JPS62224245A - Production of easily soluble hydrolyzed milk protein free from unagreeable taste - Google Patents

Production of easily soluble hydrolyzed milk protein free from unagreeable taste

Info

Publication number
JPS62224245A
JPS62224245A JP61066537A JP6653786A JPS62224245A JP S62224245 A JPS62224245 A JP S62224245A JP 61066537 A JP61066537 A JP 61066537A JP 6653786 A JP6653786 A JP 6653786A JP S62224245 A JPS62224245 A JP S62224245A
Authority
JP
Japan
Prior art keywords
milk protein
solution
milk
pancreatin
taste
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
JP61066537A
Other languages
Japanese (ja)
Other versions
JPH0622446B2 (en
Inventor
Minoru Kuribayashi
稔 栗林
Norio Kashiwara
柏原 典雄
Minoru Yanai
柳井 稔
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.)
Snow Brand Milk Products Co Ltd
Original Assignee
Snow Brand Milk Products 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
Application filed by Snow Brand Milk Products Co Ltd filed Critical Snow Brand Milk Products Co Ltd
Priority to JP61066537A priority Critical patent/JPH0622446B2/en
Publication of JPS62224245A publication Critical patent/JPS62224245A/en
Publication of JPH0622446B2 publication Critical patent/JPH0622446B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain the titled hydrolyzed product suitable as a raw material for food or drink, by hydrolyzing a milk protein (-containing material) in an alkaline solution with pancreatin and a microbial protease derived from a strain belonging to Bacillus genus and separating insoluble components from the hydrolyzed product. CONSTITUTION:A milk protein such as casein, lactoalbumin, etc., or a milk protein-containing material composed mainly of milk protein (e.g. whole milk, defatted milk, etc.) is dissolved in water and the pH of the solution is controlled to an alkaline region. The solution is made to simultaneously or successively react with pancreatin and a microbial protease (e.g. Bioplase: commercial name) originated from a microorganism belonging to Bacillus genus (e.g. Bacillus subtilis) to effect enzymatic hydrolysis of the protein. Insoluble components are separated and removed from the resultant enzymatic decomposition mixture to obtain an easily soluble hydriolyzed milk protein free from unagreeable taste. The hydrolyzed product is suitable as an transintestinal nutrient, nutrition drink, etc.

Description

【発明の詳細な説明】 産呈よ勿肌尻光互 本発明は、経腸栄養剤、栄養補強食品、栄養飲料等の飲
食品素材として利用するのに適した不快味のない、易溶
性乳蛋白加水分解物の製造方法に関する。
[Detailed Description of the Invention] The present invention provides an easily soluble milk that has no unpleasant taste and is suitable for use as a food and drink material for enteral nutritional supplements, nutritional supplements, nutritional drinks, etc. The present invention relates to a method for producing a protein hydrolyzate.

l困q及地煎皇晟 近年、蛋白質を酵素により加水分解して得られるペプチ
ド、特にジーおよびトリーペプチドを主成分とする低分
子ペプチドは、それと同一組成のアミノ酸混合物に比べ
て腸管吸収が優れていることから、経腸栄養剤、栄養補
強食品等に利用されてきている。
In recent years, peptides obtained by enzymatic hydrolysis of proteins, especially low-molecular-weight peptides whose main components are G and T peptides, have been shown to have superior intestinal absorption compared to amino acid mixtures with the same composition. Because of this, it has been used in enteral nutrients, nutritional supplements, etc.

而して、蛋白源として乳蛋白質を用い、これを酵素で従
来法に従って加水分解を行って得られるペプチドは苦味
を有することが多く、従って、その摂食上障害をきたす
ことがあり、加うるに、このペプチドには不溶性のもの
もみられるので溶液形態にした場合沈澱物を形成する。
Therefore, the peptides obtained by hydrolyzing milk protein using enzymes according to conventional methods as a protein source often have a bitter taste, which may cause problems in feeding. Additionally, some of these peptides are insoluble, so they form precipitates when put into solution form.

