JPH08112064A - New production process of peptide mixture - Google Patents

New production process of peptide mixture

Info

Publication number
JPH08112064A
JPH08112064A JP6274304A JP27430494A JPH08112064A JP H08112064 A JPH08112064 A JP H08112064A JP 6274304 A JP6274304 A JP 6274304A JP 27430494 A JP27430494 A JP 27430494A JP H08112064 A JPH08112064 A JP H08112064A
Authority
JP
Japan
Prior art keywords
protein
amino acid
amount
peptide mixture
free
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
JP6274304A
Other languages
Japanese (ja)
Other versions
JP3396001B2 (en
Inventor
Seiichi Shimamura
誠一 島村
Yoshitaka Tamura
吉隆 田村
Hiroshi Miyagawa
博 宮川
Hitoshi Saito
仁志 齋藤
Yasushi Kawaguchi
靖 川口
Yoko Akazome
陽子 赤染
Hiroshi Ochi
浩 越智
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.)
Morinaga Milk Industry Co Ltd
Original Assignee
Morinaga Milk Industry Co Ltd
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
Priority to JP27430494A priority Critical patent/JP3396001B2/en
Application filed by Morinaga Milk Industry Co Ltd filed Critical Morinaga Milk Industry Co Ltd
Priority to DK95934302T priority patent/DK0799577T3/en
Priority to PCT/JP1995/002109 priority patent/WO1996011584A1/en
Priority to US08/817,095 priority patent/US5952193A/en
Priority to EP95934302A priority patent/EP0799577B1/en
Priority to DE69523791T priority patent/DE69523791T2/en
Priority to NZ294046A priority patent/NZ294046A/en
Priority to CA002202633A priority patent/CA2202633C/en
Priority to AU36738/95A priority patent/AU692612B2/en
Publication of JPH08112064A publication Critical patent/JPH08112064A/en
Priority to AU63603/98A priority patent/AU701507B2/en
Priority to US09/316,957 priority patent/US6395508B1/en
Application granted granted Critical
Publication of JP3396001B2 publication Critical patent/JP3396001B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Peptides Or Proteins (AREA)

Abstract

PURPOSE: To stably obtain a peptide mixture having almost constant content of each free amino acid and total amount of the free amino acids. CONSTITUTION: A peptide mixture having a constant quality is obtained by adding one or more kinds of protease to an aqueous solution of raw protein composed of one or more kinds of protein or an aqueous solution of preparatorily lightly hydrolyzed raw protein, starting hydrolysis of the raw protein or previously lightly hydrolyzed raw protein, quickly determining the amount of a specific amino acid isolated into the hydrolyzing solution by hydrolysis with passage of time, calculating the ratio of an amount of free specific amino acid to the total amount of specific amino acid contained in the raw protein or previously lightly hydrolyzed raw protein and stopping the hydrolysis as soon as the calculated value reaches the prescribed specific range.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、所定量の遊離アミノ酸
を含有したペプチド混合物を、常に安定した状態で、一
定の品質で製造する方法に関するものである。詳しく
は、本発明は、1種若しくは2種以上の蛋白質からなる
原料蛋白質の水溶液又は予め軽度に加水分解した原料蛋
白質の水溶液(以下これらの水溶液をまとめて原料水溶
液と記載することがある)に、蛋白分解酵素を添加し、
原料蛋白質又は予め軽度に加水分解した原料蛋白質の加
水分解を開始し、加水分解により分解液中に遊離した特
定アミノ酸の量を経時的に測定し、原料蛋白質又は予め
軽度に加水分解した原料蛋白質に含まれる特定アミノ酸
の総量に対する遊離した特定アミノ酸の量の割合を算出
し、その算出した値が予め設定された特定の範囲内に達
したとき直ちに加水分解を停止することを特徴とするペ
プチド混合物の新規な製造法、である。本明細書におい
て、百分率は、特に断りのない限り、重量による表示で
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a peptide mixture containing a predetermined amount of free amino acids in a stable state and with a constant quality. Specifically, the present invention relates to an aqueous solution of a raw material protein consisting of one or more kinds of proteins or an aqueous solution of a raw material protein that has been slightly hydrolyzed in advance (hereinafter, these aqueous solutions may be collectively referred to as a raw material aqueous solution). , Add proteolytic enzyme,
Start the hydrolysis of the raw material protein or the raw material protein that has been slightly hydrolyzed beforehand, and measure the amount of the specific amino acid released in the decomposition solution by hydrolysis over time to obtain the raw material protein or the raw material protein that has been previously lightly hydrolyzed. The ratio of the amount of free specific amino acid to the total amount of specific amino acid contained is calculated, and the hydrolysis is immediately stopped when the calculated value reaches a preset specific range. A new manufacturing method. As used herein, percentages are by weight unless otherwise noted.

【0002】[0002]

【従来の技術】動物性蛋白質(獣乳、卵、肉類、魚類
等)又は植物性蛋白質(大豆、小麦等)を蛋白分解酵素
で分解して得られるペプチド混合物には、増粘性、起泡
性、抗酸化性、易消化吸収性、ミネラル可溶化性、低抗
原性等の性質、上皮細胞成長因子、細胞増殖因子、カル
シウム吸収促進機能、オピオイド様活性等の生理活性機
能が知られており(食品と開発、第26巻、第11号、
第28〜36ページ、1991年)、畜肉、水産練り製
品、パン、菓子、ミネラル強化食品、乳幼児用食品、ス
ポーツ飲料、一般栄養食品、経腸栄養剤、蛋白アレルギ
ー対応食品、特殊栄養食品、医薬品等の製造に不可欠な
原料の一つとなっている。
2. Description of the Related Art A peptide mixture obtained by degrading animal protein (animal milk, egg, meat, fish, etc.) or vegetable protein (soybean, wheat etc.) with a proteolytic enzyme has a thickening property and a foaming property. , Antioxidative property, digestive and absorbable property, mineral solubilizing property, low antigenic property, epidermal growth factor, cell growth factor, calcium absorption promoting function, and bioactive function such as opioid-like activity are known ( Food and Development, Volume 26, No. 11,
28-36, 1991), livestock meat, fish paste, bread, confectionery, mineral-fortified foods, infant foods, sports drinks, general nutrition foods, enteral nutritional supplements, protein allergy foods, special nutrition foods, pharmaceuticals, etc. It is one of the essential raw materials for the production of.

【0003】従来、これらの食品又は医薬品の製造に使
用されるペプチド混合物の製造方法としては、用途に応
じてそれぞれ異なるが、 a)遊離のアミノ酸の生成をできるだけ制限するために
原料蛋白質をエンドペプチダーゼのみで分解して目的の
ペプチド混合物を製造する方法 b)原料蛋白質をエンドペプチダーゼとエキソペプチダ
ーゼの組み合わせで分解し、逆に所定量の遊離アミノ酸
を含有させたペプチド混合物を製造する方法、及び、 c)これらペプチド混合物からウルトラフィルトレーシ
ョン(UF)、リバースオスモシス(RO)、ゲル濾
過、イオン交換樹脂法等の分離操作により更に目的とす
るペプチド混合物を精製、分取する方法、等に大別する
ことができる。
[0003] Conventionally, the method for producing a peptide mixture used for producing these foods or pharmaceuticals differs depending on the application, but a) In order to limit the production of free amino acids as much as possible, the starting protein is endopeptidase. A method of producing a desired peptide mixture by decomposing with only b) A method of producing a peptide mixture containing a predetermined amount of free amino acid by decomposing a starting protein with a combination of endopeptidase and exopeptidase, and c ) A method of further purifying and fractionating the desired peptide mixture from these peptide mixtures by separation operations such as ultrafiltration (UF), reverse osmosis (RO), gel filtration, ion exchange resin method, etc. can do.

【0004】それらの従来技術の幾つかを例示すれば次
のとおりである。 1)蛋白質をエンド型プロテアーゼ及びエキソ型プロテ
アーゼ共存水系下に、0.5〜10時間酵素分解し、苦
味の極めて少ない平均鎖長3〜10のオリゴペプチドを
得ることを特徴とするオリゴペプチド混合物の製造法が
開示されている(特開昭62−143697号公報)。
Some of those prior arts are as follows. 1) A mixture of oligopeptides, which is characterized by enzymatically decomposing a protein in an aqueous system coexisting with an endo-type protease and an exo-type protease for 0.5 to 10 hours to obtain an oligopeptide having an average chain length of 3 to 10 with extremely little bitterness. A manufacturing method is disclosed (Japanese Patent Laid-Open No. 62-143697).

【0005】2)任意の起源のタンパク質原料を水に5
〜20%(w/v)となるように分散させ、酸によってpH
を1〜4に調整し、2種以上の酸性プロテアーゼを同時
に又は逐次的に添加して25〜60℃の温度で8〜72
時間遊離のアミノ酸の生成をおさえつつ酵素分解反応を
行い低分子ペプチド組成物を製造する方法が開示されて
いる(特公昭57ー45560号公報)。
2) A protein raw material of arbitrary origin is added to water.
Disperse to ~ 20% (w / v) and add acid to adjust pH
Is adjusted to 1 to 4 and two or more kinds of acidic proteases are added simultaneously or sequentially to obtain 8 to 72 at a temperature of 25 to 60 ° C.
A method for producing a low-molecular peptide composition by carrying out an enzymatic decomposition reaction while suppressing the production of free amino acids has been disclosed (Japanese Patent Publication No. 57-45560).

【0006】3)カゼイン溶液をカラムに詰めた固定化
酵素で部分分解する方法において、カゼイン溶液の通液
速度を制御してカゼインの部分分解物を製造する方法が
開示されている(特公平3−31421号公報)。
3) In the method of partially decomposing a casein solution with an immobilized enzyme packed in a column, a method of producing a partially decomposed product of casein by controlling the flow rate of the casein solution has been disclosed (Japanese Patent Publication No. Hei 3). -31421 publication).

