JPH0577681B2 - - Google Patents

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Publication number
JPH0577681B2
JPH0577681B2 JP20135586A JP20135586A JPH0577681B2 JP H0577681 B2 JPH0577681 B2 JP H0577681B2 JP 20135586 A JP20135586 A JP 20135586A JP 20135586 A JP20135586 A JP 20135586A JP H0577681 B2 JPH0577681 B2 JP H0577681B2
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JP
Japan
Prior art keywords
hyaluronic acid
treatment
molecular weight
acid
alkali
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
Application number
JP20135586A
Other languages
Japanese (ja)
Other versions
JPS6357602A (en
Inventor
Masato Ishioroshi
Shunsuke Horiike
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kewpie Corp
Original Assignee
QP Corp
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Filing date
Publication date
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Priority to JP20135586A priority Critical patent/JPS6357602A/en
Publication of JPS6357602A publication Critical patent/JPS6357602A/en
Publication of JPH0577681B2 publication Critical patent/JPH0577681B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は低分子ヒアルロン酸の製造方法に関す
るものである。 〔従来の技術〕 ヒアルロン酸は、鶏冠、ヘソの緒、軟骨、皮
膚、硝子体、関節液などの生体組織中に広く分布
しており、これらから抽出されたヒアルロン酸は
人の肌をなめらかにしたり肌のシワを延ばしたり
する効果があるところから従来より化粧品の原料
として用いられている。また、このような効果は
高分子で粘度が高いヒアルロン酸であるほど顕著
であるところから、従来のこの分野では主に高分
子ヒアルロン酸に関しての研究が盛んであつた。 ところで低分子ヒアルロン酸は高分子のものと
異なり水に対して溶けやすく、かつ粘度が低く、
これを配合した化粧品は肌にべとつき感やつつぱ
り感などの違和感を与えないなどの効果があるこ
とがわかり、低分子ヒアルロン酸の化粧品原料と
しての利用も期待され始めた。 〔発明が解決しようとする問題点〕 従来より、ヒアルロン酸含有原料、例えば鶏冠
を室温で長時間放置しておくと鶏冠に含まれてい
るヒアルロニダーゼがヒアルロン酸を分解してこ
のものを低分子化することが知られている。とこ
ろがこのような原料から抽出されたヒアルロン酸
は細菌増殖により産生された細菌性ヒアルロニダ
ーゼによつて低分子化されたものであるため微生
物学上の問題点を有するだけでなく、このような
ヒアルロニダーゼを用いた低分子ヒアルロン酸の
製造方法は分解程度の制御が困難であり、しかも
収率も低いなどの問題点があることが認められて
いる。 一方、ヒアルロン酸は安定性に乏しく、上記し
たようなヒアルロニダーゼによる処理の他、熱、
強酸、強アルカリ等の処理によつても低分子化さ
れることを知られている。 しかし工業的規模での低分子ヒアルロン酸の製
造、その品質あるいは収率等の観点から低分子ヒ
アルロン酸を如何に効率的に生産するかの研究報
告は本発明者らの知る限りにおいては未だなされ
ていない。 本発明は正にこのような課題を解決することを
目的とするものである。 〔問題点を解決するための手段〕 本発明者らは上記の目的に即して鋭意研究を重
ねた結果、ヒアルロン酸含有原料をペースト化し
たものに一定の条件下でアルカリ分解処理を施す
るならば平均分子量が20万〜80万程度の低分子ヒ
アルロン酸が高い収率で得られることを見出し
た。 また、本発明者らは、アルカリ分解処理を平均
分子量が20万未満になるまで施すと最終製品の収
率が下がるだけでなく製品が褐変するようになる
ことを知見し、更に研究を重ねたところ、一旦ア
ルカリ分解処理して平均分子量を20万〜80万程度
としたものに一定の条件下で酸分解処理を施すな
らば平均分子量が1万〜20万の低分子ヒアルロン
酸を品質を損うことなく高い収率で製造しうるこ
とを見出した。本発明者らは更に又、アルカリ分
解処理してないヒアルロン酸含有原料に直接酸分
解処理を施すと、主にヒアルロン酸の末端部での
分解が生じるためか低分子化の程度は低く、その
後アルカリ分解処理を施しても低分子化の程度は
このアルカリ処理単独の場合とほとんど変わらな
いことも知見し、本発明を完成するに至つた。 本発明は、ペースト化したヒアルロン酸含有原
料にアルカリを加えて該原料中のヒアルロン酸を
アルカリ分解処理し、この際該処理を最終アルカ
リ添加濃度0.05〜0.1M、処理温度50〜70℃およ
び処理時間60〜180分間の条件下で行ない、次い
で該原料からヒアルロン酸を抽出することを特徴
とする低分子ヒアルロン酸の製法を提供するもの
である。 本発明の方法で用いるヒアルロン酸含有原料は
ペースト化してあるものである。ここにおいてヒ
アルロン酸含有原料としてはヒアルロン酸が含ま
れている動物の諸組織であれば特に制限的でな
く、例えば鶏冠、ヘソの緒、関節液、硝子体、皮
膚等を挙げることができる。尚、組織に依り異な
るが鶏冠には約1〜2%程度のヒアルロン酸が含
まれている。また、そのヒアルロン酸の平均分子
量は大体200万〜800万程度である。ペースト化に
先立つて原料中に含まれている蛋白質を熱変性さ
せるために加熱処理するのは任意である。またこ
の加熱処理前あるいは後に原料を細断機、チヨツ
パー等で細かく砕いておくとペースト化がしやす
くなるという利点がある。ペースト化は原料を破
砕、微粒子化しペースト状とさせうる限りその方
法は任意で、例えば清水を加えてホモゲナイザ
ー、高速攪拌機、擂潰機等を用いてホモゲナイズ
すればよい。ヒアルロン酸含有原料をこのように
ペースト化するのは、該原料中のヒアルロン酸の
アルカリ分解処理を効率よく行なうためである。 本発明の方法によれば、ペースト化したヒアル
ロン酸含有原料を次いで一定の条件下でアルカリ
分解処理に付す。ここにおいて一定の条件とは、
最終アルカリ添加濃度0.05〜0.1M、処理温度50
〜70℃、および処理時間60〜180分間である。こ
のような条件下でのアルカリ分解処理により平均
分子量が20万〜80万程度の低分子ヒアルロン酸が
高い収率、一般的には原料組織の0.9〜1.20%程
度、で得られる。例えば、水酸化ナトリウム
0.05M、50℃および120分の処理条件下では平均
分子量が80万程度のヒアルロン酸が得られ、また
水酸化ナトリウム0.1M、60℃および120〜150分
の処理条件下では平均分子量が20万〜30万程度の
ヒアルロン酸が得られる。処理条件が上記の各範
囲の上限を越すようになると平均分子量が20万未
満の低分子ヒアルロン酸を生産し得ても最終製品
の収率が下がるだけでなくこのものを褐変化して
しまう。また処理条件が上記の各範囲の下限に満
たないとヒアルロン酸を充分に低分子化し難いだ
けでなく収率もよくない。 尚、用いるアルカリは特に限定的でないが、典
型的には水酸化ナトリウムの他水酸化カリウムあ
るいは水酸化カルシウム等が用いられる。 本発明の方法によればアルカリ分解処理に付し
た原料から次いでヒアルロン酸を抽出する。この
際抽出に先立つてヒアルロン酸の抽出効率を高め
る目的で存在する蛋白質を分解処理して除いてお
いてもよい。尚、この蛋白質分解処理は常法に従
つて行なえばよい。ヒアルロン酸の抽出は常法に
準ずればよく、例えば蛋白質分解処理したペース
トを過して固形物を除去した後得られた液に
塩化セチルピリジニウム(CPC)溶液を添加し
てヒアルロン酸をCPCに吸着させて沈澱させれ
ばよい。別した沈澱物は食塩水中に溶解させた
後所望に応じてヒアルロン酸を更に低分子化する
目的で下記において説明する酸分解処理に付して
も、あるいは上記食塩水にエタノールを添加して
低分子ヒアルロン酸を沈澱させてもよい。更にこ
うして得られた粗製ヒアルロン酸を常法に準じて
精製し、低分子ヒアルロン酸の製品としてもよ
い。 本発明の方法によれば、更に低分子化されたヒ
アルロン酸を得るには、抽出したヒアルロン酸を
PH2.8〜4.0、0.70〜90℃および30〜180分間の条件
の下で酸分解処理する。このような条件下での酸
分解処理により平均分子量が1万〜20万程度の低
分子ヒアルロン酸が高い収率、一般的には原料組
織の0.75〜0.95%程度で得られる。処理条件がPH
について上記の下限より低く、また他のフアクタ
ーについて上記の各範囲の上限を越すようになる
と平均分子量が1万未満の低分子ヒアルロン酸を