したがって、乳蛋白質を従来法に従って酵素分解して得
られるペプチドは経口経腸栄養剤、栄養補強食品や飲料
等の窒素源として利用しがたかった。
Therefore, it has been difficult to use peptides obtained by enzymatically decomposing milk proteins according to conventional methods as a nitrogen source for oral and enteral nutrients, nutritional supplements, beverages, and the like.

、口が解ンしようとする問題慌 本発明は、乳蛋白質を酵素分解して得られるペプチドの
利用上の問題点に鑑み、なされたものであって、乳蛋白
質から不快味のない、かっ易溶性の低分子ペプチドを有
利に製造するための酵素的加水分解方法を提供すること
を目的とする。
The present invention was made in view of the problems in the use of peptides obtained by enzymatically decomposing milk proteins. The object of the present invention is to provide an enzymatic hydrolysis method for advantageously producing soluble low-molecular-weight peptides.

本発明者らは、乳蛋白質をアルカリ性領域のpHに調整
した溶液中で、パンクレアチンとバチルス属由来の微生
物プロテアーゼとを併用して酵素的に加水分解すること
により、上記目的を達成することに成功し、本発明をな
すに至った。
The present inventors achieved the above object by enzymatically hydrolyzing milk protein in a solution adjusted to an alkaline pH using a combination of pancreatin and a microbial protease derived from the genus Bacillus. This was successful and led to the present invention.

以下本発明の詳細な説明する。The present invention will be explained in detail below.

光里■構底 本発明の特徴は、乳蛋白質もしくは乳蛋白質を主成分と
する乳蛋白含有物を、pHをアルカリ性領域に調整した
溶液中で、パンクレアチンとバチルス属由来の微生物プ
ロテアーゼとを同時的もしくは段階的に作用させて酵素
的に加水分解し、得られた酵素分解混合物から不溶物を
分離し除去することにある。
A feature of the present invention is that pancreatin and a microbial protease derived from the genus Bacillus are simultaneously or The purpose is to perform enzymatic hydrolysis by acting in stages, and to separate and remove insoluble matter from the resulting enzymatically decomposed mixture.

ここで用いる乳蛋白質はカゼイン、ラクトアルブミン(
ホエー蛋白質)を包含し、乳蛋白含有物としては全乳、
脱脂乳等を例示し得る。
The milk proteins used here are casein and lactalbumin (
whey protein), and milk protein-containing substances include whole milk,
Examples include skimmed milk.

問題点を解ンするための 段 本発明では、上掲したような乳蛋白質もしくは乳蛋白含
有物を、乳蛋白質の濃度が0.5%〜30%、好ましく
は5%〜15%の水溶液になるように溶解した溶液を加
熱殺菌した後、50℃の温度に維持してアルカリにより
そのpHを7〜11、好ましくは8.0〜10.0のア
ルカリ性領域に調整する。なお、乳蛋白質として酸カゼ
インのように水中で溶解し難いものを用いる時は、水中
に可及的少量の酸もしくはアルカリを添加し、加温下に
溶解するとよい。
Steps for Solving the Problems In the present invention, the above-mentioned milk protein or milk protein-containing material is made into an aqueous solution with a milk protein concentration of 0.5% to 30%, preferably 5% to 15%. After heating and sterilizing the dissolved solution, the temperature is maintained at 50° C., and the pH thereof is adjusted to an alkaline range of 7 to 11, preferably 8.0 to 10.0, using an alkali. When using a milk protein that is difficult to dissolve in water, such as acid casein, it is preferable to add as little acid or alkali as possible to the water and dissolve it under heating.