【0007】4)溶解水等に蛋白質又は蛋白質を含有す
る物質と溶解促進剤を混合溶解した後、単数もしくは複
数の蛋白質分解酵素を添加し消化反応せしめて蛋白分解
物を製造するに際し、少なくとも前期蛋白分解物を添加
した後の溶液の粘度を経時的に計測し、該粘度が大きく
上昇して下降するその下降前に消化反応を停止すること
を特徴とする不溶解物の生成を防止した蛋白質分解物の
製造方法が開示されている(特公平3−58252号公
報)。
4) When a protein or a substance containing a protein and a dissolution accelerator are mixed and dissolved in dissolved water and the like, and one or more proteolytic enzymes are added and digested to produce a proteolytic product, at least the above A protein which prevents the formation of insoluble matter, characterized in that the viscosity of a solution after addition of a protein degradation product is measured with time, and the digestion reaction is stopped before the viscosity is greatly increased and decreased. A method for producing a decomposed product is disclosed (Japanese Patent Publication No. 3-58252).

【0008】5)獣乳κ−カゼイン由来のグリコポリペ
プチドのプロテアーゼ加水分解物であって、フィッシャ
ー値が30から60の範囲であるペプチド混合物を製造
する方法において、分解率が5〜25%となった時点で
加熱処理して酵素を失活させる方法が開示されている
(特開平2−300137号公報)。
5) A protease hydrolyzate of a glycopolypeptide derived from animal milk κ-casein, which has a decomposition rate of 5 to 25% in a method for producing a peptide mixture having a Fisher value in the range of 30 to 60. There is disclosed a method of inactivating the enzyme by heat treatment at the time when the temperature reaches (JP-A-2-300137).

【0009】6)乳蛋白質を固定化プロテアーゼで分解
して蛋白分解物を製造する方法において、ペプチドセン
サーでペプチド濃度を測定する方法及びペプチドの平均
鎖長を測定する方法が開示されている(食品産業バイオ
リアクターシステム技術研究組合編、「実践バイオリア
クター」、第166〜184ページ、食品産業バイオリ
アクターシステム技術研究組合発行、1990年)。
6) A method for producing a protein degradation product by decomposing a milk protein with an immobilized protease, a method of measuring the peptide concentration with a peptide sensor and a method of measuring the average chain length of the peptide have been disclosed. Industrial Bioreactor System Technology Research Association, "Practical Bioreactor", pp. 166-184, Food Industry Bioreactor System Technology Research Association, 1990).

【0010】7)小麦グルテンを固定化プロテアーゼで
分解してグルテン分解物を製造する方法において、グル
テン分解物の疎水性を逆相高速液体クロマトグラフィー
(以下高速液体クロマトグラフィーをHPLCと記載す
る)で経時的に計測して泡末安定性に優れたグルテン分
解物が製造できることが開示されている(食品産業バイ
オリアクターシステム技術研究組合編、「実践バイオリ
アクター」、第106〜126ページ、食品産業バイオ
リアクターシステム技術研究組合発行、1990年)。
7) In a method for producing a gluten degradation product by degrading wheat gluten with an immobilized protease, the hydrophobicity of the gluten degradation product is measured by reverse phase high performance liquid chromatography (hereinafter, high performance liquid chromatography is referred to as HPLC). It is disclosed that a gluten hydrolyzate excellent in foam stability can be produced by measuring with time (food industry bioreactor system technology research association, "Practical bioreactor", pp. 106-126, food industry bio. Published by Reactor System Technology Research Association, 1990).

【0011】8)味噌、醤油等の発酵食品の製造、リジ
ン、グルタミン酸等のアミノ酸発酵における工程管理に
おいて目的生産物である遊離アミノ酸量を測定すること
が知られている(食品工業、第34巻、第16号、第1
〜11ページ、1991年)。
8) It is known to measure the amount of free amino acid as a target product in the production of fermented foods such as miso and soy sauce, and process control in amino acid fermentation of lysine and glutamic acid (Food Industry, Volume 34). , No. 16, No. 1
~ Page 11, 1991).

【0012】[0012]

【発明が解決しようとする課題】上記従来技術に示され
るように、従来、蛋白分解酵素で原料の蛋白質を分解し
てペプチド混合物を製造する場合、分解反応の終点を、
反応時間、蛋白溶液の通液速度等を指標とし、分解物の
粘度、分解率、疎水度等を測定することにより決定して
いたが、これらの方法では、刻々変化する分解物の理化
学的性状、特に遊離のアミノ酸量を正確に把握すること
が極めて困難であり、従来のペプチド混合物の製造法に
おいては、製造バッチごとにペプチド混合物が含有する
遊離アミノ酸量及び組成が異なり、ペプチド混合物の品
質が一定しないという致命的な欠点がありその改善が強
く要請されている状況にあった。
As shown in the above-mentioned prior art, when a peptide mixture is conventionally produced by degrading a starting protein with a proteolytic enzyme, the end point of the degradation reaction is
It was determined by measuring the viscosity, decomposition rate, hydrophobicity, etc. of the decomposed product, using reaction time, flow rate of the protein solution, etc. as an index. , It is extremely difficult to accurately grasp the amount of free amino acids, and in the conventional method for producing a peptide mixture, the amount and composition of free amino acid contained in the peptide mixture are different for each production batch, and the quality of the peptide mixture is There was a fatal drawback that it was not constant and there was a strong demand for improvement.

【0013】このような状況の中で、本発明者らは、前
記従来技術に鑑みて、常に安定した状態で、一定の品質
でペプチド混合物を製造する方法について鋭意研究を行
った結果、加水分解物により分解液中に遊離する特定の
アミノ酸の量を、経時的に、かつ短時間で測定し、原料
蛋白質に含まれている該特定アミノ酸の量との割合を算
出し、その値が、特定の範囲内に達したときに直ちに加
水分解を停止することにより、所望のペプチド混合物が
得られることを見い出し、本発明を完成した。本発明の
目的は、遊離アミノ酸の量及び組成が一定し、品質が良
好であるペプチド混合物を容易に製造し得る新規な方法
を提供することにある。
Under these circumstances, the inventors of the present invention have conducted diligent research on a method for producing a peptide mixture with a constant quality in a stable state in view of the above-mentioned prior art. The amount of the specific amino acid released in the decomposition solution by the substance is measured over time and in a short time, and the ratio with the amount of the specific amino acid contained in the raw material protein is calculated. The present invention has been completed by finding that the desired peptide mixture can be obtained by stopping the hydrolysis as soon as it reaches within the range. An object of the present invention is to provide a novel method capable of easily producing a peptide mixture having a constant amount and composition of free amino acids and good quality.

【0014】[0014]

【課題を解決するための手段】前記課題を解決する本発
明は、一定品質のペプチド混合物の製造法であって、1
種若しくは2種以上の蛋白質からなる原料蛋白質の水溶
液又は予め軽度に加水分解した原料蛋白質の水溶液に、
1種若しくは2種以上の蛋白分解酵素を添加し、原料蛋
白質又は予め軽度に加水分解した原料蛋白質の加水分解
を開始し、加水分解により分解液中に遊離した特定アミ
ノ酸の量を経時的に、かつ短時間で測定し、原料蛋白質
又は予め軽度に加水分解した原料蛋白質に含まれる特定
アミノ酸の総量に対する遊離した特定アミノ酸の量の割
合を算出し、その算出した値が予め設定された特定の範
囲内に達したとき直ちに加水分解を停止することを特徴
とするペプチド混合物の製造法であり、特定アミノ酸
が、リジン、フェニルアラニン、ロイシン又はアルギニ
ンであることを望ましい態様としてもいる。
The present invention for solving the above-mentioned problems provides a method for producing a peptide mixture of constant quality, which comprises the steps of:
To an aqueous solution of a raw material protein consisting of two or more kinds of proteins, or an aqueous solution of a raw material protein which has been slightly hydrolyzed in advance,
One or more proteolytic enzymes are added to start the hydrolysis of the raw material protein or the raw material protein that has been slightly hydrolyzed in advance, and the amount of the specific amino acid released in the degradation solution by the hydrolysis can be measured with time. And measured in a short time, calculate the ratio of the amount of specific amino acid released to the total amount of specific amino acids contained in the raw material protein or raw protein slightly hydrolyzed in advance, the calculated value is a preset specific range The method for producing a peptide mixture is characterized in that the hydrolysis is stopped immediately when the content reaches the inside, and it is also a preferable embodiment that the specific amino acid is lysine, phenylalanine, leucine or arginine.

【0015】次に本発明について詳述する。本発明の方
法の出発原料として使用する原料蛋白質は、動物性蛋白
質(例えば、獣乳由来、卵由来、魚肉由来、畜肉由来
等)、植物性蛋白質(穀類由来、海草由来、種子由来
等)又はこれらの任意の混合物であり、特に限定される
ものではない。また、蛋白質を予め軽度に加水分解した
分解物であって、更に蛋白分解酵素により分解し得る大
きい分子量のペプチド混合物を出発原料とすることもで
きる。原料蛋白質又は予め軽度に加水分解した原料蛋白
質を、蛋白質換算で10%前後の濃度で水に溶解し、溶
解液のpHをアルカリ溶液又は酸溶液を用いて、使用す
る蛋白分解酵素の至適pH付近に調整し、原料水溶液を
調製する。
Next, the present invention will be described in detail. The raw material protein used as the starting material of the method of the present invention is animal protein (for example, animal milk-derived, egg-derived, fish meat-derived, meat-derived etc.), vegetable protein (cereal-derived, seaweed-derived, seed-derived, etc.) or It is an arbitrary mixture of these and is not particularly limited. Alternatively, a starting material may be a peptide mixture having a large molecular weight, which is a degradation product obtained by lightly hydrolyzing a protein in advance and which can be further degraded by a protease. The starting protein or the starting protein that has been slightly hydrolyzed in advance is dissolved in water at a concentration of about 10% in terms of protein, and the pH of the solution is adjusted to the optimum pH of the proteolytic enzyme by using an alkaline solution or an acid solution. Adjust to the vicinity and prepare the raw material aqueous solution.

