JPS6148913B2 - - Google Patents

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Publication number
JPS6148913B2
JPS6148913B2 JP54060895A JP6089579A JPS6148913B2 JP S6148913 B2 JPS6148913 B2 JP S6148913B2 JP 54060895 A JP54060895 A JP 54060895A JP 6089579 A JP6089579 A JP 6089579A JP S6148913 B2 JPS6148913 B2 JP S6148913B2
Authority
JP
Japan
Prior art keywords
autolysis
bacterial cells
yeast
alkali
added
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.)
Expired
Application number
JP54060895A
Other languages
Japanese (ja)
Other versions
JPS55153591A (en
Inventor
Osamu Uchi
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.)
Mitsubishi Kasei Corp
Original Assignee
Mitsubishi Kasei Corp
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 Mitsubishi Kasei Corp filed Critical Mitsubishi Kasei Corp
Priority to JP6089579A priority Critical patent/JPS55153591A/en
Publication of JPS55153591A publication Critical patent/JPS55153591A/en
Publication of JPS6148913B2 publication Critical patent/JPS6148913B2/ja
Granted legal-status Critical Current

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  • Coloring Foods And Improving Nutritive Qualities (AREA)

Description

【発明の詳細な説明】 本発明は菌体の自己消化法に関するものであ
り、詳しくは自己消化に先立つて菌体にアルカリ
処理を施し、菌体に自己消化に必要な酵素を失活
させない限度で変化を起こさせ、同時に他の汚染
菌の生活能を停止ないし衰退させて自己消化中に
おける腐敗を抑制する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for self-digestion of bacterial cells, and more specifically, prior to autolysis, the bacterial cells are treated with alkali to the extent that the enzymes necessary for self-digestion are not deactivated. The present invention relates to a method for suppressing putrefaction during autolysis by causing changes in bacteria and at the same time stopping or weakening the viability of other contaminating bacteria.

菌体、特に酵母を自己消化させて酵母エキスを
製造することは公知である。このような自己消化
法としては、酵母に食塩を高濃度で添加したり、
酢酸エチル等の有機溶媒を添加して強制的に原形
質分離を生起させ、酵母を泥状化させたのち30〜
70℃程度で自己消化を行なわせる方法がある。し
かし高濃度の食塩の添加は得られる酵母エキス中
の食塩濃度を高めるので好ましいことではなく、
また食塩添加物でない有機溶媒の使用も本来避け
るべきものである。このような難点を解決する方
法として、比較的少量の食塩とエタノールを併用
する方法が提案されている(特開昭49―62675参
照)。
It is known to produce yeast extract by autolyzing bacterial cells, especially yeast. Such autolysis methods include adding high concentrations of salt to yeast,
After adding an organic solvent such as ethyl acetate to forcibly cause protoplasm separation and turning the yeast into a slurry,
There is a method of autolysis at around 70°C. However, adding a high concentration of salt is not desirable as it increases the salt concentration in the yeast extract obtained.
Furthermore, the use of organic solvents other than salt additives should also be avoided. As a method to solve these difficulties, a method has been proposed in which a relatively small amount of salt and ethanol are used in combination (see Japanese Patent Application Laid-Open No. 49-62675).

本発明はかかる方法とは異なり、生菌体をPH
10.5以上でアルカリ処理し、菌体がメチレンブル
ーで明らかに染色されるに至らしめたのち、PH5
〜9で自己消化させることを特徴とする菌体の自
己消化法に存する。
The present invention differs from such methods by converting live bacterial cells into PH
After treating with alkali at a pH of 10.5 or higher to ensure that the bacterial cells are clearly stained with methylene blue,
The present invention relates to a method for self-digestion of bacterial cells, which is characterized by carrying out self-digestion at steps 9 to 9.

本発明について以下に詳細に説明すると、本発
明の自己消化法の対象となるものは種々の酵母や
細菌などの生菌体である。
The present invention will be described in detail below. The targets of the autolysis method of the present invention are live microbial cells such as various yeasts and bacteria.

