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JPH0657146B2 - Compartment rotating drum bioreactor - Google Patents
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JPH0657146B2 - Compartment rotating drum bioreactor - Google Patents

Compartment rotating drum bioreactor

Info

Publication number
JPH0657146B2
JPH0657146B2 JP63040051A JP4005188A JPH0657146B2 JP H0657146 B2 JPH0657146 B2 JP H0657146B2 JP 63040051 A JP63040051 A JP 63040051A JP 4005188 A JP4005188 A JP 4005188A JP H0657146 B2 JPH0657146 B2 JP H0657146B2
Authority
JP
Japan
Prior art keywords
tank
bioreactor
rotary drum
immobilized biocatalyst
compartment
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
JP63040051A
Other languages
Japanese (ja)
Other versions
JPH01215277A (en
Inventor
山口  剛
修明 大田
光 末永
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.)
Fukuoka Prefectural Government
Original Assignee
Fukuoka Prefectural Government
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 Fukuoka Prefectural Government filed Critical Fukuoka Prefectural Government
Priority to JP63040051A priority Critical patent/JPH0657146B2/en
Publication of JPH01215277A publication Critical patent/JPH01215277A/en
Publication of JPH0657146B2 publication Critical patent/JPH0657146B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/06Nozzles; Sprayers; Spargers; Diffusers
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/18Apparatus specially designed for the use of free, immobilized or carrier-bound enzymes
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/34Internal compartments or partitions
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02Stirrer or mobile mixing elements
    • C12M27/06Stirrer or mobile mixing elements with horizontal or inclined stirrer shaft or axis
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
    • C12M41/18Heat exchange systems, e.g. heat jackets or outer envelopes
    • C12M41/22Heat exchange systems, e.g. heat jackets or outer envelopes in contact with the bioreactor walls

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  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Genetics & Genomics (AREA)
  • General Health & Medical Sciences (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Sustainable Development (AREA)
  • Biomedical Technology (AREA)
  • Molecular Biology (AREA)
  • Clinical Laboratory Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は微生物あるいは酵素を適当な担体に保持させた
固定化生体触媒を利用して有用物質を生産するバイオリ
アクターに関するものである。
TECHNICAL FIELD The present invention relates to a bioreactor for producing a useful substance by using an immobilized biocatalyst in which a microorganism or an enzyme is supported on a suitable carrier.

「従来の技術」 従来型のバイオリアクターでは微生物、酵素の固定化方
法として担体結合法、架橋法、包括法、あるいはこれら
を組み合わせた複合法等が用いられ、これらの方法によ
り得られる固定化生体触媒の粒状、塊状、フイルム状、
シート状などの固定化形態により充填層型、流動層型、
膜型、管型、板型等のリアクターに使いわけて利用して
いる。又回転板方式も数機種開発されており高い攪拌効
率、圧力損失が少いこと、円板の着脱を容易にして生体
触媒の反応活性を維持して、生成物収率を高めることが
できる等の点でバイオリアクターとして優れた特質を持
つている。しかしこの回転円板式バイオリアクターでは
円板上に菌体を着床させるために使用可能微生物に制限
がある事、発酵を一室で実施するため固定化生体触媒の
活性が一様に低下し、活性を維持し製品濃度を一定に保
つために多数の回転円板を必要とし、その結果、設置面
積が予想外に大きくなる事、同軸上に並設した回転円板
間の間隔が施隘となり円板間隙に増殖した禁体層が肥厚
しカラム型におけるチヤンネリングに似た現象を生じ生
成物転換率が低下する事等の欠点がある。
"Conventional technology" In conventional bioreactors, a carrier binding method, a cross-linking method, an encapsulation method, or a composite method combining these is used as an immobilization method for microorganisms and enzymes. Granular, lumpy, film-like,
Depending on the fixed form such as sheet, packed bed type, fluidized bed type,
It is used properly for membrane type, tube type, plate type reactors. Also, several types of rotary plates have been developed, which have high stirring efficiency, low pressure loss, and easy attachment / detachment of the disk to maintain the reaction activity of the biocatalyst, thus increasing the product yield. In terms of, it has excellent characteristics as a bioreactor. However, in this rotating disk type bioreactor, there are restrictions on the microorganisms that can be used to implant cells on the disk, and since the fermentation is carried out in one chamber, the activity of the immobilized biocatalyst is uniformly reduced, A large number of rotating discs are required to maintain activity and keep the product concentration constant, resulting in an unexpectedly large installation area, and the spacing between the rotating discs arranged side by side on the same axis is restricted. There is a defect that the growth of the abstinence layer grown in the disc space thickens, causing a phenomenon similar to channeling in the column type and lowering the product conversion rate.

