JPS63215773A - Production of composition containing water-soluble high-molecular material - Google Patents
Production of composition containing water-soluble high-molecular materialInfo
- Publication number
- JPS63215773A JPS63215773A JP4798487A JP4798487A JPS63215773A JP S63215773 A JPS63215773 A JP S63215773A JP 4798487 A JP4798487 A JP 4798487A JP 4798487 A JP4798487 A JP 4798487A JP S63215773 A JPS63215773 A JP S63215773A
- Authority
- JP
- Japan
- Prior art keywords
- water
- stirring
- dispersion
- soluble polymer
- molecular material
- 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
- 239000000203 mixture Substances 0.000 title claims abstract description 45
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 239000000463 material Substances 0.000 title abstract description 8
- 238000003756 stirring Methods 0.000 claims abstract description 66
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 52
- 239000006185 dispersion Substances 0.000 claims abstract description 46
- 230000008961 swelling Effects 0.000 claims abstract description 9
- 239000000126 substance Substances 0.000 claims description 63
- 229920003169 water-soluble polymer Polymers 0.000 claims description 42
- 239000003960 organic solvent Substances 0.000 claims description 23
- 150000001875 compounds Chemical class 0.000 claims description 4
- 229920000642 polymer Polymers 0.000 claims description 4
- 239000007788 liquid Substances 0.000 abstract description 29
- 238000002156 mixing Methods 0.000 abstract description 9
- 230000002093 peripheral effect Effects 0.000 abstract description 5
- 239000007787 solid Substances 0.000 abstract description 4
- 239000002904 solvent Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 27
- 239000002002 slurry Substances 0.000 description 20
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 17
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 16
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 15
- 239000007864 aqueous solution Substances 0.000 description 14
- 238000009472 formulation Methods 0.000 description 11
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 10
- 238000002360 preparation method Methods 0.000 description 9
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 8
- 239000004372 Polyvinyl alcohol Substances 0.000 description 8
- 229910000019 calcium carbonate Inorganic materials 0.000 description 8
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 8
- 229920002451 polyvinyl alcohol Polymers 0.000 description 8
- 239000000843 powder Substances 0.000 description 8
- 239000002994 raw material Substances 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- 238000004090 dissolution Methods 0.000 description 7
- 239000003973 paint Substances 0.000 description 7
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 235000019441 ethanol Nutrition 0.000 description 6
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 description 5
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 description 5
- 239000001768 carboxy methyl cellulose Substances 0.000 description 5
- 235000014113 dietary fatty acids Nutrition 0.000 description 5
- 239000000194 fatty acid Substances 0.000 description 5
- 229930195729 fatty acid Natural products 0.000 description 5
- 235000011187 glycerol Nutrition 0.000 description 5
- 239000006210 lotion Substances 0.000 description 5
- 235000010413 sodium alginate Nutrition 0.000 description 5
- 239000000661 sodium alginate Substances 0.000 description 5
- 229940005550 sodium alginate Drugs 0.000 description 5
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 235000010418 carrageenan Nutrition 0.000 description 4
- 239000000679 carrageenan Substances 0.000 description 4
- 229920001525 carrageenan Polymers 0.000 description 4
- 229940113118 carrageenan Drugs 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 4
- 239000000839 emulsion Substances 0.000 description 4
- 150000004665 fatty acids Chemical class 0.000 description 4
- 239000003205 fragrance Substances 0.000 description 4
- 239000008213 purified water Substances 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 235000019812 sodium carboxymethyl cellulose Nutrition 0.000 description 4
- 229920001027 sodium carboxymethylcellulose Polymers 0.000 description 4
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 4
- UHVMMEOXYDMDKI-JKYCWFKZSA-L zinc;1-(5-cyanopyridin-2-yl)-3-[(1s,2s)-2-(6-fluoro-2-hydroxy-3-propanoylphenyl)cyclopropyl]urea;diacetate Chemical compound [Zn+2].CC([O-])=O.CC([O-])=O.CCC(=O)C1=CC=C(F)C([C@H]2[C@H](C2)NC(=O)NC=2N=CC(=CC=2)C#N)=C1O UHVMMEOXYDMDKI-JKYCWFKZSA-L 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- -1 fatty acid esters Chemical class 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 235000015243 ice cream Nutrition 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 239000000049 pigment Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 229910000859 α-Fe Inorganic materials 0.000 description 3
- 244000060011 Cocos nucifera Species 0.000 description 2
- 235000013162 Cocos nucifera Nutrition 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 229960004106 citric acid Drugs 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000006071 cream Substances 0.000 description 2
- 238000011978 dissolution method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000000265 homogenisation Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- YGSDEFSMJLZEOE-UHFFFAOYSA-N salicylic acid Chemical compound OC(=O)C1=CC=CC=C1O YGSDEFSMJLZEOE-UHFFFAOYSA-N 0.000 description 2
- WXMKPNITSTVMEF-UHFFFAOYSA-M sodium benzoate Chemical compound [Na+].[O-]C(=O)C1=CC=CC=C1 WXMKPNITSTVMEF-UHFFFAOYSA-M 0.000 description 2
- 235000010234 sodium benzoate Nutrition 0.000 description 2
- 239000004299 sodium benzoate Substances 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical compound OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 description 1
- SPSPIUSUWPLVKD-UHFFFAOYSA-N 2,3-dibutyl-6-methylphenol Chemical compound CCCCC1=CC=C(C)C(O)=C1CCCC SPSPIUSUWPLVKD-UHFFFAOYSA-N 0.000 description 1
- GVLDOZDIEFWUJQ-UHFFFAOYSA-N 5-(1h-benzimidazol-2-yl)-1,3-thiazole Chemical compound S1C=NC=C1C1=NC2=CC=CC=C2N1 GVLDOZDIEFWUJQ-UHFFFAOYSA-N 0.000 description 1
- 244000215068 Acacia senegal Species 0.000 description 1
- 239000005711 Benzoic acid Substances 0.000 description 1
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- YASYEJJMZJALEJ-UHFFFAOYSA-N Citric acid monohydrate Chemical compound O.OC(=O)CC(O)(C(O)=O)CC(O)=O YASYEJJMZJALEJ-UHFFFAOYSA-N 0.000 description 1
- 229920000084 Gum arabic Polymers 0.000 description 1
- 229920000569 Gum karaya Polymers 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
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229910001035 Soft ferrite Inorganic materials 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- LUVOJBWJNHWVNG-UHFFFAOYSA-N [Na].[Na].[Na].OC(=O)CC(O)(C(O)=O)CC(O)=O Chemical compound [Na].[Na].[Na].OC(=O)CC(O)(C(O)=O)CC(O)=O LUVOJBWJNHWVNG-UHFFFAOYSA-N 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 235000010489 acacia gum Nutrition 0.000 description 1
