JPS6358559B2 - - Google Patents
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- Publication number
- JPS6358559B2 JPS6358559B2 JP10779479A JP10779479A JPS6358559B2 JP S6358559 B2 JPS6358559 B2 JP S6358559B2 JP 10779479 A JP10779479 A JP 10779479A JP 10779479 A JP10779479 A JP 10779479A JP S6358559 B2 JPS6358559 B2 JP S6358559B2
- Authority
- JP
- Japan
- Prior art keywords
- yeast
- treatment
- culture
- sterilization
- tank
- 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
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- 238000011282 treatment Methods 0.000 claims description 54
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 36
- 238000000034 method Methods 0.000 claims description 28
- 230000001954 sterilising effect Effects 0.000 claims description 26
- 238000004659 sterilization and disinfection Methods 0.000 claims description 24
- 239000000126 substance Substances 0.000 claims description 13
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 9
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- 238000012136 culture method Methods 0.000 claims description 7
- 238000012258 culturing Methods 0.000 claims description 5
- 235000015097 nutrients Nutrition 0.000 claims description 5
- 238000005273 aeration Methods 0.000 claims description 4
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 31
- 241000894006 Bacteria Species 0.000 description 17
- 230000000694 effects Effects 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 9
- 239000003814 drug Substances 0.000 description 5
- 229940079593 drug Drugs 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- 239000005708 Sodium hypochlorite Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000005856 abnormality Effects 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 244000052616 bacterial pathogen Species 0.000 description 2
- RYYVLZVUVIJVGH-UHFFFAOYSA-N caffeine Chemical compound CN1C(=O)N(C)C(=O)C2=C1N=CN2C RYYVLZVUVIJVGH-UHFFFAOYSA-N 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 235000013379 molasses Nutrition 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 241000235646 Cyberlindnera jadinii Species 0.000 description 1
- LPHGQDQBBGAPDZ-UHFFFAOYSA-N Isocaffeine Natural products CN1C(=O)N(C)C(=O)C2=C1N(C)C=N2 LPHGQDQBBGAPDZ-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- 229940088710 antibiotic agent Drugs 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- JBIROUFYLSSYDX-UHFFFAOYSA-M benzododecinium chloride Chemical compound [Cl-].CCCCCCCCCCCC[N+](C)(C)CC1=CC=CC=C1 JBIROUFYLSSYDX-UHFFFAOYSA-M 0.000 description 1
- 229960001948 caffeine Drugs 0.000 description 1
- VJEONQKOZGKCAK-UHFFFAOYSA-N caffeine Natural products CN1C(=O)N(C)C(=O)C2=C1C=CN2C VJEONQKOZGKCAK-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- -1 chlorine Chemical class 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 238000009928 pasteurization Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000003716 rejuvenation Effects 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Description
本発明は酵母の培養法を、詳しくは培養槽から
培養液を抜き出し、該培養液を殺菌処理し、しか
るのち酵母の復活処理を行ない、酵母を培養槽に
戻しつつ培養を行う方法に関するものである。
発酵工業では雑菌の防止技術は有用物質の生産
菌の純粋発酵のために欠かすことのできない技術
であつて、わずかな雑菌汚染により生産菌の増殖
が不可能となり、そのために有用物質の生産が阻
害されてしまうことになる。そのために実際培養
を行なう際には、培養液、培養装置、通気空気等
のいずれにおいても厳重な殺菌あるいは除菌処理
が行なわれている。一方、培養液中の雑菌を排除
する方法(例えば雑菌の活性を失なわせるための
薬剤を介在させ、あるいはPHを酸性にする。その
他)が提案されている(例えば、特公昭53−
39511、特公昭47−38988、特公昭30−4440、特公
昭30−4439)。しかし、これらはいずれも雑菌の
活性が失なわせると同時に、酵母の活性の低下が
起り、培養操作の生産性が低下し、ひいては生産
コストの増嵩を伴う欠点があり、工業的採用には
