JPH01179664A - Production of yeast extract - Google Patents
Production of yeast extractInfo
- Publication number
- JPH01179664A JPH01179664A JP63000032A JP3288A JPH01179664A JP H01179664 A JPH01179664 A JP H01179664A JP 63000032 A JP63000032 A JP 63000032A JP 3288 A JP3288 A JP 3288A JP H01179664 A JPH01179664 A JP H01179664A
- Authority
- JP
- Japan
- Prior art keywords
- yeast
- enzyme
- extract
- dry
- raw
- 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.)
- Pending
Links
- 229940041514 candida albicans extract Drugs 0.000 title claims abstract description 21
- 239000012138 yeast extract Substances 0.000 title claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims abstract description 87
- 108090000790 Enzymes Proteins 0.000 claims abstract description 26
- 102000004190 Enzymes Human genes 0.000 claims abstract description 26
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 abstract description 84
- 238000006243 chemical reaction Methods 0.000 abstract description 10
- 239000002994 raw material Substances 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 8
- 210000002421 cell wall Anatomy 0.000 abstract description 7
- 239000000284 extract Substances 0.000 abstract description 7
- 239000000796 flavoring agent Substances 0.000 abstract description 7
- 235000019634 flavors Nutrition 0.000 abstract description 7
- 235000013405 beer Nutrition 0.000 abstract description 6
- 239000006227 byproduct Substances 0.000 abstract description 6
- 239000006228 supernatant Substances 0.000 abstract description 4
- 241000006364 Torula Species 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 abstract description 2
- 239000000725 suspension Substances 0.000 abstract 2
- 239000007795 chemical reaction product Substances 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 229940088598 enzyme Drugs 0.000 description 21
- 238000011084 recovery Methods 0.000 description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 16
- 238000000034 method Methods 0.000 description 15
- 208000035404 Autolysis Diseases 0.000 description 14
- 206010057248 Cell death Diseases 0.000 description 14
- 230000028043 self proteolysis Effects 0.000 description 14
- 229910052757 nitrogen Inorganic materials 0.000 description 8
- 239000007787 solid Substances 0.000 description 8
- 238000000354 decomposition reaction Methods 0.000 description 6
- 108091005804 Peptidases Proteins 0.000 description 4
- 102000035195 Peptidases Human genes 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 210000005253 yeast cell Anatomy 0.000 description 4
- 101000925662 Enterobacteria phage PRD1 Endolysin Proteins 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 3
- 210000004027 cell Anatomy 0.000 description 3
- 238000002144 chemical decomposition reaction Methods 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 230000002101 lytic effect Effects 0.000 description 3
- 102000004196 processed proteins & peptides Human genes 0.000 description 3
- 108090000765 processed proteins & peptides Proteins 0.000 description 3
- 150000001413 amino acids Chemical class 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 230000002255 enzymatic effect Effects 0.000 description 2
- 102000039446 nucleic acids Human genes 0.000 description 2
- 108020004707 nucleic acids Proteins 0.000 description 2
- 150000007523 nucleic acids Chemical class 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 229940024999 proteolytic enzymes for treatment of wounds and ulcers Drugs 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004278 EU approved seasoning Substances 0.000 description 1
- 230000002358 autolytic effect Effects 0.000 description 1
- 235000008429 bread Nutrition 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007515 enzymatic degradation Effects 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000003834 intracellular effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- 230000002797 proteolythic effect Effects 0.000 description 1
- 229940081969 saccharomyces cerevisiae Drugs 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
イ3発明の目的
−の1 ′
本発明は乾燥酵母及び生酵母を原料として、生酵母のみ
を原料とする自己消化法に匹敵する呈味性、香味を有す
る酵母エキスを製造する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION A.3 Objectives of the Invention-1' The present invention provides a yeast extract using dry yeast and fresh yeast as raw materials, which has taste and flavor comparable to an autolysis method using only fresh yeast as raw materials. The present invention relates to a method for manufacturing.
え久立且遣
従来、酵母エキスの製造法としては、生酵母を原料とす
る自己消化法や、乾燥酵母を原料とする酵素分解法、或
は酸又はアルカリによる化学分解法が知られている。Previously known methods for producing yeast extract include an autolysis method using fresh yeast as a raw material, an enzymatic decomposition method using dried yeast as a raw material, and a chemical decomposition method using acid or alkali. .