- 239000000205 acacia gum Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 235000010443 alginic acid Nutrition 0.000 description 1
- 229920000615 alginic acid Polymers 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 235000013871 bee wax Nutrition 0.000 description 1
- 239000012166 beeswax Substances 0.000 description 1
- 229960000686 benzalkonium chloride Drugs 0.000 description 1
- 235000010233 benzoic acid Nutrition 0.000 description 1
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 description 1
- CADWTSSKOVRVJC-UHFFFAOYSA-N benzyl(dimethyl)azanium;chloride Chemical compound [Cl-].C[NH+](C)CC1=CC=CC=C1 CADWTSSKOVRVJC-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 235000010354 butylated hydroxytoluene Nutrition 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 229920003123 carboxymethyl cellulose sodium Polymers 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 229940105329 carboxymethylcellulose Drugs 0.000 description 1
- 229940063834 carboxymethylcellulose sodium Drugs 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229960002303 citric acid monohydrate Drugs 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 235000020247 cow milk Nutrition 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 150000004683 dihydrates Chemical class 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000004815 dispersion polymer Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 239000003974 emollient agent Substances 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- BEFDCLMNVWHSGT-UHFFFAOYSA-N ethenylcyclopentane Chemical compound C=CC1CCCC1 BEFDCLMNVWHSGT-UHFFFAOYSA-N 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 235000019197 fats Nutrition 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 239000007970 homogeneous dispersion Substances 0.000 description 1
- 229910003480 inorganic solid Inorganic materials 0.000 description 1
- 235000010494 karaya gum Nutrition 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 239000004482 other powder Substances 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- FJKROLUGYXJWQN-UHFFFAOYSA-N papa-hydroxy-benzoic acid Natural products OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 235000008476 powdered milk Nutrition 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000000518 rheometry Methods 0.000 description 1
- 229960004889 salicylic acid Drugs 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 235000020183 skimmed milk Nutrition 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 235000010199 sorbic acid Nutrition 0.000 description 1
- 239000004334 sorbic acid Substances 0.000 description 1
- 229940075582 sorbic acid Drugs 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- SOBHUZYZLFQYFK-UHFFFAOYSA-K trisodium;hydroxy-[[phosphonatomethyl(phosphonomethyl)amino]methyl]phosphinate Chemical compound [Na+].[Na+].[Na+].OP(O)(=O)CN(CP(O)([O-])=O)CP([O-])([O-])=O SOBHUZYZLFQYFK-UHFFFAOYSA-K 0.000 description 1
- 229940099259 vaseline Drugs 0.000 description 1
- 235000010493 xanthan gum Nutrition 0.000 description 1
- 239000000230 xanthan gum Substances 0.000 description 1
- 229920001285 xanthan gum Polymers 0.000 description 1
- 229940082509 xanthan gum Drugs 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野コ
本発明は、水溶性高分子物質が均一に膨潤、溶解した組
成物を製造する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a composition in which a water-soluble polymeric substance is uniformly swollen and dissolved.
[従来の技術]
水溶性高分子物質は、増粘性、vc着性、乳化分散性、
賦型性、保水性、保護コロイド性、#酸性、#塩性、懸
濁性などの性質を有しているので、それらの性質を利用
して、近年では、食品、医薬、化粧品、繊維、建材、窯
業、土木ポーリング、製紙工業、造粒等の各種産業分野
や、泡末消化剤、塗料、接着剤、絵具等にも使用されて
いる。[Prior art] Water-soluble polymer substances have thickening properties, VC adhesion properties, emulsification and dispersion properties,
It has properties such as formability, water retention, protective colloidal, #acidic, #salt, and suspending properties.In recent years, these properties have been used to create products such as food, medicine, cosmetics, textiles, It is used in various industrial fields such as building materials, ceramics, civil engineering polling, paper manufacturing, and granulation, as well as in foam extinguishing agents, paints, adhesives, paints, etc.
しかしながら、水溶性高分子物質含有組成物の調製にお
いて、適切な配合方法がとられない場合には、水溶性高
分子物質は、これを含有する組成物に配合する他の配合
原料、たとえば食塩などの電解質やカルシウムイオンな
どの金属塩により、膨潤、溶解に悪影響を受けたり、或
いは他の分散質配合原料と添加時に直ちに吸着または反
応したりして、目的とする性質を利用できないことがあ
るので、このような問題を回避するため、またノ\ンド
リングの点から、予め5%濃度以下の水溶性高分子物質
が完全に膨潤、溶解した水溶液を予備調製する方法が多
くの場合採用されている。However, in the preparation of a water-soluble polymer substance-containing composition, if an appropriate blending method is not taken, the water-soluble polymer substance may be mixed with other ingredients, such as salt, to be blended into the composition containing it. Electrolytes and metal salts such as calcium ions may adversely affect swelling and dissolution, or they may adsorb or react with other dispersion ingredients immediately upon addition, making it impossible to utilize the desired properties. In order to avoid such problems and from the viewpoint of nodling, a method is often adopted in which an aqueous solution is prepared in advance in which a water-soluble polymer substance with a concentration of 5% or less is completely swollen and dissolved. .
そして、上記予備調製液を調製する場合や、直接水溶性
高分子物質を配合系に添加する場合は、水溶性高分子物
質がまず膨潤した後に溶解するが、いわゆる「ままこ」
を形成する場合が多く、ままこ内部への水の浸透が著し
く阻害され、膨潤、溶解時間が極端に長くなったり、場
合によっては完全な膨潤、溶解物が得られなくなるので
、次のような溶解方法がとられて(する。When preparing the above-mentioned pre-preparation liquid or directly adding a water-soluble polymeric substance to a blended system, the water-soluble polymeric substance first swells and then dissolves.
In many cases, the penetration of water into the inside of the mamako is significantly inhibited, and the swelling and dissolution time becomes extremely long, and in some cases, complete swelling and dissolution cannot be obtained. A dissolution method is used.
(a)攪拌しながら少量ずつ投入する方法。(a) Method of adding little by little while stirring.
溶解槽内に水及び必要に応じて他の配合原料を入れ、水
面付近を激しく攪拌しながら水溶性高分子物質をできる
だけ少量ずつ投入する方法。(多くの場合、目の粗いふ
るいを通しながら投入すると良い結果が得られる。)
(b)粉末原料との予備混合法。A method in which water and other mixed raw materials are placed in a dissolution tank as necessary, and the water-soluble polymer substance is added in as small a quantity as possible while vigorously stirring near the water surface. (In many cases, good results can be obtained by passing the mixture through a coarse sieve.) (b) Pre-mixing method with powdered raw materials.
水溶性高分子粒子同士の集合を防止するため、砂糖、無
機粉末原料等の他の粉末原料と併用する場合は、予めそ
れらの粉末原料とよく混合して、上記(a)の方法を用
いる。In order to prevent aggregation of water-soluble polymer particles, when using together with other powder raw materials such as sugar and inorganic powder raw materials, the powder raw materials are thoroughly mixed in advance and the above method (a) is used.
(c)有機溶剤に分散し投入する方法。(c) A method of dispersing and charging in an organic solvent.
水溶性高分子物質を溶かさない他の有機溶剤と併用する
場合において、該有機溶剤中1二分散させたうえで、攪
拌水中に投入する方法。When used in combination with another organic solvent that does not dissolve the water-soluble polymer substance, a method of dispersing the water-soluble polymer substance in the organic solvent and then adding it to stirring water.
