JPH04187079A - Rotary reactor - Google Patents
Rotary reactorInfo
- Publication number
- JPH04187079A JPH04187079A JP31579190A JP31579190A JPH04187079A JP H04187079 A JPH04187079 A JP H04187079A JP 31579190 A JP31579190 A JP 31579190A JP 31579190 A JP31579190 A JP 31579190A JP H04187079 A JPH04187079 A JP H04187079A
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- bag
- biological
- rotation
- substrate
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
- C12M23/14—Bags
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
- C12M27/06—Stirrer or mobile mixing elements with horizontal or inclined stirrer shaft or axis
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、生物反応および/または化学反応を効率よく
生せしめる装置として利用することができる回転式反応
装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a rotary reaction apparatus that can be used as an apparatus for efficiently producing biological and/or chemical reactions.
生物反応あるいは化学反応を生ぜしめる小型の装置の基
本構造は静置型、根盪型あるいは回転型の3種類が広く
用いられている。しかし、従来の装置は反応の動力学的
解析が反応槽内の低温度の基質の反応系に関して行われ
て来たことにより高濃度あるいは不溶性の基質の反応系
に対しては検討が未だ不十分である。Three types of basic structures are widely used for small-sized devices that produce biological or chemical reactions: stationary type, root type, and rotating type. However, with conventional devices, reaction kinetic analysis has been performed on reaction systems with low-temperature substrates in reaction vessels, so studies have not yet been conducted on reaction systems with high concentration or insoluble substrates. It is.
静置型としては三角コルベンあるいはビーカーなどに撹
拌子をいれて水平方向の回転運動により基質を撹拌し、
反応速度を高める反応系が一般的である。この系は溶媒
の極性あるいは腐食性などにかかわらず低廉な経費で反
応を行えるが、高粘度の系では撹拌子の回転速度が低下
してしまう。For the stationary type, a stirrer is placed in a triangular kolben or beaker, and the substrate is stirred by horizontal rotation.
Reaction systems that increase the reaction rate are common. This system allows the reaction to be carried out at low cost regardless of the polarity or corrosivity of the solvent, but in high viscosity systems the rotational speed of the stirrer decreases.
また、基質の比重が溶媒より小さい場合には基質が浮遊
してしまう欠点がある。。Furthermore, when the specific gravity of the substrate is lower than that of the solvent, there is a drawback that the substrate floats. .
振盪型としては試験管あるいは三角コルベンを固定して
恒温水槽または恒温室中で反応させる振盪培養機が広く
普及している。この系は振盪培養機の水平方向の往復運
動により基質を撹拌して反応速度を高める。しかし、前
者と同様に基質の比重が溶媒と異なる場合には基質が浮
遊あるいは沈降してしまう。また、高粘度の系では均質
化が困難である。As a shaking type, a shaking culture machine in which test tubes or triangular Kolben are fixed and reacted in a constant temperature water bath or a constant temperature room is widely used. This system uses horizontal reciprocating motion of a shaker incubator to agitate the substrate and increase the reaction rate. However, like the former, if the specific gravity of the substrate is different from that of the solvent, the substrate will float or settle. Furthermore, it is difficult to homogenize a high viscosity system.
回転型としては試験管あるいはサンプルチューブに密栓
をし、ローデークーなどで円運動などにより撹拌する方
式が普及している。この系は細胞培養など反応を穏やか
に進行させる場合に適している。しかし、前者と同様に
基質の比重が溶媒より小さい場合には基質が浮遊し、均
質化が図れない。また、密栓を施すた約、気体が発生す
る反応系には内部の圧力が上昇し反応液が漏洩する。さ
らに、装置は一般的に試料容器の保持装置と動力系統お
よびその制御部が一体的であるため装置全体を恒温室内
に設置する必要がある。しかし、恒温室は設備に高額の
費用を必要とする上、比熱の小さな空気を熱媒体として
いるため作業者の出入りなどで外気温の影響を受け、温
度が不安定になる欠点がある。As a rotary type, a method in which a test tube or a sample tube is tightly capped and stirred by circular motion using a rotary cooler is popular. This system is suitable for cases where reactions proceed slowly, such as in cell culture. However, like the former case, if the specific gravity of the substrate is lower than the solvent, the substrate will float and homogenization cannot be achieved. Furthermore, when the reaction system is sealed tightly, the internal pressure increases and the reaction liquid leaks. Furthermore, since the device generally includes a sample container holding device, a power system, and its control unit in one unit, the entire device must be installed in a constant temperature room. However, constant temperature rooms require high equipment costs, and because they use air, which has a low specific heat, as a heat medium, they are affected by the outside temperature as workers come and go, making the temperature unstable.