生産し得るが、最終製品の収率が下がるだけでな
くこのものを褐変化するようになる。また処理条
件がPHについて上記の上限より高く、また他のフ
アクターについて上記の各範囲の下限に満たない
とヒアルロン酸の一層の低分子化が計り難い。 尚、用いる酸は特に限定的でないが典型的には
塩酸、硫酸、酢酸等が用いられる。酸分解を強酸
性下、高温、長時間の条件の下で実施する際には
特に設備の材質に注意が払われるべきである。 このように本発明の方法によれば所望する低分
子量のヒアルロン酸を、アルカリ分解処理単独、
あるいは酸分解処理との組合わせにおいてそれら
の処理条件を前記した特定の範囲内で選択するこ
とにより高い収率で製造することができる。 〔発明の効果〕 以下の試験例1〜3において本発明の方法によ
れば低分子ヒアルロン酸を如何に効果的に生産し
うるかを示す。 試験例 1 この試験例は、一定の条件下でのアルカリ分解
処理により平均分子量が20万〜80万の低分子ヒア
ルロン酸が高い収率で得られることを示す。尚、
本発明において%は重量%である。 鶏冠各1Kgを80℃の熱水中に20分間浸漬して加
熱処理した後細断機で細かく砕き、これにほぼ3
倍量の清水を加えてホモゲナイザーでペースト状
としたものに、水酸化ナトリウムを加えて下記の
表1に示した条件の下でそれぞれアルカリ分解処
理をした。次いで各々蛋白質分解処理に付し、不
溶解固形物を過して除去し、得られた液に塩
化セチルピリジニウム溶液を添加してヒアルロン
酸を吸着沈澱させた。別した各沈澱物をエタノ
ールで洗浄して精製した後乾燥させた。乾燥後得
られた各製品の収率と平均分子量(極限粘度から
算出)とを求め、その結果を表1にまとめた。
[Industrial Application Field] The present invention relates to a method for producing low molecular weight hyaluronic acid. [Conventional technology] Hyaluronic acid is widely distributed in living tissues such as cock's comb, umbilical cord, cartilage, skin, vitreous body, and joint fluid, and hyaluronic acid extracted from these is used to smooth human skin. It has traditionally been used as an ingredient in cosmetics because it has the effect of smoothing out skin wrinkles. In addition, since such effects are more pronounced in hyaluronic acid, which has higher molecular weight and higher viscosity, conventional research in this field has mainly focused on high molecular weight hyaluronic acid. By the way, unlike high-molecular hyaluronic acid, low-molecular hyaluronic acid is easily soluble in water and has a low viscosity.
Cosmetics containing this product have been found to have the effect of not giving the skin any unpleasant sensations such as stickiness or tightness, and expectations have begun for the use of low-molecular-weight hyaluronic acid as a cosmetic raw material. [Problems to be solved by the invention] Conventionally, when a hyaluronic acid-containing raw material, such as a cock's comb, is left at room temperature for a long time, the hyaluronidase contained in the cock's comb decomposes the hyaluronic acid and converts it into a low-molecular-weight material. It is known to do. However, since hyaluronic acid extracted from such raw materials has been reduced to a low molecular weight by bacterial hyaluronidase produced by bacterial growth, it not only has microbiological problems, but also has problems with microbiology. It has been recognized that the method used for producing low-molecular-weight hyaluronic acid has problems such as difficulty in controlling the degree of decomposition and low yield. On the other hand, hyaluronic acid has poor stability, and in addition to treatment with hyaluronidase as described above, heat treatment,
It is known that it can also be reduced in molecular weight by treatment with strong acids, strong alkalis, etc. However, to the best of the present inventors' knowledge, there have been no research reports on how to efficiently produce low-molecular-weight hyaluronic acid from the viewpoint of production of low-molecular-weight hyaluronic acid on an industrial scale, its quality, yield, etc. Not yet. The present invention aims to solve precisely such problems. [Means for solving the problem] As a result of extensive research in accordance with the above-mentioned objective, the present inventors performed an alkali decomposition treatment under certain conditions on a paste made from a hyaluronic acid-containing raw material. In this case, it was discovered that low-molecular-weight hyaluronic acid with an average molecular weight of about 200,000 to 800,000 could be obtained in high yield. In addition, the present inventors discovered that if the alkaline decomposition treatment is applied until the average molecular weight becomes less than 200,000, the yield of the final product not only decreases, but also the product becomes brown, and conducted further research. However, if acid decomposition treatment is performed under certain conditions on a product that has been subjected to alkaline decomposition treatment to have an average molecular weight of 200,000 to 800,000, the quality of low-molecular-weight hyaluronic acid with an average molecular weight of 10,000 to 200,000 will be