JPS62240306A - Production of water-absorptive resin - Google Patents
Production of water-absorptive resinInfo
- Publication number
- JPS62240306A JPS62240306A JP8256886A JP8256886A JPS62240306A JP S62240306 A JPS62240306 A JP S62240306A JP 8256886 A JP8256886 A JP 8256886A JP 8256886 A JP8256886 A JP 8256886A JP S62240306 A JPS62240306 A JP S62240306A
- Authority
- JP
- Japan
- Prior art keywords
- oxidizing agent
- water
- polymerization
- reducing agent
- agent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000011347 resin Substances 0.000 title claims abstract description 23
- 229920005989 resin Polymers 0.000 title claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 title claims description 15
- 239000007800 oxidant agent Substances 0.000 claims abstract description 45
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 27
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims abstract description 17
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000006386 neutralization reaction Methods 0.000 claims abstract description 7
- 150000001768 cations Chemical class 0.000 claims abstract description 4
- 239000003505 polymerization initiator Substances 0.000 claims description 11
- 150000003839 salts Chemical class 0.000 claims description 9
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 8
- 229910052717 sulfur Inorganic materials 0.000 claims description 8
- 239000011593 sulfur Substances 0.000 claims description 8
- -1 Hydrogen salt Chemical class 0.000 claims description 7
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical group OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 claims description 4
- GRWZHXKQBITJKP-UHFFFAOYSA-L dithionite(2-) Chemical compound [O-]S(=O)S([O-])=O GRWZHXKQBITJKP-UHFFFAOYSA-L 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-UHFFFAOYSA-N 0.000 claims 1
- 238000006116 polymerization reaction Methods 0.000 abstract description 28
- 239000000178 monomer Substances 0.000 abstract description 13
- 239000003999 initiator Substances 0.000 abstract description 7
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 abstract description 4
- 239000002253 acid Substances 0.000 abstract description 3
- 239000000969 carrier Substances 0.000 abstract description 2
- JVBXVOWTABLYPX-UHFFFAOYSA-L sodium dithionite Chemical compound [Na+].[Na+].[O-]S(=O)S([O-])=O JVBXVOWTABLYPX-UHFFFAOYSA-L 0.000 abstract description 2
- 235000010265 sodium sulphite Nutrition 0.000 abstract description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 abstract 2
- 238000004587 chromatography analysis Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 26
- 229910001868 water Inorganic materials 0.000 description 26
- 239000000243 solution Substances 0.000 description 14
- 239000007864 aqueous solution Substances 0.000 description 13
- 238000010521 absorption reaction Methods 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 10
- 239000002250 absorbent Substances 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- 230000002745 absorbent Effects 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 5
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 4
- 229940048053 acrylate Drugs 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 230000003472 neutralizing effect Effects 0.000 description 3
- RWPGFSMJFRPDDP-UHFFFAOYSA-L potassium metabisulfite Chemical compound [K+].[K+].[O-]S(=O)S([O-])(=O)=O RWPGFSMJFRPDDP-UHFFFAOYSA-L 0.000 description 3
- 235000010263 potassium metabisulphite Nutrition 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- LCPVQAHEFVXVKT-UHFFFAOYSA-N 2-(2,4-difluorophenoxy)pyridin-3-amine Chemical compound NC1=CC=CN=C1OC1=CC=C(F)C=C1F LCPVQAHEFVXVKT-UHFFFAOYSA-N 0.000 description 2
- VAPQAGMSICPBKJ-UHFFFAOYSA-N 2-nitroacridine Chemical compound C1=CC=CC2=CC3=CC([N+](=O)[O-])=CC=C3N=C21 VAPQAGMSICPBKJ-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- XXROGKLTLUQVRX-UHFFFAOYSA-N allyl alcohol Chemical compound OCC=C XXROGKLTLUQVRX-UHFFFAOYSA-N 0.000 description 2
