JP2001178492A - Method of extracting useful substance from aquatic life - Google Patents

Method of extracting useful substance from aquatic life

Info

Publication number
JP2001178492A
JP2001178492A JP36904799A JP36904799A JP2001178492A JP 2001178492 A JP2001178492 A JP 2001178492A JP 36904799 A JP36904799 A JP 36904799A JP 36904799 A JP36904799 A JP 36904799A JP 2001178492 A JP2001178492 A JP 2001178492A
Authority
JP
Japan
Prior art keywords
jellyfish
collagen
present
aquatic organisms
treatment
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
Application number
JP36904799A
Other languages
Japanese (ja)
Other versions
JP3696018B2 (en
Inventor
Michio Ikeda
理夫 池田
Etsuji Obe
悦二 大部
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toshiba Corp filed Critical Toshiba Corp
Priority to JP36904799A priority Critical patent/JP3696018B2/en
Publication of JP2001178492A publication Critical patent/JP2001178492A/en
Application granted granted Critical
Publication of JP3696018B2 publication Critical patent/JP3696018B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Enzymes And Modification Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

PROBLEM TO BE SOLVED: To attain rough extraction of the useful substances in jellyfish efficiently. SOLUTION: This crude extraction process for useful substances from jellyfishes comprises the first step in which the jellyfishes are crushed and shred into pieces, the second step in which the shred jellyfishes are decomposed and solubilized, and the third step in which the useful substance from the jellyfishes are roughly purified whereby the protease or collagen originating from the jellyfishes can be efficiently extracted.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、水生物例えばクラ
ゲから有用物質を抽出する方法に関する。
TECHNICAL FIELD The present invention relates to a method for extracting useful substances from aquatic organisms such as jellyfish.

【0002】[0002]

【従来の技術】臨海部の工場や発電所の多くは、冷却水
として海水を取水して利用している。しかし、特に夏期
には大量に発生し海中に浮遊するクラゲやウミウシ等の
水生物のために取水量の低下を余儀なくされている。
2. Description of the Related Art Many factories and power plants in the seaside use seawater as cooling water. However, especially in summer, a large amount of water organisms such as jellyfish and sea slugs floating in the sea are forced to reduce water intake.

【0003】取水口には異物やクラゲなどの海生物を取
り込むことを防ぐために、フェンス等で覆われている。
しかし、海中に浮遊する大量のクラゲは取水の流れに乗
って上記フェンスを塞ぎ、それに伴い取水口付近の水位
が下がるために、取水量を減らさなければならなくな
り、その結果として、取水量は低下し、当然、操業や発
電の効率を下げざるを得なくなってしまう。
[0003] The water intake is covered with a fence or the like in order to prevent ingestion of foreign matter or marine life such as jellyfish.
However, a large amount of jellyfish floating in the sea gets on the flow of water and closes the fence, and as a result the water level near the water intake drops, so the water intake must be reduced, and as a result, the water intake is reduced And of course, the efficiency of operations and power generation must be reduced.

【0004】そこで、操業・発電効率を維持するため
に、取水口に近付くクラゲを捕獲・除去し、取水量の確
保を図る必要がある。取水口近傍で捕獲・除去されるク
ラゲは、一般にその殆どがミズクラゲであり、食用に適
したビゼンクラゲ,エチゼンクラゲとその近縁種とは異
なるために、そのまま廃棄処理されることがほとんどで
あり、有効な再利用は図られていないのが実状である。
[0004] Therefore, in order to maintain the operation and power generation efficiency, it is necessary to capture and remove jellyfish approaching the water intake to secure a sufficient water intake. Most jellyfish that are caught and removed near the water intake are generally jellyfishes, and because they are different from edible jellyfish and Echizen jellyfish and their closely related species, they are generally discarded as they are. The fact is that no proper reuse has been attempted.

【0005】一方、クラゲを原料として有効利用を図る
事が、特開平6−217737号公報に開示されてい
る。これは、クラゲを粉砕して液状化あるいは細片とし
た後に、pH(4.0〜8.5)と温度調節(30〜3
5℃)を行い、次いで析出剤又は凝集剤を添加してタン
パク質を析出(凝集)した後、脱水を行い、さらに加熱
乾燥させることによりクラゲの有効利用を試みると言う
技術である。
[0005] On the other hand, Japanese Patent Application Laid-Open No. 6-217737 discloses an effective use of jellyfish as a raw material. This is because the jellyfish is pulverized into liquefied or fine pieces, and then pH (4.0 to 8.5) and temperature adjustment (30 to 3).
5 ° C.), then add a precipitant or coagulant to precipitate (aggregate) the protein, dehydrate it, and then heat dry it to try to use jellyfish effectively.

【0006】しかし、この様な技術においては、クラゲ
を粉砕あるいは細片化したのみで、有用物質の析出処理
→析出物の回収を行っているだけであり、クラゲの体成
分の大部分を含むタンパク質を分解・可溶化処理してい
ないため、処理系内に体成分のうち可溶化されていない
未反応部分も多く含まれてしまう。この様な未反応部分
は有用物質の抽出の効率を低下させる問題がある。さら
には、そのまま回収したタンパク質は飼料等として利用
することは可能であるが、クラゲより有用物質を得る技
術としては、必ずしも有効な技術であるとは言い難いの
が実状である。
[0006] However, in such a technique, only jellyfish is pulverized or crushed, and only a process of precipitating a useful substance → recovery of a precipitate is performed. Since the protein is not decomposed and solubilized, many unreacted unreacted parts of the body components are included in the treatment system. Such an unreacted portion has a problem of lowering the efficiency of extracting useful substances. Furthermore, the protein recovered as it is can be used as feed or the like, but it is difficult to say that it is necessarily an effective technique for obtaining a useful substance from jellyfish.

