JP2012532629A - Marine-derived Bacillus barbaricus SCSIO02429 and method for preparing squid oligopeptide using the same - Google Patents
Marine-derived Bacillus barbaricus SCSIO02429 and method for preparing squid oligopeptide using the same Download PDFInfo
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- JP2012532629A JP2012532629A JP2012535620A JP2012535620A JP2012532629A JP 2012532629 A JP2012532629 A JP 2012532629A JP 2012535620 A JP2012535620 A JP 2012535620A JP 2012535620 A JP2012535620 A JP 2012535620A JP 2012532629 A JP2012532629 A JP 2012532629A
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- squid
- oligopeptide
- enzyme
- crude
- scsio
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Classifications
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- C—CHEMISTRY; METALLURGY
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- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
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- A23J3/00—Working-up of proteins for foodstuffs
- A23J3/30—Working-up of proteins for foodstuffs by hydrolysis
- A23J3/32—Working-up of proteins for foodstuffs by hydrolysis using chemical agents
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- A—HUMAN NECESSITIES
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- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
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- C07K14/43504—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans from invertebrates
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- C—CHEMISTRY; METALLURGY
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P21/00—Preparation of peptides or proteins
- C12P21/06—Preparation of peptides or proteins produced by the hydrolysis of a peptide bond, e.g. hydrolysate products
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
- C12R2001/00—Microorganisms ; Processes using microorganisms
- C12R2001/01—Bacteria or Actinomycetales ; using bacteria or Actinomycetales
- C12R2001/07—Bacillus
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Abstract
本発明は海洋由来のBacillus barbaricus SCSIO 02429 CCTCC NO:M 2010213に関する。また、本発明はイカオリゴペプチドの調製方法に関し、その特徴はBacillus barbaricus SCSIO 02429を酵素生産発酵誘導培地に加えて発酵させ、加水分解用粗酵素溶液を得た上で、イカ内臓をスラリー状に破砕して粗酵素溶液に加え、酵素分解を行ってグリコシル側鎖が破壊された粗タンパク質酵素分解物を得て、さらにブロメラインを加えて酵素分解を進め、得られた酵素分解物を静置して油層と水層に分離させ、油層を除去して乾燥させてイカオリゴペプチドを得る。本発明のイカオリゴペプチドの収率は40〜46%、アミノ酸の収率は16〜22%に達する。このイカオリゴペプチドには海洋養殖動物の種苗死亡率を下げ、体重増加率を高める作用があり、飼料中の魚粉など従来のタンパク質源に代わることができるため、海洋養殖配合飼料の機能性タンパク源、添加物などとして使用できる。
【選択図】なしThe present invention relates to a marine-derived Bacillus barbaricus SCSIO 02429 CCTCC NO: M 2010213. The present invention also relates to a method for preparing a squid oligopeptide, characterized by adding Bacillus barbaricus SCSIO 02429 to an enzyme-producing fermentation-inducing medium and fermenting it to obtain a crude enzyme solution for hydrolysis. Crushed and added to the crude enzyme solution. Enzymatic digestion is performed to obtain a crude protein enzyme degradation product in which the glycosyl side chain is destroyed. The oil layer and the aqueous layer are separated, and the oil layer is removed and dried to obtain a squid oligopeptide. The yield of the squid oligopeptide of the present invention is 40 to 46%, and the yield of amino acids is 16 to 22%. This squid oligopeptide has the effect of lowering the seedling mortality rate of marine aquaculture animals and increasing the rate of weight gain, and it can replace conventional protein sources such as fish meal in the feed. Can be used as an additive.
[Selection figure] None
Description
本発明は、バシラス(Bacillus)属菌に関し、具体的には、海洋由来のバシラス属菌Bacillus barbaricus SCSIO 02429菌株及びこの菌株を利用したイカオリゴペプチドの調製方法に関する。 TECHNICAL FIELD The present invention relates to a Bacillus genus, and more specifically to a marine-derived Bacillus barbaricus SCSIO 02429 strain and a method for preparing a squid oligopeptide using this strain.
我が国の海洋漁業の迅速な発展に伴い、イカの年間生産量は30万トン前後に達し、我が国の重要な水産加工原料の一つになっている。イカの加工処理過程において、15%程度の内臓廃棄物が生じ、これら廃棄物にはタンパク質が豊富に含まれているが、極めて腐乱・変質しやすいため、貯蔵が難しい。通常の処理方法ではイカ油を抽出し終わった廃棄物を埋めるが、近頃はイカ内臓に一次加工を行ってイカのスラリーを作製し、魚類の飼料に直接用いるという報告もある。しかし、こうした高度加工を経ていない飼料は生物学的利用能が高くない上、水環境を汚染し、養殖動物の病害流行の機会が増えることになる。このため、イカ内臓の開発利用を進めることは、経済的及び環境保護的に見て重要な意義がある。イカ内臓の酵素分解方法の研究も広い注目を浴びており、バイオ酵素技術を用いて、イカの粗タンパク質を、水産動物に吸収されやすく、一定の生理機能を持つオリゴペプチド類のタンパク質源に分解するのは、一つの効果的な方法であり、かつその研究もいくつか行われている。例えば薛長湖、劉春娥らによる、酵素の種類、用量、反応温度、反応時間などの要素がイカ内臓の粗タンパク質転換率に及ぼす影響についての研究(特許文献1)、袁亜輝らによる、イカ内臓の酵素分解を利用した海の旨み成分の生産、張井らによる、イカ内臓の酵素分解液中の重金属除去方法についての研究などである。 With the rapid development of Japan's marine fishery, the annual production of squid has reached around 300,000 tons, making it one of Japan's important marine products. In the process of processing squid, about 15% of visceral waste is generated, and these wastes are rich in protein, but they are very easy to perish and deteriorate, and are difficult to store. In the usual treatment method, the waste from which squid oil has been extracted is buried, but recently, there is a report that a squid slurry is primarily processed to produce a squid slurry and used directly in fish feed. However, feeds that have not undergone such advanced processing are not highly bioavailable, pollute the water environment, and increase the chances of disease outbreaks in farmed animals. For this reason, it is important to promote the development and use of squid internal organs from the viewpoint of economic and environmental protection. Research on enzymatic degradation methods of squid viscera has also attracted widespread attention. Using bioenzyme technology, squid crude proteins are easily absorbed by aquatic animals and decomposed into protein sources of oligopeptides with a certain physiological function. This is one effective method and several studies have been conducted. For example, a study on the effects of factors such as enzyme type, dose, reaction temperature, reaction time, etc. on the crude protein conversion rate of squid viscera (Patent Literature 1) by Lake Changchun, Liu Chunxi et al. This includes the production of sea flavor components using decomposition, and the research on the removal method of heavy metals in the enzymatic decomposition solution of squid viscera by Zhangi et al.