- 150000004645 aluminates Chemical class 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 229960003975 potassium Drugs 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- CHQMHPLRPQMAMX-UHFFFAOYSA-L sodium persulfate Substances [Na+].[Na+].[O-]S(=O)(=O)OOS([O-])(=O)=O CHQMHPLRPQMAMX-UHFFFAOYSA-L 0.000 description 2
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 description 2
- 235000019345 sodium thiosulphate Nutrition 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 1
- PQUXFUBNSYCQAL-UHFFFAOYSA-N 1-(2,3-difluorophenyl)ethanone Chemical compound CC(=O)C1=CC=CC(F)=C1F PQUXFUBNSYCQAL-UHFFFAOYSA-N 0.000 description 1
- BSKHPKMHTQYZBB-UHFFFAOYSA-N 2-methylpyridine Chemical compound CC1=CC=CC=N1 BSKHPKMHTQYZBB-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- 241000257465 Echinoidea Species 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
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- LEMJDBDGPTVGML-UHFFFAOYSA-N [K].ON=O Chemical compound [K].ON=O LEMJDBDGPTVGML-UHFFFAOYSA-N 0.000 description 1
- HDYRYUINDGQKMC-UHFFFAOYSA-M acetyloxyaluminum;dihydrate Chemical compound O.O.CC(=O)O[Al] HDYRYUINDGQKMC-UHFFFAOYSA-M 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 229940009827 aluminum acetate Drugs 0.000 description 1
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical class OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 150000002169 ethanolamines Chemical class 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- 239000007970 homogeneous dispersion Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 244000005700 microbiome Species 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
- 239000004745 nonwoven fabric Substances 0.000 description 1
- GSWAOPJLTADLTN-UHFFFAOYSA-N oxidanimine Chemical compound [O-][NH3+] GSWAOPJLTADLTN-UHFFFAOYSA-N 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
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 238000007868 post-polymerization treatment Methods 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 239000011736 potassium bicarbonate Substances 0.000 description 1
- 235000015497 potassium bicarbonate Nutrition 0.000 description 1
- 229910000028 potassium bicarbonate Inorganic materials 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 235000011181 potassium carbonates Nutrition 0.000 description 1
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 1
- 229940086066 potassium hydrogencarbonate Drugs 0.000 description 1
- BHZRJJOHZFYXTO-UHFFFAOYSA-L potassium sulfite Chemical compound [K+].[K+].[O-]S([O-])=O BHZRJJOHZFYXTO-UHFFFAOYSA-L 0.000 description 1
- 235000019252 potassium sulphite Nutrition 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 239000012966 redox initiator Substances 0.000 description 1
- 239000003340 retarding agent Substances 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 229940047670 sodium acrylate Drugs 0.000 description 1
- 229910001388 sodium aluminate Inorganic materials 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical class [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 1
- 150000004764 thiosulfuric acid derivatives Chemical class 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Landscapes
- Polymerization Catalysts (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【発明の詳細な説明】 く産業上の利用分野〉 この発明は、吸水性樹脂の製造方法に関する。[Detailed description of the invention] Industrial application fields> The present invention relates to a method for producing a water absorbent resin.
さらに詳細には、この発明は製造上の安全性に優れかつ
高い吸水能力を有する吸水性樹脂の製造方法に関する。More specifically, the present invention relates to a method for producing a water-absorbing resin having excellent manufacturing safety and high water-absorbing capacity.
〈従来の技術および発明が解決しようとびる問題点〉
近年、紙おむつ、生理用品、微生物や植物の培地、液体
クロマトグラフィーの担体等に、高い吸水能力および保
水能力を有する吸水性樹脂が用いられている。このよう
な吸水性樹脂の一種として、架橋型ポリアクリル酸金属
塩系が汎用されている。<Problems to be solved by conventional techniques and inventions> In recent years, water-absorbing resins with high water-absorbing and water-retaining abilities have been used for disposable diapers, sanitary products, culture media for microorganisms and plants, carriers for liquid chromatography, etc. There is. As a type of such water-absorbing resin, a crosslinked polyacrylic acid metal salt type is widely used.
