JPH08509366A - Protein hydrolysis method - Google Patents

Protein hydrolysis method

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Publication number
JPH08509366A
JPH08509366A JP6523763A JP52376394A JPH08509366A JP H08509366 A JPH08509366 A JP H08509366A JP 6523763 A JP6523763 A JP 6523763A JP 52376394 A JP52376394 A JP 52376394A JP H08509366 A JPH08509366 A JP H08509366A
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protein
preparation
hydrolyzate
hydrolysis
products
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ムンク ニールセン,ペル
ハバス,ペーター
ハンセン,キム
ブドルフセン,ギッテ
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Novo Nordisk AS
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Novo Nordisk AS
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    • C12Y301/00Hydrolases acting on ester bonds (3.1)
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    • C12N9/58Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from fungi
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    • A23C9/1322Inorganic compounds; Minerals, including organic salts thereof, oligo-elements; Amino-acids, peptides, protein-hydrolysates or derivatives; Nucleic acids or derivatives; Yeast extract or autolysate; Vitamins; Antibiotics; Bacteriocins
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    • A23J3/30Working-up of proteins for foodstuffs by hydrolysis
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    • A23JPROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J3/00Working-up of proteins for foodstuffs
    • A23J3/30Working-up of proteins for foodstuffs by hydrolysis
    • A23J3/32Working-up of proteins for foodstuffs by hydrolysis using chemical agents
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    • A23J3/00Working-up of proteins for foodstuffs
    • A23J3/30Working-up of proteins for foodstuffs by hydrolysis
    • A23J3/32Working-up of proteins for foodstuffs by hydrolysis using chemical agents
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    • A23J3/343Working-up of proteins for foodstuffs by hydrolysis using chemical agents using enzymes of animal proteins of dairy proteins
    • AHUMAN NECESSITIES
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    • A23J3/00Working-up of proteins for foodstuffs
    • A23J3/30Working-up of proteins for foodstuffs by hydrolysis
    • A23J3/32Working-up of proteins for foodstuffs by hydrolysis using chemical agents
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    • A23J3/00Working-up of proteins for foodstuffs
    • A23J3/30Working-up of proteins for foodstuffs by hydrolysis
    • A23J3/32Working-up of proteins for foodstuffs by hydrolysis using chemical agents
    • A23J3/34Working-up of proteins for foodstuffs by hydrolysis using chemical agents using enzymes
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    • A23J3/00Working-up of proteins for foodstuffs
    • A23J3/30Working-up of proteins for foodstuffs by hydrolysis
    • A23J3/32Working-up of proteins for foodstuffs by hydrolysis using chemical agents
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    • A23L27/00Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
    • A23L27/20Synthetic spices, flavouring agents or condiments
    • A23L27/21Synthetic spices, flavouring agents or condiments containing amino acids
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    • A23L27/00Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
    • A23L27/20Synthetic spices, flavouring agents or condiments
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    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/17Amino acids, peptides or proteins
    • A23L33/18Peptides; Protein hydrolysates
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    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/64Proteins; Peptides; Derivatives or degradation products thereof
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/64Proteins; Peptides; Derivatives or degradation products thereof
    • A61K8/645Proteins of vegetable origin; Derivatives or degradation products thereof
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    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/64Proteins; Peptides; Derivatives or degradation products thereof
    • A61K8/65Collagen; Gelatin; Keratin; Derivatives or degradation products thereof
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    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00Cosmetics or similar toiletry preparations
    • A61K8/18Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/64Proteins; Peptides; Derivatives or degradation products thereof
    • A61K8/66Enzymes
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    • C12N9/50Proteinases, e.g. Endopeptidases (3.4.21-3.4.25)
    • C12N9/52Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from bacteria or Archaea
    • C12N9/54Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from bacteria or Archaea bacteria being Bacillus
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Abstract

(57)【要約】 アスペルギルス オリゼから由来されそして各々がそれぞれ23kD,27kD,31kD,32kD,35kD,38kD,42kD,47kD,53kDおよび100kDから選ばれるおゝよその分子量を有する少なくとも5個のタンパク質分解成分を含んでなるタンパク分解酵素調製品、例えばフレーバーザイム(商標)と共にインキュベートすることによる植物性又は動物性タンパク質の加水分解は食品製品例えば母乳代替物、チーズ、HVP、肉エキス、矯味剤および食品製品の発酵用のプロセス助剤又は非食品製品例えばペットフード、化粧中において又はそれらとして有用なタンパク質加水分解物を提供する。この方法により高度の加水分解(DH)、風味発生および高タンパク質溶解度を得る。   (57) [Summary] A protein derived from Aspergillus oryzae and comprising at least 5 proteolytic components each having a molecular weight of about 23 kD, 27 kD, 31 kD, 32 kD, 35 kD, 38 kD, 42 kD, 47 kD, 53 kD and 100 kD. Hydrolysis of vegetable or animal proteins by incubating with degradative enzyme preparations, such as Flavorzyme ™, is a process for fermentation of food products such as milk substitutes, cheese, HVP, meat extracts, flavoring agents and food products. Provide protein hydrolysates useful in or as auxiliaries or non-food products such as pet food, makeup. This method results in a high degree of hydrolysis (DH), flavor development and high protein solubility.

