JPS60256375A - Bioreactor - Google Patents
BioreactorInfo
- Publication number
- JPS60256375A JPS60256375A JP11239484A JP11239484A JPS60256375A JP S60256375 A JPS60256375 A JP S60256375A JP 11239484 A JP11239484 A JP 11239484A JP 11239484 A JP11239484 A JP 11239484A JP S60256375 A JPS60256375 A JP S60256375A
- Authority
- JP
- Japan
- Prior art keywords
- enzyme
- active element
- reaction active
- immobilized
- passage
- 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
Links
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
Description
【発明の詳細な説明】
(イ)産業上の利用分野
本発明は、酵素や菌類等の触媒作用を利用して、種々の
化学反応を促進する場合に好適に使用できるバイオリア
クタに関するものである。[Detailed description of the invention] (a) Industrial application field The present invention relates to a bioreactor that can be suitably used to promote various chemical reactions by utilizing the catalytic action of enzymes, fungi, etc. .
(ロ)従来技術
従来の/ヘイオリアクタは、タンク状の容器の中に、酵
素またはこれを生成する菌体を固定化したカラム等を充
填しておき、この容器内に反応させるべき溶液を導入し
て前記酵素に順次接触させ得るようにしたものが一般的
である。ところが、このような構成のものは、酵素が触
媒作用をなすのに最も適した温度を確保するために、処
理すべき溶液全体の温度をコントロールしなければなら
ないが、酵素が働く際の熱等の影響を受けるため最適温
度を維持するのはきわめて難かしい。そのため、酵素が
高温になってその活性が悪化したり。(b) Prior art In a conventional/halogen reactor, a tank-shaped container is filled with a column etc. in which enzymes or bacteria that produce the enzymes are immobilized, and a solution to be reacted is introduced into this container. It is common that the enzyme is brought into contact with the enzyme in sequence. However, with this type of structure, the temperature of the entire solution to be treated must be controlled in order to ensure the most suitable temperature for the enzyme to perform its catalytic action, but the temperature of the entire solution to be treated must be controlled. It is extremely difficult to maintain the optimum temperature because of the influence of As a result, the enzyme becomes hot and its activity deteriorates.
温度条件が不当に変動して生成物の品質にばらつきが生
じるという不都合を招き易い。Undue fluctuations in temperature conditions can easily lead to variations in product quality.
(ハ)目的
本発明は、このような事情に着目してなされたもので、
反応流体と接触し得る位置に固定化された酵素等の微生
物系反応活性要素の温度条件を簡単かつ確実に制御する
ことが可能であり、該反応活性要素の機能を十分にかつ
安定した状態で発揮させることができるバイオリアクタ
を提供することを目的とする。(c) Purpose The present invention was made with attention to such circumstances,
It is possible to easily and reliably control the temperature conditions of microbial reaction active elements such as enzymes that are immobilized in positions where they can come into contact with the reaction fluid, and to maintain the functions of the reaction active elements in a sufficient and stable state. The purpose is to provide a bioreactor that can exhibit the following effects.
(ニ)構成
本発明は、かかる目的を達成するために、第1の通路に
反応流体を流通させるとともに該通路に隣接する第2の
通路に熱媒体を流し得るように構成した熱交換器と、こ
の熱交換器の第1の通路に設けた熱交換用のプレートフ
ィンに固定化した微生物系反応活性要素とを具備してな
るものにしたことを特徴とする。(D) Structure In order to achieve the above object, the present invention provides a heat exchanger configured to allow a reaction fluid to flow through a first passage and to allow a heat medium to flow through a second passage adjacent to the passage. The heat exchanger is characterized in that it includes a microbial reaction active element immobilized on a plate fin for heat exchange provided in the first passage of the heat exchanger.
(ホ)実施例 以下1本発明の一実施例を図面を参照して説明する。(e) Examples An embodiment of the present invention will be described below with reference to the drawings.
