JP2005040061A - Fermentation tank (jar fermenter) - Google Patents

Fermentation tank (jar fermenter) Download PDF

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JP2005040061A
JP2005040061A JP2003277960A JP2003277960A JP2005040061A JP 2005040061 A JP2005040061 A JP 2005040061A JP 2003277960 A JP2003277960 A JP 2003277960A JP 2003277960 A JP2003277960 A JP 2003277960A JP 2005040061 A JP2005040061 A JP 2005040061A
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Satoshi Takeuchi
聰 竹内
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    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/06Nozzles; Sprayers; Spargers; Diffusers

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a fermentation tank (jar fermenter) that is made of a membrane and circulates a culture solution and with which a yield is increased and an inexpensive culture cost is maintained by forced dispersion fall. <P>SOLUTION: This energy-saving type fermentation tank (jar fermenter) having a low running cost is equipped with a pump from a lower stirrer to an upper forced dispersion apparatus of the membrane tank, various sensors and a by-pass furnished with an inoculation port. The fermentation tank (jar fermenter) is enfolded, sterilized, mounted on a suspension system, swollen with sterile air or a mixed gas of nitrogen and carbon dioxide gas, charged with a sterilized culture solution and inoculated with a bacterium. The culture solution is circulated and an aerobic bacterium or anaerobic bacterium is cultured while forced dispersion. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、自然科学分野において、微生物の増殖を目的とする小型の汎用型醗酵タンク(ジャー・ファーメンター)に関するものである。   The present invention relates to a small general-purpose fermentation tank (jar fermenter) for the purpose of microbial growth in the field of natural science.

従来の醗酵タンク(ジャー・ファーメンター)は、外界と遮断する手段は、金属製の密閉タンクで、接種口、pH調節用酸溶液の容器とその取付口、アルカリ溶液の容器とその取付口、消泡剤用の容器とその取付口、泡検出センサー取付口、圧力計装着口及び排気口などはタンクの上部に、pH検出センサーの取付口、溶存酸素検出センサーの取付口、温度検出センサーの取付口及び邪魔板は、タンクの胴体に、無菌空気の供給部、モーターで回転させる撹拌子はタンクの底に設けていた。   In the conventional fermentation tank (jar fermenter), the means for blocking from the outside world is a metal sealed tank, the inoculation port, the pH adjusting acid solution container and its mounting port, the alkaline solution container and its mounting port, The defoamer container and its attachment port, the bubble detection sensor attachment port, the pressure gauge attachment port and the exhaust port are located at the top of the tank, the pH detection sensor attachment port, the dissolved oxygen detection sensor attachment port, and the temperature detection sensor The mounting port and baffle plate were provided on the tank body, the sterile air supply unit, and the stirring bar rotated by the motor were provided on the bottom of the tank.

このような金属性醗酵タンク(ジャー・ファーメンター)の滅菌方法は高圧蒸気法である。醗酵タンク(ジャー・ファーメンター)を定位置に固定し、高圧に耐えるタンクは勿論のこと、配管及びバルブを設けて高圧蒸気発生装置より、高圧蒸気をタンク本体へ、タンク容量以上の高圧蒸気量を送らなければならない。その結果付帯設備として高圧蒸気発生装置が必要であり、タンク自体の自重は重く、pH調節用酸溶液の容器とその取付口、アルカリ溶液の容器とその取付口、消泡剤用の容器とその取付口、泡検出センサー取付口、接種口、圧力計装着口、排気口を初め、pH検出センサー取付口、温度検出センサー取付口、溶存酸素検出センサー取付口、無菌空気投入口及び撹拌子のメカニカルシール部を、タンク本体に取り付ける加工は容易でない。また使用者にとってもタンクの清掃は困難であり、バルブの数も多く、運転操作も複雑である。   Such a metal fermentation tank (jar fermenter) is sterilized by a high pressure steam method. The fermentation tank (jar fermenter) is fixed at a fixed position, as well as a tank that can withstand high pressures, as well as piping and valves, high-pressure steam from the high-pressure steam generator to the tank body, and the amount of high-pressure steam that exceeds the tank capacity Must be sent. As a result, a high-pressure steam generator is required as ancillary equipment, and the tank itself is heavy, and the pH adjusting acid solution container and its attachment port, the alkaline solution container and its attachment port, the antifoaming agent container and its Mounting port, foam detection sensor mounting port, inoculation port, pressure gauge mounting port, exhaust port, pH detection sensor mounting port, temperature detection sensor mounting port, dissolved oxygen detection sensor mounting port, sterile air input port, and stir bar mechanical It is not easy to attach the seal part to the tank body. In addition, it is difficult for the user to clean the tank, the number of valves is large, and the operation is complicated.

一方通気方法は、タンク底部より無菌空気を送り込む方法が主流であり、撹拌により無菌空気の培養液に滞留する効果及び邪魔板の効果はあるものの、十分なガス交換は得られず、発泡の原因となり消泡翼を設けたり、消泡剤の添加が必要となる。   On the other hand, the main method of aeration is to send sterilized air from the bottom of the tank, and although there is an effect of staying in the culture medium of sterilized air by stirring and an effect of a baffle, sufficient gas exchange cannot be obtained, causing foaming. Therefore, it is necessary to provide an antifoaming wing or to add an antifoaming agent.

また現行の醗酵タンク(ジャー・ファーメンター)では、無菌空気の代わりに、無菌の窒素ガスと炭酸ガスの混合ガスを供給したとしても、嫌気性菌の培養は不可能に近く、現在のところ皆無である。   Also, in the current fermentation tank (jar fermenter), anaerobic bacteria are almost impossible to cultivate even if sterile nitrogen gas and carbon dioxide mixed gas is supplied instead of sterile air. It is.

富金原 孝:醗協誌,33,198(1975)Takashi Toganehara: Dokkyo Journal, 33, 198 (1975)

本発明が解決しようとする問題点は、ボイラーなどの付帯設備がいらず、少ない蒸気量で滅菌が出来、バルブを無くし、操作が簡単な醗酵タンク(ジャー・ファーメンター)であること。   The problem to be solved by the present invention is a fermentation tank (jar fermenter) that does not require any additional equipment such as a boiler, can be sterilized with a small amount of steam, has no valves, and is easy to operate.