Description

【発明の詳細な説明】 タンパク質の加水分解方法 技術分野 本発明は、タンパク質の加水分解方法、該方法によって得られるタンパク質加 水分解物および該タンパク質加水分解物を含有する食品以外の生産物に関する。 背景技術 タンパク質の加水分解方法は、例えば英国特許1,507,380、米国特許3,723,250 および国際公開WO 89/00272、WO 92/13964およびWO 90/05462に記載されてき た。 高度のタンパク質加水分解および秀れた感覚刺激性を有する加水分解物をもた らすタンパク質の加水分解方法に対する必要性が存在する。 発明の要約 今や以下の内容が見出された;すなわちアスペルギルス オリゼ(Aspergillu s oryzae)から由来しそして商標「フレーバーザイム」(Flavourzyme)名でノ ボ ノルディスク A/Sから市販されているタンパク質分解酵素調製品が秀れ たタンパク質加水分解特性を有し、例えば高度の加水分解と苦みのない加水分解 物を得ることが可能である。 従って、本発明はアスペルギルス オリゼから由来しそして商標「フレーバー ザイム」名でノボ ノルディスク A/Sより市販されているタンパク質分解調 製品を用いてインキュベーションするこ とによるタンパク質の加水分解方法に関する。 その第二の面において、本発明は本発明方法によって得られるタンパク質加水 分解物を提供する。 別の面において、本発明のタンパク質加水分解物を含んでなる食品および食品 以外の生産物に関する。 図面の簡単な説明 本発明を添付の図面を参照して更に説明する。 図1はpH5〜9(■:pH5、▲pH6、○pH7、□pH8、●pH9)のpH範囲内に おいてナトリウムカゼインに適用された本発明方法によって達成される加水分解 の時間(時)対加水分解の程度(%DH)を示す; 図2は本発明方法に従い22時間の加水分解後の大豆タンパク質分離物の加水分 解の程度(%DH)を示し(■:フレーバーザイム、▲:コロラーゼ(Corolase) (商標)7092、◇:コロラーゼ(Corolase)(商標)7093、◆:アルカラーゼ( Alcalase)(商標)、□:ニュートラーゼ(Neutrase)(商標);そして 図3は本発明方法に従い22時間の加水分解後、Na−カゼイネートの加水分解の 程度(%DH)を示す(■:フレーバーザイム(商標)、▲:コロラーゼ(商標) 7092、◇:コロラーゼ(商標)7093、◆:アルカラーゼ(商標)、□:ニュート ラーゼ(商標))。 発明の詳細な開示 フレーバーザイム(商標)について特性記述により以下の内容が示された;す なわちタンパク質分解アスペルギルス オリゼ調製品は幾つかのタンパク質分解 成分を含んでなる。該調製品は5個又はそれ以上のタンパク質分解酵素成分を含 んでなると思われ、その各 々は次のおおよその分子量:23kD,27kD,31kD,32kD,35kD,38kD,42KD,47KD ,53KDおよび100KDのいずれかを有することができる。 従って、本発明はアスペルギルス オリゼから由来しそしてそれぞれ23kD,27 kD,31kD,32kD,35kD,38kD,42kD,47kD,53kDおよび100kDから選ばれる、お およその分子量を有する少なくとも5個のタンパク質分解成分を含んでなるタン パク質分解酵素調製品と共にインキュベートすることによるタンパク質の加水分 解方法を提供する。 好ましい態様において、タンパク質はアスペルギルス オリゼから由来されそ してそれぞれおおよその分子量23kD,31kD,35kD,38kDおよび53kDを有する少な くとも5個のタンパク質分解成分を含んでなるタンパク質分解調製品と共にイン キュベートされる。 タンパク質分解調製品中のプロテアーゼ成分の分子量を、当業者に公知の方法 によりSDSポリアクリルアミドゲル電気泳動(SDS-PAGE)を用いて測定した。こ の方法により、各プロテアーゼ成分の分子量を測定した。 本発明方法はタンパク質の広範囲のタンパク質加水分解を行うことが可能であ り、そしてこの方法は苦みのない加水分解物並びにきわだったスープ味/肉味を 有する加水分解物をもたらす。 タンパク質の加水分解の程度は、達成される加水分解の程度により決定され得 る。本発明に関連して、加水分解の程度(DH)は次式により定義される: DHは、アドラーニッセン;Enzymic Hydrolysis of Food Proteins;エルスビ ール アプライド サイエンス出版社(1986)、122 頁に従って計算できる。 本発明方法を用いることにより、35%以上、好ましくは60%以上、より好まし くは70%以上、最も好ましくは80%以上のDHを得ることが可能である。 本発明方法により、高程度のタンパク質溶解度を得ることも可能である。タン パク質の溶解度の程度は、アドラーニッセン(前掲)により記載される如くタン パク質溶解度指数(PSI)により記載することができる。 好ましい態様において、50%PSI以上、好ましくは70%PSI以上、より好ましく は90%以上のタンパク質溶解度が得られる。 本発明方法により有利に加水分解され得るタンパク質又はタンパク質様物質は 、どんな植物性タンパク質であってもよく、例えば大豆タンパク質、穀粒タンパ ク質、例えば小麦グルテン又はゼイン、なたねタンパク質、むらさきうまごやし タンパク質、えんどうタンパク質、マメ科そら豆タンパク質、綿実タンパク質又 はごまの実タンパク質であり、又はどんな動物性タンパク質又はタンパク質様物 質であってよく、例えば乳タンパク質、乳漿タンパク質、カゼイン、肉タンパク 質、魚タンパク質、血液タンパク質、卵白又はゼラチンであってよい。 満足できる程度の加水分解を得るため、タンパク質分解酵素は100gのタンパ ク質当たりO.05−15AU、特に100gのタンパク質当たり0.1−8AUの量でタンパク 質又はタンパク質様物質に好ましく添加される。 インキュベーションは、約4〜約10のpH、好ましくは約5〜約9のpHで行うこ とができる。例2で示すように、本発明は極端なpH条件でさえ、すなわち5〜9 の範囲内の全てにおけるpH値で秀れて行うことができる。 インキュベーションは、酵素調製品が失活しない、すなわち約20℃〜約70℃の 範囲内におけるいずれの好都合の温度で行うことができる。 確立された慣習に従い、タンパク質分解酵素調製品は、インキュベーション混 合物の温度を約70℃超に増加することにより、又はインキュベーション混合物の pHを約4.0未満に減少させることにより適切に失活され得る。 別の好ましい態様において、タンパク質又はタンパク質様基質のインキュベー ションは、フレーバーザイム(商標)および1種又はそれ以上の他のプロテアー ゼ調製品の組合わせを用いて行うことができる。 好ましいプロテアーゼ調製品は、中性又はアルカリ性プロテアーゼを含んでな る。適当な中性プロテアーゼの例は、バシラス由来の中性プロテアーゼ、好まし くはバシラス ズブチリス由来の中性プロテアーゼ、例えば商標ニュートラーゼ (Neutrase)名で、ノボノルディスク(デンマーク)より市販されている酵素調 製品である。適当なアルカリプロテアーゼの例は、バシラス由来のアルカリプロ テアーゼ、好ましくはバシラス リケニホルミス(Bacillus licheniformis)由 来のアルカリプロテアーゼ、例えば商標アルカラーゼ(Alcalase)名でノボ ノ ルディスク(デンマーク)より市販されそして活性成分としてズブチリシンA( ズブチリシン カルスベルク(Subtilisin carlsberg))を含有する酵素調製品 である。 本発明方法で行なわれるインキュベーションは、またフレーバーザイム(Flav ourzyme)(商標)および1種又はそれ以上の他のリパーゼ調製品の組合わせを 用いて行うこともできる。 好ましいリパーゼ調製品は、菌類リパーゼを含んでなる。適当な菌類リパーゼ の例は、ムコール(Mucor)由来のリパーゼ、好ましく はリゾムコール マイヘイ(Rhizomucor miehei)由来のリパーゼ、例えば商標 パラターゼ(Palatase)名で、ノボ ノルディスク(デンマーク)より市販され ている酵素調製品;およびアスペルギルス(Aspergillus)由来のリパーゼ、好 ましくはアスペルギルス ニガー(Aspergillus niger)由来のリパーゼ、例え ば商標パラターゼ(Palatase)A名でノボ ノルディスク(デンマーク)より市 販されている酵素調製品を含んでなる。 別の態様において、本発明は本発明方法によって得られるタンパク質加水分解 物を提供する。AUの測定 タンパク質分解活性は、基質としてヘモグロビンを用いて測定できる。 タンパク質分解活性の測定に対するアンソン−ヘモグロビン法において、変性 ヘモグロビンが消化され、そして未消化ヘモグロビンは三塩化酢酸(TCA)によ り沈殿される。TCA可溶性生成物の量は、フェノール試薬を用いて測定され、そ のフェノール試薬はチロシンおよびトリプトファンに関して青色を与える。 1アンソン単位(AU)は、標準条件下(すなわち、25℃、pH 7.5および10分の 反応時間)、初期速度で、1分当たり1ミリ当量のチロシンと同じ色をフェノー ル試薬で与えるTCA可溶性生成物の量を遊離するような酵素の量として定義され る。 より詳細な分析方法を記載する折りたたんだ印刷物AF 4/5は、請求によりノ ボ ノルディスク A/S,DK−2880,バグスバエルト,デンマークから入手可 能であり、この印刷物をその番号を引用して本明細書に含まれる。LUの測定 リパーゼ活性の分析: リパーゼに対する基質を、乳化剤としてアラビアゴムを用いグリセリン−トリ ブチレート(MERCK)を乳化することにより調製した。 リパーゼ活性をpHスタット法を用いpH7で分析した。1単位のリパーゼ活性( LU/mg)は、1分当たり1マイクロモルの脂肪酸を遊離するために必要とされる 量として定義される。 工程1:発酵上澄みを遠心分離し、沈殿物をすてる。上澄みのpHを7に調節し 次いで同容量の冷96%エタノールを徐々に加える。混合物を30分間氷浴中に放置 する。遠心分離し次いで沈殿物をすてる。 工程2:イオン交換クロマトグラフィー。上澄みを濾過し次いで50mMのトリス ーアセテート緩衝液(pH7)で平衡にしたDEAE−高速流(ファルマシアTM)カラ ムに適用する。280nmでの吸収が0.05OD未満になるまで、同緩衝液を用いてカラ ムを洗浄する。5倍カラム容量を用い、同緩衝液の線状塩勾配(0から0.5M NaCl )で結合酵素活性を溶出する。 工程3:疎水性クロマトグラフィー。固体酢酸アンモニウムを加えることによ り、酵素活性を含有するプールのモル濃度を0.8Mに調節する。0.8Mの酢酸アン モニウムで予じめ平衡化したTSKゲルブチル−トーヨパール650Cカラム(東ソー (株)、日本から入手可能)に酵素を適用する。未結合物質を0.8M酢酸アンモ ニウムで洗い次いで結合物質を蒸留水で溶出する。 工程4:リパーゼ活性含有プールを水で希釈しコンダクタンスを2mSおよびpH を7に調節する。50mMのトリス−アセテート緩衝液(pH7)で予じめ平衡化した 高速Qセファロース(ファルマシア)カラムにプールを適用する。結合酵素を線 状塩勾配で溶出する。食品生産物 別の面において、本発明は本発明のタンパク質加水分解物を含ん でなる食品生産物に関する。 食品生産物に配合されるタンパク質加水分解物の量は、典型的には1−30重量 %の範囲にあるであろう。 本発明の重要な食品生産物は、例えば母乳代替物の成分である。本発明方法に よって得られる高程度の加水分解のため、本発明のタンパク質加水分解物は好都 合に母乳代替物中に配合でき、この加水分解物は未加水分解乳タンパク質よりも 著しくより低いアレルギー性を有する。乳代替物は、このタイプの生産物に対す る従来文献(例えば、ヨーロッパ特許出願322,589)に示された方法と実質的に 同じ方法で製剤化できるが、但し、公知生産物に含まれるタンパク質加水分解物 は本発明のタンパク質加水分解物により代替される。 本発明の食品生産物は又、タンパク質補促物として又は食品生産物の他の性質 を提供するため本発明のタンパク質加水分解物を含有できる。従って、食品生産 物中に配合されるタンパク質加水分解物は、砕いた骨を本発明方法に委ねること により骨から引き裂かれた肉又は切れはしの肉(例えばいわゆる機械的に回収さ れる肉、すなわち通常の肉片が屠殺場内の動物死体から刻まれた後に骨上に残っ ている肉)に例えば基づくことができる。