JP5252623B2 - Extraction method of proteoglycan - Google Patents

Extraction method of proteoglycan Download PDF

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JP5252623B2
JP5252623B2 JP2008011296A JP2008011296A JP5252623B2 JP 5252623 B2 JP5252623 B2 JP 5252623B2 JP 2008011296 A JP2008011296 A JP 2008011296A JP 2008011296 A JP2008011296 A JP 2008011296A JP 5252623 B2 JP5252623 B2 JP 5252623B2
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proteoglycan
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陽治 加藤
聖子 伊藤
重光 工藤
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Hirosaki University NUC
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本発明は、水棲動物組織、就中大量に廃棄されている魚類頭部からプロテオグリカンを抽出回収する方法に関するものである。   The present invention relates to a method for extracting and recovering proteoglycans from aquatic animal tissues, especially fish heads that are discarded in large quantities.

プロテオグリカンは、古くは哺乳動物軟骨に含まれるものを抽出分離していたが、牛のBSE発症が報告されてから、水産動物組織のプロテオグリカンを抽出分離することが行われてきた。鯨やサメの軟骨に含まれるプロテオグリカンの抽出はすでに行われているが、原料となる動物の捕獲量に限りがあり、プロテオグリカンの生産量が制限されている。さらに抽出分離操作が複雑であり、抽出の際に使用する溶媒は食品に適さないものが使われることが多く、製品の用途に制限が加えられ高価格になっている。   In the past, proteoglycans were extracted and separated from those contained in mammalian cartilage. However, since the occurrence of BSE in cattle has been reported, extraction and separation of proteoglycans from aquatic animal tissues has been performed. Extraction of proteoglycans contained in whale and shark cartilage has already been carried out, but the amount of animals that can be used as raw materials is limited, and the production of proteoglycans is limited. Furthermore, the extraction and separation operation is complicated, and the solvent used for the extraction is often unsuitable for food, and the use of the product is limited and the price is high.

動物組織に含まれるプロテオグリカンを抽出する方法にはいろいろあるが、抽出に際して加熱操作を加える方法では、調製されたプロテオグリカンに分解が起きて低分子化したものが多く含まれている。プロテアーゼ阻害剤を添加し加水分解を防ぐ抽出法では、回収率が悪く、組織に含まれる各種成分が混入してそれを除くための複雑な操作が必要となり、抽出コストに大きく影響している。これまで市販されている製品では製造方法が複雑であり、非常に高価なものとなっている。さらに、酢酸やアルカリのような特殊な抽出溶媒を使用するため、製品に残留した溶媒の異臭が残り、医療用など利用範囲が制限され、プロテオグリカンの持つ健康機能を引き出した方面での利用は閉ざされている。   There are various methods for extracting proteoglycans contained in animal tissues, but many methods in which the proteoglycans prepared are decomposed and reduced in molecular weight in the methods in which a heating operation is performed during extraction. In the extraction method in which a protease inhibitor is added to prevent hydrolysis, the recovery rate is poor, and various operations contained in the tissue are mixed and complicated operations are required to remove it, which greatly affects the extraction cost. The products that have been marketed so far have complicated manufacturing methods and are very expensive. In addition, because a special extraction solvent such as acetic acid or alkali is used, the odor of the solvent remaining in the product remains, limiting the range of use such as medical use, and the use of the proteoglycan's health functions is closed. It is.

また、動物はそれぞれ特有の体臭を有しており、動物から組織を取り出したときには必ず体臭やそれの変質した臭いが組織に付着している。ある時にはその臭いが好ましいものとなることもあるが、多くの場合は臭いがあることは望ましいものではない。動物の体臭は痕跡量で感じるために完全に除かなければならない。さらに体臭は油に溶けやすいものが多く組織を取り出し、精製の過程で脱臭操作を加えても、微量の脂肪分の残留により完全な脱臭は非常に困難である。
特に魚類から分離抽出した場合に付着する異臭を除去するためには各種の極性および非極性の溶媒を多量に使用したり、超臨界抽出など特別な装置を用いたりする必要がある。これら溶媒を使用する場合には食品に使用できないものが多く、食品に使用可能な溶媒は効力が低く、使用条件を厳密に設定して使用しないときは十分な効果を得ることができない。
Moreover, each animal has a peculiar body odor, and whenever a tissue is taken out from the animal, a body odor or a modified odor is attached to the tissue. Sometimes the odor may be desirable, but in many cases it is not desirable. The animal's body odor must be completely removed to feel in trace amounts. In addition, many body odors are easily dissolved in oil, and even if the tissue is taken out and deodorized during the purification process, complete deodorization is very difficult due to the residual trace amount of fat.
In particular, in order to remove the off-flavor attached when separated and extracted from fish, it is necessary to use a large amount of various polar and non-polar solvents or to use a special apparatus such as supercritical extraction. When these solvents are used, many of them cannot be used for foods. Solvents that can be used for foods have low efficacy, and a sufficient effect cannot be obtained when the use conditions are set strictly and are not used.