「発明が解決しようとする問題点」 本発明は上記の事情に鑑み使用微生物の適用範囲を拡大
すると共に基質と生体触媒の有効接触率の向上とチヤン
ネリング現象の防止をはかり、固定化生体触媒にかかる
負荷を段階的に軽減せしめ触媒の活性を平均的に維持
し、製品の品質安定化をはかることを目的とするもので
ある。
"Problems to be Solved by the Invention" In view of the above circumstances, the present invention aims to improve the effective contact rate of the substrate and the biocatalyst and to prevent the channeling phenomenon, and to improve the immobilized biocatalyst by expanding the application range of the microorganism to be used. The purpose is to gradually reduce the load, maintain the activity of the catalyst evenly, and stabilize the quality of the product.

「問題点を解決するための手段」 本発明は上記の目的を達成するため上部にガス導入口及
び基質注入口を備えた横置円筒密閉型槽内を隔壁によっ
て数個の反応室に区分し各室に回転軸を軸受上で連結す
る着脱任意で、しかも、担体に保持させた固定化生体触
媒を充填保持でき、反応液が容易に出入りできる孔を有
する多孔回転ドラムを有し、上記隔壁には上部に通気
口、中程に反応液溢流口を有し、かつ上記槽の中程には
生成物溢流口を有することを特徴とする隔室回転ドラム
式バイオリアクターによつて構成される。
[Means for Solving the Problems] In order to achieve the above-mentioned object, the present invention divides a horizontal cylindrical closed type tank having a gas inlet and a substrate inlet at the top into several reaction chambers by partition walls. Each chamber has a perforated rotary drum having a hole in which a rotating shaft is connected on a bearing, which can be freely attached and detached, and which can be filled and held with an immobilized biocatalyst held on a carrier and through which a reaction solution can easily enter and leave, and the partition wall. It has a vent hole in the upper part, a reaction liquid overflow port in the middle, and a product overflow port in the middle of the tank. To be done.

「作用」 従つて横置円筒密閉型槽(リアクター槽)1の本体1′
から蓋2を外し、各反応室8、8、8内に回転軸11に
よつて支持されている多孔回転ドラム15、15、15
内に固定化生体触媒を充填した後蓋2で本体1′を密閉
し、本体1′の外周に設けたジヤケツト16に恒温水を
循環させ、リアクター槽1内にガス導入口5から使用ガ
スを導入し蒸発成分凝縮器に冷却水を通水する。この状
態において上記回転ドラム15、15、15を回動し、
基質注入口4から基質を注入し、リアクター槽1の液性
制御回路を作動して運転する。従つて基質は反応液溢流
口14、14′を溢流して反応室8を通過すると同時に
上記回転ドラム15、15、15は反応液溢流面の上下
に回転する。そして該ドラム15、15、15内に保持
されている固定化生体触媒によつて目的生成物成分の濃
度が徐々に上り、リアクター槽1の生成物溢流口18、
18′から目標濃度の生成物が溢流する。又必要に応じ
て下部試料採取口19からサンプリングして発酵状態を
掌握し、又必要に応じて上記槽1の底部のガス散気口2
0よりガスを供給することができる。
"Operation" Therefore, the main body 1'of the horizontal cylindrical closed type tank (reactor tank) 1 '
The lid 2 is removed from the perforated rotary drum 15, 15, 15 supported by the rotary shaft 11 in each reaction chamber 8, 8, 8.
After filling the inside with the immobilized biocatalyst, the main body 1'is sealed with the lid 2, the constant temperature water is circulated in the jacket 16 provided on the outer periphery of the main body 1 ', and the working gas is supplied from the gas introduction port 5 into the reactor tank 1. The cooling water is introduced and the cooling water is passed through the condenser. In this state, the rotary drums 15, 15, 15 are rotated,
A substrate is injected from the substrate inlet 4 and the liquid control circuit of the reactor tank 1 is operated to operate. Accordingly, the substrate overflows the reaction solution overflow ports 14 and 14 'and passes through the reaction chamber 8, and at the same time, the rotary drums 15, 15 and 15 rotate above and below the reaction solution overflow surface. Then, the concentration of the target product component gradually increases due to the immobilized biocatalyst held in the drums 15, 15 and 15, and the product overflow port 18 of the reactor tank 1
The target concentration of product overflows from 18 '. If necessary, the fermentation state is grasped by sampling from the lower sampling port 19, and if necessary, the gas diffusion port 2 at the bottom of the tank 1 described above.
Gas can be supplied from 0.