一般的手順のより詳しい記載に対して は、出願人の同時係属国際特許出願WO 90/05462を参照のこと。肉産業からの他 のタンパク質副生産物もまた使用できる。 次いで得られたタンパク質加水分解物は乳化肉製品、例えばソーセージ又はパ テス(pates)に適当に添加できあるいは又スープもしくは他の食品製品中調味 料成分として添加できる。 本発明方法によりウシのミルクから得られる食品製品は、チーズ風味製品であ る。ミルクタンパク質の広範囲な加水分解は、非常に明確なチーズ風味を有する 風味化合物をもたらす。本発明のそのよ うなチーズ風味製品は、スナック製品、模擬チーズ製品において、又は一般にチ ーズ風味の増強剤として好ましく適用を見出す。チーズ風味は十分確立された慣 習に従いリパーゼの使用によって調節され得る。 調味料製品として使用するための加水分解された植物性タンパク質(HVP)を 製造するための伝統的方法は、高温でかつ長期間塩酸中で煮沸することを基礎に する。これは塩素含有化合物の未所望の形成を引き起こすことが知られている。 本発明方法により、酵素的に生産されたHVP製品(これはより健康的製品である と考えられる)を得ることが今や可能である。本発明方法により得ることのでき る高DHは、望ましい風味特性および風味増強特性をもたらす。 本発明方法はまた、本発明方法によって得られる苦みのない風味のためタンパ ク質に富んだ規定食製品に対しても使用できる。本発明方法に関連した非常に幅 広いpH域における極めて高いタンパク質の可溶性もまた有利である。 驚くべきことに次の内容が見出された;すなわち秀れた発酵培地がミルクを本 発明方法に委ねることにより製造できる。そのようなミルク加水分解物は、比較 的少量で添加することによりヨーグルト製造における発酵の加促のためまたは乳 酸スターター細菌培養物の製造において使用できる。プロセス時間を短縮すると 、生産能力が増加しそして感染、例えばバクテリオファージ感染の危険性が減少 する。 従って、本発明方法は発酵プロセス、好ましくは食品製品の製造に対する発酵 プロセスと組合わせて用いることができる。従って、本発明方法で用いられるタ ンパク質分解調製品、例えばフレーバーザイム(Flavourzyme)(商標)又は本 発明のタンパク質加水分解物又は双方は、発酵プロセス、好ましくは食品発酵プ ロセスにおいて発 酵プロセスの生産性を高めるために加えることができる。そのような発酵プロセ スの例は、魚(魚ソース)、ココア豆又は大豆(例えば大豆ソース、テンペ(te mpeh)、ミソ(miso))を含むか又は発酵プロセスである。タンパク質分解酵素 の添加又はタンパク質加水分解物の添加は、総プロセス時間の減少、すなわち発 酵速度の増加に対して有用である。非食品製品 本発明方法はその適用を非食品分野にも見出し得る。本発明によって得られる 風味特性は、ペットフードの生産に対して好都合に用いられる。 ゼラチンからの極めて高いDH−加水分解物の生産は、化粧品例えばクリームお よびシャンプーに配合すべきゼラチン製品を改良する。 前述の発酵媒質としての特別の効果は、本発明の加水分解物をして同様に他の 発酵に対して有用なさしめることが期待される。次の実施例により更に本発明を 説明するがそれらはいかなる場合も権利要求される本発明の範囲を制限するもの ではない。 例 1牛肉加水分解 この例において、次の酵素調製品(タンパク質含量基準で%w/wで示される )を用いて行った: 調製品A)2%フレーバーザイム(Flavourzyme)(商標)(2.30AU/g)、 調製品B)1%フレーバーザイム(Flavourzyme)(商標)、2%ニュートラー ゼ(Neutrase)(商標)0.5L、および0.15%アルカラーゼ(Alcalase)(商標 )2.4L。 全ての酵素は、ノボ ノルディスク A/S,デンマークから入手可能である 。フレーバーザイム(Flavourzyme)(商標)は、アルペ ルギルス オリゼ(Aspergillus oryzae)から由来するタンパク質分解調製品で あり、ニュートラーゼ(Neutrase)(商標)0.5Lはバシラス ズブチリス(Bac illus subtilis)由来のタンパク質分解調製品でありそしてアルカラーゼ(Alca lase)2.4Lは、バシラス リケニホルミス(Bacillus licheniformis)由来の タンパク質分解調製品である。 408gの牛肉を2回細かく切り刻み次いで392gの水と混合し10%w/wのタン パク質含量とした。混合物を30秒間混合し次いで55℃に加熱した。初期浸透圧重 量モル濃度(mOsm)および可溶性乾燥物質(°Brix)を測定し、次いで引き続き 加水分解をこれらの値により監視した。 4時間のインキュベーション後、酵素を90℃で30分間加熱することにより失活 させた。加水分解物を3000×Gで15分間遠心分離に委ねそして釈量した。遠心分 離物を翌日まで冷蔵庫内で保存し、脂質相が分離しそして釈量した。遠心分離物 のpHは5.85であった。 結果を下記の表1および表2に示す。 表から計算される如く、これらの実験において用いられたフレーバーザイム( Flavourzyme)(商標)の用量は収率を通常45%から81.5%に増加させ、そして 溶解度は通常57%から89.9%PSIに増加する。加水分解の程度70.2%DHが達成さ れた。 加水分解物を試験パネル前に4%溶液中に保存した。肉風味は、調製品Aを用 いて得られた加水分解物において最も明確であった。 例 2種々のpHでの加水分解 この実験において、本発明方法を基質としてナトリウムカゼイネートを用い5 〜9の範囲内のpH値で行った。 ナトリウムカゼイネート(ミプロダン(Miprodan)(商標)30、MDフードAmba (デンマーク)から得られる)の8%(w/w)溶液を、80℃に加熱することに より製造した。800gのこの溶液に、1gのメチル−4−ヒドロキシベンゾエー トおよび0.15gのプロピル−4−ヒドロキシベンゾエートを添加し、次いで溶液 の温度を50℃に下げた。4NのNaOH又は4NのHClを用いてpHを所望値に調節し た。 タンパク質含量基準で1%w/wのフレーバーザイム(Flavourzyme)(商標 )(2.30AU/g、ノボ ノルディスク A/S,デンマーク)を溶液に加え、次 いでインキュベーションを行い最大の加水分解まで進行せしめた(約22時間)。 pH9.00,8.00、および7.00で、加水分解をpHスタット中で行い、次いでインキ ュベーションをNaOHの消費により監視した。pH6.00および5.00(初期pH)で、減 少したpHおよび増加した浸透圧重量モル濃度により加水分解を監視した。 0.25,1,2,4.5および22時間のインキュベーション後サンプルを得た。85 ℃で3時間加熱し、次いで氷−水中で冷却することにより酵素を失活させた。結 果を図1に示す。この図から明らかなように本発明方法はpH5−pH9のpH域で加 水分解を与えることが可能である。 例 3比較例 この例において、本発明方法(フレーバーザイム(Flavourzyme)( 商標)を用いたインキュベーション)によって得られる加水分解の程度(DH)を 、他の公知のタンパク質分解調製品を用いてインキュベーションすることによっ て得られたDHと比較した。 4N NaOHで調節されたpH7.00で開始し、実験を非pHスタット加水分解として (加水分解中pHの調節なし)50℃で行なった。同じ酵素用量を確保するため、AU /gで現わされた(注:AUの定義については前記参照)同じタンパク質加水分解 活性を用い各加水分解を行った。 2種のタンパク質原料を試験した: 1)Na−カゼイネート(MDフードAmba(デンマーク)より市販) 2)大豆タンパク質単離物(タンパク質テクノロジーインタナショナル(米国) より市販)。 タンパク質原料の8%(タンパク質含量基準w/w)溶液2500gを調製した。 タンパク質溶液を85℃で3分間熱処理し次いで加水分解温度50℃に冷却した。 400gのサンプルを加水分解に対して調整した。以下の酵素および酵素用量を 用いた: 加水分解を22時間続けて行った。 加水分解の程度を、加水分解の5時間および22時間後それぞれ測定した。結果 を図2(大豆タンパク質単離物)および図3(Na−カゼイネート)に示す。結果 から、フレーバーザイム(Flavourzyme)を用いた加水分解は最高度の加水分解 を生じさせることが明らかである。 例 4チーズ風味生産 全乳を100℃で2分間加熱処理し次いで引き続き50℃に冷却した。各々200mlの 4個の部分を調製した(タンパク質含量を基準に%w/wで示す) 1)1%のフレーバーザイム(Flavourzyme)(商標)(2.30AU/g) 2)1%のフレーバーザイム(Flavourzyme)(商標)(2.30AU/g)+0.15% パラターゼ(Palatase)(商標)M 200L(ノボ ノルディスク A/S,デン マークから市販200LU/g) 3)0.15%のパラターゼ(Palatase)(商標)M 200L(ノボ ノルディスク A/S,デンマークより市販200LU/g) 4)対照 加水分解を50℃で20時間行った。強いチーズ風味がサンプル1,2および3に おいて現われたが、一方対照は殆ど中性であった。 風味−サンプル1,2および3を今やクリームチーズ内に希釈し、そして4番 目のサンプルを対照として調製した。 1.1)0.5gのサンプルNo.1+20gのチーズ 2.1)6.0gのサンプルNo.2+20gのチーズ 3.1)6.0gのサンプルNo.3+20gのチーズ 4.1)6.0gの新鮮なミルク+20gのチーズ。 サンプルNo.1.1(フレーバーザイム(商標))は非常に強くかつ濃い風味およ び十分熟したチーズの味を有するように思われた。サン プルNo.2.1(フレーバーザイム(商標)+パラターゼ(商標))は良好に均衡し たチーズ風味を有するように思われた。サンプルNo.1.1およびNo.2.1に比較する と、サンプルNo.3.1は最も希薄な味覚印象を与えた。参考サンプルNo.4.1は、す っぱい/少しすっぱいであると評価した。 結論として、酵素フレーバーザイム(Flavourzyme)(商標)並びにフレーバ ーザイム(商標)とパラターゼ(Palatase)(商標)の組合わせをミルクに直接 加え秀れたチーズ風味を形成することが可能である。 チーズ風味を生産する伝統的方法は、リパーゼおよびプロテアーゼをチーズに 添加することにより行なわれる。すなわち、フレーバーザイム(Flavourzyme) (商標)並びにパラターゼ(Palatase)(商標)と組合わせたフレーバーザイム は、チーズ風味を生産するために新規かつはるかにより簡単な方法を与える。 例 5加促されたヨーグルト発酵 全乳を100℃で2分間熱処理し次いで引き続き50℃に冷却した。200mlの2つの 部分を調製した(タンパク質含量に基づき%w/wで示す): 1)1%フレーバーザイム(商標)(2.30AU/g) 2)対照 加水分解を50℃で20時間行った。次いで酵素を80℃で5分間熱処理することに より変性した。 スキムミルクを90℃で2分間熱処理し次いでこれらのサンプル200mlを調製し た。 1.1)200mlのミルク+10mlのサンプルNo.1 2.1)200mlのミルク+10mlのサンプルNo.1 3.1)200mlのミルク 温度を41℃に調節し、次いでChr.ハンセンスラボラトリーからのヨーグルト 培養菌YC DVSを、g当たり106個の細菌のレベルで全ての3個のサンプルに加え た。 発酵曲線をpHを測定することにより追跡した、下記表4参照。 pH測定から以下の内容が明らかである;すなわち、フレーバーザイム(商標) 加水分解ミルクの添加は発酵を加促し、このことは発酵された乳製品の生産時間 が相当に減少され得ることを意味する。