【0016】次いで、前記原料水溶液に動物由来(例え
ば、パンクレアチン、ペプシン、トリプシン等)、植物
由来(例えば、パパイン、ブロメライン等)、微生物由
来(例えば、かび、放線菌、細菌、乳酸菌等)の蛋白分
解酵素又はこれらの任意の組合わせの蛋白分解酵素を目
的に応じ適宜選択し、所定量を添加する。例えば、エン
ドペプチダーゼを原料蛋白質1g当たり2000〜50
00PUN単位、エキソペプチダーゼを原料蛋白質1g
当たり20〜100活性単位の添加を、望ましい態様と
して例示することができる(PUN単位及び活性単位に
ついては後記する)。
Then, the raw material aqueous solution may be of animal origin (eg, pancreatin, pepsin, trypsin, etc.), plant origin (eg, papain, bromelain, etc.), microbial origin (eg, mold, actinomycete, bacterium, lactic acid bacterium, etc.). A proteolytic enzyme or a proteolytic enzyme in any combination thereof is appropriately selected according to the purpose, and a predetermined amount is added. For example, endopeptidase is added in an amount of 2000 to 50 per 1 g of the starting protein.
00 PUN unit, exopeptidase as raw material protein 1 g
Addition of 20 to 100 active units per unit can be exemplified as a desirable mode (PUN units and active units will be described later).

【0017】所定量の酵素を添加した原料水溶液は、通
常は酵素の至適温度に所定時間保持して蛋白質の酵素に
よる加水分解を行い、分解中に微生物の増殖が懸念され
る場合は、必要に応じて酵素の至適温度より高温域又は
低温域の温度に所定時間保持して蛋白質の酵素による加
水分解を行うこともできる。
A raw material aqueous solution to which a predetermined amount of enzyme has been added is usually kept at the optimum temperature of the enzyme for a predetermined time to hydrolyze the protein by the enzyme, and it is necessary if the growth of microorganisms is concerned during the decomposition. Depending on the conditions, the temperature of the enzyme may be kept at a temperature higher or lower than the optimum temperature for a predetermined time to hydrolyze the protein by the enzyme.

【0018】加水分解を開始し、分解液中に遊離した特
定アミノ酸の量を経時的に、かつ短時間で測定する。具
体的には、例えば、HPLC、バイオテックアナライザ
ー(旭化成工業社製)、パフュージョン・クロマトグラ
フィー(パーセプティブ・バイオシステム社製。BioCA
D)等を用いることができる。使用する原料蛋白質及び
酵素の種類により遊離するアミノ酸の量が異なるので、
大量に遊離するアミノ酸を特定アミノ酸として選択する
のが望ましい。特に望ましい態様として、分解液中に遊
離した特定アミノ酸の量をオンラインにより、測定する
ことを例示できる。また、特定アミノ酸としては、リジ
ン、フェニルアラニン、ロイシン、アルギニン等が特に
好適なものとして例示される。これらにより、分解液中
に遊離した特定アミノ酸の量を経時的に、かつ短時間に
測定し、出発原料である蛋白質に含まれる特定アミノ酸
の総量に対する遊離した特定アミノ酸量の割合が予め設
定された特定の範囲に達した時、直ちに反応液中の酵素
を失活又は除去し、加水分解を停止する。前記特定の範
囲は、目的とするペプチド混合物、使用する原料、使用
する酵素等により異なるが、例えば、遊離したリジンの
量を経時的、かつ短時間で測定しながら、乳清蛋白質を
加水分解する場合、遊離リジンの量の範囲として5〜4
0%を例示することができる。
After the hydrolysis is started, the amount of the specific amino acid released in the decomposition solution is measured with time and in a short time. Specifically, for example, HPLC, Biotech analyzer (manufactured by Asahi Kasei Corporation), perfusion chromatography (manufactured by Perceptive Biosystems. BioCA.
D) etc. can be used. Since the amount of released amino acid varies depending on the type of raw material protein and enzyme used,
It is desirable to select an amino acid that is released in a large amount as the specific amino acid. As a particularly desirable mode, online measurement of the amount of the specific amino acid released in the decomposition solution can be exemplified. Further, as the specific amino acid, lysine, phenylalanine, leucine, arginine and the like are exemplified as particularly preferable ones. With these, the amount of the specific amino acid released in the decomposition solution was measured over time and in a short time, and the ratio of the amount of the specific amino acid released to the total amount of the specific amino acid contained in the protein as the starting material was preset. When the specific range is reached, the enzyme in the reaction solution is immediately inactivated or removed to stop the hydrolysis. The specific range varies depending on the target peptide mixture, the starting material used, the enzyme used, etc., but for example, the whey protein is hydrolyzed while measuring the amount of free lysine over time and in a short time. In this case, the range of the amount of free lysine is 5 to 4
0% can be exemplified.

【0019】本発明において、反応液中の酵素を失活又
は除去して加水分解を停止する方法は、特に限定される
ものではなく、適宜の方法が使用されるが、該加水分解
を停止するまでに、時間的ずれを伴う場合もあり(例え
ば、ある量の分解液を加熱し、酵素を失活させるまで、
30〜60分を要する場合もある)、この場合加水分解
が進行するおそれがあるので、予め予備試験を行い、所
定の条件のもとに、分解の進行程度(例えば、特定の遊
離アミノ酸の生成速度)を測定し、酵素の失活又は除去
に要する時間を考慮し、前記特定の範囲を決定し、設定
することが望ましい。
In the present invention, the method of inactivating or removing the enzyme in the reaction solution to stop the hydrolysis is not particularly limited, and an appropriate method can be used, but the hydrolysis is stopped. May be accompanied by a time lag (for example, until a certain amount of decomposition solution is heated to inactivate the enzyme,
It may take 30 to 60 minutes). In this case, hydrolysis may proceed, so a preliminary test is performed in advance, and the degree of progress of the decomposition (for example, production of a specific free amino acid is performed under predetermined conditions). It is desirable that the specific range is determined and set in consideration of the time required to inactivate or remove the enzyme by measuring the (rate).

【0020】分解を終了したペプチド混合物を含有する
分解液を、公知の方法により濃縮し、濃縮液とすること
もでき、また、この濃縮液を公知の方法により乾燥し、
粉末とすることもできる。更に、ペプチド混合物を含有
する液を、限外濾過、ゲル濾過等公知の方法により精製
し、公知の方法により濃縮し、濃縮液とすることもで
き、また、この濃縮液を公知の方法により乾燥し、粉末
とすることもできる。
The decomposed solution containing the peptide mixture after the decomposition can be concentrated by a known method to obtain a concentrated solution, and the concentrated solution is dried by a known method.
It can also be made into powder. Further, the liquid containing the peptide mixture can be purified by a known method such as ultrafiltration and gel filtration, and concentrated by a known method to give a concentrated solution, and the concentrated solution is dried by a known method. However, it can also be made into powder.

【0021】また、加水分解を行う反応容器の形状(例
えば、タンク式、チューブ式、カラム式等)、分解処理
方式(例えば、回分式、連続式、逐次式等)、酵素の失
活、分離又は除去方法、ペプチドの精製方法等は、公知
の方法及び装置を使用することが可能であり、特に限定
されるものではない。以上のようにして、遊離アミノ酸
の量及び組成が常に一定であり、かつ品質が変動しない
ペプチド混合物を製造し得る。
The shape of the reaction vessel for hydrolysis (eg tank type, tube type, column type, etc.), decomposition treatment method (eg batch type, continuous type, sequential type, etc.), enzyme deactivation, separation Alternatively, known methods and devices can be used for the removal method, the peptide purification method, etc., and are not particularly limited. As described above, a peptide mixture in which the amount and composition of free amino acids are always constant and the quality does not change can be produced.

【0022】前記PUN単位及び活性単位は、次のとお
りである。エンドペプチダーゼのPUN単位は、カゼイ
ン[ハマーシュタイン(Hammerstein)。メルク社製]に
エンドペプチダーゼを作用させ、30℃で1分間に1μ
gのチロシンに相当するアリルアミノ酸のフォリン試薬
での呈色反応を示す酵素活性が1PUN単位である。
The PUN unit and the activity unit are as follows. The PUN unit of endopeptidase is casein [Hammerstein]. Manufactured by Merck & Co., Inc.] is treated with endopeptidase, and 1 μm per minute at 30 ° C.
The enzyme activity showing the color reaction of the allyl amino acid corresponding to g of tyrosine with the Folin reagent is 1 PUN unit.

【0023】また、エキソペプチダーゼの活性単位は、
次の方法により測定した。エキソペプチダーゼを含有す
る粉末を0.2g/100mlの割合で0.1モルのリ
ン酸緩衝液(pH7.0)に分散又は溶解し酵素溶液と
する。一方、ロイシルパラニトロアニリド(国産化学社
製。以下Leu−pNAと記載する)を0.1モルのリ
ン酸緩衝液(pH7.0)に溶解して2mMの基質溶液
を調製する。酵素溶液1mlに基質溶液1mlを加え3
7℃で5分間反応させた後、30%の酢酸溶液2mlを
加えて反応を停止させる。反応液をメンブランフィルタ
ーで濾過し、波長410nmで濾液の吸光度を測定す
る。エキソペプチダーゼの活性単位は、1分間に1μm
olのLeu−pNAを分解するのに必要な酵素量が1
活性単位であり、次式により算出した。 活性単位(粉末1g当たり)=20×(A/B) (ただし、前記の式においてA及びBは、それぞれ波長
410nmにおける試料の吸光度及び0.25mMパラ
ニトロアニリンの吸光度である)
The activity unit of exopeptidase is
It was measured by the following method. A powder containing exopeptidase is dispersed or dissolved in a 0.1 mol phosphate buffer (pH 7.0) at a ratio of 0.2 g / 100 ml to prepare an enzyme solution. On the other hand, leucyl paranitroanilide (manufactured by Kokusan Kagaku KK, hereinafter referred to as Leu-pNA) is dissolved in 0.1 mol of a phosphate buffer (pH 7.0) to prepare a 2 mM substrate solution. Add 1 ml of substrate solution to 1 ml of enzyme solution 3
After reacting at 7 ° C. for 5 minutes, 2 ml of a 30% acetic acid solution is added to stop the reaction. The reaction solution is filtered with a membrane filter, and the absorbance of the filtrate is measured at a wavelength of 410 nm. The activity unit of exopeptidase is 1 μm per minute
The amount of enzyme required to decompose Leu-pNA of ol is 1
It is an activity unit and calculated by the following formula. Activity unit (per 1 g of powder) = 20 × (A / B) (where A and B are the absorbance of the sample at a wavelength of 410 nm and the absorbance of 0.25 mM paranitroaniline, respectively)

【0024】次に、試験例を示して本発明を詳述する
が、本発明においては、次の試験方法を採用した。 (1)アミノ酸組成の測定方法 トリプトファン、システイン及びメチオニン以外のアミ
ノ酸については、試料を6N塩酸で110℃、24時間
加水分解し、トリプトファンについては、水酸化バリウ
ムで110℃、22時間アルカリ分解し、システイン及
びメチオニンについては、過ぎ酸処理後、6N塩酸で1
10℃、18時間加水分解し、それぞれアミノ酸分析機
(日立製作所製。835型)により分析し、アミノ酸の
質量を測定した。
Next, the present invention will be described in detail by showing test examples. In the present invention, the following test method was adopted. (1) Measuring method of amino acid composition For amino acids other than tryptophan, cysteine and methionine, the sample was hydrolyzed with 6N hydrochloric acid at 110 ° C. for 24 hours, and for tryptophan, it was alkali decomposed with barium hydroxide at 110 ° C. for 22 hours, For cysteine and methionine, treat with 1N of 6N hydrochloric acid after the treatment with excess acid.
It was hydrolyzed at 10 ° C. for 18 hours and analyzed with an amino acid analyzer (manufactured by Hitachi Ltd., model 835) to measure the mass of amino acids.

