JPS59173086A - Alcoholic fermentation process using immobilized yeast - Google Patents

Alcoholic fermentation process using immobilized yeast

Info

Publication number
JPS59173086A
JPS59173086A JP58047911A JP4791183A JPS59173086A JP S59173086 A JPS59173086 A JP S59173086A JP 58047911 A JP58047911 A JP 58047911A JP 4791183 A JP4791183 A JP 4791183A JP S59173086 A JPS59173086 A JP S59173086A
Authority
JP
Japan
Prior art keywords
reactor
yeast
immobilized yeast
alcohol
substrate solution
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.)
Granted
Application number
JP58047911A
Other languages
Japanese (ja)
Other versions
JPH0332359B2 (en
Inventor
Teruya Shirata
白田 輝也
Takeo Otani
大谷 武夫
Yasuo Ikesue
池末 康男
Hiroi Yoshii
吉井 寛依
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.)
Research Association for Petroleum Alternatives Development
Original Assignee
Research Association for Petroleum Alternatives Development
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 Research Association for Petroleum Alternatives Development filed Critical Research Association for Petroleum Alternatives Development
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

Abstract

PURPOSE:To achieve the selective extermination of sundry germs, in high efficency, without lowering the alcohol productivity of an immobilized enzyme, by treating the enzyme with sulfurous acid, metabisulfite, etc. within a specific pH range. CONSTITUTION:Alcoholic fermentation is carried out by introducing a substrate solution into a reactor filled with an immobilized enzyme. When the reactor is contaminated with sundry germs, a solution containing one or more compounds selected from sulfurous acid, metabisulfate, hypochlorous acid and their salts and having a pH of 2.5-4.5, preferably 3.5-4.0 is introduced into the reactor. As an alternative method, the substrate solution used in the above alcoholic fermentation is added with one or more compounds selected from sulfurous acid, metabisulfite, hypochlorous acid and their salts in an amount to give a pH of about 2.7-5.5.

Description

【発明の詳細な説明】 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。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for fermentative production of alcohol using immobilized yeast, in which a decrease in alcohol productivity due to bacterial contamination is prevented by a simple means.

発酵生産法においては雑菌汚染が常に問題になっておシ
、固定化酵母を用いたアルコール発酵においても例外で
は外い。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って容易に殺菌する
ことができる。
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.

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。
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.

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シ、労力の面のみ々らず操業時間
が減ることによる生産性の低下の面でも大きな問題であ
った。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った。
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 big 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.

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ろ
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った。
The present inventors conducted various studies to develop a simple means to solve the problem of bacterial contamination, and found that when sulfite, metabisulfite, and hypochlorous acid are applied in a specific low pH range, immobilized yeast can be destroyed. We have discovered scales that can efficiently kill only bacteria while keeping them alive, and if we add these compounds to the substrate solute, these compounds will exert a bacteriostatic effect and suppress the alcohol fermentation inhibiting effect caused by bacteria. The present invention was completed based on the discovery that the ability of yeast to produce alcohol is not inhibited.

すなわち本発明は、(11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 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。
That is, the present invention provides (11) 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, An alcoholic fermentation method characterized by introducing into a reactor a solution with a pH of 2.5 to 4.5 containing one or more of chlorous acid and these salts, and (2) filling with immobilized yeast. A method for carrying out alcoholic fermentation by introducing a substrate solution into a reactor, characterized in that the substrate solution contains one or more of sulfurous acid, metabisulfite, hypochlorous acid and salts thereof. The invention relates to an alcoholic fermentation method.

酵母はアルコール生産能を翁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・7オ
ルモセンシス(Saccharomycesformo
sensis) IFOO216、同セレビシェ(S。
Yeast is not particularly limited as long as it has the ability to produce alcohol, and examples include Saccharomyces 7ormocensis (Saccharomyces formocensis).
sensis) IFOO216, same cereviche (S.

cerevlsiael協会7号菌(大蔵省醸協会7所
菌、同カールスペルグンシス(S、carlsberg
ensis)。
Cerevlsiael Association Bacteria No. 7 (Ministry of Finance Brewing Association Bacteria No. 7)
ensis).

同ロブスメス(S、robustus)、同ロキシイ(
S。
Robustus female (S, robustus), Roxyi (S, robustus)
S.

rouxii)などを挙げることができる。rouxii).