このアクリル酸金属塩系吸水性樹脂は、アクリル酸すi
・リウム、アクリル酸カリウム等のアクリル醒アルカリ
金属塩水溶液に、重合開始剤を添加して重合させた後、
水分を除去して製造されている。この際、重合開始剤と
しては、例えば、過硫酸ナリウム、過硫酸ナトリウム等
の過iiQ酸塩、酸化剤と還元剤との組合せよりなるレ
ドックス触媒(例えば、前記過硫F[[塩と一価銅イオ
ン、過酸化水素と二価鉄イオン等)が使用されるが、こ
れらの過硫酸塩やレドックス触媒を開始剤として用いる
と、重合反応が極めて急激で、例えば、Φ合開始温度は
常温でも重合の進行とともに急激に発熱する。符に、工
業的な生産のJ:うに、大量且つ高上ツマー濃度で実施
される場合には、特別な配慮をしない限りその制御は困
難で、時には暴走反応を生じ、危険性が極めて高いもの
である。かかる観点から、暴走反応を防止するため、モ
ノマー濃度を低くすることや、温度制御システムを用い
て、前記アクリルB塩の重合を行っているが、モノマー
濃度を低くすることは、水分の蒸発に多大の熱量を要し
非ai的であり、また温度制御システムを導入した装置
も高価となる問題がある。This acrylic acid metal salt-based water absorbent resin is
・After adding a polymerization initiator to an aqueous solution of an alkali metal salt such as potassium acrylate or potassium acrylate and polymerizing it,
Manufactured by removing moisture. In this case, as a polymerization initiator, for example, a periiQ acid salt such as sodium persulfate or sodium persulfate, a redox catalyst consisting of a combination of an oxidizing agent and a reducing agent (for example, the persulfur F[[salt and monovalent copper ions, hydrogen peroxide, divalent iron ions, etc.), but when these persulfates or redox catalysts are used as initiators, the polymerization reaction is extremely rapid, and for example, the Φ polymerization initiation temperature is low even at room temperature. As polymerization progresses, heat is generated rapidly. In particular, when industrial production of sea urchin is carried out in large quantities and at high concentrations, it is difficult to control unless special consideration is taken, and sometimes runaway reactions occur, which is extremely dangerous. It is. From this point of view, in order to prevent runaway reactions, the acrylic B salt is polymerized by lowering the monomer concentration and using a temperature control system, but lowering the monomer concentration prevents moisture evaporation. There are problems in that it requires a large amount of heat and is unsuitable for AI, and the equipment incorporating the temperature control system is also expensive.
く目 的ン
この発明は上記問題点に鑑みてなされたものであり、特
殊な重合開始剤を使用することにより、極めて温和な条
件下にアクリル酸金属塩の重合が進行し、安全性が高い
とともに高い吸水能力を有する吸水性I4脂の製造方法
を提供することを目的とする。Purpose This invention was made in view of the above problems, and by using a special polymerization initiator, the polymerization of acrylic acid metal salt proceeds under extremely mild conditions, resulting in a highly safe method. It is also an object of the present invention to provide a method for producing a water-absorbing I4 fat having a high water-absorbing capacity.
く問題を解決するための手段〉
上記目的を達成ヅるためになされた、この発明の吸水性
樹脂の製造方法は、1価陽イオンによる中和度が30%
以上100%未満のアクリル酸を、含硫黄系還元剤と酸
化剤とからなる重合開始剤を用いて重合し、さらに酸化
剤で処3!Jl!することを特徴とするものである。Means for Solving the Problems> The method for producing a water-absorbing resin of the present invention, which has been devised to achieve the above object, has a degree of neutralization by monovalent cations of 30%.
The above 100% acrylic acid is polymerized using a polymerization initiator consisting of a sulfur-containing reducing agent and an oxidizing agent, and then treated with an oxidizing agent.3! Jl! It is characterized by:
なtB、この明llI出において、中和度とは、仕込み
七ツマー中のアクリル酸とアクリルi1mの総計に対す
るアクリル酸塩の比率をいい、下記の式で定義きれる。In this paper, the degree of neutralization refers to the ratio of acrylate to the total amount of acrylic acid and acrylic i1m in the seven-layer mixture, and can be defined by the following formula.
アクIJルMJu(−E/Iz) X100中和度(
%)=
アクリル酸+アクリル酸塩(モル)
上記の構成において、アクリル酸の中和に使用される中
和剤としては、最終製品たる吸水性樹脂の使用目的に応
じて適宜選択されるが、例えば、水酸化ナトリウム、水
酸化カリウム、水酸化リチウム等のアルカリ金属水酸化
物、炭酸すI−リウム、炭酸カリウム、炭酸水素ナトリ
ウム、炭酸水素カリウム等のアルカリ金FA炭酸塩また
は炭酸水素塩、水酸化アンモニウム、トリエチルアミン
、エタノールアミン類、ピリジン、ピコリン等の有機ア
ミン類等、−価の陽イオンとして作用しえるfiI基の
内から任意に選択できるが、経済性、安全性および1!
