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JPH0332359B2 - - Google Patents
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JPH0332359B2 - - Google Patents

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Publication number
JPH0332359B2
JPH0332359B2 JP58047911A JP4791183A JPH0332359B2 JP H0332359 B2 JPH0332359 B2 JP H0332359B2 JP 58047911 A JP58047911 A JP 58047911A JP 4791183 A JP4791183 A JP 4791183A JP H0332359 B2 JPH0332359 B2 JP H0332359B2
Authority
JP
Japan
Prior art keywords
reactor
yeast
solution
bacteria
alcohol
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
JP58047911A
Other languages
Japanese (ja)
Other versions
JPS59173086A (en
Inventor
Teruya Shirata
Takeo Ootani
Yasuo Ikesue
Hiroi Yoshii
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.)
SHINNENRYOYU KAIHATSU GIJUTSU KENKYU KUMIAI
Original Assignee
SHINNENRYOYU KAIHATSU GIJUTSU KENKYU KUMIAI
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 SHINNENRYOYU KAIHATSU GIJUTSU KENKYU KUMIAI filed Critical SHINNENRYOYU KAIHATSU GIJUTSU KENKYU KUMIAI
Priority to JP58047911A priority Critical patent/JPS59173086A/en
Publication of JPS59173086A publication Critical patent/JPS59173086A/en
Publication of JPH0332359B2 publication Critical patent/JPH0332359B2/ja
Granted legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、固定化酵母を用いてアルコールを発
酵生産する方法において、雑菌の汚染によるアル
コール生産性の低下を簡便な手段で防止する方法
に関するものである。 発酵生産法においては雑菌汚染が常に問題にな
つており、固定化酵母を用いたアルコール発酵に
おいても例外ではない。酵母を固定化しないで行
なう通常の回分培養法においては、発酵終了後発
酵液を発酵槽から抜き出すところから装置全体を
加熱殺菌等によつて容易に殺菌することができ
る。しかしながら、固定化酵母を用いる場合には
反応器内に常に固定化酵母があるところから、こ
の固定化酵母を死滅させずに雑菌のみを死滅させ
ることは容易ではない。そこで、従来反応器内が
雑菌で汚染された場合には、装置を解体して全体
を殺菌し、固定化酵母を新たに製造して反応器内
に充填してから運転を再開していたが、この作業
は大変な作業であり、労力の面のみならず操業時
間が減ることによる生産性の低下の面でも大きな
問題点であつた。特にアルコール発酵の場合には
安価に大量生産する必要があるところからこの雑
菌汚染対策は固定化酵母を用いる方法の死命を制
するものであつた。 本発明者らはこの雑菌汚染の問題を解決する簡
便な手段を開発すべく種々の検討の結果、亜硫
酸、メタ重亜硫酸及び次亜塩素酸を特定の低PH域
で作用させると、固定化酵母を生存させたまま雑
菌のみを効率よく死滅させうることを見出し、さ
らに、これらの化合物を基質溶質に加えれば、こ
れらの化合物は制菌作用を発揮して雑菌によるア
ルコール発酵阻害作用を抑止するが固定化酵母の
アルコール生産能は阻害しないことを見出して、
これに基いて本発明を完成するに至つた。 すなわち本発明は、(1)固定化酵母を充填した反
応器に基質溶液を導入してアルコール発酵を行な
わせる方法において、該反応器内が雑菌で汚染さ
れた際に、亜硫酸、メタ重亜硫酸、次亜塩素酸及
びこれらの塩のうち一種又は二種以上を含むPH
2.5〜4.5の溶液を反応器内に導入することを特徴
とするアルコール発酵方法と、(2)固定化酵母を充
填した反応器に基質溶液を導入してアルコール発
酵を行なわせる方法において、基質溶液に亜硫
酸、メタ重亜硫酸、次亜塩素酸及びこれらの塩の
うち一種又は二種以上を含有せしめたことを特徴
とするアルコール発酵方法に関するものである。 酵母はアルコール生産能を有するものであれば
特に限定されるものではなく、例としてはサツカ
ロミセス・フオルモセンシス(Saccharomyces
formosensis)IFO0216、同セレビシエ(S.
cerevisiae)協会7号菌(大蔵省醸造試験所)、
同カールスベルゲンシス(S.carlsbergensis)、同
ロブスタス(S.robustus)、同ロキシイ(S.
rouxii)などを挙げることができる。 酵母の固定化方法も特に限定されるものではな
く例えば多孔性ガラスビーズなどに吸着させる方
法であつてもよいが、本発明の方法にはゲル包括
法が好適であり、特に、少量の酵母菌体を担体に
固定化後この固定化物を栄養培地中で培養して酵
母を増殖させたいわゆる固定化増殖酵母を用いる
のがよい。担体の種類は特に限定されるものでは
なく、例えばポリアクリルアミド、ポリビニルア
ルコール、寒天、カラギーナン、コラーゲンなど
を用いることができる。特公昭56−43234号、特
公昭56−43235号、特開昭56−131391号などによ
つて開示されている光硬化性樹脂を用いて酵母を
固定化する方法は本発明の方法に好適である。光
硬化性樹脂の例としては無水マレイン酸などの不
飽和多塩期酸と多価アルコールとのポリエステル
類、ポリエチレングリコールとメタアクリル酸と
のポリエステル類、不飽和ウレタン類、非イオン
性不飽和アクリル樹脂、アニオン性不飽和アクリ
ル樹脂、カチオン性不飽和アクリル樹脂、不飽和
ポリビニルアルコール、不飽村ポリアミド類、不
飽和エポキシ類などを挙げることができる。固定
化方法としては、これらのいずれかの光硬化性樹
脂と前記酵母菌体の懸濁液とを混合し、これに
250〜600nmの活性光線を照射して得られた固定
化物を球状、膜状、シート状、管状など任意の形
状にすればよい。 固定化酵母を充填する反応器、発酵原料である
基質溶液および発酵条件は従来と同様でよく、例
えばケインモラセス、ビートモラセス等の精蜜を
糖濃度として10〜25g/dl程度、そして硫安を
0.01〜1g/dl程度含む基質溶液を反応器内に滞
留時間が2〜10時間程度になるように通液し、反
応器内の温度を25〜40℃程度、好ましくは28〜35
℃程度に保てばよい。蜜相糖蜜、パイナツプル糖
蜜などのような果実の搾汁粕を原料としたものな
ど他の原料を用いるときは原料に応じて適宜ビタ
ミン類、有機栄養物、無機塩などを補充すればよ