雑菌防止と培養生産性のバランスが大きな問題と
なつてくる。
そこで、雑菌の適切な排除と同時に生産性の高
い酵母培養法の創出が当業界の課題であり、本発
明はこの課題を見事に解決したものである。即
ち、本発明者らは、雑菌汚染の影響を受けず、し
かも高い生産性を得る酵母の培養方法について鋭
意研究した結果、培養液を抜き出し、殺菌処理を
行ない更に酵母の復活処理を施した後、酵母を培
養槽に戻しつつ培養を行なえば、強い殺菌処理に
よる酵母の活性の低下を防止できることを見出
し、本発明を完成させた。以下に本発明を更に詳
細に説明する。
図1に本発明の概略工程図を示すが、これは本
発明の一例であつて全てを示すものではない。1
は培養槽、2は殺菌処理装置、3は復活処理槽で
ある。2の殺菌処理装置は1の培養槽より導入さ
れた培養液を殺菌処理する装置である。殺菌処理
法として薬剤処理、紫外線殺菌、放射線殺菌、低
温殺菌等の方法が使用できるが、一般的に経済的
に有利な薬剤処理を行なう方が好ましい。従つて
殺菌処理としては以下、主に薬剤処理について述
べる。
薬剤の添加量及び処理時間等の条件は、雑菌を
死滅ないし失活させるが、酵母を死滅させない条
件で処硫しなければならない。これは他の殺菌処
理法でも同じである。それらの条件は雑菌の種
類、酵母の種類、薬剤の種類等によつて相違する
から一義的には規定できないが、これらの条件は
前もつて薬剤による酵母と雑菌の活性度をテスト
しておくことによつて適切な条件を知ることがで
きる。又他の殺菌法についても、前もつてテスト
を行ない適切な条件を決定することができる。い
うまでもないが、これらの条件は酵母の活性低下
に考慮を払わず、雑菌だけに注目して決めること
ができる。
例えば薬剤処理として、酸性処理を行なう場合
には、一般的にはPHが1.5〜3で処理時間が20〜
120分となるように酸を添加し処理すればよく、
また、次亜塩素酸ソーダによつて殺菌を行なう場
合には有効塩素濃度として40ppm以下で処理時間
が10分以下の処理を施してやればよい。更にその
他の例として、例えばラウリルジメチルベンジル
アンモニウムクロリドのような界面活性剤の場合
には、500ppm以下で処理時間を20時間以下にす
れば効果的である。薬剤の種類を挙げると、酸
類、塩基類、過酸化水素、次亜塩素酸ソーダ、フ
オルマリン、カフエイン、アルデヒド類、界面活
性剤、更にオゾン、塩素等のガス類及び抗生物質
類等のあらゆる薬剤が使用でき、それらの処理条
件は前もつてテストを行なうことによつて適切な
条件が決定できる。薬剤を用いた場合、殺菌装置
としては一般的にタンクを用いればよく、撹拌機
の有無にかかわらず、あらゆる型式のものが使用
できる。他の殺菌法の場合の装置は、それぞれの
処理に見合つた公知の装置を用いればよい。以上
のように殺菌処理された培養液は3の復活槽に導
入されるが、ここでは殺菌処理によつて失活した
酵母を再び復活させる区域である。失活した酵母
をそのまま培養槽に戻して培養を行なうと、全体
としての酵母の増殖が低下し生産性が低下する。
従つて、この復活処理は本発明におて必須不可欠
の処理である。
復活処理を行なう方法条件は、2の殺菌処理に
よる失活度及び酵母の種類等によつて変化するの
で一義的には規定できないが、一般的にはPH4〜
8で処理時間10分以上、より好ましくはPH4〜6
で処理時間20〜120分の条件が酵母を復活させる
ために、主炭素源及びその他の栄養源の供給(ラ
イン6)や好気培養の場合には、通気(ライン
7)を行えばより効果的である。しかし、これら
の条件は前もつて復活度をテストすることによつ
て適切な条件を決定することができる。例えば酵
母の呼吸速度とか増殖速度等から復活させる条件
(PH、温度、処理時間等)を選定すればよい。一
例を挙げると、酵母を酸処理(PHが約2で処理時
間が約20分)を行つた場合、わずかの主炭素源や
その他の栄養源を添加し、又通気も行ないながら
復活条件としてPH4〜6で処理時間が約60分で復
活処理を行なえば、酵母はほぼ復活する。その他
の薬剤処理及び殺菌処理についても同様に求める
ことができる。復活処理を行なう装置としては、
一般的にタンクを用い、撹拌機の有無にかかわら
ずあらゆる型式のタンク類を使用することができ
る。このようにして復活した酵母は再び培養槽1
に導入され培養される。
以上のように本発明は、殺菌処理と復活処理の
2つの処理を行ないつつ培養するところに特徴が
あり、これらの処理を行なつて始めて雑菌汚染の
影響がなくなり、しかも高い性産性が得られるの
である。
本発明法は原理から明らかなように、酵母の種
類あるいは培養の種類(回分法、半回分法、連続
培養法等の種類)にかかわらず、いづれの場合で
も適用できる方法である。勿論、多段の培養槽と
組み合せることができ、その例として2段式のも
のを図2に示しておく。
次に実施例をもつて本発明を更に説明する。
実施例 1
図1に示したプロセスを用い、酵母としてSa
−ccharomyces cerevisiae(パン酵母)を用いて
連続培養を行なつた。培養槽は30容ジヤーフア
ーメンターを用い、温度33℃、PH4.5の条件で培
養した。殺菌処理としては薬剤処理を行ない、薬
剤には硫酸を用い、処理条件はPH2.0で約30分、
復活処理はアンモニア水を用い、処理条件はPH
4.5で約30分そしてわずかの主炭素源を供給し、
又空気も通気した。処理温度はいずれも30℃、又
主炭素源として6%糖密を用い、培養槽及び復活
槽に供給した。培養槽への主炭素源の供給は2.0
/hで行ない培養槽内の液面が一定となるよう
に製品抜きの出しを行なつた。
比較例1は殺菌処理として実施例1と同じく酸
処理を行なうが、復活処理を行なわない例であ
り、比較例2はごく普通のケモスタツト系の連続
培養であり、殺菌処理及び復活処理を行なわない
例でいずれの場合も、その他の条件及び方法は実
施例1と同一条件下で行なつた。実験結果を次に
示す。
The present invention relates to a method for culturing yeast, and more specifically to a method in which a culture solution is extracted from a culture tank, the culture solution is sterilized, the yeast is then revived, and the yeast is cultured while being returned to the culture tank. be. In the fermentation industry, bacteria prevention technology is indispensable for pure fermentation of bacteria producing useful substances, and even a small amount of bacterial contamination makes it impossible for the producing bacteria to grow, thereby inhibiting the production of useful substances. You will end up being rejected. For this reason, when culturing is actually carried out, strict sterilization or sterilization treatment is performed on the culture solution, culture equipment, ventilation air, etc. On the other hand, methods for eliminating bacteria in the culture solution (for example, intervening drugs to eliminate the activity of bacteria, making the pH acidic, etc.) have been proposed (for example,
