JPH0336499B2 - - Google Patents

Info

Publication number
JPH0336499B2
JPH0336499B2 JP58059776A JP5977683A JPH0336499B2 JP H0336499 B2 JPH0336499 B2 JP H0336499B2 JP 58059776 A JP58059776 A JP 58059776A JP 5977683 A JP5977683 A JP 5977683A JP H0336499 B2 JPH0336499 B2 JP H0336499B2
Authority
JP
Japan
Prior art keywords
autolysis
yeast
fatty acid
slurry
acid ester
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
Application number
JP58059776A
Other languages
Japanese (ja)
Other versions
JPS59183671A (en
Inventor
Shoichi Ishii
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.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co Inc
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 Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP58059776A priority Critical patent/JPS59183671A/en
Publication of JPS59183671A publication Critical patent/JPS59183671A/en
Publication of JPH0336499B2 publication Critical patent/JPH0336499B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は自己消化法による酵母エキスの製造方
法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing yeast extract by autolysis.

従来、酵母エキスの製造法としては自己消化法
が知られている。
Conventionally, an autolysis method has been known as a method for producing yeast extract.

自己消化は酵母菌体自身の酵素を利用して酵素
分解せしめる方法であり、生酵母菌体、特に培養
して得られる新鮮な菌体はそのままでは自己消化
しにくいので一般には酢酸エチル、トルオール等
の有機溶媒や食塩等いわゆる自己消化促進剤を添
加して自己消化を誘発せしめるものが添加され
る。このような自己消化法は得られた酵母エキス
の品質が一般に他のものに比べて優れている。
Autolysis is a method of enzymatic decomposition using yeast cells' own enzymes, and since live yeast cells, especially fresh cells obtained by culturing, are difficult to self-digest as they are, ethyl acetate, toluol, etc. are generally used. So-called autolysis promoters such as organic solvents and salt are added to induce autolysis. The quality of the yeast extract obtained from such autolysis methods is generally superior to other methods.

従来、酵母菌体を自己消化法でエキス化する際
には酵母菌体スラリーに酢酸エチル、トルオール
等の自己消化促進剤を少量(0.5〜5.0%)添加し
て行われ、自己消化促進剤を添加しないと自己消
化の誘発が遅くエキス化は不充分となる。例え
ば、パン酵母を45℃で21時間及び50時間自己消化
させた時の自己消化率はそれぞれ15%、48%と低
い。
Conventionally, when yeast cells are extracted using the autolysis method, a small amount (0.5-5.0%) of an autolysis promoter such as ethyl acetate or toluol is added to the yeast cell slurry. If it is not added, the induction of autolysis will be slow and the extraction will be insufficient. For example, when baker's yeast is autolysed at 45°C for 21 hours and 50 hours, the autolysis rates are low at 15% and 48%, respectively.

本発明者は、このような有機溶媒をもちいない
で、かつ自己消化を短時間で効率良く進める方法
を開発すべく鋭意研究を重ねた結果、酵母菌体濃
度5%から30%の酵母菌体スラリーにシヨ糖脂肪
酸エステル又はソルビタン脂肪酸エステルを0.5
%から3.0%になるように添加して自己消化せし
めると短時間で効率良く自己消化が進みかつ品質
の良い酵母エキスが得られる事を発見し、本発明
を完成するに至つた。
As a result of intensive research to develop a method for efficiently promoting autolysis in a short time without using such organic solvents, the present inventor has found that yeast cells with a yeast cell concentration of 5% to 30% have been developed. Add 0.5 sucrose fatty acid ester or sorbitan fatty acid ester to the slurry
The inventors discovered that when the yeast extract is added in an amount of 3.0% to 3.0% for self-digestion, the self-digestion progresses efficiently in a short period of time, and a yeast extract of good quality can be obtained, leading to the completion of the present invention.