WO2004/083275には、軟骨魚類由来の軟骨を粉砕し、水を加えて水溶性成分を抽出し、水層を分離し、アルコールを加えて沈殿物を得てプロテオグリカンを製造する方法が開示されている。しかしながら、この方法は、脂質を多く含む軟骨原料からプロテオグリカンと脂肪分を完全に分離することは困難であり、魚臭が残るという問題がある。   WO 2004/083275 discloses a method for producing a proteoglycan by pulverizing cartilage derived from cartilaginous fish, adding water to extract a water-soluble component, separating an aqueous layer, adding an alcohol to obtain a precipitate. Yes. However, this method has a problem that it is difficult to completely separate proteoglycan and fat from a cartilage raw material containing a large amount of lipid, and a fishy odor remains.

WO2004/083257WO2004 / 083257

本発明の目的は、大量に漁獲される魚、特に北洋において漁獲、加工された後に残渣として廃棄されている鮭、鱒の頭部の軟骨組織から効率よく分離抽出精製する方法を提供することである。本発明の他の目的は異臭がほとんどなく、幅広い用途を有するプロテオグリカン組成物を得る方法を提供することである。   An object of the present invention is to provide a method for efficiently separating, extracting and purifying fish that are caught in large quantities, particularly from cartilage tissues of salmon and carp heads that are discarded as residues after being caught and processed in the North Sea. is there. Another object of the present invention is to provide a method for obtaining a proteoglycan composition having almost no off-flavor and having a wide range of uses.

本発明者は、上記目的を達成するためにプロテオグリカンの抽出条件を種々検討の結果、本発明に到達した。即ち、本発明は以下のとおりである。
1.下記のA〜E工程よりなるプロテオグリカン組成物の抽出方法。
A.凍結した水棲動物組織を破砕し、これに水を加え、温度0〜20℃、pH4.8〜7で処理する工程、
B.Aの固液混合物を遠心分離し、最上部の脂質層と中間層の水層を取り除き、沈殿物を回収する工程、
C.沈殿物を乾燥し、微粉末化する工程、
D.得られた乾燥微粉末に、溶媒としてヘキサン、アセトン又はエタノールを加え、残存脂質を抽出除去する工程、
E.溶媒を除去する工程。
2.有機溶媒がエタノールである前記1の抽出方法。
3.乾燥沈殿物と有機溶媒の体積比が1:1〜10である請求項1又は2の方法。
4.前記1、2又は3の方法により得られるプロテオグリカン組成物。
As a result of various studies on the extraction conditions for proteoglycans in order to achieve the above object, the present inventor has reached the present invention. That is, the present invention is as follows.
1. A method for extracting a proteoglycan composition comprising the following steps A to E.
A. Crushing frozen aquatic animal tissue, adding water thereto, and treating at a temperature of 0 to 20 ° C. and a pH of 4.8 to 7,
B. Centrifuging the solid-liquid mixture of A, removing the uppermost lipid layer and the intermediate aqueous layer, and collecting the precipitate;
C. Drying the precipitate and pulverizing it,
D. A step of adding hexane, acetone or ethanol as a solvent to the resulting dry fine powder, and extracting and removing residual lipids;
E. Removing the solvent.
2. 2. The extraction method according to 1 above, wherein the organic solvent is ethanol.
3. The method according to claim 1 or 2, wherein the volume ratio of the dried precipitate to the organic solvent is 1: 1 to 10.
4). A proteoglycan composition obtained by the method of 1, 2 or 3.

