JP2731545B2 - Method for purifying hyaluronic acid - Google Patents
Method for purifying hyaluronic acidInfo
- Publication number
- JP2731545B2 JP2731545B2 JP25498688A JP25498688A JP2731545B2 JP 2731545 B2 JP2731545 B2 JP 2731545B2 JP 25498688 A JP25498688 A JP 25498688A JP 25498688 A JP25498688 A JP 25498688A JP 2731545 B2 JP2731545 B2 JP 2731545B2
- Authority
- JP
- Japan
- Prior art keywords
- hyaluronic acid
- alumina
- silica gel
- solution
- containing liquid
- 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.)
- Expired - Lifetime
Links
- KIUKXJAPPMFGSW-DNGZLQJQSA-N (2S,3S,4S,5R,6R)-6-[(2S,3R,4R,5S,6R)-3-Acetamido-2-[(2S,3S,4R,5R,6R)-6-[(2R,3R,4R,5S,6R)-3-acetamido-2,5-dihydroxy-6-(hydroxymethyl)oxan-4-yl]oxy-2-carboxy-4,5-dihydroxyoxan-3-yl]oxy-5-hydroxy-6-(hydroxymethyl)oxan-4-yl]oxy-3,4,5-trihydroxyoxane-2-carboxylic acid Chemical compound CC(=O)N[C@H]1[C@H](O)O[C@H](CO)[C@@H](O)[C@@H]1O[C@H]1[C@H](O)[C@@H](O)[C@H](O[C@H]2[C@@H]([C@@H](O[C@H]3[C@@H]([C@@H](O)[C@H](O)[C@H](O3)C(O)=O)O)[C@H](O)[C@@H](CO)O2)NC(C)=O)[C@@H](C(O)=O)O1 KIUKXJAPPMFGSW-DNGZLQJQSA-N 0.000 title claims description 73
- 229920002674 hyaluronan Polymers 0.000 title claims description 73
- 229960003160 hyaluronic acid Drugs 0.000 title claims description 73
- 238000000034 method Methods 0.000 title claims description 35
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 25
- 239000007788 liquid Substances 0.000 claims description 25
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 23
- 229910002027 silica gel Inorganic materials 0.000 claims description 22
- 239000000741 silica gel Substances 0.000 claims description 22
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 25
- 239000000243 solution Substances 0.000 description 20
- 239000012535 impurity Substances 0.000 description 19
- 238000011282 treatment Methods 0.000 description 18
- 229910052751 metal Inorganic materials 0.000 description 13
- 239000002184 metal Substances 0.000 description 13
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 10
- 229920002385 Sodium hyaluronate Polymers 0.000 description 8
- 238000000855 fermentation Methods 0.000 description 8
- 230000004151 fermentation Effects 0.000 description 8
- 229940010747 sodium hyaluronate Drugs 0.000 description 8
- YWIVKILSMZOHHF-QJZPQSOGSA-N sodium;(2s,3s,4s,5r,6r)-6-[(2s,3r,4r,5s,6r)-3-acetamido-2-[(2s,3s,4r,5r,6r)-6-[(2r,3r,4r,5s,6r)-3-acetamido-2,5-dihydroxy-6-(hydroxymethyl)oxan-4-yl]oxy-2-carboxy-4,5-dihydroxyoxan-3-yl]oxy-5-hydroxy-6-(hydroxymethyl)oxan-4-yl]oxy-3,4,5-trihydroxyoxane-2- Chemical compound [Na+].CC(=O)N[C@H]1[C@H](O)O[C@H](CO)[C@@H](O)[C@@H]1O[C@H]1[C@H](O)[C@@H](O)[C@H](O[C@H]2[C@@H]([C@@H](O[C@H]3[C@@H]([C@@H](O)[C@H](O)[C@H](O3)C(O)=O)O)[C@H](O)[C@@H](CO)O2)NC(C)=O)[C@@H](C(O)=O)O1 YWIVKILSMZOHHF-QJZPQSOGSA-N 0.000 description 8
- 238000004458 analytical method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- 239000002245 particle Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 239000011780 sodium chloride Substances 0.000 description 6
- 102000039446 nucleic acids Human genes 0.000 description 5
- 108020004707 nucleic acids Proteins 0.000 description 5
- 150000007523 nucleic acids Chemical class 0.000 description 5
- 239000003960 organic solvent Substances 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- 241000194017 Streptococcus Species 0.000 description 4
- 239000012533 medium component Substances 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 102000004169 proteins and genes Human genes 0.000 description 4
- 108090000623 proteins and genes Proteins 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000001471 micro-filtration Methods 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 229960001927 cetylpyridinium chloride Drugs 0.000 description 2
- YMKDRGPMQRFJGP-UHFFFAOYSA-M cetylpyridinium chloride Chemical compound [Cl-].CCCCCCCCCCCCCCCC[N+]1=CC=CC=C1 YMKDRGPMQRFJGP-UHFFFAOYSA-M 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000012510 hollow fiber Substances 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002510 pyrogen Substances 0.000 description 2
- 230000001698 pyrogenic effect Effects 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 2
- 229910001948 sodium oxide Inorganic materials 0.000 description 2