【0007】このような状況下、捕獲・除去されるクラ
ゲ類を効率よく処理し、かつ、有効な再利用を目指した
付加価値の高い有用物質の抽出技術の開発が求められて
いる。
[0007] Under these circumstances, there is a need for the development of a technology for extracting valuable substances with high added value that aims at efficiently treating jellyfish to be trapped and removed and for effective reuse.

【0008】[0008]

【発明が解決しようとする課題】従来のクラゲからの析
出物の回収方法では、たんぱく質を分解・可溶化処理し
ていなかったため可溶化されていない未反応部分も多く
生じ、有用物質の抽出の効率を低下させ、さらには回収
物も試料用のたんぱく質程度であり付加価値の低い有用
物質の抽出しかできなかった。
In the conventional method for recovering precipitates from jellyfish, since the protein has not been decomposed and solubilized, many unreacted portions remain unsolubilized, and the extraction efficiency of useful substances is increased. In addition, the recovered material was only a protein for a sample, and only useful substances with low added value could be extracted.

【0009】本発明は上記問題点に鑑みてなされたもの
で、未反応部分を少なくして有用物質の抽出の効率向上
を図り、しかも水生物由来の付加価値の高い有用物質を
回収する水生物の有用物質の抽出方法を提供することを
課題とする。
The present invention has been made in view of the above problems, and aims to improve the efficiency of extracting useful substances by reducing the unreacted portion, and to recover water-derived valuable added valuable substances derived from aquatic organisms. An object of the present invention is to provide a method for extracting useful substances.

【0010】[0010]

【課題を解決するための手段】上記課題を解決するため
に請求項1の水生物の有用物質の抽出方法は、水生物を
破砕・細断した断片にし前記水生物から酵素を遊離する
第1の工程と、この断片中のたんぱく質に前記酵素を作
用させ前記断片を分解して液状物質にする第2の工程
と、前記液状物質から有用物質を抽出する第3の工程と
を具備することを特徴とする。
In order to solve the above-mentioned problems, the method for extracting useful substances of aquatic organisms according to the first aspect of the present invention is a method of extracting enzymes from the aquatic organisms by fragmenting and shredding the aquatic organisms. And a second step of causing the enzyme to act on the protein in the fragment to decompose the fragment into a liquid substance, and a third step of extracting a useful substance from the liquid substance. Features.

【0011】本発明の骨子は、水生物の体内酵素を水生
物自体のタンパク質を分解するのに使用することにあ
る。そのために、体内酵素がタンパク質と混合された状
態で、体内酵素が活性化する条件例えば、温度、pH、
イオン強度等を所定の酵素活性可能条件に設定すること
で、タンパク質を分解する様にしている。
The gist of the present invention is to use enzymes in the body of aquatic organisms to degrade proteins of the aquatic organisms themselves. Therefore, in the state where the in-vivo enzyme is mixed with the protein, the conditions under which the in-vivo enzyme is activated, for example, temperature, pH,
The protein is decomposed by setting the ionic strength and the like to a predetermined enzyme activity enabling condition.

【0012】ここでの水生物とは、海水クラゲあるいは
淡水クラゲ以外の刺胞動物例えばイソギンチャク、サン
ゴ等、貝類例えば、貝、ウミウシ等、軟体動物例えば、
たこ類、イカ類等、甲殻類例えば、海老、カニ等でも同
様に本発明の処理方法によって有用物を抽出することが
可能である。
The term "aquatic organism" as used herein means a cnidarian other than seawater jellyfish or freshwater jellyfish, such as sea anemones and corals, shellfish such as shellfish, sea urchins, and mollusks such as sea urchins.
Similarly, useful substances can be extracted by the treatment method of the present invention from crustaceans such as octopus and squid, and crustaceans such as shrimp and crab.

【0013】請求項2の水生物の有用物質の抽出方法
は、請求項1において、前記酵素がアルカリプロテアー
ゼであることを特徴とする。この酵素は、水生物の体内
に存在する酵素を使用することが望ましいが、第2工程
で外部から添加しても良い。特に季節変動によって、水
生物細胞中の酵素含有量が低下している場合などには、
予め抽出しておいた酵素を添加することにより処理の効
率向上を図ることが出来る。
[0013] The method for extracting useful substances of aquatic organisms according to claim 2 is characterized in that in claim 1, the enzyme is an alkaline protease. As this enzyme, it is desirable to use an enzyme present in the body of aquatic organisms, but it may be added from the outside in the second step. Especially when the enzyme content in aquatic cells is decreasing due to seasonal fluctuations,
The efficiency of the treatment can be improved by adding the enzyme extracted in advance.

【0014】請求項3の水生物の有用物質の抽出方法
は、請求項1において、前記有用物質がコラーゲンであ
ることを特徴とする。
[0014] The method for extracting useful substances of aquatic organisms according to claim 3 is characterized in that, in claim 1, the useful substance is collagen.

【0015】[0015]

【発明の実施の形態】上述の目的は以下の本発明により
達成される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The above-mentioned object is achieved by the present invention described below.

【0016】本発明者らはクラゲ類、特に発電所や工場
用取水路で除去・水揚げされるミズクラゲ等の水生物に
含まれる有用物質の検索を行い、特にミズクラゲ等には
体内にアルカリプロテアーゼを多量に有することを見出
した。
The present inventors have searched for jellyfish, particularly useful substances contained in aquatic organisms such as water jellyfish which are removed and landed in water intakes for power plants and factories. It was found to have a large amount.