本発明において上記溶液中の乳蛋白質に作用させるのに
用いる酵素、パンクレアチンは、豚の膵臓より得られる
ものであって、日本薬局方に掲載のものに準じたものを
用いるのが好ましい。また、本発明で同じく用いるバチ
ルス属由来の微生物プロテアーゼとしてはバチルス・ス
フ゛チリス(Bacillussubtilis)由来
のプロテアーゼである「ビオプラーゼ」(ナガセ生化学
工業社製)、「中性プロテアーゼ」(同社製)および「
プロテアーゼN」(天野製薬社製)等の中性ならびにア
ルカリ性領域で作用するものが好ましい。
In the present invention, the enzyme pancreatin used to act on the milk protein in the solution is obtained from pig pancreas, and it is preferable to use an enzyme similar to that listed in the Japanese Pharmacopoeia. In addition, the microbial proteases derived from the genus Bacillus that are also used in the present invention include "Bioplase" (manufactured by Nagase Seikagaku Kogyo Co., Ltd.), which is a protease derived from Bacillus subtilis, "Neutral Protease" (manufactured by the same company) and "
Preferred are those that act in the neutral and alkaline regions, such as "Protease N" (manufactured by Amano Pharmaceutical Co., Ltd.).

これらの酵素の使用量は、基質である乳蛋白質の種類、
濃度および消化温度と時間により異なるも、一般的には
基質に対して0.05〜10重景%、好ましくは0.1
〜5重量%である。
The amount of these enzymes used depends on the type of milk protein that is the substrate,
Although it varies depending on the concentration and digestion temperature and time, it is generally 0.05 to 10%, preferably 0.1% based on the substrate.
~5% by weight.

また、これらの酵素を作用させるための反応温度は、該
酵素の至適温度である30〜60℃、好ましくは40〜
50℃であり、一方反応時間は乳蛋白質の種類、濃度、
酵素量および反応温度により異なるが、通常3〜48時
間、好ましくは6〜24時間である。
In addition, the reaction temperature for making these enzymes act is 30 to 60°C, which is the optimum temperature of the enzyme, preferably 40 to 60°C.
50℃, while the reaction time depends on the type of milk protein, concentration,
Although it varies depending on the amount of enzyme and reaction temperature, it is usually 3 to 48 hours, preferably 6 to 24 hours.

本発明では、パンクレアチンとバチルス属由来の微生物
プロテアーゼを併用するものであるが、その使用に当っ
ては、上記両者の酵素をそれぞれ水溶液としたものを、
乳蛋白質の水溶液へ同時に添加して作用させるか、段階
的に添加して作用させてもよく、段階的に添加する場合
は両酵素の添加順序は問わない。
In the present invention, pancreatin and a microbial protease derived from the genus Bacillus are used together.
They may be added to the milk protein aqueous solution at the same time to act, or they may be added in stages to act, and when they are added in stages, the order of addition of both enzymes does not matter.

基準としての乳蛋白質に対して上記両者の酵素を作用さ
せるに当っての反応液のp++は、酵素添加前の原料水
溶液のpHを前述のようにアルカリ性領域に調整した後
は特に調整を行うことなく、反応を進行させる。そのた
め、反応中のpHは急激に低くなって中性付近(pH6
,6〜7.0)になるが、反応終了時までこのρ11の
ままで加水分解反応は進行する。
The p++ of the reaction solution when both enzymes are allowed to act on the milk protein as a standard should be adjusted especially after the pH of the raw material aqueous solution before addition of the enzyme is adjusted to the alkaline range as described above. Allow the reaction to proceed. Therefore, the pH during the reaction suddenly decreases to around neutrality (pH 6).
, 6 to 7.0), but the hydrolysis reaction proceeds with this ρ11 maintained until the end of the reaction.

なお、上記反応に際し、乳蛋白質として酸カゼインを用
いた場合には、その溶液中の濃度が10%以上になると
粘性が増大するため、適度の攪拌を行いながら、反応を
進行させることが好ましい。
In addition, when acid casein is used as the milk protein in the above reaction, the viscosity increases when the concentration in the solution exceeds 10%, so it is preferable to proceed with the reaction while performing appropriate stirring.

