JPH0251587B2 - - Google Patents
Info
- Publication number
- JPH0251587B2 JPH0251587B2 JP57097775A JP9777582A JPH0251587B2 JP H0251587 B2 JPH0251587 B2 JP H0251587B2 JP 57097775 A JP57097775 A JP 57097775A JP 9777582 A JP9777582 A JP 9777582A JP H0251587 B2 JPH0251587 B2 JP H0251587B2
- Authority
- JP
- Japan
- Prior art keywords
- yeast
- ethyl alcohol
- yeast extract
- extract
- producing
- 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 - Lifetime
Links
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 39
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 35
- 239000012138 yeast extract Substances 0.000 claims description 21
- 229940041514 candida albicans extract Drugs 0.000 claims description 20
- 235000019441 ethanol Nutrition 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 7
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 33
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 12
- 208000035404 Autolysis Diseases 0.000 description 8
- 206010057248 Cell death Diseases 0.000 description 8
- 239000002994 raw material Substances 0.000 description 8
- 230000028043 self proteolysis Effects 0.000 description 8
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 239000000243 solution Substances 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 235000019658 bitter taste Nutrition 0.000 description 3
- 238000004040 coloring Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229920001817 Agar Polymers 0.000 description 1
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 1
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 1
- 238000007696 Kjeldahl method Methods 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 238000005903 acid hydrolysis reaction Methods 0.000 description 1
- 239000008272 agar Substances 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000003385 bacteriostatic effect Effects 0.000 description 1
- 235000013405 beer Nutrition 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000006103 coloring component Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- YPHMISFOHDHNIV-FSZOTQKASA-N cycloheximide Chemical compound C1[C@@H](C)C[C@H](C)C(=O)[C@@H]1[C@H](O)CC1CC(=O)NC(=O)C1 YPHMISFOHDHNIV-FSZOTQKASA-N 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229960004279 formaldehyde Drugs 0.000 description 1
- 235000019256 formaldehyde Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000003834 intracellular effect Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 210000005253 yeast cell Anatomy 0.000 description 1
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
Description
本発明は酵母エキスの製造法に関する。
酵母エキスに関しては、いわゆる酵母臭のほか
濃厚な着色、製造工程中の雑菌汚染などが従来か
ら問題となつている。この問題を解決するための
方法が数多く提案され、かつ実施されており、或
程度の効果も奏されているが、現在なお酵母エキ
スの利用拡大を阻んでいるのは依然として上記の
問題であると云える。また、自己消化法により酵
母エキスを製造する場合、酢酸エチル、トルエン
などの溶剤が添加されるが、該溶剤の使用は酵母
エキスの用途、品質面からみて好ましいものでは
なく、かつ防炎上からも望ましくない。さらに、
酵母エキス製造原料としてビール酵母を使用する
場合は、ホツプ苦味質を除去するための工程が必
要とされる。
上記のような事情に鑑み、本発明者らは酵母エ
キスの製造法を改良すべく検討を重ねた。その結
果、原料酵母をエチルアルコール水溶液にて予備
処理することによつて上記の問題点が一挙に解消
されることを見出し、この知見に基いて本発明を
完成したのである。
本発明は、酵母エキスを製造するにあたり、原
料酵母を濃度10〜40%のエチルアルコール水溶液
で予備処理するとを特徴とする酵母エキスの製造
法である。
酵母エキスの製造法には酸加水分解法、酵素
法、自己消化法など種々の方法があるが、本発明
は既知のどのような製造法にも適用できる。同様
に、使用する原料酵母も制限されず、任意のもの
を用いることができる。
自己消化法による酵母エキスの製造法は広く行
なわれており、かつ菌体内酵素の作用に依存する
ものであるため、原料酵母の処理方法が制約され
る方法である。そこで、自己消化法による酵母エ
キスの製造法を例として以下に本発明を説明す
る。
本発明では原料酵母を濃度10〜40%のエチルア
ルコール水溶液を用いて予備処理する。なお、エ
チルアルコールは外部から添加すること以外に原
料酵母の発酵によつて生成するエチルアルコール
をエチルアルコールの一部または全部として用い
ることができる。
前記した如く、アルコール水溶液は原料酵母と
混和したときプレス状の酵母(水分75%)に対し
て10〜40%の濃度にて接触させて作用させるが、
これは酵母が多くの場合、スラリー状で取扱われ
るのでエチルアルコール添加後の全体としての濃
度を意味する。また、エチルアルコールの使用目
的別に経済的な有効濃度を示すと、酵母臭除去に
は20%以上、着色の淡色化には40%程度、雑菌防
除のためには10%以上、溶剤代替のためには10%
以上、苦味質除去のためには40%程度である。
予備処理の温度については特に制限はないが、
一般的には自己消化が起る40℃以上とすべきでな
く、通常の製造環境の温度、すなわち40℃以下、
通常は0〜30℃程度で充分な効果が得られる。処
理時間についてはアルコール水溶液と酵母を混
和、撹拌後直ちに分離する程度の短時間から8時
間までであり、通常は1時間以内、好ましくは5
分間乃至1時間である。このようにして原料酵母
をエチルアルコールと接触させて予備処理した
後、エチルアルコール水溶液と酵母とを分離し、
酵母は酵母エキスの製造に供する。なお、酵母中
の有臭成分、着色成分などの有害成分は、この処
理によつてエチルアルコール側に移行する。
本発明によれば、原料酵母から酵母臭が除去さ
れ、着色も淡色化されるため、得られる酵母エキ
スには従来のような不快な臭いや着色がない。し
かも、原料酵母の汚染菌が除去され、かつ酢酸エ
チル、トルエンなどの溶剤の使用が不要となり、
またホツプ苦味質なども低減ないし除去される。
なお、本発明の方法を適用することによつて酵母