E発明が解決しようとする課題〕
本発明の目的は、反応系の粘度、比重あるいは発生気体
などにより従来の装置の利用が困難な場合の反応を進行
せし島る反応装置を提供することである。E Problems to be Solved by the Invention] An object of the present invention is to provide a reaction device that can proceed in cases where it is difficult to use conventional devices due to the viscosity, specific gravity, or generated gas of the reaction system. be.
本発明は上記の課題を解決するために開発された。以下
の特徴を有する生物反応および/または化学反応に適し
た装置である。即ち、生物あるいは化学物質の存在下で
基質に対する生物および化学反応を行わせる反応バッグ
と、反応バッグを取り付け基質の垂直方向の撹拌(上下
動)と磨砕により反応を昂進させる回転装置と、回転装
置を任意の方向および速度で回転させるための駆動装置
と、反応槽内の液温を一定に保つ恒温装置と、駆動装置
および恒温装置を制御する制御装置からなる回転式反応
装置である。The present invention was developed to solve the above problems. It is an apparatus suitable for biological and/or chemical reactions having the following characteristics. In other words, a reaction bag for carrying out biological and chemical reactions on a substrate in the presence of living organisms or chemical substances, a rotating device to which the reaction bag is attached and accelerating the reaction by vertical stirring (up and down movement) and grinding of the substrate, and a rotating This is a rotary reaction device that consists of a drive device that rotates the device in any direction and speed, a constant temperature device that keeps the liquid temperature in the reaction tank constant, and a control device that controls the drive device and the constant temperature device.
また、反応バッグは、チャック付プラスチック袋と、そ
の内部の撹拌・磨砕用粒子からなることを特徴とし、前
記回転装置は、アクリル樹脂製の円筒と、その裏面に反
応バッグをスプリングで押し付ける反応バッグ取り付け
棒と、駆動装置の回転運動を円筒に伝達する回転軸から
なることを特徴とする。Further, the reaction bag is characterized in that it consists of a plastic bag with a zipper and particles for stirring and grinding inside the bag, and the rotating device includes a cylinder made of acrylic resin and a reaction bag that presses the reaction bag against the back surface of the cylinder with a spring. It is characterized by consisting of a bag attachment rod and a rotating shaft that transmits the rotational movement of the drive device to the cylinder.
更に、前記駆動装置は、駆動用モーターと、その動力を
回転装置に伝達するための機構からなり、前記恒温装置
は、恒温水槽と循環ポンプから構成され、その制御装置
は、駆動装置の運動を制御するコンピューターおよびイ
ンターフェースと、回転装置を設置した反応槽内の液温
を制御する温度制御装置からなる。Further, the drive device includes a drive motor and a mechanism for transmitting its power to the rotating device, the constant temperature device includes a constant temperature water tank and a circulation pump, and the control device controls the movement of the drive device. It consists of a computer and an interface to control it, and a temperature control device to control the temperature of the liquid in the reaction tank equipped with a rotating device.
本発明が具備する機構により実現が可能な反応系は生物
および/または化学反応系一般にわたる。Reaction systems that can be realized by the mechanism provided by the present invention include biological and/or chemical reaction systems in general.
これらの反応において特に本発明で効果が明らかになっ
た反応は以下のとおりである。Among these reactions, the reactions that have been particularly effective in the present invention are as follows.