反応終了後、得られた乳蛋白加水分解物は、酵素失活の
ための85℃以上の温度で5分以上加熱処理した後、冷
却して5℃以下の温度に16時間以上放置して不溶物を
形成させ、該不溶物を分離、除去する。この不溶物は、
変成ペプチドおよび難溶性ペプチドから成ると考えられ
るが、これらは下記方法により効率的に分離、除去され
る・不溶物の分離、除去のための第一の手段は連続高速
遠心分離法の適用であり、これにより比較的比重の大き
い不溶物を除去することができる。次に第二の手段は濾
過法の適用であり、これには濾過綿を使用した方法と、
ゼータプラス濾材を使用した方法とがそれぞれ単独に、
もしくは組合わせて使用し得る。
After the reaction, the obtained milk protein hydrolyzate is heated at a temperature of 85°C or higher for 5 minutes or more to inactivate the enzyme, then cooled and left at a temperature of 5°C or lower for 16 hours or more to make it insoluble. The insoluble matter is separated and removed. This insoluble matter is
Although it is thought to consist of denatured peptides and poorly soluble peptides, these can be efficiently separated and removed by the following method.The first means of separating and removing insoluble matter is the application of continuous high-speed centrifugation. This makes it possible to remove insoluble matter with a relatively high specific gravity. The second method is to apply a filtration method, which includes a method using filter cotton,
The method using Zeta Plus filter media and the method using Zeta Plus filter media each separately,
Or they can be used in combination.

これらの二つの手段の適用により、不溶物を完全に分離
、除去し乳蛋白加水分解物溶液を清澄することが可能で
ある。
By applying these two means, it is possible to completely separate and remove insoluble matter and clarify the milk protein hydrolyzate solution.

因に、濾過綿とは綿状のセルロースであって、これを水
中に分散させ、濾過筒中に積層してフィルターとして使
用する。
Incidentally, filter cotton is cotton-like cellulose, and is used as a filter by dispersing it in water and layering it in a filter cylinder.

また、ゼータプラス濾材とはセルロースと珪藻土とから
成る濾材であって、これをフィルターに形成したもので
ある。
Moreover, Zeta Plus filter medium is a filter medium made of cellulose and diatomaceous earth, and is formed into a filter.

該フィルターは、ゼータ電位による吸着作用と通常の多
孔性物質による物理的濾過作用との相乗的作用により高
い濾過効率で濾別を行い得るものであって、コロイド状
の微細な不純物も有効に濾別し得る。
This filter can filter with high filtration efficiency due to the synergistic effect of the adsorption effect of zeta potential and the physical filtration effect of ordinary porous materials, and can effectively filter even fine colloidal impurities. Can be separated.

さらに、上記ゼータプラス濾材を、セライト(和光純薬
社製、ハイフロス−パーセル)と1=4の割合で混合し
たものを濾過助剤として用いると、−そう高い濾過効率
で上記不純物を濾別することができる。
Furthermore, when a mixture of the above Zeta Plus filter medium and Celite (manufactured by Wako Pure Chemical Industries, Ltd., Hyfloth Purcel) in a ratio of 1=4 is used as a filter aid, the above impurities can be filtered out with a very high filtration efficiency. be able to.

上述のようにして、不溶物を除去して得られる乳蛋白加
水分解物は、通常の乾燥手段である凍結乾燥もしくは噴
霧乾燥により乾燥することにより粉末化して製品とする
The milk protein hydrolyzate obtained by removing insoluble matter as described above is dried by freeze drying or spray drying, which is a usual drying method, to form a powder into a product.

このようにして得られる乳蛋白加水分解物製品は、アミ
ノ酸とジペプチドおよびトリペプチドを主要成分とする
低ペプチドであって、水に対する溶解性が良好でしって
、4何/−%濃度の水溶液でのpHは6.0〜7.0の
中性であり、苦味もほとんど感じない。
The milk protein hydrolyzate product obtained in this way is a low peptide containing amino acids and dipeptides and tripeptides as main components, has good solubility in water, and has a concentration of 4/-% in aqueous solution. The pH is neutral between 6.0 and 7.0, and there is almost no bitterness.

したがって、本発明により得られる製品は、経腸栄養剤
、栄養補給飲食品等の窒素源素材乃至は医薬品素材とし
て有効に利用し得る。
Therefore, the product obtained according to the present invention can be effectively used as a nitrogen source material for enteral nutrients, nutritional supplement foods and drinks, or as a pharmaceutical material.