TECHNICAL FIELD The present invention relates to a protein hydrolysis method, a protein hydrolyzate obtained by the method, and a product other than a food containing the protein hydrolyzate. Background Art Protein hydrolysis methods have been described, for example, in British Patent 1,507,380, US Patent 3,723,250 and International Publications WO 89/00272, WO 92/13964 and WO 90/05462. There is a need for methods of hydrolyzing proteins that result in hydrolysates that have a high degree of protein hydrolysis and excellent organoleptic properties. SUMMARY OF THE INVENTION The following has now been found: a proteolytic enzyme preparation derived from Aspergillus oryzae and commercially available from Novo Nordisk A / S under the trademark "Flavourzyme". The product has excellent proteolytic properties, for example it is possible to obtain a high degree of hydrolysis and a bitter-free hydrolyzate. The present invention therefore relates to a process for the hydrolysis of proteins by incubation with a proteolytic preparation derived from Aspergillus oryzae and marketed by Novo Nordisk A / S under the trademark "Flavourzyme". In its second aspect, the present invention provides a protein hydrolyzate obtained by the method of the present invention. In another aspect, it relates to food products and non-food products comprising the protein hydrolyzate of the present invention. BRIEF DESCRIPTION OF THE DRAWINGS The present invention will be further described with reference to the accompanying drawings. FIG. 1 shows the time (hours) of hydrolysis versus the time of hydrolysis achieved by the method of the present invention applied to sodium casein within the pH range of pH 5-9 (■: pH 5, ▲ pH 6, ○ pH 7, □ pH 8, ● pH 9). Fig. 2 shows the degree of hydrolysis (% DH); Fig. 2 shows the degree of hydrolysis (% DH) of the soybean protein isolate after 22 hours of hydrolysis according to the method of the present invention (■: flavorzyme, ▲: corolase (Corolase). ) (Trademark) 7092, ◇: Corolase (trademark) 7093, ◆: Alcalase (trademark), □: Neutrase (trademark); and FIG. After the decomposition, the degree of hydrolysis (% DH) of Na-caseinate is shown (■: Flavorzyme (trademark), ▲: Corolase (trademark) 7092, ◇: Corolase (trademark) 7093, ◆: Alcalase (trademark), □ : Neutrase ( DETAILED DESCRIPTION OF THE INVENTION The characterization of Flavorzyme ™ has shown that the proteolytic Aspergillus oryzae preparation comprises several proteolytic components. Probably containing one or more proteolytic enzyme components, each of which has an approximate molecular weight of 23kD, 27kD, 31kD, 32kD, 35kD, 38kD, 42KD, 47KD, 53KD and 100KD. Therefore, the present invention is derived from Aspergillus oryzae and has at least 5 proteolytic cleavages with an approximate molecular weight selected from 23 kD, 27 kD, 31 kD, 32 kD, 35 kD, 38 kD, 42 kD, 47 kD, 53 kD and 100 kD, respectively. A method for hydrolyzing a protein by incubating with a proteolytic enzyme preparation comprising the components is provided. In one embodiment, the protein is derived from Aspergillus oryzae and incubated with a proteolytic preparation comprising at least 5 proteolytic preparations having approximate molecular weights of 23 kD, 31 kD, 35 kD, 38 kD and 53 kD, respectively. The molecular weight of the protease component in the product was measured by SDS polyacrylamide gel electrophoresis (SDS-PAGE) by a method known to those skilled in the art, and the molecular weight of each protease component was measured by this method. The method of the invention is capable of performing a wide range of protein hydrolysis of proteins, and this method results in a hydrolyzate which is bitter-free as well as having a pronounced soup / meat taste. The degree of protein hydrolysis can be determined by the degree of hydrolysis achieved. In the context of the present invention, the degree of hydrolysis (DH) is defined by the formula: DH can be calculated according to Adler Nissen; Enzymic Hydrolysis of Food Proteins; Els Brewer Applied Science Publishing Co. (1986), page 122. By using the method of the present invention, it is possible to obtain DH of 35% or more, preferably 60% or more, more preferably 70% or more, and most preferably 80% or more. It is also possible to obtain a high degree of protein solubility by the method of the present invention. The degree of protein solubility can be described by the protein solubility index (PSI) as described by Adler Nissen (supra). In a preferred embodiment, a protein solubility of 50% PSI or higher, preferably 70% PSI or higher, more preferably 90% or higher is obtained. The protein or proteinaceous substance which can be advantageously hydrolyzed by the method according to the invention may be any vegetable protein, such as soy protein, grain protein such as wheat gluten or zein, rapeseed protein, purple horse mackerel protein, noodles. Any protein, legume broad bean protein, cottonseed protein or sesame seed protein, or any animal protein or proteinaceous substance, such as milk protein, whey protein, casein, meat protein, fish protein, blood It may be protein, egg white or gelatin. In order to obtain a satisfactory degree of hydrolysis, the proteolytic enzyme is preferably added to the protein or protein-like substance in an amount of 0.05-5 AU per 100 g of protein, in particular 0.1-8 AU per 100 g of protein. Incubation can be performed at a pH of about 4 to about 10, preferably about 5 to about 9. As shown in Example 2, the present invention can be performed excellently even under extreme pH conditions, i.e. pH values in all in the range 5-9. Incubation can be performed at any convenient temperature within which the enzyme preparation is not inactivated, ie, in the range of about 20 ° C to about 70 ° C. According to established practice, the proteolytic enzyme preparation may be suitably inactivated by increasing the temperature of the incubation mixture above about 70 ° C or by reducing the pH of the incubation mixture below about 4.0. In another preferred embodiment, the incubation of the protein or protein-like substrate can be carried out with a combination of Flavorzyme ™ and one or more other protease preparations. A preferred protease preparation comprises neutral or alkaline proteases. Examples of suitable neutral proteases are neutral proteases from Bacillus, preferably neutral