微生物または代謝生産物の収量を多くするために、培養液中の微生物が要求する溶存酸素濃度の維持を満たす通気方法で、従来に比べて少ない量の無菌空気でも可能な醗酵タンク(ジャー・ファーメンター)であること。   In order to increase the yield of microorganisms or metabolites, a fermentation tank that can maintain the dissolved oxygen concentration required by microorganisms in the culture solution and can be used with a smaller amount of aseptic air than before. Mentor).

消泡剤が不要または少量ですむ醗酵タンク(ジャー・ファーメンター)であること。   A fermentation tank (jar fermenter) that requires no or a small amount of antifoam.

嫌気性菌が培養可能な醗酵タンク(ジャー・ファーメンター)であること。   It must be a fermentation tank (jar fermenter) that can cultivate anaerobic bacteria.

これらの課題を解決するためには、醗酵タンク(ジャー・ファーメンター)の容器自体をフレキシブルの膜で円柱形の容器を作る。例えばビニール膜またはシリコンゴム膜で作製し、折り畳んで前者の場合はエチレンオキサイドガス(EOG)滅菌器で、後者は高圧蒸気滅菌器(オートクレーブ)で滅菌すればよい。   In order to solve these problems, the container of the fermentation tank (jar fermenter) itself is made into a cylindrical container with a flexible membrane. For example, it may be made of a vinyl film or a silicon rubber film, folded and then sterilized with an ethylene oxide gas (EOG) sterilizer in the former case and a high-pressure steam sterilizer (autoclave) in the latter case.

従来のものに比べ供給する無菌の空気量を少なくしても、微生物の要求する溶存酸素濃度を満たすために、バイパスを設けて培養液を循環させ、上部に取り付けた強制分散装置を通して表面積を多くして、タンク内を落下させることにより、効果的なガス交換を行い、培養液面に落下し衝突する際に、タンク内の気体を液中に巻き込み、溶存酸素の増加が期待できる。   In order to meet the dissolved oxygen concentration required by microorganisms even if the amount of sterile air to be supplied is less than that of conventional ones, a bypass is provided to circulate the culture solution and increase the surface area through a forced dispersion device attached to the top. Then, by dropping the inside of the tank, effective gas exchange is performed, and when falling and colliding with the culture liquid surface, the gas in the tank is involved in the liquid, and an increase in dissolved oxygen can be expected.

また強制分散装置を通過して培養液の表面積が多くなり、粒状となり培養液面に落下し衝突する際、泡を消す消泡効果があるので、培地組成の炭素源が2%程度ならば、培養過程の消泡剤は不要である。   In addition, the surface area of the culture solution increases through the forced dispersion device, and when it falls into the culture solution surface and collides, it has a defoaming effect to eliminate bubbles, so if the carbon source of the medium composition is about 2%, No antifoaming agent is required during the culture process.

さらに折り畳んで滅菌したタンクを、フィルターなどで濾過滅菌した窒素ガスと炭酸ガスの混合ガスで膨らませれば、従来の金属製醗酵タンク(ジャー・ファーメンター)では不可能であった嫌気性菌の培養が可能である。   Furthermore, if the tank sterilized by inflating it is inflated with a mixed gas of nitrogen gas and carbon dioxide gas that has been sterilized by filtration with a filter, etc., anaerobic bacteria culture that was impossible with conventional metal fermentation tanks (jar fermenters) Is possible.

タンク自体を折りたたむことにより、実験室レベルの小さな高圧蒸気滅菌器とEOG滅菌器またはEOGガスボンベとヒーター装備減圧弁及びEOGガス処理機さえあれば滅菌可能で、従来の金属製タンク(ジャー・ファーメンター)には必要なボイラー及び配管などは不要である。すなわち設備投資が少なくて済む経済的な効果は大きい。   By folding the tank itself, it can be sterilized with a small laboratory-level high-pressure steam sterilizer and EOG sterilizer or EOG gas cylinder, heater equipped pressure reducing valve, and EOG gas processing machine. ) Does not require the necessary boiler and piping. In other words, the economic effect of requiring less capital investment is great.

従来の金属製醗酵タンク(ジャー・ファーメンター)の培地滅菌方法は、全体を高圧蒸気滅菌法で、培養至適温度まで冷却する必要があるのに対し、本発明の醗酵タンク(ジャー・ファーメンター)では、有機物の培地成分は出来るだけ少ない精製水で溶かしたものを、実験室レベルの小型の高圧蒸気滅菌器で滅菌し、精製水はメンブランフィルターで濾過滅菌し、予め滅菌した本発明の醗酵タンク(ジャー・ファーメンター)に無菌的に注入すればよいので、エネルギーの節約になることは勿論のこと、培地成分の易熱性栄養分の破壊は最小限度にとどめることができ、培地成分及び無菌水を培養至適温度に保って醗酵タンク(ジャー・ファーメンター)に注入すれば、すぐ接種できるので時間の節約は勿論のこと、エネルギーの節約にもなり、培養のランニングコストは少なくて済む。   The conventional medium sterilization method for metal fermentation tanks (jar fermenters) requires high-pressure steam sterilization to cool the whole to the optimum temperature for cultivation, whereas the fermentation tank (jar fermenters) of the present invention ), The organic medium components dissolved in as little purified water as possible are sterilized in a small laboratory-sized high-pressure steam sterilizer, and the purified water is sterilized by filtration through a membrane filter and sterilized in advance. Since the tank (jar fermenter) can be injected aseptically, not only energy can be saved, but also the destruction of the heat-sensitive nutrients of the medium components can be kept to a minimum. Can be inoculated immediately if it is poured into a fermentation tank (jar fermenter) while keeping the temperature at the optimum temperature for cultivation. Ri, the running cost of the culture requires less.

折りたたんでタンクを滅菌した後、懸架装置に取り付けて組み立てる時、好気性菌を培養する時は無菌空気を、また嫌氣性菌を培養する時は、無菌の窒素ガスと炭酸ガスの混合ガスで本醗酵タンク(ジャー・ファーメンター)を膨らませれば良い。従来の金属製醗酵タンク(ジャー・ファーメンター)では不可能であった嫌氣性菌を効率よく、容易に培養出来ることは嫌氣性菌の分野における学問の進歩に寄与することが出来る。   After folding and sterilizing the tank, and assembling it on a suspension system, when cultivating aerobic bacteria, use sterile air, and when cultivating anaerobic bacteria, use a mixture of sterile nitrogen gas and carbon dioxide. What is necessary is just to inflate this fermentation tank (jar fermenter). Efficient and easy cultivation of anaerobes that were impossible with conventional metal fermentation tanks (jar fermenters) can contribute to academic progress in the field of anaerobes.