(d)分散、膨潤、溶解の温度を変化させる方法。(d) A method of varying the temperature of dispersion, swelling, and dissolution.
水溶性高分子粒子が凝集しない(ままこを形成しない)
温度で一旦水に分散させ、その後残りの水を添加し、水
溶性高分子が溶解可能な温度とする方法。Water-soluble polymer particles do not aggregate (do not form lumps)
A method where the polymer is dispersed in water at a certain temperature, and then the remaining water is added to bring the temperature to a level where the water-soluble polymer can dissolve.
しかしながら、これらの方法は次のような問題点を有し
ている。However, these methods have the following problems.
(A) 目的とする配合物の配合水量が少1.X場合
は、水溶性高分子物質の膨潤溶解物の予備yA製液用の
水と、その他の原料を混合する木とを個別に確保できな
くなることが多いので、予め水溶性高分子物質を膨潤、
溶解させた木#液を調製した後に、その水溶液の中に残
りの配合物を添加するか、或いは配合系に上記(a)〜
(d)の方法で水溶性高分子物質を添加しなければなら
ないが、前者の場合、予備調製液は水溶性高分子物質の
水溶液に特有である粘稠で「えいし」性を示すために、
混合分散性が悪く、強力な攪拌装置で多大のエネルギー
と時間とが必要になる。しかも、この場合、目的とする
混合性、分散性を得ようとすると、過大な機械力によっ
て水溶性高分子物質の分子破壊が起り、要求される増粘
性、賦型性などが果せなくなることがある。(A) The amount of water in the target formulation is small.1. In case of ,
After preparing the dissolved wood sap, add the remaining ingredients to the aqueous solution, or add the above (a) to (a) to the formulation system.
The water-soluble polymeric substance must be added using method (d); however, in the former case, the pre-prepared liquid exhibits the viscous and "sticky" properties characteristic of aqueous solutions of water-soluble polymeric substances. ,
Mixing and dispersion properties are poor, and a large amount of energy and time is required using a powerful stirring device. Moreover, in this case, when trying to obtain the desired mixability and dispersibility, excessive mechanical force causes molecular destruction of the water-soluble polymer substance, making it impossible to achieve the required thickening and shaping properties. There is.
(B) 水溶性高分子物質の予備調製液の調製法。(B) Method for preparing a pre-prepared solution of water-soluble polymeric substance.
または水溶性高分子物質の主配合系への添加法として、
上記(a)及び(b)の方法は、比較的低濃度の低粘度
高分子水溶液を調製する場合は特に問題がないが、多く
の場合は高粘度液となるので、水溶性高分子物質の添加
後半において巻き込みが悪くなり、均質化には多大の時
間とエネルギーを必要とし、しかも均一な分散、溶解が
困難となる。Or as a method of adding water-soluble polymeric substances to the main formulation system.
Methods (a) and (b) above have no particular problems when preparing a relatively low concentration, low viscosity polymer aqueous solution, but in many cases the resulting liquid is high viscosity, so In the latter half of the addition, entrainment becomes poor, and homogenization requires a great deal of time and energy, and furthermore, uniform dispersion and dissolution become difficult.
特に(b)の方法は、粉体の量が多いと、粉体同士での
混合にも多大の労力を必要とする。In particular, method (b) requires a great deal of effort to mix the powders together if the amount of powder is large.
(C)上記(c)の方法は、比較的よい調製法であるが
、調製中は有機溶剤分散液を終始強く攪拌していないと
高分子物質が有機溶剤中に沈降するため、たえず継続的
に攪拌を加えておかなければならない、この場合、該分
散液の添加終了時゛には攪拌χが分散液と触れなくなり
、分散液に攪拌を加えることができなくなることがある
。或いは、水溶性高分子物質を該有機溶剤で洗い流しな
がら添加しなければならず、それだけの有機溶剤量が確
保できる配合組成系でなければ実施できない。(C) Method (c) above is a relatively good preparation method, but if the organic solvent dispersion is not strongly stirred throughout the preparation, the polymer substance will settle in the organic solvent, so it must be continuously stirred. In this case, when the addition of the dispersion liquid is finished, the stirring χ may no longer come into contact with the dispersion liquid, and the dispersion liquid may not be stirred. Alternatively, the water-soluble polymer substance must be added while being washed away with the organic solvent, and this cannot be carried out unless the formulation system can secure that amount of organic solvent.
さらに、これらの問題がない場合でも、予備調製液を調
製せずに有機溶剤分散液を直接配合系へ添加する場合は
、電M質、金属塩、分散物の影響を受けて、水溶性高分
子物質の目的とする性能が果せなくなることがある。特
に、多量生産で連続して製・立する場合には、有機溶剤
中の水溶性高分子物質が沈降してしまったり、或いはポ
ンプ移送が不能となることが多い。Furthermore, even if these problems do not exist, if an organic solvent dispersion is directly added to a blended system without preparing a pre-prepared solution, it may be affected by electrolytes, metal salts, and dispersions, resulting in high water solubility. The intended performance of the molecular substance may not be achieved. Particularly in the case of continuous mass production, the water-soluble polymeric substance in the organic solvent often settles or becomes impossible to pump.
(D) 上記(d)の方法で予備調製液を調製する場
合も操作が複雑であり、直接配合系へ添加する場合は、
その他の配合原料が熱による品質劣化や、変質等の影テ
が少ないものに限られる。(D) Preparing the pre-prepared liquid using the method described in (d) above also requires complicated operations, and when adding it directly to the blending system,
Other blended raw materials are limited to those that have little quality deterioration or alteration due to heat.
[発明が解決しようとする問題点j
本発明は、水溶性高分子物質を均一に膨潤、溶解させた
組成物を、「ままこ」を生じさせることなく、短時間に
少いエネルギーで調製することを、解決しようとする問
題点とするものである。[Problems to be Solved by the Invention j The present invention provides a method for preparing a composition in which a water-soluble polymer substance is uniformly swollen and dissolved, without causing "stickiness", in a short time and with less energy. This is the problem we are trying to solve.
[問題点を解決するための手段]
上記問題点を解決するため、本発明は、水溶性高分子物
質、該高分子物質が実質的に不溶の有機溶剤、及び少量
の水の混合物を攪拌して、水溶性高分子物質の微膨潤分
散液を調製する第1工程。[Means for Solving the Problems] In order to solve the above problems, the present invention includes stirring a mixture of a water-soluble polymeric substance, an organic solvent in which the polymeric substance is substantially insoluble, and a small amount of water. The first step is to prepare a slightly swollen dispersion of a water-soluble polymeric substance.
及び該水溶性高分子物質の微膨潤分散液と水及びその他
の配合物とを、先端の周速を2 tn/sec以上とし
た攪拌翼で攪拌混合して、水溶性高分子物質を膨潤5溶
解させる第2工程よりなることを特徴とするものである
。The slightly swollen dispersion of the water-soluble polymer substance, water and other compounds are stirred and mixed using a stirring blade whose tip has a circumferential speed of 2 tn/sec or more to swell the water-soluble polymer substance. This method is characterized by comprising a second step of dissolving.