proteases from Bacillus subtilis, such as the enzyme preparations marketed by Novo Nordisk (Denmark) under the trade name Neutrase. Is. Examples of suitable alkaline proteases are those from Bacillus, preferably those from Bacillus licheniformis, such as those commercially available from Novo Nordisk (Denmark) under the trade name Alcalase and as an active ingredient subtilisin A. (Subtilisin carlsberg) is an enzyme preparation containing the same. The incubations carried out in the method of the present invention can also be carried out using a combination of Flavourzyme ™ and one or more other lipase preparations. A preferred lipase preparation comprises fungal lipase. Examples of suitable fungal lipases are lipases from Mucor, preferably lipases from Rhizomucor miehei, such as the enzyme preparation commercially available from Novo Nordisk (Denmark) under the trade name Palatase. A product; and a lipase derived from Aspergillus, preferably a lipase derived from Aspergillus niger, eg an enzyme preparation marketed by Novo Nordisk (Denmark) under the trademark Palatase A . In another aspect, the invention provides a protein hydrolyzate obtained by the method of the invention. Measurement of AU Proteolytic activity can be measured using hemoglobin as a substrate. In the Anson-hemoglobin method for measuring proteolytic activity, denatured hemoglobin is digested and undigested hemoglobin is precipitated with trichloroacetic acid (TCA). The amount of TCA soluble product is measured with a phenolic reagent which gives a blue color with respect to tyrosine and tryptophan. One Anson unit (AU) is a TCA soluble product that gives the same color as phenol equivalent to 1 milliequivalent of tyrosine per minute at standard rate under standard conditions (ie 25 ° C, pH 7.5 and reaction time of 10 minutes). It is defined as the amount of enzyme that liberates the amount of material. Folded print AF 4/5, which describes a more detailed analysis method, is available on request from Novo Nordisk A / S, DK-2880, Bagsbaert, Denmark, which print is referred to herein by its number. Included in the calligraphy. Measurement of LU Analysis of lipase activity: A substrate for lipase was prepared by emulsifying glycerin-tributyrate (MERCK) using gum arabic as emulsifier. Lipase activity was analyzed at pH 7 using the pH stat method. One unit of lipase activity (LU / mg) is defined as the amount required to release 1 micromol of fatty acid per minute. Step 1: Centrifuge the fermentation supernatant and drain the precipitate. The pH of the supernatant is adjusted to 7 and then an equal volume of cold 96% ethanol is added slowly. The mixture is left in the ice bath for 30 minutes. Centrifuge then drain the precipitate. Step 2: Ion exchange chromatography. The supernatant is filtered and then applied to a DEAE-fast flow (Pharmacia ™) column equilibrated with 50 mM Tris-acetate buffer (pH 7). The column is washed with the same buffer until the absorption at 280 nm is less than 0.05 OD. The bound enzyme activity is eluted with a linear salt gradient of the same buffer (0 to 0.5 M NaCl) using 5 column volumes. Step 3: Hydrophobic chromatography. The molarity of the pool containing enzyme activity is adjusted to 0.8 M by adding solid ammonium acetate. The enzyme is applied to a TSK gel butyl-Toyopearl 650C column (available from Tosoh Corporation, Japan) that has been pre-equilibrated with 0.8 M ammonium acetate. Unbound material is washed with 0.8 M ammonium acetate and the bound material is eluted with distilled water. Step 4: Dilute the pool containing lipase activity with water to adjust the conductance to 2 mS and pH. The pool is applied to a fast Q Sepharose (Pharmacia) column pre-equilibrated with 50 mM Tris-acetate buffer (pH 7). Bound enzyme is eluted with a linear salt gradient. Food Product In another aspect, the invention relates to a food product comprising the protein hydrolyzate of the invention. The amount of protein hydrolyzate incorporated into the food product will typically be in the range 1-30% by weight. An important food product of the invention is, for example, a component of breast milk substitutes. Due to the high degree of hydrolysis obtained by the method of the present invention, the protein hydrolyzate of the present invention can be conveniently incorporated into a milk substitute, which hydrolyzate has significantly lower allergenicity than unhydrolyzed milk protein. Have. The milk replacer can be formulated in substantially the same manner as shown in the prior art literature for this type of product (eg European patent application 322,589), except that the protein hydrolysates contained in known products are Is replaced by the protein hydrolyzate of the present invention. The food product of the invention may also contain a protein hydrolyzate of the invention as a protein enhancer or to provide other properties of the food product. Therefore, the protein hydrolyzate that is incorporated into the food product is meat that has been torn from the bone by subjecting the crushed bone to the method of the present invention or cut meat (e.g. so-called mechanically recovered meat, That is, it can be based, for example, on the meat that remains on the bone after a normal piece of meat has been carved from an animal carcass in a slaughterhouse. For a more detailed description of the general procedure, see Applicant's co-pending International Patent Application WO 90/05462. Other protein by-products from the meat industry can also be used. The resulting protein hydrolyzate can then be suitably added to emulsified meat products such as sausages or pates, or alternatively as a seasoning ingredient in soups or other food products. The food product obtained from bovine milk