- FKHIFSZMMVMEQY-UHFFFAOYSA-N talc Chemical compound [Mg+2].[O-][Si]([O-])=O FKHIFSZMMVMEQY-UHFFFAOYSA-N 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- SQDAZGGFXASXDW-UHFFFAOYSA-N 5-bromo-2-(trifluoromethoxy)pyridine Chemical compound FC(F)(F)OC1=CC=C(Br)C=N1 SQDAZGGFXASXDW-UHFFFAOYSA-N 0.000 description 1
- 229920001287 Chondroitin sulfate Polymers 0.000 description 1
- 241000287828 Gallus gallus Species 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 108010003272 Hyaluronate lyase Proteins 0.000 description 1
- 102000001974 Hyaluronidases Human genes 0.000 description 1
- 239000004909 Moisturizer Substances 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- 241000194022 Streptococcus sp. Species 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 229940041514 candida albicans extract Drugs 0.000 description 1
- 229940059329 chondroitin sulfate Drugs 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 238000004737 colorimetric analysis Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229960002773 hyaluronidase Drugs 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 235000013490 limbo Nutrition 0.000 description 1
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 1
- 239000000391 magnesium silicate Substances 0.000 description 1
- 229910052919 magnesium silicate Inorganic materials 0.000 description 1
- 235000019792 magnesium silicate Nutrition 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 229940126601 medicinal product Drugs 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001333 moisturizer Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000000399 orthopedic effect Effects 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- -1 polypeptone Substances 0.000 description 1
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 238000001356 surgical procedure Methods 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000012138 yeast extract Substances 0.000 description 1
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ヒアルロン酸含有液からヒアルロン酸を精
製する方法に関する。ヒアルロン酸は化粧品の保湿剤の
他、眼科、整形外科、皮膚科等で医薬品としての用途が
開かれてきている。Description: TECHNICAL FIELD The present invention relates to a method for purifying hyaluronic acid from a hyaluronic acid-containing solution. Hyaluronic acid has been used as a pharmaceutical in ophthalmology, orthopedic surgery, dermatology, etc. in addition to cosmetic moisturizers.
従来、ヒアルロン酸は、動物組織、例えば、工業規模
では、ニワトリのトサカ等からの抽出法により製造され
ているが、夾雑物としてコンドロイチン硫酸が混入した
り、組織内に含まれるヒアルロニダーゼなどによつて低
分子量化されやすい、従つて高分子で高純度に精製され
たものは、コスト高になる。Conventionally, hyaluronic acid has been produced by extraction from animal tissues, for example, chicken limbo, etc. on an industrial scale.However, as a contaminant, chondroitin sulfate is mixed in, or hyaluronidase contained in the tissue is used. Those which are easily reduced in molecular weight and therefore purified with high purity by using a polymer have a high cost.
これら問題点を解決するため、近年醗酵法によりヒア
ルロン酸を製造することが行なわれている。ヒアルロン
酸がストレプトコツカス属のある群のバクテリアにより
生産されることは、古くから知られ、多くの報告がある
(ジエービー、ウールコツク(J.B.Woolcock)、ジヤー
ナル・オブ・ジエネラルマイクロバイオロジイ85 372−
375 1976)。In order to solve these problems, production of hyaluronic acid by a fermentation method has recently been performed. It has been known for a long time that hyaluronic acid is produced by a group of bacteria belonging to the genus Streptococcus, and there have been many reports (JBWoolcock, Journal of General Microbiology 85 372-).
375 1976).
醗酵法によつて製造されるヒアルロン酸は、抽出法に
比べ、一定の原料で、一定の方法で製造されるため、製
品の品質が一定に保たれることから、産業上の利用価値
は大きい。Hyaluronic acid produced by the fermentation method is produced with a constant raw material and a constant method as compared with the extraction method, and therefore, the quality of the product is kept constant, so that the industrial utility value is large. .
しかしながら、醗酵液には、高分子化合物が不純物と
して存在し、それらを分離除去して高純度の製品を得る
方法が検討されてきた。However, a method for obtaining a high-purity product by separating and removing high-molecular compounds as impurities in a fermentation solution has been studied.
例えば、塩化セチルピリジニウム等の第4級アンモニ
ウム塩とヒアルロン酸とのアダクトを形成させ不純物を
分離し、さらにフロリジルのようなケイ酸マグネシウム
のカラムに不純物を吸着させる方法(公表特許昭62−50
1471号公報)がある。For example, a method of forming an adduct of a quaternary ammonium salt such as cetylpyridinium chloride and hyaluronic acid to separate impurities and further adsorbing the impurities to a column of magnesium silicate such as florisil (Japanese Patent Publication No. 62-50)
No. 1471).