本体自体は軽量であり、汚染源となる排水溝への配管は不必要であり、電源さえあれば密閉された無菌室に移動させて培養することが出来る。その結果雑菌に汚染される危険率は低くなる一方、遺伝子操作による人工的に作られた菌を外界に出さない、封じ込めが容易に出来る利点がある。   The main body itself is lightweight and does not require piping to a drainage channel that is a source of contamination, and if it has a power source, it can be moved to a sealed aseptic room and cultured. As a result, there is an advantage that the risk of being contaminated with various germs is low, but the artificially produced germs by genetic manipulation are not released to the outside and can be easily contained.

本発明の醗酵タンク(ジャー・ファーメンター)には、汚染源となる配管や現在用いられているバルブ類がないので、培養液を取り出した後、高圧蒸気滅菌した培地成分及び濾過滅菌した精製水を、予め培養至適温度に保ち無菌室内で補給すれば、二回目の培養が可能であり、種菌の準備もいらず連続培養が可能である。   In the fermentation tank (jar fermenter) of the present invention, there are no pipes that are a source of contamination or valves that are currently used. Therefore, after removing the culture solution, the medium components sterilized by autoclaving and purified water sterilized by filtration are used. If the temperature is optimally maintained in advance and replenished in a sterile room, the second culture is possible, and continuous culture is possible without preparation of the inoculum.

従来の金属製醗酵タンク(ジャー・ファーメンター)、ボイラー及び配管からの鉄イオンが、悪影響を及ぼす場合がある。例えばジフテリア毒素の調製を目標とした時、毒素産生量は鉄イオンの濃度に左右されるが、培養液が金属に接することを最小限に止めた本醗酵タンク(ジャー・ファーメンター)は最適である。   Iron ions from conventional metal fermentation tanks (jar fermenters), boilers and piping may have adverse effects. For example, when targeting diphtheria toxin preparation, the amount of toxin production depends on the iron ion concentration, but this fermentation tank (jar fermenter) that minimizes the contact of the culture medium with metal is optimal. is there.

pHを一定にして培養したい場合、pH調製剤として、塩酸及び水酸化ナトリウムの使用が望ましい。アルカリ性に傾いた時、従来のステンレス製の醗酵タンク(ジャー・ファーメンター)では、塩酸によりステンレスが腐食されるので使用されないが、本醗酵タンク(ジャー・ファーメンター)では、塩酸の使用が可能であり好都合である。   When culturing at a constant pH, it is desirable to use hydrochloric acid and sodium hydroxide as pH adjusters. In the case of leaning to alkalinity, the conventional stainless steel fermentation tank (jar fermenter) is not used because the stainless steel is corroded by hydrochloric acid, but the fermentation tank (jar fermenter) can use hydrochloric acid. It is convenient.

強制分散装置より培養液を分散落下させることにより、培養液の表面積が多くなり、タンク内の気体に接する面積が多くなり、効果的なガス交換が行われること、また分散落下することにより、培養液表面に落ちる際にタンク内の気体の巻き込み効果のため、少ない通気量で済む。   By dispersing and dropping the culture solution from the forced dispersion device, the surface area of the culture solution is increased, the area in contact with the gas in the tank is increased, effective gas exchange is performed, and the culture is performed by being dispersed and dropped. Because of the gas entrainment effect when it falls to the liquid surface, a small amount of air flow is sufficient.

本発明の醗酵タンク(ジャー・ファーメンター)の強制分散装置より培養液が分散落下することにより、泡は物理的な衝突により消える。従って培地の炭素源の成分が通常の2%以内ならば、消泡剤は不要である。   When the culture solution is dispersed and dropped from the forced dispersion device of the fermentation tank (jar fermenter) of the present invention, the bubbles disappear due to physical collision. Therefore, if the carbon source component of the medium is within 2% of the usual amount, an antifoaming agent is unnecessary.

本発明の醗酵タンク(ジャー・ファーメンター)は、電源さえあれば密閉された無菌室に移動させて培養することが出来る。その結果接種菌を一度氷水に5分間浸けて少量接種すれば、遅滞期は長くなるものの、対数増殖期の勾配が大きくなり、静止期のOD値は、従来の醗酵タンク(ジャー・ファーメンター)に比較して高くなり、培地当たりの菌量(代謝生産物)が多く取ることが出来る。またOD値が大きいことの相乗効果として、比較的早い時期での静止期に於いて培養菌の自己融解が効率よく起こり、遺伝子操作により菌体内に目的物を作らせた場合、培養液中に出てくるので、培養菌を壊す作業が省け、容易に目的物を取り出すことが出来る利点がある。いずれにせよ収量が多い理由は、バイパスを設けて強制分散装置から培養液を分散落下させる循環方法による、新しい通気方法によることが大きな要因である。   The fermentation tank (jar fermenter) of the present invention can be transferred to a sealed aseptic room and cultured if there is a power source. As a result, if the inoculum is immersed in ice water for 5 minutes and inoculated in a small amount, the lag phase will be longer, but the slope of the logarithmic growth phase will be larger, and the OD value in the stationary phase will be the conventional fermentation tank (jar fermenter) The amount of bacteria per culture medium (metabolite) can be increased. In addition, as a synergistic effect of the large OD value, the autolysis of the cultured bacteria occurs efficiently in the stationary phase at a relatively early stage, and when the target substance is made in the cells by genetic manipulation, Since it comes out, there is an advantage that the work of breaking the culture can be omitted and the object can be easily taken out. In any case, the reason why the yield is high is largely due to a new aeration method using a circulation method in which a culture solution is dispersed and dropped from a forced dispersion device by providing a bypass.

同じ規模の本発明の醗酵タンク(ジャー・ファーメンター)を、2台並列に並べて培養すると、1カ所条件を変えた成績が、接種菌の状態が全く同じ条件で実験が出来るので、解析の際は接種菌のことは考慮しなくてもよいので実験結果の解析がしやすい。   When two fermentation tanks (jar fermenters) of the present invention of the same scale are arranged side by side and cultured, the results of changing the conditions at one place can be experimented under the same conditions of the inoculum. Since it is not necessary to consider the inoculum, it is easy to analyze the experimental results.