本発明の方法によれば、水棲動物組織からプロテオグリカンを中心とした成分を分離抽出し、食品に使用する組成物を提供することができる。本発明の処理操作を行うことで、組成物には食品に使用が許されている溶媒を使用して異臭を除去し、食品およびそれ以外の素材として使用が可能な状態とすることができる。さらに本発明で得た組成物はさらに精製することで、食品およびそれ以外の各種用途に使用できる組成物を提供できる。   According to the method of the present invention, a composition mainly used for proteoglycan can be separated and extracted from aquatic animal tissues to provide a composition for use in foods. By carrying out the treatment operation of the present invention, the composition can be made into a state where it can be used as a food and other materials by removing the off-flavor by using a solvent permitted for the food. Furthermore, the composition obtained in the present invention can be further purified to provide a composition that can be used for food and various other uses.

本発明の抽出方法は、水棲動物からの抽出に使用する水の微妙な温度およびpHを適正に設定して脂質を上部に浮上させて抽出を行うことで、プロテオグリカンの分解を防ぎながら不要な脂質を除く第1段階の工程A〜Cと、エタノールのような有機溶媒を使用して微量に残存する脂質に共存している異臭を取り除く第2段階の工程D〜Eよりなる。   In the extraction method of the present invention, the delicate temperature and pH of water used for extraction from aquatic animals are set appropriately, and the lipid is levitated to the upper part to perform extraction, thereby preventing unnecessary lipid degradation while preventing proteoglycan degradation. And the second stage of processes D to E that removes a bad odor coexisting in the lipid remaining in a trace amount using an organic solvent such as ethanol.

生体組織に含まれる脂質とその他組成物とは完全に一体化して組織体を構成しており、両者を分離するためには加熱抽出のような強力な操作法を用いるために、通常は組成物の変性を引き起こすことが多い。本発明においては脂質と水溶性組成物を分離する第1段階の操作としては鋭意研究の結果、磨砕した軟骨組織に含まれる脂質を比重の差により分離することで脂質の75%を除去することが可能である。   Since the lipids contained in living tissue and other compositions are completely integrated to form a tissue body, a powerful operation method such as heat extraction is used to separate the two, so usually the composition Often cause denaturation. In the present invention, as a first step operation for separating the lipid and the water-soluble composition, as a result of earnest research, 75% of the lipid is removed by separating the lipid contained in the ground cartilage tissue by the difference in specific gravity. It is possible.

本発明における水棲動物とは、例えばサメ、鯨、鮭、鱒等であり、好ましくは鮭と鱒である。水棲動物の組織とは、いずれの組織でも差し支えないが、北洋において漁獲、加工された後に残渣として廃棄されている鮭、鱒の頭部の軟骨組織が資源の有効利用という点から好ましい。これらの軟骨組織は、軟骨組織に含まれるプロテオグリカンの加水分解酵素による分解を抑制するために、凍結したものを用いる必要がある。参考として、サケ鼻軟骨の組成を表1に示す。   Examples of the aquatic animal in the present invention include sharks, whales, sharks, and sharks, and preferably sharks and sharks. The aquatic animal tissue may be any tissue, but salmon that has been caught and processed in the North Sea and discarded as a residue is preferred from the viewpoint of effective use of resources. These cartilage tissues need to be frozen in order to suppress degradation of proteoglycans contained in the cartilage tissues by hydrolase. For reference, the composition of salmon nasal cartilage is shown in Table 1.