さらに詳細に説明すると1本発明においては、水溶性高
分子物質を、それが不溶の有機溶剤に分散した後に1m
の水を加えるか、または水溶性高分子物質を微量の水を
含む有機溶剤に加えて攪拌することにより、微膨潤した
水溶性高分子物質の均一分散液を調製し、この微膨潤分
散液を残りの配合物に加えて攪拌混合することにより、
所望の配合物を製造する。この場合に、残りの配合物の
混合液は、必要に応じて分割して調製してもよい。To explain in more detail, 1 In the present invention, after dispersing a water-soluble polymer substance in an organic solvent in which it is insoluble,
A uniform dispersion of a slightly swollen water-soluble polymer is prepared by adding water or adding a water-soluble polymer to an organic solvent containing a small amount of water and stirring. By adding to the rest of the formulation and stirring,
Prepare the desired formulation. In this case, the remaining mixed solution of the formulation may be prepared by dividing the mixture as necessary.
上記水溶性高分子物質としては、カルポキシメチルセル
ロースナトリ7ム、メチルセルロース、ヒトロキシニチ
ルセルロース等のセルロース誘導体、アルギン酸ナトリ
ウム、カラ二一ナン等のアルカリ金属アルギネート、キ
サンタンガム、トラ力カントガム、カラヤガム、アラビ
アガム等の力′ム類、ポリビニルアルコール、ポリアク
リル酸ナトリウム、カルホキジビニルポリマ等の合成粘
結材かあり、これらの1種または2種以上を使用するこ
とができる。The above-mentioned water-soluble polymer substances include cellulose derivatives such as sodium carboxymethylcellulose, methylcellulose, and hydroxynitylcellulose, alkali metal alginates such as sodium alginate and cara dinan, xanthan gum, gum karaya, and gum arabic. There are synthetic binders such as polyvinyl alcohol, sodium polyacrylate, carboxyvinyl polymer, etc., and one or more of these can be used.
また、有機溶剤としては、メチルアルコール。Also, as an organic solvent, methyl alcohol is used.
エチルアルコール、アセトン、エチレングリコール、ポ
リエチレングリー−ル、プロピレングリコール、ポリプ
ロピレングリコール、グリセリン、油脂、脂肪酸エステ
ル、脂肪酸(常温で固体の場合は、溶解したもの)、そ
の他香料などの使用時に低粘性で水溶性高分子物質を溶
かさないものであればよく、これらの溶剤中に油溶性の
任意の添加物を加えてもよい。Ethyl alcohol, acetone, ethylene glycol, polyethylene glycol, propylene glycol, polypropylene glycol, glycerin, fats and oils, fatty acid esters, fatty acids (dissolved if solid at room temperature), and other fragrances with low viscosity when used. Any oil-soluble additive may be added to these solvents as long as they do not dissolve the polymeric substance.
水溶性高分子物質の微膨潤分散液に加えるその他の配合
物としては、安息香酸、ソルビン酸。Other compounds added to the slightly swollen dispersion of water-soluble polymeric substances include benzoic acid and sorbic acid.
P−オキシ安息香酸ブチルなどの保存剤、 2,4チア
ゾリルベンズイミダゾールのような防菌、防出剤、ニリ
ンルピン酸、ジブチルヒドロキシトルエンなどの酸化防
止剤、サリチル酸系、ベンツフェノン系などの紫外線吸
収剤、その他顔料、染料、着色剤等がある。Preservatives such as butyl P-oxybenzoate, antibacterial and antibacterial agents such as 2,4 thiazolylbenzimidazole, antioxidants such as nilinelupic acid and dibutylhydroxytoluene, and ultraviolet rays such as salicylic acid and benzphenone. There are absorbents, other pigments, dyes, colorants, etc.
さらに、添加により水溶性高分子微膨潤分散液の流動性
をそこなわせない無機、有機固形物質等も加えることが
できる。この場合、無機固形物質として酸化アルミニウ
ムゼオライトが、有機固形物質としてポリエチレン、ポ
リプロピレンの粉末、ビーズなどが挙げられる。Furthermore, inorganic or organic solid substances can also be added that do not impair the fluidity of the slightly swollen water-soluble polymer dispersion. In this case, the inorganic solid substance may be aluminum oxide zeolite, and the organic solid substance may be polyethylene or polypropylene powder, beads, or the like.
水溶性高分子物質と有機溶剤の比率は1 : 1.1〜
l:5、好ましくは1 : 1.5〜l:3とし、水溶
性高分子物質の有機溶剤分散液中に添加する水の量は、
水溶性高分子物質の5〜70%、特に8〜40%が好ま
しく、微膨潤分散液の粘度は、他の調製液との混合時に
2〜8ポイズとすることが好ましい。The ratio of water-soluble polymer substance to organic solvent is 1:1.1~
1:5, preferably 1:1.5 to 1:3, and the amount of water added to the organic solvent dispersion of the water-soluble polymer substance is:
It is preferably 5 to 70%, particularly 8 to 40%, of the water-soluble polymeric substance, and the viscosity of the slightly swollen dispersion is preferably 2 to 8 poise when mixed with other preparations.
水溶性高分子物質の微膨潤分散液と他の配合物の混合液
との攪拌混合は、微膨潤した高分子物質をできるだけ多
く水に接触させるために、攪拌翼先端の周速は少なくと
も2m/see、好ましくは3m1sec以上とするの
がよい。When stirring and mixing a slightly swollen dispersion of a water-soluble polymeric substance and a mixture of other compounds, the circumferential speed of the tip of the stirring blade is at least 2 m/min in order to bring the slightly swollen polymeric substance into contact with water as much as possible. see, preferably 3 m 1 sec or more.
また、水溶性高分子物質の微膨潤分散液調製時における
水の添加は。Also, the addition of water when preparing a slightly swollen dispersion of a water-soluble polymer substance.
(a)有機溶剤に水溶性高分子物質を分散した後、所定
量の水を添加する。(a) After dispersing a water-soluble polymer substance in an organic solvent, a predetermined amount of water is added.
(b)有機溶剤に水溶性高分子物質を分散した後。(b) After dispersing a water-soluble polymer substance in an organic solvent.
所定量の水を予め混合した有機溶剤及びまたは水を含む
物質を添加する。Adding an organic solvent and/or water-containing substance premixed with a predetermined amount of water.
(C)所定量の水を有機溶剤に添加後攪拌しているとこ
ろに、水溶性高分子物質を添加する。(C) After adding a predetermined amount of water to an organic solvent and stirring, a water-soluble polymer substance is added.
(d)上記(C)と(a)または(b)の組合わせに水
を加える。(d) Add water to the combination of (C) and (a) or (b) above.
という、(a)ないしくd)のいずれでもよい。Any one of (a) to d) may be used.
第1図は上記方法を実施する装置例の概要を示し、攪拌
容器1において、水溶性高分子物質、これが不溶の有機
溶剤、及び少量の水が攪拌され。FIG. 1 shows an outline of an example of an apparatus for carrying out the above method. In a stirring vessel 1, a water-soluble polymer substance, an organic solvent in which it is insoluble, and a small amount of water are stirred.