の死細胞が増加したり、静菌化したり、あるいは
脱水現象が起こることがあるけれども、これらは
酵母の自己消化の進行や酵母エキス収量には影響
しない。また、使用したエチルアルコール水溶液
は回収して再利用することができる。
次に、本発明を実施例によつて説明する。
実施例 1
ビール工場より副生する泥状酵母(プレス状酵
母40%含有)に99.5%濃度のエチルアルコールの
所定量を加えて下表の如きエチルアロコール濃度
となるように調整し、5分間撹拌した後、遠心分
離により酵母を回収した。この酵母を計量し、一
部は水分測定と汚染雑菌数の測定に供し、残余の
酵母は10倍量の水に懸濁し、常法の自己消化法に
よつて酵母エキスを製造した。但し、無処理酵母
には酢酸エチル(対液)0.5%添加し、エチルア
ルコール水溶液処理酵母には酢酸エチルは無添加
である。なお、エチルアルコール濃度は比重法、
エキス分は屈折計法、雑菌数はアクチジオン添加
標準寒天培地、エキス着色度は自己消化液を
0.45μのメンブラン濾過後420mmにおける吸光度で
それぞれ測定した。酵素作用の程度を知るため全
窒素とアミノ態窒素をそれぞれキエルダール法お
よびフオルモール法で測定した。また、酵母エキ
スの酵母臭評価と苦味評価は酵母エキス製造技術
者5名の一致した見解によつた。比較のためにエ
チルアルコール水溶液による予備処理をしない無
処理の酵母を用いて酵母エキスを製造した。結果
を第1表に示す。
The present invention relates to a method for producing yeast extract. Yeast extracts have long had problems such as yeast odor, strong coloring, and bacterial contamination during the manufacturing process. Although many methods to solve this problem have been proposed and implemented, and some results have been achieved, the above problem still hinders the expansion of the use of yeast extract. I can say that. Furthermore, when producing yeast extract by the autolysis method, solvents such as ethyl acetate and toluene are added, but the use of such solvents is not preferable from the viewpoint of the purpose and quality of the yeast extract, and from the viewpoint of flame resistance. Undesirable. moreover,
When brewer's yeast is used as a raw material for producing yeast extract, a step is required to remove hop bitter substances. In view of the above circumstances, the present inventors conducted repeated studies to improve the method for producing yeast extract. As a result, they discovered that the above-mentioned problems could be solved at once by pre-treating the raw material yeast with an aqueous ethyl alcohol solution, and based on this knowledge, they completed the present invention. The present invention is a method for producing a yeast extract, which is characterized in that, in producing the yeast extract, raw yeast is pretreated with an aqueous ethyl alcohol solution having a concentration of 10 to 40%. There are various methods for producing yeast extract, such as acid hydrolysis, enzymatic methods, and autolysis, and the present invention can be applied to any known production method. Similarly, the raw material yeast to be used is not limited, and any yeast can be used. The method for producing yeast extract by autolysis is widely practiced, and because it relies on the action of intracellular enzymes, it is a method that is limited in the processing of raw yeast. Therefore, the present invention will be explained below by taking as an example a method for producing yeast extract using an autolysis method. In the present invention, raw material yeast is pretreated using an aqueous ethyl alcohol solution with a concentration of 10 to 40%. In addition to adding ethyl alcohol from the outside, ethyl alcohol produced by fermentation of raw material yeast can be used as part or all of the ethyl alcohol. As mentioned above, when the alcohol aqueous solution is mixed with the raw material yeast, it is brought into contact with the pressed yeast (moisture 75%) at a concentration of 10 to 40% to act on it.
This refers to the overall concentration after addition of ethyl alcohol, since yeast is often handled in slurry form. In addition, the economically effective concentration of ethyl alcohol for each purpose is 20% or more for removing yeast odor, about 40% for lightening coloring, 10% or more for controlling germs, and 10% or more for solvent replacement. 10% for
The amount above is about 40% for removing bitter substances. There are no particular restrictions on the temperature of pretreatment, but
In general, the temperature should not be above 40℃, where autolysis occurs, but should be at the temperature of the normal manufacturing environment, that is, below 40℃.
Usually, a sufficient effect can be obtained at a temperature of about 0 to 30°C. The treatment time ranges from a short period of time, such as mixing and stirring the alcoholic aqueous solution with yeast and immediately separating it, to 8 hours, usually within 1 hour, preferably 5 hours.