例えばサツカロマイセス・セレビシエ
(Saccharomycess cerevisiae)、サツカロマイセ
ス・カールスベルゲンシス(Saccharomycess
carlsbergensis)等のサツカロマイセス属酵母、
キヤンデイダ・ウチリス(Candida utilis)、キ
ヤンデイダ・トロピカリス(Candida
tropicalis)等のキヤンデイダ属酵母、ピヒア・
ミソ(Pichia miso)等の酵母及びプレビバクテ
リウム属(Brevibacterium sp.)やコリネバクテ
リウム属(Corynebacterium sp.)で代表される
アミノ酸発酵細菌等が原料として用いられる。こ
れらの酵母や細菌は種々の発酵工業の副産物とし
て得られたものを利用してもよく、また菌体生産
を目的として培養したものを用いてもよい。例え
ばビール工業の副産物であるビール酵母は、本発
明方法の代表的な原料菌体である。これらの菌体
は生菌体であることが必要である。生菌体は後述
のメチレンブルー染色法で洗色されないので容易
に識別できる。もちろん生菌体中に若干のメチレ
ンブル染色法で染色され得る菌体を含んでいるも
のも本発明方法の原料とすることができる。従つ
て本発明方法の原料は実質的に生菌体であればよ
い。
For example, Saccharomyces cerevisiae, Saccharomyces carlsbergensis
yeasts of the genus Satucharomyces, such as Carlsbergensis),
Candida utilis, Candida tropicalis
yeasts of the Candeida genus, such as Pichia
Yeast such as Pichia miso and amino acid-fermenting bacteria represented by Brevibacterium sp. and Corynebacterium sp. are used as raw materials. These yeasts and bacteria may be obtained as by-products of various fermentation industries, or may be cultured for the purpose of producing bacterial cells. For example, brewer's yeast, which is a byproduct of the beer industry, is a typical raw material bacterial cell for the method of the present invention. These microbial cells need to be viable microbial cells. Live bacteria can be easily identified because they are not washed by the methylene blue staining method described below. Of course, viable cells containing some cells that can be stained with methylene blue staining can also be used as the raw material for the method of the present invention. Therefore, the raw material for the method of the present invention may be substantially viable bacterial cells.

本発明でこれらの菌体をPH10.5以上でアルカリ
処理する。通常は所定のPHのアルカリ水溶液に菌
体を懸濁させて若干撹拌するだけでよい。アルカ
リとしては苛性ソーダ、水酸化カルシウム、アン
モニア等のいずれをも用いることができるが、通
常は苛性ソーダ、水酸化カルシウム又はこの両者
を併用する。アルカリ処理のPHが低いと、アルカ
リ処理に長時間を要し且つ汚染菌の不活性化が不
十分で、後続する自己消化中に腐敗を起こすこと
がある。一方、PHが高すぎるとアルカリ処理中に
菌体から核酸や蛋白質が溶出し且つ酵素の活性も
損なわれ易い。従つてアルカリ処理はPH11〜13、
特に11.5〜12.5で行なうのが好ましい。なお、ア
ルカリ処理中にPHが漸次低下するが、通常はその
まま放置して差支えない。
In the present invention, these bacterial cells are treated with alkali at a pH of 10.5 or higher. Normally, it is sufficient to suspend the bacterial cells in an aqueous alkaline solution of a specified pH and stir it slightly. As the alkali, any of caustic soda, calcium hydroxide, ammonia, etc. can be used, but usually caustic soda, calcium hydroxide, or both are used in combination. If the pH of the alkaline treatment is low, the alkaline treatment takes a long time and the inactivation of contaminants is insufficient, which may cause spoilage during the subsequent autolysis. On the other hand, if the pH is too high, nucleic acids and proteins are likely to be eluted from the bacterial cells during alkaline treatment, and enzyme activity is likely to be impaired. Therefore, alkaline treatment has a pH of 11 to 13,
In particular, it is preferable to carry out at 11.5 to 12.5. Note that the pH will gradually decrease during the alkali treatment, but normally it can be left as is.