by the method of the present invention is a cheese flavored product. Extensive hydrolysis of milk proteins results in flavor compounds with a very distinct cheese flavor. Such cheese flavored products of the present invention find preferred application in snack products, simulated cheese products, or generally as cheese flavor enhancers. Cheese flavor can be adjusted by the use of lipase according to well-established practices. The traditional method for producing hydrolyzed vegetable protein (HVP) for use as a seasoning product is based on boiling at high temperature and for a long time in hydrochloric acid. This is known to cause the undesired formation of chlorine containing compounds. By the method of the present invention it is now possible to obtain enzymatically produced HVP products, which are considered to be healthier products. The high DH obtainable by the method of the present invention provides desirable flavor and flavor enhancing properties. The method of the present invention can also be used for dietary products that are rich in protein due to the bitter-free flavor obtained by the method of the present invention. The extremely high protein solubility in the very wide pH range relevant to the method of the invention is also advantageous. Surprisingly the following has been found: a good fermentation medium can be produced by subjecting milk to the process of the invention. Such milk hydrolysates can be used by adding in relatively small amounts to enhance fermentation in yogurt production or in the production of lactic starter bacterial cultures. Shortening the process time increases the production capacity and reduces the risk of infection, eg bacteriophage infection. Therefore, the method of the invention can be used in combination with a fermentation process, preferably a fermentation process for the production of food products. Thus, the proteolytic preparations used in the method of the invention, such as Flavorzyme ™ or the protein hydrolysates of the invention or both, enhance the productivity of the fermentation process in a fermentation process, preferably a food fermentation process. Can be added for. Examples of such fermentation processes include or are fish (fish sauce), cocoa beans or soybeans (eg soy sauce, tempeh, miso) or are fermentation processes. The addition of proteolytic enzymes or protein hydrolysates is useful for reducing the total process time, ie increasing the fermentation rate. Non-food products The method of the invention may find its application in the non-food field. The flavor profile obtained according to the invention is advantageously used for the production of pet food. The extremely high production of DH-hydrolyzate from gelatin improves gelatin products to be incorporated into cosmetics such as creams and shampoos. It is expected that the above-mentioned special effects as a fermentation medium will make the hydrolyzate of the present invention useful for other fermentations as well. The invention is further illustrated by the following examples, which in no way limit the scope of the invention claimed. Example 1 Beef Hydrolysis In this example the following enzyme preparations (expressed in% w / w on protein content basis) were used: Preparation A) 2% Flavorzyme ™ (2.30AU) / G), Preparation B) 1% Flavorzyme ™, 2% Neutrase ™ 0.5L, and 0.15% Alcalase ™ 2.4L. All enzymes are available from Novo Nordisk A / S, Denmark. Flavorzyme ™ is a proteolytic preparation derived from Aspergillus oryzae, Neutrase ™ 0.5L is a proteolytic preparation derived from Bacillus subtilis. And Alcalase 2.4L is a proteolytic preparation from Bacillus licheniformis. 408 g of beef was chopped twice and mixed with 392 g of water to give a protein content of 10% w / w. The mixture was mixed for 30 seconds and then heated to 55 ° C. Initial osmolality (mOsm) and soluble dry matter (° Brix) were measured and subsequently hydrolysis was monitored by these values. After incubation for 4 hours, the enzyme was inactivated by heating at 90 ° C for 30 minutes. The hydrolyzate was subjected to centrifugation at 3000 x G for 15 minutes and diluted. The centrifuge was stored in the refrigerator until the next day, the lipid phase separated and weighed. The pH of the centrifuge was 5.85. The results are shown in Tables 1 and 2 below. As calculated from the table, the dose of Flavorzyme ™ used in these experiments typically increased the yield from 45% to 81.5%, and the solubility usually from 57% to 89.9% PSI. To do. A degree of hydrolysis of 70.2% DH was achieved. The hydrolyzate was stored in a 4% solution before the test panel. The meat flavor was most pronounced in the hydrolyzate obtained with Preparation A. Example 2 Hydrolysis at Different pHs In this experiment, the process according to the invention was carried out with sodium caseinate as substrate at pH values in the range 5-9. An 8% (w / w) solution of sodium caseinate (Miprodan ™ 30, obtained from MD Hood Amba (Denmark)) was prepared by heating to 80 ° C. To 800 g of this solution was added 1 g of methyl-4-hydroxybenzoate and 0.15 g of propyl-4-hydroxybenzoate, then the temperature of the solution was reduced to 50 ° C. The pH was adjusted to the desired value with 4N NaOH or 4N HCl. Flavorzyme ™ (2.30 AU / g, Novo Nordisk A / S, Denmark) at 1% w / w based on protein content was added to the solution followed by incubation to allow maximum hydrolysis. (About 22 hours). At pH 9.00, 8.00, and 7.00, hydrolysis was performed in a pH stat, then incubation was monitored by NaOH consumption. Hydrolysis was monitored by decreasing pH and increasing osmolality at pH 6.00 and 5.00 (initial pH). Samples were obtained after 0.25, 1, 2, 4.5 and 22 hours of incubation. The enzyme was inactivated