い。また、この基質溶液は予め殺菌を行なつたも
ののほか無殺菌のままのものであつてもよい。 本発明において雑菌阻害を排除する方法のひと
つは、このようなアルコール発酵生産方法におい
て反応器内が雑菌で汚染された際に、亜硫酸、メ
タ重亜硫酸、次亜塩素酸及びこれらの塩のうち一
種又は二種以上を含むPH2.5〜4.5の溶液を反応器
内に導入するところに特徴がある。 反応器が雑菌で汚染されているか否かは、反応
器から排出される発酵液を平板培養しあるいは顕
微鏡で観察することによつて確認できる。また、
アルコール生産量の低下によつて推定することも
できる。このほか、雑菌汚染の有無を検出せずに
下記の殺菌操作を定期的に行なつてもよい。 殺菌剤として用いるものは亜硫酸、メタ重亜硫
酸、次亜塩素酸及びこれらの塩のいずれかであ
る。塩は、ナトリウム、カリウム等のアルカリ金
属塩、及びカルシウムなどのアルカリ土族塩が適
当である。例としては、亜硫酸ナトリウム、メタ
重亜硫酸カリウム、次亜塩素酸ナトリウム、サラ
シ粉などを挙げることができる。濃度は、固定化
酵母への影響が少なくかつ雑菌を殺菌する効果が
大きい程よいわけであるが、この濃度は殺菌剤の
種類、溶液のPH、反応器に残存する糖の量などに
よつて異なるもので、予め試験をして定めるのが
よい。一般的には、例えばメタ重亜硫酸カリウム
の場合には30〜2000ppm程度、そして次亜塩素酸
ナトウムの場合には30〜2000ppm程度が適当であ
る。 溶液のPHは2.5から4.5の範囲内にする。PH5以
上では殺菌効率が悪くなり、PH2以下では酵母の
被害も甚大になる。この範囲内では特にPH3.5〜
4.0の範囲が適当である。溶液のPH調整には塩酸、
硫酸等の鉱酸、及び/または蟻酸、酢酸等の有機
酸を使用することができる。この調整は、溶液を
固定化酵母の反応器に導入する前に行つても、導
入後に行つてもよい。 次に、メタ重亜硫酸カリウムの濃度及びPHを変
えて固定化酵母及び雑菌に対する殺菌効果を測定
した結果を示す。 この実験に用いた酵母はサツカロミセス・フオ
ルモセンシスIFO0216であり、固定化方法は実施
例1と同様にして行なつた。雑菌は固定化酵母を
用いてアルコールを連続的に発酵生産している装
置の反応器から得たものを用いた。実験方法とし
ては、固定化酵母については糖蜜を糖濃度として
20g/dlそして硫安を0.1g/dl含む溶液で30℃
で24時間予備培養したものを用い、雑菌について
はグルコール1.0g/dl、酵母エキス1.0g/dl、
ペプトン1.0g/dl、NaCl0.5g/dlおよび麦芽エ
キス0.3g/dlを含有するPH6.0の培地でやはり30
℃で24時間培養したものを用いた。そして、各菌
とも下表に示すメタ重亜硫酸カリウム濃度及びPH
で糖濃度2g/dlの糖蜜液に107〜108個/mlにな
るように添加して30℃で24時間静置し、残存する
生菌数を測定した。得られた結果を下表に示す。
The present invention relates to a method for fermentatively producing alcohol using immobilized yeast, in which a decrease in alcohol productivity due to bacterial contamination is prevented by a simple means. Bacterial contamination is always a problem in fermentation production methods, and alcohol fermentation using immobilized yeast is no exception. In a conventional batch culture method in which yeast is not immobilized, the entire apparatus can be easily sterilized by heat sterilization or the like from the point where the fermented liquid is extracted from the fermenter after completion of fermentation. However, when immobilized yeast is used, since the immobilized yeast is always present in the reactor, it is not easy to kill only the miscellaneous bacteria without killing the immobilized yeast. Therefore, in the past, if the inside of the reactor became contaminated with bacteria, the equipment was dismantled, the entire device was sterilized, and immobilized yeast was newly produced and filled into the reactor before operation was resumed. This work is very difficult and is a major problem not only in terms of labor but also in terms of reduced productivity due to reduced operating time. Particularly in the case of alcoholic fermentation, since it is necessary to mass-produce at low cost, this countermeasure against bacterial contamination was the life-or-death of the method using immobilized yeast. The present inventors conducted various studies in order to develop a simple means to solve this problem of bacterial contamination, and found that when sulfite, metabisulfite, and hypochlorous acid are applied in a specific low pH range, immobilized yeast We discovered that it is possible to efficiently kill only the bacteria while keeping the bacteria alive, and furthermore, when these compounds are added to the substrate solute, these compounds exert a bacteriostatic effect and suppress the alcohol fermentation inhibiting effect caused by the bacteria. We discovered that the alcohol production ability of immobilized yeast was not inhibited.