本発明で使用する酵母はサツカロミセス属やカ
ンデイダ属などに属する可食性の酵母であれば良
く、例えばサツカロミセス・セレビシエー
AJ14502、CBC1523、FERM−P5705、CBS1172
等のパン酵母、サツカロミセス・セレビシエー
CBS1171、CBS1230等のビール酵母あるいはサ
ツカロミセス・ルキシーCBS4632カンデイダウ
チルスATCC9226等の酵母を挙げる事が出来る。
酵母菌体としては、これら酵母を炭素源、窒素源
および無機塩類を含有する通常の栄養培地で培養
して得られる菌体が使用される。又、市販のパン
酵母(ケーキ)等も良好に使用される。エキス化
する際には酵母菌体濃度5〜30%の菌体スラリー
を調製する。酵母菌体濃度が5%以下の水分含量
の多い菌体スラリーの場合は自己消化の目的の為
の脂肪酸エステルの添加量が増大し、かつ希釈な
自己消化液しか得れない。また、酵母菌体濃度が
30%以上の菌体濃度の高い菌体スラリーの場合に
は、自己消化の目的の為に添加する脂肪酸エステ
ルが均一に酵母菌体に作用しにくく、品質の一定
の良好な酵母エキスは製造されにくい。本発明に
おいては酵母菌体濃度5〜30%にされた菌体スラ
リーに自己消化の目的のために、この菌体スラリ
ー当り0.5%から3.0%、望ましくは0.8%から2.0
%のシヨ糖脂肪酸エステル又はソルビタン脂肪酸
エステルのみを添加して自己消化を誘発せしめ
る。本発明においてはシヨ糖脂肪酸エステルはモ
ノエステルが好ましく、その脂肪酸は飽和あるい
は不飽和の鎖長C6〜C22が用いられ、特に、鎖長
C8〜C18の脂肪酸エステルが酵母菌体の自己消化
を効果的に促進する。また、ソルビタン脂肪酸エ
ステルはモノエステルが好ましく、飽和あるいは
不飽和鎖長C6〜C14の脂肪酸が用いられ、特にC8
〜C12の鎖長の脂肪酸モノエステルが酵母菌体の
自己消化を効果的に促進する。自己消化促進のた
めに添加する脂肪酸エステルの量に関しては、菌
体スラリー当り0.5%以下の脂肪酸エステルを添
加した場合には酵母菌体の自己消化速度が低く自
己消化率を向上させるためには反応時間を長くす
る必要がある。また、3.0%以上の脂肪酸エステ
ルを添加しても0.5%から3.0%の添加量に比べて
自己消化速度はかわらない。本発明においては反
応温度、反応時間および反応PHは従来と同様の方
法で行えば良い。即ち、反応温度は、43℃ないし
55℃の範囲で、反応時間は20〜45時間で、PHは
5.5ないし6.5の範囲で行えば良好なエキスが生成
する。エキス化後は遠心分離等により不溶性残渣
を除去して酵母エキスを得ることができる。この
ように調製したエキスはそのままで使用できる
が、保存上、更に濃縮して水分30〜60%のペース
ト状とするか又は噴霧性乾燥等により粉末状とす
ることが望ましい。本発明の方法で得られる酵母
エキスの品質はまろやかな呈味を有する良好な酵
母エキスであり、種々の調味料や食品の原料とし
て使用されるものである。
The yeast used in the present invention may be any edible yeast belonging to the genus Satucharomyces or Candeida, such as Satucharomyces cerevisiae.
AJ14502, CBC1523, FERM−P5705, CBS1172
Baker's yeast such as Satscharomyces cerevisiae
Examples include brewer's yeast such as CBS1171 and CBS1230, and yeast such as Satucharomyces luxii CBS4632 and Candidauchillus ATCC9226.
As yeast cells, cells obtained by culturing these yeasts in a conventional nutrient medium containing a carbon source, a nitrogen source, and inorganic salts are used. In addition, commercially available baker's yeast (cake) etc. can also be used satisfactorily. When making an extract, prepare a yeast cell slurry with a yeast cell concentration of 5 to 30%. In the case of a yeast cell slurry with a high water content and a yeast cell concentration of 5% or less, the amount of fatty acid ester added for the purpose of autolysis increases, and only a dilute autolysis solution can be obtained. In addition, yeast cell concentration
In the case of a bacterial cell slurry with a high bacterial cell concentration of 30% or more, it is difficult for the fatty acid ester added for the purpose of autolysis to act uniformly on the yeast cells, making it difficult to produce a yeast extract of constant quality. Hateful. In the present invention, for the purpose of autolysis, yeast cell slurry with a yeast cell concentration of 5 to 30% is added to a yeast cell slurry of 0.5% to 3.0%, preferably 0.8% to 2.0%, per yeast cell slurry.
% of sucrose fatty acid ester or sorbitan fatty acid ester alone to induce autolysis. In the present invention, the sucrose fatty acid ester is preferably a monoester, and the fatty acid used is saturated or unsaturated and has a chain length of C6 to C22 .
C8 to C18 fatty acid esters effectively promote autolysis of yeast cells. Further, the sorbitan fatty acid ester is preferably a monoester, and fatty acids with a saturated or unsaturated chain length of C 6 to C 14 are used, particularly C 8
A fatty acid monoester with a chain length of ~ C12 effectively promotes the autolysis of yeast cells. Regarding the amount of fatty acid ester added to promote autolysis, if less than 0.5% fatty acid ester is added per bacterial cell slurry, the autolysis rate of yeast cells will be low and the reaction will be insufficient to improve the autolysis rate. It is necessary to increase the time. Furthermore, even if 3.0% or more of fatty acid ester is added, the autolysis rate remains unchanged compared to addition of 0.5% to 3.0%. In the present invention, the reaction temperature, reaction time and reaction pH may be carried out in the same manner as conventional methods. That is, the reaction temperature is between 43°C and
In the range of 55℃, reaction time is 20-45 hours, PH is
A good extract will be produced if it is carried out within the range of 5.5 to 6.5. After making the extract, insoluble residues can be removed by centrifugation or the like to obtain a yeast extract. The extract prepared in this manner can be used as is, but for storage purposes, it is desirable to further concentrate it to form a paste with a moisture content of 30 to 60%, or to form it into a powder form by spray drying or the like. The quality of the yeast extract obtained by the method of the present invention is that it has a mellow taste and is of good quality, and can be used as a raw material for various seasonings and foods.

