JPS60234585A - Method and apparatus for membrane-transmission fermentation or reaction - Google Patents

Method and apparatus for membrane-transmission fermentation or reaction

Info

Publication number
JPS60234585A
JPS60234585A JP9080184A JP9080184A JPS60234585A JP S60234585 A JPS60234585 A JP S60234585A JP 9080184 A JP9080184 A JP 9080184A JP 9080184 A JP9080184 A JP 9080184A JP S60234585 A JPS60234585 A JP S60234585A
Authority
JP
Japan
Prior art keywords
fermentation
membrane
liquid
yeast
reaction
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.)
Pending
Application number
JP9080184A
Other languages
Japanese (ja)
Inventor
Shiro Nagai
史郎 永井
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP9080184A priority Critical patent/JPS60234585A/en
Publication of JPS60234585A publication Critical patent/JPS60234585A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To obtain fermented liquid or reacted liquid in a short time, without causing adverse effect to the microbial cell, by passing the feed liquid for fermentation or reaction in one direction through a membrane or a tube prepared by mixing living microbial cell or enzyme with an immobilization carrier and a porous substance. CONSTITUTION:Living microbial cells or enzyme cultured in a culture liquid composed of glucose, peptone, yeast extract and water (e.g. Saccharomyces cerevisiae) are mixed with an immobilization carrier (e.g. K-carrageenan, aluminum alginate, etc.) and a porous substance (e.g. celite 545), and the mixture is formed to a membrane or a tube. The membrane, etc. is inserted between a pair of metal meshes having opening of about 1mm. and placed in a cylindrical bioreactor to obtain an immobilized yeast tank. The liquid for fermentation is sent from the feed tank 3 to the yeast tank under the nitrogen pressure of about 0.2kg/cm<2> applied by the nitrogen bomb 2 via the pressure regulator 1, and passed through the yeast layer with a residence time of about 2hr to complete the fermentation. The obtained product (e.g. alcohol) and CO2 are taken out of the reactor through the bottom.

Description

【発明の詳細な説明】 本発明は、膜通過型究明又は反応方法と装置に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a transmembrane investigation or reaction method and apparatus.

より詳細に言えば、本発明は、生菌体又は酵素を多孔質
物質と固定化担体(例えばに−カラギーナン、アルギン
酸アルミニウム等)とを混合し、膜又はチューブを作り
、その膜又はチューブの一方向から発酵用の液又は反応
用の液を通すことにより、目的とする発酵液又゛は反応
液を得る方法と装置に関するものCある。
More specifically, the present invention involves mixing viable bacterial cells or enzymes with a porous material and an immobilization carrier (for example, carrageenan, aluminum alginate, etc.) to form a membrane or tube, and then disposing of one part of the membrane or tube. C relates to a method and apparatus for obtaining a desired fermentation liquid or reaction liquid by passing the fermentation liquid or reaction liquid from the direction.

従来、固定化微生物や固定化酵素は、K−カラギ一ナン
やアルギン酸カルシウム等の固定化担体と菌体又は酵素
を混合し、1〜3mm程度の粒子を作り、充填塔や流動
層に入れて使用していた。
Conventionally, immobilized microorganisms and immobilized enzymes are produced by mixing microbial cells or enzymes with an immobilizing carrier such as K-carrageenan or calcium alginate to form particles of about 1 to 3 mm, and then placing them in a packed tower or fluidized bed. I was using it.

従来の方法では微生物や酵素は粒子の中又は表面に固定
化されているので、発酵液や反応液は粒子の中にある菌
体や酵素に粒内拡散でもって浸透して菌体又は酵素と接
触しなければ反応が進まないし、反応したものが粒子か
ら再び拡散でもって粒子の外部に出てくる必要がする。
In conventional methods, microorganisms and enzymes are immobilized inside or on the surface of the particles, so the fermentation solution or reaction solution penetrates the microorganisms and enzymes in the particles through intragranular diffusion and converts them into microorganisms or enzymes. If there is no contact, the reaction will not proceed, and the reacted substances must diffuse out of the particles again.