【0025】(2)遊離アミノ酸組成の測定方法 スルホサリチル酸で試料を除蛋白し、アミノ酸分析機
(日立製作所製。835型)により分析し、遊離アミノ
酸の質量を測定した。そして前記アミノ酸組成の分析で
得られた各アミノ酸の質量に対する遊離アミノ酸質量の
百分率を算出した。
(2) Method for measuring free amino acid composition The sample was deproteinized with sulfosalicylic acid and analyzed by an amino acid analyzer (Hitachi Ltd. model 835) to measure the mass of the free amino acid. Then, the percentage of the free amino acid mass to the mass of each amino acid obtained by the analysis of the amino acid composition was calculated.

【0026】(3)遊離リジン含量の測定方法 リジン測定用酵素電極、20mML−リジン標準液、
0.1M燐酸L−リジン測定用緩衝液及び洗浄用界面活
性剤(いずれも旭化成工業社製)を用い、バイオテック
アナライザー(旭化成工業社製)により遊離リジン濃度
を測定し、原料蛋白質のリジン含有量に対する分解溶液
のリジン含有量から全リジンに対する遊離リジンの量の
割合を算出した。
(3) Method for measuring free lysine content Enzyme electrode for lysine measurement, 20 mM L-lysine standard solution,
Free lysine concentration was measured by a Biotech analyzer (manufactured by Asahi Kasei Co., Ltd.) using a buffer for measuring L-lysine phosphate 0.1M and a surfactant for washing (both manufactured by Asahi Kasei Co., Ltd.), and the content of lysine in the raw material protein was measured. The ratio of the amount of free lysine to the total lysine was calculated from the lysine content of the decomposition solution with respect to the amount.

【0027】(4)HPLC Inertsil PREP-ODS(GLサイエンス社製。6.5×25
0mm)カラムをHPLC(島津製作所製)に装着し、
分解液0.1mlを供給し、溶離液A(0.1%トリフ
ルオロ酢酸溶液)に対する溶離液B(0.1%トリフル
オロ酢酸−アセトニトリル溶液)の割合が100分間で
50%となる濃度勾配で1.5ml/分の流速で溶出を
行った。
(4) HPLC Inertsil PREP-ODS (GL Science Co., Ltd. 6.5 × 25)
0mm) column is attached to HPLC (manufactured by Shimadzu Corporation),
A concentration gradient in which 0.1 ml of the decomposition solution is supplied and the ratio of the eluent B (0.1% trifluoroacetic acid-acetonitrile solution) to the eluent A (0.1% trifluoroacetic acid solution) becomes 50% in 100 minutes. Elution was carried out at a flow rate of 1.5 ml / min.

【0028】(5)分解率 分解率(%)は、原料蛋白質溶液の全窒素量当たりの分
解溶液のホルモル態窒素量の百分率であり、次の方法に
より求めた。蛋白分解溶液4mlと蒸留水30mlを混
合し、0.2N水酸化ナトリウム溶液又は塩酸溶液でp
Hを6.8に調整する。この溶液を0.2N水酸化ナト
リウム溶液でpHを8.0に調整したホルマリン溶液5
mlを添加し、0.1N水酸化ナトリウム溶液でpHが
7.9に達するまで滴定する。この時の滴定量をAm
l、0.1N水酸化ナトリウム溶液のファクターをF、
原料蛋白質溶液の蛋白濃度をB(%)として、分解率を
次式から算出した。 分解率(%)=22.3×A×F/B
(5) Degradation rate Degradation rate (%) is a percentage of the amount of formol nitrogen in the degradation solution per the total amount of nitrogen in the raw material protein solution, and was determined by the following method. Mix 4 ml of proteolytic solution with 30 ml of distilled water and p with 0.2N sodium hydroxide solution or hydrochloric acid solution.
Adjust H to 6.8. This solution was adjusted to pH 8.0 with 0.2N sodium hydroxide solution, formalin solution 5
ml is added and titrated with 0.1 N sodium hydroxide solution until the pH reaches 7.9. The titer at this time is Am
l, the factor of 0.1N sodium hydroxide solution is F,
The decomposition rate was calculated from the following equation, with the protein concentration of the raw material protein solution as B (%). Decomposition rate (%) = 22.3 x A x F / B

【0029】試験例1 この試験は、従来から採用されているペプチド混合物の
製造方法、即ち、反応時間を指標にして酵素分解を停
止する方法及び分解率を指標にして酵素分解を停止す
る方法と、本発明の方法とにより、ペプチド混合物を
製造し、得られたペプチド混合物の品質(遊離アミノ酸
組成及び遊離アミノ酸量の変動)に及ぼす影響を比較検
討した。
Test Example 1 This test consists of a conventionally used method for producing a peptide mixture, that is, a method of stopping the enzymatic decomposition using the reaction time as an index and a method of stopping the enzymatic decomposition using the decomposition rate as an index. The peptide mixture was produced by the method of the present invention, and the effects on the quality of the obtained peptide mixture (change in free amino acid composition and free amino acid amount) were compared and examined.

【0030】1)試料の調製 前記の方法では、酵素分解を4時間で停止したこと、
前記の方法では、酵素分解を分解率が23%に達した
時に停止したこと、前記の本発明の方法では、分解液
中の遊離リジン濃度を経時的に、かつ短時間で測定し、
リジンの遊離率が15%に達した時点で酵素分解を停止
したこと、を除き、実施例1と同一の方法により乳清蛋
白質溶液の加水分解をそれぞれ5回反復して実施し、合
計15種類の試料を調製した。
1) Preparation of sample In the above method, the enzymatic decomposition was stopped in 4 hours,
In the above method, enzymatic decomposition was stopped when the decomposition rate reached 23%, and in the above method of the present invention, the concentration of free lysine in the decomposition solution was measured over time and in a short time,
Hydrolysis of the whey protein solution was repeated 5 times in the same manner as in Example 1 except that the enzymatic degradation was stopped when the release rate of lysine reached 15%, and a total of 15 types were obtained. Samples were prepared.

【0031】2)試験方法 各試料の遊離アミノ酸量及び遊離アミノ酸組成を前記の
方法により測定し、5回の結果の平均値と標準偏差を算
出した。
2) Test Method The free amino acid amount and free amino acid composition of each sample were measured by the above-mentioned method, and the average value and standard deviation of the results of 5 times were calculated.

【0032】3)試験結果 この試験結果は表1に示すとおりである。表1から明ら
かなように、各方法で製造したペプチド混合物の各遊離
アミノ酸量及び遊離アミノ酸の合計量の平均値には多少
の差はあったが、遊離した各アミノ酸の量の標準偏差及
び遊離アミノ酸量の合計の標準偏差は、の本発明の方
法が最も小さく、安定しており、次いでの方法の変動
が少なく、の方法は最も変動が大きく製造上品質が不
安定であることが認められた。
3) Test Results The test results are shown in Table 1. As is clear from Table 1, although there were some differences in the average value of each free amino acid amount and the total amount of free amino acids in the peptide mixture produced by each method, the standard deviation and the free amount of each free amino acid were different. The standard deviation of the total amount of amino acids was found to be the smallest and stable for the method of the present invention, and the least for the following method, and for the method, the largest variation and unstable production quality were observed. It was

【0033】[0033]

【表1】 [Table 1]

【0034】試験例2 この試験は、試験例1とは異なる原料蛋白質及び分解条
件で、加水分解を実施した場合の各方法を比較するため
に行った。 1)試料の調製及び試験方法 蛋白質原料として牛乳カゼイン(商品名ALACID。
蛋白質含量90%。ニュージーランドデーリーボード
製)1kgを脱イオン水9kgに懸濁させ、20%カセ
イソーダ溶液でpHを7.0に調整して溶解したこと、
前記の方法では、酵素分解を9時間で停止したこと、
前記の方法では、酵素分解を分解率が30%に達した
時に停止したこと、及び前記の本発明の方法では、分
解液中の遊離リジン濃度を経時的に、かつ短時間で測定
し、リジンの遊離率が32%に達した時点で酵素分解を
停止したこと、を除き、試験例1と同一の方法により加
水分解をそれぞれ5回反復して実施し、合計15種類の
試料を調製した。
Test Example 2 This test was carried out in order to compare each method in the case where hydrolysis was carried out under different starting protein and decomposition conditions from Test Example 1. 1) Preparation of sample and test method Milk casein (trade name ALACID.
90% protein content. 1 kg of New Zealand Daily Board) was suspended in 9 kg of deionized water, and the pH was adjusted to 7.0 with a 20% caustic soda solution and dissolved.
In the above method, the enzymatic decomposition was stopped in 9 hours,
In the above method, the enzymatic decomposition was stopped when the decomposition rate reached 30%, and in the above method of the present invention, the concentration of free lysine in the decomposition solution was measured over time and in a short time. Hydrolysis was repeated 5 times in the same manner as in Test Example 1 except that the enzymatic decomposition was stopped when the liberation rate of was reached 32%, and a total of 15 types of samples were prepared.