第1図は、本発明に係るバイオリアクタの全体を示す斜
視図である。このバイオリアクタは、熱交換器1と、こ
の熱交換器1のプレートフィン2に固定化した微生物系
反応活性要素、例えば、酵素3とを具備してなる。詳述
すれば、熱交換器1は、アルミニウム製の仕切板4と、
プレートフィン2.3とを交互に積層固着してなるプレ
ートフィン形のもので、例えば、偶数段目に形成され一
側面に開口する第1の通路7に反応流体たる適宜な溶液
Aを流通させるとともに、奇数段目に形成され他側面に
開口する第2の通路8に熱媒体Bを流し得るようになっ
ている。プレートフィン2.6は例えば第2図に示すよ
うに、一枚の薄板にプレス加工を施すことによって作ら
れたもので、その上面2a、6aと下面2b、6bとを
前記仕切板4にロー付または拡散接合により接合させて
いる。なお、前記第1の通路7に介設yれるプレートフ
ィン2の表面部2Cには、多孔質陽極酸化皮膜処理(ア
ノダイズ処理)を施すことによって、規則正しい多数の
微小孔9を形成してあ 、る。そして、これらの微小孔
9内に酵素3を吸着 1させ固定化している。多孔質陽
極酸化皮膜処理を施す場合、リン酸等を電解液と1〜で
使用しており、それによって前記各微小孔9の径dを、
例えば、1100n程度のものにしている。FIG. 1 is a perspective view showing the entire bioreactor according to the present invention. This bioreactor comprises a heat exchanger 1 and a microbial reaction active element, such as an enzyme 3, immobilized on plate fins 2 of the heat exchanger 1. To be more specific, the heat exchanger 1 includes an aluminum partition plate 4,
The plate fin type is formed by alternately stacking and fixing plate fins 2 and 3, and for example, a suitable solution A as a reaction fluid is passed through the first passage 7 formed in an even number of stages and opening on one side. At the same time, the heat medium B can be allowed to flow through second passages 8 formed at odd-numbered stages and open to the other side. For example, as shown in FIG. 2, the plate fin 2.6 is made by pressing a single thin plate, and its upper surfaces 2a, 6a and lower surfaces 2b, 6b are rolled onto the partition plate 4. They are bonded by bonding or diffusion bonding. Note that a large number of regular micropores 9 are formed on the surface portion 2C of the plate fin 2 interposed in the first passage 7 by applying a porous anodic oxide film treatment (anodization treatment). Ru. The enzyme 3 is adsorbed and immobilized within these micropores 9. When performing porous anodic oxide film treatment, phosphoric acid or the like is used in combination with an electrolytic solution, whereby the diameter d of each micropore 9 is
For example, it is set to about 1100n.
このような構成のものであれば 第1の通路7を液通ず
る溶液Aが、該通路7中のプレートフィン2に固定化し
た酵素3に接触することになる。With such a configuration, the solution A passing through the first passage 7 comes into contact with the enzyme 3 immobilized on the plate fin 2 in the passage 7.
そのため、溶液Aの種類および促進すべき反応に対応す
る酵素3を逮択して前記プレートフィン2に画定化して
おけば、バイオリアクタとしての機能が発揮されるもの
である。しかも、このものは、第2の通路8を流れる熱
媒体Bの熱的影響を最も受け易いプレートフィン2に酵
素3を固定化している。そのため、酵素3自体の温度条
件を最適な値に維持することが容易であり、酵素3の触
媒作用を最大限に引き出すことが可能となる。具体的に
は、酵素3が働く際の熱は、直接プレートフィン2を介
して熱媒体B側へ取り出すことができるため、高温では
活性が悪化する酵素3でも容易に活動を引き出すことが
できる。また、酵素3の働く温度条件により生成物の品
質が変化する場合でも、一定温度の熱媒体Bを第2の通
路8に流通させておきさえすれば1品質の安定化を図る
ことかできる。また、必要なら、酵素3の活動温度を、
前記熱媒体Bの温度コントロールにより変化させるよう
なことも、簡単かつ確実に行なうことができる。Therefore, if enzymes 3 corresponding to the type of solution A and the reaction to be promoted are selected and defined in the plate fins 2, the function as a bioreactor will be exhibited. Moreover, in this device, the enzyme 3 is immobilized on the plate fin 2, which is most susceptible to the thermal influence of the heat medium B flowing through the second passage 8. Therefore, it is easy to maintain the temperature conditions of the enzyme 3 itself at an optimal value, and it is possible to maximize the catalytic action of the enzyme 3. Specifically, the heat generated when the enzyme 3 works can be taken out directly to the heat medium B side through the plate fins 2, so that even the enzyme 3, whose activity deteriorates at high temperatures, can be easily activated. Further, even if the quality of the product changes depending on the temperature conditions under which the enzyme 3 operates, the quality can be stabilized as long as the heat medium B at a constant temperature is allowed to flow through the second passage 8. In addition, if necessary, the activity temperature of enzyme 3,
It is also possible to change the temperature of the heat medium B easily and reliably.
なお、プレートフィンに固定化する微生物系反応活性要
素は、酵素に限らず、各種の菌類等であってもよい。Note that the microbial reaction active element to be immobilized on the plate fin is not limited to enzymes, and may be various types of fungi.
また、微生物系反応活性要素をプレートフィンに固定化
する方法も、前記のものに限られないのは勿論であり、
例えば、プレートフィンの表面に高分子材料を接着また
は溶着させ、これら高分子の?さまに酵素等の微生物系
反応活性要素を固定化するようにしてもよい。Furthermore, it goes without saying that the method for immobilizing the microbial reaction active element on the plate fin is not limited to the above method.
For example, by adhering or welding polymeric materials to the surface of plate fins, what about these polymeric materials? Alternatively, microbial reaction active elements such as enzymes may be immobilized.
さらに、熱交換器内における反応流体および熱媒体の流
れ方向は、パラレルフローでもクロスフローでもよ(、
また、反応流体を折り返し流すようにしてもよい。Furthermore, the flow direction of the reaction fluid and heat medium in the heat exchanger may be parallel flow or cross flow (
Alternatively, the reaction fluid may be turned around.