Based on this, we have completed the present invention. That is, the present invention provides (1) a method for performing alcoholic fermentation by introducing a substrate solution into a reactor filled with immobilized yeast, and when the inside of the reactor is contaminated with bacteria, sulfite, metabisulfite, PH containing one or more of hypochlorous acid and these salts
An alcohol fermentation method characterized by introducing a solution of 2.5 to 4.5 into a reactor, and (2) a method of introducing a substrate solution into a reactor filled with immobilized yeast to perform alcohol fermentation. The present invention relates to an alcohol fermentation method characterized by containing one or more of sulfite, metabisulfite, hypochlorous acid, and salts thereof. Yeast is not particularly limited as long as it has the ability to produce alcohol; examples include Saccharomyces formocensis.
formosensis) IFO0216, S. cerevisiae (S.
cerevisiae) Association No. 7 (Ministry of Finance Brewing Laboratory),
S.carlsbergensis, S.robustus, and S.roxyi.
rouxii). The method of immobilizing yeast is not particularly limited, and may be, for example, a method of adsorbing it to porous glass beads, etc., but the gel entrapment method is suitable for the method of the present invention. It is preferable to use so-called immobilized propagated yeast, which is obtained by immobilizing the yeast on a carrier and then culturing the immobilized product in a nutrient medium to proliferate the yeast. The type of carrier is not particularly limited, and for example, polyacrylamide, polyvinyl alcohol, agar, carrageenan, collagen, etc. can be used. The method of immobilizing yeast using a photocurable resin disclosed in Japanese Patent Publication No. 56-43234, Japanese Patent Publication No. 56-43235, Japanese Patent Publication No. 56-131391, etc. is suitable for the method of the present invention. be. Examples of photocurable resins include polyesters of unsaturated polyhydric acids such as maleic anhydride and polyhydric alcohols, polyesters of polyethylene glycol and methacrylic acid, unsaturated urethanes, and nonionic unsaturated acrylics. Examples include resins, anionic unsaturated acrylic resins, cationic unsaturated acrylic resins, unsaturated polyvinyl alcohols, unsaturated polyamides, and unsaturated epoxies. The immobilization method involves mixing one of these photocurable resins with the suspension of yeast cells, and then adding
The immobilized product obtained by irradiation with actinic rays of 250 to 600 nm may be shaped into any shape such as a sphere, a film, a sheet, or a tube. The reactor filled with immobilized yeast, the substrate solution as the fermentation raw material, and the fermentation conditions may be the same as conventional ones, such as sugar concentration of cane molasses, beet molasses, etc., of about 10 to 25 g/dl, and ammonium sulfate.
A substrate solution containing about 0.01 to 1 g/dl is passed through the reactor so that the residence time is about 2 to 10 hours, and the temperature inside the reactor is set to about 25 to 40°C, preferably 28 to 35°C.