Figure 0005252623
Figure 0005252623

A工程における破砕は、公知の破砕機、例えばチョッパー(冷凍用・骨用肉挽機)で行って差し支えない。水棲動物組織に加える水は水道水でも脱イオン水でも蒸留水でも差し支えない。水の量は、ウェットベースで、水棲動物組織100重量部に対して100〜200重量部が好ましい。本発明においては、A工程でpHが4.8〜7、温度が0〜20℃で十分混合した後、好ましくは0〜15℃にて遠心分離することが重要である。pHが4.8未満の酸性条件では、溶媒として酢酸などを使用し、沈殿物から溶媒を完全に除去することが困難となるため、利用範囲が限られてくる。pH7を超えるアルカリ条件だと、脂肪分の溶解率は高まるが、プロテオグリカンのグリコサミノグリカン糖鎖とコアタンパク質も分解されてしまう。温度が0℃より低いと氷となり抽出溶媒として使用できず、20℃より高いと水棲動物組織に含まれるプロテオグリカン加水分解酵素の働きを促進し、プロテオグリカンが低分子化する。特に好ましくはpH5.0〜6.5、温度10〜15℃である。水を加え、pHと温度を所望の範囲に調整したら、好ましくは撹拌して十分混合する。脂質は上部付近に浮き上がり、プロテオグリカン組成物は沈殿する。   The crushing in the step A may be performed by a known crusher, for example, a chopper (freezing / bone meat grinder). The water added to the aquatic animal tissue can be tap water, deionized water or distilled water. The amount of water is preferably 100 to 200 parts by weight with respect to 100 parts by weight of aquatic animal tissue on a wet basis. In the present invention, in Step A, it is important that the pH is 4.8 to 7 and the temperature is sufficiently mixed at 0 to 20 ° C., and then preferably centrifuged at 0 to 15 ° C. Under acidic conditions where the pH is less than 4.8, acetic acid or the like is used as a solvent, and it becomes difficult to completely remove the solvent from the precipitate, so that the range of use is limited. Under alkaline conditions exceeding pH 7, the dissolution rate of fat increases, but the glycosaminoglycan sugar chain and core protein of proteoglycan are also degraded. If the temperature is lower than 0 ° C., it becomes ice and cannot be used as an extraction solvent. If the temperature is higher than 20 ° C., the function of proteoglycan hydrolase contained in aquatic animal tissues is promoted, and the proteoglycan is reduced in molecular weight. Particularly preferably, the pH is 5.0 to 6.5 and the temperature is 10 to 15 ° C. When water is added and the pH and temperature are adjusted to the desired ranges, they are preferably mixed well with stirring. Lipids float near the top and the proteoglycan composition precipitates.

ついで、B段階として、ただちに遠心分離で脂質とプロテオグリカン組成物を分ける。遠心分離の回転数と分離時間は相関があるが、3,000〜12,000rpm、10〜40分が好ましく、より好ましくは5,000〜10,000rpm、20〜30分である。遠心分離層は3層に分かれ、最上部の脂質層と中間層の水層を取り除き、沈殿物を回収する。遠心分離の際の温度は、明確な3層を形成するため、好ましくは0〜15℃である。   Next, as the B stage, the lipid and the proteoglycan composition are immediately separated by centrifugation. Although the rotation speed of centrifugation and the separation time have a correlation, 3,000 to 12,000 rpm and 10 to 40 minutes are preferable, and 5,000 to 10,000 rpm and 20 to 30 minutes are more preferable. The centrifugal separation layer is divided into three layers, and the uppermost lipid layer and the intermediate aqueous layer are removed to collect the precipitate. The temperature at the time of centrifugation is preferably 0 to 15 ° C. in order to form clear three layers.

次いでC工程として、沈殿物を乾燥、好ましくは凍結乾燥した後、粉砕機にて微粉末とする。粉砕は、公知の粉砕機、例えば遠心式および衝撃式微粉砕機で行って差し支えない。粉砕の程度は概ね100〜300メッシュである。得られた乾燥微粉末の脂質は約10%となる。よって、A〜C工程にて脂質が約75%除去されたこととなる。   Next, in step C, the precipitate is dried, preferably freeze-dried, and then made into a fine powder by a pulverizer. The pulverization may be performed by a known pulverizer such as a centrifugal type or impact type pulverizer. The degree of grinding is approximately 100 to 300 mesh. The resulting dry fine powder has about 10% lipid. Therefore, about 75% of lipid was removed in the A to C steps.

本発明における第1段階の処理であるA〜C工程により、共存することが好ましくない大部分の脂質を除去することができるが、プロテオグリカン組成物中に市販されている組成物と同じ程度ではあるがまだ異臭が残留しており、使用される食品に制限があった。そこで、本発明においては種々の機能を有するプロテオグリカンの用途をさらに拡大することを第一の目的として鋭意研究を行った。このような意味から残留する異臭は除かなければならない。   The steps A to C, which are the first stage treatment in the present invention, can remove most of the lipids that are not preferred to coexist, but are about the same as the compositions marketed in proteoglycan compositions. However, there was still a strange odor and there was a limit to the food used. Therefore, in the present invention, intensive studies were conducted with the primary purpose of further expanding the use of proteoglycans having various functions. In this sense, the remaining off-flavor must be removed.

これまで臭いに関する研究は数多くあり、多くは臭いが単一成分で構成されることはほとんどなく、数多くの化学物質の特定両の集合によりそれぞれ特有の臭いが構成されている。特に好ましい臭いすなわち「香り」に関する研究結果は市場において数多く利用されている。本発明で対象となる臭いは好ましくないもので除去することが目的となるが、その全体の性質を知る必要があり、本発明は鋭意研究を行い、それが脂質と共存していることを突き止めた。   There have been many studies on odor so far, and most odors are rarely composed of a single component, and specific odors are constituted by specific collections of many chemical substances. There are many research results on the market regarding particularly favorable odors or “scents”. The object of the present invention is to remove the odor that is the object of objection, but it is necessary to know its overall properties, and the present invention conducts intensive research to find out that it coexists with lipids. It was.