本発明の醗酵タンク(ジャー・ファーメンター)の本体は滅菌時に、出来るだけ容積を小さくするために、従来のステンレス金属の代わりに、膜例えば塩化ビニール膜またはシリコンゴム膜1を使用して、円柱形の容器を作る。この円柱形容器の上下の中心から一部を円形に切り、そこに合成樹脂またはステンレス金属で出来たボルト2付きフラットのリング3を内側から装着し、パッキング4、上部円形板5、座金、ナット6を用いて取り付け、外界と完全に遮断する。上部の円形板には、従来の醗酵タンク(ジャー・ファーメンター)には無い強制分散装置(スプレイノズル)7、その周りに従来からある消泡剤添加口8、泡検出センサー取付口9、圧力スイッチ10付き圧力計装着口11、排気口12及びフィルター13付き無菌空気投入口14を取り付ける。タンク底部も同様にして底部円形板15を取り付け、底部円形板には、従来からある無菌空気拡散装置16、従来とは方式が異なる撹拌装置17とその撹拌子18を取り付ける。上部の無菌空気投入口から底部の無菌空気拡散装置はシリコンゴム管19で繋ぐ。また撹拌装置の培養液出口から上部の強制分散装置に向かってシリコンゴム管を用いてバイパス 20を設け、このバイパスにメカニカルシールフリーの、マグネットポンプ回転子部分21、温度検出センサー取付口22、pH検出センサー取付口23、溶存酸素検出センサー取付口24、pH調節用酸溶液送入口25、pH調節用アルカリ溶液送入口26、OD測定用サンプル取出口27とOD測定用サンプル戻口28及び培養液注入口兼接種口29を取り付ける。   The main body of the fermentation tank (jar fermenter) of the present invention is a cylinder using a film such as a vinyl chloride film or a silicon rubber film 1 instead of a conventional stainless metal in order to reduce the volume as much as possible during sterilization. Make a shaped container. A part of this cylindrical container is cut into a circular shape from the upper and lower centers, and a flat ring 3 with a bolt 2 made of synthetic resin or stainless steel is attached to the inside from the inside, packing 4, upper circular plate 5, washer, nut Install with 6 and completely shut off from the outside world. The upper circular plate has a forced dispersion device (spray nozzle) 7 not present in a conventional fermentation tank (jar fermenter), a conventional antifoaming agent addition port 8, a foam detection sensor attachment port 9, and pressure. A pressure gauge mounting port 11 with a switch 10, an exhaust port 12 and a sterile air input port 14 with a filter 13 are attached. Similarly, a bottom circular plate 15 is attached to the bottom of the tank, and a conventional aseptic air diffusion device 16, a stirrer 17 having a method different from the conventional method, and its stirrer 18 are attached to the bottom circular plate. The aseptic air diffusion device at the bottom is connected by a silicone rubber tube 19 from the aseptic air inlet at the top. In addition, a bypass 20 is provided using a silicon rubber tube from the culture medium outlet of the stirring device to the upper forced dispersion device, and a mechanical seal-free magnet pump rotor portion 21, temperature detection sensor attachment port 22, pH is provided in this bypass. Detection sensor attachment port 23, dissolved oxygen detection sensor attachment port 24, pH adjustment acid solution inlet 25, pH adjustment alkali solution inlet 26, OD measurement sample outlet 27 and OD measurement sample return port 28, and culture solution Attach the injection / inoculation port 29.

微生物を培養する際は、マグネットポンプの回転子部分をマグネットポンプ駆動モーター部分30に装着して、回転子を回転させてバイパス内に培養液を流し、強制分散装置を出た培養液は、分散して表面積が増加しながら落下し衝突することにより、発泡した大きな泡を消す効果があると同時に、タンク内の気体を液中に巻き込み、溶存酸素の増加が期待でき、且つタンク内の気体に接する表面積が多くなり、ガス交換が効率よく行われる結果、少ない通気量で済む。   When cultivating microorganisms, the rotor part of the magnet pump is attached to the magnet pump drive motor part 30 and the rotor is rotated to flow the culture medium into the bypass. By dropping and colliding while increasing the surface area, there is an effect of eliminating the large foamed bubbles, and at the same time, the gas in the tank is entrained in the liquid, and an increase in dissolved oxygen can be expected, and the gas in the tank As a result of the increased surface area in contact and efficient gas exchange, a small amount of air flow is sufficient.

この撹拌装置は、従来のモーターで撹拌子を回転させる方式と異なり、培養液を循環させるポンプの吸入の水流を利用して、撹拌装置の回転子を回転運動に変えて撹拌子を回転させる。   Unlike the conventional method in which the stirrer is rotated by a motor, this stirrer rotates the stirrer by changing the rotor of the stirrer into a rotational motion by using the suction water flow of a pump that circulates the culture solution.

溶存酸素を多くしたい場合は、通気量を多くすることは勿論のこと、培養液を循環させるポンプの回転数を若干上げればコントロール可能である。もっと多くしたい場合は、もう一本バイバスを設けて、ポンプと強制分散装置から培養液を循環落下させれば良い。   In order to increase the amount of dissolved oxygen, it is possible to control by increasing the number of rotations of the pump for circulating the culture solution as well as increasing the aeration amount. If you want more, you can install another bypass and circulate and drop the culture fluid from the pump and forced dispersion device.

pHのコントロールはセットしたpHよりかけ離れた場合に、ペリスタポンプ31が回転して酸又はアルカリ溶液が、酸貯留瓶32又は塩基貯留瓶33から送入口に送れるようにすれば良い。   When the pH is far from the set pH, the peristaltic pump 31 may be rotated so that the acid or alkali solution can be sent from the acid storage bottle 32 or the base storage bottle 33 to the inlet.

消泡剤は、タンク内の端につけたフレキシブルな消泡センサー34の先端に培養液が触れている時、自動的にペリスタポンプが回転して消泡剤貯留瓶35から消泡剤がタンク内に入るように泡計測装置36によりコントロールすれば良い。   When the culture solution is in contact with the tip of the flexible defoaming sensor 34 attached to the end of the tank, the peristaltic pump automatically rotates to remove the defoamer from the defoamer storage bottle 35 into the tank. What is necessary is just to control by the bubble measuring device 36 so that it may enter.