すでに報告されているイカ内臓の酵素分解方法において、使用酵素の種類には、トリプシン、ペプシン、中性プロテアーゼ、アルカリプロテアーゼ、パパイン、ブロメライン及びこれら酵素の混合物がある。しかし現段階のイカ内臓の加水分解方法にはまだ、粗タンパク質の加水分解率が低い、酵素分解生成物の残留粗タンパク質が海洋養殖動物に吸収・利用されにくいといった問題がある。また反応温度の向上、反応時間の延長、触媒使用量の増加などの手段により粗タンパク質の加水分解度を高めると、今度は分解が進み過ぎる現象が起こり、目標とするオリゴペプチドの収率が大幅に下がる。例えば、イカ内臓の加水分解によるアミノ酸の収率が70%を超えるが、オリゴペプチドの収率は却って非常に低くなるという文献報告がある。粗タンパク質の加水分解効率を高めると同時に、目標とするオリゴペプチドの収率を保証できれば、イカ内臓の利用水準は大きく向上する。 In the already reported method for enzymatic degradation of squid viscera, the types of enzymes used include trypsin, pepsin, neutral protease, alkaline protease, papain, bromelain and mixtures of these enzymes. However, there are still problems with the hydrolysis method of squid viscera at this stage, such that the hydrolysis rate of the crude protein is low and the residual crude protein of the enzymatic degradation product is difficult to be absorbed and used by marine aquaculture animals. Moreover, if the degree of hydrolysis of the crude protein is increased by measures such as increasing the reaction temperature, extending the reaction time, or increasing the amount of catalyst used, this will cause excessive degradation of the protein, which will greatly increase the yield of the target oligopeptide. Go down. For example, there is a literature report that the yield of amino acids by hydrolysis of squid viscera exceeds 70%, but the yield of oligopeptides is extremely low. If the yield of the target oligopeptide can be ensured while enhancing the hydrolysis efficiency of the crude protein, the utilization level of the squid viscera will be greatly improved.
本発明の目的は、海洋中から新しいバシラス属菌を開発することにあり、もう一つの目的は、このバシラス属菌を利用してイカ内臓を酵素分解し、粗タンパク質の加水分解率が高くオリゴペプチドの収率が高い、イカオリゴペプチドの調製方法を提供することである。 An object of the present invention is to develop a new Bacillus genus from the ocean, and another object is to enzymatically decompose the squid viscera using this Bacillus genus and to increase the hydrolysis rate of the crude protein. It is to provide a method for preparing a squid oligopeptide with a high peptide yield.
我々は中国南海(南シナ海)の深海堆積物からBacillus barbaricus SCSIO 02429を分離し、Bacillus barbaricus SCSIO 02429による発酵で得られた粗酵素溶液で、内臓タンパク質中のペプチド鎖につながったグリコサミノグリカン(GAG)側鎖を破壊し、さらにブロメラインを加えてタンパク質ペプチド鎖の加水分解を触媒した。得られたイカオリゴペプチドの収率は40%〜46%、アミノ酸の収率は16%〜22%で、これにより本発明の目的を実現した。 We isolated Bacillus barbaricus SCSIO 02429 from deep sea sediments in the South Sea of China (South China Sea), and obtained a crude enzyme solution obtained by fermentation with Bacillus barbaricus SCSIO 02429. ) Side chains were broken and bromelain was added to catalyze the hydrolysis of protein peptide chains. The yield of the obtained squid oligopeptide was 40% to 46%, and the yield of amino acids was 16% to 22%, thereby realizing the object of the present invention.
Bacillus barbaricus SCSIO 02429は2010年8月31日に中国典型培養物保蔵センター(China Center for Type Culture Collection、略称CCTCC)に保管されており、所在地は武漢市武昌珞珈山、保管番号はCCTCC NO:M 2010213である。 Bacillus barbaricus SCSIO 02429 is stored on August 31, 2010 at the China Center for Type Culture Collection (abbreviated as CCTCC), located in Wuchang, Wuchang, and storage number is CCTCC NO: M 2010213.
上記のBacillus barbaricus SCSIO 02429は2009年に採取された南シナ海の深海堆積環境(経度:119°57.260′、緯度:20°59.877′、水深229m)から分離されたものである。細菌培地を用いて平板希釈法により分離し、画線法で単離した。16S rRNA塩基配列の相似解析により、Bacillus barbaricusと99%(722/728bp)の相似度があることがわかり、Bacillus barbaricus種の菌株の一つSCSIO 02429と鑑別された。この菌株はISP2培地(蒸留水1リットル当たり酵母エキス4.0g、麦汁10.0g、ブドウ糖4.0g、寒天20.0gを加える、pH 7.0)において28〜37℃で良好に生育する。 The Bacillus barbaricus SCSIO 02429 was separated from the deep sea sedimentary environment (longitude: 119 ° 57.260 ′, latitude: 20 ° 59.877 ′, depth of 229 m) collected in 2009. It isolate | separated by the plate dilution method using the bacterial culture medium, and isolated by the streak method. Similarity analysis of the 16S rRNA nucleotide sequence revealed that there was a similarity of 99% (722/728 bp) with Bacillus barbaricus, which was differentiated from SCSIO 02429, one of the strains of Bacillus barbaricus species. This strain grows well at 28-37 ° C. in ISP2 medium (4.0 g yeast extract, 10.0 g wort, 4.0 g glucose, 20.0 g agar, pH 7.0 per liter distilled water) .