A〜C工程で得られたプロテオグリカン組成物には微量ではあるが、まだ脂質が残留している。残留する脂質を除くためには脂質を溶解する溶媒を利用することが必要である。本発明におけるプロテオグリカン組成物は食品用を含めた幅広い用途を対象とすることから、脂質を溶解する溶媒には制限が加えられる。この点から溶媒としては、作業者並びに製品の使用者にも安全な、食品衛生法により許可されたヘキサン、アセトン又はエタノールを用いる。好ましくはエタノールである。
溶媒を加えて脂質を抽出する際には脂質と共存するコラーゲン等のタンパク質が乳化状況を示すことが多く、できるだけ操作を簡便化し、低コストで異臭を含む脂質を除く方法を開発した。
Although the amount of the proteoglycan composition obtained in the steps A to C is very small, lipids still remain. In order to remove the remaining lipid, it is necessary to use a solvent that dissolves the lipid. Since the proteoglycan composition in the present invention is intended for a wide range of uses including foods, restrictions are imposed on the solvent that dissolves lipids. From this point, hexane, acetone or ethanol permitted by the Food Sanitation Law, which is safe for workers and product users, is used as the solvent. Ethanol is preferable.
When extracting a lipid by adding a solvent, proteins such as collagen coexisting with the lipid often show an emulsified state, and a method has been developed that simplifies the operation as much as possible and removes lipids containing off-flavors at low cost.

即ち、本発明においては脂質を溶解した溶媒とプロテオグリカン組成物との乳化を防ぐために、D工程として、C工程で得られた乾燥微粉末に、特定の溶媒を加え、残存脂質を抽出除去する。このように、水分と体積を減少させて溶媒を添加することで、使用する溶媒の量を少なくすることができる。溶媒の量は、体積比で乾燥沈殿物1に対して有機溶媒が1〜10が好ましく、更に好ましくは5〜10である。
最後にE工程として、使用した溶媒を風乾または低温真空乾燥することで、組成物中のプロテオグリカンを分解させることもなく目的とする異臭を除くことができる。溶媒抽出は必要に応じて1回乃至複数回行うことができる。
That is, in the present invention, in order to prevent emulsification of the solvent in which the lipid is dissolved and the proteoglycan composition, as the step D, a specific solvent is added to the dry fine powder obtained in the step C, and the residual lipid is extracted and removed. Thus, the amount of the solvent to be used can be reduced by adding the solvent while reducing the moisture and volume. As for the quantity of a solvent, 1-10 are preferable for an organic solvent with respect to the dry precipitate 1 by volume ratio, More preferably, it is 5-10.
Finally, as the step E, the target solvent can be removed without decomposing proteoglycans in the composition by air drying or low-temperature vacuum drying of the solvent used. Solvent extraction can be performed once to multiple times as necessary.

実施例1
凍結サケ鼻軟骨100gを破砕し、これに15℃の水道水を同容量加え、緩やかに撹件して十分混ぜ合わせ、5℃前後に維持された混合物をただちに遠心分離器9,000rpm、30分、4℃で遠心分離し、脂質とプロテオグリカン他組成物を分けた。遠心分離層は3層に分かれ、最上部の脂質層と中間層の水層を取り除き、沈殿物を回収した。沈殿物は凍結乾燥後、遠心式粉砕機で粉砕し、水脱脂微粉末を得た。この段階で、一部をエーテル抽出にて脂質を測定した結果、脂質は8.8%残存しており、脱脂前の脂質を100%とした場合の除去率は75.0%となり、弱い異臭を含んでいた。
Example 1
100 g of frozen salmon nasal cartilage was crushed, and the same volume of tap water at 15 ° C. was added thereto, gently stirred and mixed thoroughly, and the mixture maintained at around 5 ° C. was immediately centrifuged at 9,000 rpm for 30 minutes. Centrifugation was performed at 4 ° C. to separate lipids and proteoglycan and other compositions. The centrifugal separation layer was divided into three layers, the uppermost lipid layer and the intermediate aqueous layer were removed, and the precipitate was collected. The precipitate was freeze-dried and then pulverized with a centrifugal pulverizer to obtain a water-defatted fine powder. At this stage, lipids were partially extracted by ether extraction, and as a result, 8.8% of the lipids remained. The removal rate when the lipids before degreasing was 100% was 75.0%, with a weak odor. Was included.