生酵母を原料とする自己消化法は菌体酵素により酵母菌
体中の蛋白質等を分解し呈味物質であるアミ八1ペプチ
ド、核酸等をバランスよく生成するので、呈味性、香味
など品質の優れた調味料の製造法として多く採用されて
いる。The autolysis method using live yeast as a raw material uses bacterial enzymes to decompose proteins in the yeast cells and produce taste substances such as Ami81 peptides and nucleic acids in a well-balanced manner, resulting in improved quality such as taste and flavor. It is widely used as a method for producing excellent seasonings.
一方、乾燥酵母を原料とする場合は、酵素分解法では植
物又は微生物より得られる主として蛋白分解酵素を用い
、また化学分解法では酸又はアルカリを用いて、乾燥酵
母を分解して前記呈味物質であるアミノ酸ペプチド、核
酸を生成する。On the other hand, when dry yeast is used as a raw material, the enzymatic decomposition method mainly uses proteolytic enzymes obtained from plants or microorganisms, and the chemical decomposition method uses acid or alkali to decompose the dry yeast and produce the taste substances. Generates amino acid peptides and nucleic acids.
自己消化法では酵母菌体内の複合酵素系を用いて酵母菌
体蛋白質等を分解するのに対し、乾燥酵母の酵素分解法
では単一、或は数種の酵素系ての分解であり、また化学
分解法では酸又はアルカリによる単純な加水分解となる
ので、生成するアミノ酸、ペプチドの形態及び割合は若
干具なり、呈味性、香味も異なったものとなる。The autolysis method uses a complex enzyme system within the yeast cell to degrade yeast cell proteins, whereas the dry yeast enzymatic degradation method uses a single enzyme system or several types of enzyme systems. Since the chemical decomposition method involves simple hydrolysis with acid or alkali, the forms and proportions of the amino acids and peptides produced will vary slightly, and the taste and flavor will also differ.
自己消化法で用いられる酵母は培養直後の生酵母であり
、良好な品質の酵母エキスを得るには雑菌汚染上保管・
取扱いに充分な配慮を要する。The yeast used in the autolysis method is live yeast that has just been cultured, and in order to obtain a yeast extract of good quality, it must be stored and stored to prevent bacterial contamination.
Requires sufficient consideration when handling.
一方乾仔酵母は通常、加熱乾燥されているのて長期保存
等、保管・取扱いは容易である。On the other hand, dry yeast yeast is usually heated and dried, so it is easy to store and handle for long periods of time.
か しよ゛と る、1
生酵母を原料とする自己消化法で得られる酵母エキスに
匹敵する呈味性、香味等を有する酵母エキスを乾燥酵母
から得るため、乾燥酵母と生酵母を混合し、自己消化条
件に置き、生酵母の持つ菌体内酵素により分解しようと
しても、分解は生酵母のみにとどまり、乾燥酵母は殆ん
ど分解されない。1. In order to obtain a yeast extract from dry yeast that has taste characteristics, flavor, etc. comparable to yeast extract obtained by autolysis using live yeast as raw material, dry yeast and live yeast are mixed. Even if an attempt is made to decompose the yeast by the intracellular enzymes of the live yeast under autolytic conditions, only the live yeast will be decomposed, and the dried yeast will hardly be decomposed.
本発明は生酵母の自己消化法で得られている呈味性、香
味に優れた酵母エキスを、乾燥酵母から効率よく得るこ
とを目的とする。The purpose of the present invention is to efficiently obtain a yeast extract with excellent taste and flavor, which is obtained by an autolysis method of fresh yeast, from dried yeast.
木発明者らは、生酵母を酵素、特に細胞壁溶解酵素で処
理することにより菌体内の酵素は乾燥酵母に作用活性が
生じ分解されることを見出し、本発明を完成した。The inventors of the present invention completed the present invention by discovering that by treating live yeast with enzymes, particularly cell wall lytic enzymes, the enzymes within the bacterial cells become active on dry yeast and are decomposed.
口0発明の構成
、哩 占t た の ゛本発明の酵
母エキスの製造法は、乾燥酵母を、酵素処理した生酵母
により分解することを特徴とする。Structure of the Invention: The method for producing yeast extract of the present invention is characterized in that dry yeast is decomposed by enzyme-treated live yeast.
本発明て使用される乾燥酵母としては、ビール副生乾燥
酵母が代表的なものとして挙げられる。A typical example of the dry yeast used in the present invention is beer by-product dry yeast.