畝上のとおり、本発明は、乳蛋白質をパンクレアチンと
バチルス属由来の微生物プロテアーゼとを併用して加水
分解することにより、酵素分解反応中のpHを調整した
り、反応後の反応液を中和し、脱塩する等の操作を行う
ことなく、上記窒素源として良好な低分子ペプチドを有
利に製造することを可能としたものである。以下に実施
例を示して本発明をさらに具体的に説明する。
As mentioned above, the present invention hydrolyzes milk protein using a combination of pancreatin and a microbial protease derived from the genus Bacillus to adjust the pH during the enzymatic decomposition reaction and to neutralize the reaction solution after the reaction. This makes it possible to advantageously produce a low-molecular-weight peptide that is good as the nitrogen source without performing operations such as mixing and desalting. EXAMPLES The present invention will be explained in more detail with reference to Examples below.

なお、実施例に示した低分子ペプチドの収率、平均ペプ
チド鎖長、遊離アミノ酸含量および分子量分布は下記に
より測定した。
The yield, average peptide chain length, free amino acid content, and molecular weight distribution of the low-molecular-weight peptides shown in Examples were measured as follows.

■ペプチドの収率 原料蛋白質中の全窒素量 ■ペプチドの平均ペプチド鎖長(A P L)アミノ基
の定量はTNBS()リニトロベンゼンスルホン酸)法
により行い、完全加水分解は6N IIcI中で110
℃で24時間行った。
■Peptide yield Total nitrogen content in raw protein ■Average peptide chain length of peptide (APL) Quantification of amino groups was performed by the TNBS (linitrobenzenesulfonic acid) method, and complete hydrolysis was performed in 6N IIcI at 110%
℃ for 24 hours.

■遊離アミノ酸定量 測定可能な濃度の溶液としたものについて、日立835
型アミノ酸自動分析計で定量した。
■For solutions with a concentration that allows quantitative measurement of free amino acids, Hitachi 835
It was quantified using an automatic amino acid analyzer.

■分子量分布 5ephadex (セフシデツクス)G−15カラム
(1,5X 150cm)を用い、1%酢酸溶液を平衡
溶出液として使用してゲル濾過を行った。検出は各フラ
クションを完全加水分解し、ニンヒドリン法によりアミ
ノ酸量として定量した。さらに、各フラクションのAP
Lを上記■の方法により測定して分子量分布を求めた。
(2) Molecular weight distribution Gel filtration was performed using a 5 ephadex G-15 column (1.5 x 150 cm) using a 1% acetic acid solution as the equilibrium eluent. For detection, each fraction was completely hydrolyzed and the amount of amino acids was quantified by the ninhydrin method. Furthermore, the AP of each fraction
L was measured by the method described in (2) above to determine the molecular weight distribution.

実施例1 酸カゼインにュージーランド製、ラフティックカゼイン
) 1kgをKzCOz 20g及び1Ja2c032
0g添加した水10Zに加え、60℃まで加温しながら
溶解させた溶液を、90℃以上の温度で15分間加熱殺
菌を行った。
Example 1 1 kg of acid casein (made in New Zealand, raftic casein) was mixed with 20 g of KzCOz and 1Ja2c032
A solution prepared by adding 0 g of water 10Z and dissolving it while heating it to 60°C was heat sterilized at a temperature of 90°C or higher for 15 minutes.

次いで、この溶液に50℃の温度で4規定苛性ソ一ダ水
溶液loom f!を添加してpH8,0〜9.0に調
整した。
Next, a 4N aqueous solution of caustic soda was added to this solution at a temperature of 50°C. was added to adjust the pH to 8.0 to 9.0.