「実施例」 本発明の実施例を添付図面によつて以下詳述する。第1
図は隔室回転ドラム式バイオリアクターの縦断面図、第
2図はバイオリアクター本体の分解斜視図、第3図は回
転ドラムの分解斜視図を示している。1は上半部の蓋2
と下半部の本体1′を有する横置円筒密閉型槽、蓋2は
槽内液のPHを一定に保つための薬液注入口3、基質注
入口4、好気性発酵、通性嫌気性発酵等の発酵形態に応
じて供給する空気、酸素、炭酸ガス、窒素等のガス導入
口5、蓋体内部を三個の反応室8に区分し通気口6、6
を有する隔壁7、7を設け、反応制御のためのセンサー
挿入口9、蒸発成分凝縮器を接続する脱気口10、蓋2
及び本体1′の両端壁中心部および隔壁中心部に回転軸
11のシール装備を有する軸受12を設け、蓋2を本体
1′と締結する蝶型ネジ13を具備し、上記隔壁7、7
の中程には反応液溢流口14、14′を設ける。上記回
転軸11には上記反応室8の内部に網製多孔回転ドラム
15を設け、該ドラム15には固定化生体触媒を充填す
る扉15′が設けられる。又本体1′の外周には槽温度
を一定に保つためのジヤケツト16、ジヤケツト用恒温
循環水入出口17、17′、生成物溢流口18、1
8′、試料採取口19、槽底部からの供給ガス散気口2
0、蓋2と本体1′のシール用埋込ボルト21、同部の
シール用摺接挾帯22を具備し、槽内部の各室8、8、
8に固定化生体触媒を保持した各個着脱任意の回転ドラ
ム15がシール軸受上に懸架された状態で回転軸11方
向に並設され、回転軸11の一端は閉塞軸受12′、1
2′に支持され、他端は上記槽1外に設置する回転ドラ
ム駆動装置23にギアヘツド24を介して接続される。
固定化生体触媒は天然高分子ゲル、合成高分子ゲル、天
然繊維、合成繊維、多孔質高分子、多孔質セラミツクス
等による担体に包括、架橋或は吸着された微生物又は酵
素であり、使用ガスは空気、窒素、炭酸ガス、窒素ガス
等を変換可能であり、かつ上記固定化生体触媒を交換又
は変換することによつて上記槽1内において好気性発酵
や通性嫌気性発酵を行うことができるものである。尚上
記回転軸11は軸受上で一体に連結した1個の共通回転
軸11でも又軸受上で回転方向に固定した分離可能な共
通中心線上の3個の回転軸11でも差支えない。
[Examples] Examples of the present invention will be described in detail below with reference to the accompanying drawings. First
The figure shows a longitudinal sectional view of a compartment rotary drum type bioreactor, FIG. 2 shows an exploded perspective view of a bioreactor main body, and FIG. 3 shows an exploded perspective view of a rotary drum. 1 is the lid 2 on the upper half
And a horizontal cylindrical closed type tank having a lower half body 1 ', a lid 2 is a chemical solution inlet 3 for maintaining a constant pH of the tank liquid, a substrate inlet 4, an aerobic fermentation, a facultative anaerobic fermentation Such as air to be supplied according to the fermentation form such as oxygen, oxygen, carbon dioxide, nitrogen, etc., and the inside of the lid are divided into three reaction chambers 8, and vents 6, 6
Is provided with partition walls 7, 7, a sensor insertion port 9 for controlling the reaction, a degassing port 10 for connecting a vaporized component condenser, and a lid 2
Further, a bearing 12 having a seal for the rotary shaft 11 is provided at the center of both end walls of the main body 1'and the center of the partition wall, and a butterfly screw 13 for fastening the lid 2 to the main body 1'is provided.
Reaction solution overflow ports 14 and 14 'are provided in the middle. The rotary shaft 11 is provided with a net-made perforated rotary drum 15 inside the reaction chamber 8, and the drum 15 is provided with a door 15 'for filling the immobilized biocatalyst. Further, on the outer periphery of the main body 1 ', a jacket 16 for keeping the tank temperature constant, constant temperature circulating water inlet / outlet 17, 17' for the jacket, product overflow port 18, 1
8 ', sample collection port 19, gas supply port 2 from the bottom of the tank
0, a lid 2 and a seal embedding bolt 21 for the main body 1 ′, and a sliding contact strip 22 for sealing in the same portion, and each chamber 8, 8 inside the tank,
8, individual rotating drums 15 each holding a fixed biocatalyst are attached and detached in parallel in the direction of the rotating shaft 11 while being suspended on a seal bearing, and one end of the rotating shaft 11 is a closed bearing 12 ′, 1
2'is supported, and the other end is connected to a rotary drum driving device 23 installed outside the tank 1 via a gear head 24.
The immobilized biocatalyst is a natural polymer gel, synthetic polymer gel, natural fiber, synthetic fiber, porous polymer, microbe or enzyme entrapped in a carrier such as porous ceramics, crosslinked or adsorbed, and used gas is It is possible to convert air, nitrogen, carbon dioxide, nitrogen gas, etc., and by exchanging or converting the immobilized biocatalyst, aerobic fermentation or facultative anaerobic fermentation can be performed in the tank 1. It is a thing. The rotating shaft 11 may be one common rotating shaft 11 integrally connected on the bearing or three rotating shafts 11 on the separable common center line fixed in the rotating direction on the bearing.