【0035】2)試験結果 この試験結果は表2に示すとおりである。表2から明ら
かなように、各方法で製造したペプチド混合物の各遊離
アミノ酸量及び遊離アミノ酸の合計量の平均値には多少
の差はあったが、遊離した各アミノ酸の量の標準偏差及
び遊離アミノ酸量の合計の標準偏差は、の本発明の方
法が最も小さく、安定しており、次いでの方法であ
り、の方法は最も変動が大きく製造上品質が不安定で
あることが認められた。
2) Test Results The test results are shown in Table 2. As is clear from Table 2, although there were some differences in the average value of each free amino acid amount and the total amount of free amino acids in the peptide mixture produced by each method, the standard deviation and the free amount of each free amino acid were found. The standard deviation of the total amount of amino acids was found to be the smallest and stable in the method of the present invention, and the second method, and it was recognized that the method had the largest fluctuation and the production quality was unstable.

【0036】[0036]

【表2】 [Table 2]

【0037】試験例3 この試験は、試験例1及び試験例2とは異なる原料蛋白
質及び分解条件で、加水分解を実施した場合の各方法を
比較するために行った。 1)試料の調製及び試験方法 蛋白質原料として大豆蛋白(商品名SUPRO。蛋白含
量90%。不二製油社製)に変更したこと、前記の方
法では、酵素分解を6時間で停止したこと、前記,方
法では、酵素分解を分解率が13%に達した時に停止し
たこと、及び前記の本発明の方法では、分解液中の遊
離リジン濃度を経時的に、かつ短時間に測定し、リジン
の遊離率が21%に達した時点で酵素分解を停止したこ
と、を除き、試験例1と同一の方法により加水分解をそ
れぞれ5回反復して実施し、合計15種類の試料を調製
した。
Test Example 3 This test was carried out in order to compare the respective methods when hydrolysis was carried out under different starting protein and decomposition conditions from Test Example 1 and Test Example 2. 1) Preparation of sample and test method Soybean protein (trade name SUPRO. Protein content 90%, manufactured by Fuji Oil Co., Ltd.) was used as a protein raw material, and in the above method, enzymatic decomposition was stopped in 6 hours. In the method, the enzymatic decomposition was stopped when the decomposition rate reached 13%, and in the above-mentioned method of the present invention, the concentration of free lysine in the decomposition solution was measured with time and in a short time, and Hydrolysis was repeated 5 times in the same manner as in Test Example 1 except that the enzymatic decomposition was stopped when the liberation rate reached 21%, and a total of 15 types of samples were prepared.

【0038】2)試験結果 この試験結果は表3に示すとおりである。表3から明ら
かなように、各方法で製造したペプチド混合物の各遊離
アミノ酸量及び遊離アミノ酸の合計量の平均値には多少
の差はあったが、遊離した各アミノ酸の量の標準偏差及
び遊離アミノ酸量の合計の標準偏差は、の本発明の方
法が最も小さく、安定しており、次いでの方法であ
り、の方法は最も変動が大きく製造上品質が不安定で
あることが認められた。尚、蛋白質原料を畜肉、魚肉、
卵等に変更して同様に試験したが、いずれの場合も遊離
アミノ酸組成及び遊離アミノ酸量は、本発明の方法が最
も変動が少なく、安定していることが判明した。
2) Test Results The test results are shown in Table 3. As is clear from Table 3, although there were some differences in the average value of each free amino acid amount and the total amount of free amino acids of the peptide mixture produced by each method, the standard deviation and the free amount of each free amino acid were The standard deviation of the total amount of amino acids was found to be the smallest and stable in the method of the present invention, and the second method, and it was recognized that the method had the largest fluctuation and the production quality was unstable. In addition, protein raw material is used for livestock meat, fish meat,
The same test was carried out by changing to eggs and the like, and in each case, the free amino acid composition and the amount of free amino acids were found to be the least varied and stable in the method of the present invention.

【0039】[0039]

【表3】 [Table 3]

【0040】試験例4 この試験は、特定の遊離アミノ酸の測定方法を調べるた
めに行った。 1)試料の調製及び試験方法 バイオテックアナライザー(旭化成工業社製)の代わり
にHPLC(島津製作所製)を用いて経時的に、かつ短
時間で分解液の遊離リジンの量を測定したこと以外は、
前記試験例1のの方法と同一の方法により乳清蛋白質
からペプチド混合物を調製した。
Test Example 4 This test was conducted to investigate the method for measuring a specific free amino acid. 1) Preparation of sample and test method Except that the amount of free lysine in the decomposition solution was measured over time and in a short time by using HPLC (manufactured by Shimadzu Corporation) instead of Biotech Analyzer (manufactured by Asahi Kasei Corporation). ,
A peptide mixture was prepared from whey protein by the same method as in Test Example 1 above.

【0041】2)試験結果 この試験結果は表4に示すとおりである。表4から明ら
かなように、分解液の遊離リジンの量をバイオテックア
ナライザーで測定した場合も、HPLCで測定した場合
も、各アミノ酸の遊離量の平均値及び遊離アミノ酸量の
合計の平均値は異なるが、各アミノ酸の遊離量の標準偏
差及び遊離アミノ酸量の合計の標準偏差は、両者に大差
のないことが認められた。従って、これら遊離アミノ酸
量のいずれの測定方法も、本発明に使用し得ることが判
明した。尚、蛋白質の種類及び加水分解条件を変更して
試験したが、ほぼ同様な結果が得られた。
2) Test Results The test results are shown in Table 4. As is clear from Table 4, the average value of the free amount of each amino acid and the average value of the total amount of free amino acids were measured regardless of whether the amount of free lysine in the degradation solution was measured by a Biotech analyzer or HPLC. Although different, it was recognized that the standard deviation of the free amount of each amino acid and the standard deviation of the total amount of free amino acids were not significantly different between the two. Therefore, it was found that any of these measuring methods for the amount of free amino acid can be used in the present invention. It should be noted that, although the test was carried out by changing the kind of protein and the hydrolysis condition, almost the same result was obtained.

【0042】[0042]

【表4】 [Table 4]

【0043】試験例5 この試験は、測定する特定の遊離アミノ酸の種類を調べ
るために行った。 1)試料の調製及び試験方法 HPLC(島津製作所製)を用いて経時的に、かつ短時
間で分解液の遊離フェニルアラニンの量を測定し、遊離
フェニルアラニン量が25%に達した時点で酵素分解を
停止したことを除き、試験例2のの方法と同一の方法
によりカゼインからペプチド混合物を調製した。
Test Example 5 This test was conducted to examine the type of specific free amino acid to be measured. 1) Preparation of sample and test method Using HPLC (Shimadzu Corporation), the amount of free phenylalanine in the decomposition solution was measured over time and in a short time. When the amount of free phenylalanine reached 25%, enzymatic decomposition was performed. A peptide mixture was prepared from casein by the same method as in Test Example 2 except that it was stopped.

【0044】2)試験結果 この試験結果は表5に示すとおりである。表5から明ら
かなように、分解液の遊離フェニルアラニンの量を測定
した場合も、各アミノ酸の遊離量の標準偏差及び遊離ア
ミノ酸量の合計の標準偏差は小さく、カゼインから品質
の一定したペプチド混合物が、得られることが認められ
た。尚、蛋白質の種類及び加水分解条件を変更して試験
したが、ほぼ同様な結果が得られた。
2) Test Results The test results are shown in Table 5. As is clear from Table 5, even when the amount of free phenylalanine in the degradation solution was measured, the standard deviation of the free amount of each amino acid and the standard deviation of the total free amino acid amount were small, and a peptide mixture of constant quality was obtained from casein. , Was confirmed to be obtained. It should be noted that, although the test was carried out by changing the kind of protein and the hydrolysis condition, almost the same result was obtained.

【0045】[0045]

【表5】 [Table 5]

【0046】試験例6 この試験は、前記試験例5と同様に測定する特定の遊離
アミノ酸の種類を変更して試験した。 1)試料の調製及び試験方法 HPLC(島津製作所製)を用いて経時的に、かつ短時
間で分解液の遊離ロイシンの量を測定し、遊離ロイシン
量が10%に達した時点で酵素分解を停止したことを除
き、試験例3のの方法と同一の方法により大豆蛋白質
からペプチド混合物を調製した。
Test Example 6 This test was carried out in the same manner as in Test Example 5 except that the type of specific free amino acid measured was changed. 1) Preparation of sample and test method Using HPLC (manufactured by Shimadzu Corporation), the amount of free leucine in the decomposed solution was measured over time and in a short time, and enzymatic decomposition was performed when the amount of free leucine reached 10%. A peptide mixture was prepared from soybean protein by the same method as in Test Example 3 except that it was stopped.

【0047】2)試験結果 この試験結果は表6に示すとおりである。表6から明ら
かなように、分解液の遊離ロイシンの量を測定した場合
も、各アミノ酸の遊離量の標準偏差及び遊離アミノ酸量
の合計の標準偏差は小さく、大豆蛋白質から品質の一定
したペプチド混合物が、得られることが認められた。ま
た、遊離アルギニンの量を測定した場合についても、ほ
ぼ同様の結果が得られた。測定する特定アミノ酸の種類
を前記ロイシン及びアルギニン以外のアミノ酸に変更し
た場合、又は、蛋白質の種類及び加水分解条件を変更し
た場合についても試験したが、ほぼ同様な結果が得られ
た。
2) Test Results The test results are shown in Table 6. As is clear from Table 6, even when the amount of free leucine in the decomposition solution was measured, the standard deviation of the free amount of each amino acid and the standard deviation of the total amount of free amino acids were small, and the peptide mixture of soybean protein with a constant quality was obtained. Was found to be obtained. Also, when the amount of free arginine was measured, almost the same result was obtained. Tests were also performed when the type of the specific amino acid to be measured was changed to an amino acid other than leucine and arginine, or when the type of protein and the hydrolysis conditions were changed, but almost the same results were obtained.