lost. It has been found that it can be produced in high yield without any problems. The present inventors further found that when hyaluronic acid-containing raw materials that have not been subjected to alkaline decomposition treatment are directly subjected to acid decomposition treatment, the degree of decomposition is low, probably because decomposition occurs mainly at the terminal end of hyaluronic acid; It was also found that even when alkali decomposition treatment is applied, the degree of molecular weight reduction is almost the same as when the alkali treatment is performed alone, leading to the completion of the present invention. The present invention involves adding an alkali to a pasted hyaluronic acid-containing raw material to decompose the hyaluronic acid in the raw material with an alkali, and at this time, the treatment is carried out at a final alkali concentration of 0.05 to 0.1M, a treatment temperature of 50 to 70°C, and a treatment temperature of 50 to 70°C. The present invention provides a method for producing low-molecular-weight hyaluronic acid, which is characterized by carrying out the method for 60 to 180 minutes, and then extracting hyaluronic acid from the raw material. The hyaluronic acid-containing raw material used in the method of the present invention is made into a paste. Here, the hyaluronic acid-containing raw material is not particularly limited as long as it contains animal tissues that contain hyaluronic acid, and includes, for example, a cock's comb, umbilical cord, joint fluid, vitreous body, and skin. Although it varies depending on the tissue, a cock's comb contains about 1 to 2% hyaluronic acid. Furthermore, the average molecular weight of hyaluronic acid is approximately 2 million to 8 million. It is optional to perform a heat treatment to thermally denature the proteins contained in the raw materials prior to making them into a paste. Furthermore, if the raw material is finely ground using a shredder, chopper, etc. before or after this heat treatment, there is an advantage that it becomes easier to make a paste. The paste can be made by any method as long as the raw material can be crushed and made into fine particles to form a paste. For example, fresh water may be added and the material may be homogenized using a homogenizer, a high-speed stirrer, a crusher, or the like. The reason why the hyaluronic acid-containing raw material is made into a paste in this way is to efficiently carry out the alkaline decomposition treatment of the hyaluronic acid in the raw material. According to the method of the present invention, the pasted hyaluronic acid-containing raw material is then subjected to alkaline decomposition treatment under certain conditions. The certain conditions here are:
Final alkali addition concentration 0.05-0.1M, treatment temperature 50
~70 °C, and treatment time 60-180 minutes. By alkaline decomposition treatment under such conditions, low molecular weight hyaluronic acid with an average molecular weight of about 200,000 to 800,000 can be obtained in a high yield, generally about 0.9 to 1.20% of the raw material structure. For example, sodium hydroxide
Hyaluronic acid with an average molecular weight of about 800,000 was obtained under treatment conditions of 0.05M, 50℃ and 120 minutes, and hyaluronic acid with an average molecular weight of about 200,000 was obtained under treatment conditions of 0.1M sodium hydroxide, 60℃ and 120-150 minutes. ~300,000 hyaluronic acid can be obtained. If the processing conditions exceed the upper limits of each of the above ranges, even if low-molecular-weight hyaluronic acid with an average molecular weight of less than 200,000 can be produced, the yield of the final product will not only decrease, but it will also turn brown. Furthermore, if the treatment conditions do not fall within the lower limits of each of the above ranges, it will not only be difficult to sufficiently reduce the molecular weight of hyaluronic acid, but also the yield will be poor. The alkali used is not particularly limited, but typically potassium hydroxide, calcium hydroxide, etc. in addition to sodium hydroxide are used. According to the method of the present invention, hyaluronic acid is then extracted from the raw