39511, Special Publication No. 47-38988, Special Publication No. 30-4440, Special Publication No. 30-4439). However, all of these methods have the disadvantage that they cause the activity of various bacteria to be lost and at the same time, the activity of yeast to decrease, resulting in a decrease in the productivity of the culture operation and an increase in production costs. The balance between prevention of germs and culture productivity becomes a major issue. Therefore, it is a challenge in the art to create a yeast culture method that is highly productive while appropriately eliminating contaminant bacteria, and the present invention has successfully solved this challenge. That is, as a result of intensive research by the present inventors on a method for culturing yeast that is not affected by bacterial contamination and that achieves high productivity, the present inventors extracted the culture solution, performed sterilization treatment, and further performed yeast rejuvenation treatment. discovered that by culturing yeast while returning it to the culture tank, it was possible to prevent a decrease in yeast activity caused by strong sterilization treatment, and completed the present invention. The present invention will be explained in more detail below. Although FIG. 1 shows a schematic process diagram of the present invention, this is an example of the present invention and does not show the entire process. 1
2 is a culture tank, 2 is a sterilization treatment device, and 3 is a revival treatment tank. The sterilization device No. 2 is a device for sterilizing the culture solution introduced from the culture tank No. 1. As a sterilization treatment method, methods such as chemical treatment, ultraviolet sterilization, radiation sterilization, and pasteurization can be used, but it is generally preferable to perform chemical treatment because it is economically advantageous. Therefore, as a sterilization treatment, chemical treatment will mainly be described below. The sulfur treatment must be conducted under conditions such as the amount of chemicals added and the treatment time that kill or deactivate bacteria but do not kill yeast. This also applies to other sterilization methods. These conditions cannot be defined unambiguously because they differ depending on the type of bacteria, yeast, and drug, but these conditions should be determined by testing the activity of yeast and bacteria by the drug in advance. This will help you find the appropriate conditions. Other sterilization methods can also be tested in advance to determine appropriate conditions. Needless to say, these conditions can be determined by focusing only on miscellaneous bacteria without considering the reduction in yeast activity. For example, when performing acidic treatment as a chemical treatment, the pH is generally 1.5 to 3 and the treatment time is 20 to 30 minutes.
All you need to do is add acid and process for 120 minutes.