また生酵母としては、パン製造用のパン酵母やバルブ廃
液よりのトルラ酵母等の培養酵母、或はビール製造咋の
副生酵母の生菌体が挙げられる。Examples of live yeast include baker's yeast for bread production, cultured yeast such as torula yeast from valve waste liquid, and live cells of by-product yeast from beer production.
生酵母を処理する酵素としては、細胞壁溶解酵素として
知られているものが適当である。また細胞壁溶解酵素と
蛋白分解酵素を併用してもよい。Suitable enzymes for treating live yeast include those known as cell wall lytic enzymes. Further, a cell wall lytic enzyme and a proteolytic enzyme may be used in combination.
市1反されている細胞壁溶解酵素剤には、蛋白分解活性
を持つものが多い。Many of the cell wall-dissolving enzymes currently in use have proteolytic activity.
市INの細胞壁溶解酵素剤としては、ツニカーゼ(大和
化ffllnm ) 、 Y t、 −5(天!’IJ
薬v4製)、キタラーゼ(クミアイ化学工業■製)等が
あり、併用する市販の蛋白分解酵素剤としては、A−2
(天野製薬■製)、 プロチンFN(大和化成鞠製)、
ブナチーム(長瀬産業鈎製)等がある。本発明を実施す
る場合、予め酵素処理した生酵母に乾燥酵母を加え自己
消化条件で反応させても良いし、生酵母と乾燥酵母を同
時に混合し1g素剤を添加して自己消化条件で反応させ
ても良い。Cell wall lytic enzyme agents available in Ichi IN include Tunicase (Yamatoka ffllnm), Yt, -5 (Ten!'IJ
commercially available proteolytic enzymes used in conjunction with A-2.
(manufactured by Amano Pharmaceutical ■), Protin FN (manufactured by Daiwa Kasei Mari),
There are Buna Team (manufactured by Nagase Sangyo Kagi), etc. When carrying out the present invention, dry yeast may be added to live yeast that has been enzyme-treated in advance and reacted under autolysis conditions, or fresh yeast and dry yeast may be mixed at the same time, 1g of the ingredient is added, and the reaction is carried out under autolysis conditions. You can let me.
本発明の実施に際して適用される分解反応条件は、生酵
母を原料とする自己消化法に準するが、以下具体的に説
明する。The decomposition reaction conditions applied in carrying out the present invention are based on the autolysis method using live yeast as a raw material, and will be specifically explained below.
生酵母を適当な濃度、例えば15%程度に水で懸濁させ
、使用する酵素の最適pH城に酸或はアルカリで調整し
、細胞壁溶解酵素等を添加し、自己消化条件にて2〜5
時間反応させ、次いて乾燥酵母を添加し、さらに自己消
化条件で合計15〜24時間反応させる。Suspend fresh yeast in water to an appropriate concentration, for example, about 15%, adjust the pH to the optimum pH for the enzyme used with acid or alkali, add cell wall lytic enzyme, etc., and incubate for 2 to 5 hours under autolysis conditions.
Allow to react for an hour, then add dry yeast and further react under autolysis conditions for a total of 15 to 24 hours.
自己消化条件としてはpH3〜6、温度30〜55°C
1酵母濃度10〜30%程度とするのが適当である。生
酵母の乾燥酵母に対する割合は10%以上、望ましくは
30%以上である。Autolysis conditions include pH 3-6 and temperature 30-55°C.
It is appropriate to set the yeast concentration to about 10 to 30%. The ratio of fresh yeast to dry yeast is 10% or more, preferably 30% or more.
なお、この反応において生酵母の使用割合が少ない場合
や、或はさらに分解率を増大させるためには、市販の蛋
白分解酵素の添加により改善か回部である。In addition, when the proportion of live yeast used in this reaction is small, or in order to further increase the decomposition rate, it is possible to improve the reaction by adding a commercially available proteolytic enzyme.
反応液は80°Cに加温し酵素を失活させた後遠心分離
し、上澄液を濃縮し、エキスとして回収する。The reaction solution is heated to 80°C to inactivate the enzyme, then centrifuged, and the supernatant is concentrated and recovered as an extract.