【0017】また、ミズクラゲには大量のコラーゲンが
含まれており、現在、実際に利用されている天然可溶性
コラーゲン、不溶性コラーゲン、および牛・豚の骨,皮
等を酸,アルカリ,酵素等で分解した可溶化コラーゲン
等が、2本の異種ポリペプチドさよりなるコラーゲンの
サブユニット構造(α1・α1・α2)を有し、かつ、
結合糖含有量が約1重量%結合したものであるのに対し
て、クラゲ類由来のコラーゲンは、3本の異種ポリペプ
チド鎖からなるラセン構造(サブユニット:α1・α2
・α3)を有しており、かつ、コラーゲン中には糖が3
〜5重量%以上結合しているという特徴的な構造を有
し、適度な保湿性と放湿性を維持しつつ、皮膚閉塞能を
有するため皮膚保水効果に優れている。本発明では、た
んぱく質を分解することでこの様な質の高いコラーゲン
を回収・抽出できる。
Moon jellyfish contains a large amount of collagen. Naturally soluble collagen, insoluble collagen, and bovine / pork bone and skin, which are actually used at present, are decomposed with acids, alkalis, enzymes and the like. The solubilized collagen or the like has a collagen subunit structure (α1, α1, α2) composed of two heterologous polypeptides, and
Collagen derived from jellyfish has a helical structure composed of three heterologous polypeptide chains (subunit: α1 · α2
・ Has α3) and collagen contains 3 sugars
It has a characteristic structure of being bound by 特 徴 5% by weight or more, and has an excellent skin water-retaining effect because it has skin occlusive ability while maintaining appropriate moisture retention and moisture release properties. In the present invention, such high-quality collagen can be recovered and extracted by decomposing proteins.

【0018】さて、ミズクラゲは、一般に体成分のうち
水分が95〜96%を占めているが、それ以外の成分と
しては、一般にはタンパク質1.7%,炭水化物0.9
%,脂質0.0%,灰分2.1%程度であり、水分以外
ではその殆どをタンパク質が占めている。このため、こ
のタンパク質部分を効率よく分解することにより、ミズ
クラゲを容易に分解することが可能となるわけである。
The moon jellyfish generally comprises 95 to 96% of water in the body components, but the other components are generally 1.7% protein and 0.9 carbohydrate.
%, Fat 0.0%, and ash content 2.1%, and most of them are proteins except water. For this reason, by efficiently decomposing this protein portion, it is possible to easily decompose moon jellyfish.

【0019】そこで、本発明者らは、上述のミズクラゲ
体内に含まれるアルカリプロテアーゼを有効に利用する
ことにより、ミズクラゲを効率よく分解・可溶化するこ
とにより、該プロテアーゼや前述のミズクラゲの体の構
成成分であるコラーゲン等の有用物質の抽出を極めて容
易にすることが可能となることを見出し、本発明の完成
に至った。
Therefore, the present inventors have made effective use of the above-mentioned alkaline protease contained in the jellyfish body to efficiently decompose and solubilize the jellyfish, thereby contributing to the structure of the body of the jellyfish jellyfish. They have found that it is possible to extremely easily extract useful substances such as collagen as a component, and have completed the present invention.

【0020】本発明の方法は、まず第1の工程としてク
ラゲを破砕・細断することにより、クラゲの体内に局在
化しているアルカリプロテアーゼを細胞内外へ遊離させ
ることが可能となる。次に、第1の工程に続いて第2の
工程として、破砕・細断したクラゲをクラゲ由来のアル
カリプロテアーゼが好適に作用する条件下で処理するこ
とにより、クラゲの体成分を極めて短時間に容易に分解
・可溶化することが可能となる。すなわち、第1工程で
クラゲから遊離したプロテアーゼの作用により、クラゲ
の構造維持に関わるタンパク質を加水分解し、クラゲを
分解・可溶化するわけである。さらに第2工程に続い
て、第3の工程として、ミズクラゲを分解・可溶化した
液体からアルカリプロテアーゼやコラーゲン等の有用物
質を粗抽出する。以上三工程を具備することを特徴とし
ている。
In the method of the present invention, the jellyfish is first crushed and shredded as a first step, so that the alkaline protease localized in the body of the jellyfish can be released into and out of the cell. Next, as a second step following the first step, the jellyfish body components are treated in an extremely short time by treating the crushed and shredded jellyfish under conditions in which the jellyfish-derived alkaline protease suitably acts. It can be easily decomposed and solubilized. That is, by the action of the protease released from the jellyfish in the first step, the protein involved in maintaining the structure of the jellyfish is hydrolyzed to decompose and solubilize the jellyfish. Further, following the second step, as a third step, crude substances such as alkaline protease and collagen are roughly extracted from the liquid obtained by decomposing and solubilizing the moon jellyfish. It is characterized by comprising the above three steps.

【0021】本発明の第1工程におけるミズクラゲの破
砕・細断方法としては、ミズクラゲを効率よく破砕・細
断可能な方法であれば如何なる方法を採用することも可
能であり、例えば2軸破砕機やシュレッダー装置等を利
用することが可能である。
As a method of crushing and shredding water jellyfish in the first step of the present invention, any method can be employed as long as it can efficiently crush and shred water jellyfish, for example, a biaxial crusher. And a shredder device can be used.