また、マクロレテイキユラー型アニオン交換樹脂を用
いて、醗酵液から発熱性物質、蛋白質等を除去するヒア
ルロン酸の精製法が開示されている(特開昭63−12293
号公報)。Also disclosed is a method for purifying hyaluronic acid by using a macroreticular type anion exchange resin to remove pyrogens, proteins, and the like from the fermentation broth (JP-A-63-12293).
No.).
本発明者らも、ヒアルロン酸を高純度に精製する方法
について検討し、ヒアルロン酸含有液をアルミナに接触
させる方法について提案した(特願昭63−144728号)。The present inventors have also studied a method of purifying hyaluronic acid with high purity, and have proposed a method of bringing a hyaluronic acid-containing solution into contact with alumina (Japanese Patent Application No. 63-144728).
ヒアルロン酸を医薬品として用いるには発熱性物質、
蛋白質、核酸、金属不純物等の少ない高純度のヒアルロ
ン酸を製造しなければならない。In order to use hyaluronic acid as a medicinal product, pyrogenic substances,
It is necessary to produce high-purity hyaluronic acid with few proteins, nucleic acids, metal impurities and the like.
しかしながら、上にあげた方法では、発熱性物質、蛋
白質、核酸等はある程度除去効果を有すが、金属不純物
の除去は、不充分である。即ち、精製不充分なヒアルロ
ン酸中には、マグネシウム、カルシウム、ケイ素、鉄の
ような金属不純物が検出され、従来の方法では、これら
の除去効果が少ない。However, in the above-mentioned methods, pyrogenic substances, proteins, nucleic acids, and the like have an effect of removing to some extent, but the removal of metal impurities is insufficient. That is, metal impurities such as magnesium, calcium, silicon, and iron are detected in incompletely purified hyaluronic acid, and the conventional method has little effect of removing these impurities.
ヒアルロン酸含有液をアルミナに接触させる方法で
は、これらの金属不純物の除去効果も大きいが、アルミ
ナ由来のアルミニウムが混入する可能性がある。In the method in which the hyaluronic acid-containing liquid is brought into contact with alumina, the effect of removing these metal impurities is large, but aluminum derived from alumina may be mixed.
従つて医薬品としても使用できる金属不純物の少な
い、高品質の製品を得る方法の開発が待たれていた。Therefore, development of a method for obtaining a high-quality product with a small amount of metal impurities that can be used as a pharmaceutical has been awaited.
本発明は、簡便かつ高品質にヒアルロン酸を精製する
方法を提供することを目的とする。An object of the present invention is to provide a simple and high-quality method for purifying hyaluronic acid.
本発明は、金属不純物を含まない高純度のヒアルロン
酸を精製する方法について種々検討した結果、ヒアルロ
ン酸含有液をシリカゲルに接触させることにより、ヒア
ルロン酸に含まれる鉄、アルミニウム等の金属不純物が
吸着除去されること見出し、本発明を完成するに到つ
た。The present invention has conducted various studies on a method for purifying high-purity hyaluronic acid containing no metal impurities.As a result of contacting the hyaluronic acid-containing solution with silica gel, metal impurities such as iron and aluminum contained in hyaluronic acid are adsorbed. It has been found that the present invention has been removed, and the present invention has been completed.
また、ヒアルロン酸含有液をあらかじめアルミナと接
触させたのち、シリカゲルと接触させることにより、発
熱性物質、蛋白質、核酸、金属不純物等を含まない高純
度のヒアルロン酸に精製できることが明らかになつた。In addition, it has been clarified that by contacting a hyaluronic acid-containing solution with alumina beforehand and then with silica gel, high-purity hyaluronic acid containing no exothermic substances, proteins, nucleic acids, metal impurities, etc. can be purified.
本発明は、 1. ヒアルロン酸含有液をシリカゲルに接触させること
を特徴とするヒアルロン酸の精製方法及び 2. ヒアルロン酸含有液が、あらかじめアルミナに接触
させたものである請求項1記載のヒアルロン酸の精製方
法である。The present invention provides: 1. a method for purifying hyaluronic acid, which comprises contacting a hyaluronic acid-containing liquid with silica gel; and 2. the hyaluronic acid according to claim 1, wherein the hyaluronic acid-containing liquid has been brought into contact with alumina in advance. Is a purification method.
本発明で用いるシリカゲルは、ケイ酸ソーダを無機酸
で分解し、凝固したものを水洗し、不純物を除去した
後、乾燥することによつて製造されるが、必ずしもこの
製造方法にとらわれるものではない。The silica gel used in the present invention is produced by decomposing sodium silicate with an inorganic acid, washing the coagulated product with water, removing impurities, and then drying, but is not necessarily limited to this production method. .