災」11ユ
パン用酵母Saccharomyces Cerevi
siaeの一菌体を糖蜜培地で培養し、遠心分離、冷水
洗浄を数回繰返してずりられた生酵母を15%濃度に水
て懸濁し、酵素剤ツニカーゼF30を0.5%添加し、
35°Cで4時間自己消化させた後、15%濃度に水に
懸濁したビール副生乾燥酵母を添加しく生酵母:乾燥酵
母=50 : 50)、45℃て13時間−引続き反応
させた0反応終了後遠心分敲し、上澄液を減圧濃縮し、
酵母エキスを得た。Saccharomyces Cerevi
siae was cultured in molasses medium, centrifugation and washing with cold water were repeated several times, and the sheared live yeast was suspended in water to a concentration of 15%, and 0.5% of the enzyme agent Tunicase F30 was added.
After autolysis at 35°C for 4 hours, beer by-product dry yeast suspended in water to a concentration of 15% was added (fresh yeast: dry yeast = 50:50), and the reaction was continued at 45°C for 13 hours. After the completion of the 0 reaction, centrifuge and concentrate the supernatant under reduced pressure.
Yeast extract was obtained.
イリられた酵母エキスは生酵母の自己消化法のエキスに
近い呈味性、香気を持つ良好な品質であった。The fermented yeast extract was of good quality and had a taste and aroma similar to that of the autolyzed raw yeast extract.
酵母エキスの酵母当り(乾物)の固型分回収率は72.
1%、窒素回収率は66.4%とエキス回収効率が高か
った。The solid content recovery rate per yeast (dry matter) of yeast extract is 72.
The extract recovery efficiency was high, with a nitrogen recovery rate of 66.4%.
この窒素回収率(0印)及び固型分回収率(O印)を第
1図に示す、後述の比較例に比し高い値を示している。The nitrogen recovery rate (marked 0) and the solids recovery rate (marked O) are shown in FIG. 1 and show higher values than the comparative example described below.
第1図において横軸は乾燥酵母と生酵母の合計量に対す
る生酵母の割合(重量%)、縦軸は窒素回収率又は固型
分回収″8(%)を表ス。In FIG. 1, the horizontal axis represents the ratio of live yeast to the total amount of dry yeast and live yeast (% by weight), and the vertical axis represents the nitrogen recovery rate or solid content recovery''8 (%).
支五亘1
実施例1で使用した生酵母を15%濃度に水で懸濁し、
酵素剤ツニカーゼF30を0.5%添加し、35°Cで
4吟間自己消化した後、15%濃度に水で懸濁したビー
ル副生乾燥酵母を添加しく生酵母:乾燥酵母=50 :
50)、更に酵素剤A−2を1%添加し、50°Cで
13時間引続き反応させた0反応終了後遠心分離し、上
澄液を減圧濃縮し、/?I母エキスを得た。Shigohan 1 Suspend the live yeast used in Example 1 with water to a concentration of 15%,
After adding 0.5% of the enzyme agent Tunicase F30 and autolyzing it at 35°C for 4 minutes, add beer by-product dry yeast suspended in water to a concentration of 15%. Fresh yeast: Dry yeast = 50:
50), further added 1% of enzyme agent A-2, and continued to react at 50°C for 13 hours. After completion of the reaction, centrifugation was performed, and the supernatant was concentrated under reduced pressure. I mother extract was obtained.
得られた酵母エキスは生酵母の自己消化法のエキスに近
い呈味性、香気を持つ良好な品質であった。The obtained yeast extract was of good quality and had a taste and aroma close to that of an extract obtained by autolyzing raw yeast.
得られた酵母エキスの酵母当り(乾物)の固型分回収率
は82.7%、窒素回収率は84.6%てあった。The solid content recovery rate per yeast (dry matter) of the obtained yeast extract was 82.7%, and the nitrogen recovery rate was 84.6%.
この窒素回収率(2印)及び固型分回収率(■印)を第
1図に示す、後述の比較例に比し高い値を示している。The nitrogen recovery rate (2 mark) and the solid content recovery rate (■ mark) are shown in FIG. 1 and show higher values than the comparative example described below.
几」L例
実施例1て使用した生酵母な水て15%e度に懸濁し、
更にビール副生乾燥酵母を15%濃度に懸濁し、生酵母
と乾燥酵母の比率をO: 100、から100:Oの範
囲で変えて混合したものを。The fresh yeast used in Example 1 was suspended in 15% water and
Furthermore, beer by-product dry yeast was suspended to a concentration of 15%, and the ratio of fresh yeast to dry yeast was mixed in a range of 0:100 to 100:0.