material subjected to alkaline decomposition treatment. At this time, prior to extraction, existing proteins may be removed by decomposition treatment for the purpose of increasing the extraction efficiency of hyaluronic acid. Incidentally, this proteolytic treatment may be carried out according to a conventional method. Extraction of hyaluronic acid can be carried out using conventional methods. For example, after removing solids by passing through a protein-decomposed paste, a cetylpyridinium chloride (CPC) solution is added to the resulting liquid to convert hyaluronic acid into CPC. It may be adsorbed and precipitated. The separated precipitate may be dissolved in saline and then subjected to the acid decomposition treatment described below for the purpose of further reducing the molecular weight of hyaluronic acid, or by adding ethanol to the above saline to further reduce the molecular weight of hyaluronic acid. Molecular hyaluronic acid may be precipitated. Furthermore, the crude hyaluronic acid thus obtained may be purified according to a conventional method to produce a low-molecular-weight hyaluronic acid product. According to the method of the present invention, in order to obtain hyaluronic acid with a lower molecular weight, the extracted hyaluronic acid is
Acid decomposition treatment under the conditions of PH2.8~4.0, 0.70~90℃ and 30~180 minutes. By acid decomposition treatment under such conditions, low molecular weight hyaluronic acid having an average molecular weight of about 10,000 to 200,000 can be obtained in a high yield, generally at about 0.75 to 0.95% of the raw material structure. Processing conditions are PH
If it is lower than the lower limit above for other factors and exceeds the upper limit of each range above for other factors, it is possible to produce low molecular weight hyaluronic acid with an average molecular weight of less than 10,000, but not only will the yield of the final product decrease; This stuff starts to turn brown. Furthermore, if the treatment conditions are higher than the upper limit for pH than the above-mentioned upper limit, and lower than the lower limits of each of the above-mentioned ranges for other factors, it is difficult to predict further reduction in the molecular weight of hyaluronic acid. Although the acid used is not particularly limited, hydrochloric acid, sulfuric acid, acetic acid, etc. are typically used. Particular attention should be paid to the material of the equipment when carrying out acid decomposition under conditions of strong acidity, high temperature, and long periods of time. As described above, according to the method of the present invention, desired low molecular weight hyaluronic acid can be treated with alkaline decomposition alone,
Alternatively, by selecting the treatment conditions within the above-mentioned specific range in combination with acid decomposition treatment, high yield production can be achieved. [Effects of the Invention] The following Test Examples 1 to 3 show how low-molecular-weight hyaluronic acid can be effectively produced according to the method of the present invention. Test Example 1 This test example shows that low molecular weight hyaluronic acid having an average molecular weight of 200,000 to 800,000 can be obtained in high yield by alkaline decomposition treatment under certain conditions. still,
In the present invention, % is % by weight. Each 1 kg of chicken comb is immersed in hot water at 80°C for 20 minutes, heat-treated, and then finely chopped with a shredder.
Double the amount of fresh water was added to form a paste using a homogenizer, and sodium hydroxide was added to the paste, which was then subjected to alkaline decomposition treatment under the conditions shown in Table 1 below. Each sample was then subjected to proteolytic treatment, and undissolved solids were removed by filtration, and a cetylpyridinium chloride solution was added to the resulting liquid to adsorb and precipitate hyaluronic acid. Each separated precipitate was purified by washing with ethanol and then dried. The yield and average molecular weight (calculated from the intrinsic viscosity) of each product obtained after drying were determined, and the results are summarized in Table 1.