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
多孔性ガラスピーズなどに吸着させる方法であってもよ
いが、本発明の方法にはケゝル包括法が好適であり、特
に、少l″の酵母菌体を担体に固定化後との固定化物を
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−ダンなどを
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
どによっ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基酸
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、不飽和ポリアミド類、
不飽和エポキシ類などを挙げることができる。
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 kale entrapment method is suitable for the method of the present invention. It is preferable to use so-called immobilized and propagated yeast, which is obtained by immobilizing yeast cells of 20% on a carrier and then culturing the immobilized product in a nutrient medium to propagate yeast.The type of carrier is not particularly limited. For example, polyacrylamide, polyvinyl alcohol, agar, carrageenan, colladan, etc. can be used. A method of immobilizing yeast using a curable resin is suitable for the method of the present invention. Examples of photocurable resins include polyesters of unsaturated polybasic acids such as maleic anhydride and polyhydric alcohols, and polyethylene. Polyesters of glycol and methacrylic acid, unsaturated urethanes, nonionic unsaturated acrylic resins, anionic unsaturated acrylic resins, cationic unsaturated acrylic resins, unsaturated polyvinyl alcohol, unsaturated polyamides,
Examples include unsaturated epoxies.

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250〜6
00 nm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
The immobilization method involves mixing any of these photocurable resins with the yeast cell suspension, and adding 250 to 6
The immobilized product obtained by irradiation with 00 nm actinic light may be shaped into any shape such as a sphere, a film, a sheet, or a tube.

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糖蜜を糖濃度として10〜2
51を程度、そして硫安を0.01〜1 t/dt程度
含む基質溶液を反応器内に滞留時間が2〜10時間程時
間外るように通液し、反応器内の温度を25〜40℃程
度、好ましくは28〜35℃程度に保てによい。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i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ったもののほ
か無殺菌のままのものであってもよい。
The reactor filled with immobilized yeast, the substrate solution that is the fermentation raw material, and the fermentation conditions may be the same as conventional ones.
A substrate solution containing about 51% of ammonium sulfate and about 0.01 to 1 t/dt of ammonium sulfate was passed through the reactor so that the residence time was about 2 to 10 hours, and the temperature inside the reactor was set to 25 to 40%. The temperature can be kept at about 0.degree. C., preferably about 28 to 35.degree. When using other raw materials such as those made from fruit juice lees such as honey phase molasses and pineapple molasses, bimins, 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 left unsterilized.

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。
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. or PH2 containing two or more types
, 5 to 4,5 are introduced into the reactor.

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tb;り発酵液を平板培養しあるいは顕微鏡で観察
することによって確認できる。また、アルコール生産量
の低下によって推定することもでさる。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足期朗1に行
なってもよい。
Whether or not the reactor is contaminated with bacteria can be confirmed by culturing the fermentation liquid discharged from the reactor on a plate or observing it with a microscope. It is also possible to estimate it based on the decrease in alcohol production. In addition, the following sterilization operation may be performed without detecting the presence or absence of bacterial contamination.

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。
The disinfectant used is sulfurous acid, metabisulfite, hypochlorous acid, or salts thereof.

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垣が適当である。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PR1反応器に残存する糖の量などに
よって異なるもので、予め試験をして定めるのかよい。
Suitable salts include alkali metal salts such as sodium and potassium salts, and alkaline earth metal salts such as calcium. Examples include sodium sulfite, potassium metabisulfite, sodium hypochlorite, and white flour. The concentration is better as it has less influence on the immobilized yeast and has a greater effect on sterilizing bacteria, but this concentration varies depending on the type of disinfectant, the amount of sugar remaining in the PR1 reactor of the solution, etc. It would be better to test and determine this in advance.

一般的には、例えはメタ重亜硫酸カリウムの場合には3
0〜2000 ppm程度、そして次亜塩素酸ナトウム
の場合には30〜2000 ppm程度が適邑である。
In general, for example, in the case of potassium metabisulfite, 3
Approximately 0 to 2000 ppm, and in the case of sodium hypochlorite, 30 to 2000 ppm is appropriate.

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々す、P)(2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。
The pH of the solution is in the range 2.5 to 4.5. PH5
If the pH is above 2, the sterilization efficiency will be poor, and if it is below 2, the damage to yeast will be severe.
.. A range of 0 is appropriate.