以下、実施例にて詳細に説明する。 Hereinafter, this will be explained in detail in Examples.

実施例 1 第1表に示す組成の培地50を70容のジヤー
フアーメンターに張り込み120℃で15分間滅菌し
た。
Example 1 A 70-volume jar fermenter was filled with 50 liters of a medium having the composition shown in Table 1 and sterilized at 120° C. for 15 minutes.

第一表 培地組成 成 分 含 量 グルコース 5.0% (NH42SO4 1.0% KH2PO4 0.3% MgSO4・7H2O 0.1% CaCl2・2H2O 0.05% コーン・ステイーブ・リカー 10ml/dl PH 5.5 これに、同組成の培地を用いて30℃、18時間フ
ラスコ振盪培養して得られたサツカロミセス・セ
レビシエーAJ14502(FERM−P5705)の種培養
液200mlを接種し、通気量1/2V.V.M.撹拌数500r.
p.m.、内圧0.5Kg/cm2、温度30℃で20時間通気撹
拌培養を行い、乾燥菌体重量5.0g/dlのパン酵
母培養液を得た。この培養液を遠心分離してパン
酵母スラリー(菌体濃度17%)を得た。このパン
酵母スラリー1500gを2容のガラス容器に移し
てソルビタンラウリン酸モノエステル
(「SPAN20(F)」15g(1.0%対スラリー)を添加
後、恒温槽で45℃に保ちたまに撹拌して21時間自
己消化を行つた(自己消化率57%)。自己消化終
了後1.5の水を添加して遠心分離し得られる上
澄液を減圧下で濃縮し水分53%のペースト状酵母
エキス標品326gを得た(処理収率※60%)。
Table 1 Medium composition Component Content Glucose 5.0% (NH 4 ) 2 SO 4 1.0% KH 2 PO 4 0.3% MgSO 4・7H 2 O 0.1% CaCl 2・2H 2 O 0.05% Corn stave liquor 10ml/ dl PH 5.5 This was inoculated with 200 ml of a seed culture of Satucharomyces cerevisiae AJ14502 (FERM-P5705) obtained by flask shaking culture at 30°C for 18 hours using a medium of the same composition, and the aeration rate was 1/2 V. VM stirring number 500r.
pm, an internal pressure of 0.5 Kg/cm 2 , and a temperature of 30° C. for 20 hours with aeration and stirring to obtain a baker's yeast culture solution with a dry bacterial weight of 5.0 g/dl. This culture solution was centrifuged to obtain baker's yeast slurry (17% bacterial cell concentration). Transfer 1,500 g of this baker's yeast slurry to a 2-volume glass container, add 15 g of sorbitan lauric acid monoester (SPAN20(F) (1.0% vs. slurry), and then keep it at 45°C in a constant temperature bath with occasional stirring for 21 hours. Autolysis was performed (autolysis rate 57%).After autolysis, 1.5 ml of water was added, centrifuged, and the resulting supernatant was concentrated under reduced pressure to obtain 326 g of a pasty yeast extract sample with a water content of 53%. (processing yield *60%).

同様に上記パン酵母スラリー500gづつもちい
てソルビタンラウリン酸エステル(「Span20(F)」)
の添加量を変えて、45%℃、21時間保持して自己
消化を行い自己消化率※※を求めた。
Similarly, use 500g of the above baker's yeast slurry to prepare sorbitan laurate ("Span20(F)").
Autolysis was performed by changing the amount of added and holding at 45% °C for 21 hours to determine the autolysis rate ※※.

その結果を第二表に示す。 The results are shown in Table 2.