「発明の効果」 本発明は多孔回転ドラムの採用により使用微生物又は酵
素の適用範囲が広い事、リアクター槽内を数室に区分し
基質溶液を順次次室へ溢流移動させることにより固定化
生体触媒にかかる負荷が段階的に軽減でき、その結果活
性の平均的な維持が可能となる事、回転ドラム内への固
定化生体触媒の充填により触媒の比表面積を大きくとる
ことができ、その結果基質の生成物への転換率が高い
事、隔室前後の多孔回転ドラムの着脱交換あるいは該回
転ドラム内の固定化生体触媒の交換により製品の品質が
安定する事等の利点を持つている。
[Advantages of the Invention] The present invention has a wide application range of microorganisms or enzymes to be used due to the adoption of a perforated rotary drum. The reactor is divided into several chambers and the substrate solution is sequentially overflowed to the next chamber to be immobilized. The load on the catalyst can be gradually reduced, and as a result, the activity can be maintained on average, and the specific surface area of the catalyst can be increased by filling the immobilized biocatalyst in the rotating drum. It has advantages such as high conversion rate of substrate to product, detachable replacement of the porous rotary drum before and after the compartment, or replacement of immobilized biocatalyst in the rotary drum to stabilize product quality.

又各種担体による微生物又は酵素よりなる固定化生体触
媒を充分利用し得るし、 さらに好気性、通性嫌気性何れの発酵にも適用し得る効
果がある。
Further, the immobilized biocatalyst consisting of microorganisms or enzymes by various carriers can be sufficiently utilized, and further, it can be applied to both aerobic and facultative anaerobic fermentation.