アルカリ処理に際しては後続する自己消化が阻
害されないように、すなわち菌体の酵素活性がで
きるだけ保存されるようにすることが重要であ
る。従つてアルカリ処理は低温で行なうことが好
ましく、通常は0〜40℃、好ましくは5〜30℃で
行なれる。アルカリ処理は菌体がメチレンブルー
染色法により、明らかに染色されるようになるま
で行なう。なおメチレンブルー染色法とは、アル
カリ処理した菌体懸濁液を水で稀釈してスライド
ガラス上に一滴とり、これにメチレンブルー液
(メチレンブルー0.02gを蒸留水50mlに溶解させ
た溶液と、Na2HPO4・12H2O0.018gと
KH2PO42.70gを蒸留水50mlに溶解させた溶液と
を一緒にした溶液)を一滴加え、菌体が染色され
たか否かを顕微鏡で観察する方法である。メチレ
ンブルー染色法で明らかに染色されるようになれ
ば、染色された菌体だけでなく未染色の菌体も既
に変化しているので、アルカリ処理を中止して未
染色の菌体は短時間のうちに染色されるに至る。
通常は菌体の50%以上が染色されるまでアルカリ
処理を行なう。染色された菌体の比率は血球盤を
用いることにより容易に算出することができき
る。
During alkaline treatment, it is important to ensure that the subsequent autolysis is not inhibited, that is, that the enzymatic activity of the bacterial cells is preserved as much as possible. Therefore, it is preferable to carry out the alkali treatment at a low temperature, usually from 0 to 40°C, preferably from 5 to 30°C. The alkaline treatment is carried out until the bacterial cells become clearly stained by methylene blue staining. The methylene blue staining method involves diluting an alkali-treated bacterial cell suspension with water, placing a drop on a slide glass, and adding methylene blue solution (a solution of 0.02 g of methylene blue dissolved in 50 ml of distilled water) and Na 2 HPO. 4・12H 2 O0.018g
In this method, one drop of a solution (combined with a solution of 2.70 g of KH 2 PO 4 dissolved in 50 ml of distilled water) is added, and the microbial cells are observed under a microscope to see if they are stained. If the methylene blue staining method clearly stains the cells, not only the stained cells but also the unstained cells have already changed, so stop the alkali treatment and remove the unstained cells for a short period of time. It ended up being dyed.
Usually, alkaline treatment is carried out until 50% or more of the bacterial cells are stained. The ratio of stained bacterial cells can be easily calculated using a hemocyte disc.

アルカリ処理の時間は通常1〜60分であり、ア
ルカリ性が強いほど、また温度が高いほど短時間
の処理でよい。例えばPH12以上の強アルカリ性で
は、通常、1分未満の極めて短い時間で明らかに
染色が認められる。処理時間が長いと酵素が失活
するおそれがあるので、必要以上に長時間の処理
をするのは好ましくない。好ましいアルカリ処理
時間は20分以内である。特にPH11.5〜12.5で5分
以内の処理が好ましい。
The time for the alkaline treatment is usually 1 to 60 minutes, and the stronger the alkalinity or the higher the temperature, the shorter the treatment may be. For example, in strong alkalinity with a pH of 12 or higher, staining is usually clearly observed in an extremely short time of less than 1 minute. If the treatment time is too long, the enzyme may be deactivated, so it is not preferable to carry out the treatment for a longer time than necessary. The preferred alkali treatment time is within 20 minutes. In particular, treatment within 5 minutes at pH 11.5 to 12.5 is preferred.

アルカリ処理が終つた菌体は、所望により遠心
分離してアルカリ水溶液の大部分を除去し、更に
要すれば水洗したのち、直ちに酸を加えてPHを下
げ次の自己消化を行なわせる。例えば原料菌体が
多量の不純物を含む場合及びアルカリ処理工程で
多量のアルカリを使用したためそのまま中和した
のでは得られる自己消化液中に許容量以上の塩類
が混入する場合には、遠心分離を行なうのが好ま
しい。
After the alkaline treatment, the bacterial cells are centrifuged if desired to remove most of the alkaline aqueous solution, and if necessary, washed with water, and then acid is immediately added to lower the pH and carry out the next autolysis. For example, if the raw material contains a large amount of impurities, or if a large amount of alkali was used in the alkali treatment process and the resulting autolysis solution would contain more than the allowable amount of salts, centrifugation is necessary. It is preferable to do so.