When sterilizing with sodium hypochlorite, the effective chlorine concentration is 40 ppm or less and the treatment time is 10 minutes or less. As another example, in the case of a surfactant such as lauryldimethylbenzylammonium chloride, it is effective if the treatment time is 500 ppm or less and the treatment time is 20 hours or less. The types of drugs include acids, bases, hydrogen peroxide, sodium hypochlorite, formalin, caffeine, aldehydes, surfactants, ozone, gases such as chlorine, and antibiotics. Appropriate processing conditions can be determined by prior testing. When a chemical is used, a tank may generally be used as the sterilizer, and any type of sterilizer can be used, regardless of the presence or absence of a stirrer. For other sterilization methods, any known device suitable for each treatment may be used. The culture solution sterilized as described above is introduced into the revival tank 3, which is an area where the yeast that has been deactivated by the sterilization treatment is revived again. If the inactivated yeast is directly returned to the culture tank and cultured, the overall growth of the yeast will decrease and productivity will decrease.
Therefore, this restoration process is an essential process in the present invention. The method conditions for performing the revival treatment cannot be unambiguously defined because they vary depending on the degree of inactivation by the sterilization treatment in 2, the type of yeast, etc., but in general, the conditions are PH4~
8, treatment time is 10 minutes or more, more preferably PH4-6
In order to revive the yeast, a treatment time of 20 to 120 minutes will be more effective if the main carbon source and other nutrient sources are supplied (line 6), or if aeration is performed (line 7) in the case of aerobic culture. It is true. However, appropriate conditions can be determined by testing the degree of resurgence in advance. For example, conditions for revival (PH, temperature, treatment time, etc.) may be selected based on the respiration rate, growth rate, etc. of the yeast. For example, when yeast is acid-treated (pH is about 2 and treatment time is about 20 minutes), a small amount of the main carbon source and other nutrients is added, and while aeration is performed, the pH is raised to 4. If the revival process is performed in steps 6 to 6 with a processing time of about 60 minutes, most of the yeast will be revived. Similar calculations can be made for other chemical treatments and sterilization treatments. As a device for performing the restoration process,
Tanks are generally used, and any type of tank may be used, with or without a stirrer. The yeast revived in this way is returned to culture tank 1.
and cultured. As described above, the present invention is characterized in that it is cultured while performing two treatments, sterilization treatment and revival treatment, and only by performing these treatments can the effects of bacterial contamination be eliminated and high productivity can be achieved. It will be done. As is clear from the principle, the method of the present invention can be applied in any case, regardless of the type of yeast or the type of culture (batch method, semi-batch method, continuous culture method, etc.). Of course, it can be combined with a multi-stage culture tank, and a two-stage type is shown in FIG. 2 as an example. Next, the present invention will be further explained with reference to Examples. Example 1 Using the process shown in Figure 1, Sa
- Continuous culture was performed using ccharomyces cerevisiae (baker's yeast). A 30-volume jar fermenter was used as the culture tank, and the culture was carried out at a temperature of 33°C and a pH of 4.5. As a sterilization treatment, a chemical treatment is performed, using sulfuric acid as the chemical, and the treatment conditions are PH2.0 for about 30 minutes.