【0022】本発明の第2工程は、第1工程で破砕・細
断されたクラゲについて、あるいは、破砕・細断された
クラゲと水系媒体を混合し、クラゲ由来のプロテアーゼ
を効率よく作用させることによってクラゲを分解・可溶
化するものである。本工程に於いては分解・可溶化処理
における温度,pH,クラゲ負荷量をクラゲ由来のプロ
テアーゼ処理を好適に行える条件範囲内に制御すること
により、数時間〜半日でクラゲを分解・可溶化すること
が可能となる。また、上記の様な分解・可溶化処理条件
を制御することにより、処理終了後の可溶化処理液中に
於けるアルカリプロテアーゼの活性を高いままに維持
し、さらに、該処理液中のコラーゲンを損なうことな
く、各々可溶化したままで第3工程である粗抽出工程へ
送ることが可能となる。このため、第2工程の後段で煩
雑な前処理を行うことなく、第3工程の粗抽出処理を実
施することが可能となる。
In the second step of the present invention, the jellyfish crushed and shredded in the first step, or the crushed and shredded jellyfish and an aqueous medium are mixed to allow the jellyfish-derived protease to act efficiently. It decomposes and solubilizes jellyfish. In this step, the jellyfish is decomposed and solubilized within several hours to half a day by controlling the temperature, pH, and jellyfish load in the decomposition / solubilization treatment within a range in which the jellyfish-derived protease treatment can be suitably performed. It becomes possible. Further, by controlling the decomposition / solubilization treatment conditions as described above, the activity of the alkaline protease in the solubilization treatment solution after the treatment is maintained at a high level, and the collagen in the treatment solution is further reduced. Without any loss, it is possible to send each solubilized state to the crude extraction step, which is the third step. For this reason, it is possible to perform the rough extraction processing of the third step without performing complicated pretreatment at the subsequent stage of the second step.

【0023】ここで、本発明における可溶化とは、溶媒
にほぼ完全に溶解した状態を指すものであり、単に微細
細片が拡散しただけで液体様になっている状態のことを
指すものではない。
Here, the solubilization in the present invention refers to a state in which it is almost completely dissolved in a solvent, and does not refer to a state in which the fine flakes are in a liquid state only by diffusion. Absent.

【0024】第2工程における処理条件としては、ま
ず、温度条件としては、20℃〜50℃の範囲で目的と
する有用物質に影響を与えない条件を設定することが出
来る。例えば、好ましくは25℃〜45℃、特に30℃
付近27℃〜37℃が好ましい。つづいて、pH条件
は、6〜12、好ましくは7〜11、特に10付近8〜
10.5が好ましい。また、分解・可溶化処理槽内の反
応を均一に進めるために、処理液は撹拌することが望ま
しい。撹拌の条件は、本発明における分解・可溶化処理
を好適に行える条件であれば良く、反応槽の形状やクラ
ゲの負荷量等により随時好適な条件で設定することが可
能である。
As the processing conditions in the second step, first, as the temperature conditions, conditions that do not affect the intended useful substance can be set in the range of 20 ° C. to 50 ° C. For example, preferably 25 ° C to 45 ° C, especially 30 ° C
A neighborhood of 27 ° C to 37 ° C is preferred. Subsequently, the pH conditions are from 6 to 12, preferably from 7 to 11, and especially from around 10 to 8 to
10.5 is preferred. Further, it is desirable to stir the treatment liquid in order to promote the reaction in the decomposition / solubilization treatment tank uniformly. The stirring conditions may be any conditions under which the decomposition / solubilization treatment in the present invention can be suitably performed, and can be set as appropriate at any time according to the shape of the reaction tank, the load of the jellyfish, and the like.

【0025】第3の工程における有用物質の粗抽出方法
は、該第2工程で分解・可溶化したクラゲ可溶化液から
目的の有用物質を効率良く粗抽出可能であれば、いかな
る方法を用いても良く、例えば塩析,有機溶媒による沈
殿法,等電点沈殿,水溶性高分子を用いた沈殿法,遠心
法,限外濾過法,膜濾過法,イオン交換クラマトグラフ
ィー,吸着クロマトグラフィー,分配クロマトグラフィ
ー,ゲル濾過クロマトグラフィー,アフィニティークロ
マトグラフィー,等電点クロマトグラフィー等の方法を
抽出対象や処理条件等によって適宜選択することが出来
る。
The method of crude extraction of a useful substance in the third step is carried out by any method as long as the target useful substance can be efficiently crudely extracted from the jellyfish solubilized solution decomposed and solubilized in the second step. For example, salting out, precipitation with an organic solvent, isoelectric precipitation, precipitation with a water-soluble polymer, centrifugation, ultrafiltration, membrane filtration, ion exchange chromatography, adsorption chromatography, distribution Methods such as chromatography, gel filtration chromatography, affinity chromatography, and isoelectric focusing can be appropriately selected depending on the extraction target, processing conditions, and the like.

【0026】本発明の水生物由来の有用物質の抽出方法
は、以上の三工程を具備することを特徴としている。本
発明の水生物由来の有用物質の抽出方法の工程のフロー
チャートを図1に示す。1は破断・細断化工程、2は分
解・可溶化工程、3は有用物質粗抽出工程、4は有用物
質の抽出であり、本発明は以上の工程の順番にて行う。
The method for extracting useful substances derived from aquatic organisms according to the present invention is characterized by comprising the above three steps. FIG. 1 shows a flowchart of the steps of the method for extracting a useful substance derived from aquatic organisms of the present invention. 1 is a breaking / shredding step, 2 is a decomposing / solubilizing step, 3 is a rough extraction step of a useful substance, and 4 is an extraction of a useful substance. The present invention is carried out in the order of the above steps.

【0027】[0027]

【実施例】以下、例示的ではあるが限定的ではない実施
例を説明することによって本発明をより深く理解するこ
とができる。 (実施例1)図2に示すような処理装置を作製し、試験
を行った。4は撹拌翼モーター、21はクラゲ破砕装
置、22は分解・可溶化処理槽、23は粗抽出装置(限
外濾過装置)、25は加熱装置、26は送液ポンプ、2
7はバルブである。水1mを添加した内容積3m
処理槽に、ミズクラゲ200kgを破砕・細断装置を経
て破砕・細断してミズクラゲの断片を形成した後、25
℃恒温下,120rpmの条件下で撹拌処理を行った。
The invention can be better understood by describing the following illustrative but non-limiting examples. (Example 1) A processing apparatus as shown in FIG. 2 was manufactured and tested. 4 is a stirring blade motor, 21 is a jellyfish crusher, 22 is a decomposition / solubilization tank, 23 is a coarse extraction device (ultrafiltration device), 25 is a heating device, 26 is a liquid sending pump,
7 is a valve. A treatment tank having an inner volume of 3m 3 of water was added 1 m 3, after forming a fragment of Aurelia by crushing and shredding through the crushing and shredding device Aurelia 200 kg, 25
The stirring treatment was performed at a constant temperature of 120 ° C. and a constant temperature of 120 ° C.