Just keep it at around ℃. When using other raw materials, such as those made from fruit juice lees such as honey phase molasses and pineapple molasses, vitamins, organic nutrients, inorganic salts, etc. may be supplemented as appropriate depending on the raw material. Further, this substrate solution may be sterilized in advance or may be unsterilized. One of the methods of eliminating bacterial inhibition in the present invention is to remove one of sulfite, metabisulfite, hypochlorous acid, and their salts when the inside of the reactor is contaminated with bacteria in such an alcohol fermentation production method. Alternatively, it is characterized in that a solution containing two or more species with a pH of 2.5 to 4.5 is introduced into the reactor. Whether or not the reactor is contaminated with germs can be confirmed by culturing the fermentation liquid discharged from the reactor on a plate or observing it with a microscope. Also,
It can also be estimated by the decrease in alcohol production. In addition, the following sterilization operation may be performed periodically without detecting the presence or absence of bacterial contamination. The disinfectant used is sulfurous acid, metabisulfite, hypochlorous acid, or salts thereof. Suitable salts include alkali metal salts such as sodium and potassium salts, and alkaline earth salts such as calcium. Examples include sodium sulfite, potassium metabisulfite, sodium hypochlorite, and white flour. The concentration is better as it has less effect on the immobilized yeast and has a greater effect on sterilizing bacteria, but this concentration varies depending on the type of disinfectant, the pH of the solution, the amount of sugar remaining in the reactor, etc. It is best to test and determine this in advance. Generally, for example, in the case of potassium metabisulfite, about 30 to 2000 ppm is appropriate, and in the case of sodium hypochlorite, about 30 to 2000 ppm is appropriate. The pH of the solution should be within the range of 2.5 to 4.5. If the pH is higher than 5, the sterilization efficiency will be poor, and if the pH is lower than 2, the damage caused by yeast will be severe. Within this range, especially PH3.5~
A range of 4.0 is appropriate. To adjust the pH of the solution, use hydrochloric acid,
Mineral acids such as sulfuric acid and/or organic acids such as formic acid and acetic acid can be used. This adjustment may be performed before or after introducing the solution into the reactor of immobilized yeast. Next, the results of measuring the bactericidal effect on immobilized yeast and various bacteria by varying the concentration and pH of potassium metabisulfite are shown. The yeast used in this experiment was Satucharomyces formocensis IFO0216, and the immobilization method was the same as in Example 1. The bacteria used were those obtained from a reactor of a device that continuously ferments and produces alcohol using immobilized yeast. As for the experimental method, for immobilized yeast, molasses was used as the sugar concentration.
20g/dl and a solution containing ammonium sulfate 0.1g/dl at 30°C.
For bacteria, 1.0g/dl of glycol, 1.0g/dl of yeast extract,
30 in a medium with a pH of 6.0 containing 1.0 g/dl of peptone, 0.5 g/dl of NaCl, and 0.3 g/dl of malt extract.
The cells cultured at ℃ for 24 hours were used. For each bacteria, the potassium metabisulfite concentration and PH are shown in the table below.
They were added to a molasses solution with a sugar concentration of 2 g/dl at a concentration of 10 7 to 10 8 cells/ml, allowed to stand at 30°C for 24 hours, and the number of remaining viable bacteria was measured. The results obtained are shown in the table below.