次に、メタ重亜硫酸カリウムの濃度及びP′Hを変えて
固1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。
Next, the results of measuring the bactericidal effect on immobilized yeast and various bacteria by varying the concentration and P'H of potassium metabisulfite are shown.

この実験に用いた酵母はサツカロミセス・フォルモセン
シスIFOO216であシ、固定化方法は実施例1と同
様にして行なった、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20 ?/dtそして硫安を0.1
 f/dt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ス1.0 r/d)
、酵母エキス1.0 f/dt %  ベプト71.O
t/dl 、NaC60,!M/dtおよび麦芽エキス
0.31!、/dtを含有するPH6,0の培地でやけ
#)30℃で24時間培養したものを用いた。そして、
各画とも下表に示すメタ重亜硫酸カリウム濃度及びpH
糖濃度2 f/dtの糖蜜液に107〜108個/−に
なるように添加して30℃で24時間靜装し、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 yeast used in this experiment was Satucharomyces formocensis IFOO216, and the immobilization method was the same as in Example 1. The one obtained from the reactor was used. The experimental method for immobilized yeast is to use molasses as a sugar concentration of 20? /dt and ammonium sulfate at 0.1
Use a solution that has been pre-cultured at 30°C for 24 hours in a solution containing f/dt, and for bacteria, glucose 1.0 r/d)
, yeast extract 1.0 f/dt % Vept 71. O
t/dl, NaC60,! M/dt and malt extract 0.31! , /dt and cultured at 30° C. for 24 hours. and,
Potassium metabisulfite concentration and pH shown in the table below for each image
The bacteria were added to a molasses solution with a sugar concentration of 2 f/dt at a concentration of 107 to 108 cells/-, and the number of viable bacteria remaining was measured at 30°C for 24 hours. The results obtained are shown in the table below.

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5 f/dtを越えると殺菌作用が大巾に低下す
るので、5 ff/dt以下になるように留意する必要
がある。好ましくは2 t/c)を以下にするのがよい
Sugar remaining in the reactor may be mixed into the solution, but this sugar reduces the bactericidal action. In particular, if the sugar concentration exceeds 5 ff/dt, the bactericidal effect will be greatly reduced, so care must be taken to keep it below 5 ff/dt. It is preferable to set the t/c) to 2 t/c or less.

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。導入後は必要にょシ液を循環させ
るなどして攪拌しながら雑菌を死滅させるのに必要な時
間放置する。との時間は殺菌剤の種類、濃度、糖の濃度
等によって異方るが、30分間〜24時間程度にするの
が操作上便宜である。
The solution may be introduced from the top of the reactor or from the bottom. After introduction, the solution is circulated and stirred as needed for a period of time necessary to kill germs. Although the 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.

その後は、との溶液を反応器から抜き出し、必要によシ
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
Thereafter, the solution may be extracted from the reactor, and if necessary, a substrate solution or other medium solution may be introduced into the reactor to enhance and culture the yeast, and then normal operation may be resumed.

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1(亜硫酸、次亜塩素酸
及びとね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。
Another method of eliminating bacterial inhibition in the present invention is characterized in that the substrate solution itself contains one or more of sulfurous acid, meta-1 (sulfurous acid, hypochlorous acid, and tonera salt).

この方法においては、前述の殺菌剤に用いた亜硫酸尋を
制菌剤として用いておシ、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。
In this method, sulfite, which was used as the bactericidal agent described above, is used as a bacteriostatic agent to prevent the growth of germs in the substrate solution and to facilitate alcoholic fermentation.

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、との濃
度は亜硫酸等の種類、溶液のPH1糖濃度などによって
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
500〜1500 ppm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。
The concentration should be determined so that the immobilized yeast has sufficient antibacterial effect without reducing its alcohol production ability, but the concentration should be determined in advance because it varies depending on the type of sulfite, etc., the PH1 sugar concentration of the solution, etc. It is best to determine this through testing. 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.

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。
The lower the pH of the substrate solution, the better, and the pH is between 2.7 and 5.
.. A value of about 5, particularly about 3.5 to 5, is appropriate.

