JP2015053892A - Semicontinuous culture apparatus - Google Patents

Semicontinuous culture apparatus Download PDF

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JP2015053892A
JP2015053892A JP2013188748A JP2013188748A JP2015053892A JP 2015053892 A JP2015053892 A JP 2015053892A JP 2013188748 A JP2013188748 A JP 2013188748A JP 2013188748 A JP2013188748 A JP 2013188748A JP 2015053892 A JP2015053892 A JP 2015053892A
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culture
culture solution
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filtration
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友裕 今井
Tomohiro Imai
友裕 今井
昭司 磯部
Shoji Isobe
昭司 磯部
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Honda Motor Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a semicontinuous culture apparatus which has a simple structure, can separate a fungus body from a culture solution, and can maintain permeability performance over a long period of time.SOLUTION: A semicontinuous culture apparatus 1 includes: a culture tank 3 for holding a culture solution 2 and culturing a fungus; first filtering means 5 for filtering the culture solution 2 extracted from the culture tank 3 and collecting the product produced by the fungus as filtered matter; and filtrate circulating means 8 for circulating the filtrate produced by the first filtering means 5 to the culture tank 3. The semicontinuous culture apparatus also includes: solid-liquid separating means 4 which is disposed inside the culture tank 3 to separate the fungus body from the culture solution 2; and culture solution supplying means 6 for supplying the culture solution 2 from which the fungus body is separated by the solid-liquid separating means 4 to the first filtering means 5.

Description

本発明は、菌が産生した酵素等の生成物を回収するために該菌を培養する半連続培養装置に関する。   The present invention relates to a semi-continuous culture apparatus for culturing a bacterium to recover a product such as an enzyme produced by the bacterium.

従来、菌を培養する培養槽から培養液を抽出し、該培養液を濾過して、該菌が産生した酵素等の生成物を濾液として回収すると共に、濾過されなかった該培養液を該培養槽に循環させる半連続培養装置が知られている(例えば、特許文献1参照)。   Conventionally, a culture solution is extracted from a culture tank for cultivating bacteria, the culture solution is filtered, and a product such as an enzyme produced by the bacteria is collected as a filtrate, and the culture solution that has not been filtered is cultured in the culture medium. A semi-continuous culture apparatus that circulates in a tank is known (see, for example, Patent Document 1).

前記従来の半連続培養装置では、前記培養液の濾過に平均細孔径が0.01〜2.0μmの範囲にある多孔性膜を用いることにより、該培養液から前記菌を分離して前記生成物を回収することができるとされている。また、前記多孔性膜は、目詰まりしにくく、高い透過性能を長時間に亘り保持できるとされている。ところが、前記従来の半連続培養装置では、糸状菌等のように菌塊を形成する真菌等の培養を行うときには、該菌塊等の菌体により前記多孔性膜が目詰まりを起こしやすく、前記生成物を回収する性能を保持することが難しくなるという問題がある。   In the conventional semi-continuous culture apparatus, by using a porous membrane having an average pore diameter in the range of 0.01 to 2.0 μm for filtration of the culture solution, the bacteria are separated from the culture solution and generated. It is said that things can be recovered. In addition, the porous film is less likely to be clogged and can maintain high permeation performance for a long time. However, in the conventional semi-continuous culture apparatus, when culturing a fungus that forms a bacterial mass such as a filamentous fungus, the porous membrane is easily clogged by the bacterial body such as the bacterial mass, There is a problem that it is difficult to maintain the performance of recovering the product.

前記問題を解決するために、前記培養槽から抽出された培養液から前記菌体を分離するフィルタープレス等の固液分離装置を該培養槽の外部に設け、該固液分離装置で該菌体が分離された該培養液を濾過して前記生成物を濾液として回収することが考えられる。   In order to solve the above problem, a solid-liquid separation device such as a filter press for separating the bacterial cells from the culture solution extracted from the culture vessel is provided outside the culture vessel, and the bacterial cells are separated by the solid-liquid separation device. It is conceivable to collect the product as a filtrate by filtering the culture solution from which the product has been separated.

特開2009−296921号公報JP 2009-296921 A

しかしながら、前記培養槽の外部に前記固液分離装置を設けると、該固液分離装置を洗浄し、或いは滅菌する機構も必要となり、装置が複雑且つ大型化するばかりか、装置の複雑化に伴ってコンタミネーションの虞が増大するという不都合がある。   However, when the solid-liquid separation device is provided outside the culture tank, a mechanism for cleaning or sterilizing the solid-liquid separation device is also required, which not only increases the complexity and size of the device but also increases the complexity of the device. There is a disadvantage that the risk of contamination increases.

本発明は、かかる不都合を解消して、簡単な構成で前記培養液から前記菌体を分離することができ、長時間に亘って前記生成物を回収する性能を保持することができる半連続培養装置を提供することを目的とする。   The present invention eliminates such inconvenience, can separate the cells from the culture solution with a simple configuration, and can maintain the ability to recover the product over a long period of time. An object is to provide an apparatus.