その為に反応が遅(なっている。That's why the reaction is slow.

本発明は、このような欠点を克服する方法及び装置につ
いて種々研究した結果、菌体又は酵素を固定化する際に
多孔質物質を混合し、平膜やチューブにし、発酵液又は
反応液を強制的に通過させることにより短時間で発酵又
は反応を終了に近くもっていけることを発見した。
As a result of various research into methods and devices to overcome these drawbacks, the present invention was developed by mixing porous materials when immobilizing bacterial cells or enzymes, forming a flat membrane or tube, and forcing the fermentation liquid or reaction liquid. We have discovered that by passing the mixture through the medium, the fermentation or reaction can be brought to near completion in a short period of time.

次に本発明の実施例として菌体として酵母を使用したア
ルコール光醇を示す。酵母はS a c e rvis
iaeを用いた。酵母はグルコース、ペプトン、酵母エ
キスと水とを混ぜた液で培養したその後に、K−カラギ
ーナンとローカストビーンを混ぜ、それに多孔質として
セライト545を入れて、図1に示したように直径26
111111の円筒のバイオリアクターに1mm目の金
網を入れて、今発明の膜を入れて、その上にまたIm’
m目の金網でおさえた。発酵液は上から供給してやり膜
を通過しやすいように022kg/dの圧をかけアルコ
ール発酵では生産物として、アルコールだけではなく、
炭酸ガスも生産されるが多孔質の物質を通して供給液と
は反対方向に出ていくことができた。
Next, as an example of the present invention, an alcoholic sake using yeast as a bacterial cell will be shown. Yeast is Sacervis
iae was used. Yeast was cultured in a mixture of glucose, peptone, yeast extract, and water. After that, K-carrageenan and locust bean were mixed, and Celite 545 was added to make it porous.
Put a 1 mm wire mesh into the cylindrical bioreactor of No. 111111, put the membrane of the present invention in it, and put Im' again on top of it.
I held it down with the m-th wire mesh. The fermentation liquid is supplied from above and a pressure of 0.22 kg/d is applied to make it easier to pass through the membrane.In alcohol fermentation, not only alcohol is produced, but also alcohol.
Carbon dioxide gas was also produced, but could exit through the porous material in the opposite direction to the feed liquid.

図2に示したように長時間の連続運転を行うとアルコー
ル生産速度は5日目位から一定となり安定しているが、
膜を通過するための圧力は少しづつ上げる必要があった
。酵母菌数が最初の状態より増殖して8 X 10q 
個7m1−ゲルという非常に多数になってきたためと思
われる。アルコール生成速度は滞留時間約2時間で、図
2に示した結果が得られた。これは従来の固定化酵母(
粒子型)によるアルコール発酵の滞留時間10〜12時
間の5倍近い生成速度であり、装置の小型化ができる乙
とを示している。
As shown in Figure 2, when continuous operation is performed for a long time, the alcohol production rate becomes constant and stable from about the 5th day.
The pressure had to be increased gradually to pass through the membrane. The number of yeast bacteria has increased from the initial state to 8 x 10q
This is probably due to the fact that the number of gels has increased to 7 ml per gel. The rate of alcohol production was approximately 2 hours in residence time, and the results shown in FIG. 2 were obtained. This is the conventional immobilized yeast (
The production rate is nearly five times that of the residence time of 10 to 12 hours in alcoholic fermentation using particle type), and it shows that the apparatus can be downsized.

実施例2.として図3に示した装置を用い、膜は前の実
施例と同じようにに一カラギナンとセライト545を混
合し2層並へた。この装置では図4に示したように1ケ
月の連続運転が行われた。
Example 2. Using the apparatus shown in FIG. 3, a membrane was prepared by mixing carrageenan and Celite 545 and forming two layers in the same manner as in the previous example. This device was operated continuously for one month as shown in Figure 4.