ついで、水脱脂微粉末に10倍容量のエタノールを加えて、異臭を含む脂質を溶解抽出した。本操作を2回繰り返してエタノール溶液を濾過除去し、溶媒を蒸発させると微黄褐色無臭のプロテオグリカン組成物粉末を得た。サケ鼻軟骨に対する収率58.7%(ドライベース)、プロテオグリカン含有率77.7%であった。プロテオグリカン組成物粉末の異臭は全く消失した。   Subsequently, 10-fold volume of ethanol was added to the water-degreased fine powder to dissolve and extract the lipid containing off-flavor. This operation was repeated twice to remove the ethanol solution by filtration and evaporate the solvent to obtain a slightly yellowish brown odorless proteoglycan composition powder. The yield based on salmon nasal cartilage was 58.7% (dry base), and the proteoglycan content was 77.7%. The off-flavor of the proteoglycan composition powder disappeared at all.

試料、水脱脂粉末及び水−エタノール脱脂粉末のプロテオグリカン組成物の組成を表2に、水脱脂微粉末中に含まれるプロテオグリカンの分子量構成を図1に示した。比較として、一般的な脱脂法であるクロロホルム−メタノールを用いた有機溶剤脱脂後に得られるプロテオグリカン組成物の組成を表3に、分子量構成を図2に示した。   The composition of the proteoglycan composition of the sample, water degreased powder and water-ethanol degreased powder is shown in Table 2, and the molecular weight constitution of proteoglycan contained in the water degreased fine powder is shown in FIG. For comparison, Table 3 shows the composition of the proteoglycan composition obtained after organic solvent degreasing using chloroform-methanol, which is a general degreasing method, and FIG. 2 shows the molecular weight structure.

Figure 0005252623
Figure 0005252623

Figure 0005252623
Figure 0005252623

本発明の方法により得られるプロテオグリカン組成物は、異臭がないために、特に食品分野での使用に適している。   Since the proteoglycan composition obtained by the method of the present invention has no off-flavor, it is particularly suitable for use in the food field.

実施例1の中間段階で得られた水脱脂粉末に含まれるプロテオグリカンの分子量構成を表した図である。2 is a diagram showing the molecular weight structure of proteoglycan contained in the water-degreased powder obtained in the intermediate stage of Example 1. FIG. 有機溶剤脱脂(クロロホルム−メタノール)で得られた粉末に含まれるプロテオグリカンの分子量構成を表した図である。It is a figure showing the molecular weight structure of the proteoglycan contained in the powder obtained by organic solvent degreasing (chloroform-methanol).

Claims (3)

下記のA〜E工程よりなるプロテオグリカン組成物の抽出方法。
A.凍結した水棲動物組織を破砕し、これに水を加え、温度0〜20℃、pH4.8〜7で処理する工程、
B.Aの固液混合物を遠心分離し、最上部の脂質層と中間層の水層を取り除き、沈殿物を回収する工程、
C.沈殿物を乾燥し、微粉末化する工程、
D.得られた乾燥微粉末に、溶媒としてヘキサン、アセトン又はエタノールを加え、残存脂質を抽出除去する工程、
E.溶媒を除去する工程。
A method for extracting a proteoglycan composition comprising the following steps A to E.
A. Crushing frozen aquatic animal tissue, adding water thereto, and treating at a temperature of 0 to 20 ° C. and a pH of 4.8 to 7,
B. Centrifuging the solid-liquid mixture of A, removing the uppermost lipid layer and the intermediate aqueous layer, and collecting the precipitate;
C. Drying the precipitate and pulverizing it,
D. A step of adding hexane, acetone or ethanol as a solvent to the resulting dry fine powder, and extracting and removing residual lipids;
E. Removing the solvent.
溶媒がエタノールである請求項1の抽出方法。   The extraction method according to claim 1, wherein the solvent is ethanol. 乾燥沈殿物と有機溶媒の体積比が1:1〜10である請求項1又は2の方法。
The method according to claim 1 or 2, wherein the volume ratio of the dried precipitate to the organic solvent is 1: 1 to 10.
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