得られた酸カゼイン溶液に、予め、適当量の水に熔解も
しくは懸濁したパンクレアチン(天野製薬社製:日本薬
局方記載品) 7g及びバチルス・ズブチリス(Bac
illus 5ubttlis)由来のプロテアーゼN
(天野製薬社製)15gを別々の溶液として順次添加し
、50℃に保持したまま16時間反応させた。反応終了
後、85℃で10分以上加熱して酵素を失活させた後、
5℃以下で16時間放1した。放置後、室温にもどすこ
となく、高速遠心機で不純物を除去し、さらに濾過綿濾
過及びゼータプラスフィルター濾過により処理して反応
液を清澄化した。このン夜をロータリーエバポレーター
で?届縮し、さらに凍結乾燥してペプチド粉末860g
を得た(収率86%)。
To the obtained acid casein solution, 7 g of pancreatin (manufactured by Amano Pharmaceutical Co., Ltd., listed in the Japanese Pharmacopoeia) dissolved or suspended in an appropriate amount of water and Bacillus subtilis (Bacillus subtilis) were added.
Protease N derived from S. illus 5ubttlis)
(manufactured by Amano Pharmaceutical Co., Ltd.) were sequentially added as separate solutions, and the mixture was reacted for 16 hours while being maintained at 50°C. After the reaction was completed, the enzyme was deactivated by heating at 85°C for 10 minutes or more, and then
It was left at 5° C. or lower for 16 hours. After standing, impurities were removed using a high-speed centrifuge without returning to room temperature, and the reaction solution was further treated by cotton filtration and Zeta Plus filter filtration to clarify the reaction solution. Spending this night on a rotary evaporator? Shrink it and freeze-dry it to make 860g of peptide powder.
was obtained (yield 86%).

この標品は平均ペプチド鎖長2.0、ジ及びトリペプチ
ド含量が30%以下であった。
This preparation had an average peptide chain length of 2.0 and a di- and tripeptide content of 30% or less.

また、上記標品のゲル濾過による分子量分布(ゲル濾過
バクーン)は添付図に示すとおりであった。
Moreover, the molecular weight distribution (gel filtration bagun) of the above sample obtained by gel filtration was as shown in the attached figure.

次に、上述のようにして得られた乳蛋白加水分解物の呈
味性についてパネルテストにより試験した結果を下記表
に示す。なお、比較として本発明の方法に従わないで調
製した乳蛋白加水分解物についても同様にして試験を行
い、その結果を併せて表に示した。
Next, the taste of the milk protein hydrolyzate obtained as described above was tested by a panel test, and the results are shown in the table below. For comparison, a milk protein hydrolyzate prepared without following the method of the present invention was also tested in the same manner, and the results are also shown in the table.

試料の調製: ■試料A(本発明) 実施例1で得られたペプチド粉末を4W/W%濃度にな
るように水に溶解した溶液。
Preparation of samples: ■Sample A (invention) A solution in which the peptide powder obtained in Example 1 was dissolved in water to a concentration of 4 W/W%.

■試料B(比較例) 実施例1において、プロテアーゼNを用いずにパンクレ
アチンのみを用いるほかは、実施例1に記載したと同様
の手順により調製したペプチド粉末を4−/−%濃度に
なるように水に溶解した溶液。
■Sample B (comparative example) Peptide powder prepared by the same procedure as described in Example 1 except that only pancreatin was used without using protease N was prepared at a concentration of 4-/-%. solution dissolved in water.

■試料C(比較例) 実施例1において、パンクレアチンを用いずにプロテア
ーゼNのみを用いるほかは、実施例1に記載したと同様
の手順により調製したペプチド粉末を4−/−%濃度に
なるように水に溶解した溶液。
■Sample C (comparative example) Peptide powder prepared by the same procedure as described in Example 1 except that only protease N was used without using pancreatin was prepared at a concentration of 4-/-%. solution dissolved in water.

■試料D(比較例) 実施例1において、酵素としてパンクレアチン及びプロ
テアーゼNに代えてトリプシンLOgを用いるほかは、
実施例1に記載と同様の手順によりtA製したペプチド
粉末を4−八%の濃度になるように水に溶解した溶液。
■Sample D (comparative example) In Example 1, except that trypsin LOg was used instead of pancreatin and protease N as enzymes,
A solution in which tA-produced peptide powder was dissolved in water to a concentration of 4-8% according to the same procedure as described in Example 1.