次にこのフレキシブルな醗酵タンク(ジャー・ファーメンター)を自立させるために、高さが可変な懸架装置37に、タンクの上下の円形板を取り付けてから、タンク内に無菌空気を送り込めばよい。無菌空気を送り込むことにより、タンクが膨らみ初める。この時懸架装置のタンク上部は、重り38により徐々に上昇するのを助けるようにしておけば、フレキシブルなタンクは容易に自立する。   Next, in order to make this flexible fermentation tank (jar fermenter) self-supporting, the upper and lower circular plates of the tank are attached to the suspension device 37 having a variable height, and then aseptic air is fed into the tank. . By sending sterile air, the tank begins to swell. At this time, if the upper part of the tank of the suspension system is assisted to gradually rise by the weight 38, the flexible tank can easily stand by itself.

無菌空気はコンプレッサー39により作られた圧搾空気を、プレフィルター40及びフィルターを通過させれば容易に作れる。嫌氣性菌の場合は窒素ガスと炭酸ガスの混合ガスボンベ41のガスを、同様にしてプレフィルター及びフィルターを通過させて調製すればよい。   Aseptic air can be easily produced by passing the compressed air produced by the compressor 39 through the pre-filter 40 and the filter. In the case of anaerobic bacteria, the gas in the mixed gas cylinder 41 of nitrogen gas and carbon dioxide gas may be prepared by passing through a prefilter and a filter in the same manner.

培養液を培養液注入口兼接種口よりタンクに入れた時、膜が破れないように、タンクを保護するための二重構造をした保護カバー42を設け、そこに温度が制御された液体を循環させて、培養液の温度を制御すれば良い。特に醗酵により生じる反応熱の除去が迅速に行わなければならない時は、冷水を流すようにコントロールすれば良い。   A protective cover 42 having a double structure for protecting the tank is provided so that the membrane is not broken when the culture solution is put into the tank from the culture solution inlet / inoculation port, and the temperature-controlled liquid is provided there. Circulating and controlling the temperature of the culture solution. In particular, when removal of reaction heat generated by fermentation must be performed quickly, control may be performed so that cold water flows.

この二重構造をした保護カバーの下半分は固定式で、上半分は支柱43を設け、蝶番状の金具44でカバーが左右に開くようにすると、本醗酵タンク(ジャー・ファーメンター)の組立て操作がし易いようにする。   The bottom half of the protective cover with this double structure is fixed, the upper half is provided with a support 43, and the cover is opened to the left and right with a hinge-shaped metal fitting 44. Assembling this fermentation tank (jar fermenter) Make it easy to operate.

またタンク内圧が一定以上の陽圧になった場合は、圧力スイッチが働いて、排気処理装置45の殺菌液を循環させるポンプ46が作動して、殺菌液がアスピレーター47を通過した時、吸引するようにして、タンク内圧を平衡に保つようにする。途中のラインにフィルターを設けておけば、培養する微生物が外界に出るのを防ぐ。万が一フィルターが破れた時でも、殺菌液中に分散し、微生物が殺菌されるように配慮する。   Further, when the tank internal pressure becomes a positive pressure above a certain level, the pressure switch works to activate the pump 46 for circulating the sterilizing liquid in the exhaust treatment device 45, and the sterilizing liquid is sucked when it passes through the aspirator 47. In this way, the tank internal pressure is kept in equilibrium. If a filter is installed in the middle of the line, the microorganisms to be cultured are prevented from coming out to the outside world. Even if the filter breaks, take care to disperse it in the sterilizing solution and sterilize the microorganisms.

この懸架装置に、キャスター48を取り付け、pH計測装置49・溶存酸素計測装置50・OD計測装置51・排気処理装置・コンプレッサー及び培養液の至適温度制御に必要な温水発生装置52・冷水発生装置53を設けて移動を可能にすれば、高圧滅菌装置及びガス滅菌器の設備さえあれば、場所を選ばす培養が可能である。   A caster 48 is attached to the suspension device, and a pH measuring device 49, a dissolved oxygen measuring device 50, an OD measuring device 51, an exhaust treatment device, a compressor, and a hot water generating device 52 and a cold water generating device necessary for optimum temperature control of the culture solution. If it is possible to move by providing 53, it is possible to perform culture at any location as long as there is a high-pressure sterilizer and a gas sterilizer.

ここで従来の金属醗酵タンク(ジャー・ファーメンター)の培養工程は、所定の培地成分及び精製水をタンクに入れ、外釜に高圧蒸気を送り込み、培養液を滅菌すると同時に、pH調整用酸溶液の容器、アルカリ溶液の容器、消泡剤溶液の容器などを滅菌していた。滅菌終了後、外釜に水道水を循環させ、至適培養温度まで冷やしてから、種菌を接種して培養を開始し、滅菌したpH調整用酸溶液、pH調整用アルカリ溶液、消泡剤溶液を無菌分注するのが常法であるのに対して、本発明のフレキシブルな醗酵タンク(ジャー・ファーメンター)の培養操作の工程は異なり、下記のように実施すれば良い。   Here, the culture process of the conventional metal fermentation tank (jar fermenter) is carried out by putting predetermined medium components and purified water into the tank, sending high-pressure steam into the outer pot, sterilizing the culture solution, and at the same time, acid solution for pH adjustment , The alkaline solution container, the defoamer solution container, etc. After sterilization, tap water is circulated in the outer pot, cooled to the optimum culture temperature, inoculated with the inoculum, and then cultivated and sterilized acid solution for pH adjustment, alkaline solution for pH adjustment, antifoam solution Is a conventional method, but the culture process of the flexible fermentation tank (jar fermenter) of the present invention is different and may be carried out as follows.

本醗酵タンク(ジャー・ファーメンター)本体、バイパス及び各種センサー類などを高圧滅菌器又はEOGガス滅菌器などで別々に滅菌しておく。これらを無菌操作で組み立てる。本醗酵タンク(ジャー・ファーメンター)の上部及び下部を、懸架装置に固定し、バイパスを連結し、マグネットポンプ回転子を駆動部に固定した後、無菌空気を、無菌空気投入口から送り込み、本醗酵タンク(ジャー・ファーメンター)を膨らませる。嫌気性菌培養の時は、無菌の窒素ガスと炭酸ガスの混合ガスで、本醗酵タンク(ジャー・ファーメンター)を膨らませる。   This fermentation tank (jar fermenter) main body, bypass and various sensors are sterilized separately with a high-pressure sterilizer or an EOG gas sterilizer. These are assembled by aseptic operation. The upper and lower parts of the fermentation tank (jar fermenter) are fixed to the suspension system, the bypass is connected, the magnet pump rotor is fixed to the drive unit, and aseptic air is fed from the aseptic air input port. Inflate the fermentation tank (jar fermenter). When anaerobic bacteria are cultured, the fermentation tank (jar fermenter) is inflated with a mixture of aseptic nitrogen gas and carbon dioxide.