Ammonia water is used for the revival treatment, and the treatment conditions are PH.
4.5 for about 30 minutes and provide a small amount of the main carbon source,
Air was also ventilated. The treatment temperature was 30°C in both cases, and 6% molasses was used as the main carbon source, which was supplied to the culture tank and revival tank. The main carbon source supply to the culture tank is 2.0
/h, and the product was removed so that the liquid level in the culture tank remained constant. Comparative Example 1 is an example in which acid treatment is performed as in Example 1 as a sterilization treatment, but no revival treatment is performed, and Comparative Example 2 is an ordinary chemostat-based continuous culture without sterilization treatment or revival treatment. In each case, the other conditions and methods were the same as in Example 1. The experimental results are shown below.
【表】
培養経過各時間で検鏡を行なつたが、雑菌はほ
とんどみられず、又酵母の増殖にも異常がなかつ
た。比較例1は雑菌の増殖はあまりみられなかつ
たが、酵母の活性も低下したため、約5時間目よ
りウオツシユアウトする傾向が見られた。又比較
例2は約24時間目より雑菌数が増加し、酵母の増
殖も大きく低下した。
以上のことから、薬剤処理、復活処理の2つの
処理を行うことで、雑菌の影響を受けずに高い生
産性を得る。本発明法による効果が示された。
実施例 2
図1に示したプロセスを用い、酵母として
Candida utilis IAM4215を用いて連続培養を行
なつた。培養槽、殺菌処理装置、復活槽は実施例
1と同じものを用い、培養温度30℃、PHは4.6と
した。主炭素源は4.2%糖密を用い、約4.0/h
で供給し、培養槽内の液面が一定となるように製
品抜き出しを行なつた。殺菌処理の薬剤として次
亜塩素酸ソーダを用い、有効塩素濃度40ppm以下
で処理時間10分以下の条件、復活処理はわずかの
上記の主炭素源栄養液を添加し、通気を施しなが
らPHを4.5に調整しつつ約30分処理した。比較例
1,2は実施例1の場合と同じ条件である。結果
を次に示す。[Table] A microscopic examination was performed at each time point during the course of the culture, and almost no bacteria were observed, and there was no abnormality in the growth of yeast. In Comparative Example 1, there was not much growth of bacteria, but the activity of yeast was also reduced, so there was a tendency to wash out after about 5 hours. Furthermore, in Comparative Example 2, the number of miscellaneous bacteria increased after about 24 hours, and the growth of yeast also decreased significantly. From the above, high productivity can be obtained without being affected by germs by performing two treatments: chemical treatment and revival treatment. The effect of the method of the present invention was demonstrated. Example 2 Using the process shown in Figure 1, as yeast
Continuous culture was performed using Candida utilis IAM4215. The same culture tank, sterilization equipment, and resurrection tank as in Example 1 were used, and the culture temperature was 30°C and the pH was 4.6. The main carbon source is 4.2% molasses, approximately 4.0/h
The product was removed so that the liquid level in the culture tank remained constant. Sodium hypochlorite is used as a sterilization agent, and the effective chlorine concentration is 40 ppm or less and the treatment time is 10 minutes or less. For the revival treatment, a small amount of the above-mentioned main carbon source nutrient solution is added, and the pH is raised to 4.5 while aeration is performed. Processed for about 30 minutes while adjusting the temperature. Comparative Examples 1 and 2 were under the same conditions as Example 1. The results are shown below.