「一般細菌鑑別マニュアル」及び「バージィズ鑑別細菌学マニュアル」の基準、方法、種の分類特徴に従い、被験菌株に細菌の形態観察、生理・生化学テストなどの試験を行った。この菌株はPYES培地(0.3%カゼインペプトン、0.3%酵母エキス、0.23%コハク酸二ナトリウム、pH7.2)においても同じく良好に生育し、褐色、不透明、平坦な円形コロニーで、最大コロニー径は5mmである。コロニーは生育初期には完全な境界を有するが、それに続く生育過程において境界は徐々に消失する。細胞は桿状を示し、芽胞は楕円形で、細胞はグラム陽性である。PYES培地において、28〜37℃ではいずれも良好に生育し、3週間培養した後は、4〜47℃で明らかな生育が観察できる。この菌は2%及び5%塩化ナトリウムを含むPYES培地において生育でき、3週間培養した後、12%NaClを含むPYES培地培地で生育が観察できる。菌株はpH6.0で生育を観察でき、pH7.0、8.0、9.5では迅速に生育できるため、この菌には耐アルカリ性があることがわかる。SCSIO 02429株菌の生理・生化学テストの結果は表1の通りで、表中の「+」は陽性又は利用できる、「−」は陰性又は利用できないことを示す。 In accordance with the standards, methods, and species classification characteristics of the “General Bacteriology Manual” and “Virges Bacteriology Manual”, tests such as bacterial morphology observation and physiological / biochemical tests were performed on the test strains. This strain also grows well in PYES medium (0.3% casein peptone, 0.3% yeast extract, 0.23% disodium succinate, pH 7.2) and is a brown, opaque, flat circular colony The maximum colony diameter is 5 mm. The colony has a complete boundary in the early stage of growth, but the boundary gradually disappears in the subsequent growth process. The cells are rod-shaped, the spores are oval, and the cells are gram positive. In PYES medium, all grow well at 28 to 37 ° C., and after 3 weeks of culture, obvious growth can be observed at 4 to 47 ° C. This bacterium can grow in a PYES medium containing 2% and 5% sodium chloride, and after culturing for 3 weeks, the growth can be observed in a PYES medium containing 12% NaCl. The strain can be observed to grow at pH 6.0, and can grow rapidly at pH 7.0, 8.0, and 9.5, indicating that this bacterium has alkali resistance. The results of the physiological and biochemical tests of the SCSIO 02429 strain are as shown in Table 1. “+” in the table indicates positive or usable, and “−” indicates negative or unavailable.
SCSIO 02429 株菌と、最も近い菌株Bacillus barbaricus V2−BIII−A2(参考文献:Taubel M.,Kampfer P,Buczolits S,Lubitz W,Busse H−J R. Bacillus barbaricus sp. nov.,isolated from an experimental wall painting. International Journal of Systematic and Evolutionary Microbiology,2003年,第53巻、p.725−730。この菌の16S rDNA配列のGenBank/EMBL/DDBJにおける登録番号はAJ422145である)とは、生理学的特性において大部分が一致するが、D−リボース、クエン酸塩、スクロースの利用、最高耐容塩分濃度が5%という特徴において異なる。このため、SCSIO 02429はBacillus barbaricusの菌株の一つと鑑別され、Bacillus barbaricusには現在まだ中国語の訳語はない。 SCSIO 02429 strain and the closest strain Bacillus barbaricus V2-BIII-A2 (references: Taubel M., Kampfer P, Buczolits S, Lubitz W, Busse H-J R. Bacillus barbolimus sp. wall painting. International Journal of Systemic and Evolutionary Microbiology, 2003, Vol. 53, p. 725-730. The characteristic number of Genus / EMBL / DDB42 in GenBank / EMBL / DDB42 is 21 in the Physiology 16S rDNA sequence. Mostly in Matching, but different D- ribose, citrate, utilization of sucrose, in the feature that the highest tolerable salt concentration of 5%. For this reason, SCSIO 02429 is distinguished from one of the strains of Bacillus barbaricus, and Bacillus barbaricus does not yet have a Chinese translation.
本発明のイカオリゴペプチドの調製方法は、以下の手順を含むことを特徴とする。
(1)Bacillus barbaricus SCSIO 02429菌種を菌種活性化培地に接種し、30〜37℃で18〜24時間培養し、活性化後、酵素生産誘導発酵培地を入れた容器に加え、pH=7.0〜8.0、30〜37℃の条件で12〜24時間発酵させ、発酵液のプロテアーゼ活性が2000〜3000ユニット/mLに達し、グリコサミノグリカナーゼ活性が0.95〜1.12ユニット/mLに達したときのグリコシル加水分解用粗酵素溶液を得る工程であって、前記酵素生産誘導発酵培地は、イカ内臓スラリー、ペプトン、酵母エキス、複合塩及び水を質量比20〜30:5:5:10:1000で混合加熱し溶かして作成したものであり、前記複合塩は、塩化ナトリウム、硫酸カリウム、塩化マグネシウム及び塩化アンモニウムを質量比5〜8:2:2:3で混合したものである工程、
(2)イカ内臓原料をスラリー状に破砕後、手順(1)に記載した粗酵素溶液と体積比1:1〜2:1で混ぜて酵素分解を行い、反応開始時のpHは6.5〜7.0、温度は40〜50℃、時間は5〜8時間で、グリコシル側鎖が破壊された粗タンパク質酵素分解物を得る工程、及び、
(3)イカ内臓原料1グラムにつきブロメライン1000〜1500ユニット(酵素活性)を加える比率により、ブロメラインを手順(2)で得られた粗タンパク質酵素分解物に加え、pHを6.5〜7.0に調節し、35〜40℃で4〜6時間反応させ、得られた酵素分解物を静置し、粗脂肪層と水層に分離し、脂肪層を除去し乾燥させて、イカオリゴペプチドを得る工程。
The preparation method of the squid oligopeptide of this invention is characterized by including the following procedures.
(1) Inoculating Bacillus barbaricus SCSIO 02429 into a bacterial species activation medium, culturing at 30-37 ° C. for 18-24 hours, and after activation, adding to a container containing an enzyme production induction fermentation medium, pH = 7 Fermentation is carried out for 12 to 24 hours under the conditions of 0.0 to 8.0 and 30 to 37 ° C., the protease activity of the fermentation solution reaches 2000 to 3000 units / mL, and the glycosaminoglycanase activity is 0.95 to 1.12. The step of obtaining a crude enzyme solution for glycosyl hydrolysis when the unit / mL is reached, wherein the enzyme production-inducing fermentation medium comprises squid visceral slurry, peptone, yeast extract, complex salt and water in a mass ratio of 20-30: It was prepared by mixing and heating at 5: 5: 10: 1000, and the composite salt was sodium chloride, potassium sulfate, magnesium chloride and salt Ammonium weight ratio 5-8: 2: 2: step is a mixture with 3,
(2) After crushing the squid viscera raw material into a slurry, it is mixed with the crude enzyme solution described in the procedure (1) at a volume ratio of 1: 1 to 2: 1 to perform enzymatic decomposition, and the pH at the start of the reaction is 6.5. -7.0, temperature is 40-50 ° C, time is 5-8 hours, obtaining a crude protein enzyme degradation product in which the glycosyl side chain is broken; and
(3) Bromelain is added to the crude protein enzyme degradation product obtained in step (2) at a ratio of adding 1000-1500 units (enzyme activity) of bromelain per gram of squid viscera, and the pH is adjusted to 6.5-7.0. And the reaction is carried out at 35 to 40 ° C. for 4 to 6 hours. The obtained enzyme degradation product is left standing, separated into a crude fat layer and an aqueous layer, the fat layer is removed and dried, and the squid oligopeptide is removed. Obtaining step.