パネルテスト: 1掲の各試料について、年令が10代乃至50代の各1
0名づつ(計50名)を選んで官能テストを行い、その
評価の平均値で示した。
Panel test: For each sample listed, one panelist aged between 10 and 50
A sensory test was conducted on 0 people (total of 50 people), and the average value of the evaluations was shown.

上表にみられるとおり、本発明の方法に従って調製され
た乳蛋白加水分解物(試料A)は、従来法により調製さ
れたものに比べて不快味のないことがわかる。
As seen in the above table, it can be seen that the milk protein hydrolyzate (Sample A) prepared according to the method of the present invention has no unpleasant taste compared to that prepared by the conventional method.

実施例2 実施例1において、パンクレアチン50gとプロテアー
ゼN LOgを添加し、50℃で8時間作用させること
を除いては、実施例1記載と同様の手順に従って820
gのペプチドを得た。この標品は、平均ペプチド鎖長1
.8、遊離アミノ酸は32%で、ゲル濾過による分子量
分布は実施例1でのペプチドとほぼ同様なパターンを示
した。
Example 2 The same procedure as described in Example 1 was followed except that 50 g of pancreatin and LOg of protease NLO were added and allowed to react at 50° C. for 8 hours.
g peptide was obtained. This preparation has an average peptide chain length of 1
.. 8. The free amino acid content was 32%, and the molecular weight distribution by gel filtration showed almost the same pattern as the peptide in Example 1.

実施例3 実施例1において、プロテアーゼNの代わりにナガセ生
化学工業製の「ビオプラーゼコンク(150,000P
IN/g)15gを添加し、50℃、16時間作用させ
る以外は実施例1に記載と同様の手順に従って850g
のペプチド粉末を得た。この製品の平均ペプチド鎖長は
2.0、遊離アミノ酸含量は30%であった。また、分
子量分布は実施例1におけるペプチドとほぼ同様のパタ
ーンを示した。
Example 3 In Example 1, "Bioprase Conc (150,000P) manufactured by Nagase Seikagaku Kogyo was used instead of Protease N.
850 g according to the same procedure as described in Example 1 except that 15 g of IN/g) was added and allowed to act at 50° C. for 16 hours.
peptide powder was obtained. The average peptide chain length of this product was 2.0, and the free amino acid content was 30%. Moreover, the molecular weight distribution showed almost the same pattern as the peptide in Example 1.

実施例4 実施例1において酵素を同時に添加することなく、まず
、プロテアーゼN 15gを50℃で3時間作用させた
後、パンクレアチン7gを添加し、さらに12時間作用
させる以外は実施例1に記載したと同様の手順に従って
890gのペプチドを得た。この標品は、平均のペプチ
ド鎖長2.0、遊離アミノ酸含量は30%であり、ゲル
濾過による分子量分布は実施例1とほぼ同様であった。
Example 4 Same as in Example 1 except that 15 g of protease N was first allowed to act at 50°C for 3 hours, then 7 g of pancreatin was added and allowed to act for a further 12 hours, without adding enzymes at the same time. Following the same procedure as above, 890 g of peptide was obtained. This preparation had an average peptide chain length of 2.0, a free amino acid content of 30%, and a molecular weight distribution determined by gel filtration that was almost the same as in Example 1.

実施例5 実施例1において、基質を酸カゼインの代わりに牛乳の
ホエー蛋白質であるラクトアルブミン(バイオプロ:バ
イオアイソレート社製Hkgを用いて水101に溶解さ
せ、90“C15分間加熱殺菌後p11を4N Koj
iでpH9,3に調整し、パンクレアチンとプロテアー
ゼNを50℃、16時間作用させることを除いては、実
施例1に記載と同様の手順に従って810gのペプチド
組成物を調製した。得られたペプチド標品の平均ペプチ
ド鎖長2.3、遊離アミノ酸27%で分子量分布もほぼ
実施例1と同様であった。
Example 5 In Example 1, the substrate was replaced with acid casein by dissolving it in water 101 using lactalbumin, which is a milk whey protein (Biopro: Hkg manufactured by Bioisolate), and heating it at 90"C for 15 minutes and then heating it at p11. 4N Koj
810 g of a peptide composition was prepared according to the same procedure as described in Example 1, except that the pH was adjusted to 9.3 with i. The average peptide chain length of the obtained peptide sample was 2.3, the free amino acid was 27%, and the molecular weight distribution was almost the same as in Example 1.