これと別に、攪拌容器2においてその他の配合物の混合
液が作成され、これらが定量ポンプ3.3によって一定
の比率で固液分散機4に送られ、該固液分散機4で短時
間攪拌混合して所望の配合物が製造される。また、固液
分数94で攪拌混合した配合物を、点線で示す還流路5
によって攪拌容器2に還流させ、再度水溶性高分子物質
が微膨潤した均一分散液を攪拌混合してもよい。Separately, a mixed solution of other formulations is prepared in the stirring container 2, which is sent to the solid-liquid disperser 4 at a constant ratio by a metering pump 3.3, and stirred for a short time by the solid-liquid disperser 4. Mix to produce the desired formulation. In addition, the mixture mixed with stirring at a solid-liquid fraction of 94 was added to the reflux path 5 indicated by the dotted line.
The mixture may be refluxed into the stirring vessel 2 by stirring, and the uniform dispersion in which the water-soluble polymer substance is slightly swollen may be stirred and mixed again.
さらに、目的とする水溶性高分子含有組成物が、比較的
低粘度(約50ボイズ以下)のものの場合には、攪拌容
器1で調製した微膨潤分散液を。Furthermore, if the target water-soluble polymer-containing composition has a relatively low viscosity (approximately 50 voids or less), use the slightly swollen dispersion prepared in the stirring vessel 1.
点線6で示すように直接攪拌容器2へ添加してもよい。It may also be added directly to the stirring vessel 2 as shown by the dotted line 6.
また、第2図に示すように、攪拌容器7において微膨潤
した水溶性高分子物質の均一分散液を調製し、これを定
量ポンプまたは流量調製バルブ8によってその他の物質
の混合液を作成する攪拌容器9内に直接供給し、該容器
θ内に設けたミキサlOによって所望の混合物とするこ
ともできる。Further, as shown in FIG. 2, a uniform dispersion of a slightly swollen water-soluble polymer substance is prepared in a stirring vessel 7, and this is stirred using a metering pump or a flow rate adjustment valve 8 to create a mixed liquid of other substances. It is also possible to supply the mixture directly into the container 9 and form a desired mixture using a mixer IO provided in the container θ.
本発明においては、水溶性高分子物質が不溶の有機溶剤
と少量の水によって水溶性高分子物質をtafv/潤さ
せているだけなので、微膨潤した高分子物質の予備分散
液は、水溶性高分子物質を完全に膨潤、溶解した予備水
溶液を調製する場合と比較し、予備調製液の量において
176〜1/40、また、予備液の調製開始から全組成
物配合終了時までの時間において173〜l/20にす
ることができる。しかも、前述の (a)〜(d)の溶
解方法のように、高分子物質をそのまま配合するのでは
なく、微膨潤後に他の配合物質を配合するので、電解質
等の配合物の影響を殆ど受けることがない。In the present invention, since the water-soluble polymeric substance is only tafv/wetted by the organic solvent in which the water-soluble polymeric substance is insoluble and a small amount of water, the preliminary dispersion of the slightly swollen polymeric substance is Compared to preparing a preliminary aqueous solution in which the molecular substance is completely swollen and dissolved, the amount of the preliminary solution is 176 to 1/40, and the time from the start of preparation of the preliminary solution to the end of blending the entire composition is 173%. ~l/20. Moreover, as in the above-mentioned dissolution methods (a) to (d), the polymeric substances are not blended as they are, but other blended substances are blended after slight swelling, so the influence of blended substances such as electrolytes is almost eliminated. I never receive it.
また、微膨潤した高分子物質を攪拌して瞬時に多量の水
に接触させるので、水溶性高分子物質が速やかに膨潤、
溶解するから、配合物によっては均質化操作を省略する
ことが可能なばかりでなく、配合系全体の連続製造も可
能にすることができる。In addition, since the slightly swollen polymer material is stirred and instantly brought into contact with a large amount of water, the water-soluble polymer material quickly swells.
Since it dissolves, it is not only possible to omit a homogenization operation depending on the formulation, but also to enable continuous production of the entire formulation system.
[実施例コ
〈実施例1〉液体クレンザ−の調製
組 成
炭酸カルシウム 50,0%エチレ
ングリコール 2.0ヤシ脂肪酸ジエタ
ールアミド 2.0クエン酸・3ナトリウム・
2水塩 1.3クエン酸・1水塩(30%水溶液)
0.45香 $40.2
安息香酸ナトリウム(20%水溶液)1.5水
残部
上記組成よりなる液体クレンザ−の調製にあたり、まず
、エチレングリコールにクレンザ−全体の0,25%の
水(カルボキシメチルセルロースに対して2596 )
を予め添加し、攪拌しながらCMCを添加分散し、CM
Cが微膨潤した均一分散液を調製した。[Example 1] Preparation composition of liquid cleanser Calcium carbonate 50.0% ethylene glycol 2.0 Coconut fatty acid diethalamide 2.0 Citric acid, trisodium,
Dihydrate 1.3 Citric acid monohydrate (30% aqueous solution)
0.45 fragrance $40.2 Sodium benzoate (20% aqueous solution) 1.5 water
To prepare a liquid cleanser with the remainder having the above composition, first add 0.25% water (2596 to carboxymethyl cellulose) to ethylene glycol based on the entire cleanser.
is added in advance, CMC is added and dispersed while stirring, and CM
A homogeneous dispersion in which C was slightly swollen was prepared.
別に、残りの水に、できるだけ発泡を抑えた攪拌を行な
いながら、順次クエン酸・3ナトリウムφ2水塩、ヤシ
脂肪酸ジェタノールアミド溶解物、クエン酸水溶液、炭
酸カルシウム、アルキルベンゼンスルホン酸ナトリウム
スラリー、香料、安息香酸ナトリウム水容液を添加して
、研磨剤スラリーを:JJ製した。Separately, add citric acid trisodium φ2 hydrate, coconut fatty acid jetanolamide solution, citric acid aqueous solution, calcium carbonate, sodium alkylbenzenesulfonate slurry, fragrance, An abrasive slurry was prepared by adding an aqueous sodium benzoate solution.
次に、上記CMCの微膨潤分散液と研磨剤スラリーを、
それぞれ定量ポンプによって、所定の比率で固液連続分
散#!(特殊機化工業型、パイプラインホモミキサ)に
処理速度500kg/hr テ供N。Next, the slightly swollen dispersion of CMC and the abrasive slurry were added,
Continuous solid-liquid dispersion at a predetermined ratio by each metering pump #! (Special mechanical industrial type, pipeline homomixer) with a processing speed of 500 kg/hr.
し、該連続分散機の攪拌先端翼周速を5 m/seeで
攪拌し、このスラリーを製品移送ポンプで製品槽に送っ
た。Then, the slurry was stirred at a circumferential speed of the stirring tip blade of the continuous disperser of 5 m/see, and the slurry was sent to the product tank by a product transfer pump.
製品槽から取出したスラリーは、炭酸カルシウムが均一
に分散した安定な液体クレンザ−であった。The slurry taken out from the product tank was a stable liquid cleanser in which calcium carbonate was uniformly dispersed.