基質溶液はこのほかは通常と同じでよく、この基質溶液
を用いた発酵条件も通常と同じでよい。
The substrate solution may otherwise be the same as usual, and the fermentation conditions using this substrate solution may also be the same as usual.

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。
You may use only one of the two methods mentioned above.
It goes without saying that they may also be used together.

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って制菌作用を
発揮させつつアルコール発酵を行なわせ、そのことによ
って反応系の殺菌回数を大巾に減少させてお、す、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
って殺菌の際の反応装置の分解作業を不要にしている。
In the method of the present invention, alcoholic fermentation is carried out while exerting a bactericidal effect by adding a specific bactericide such as potassium metabisulfite to the substrate, thereby greatly increasing the number of times the reaction system is sterilized. The other method is to use a specific disinfectant such as potassium metabisulfite at a specific pH as a disinfectant solution, which eliminates the need to disassemble the reactor during disinfection. I have to.

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。
The method of the present invention greatly reduces the labor involved in sterilization work during alcohol fermentation, and also greatly contributes to cost reduction.

以下、実施例を示す。Examples are shown below.

実施例1 ポリエチレングリコール、インホロンジイソシアネート
、およびメタアクリル@−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・フォルモセンシスIFOO216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、とわらをホモジナイザーで均一に分散〔
7た。この分散液に主波長360 nmの低圧水鉄釘を
約3分間照射して肉厚約1簡の膜状の固定化酵母を製造
した。
Example 1 A suspension of Satucharomyces formocensis IFOO216 was added to a urethanized prepolymer of polyethylene glycol, inphorone diisocyanate, and methacrylic@-2-hydroxyethyl with an average molecular weight of about 5000, and benzoin was added as a photosensitizer. Add ethyl ether and disperse the straw uniformly with a homogenizer.
7. This dispersion was irradiated with a low-pressure water iron nail having a main wavelength of 360 nm for about 3 minutes to produce a film-like immobilized yeast with a thickness of about 1 layer.

この固定化酵母を短冊形に切断して、縦・横とも90m
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
This immobilized yeast was cut into a rectangular shape with a length and width of 90 m.
A reactor is formed by arranging rectangular cylindrical tanks with a height of 700 m via spacers, and connecting these tanks into 4 stages to form a reactor.
A series of reactors connected in series was used as the reactor.

この反応器に、糖蜜を糖濃度として20 f/dtそし
て硫安0.1 t/dt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
ないガから30℃でアルコールを連続生産させた。そし
て毎日1回、末端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給苗用の合成培
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、反応器よシ反応液を抜き取シ、反応器pHが3.
5で糖濃度が217dt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500 ppmになるよ
うに加えた。30℃で3時間程液循猿を行なってからこ
の液を抜きだし、糖濃度20 f/dtの糖蜜および0
.1 f/dtの硫安を含む基質溶質を張込んで30℃
に保っ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。
An unsterilized substrate solution containing molasses with a sugar concentration of 20 f/dt and ammonium sulfate 0.1 t/dt was passed through this reactor so that the residence time in the reactor was 5 hours, and ventilation was performed. Alcohol was continuously produced from moths at 30°C. Then, once a day, the alcohol-containing liquid flowing out from the end reactor was removed to the synthetic medium for feeding seedlings to which the above-mentioned moldicidin was added and cultured, and the presence or absence of germs was monitored, and 350 hours passed. It was discovered that bacteria had developed. Then, the reaction liquid was extracted from the reactor and the pH of the reactor was 3.
In Step 5, a molasses solution with a sugar concentration of 217 dt was charged, and then sodium hypochlorite was added so that the chlorine concentration was 500 ppm. After circulating the liquid at 30°C for about 3 hours, the liquid was extracted and molasses with a sugar concentration of 20 f/dt and 0.
.. Pour a substrate solute containing ammonium sulfate at 1 f/dt and heat at 30°C.
Enhancement culture was repeated 4 times with aeration and maintained at a constant temperature, and then normal operation was resumed.

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7.2 f/diであシ、雛菌数が4×10個/
−であったが、仁の処置後の反応器流出液はアルコ−1
し濃度が7.7 t/dtであ広雑菌数は0個/dにな
っていた。
The reactor effluent immediately before this sterilization treatment had an alcohol concentration of 7.2 f/di and a brood count of 4 x 10/
-, but the reactor effluent after treatment of jin was alcohol-1
The concentration was 7.7 t/dt, and the number of common bacteria was 0/d.