(1)浮遊あるいは沈降する基質を溶媒あるいは培地中
に分散できる。(1) Floating or settling substrates can be dispersed in a solvent or medium.
(2)粘度の高い条件下における反応の進行を維持でき
る。(2) Progress of the reaction can be maintained under conditions of high viscosity.
(3)反応バッグ内に気体を密封出来るため、生物反応
系において好気的あるいは嫌気的反応のいずれをも選択
できる。(3) Since gas can be sealed in the reaction bag, either aerobic or anaerobic reaction can be selected in the biological reaction system.
(4)基質の撹拌条件をコンピューターで制御できるた
め、その条件を穏やかな撹拌が必要な細胞培養から激し
い撹拌が必要なスラリー状の反応まで任意に再現性よく
設定できる。(4) Since the substrate stirring conditions can be controlled by a computer, the conditions can be arbitrarily set with good reproducibility, from cell culture requiring gentle stirring to slurry reactions requiring vigorous stirring.
(5)基質が疎剛な場合には、撹拌・磨砕用粒子により
物理的な磨砕を生せしめることが可能なため、試料を予
め微粉末に調製する必要が無い。(5) When the substrate is loose and rigid, it is possible to cause physical grinding using particles for stirring and grinding, so there is no need to prepare the sample into a fine powder in advance.
本発明の反応装置において、反応バッグ内の基質に対す
る生物あるいは化学物質を導入し、そして撹拌・磨砕用
粒子を投入した後、調製した気体を封入し、次いで密封
後回転装置に装着し、正・逆側方向に回転させながら生
物反応および/または化学反応を行わせる。In the reaction apparatus of the present invention, a biological or chemical substance is introduced to the substrate in the reaction bag, particles for stirring and grinding are introduced, the prepared gas is sealed, and then the bag is sealed and then installed in a rotating device. - Perform biological and/or chemical reactions while rotating in the opposite direction.
反応バッグは市販のチャック付プラスチック袋の開口部
をさらにポリシーラーて熱溶着して密封する。このた約
反応生成物あるいは培地の漏洩は皆無である。また、気
体が発生する場合には袋が膨張し、急激な内圧の上昇を
回避することが可能である。The reaction bag is made by sealing the opening of a commercially available plastic bag with a zipper by heat-welding it with polystyrene. Due to this, there is no leakage of reaction products or medium. Further, when gas is generated, the bag expands, making it possible to avoid a sudden increase in internal pressure.
本発明の回転装置は回転軸を中心として反応バッグを回
転させる。回転中に反応バッグは倒立するたt基質を含
む液相と気相が周期的に反転する。The rotation device of the present invention rotates the reaction bag around the rotation axis. During rotation, the reaction bag is inverted and the liquid phase containing the substrate and the gas phase are periodically reversed.
このため比重の大小に関係なく基質は培地中によく分散
させられる。また、スラリー状の培地に対しては比重の
大きなセラミック製あるいは金属製の撹拌・磨砕用粒子
を用いると内部の撹拌が効率よく行われる。反応バッグ
内では溶媒による基質の膨潤効果と撹拌・磨砕用粒子の
磨砕効果が相俟って疎剛な基質も反応を受けやすくなる
。Therefore, the substrate is well dispersed in the medium regardless of its specific gravity. Furthermore, for a slurry-like culture medium, internal stirring can be efficiently performed by using ceramic or metal stirring/grinding particles having a large specific gravity. In the reaction bag, the swelling effect of the substrate by the solvent and the grinding effect of the stirring/grinding particles combine to make even loose and rigid substrates susceptible to reaction.
駆動装置の運動を制御する制御装置は、コンピューター
の数値制御により緩慢な回転から高速回転まで任意に変
えることが可能である。本装置は特に低速回転条件下に
おいて微生物の生理活性を損なうことなく生物および化
学反応を昂進させることに好適である。The control device that controls the movement of the drive device can be arbitrarily changed from slow rotation to high speed rotation by computer numerical control. This device is particularly suitable for accelerating biological and chemical reactions without impairing the physiological activity of microorganisms under low-speed rotation conditions.