シリカゲルは、一般的な脱湿乾燥用、ガス・空気の乾
燥剤、有機溶剤の脱水用、一般精製用等の種々の用途に
使用されている。その用途に応じて、形、粒径、細孔
径、表面積、スラリーのpHの異なるグレードのものが市
販されている。本発明において使用するシリカゲルは、
そのような物性で制限されるものではない。Silica gel is used for various purposes such as general dehumidification drying, gas / air drying agent, dehydration of organic solvent, general purification and the like. Depending on the application, grades having different shapes, particle sizes, pore diameters, surface areas, and slurry pHs are commercially available. Silica gel used in the present invention,
It is not limited by such physical properties.
しかしながら、粒径は30−200μが好ましい。粒径が3
0μより小さいと、シリカゲルの除去操作等の操作性が
わるくなり、カラムに充填してクロマト処理を行なうこ
とも目づまり等の点で難しくなる、200μを越えると、
金属不純物の除去効果がわるくなる。However, the particle size is preferably 30-200μ. Particle size 3
If it is smaller than 0μ, the operability such as the removal operation of silica gel becomes poor, and it becomes difficult to pack the column and perform chromatographic treatment in terms of clogging, etc.
The effect of removing metal impurities becomes worse.
また使用するシリカゲルは、金属不純物の含量が少な
く、その溶出も少ないグレードが好ましい。Further, the silica gel to be used is preferably a grade having a small content of metal impurities and a small elution.
本発明で使用するヒアルロン酸含有液は動物組織から
抽出したものでも、又醗酵法で製造したものでも使用す
ることはできるが工業的に安価に、高品質な製品を安定
に製造するためには醗酵法で製造したものが望ましい。The hyaluronic acid-containing liquid used in the present invention can be used either as extracted from animal tissues or as produced by a fermentation method.However, in order to stably produce high-quality products at low cost industrially. Those manufactured by fermentation are desirable.
醗酵法によるヒアルロン酸はストレプトコツカス属等
のバクテリアを使用して既知の方法で得ることができ
る。醗酵法で使用する菌株は、自然界から分離されるス
トレプトコツカス属等のヒアルロン酸生産能を有する微
生物、または、特開昭63−123392号公報に記したストレ
プトコツカス・エキFM−100(微工研菌寄第9027号)の
ような高収率で安定にヒアルロン酸を生産する変異株が
好ましい。Hyaluronic acid by fermentation can be obtained by a known method using bacteria such as Streptococcus. The strain used in the fermentation method may be a microorganism having hyaluronic acid-producing ability, such as Streptococcus sp. Isolated from the natural world, or Streptococcus ex FM-100 (microscopic) described in JP-A-63-123392. A mutant that stably produces hyaluronic acid at a high yield, such as Koken Bacteria No. 9027) is preferred.
そのようなヒアルロン酸生産能を有する微生物をグル
コース、シユークロース等の炭素源、ペプトン、ポリペ
プトン、酵母エキス等の窒素源、ビタミン、無機塩等を
用いた培地中で好気的に培養して得られる培養液をヒア
ルロン酸が0.1〜5g/濃度になるように希釈後、既知の
方法、例えば遠心分離による除菌、濾過による除菌、凝
集剤による除菌、カーボン、セライト等による除菌など
の方法で除菌した液を使用することが望ましい。A microorganism having such a hyaluronic acid-producing ability is obtained by aerobically culturing in a medium using glucose, a carbon source such as sucrose, a nitrogen source such as peptone, polypeptone, and yeast extract, vitamins, and inorganic salts. After diluting the culture solution so that the hyaluronic acid has a concentration of 0.1 to 5 g / concentration, known methods, for example, sterilization by centrifugation, sterilization by filtration, sterilization by a flocculant, carbon, celite etc. It is desirable to use a solution that has been disinfected in step 1.
さらに透析処理による低分子化合物の除去、精密濾過
処理による水不溶微粒子の除去またはヒアルロン酸含有
液にアルコール、アセトン、ジオキサンなどの水溶性有
機溶剤を添加してヒアルロン酸を析出分離後、再度0.1
〜5g/濃度にヒアルロン酸を溶解する操作等を行なつ
た液を使用することができる。Furthermore, removal of low molecular compounds by dialysis treatment, removal of water-insoluble fine particles by microfiltration treatment or addition of a water-soluble organic solvent such as alcohol, acetone and dioxane to a solution containing hyaluronic acid, precipitation and separation of hyaluronic acid, and then 0.1
A liquid obtained by performing an operation of dissolving hyaluronic acid to a concentration of about 5 g / concentration can be used.
医薬品として使用できるヒアルロン酸を製造する場合
には、上記の処理を行なつた後、アルミナ処理を行なう
のが望ましい。In the case of producing hyaluronic acid that can be used as a pharmaceutical, it is desirable to carry out the above treatment and then carry out an alumina treatment.