第二表 ソルビタンラウリル酸エステル(SPAN20(F))
の添加効果 添加量(%対スラリー) 自己消化率(%) 0 15 0.15 24 0.5 37 0.8 57 1.0 57 1.5 57 3.0 57 ※処理収率(%)=100×標品中の(乾燥)固
形分/使用(乾燥)菌体量 ※※自己消化率(%)=100×[1−自己消化
後の(乾燥)菌体濃度(%)/自己消化前の(乾燥)菌
体濃度(%)] 実施例 2 実施例1の方法で得られたパン酵母スラリー
1500gにシヨ糖ステアリン酸エステル(「DKエ
ステルSS」)15g(1.0%対スラリー)を添加し45
℃で21時間自己消化を行い(自己消化率50%)、
得られた反応液を実施例1と同様の方法で処理し
て水分53%のペースト状酵母エキス標品288gを
得た(処理収率53%)。
Table 2 Sorbitan lauryl ester (SPAN20(F))
Addition effect Added amount (% vs. slurry) Autolysis rate (%) 0 15 0.15 24 0.5 37 0.8 57 1.0 57 1.5 57 3.0 57 *Processing yield (%) = 100 x (dry) solid content in sample / Amount of (dry) bacterial cells used ※※Autolysis rate (%) = 100 × [1 - (dry) bacterial cell concentration after autolysis (%) / (dry) bacterial cell concentration before autolysis (%)] Implementation Example 2 Baker's yeast slurry obtained by the method of Example 1
Add 15 g of sucrose stearate (“DK Ester SS”) to 1500 g (1.0% slurry) and make 45
Autolysis was performed at ℃ for 21 hours (autolysis rate 50%).
The obtained reaction solution was treated in the same manner as in Example 1 to obtain 288 g of a pasty yeast extract sample with a moisture content of 53% (processing yield 53%).

Claims (1)

【特許請求の範囲】[Claims] 1 菌体濃度5%から30%の可食性酵母菌体スラ
リーにシヨ糖脂肪酸エステル又はソルビタン脂肪
酸エステルを菌体スラリー当り0.5%から3.0%に
なるように添加して自己消化せしめる事を特徴と
する酵母エキスの製造法。
1. It is characterized by adding sucrose fatty acid ester or sorbitan fatty acid ester to an edible yeast cell slurry with a cell concentration of 5% to 30% at a concentration of 0.5% to 3.0% per cell slurry for autolysis. Method for producing yeast extract.
JP58059776A 1983-04-05 1983-04-05 Production of yeast extract Granted JPS59183671A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58059776A JPS59183671A (en) 1983-04-05 1983-04-05 Production of yeast extract

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58059776A JPS59183671A (en) 1983-04-05 1983-04-05 Production of yeast extract

Publications (2)

Publication Number Publication Date
JPS59183671A JPS59183671A (en) 1984-10-18
JPH0336499B2 true JPH0336499B2 (en) 1991-05-31

Family

ID=13123026

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58059776A Granted JPS59183671A (en) 1983-04-05 1983-04-05 Production of yeast extract

Country Status (1)

Country Link
JP (1) JPS59183671A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016080490A1 (en) * 2014-11-19 2016-05-26 テーブルマーク株式会社 Flavor improvement method for yeast cells and food quality improving agent

Also Published As

Publication number Publication date
JPS59183671A (en) 1984-10-18

Similar Documents

Publication Publication Date Title
EP0417481B1 (en) Process for preparing a soy sauce
EP0249435B1 (en) Method for producing yeast extract
CA2438233A1 (en) Glucosamine and method of making glucosamine from microbial biomass
RU2000130156A (en) PRODUCTION OF CONDITION FROM HYDROLYSIS
JP3519572B2 (en) Yeast extract composition and yeast mutant for obtaining the same
FR2545838A1 (en) PROCESS FOR THE PRODUCTION OF ETHANOL FROM A SUBSTANCE CONTAINING XYLOSE
GB1372870A (en) Process for treating single-cell protein food material
JPH0739386A (en) Production of bacterial cellulose
JPH0336499B2 (en)
JPH03117494A (en) Gamma-lactone, method of its preparation and spice and food containing said gamma-lactone
RU2003111457A (en) ANIMAL FEED ADDITIVE CONTAINING D-PANTOTENIC ACID AND / OR ITS SALTS, IMPROVED METHOD FOR PRODUCING AND APPLICATION
US4418081A (en) Natural red coloring prepared from an oat substrate
JPS59109152A (en) Preparation of yeast extract
JPS6219822B2 (en)
EP0466922B1 (en) Production of yeast extract
JPH01132315A (en) Mushroom cultivation
CZ6797A3 (en) Extract of low-molecular active substances from yeast and process for preparing thereof
US4407826A (en) Method of producing Koji products
WO2007066458A1 (en) Yeast for extraction of lipid-soluble component, method for producing the same, color-improving agent using the same and method for producing lipid-soluble component
JPH02142486A (en) Production of unsaturated fatty acid-containing lipid
JPS5929212B2 (en) Method for producing yeast extract
JP2547197B2 (en) Manufacturing method of edible blood products
JPH10165191A (en) Production of gamma-aminobutyric acid by aspergillus oryzae
JP3798336B2 (en) Enzyme production method using rush
JPH01199586A (en) Production of composition containing citric acid