以下、本発明の特定の実施例を、その一実施態様を示す
図面に基づきより具体的に説明する。Hereinafter, specific embodiments of the present invention will be described in more detail based on drawings showing one embodiment thereof.
第1図は、生物反応および/または化学反応に適用した
回転式反応装置を示す断面図である。FIG. 1 is a sectional view showing a rotary reactor applied to biological and/or chemical reactions.
回転式反応装置1は、反応バッグ3を反応バッグ取り付
け棒6で円筒7に保持する回転装置を設置した培養槽2
と、駆動用モーター9からなる駆動装置と、恒温水槽1
0および循環ポンプ11からなる恒温装置と、コンピュ
ーター13及びその制御盤12からなる制御装置とによ
って構成される。The rotary reaction device 1 includes a culture tank 2 equipped with a rotation device that holds a reaction bag 3 in a cylinder 7 with a reaction bag attachment rod 6.
, a drive device consisting of a drive motor 9, and a constant temperature water tank 1
0 and a circulation pump 11, and a control device consisting of a computer 13 and its control panel 12.
反応バッグ3は、プラスチック袋の内部にガラスピーズ
、セラミックビーズあるいはステンレスポール製の撹拌
・磨砕用粒子4が封入されている。In the reaction bag 3, stirring/grinding particles 4 made of glass beads, ceramic beads, or stainless steel poles are sealed inside a plastic bag.
生物反応および/または化学反応については反応バッグ
3のチャックを開けてイノキニラムあるいは反応基質と
培地量たは溶媒を投入する。調製した気体を通気後チャ
ックを閉じ、さらにその上部の開口部を熱溶着して密封
する。その後、密封した反応バッグ3を回転装置に装着
しコンピュータ13を操作してそのプログラムにより駆
動用モーター9を回転させる。回転装置5は反応バッグ
3を正逆の両方向に周期的に回転させるがその過程で反
応バッグ3が倒立して撹拌・磨砕用粒子4が下部に落下
すると共に、液相と気相の位置が逆転し効率的に垂直方
向の撹拌と磨砕が起こり反応が昂進する。For biological reactions and/or chemical reactions, the reaction bag 3 is opened and the inoquinilum or reaction substrate and the amount of medium or solvent are added. After venting the prepared gas, the chuck is closed, and the upper opening is sealed by heat welding. Thereafter, the sealed reaction bag 3 is mounted on a rotating device, and the computer 13 is operated to rotate the drive motor 9 according to the program. The rotating device 5 periodically rotates the reaction bag 3 in both forward and reverse directions, but in the process, the reaction bag 3 is turned upside down and the particles 4 for stirring and grinding fall to the bottom, and the positions of the liquid phase and gas phase are changed. is reversed, and efficient vertical stirring and grinding occur, accelerating the reaction.
培養槽2の液温は検出器のサーミスターの抵抗変化を制
御盤内の温度コントローラーで感知する。The temperature of the liquid in the culture tank 2 is determined by the change in resistance of a thermistor of a detector using a temperature controller in the control panel.
水槽の加温はソリッドステートリレーを作動させて恒温
水素内10のヒーターで行う。The water tank is heated by 10 heaters inside the constant-temperature hydrogen tank by activating a solid-state relay.
第1図の回転式反応装置を用いて微生物の培養試験を行
いその性能評価を行った結果は以下のとおりである。A microorganism culture test was conducted using the rotary reaction apparatus shown in FIG. 1, and the performance was evaluated. The results are as follows.
第1図の装置において、乾草(オーチャード−番車)6
00g/日と濃厚飼料(新・乳牛17号二日本配合飼料
)300 g /日を10:00と22:00の1日2
回に分けて給与している成緬羊(コリゾール種♂、体重
約40kg)より、飼料給与8時間後にルーメンフィス
テルより採取したルーメン内容物の2重ガ−ゼ搾汁をイ
ノキニラムとして用いて生物反応試験を行なった。In the apparatus shown in Fig. 1, hay (orchard wheel) 6
00g/day and 300g/day of concentrated feed (new dairy cow No. 17 Nippon compound feed) 2 times a day at 10:00 and 22:00.