本発明で用いられるアルミナはいわゆる酸化アルミニ
ウムで、一般的には水酸化アルミニウムを高温度で脱
水、焼成して製造されるが、必ずしもこの製造方法にと
らわれるものではない。The alumina used in the present invention is so-called aluminum oxide, which is generally produced by dehydrating and firing aluminum hydroxide at a high temperature, but is not necessarily limited to this production method.
アルミナはその粒径により、微粒(10μ以下)、普通
粒(40−60μ)、粗粒(70μ以上)に分類される。市販
のアルミナはそのアルミナ含量あるいは含有不純物量に
より、一般的なアルミナ純分約90%〜99%のグレードの
ものに対し、純度99.99%以上の高純度アルミナと称さ
れるもの、またアルミナ中の酸化ナトリウム含量が通常
の0.3−0.4%に対し、0.1%以下に精製したローソーダ
アルミナと称されるものがある。また表面積が1gにつき
50−400m2と大きく、吸着能力が高い活性アルミナがあ
るが、本発明において使用するアルミナは上記に制限さ
れるものではない。Alumina is classified into fine particles (10μ or less), normal particles (40-60μ), and coarse particles (70μ or more) according to the particle size. Depending on the alumina content or the content of impurities, commercially available alumina has a purity of 99.99% or more compared to a general alumina pure content of about 90% to 99%. There is a so-called low soda alumina having a sodium oxide content of 0.1% or less, which is usually 0.3-0.4%. Also, the surface area per 1g
Although there is activated alumina having a large adsorption capacity of 50 to 400 m 2 , the alumina used in the present invention is not limited to the above.
α,β,γの鉱物形態及びハニカム体、顆粒、球状等
の粒の形状に関しても、いずれのものも本発明において
使用することができる。Regarding the mineral forms of α, β, and γ and the shapes of grains such as honeycomb bodies, granules, and spheres, any of them can be used in the present invention.
ヒアルロン酸含有液のアルミナ処理を行うに当り、水
溶液のpHは3〜10特に6〜9、温度は0〜40℃、ヒアル
ロン酸の濃度は0.1〜5g/特に0.〜2g/がよい。In performing the alumina treatment of the hyaluronic acid-containing liquid, the pH of the aqueous solution is preferably 3 to 10, particularly 6 to 9, the temperature is 0 to 40 ° C, and the concentration of hyaluronic acid is 0.1 to 5 g / particularly 0.1 to 2 g /.
アルミナ処理の方法としては、ヒアルロン酸含有液に
粉状又は粒状のアルミナを添加して、バツチ式で撹拌す
る方法と、充填塔等に粒状又は成型したアルミナを充填
後、ヒアルロン酸含有液を通液処理する方法、またその
組合せや反復も可能であるが、通常は、処理条件の選択
により、1回の処理で充分である。As the alumina treatment method, powdery or granular alumina is added to the hyaluronic acid-containing liquid, and the mixture is stirred in a batch type. Alternatively, the granular or shaped alumina is filled in a packed tower or the like, and then the hyaluronic acid-containing liquid is passed through. Although a liquid treatment method, and a combination or repetition thereof are also possible, one treatment is usually sufficient depending on the selection of treatment conditions.
バツチ式に比べて、充填塔方式の方が効果的である
が、アルミナを充填塔等に充填してヒアルロン酸含有液
を処理する場合は、使用するアルミナの粒径に応じて、
充填塔の層高、ヒアルロン酸含有液の線速を考慮しなけ
ればならない。従つて、処理スピードは、カラムの目詰
り及び処理効率を考慮してSV=0.1〜2が好ましい。Compared with the batch type, the packed tower method is more effective, but when treating the hyaluronic acid-containing liquid by filling alumina into a packed tower or the like, according to the particle size of the alumina used,
The bed height of the packed tower and the linear velocity of the liquid containing hyaluronic acid must be considered. Therefore, the processing speed is preferably SV = 0.1 to 2 in consideration of column clogging and processing efficiency.
ヒアルロン酸含有液をシリカゲルで処理するに当りヒ
アルロン酸溶液のpHは3−12、温度は0−40℃、ヒアル
ロン酸の濃度は0.1〜5g/時に0.5〜2g/がよい。In treating the hyaluronic acid-containing solution with silica gel, the pH of the hyaluronic acid solution is preferably 3-12, the temperature is 0-40 ° C, and the concentration of hyaluronic acid is preferably 0.1-5 g / hour and 0.5-2 g / hour.
ヒアルロン酸含有液のpHが3未満の場合は、ヒアルロ
ン酸の分解が起こつたり、粘度の上昇が起り操作性が悪
くなるし、pHが12を越えた場合も、ヒアルロン酸の分解
が問題となる。If the pH of the hyaluronic acid-containing solution is less than 3, hyaluronic acid may be decomposed or the viscosity may increase, resulting in poor operability. Become.