7られた吸水性樹脂の吸水性能等を考慮づると水酸化す
トす・クムが適切である。Ac IJ Le MJu (-E/Iz) X100 Neutralization degree (
%) = acrylic acid + acrylate (mol) In the above configuration, the neutralizing agent used to neutralize the acrylic acid is appropriately selected depending on the purpose of use of the final product, the water-absorbing resin. For example, alkali metal hydroxides such as sodium hydroxide, potassium hydroxide, lithium hydroxide, alkali gold FA carbonates or hydrogen carbonates such as sodium carbonate, potassium carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, water Any fiI group that can act as a -valent cation can be selected, such as ammonium oxide, triethylamine, ethanolamines, pyridine, organic amines such as picoline, etc., but it is economical, safe and 1!
Taking into account the water absorption performance of the water absorbent resin, hydroxylated soot and cum are suitable.
また、アクリル酸の中和度としては、30%以上、好ま
しくは50%以上、さらに好ましくは70%以上95%
以下のものが、得られた吸水性樹脂の吸水性能からして
好ましい。また、アクリル酸の一価陽イオン塩とアクリ
ル酸を適宜な割合で混合して、前記のアクリル酸塩水溶
液を調製してもよい。重台溶液の濃度は発熱の少ないと
いうこの発明の特徴からすると、溶液中のモノマー濃度
は高い程、この発明の技術的、装置的、性能的効果が顕
著となるが、水酸化ナトリウムで中性付近に中和を行う
場合、水分濃度が45%〜50%以下になるとアクリル
酸ナトリウムが析出するので、七ツマーaj斐をより高
くする場合には、混合撹拌等により溶液の均質化を図る
必要がある。Further, the degree of neutralization of acrylic acid is 30% or more, preferably 50% or more, more preferably 70% or more and 95%.
The following are preferable in terms of the water absorption performance of the obtained water absorbent resin. Alternatively, the aqueous acrylate solution may be prepared by mixing a monovalent cation salt of acrylic acid and acrylic acid in an appropriate ratio. Considering the feature of this invention that the concentration of the heavy-base solution generates less heat, the higher the monomer concentration in the solution, the more remarkable the technical, equipment, and performance effects of this invention are. When neutralizing the solution, sodium acrylate will precipitate if the water concentration falls below 45% to 50%, so if you want to increase the water content even higher, it is necessary to homogenize the solution by mixing, stirring, etc. There is.
また、この発明で得られる吸水性樹脂の吸水能力、ゲル
強度等を改質するために、前記のアクリル酸にはアクリ
ルアミド、メチレンビスアクリルアミド、N−ビニルビ
Oリドン等を添加して共重合体としてもよい。In addition, in order to modify the water absorption ability, gel strength, etc. of the water absorbent resin obtained by this invention, acrylamide, methylenebisacrylamide, N-vinyl biOlidone, etc. are added to the acrylic acid to form a copolymer. Good too.
この発明の製造方法では、重合開始剤として含硫黄系還
元剤と酸化剤が併用される。使用される含硫黄系還元剤
としては、例えば、亜硫酸ナトリウム、亜i酸カリウム
等の亜硫Fi塩、亜硫酸水素ナトリウム、亜’fAM水
素カリウム等の亜硫酸水素塩、チオ硫酸ナトリウム、チ
オ硫酸ナトリウム等のチオ硫酸塩、亜二チオン酸ナトリ
ウム等の化ニチオン酸塩等またはこれらの混合物が例示
でき、特に亜硫酸塩、亜二チオン酸塩が好ましい。これ
らの含硫黄系還元剤は、粉末状態のままでも使用できる
が、通常水溶液として使用される。In the production method of the present invention, a sulfur-containing reducing agent and an oxidizing agent are used together as a polymerization initiator. Examples of the sulfur-containing reducing agent used include sulfite Fi salts such as sodium sulfite and potassium sulfite, hydrogen sulfites such as sodium bisulfite and potassium hydrogen nitrite, sodium thiosulfate, sodium thiosulfate, etc. Examples include thiosulfates, dithionates such as sodium dithionite, and mixtures thereof, with sulfites and dithionites being particularly preferred. Although these sulfur-containing reducing agents can be used in powder form, they are usually used as an aqueous solution.
また、酸化剤としては、慣用の酸化剤、例えば、ベルオ
キソニVA1%!ナトリウム、ベルオキソニRMカリウ
ム、ベルオキソニ硫酸アンモニウム等のベルオキソニ硫
酸塩等が挙げられ、単独で、または混合物として使用さ
れる。また、粉末状態で6使用できるが、通常水溶液と
して使用される。In addition, as the oxidizing agent, a conventional oxidizing agent such as Beloxoni VA1%! Examples include peroxonisulfates such as sodium, peroxoniRM potassium, and ammonium peroxonisulfate, which are used alone or as a mixture. Although it can be used in powder form, it is usually used as an aqueous solution.