【表】 備考:4と5の条件下では製品は褐変化して
いた。
試験例 2 この試験例は、一旦一定の条件下でアルカリ分
解処理をしたものに更に一定の条件下で酸分解処
理することにより平均分子量が20万以下の低分子
ヒアルロン酸が得られることを示す。 鶏冠各1Kgから上記試験例1の方法に従い、尚
この際アルカリ分解処理を最終アルカリ添加濃度
0.1MNaOH、処理温度60℃、処理時間120分の条
件の下で行なつた他はすべて同様に処理していず
れも2%食塩水に溶かしたヒアルロン酸溶液を得
た。これら溶液に4N塩酸を加えて下表2に示し
た条件の下でそれぞれ酸分解処理をした。冷却後
エタノールを加えてヒアルロン酸を沈澱させ、次
いで過した各沈澱物をエタノールで洗浄して精
製した後乾燥させた。乾燥後得られた各製品の収
率と平均分子量(極限粘度より算出)とを求め、
その結果を表2にまとめた。
[Table] Note: Under conditions 4 and 5, the product turned brown.
Test Example 2 This test example shows that low-molecular-weight hyaluronic acid with an average molecular weight of 200,000 or less can be obtained by performing alkaline decomposition treatment under certain conditions and then acid decomposition treatment under certain conditions. . Follow the method of Test Example 1 above from each 1 kg of chicken comb, and perform alkali decomposition treatment at the final alkali addition concentration.
Hyaluronic acid solutions dissolved in 2% saline were obtained by the same treatment except that the treatment was carried out under the conditions of 0.1M NaOH, treatment temperature 60° C., and treatment time 120 minutes. 4N hydrochloric acid was added to these solutions, and each solution was subjected to acid decomposition treatment under the conditions shown in Table 2 below. After cooling, ethanol was added to precipitate hyaluronic acid, and each precipitate was then purified by washing with ethanol, followed by drying. Determine the yield and average molecular weight (calculated from the intrinsic viscosity) of each product obtained after drying,
The results are summarized in Table 2.