Biological reaction test using double gauze squeezed juice of rumen contents collected from rumen stent 8 hours after feeding from adult Burmese sheep (Coryzor type male, weighing approximately 40 kg), which are fed in divided doses, as Inokiniram. I did this.
金属微粒子として、0〜4μの鉄粉を50■ずつ、反応
バッグとして用いたポリエチレン製ビニール袋(85X
60mm)に入れたもの、および微粒子を入れないもの
を各々3袋ずつ用意した。As metal particles, 50 μ of iron powder of 0 to 4 μm were placed in a polyethylene plastic bag (85X) used as a reaction bag.
Three bags each were prepared, one containing the microparticles (60 mm) and the other containing no microparticles.
それぞれのビニール袋にルーメン搾汁10ccとガラス
ピーズ(粒径4.7〜5.6 mm) 20個を入れ、
CD2を充填した。次に、富士ポリシーラーを用いてビ
ニール袋にシールを行ない、39℃に保温された培養槽
内の回転装置にセットし、円筒を回転(正方向lrpm
で1.5回転、逆方向にlrp+nで1回転を交互に繰
り返す)させ、生物反応試験を開始した。Put 10 cc of rumen juice and 20 glass peas (particle size: 4.7 to 5.6 mm) into each plastic bag.
Filled with CD2. Next, seal the plastic bag using Fuji Polysiler, set it in a rotating device in a culture tank kept at 39℃, and rotate the cylinder (forward direction lrpm).
(alternately repeating 1.5 rotations in the opposite direction and 1 rotation in the opposite direction in lrp+n), and the biological reaction test was started.
試験開始時、0.5,1.2・4・8.12・16およ
び24時間後に、それぞれ微粒子育、無の各1袋からサ
ンプリングし、再びCO2を通気し、次いで密閉後試験
を行なった。At the start of the test, 0.5, 1.2, 4, 8, 12, 16, and 24 hours later, samples were taken from one bag each for microparticle growth and one without, aerated with CO2 again, and then tested after sealing. .
試験期間中の反応バッグ内のプロトシア数の変化を第2
図に、pHの変化を第3図に、揮発性脂肪酸(VFA)
濃度の変化を第4図に示す。The change in the number of protosia in the reaction bag during the test period was measured as a second
Figure 3 shows changes in pH, volatile fatty acids (VFA)
Figure 4 shows the change in concentration.
以上の結果より、回転式生物反応装置はルーメンと同様
の生物反応が行なわれることがわかる。From the above results, it can be seen that biological reactions similar to those in the rumen occur in the rotary biological reaction device.
なお、微粒子として鉄粉の代わりに酸化鉄(マグネタイ
ト)(平均粒径1p、飽和磁化9Qemu/ g )を
使用した場合でも、同様の生物反応が示された。Note that similar biological reactions were observed even when iron oxide (magnetite) (average particle size 1 p, saturation magnetization 9 Qemu/g) was used as the fine particles instead of iron powder.
次に本発明で開発した回転式反応装置における比重の重
い基質に対する撹拌装置については以下の実験を行って
評価を行った。実験は前述の培養実験と同様の系で行い
、酸化鉄(マグネタイト)を加えて嫌気性条件下で生育
する綿羊の反別胃内微生物を培養した。その結果、マグ
ネタイトは反応バッグの回転運動で分散し原生動物によ
く取り込まれた。培養終了後、培養液をスライドグラス
に移しスライドグラスの裏側に希土類磁石を置いて生理
食塩水で培養液を洗浄すると、マグネタイトを摂食した
多数の原生動物が磁力によりスライドグラス上に保持さ
れた。しかし、通常の振盪培養では、同様の操作でスラ
イド上に保持される原生動物が殆ど認められなかった。Next, the following experiment was conducted to evaluate the stirring device for a substrate with a heavy specific gravity in the rotary reaction apparatus developed in the present invention. The experiment was conducted in the same system as the culture experiment described above, and microorganisms in the rumen of cotton sheep that grow under anaerobic conditions were cultured with the addition of iron oxide (magnetite). As a result, the magnetite was dispersed by the rotational movement of the reaction bag and was well taken up by the protozoa. After culturing, the culture solution was transferred to a glass slide, a rare earth magnet was placed on the back side of the slide glass, and the culture solution was washed with physiological saline. Many protozoa that had ingested the magnetite were held onto the slide glass by magnetic force. . However, in normal shaking culture, almost no protozoa were observed on the slides using the same procedure.