実施例2 サツカロミセス・フォルモセンシスIFOO216のか
わりにサツカロミセス・セレビシェ協会7芳菌を用いて
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
っていたきころ、生産開始後400時間目に反応器内に
頼菌が発生していることが確認された。
Example 2 Instead of Satucharomyces formocensis IFOO216, Satucharomyces cerevisiae association 7 aromatic bacteria was immobilized in the same manner as in Example 1, and this immobilized yeast was installed in the same reactor as in Example 1 and alcohol fermentation was carried out in the same manner. During production, it was confirmed that bacteria had grown in the reactor 400 hours after the start of production.

そこで反応器よシ反応液を抜き取シ、反応器にPH3,
5で糖濃度として5f/dtの糖蜜液を張込み、SO,
として1000 ppmにガるXうにメタ重亜硫酸カリ
ウムを加えた。30℃で3時間液循環を行なってからこ
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。
Then, the reaction liquid was extracted from the reactor, and PH3 was added to the reactor.
In step 5, add molasses solution with a sugar concentration of 5 f/dt,
Potassium metabisulfite was added to 1000 ppm. 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.

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7.4 t/dtであシ、雑菌数が5×107個
/mlであったが、この処置後の反応器流出液はアルコ
ール濃度が7.9 fi’/dtであシ、雑菌数はO個
/−になっていた。
The alcohol concentration of the reactor effluent immediately before this sterilization treatment was 7.4 t/dt and the number of miscellaneous bacteria was 5 x 107 cells/ml, but the alcohol concentration of the reactor effluent after this treatment was was 7.9 fi'/dt, and the number of miscellaneous bacteria was 0/-.

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802として1
000 pprnにガるように加えたt−t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。
Example 3 Using the same reactor equipped with the same immobilized yeast as in Example 1, potassium metabisulfite was added as 802 and 1
Alcohol was produced continuously for 600 hours in the same manner as in Example 1 by supplying the same substrate solution (pH 5,0) as in Example 1, which was added at a rate of 0.000 pprn.

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80 f/dtでほぼ一定であり、雑
菌数も10個/−でほぼ一定であった。
During this time, the alcohol concentration of the alcohol-containing liquid flowing out from the reactor was approximately constant at about 80 f/dt, and the number of miscellaneous bacteria was also approximately constant at 10/-.

特 許 出 願 人  新燃料油開発技術研究組合代 
理 人 弁理士 1) 中  政  浩15− 491−
Patent applicant New fuel oil development technology research association representative
Patent Attorney 1) Masahiro Naka 15- 491-

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
塩素酸及びとわらの塩のうち一種又は二種以上を含むP
!(25〜4;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、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、
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, P containing one or more of chlorous acid and towara salt
! (25-4; Alcohol fermentation method 2 using immobilized yeast, characterized by introducing the solution of 5 into a reactor. Alcohol fermentation is carried out by introducing a substrate solution into a reactor filled with immobilized yeast. a method characterized in that the substrate solution contains one or more of sulfurous acid, metabisulfite, hypochlorous acid, and salts thereof;
Alcohol fermentation method using immobilized yeast
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 true JPS59173086A (en) 1984-09-29
JPH0332359B2 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)

Cited By (4)

* 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
US6686194B1 (en) 1998-12-04 2004-02-03 Institut Pasteur Method and device for selecting accelerated proliferation of living cells in suspension
JP2008253154A (en) * 2007-03-30 2008-10-23 Mitsui Eng & Shipbuild Co Ltd Method for producing alcohol
JP2009261377A (en) * 2008-04-30 2009-11-12 Ecolog Recycling Japan:Kk Production method of ethanol

Citations (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

Patent Citations (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

Cited By (4)

* 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
US6686194B1 (en) 1998-12-04 2004-02-03 Institut Pasteur Method and device for selecting accelerated proliferation of living cells in suspension
JP2008253154A (en) * 2007-03-30 2008-10-23 Mitsui Eng & Shipbuild Co Ltd Method for producing alcohol
JP2009261377A (en) * 2008-04-30 2009-11-12 Ecolog Recycling Japan:Kk Production method of ethanol

Also Published As

Publication number Publication date
JPH0332359B2 (en) 1991-05-10

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