【表】 試験例 3 この試験例は、酸分解の処理条件を適宜選択す
ることにより平均分子量が10万以下の低分子ヒア
ルロン酸が高い収率で得られることを示す。 鶏冠各1Kgから上記試験例1の方法に従い、尚
この際アルカリ分解処理を最終アルカリ添加濃度
0.1MNaOH、処理温度60℃、処理時間150分の条
件の下で行なつた他はすべて同様に処理していず
れも2%食塩水に溶かしたヒアルロン酸溶液を得
た。これら溶液に4N塩酸を加えて下表3に示し
た条件の下でそれぞれ酸分解処理をした。冷却後
エタノールを加えてヒアルロン酸を沈澱させ、次
いで別した各沈澱物をエタノールで洗浄して精
製した後乾燥させた。乾燥後得られた各製品の収
率と平均分子量(極限粘度より算出)とを求め、
その結果を表3にまとめた。
[Table] Test Example 3 This test example shows that low molecular weight hyaluronic acid having an average molecular weight of 100,000 or less can be obtained in high yield by appropriately selecting the treatment conditions for acid decomposition. Follow the method of Test Example 1 above from each 1 kg of chicken comb, and perform alkali decomposition treatment at the final alkali addition concentration.
Hyaluronic acid solutions dissolved in 2% saline were obtained by the same treatment except that the treatment was carried out under the conditions of 0.1M NaOH, treatment temperature 60° C., and treatment time 150 minutes. 4N hydrochloric acid was added to these solutions, and each solution was subjected to acid decomposition treatment under the conditions shown in Table 3 below. After cooling, ethanol was added to precipitate hyaluronic acid, and then each separated precipitate was washed with ethanol, purified, and then dried. Determine the yield and average molecular weight (calculated from the intrinsic viscosity) of each product obtained after drying,
The results are summarized in Table 3.