【0048】[0048]

【表6】 [Table 6]

【0049】参考例1 コーンスティープリカー20部(重量。以下同じ)に水
道水100部及び石灰5部を添加し、コーンスティープ
リカーに含まれている酸を中和し、濾過助剤としてセラ
イト50部を添加して濾過し、濾液Aを得た。これとは
別に、フィシュリバー20部、モラセス35部及び水道
水200部の混合液にセライト50部を添加して濾過
し、濾液Bを得た。前記濾液A及び濾液B当量混合液5
00部にグルコース5部、リン酸一カリウム2.5部、
リン酸二カリウム2.5部及び酢酸ナトリウム5部を添
加し、30%水酸化ナトリウムでpHを6.4に調整
し、水を添加して1000部に調整した。
Reference Example 1 100 parts of tap water and 5 parts of lime were added to 20 parts of corn steep liquor (weight, the same applies hereinafter) to neutralize the acid contained in the corn steep liquor, and Celite 50 as a filter aid. And then filtered to obtain a filtrate A. Separately from this, 50 parts of Celite was added to a mixed solution of 20 parts of fish river, 35 parts of molasses and 200 parts of tap water and filtered to obtain a filtrate B. Equivalent mixture 5 of filtrate A and filtrate B
Glucose 5 parts to 00 parts, monopotassium phosphate 2.5 parts,
2.5 parts of dipotassium phosphate and 5 parts of sodium acetate were added, pH was adjusted to 6.4 with 30% sodium hydroxide, and water was added to adjust to 1000 parts.

【0050】滅菌した前記組成の培地10lにラクトバ
シラス・ヘルベティカスを培養し、得られた培養液を遠
心分離して乳酸菌菌体を回収し、滅菌水に菌体を懸濁
し、遠心分離して乳酸菌菌体を回収する操作を2回反復
して菌体を洗浄し、のち20%の濃度で菌体を滅菌水に
懸濁し、超音波破砕機(ブランソン社製。SONIFIER mod
el 250)により菌体を破砕し、凍結乾燥し、乳酸菌由来
のエキソペプチダーゼ粉末約25gを得た。
Lactobacillus helveticus was cultivated in 10 l of the sterilized medium having the above-mentioned composition, and the obtained culture solution was centrifuged to recover the lactic acid bacterium cells, which were suspended in sterilized water and centrifuged to remove the lactic acid bacterium. The operation of collecting the body is repeated twice to wash the cells, and then the cells are suspended in sterilized water at a concentration of 20%, and then ultrasonically disrupted (manufactured by Branson. SONIFIER mod
El 250), the cells were crushed and freeze-dried to obtain about 25 g of lactic acid bacterium-derived exopeptidase powder.

【0051】[0051]

【実施例】次に実施例を示して本発明を更に詳述する
が、本発明は以下の実施例に限定されるものではない。 実施例1 乳清蛋白質含量75%の市販乳清蛋白質粉末(カリフォ
ルニア・プロテイン社製)1kgを、脱イオン水9kg
に溶解し、70℃に5分間保持して殺菌し、pHを9.
0に調整し、市販のプロテアーゼNアマノ(天野製薬社
製)150万PUN単位(乳清蛋白質1g当たり200
0PUN単位)及び前記参考例1と同一の方法で調整し
たラクトバシラス・ヘルベチカス菌体破砕物4万活性単
位(乳清蛋白質1g当たり60活性単位)を添加し、5
0℃に保持して加水分解を開始し、バイオテックアナラ
イザー(旭化成工業社製)を用いて経時的に、かつ短時
間で遊離リジンの量を測定し、遊離リジン量が14%に
達した時点で、80℃で6分間加熱して酵素を失活さ
せ、酵素分解を停止させ、のち常法により凍結乾燥し、
乳清蛋白質からペプチド混合物約950gを得た。前記
の製造法を2回反復して得られたペプチド混合物を、前
記試験方法により試験した結果、各遊離アミノ酸の量及
び遊離アミノ酸の合計量にはほとんど差異が認められな
かった。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to the following examples. Example 1 1 kg of a commercial whey protein powder having a whey protein content of 75% (manufactured by California Protein Co.) and 9 kg of deionized water
And sterilized by holding at 70 ° C. for 5 minutes to adjust the pH to 9.
Adjusted to 0, commercially available Protease N Amano (manufactured by Amano Pharmaceutical Co., Ltd.) 1.5 million PUN units (200 per 1 g of whey protein)
0 PUN unit) and 40,000 active units of Lactobacillus helveticus cell disrupted product (60 active units per 1 g of whey protein) prepared by the same method as in Reference Example 1 were added, and 5
When hydrolysis was started by maintaining at 0 ° C, the amount of free lysine was measured with a biotech analyzer (manufactured by Asahi Kasei Kogyo Co., Ltd.) over time and in a short time, and when the amount of free lysine reached 14%. Then, heat at 80 ° C for 6 minutes to inactivate the enzyme, stop the enzymatic decomposition, and then freeze-dry by a conventional method,
About 950 g of a peptide mixture was obtained from whey protein. The peptide mixture obtained by repeating the above production method twice was tested by the above test method, and as a result, almost no difference was observed in the amount of each free amino acid and the total amount of the free amino acids.

【0052】実施例2 蛋白質含量80%の市販小麦蛋白粉末(理研ビタミン社
製。エマソフトEX−100)1kgを、脱イオン水9
kgに溶解し、pHを7.0に調整し、70℃で5分間
保持して殺菌した。この小麦蛋白質溶液に市販のパンク
レアチン(天野製薬社製)を200万PUN単位(小麦
蛋白質1g当たり2500PUN単位)及び前記参考例
1と同一の方法で調製したラクトバチルス・ヘルベチカ
ス菌体破砕物6万活性単位(小麦蛋白質1g当たり75
活性単位)を添加し、50℃に保持して加水分解を開始
し、バイオテックアナライザー(旭化成工業社製)を用
いて経時的に、かつ短時間で遊離リジンの量を測定し、
遊離リジン量が34%に達した時点で、80℃で10分
間加熱して酵素を失活させ、酵素分解を停止させ、のち
凍結乾燥し、小麦蛋白質からペプチド混合物約950g
を得た。前記の製造法を2回反復して得られたペプチド
混合物を、前記試験方法により試験した結果、各遊離ア
ミノ酸の量及び遊離アミノ酸の合計量にはほとんど差異
が認められなかった。
Example 2 1 kg of commercially available wheat protein powder (manufactured by Riken Vitamin Co., Emmasoft EX-100) having a protein content of 80% was mixed with 9 parts of deionized water.
It was dissolved in kg, the pH was adjusted to 7.0, and the mixture was kept at 70 ° C. for 5 minutes for sterilization. Commercially available pancreatin (manufactured by Amano Pharmaceutical Co., Ltd.) was added to this wheat protein solution in the amount of 2 million PUN units (2,500 PUN units per 1 g of wheat protein) and the Lactobacillus helveticus cell disruption product 6 prepared in the same manner as in Reference Example 1 above. 10,000 activity units (75 g / g wheat protein)
Activity unit), and the mixture is kept at 50 ° C. to start hydrolysis, and the amount of free lysine is measured with a biotech analyzer (Asahi Kasei Kogyo Co., Ltd.) over time and in a short time.
When the amount of free lysine reached 34%, the enzyme was inactivated by heating at 80 ° C for 10 minutes to stop the enzymatic decomposition, and then freeze-dried, and about 950 g of a peptide mixture from wheat protein was obtained.
I got The peptide mixture obtained by repeating the above production method twice was tested by the above test method, and as a result, almost no difference was observed in the amount of each free amino acid and the total amount of the free amino acids.

【0053】実施例3 蛋白質含量80%の市販小麦蛋白粉末(理研ビタミン社
製。エマソフトEX−100)500g及び蛋白質含量
90%の市販大豆蛋白粉末(不二製油社製。商品名SU
PRO)500gを脱イオン水9kgに溶解し、pHを
7.0に調整し、70℃で5分間保持して殺菌した。こ
の混合蛋白質溶液に市販のパンクレアチン(天野製薬社
製)85万PUN単位(蛋白質1g当たり1000PU
N単位)、プロテアーゼNアマノ(天野製薬社製)17
0万PUN単位(蛋白質1g当たり2000PUN単
位)及び前記参考例1と同一の方法で調製したラクトバ
チルス・ヘルベチカス菌体破砕物4万活性単位(蛋白質
1g当たり47活性単位)を添加し、50℃に保持して
加水分解を開始し、HPLC(島津製作所製)を用いて
経時的に、かつ短時間で遊離アルギニンの量を測定し、
遊離アルギニン量が21%に達した時点で80℃で10
分間加熱し、酵素を失活させ、酵素分解を停止させ、の
ち凍結乾燥し、ペプチド混合物約950gを得た。前記
の製造法を2回反復して得られたペプチド混合物を、前
記試験方法により試験した結果、各遊離アミノ酸の量及
び遊離アミノ酸の合計量にはほとんど差異が認められな
かった。
Example 3 500 g of a commercial wheat protein powder having a protein content of 80% (manufactured by Riken Vitamin Co., Emmasoft EX-100) and a commercially available soybean protein powder having a protein content of 90% (manufactured by Fuji Oil Co., trade name SU.
500 g of PRO) was dissolved in 9 kg of deionized water, the pH was adjusted to 7.0, and the mixture was kept at 70 ° C. for 5 minutes for sterilization. In this mixed protein solution, commercially available pancreatin (manufactured by Amano Pharmaceutical Co., Ltd.) 850,000 PUN units (1000 PU per 1 g of protein)
N units), Protease N Amano (manufactured by Amano Pharmaceutical Co., Ltd.) 17
Add 50,000 PUN units (2,000 PUN units per 1 g of protein) and 40,000 active units (47 active units per 1 g of protein) of Lactobacillus helveticus cell disruption product prepared by the same method as in Reference Example 1 above, and add at 50 ° C. To start hydrolysis and measure the amount of free arginine with HPLC (manufactured by Shimadzu Corporation) over time and in a short time,
When the amount of free arginine reaches 21%, 10 at 80 ° C
The mixture was heated for a minute to inactivate the enzyme, stop the enzymatic decomposition, and then freeze-dried to obtain about 950 g of a peptide mixture. The peptide mixture obtained by repeating the above production method twice was tested by the above test method, and as a result, almost no difference was observed in the amount of each free amino acid and the total amount of the free amino acids.