Claims (2)

【特許請求の範囲】[Claims] (1)乳蛋白質もしくは乳蛋白質を主成分とする乳蛋白
含有物を、pHをアルカリ性領域に調整した溶液中で、
パンクレアチンとバチルス属由来の微生物プロテアーゼ
とを同時的もしくは段階的に作用させ酵素的に加水分解
し、得られた酵素分解混合物から不溶物を分離し、除去
することを特徴とする不快味のない易溶性乳蛋白加水分
解物を製造する方法。
(1) Milk protein or a milk protein-containing material whose main component is milk protein, in a solution whose pH is adjusted to an alkaline region,
An unpleasant taste-free method characterized by enzymatically hydrolyzing pancreatin and a microbial protease derived from the genus Bacillus by acting simultaneously or in stages, and separating and removing insoluble matter from the resulting enzymatically decomposed mixture. A method for producing a readily soluble milk protein hydrolyzate.
(2)乳蛋白質もしくはその含有物の溶液のpHを7〜
11、好ましくは8.0〜10.0に調整する特許請求
の範囲第(1)項記載の製造方法。
(2) Adjust the pH of the solution of milk protein or its contents to 7 or more.
11, preferably 8.0 to 10.0.
JP61066537A 1986-03-25 1986-03-25 Method for producing easily soluble milk protein hydrolyzate having no unpleasant taste Expired - Lifetime JPH0622446B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61066537A JPH0622446B2 (en) 1986-03-25 1986-03-25 Method for producing easily soluble milk protein hydrolyzate having no unpleasant taste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61066537A JPH0622446B2 (en) 1986-03-25 1986-03-25 Method for producing easily soluble milk protein hydrolyzate having no unpleasant taste

Publications (2)

Publication Number Publication Date
JPS62224245A true JPS62224245A (en) 1987-10-02
JPH0622446B2 JPH0622446B2 (en) 1994-03-30

Family

ID=13318745

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61066537A Expired - Lifetime JPH0622446B2 (en) 1986-03-25 1986-03-25 Method for producing easily soluble milk protein hydrolyzate having no unpleasant taste

Country Status (1)

Country Link
JP (1) JPH0622446B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009521955A (en) * 2006-01-04 2009-06-11 レプリノ フーズ カンパニー Protein hydrolyzate and method of making the same

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5718741B2 (en) 2011-06-24 2015-05-13 カルピス株式会社 Enzymatic production of peptide for improving brain function
US9523109B2 (en) 2011-06-24 2016-12-20 Calpis Co., Ltd. Method for enzymatically preparing peptides for use in improvement of brain function

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5279083A (en) * 1975-12-26 1977-07-02 Morinaga Milk Industry Co Ltd Production of protein decomposed substance not having bitterness and antigen property
JPS57194753A (en) * 1981-05-11 1982-11-30 Miles Lab Production of protein hydrolysate from milk protein
JPS58158136A (en) * 1982-02-22 1983-09-20 ストウフア−・ケミカル・カンパニ− Production of enzymatically hydrolyzed protein substance

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5279083A (en) * 1975-12-26 1977-07-02 Morinaga Milk Industry Co Ltd Production of protein decomposed substance not having bitterness and antigen property
JPS57194753A (en) * 1981-05-11 1982-11-30 Miles Lab Production of protein hydrolysate from milk protein
JPS58158136A (en) * 1982-02-22 1983-09-20 ストウフア−・ケミカル・カンパニ− Production of enzymatically hydrolyzed protein substance

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009521955A (en) * 2006-01-04 2009-06-11 レプリノ フーズ カンパニー Protein hydrolyzate and method of making the same

Also Published As

Publication number Publication date
JPH0622446B2 (en) 1994-03-30

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