自己消化はアルカリ処理の終つた菌体に酸を加
え、PHを5〜9に調整しながら行なう。酸として
は塩酸、燐酸等の無機酸及び酢酸、クエン酸、リ
ンゴ酸、乳酸等の有機酸が用いられる。アルカリ
処理を水酸化カルシウムを含む水溶液中で行なつ
た場合には、酸として燐酸ないし燐酸と他の酸と
を併用して、カルシウムを燐酸カルシウムとして
析出させるのが好ましく、かくすることにより更
にすぐれた自己消化液が得られる。
Autolysis is carried out by adding acid to the bacterial cells that have been treated with alkali and adjusting the pH to 5-9. As the acid, inorganic acids such as hydrochloric acid and phosphoric acid, and organic acids such as acetic acid, citric acid, malic acid, and lactic acid are used. When the alkali treatment is carried out in an aqueous solution containing calcium hydroxide, it is preferable to use phosphoric acid or a combination of phosphoric acid and another acid as the acid to precipitate the calcium as calcium phosphate, which provides an even better result. An autolyzed solution can be obtained.

特に生菌体にビール工業の副産物であるビール
酵母を用いた場合には、自己消化液中にホツプに
由来すると考えられるにがみがあるが、アルカリ
として水酸化カルシウムを用い且つ酸として燐酸
を用いてカルシウムを燐酸カルシウムとして析出
させると、自己消化液のにがみも同時に除去する
ことができる。自己消化は菌体を5〜25(重量)
%の懸濁液とし、若干撹拌しつつ20〜50℃、特に
30〜50℃に保持することにより容易に行なうこと
ができる。なお、自己消化中に液のPHは漸次低下
するので、本発明ではアルカリ処理した菌体をPH
9より若干高いPHまで中和して自己消化を開始さ
せ、自己消化の実質的部分はPH5〜9で行なわせ
るようにすることもできる。しかしPH5〜9の範
囲外では自己消化は著るしく遅いので、最初から
PH5〜9に調整して自己消化させるのが好まし
い。自己消化に要する時間は温度及びアルカリ処
理の条件によつても異なるが、通常10〜30時間程
度である。なお、自己消化に際しては、アルカリ
処理を経た菌体に食塩、グルタミン酸ソーダ、蛋
白分解アミノ酸液、魚肉エキス、野菜エキス、肉
エキス、酵母エキス等を添加してもよい。これら
の添加物を加えると、アルカリ処理は経たが未だ
未染色の菌体も速かに染色されて自己消化が均一
に進行する。また自己消化液の浸透圧が高くなつ
て防腐能が向上する利点もある。添加量は通常、
自己消化液中の濃度として1〜数(重量)%程度
で十分である。自己消化が終了したならば、加熱
して酵素を失活させる。かくして得られた自己消
化液は残渣を分離したのち濃縮して酵母エキス等
としてもよく、またそのまま濃縮して調味料とす
ることもできる。所望ならば濃縮に先立ち骨粉や
他のエキス、油脂等を添加してもよい。
In particular, when brewer's yeast, a byproduct of the beer industry, is used as the living microbial cell, there is a bitterness in the autolysis liquid that is thought to originate from hops, but calcium hydroxide is used as the alkali and phosphoric acid is used as the acid. When calcium is precipitated as calcium phosphate, the bitterness of the autolytic fluid can be removed at the same time. Autolysis reduces bacterial cells to 5-25 (weight)
% suspension, and stir it slightly at 20-50℃, especially
This can be easily done by maintaining the temperature at 30 to 50°C. Note that the pH of the liquid gradually decreases during autolysis, so in the present invention, the pH of the alkali-treated bacterial cells is reduced.
It is also possible to initiate autolysis by neutralizing to a pH slightly above 9, with a substantial portion of the autolysis occurring at a pH of 5-9. However, autolysis is extremely slow outside the pH range of 5 to 9, so from the beginning
It is preferable to adjust the pH to 5 to 9 for autolysis. The time required for autolysis varies depending on the temperature and alkali treatment conditions, but is usually about 10 to 30 hours. For autolysis, salt, sodium glutamate, proteolytic amino acid solution, fish extract, vegetable extract, meat extract, yeast extract, etc. may be added to the alkaline-treated bacterial cells. When these additives are added, even unstained bacterial cells that have undergone alkali treatment are rapidly stained, and autolysis progresses uniformly. There is also the advantage that the osmotic pressure of the autolyzing fluid is increased and the preservative ability is improved. The amount added is usually
A concentration of about 1 to several (weight) % in the autolysis fluid is sufficient. Once autolysis is complete, the enzymes are deactivated by heating. After separating the residue, the autolyzed liquid obtained in this manner may be concentrated to produce a yeast extract or the like, or it may be directly concentrated to be used as a seasoning. If desired, bone meal, other extracts, oils, etc. may be added prior to concentration.