【0028】15時間後に処理液を濾過し、濾紙上の残
さ重量を測定した。結果を表1に示す。ここでは、処理
液についてプロテアーゼ活性を測定した。サンプリング
はn=3で行い、試験は3回繰り返し実施した。この実
施例によって、有用物質として酵素、即ちミズクラゲの
たんぱく質を分解する酵素の一種であるアルカリプロテ
アーゼを遊離して抽出することができる。 (比較例1)水1mを添加した内容積3mの処理槽
に、ミズクラゲ200kgを細片化したものを添加し
た。これを濾過し、膜上の残さ重量を測定した。結果を
表1に示す。また、濾液についてプロテアーゼ活性を測
定した。結果を表1に示す。
After 15 hours, the treatment liquid was filtered, and the weight of the residue on the filter paper was measured. Table 1 shows the results. Here, protease activity was measured for the treatment solution. Sampling was performed with n = 3, and the test was repeated three times. According to this embodiment, an enzyme as a useful substance, that is, an alkaline protease which is a kind of an enzyme for decomposing proteins of moon jellyfish can be released and extracted. A treatment tank (Comparative Example 1) internal volume 3m 3 of water was added 1 m 3, was added as a Aurelia 200kg was minced. This was filtered and the residue weight on the membrane was measured. Table 1 shows the results. In addition, protease activity was measured for the filtrate. Table 1 shows the results.

【0029】重量測定終了後、残さを濾過した処理液に
戻し、硫酸アンモニウムを用いて塩析を行い、タンパク
質を析出させた後、遠沈により上清と分離して回収し
た。これを37℃で乾燥させることにより脱水処理を行
った。
After completion of the weight measurement, the residue was returned to the filtered solution, salted out using ammonium sulfate to precipitate the protein, and separated from the supernatant by centrifugation and collected. This was dried at 37 ° C. to perform a dehydration treatment.

【0030】脱水処理後、再度該回収タンパク質を含む
物質を蒸留水に懸濁し、透析処理を行った後にプロテア
ーゼ活性を測定した。その結果、この様にして得られた
タンパク質にはプロテアーゼ活性は検出されなかった。
サンプリングはn=2で行い、試験は3回繰り返し実施
した。 (比較例2)水1mを添加した内容積3mの処理槽
に、ミズクラゲ200kgを細断した後添加し、オート
クレーブ滅菌後25℃恒温下,120rpm条件下で振
盪した。15時間後に処理液を濾過し、膜上の残さ重量
を測定した。結果を表1に示す。また、処理液について
プロテアーゼ活性を測定した。結果を表1に示す。試験
はn=2で行い、3回繰り返し実施した。
After the dehydration treatment, the substance containing the recovered protein was suspended again in distilled water, dialyzed, and the protease activity was measured. As a result, no protease activity was detected in the protein thus obtained.
Sampling was performed at n = 2, and the test was repeated three times. (Comparative Example 2) 200 kg of moon jellyfish was added to a treatment tank having an internal volume of 3 m 3 to which 1 m 3 of water had been added, and shredded. The mixture was sterilized in an autoclave, and shaken at 120 ° C under a constant temperature of 25 ° C. After 15 hours, the treatment liquid was filtered, and the weight of the residue on the membrane was measured. Table 1 shows the results. In addition, protease activity was measured for the treatment solution. Table 1 shows the results. The test was performed with n = 2, and was repeated three times.

【表1】 以上の実施例1では有用物質である酵素を大幅に抽出す
ることが出来る。つまり、従来水生物を破断するだけで
も多少の酵素を取り出すことは出来たが、取り出した酵
素を本実施例のように酵素が作用する最適条件に設定し
て海生物の組織、例えば細胞に直接作用させタンパク質
を分解して水生物の細胞を壊すことで、細胞内に閉じこ
められていた酵素を大量に放出させることができためと
考えられる。 (実施例2)以下の実施例の説明では、実施例1と同一
工程あるいは同一条件、同一装置の説明等については説
明の重複を避けた。
[Table 1] In Example 1 described above, the enzyme, which is a useful substance, can be significantly extracted. In other words, although some enzymes could be taken out by simply breaking water organisms in the past, the taken-out enzymes were set to the optimal conditions under which the enzymes act as in the present example, and were directly applied to tissues of sea organisms, for example, cells. It is thought that by acting on the protein to break down the cells of aquatic organisms, a large amount of enzymes trapped in the cells can be released. (Embodiment 2) In the following description of the embodiment, repetition of the same steps, the same conditions, the same apparatus, and the like as in the first embodiment will be avoided.

【0031】本実施例では、酵素を作用させるpH条件
を変え、より最適な条件を探索した。実施例1の処理液
のプロテアーゼ活性を、異なるpH条件下で測定した。
それ以外は実施例1と同様にして海生物から有用物の回
収を図った。測定結果を図3に示す。
In the present example, more optimum conditions were searched for by changing the pH conditions under which the enzyme acts. The protease activity of the treatment solution of Example 1 was measured under different pH conditions.
Otherwise, the recovery of useful substances from marine organisms was attempted in the same manner as in Example 1. FIG. 3 shows the measurement results.