したがって、振盪培養では比重の重いマグネタイトは沈
降したまま反応バッグ中に殆ど分散せず、原生動物は摂
食出来なかったものと考えられる。Therefore, it is considered that in the shaking culture, the magnetite with a heavy specific gravity remained precipitated and was hardly dispersed in the reaction bag, so that the protozoa could not eat it.
以上の例は微生物と基質の生物反応に関するものである
が、発明の装置は他の一般的な生物反応および/または
化学反応すなわち発酵、汚水処理あるいは有機および無
機の化学反応などにも応用が可能である。Although the above examples relate to biological reactions between microorganisms and substrates, the device of the invention can also be applied to other common biological and/or chemical reactions, such as fermentation, sewage treatment or organic and inorganic chemical reactions. It is.
本発明によれば、反応バッグの回転運動および内部の撹
拌・磨砕用粒子の効果で、浮遊あるいは沈降する基質を
培地中に分散できる回転式反応装置が提供される。基質
が練剤な場合には、物理的な磨砕を生せしめることが可
能となり、微粉末の基質でなくとも生物反応あるいは化
学反応に供することができるようになった。According to the present invention, a rotary reaction device is provided in which suspended or sedimented substrates can be dispersed in a medium by the rotational movement of a reaction bag and the effect of stirring/grinding particles inside. When the substrate is a paste, it has become possible to cause physical grinding, and it has become possible to apply it to biological or chemical reactions even if the substrate is not a fine powder.
また、反応バッグ内に気体を密封出来るため、生物反応
系において好気的あるいは嫌気的反応のいずれをも選択
できるようになり、実施例で述べたような綿羊の反別胃
内の偏性嫌気性の微生物の培養も容易に行うことが可能
になった。In addition, since the gas can be sealed in the reaction bag, it is now possible to select either an aerobic or anaerobic reaction in the biological reaction system. It has also become possible to easily cultivate sexually active microorganisms.
さらに、本装置は培地の撹拌条件をコンピューターで制
御するため穏やかな撹拌が可能になり強固な細胞壁を持
たない原生動物の維持に効果が認められた。Furthermore, since this device controls the stirring conditions of the culture medium using a computer, it is possible to perform gentle stirring, which has been shown to be effective in maintaining protozoa that do not have strong cell walls.
第1図は実施例の回転式反応装置を示す。第2図は生物
反応試験期間中における反応バッグ式反応槽内のプロト
シア数の変化を示し、第3図はそのpHの変化を示し、
そして第4図は揮発性脂肪酸(VFA)濃度の変化を示
す。
第1図中の符号は、それぞれ次の意味を有する。
2・・・培養槽、 3・・・反応バッグ、4・
・・撹拌・磨砕用粒子、5・・・回転装置、6・・・反
応バッグ取り付け棒、
7・・・円筒、 8・・・回転軸、9・・・
駆動用モーター、 10・・・恒温水槽、11・・・循
環ポンプ、 12・・・制御盤、13・・・コンピ
ューター。
第1 図
培養時間(時間)
口 対照+Fe
培養時間(時間)
口 対照十Fe
襄 3田FIG. 1 shows a rotary reactor according to an example. Figure 2 shows the change in the number of protosia in the reaction bag type reaction tank during the biological reaction test period, and Figure 3 shows the change in pH.