45℃て17時間反応させた。それぞれの反応液を遠心
分離し、減圧濃縮し酵母エキスを得た。得られた酵母エ
キスの酵母当りの固型分回収率及び窒素回収率は第1表
に示す通りである。The reaction was carried out at 45°C for 17 hours. Each reaction solution was centrifuged and concentrated under reduced pressure to obtain a yeast extract. The solid content recovery rate and nitrogen recovery rate per yeast of the obtained yeast extract are as shown in Table 1.
この窒素回収率(冒印)及び固型分回収率(・印)を第
1図に示す。The nitrogen recovery rate (marked in red) and the solids recovery rate (marked) are shown in FIG.
第1表及び第1図よれば、生酵母の添加割合の増加に従
って固型分回収率及び窒素回収率は直線的に上昇するこ
とから、生酵母の分解によるのみてあり、乾燥酵母の分
解は殆んど生じていないことかわかる。According to Table 1 and Figure 1, the solid content recovery rate and nitrogen recovery rate increase linearly as the addition ratio of live yeast increases, so it is only due to the decomposition of live yeast, and the decomposition of dry yeast is I can see that very little has happened.
■
生酵母を酵素、特に細胞壁溶解酵素で処理することによ
り、生酵母菌体内の複合酵素系が乾燥酵母に作用するよ
うになり、良質の酵母エキスか高収率で得られる。■ By treating fresh yeast with enzymes, especially cell wall lytic enzymes, the complex enzyme system within the live yeast cells acts on dry yeast, resulting in a high yield of high-quality yeast extract.
ハ0発明の効果
本発明て得られた酵母エキスの呈味性、香味は従来の乾
燥酵母を原料とする酵素分解エキスに比べ大きく改善さ
れ、生酵母の自己消化分解エキスに匹敵するものとなっ
た。Effects of the Invention The taste and flavor of the yeast extract obtained by the present invention are greatly improved compared to conventional enzymatically decomposed extracts made from dry yeast, and are comparable to the autolyzed extracts of fresh yeast. Ta.
また生酵母と乾燥酵母の比率を適当に選ぶことにより、
製造上の適用範囲か拡がる。即ち生酵母の使用量が少な
くてよく、珈扱いの容易な乾燥酵母の適用が増大し、製
造コスト、管理面で有利となる。In addition, by appropriately selecting the ratio of fresh yeast and dry yeast,
Expands the scope of manufacturing applications. That is, the amount of fresh yeast used may be small, and the use of dry yeast, which is easy to handle, will increase, which will be advantageous in terms of production costs and management.
第1図は実施例1、実施例2及び比較例の結果を示した
図である。FIG. 1 is a diagram showing the results of Example 1, Example 2, and Comparative Example.
Claims (1)
特徴とする酵母エキスの製造法。A method for producing yeast extract, which comprises decomposing dry yeast with enzyme-treated live yeast.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63000032A JPH01179664A (en) | 1988-01-04 | 1988-01-04 | Production of yeast extract |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63000032A JPH01179664A (en) | 1988-01-04 | 1988-01-04 | Production of yeast extract |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01179664A true JPH01179664A (en) | 1989-07-17 |
Family
ID=11463008
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63000032A Pending JPH01179664A (en) | 1988-01-04 | 1988-01-04 | Production of yeast extract |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01179664A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5427921A (en) * | 1990-04-21 | 1995-06-27 | Cpc International Inc. | Method of preparing yeast extract containing hydrolyzed non-yeast protein with yeast autolytic enzymes |
KR19980061479A (en) * | 1996-12-31 | 1998-10-07 | 백운화 | Manufacturing method of yeast extract for microbial culture |
WO2019189795A1 (en) * | 2018-03-30 | 2019-10-03 | 合同会社レビアスファーマ | Method for producing yeast-derived microparticles |
-
1988
- 1988-01-04 JP JP63000032A patent/JPH01179664A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5427921A (en) * | 1990-04-21 | 1995-06-27 | Cpc International Inc. | Method of preparing yeast extract containing hydrolyzed non-yeast protein with yeast autolytic enzymes |
KR19980061479A (en) * | 1996-12-31 | 1998-10-07 | 백운화 | Manufacturing method of yeast extract for microbial culture |
WO2019189795A1 (en) * | 2018-03-30 | 2019-10-03 | 合同会社レビアスファーマ | Method for producing yeast-derived microparticles |
JPWO2019189795A1 (en) * | 2018-03-30 | 2021-04-01 | 合同会社レビアスファーマ | Method for producing fine particles derived from yeast |
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