重合に使用される」−記の還元剤および酸化剤の量は、
組合される還元剤と酸化剤の種類、重合温度、モノマー
水溶液の濃度、吸水性樹脂に要求される特性等により異
なるが、通常、七ツマー仕込みff1100重吊部に対
重量、それぞれ0.001〜0.5重量部の範囲から適
宜選択される。還元剤おJ:び酸化剤の添加量が、それ
ぞれ0.001重市1未満では、反応が遅く重合時間が
長くなる。The amounts of reducing agent and oxidizing agent used in the polymerization are:
Although it varies depending on the type of reducing agent and oxidizing agent to be combined, the polymerization temperature, the concentration of the monomer aqueous solution, the properties required of the water-absorbing resin, etc., it is usually 0.001 to 0.001 to 100% by weight, respectively, relative to the weight of the FF1100 heavy hanging section for seven months preparation. It is appropriately selected from a range of 0.5 parts by weight. If the amount of the reducing agent, J and oxidizing agent added is less than 0.001 and 1, the reaction will be slow and the polymerization time will be long.
また、還元剤および酸化剤の添加量が、それぞれ0.5
重量部を越えると、重合溶液が高粘度となり、モノマー
濃度を下げないと撹拌混合が困難になる。還元剤と酸化
剤の好ましい添加量は、それぞれ0.01〜0.11伍
部である。In addition, the amount of the reducing agent and the oxidizing agent added was 0.5 each.
If the amount exceeds 1 part by weight, the polymerization solution will have a high viscosity, and stirring and mixing will become difficult unless the monomer concentration is lowered. The preferable addition amounts of the reducing agent and the oxidizing agent are 0.01 to 0.11 parts, respectively.
この発明において、重合後の処理に使用される酸化剤と
しては、前記で例示した酸化剤と同様なものが挙げられ
る。この酸化剤は、通常、モノマー仕込みff1100
重量部に対して、0.001〜0.5小量部程度添加さ
れる。また、この酸化剤は、上記の重合開始剤としての
還元剤と酸化剤の組合じにおける酸化剤に合わせて添加
してもよく、また車台が終了した後、反応系に添加して
もよい。In this invention, the oxidizing agent used in the post-polymerization treatment includes the same oxidizing agents as exemplified above. This oxidizing agent is usually used for monomer preparation ff1100.
It is added in an amount of about 0.001 to 0.5 parts by weight. Further, this oxidizing agent may be added together with the oxidizing agent in the above-mentioned combination of a reducing agent and an oxidizing agent as a polymerization initiator, or may be added to the reaction system after the car chassis is completed.
この発明の製造方法で1琴られる吸水性樹脂は、重合開
始剤として使用される還元剤および酸化剤ならびに後処
理用として使用される酸化剤の使用量により、吸水能力
、吸水後のゲル強度等を適宜変更することができる。一
般的に、例えば、酸化剤の総對添加量を一定にして、還
元剤の使用量を変更した場合、還元剤の使用量の増加と
共に吸水能力が大きくなるがある範囲を越えると可溶化
傾向が大きくなる。また、還元剤の使用量を一定にして
、酸化剤の総計使用量を増加すると、吸水量が減少し、
吸水後のゲル状態が硬くなり、また減少させると軟らか
くなる傾向にある。しかし、各々が前記の添加範囲内で
比例的に増加、減少して使用された場合には得られたポ
リマーの性能には大きな差異が認められない。The water-absorbing resin produced by the production method of the present invention has a water-absorbing capacity, gel strength after water absorption, etc. depending on the amount of the reducing agent and oxidizing agent used as a polymerization initiator and the oxidizing agent used for post-treatment. can be changed as appropriate. Generally, for example, when the total amount of oxidizing agent added is constant and the amount of reducing agent used is changed, as the amount of reducing agent used increases, the water absorption capacity increases. becomes larger. In addition, if the total amount of oxidizing agent used is increased while the amount of reducing agent used is constant, the amount of water absorption decreases,
The gel state tends to become hard after absorbing water, and becomes soft when reduced. However, when each is used in a proportionately increased or decreased amount within the above-mentioned addition range, no significant difference is observed in the performance of the resulting polymers.