【表】 溶液中には反応器内に残存する糖分が混入して
くることがあるが、この糖分は殺菌作用を低下せ
しめる。糖濃度が特に5g/dlを越えると殺菌作
用が大巾に低下するので、5g/dl以下になるよ
うに留意する必要がある。好ましくは2g/dl以
下にするのがよい。 溶液は反応器の上部から導入してもよく、ある
いは下部から導入してもよい。導入後は必要によ
り液を循環させるなどして撹拌しながら雑菌を死
滅させるのに必要な時間放置する。この時間は殺
菌剤の種類、濃度、糖の濃度等によつて異なる
が、30分間〜24時間程度にするのが操作上便宜で
ある。 その後は、この溶液を反応器から抜き出し、必
要により基質溶液あるいはその他の培地溶液を反
応器内に導入して酵母を増強培養してから通常の
運転に復帰すればよい。 本発明において雑菌阻害を排除するもうひとつ
の方法は、基質溶液自身に亜硫酸、メタ重亜硫
酸、次亜塩素酸及びこれらの塩のうち一種又は二
種以上を含有せしめるところに特徴がある。 この方法においては、前述の殺菌剤に用いた亜
硫酸等を制菌剤として用いており、基質溶液内に
おける雑菌の増殖を防止してアルコール発酵を円
滑に行なわせている。濃度は固定化酵母のアルコ
ール生産能を低下させずに制菌作用を充分に発揮
させればよいわけであるが、この濃度は亜硫酸等
の種類、溶液のPH、糖濃度などによつて異なると
ころから予め試験をして定めるのがよい。しかし
ながら、例えばメタ重亜硫酸カリウムの場合には
通例500〜1500ppm程度、そして次亜塩素酸ナト
リウムの場合には通例500〜2000ppm程度が適当
である。 基質溶液のPHは低いほうが好ましく、PH2.7〜
5.5程度、特に3.5〜5程度が適当である。 基質溶液はこのほかは通常と同じでよく、この
基質溶液を用いた発酵条件と通常と同じでよい。 以上、述べた二つの方法は一方のみを使用して
もよく、また併用してもよいことはいうまでもな
い。 本発明の方法は、ひとつは、基質にメタ重亜硫
酸カリのような特定の殺菌剤を添加することによ
つて制菌作用を発揮させつつアルコール発酵を行
なわせ、そのことによつて反応系の殺菌回数を大
巾に減少させており、もうひとつは殺菌溶液とし
てメタ重亜硫酸カリのような特定の殺菌剤を特定
のPHにして用いており、そのことによつて殺菌の
際の反応装置の分解作業を不要にしている。本発
明の方法はアルコール発酵における殺菌作業を大
巾に省力化するとともにコスト低下にも大きく寄
与するものである。 以下、実施例を示す。 実施例 1 ポリエチレングリコール、イソホロンジイソシ
アネート、およびメタアクリル酸−2−ヒドロキ
シエチルからなる平均分子量約5000のウレタン化
プレポリマーにサツカロミセス・フオルモセンシ
スIFO0216の懸濁液を加え、さらに光増感剤とし
てベンゾインエチルエーテルを加えて、これらを
ホモジナイザーで均一に分散した。この分散液に
主波長360nmの低圧水銀灯を約3分間照射して
肉厚約1mmの膜状の固定化酵母を製造した。 この固定化酵母を矩冊形に切断して、縦・横と
も90mmで高さが700mの角筒形の槽にスペーサー
を介して並べ、この槽を4段に連結したものを反
応器1基とし、3基の反応器を直列に連結したも
のを反応器として用いた。 この反応器に、糖蜜を糖濃度として20g/dlそ
して硫安0.1g/dlを含む無殺菌の基質溶液を反
応器内の滞留時間が5時間になるように通液し、
通気を行ないながら30℃でアルコールを連続生産
させた。そして毎日1回、末満の反応器から流出
してくるアルコール含有液を前述のカビサイジン
を添加した雑菌用の合成培地に撤いて培養し、雑
菌の発生の有無を監視していたところ350時間目
に雑菌が発生したことを発見した。そこで、反応
器より反応液を抜き取り、反応器PHが3.5で糖濃
度が2g/dlの糖蜜液を張込み、続いて次亜塩素
酸ソーダを塩素濃度として500ppmになるように
加えた。30℃で3時間程度循環を行なつてからこ
の液を抜きだし、糖濃度20g/dlの糖蜜および
0.1g/dlの硫安を含む基質溶質を張込んで30℃
に保つて通気を行なう増強培養を4回繰返し、そ
の後定常運転に復帰させた。 この殺菌処置を行なう直前の反応器流出液はア
ルコール濃度が7.2g/dlであり、雑菌数が4×
108個/mlであつたが、この処置後の反応器流出
液はアルコール濃度が7.7g/dlであり、雑菌数
は0個/mlになつていた。 実施例 2 サツカロミセス・フオルモセンシスIFO0216の
かわりにサツカロミセス・セレビシエ協会7号菌
を用いて実施例1と同様に固定し、この固定化酵
母を実施例1と同じ反応器に装着して同様にアル
コール発酵生産を行なつていたところ、生産開始
後400時間目に反応器内に雑菌が発生しているこ
とが確認された。 そこで反応器より反応液を抜き取り、反応器に
PH3.5で糖濃度として5g/dlの糖蜜液を張込み、
SO2として1000ppmになるようにメタ重亜硫酸カ
リウムを加えた。30℃で3時間液循環を行なつて
からこの液を抜き出し、実施例1と同様にして定
常運転に復帰させた。 この殺菌処置を行なう直前の反応器流出液はア
ルコール濃度が7.4g/dlであり、雑菌数が5×
107個/mlであつたが、この処置後の反応器流出
液はアルコール濃度が7.9g/dlであり、雑菌数
は0個/mlになつていた。 実施例 3 実施例1と同じ固定化酵母を装着した同じ反応
器を用い、この反応器にメタ重亜硫酸カリウムを
SO2として1000ppmになるように加えたほかは実
施例1と同じ基質溶液(PH5.0)を供給して実施
例1と同様にしてアルコールを600時間連続生産
させた。 その間、反応器から流出して来るアルコール含
有液のアルコール濃度は約80g/dlでほぼ一定で
あり、雑菌数も102個/mlでほぼ一定であつた。
[Table] Sugar remaining in the reactor may be mixed into the solution, but this sugar reduces the bactericidal effect. If the sugar concentration exceeds 5 g/dl, the bactericidal effect will be greatly reduced, so care must be taken to keep it below 5 g/dl. Preferably it is 2 g/dl or less. The solution may be introduced from the top of the reactor or from the bottom. After introduction, the liquid is circulated and stirred if necessary, and left for a period of time necessary to kill germs. Although this time varies depending on the type and concentration of the disinfectant, the concentration of sugar, etc., it is convenient for operation to set it to about 30 minutes to 24 hours. Thereafter, this solution is extracted from the reactor, and if necessary, a substrate solution or other medium solution is introduced into the reactor to enhance yeast culture, and then normal operation can be resumed. Another method of eliminating bacterial inhibition in the present invention is characterized in that the substrate solution itself contains one or more of sulfite, metabisulfite, hypochlorous acid, and salts thereof. In this method, sulfurous acid, etc., which were used as the above-mentioned disinfectant, are used as a bacteriostatic agent, and the growth of various bacteria in the substrate solution is prevented and alcohol fermentation is carried out smoothly. The concentration should be sufficient to exert the bacteriostatic effect without reducing the alcohol production ability of the immobilized yeast, but this concentration varies depending on the type of sulfite, etc., the pH of the solution, the sugar concentration, etc. It is best to determine this by testing in advance. However, for example, in the case of potassium metabisulfite, it is usually about 500 to 1500 ppm, and in the case of sodium hypochlorite, it is usually about 500 to 2000 ppm. The lower the PH of the substrate solution, the better, PH2.7~