【0032】図中30は100mMリン酸緩衝液を使用
した場合、31は50mMホウ酸塩化カリウム緩衝液を
使用した場合、32は100mMグリシン塩化ナトリウ
ム水酸化ナトリウム緩衝液を使用した場合である。
In the figure, 30 is the case where a 100 mM phosphate buffer was used, 31 is the case where a 50 mM potassium borate buffer was used, and 32 is the case where a 100 mM glycine sodium chloride sodium hydroxide buffer was used.

【0033】試験はn=2で行い、3回繰り返し実施し
た。 (実施例3)この実施例3は酵素を活性化させる条件と
して温度を種々変えて、最もタンパク質を分解させる効
率の高い温度条件を探索した。そして、望ましい温度条
件によって第2工程を実施した以外は、実施例1と同様
に行った。温度の設定については、ヒーター25を使用
した。
The test was performed with n = 2, and was repeated three times. (Example 3) In Example 3, various temperatures were used as conditions for activating the enzyme, and a temperature condition with the highest efficiency for decomposing proteins was searched for. And it carried out similarly to Example 1 except having performed the 2nd process on desirable temperature conditions. The heater 25 was used for setting the temperature.

【0034】分解・可溶化処理時の温度を25℃,35
℃,45℃,55℃および65℃の5つの温度設定で行
った以外は、実施例1と同様の振盪処理を行った。振盪
処理後、各々の処理液のプロテアーゼ活性を測定した。
結果を図4に示す。
The temperature for the decomposition and solubilization treatment is 25 ° C., 35
The same shaking treatment as in Example 1 was performed, except that the temperature was set at five temperature settings of ° C, 45 ° C, 55 ° C, and 65 ° C. After the shaking treatment, the protease activity of each treatment solution was measured.
FIG. 4 shows the results.

【0035】サンプリングはn=5で行い、試験は3回
繰り返し実施した。 (実施例4)実施例4は実施例1で抽出した最終処理液
から抽出する有用物の種類をコラーゲンとした実施例で
ある。その点以外は実施例1と同一である。
The sampling was performed at n = 5, and the test was repeated three times. (Example 4) Example 4 is an example in which the type of useful substance extracted from the final treatment solution extracted in Example 1 was collagen. The other points are the same as the first embodiment.

【0036】滅菌蒸留水100mLを添加した内容積5
00mLの三角フラスコに、クラゲ20gを破砕したも
のを添加し、35℃条件下120rpm条件下で5時間
振盪した。
[0036] Inner volume 5 with 100 mL of sterile distilled water added
A crushed jellyfish (20 g) was added to a 00 mL Erlenmeyer flask, and shaken at 35 ° C. and 120 rpm for 5 hours.

【0037】その結果、クラゲは分解・可溶化された。
この可溶化処理液50mLを限外濾過膜を用いて分画分
子量3×10で分画した濾液をさらに限外濾過膜によ
り分画分子量1×10することによりコラーゲンの粗
抽出を行った。限外濾過後のサンプルからコラーゲンの
抽出を試みた結果、最大でクラゲ質重量の3重量%程度
のコラーゲンを抽出することが可能であった。抽出スキ
ームを図4に示す。 (比較例3)クラゲ10gから常法によりコラーゲンの
抽出を行った。その結果、最大でクラゲ重量の2.8重
量%程度のコラーゲンを抽出された。抽出スキームを図
5に示す。50は比較例5におけるコラーゲンの抽出処
理のフローチャートを示すもので、51は洗浄工程、5
2は脱脂工程、53はペプシンによる消化工程、54は
塩析工程、55は緩衝液を使用した透析工程、56は酢
酸を使用した透析工程である。また、60は実施例5に
おけるコラーゲンの抽出処理のフローチャートを示すも
ので、61は脱脂工程、62はペプシンによる消化工
程、63は塩析工程、64は緩衝液を使用した透析工
程、65は酢酸を使用した透析工程を夫々示している。
As a result, the jellyfish was decomposed and solubilized.
The filtrate obtained by fractionating 50 mL of the solubilized solution with an ultrafiltration membrane with a molecular weight cutoff of 3 × 10 5 was further subjected to a molecular weight cutoff of 1 × 10 4 with an ultrafiltration membrane to perform crude extraction of collagen. . As a result of attempting to extract collagen from the sample after ultrafiltration, it was possible to extract collagen of up to about 3% by weight of jellyfish weight. The extraction scheme is shown in FIG. (Comparative Example 3) Collagen was extracted from 10 g of jellyfish by a conventional method. As a result, collagen of up to about 2.8% by weight of the jellyfish weight was extracted. The extraction scheme is shown in FIG. 50 shows a flowchart of a collagen extraction process in Comparative Example 5, and 51 shows a washing step, 5
2 is a defatting step, 53 is a pepsin digestion step, 54 is a salting-out step, 55 is a dialysis step using a buffer, and 56 is a dialysis step using acetic acid. 60 is a flow chart of the collagen extraction process in Example 5, 61 is a delipidation step, 62 is a pepsin digestion step, 63 is a salting-out step, 64 is a dialysis step using a buffer, and 65 is acetic acid. Each shows the dialysis process using.

【0038】実施例1と比較例1,比較例2の結果、お
よび、実施例4と比較例3の結果より、本発明の水生物
由来の有用物質の抽出方法を用いれば、水生物由来のプ
ロテアーゼを効率よく活用することにより、従来提案さ
れてた技術に比べ、効率よくクラゲ有用物質を粗抽出す
ることが可能となることを容易に理解できる。また、実
施例2,3の結果より、本発明の好適な処理条件範囲を
容易に理解することができる。
From the results of Example 1 and Comparative Examples 1 and 2, and from the results of Example 4 and Comparative Example 3, if the method for extracting useful substances derived from aquatic organisms of the present invention is used, It can be easily understood that the efficient use of protease makes it possible to extract crude jellyfish useful substances more efficiently than conventionally proposed techniques. Further, from the results of Examples 2 and 3, the suitable processing condition range of the present invention can be easily understood.

