずれか1項に記載の吸水性樹脂の製造方法。
- 界面活性剤が、ポリグリセリン脂肪酸エステル、ショ糖脂肪酸エステルおよびソルビタン脂肪酸エステルからなる群より選ばれた少なくとも1種であることを特徴とする請求項1~4のいずれか1項に記載の吸水性樹脂の製造方法。
- 水溶性エチレン性不飽和単量体が、アクリル酸およびその塩、メタクリル酸およびその塩、ならびにアクリルアミドからなる群より選ばれた少なくとも1種であることを特徴とする請求項1~5のいずれか1項に記載の吸水性樹脂の製造方法。
- 石油系炭化水素分散媒が、炭素数6~8の脂肪族炭化水素および脂環族炭化水素からなる群より選ばれた少なくとも1種であることを特徴とする請求項1~6のいずれか1項に記載の吸水性樹脂の製造方法。
- 請求項1~7のいずれかに記載の製造方法により得られる吸水性樹脂。
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WO2014034897A1 (ja) | 2012-08-30 | 2014-03-06 | 株式会社日本触媒 | 粒子状吸水剤及びその製造方法 |
JP2017061657A (ja) * | 2015-09-25 | 2017-03-30 | 日本酢ビ・ポバール株式会社 | 懸濁重合用添加剤およびその水性分散体、並びに、それらを用いるビニル系樹脂の製造方法 |
Also Published As
Publication number | Publication date |
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EP2599796A4 (en) | 2014-11-26 |
US20130119309A1 (en) | 2013-05-16 |
EP2599796B1 (en) | 2019-01-23 |
CN103003313B (zh) | 2015-08-19 |
TWI543991B (zh) | 2016-08-01 |
BR112013003648A2 (pt) | 2023-12-19 |
KR20130131289A (ko) | 2013-12-03 |
JPWO2012014749A1 (ja) | 2013-09-12 |
JP5805640B2 (ja) | 2015-11-04 |
TW201211070A (en) | 2012-03-16 |
US9132413B2 (en) | 2015-09-15 |
EP2599796A1 (en) | 2013-06-05 |
KR101778340B1 (ko) | 2017-09-13 |
CN103003313A (zh) | 2013-03-27 |
SA111320656B1 (ar) | 2014-06-25 |
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