〔実施例〕〔Example〕

以下、本発明を実施例でもつて更に詳しく説明
する。 実施例 1 鶏冠1Kgを80℃の熱水中に20分間浸漬して加熱
処理した後細断機で細かく砕き、これにほぼ3倍
量の清水を加えてホモゲナイザーでペースト状と
したものに、水酸化ナトリウム(最終アルカリ添
加濃度0.1M)を加えて60℃で120分間の条件下攪
拌しながらアルカリ分解処理をした。次いで蛋白
質分解処理に付し、不溶解固形物を過して除去
し、得られた液に塩化セチルピリジニウム溶液
を添加してヒアルロン酸を吸着沈澱させた。別
した沈澱物を2%食塩水に溶解させた後この溶液
に4N塩酸を加えてPHを3.0に調整して90℃で40分
間の条件下で酸分解処理をした。冷却後エタノー
ルを加えてヒアルロン酸を沈澱させ、次いで別
した沈澱物をエタノールで洗浄して精製した後乾
燥させ、白色粉末8.4gを得た。このものの平均
分子量は7万で、収率は0.84%であつた。 実施例 2 上記実施例1の方法において酸分解処理をPH
3.8、80℃および100分間の条件の下で実施した他
はすべて同様にして鶏冠1Kgから白色粉末9.6g
を得た。このものの平均分子量は16万で、収率は
0.96%であつた。 実施例 3 上記実施例1の方法においてアルカリ分解処理
を最終アルカリ添加濃度0.1M、処理温度60℃、
処理時間150分で実施し、更に酸分解処理をPH
2.8、90℃および150分間の条件の下で実施した他
はすべて同様にして鶏冠1Kgから白色粉末7.9g
を得た。このものの平均分子量は1万で、収率
0.79%であつた。
Hereinafter, the present invention will be explained in more detail with reference to Examples. Example 1 1 kg of chicken comb was immersed in hot water at 80°C for 20 minutes, heat-treated, and then finely crushed with a shredder. Approximately three times the amount of fresh water was added to this, and the mixture was made into a paste using a homogenizer. Sodium oxide (final alkali addition concentration 0.1M) was added, and alkali decomposition treatment was carried out under stirring conditions at 60°C for 120 minutes. The mixture was then subjected to proteolytic treatment to remove undissolved solids by filtration, and a cetylpyridinium chloride solution was added to the resulting liquid to adsorb and precipitate hyaluronic acid. After the separated precipitate was dissolved in 2% saline, 4N hydrochloric acid was added to this solution to adjust the pH to 3.0, and acid decomposition treatment was performed at 90°C for 40 minutes. After cooling, ethanol was added to precipitate hyaluronic acid, and the separated precipitate was purified by washing with ethanol and dried to obtain 8.4 g of white powder. The average molecular weight of this product was 70,000, and the yield was 0.84%. Example 2 In the method of Example 1 above, acid decomposition treatment was performed at PH
3.8, 9.6 g of white powder was obtained from 1 kg of chicken comb in the same manner except that it was carried out under the conditions of 80°C and 100 minutes.
I got it. The average molecular weight of this product is 160,000, and the yield is
It was 0.96%. Example 3 In the method of Example 1 above, the alkali decomposition treatment was carried out at a final alkali addition concentration of 0.1M, a treatment temperature of 60°C,
The treatment time was 150 minutes, and the acid decomposition treatment was performed at PH.
2.8, 7.9 g of white powder from 1 Kg of chicken comb was carried out in the same manner except that it was carried out under the conditions of 90°C and 150 minutes.
I got it. The average molecular weight of this product is 10,000, and the yield is
It was 0.79%.