または泡検出センサー、圧力計、無菌空気投入口から無菌空気拡散装置へのシリコン管での連結及び各種センサーを装着したバイパスの連結など、予めタンクを組み立てておき、排気処理装置のポンプを作動させて、タンク内の空気を排出後、無菌空気投入口・排気口及び培養液注入口兼接種口からEOGガスを注入し、タンクを膨らませた後、数時間閉鎖状態にして、滅菌と同時に容器のリークテストを行う。次に排気処理装置のポンプを作動させて、陰圧にしてEOGを排気口より抜き、圧搾空気を無菌空気投入口から送り込み、タンクを膨らませた後に、排気口よりタンク内の無菌空気を抜く。この無菌空気の出し入れを数回繰り返し、残留しているEOGを出来るだけ除去する。   Alternatively, assemble the tank in advance, such as a bubble detection sensor, a pressure gauge, a silicone tube connection from the sterile air inlet to the sterile air diffusion device, and a bypass connection equipped with various sensors, and operate the pump of the exhaust treatment device. After exhausting the air in the tank, inject EOG gas from the sterile air inlet / exhaust port and the culture solution inlet / inoculation port, inflate the tank, close it for several hours, Perform a leak test. Next, the pump of the exhaust treatment device is operated to make negative pressure, and EOG is extracted from the exhaust port, compressed air is sent from the sterile air input port, the tank is inflated, and then the sterile air in the tank is extracted from the exhaust port. This aseptic air flow is repeated several times to remove the remaining EOG as much as possible.

また懸架装置の下半分の保護カバーをセットし、タンクの直径よりも小さな直径の円柱状のアダプターを取り付け、タンク自体を凹状にしてガス滅菌をすれば、EOG量又は無菌空気量は少なくてすむ。   Also, if the protective cover on the lower half of the suspension system is set, a cylindrical adapter with a diameter smaller than the tank diameter is attached, and the tank itself is recessed to perform gas sterilization, the amount of EOG or aseptic air can be reduced. .

排出するEOGガスは、300℃下で白金触媒を使用したEOGガス処理装置54で処理すればよい。   What is necessary is just to process the EOG gas discharged | emitted by the EOG gas processing apparatus 54 using a platinum catalyst under 300 degreeC.

本タンク(ジャー・ファーメンター)を滅菌後、培養量の1/10〜1/5量の精製水に培地成分を溶かし、高圧滅菌後、サイフォン又はポンプを使用して、培養液注入口兼接種口よりタンク内に入れた後、濾過滅菌しながら、9/10〜4/5量の精製水を、タンク内に入れる。温度制御された温水を、二重構造のカバー内に循環させる。   After sterilizing this tank (jar fermenter), dissolve the medium components in 1/10 to 1/5 volume of purified water, and after high-pressure sterilization, use a siphon or pump to inoculate and inoculate the culture medium. After putting into the tank from the mouth, 9/10 to 4/5 amount of purified water is put into the tank while sterilizing by filtration. Temperature-controlled hot water is circulated in the double-structured cover.

準備した種菌を滅菌注射器に採り、培養液注入口兼接種口のゴム栓をアルコール綿で拭き、注射する要領で種菌を接種した後、ポンプのスイッチを入れ、培養液を循環させ培養を開始する。   Take the prepared inoculum in a sterilized syringe, wipe the rubber stopper of the culture solution inlet / inoculation port with alcohol cotton, inoculate the inoculum in the manner of injection, turn on the pump, circulate the culture solution and start culture .

培養終了後、培養液注入兼接種口のゴム栓部分を取り外し、シリコンゴム管に取り付け変えてポンプを作動させて、培養液を取り出す。連続培養したい場合は、培地を注入すれば残っていた培養液が、種菌となって培養が可能であり、種菌の準備も不要である。   After completion of the culture, the rubber plug portion of the culture solution injection / inoculation port is removed, and the culture solution is taken out by changing the attachment to the silicon rubber tube and operating the pump. When continuous culture is desired, if the medium is injected, the remaining culture solution becomes a seed fungus and can be cultured, and preparation of the seed fungus is unnecessary.

緑膿菌N―10株を合成培地(グルタミン酸ソーダ2%、グルコース0.5%、硫酸マグネシュウム7水和物0.01%、硝酸カルシュウム0.0001%硫酸鉄7水和物0.000005%、燐酸二水素カリウム0.0252%、燐酸水素二ナトリウム12水和物0.563%、pH7.6)で従来の金属性醗酵タンク(ジャー・ファーメンター)と本発明の醗酵タンク(ジャー・ファーメンター)で培養した時の菌量をOD値で比較した結果、従来の金属性タンク(ジャー・ファーメンター)に比較して本発明のタンク(ジャー・ファーメンター)は、静止期のOD値は2.5で、従来の金属製醗酵タンク(ジャー・ファーメンター)の1.8〜2.0に比較して高く、遅滞期は長いものの、対数増殖期の立ち上が大きく、最終精製物は培地リッターあたり2倍前後で、最終精製物の蛋白含有量は金属製醗酵タンク(ジャー・ファーメンター)では70%であったのに対して、90%と優れていた。これは対数増殖期に増殖が顕著であったために、培地が有効に使われ、その後の自己融解が良好に行われたと考えられ、このことは遺伝子操作により、目的物を微生物に作らせ取り出す精製工程が、容易になることが期待される。また本菌を培養中に従来の金属製タンク(ジャー・ファーメンター)は、消泡剤が必要であったのに対し、本発明のタンク(ジャー・ファーメンター)では、消泡剤の消費量はゼロであった。   Pseudomonas aeruginosa N-10 strain was synthesized in a synthetic medium (sodium glutamate 2%, glucose 0.5%, magnesium sulfate heptahydrate 0.01%, calcium nitrate 0.0001% iron sulfate heptahydrate 0.000005%, Potassium dihydrogen phosphate 0.0252%, disodium hydrogen phosphate dodecahydrate 0.563%, pH 7.6) and the conventional metal fermentation tank (jar fermenter) and the fermentation tank of the present invention (jar fermenter) As a result of comparing the amount of bacteria when cultivated in) in terms of OD value, the tank (jar fermenter) of the present invention has an OD value of 2 in the stationary phase compared to the conventional metal tank (jar fermenter). .5, which is higher than 1.8-2.0 of the conventional metal fermentation tank (jar fermenter), the lag phase is long, but the rise of the logarithmic growth phase is large, and the final purified product is In about twice per land liter, protein content of the final purified product whereas was 70% for metallic fermentation tanks (jar fermentor) was superior to 90%. This is because the growth was significant during the logarithmic growth phase, so the medium was used effectively, and the subsequent autolysis was considered to have been successfully performed. The process is expected to be easy. In addition, the conventional metal tank (jar fermenter) needed an antifoaming agent while culturing the bacteria, whereas the tank (jar fermenter) of the present invention consumed the defoaming agent. Was zero.