【0039】[0039]

【発明の効果】以上説明したように、本発明によれば未
反応部分を少なくして有用物質の抽出の効率向上がで
き、しかも水生物由来の付加価値の高い有用物質を回収
できる。
As described above, according to the present invention, the efficiency of extraction of a useful substance can be improved by reducing the unreacted portion, and a valuable added substance derived from aquatic organisms can be recovered.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明におけるクラゲ由来の有用物質の抽出法
の工程を示すフローチャート
FIG. 1 is a flowchart showing steps of a method for extracting a jellyfish-derived useful substance according to the present invention.

【図2】本発明の実施例1に用いた試験装置の模式図FIG. 2 is a schematic view of a test apparatus used in Example 1 of the present invention.

【図3】本発明の実施例2における好適な結果を示すグ
ラフ
FIG. 3 is a graph showing preferable results in Example 2 of the present invention.

【図4】本発明の実施例3における好適な結果を示すグ
ラフ
FIG. 4 is a graph showing preferable results in Example 3 of the present invention.

【図5】本発明の実施例5と比較例4におけるコラーゲ
ンの抽出処理のフローチャート
FIG. 5 is a flowchart of collagen extraction processing in Example 5 and Comparative Example 4 of the present invention.

【符号の説明】[Explanation of symbols]

4 撹拌翼モーター 21 クラゲ破砕装置 22 分解・可溶化処理槽 23 粗抽出装置(限外濾過装置) 25 加熱装置 26 送液ポンプ 27 バルブ 4 Stirring blade motor 21 Jellyfish crusher 22 Decomposition / solubilization tank 23 Coarse extraction device (Ultrafiltration device) 25 Heating device 26 Liquid feed pump 27 Valve

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4B029 AA02 DA01 DB01 4B050 CC01 DD11 LL05 4B064 AG01 CA21 CD21 CE02 DA16 4D056 AB12 AB20 AC22 BA08 CA06 CA22 DA01  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4B029 AA02 DA01 DB01 4B050 CC01 DD11 LL05 4B064 AG01 CA21 CD21 CE02 DA16 4D056 AB12 AB20 AC22 BA08 CA06 CA22 DA01

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】水生物を破砕・細断して断片にし前記水生
物から酵素を遊離する第1の工程と、この断片中のたん
ぱく質に前記酵素を作用させ前記断片を分解して液状物
質にする第2の工程と、前記液状物質から有用物質を抽
出する第3の工程とを具備することを特徴とする水生物
の有用物質の抽出方法。
1. A first step of crushing and shredding aquatic organisms into fragments to release enzymes from the aquatic organisms, and the enzyme acting on proteins in the fragments to decompose the fragments into liquid substances A method for extracting useful substances from aquatic organisms, comprising: a second step of extracting useful substances from the liquid substance.
【請求項2】前記酵素がアルカリプロテアーゼであるこ
とを特徴とする請求項1に記載の水生物の有用物質の抽
出方法。
2. The method for extracting useful substances of aquatic organisms according to claim 1, wherein the enzyme is an alkaline protease.
【請求項3】前記有用物質がコラーゲンであることを特
徴とする請求項1に記載の水生物の有用物質の抽出方
法。
3. The method according to claim 1, wherein the useful substance is collagen.
JP36904799A 1999-12-27 1999-12-27 Extracting Jellyfish Collagen Expired - Fee Related JP3696018B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP36904799A JP3696018B2 (en) 1999-12-27 1999-12-27 Extracting Jellyfish Collagen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP36904799A JP3696018B2 (en) 1999-12-27 1999-12-27 Extracting Jellyfish Collagen

Publications (2)

Publication Number Publication Date
JP2001178492A true JP2001178492A (en) 2001-07-03
JP3696018B2 JP3696018B2 (en) 2005-09-14

Family

ID=18493431

Family Applications (1)

Application Number Title Priority Date Filing Date
JP36904799A Expired - Fee Related JP3696018B2 (en) 1999-12-27 1999-12-27 Extracting Jellyfish Collagen

Country Status (1)

Country Link
JP (1) JP3696018B2 (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007020889A1 (en) 2005-08-12 2007-02-22 Riken Novel mucin glycoprotein and use thereof
JP2007051191A (en) * 2005-08-17 2007-03-01 Fukui Prefecture Method for recovering collagen from jellyfish
JP2008031106A (en) * 2006-07-28 2008-02-14 Fukui Prefectural Univ Method for recovering collagen from jellyfish
JP2011116672A (en) * 2009-12-01 2011-06-16 Kyoei Kagaku Kogyo Kk Skin care preparation
JP2011520927A (en) * 2008-05-20 2011-07-21 ▲張▼▲麗▼▲麗▼ Collagen peptide with immunity-enhancing activity derived from the yellow jellyfish and its preparation and use
CN102392010A (en) * 2011-12-02 2012-03-28 华南农业大学 Protease extracted by using squid viscera as raw materials and extraction method and application thereof
CN103549121A (en) * 2013-11-13 2014-02-05 朱勤 Method for preparing protein peptide by carrying out enzymolysis on marine low-value small fishes by squid visceral enzyme
WO2014030323A1 (en) 2012-08-23 2014-02-27 株式会社海月研究所 Method for fractionally extracting mucin and collagen
CN103931735A (en) * 2014-04-23 2014-07-23 昆山市富众网络科技有限公司 Mechanical filter of enzymatic hydrolysis pool for crab shell
CN106632668A (en) * 2017-01-13 2017-05-10 上海华惠海洋生物科技有限公司 Preparation method and application of sleeve-fish collagen polypeptide and iron complex thereof
US20180327799A1 (en) * 2017-05-10 2018-11-15 Robert den Hoed Method of producing jellyfish collagen extract
CN110129292A (en) * 2019-04-24 2019-08-16 赖鹏 A kind of Rosa roxburghii Tratt SOD extracting method and device
CN112931306A (en) * 2021-01-26 2021-06-11 浙江省海洋水产研究所 Lissajous transplanting device for attracting cephalopoda to lay eggs