本発明方法によれば、食品添加物として許容さ
れているものだけを用いて、腐敗をおこさせるこ
となく自己消化を行なわせることができ、得られ
る自己消化液は風味にすぐれている。
According to the method of the present invention, autolysis can be carried out without causing spoilage by using only food additives that are allowed, and the resulting autolysis liquid has excellent flavor.

次に実施例により本発明を更に詳細に説明する
が、本発明は以下の実施例に限定されるものでは
ない。
EXAMPLES Next, the present invention will be explained in more detail with reference to examples, but the present invention is not limited to the following examples.

なお、実施例で用いたパン酵母は下記の方法に
より取得したものである。市販のパン酵母10Kgを
水道水で6倍に稀釈してスラリーとしたのち、遠
心清浄機で酵母を濃縮する操作を5回反復して、
固形分18(重量)%の酵母を得た。糖8(重量)
%(糖としてはスラツジを分離した糖蜜を使
用)、硫安1(重量)%、KH2PO4 0.2(重量)
%、NH4H2PO4 0.6(重量)%、MgSO4・7H2O
0.03(重量)%、酵母エキス0.2(重量)%、ビ
チオン2μg/の培地を加熱殺菌して、撹拌機
を備えた100の培養槽に仕込んだ。これに前記
の固形分18%の酵母を投入し、アンモニア水でPH
を5に保ちながら20℃で8時間培養し、酵母が分
裂したことを確認した。次いで10℃で24時間静置
培養を行なつたのち、遠心分離して酵母を回収し
た。酵母は5回水洗したのち遠心分離機で脱水し
て、固形分26(重量)%、乾物の粗蛋白質含量
52.4(重量)%のパン酵母とした。
The baker's yeast used in the examples was obtained by the following method. After diluting 10kg of commercially available baker's yeast 6 times with tap water to make a slurry, the process of concentrating the yeast using a centrifugal cleaner was repeated 5 times.
Yeast with a solid content of 18% (by weight) was obtained. Sugar 8 (weight)
% (molasses separated from sludge is used as sugar), ammonium sulfate 1% (by weight), KH 2 PO 4 0.2 (by weight)
%, NH4H2PO4 0.6 ( weight )%, MgSO47H2O
A medium containing 0.03% (by weight), 0.2% (by weight) yeast extract, and 2 μg/bithion was heat sterilized and placed in 100 culture vessels equipped with a stirrer. Add the above-mentioned yeast with a solid content of 18% to this, and pH it with ammonia water.
After culturing at 20°C for 8 hours while maintaining the temperature at 5, it was confirmed that the yeast had split. After static culture was then performed at 10°C for 24 hours, the yeast was collected by centrifugation. The yeast was washed with water five times and then dehydrated using a centrifuge to reduce the solid content to 26% (by weight) and the crude protein content on the dry matter.
It was made into 52.4 (weight)% baker's yeast.

実施例 1 パン酵母100gに、30℃の水30ml及び1N―
NaOHを加えてPH10.7のスラリーとし、20分間撹
拌した。メチレンブルー染色率は80%以上であつ
た。次いでこのスラリーに1N―HClを加えてPHを
9.2とし、38〜40℃で16時間自己消化を行なわせ
た。自己消化終了時のPHは6.5であつた。得られ
た自己消化液は1N―HClでPH6.0に調節し、水を
加えて500gとし、95〜99℃に5分間保持した。
次いで遠心沈降管で上澄液と沈澱とに分離し、沈
澱は水を加えて500gとしたのち再び遠心沈降管
で上澄液と沈澱とに分離した。沈澱の乾物重量は
15.1gであつた。従つて酵母の乾物重量の42%が
自己消化により菌体外に抽出されたことになる
(以下、これをエキス抽出率という)。
Example 1 100g of baker's yeast, 30ml of water at 30℃ and 1N
NaOH was added to make a slurry of pH 10.7, and the mixture was stirred for 20 minutes. The methylene blue staining rate was over 80%. Next, add 1N HCl to this slurry to adjust the pH.
9.2, and autolysis was performed at 38-40°C for 16 hours. The pH at the end of autolysis was 6.5. The resulting autolysis solution was adjusted to pH 6.0 with 1N-HCl, water was added to make 500 g, and the solution was kept at 95-99°C for 5 minutes.
Next, it was separated into a supernatant liquid and a precipitate using a centrifugal sedimentation tube, and the precipitate was made up to 500 g by adding water, and then separated into a supernatant liquid and a precipitate using a centrifugal sedimentation tube again. The dry weight of the precipitate is
It was 15.1g. Therefore, 42% of the dry weight of yeast was extracted outside the cells by autolysis (hereinafter, this is referred to as extract extraction rate).