また、この発明の製造方法において、硝酸アルミニウム
、酢酸アルミニウム、塩化アルミニウム、114Mアル
ミニウム等のアルミニウム塩、アルミニウムアルコラー
ド、アルミン酸ナトリウム等のアルミン酸塩a塩等のア
ルミニウム化合物を添加することにより、重合体の架m
度を調整することもできる。特に開始剤濃度が低い条件
下で製造された吸水性樹脂は、可溶性部分を含有したり
吸水後のゲル状態が軟らかくなる傾向があるので、この
ような場合に上記アルミニウム化合物を添加すると、吸
水量の増加およびゲル強度の改良を図ることができる。In addition, in the production method of the present invention, aluminum compounds such as aluminum salts such as aluminum nitrate, aluminum acetate, aluminum chloride, and 114M aluminum, aluminate a salts such as aluminum alcoholade, and sodium aluminate can be added. Combined frame m
You can also adjust the degree. In particular, water-absorbent resins produced under conditions with low initiator concentration tend to contain soluble portions or become soft after water absorption, so adding the above aluminum compound in such cases will reduce the amount of water absorbed. and improve gel strength.
なお、上記アルミニウム化合物中、アルミニウム塩等は
モノマー水溶液または開始剤水溶液のいずれに添加して
も使用できるが、アルミン酸塩の場合には、開始剤水溶
液に添加づるとアルカリが開始剤を分解する恐れがある
ので、モノマー水溶液中に添加す゛るのがよい。これら
のアルミニウム化合物は、通常、モノマー仕込みff1
100重量部に対して5重量部以下、好ましくは0.1
〜0.51!吊部程度添加される。Note that among the above aluminum compounds, aluminum salts can be used by adding them to either the monomer aqueous solution or the initiator aqueous solution, but in the case of aluminate, when added to the initiator aqueous solution, the alkali decomposes the initiator. Therefore, it is best to add it to the monomer aqueous solution. These aluminum compounds are usually prepared by monomer charging ff1
5 parts by weight or less, preferably 0.1 parts by weight per 100 parts by weight
~0.51! A hanging part is added.
次に、この発明の製造方法の一例を詳細に説明する。Next, an example of the manufacturing method of the present invention will be explained in detail.
まず、アクリル酸を前記の中和剤水溶液にて所望の中和
度および重合に適当な濃度となるようにに中和する。こ
の溶液に前記の還元剤水溶液および酸化剤水溶液を添加
し重合を開始する。重合の進行と共に該溶液は粘度が上
昇し、ある程度重合が進行し高粘度となった時、前記の
酸化剤水溶液を反応系にさらに添加して、必要に応じて
加熱し、処理した後、反応液を脱水乾燥させて、この発
明の吸水性樹脂が得られる。First, acrylic acid is neutralized with the aqueous neutralizing agent solution to a desired degree of neutralization and a concentration suitable for polymerization. The aforementioned reducing agent aqueous solution and oxidizing agent aqueous solution are added to this solution to initiate polymerization. As the polymerization progresses, the viscosity of the solution increases, and when the polymerization progresses to a certain extent and the viscosity becomes high, the above-mentioned oxidizing agent aqueous solution is further added to the reaction system, heated as necessary, and after treatment, the reaction is started. The water absorbent resin of the present invention is obtained by dehydrating and drying the liquid.
上記の工程においては、還元剤および酸化剤を同時に反
応系に添加しているが、この場合には酸化剤の使用量を
増加する方が好ましい結果を得ることができる。また、
あらかじめモノマー水溶液に酸化剤を添加した溶液に還
元剤を添加して重合反応を開始することもできる。In the above process, the reducing agent and the oxidizing agent are added to the reaction system at the same time, but in this case, a more favorable result can be obtained by increasing the amount of the oxidizing agent used. Also,
The polymerization reaction can also be started by adding a reducing agent to a solution in which an oxidizing agent is added to an aqueous monomer solution in advance.
また、上記工程において、還元剤および酸化剤とからな
る重合開始剤による重合は通常室温で充分に進行するが
、必要に応じて加温または加熱してもよい。加温または
加熱した場合には、重合反応は速やかに進行し、粘度は
急激に上昇するので、後処理用の酸化剤の添加時期は重
要であり、得られる樹脂の吸水能力に大きく影響する。Further, in the above step, polymerization using a polymerization initiator consisting of a reducing agent and an oxidizing agent normally proceeds sufficiently at room temperature, but heating or heating may be performed as necessary. When heated or heated, the polymerization reaction proceeds quickly and the viscosity rapidly increases, so the timing of addition of the oxidizing agent for post-treatment is important and greatly affects the water absorption ability of the resulting resin.