And FIG. 4 shows changes in volatile fatty acid (VFA) concentration. The symbols in FIG. 1 have the following meanings. 2... Culture tank, 3... Reaction bag, 4...
...Particles for stirring/grinding, 5...Rotating device, 6...Reaction bag attachment rod, 7...Cylinder, 8...Rotating shaft, 9...
Drive motor, 10... constant temperature water tank, 11... circulation pump, 12... control panel, 13... computer. Figure 1 Culture time (hours) Control + Fe Culture time (hours) Control 10 Fe 3 fields
Claims (1)
反応および/または化学反応を行わせる反応バッグと、
反応バッグを取り付け基質の撹拌と磨砕により反応を昂
進させる回転装置と、回転装置を任意の方向および速度
で回転させるための駆動装置と、反応槽内の液温を一定
に保つ恒温装置と、駆動装置および恒温装置を制御する
制御装置からなる回転式反応装置。 2、反応バッグが、チャック付プラスチック袋と、その
内部の撹拌・磨砕用粒子からなる請求項1記載の回転式
反応装置。 3、回転装置が、アクリル樹脂製の円筒と、その裏面に
反応バッグをスプリングで押し付ける反応バッグ取り付
け棒と、駆動装置の回転運動を円筒に伝達する回転軸か
らなる請求項1または2記載の回転式反応装置。 4、駆動装置が、駆動用モーターと、その動力を回転装
置に伝達するための機構からなる請求項1、2または3
記載の回転式反応装置。 5、恒温装置が、恒温水槽と循環ポンプからなる1、2
、3または4記載の回転式反応装置。 6、制御装置が、駆動装置の運動を制御するコンピュー
ターおよびインターフェースと、回転装置を設置した反
応槽内の液温を制御する温度制御装置からなる請求項1
、2、3、4または5記載の回転式反応装置。[Claims] 1. A reaction bag for carrying out a biological reaction and/or a chemical reaction on a substrate in the presence of a biological or chemical substance;
A rotation device to which a reaction bag is attached and accelerates the reaction by stirring and grinding the substrate, a drive device to rotate the rotation device in any direction and speed, and a constant temperature device to keep the liquid temperature in the reaction tank constant. A rotary reactor consisting of a drive device and a control device that controls a constant temperature device. 2. The rotary reaction apparatus according to claim 1, wherein the reaction bag comprises a plastic bag with a zipper and particles for stirring and grinding inside the bag. 3. The rotation according to claim 1 or 2, wherein the rotation device comprises a cylinder made of acrylic resin, a reaction bag attachment rod that presses the reaction bag against the back surface of the cylinder with a spring, and a rotation shaft that transmits the rotational movement of the drive device to the cylinder. formula reactor. 4. Claim 1, 2 or 3, wherein the drive device comprises a drive motor and a mechanism for transmitting its power to the rotating device.
Rotary reactor as described. 5. The constant temperature device consists of a constant temperature water tank and a circulation pump 1, 2
, 3 or 4. The rotary reactor according to . 6. Claim 1, wherein the control device comprises a computer and an interface that control the movement of the drive device, and a temperature control device that controls the temperature of the liquid in the reaction tank in which the rotating device is installed.
, 2, 3, 4 or 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31579190A JPH04187079A (en) | 1990-11-22 | 1990-11-22 | Rotary reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31579190A JPH04187079A (en) | 1990-11-22 | 1990-11-22 | Rotary reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04187079A true JPH04187079A (en) | 1992-07-03 |
Family
ID=18069600
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP31579190A Pending JPH04187079A (en) | 1990-11-22 | 1990-11-22 | Rotary reactor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04187079A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100365379B1 (en) * | 2000-07-27 | 2002-12-18 | 삼성종합화학주식회사 | A Reactor for Manufacture of a Chemicals |
-
1990
- 1990-11-22 JP JP31579190A patent/JPH04187079A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100365379B1 (en) * | 2000-07-27 | 2002-12-18 | 삼성종합화학주식회사 | A Reactor for Manufacture of a Chemicals |
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