実施例 2 パン酵母100gに20℃の水30ml及び1N―NaOH
を加えてPH12.4のスラリーとし、10分間撹拌し
た。メチレンブルー染色率は80%以上であつた。
次いでこのスラリーに1N―NClを加えてPH9.0と
し、38〜40℃で16時間自己消化を行なわせた。自
己消化終了時のPHは6.5であつた。自己消化液は
実施例1と同様に処理し、エキス抽出率38%を得
た。
Example 2 100g of baker's yeast, 30ml of water at 20℃ and 1N-NaOH
was added to make a slurry with a pH of 12.4, and the mixture was stirred for 10 minutes. The methylene blue staining rate was over 80%.
Next, 1N-NCl was added to this slurry to adjust the pH to 9.0, and autolysis was performed at 38 to 40°C for 16 hours. The pH at the end of autolysis was 6.5. The autolytic solution was treated in the same manner as in Example 1 to obtain an extract extraction rate of 38%.

実施例 3 ビール前発酵酵母(固形分13(重量)%)1Kg
に6N―NaOHを加えてPH12.7のスラリーとし、10
℃で10分間撹拌した。メチレンブルー染色率は90
%以上であつた。このスラリーに6N―HClを加え
てPH8.0とし、38℃で20時間自己消化を行なわせ
た。自己消化終了時のPHは6.2であつた。自己消
化液は70℃以上に10分間加熱したのち遠心沈降機
で上澄液と沈澱とに分離した。沈澱は沸騰水600
gを加えて1時間撹拌したのち再び遠心沈降機で
上澄液と沈澱とに分離した。エキス抽出率は34%
であつた。
Example 3 Beer pre-fermentation yeast (solid content 13 (weight)%) 1Kg
Add 6N-NaOH to make a slurry with pH 12.7,
Stir for 10 minutes at °C. Methylene blue staining rate is 90
% or more. 6N-HCl was added to this slurry to adjust the pH to 8.0, and autolysis was performed at 38°C for 20 hours. The pH at the end of autolysis was 6.2. The autolysis solution was heated to 70°C or higher for 10 minutes and then separated into a supernatant and a precipitate using a centrifugal sedimentation machine. Precipitate with boiling water 600
After stirring for 1 hour, the mixture was again separated into a supernatant liquid and a precipitate using a centrifugal sedimentation machine. Extract extraction rate is 34%
It was hot.

実施例 4 ビール前発酵酵母(固形分13(重量)%)1Kg
に6N―NaOHを加えてPH8.0とし、更に水酸化カ
ルシウムを加えてPH12.3とし、8℃で10分間撹拌
した。メチレンブルー染色率は80%以上であつ
た。このスラリーに冷水2Kgを加えて遠心沈降機
で上澄液と沈澱とに分離し、沈澱は冷水2Kgを加
えて再び遠心沈降機で上澄液と沈澱とに分離し
た。この沈澱に1N―H3PO4を加えてPH7.5とし、
40℃で16時間自己消化を行なわせた。自己消化終
了時のPHは6.8であり、エキス抽出率は37%であ
つた。
Example 4 Beer pre-fermentation yeast (solid content 13 (weight)%) 1Kg
6N-NaOH was added to adjust the pH to 8.0, calcium hydroxide was further added to adjust the pH to 12.3, and the mixture was stirred at 8°C for 10 minutes. The methylene blue staining rate was over 80%. 2 kg of cold water was added to this slurry, and the slurry was separated into a supernatant liquid and a precipitate using a centrifugal sedimentation machine, and the precipitate was separated into a supernatant liquid and a precipitate using a centrifugal sedimentation machine again after adding 2 kg of cold water. Add 1N-H 3 PO 4 to this precipitate to adjust the pH to 7.5,
Autolysis was performed at 40°C for 16 hours. The pH at the end of autolysis was 6.8, and the extract extraction rate was 37%.