The duration ranges from a minute to an hour. After pre-treating the raw material yeast by contacting it with ethyl alcohol in this way, the ethyl alcohol aqueous solution and the yeast are separated,
Yeast is used for producing yeast extract. Note that harmful components such as odorous components and coloring components in the yeast are transferred to the ethyl alcohol side by this treatment. According to the present invention, the yeast odor is removed from the raw material yeast and the coloring is also lightened, so the obtained yeast extract does not have the unpleasant odor or coloration that is conventional. Moreover, contaminating bacteria from raw yeast are removed, and there is no need to use solvents such as ethyl acetate or toluene.
Hop bitterness is also reduced or eliminated.
By applying the method of the present invention, the number of dead yeast cells may increase, the yeast may become bacteriostatic, or dehydration may occur, but these may affect the progress of yeast autolysis and the yield of yeast extract. has no effect. Further, the used ethyl alcohol aqueous solution can be recovered and reused. Next, the present invention will be explained with reference to examples. Example 1 A predetermined amount of 99.5% ethyl alcohol was added to muddy yeast produced as a by-product from a beer factory (containing 40% pressed yeast) to adjust the ethyl alcohol concentration as shown in the table below, and the mixture was heated for 5 minutes. After stirring, yeast was collected by centrifugation. This yeast was weighed, and a portion was used for water content measurement and measurement of the number of contaminant bacteria, and the remaining yeast was suspended in 10 times the amount of water, and a yeast extract was produced by a conventional autolysis method. However, 0.5% ethyl acetate (to liquid) was added to untreated yeast, and no ethyl acetate was added to yeast treated with ethyl alcohol aqueous solution. In addition, the ethyl alcohol concentration is determined by the specific gravity method.
The extract content was determined using a refractometer method, the number of bacteria was determined using standard agar medium supplemented with actidione, and the degree of coloration of the extract was determined using autolysis liquid.
The absorbance at 420 mm was measured after filtration with a 0.45μ membrane. To determine the extent of enzyme action, total nitrogen and amino nitrogen were measured using the Kjeldahl method and the formol method, respectively. Furthermore, the yeast odor and bitterness evaluations of the yeast extract were based on the consensus opinion of five yeast extract manufacturing engineers. For comparison, a yeast extract was produced using untreated yeast that was not pretreated with an aqueous ethyl alcohol solution. The results are shown in Table 1.
【表】【table】
【表】
酵母臭 有り 弱い
なし なし なし
苦味 有り 少い
微弱 殆んどなし なし
*1 予備処理前後の重量比
[Table] Yeast odor present weak
None None None
Bitterness present little
Weak Almost none None
*1 Weight ratio before and after pretreatment
Claims (1)
10〜40%のエチルアルコール水溶液で予備処理す
ることを特徴とする酵母エキスの製造法。 2 予備処理が40℃以下の温度で1時間以内の時
間接触した後、エチルアルコール水溶液と酵母を
分離するものである特許請求の範囲第1項記載の
方法。[Claims] 1. In producing yeast extract, yeast is
A method for producing yeast extract, characterized by pretreatment with a 10-40% ethyl alcohol aqueous solution. 2. The method according to claim 1, wherein the pretreatment is to separate the ethyl alcohol aqueous solution and the yeast after contacting them at a temperature of 40° C. or less for a period of up to 1 hour.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57097775A JPS58216669A (en) | 1982-06-09 | 1982-06-09 | Preparation of yeast extract |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57097775A JPS58216669A (en) | 1982-06-09 | 1982-06-09 | Preparation of yeast extract |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58216669A JPS58216669A (en) | 1983-12-16 |
JPH0251587B2 true JPH0251587B2 (en) | 1990-11-07 |
Family
ID=14201208
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57097775A Granted JPS58216669A (en) | 1982-06-09 | 1982-06-09 | Preparation of yeast extract |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58216669A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6131083A (en) * | 1984-07-25 | 1986-02-13 | Asahi Breweries Ltd | Preparation of bitterless dried yeast |
AU725676B2 (en) * | 1997-04-16 | 2000-10-19 | Sapporo Breweries Limited | Method for producing yeast extract |
CN1926243A (en) * | 2004-03-04 | 2007-03-07 | 三得利株式会社 | A process for producing astaxanthin-containing lipids |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52128268A (en) * | 1976-04-19 | 1977-10-27 | Idemitsu Kosan Co | Production of yeast extract |
JPS5568272A (en) * | 1978-11-16 | 1980-05-22 | Idemitsu Kosan Co Ltd | Preparation of improved yeast product |
-
1982
- 1982-06-09 JP JP57097775A patent/JPS58216669A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52128268A (en) * | 1976-04-19 | 1977-10-27 | Idemitsu Kosan Co | Production of yeast extract |
JPS5568272A (en) * | 1978-11-16 | 1980-05-22 | Idemitsu Kosan Co Ltd | Preparation of improved yeast product |
Also Published As
Publication number | Publication date |
---|---|
JPS58216669A (en) | 1983-12-16 |
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