手順(3)に述べる乾燥は、噴霧乾燥などでよい。本発明に用いるペプトンと酵母エキスは市販のものである。 The drying described in the procedure (3) may be spray drying. The peptone and yeast extract used in the present invention are commercially available.
本発明は、Bacillus barbaricus SCSIO 02429の生産する粗酵素の酵素分解により内臓タンパク質中のペプチド鎖につながったグリコサミノグリカン側鎖を破壊し、グリコシル基によるタンパク質ペプチド鎖の加水分解点への保護作用を除去するもので、反応の過度の加水分解が防がれるような温和な条件では、イカオリゴペプチドの収率は40〜46%、アミノ酸の収率は16〜22%に達する。このイカオリゴペプチドには海洋養殖動物の種苗死亡率を下げ、体重増加率を高める作用があり、飼料中の魚粉など従来のタンパク質源に代えることができる。また一定の生理活性を持ち、水産動物の体重増加率と生存率を有意に高めることができるため、海洋養殖配合飼料の機能性タンパク質源、添加物などとして使用できる。 The present invention destroys the glycosaminoglycan side chain connected to the peptide chain in the visceral protein by enzymatic degradation of the crude enzyme produced by Bacillus barbaricus SCSIO 02429, and protects the protein peptide chain from hydrolysis by the glycosyl group. In mild conditions that prevent excessive hydrolysis of the reaction, the yield of squid oligopeptide reaches 40-46% and the yield of amino acid reaches 16-22%. This squid oligopeptide has the effect of lowering the seedling mortality rate of marine aquaculture animals and increasing the weight gain rate, and can be replaced by conventional protein sources such as fish meal in feed. Moreover, since it has a certain physiological activity and can significantly increase the weight gain rate and survival rate of aquatic animals, it can be used as a functional protein source, an additive and the like for a marine aquaculture feed.
以下の実施例は本発明についてのさらなる説明であり、本発明に対する制限ではない。 The following examples are further illustrations of the present invention and are not a limitation on the present invention.
実施例におけるBacillus barbaricus SCSIO 02429は中国典型培養物保蔵センターに保管され、保管番号はCCTCC NO:M 2010213である。使用したイカは広州市黄沙海産市場で購入し、鑑別によりアカイカ(Ommastrephes bartrami)と同定され、内臓を採取し、−18℃で保存し、使用の24時間前に4℃で解凍した。使用したブロメラインは南寧▲ぱん▼博生物工程有限公司の生産であり、80万ユニット(酵素活性)/gである。ペプトンはOxide社の生産で、酵母エキス(Yeast extract)は碧雲天生物技術研究所より購入した。 In the examples, Bacillus barbaricus SCSIO 02429 is stored in the Chinese Typical Culture Storage Center, and the storage number is CCTCC NO: M 2010213. The squid used was purchased from the Guangzhou Huangsha seafood market, identified as squid (Ommastrefeth bartrami) by differentiation, the internal organs were collected, stored at -18 ° C, and thawed at 4 ° C 24 hours prior to use. The bromelain used was produced by Nanning Panbo Biotechnology Co., Ltd., with 800,000 units (enzyme activity) / g. Peptone was produced by Oxide, and yeast extract was purchased from Ryukyuten Biotechnology Institute.
1Lの水にペプトン10g、酵母エキス5g、塩化ナトリウム10g、寒天15gを加え、pHを7.0に調節し、菌種活性化培地を得た。 To 1 L of water, 10 g of peptone, 5 g of yeast extract, 10 g of sodium chloride and 15 g of agar were added to adjust the pH to 7.0 to obtain a bacterial species activation medium.
イカ内臓スラリー100g、ペプトン25g、酵母エキス25g、複合塩50gを量って取り、脱イオン水5000mLを加え、加熱して溶かし、pHを7.0に調節し、発酵槽に移し入れ、蒸気滅菌し、酵素生産発酵培地を得た。この中の複合塩は塩化ナトリウム20.9g、硫酸カリウム8.3g、塩化マグネシウム8.3g及び塩化アンモニウム12.5gからなる。 Take 100 g of squid visceral slurry, 25 g of peptone, 25 g of yeast extract and 50 g of complex salt, add 5000 mL of deionized water, heat to dissolve, adjust pH to 7.0, transfer to fermenter, steam sterilize The enzyme production fermentation medium was obtained. The complex salt is composed of 20.9 g of sodium chloride, 8.3 g of potassium sulfate, 8.3 g of magnesium chloride and 12.5 g of ammonium chloride.
Bacillus barbaricus SCSIO 02429の菌種を菌種活性化培地に接種し、30℃で24時間培養した。活性化後、菌種を酵素生産発酵培地5Lの入った発酵槽に加え、pH=7.0、30℃、撹拌速度100r/min、換気率0.2の条件において24時間発酵させ、プロテアーゼ活性2000ユニット/mL、グリコサミノグリカナーゼ活性0.95ユニット/mLになったら発酵完了とし、加水分解用粗酵素溶液4.7Lを得た。 The bacterial species of Bacillus barbaricus SCSIO 02429 was inoculated into the bacterial species activation medium and cultured at 30 ° C. for 24 hours. After activation, the bacterial species is added to a fermentor containing 5 L of enzyme-producing fermentation medium, and fermented for 24 hours under the conditions of pH = 7.0, 30 ° C., stirring rate 100 r / min, and ventilation rate 0.2, and protease activity When 2000 units / mL and glycosaminoglycanase activity reached 0.95 units / mL, the fermentation was completed, and 4.7 L of a crude enzyme solution for hydrolysis was obtained.