一般的な傾向として、該酸化剤の添加時期が遅れると、
高粘度のため、添加された酸化剤の均質な分散が妨げら
れ、重合物が不均質なものとなり、可溶性の部分が生ず
る恐れがある。従って、加温または加熱する場合には、
後処理用の酸化剤をあらかじめ添加した系とするか、ま
たはアリルアルコール、プロピレングリコール等のΦ合
遅延剤の併用が好ましい。As a general tendency, if the timing of adding the oxidizing agent is delayed,
The high viscosity prevents homogeneous dispersion of the added oxidizing agent, resulting in a non-homogeneous polymer, which may result in soluble portions. Therefore, when warming or heating,
It is preferable to use a system in which an oxidizing agent for post-treatment is added in advance, or to use a Φ-retarding agent such as allyl alcohol or propylene glycol in combination.
後処理用の酸化剤を添加俊の51!L理温度は、使用す
る酸化剤が分解または活性化する温度ないしそれ以上の
温度でよく、また、還元剤と酸化剤を同時に使用する場
合には室温程度でもよい。酸化剤による処理後、反応系
内の水分を除去し乾燥すること、また100℃程度で酸
化剤処理をしても性能その他になんら変化が認められな
かったことなどを考慮1yると系内に共存する水分の沸
点程度で51!!即するのが好都合である。Shun's 51 with added oxidizing agent for post-processing! The temperature may be at or above the temperature at which the oxidizing agent used is decomposed or activated, or may be around room temperature when a reducing agent and an oxidizing agent are used simultaneously. After treatment with an oxidizing agent, water in the reaction system must be removed and dried, and even after treatment with an oxidizing agent at around 100°C, no changes in performance or other aspects were observed. 51 at the boiling point of the coexisting water! ! It is convenient to do so immediately.
く作 用〉
この発明は上記の構成よりなり、従来のレドックス開始
剤による重合と異なり、含硫黄系還元剤と酸化剤とから
なる重合開始剤によるアクリル酸塩の重合は極めて発熱
性が低く、温和な条件下に速やかに進行し、ある程度重
合が進行した後酸化剤により処即し、さらなる重合また
は架橋反応等を行うので、重合中における温度制御が容
易となり、暴走反応等を防止できる。Effects> The present invention has the above configuration, and unlike polymerization using a conventional redox initiator, the polymerization of acrylate using a polymerization initiator consisting of a sulfur-containing reducing agent and an oxidizing agent has extremely low exothermicity. The polymerization proceeds rapidly under mild conditions, and after the polymerization has progressed to some extent, it is treated with an oxidizing agent and further polymerization or crosslinking reactions are performed, making it easy to control the temperature during polymerization and preventing runaway reactions.
また、重合が温和な条件下に進行するので、副反応等が
少なく、吸水能力の大きな吸水性樹脂を青ることができ
る。In addition, since the polymerization proceeds under mild conditions, there are few side reactions, etc., and a water-absorbing resin with a large water-absorbing capacity can be produced.
〈実施例〉
以下、実施例をもって、この発明をより詳細に説明する
。<Examples> The present invention will be described in more detail below with reference to Examples.
実施例1
アクリル110gに25%淵度の水酸化ナトリウム水溶
液20gを加えて中和したものに、常温で1%濃度のベ
ルオキソニ1ilQ酸カリウム水溶液13を加えた後、
1%濃度のピロ亜硫酸カリウム水溶液3Jを加えると、
溶液温度が35℃乃至40℃となって直ちに重合し、約
1時間俊にはタック性のほとんどないゴム状重合体とな
り、数時間以上経過したものは緩慢な吸水性を示し可溶
性の部分も存在するが、ピロ亜硫酸カリウムの添加後1
時間以内に60°C以上に加熱して脱水乾燥したものは
水道水中800〜1000倍の吸水性能を示し、可溶部
分はなかつった。ピロ亜硫酸カリウム添加後の重合によ
る粘度1胃が生じる初期に加熱容器中に流しこむと数分
後にはゴム状となり、重合時の特別な光熱や突沸現鍮は
全く観察されない。Example 1 110 g of acrylic was neutralized by adding 20 g of a 25% aqueous sodium hydroxide solution, and then a 1% aqueous solution of potassium belloxoniilQ acid 13 was added at room temperature.