温度も40℃を越えると、ヒアルロン酸が分解し、分子
量が低下する。If the temperature also exceeds 40 ° C., hyaluronic acid is decomposed and the molecular weight decreases.
ヒアルロン酸の濃度は0.1g/未満では、処理効率に
劣り、5g/を越えると粘度が高くなり、操作が難しく
なる。When the concentration of hyaluronic acid is less than 0.1 g /, the treatment efficiency is inferior. When it exceeds 5 g /, the viscosity becomes high and the operation becomes difficult.
本発明の処理方法としては、ヒアルロン酸含有液に、
シリカゲルを添加して、バツチ式で撹拌する方法と充填
塔に充填後、ヒアルロン酸含有液を通液処理する方法、
またその組合せや反復も可能であるが、充填塔を用いる
方法が好ましく、処理回数も条件の選択により、1回の
処理で充分である。As the treatment method of the present invention, a hyaluronic acid-containing liquid
A method of adding silica gel and stirring with a batch type and a method of passing a hyaluronic acid-containing liquid after filling the packed tower,
Although a combination or repetition thereof is also possible, a method using a packed tower is preferable, and the number of treatments is sufficient by selecting one condition, and one treatment is sufficient.
シリカゲルを充填塔の充填して、ヒアルロン酸含有液
を処理する場合には、シリカゲルの粒径やヒアルロン酸
の濃度等により、充填塔の層高、ヒアルロン酸含有液の
線速を考慮しなければならないが、処理スピードはSV=
0.1〜3が好ましい。When treating a hyaluronic acid-containing liquid by packing silica gel in a packed tower, the bed height of the packed tower and the linear velocity of the hyaluronic acid-containing liquid must be taken into account according to the particle size of the silica gel and the concentration of hyaluronic acid. No, but the processing speed is SV =
0.1 to 3 is preferred.
ヒアルロン酸量に対するシリカゲルの使用量は、ヒア
ルロン酸中の金属不純物の含量に応じて、決定する必要
があるが通常ヒアルロン酸1gを精製する場合、シリカゲ
ルは、10g−300g必要である。The amount of silica gel to be used relative to the amount of hyaluronic acid needs to be determined according to the content of metal impurities in hyaluronic acid. However, when 1 g of hyaluronic acid is purified, silica gel requires 10 g to 300 g.
ヒアルロン酸含有液をアルミナやシリカゲルで処理す
るに当り、ヒアルロン酸含有液中に、水と混合する有機
溶剤を溶解すると、処理効果が向上する場合がある。When treating a hyaluronic acid-containing liquid with alumina or silica gel, dissolving an organic solvent mixed with water in the hyaluronic acid-containing liquid may improve the treatment effect in some cases.
水と混合する有機溶剤としては、メタノール、エタノ
ールなどのアルコール類やアセトンが挙げられ、これら
を5〜50%濃度に溶解する。Examples of the organic solvent to be mixed with water include alcohols such as methanol and ethanol and acetone, and these are dissolved to a concentration of 5 to 50%.
5%未満では、効果が少なく、50%を越えると、液の
粘度が高くなり、またヒアルロン酸が析出する場合があ
る。If it is less than 5%, the effect is small, and if it exceeds 50%, the viscosity of the solution becomes high and hyaluronic acid may be precipitated.
シリカゲルで処理を行なつたヒアルロン酸含有液は、
必要ならば、pH調整や孔径0.2〜1μのメンブレンフイ
ルターを用いる精密ろ過を行なつたのち、有機溶剤沈殿
法等で分離後、真空乾燥法等により、乾燥品とすること
ができる。Hyaluronic acid-containing liquid treated with silica gel
If necessary, after performing pH adjustment and microfiltration using a membrane filter having a pore size of 0.2 to 1 μm, the product can be separated by an organic solvent precipitation method or the like, and then dried by a vacuum drying method or the like.
次に参考例及び本発明の実施例を示す。 Next, reference examples and examples of the present invention will be described.
参考例 ストレプトコツカス・エクイFM−100(微工研菌寄第9
027号)を用いて培養した培養液15を純水で50に希
釈し(ヒアルロン酸濃度1.10g/)、遠心分離、ホロー
フアイバー型限外ろ過を行ない、菌体と培地成分を除い
た。Reference example Streptococcus equii FM-100
No. 027) was diluted to 50 with pure water (hyaluronic acid concentration: 1.10 g /), centrifuged, and hollow fiber type ultrafiltration to remove bacterial cells and medium components.