プロテアーゼ活性の測定方法:中華人民共和国専門標準「プロテアーゼ活性測定法SB/T 10317−1999」の方法により測定した。 Method for measuring protease activity: The protease activity was measured by the method of the professional standard of the People's Republic of China “Protease activity measurement method SB / T 10317-1999”.
グリコサミノグリカナーゼのユニット(酵素活性)の定義:60 ℃、pH 5.2、反応30分で、グルコサミン1μmolを形成するのに必要な1分当たりの酵素量。グリコサミノグリカナーゼ活性の測定方法:一定量のグリコサミノグリカンを量って取り、0.2mol/Lの酢酸溶液に溶かし、0.2mol/Lの酢酸ナトリウムでpHを5.2に調節し、0.5%のグリコサミノグリカン溶液に調合した。グリコサミノグリカン溶液1.5mLを吸って取り、60 ℃で2 分保温した後、酵素液0.5mLを加え、振とうし、30min反応させた後、フェリシアン化カリウム試薬3mLを加え、反応を止め、Imoto法でその還元糖量を測定し、グリコサミノグリカンの分解速度を計算した。 Definition of unit of glycosaminoglycanase (enzyme activity): the amount of enzyme per minute required to form 1 μmol of glucosamine at 60 ° C., pH 5.2, 30 minutes of reaction. Method for measuring glycosaminoglycanase activity: Weigh out a certain amount of glycosaminoglycan, dissolve in 0.2 mol / L acetic acid solution, and adjust pH to 5.2 with 0.2 mol / L sodium acetate. And formulated into a 0.5% glycosaminoglycan solution. Inhale 1.5 mL of glycosaminoglycan solution, incubate at 60 ° C for 2 minutes, add 0.5 mL of enzyme solution, shake, react for 30 min, add 3 mL of potassium ferricyanide reagent to stop the reaction. The amount of reducing sugar was measured by the Imoto method, and the degradation rate of glycosaminoglycan was calculated.
イカ内臓の切片5kgを量って取り、均質化装置を用いて2000r/minで10分粉砕し、約4.7Lのペースト状物を得、酵素生産発酵生成物を入れた発酵槽に移し、2.0mol/Lの酢酸で溶液のpHを6.5に調節し、温度を40℃にし、撹拌速度100r/minで8時間反応させ、グリコシル側鎖が破壊された粗タンパク質酵素分解物を得た。 Take a 5 kg slice of squid viscera and grind it at 2000 r / min for 10 minutes using a homogenizer to obtain about 4.7 L of a paste, which is transferred to a fermentor containing the enzyme-producing fermentation product, The pH of the solution was adjusted to 6.5 with 2.0 mol / L acetic acid, the temperature was adjusted to 40 ° C., and the reaction was performed at a stirring rate of 100 r / min for 8 hours to obtain a crude protein enzyme degradation product in which the glycosyl side chain was broken. It was.
グリコシル側鎖が破壊された粗タンパク質酵素分解物にブロメライン6.25gを加え、酵素用量をイカ内臓原料1gにつき約1000ユニット(酵素活性)にした。均一になるまで撹拌した後、反応温度を40℃に設定し、撹拌速度50回転/分、pHは7.0、反応時間6時間とした。反応が終わったら、撹拌を止め、生成物を静置して油層と水層に分離させ、上層の粗油を除去した後、サンプリングしイカオリゴペプチドの収率とアミノ酸収率を測定すると、結果はそれぞれ40%と16%であった。酵素分解物はただちに噴霧乾燥し、イカオリゴペプチド粉末853gを得た。 Bromelain (6.25 g) was added to the crude protein enzyme degradation product in which the glycosyl side chain was broken, and the enzyme dose was adjusted to about 1000 units (enzyme activity) per gram of squid viscera material. After stirring until uniform, the reaction temperature was set to 40 ° C., the stirring speed was 50 revolutions / minute, the pH was 7.0, and the reaction time was 6 hours. After the reaction is completed, stirring is stopped, the product is allowed to stand to separate into an oil layer and an aqueous layer, the crude oil in the upper layer is removed, and sampling is performed to measure the yield of squid oligopeptide and amino acid yield. Were 40% and 16%, respectively. The enzyme degradation product was immediately spray-dried to obtain 853 g of squid oligopeptide powder.
ゲルクロマトグラフィーでオリゴペプチドの収率とアミノ酸収率を測定した。このとき、オリゴペプチド収率(%)=N2/N1×100、アミノ酸収率%=N3/N1×100で、N1は酵素分解液中に含まれるアミノ酸態窒素の全量、N2は分子質量300〜1000Daのペプチド類流出分に含まれるアミノ酸態窒素量(g)、N3は分子質量100〜250Daの流出分に含まれるアミノ酸態窒素量(g)である。ケルダール窒素定量法によりN1を測定した。酵素分解物は脱脂、遠心分離し不溶物を除去して重量を量り、0.2mol/Lリン酸ナトリウム緩衝液に溶かし、SephadexLH 20ゲルカラムに装填し、0.2mol/Lリン酸ナトリウム緩衝液で溶出し、順にそれぞれの保持容積の流出分を収集し、その後ゲル浸透HPLCで各流出分の分子質量分布を測定した。300〜1000Da分子質量範囲内の流出分を合わせたものがオリゴペプチドフラグメントであり、ケルダール窒素定量法でそれに含まれるアミノ酸態窒素量を測定したものがN2である。100〜250Da分子質量範囲内の流出分を合わせたものが遊離アミノ酸フラグメントであり、ケルダール窒素定量法で含まれるアミノ酸態窒素量を測定したものがN3である。各流出分の分子質量分布はゲル浸透HPLCで測定した。このとき、計算公式はVe=−b’lgMw+c’であり、式中のVeは保持容積、Mwは分子質量、b’とc’は定数である。定数b’とc’は、0.2mol/Lリン酸ナトリウム緩衝液を用いて1mL/minでクロマトグラフカラム(PL aquagel−OH 30 8um、SEC社、英国)を平衡化し、吸光度214nmで一定化し、ブルーデキストラン溶液を用いて試料注入しV0(死容積)を測定し、グリシン溶液を用いて試料注入しVt(ゲルカラムベッドの全容積)を測定し、標準タンパク質混合液を用いて試料注入し、流速1.0mL/minで、各種標準タンパク質の溶出容積Veを記録し、分子量対数―Veの検量線を作成することで得られる。直接Sephadex LH−20カラムのクロマト分離で得た各流出分を試料とし、試料注入して保持容積Veを測定し、公式により分子質量分布範囲を計算した。 