【0054】実施例4 乳清蛋白質含量75%の市販乳清蛋白質粉末(カリフォ
ルニア・プロテイン社製)500g及び蛋白質含量90
%の市販大豆蛋白粉末(不二製油社製。商品名SUPR
O)500gを脱イオン水9kgに溶解し、70℃に5
分間保持して殺菌し、pHを9.0に調整し、市販のプ
ロテアーゼNアマノ(天野製薬社製)250万PUN単
位(蛋白質1g当たり4848PUN単位)及び前記参
考例1と同一の方法で製造したラクトバチルス・ヘルベ
チカス菌体破砕物4万活性単位(蛋白質1g当たり48
活性単位)を添加し、50℃に保持して加水分解を開始
し、バイオテックアナライザー(旭化成工業社製)を用
いて経時的に、かつ短時間で遊離リジンの量を測定し、
遊離リジン量が18%に達した時点で80℃で6分間加
熱し、酵素を失活させ、酵素分解を停止させ、凍結乾燥
し、ペプチド混合物約950gを得た。前記の製造法を
2回反復して得られたペプチド混合物を、前記試験方法
により試験した結果、各遊離アミノ酸の量及び遊離アミ
ノ酸の合計量にはほとんど差異が認められなかった。
Example 4 500 g of a commercial whey protein powder (manufactured by California Protein Co.) having a whey protein content of 75% and a protein content of 90
% Commercial soy protein powder (manufactured by Fuji Oil Co., Ltd., trade name SUPR
O) 500 g is dissolved in 9 kg of deionized water and the mixture is heated to 70 ° C. for 5 times.
It was kept for minutes to be sterilized, the pH was adjusted to 9.0, and commercially available protease A Amano (manufactured by Amano Pharmaceutical Co., Ltd.) 2.5 million PUN units (4848 PUN units per 1 g of protein) and the same method as in Reference Example 1 were used. Lactobacillus helveticus cell disrupted product 40,000 activity units (48 per 1 g protein)
Activity unit), and the mixture is kept at 50 ° C. to start hydrolysis, and the amount of free lysine is measured with a biotech analyzer (manufactured by Asahi Kasei Kogyo Co., Ltd.) over time and in a short time.
When the amount of free lysine reached 18%, the mixture was heated at 80 ° C. for 6 minutes to inactivate the enzyme, stop the enzymatic decomposition, and freeze-dry to obtain about 950 g of a peptide mixture. The peptide mixture obtained by repeating the above production method twice was tested by the above test method, and as a result, almost no difference was observed in the amount of each free amino acid and the total amount of the free amino acids.

【0055】[0055]

【発明の効果】以上詳記したとおり本発明は、ペプチド
混合物の新規な製造法であり、本発明によって奏せられ
る効果は次のとおりである。 1)各遊離アミノ酸の量及び遊離アミノ酸の合計量がほ
ぼ一定のペプチド混合物が得られる。 2)目的とするペプチド混合物が常に安定して得られ
る。 3)一定品質のペプチド混合物を簡便に製造することが
できる。
As described above in detail, the present invention is a novel method for producing a peptide mixture, and the effects of the present invention are as follows. 1) A peptide mixture is obtained in which the amount of each free amino acid and the total amount of free amino acids are almost constant. 2) The desired peptide mixture is always stably obtained. 3) A peptide mixture of constant quality can be easily produced.

【手続補正書】[Procedure amendment]

【提出日】平成7年12月13日[Submission date] December 13, 1995

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0026[Correction target item name] 0026

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0026】(3)遊離リジン含量の測定方法 リジン測定用酵素電極、20mML−リジン標準液、
0.1M燐酸L−リジン測定用緩衝液及び洗浄用界面活
性剤(いずれも旭化成工業社製)を用い、バイオテック
アナライザー(旭化成工業社製)により遊離リジン濃度
を測定し、原料蛋白質のリジン含有量に対する分解溶液
遊離リジン含有量から全リジンに対する遊離リジンの
量の割合を算出した。
(3) Method for measuring free lysine content Enzyme electrode for lysine measurement, 20 mM L-lysine standard solution,
Free lysine concentration was measured by a Biotech analyzer (manufactured by Asahi Kasei Co., Ltd.) using a buffer for measuring L-lysine phosphate 0.1M and a surfactant for washing (both manufactured by Asahi Kasei Co., Ltd.), and the content of lysine in the raw material protein was measured. The ratio of the amount of free lysine to the total lysine was calculated from the free lysine content of the decomposition solution with respect to the amount.

【手続補正2】[Procedure Amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0051[Correction target item name] 0051

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0051】[0051]

【実施例】次に実施例を示して本発明を更に詳述する
が、本発明は以下の実施例に限定されるものではない。 実施例1 乳清蛋白質含量75%の市販乳清蛋白質粉末(カリフォ
ルニア・プロテイン社製)1kgを、脱イオン水9kg
に溶解し、70℃に5分間保持して殺菌し、pHを9.
0に調整し、市販のプロテアーゼNアマノ(天野製薬社
製)150万PUN単位(乳清蛋白質1g当たり200
0PUN単位)及び前記参考例1と同一の方法で調製
たラクトバシラス・ヘルベチカス菌体破砕物4万活性単
位(乳清蛋白質1g当たり60活性単位)を添加し、5
0℃に保持して加水分解を開始し、バイオテックアナラ
イザー(旭化成工業社製)を用いて経時的に、かつ短時
間で遊離リジンの量を測定し、遊離リジン量が14%に
達した時点で、80℃で6分間加熱して酵素を失活さ
せ、酵素分解を停止させ、のち常法により凍結乾燥し、
乳清蛋白質からペプチド混合物約950gを得た。前記
の製造法を2回反復して得られたペプチド混合物を、前
記試験方法により試験した結果、各遊離アミノ酸の量及
び遊離アミノ酸の合計量にはほとんど差異が認められな
かった。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to the following examples. Example 1 1 kg of a commercial whey protein powder having a whey protein content of 75% (manufactured by California Protein Co.) and 9 kg of deionized water
And sterilized by holding at 70 ° C. for 5 minutes to adjust the pH to 9.
Adjusted to 0, commercially available Protease N Amano (manufactured by Amano Pharmaceutical Co., Ltd.) 1.5 million PUN units (200 per 1 g of whey protein)
0 PUN unit) and 40,000 active units of Lactobacillus helveticus cell disruption product (60 active units per 1 g of whey protein) prepared by the same method as in Reference Example 1 were added, and
When hydrolysis was started by maintaining at 0 ° C, the amount of free lysine was measured with a biotech analyzer (manufactured by Asahi Kasei Kogyo Co., Ltd.) over time and in a short time, and when the amount of free lysine reached 14%. Then, heat at 80 ° C for 6 minutes to inactivate the enzyme, stop the enzymatic decomposition, and then freeze-dry by a conventional method,
About 950 g of a peptide mixture was obtained from whey protein. The peptide mixture obtained by repeating the above production method twice was tested by the above test method, and as a result, almost no difference was observed in the amount of each free amino acid and the total amount of the free amino acids.

【手続補正3】[Procedure 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0052[Correction target item name] 0052

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0052】実施例2 蛋白質含量80%の市販小麦蛋白粉末(理研ビタミン社
製。エマソフトEX−100)1kgを、脱イオン水9
kgに溶解し、pHを7.0に調整し、70℃で5分間
保持して殺菌した。この小麦蛋白質溶液に市販のパンク
レアチン(天野製薬社製)を200万PUN単位(小麦
蛋白質1g当たり2500PUN単位)及び前記参考例
1と同一の方法で調製したラクトバシラス・ヘルベチカ
ス菌体破砕物6万活性単位(小麦蛋白質1g当たり75
活性単位)を添加し、50℃に保持して加水分解を開始
し、バイオテックアナライザー(旭化成工業社製)を用
いて経時的に、かつ短時間で遊離リジンの量を測定し、
遊離リジン量が34%に達した時点で、80℃で10分
間加熱して酵素を失活させ、酵素分解を停止させ、のち
凍結乾燥し、小麦蛋白質からペプチド混合物約950g
を得た。前記の製造法を2回反復して得られたペプチド
混合物を、前記試験方法により試験した結果、各遊離ア
ミノ酸の量及び遊離アミノ酸の合計量にはほとんと差異
が認められなかった。
Example 2 1 kg of commercially available wheat protein powder (manufactured by Riken Vitamin Co., Emmasoft EX-100) having a protein content of 80% was mixed with 9 parts of deionized water.
It was dissolved in kg, the pH was adjusted to 7.0, and the mixture was kept at 70 ° C. for 5 minutes for sterilization. Commercially available pancreatin (manufactured by Amano Pharmaceutical Co., Ltd.) was added to this wheat protein solution for 2 million PUN units (2,500 PUN units per 1 g of wheat protein) and 60,000 crushed Lactobacillus helveticus cells prepared in the same manner as in Reference Example 1. Activity unit (75 per 1 g wheat protein)
Activity unit), and the mixture is kept at 50 ° C. to start hydrolysis, and the amount of free lysine is measured with a biotech analyzer (Asahi Kasei Kogyo Co., Ltd.) over time and in a short time.
When the amount of free lysine reached 34%, the enzyme was inactivated by heating at 80 ° C for 10 minutes to stop the enzymatic decomposition, and then freeze-dried, and about 950 g of a peptide mixture from wheat protein was obtained.
I got The peptide mixture obtained by repeating the above production method twice was tested by the above-mentioned test method, and as a result, almost no difference was observed in the amount of each free amino acid and the total amount of the free amino acids.