(へ)効果
本発明は、以1−のような構成であるから、反応流体と
接触し得る位置に固定化された酵素等の微生物系反応活
性要素の温度条件を簡単かつ確実に制御することが可能
であり、該反応活性要素の機能を十分にかつ安定した状
態で発揮させることができるバイオリアクタを提供でき
るものである。(f) Effects Since the present invention has the configuration as described in 1- below, it is possible to easily and reliably control the temperature conditions of microbial reaction active elements such as enzymes immobilized at positions where they can come into contact with reaction fluids. It is possible to provide a bioreactor in which the functions of the reaction active elements can be fully and stably exhibited.
図面は本発明の一実施例を示し、第1図は斜視図、第2
図は分解した斜視図、第3図はプレートフィンの表面部
分を示す拡大断面図である。
1・・・熱交換器
21@プレートフイン
3・・・微生物系反応活性要素(酵素)7・・1第1の
通路
81・第2の通路
繁 A・・・反応流体(溶液。
B・・・熱媒体
第1図
第2図 第3図The drawings show one embodiment of the present invention, with the first figure being a perspective view and the second figure being a perspective view.
The figure is an exploded perspective view, and FIG. 3 is an enlarged sectional view showing the surface portion of the plate fin. 1... Heat exchanger 21 @ plate fin 3... Microbial reaction active element (enzyme) 7... 1 First passage 81/Second passage A... Reaction fluid (solution. B...・Heating medium Figure 1 Figure 2 Figure 3
Claims (4)
路に隣接する第2の通路に熱媒体を流し得るように構成
した熱交換器と、この熱交換器の第1の通路に設けた熱
交換用のプレー)・フィンに固定化した微生物系反応活
性要素とを具備してなることを特徴とするバイオリアク
タ。(1) A heat exchanger configured to allow a reaction fluid to flow through a first passage and a heat medium to flow through a second passage adjacent to the passage, and a heat exchanger provided in the first passage of the heat exchanger. A bioreactor comprising a heat exchange plate) and a microbial reaction active element immobilized on fins.
する菌体である特許請求の範囲第1項記載の/買オリア
クタ。(2) #The bioreactor according to claim 1, wherein the biological reaction active element is an enzyme or a bacterial cell that produces the enzyme.
理を施したプレートフィンの表面部に直接固定化されて
いることを特徴とする特許請求の範囲第1項または第2
項記載のバイオリアクタ。(3) Claim 1 or 2, characterized in that the microbial reaction active element is directly immobilized on the surface of the plate fin that has been treated with a porous anodic oxide film.
Bioreactor as described in Section.
に付着させた高分子材料に吸着固定させであることを特
徴とする特許請求の範囲第1項または第2項記載のバイ
オリアクタ。(4) #The bioreactor according to claim 1 or 2, wherein the biological reaction active element is adsorbed and fixed to a polymeric material attached to the surface of the plate fin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11239484A JPS60256375A (en) | 1984-05-31 | 1984-05-31 | Bioreactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11239484A JPS60256375A (en) | 1984-05-31 | 1984-05-31 | Bioreactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60256375A true JPS60256375A (en) | 1985-12-18 |
| JPH0586180B2 JPH0586180B2 (en) | 1993-12-10 |
Family
ID=14585563
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11239484A Granted JPS60256375A (en) | 1984-05-31 | 1984-05-31 | Bioreactor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60256375A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4937196A (en) * | 1989-08-18 | 1990-06-26 | Brunswick Corporation | Membrane bioreactor system |
| WO1994001529A1 (en) * | 1992-07-01 | 1994-01-20 | Keiichi Katoh | Ceramic heating/cooling device |
| AU665657B2 (en) * | 1992-07-01 | 1996-01-11 | Keiichi Katoh | Ceramic device for heating or cooling |
| JP2010175245A (en) * | 2000-07-28 | 2010-08-12 | Honda Motor Co Ltd | Multi-purpose micro-channel micro-component |
| JP2010226975A (en) * | 2009-03-26 | 2010-10-14 | Fujifilm Corp | Cell culture membrane |
-
1984
- 1984-05-31 JP JP11239484A patent/JPS60256375A/en active Granted
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4937196A (en) * | 1989-08-18 | 1990-06-26 | Brunswick Corporation | Membrane bioreactor system |
| WO1994001529A1 (en) * | 1992-07-01 | 1994-01-20 | Keiichi Katoh | Ceramic heating/cooling device |
| AU665657B2 (en) * | 1992-07-01 | 1996-01-11 | Keiichi Katoh | Ceramic device for heating or cooling |
| EP0603411B1 (en) * | 1992-07-01 | 1998-08-19 | KATOH, Keiichi | Ceramic heating/cooling device |
| JP2010175245A (en) * | 2000-07-28 | 2010-08-12 | Honda Motor Co Ltd | Multi-purpose micro-channel micro-component |
| JP2010226975A (en) * | 2009-03-26 | 2010-10-14 | Fujifilm Corp | Cell culture membrane |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0586180B2 (en) | 1993-12-10 |
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