by heating at 85 ° C for 3 hours and then cooling in ice-water. The results are shown in Fig. 1. As is clear from this figure, the method of the present invention can give hydrolysis in the pH range of pH 5 to pH 9. Example 3 Comparative Example In this example, the degree of hydrolysis (DH) obtained by the method of the invention (incubation with Flavorzyme ™) is incubated with other known proteolytic preparations. It was compared with the DH obtained by Starting at pH 7.00 adjusted with 4N NaOH, experiments were performed as non-pH stat hydrolysis (no pH adjustment during hydrolysis) at 50 ° C. Each hydrolysis was performed with the same proteolytic activity expressed in AU / g (Note: see above for definition of AU) to ensure the same enzyme dose. Two protein sources were tested: 1) Na-caseinate (commercially available from MD Foods Amba (Denmark)) 2) Soy protein isolate (commercially available from Protein Technology International (USA)). 2500 g of 8% (w / w based on protein content) solution of protein raw material was prepared. The protein solution was heat treated at 85 ° C for 3 minutes and then cooled to a hydrolysis temperature of 50 ° C. A 400 g sample was prepared for hydrolysis. The following enzymes and enzyme doses were used: The hydrolysis was continued for 22 hours. The extent of hydrolysis was measured 5 and 22 hours after hydrolysis, respectively. The results are shown in Figure 2 (soy protein isolate) and Figure 3 (Na-caseinate). The results show that hydrolysis with Flavorzyme produces the highest degree of hydrolysis. Example 4 Cheese flavored whole milk was heat treated at 100 ° C for 2 minutes and then cooled to 50 ° C. Four portions of 200 ml each were prepared (% w / w based on protein content) 1) 1% Flavorzyme ™ (2.30 AU / g) 2) 1% flavorzyme ( Flavourzyme (TM) (2.30 AU / g) + 0.15% Palatase (TM) M 200L (Novo Nordisk A / S, commercially available from Denmark 200 LU / g) 3) 0.15% Palatase (TM) ) M 200 L (Novo Nordisk A / S, commercially available from Denmark 200 LU / g) 4) Control Hydrolysis was carried out at 50 ° C. for 20 hours. A strong cheese flavor appeared in Samples 1, 2 and 3, while the control was mostly neutral. Flavor-Samples 1, 2 and 3 are now diluted in cream cheese and a fourth sample was prepared as a control. 1.1) 0.5g sample No. 1 + 20g cheese 2.1) 6.0g sample No. 2 + 20g cheese 3.1) 6.0g sample No. 3 + 20g cheese 4.1) 6.0g fresh milk + 20g cheese. Sample No. 1.1 (Flavourzyme ™) appeared to have a very strong and intense flavor and a taste of ripe cheese. Sample No. 2.1 (Flavourzyme ™ + Paratase ™) appeared to have a well balanced cheese flavor. Compared to samples No.1.1 and No.2.1, sample No.3.1 gave the leanest taste impression. The reference sample No.4.1 was evaluated to be sour / slightly sour. In conclusion, it is possible to add the enzyme Flavorzyme ™ and the combination of Flavorzyme ™ and Palatase ™ directly to the milk to form an excellent cheese flavor. The traditional method of producing cheese flavor is performed by adding lipase and protease to cheese. Thus, flavorzymes in combination with Flavorzyme ™ as well as Palatase ™ provide a new and much simpler way to produce cheese flavor. Example 5 Accelerated yogurt fermented whole milk was heat treated at 100 ° C for 2 minutes and subsequently cooled to 50 ° C. Two 200 ml portions were prepared (% w / w based on protein content): 1) 1% Flavorzyme ™ (2.30 AU / g) 2) Control Hydrolysis was carried out at 50 ° C. for 20 hours. The enzyme was then denatured by heat treatment at 80 ° C for 5 minutes. Skim milk was heat treated at 90 ° C. for 2 minutes and then 200 ml of these samples were prepared. 1.1) 200 ml milk + 10 ml sample No.1 2.1) 200 ml milk + 10 ml sample No.1 3.1) 200 ml milk Adjust the temperature to 41 ° C and then Chr. Yogurt culture YC DVS from Hansense Laboratory was added to all three samples at a level of 10 6 bacteria per gram. The fermentation curve was followed by measuring pH, see Table 4 below. From the pH measurement it is clear that: the addition of Flavorzyme ™ hydrolyzed milk promotes fermentation, which means that the production time of fermented dairy products can be significantly reduced. .

───────────────────────────────────────────────────── 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 //(C12N 9/20 C12R 1:685) (C12N 9/20 C12R 1:785) (C12N 9/54 C12R 1:10) (C12N 9/54 C12R 1:125) (C12N 9/62 C12R 1:685) (81)指定国 EP(AT,BE,CH,DE, DK,ES,FR,GB,GR,IE,IT,LU,M C,NL,PT,SE),OA(BF,BJ,CF,CG ,CI,CM,GA,GN,ML,MR,NE,SN, TD,TG),AU,BB,BG,BR,BY,CA, CN,CZ,FI,HU,JP,KP,KR,KZ,L K,LV,MG,MN,MW,NO,NZ,PL,RO ,RU,SD,SK,UA,US,UZ,VN (72)発明者 ハンセン,キム デンマーク国,デーコー―4632 ベベルス コウ,カスタニィエバイ 30 (72)発明者 ブドルフセン,ギッテ デンマーク国,デーコー―2000 フレデリ ックスベルウ,3.テーベー.リィエバイ 3─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI // (C12N 9/20 C12R 1: 685) (C12N 9/20 C12R 1: 785) (C12N 9/54 C12R 1:10) (C12N 9/54 C12R 1: 125) (C12N 9/62 C12R 1: 685) (81) Designated countries EP (AT, BE, CH, DE, DK, ES, FR, GB, GR, IE) , IT, LU, MC, NL, PT, SE), OA (BF, BJ, CF, CG, CI, CM, GA, GN, ML, MR, NE, SN, TD, TG), AU, BB, BG, BR, BY, CA, CN, CZ, FI, HU, JP, KP, KR, KZ, LK, LV, MG, MN, MW, NO, NZ, PL, RO, RU, SD, SK, UA , S, UZ, VN (72) inventor Hansen, Kim Denmark, Deko -4632 Beberusu Kou, Kasutanyiebai 30 (72) inventor Budorufusen, Gitte Denmark, Deko -2000 Furederi Kkusuberuu, 3. tuberculosis. Liebye 3

Claims (1)