About 5.5, especially about 3.5 to 5 is appropriate. Other than this, the substrate solution may be the same as usual, and the fermentation conditions using this substrate solution may be the same as usual. It goes without saying that the two methods described above may be used alone or in combination. In the method of the present invention, alcoholic fermentation is carried out while exerting a bacteriostatic effect by adding a specific bactericide such as potassium metabisulfite to the substrate, thereby controlling the reaction system. The number of sterilizations is greatly reduced.The other method is to use a specific sterilizing agent such as potassium metabisulfite at a specific pH as a sterilizing solution, which reduces the number of sterilizations in the reactor during sterilization. Eliminates disassembly work. The method of the present invention greatly reduces the labor involved in sterilization work during alcohol fermentation, and also greatly contributes to cost reduction. Examples are shown below. Example 1 A suspension of Satucharomyces formocensis IFO0216 was added to a urethanized prepolymer of polyethylene glycol, isophorone diisocyanate, and 2-hydroxyethyl methacrylate with an average molecular weight of about 5000, and benzoin ethyl ether was added as a photosensitizer. were added and uniformly dispersed using a homogenizer. This dispersion was irradiated with a low-pressure mercury lamp with a dominant wavelength of 360 nm for about 3 minutes to produce a film-like immobilized yeast with a thickness of about 1 mm. This immobilized yeast is cut into rectangular shapes and arranged in a rectangular cylindrical tank with a length and width of 90 mm and a height of 700 m via spacers, and these tanks are connected in four stages to form one reactor. A reactor consisting of three reactors connected in series was used. An unsterilized substrate solution containing molasses with a sugar concentration of 20 g/dl and ammonium sulfate 0.1 g/dl was passed through the reactor so that the residence time in the reactor was 5 hours.
Alcohol was produced continuously at 30°C with ventilation. Then, once a day, the alcohol-containing liquid flowing out from the reactor was removed to a synthetic medium for bacteria containing the above-mentioned moldicidin, and cultured, and the presence or absence of bacteria was monitored for 350 hours. It was discovered that bacteria had developed. Therefore, the reaction solution was extracted from the reactor, and a molasses solution with a pH of 3.5 and a sugar concentration of 2 g/dl was charged into the reactor, and then sodium hypochlorite was added to the reactor so that the chlorine concentration was 500 ppm. After circulating at 30℃ for about 3 hours, this liquid was extracted and molasses with a sugar concentration of 20g/dl and
Filled with a substrate solute containing 0.1 g/dl ammonium sulfate and heated at 30°C.
Enhancement culture was repeated four times with aeration while maintaining the temperature, and then normal operation was resumed. The alcohol concentration of the reactor effluent immediately before this sterilization treatment was 7.2 g/dl, and the number of bacteria was 4×.
However, the alcohol concentration of the reactor effluent after this treatment was 7.7 g/dl, and the number of miscellaneous bacteria was 0. Example 2 Saccharomyces cerevisiae association No. 7 bacteria was used instead of Saccharomyces formocensis IFO0216 to immobilize it in the same manner as in Example 1, and this immobilized yeast was installed in the same reactor as in Example 1 to produce alcohol by fermentation in the same manner. During this process, it was confirmed that bacteria had grown inside the reactor 400 hours after the start of production. Then, the reaction liquid was extracted from the reactor and put into the reactor.
Filled with molasses solution with a sugar concentration of 5 g/dl at pH 3.5,
Potassium metabisulfite was added to give a concentration of 1000 ppm as SO 2 . After the liquid was circulated at 30°C for 3 hours, the liquid was extracted and normal operation was resumed in the same manner as in Example 1. The alcohol concentration of the reactor effluent immediately before this sterilization treatment was 7.4 g/dl, and the number of bacteria was 5x.
However, the alcohol concentration of the reactor effluent after this treatment was 7.9 g/dl, and the number of miscellaneous bacteria was 0. Example 3 Using the same reactor equipped with the same immobilized yeast as in Example 1, potassium metabisulfite was added to the reactor.
Alcohol was continuously produced for 600 hours in the same manner as in Example 1 except that SO 2 was added at 1000 ppm, and the same substrate solution (PH5.0) as in Example 1 was supplied. During this period, the alcohol concentration of the alcohol-containing liquid flowing out from the reactor was approximately constant at about 80 g/dl, and the number of bacteria was also approximately constant at 10 2 cells/ml.