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

第1図は本発明の隔室回転ドラム式バイオリアクターを
示す縦断側面図、第2図は上記リアクターの分解斜視
図、第3図は回転ドラムの斜視図である。 1……横置円筒密閉型槽、4……基質注入口、5……ガ
ス導入口、6……通気口、7……隔壁、8……反応室、
11……回転軸、14、14′……反応液溢流口、15
……多孔回転ドラム、18、18′……生成物溢流口。
FIG. 1 is a vertical sectional side view showing a compartment rotary drum type bioreactor of the present invention, FIG. 2 is an exploded perspective view of the reactor, and FIG. 3 is a perspective view of a rotary drum. 1 ... Horizontal cylindrical sealed tank, 4 ... Substrate inlet, 5 ... Gas inlet, 6 ... Vent, 7 ... Partition, 8 ... Reaction chamber,
11 ... Rotary shaft, 14, 14 '... Reaction liquid overflow port, 15
...... Perforated rotary drum, 18, 18 '... Product overflow port.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】上部にガス導入口及び基質注入口を備えた
横置円筒密閉型槽内を隔壁によって数個の反応室に区分
し各室に回転軸を軸受上で連結する着脱任意で、しか
も、担体に保持させた固定化生体触媒を充填保持でき、
反応液が容易に出入りできる孔を有する多孔回転ドラム
を有し、上記隔壁には上部に通気口、中程に反応液溢流
口を有し、かつ上記槽の中程には生成物溢流口を有する
ことを特徴とする隔室回転ドラム式バイオリアクター。
1. A horizontal cylindrical closed type tank having a gas inlet and a substrate inlet at the top is divided into several reaction chambers by partition walls, and a rotary shaft is connected to each chamber on a bearing. Moreover, the immobilized biocatalyst held on the carrier can be filled and held,
It has a perforated rotary drum with holes through which the reaction solution can easily enter and exit, the partition wall has a vent hole in the upper part, a reaction solution overflow port in the middle, and a product overflow in the middle of the tank. A compartment-rotating drum type bioreactor having a mouth.
【請求項2】天然高分子ゲル、合成高分子ゲル、天然繊
維、合成繊維、多孔質高分子、多孔質セラミックス等の
担体に包括あるいは架橋、吸着された微生物または酵素
よりなる固定化生体触媒を多孔回転ドラム内に充填する
請求項(1)記載の隔室回転ドラム式バイオリアクター。
2. An immobilized biocatalyst comprising a microorganism or an enzyme which is entrapped, crosslinked or adsorbed on a carrier such as a natural polymer gel, a synthetic polymer gel, a natural fiber, a synthetic fiber, a porous polymer or a porous ceramics. The compartmental rotary drum type bioreactor according to claim 1, wherein the bioreactor is filled in a perforated rotary drum.
【請求項3】空気、酸素、炭酸ガス、窒素等槽内供給ガ
スの交換および固定化生体触媒の交換により好気性発
酵、通性嫌気性発酵いずれをも実施可能とする請求項
(1)記載の隔室回転ドラム式バイオリアクター。
3. An aerobic fermentation and a facultative anaerobic fermentation can be carried out by exchanging supply gas in the tank such as air, oxygen, carbon dioxide and nitrogen and exchanging immobilized biocatalyst.
The compartment-rotating drum bioreactor described in (1).
JP63040051A 1988-02-23 1988-02-23 Compartment rotating drum bioreactor Expired - Lifetime JPH0657146B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63040051A JPH0657146B2 (en) 1988-02-23 1988-02-23 Compartment rotating drum bioreactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63040051A JPH0657146B2 (en) 1988-02-23 1988-02-23 Compartment rotating drum bioreactor

Publications (2)

Publication Number Publication Date
JPH01215277A JPH01215277A (en) 1989-08-29
JPH0657146B2 true JPH0657146B2 (en) 1994-08-03

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Country Link
JP (1) JPH0657146B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH072109B2 (en) * 1989-12-28 1995-01-18 雪印乳業株式会社 Method and apparatus for gas sparging of rotary reactor

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6025112B2 (en) * 1981-12-02 1985-06-17 日東電工株式会社 immobilized enzyme reactor
JPS6019598U (en) * 1983-07-15 1985-02-09 日産自動車株式会社 Ram device of cargo handling vehicle
JPH0644860B2 (en) * 1985-07-03 1994-06-15 日本合成ゴム株式会社 Incubator

Also Published As

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JPH01215277A (en) 1989-08-29

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