The yield of oligopeptide and amino acid yield were measured by gel chromatography. Here, oligopeptide yield (%) = N 2 / N 1 × 100, amino acid yield% = N 3 / N1 × 100, where N 1 is the total amount of amino acid nitrogen contained in the enzymatic degradation solution, N 2 Is the amount of amino acid nitrogen (g) contained in the effluent of peptides having a molecular mass of 300 to 1000 Da, and N 3 is the amount of amino acid nitrogen (g) contained in the effluent of molecular weight 100 to 250 Da. N1 was measured by Kjeldahl nitrogen determination. Enzymatic degradation products are degreased, centrifuged to remove insoluble matter, weighed, dissolved in 0.2 mol / L sodium phosphate buffer, loaded onto Sephadex LH 20 gel column, and 0.2 mol / L sodium phosphate buffer. Elution was performed, and the effluent of each holding volume was collected in order, and then the molecular mass distribution of each effluent was measured by gel permeation HPLC. The combined spillage in 300~1000Da molecular mass range is an oligopeptide fragment, a measure of the amino acid nitrogen content in it in Kjeldahl nitrogen determination method is N 2. A combination of effluents within the molecular mass range of 100 to 250 Da is a free amino acid fragment, and N 3 is the amount of amino acid nitrogen contained in the Kjeldahl nitrogen determination method. The molecular mass distribution of each effluent was measured by gel permeation HPLC. At this time, the calculation formula is V e = −b′lgM w + c ′, where V e is the retention volume, M w is the molecular mass, and b ′ and c ′ are constants. The constants b ′ and c ′ were equilibrated with a chromatographic column (PL aquagel-OH 30 8um, SEC, UK) at 1 mL / min using 0.2 mol / L sodium phosphate buffer, and constant at an absorbance of 214 nm. The sample was injected using a blue dextran solution, V 0 (dead volume) was measured, the sample was injected using a glycine solution, V t (total volume of the gel column bed) was measured, and the sample was prepared using a standard protein mixture. It is obtained by injecting, recording the elution volume V e of various standard proteins at a flow rate of 1.0 mL / min, and creating a calibration curve of logarithm of molecular weight-V e . Each effluent obtained by direct chromatographic separation on a Sephadex LH-20 column was used as a sample, the sample was injected, the retention volume Ve was measured, and the molecular mass distribution range was calculated according to the formula.
1Lの水にペプトン10g、酵母エキス5g、塩化ナトリウム10g、寒天15 gを加え、pHを7.0に調節して菌種活性化培地を得た。 To 1 L of water, 10 g of peptone, 5 g of yeast extract, 10 g of sodium chloride and 15 g of agar were added, and the pH was adjusted to 7.0 to obtain a bacterial species activation medium.
イカスラリー150g、ペプトン25g、酵母エキス25g、複合塩50gを量って取り、脱イオン水5000mLを加え、加熱して溶かし、pHを8.0に調節し、発酵槽に移し、蒸気滅菌し、酵素生産発酵培地を得た。この中の複合塩は塩化ナトリウム26.6g、硫酸カリウム6.7g、塩化マグネシウム6.7g及び塩化アンモニウム10.0gからなる。 Take 150 g of squid slurry, 25 g of peptone, 25 g of yeast extract, 50 g of complex salt, add 5000 mL of deionized water, dissolve by heating, adjust pH to 8.0, transfer to fermentor, steam sterilize, An enzyme-producing fermentation medium was obtained. The complex salt in this consists of 26.6 g of sodium chloride, 6.7 g of potassium sulfate, 6.7 g of magnesium chloride and 10.0 g of ammonium chloride.
Bacillus barbaricus SCSIO 02429の菌種を活性化培地に接種し、37℃で18時間培養した。活性化したら、菌種を酵素生産発酵培地5Lの入った発酵槽に加え、pH=8.0、37℃、撹拌速度100r/min、換気率0.2の条件において12時間発酵させ、プロテアーゼ活性が3000ユニット/mL、グリコサミノグリカナーゼ活性が1.12ユニット/mLになったら発酵完了とし、加水分解用粗酵素溶液4.7Lを得た。プロテアーゼ活性とグリコサミノグリカナーゼ活性は実施例1の方法で測定した。 Bacillus barbaricus SCSIO 02429 was inoculated into the activation medium and cultured at 37 ° C. for 18 hours. Once activated, the bacterial species is added to a fermentor containing 5 L of enzyme-producing fermentation medium and fermented for 12 hours under the conditions of pH = 8.0, 37 ° C., stirring rate 100 r / min, ventilation rate 0.2, and protease activity Was 3000 units / mL and the glycosaminoglycanase activity was 1.12 units / mL, the fermentation was completed, and 4.7 L of a crude enzyme solution for hydrolysis was obtained. Protease activity and glycosaminoglycanase activity were measured by the method of Example 1.
イカ内臓の切片10kgを量って取り、均質装置を用いて2000r/minで10分粉砕し、約9.4Lのペースト状物を得、酵素生産発酵生成物を入れた発酵槽に移し、2.0mol/Lの酢酸で溶液のpHを7.0に調節し、温度を50℃にし、撹拌速度100r/minで5時間反応させ、グリコシル側鎖が破壊された粗タンパク質酵素分解物を得た。 Take a 10 kg slice of squid viscera and grind it at 2000 r / min for 10 minutes using a homogenizer to obtain a paste of about 9.4 L, transfer to a fermentor containing the enzyme-produced fermentation product, 2 The pH of the solution was adjusted to 7.0 with 0.0 mol / L acetic acid, the temperature was adjusted to 50 ° C., and the mixture was reacted at a stirring speed of 100 r / min for 5 hours to obtain a crude protein enzyme degradation product in which the glycosyl side chain was broken. .