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102092572B1 (en) * 2019-10-30 2020-03-25 이수지 an ecofriendly bio-plastic using a jellyfish and the ecofriendly bio-plastic
KR102225152B1 (en) * 2020-09-08 2021-03-09 박진목 Color changing soap composition

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007020889A1 (en) 2005-08-12 2007-02-22 Riken Novel mucin glycoprotein and use thereof
US7829679B2 (en) 2005-08-12 2010-11-09 Riken Mucin-type glycoprotein and use thereof
JP2007051191A (en) * 2005-08-17 2007-03-01 Fukui Prefecture Method for recovering collagen from jellyfish
JP2008031106A (en) * 2006-07-28 2008-02-14 Fukui Prefectural Univ Method for recovering collagen from jellyfish
JP2011520927A (en) * 2008-05-20 2011-07-21 ▲張▼▲麗▼▲麗▼ Collagen peptide with immunity-enhancing activity derived from the yellow jellyfish and its preparation and use
JP2011116672A (en) * 2009-12-01 2011-06-16 Kyoei Kagaku Kogyo Kk Skin care preparation
CN102392010A (en) * 2011-12-02 2012-03-28 华南农业大学 Protease extracted by using squid viscera as raw materials and extraction method and application thereof
KR20150042151A (en) 2012-08-23 2015-04-20 가부시키가이샤 구라게 겡큐쇼 Method for fractionally extracting mucin and collagen
WO2014030323A1 (en) 2012-08-23 2014-02-27 株式会社海月研究所 Method for fractionally extracting mucin and collagen
CN103549121A (en) * 2013-11-13 2014-02-05 朱勤 Method for preparing protein peptide by carrying out enzymolysis on marine low-value small fishes by squid visceral enzyme
CN103931735A (en) * 2014-04-23 2014-07-23 昆山市富众网络科技有限公司 Mechanical filter of enzymatic hydrolysis pool for crab shell
CN103931735B (en) * 2014-04-23 2015-07-29 昆山市富众网络科技有限公司 The mechanical filtration device in Carapax Eriocheir sinensis enzymolysis pond
CN106632668A (en) * 2017-01-13 2017-05-10 上海华惠海洋生物科技有限公司 Preparation method and application of sleeve-fish collagen polypeptide and iron complex thereof
CN106632668B (en) * 2017-01-13 2020-04-14 上海华惠海洋生物科技有限公司 Squid collagen polypeptide and preparation method and application of iron complex thereof
US20180327799A1 (en) * 2017-05-10 2018-11-15 Robert den Hoed Method of producing jellyfish collagen extract
US11060122B2 (en) * 2017-05-10 2021-07-13 Robert den Hoed Method of producing jellyfish collagen extract
CN110129292A (en) * 2019-04-24 2019-08-16 赖鹏 A kind of Rosa roxburghii Tratt SOD extracting method and device
CN110129292B (en) * 2019-04-24 2023-05-26 赖鹏 Rosa roxburghii SOD extraction method and device
CN112931306A (en) * 2021-01-26 2021-06-11 浙江省海洋水产研究所 Lissajous transplanting device for attracting cephalopoda to lay eggs
CN112931306B (en) * 2021-01-26 2022-04-05 浙江省海洋水产研究所 Lissajous transplanting device for attracting cephalopoda to lay eggs

Also Published As

Publication number Publication date
JP3696018B2 (en) 2005-09-14

Similar Documents

Publication Publication Date Title
JP2001178492A (en) Method of extracting useful substance from aquatic life
JPS6283849A (en) Method of purifying collagen
JP2722014B2 (en) Method for extracting natural collagen from pigment-free fish skin, natural collagen obtained from pigment-free fish skin and biomaterial
CN106967169B (en) Extraction method of fish collagen
US5840848A (en) Method for preparation of type II collagen
KR101871395B1 (en) Method for production collagen with high yield
CN1478421A (en) Seacucumbus whole powder food and its preparation method
CN114957386B (en) Method for producing collagen tripeptide from fish scales
US4363760A (en) Partially hydrolyzed elastin from limed hide trimmings
KR100679712B1 (en) Process for preparing collagen from starfish
WO2005027657A1 (en) Process for producing protein hydrolysate and protein hydrolysate
JPH05125100A (en) High-purity pepsin soluble scale collagen and its production
US4879375A (en) Preparation of hyaluronic acid from synovial fluid
US20060014256A1 (en) Sodium chondroitin sulfate, chondroitin-sulfate-containing material and processes for producing the same
CN103740793B (en) A kind of method of producing collagen of fish skin
JP2004300109A (en) Method for producing animal protein, production apparatus and animal protein
JP2013014529A (en) Type ii collagen obtained from notochord of sturgeons by simple extraction method
CN107815480A (en) With the method for catfish fish guts protease extraction collagen
JP2004083451A (en) Skin lotion
JP3155746B1 (en) Method for producing type II collagen
JPH10215809A (en) Manufacture of fermented seasoning
CN113603768B (en) Preparation method of fish-source collagen
CN110759969B (en) Preparation method of antioxidant enzymolysis oligopeptide from peripherical glands of northern pacific squid
JP4239143B2 (en) Method for producing non-bovine modified collagen
CN116554304A (en) Collagen and purification method, extraction method and application thereof

Legal Events

Date Code Title Description
A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050107

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050307

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050329

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20050414

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050530

RD04 Notification of resignation of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7424

Effective date: 20050606

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050621

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050628

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090708

Year of fee payment: 4

LAPS Cancellation because of no payment of annual fees