Claims (1)

【特許請求の範囲】 1 固定化酵母を充填した反応器に基質溶液を導
入してアルコール発酵を行なわせる方法におい
て、該反応器内が雑菌で汚染された際に、亜硫
酸、メタ重亜硫酸、次亜塩素酸及びこれらの塩の
うち一種又は二種以上を含むPH2.5〜4.5の溶液を
反応器内に導入することを特徴とする、固定化酵
母を用いたアルコール発酵方法。 2 固定化酵母を充填した反応器に基質溶液を導
入してアルコール発酵を行なわせる方法におい
て、亜硫酸、メタ重亜硫酸、次亜塩素酸及びこれ
らの塩のうち一種又は二種以上を含有せしめた基
質溶液を用いてアルコール発酵を行なうことを特
徴とする、固定化酵母を用いたアルコール発酵方
法。
[Claims] 1. In a method for performing alcoholic fermentation by introducing a substrate solution into a reactor filled with immobilized yeast, when the inside of the reactor is contaminated with bacteria, sulfite, metabisulfite, An alcoholic fermentation method using immobilized yeast, which comprises introducing into a reactor a solution with a pH of 2.5 to 4.5 containing one or more of chlorous acid and salts thereof. 2. A substrate containing one or more of sulfurous acid, metabisulfite, hypochlorous acid, and salts thereof, in a method of carrying out alcoholic fermentation by introducing a substrate solution into a reactor filled with immobilized yeast. An alcohol fermentation method using immobilized yeast, characterized by carrying out alcohol fermentation using a solution.
JP58047911A 1983-03-24 1983-03-24 Alcoholic fermentation process using immobilized yeast Granted JPS59173086A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58047911A JPS59173086A (en) 1983-03-24 1983-03-24 Alcoholic fermentation process using immobilized yeast