グリコシル側鎖が破壊された粗タンパク質酵素分解物にブロメライン18.15gを加え、酵素用量をイカ内臓原料1gにつき約1500ユニット(酵素活性)にする。均一になるまで撹拌した後、反応温度を35℃に設定し、撹拌速度50 r/min、pHは6.5、反応時間4時間とした。反応が終わったら、撹拌を止め、生成物を静置して油層と水層に分離させ、上層の粗油を除去してから、サンプリングしイカオリゴペプチドの収率とアミノ酸収率を測定したところ、結果はそれぞれ46%と22%であった。酵素分解物はただちに噴霧乾燥し、イカオリゴペプチド粉末1630gを得た。オリゴペプチド収率とアミノ酸収率は実施例1の方法で計算した。 Bromelain (18.15 g) is added to the crude protein enzyme degradation product in which the glycosyl side chain is broken, and the enzyme dose is about 1500 units (enzyme activity) per g of squid viscera raw material. After stirring until uniform, the reaction temperature was set to 35 ° C., the stirring speed was 50 r / min, the pH was 6.5, and the reaction time was 4 hours. When the reaction is over, the stirring is stopped, the product is allowed to stand to separate into an oil layer and an aqueous layer, the crude oil in the upper layer is removed, and then the yield of the squid oligopeptide and the amino acid yield are measured by sampling. The results were 46% and 22%, respectively. The enzyme degradation product was immediately spray-dried to obtain 1630 g of squid oligopeptide powder. The oligopeptide yield and amino acid yield were calculated by the method of Example 1.
ハイブリッドティラピア(Oreochromis niloticus x O. aureus)の種苗は広東柏士聯羅非魚苗養殖場の提供で、孵化1日の同一群のハイブリッドティラピア仔魚である。実験前にまず仔魚を50リットルのプラスチック槽に放して2日馴化させ、馴化期間は給餌しなかった。 Hybrid tilapia (Oreochromis niloticus x O. aureus) seedlings are provided by Guangdong Mandala non-fish seedling farm and are the same group of hybrid tilapia larvae on the day of hatching. Prior to the experiment, the larvae were first released into a 50 liter plastic tank and acclimatized for 2 days, and were not fed during the acclimatization period.
ハイブリッドティラピア種苗を1つの対照群と4つの実験群に分けた。このうち対照群に用いる飼料配合は魚粉46%、麦芽根15%、タピオカでん粉19%、酵母3%、大豆レシチン1%、コリン0.5%、リン酸水素カルシウム0.5%、調合ビタミン0.4%、調合ミネラル塩0.6%、セルロース8%、大豆油1%、アルギン酸ナトリウム1%、ゼラチン4%、実験群1に用いる飼料配合は魚粉41%、実施例1で得られたイカオリゴペプチド5%、麦芽根15%、タピオカでん粉19%、酵母3%、大豆レシチン1%、コリン0.5%、リン酸水素カルシウム0.5%、調合ビタミン0.4%、調合ミネラル塩0.6%、セルロース8%、大豆油1%、アルギン酸ナトリウム1%、ゼラチン4%、実験群2に用いる飼料配合は魚粉41%、実施例2で得られたイカオリゴペプチド5%、麦芽根15%、タピオカでん粉19%、酵母3%、大豆レシチン1%、コリン0.5%、リン酸水素カルシウム0.5%、調合ビタミン0.4%、調合ミネラル塩0.6%、セルロース8%、大豆油1%、アルギン酸ナトリウム1%、ゼラチン4%、実験群3に用いる飼料配合は魚粉36%、実施例1で得られたイカオリゴペプチド10%、麦芽根15%、タピオカでん粉19%、酵母3%、大豆レシチン1%、コリン0.5%、リン酸水素カルシウム0.5%、調合ビタミン0.4%、調合ミネラル塩0.6%、セルロース8%、大豆油1%、アルギン酸ナトリウム1%、ゼラチン4%、実験群4に用いる飼料配合は魚粉36%、実施例2で得られたイカオリゴペプチド10%、麦芽根15%、タピオカでん粉19%、酵母3%、大豆レシチン1%、コリン0.5%、リン酸水素カルシウム0.5%、調合ビタミン0.4%、調合ミネラル塩0.6%、セルロース8%、大豆油1%、アルギン酸ナトリウム1%、ゼラチン4%とした。相応の飼料配合を高水分条件において混ぜてスラリー状にし、50℃負圧(0.097 mPa)で乾燥、破砕し、篩にかけ、粒子の大きさ60〜80μmとし、得られた飼料は20℃の冷蔵庫に保管した。 Hybrid tilapia seedlings were divided into one control group and four experimental groups. Of these, the feed composition used for the control group is 46% fish meal, 15% malt root, 19% tapioca starch, 3% yeast, 1% soy lecithin, 0.5% choline, 0.5% calcium hydrogen phosphate, and 0% mixed vitamin .4%, formulated mineral salt 0.6%, cellulose 8%, soybean oil 1%, sodium alginate 1%, gelatin 4%, feed composition used in Experiment Group 1 was 41% fish meal, squid obtained in Example 1 Oligopeptide 5%, malt root 15%, tapioca starch 19%, yeast 3%, soybean lecithin 1%, choline 0.5%, calcium hydrogen phosphate 0.5%, formulated vitamin 0.4%, formulated mineral salt 0 .6%, cellulose 8%, soybean oil 1%, sodium alginate 1%, gelatin 4%, feed composition used in experimental group 2 is fish meal 41%, squid oligopeptide 5% obtained in Example 2, malt root 15 %, Pioca starch 19%, yeast 3%, soy lecithin 1%, choline 0.5%, calcium hydrogen phosphate 0.5%, formulated vitamin 0.4%, formulated mineral salt 0.6%, cellulose 8%, soybean oil 1%, sodium alginate 1%, gelatin 4%, feed composition used in Experimental Group 3 is fish meal 36%, squid oligopeptide 10% obtained in Example 1, malt root 15%, tapioca starch 19%, yeast 3% 1% soybean lecithin, 0.5% choline, 0.5% calcium hydrogen phosphate, 0.4% formulated vitamin, 0.6% formulated mineral salt, 8% cellulose, 1% soybean oil, 1% sodium alginate, Gelatin 4%, feed composition used in experimental group 4 is fish meal 36%, squid oligopeptide 10% obtained in Example 2, malt root 15%, tapioca starch 19%, yeast 3%, soybean lecithin 1%, coli 0.5%, 0.5% calcium hydrogen phosphate, formulated vitamins 0.4%, 0.6% Formulation mineral salts, cellulose 8%, 1% soybean oil, sodium alginate 1% and 4% gelatin. The corresponding feed composition was mixed in a high moisture condition to form a slurry, dried at 50 ° C. negative pressure (0.097 mPa), crushed, sieved to a particle size of 60-80 μm, and the resulting feed was 20 ° C. Stored in the refrigerator.