実施例 5 ビール後発酵酵母(固形分15(重量)%)1Kg
に1N―NaOHを加えてPH7.5とし、更に水酸化カ
ルシウムを加えてPH11.5とし、10℃で10分間撹拌
した。メチレンブルー染色率は90%以上であつ
た。このスラリーを遠心沈降機で上澄液液と沈澱
とに分離し、沈澱は冷水500gを加えて再び上澄
液と沈澱とに分離した。この沈澱に1N―H3PO4
を加えてPH7.5とし、40℃で16時間自己消化を行
なわせた。エキス抽出率は33%であつた。
Example 5 Beer post-fermenting yeast (solid content 15% (weight)) 1Kg
1N-NaOH was added to adjust the pH to 7.5, calcium hydroxide was added to adjust the pH to 11.5, and the mixture was stirred at 10°C for 10 minutes. The methylene blue staining rate was over 90%. This slurry was separated into a supernatant liquid and a precipitate using a centrifugal sedimentation machine, and the precipitate was separated into a supernatant liquid and a precipitate again by adding 500 g of cold water. 1N―H 3 PO 4 to this precipitate
was added to adjust the pH to 7.5, and autolysis was performed at 40°C for 16 hours. The extract extraction rate was 33%.

実施例 6 キヤンデイダ・ウチリス(Candida utilis)を
廃糖蜜培地で培養し、培養液から酵母を回収し
た。これを水洗して不純物を殆んど含まない酵母
(固形分20(重量)%)を得た。この酵母に1N―
NaOHを加えてPH12.5とし10℃で10分間撹拌し
た。メチレンブルー染色率は90%以上であつた。
これに1N―HClを加えてPH7.5とし、このPHを維
持しながら40℃で16時間自己消化を行なせた。次
いで実施例3と同様に処理してエキス抽出率31%
得た。
Example 6 Candida utilis was cultured in a molasses medium, and yeast was collected from the culture solution. This was washed with water to obtain yeast (solid content 20% (weight)) containing almost no impurities. 1N for this yeast
NaOH was added to adjust the pH to 12.5 and the mixture was stirred at 10°C for 10 minutes. The methylene blue staining rate was over 90%.
1N-HCl was added to this to adjust the pH to 7.5, and autolysis was carried out at 40°C for 16 hours while maintaining this pH. Then, it was treated in the same manner as in Example 3 to obtain an extract extraction rate of 31%.
Obtained.

実施例 7 ビール前発酵酵母(固形分16(重量)%)234
g同量水加えてスラリーとし、更に1N―NaOHを
加えてPH10.9とし、11℃で5分間処理した。メチ
レンブルー染色率は20〜30%であつた。このスラ
リーを遠心分離して上澄液を捨て、沈澱114gに
0.5%塩酸を加えてPH8.4とし、更に食塩1.2gを加
えて、40℃で18時間自己消化を行なわせた。自己
消化終了時のPHは5.7でエキス抽出率は43%であ
つた。なお、食塩添加5分後のメチレンブルー染
色率は80%以上であつた。
Example 7 Beer pre-fermentation yeast (solid content 16 (weight)%) 234
The same amount of water was added to form a slurry, and 1N-NaOH was further added to adjust the pH to 10.9, followed by treatment at 11°C for 5 minutes. The methylene blue staining rate was 20-30%. Centrifuge this slurry and discard the supernatant, leaving 114 g of precipitate.
0.5% hydrochloric acid was added to adjust the pH to 8.4, 1.2 g of common salt was added, and autolysis was carried out at 40°C for 18 hours. At the end of autolysis, the pH was 5.7 and the extract extraction rate was 43%. In addition, the methylene blue staining rate 5 minutes after adding the salt was 80% or more.

実施例 8 ビール前発酵酵母(固形分16(重量)%)234
gに5〜7℃の水を同量加え、1N―NaOHでPH
12.3として20秒間保持した。メチレンブルー染色
率は約50%であつた。直ちに遠心分離して上澄液
を捨て、沈澱に1%塩酸を加えてPH8.0とし、40
℃で18時間自己消化を行なわせた。自己消化終了
時のPHは5.6でエキス抽出率は46%であつた。
Example 8 Beer pre-fermentation yeast (solid content 16 (weight)%) 234
Add the same amount of water at 5-7℃ to g, and pH it with 1N-NaOH.
12.3 and held for 20 seconds. The methylene blue staining rate was approximately 50%. Immediately centrifuge, discard the supernatant, add 1% hydrochloric acid to the precipitate to adjust the pH to 8.0, and add 1% hydrochloric acid to the precipitate.
Autolysis was performed for 18 hours at ℃. At the end of autolysis, the pH was 5.6 and the extract extraction rate was 46%.