緑膿菌IFO3080株を半合成培地(グルコース7%、燐酸水素二ナトリウム12水和物0.05%、燐酸水素二アンモニウム1%、酵母エキス0.2%)で蛋白分解酵素を産生させる目的で、従来の金属製醗酵タンク(ジャー・ファーメンター)と本発明の醗酵タンク(ジャー・ファーメンター)で培養した。従来の金属製醗酵タンク(ジャー・ファーメンター)の場合、pH調製剤として、沈降性炭酸カルシュウム2.5%になるように無菌的に添加して培養を実施した。培養後24時間目から発熱が始まり、30時間目には泡立ちが更に激しくなり培養を中止せざるを得なかった。この時の酵素力価は0.4mPUであった。これに対し本発明の醗酵タンク(ジャー・ファーメンター)では、1規定の水酸化ナトリュウム溶液を用いて自動的にpH5.5に調製しながら60時間培養した。その結果気泡と気泡の間に培養液があるような感じで、消泡剤の自動添加でタンクから培養液が溢れることがなかった。酵素力価は2.0mPUであった。   For the purpose of producing proteolytic enzyme from Pseudomonas aeruginosa IFO 3080 strain in semi-synthetic medium (glucose 7%, disodium hydrogen phosphate dodecahydrate 0.05%, diammonium hydrogen phosphate 1%, yeast extract 0.2%) They were cultured in a conventional metal fermentation tank (jar fermenter) and the fermentation tank of the present invention (jar fermenter). In the case of a conventional metal fermentation tank (jar fermenter), culture was carried out by adding aseptically as a pH adjuster so that the precipitated calcium carbonate was 2.5%. The fever started from 24 hours after the culture, and the foaming became more intense at 30 hours, and the culture had to be stopped. The enzyme titer at this time was 0.4 mPU. On the other hand, the fermentation tank (jar fermenter) of the present invention was cultured for 60 hours while automatically adjusting to pH 5.5 using a 1N sodium hydroxide solution. As a result, the culture solution did not overflow from the tank by the automatic addition of the antifoaming agent, as if there was a culture solution between the bubbles. The enzyme titer was 2.0 mPU.

培養操作工程で本醗酵タンク(ジャー・ファーメンター)を組み立てなければならないものの、視点を変えて現行の金属製醗酵タンク(ジャー・ファーメンター)と比較して考えてみると、本醗酵タンク(ジャー・ファーメンター)の通気方法は高率的に目的とする微生物が容易に培養することが出来、少ない運転経費で済み、閉鎖的環境下で、好気性菌は勿論のこと、嫌氣性菌も大量に容易に培養可能なことを考慮すると、本醗酵タンク(ジャー・ファーメンター)の利用可能性は大きく、社会に本醗酵タンク(ジャー・ファーメンター)が受け入れられると考えられる。   Although this fermentation tank (jar fermenter) must be assembled in the culture operation process, when compared with the current metal fermentation tank (jar fermenter) from a different perspective, this fermentation tank (jar)・ Fermenter's aeration method allows the target microorganisms to be easily cultivated at a high rate, and requires only a small operating cost. In a closed environment, not only aerobic bacteria but also anaerobes Considering that it can be easily cultured in large quantities, the availability of this fermentation tank (jar fermenter) is great, and it is considered that this fermentation tank (jar fermenter) is accepted by society.

本醗酵タンク(ジャー・ファーメンター)の上部平面図である。It is an upper top view of this fermentation tank (jar fermenter). 本醗酵タンク(ジャー・ファーメンター)の膜(塩化ビニール膜又はシリコンゴム膜)から構成するタンク胴体部分の斜視図である。It is a perspective view of the tank body part constituted from the film (vinyl chloride film or silicon rubber film) of this fermentation tank (jar fermenter). 本醗酵タンク(ジャー・ファーメンター)の内部より視た底部平面図である。It is the bottom part top view seen from the inside of this fermentation tank (jar fermenter). 本醗酵タンク(ジャー・ファーメンター)で培養中の断面図法により各種センサー取付口などをゴム栓に置き換えて描いた説明図である。It is explanatory drawing which replaced various sensor attachment ports etc. with the rubber stopper by the cross-sectional view method during culture | cultivation with this fermentation tank (jar fermenter). 本醗酵タンク(ジャー・ファーメンター)のフローシートによる説明図である。It is explanatory drawing by the flow sheet of this fermentation tank (jar fermenter).