(比較例1)
上記と同方法で、固液連続分散機の攪拌先端翼周速を
0.5m/secにして攪拌したところ、得られた液体
クレンザ−は、炭酸カルシウムが凝集したざらつきのあ
るものであった。(Comparative Example 1) Using the same method as above, the circumferential speed of the stirring tip blade of the solid-liquid continuous disperser was
When stirred at 0.5 m/sec, the resulting liquid cleanser had a rough texture due to agglomeration of calcium carbonate.
(比較例2)
炭酸カルシウムを水に分散したスラリーを調製する場合
は、炭酸カルシウムDMで65%以下でなければ、流動
型のあるスラリーを調製することができない。(Comparative Example 2) When preparing a slurry in which calcium carbonate is dispersed in water, a fluid type slurry cannot be prepared unless the calcium carbonate DM is 65% or less.
上記実施例の場合、炭酸カルシウムスラリー調製用にク
レンザ−全体の27%の水を必要とし、したがって、C
MCの予備rA製に使用可能な水の量は9.55%であ
った。In the case of the above example, 27% of the water of the total cleanser is required for preparing the calcium carbonate slurry, and therefore the C
The amount of water available for pre-rA production of MC was 9.55%.
この水を使って、CMCの予備水溶液電調製しようと試
みたが、非常に粘稠なものとなり、調製することができ
なかった。An attempt was made to prepare a preliminary aqueous solution of CMC using this water, but the solution became extremely viscous and could not be prepared.
(比較例3)
CMCのエチレングリコールへの分散液を、微膨潤を行
わずに定量ポンプで移送を行ったところ、CMCが沈降
、ブロッキングして移送ができなかったので、研磨剤ス
ラリーに攪拌しながら上面より添加したところ、目的と
する液体クレンザ−の粘度が得られなかった。(Comparative Example 3) When a dispersion of CMC in ethylene glycol was transferred using a metering pump without slight swelling, the CMC sedimented and blocked, making transfer impossible. However, when it was added from the top, the desired viscosity of the liquid cleanser could not be obtained.
(比較例4)
液体クレンザ−全配合量の水の中に、CMCのエチレン
グリコール分散液を全量添加してCMCを膨潤、溶解さ
せたところ、室温で約10ポイズであった。(Comparative Example 4) Liquid Cleanser - When the entire amount of the ethylene glycol dispersion of CMC was added to the total amount of water to swell and dissolve CMC, it was about 10 poise at room temperature.
このものは、プリプリとした弾性を帯びた掖であり、ワ
イゼンベルグ効果によって液が撹拌棒をったってはい上
がってくるものであった。したがって、この中へ炭酸カ
ルシウム以下の原料を配合するのは、極めて困難なもの
であった。This was a jiggly, elastic bowl, and the Weisenberg effect caused the liquid to crawl up the stirring rod. Therefore, it has been extremely difficult to blend raw materials lower than calcium carbonate into this.
〈実施例2〉屋内壁塗装用塗料(水性塗$4)組
成
酸化チタン 25.0%カラギーナ
ン 1.5エタノール(工業用)2.
0
塩化ヘンザルコニウム 0.1水
残部
lq全全体 1.8%のエタノールに、TEZを!加攪
拌してTBZの溶解を確認後、水を塗料全体の0.24
%(カラギーナンに対して16%)加え、J!l!拌し
ながらカラギーナンを加えた。さらに、残りのエタノー
ルに塗料全体の0.06%の水を予め混合溶解したもの
を、攪拌しながら添加した。<Example 2> Indoor wall paint (water-based paint $4) set
Synthetic titanium oxide 25.0% carrageenan 1.5 Ethanol (industrial) 2.
0 Henzalkonium chloride 0.1 Water
Add TEZ to the remaining lq total 1.8% ethanol! After stirring and confirming the dissolution of TBZ, add water to 0.24% of the entire paint.
% (16% relative to carrageenan) plus J! l! Carrageenan was added while stirring. Furthermore, a premixed solution of 0.06% of the total paint water in the remaining ethanol was added with stirring.
このものは、カラギーナンが微膨潤した均一な分散液で
あった。This was a uniform dispersion in which carrageenan was slightly swollen.
第1図に示す装置を用いて、残りの水を攪拌しながら塩
化ベンザルコニウム、酸化チタンを加え、顔料スラリー
を調製した。Using the apparatus shown in FIG. 1, benzalkonium chloride and titanium oxide were added to the remaining water while stirring to prepare a pigment slurry.
次に、この顔料スラリーを固液分散機を通してリサイク
ルしているところに、上記力ラーキーナン微膨濶物分散
液を実施例1と同゛じ固液分散機に供給し、瞬時に分散
させた。このときのリサイクル量は600kg/hrで
、固液分散機4の攪拌先端翼周速は4 m/secであ
り、攪拌容器2の攪拌先端翼周速は1 m1secであ
った・
得られたスラリーは、酸化チタンが均一に分散した安定
な水性塗料であった。Next, while this pigment slurry was being recycled through a solid-liquid dispersion machine, the above-mentioned Larkinan slightly expanded pellet dispersion was supplied to the same solid-liquid dispersion machine as in Example 1 and instantly dispersed. The recycling amount at this time was 600 kg/hr, the circumferential speed of the stirring tip blade of the solid-liquid disperser 4 was 4 m/sec, and the circumferential speed of the stirring tip blade of the stirring container 2 was 1 m1sec. was a stable water-based paint in which titanium oxide was uniformly dispersed.
(比較例1)
上記と同じ方法で、固液分散機4の攪拌先端翼周速を
0.5国/sacにして調製してみたところ、得られた
スラリーは、酸化チタンが凝集したざらつきのあるもの
であった。(Comparative Example 1) Using the same method as above, change the circumferential speed of the stirring tip blade of solid-liquid disperser 4.
When prepared at a rate of 0.5 mm/sac, the resulting slurry had a rough texture due to agglomeration of titanium oxide.
〈実施例3〉アイスクリームミックスの調製法(凍結す
る前のアイスクリームの混合物)組 成
牛 乳
37.1%/ヘクー(水分15%)0.5
クリーム(40%) 18.0脱脂粉
乳 6.1砂 糖
14.5アルギン
酸ナトリウム 03脂肪酸モノグリセリド
0.2水 残部
第2図に示す攪拌容器7の周囲に加温手段を。<Example 3> Method for preparing ice cream mix (ice cream mixture before freezing) Composition Cow Milk
37.1%/Heku (moisture 15%) 0.5 Cream (40%) 18.0 Skim milk powder 6.1 Sugar
14.5 Sodium alginate 03 Fatty acid monoglyceride
0.2 Water Remainder Place heating means around the stirring vessel 7 shown in Figure 2.
攪拌容器9の周囲に、加温、冷却手段を設けた装置にお
いて、!拌容器9に水、牛乳、クリーム。In an apparatus in which heating and cooling means are provided around the stirring vessel 9,! Add water, milk, and cream to mixing container 9.