When 3J of 1% potassium pyrosulfite aqueous solution is added,
When the solution temperature reaches 35°C to 40°C, it immediately polymerizes, becoming a rubbery polymer with almost no tackiness after about an hour, and after several hours it shows slow water absorption and some soluble parts are present. However, after addition of potassium pyrosulfite, 1
Those that were dehydrated and dried by heating to 60° C. or higher within an hour showed water absorption performance 800 to 1000 times higher than that of tap water, and there was no soluble portion. If the mixture is poured into a heating container at the initial stage when a viscosity due to polymerization after addition of potassium pyrosulfite is produced, it becomes rubbery after a few minutes, and no special light heat or bumping is observed during polymerization.
このゴム状物を脱水乾燥したものは、水道水中で120
0倍以上、0.9%食塩水中で12018以上の吸水性
能を示した。After dehydrating and drying this rubbery material, it can be immersed in tap water at 120%
It showed water absorption performance of 0 times or more and 12018 or more in 0.9% saline.
く効果〉
以上のJ:うに、この発明の吸水性樹脂の製造方法によ
れば、特殊な重合開始剤を使用することにより温和な条
件下に重合が進行し、温度制御が容易になるので、安全
かつ広い範囲で重合条件を設定でd゛る。また、技術的
、装置的に容易かつ簡易であり、安全性および経済性に
も優れる。得られる吸水性樹脂6、その吸水性能に優れ
るとともに、使用される含硫黄系還元剤および酸化剤の
帛を適宜変更覆ることにJ、す、その性状おJ:び性能
を変更でき、所望の製品かえられ、その適用範囲を拡大
することができる。さらに、その製法においても、公知
のものを含め幅広い方法を利用でき、例えば、回転移動
するベルト上に連続的にモノマー溶液を均一に流しこめ
ば、フィルムまたは板状物が得られるし、上下に回転す
る加熱板や加熱した不活性気体または空気中に噴霧すれ
ば粉末状にすることができる。また、形状物や不織布等
への塗布含浸後の加熱や、ロールやスクリュー或いはミ
キサー中での混練加熱、さらには溶媒の沸点を利用して
脱水粉末状にする逆相乳化用合法等、種々の製造方法を
利用することができるという利点を有する。According to the method for producing a water-absorbing resin of the present invention, polymerization proceeds under mild conditions by using a special polymerization initiator, and temperature control becomes easy. Polymerization conditions can be set within a safe and wide range. In addition, it is technically and equipment-wise easy and simple, and has excellent safety and economical efficiency. The obtained water absorbent resin 6 has excellent water absorption performance, and its properties and performance can be changed by appropriately changing the sulfur-containing reducing agent and oxidizing agent used, and the desired properties can be achieved. The product can be changed and its scope of application can be expanded. Furthermore, a wide range of methods including well-known methods can be used for its production. For example, if a monomer solution is continuously and uniformly poured onto a rotating belt, a film or plate-like product can be obtained; It can be made into a powder by spraying it into a rotating heating plate, heated inert gas, or air. In addition, various methods are used, such as heating after coating and impregnating shaped objects and nonwoven fabrics, kneading and heating in rolls, screws, or mixers, and inverse emulsification methods that utilize the boiling point of the solvent to dehydrate and form powders. It has the advantage that the manufacturing method can be used.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61082568A JPH0794501B2 (en) | 1986-04-10 | 1986-04-10 | Method for producing water absorbent resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61082568A JPH0794501B2 (en) | 1986-04-10 | 1986-04-10 | Method for producing water absorbent resin |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62240306A true JPS62240306A (en) | 1987-10-21 |
JPH0794501B2 JPH0794501B2 (en) | 1995-10-11 |
Family
ID=13778089
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61082568A Expired - Lifetime JPH0794501B2 (en) | 1986-04-10 | 1986-04-10 | Method for producing water absorbent resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0794501B2 (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5823811A (en) * | 1981-08-04 | 1983-02-12 | Japan Exlan Co Ltd | Preparation of water-soluble polymer having high stability |
-
1986
- 1986-04-10 JP JP61082568A patent/JPH0794501B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5823811A (en) * | 1981-08-04 | 1983-02-12 | Japan Exlan Co Ltd | Preparation of water-soluble polymer having high stability |
Also Published As
Publication number | Publication date |
---|---|
JPH0794501B2 (en) | 1995-10-11 |
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