幼魚飼育槽にはエアストーンを置き、24時間空気を供給し、毎日50%の水を替え、槽底の廃棄物を吸引し(吸出し)、またサーモスタットで温度を27℃に制御した。毎日仔魚体重の10%の配合飼料を3回給餌し、実験周期は21日で、3回繰り返した。 An air stone was placed in the juvenile fish breeding tank, air was supplied for 24 hours, 50% of water was changed every day, waste at the bottom of the tank was sucked (sucked out), and the temperature was controlled at 27 ° C. with a thermostat. Each day, the diet containing 10% of the larvae's body weight was fed three times, and the experiment cycle was 21 days, which was repeated three times.
死亡率と体重増加率は下の方法により計算した。
実験の開始時と終了時にそれぞれハイブリッドティラピアの体重(0.001gまで正確に)及び幼魚の数を測定する。
死亡率=(実験開始時の幼魚数−実験終了時の幼魚数)/実験開始時の種苗数×100%
絶対体重増加率=(実験終了時の幼魚重量(g)−実験開始時の幼魚重量(g))/実験日数
Mortality and weight gain were calculated by the following methods.
The weight of the hybrid tilapia (accurately to 0.001 g) and the number of juveniles are measured at the start and end of the experiment, respectively.
Mortality = (number of larvae at start of experiment-number of larvae at end of experiment) / number of seedlings at start of experiment x 100%
Absolute weight gain rate = (weight of young fish at the end of experiment (g) −weight of young fish at the start of experiment (g)) / number of days of experiment
結果は、対照群の幼魚の死亡率は53%±8%、絶対体重増加率0.0053±0.0012g/日、実験群1の幼魚の死亡率は42%±10%、絶対体重増加率0.0062±0.0005g/日、実験群2の幼魚の死亡率は45%±10%、絶対体重増加率0.0068±0.0011g/日、実験群3の幼魚の死亡率は38%±2%、絶対体重増加率0.0075±0.0015g/日、実験群4の幼魚の死亡率は39%±6%、絶対体重増加率0.0069±0.0012g/日であった。 As a result, the mortality rate of the young fish in the control group was 53% ± 8%, the absolute weight gain rate was 0.0053 ± 0.0012 g / day, the mortality rate of the young fish in the experimental group 1 was 42% ± 10%, and the absolute weight gain rate. 0.0062 ± 0.0005 g / day, experimental group 2 larval mortality 45% ± 10%, absolute weight gain 0.0068 ± 0.0011 g / day, experimental group 3 larval mortality 38% ± 2%, absolute weight gain rate 0.0075 ± 0.0015 g / day, experimental group 4 larval mortality rate was 39% ± 6%, absolute weight gain rate 0.0069 ± 0.0012 g / day.
Claims (3)
(1)請求項1に記載のBacillus barbaricus SCSIO 02429の菌種を菌種活性化培地に移し入れ、30〜37℃で18〜24時間培養し、活性化後に、酵素生産誘導発酵培地を入れた容器に加え、pH=7.0〜8.0、30〜37℃の条件で12〜24時間発酵させ、発酵液のプロテアーゼ活性が2000〜3000ユニット/mLに達し、グリコサミノグリカナーゼ活性が0.95〜1.12ユニット/mLに達したときのグリコシル基加水分解用粗酵素溶液を得る工程であって、前記酵素生産誘導発酵培地は、イカ内臓スラリー、ペプトン、酵母エキス、複合塩及び水を質量比20〜30:5:5:10:1000で混合・加熱して溶かして作成され、前記複合塩は、塩化ナトリウム、硫酸カリウム、塩化マグネシウム及び塩化アンモニウムを質量比5〜8:2:2:3で混合したものである工程、
(2)イカ内臓原料をスラリー状に破砕後、手順(1)に記載の粗酵素溶液と体積比1:1〜2:1で混ぜて酵素分解を行い、反応開始時のpHが6.5〜7.0、温度が40〜50℃、時間が5〜8時間で、グリコシル側鎖が破壊された粗タンパク質酵素分解物を得る工程、及び、
(3)イカ内臓原料1グラムにつきブロメライン1000〜1500ユニット(酵素活性)の比率で、ブロメラインを手順(2)で得られた粗タンパク質酵素分解物に加え、pHを6.5〜7.0に調節し、35〜40℃で4〜6時間反応させ、得られた酵素分解物を静置して粗脂肪層と水層に分離し、脂肪層を除去し乾燥させてイカオリゴペプチドを得る工程を含む方法。 A method for preparing squid oligopeptides, comprising:
(1) The Bacillus barbaricus SCSIO 02429 bacterial species according to claim 1 was transferred to a bacterial species activation medium, cultured at 30 to 37 ° C. for 18 to 24 hours, and after activation, an enzyme production induction fermentation medium was added. In addition to the container, fermentation is carried out for 12 to 24 hours under the conditions of pH = 7.0 to 8.0 and 30 to 37 ° C., the protease activity of the fermentation solution reaches 2000 to 3000 units / mL, and the glycosaminoglycanase activity is A step of obtaining a crude enzyme solution for glycosyl group hydrolysis when reaching 0.95 to 1.12 units / mL, wherein the enzyme production induction fermentation medium comprises squid visceral slurry, peptone, yeast extract, complex salt and It is made by mixing and heating water at a mass ratio of 20-30: 5: 5: 10: 1000 and dissolving, and the complex salt is made of sodium chloride, potassium sulfate, chloride Magnesium and ammonium chloride weight ratio 5-8: 2: 2: step is a mixture with 3,
(2) After crushing the squid viscera raw material into a slurry, it is mixed with the crude enzyme solution described in the procedure (1) at a volume ratio of 1: 1 to 2: 1 to perform enzymatic decomposition, and the pH at the start of the reaction is 6.5. -7.0, obtaining a crude protein enzyme degradation product having a glycosyl side chain broken at a temperature of 40-50 ° C for 5-8 hours, and
(3) Bromelain is added to the crude protein enzyme degradation product obtained in step (2) at a ratio of 1000-1500 units (enzyme activity) of bromelain per gram of squid viscera, and the pH is adjusted to 6.5-7.0. Adjusting, reacting at 35 to 40 ° C. for 4 to 6 hours, allowing the obtained enzyme degradation product to stand to separate into a crude fat layer and an aqueous layer, removing the fat layer and drying to obtain a squid oligopeptide Including methods.
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