このヒアルロン酸含有液500mlに食塩15gを溶解、pH7
に調節後、エタノール750mlで析出、エタノール100mlで
洗浄を行い、40℃で真空乾燥し、0.49gのヒアルロン酸
ナトリウムを得た。分析結果を表1に示す。Dissolve 15 g of sodium chloride in 500 ml of this hyaluronic acid-containing solution, pH 7
Then, the precipitate was precipitated with 750 ml of ethanol, washed with 100 ml of ethanol, and dried at 40 ° C. under vacuum to obtain 0.49 g of sodium hyaluronate. Table 1 shows the analysis results.
実施例1 参考例1で得られる菌体と培地成分を除いたヒアルロ
ン酸含有液500mlを内径5cm、高さ30cmのガラスカラムに
和光純薬社製クロマト用活性アルミナ(300メツシユ)
を150ml充填し、純水で充分洗浄後、SV=0.3(45ml/
時)で通液した。カラム通過液を、同じカラムに、和光
純薬社製シリカゲル ワコーゲルQ−50を150ml充填
し、SV=0.6(90ml/時)で通液した。このカラム通過液
500mlを集め、食塩15gを加え、pH7に調節後、エタノー
ル750mlで析出、エタノール100mlで洗浄を行い、40℃で
真空乾燥し、0.40gのヒアルロン酸ナトリウムを得た。
分析結果を表1に示す。Example 1 500 ml of a hyaluronic acid-containing liquid obtained by removing the cells and medium components obtained in Reference Example 1 was placed in a glass column having an inner diameter of 5 cm and a height of 30 cm, and activated alumina for chromatography (300 mesh) manufactured by Wako Pure Chemical Industries, Ltd.
After filling with 150 ml of water and washing thoroughly with pure water, SV = 0.3 (45 ml /
At the time). The same column was filled with 150 ml of Wako Pure Chemical Industries silica gel Wakogel Q-50 and passed through the column at SV = 0.6 (90 ml / hr). Liquid passing through this column
After collecting 500 ml and adding 15 g of sodium chloride to adjust the pH to 7, it was precipitated with 750 ml of ethanol, washed with 100 ml of ethanol, and dried in vacuo at 40 ° C. to obtain 0.40 g of sodium hyaluronate.
Table 1 shows the analysis results.
比較例1 実施例1で、アルミナカラム通過液500mlを、シリカ
ゲル処理をせずに、同様の操作を行ない、ヒアルロン酸
ナトリウ0.47gを得た。Comparative Example 1 The same operation as in Example 1 was carried out on 500 ml of the liquid passed through the alumina column without silica gel treatment, to obtain 0.47 g of sodium hyaluronate.
分析結果を表1に示す。 Table 1 shows the analysis results.
実施例2 実施例1の菌体と培地成分を除いたヒアルロン酸含有
液500mlに、0.15Mの塩化ナトリウム中の塩化セチルピリ
ジニウム10%溶液25mlを添加し、沈殿を遠心分離により
集め、100mlの水で2回洗浄後、6%の食塩水500mlに溶
解した。750mlのエタノールを加えて、析出させ、析出
物を、6%食塩水500mlに溶解した。この溶液を20gの、
60−100メツシユのフロリジルを充填したカラム(直径
1.5cm)にSV=1で通液した。 Example 2 25 ml of a 10% solution of cetylpyridinium chloride in 0.15 M sodium chloride was added to 500 ml of the hyaluronic acid-containing solution from which the cells and the medium components of Example 1 had been removed, and the precipitate was collected by centrifugation. , And dissolved in 500 ml of 6% saline. 750 ml of ethanol was added for precipitation, and the precipitate was dissolved in 500 ml of 6% saline. 20 g of this solution,
Column filled with 60-100 mesh florisil (diameter
1.5 cm) at SV = 1.
この溶液を、分画分子量10万のホロ−フアイバーを用
いて脱塩処理した後、和光純薬社製シリカゲルワコーゲ
ルQ−50を150ml充填したカラムに、SV=0.6(90ml/
時)で通液した。このカラム通過液500mlを集め、食塩1
5gを加え、pH7に調節後エタノール750mlで析出、エタノ
ール100mlで洗浄を行い、40℃で真空乾燥し、0.38gのヒ
アルロン酸ナトリウムを得た。分析結果を表2に示す。This solution was desalted using a hollow fiber having a molecular weight cut off of 100,000, and then applied to a column packed with 150 ml of silica gel Wakogel Q-50 manufactured by Wako Pure Chemical Industries, Ltd., to give SV = 0.6 (90 ml / 90 ml).
At the time). Collect 500 ml of the liquid passed through the column, and add
5 g was added to adjust the pH to 7, followed by precipitation with 750 ml of ethanol, washing with 100 ml of ethanol, and vacuum drying at 40 ° C. to obtain 0.38 g of sodium hyaluronate. Table 2 shows the analysis results.
比較例2 実施例2で、シリカゲルカラム処理を行なわない以外
は、同様の操作を行なつた。得られた0.39gのヒアルロ
ン酸ナトリウムを分析した結果を表2に示す。Comparative Example 2 The same operation was performed as in Example 2, except that the silica gel column treatment was not performed. Table 2 shows the result of analysis of the obtained 0.39 g of sodium hyaluronate.