砂糖、粉乳、乳化剤の順に攪拌(イカリ型攪拌のみ)し
ながら添加する。よく攪拌しながら70°Cに20分間
加温した後40°Cに冷却する。別に1攪拌容器7でパ
ターを溶かしながら攪拌しているところへアルギン酸ナ
トリウムを添加し、最終温度が40〜50°Cのアルギ
ン酸ナトリウムの微膨潤分散液を:A製しておく。Add sugar, powdered milk, and emulsifier in this order while stirring (only using a quick stirring method). Heat to 70°C for 20 minutes while stirring well, then cool to 40°C. Separately, sodium alginate is added to the stirred container 7 while the putter is melted and stirred to prepare a slightly swollen dispersion of sodium alginate having a final temperature of 40 to 50°C.
この微膨潤分散液を、イカリ型攪拌及びホモミキサー攪
拌を同時に行っている上記液中のホモミキサー10の攪
拌χ近傍に添加し、イカリ型攪拌スの周速を2m1se
c、ホモミキサーの周速を6Ill/SeCとして5分
間よく攪拌した。This slightly swollen dispersion liquid was added to the vicinity of the stirring χ of the homomixer 10 in the above-mentioned liquid, which was simultaneously performing the Ikari type stirring and homomixer stirring, and the peripheral speed of the Ikari type stirring station was set to 2 m1se.
c. The homomixer was stirred well for 5 minutes at a circumferential speed of 6 Ill/SeC.
得られたアイスクリームミックスは、粘度が出て著しく
良好なものであった。The resulting ice cream mix had a very good viscosity.
(比較例1)
アルギン酸ナトリウムを砂糖とよく混合して、粉体にて
攪拌容器s内に添加する方法を行ったが、上記と同じ均
一で粘稠な液を得るのに、6倍の30分かかった。(Comparative Example 1) Sodium alginate was thoroughly mixed with sugar and added as a powder into a stirring container s, but in order to obtain the same uniform and viscous liquid as above, it took 30 I understand.
<1m例4>エモリエントローション(柔軟乳液または
栄養乳液、O/W非イオン乳化型)組 成
油性成分
スラリラン 5.0%ワセリン
2.0ミツロウ
0.5香 料
0.5パラオキシ
安、9.香酸ブチル 0.01プロブレンゲ
リコール 5.0エタノール
5,0水酸化カリウム(10%水溶液
)1.0精 製 木 残部実施
例3と同様の装置において、予め攪拌容器7にて油性成
分を混合加熱して70°Cとする。また、これとは別に
、ローション全体の0.6%のプコピレンゲリコールに
パラオキシ安忘香醇ブチルを添加し、攪拌下においてロ
ーション全体の0.1%の精製水、カルボキシメチルセ
ルロースナトリウムを順次添加し、カルボキシメチルセ
ルロースナトリウムの微膨潤分散液を調製しておく。攪
拌容器9に、残りの精製水、プロピレングリコールを加
えて加熱混合し、さらに、エタノールを加えた後70
’Cとする。これに予め70”Cに混合加熱しておいた
油性成分を加えて予備乳化を行った。この時のホモミキ
サー10の周速は7ffi/SeCテアった。<1m Example 4> Emollient lotion (softening emulsion or nutritional emulsion, O/W non-ionic emulsion type) Composition Oil-based component Sluriran 5.0% Vaseline 2.0 Beeswax
0.5 fragrance
0.5 paraoxyamin, 9. Butyl fragrant 0.01 Problen gelicol 5.0 Ethanol
5.0 Potassium hydroxide (10% aqueous solution) 1.0 Purified wood Remainder In the same apparatus as in Example 3, the oily components were mixed and heated in advance in the stirring vessel 7 to 70°C. Separately, paraoxyammobutyl was added to 0.6% of the entire lotion of pucopylene gellicol, and while stirring, 0.1% of the entire lotion of purified water and sodium carboxymethyl cellulose were sequentially added. , a slightly swollen dispersion of sodium carboxymethyl cellulose is prepared in advance. Add the remaining purified water and propylene glycol to the stirring container 9, heat mix, and then add ethanol.
'C. To this was added an oily component that had been mixed and heated to 70''C in advance for preliminary emulsification. At this time, the peripheral speed of the homomixer 10 was 7ffi/SeC tare.
この予備乳化物にカルボキシメチルセルロースナトリウ
ムの微膨潤分散液を攪拌容器7より油性成分と同様に添
加し、均一に混和した後、さらに、撹拌容器7より水酸
化カリウム水溶液を加えて中和し、ホモミキサーにより
均一に乳化した後ホモミキサーを停止し、イカリ型攪拌
ズをゆっくり回転させながら攪拌容器9を冷却し、30
°Cまで冷却してローションを調製した。A slightly swollen dispersion of sodium carboxymethylcellulose was added to this pre-emulsion from the stirring vessel 7 in the same manner as the oily component, and after uniformly mixing, an aqueous potassium hydroxide solution was further added from the stirring vessel 7 to neutralize and homogenize. After uniformly emulsifying with the mixer, the homomixer was stopped, and the stirring container 9 was cooled while slowly rotating the Ikari type stirring bowl.
The lotion was prepared by cooling to °C.
(比較例1)
実施例4と同様に、均一安定なローションを得るのに、
カルボキシメチルセルロースナトリウムの水溶液を調製
したところ、1%水溶液まで希釈する必要があり、体積
比で20倍以上、また、水溶液調製には5倍以上の時間
を要した。(Comparative Example 1) Similar to Example 4, to obtain a uniform and stable lotion,
When an aqueous solution of carboxymethyl cellulose sodium was prepared, it was necessary to dilute it to a 1% aqueous solution, which required more than 20 times the volume ratio, and more than 5 times as much time to prepare the aqueous solution.
(実施例5〉ソフトフェライト(磁気へットコア)製造
におけるスラリーの調製性
近年、機能性セラミックスとして、磁気ヘッドコア等の
精密形状部品の成形に際して、スプレードライヤによる
造粒粉(!D粒)を使用する方法が用いられるようにな
った。同法によって得られた顆粒は流動性にすぐれ、成
形時の金型への充填が安定であり、また密度の高い成形
体が得られ易いからである。(Example 5) Preparation of slurry in the production of soft ferrite (magnetic head core) In recent years, granulated powder (!D grains) using a spray dryer has been used in the molding of precision-shaped parts such as magnetic head cores as functional ceramics. This method has come to be used because the granules obtained by this method have excellent fluidity, can be stably filled into a mold during molding, and can easily produce a molded product with high density.
ここでは、造粒前のスラリー調製法について述へる。な
お、下記組成物中、ポリビニルアルコールCPVA)
r士球形粒子を安定なものにするための粘着性と、成形
体の強度保持のためであり、グリセリンは、レオロジー
性の付与と可塑性、柔軟性を与えるためであり、 PV
Aの固化をふせぎ、軟かい!σ粒を造るために添加した
。Here, the slurry preparation method before granulation will be described. In addition, in the following composition, polyvinyl alcohol CPVA)
Glycerin is used to provide adhesiveness to make the spherical particles stable and to maintain the strength of the molded product, and glycerin is used to provide rheology, plasticity, and flexibility.PV
Prevents solidification of A and makes it soft! Added to create σ grains.