【手続補正4】[Procedure amendment 4]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0053[Correction target item name] 0053

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0053】実施例3 蛋白質含量80%の市販小麦蛋白粉末(理研ビタミン社
製。エマソフトEX−100)500g及び蛋白質含量
90%の市販大豆蛋白粉末(不二製油社製。商品名SU
PRO)500gを脱イオン水9kgに溶解し、pHを
7.0に調整し、70℃で5分間保持して殺菌した。こ
の混合蛋白質溶液に市販のパンクレアチン(天野製薬社
製)85万PUN単位(蛋白質1g当たり1000PU
N単位)、プロテアーゼNアマノ(天野製薬社製)17
0万PUN単位(蛋白質1g当たり2000PUN単
位)及び前記参考例1と同一の方法で調製したラクトバ
シラス・ヘルベチカス菌体破砕物4万活性単位(蛋白質
1g当たり47活性単位)を添加し、50℃に保持して
加水分解を開始し、HPLC(島津製作所製)を用いて
経時的に、かつ短時間で遊離アルギニンの量を測定し、
遊離アルギニン量が21%に達した時点で80℃で10
分間加熱し、酵素を失活させ、酵素分解を停止させ、の
ち凍結乾燥し、ペプチド混合物約950gを得た。前記
の製造法を2回反復して得られたペプチド混合物を、前
記試験方法により試験した結果、各遊離アミノ酸の量及
び遊離アミノ酸の合計量にはほとんど差異が認められな
かった。
Example 3 500 g of a commercial wheat protein powder having a protein content of 80% (manufactured by Riken Vitamin Co., Emmasoft EX-100) and a commercially available soybean protein powder having a protein content of 90% (manufactured by Fuji Oil Co., trade name SU.
500 g of PRO) was dissolved in 9 kg of deionized water, the pH was adjusted to 7.0, and the mixture was kept at 70 ° C. for 5 minutes for sterilization. In this mixed protein solution, commercially available pancreatin (manufactured by Amano Pharmaceutical Co., Ltd.) 850,000 PUN units (1000 PU per 1 g of protein)
N units), Protease N Amano (manufactured by Amano Pharmaceutical Co., Ltd.) 17
100,000 PUN units (2000 PUN units per gram of protein) and lactobacco prepared by the same method as in Reference Example 1 above.
Was added Shirasu helveticus disrupted cells 40,000 activity units (protein 1g per 47 activity units), and held at 50 ° C. to initiate hydrolysis, over time using HPLC (manufactured by Shimadzu Corporation), and Measure the amount of free arginine in a short time,
When the amount of free arginine reaches 21%, 10 at 80 ° C
The mixture was heated for a minute to inactivate the enzyme, stop the enzymatic decomposition, and then freeze-dried to obtain about 950 g of a peptide mixture. The peptide mixture obtained by repeating the above production method twice was tested by the above test method, and as a result, almost no difference was observed in the amount of each free amino acid and the total amount of the free amino acids.

【手続補正5】[Procedure Amendment 5]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0054[Correction target item name] 0054

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0054】実施例4 乳清蛋白質含量75%の市販乳清蛋白質粉末(カリフォ
ルニア・プロテイン社製)500g及び蛋白質含量90
%の市販大豆蛋白粉末(不二製油社製。商品名SUPR
O)500gを脱イオン水9kgに溶解し、70℃に5
分間保持して殺菌し、pHを9.0に調整し、市販のプ
ロテアーゼNアマノ(天野製薬社製)250万PUN単
位(蛋白質1g当たり4848PUN単位)及び前記参
考例1と同一の方法で製造したラクトバシラス・ヘルベ
チカス菌体破砕物4万活性単位(蛋白質1g当たり48
活性単位)を添加し、50℃に保持して加水分解を開始
し、バイオテックアナライザー(旭化成工業社製)を用
いて経時的に、かつ短時間で遊離リジンの量を測定し、
遊離リジン量が18%に達した時点で80℃で6分間加
熱し、酵素を失活させ、酵素分解を停止させ、凍結乾燥
し、ペプチド混合物約950gを得た。前記の製造法を
2回反復して得られたペプチド混合物を、前記試験方法
により試験した結果、各遊離アミノ酸の量及び遊離アミ
ノ酸の合計量にはほとんど差異が認められなかった。
Example 4 500 g of a commercial whey protein powder (manufactured by California Protein Co.) having a whey protein content of 75% and a protein content of 90
% Commercial soy protein powder (manufactured by Fuji Oil Co., Ltd., trade name SUPR
O) 500 g is dissolved in 9 kg of deionized water and the mixture is heated to 70 ° C. for 5
It was kept for minutes to sterilize, the pH was adjusted to 9.0, and commercially available protease A Amano (manufactured by Amano Pharmaceutical Co., Ltd.) 2.5 million PUN units (4848 PUN units per 1 g of protein) and the same method as in Reference Example 1 were used. Lactobacillus helveticus cell disruption product 40,000 active units (48 per 1 g protein)
Activity unit), and the mixture is kept at 50 ° C. to start hydrolysis, and the amount of free lysine is measured with a biotech analyzer (Asahi Kasei Kogyo Co., Ltd.) over time and in a short time.
When the amount of free lysine reached 18%, the mixture was heated at 80 ° C. for 6 minutes to inactivate the enzyme, stop the enzymatic decomposition, and freeze-dry to obtain about 950 g of a peptide mixture. The peptide mixture obtained by repeating the above production method twice was tested by the above test method, and as a result, almost no difference was observed in the amount of each free amino acid and the total amount of the free amino acids.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 // A23L 1/305 (72)発明者 齋藤 仁志 神奈川県座間市東原5−1−83 森永乳業 株式会社栄養科学研究所内 (72)発明者 川口 靖 神奈川県座間市東原5−1−83 森永乳業 株式会社栄養科学研究所内 (72)発明者 赤染 陽子 神奈川県座間市東原5−1−83 森永乳業 株式会社栄養科学研究所内 (72)発明者 越智 浩 神奈川県座間市東原5−1−83 森永乳業 株式会社栄養科学研究所内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Reference number within the agency FI Technical indication location // A23L 1/305 (72) Inventor Hitoshi Saito 5-1-83 Higashihara, Zama City, Kanagawa Prefecture Morinaga Milk Industry Institute of Nutrition Science Co., Ltd. (72) Inventor Yasushi Kawaguchi 5-1-83 Higashihara, Zama City, Kanagawa Prefecture Morinaga Milk Industry Co., Ltd. (72) Inventor Yoko 5-1-5-83 Higashihara, Zama City, Kanagawa Prefecture Morinaga Milk Industry (72) Inventor Hiroshi Ochi 5-1-83 Higashihara, Zama City, Kanagawa Prefecture Morinaga Milk Industry Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 一定品質のペプチド混合物の製造法であ
って、1種若しくは2種以上の蛋白質からなる原料蛋白
質の水溶液又は予め軽度に加水分解した原料蛋白質の水
溶液に、1種若しくは2種以上の蛋白分解酵素を添加
し、原料蛋白質又は予め軽度に加水分解した原料蛋白質
の加水分解を開始し、加水分解により分解液中に遊離し
た特定アミノ酸の量を経時的に、かつ短時間で測定し、
原料蛋白質又は予め軽度に加水分解した原料蛋白質に含
まれる特定アミノ酸の総量に対する遊離した特定アミノ
酸の量の割合を算出し、その算出した値が予め設定され
た特定の範囲内に達したとき直ちに加水分解を停止する
ことを特徴とするペプチド混合物の製造法。
1. A method for producing a peptide mixture of constant quality, which comprises one or more aqueous solutions of a raw material protein consisting of one or more proteins or an aqueous solution of a raw protein which has been slightly hydrolyzed in advance. The proteolytic enzyme is added to start the hydrolysis of the raw material protein or the raw material protein that has been slightly hydrolyzed beforehand, and the amount of the specific amino acid released in the degradation solution due to the hydrolysis is measured with time and in a short time. ,
Calculate the ratio of the amount of the specific amino acid released to the total amount of the specific amino acid contained in the raw material protein or the raw material protein that has been slightly hydrolyzed in advance, and immediately hydrolyze when the calculated value reaches the preset specific range. A method for producing a peptide mixture, which comprises stopping the decomposition.
【請求項2】 遊離した特定アミノ酸が、リジン、フェ
ニルアラニン、ロイシン又はアルギニンである請求項1
に記載のペプチド混合物の製造法。
2. The released specific amino acid is lysine, phenylalanine, leucine or arginine.
The method for producing the peptide mixture according to 1.
JP27430494A 1994-10-14 1994-10-14 A new method for producing peptide mixtures Expired - Fee Related JP3396001B2 (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
JP27430494A JP3396001B2 (en) 1994-10-14 1994-10-14 A new method for producing peptide mixtures
AU36738/95A AU692612B2 (en) 1994-10-14 1995-10-13 Peptide mixture and products thereof
US08/817,095 US5952193A (en) 1994-10-14 1995-10-13 Peptide mixture and products thereof
EP95934302A EP0799577B1 (en) 1994-10-14 1995-10-13 Peptide mixture and products thereof
DE69523791T DE69523791T2 (en) 1994-10-14 1995-10-13 PEPTIDE MIXTURE AND PRODUCTS THEREOF
NZ294046A NZ294046A (en) 1994-10-14 1995-10-13 A palatable whey protein hydrolysate having antioxidant activity
DK95934302T DK0799577T3 (en) 1994-10-14 1995-10-13 Peptide Mixture and Products thereof
PCT/JP1995/002109 WO1996011584A1 (en) 1994-10-14 1995-10-13 Peptide mixture and products thereof
CA002202633A CA2202633C (en) 1994-10-14 1995-10-13 Peptide mixture and products thereof
AU63603/98A AU701507B2 (en) 1994-10-14 1998-04-24 Peptide mixture and products thereof
US09/316,957 US6395508B1 (en) 1994-10-14 1999-05-24 Peptide mixture and products thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27430494A JP3396001B2 (en) 1994-10-14 1994-10-14 A new method for producing peptide mixtures

Publications (2)

Publication Number Publication Date
JPH08112064A true JPH08112064A (en) 1996-05-07
JP3396001B2 JP3396001B2 (en) 2003-04-14

Family

ID=17539784

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27430494A Expired - Fee Related JP3396001B2 (en) 1994-10-14 1994-10-14 A new method for producing peptide mixtures

Country Status (1)

Country Link
JP (1) JP3396001B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013193974A (en) * 2012-03-19 2013-09-30 Fancl Corp Tablet with high amino acid content

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013193974A (en) * 2012-03-19 2013-09-30 Fancl Corp Tablet with high amino acid content

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Publication number Publication date
JP3396001B2 (en) 2003-04-14

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