符号の説明Explanation of symbols

1 膜
2 ボルト
3 リング
4 パッキング
5 上部円形板
6 ナット
7 強制分散装置(スプレイノズル)
8 消泡剤添加口
9 泡検出センサー取付口
10 圧力スイッチ
11 圧力計取付口
12 排気口
13 フィルター
14 無菌空気投入口
15 底部円形板
16 無菌空気拡散装置
17 撹拌装置
18 撹拌子
19 シリコンゴム管
20 バイパス
21 マグナットポンプ回転子部分
22 温度検出センサー取付口
23 pH検出センサー取付口
24 溶存酸素検出センサー取付口
25 pH調節用酸溶液送入口
26 pH調節用アルカリ溶液送入口
27 OD測定用サンプル取出口
28 OD測定用サンプル戻口
29 培養液注入口兼接種口
30 マグネットポンプ駆動モーター部分
31 ペリスタポンプ
32 酸貯留瓶
33 塩基貯留瓶
34 消泡センサー
35 消泡剤貯留瓶
36 泡計測装置
37 懸架装置
36 泡計測装置
37 懸架装置
38 重り
39 コンプレッサー
40 プレフィルター
41 窒素ガスと炭酸ガス混合ガスボンベ
42 保護カバー
43 支柱
44 蝶番状金具
45 排気処理装置
46 ポンプ
47 アスピレーター
48 キャスター
49 pH計測装置
50 溶存酸素計測装置
51 OD計測装置
52 温水発生装置
53 冷水発生装置
54 EOGガス処理装置
1 Membrane 2 Bolt 3 Ring 4 Packing 5 Upper Circular Plate 6 Nut 7 Forced Dispersion Device (Spray Nozzle)
8 Defoamer addition port 9 Foam detection sensor mounting port 10 Pressure switch 11 Pressure gauge mounting port 12 Exhaust port 13 Filter 14 Aseptic air inlet 15 Bottom circular plate 16 Aseptic air diffusion device 17 Stirrer 18 Stirrer 19 Silicon rubber tube 20 Bypass 21 Magnut pump rotor portion 22 Temperature detection sensor mounting port 23 pH detection sensor mounting port 24 Dissolved oxygen detection sensor mounting port 25 Acid solution inlet 26 for pH adjustment Alkaline solution inlet 27 for pH adjustment Sample outlet 28 for OD measurement Sample return port for OD measurement 29 Culture solution inlet / inoculation port 30 Magnet pump drive motor portion 31 Peristal pump 32 Acid storage bottle 33 Base storage bottle 34 Antifoam sensor 35 Antifoam agent storage bottle 36 Foam measuring device 37 Suspension device 36 Foam measurement Device 37 Suspension device 38 Weight 39 Compressor 40 Pre Filter 41 Nitrogen gas and carbon dioxide mixed gas cylinder 42 Protective cover 43 Strut 44 Hinge fitting 45 Exhaust treatment device 46 Pump 47 Aspirator 48 Caster 49 pH measurement device 50 Dissolved oxygen measurement device 51 OD measurement device 52 Hot water generation device 53 Cold water generation device 54 EOG gas processing equipment

Claims (3)

外界と完全に遮断する手段として、柔軟な膜(例えば塩化ビニール膜またはシリコンゴム膜)を使用して、折りたたんで滅菌することが可能な小型の醗酵タンク(ジャー・ファーメンター)。   A small fermentation tank (jar fermenter) that can be folded and sterilized using a flexible membrane (for example, a vinyl chloride membrane or a silicone rubber membrane) as a means of completely blocking the outside. タンクの底から上部に向かってバイパスを設けて、このバイパスに各種のセンサー取付口、培養液注入口兼接種口及びマグネットポンプを取り付けて、培養液を循環させてタンク内へ出来るだけ表面積を多くして落下させるために、タンク上部に強制分散装置を付けた特許請求の範囲第1項記載の醗酵タンク(ジャー・ファーメンター)。   A bypass is provided from the bottom to the top of the tank, and various sensor attachment ports, culture solution injection / inoculation ports and a magnet pump are attached to the bypass to circulate the culture solution and increase the surface area as much as possible into the tank. The fermentation tank (jar fermenter) according to claim 1, wherein a forcible dispersion device is attached to the upper part of the tank so as to be dropped. タンクの上層部と基底部を、高さ可変な懸架装置に取り付けて、フレキシブルなタンクを自立させ、タンクを保護するための二重構造をしたカバー中に、タンクの温度を制禦するための液体を流すことが可能な、保護カバー装置を設けた特許請求の範囲第1項記載の醗酵タンク(ジャー・ファーメンター)。
To control the temperature of the tank in a double-structured cover to protect the tank by attaching the upper layer and the base of the tank to a suspension system with a variable height so that the flexible tank can stand on its own. The fermentation tank (jar fermenter) according to claim 1, wherein a protective cover device capable of flowing a liquid is provided.
JP2003277960A 2003-07-23 2003-07-23 Fermentation tank (jar fermenter) Pending JP2005040061A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102250752A (en) * 2011-04-21 2011-11-23 吕长山 Independent air lifting dual circulation fermentation tank
JP2015128381A (en) * 2014-01-06 2015-07-16 株式会社丸菱バイオエンジ Culture device
CN107058089A (en) * 2017-03-24 2017-08-18 大连富森智能科技有限公司 Liquid spawn fermentation tank
CN108441425A (en) * 2018-04-28 2018-08-24 大连普瑞康生物技术有限公司 A kind of plant cell, organ culture device
CN110734843A (en) * 2019-11-12 2020-01-31 晨光生物科技集团股份有限公司 fermentation system and fermentation method for simulating colon environment
CN111378575A (en) * 2020-04-29 2020-07-07 湖北中向生物工程有限公司 Metarrhizium anisopliae culture apparatus
CN112170460A (en) * 2020-09-30 2021-01-05 王礼红 Organic garbage high-temperature dry-type anaerobic fermentation equipment
CN112877202A (en) * 2021-01-18 2021-06-01 刘永昶 Automatic monitoring control system of edible and medicinal fungus liquid culture fermentation system

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102250752A (en) * 2011-04-21 2011-11-23 吕长山 Independent air lifting dual circulation fermentation tank
JP2015128381A (en) * 2014-01-06 2015-07-16 株式会社丸菱バイオエンジ Culture device
CN107058089A (en) * 2017-03-24 2017-08-18 大连富森智能科技有限公司 Liquid spawn fermentation tank
CN108441425A (en) * 2018-04-28 2018-08-24 大连普瑞康生物技术有限公司 A kind of plant cell, organ culture device
CN110734843A (en) * 2019-11-12 2020-01-31 晨光生物科技集团股份有限公司 fermentation system and fermentation method for simulating colon environment
CN110734843B (en) * 2019-11-12 2023-01-17 晨光生物科技集团股份有限公司 Fermentation system and fermentation method for simulating colon environment
CN111378575A (en) * 2020-04-29 2020-07-07 湖北中向生物工程有限公司 Metarrhizium anisopliae culture apparatus
CN111378575B (en) * 2020-04-29 2023-09-19 湖北中向生物工程有限公司 Metarrhizium anisopliae culture device
CN112170460A (en) * 2020-09-30 2021-01-05 王礼红 Organic garbage high-temperature dry-type anaerobic fermentation equipment
CN112877202A (en) * 2021-01-18 2021-06-01 刘永昶 Automatic monitoring control system of edible and medicinal fungus liquid culture fermentation system
CN112877202B (en) * 2021-01-18 2024-04-16 天津山珍科技有限公司 Automatic monitoring control system of edible and medicinal fungus liquid culture fermentation system

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