実施例3 実施例1の菌体と培地成分を除いたヒアルロン酸含有
液400mlに、100mlのエタノールを添加して500mlとした
後、同様にアルミナ処理、シリカゲル処理を行なつた。
この処理液に15gの食塩を添加した後、0.2ミクロン孔径
のメンブレンフイルターで精密ろ過を行ない、750mlの
エタノールで析出、100mlのエタノールで洗浄して、40
℃で真空乾燥した。得られたヒアルロン酸ナトリウムは
0.37gであつた。このヒアルロン酸ナトリウムの分析結
果は、次のとおりであった。 Example 3 100 ml of ethanol was added to 400 ml of the hyaluronic acid-containing liquid excluding the cells and the medium components of Example 1 to make 500 ml, and then similarly treated with alumina and silica gel.
After adding 15 g of sodium chloride to this treatment solution, the solution was subjected to microfiltration with a membrane filter having a pore size of 0.2 μm, precipitated with 750 ml of ethanol, washed with 100 ml of ethanol, and washed with 40 ml of ethanol.
Vacuum dried at ℃. The resulting sodium hyaluronate is
0.37g. The analysis results of this sodium hyaluronate were as follows.
蛋白質量 検出せず 核酸 検出せず 発熱性物質 5.1Pg/mg 金属不純物 アルミニウム 1ppm以下 カルシウム 1ppm マグネシウム 検出せず 鉄 検出せず ケイ素 検出せず 測定法 1)蛋白質含量:精製ヒアルロン酸を、0.1N水酸化ナト
リウムに溶解し、ローリー法にて行なつた。Protein content Not detected Nucleic acid Not detected Pyrogenic substance 5.1 Pg / mg Metal impurities Aluminum 1 ppm or less Calcium 1 ppm Magnesium Not detected Iron Not detected Silicon Not detected Measurement method 1) Protein content: purified hyaluronic acid, 0.1N water It was dissolved in sodium oxide, and was carried out by the Lowry method.
2)核酸 :0.1%ヒアルロン酸ナトリウム溶液の26
0nmにおける吸光度を測定した。2) Nucleic acid: 0.1% sodium hyaluronate solution 26
The absorbance at 0 nm was measured.
3)発熱性物質:生化学工業社製トキシカラ−システム
により比色分析することにより行なつた。3) Exothermic substance: This was carried out by colorimetric analysis using a Toxicolor system manufactured by Seikagaku Corporation.
4)金属不純物:発光分析によつた。4) Metal impurities: Emission analysis.
本発明によれば、高品質なヒアルロン酸を簡便な方法
で製造することができる。またこの方法で得られたヒア
ルロン酸は、医薬方面の用途が期待される。According to the present invention, high-quality hyaluronic acid can be produced by a simple method. The hyaluronic acid obtained by this method is expected to be used in medicine.
Claims (2)
せることを特徴とするヒアルロン酸の精製方法。1. A method for purifying hyaluronic acid, comprising contacting a hyaluronic acid-containing liquid with silica gel.
ナに接触させたものである請求項1.記載のヒアルロン酸
の精製方法。2. The method for purifying hyaluronic acid according to claim 1, wherein the hyaluronic acid-containing liquid has been brought into contact with alumina in advance.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25498688A JP2731545B2 (en) | 1988-10-12 | 1988-10-12 | Method for purifying hyaluronic acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25498688A JP2731545B2 (en) | 1988-10-12 | 1988-10-12 | Method for purifying hyaluronic acid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02103204A JPH02103204A (en) | 1990-04-16 |
| JP2731545B2 true JP2731545B2 (en) | 1998-03-25 |
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ID=17272621
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| IT1247175B (en) * | 1991-04-19 | 1994-12-12 | Fidia Spa | PROCEDURE FOR PURIFICATION OF HYALURONIC ACID AND FRACTION OF PURE HYALURONIC ACID FOR OPHTHALMIC USE. |
| CN101089021B (en) | 2007-07-12 | 2010-04-14 | 华东理工大学 | Method for separating and extracting hyaluronic acid from microbial fermentation broth |
| WO2012118194A1 (en) * | 2011-03-02 | 2012-09-07 | 電気化学工業株式会社 | Pre-filled syringe filling syringe having resin barrel with aqueous solution containing hyaluronic acid or salt thereof |
| KR102762718B1 (en) * | 2022-02-23 | 2025-02-06 | 주식회사 스카이테라퓨틱스 | A structure of polymer hyaluronic acid, manufacturing method thereof and cosmetic composition comprising the same |
-
1988
- 1988-10-12 JP JP25498688A patent/JP2731545B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02103204A (en) | 1990-04-16 |
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