【表】
培養経過各時間で検鏡を行なつたが、実施例2
は雑菌はほとんど見られず、酵母の増殖にも異常
がなかつた。比較例1は、実施例1の場合の比較
例1と同じく、雑菌の増殖はあまりみられなかつ
たが、酵母の活性が低下したため、ウオツシユア
ウト現象が約5〜6時間目より、みられた。比較
例2も又、実施例1の場合の比較例2と同じく、
約24時間後より急激に雑菌数が増加し酵母の増殖
を阻害した。以上のことから、本発明の効果が証
明された。[Table] A microscopic examination was performed at each time of the culture progress, but Example 2
Almost no bacteria were observed, and there was no abnormality in the growth of yeast. In Comparative Example 1, as in Comparative Example 1 in Example 1, there was not much growth of bacteria, but the washout phenomenon was observed from about 5 to 6 hours due to the decrease in yeast activity. Ta. Comparative Example 2 is also similar to Comparative Example 2 in Example 1,
After about 24 hours, the number of miscellaneous bacteria increased rapidly and inhibited yeast growth. From the above, the effects of the present invention were proven.
図1は、本発明の培養槽が単槽である場合のプ
ロセス説明図、図2は、多段の培養槽として2段
の培養槽を用いた場合のプロセス説明図である。
1……培養槽、2……殺菌処理装置、3……復
活槽、4……薬剤添加ライン、5……塩基添加ラ
イン、5′……培養槽から培養槽への送液ライン、
6……主炭素源及び栄養添加ライン、7……通気
ライン、8……製品としての液抜出しライン。
FIG. 1 is a process explanatory diagram when the culture tank of the present invention is a single tank, and FIG. 2 is a process explanatory diagram when a two-stage culture tank is used as a multistage culture tank. 1... Culture tank, 2... Sterilization treatment device, 3... Resurrection tank, 4... Drug addition line, 5... Base addition line, 5'... Liquid feeding line from the culture tank to the culture tank,
6... Main carbon source and nutrient addition line, 7... Ventilation line, 8... Liquid extraction line as a product.
Claims (1)
抜き出し、培養液を殺菌処理した後、酵母の復活
処理を行ない、酵母を培養槽に戻しつつ培養する
酵母の培養方法。 2 殺菌処理に薬剤を用いる特許請求の範囲第1
項記載の培養方法。 3 酵母をPH4〜8で処理時間10分以上の条件で
復活処理を行なう特許請求の範囲第1項記載の培
養方法。 4 酵母をPH4〜6で処理時間20〜120分の条件
で復活処理を行なう特許請求の範囲第3項記載の
培養方法。 5 主炭素源及びその他の栄養源を供給しつつ復
活処理を行う特許請求の範囲第1項記載の培養方
法。 6 通気を行ないつつ復活処理を行う特許請求の
範囲第1項記載の培養方法。[Scope of Claims] 1. A method for culturing yeast, in which a culture solution is extracted from a culture tank, the culture solution is sterilized, the yeast is revived, and the yeast is cultured while being returned to the culture tank. 2 Claim 1 that uses chemicals for sterilization treatment
Culture method described in section. 3. The culture method according to claim 1, wherein the yeast is revived at pH 4 to 8 for a treatment time of 10 minutes or more. 4. The culture method according to claim 3, wherein the yeast is revived at pH 4 to 6 for a treatment time of 20 to 120 minutes. 5. The culture method according to claim 1, wherein the revival treatment is carried out while supplying the main carbon source and other nutrient sources. 6. The culture method according to claim 1, wherein the revival treatment is performed while aeration is performed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10779479A JPS5632988A (en) | 1979-08-23 | 1979-08-23 | Cultivation of yeast |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10779479A JPS5632988A (en) | 1979-08-23 | 1979-08-23 | Cultivation of yeast |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5632988A JPS5632988A (en) | 1981-04-02 |
JPS6358559B2 true JPS6358559B2 (en) | 1988-11-16 |
Family
ID=14468191
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10779479A Granted JPS5632988A (en) | 1979-08-23 | 1979-08-23 | Cultivation of yeast |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5632988A (en) |
-
1979
- 1979-08-23 JP JP10779479A patent/JPS5632988A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5632988A (en) | 1981-04-02 |
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