【特許請求の範囲】 1.タンパク質分解酵素調製品と共にインキュベートすることによるタンパク 質の加水分解方法であって、タンパク質分解調製品がアスペルギルス オリゼ( Aspergillus oryzae)から由来しそして各々がそれぞれ23kD,27kD,31kD,32kD ,35kD,38kD,42kD,47kD,53kD、および100kDから選ばれる、おおよその分子 量を有する少なくとも5個のタンパク質分解成分を含んでなる、前記方法。 2.タンパク質調製品が、それぞれおおよその分子量23kD,31kD,35kD,38kD および53kDを有する少なくとも5個のタンパク質分解成分を含んでなる、請求の 範囲第1項記載の方法。 3.35%超、好ましくは60%超、より好ましくは70%超、特に80%超のタンパ ク加水分解の程度(DH)が得られる、請求の範囲第1又は2項記載の方法。 4.50%超のPSI、好ましくは70%超のPSI、より好ましくは90%超のPSI(タ ンパク質溶解度脂標(PSI))が得られる、請求の範囲第1項記載の方法。 5.タンパク質が植物性タンパク質、好ましくは大豆タンパク質;穀粒タンパ ク質、例えば小麦グルテン又はゼイン;なたねタンパク質;アルファータンパク 質;エンドウ豆タンパク質;マメ科そら豆タンパク質;綿実タンパク質;又はご まの実タンパク質である請求の範囲第1〜4項のいずれか1項に記載の方法。 6.タンパク質が動物性タンパク質、好ましくはミルクタンパク質、乳漿タン パク質、カゼイン、肉タンパク質、魚タンパク質、血液タンパク質、卵白又はゼ ラチンである、請求の範囲第1〜4項のいずれか1項に記載の方法。 7.インキュベーションを約4〜約10のpHで、好ましくは約5〜 約9のpHで行う、請求の範囲第1〜6項のいずれか1項に記載の方法。 8.タンパク質を、1種又はそれ以上のプロテアーゼ調製品と組合せたタンパ ク質分解調製品と共にインキュベートする、請求の範囲第1〜7項のいずれか1 項に記載の方法。 9.プロテアーゼ調製品が、バシラス(Bacillus)、好ましくはバシラス ズ ブチリス(Bacillus subtilis)由来の中性プロテアーゼである、請求の範囲第 8項記載の方法。 10.プロテアーゼ調製品が、バシラス(Bacillus)、好ましくはバシラス リ ケニホルミス(Bacillus licheniformis)由来のアルカリプロテアーゼである、 請求の範囲第8項記載の方法。 11.タンパク質を、1種又はそれ以上のリパーゼ調製品と組合わせたタンパク 質分解調製品と共にインキュベートする、請求の範囲第1〜10項のいずれか1項 に記載の方法。 12.リパーゼ調製品が、ムコール(Mucor)、好ましくはリゾムコール マイ ヘイ(Rhizomucor miehei)に由来する真菌リパーゼを含んでなる、請求の範囲 第11項記載の方法。 13.リパーゼ調製品が、アスペルギルス(Aspergillus)、好ましくはアスペ ルギルス ニガー(Aspergillus niger)由来の真菌リパーゼを含んでなる、請 求の範囲第11項記載の方法。 14.タンパク質が加水分解されそして同時に食品製品に発酵される、請求の範 囲第1〜13項のいずれか1項に記載の方法。 15.請求の範囲第1〜13項のいずれか1項に記載の方法によって得られるタン パク質加水分解物。 16.加水分解タンパク質が、ミルクタンパク質、乳漿タンパク質、カゼイン、 肉タンパク質、魚タンパク質、血液タンパク質、卵白又はゼラチンから成る群か ら選ばれる動物性タンパク質である、請 求の範囲第15項記載のタンパク質加水分解物。 17.加水分解タンパク質が、大豆タンパク質;穀粒タンパク質、例えば小麦グ ルテン又はゼイン;なたねタンパク質;アルファータンパク質;エンドウ豆タン パク質;マメ科そら豆タンパク質;綿実タンパク質;およびごまの実タンパク質 から成る群から選ばれる植物性タンパク質である、請求の範囲第15項記載のタン パク質加水分解物。 18.請求の範囲第15〜17項のいずれか1項に記載のタンパク質加水分解物を含 んでなる食品製品。 19.母乳代替品成分;チーズ風味製品;酵素的に生産されたHVP;タンパク質 富化ダイエット製品;スープ−、ブイヨン−又は肉−風味製品;肉エキス製品; 又はスタータ−培養の生産を改善するための加水分解物である、請求の範囲第18 項記載の食品製品。 20.請求の範囲第15〜17項のいずれか1項に記載のタンパク質加水分解物を含 んでなる、非食品製品。 21.ペットフード、化粧品又は発酵ブロスである、請求の範囲第20項記載の非 食品製品。[Claims]   1. Protein by incubating with proteolytic enzyme preparation A method of hydrolyzing proteins, in which the proteolytic preparation is Aspergillus oryzae ( Aspergillus oryzae) and each 23kD, 27kD, 31kD, 32kD respectively Approximate molecule selected from 35kD, 38kD, 42kD, 47kD, 53kD, and 100kD Such a method comprising at least 5 proteolytic components in an amount.   2. Protein preparations have approximate molecular weights of 23kD, 31kD, 35kD, 38kD And at least 5 proteolytic components having 53 kD. The method according to claim 1.   Tamper of more than 3.35%, preferably more than 60%, more preferably more than 70%, especially more than 80% 3. The method according to claim 1 or 2, wherein the degree of hydrolysis (DH) is obtained.   4. Over 50% PSI, preferably over 70% PSI, more preferably over 90% PSI The method according to claim 1, wherein a protein solubility index (PSI) is obtained.   5. The protein is a vegetable protein, preferably soy protein; grain tamper Quality, such as wheat gluten or zein; rapeseed protein; alpha protein Quality; Pea Protein; Legume Broad Bean Protein; Cottonseed Protein; or Go The method according to any one of claims 1 to 4, which is a real protein.   6. The protein is an animal protein, preferably milk protein, whey tongue Protein, casein, meat protein, fish protein, blood protein, egg white or zebra The method according to any one of claims 1 to 4, which is ratin.   7. Incubation is at a pH of about 4 to about 10, preferably about 5 7. A method according to any one of claims 1-6, carried out at a pH of about 9.   8. Tampa combining protein with one or more protease preparations 8. Incubating with a quality degradation preparation, any one of claims 1-7. The method described in the section.   9. The protease preparation is Bacillus, preferably Bacillus A neutral protease derived from Bacillus subtilis. The method according to item 8.   Ten. The protease preparation is Bacillus, preferably Bacillus It is an alkaline protease derived from Keniformis (Bacillus licheniformis), The method according to claim 8.   11. Proteins that combine proteins with one or more lipase preparations 11. Incubation with a quality-prepared preparation, according to any one of claims 1-10. The method described in.   12. The lipase preparation is Mucor, preferably Rhizomucor Claims comprising a fungal lipase derived from Rhizomucor miehei The method described in paragraph 11.   13. The lipase preparation is Aspergillus, preferably Aspergillus. A contract comprising a fungal lipase from Aspergillus niger. The method described in the scope of claim 11.   14. Claims where the protein is hydrolyzed and simultaneously fermented into a food product. The method according to any one of items 1 to 13.   15. A tan obtained by the method according to any one of claims 1 to 13. Pak hydrolyzate.   16. Hydrolyzed protein is milk protein, whey protein, casein, A group consisting of meat protein, fish protein, blood protein, egg white or gelatin Is an animal protein selected from A protein hydrolyzate according to claim 15.   17. Hydrolyzed protein is soybean protein; grain protein such as wheat flour Ruten or Zein; Rapeseed Protein; Alpha Protein; Pea Tan Protein; legume broad bean protein; cottonseed protein; and sesame seed protein The plant protein according to claim 15, which is a vegetable protein selected from the group consisting of: Pak hydrolyzate.   18. A protein hydrolyzate according to any one of claims 15 to 17 is included. Food products   19. Breast milk substitute ingredients; cheese flavored products; enzymatically produced HVP; protein Enriched diet products; soup-, bouillon- or meat-flavored products; meat extract products; Or a hydrolyzate for improving the production of starter cultures. The food product described in paragraph.   20. A protein hydrolyzate according to any one of claims 15 to 17 is included. It is a non-food product.   twenty one. Pet food, cosmetics or fermentation broth, non-claim 20 Food products.
JP6523763A 1993-04-26 1994-04-25 Protein hydrolysis method Ceased JPH08509366A (en)

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