スラリー組成
ポリビニルアルコール 1.0グリセリ
ン 2.0精製水
1.0実施例3と同様の装置において
、予め攪拌容器7にてグリセリンに精製水を添加し、攪
拌下においてポリビニルアルコールを添加し、ポリビニ
ルアルコールの微膨潤分散液を調製しておく。Slurry composition Polyvinyl alcohol 1.0 Glycerin 2.0 Purified water
1.0 In the same apparatus as in Example 3, purified water is added to glycerin in advance in a stirring vessel 7, and polyvinyl alcohol is added under stirring to prepare a slightly swollen dispersion of polyvinyl alcohol.
攪拌容器8にフェライトスラリーを入れ、約60〜65
°Cに加熱する。この時イカリ型攪拌買のみの攪拌で、
周速はlIl/SeCである。上記温度に達してから、
ホモミキサー10も周速6 ffl/seaで攪拌を開
始し、その攪拌翼近傍にポリビニルアルコールの微膨潤
分散液を添加し、約5分間よく攪拌した。Put the ferrite slurry into the stirring container 8 and make it about 60-65
Heat to °C. At this time, by stirring only with the Ikari type stirring purchase,
The circumferential speed is lIl/SeC. After reaching the above temperature,
The homomixer 10 also started stirring at a circumferential speed of 6 ffl/sea, and the slightly swollen dispersion of polyvinyl alcohol was added to the vicinity of the stirring blade, followed by thorough stirring for about 5 minutes.
このスラリーは、ポリビニルアルコールが完全に膨潤、
溶解し、フェライトが均一に分散したものであった。This slurry is completely swollen with polyvinyl alcohol.
It was dissolved and the ferrite was uniformly dispersed.
このものに若干の消泡剤を添加した後、スプレードライ
ヤにより顆粒を造り、ステアリン酸亜鉛を適当量加えて
、プレス(焼結)成形して、高密度で寸法安定性の良い
セラミックスを得た。After adding some antifoaming agent to this material, granules were made using a spray dryer, an appropriate amount of zinc stearate was added, and press (sintering) molding was performed to obtain ceramics with high density and good dimensional stability. .
(比較例1)
ポリビニルアルコールの一般的添加方法として、10%
水溶液を調製し、フェライトスラリーに添加する方法を
行ったが、スラリー濃度が下がり、スプレードライヤに
より目的とする嵩密度の顆粒が得られなかった。(Comparative Example 1) As a general method of adding polyvinyl alcohol, 10%
An aqueous solution was prepared and added to the ferrite slurry, but the slurry concentration decreased and granules with the desired bulk density could not be obtained using a spray dryer.
なお、窯業において、同実施例と同様な目的で水溶性高
分子物質を添加するが、原料スラリーそのものが既に3
0%の水分を含み、成形品の密度及び乾燥費用の面から
、いかに水分を増さずに水溶性高分子物質を配合するか
が問われている。したがって、同業において、本発明の
製造方法はそれに十分答えるものである。In addition, in the ceramic industry, a water-soluble polymer substance is added for the same purpose as in the same example, but the raw material slurry itself is already
It contains 0% water, and from the viewpoint of the density of the molded product and the cost of drying, the question is how to incorporate water-soluble polymer substances without increasing the water content. Therefore, in the same industry, the manufacturing method of the present invention satisfies this need.
[発明の効果]
本発明によれば、水溶性高分子物質を、それが不溶の有
機溶剤と少量の水とによって微W潤させるので、水溶性
高分子物質の微膨潤分散液が少量かつ短時間で調製でき
るばかりでなく、該分散液を先端の周速が2 mlse
c以上の攪拌翼で攪拌して短時間に多量の水に接触させ
ることによって、水溶性高分子物質が速やかに膨潤、溶
解するので。[Effects of the Invention] According to the present invention, a water-soluble polymer substance is slightly wetted with an organic solvent in which it is insoluble and a small amount of water, so that a slightly swollen dispersion of a water-soluble polymer substance is formed in a small amount and in a short period of time. Not only can the dispersion be prepared in an hour, but the dispersion can be prepared at a peripheral speed of 2 mlse at the tip.
By stirring with a stirring blade of c or more and bringing it into contact with a large amount of water in a short period of time, the water-soluble polymer substance quickly swells and dissolves.
水溶性高分子物質を含有する組成物を、短時間でかつ少
いエネルギーで製造することができる。Compositions containing water-soluble polymeric substances can be produced in a short time and with less energy.
第1図及び第2図は1本発明の実施に使用する装置の概
略説明図である。
1.2,7.9 ・・攪拌容器、
4 拳・・固液分散機。FIGS. 1 and 2 are schematic explanatory diagrams of an apparatus used to carry out the present invention. 1.2,7.9 Stirring vessel, 4 fists...Solid-liquid dispersion machine.
Claims (1)
有機溶剤、及び少量の水の混合物を攪拌して、水溶性高
分子物質の微膨潤分散液を調製する第1工程、 該水溶性高分子物質の微膨潤分散液と水及びその他の配
合物とを、先端の周速を2m/sec以上とした攪拌翼
で攪拌混合して、水溶性高分子物質を膨潤、溶解させる
第2工程、 よりなることを特徴とする水溶性高分子物質含有組成物
の製造方法。[Claims] 1. A slightly swollen dispersion of a water-soluble polymer is prepared by stirring a mixture of a water-soluble polymer, an organic solvent in which the polymer is substantially insoluble, and a small amount of water. The first step is to stir and mix the slightly swollen dispersion of the water-soluble polymer substance with water and other compounds using a stirring blade whose tip has a circumferential speed of 2 m/sec or more to form the water-soluble polymer substance. A method for producing a water-soluble polymer substance-containing composition, comprising: a second step of swelling and dissolving the water-soluble polymer substance.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4798487A JPH07122025B2 (en) | 1987-03-03 | 1987-03-03 | Method for producing composition containing water-soluble polymer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4798487A JPH07122025B2 (en) | 1987-03-03 | 1987-03-03 | Method for producing composition containing water-soluble polymer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63215773A true JPS63215773A (en) | 1988-09-08 |
JPH07122025B2 JPH07122025B2 (en) | 1995-12-25 |
Family
ID=12790579
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4798487A Expired - Fee Related JPH07122025B2 (en) | 1987-03-03 | 1987-03-03 | Method for producing composition containing water-soluble polymer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07122025B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006232926A (en) * | 2005-02-23 | 2006-09-07 | Konishi Co Ltd | Vinyl acetate resin emulsion and method for producing the same |
JP2006232927A (en) * | 2005-02-23 | 2006-09-07 | Konishi Co Ltd | Vinyl acetate resin emulsion and method for producing the same |
-
1987
- 1987-03-03 JP JP4798487A patent/JPH07122025B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006232926A (en) * | 2005-02-23 | 2006-09-07 | Konishi Co Ltd | Vinyl acetate resin emulsion and method for producing the same |
JP2006232927A (en) * | 2005-02-23 | 2006-09-07 | Konishi Co Ltd | Vinyl acetate resin emulsion and method for producing the same |
Also Published As
Publication number | Publication date |
---|---|
JPH07122025B2 (en) | 1995-12-25 |
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