以上の実施例からも分かるように、膜通過型の発酵又は
反応法及び装置は有効で、従来の装置に比較して、コン
バクとにすることが出来た。一つの理由として糖から出
来るエタノールはそれ自身が菌に悪影響を与えるが、こ
の膜通過型であれば生産されたエタノールはすぐに排出
されて菌体に影響を与えにくいと考えられる。
As can be seen from the above examples, the membrane-passing fermentation or reaction method and device were effective and were able to produce a more compact product compared to conventional devices. One reason is that ethanol produced from sugar itself has a negative effect on bacteria, but with this membrane-passing type, the produced ethanol is immediately excreted and is thought to be less likely to affect the bacteria.

従来の方法では液体中に菌又は固定化菌体が浸かってい
て発酵終了まで生産物の影響を受けているので、菌体に
悪影響を与えてるような物質は非常に生産しに(かった
。しかし、この方法であれば、菌体に阻害を与えるよう
な物質をも生産出来る可能性をもっていると考えられる
In conventional methods, bacteria or immobilized bacterial cells are immersed in liquid and are affected by the product until the end of fermentation, so it is very difficult to produce substances that may have a negative effect on the bacterial cells. However, it is thought that this method has the potential to produce substances that inhibit bacterial cells.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は円筒型の膜通過型実験装置 1・・・圧力調節器 2・・・チッソボンベ 3・・・原料槽 第2図は運転結果 生成エタノールと残グルコースと膜通過圧損を示した。 第3図は二層型装置 第4図は二層型装置の運転結果 第 1 図 友練かゝ^ 第 2 四 遍軌昨尚 (h) 第 、3 図 #斜 瓦 固)1べ Figure 1 shows a cylindrical membrane-passing experimental device. 1...Pressure regulator 2...Chisso cylinder 3... Raw material tank Figure 2 shows the operation results. The produced ethanol, residual glucose, and transmembrane pressure drop are shown. Figure 3 shows a two-layer device. Figure 4 shows the operational results of the two-layer device. Figure 1 Friendship huh? 2nd 4th Hengeki Sensho (h) Figures 3 and 3 #Slanted tile Hard) 1be

Claims (2)

【特許請求の範囲】[Claims] (1)生菌体又は酵素と多孔質物質と固定化担体を混合
し膜又はチューブを作り、発酵又は反応液を一方向に通
過させることを特徴とする処理方法。
(1) A treatment method characterized by mixing viable bacterial cells or enzymes, a porous substance, and an immobilization carrier to form a membrane or tube, and passing the fermentation or reaction solution in one direction.
(2)生菌体又は酵素と多孔質物質と固定化担体を混合
し、膜又はチューブを作り、発酵又は反応液を一方向に
通過させることを特徴とする発酵又は反応装置。
(2) A fermentation or reaction device characterized by mixing living bacterial cells or enzymes, a porous substance, and an immobilization carrier to form a membrane or tube, through which a fermentation or reaction solution passes in one direction.
JP9080184A 1984-05-08 1984-05-08 Method and apparatus for membrane-transmission fermentation or reaction Pending JPS60234585A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9080184A JPS60234585A (en) 1984-05-08 1984-05-08 Method and apparatus for membrane-transmission fermentation or reaction

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9080184A JPS60234585A (en) 1984-05-08 1984-05-08 Method and apparatus for membrane-transmission fermentation or reaction

Publications (1)

Publication Number Publication Date
JPS60234585A true JPS60234585A (en) 1985-11-21

Family

ID=14008689

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9080184A Pending JPS60234585A (en) 1984-05-08 1984-05-08 Method and apparatus for membrane-transmission fermentation or reaction

Country Status (1)

Country Link
JP (1) JPS60234585A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62198383A (en) * 1986-02-26 1987-09-02 Ngk Insulators Ltd Bioreactor element and its production
JPS62269680A (en) * 1986-05-16 1987-11-24 Chiyoda Seisakusho:Kk Cultivation apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62198383A (en) * 1986-02-26 1987-09-02 Ngk Insulators Ltd Bioreactor element and its production
JPS62269680A (en) * 1986-05-16 1987-11-24 Chiyoda Seisakusho:Kk Cultivation apparatus

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