Claims (1)

【特許請求の範囲】 1 生菌体をPH10.5以上でアルカリ処理して、菌
体がメチレンブルーで明らかに染色されるに至ら
しめたのち、PH5〜9で自己消化させることを特
徴とする菌体の自己消化法。 2 特許請求の範囲第1項記載の菌体の自己消化
法において、菌体の50%以上が染色される状態と
なつたのち自己消化を行なわせることを特徴とす
る方法。 3 特許請求の範囲第1項又は第2項記載の菌体
の自己消化法において、生菌体をPH11.5〜12.5で
アルカリ処理することを特徴とする方法。 4 特許請求の範囲第1項ないし第3項のいずれ
かに記載の菌体の自己消化法において、生菌体の
アルカリ処理を5〜30℃で行なうことを特徴とす
る方法。 5 特許請求の範囲第1項ないし第4項のいずれ
かに記載の菌体の自己消化法において、自己消化
を30〜50℃で行なうことを特徴とする方法。 6 特許請求の範囲第1項ないし第5項のいずれ
かに記載の菌体の自己消化法において、アルカリ
処理後に菌体からアルカリ水溶液の大部分を分離
し、次いで酸を加えてPH5〜9として自己消化を
行なわせることを特徴とする方法。 7 特許請求の範囲第1項ないし第6項のいずれ
かに記載の菌体の自己消化法において、アルカリ
処理を水酸化カルシウムを含むアルカリ水溶液中
で行ない、次いで燐酸を含む酸を用いてPHを5〜
9にすることを特徴とする方法。
[Scope of Claims] 1. A bacterium characterized by treating live bacterial cells with an alkali at a pH of 10.5 or higher so that the bacterial cells are clearly stained with methylene blue, and then autolyzing the cells at a pH of 5 to 9. The body's self-digestion method. 2. The method for autolysis of bacterial cells according to claim 1, characterized in that the autolysis is carried out after 50% or more of the bacterial cells are stained. 3. The method for self-digestion of bacterial cells according to claim 1 or 2, characterized in that viable bacterial cells are treated with alkali at a pH of 11.5 to 12.5. 4. The method for self-digestion of bacterial cells according to any one of claims 1 to 3, characterized in that the viable bacterial cells are treated with alkali at 5 to 30°C. 5. The method for autolysis of bacterial cells according to any one of claims 1 to 4, characterized in that the autolysis is carried out at 30 to 50°C. 6. In the autolysis method for bacterial cells according to any one of claims 1 to 5, most of the alkaline aqueous solution is separated from the bacterial cells after alkali treatment, and then acid is added to adjust the pH to 5 to 9. A method characterized by causing autolysis. 7 In the method for self-digestion of bacterial cells according to any one of claims 1 to 6, the alkali treatment is performed in an alkaline aqueous solution containing calcium hydroxide, and then the pH is adjusted using an acid containing phosphoric acid. 5~
A method characterized by making the number 9.
JP6089579A 1979-05-17 1979-05-17 Autolysis of mycelium Granted JPS55153591A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6089579A JPS55153591A (en) 1979-05-17 1979-05-17 Autolysis of mycelium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6089579A JPS55153591A (en) 1979-05-17 1979-05-17 Autolysis of mycelium

Publications (2)

Publication Number Publication Date
JPS55153591A JPS55153591A (en) 1980-11-29
JPS6148913B2 true JPS6148913B2 (en) 1986-10-27

Family

ID=13155539

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6089579A Granted JPS55153591A (en) 1979-05-17 1979-05-17 Autolysis of mycelium

Country Status (1)

Country Link
JP (1) JPS55153591A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0377573A1 (en) * 1987-07-22 1990-07-18 Imperial Cancer Research Technology Limited Digestion method

Also Published As

Publication number Publication date
JPS55153591A (en) 1980-11-29

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