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58047911A JPS59173086A (en) 1983-03-24 1983-03-24 Alcoholic fermentation process using immobilized yeast

Publications (2)

Publication Number Publication Date
JPS59173086A JPS59173086A (en) 1984-09-29
JPH0332359B2 true JPH0332359B2 (en) 1991-05-10

Family

ID=12788551

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58047911A Granted JPS59173086A (en) 1983-03-24 1983-03-24 Alcoholic fermentation process using immobilized yeast

Country Status (1)

Country Link
JP (1) JPS59173086A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02238880A (en) * 1989-03-10 1990-09-21 Ngk Insulators Ltd Regeneration of bioreactor
DE19856136C2 (en) 1998-12-04 2002-10-24 Pasteur Institut Method and device for the selection of accelerated proliferation of living cells in suspension
JP4854568B2 (en) * 2007-03-30 2012-01-18 三井造船株式会社 Alcohol production method
JP5308708B2 (en) * 2008-04-30 2013-10-09 株式会社エコログ・リサイクリング・ジャパン Ethanol production method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58179493A (en) * 1982-04-14 1983-10-20 Res Assoc Petroleum Alternat Dev<Rapad> Removal of contamination from immobilized yeast

Also Published As

Publication number Publication date
JPS59173086A (en) 1984-09-29

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