Claims (1)

【特許請求の範囲】 1 ペースト化したヒアルロン酸含有原料にアル
カリを加えて該原料中のヒアルロン酸をアルカリ
分解処理し、この際該処理を最終アルカリ添加濃
度0.05〜0.1M、処理温度50〜70℃および処理時
間60〜180分間の条件下で行ない、次いで該原料
からヒアルロン酸を抽出することを特徴とする低
分子ヒアルロン酸の製法。 2 アルカリとして水酸化ナトリウムを用いる、
特許請求の範囲第1項記載の低分子ヒアルロン酸
の製法。
[Claims] 1. Add an alkali to a pasted hyaluronic acid-containing raw material to decompose the hyaluronic acid in the raw material with an alkali, and at this time, the treatment is carried out at a final alkali concentration of 0.05 to 0.1M and a treatment temperature of 50 to 70%. 1. A method for producing low-molecular-weight hyaluronic acid, which is carried out under conditions of temperature and treatment time of 60 to 180 minutes, and then extracting hyaluronic acid from the raw material. 2 Using sodium hydroxide as the alkali,
A method for producing low molecular weight hyaluronic acid according to claim 1.
JP20135586A 1986-08-29 1986-08-29 Production of low-molecular hyaluronic acid Granted JPS6357602A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20135586A JPS6357602A (en) 1986-08-29 1986-08-29 Production of low-molecular hyaluronic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20135586A JPS6357602A (en) 1986-08-29 1986-08-29 Production of low-molecular hyaluronic acid

Publications (2)

Publication Number Publication Date
JPS6357602A JPS6357602A (en) 1988-03-12
JPH0577681B2 true JPH0577681B2 (en) 1993-10-27

Family

ID=16439665

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20135586A Granted JPS6357602A (en) 1986-08-29 1986-08-29 Production of low-molecular hyaluronic acid

Country Status (1)

Country Link
JP (1) JPS6357602A (en)

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JP2587268B2 (en) * 1988-04-18 1997-03-05 チッソ株式会社 Method for producing low-viscosity hyaluronic acid or salt thereof
JP4576583B2 (en) * 2005-03-22 2010-11-10 キユーピー株式会社 Hyaluronic acid or a salt thereof, method for producing the same, and cosmetics and food compositions containing the same
KR100665916B1 (en) * 2005-06-27 2007-01-10 주식회사 바이오랜드 Low molecular weight polysaccharides and their preparation method
JP2007186689A (en) * 2005-12-13 2007-07-26 Shiseido Co Ltd Method for producing low-molecular weight hyaluronic acid
JP2007186688A (en) * 2005-12-13 2007-07-26 Shiseido Co Ltd Method for producing low-molecular weight hyaluronic acid
JP5289936B2 (en) 2006-02-24 2013-09-11 キユーピー株式会社 Novel low molecular weight hyaluronic acid and / or salt thereof, and cosmetics, pharmaceutical compositions and food compositions using the same
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JP2009155486A (en) * 2007-12-27 2009-07-16 Kikkoman Corp Depolymerized hyaluronic acid and production method thereof
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WO2015053280A1 (en) 2013-10-08 2015-04-16 キユーピー株式会社 Carboxymethyl-group-containing modified hyaluronic acid and/or salt thereof and/or production method for carboxymethyl-group-containing modified hyaluronic acid and/or salt thereof
EP3608343B1 (en) * 2017-04-07 2024-08-07 Youreh Co., Ltd. Method for preparing low molecular weight hyaluronic acid

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011070948A1 (en) 2009-12-08 2011-06-16 キユーピー株式会社 Method for manufacturing purified hyaluronic acids

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