かかる目的を達成するために、本発明は、培養液を収容すると共に該培養液中で菌を培養する培養槽と、該培養槽から抽出された該培養液を濾過し濾物として該菌が産生した生成物を回収する第1の濾過手段と、該第1の濾過手段の濾液を該培養槽に循環させる濾液循環手段とを備える半連続培養装置において、該培養槽内に配設された中空円筒状のフィルタを軸回りに回転させることにより、該培養液を該フィルタに対して平行に流動させ、クロスフロー濾過を行うことにより該培養液から菌体を分離する固液分離手段と、該固液分離手段により該菌体が分離された該培養液を該第1の濾過手段に供給する培養液供給手段とを備えることを特徴とする。   In order to achieve such an object, the present invention includes a culture vessel that contains a culture solution and cultures bacteria in the culture solution, and the culture solution extracted from the culture vessel is filtered to obtain the fungus as a filtrate. A semi-continuous culture apparatus comprising a first filtration means for recovering a produced product and a filtrate circulation means for circulating a filtrate of the first filtration means to the culture tank. A solid-liquid separation means for separating the cells from the culture solution by causing the culture solution to flow in parallel to the filter by rotating a hollow cylindrical filter around the axis, and performing cross-flow filtration; A culture liquid supply means for supplying the culture liquid from which the cells have been separated by the solid-liquid separation means to the first filtration means.

本発明の半連続培養装置では、前記培養槽に収容された培養液中で前記菌を培養し、該菌に酵素等の生成物を産生させることにより、該生成物を含む培養液を得ることができる。そこで、前記培養槽から抽出された前記培養液を前記第1の濾過手段で濾過することにより、濾物として該生成物を回収する一方、濾液としての該培養液を前記濾液循環手段により前記培養槽に循環させることにより、半連続培養を行う。   In the semi-continuous culture apparatus of the present invention, a culture solution containing the product is obtained by culturing the bacterium in a culture solution accommodated in the culture tank and causing the bacterium to produce a product such as an enzyme. Can do. Therefore, the culture solution extracted from the culture tank is filtered by the first filtration means to collect the product as a filtrate, while the culture solution as a filtrate is collected by the filtrate circulation means. Semi-continuous culture is performed by circulating in a tank.

このとき、前記菌の菌体が菌塊を形成する等して、前記第1の濾過手段が目詰まりを起こすことが懸念される。そこで、本発明の半連続培養装置は、前記培養槽内に前記固液分離手段を備え、該固液分離手段により前記菌体が分離された前記培養液を、前記培養液供給手段により前記第1の濾過手段に供給する。   At this time, there is a concern that the first filtering means may be clogged, for example, because the bacterial cells form a bacterial mass. Therefore, the semi-continuous culture apparatus of the present invention comprises the solid-liquid separation means in the culture tank, and the culture liquid from which the cells have been separated by the solid-liquid separation means is 1 filtration means.

前記固液分離手段は、前記中空円筒状のフィルタを軸回りに回転させることにより、前記培養槽中で前記培養液が該フィルタに対して平行に流動する流れを形成する。この結果、前記培養液に含まれる前記菌体は実質的に前記フィルタを透過することがなく、前記生成物を含む前記培養液が該フィルタを透過する。   The solid-liquid separation means forms a flow in which the culture solution flows in parallel to the filter in the culture tank by rotating the hollow cylindrical filter about its axis. As a result, the bacterial cells contained in the culture solution do not substantially permeate the filter, and the culture solution containing the product permeates the filter.

従って、前記固液分離手段はそれ自体目詰まりすることなく前記培養液から前記菌体を分離することができ、該固液分離手段により実質的に該菌体が分離された前記培養液を前記第1の濾過手段に供給することにより、該第1の濾過手段の目詰まりも防止することができる。   Therefore, the solid-liquid separation means can separate the cells from the culture without clogging itself, and the culture liquid from which the cells have been substantially separated by the solid-liquid separation means By supplying the first filtration means, clogging of the first filtration means can be prevented.

従って、本発明の半連続培養装置は、長時間に亘って前記生成物を回収する性能を保持することができる。   Therefore, the semi-continuous culture apparatus of the present invention can maintain the performance of recovering the product for a long time.

また、本発明の半連続培養装置によれば、前記固液分離手段を前記培養槽内に配設したので、該固液分離手段は該培養槽と同時に洗浄及び滅菌を行うことができ、該固液分離手段に独立の洗浄又は滅菌のための機構を設ける必要が無い。従って、本発明の半連続培養装置は、簡単な構成で前記培養液から前記菌体を分離することができ、コンタミネーションの虞も低減させることができる。   Further, according to the semi-continuous culture apparatus of the present invention, since the solid-liquid separation means is disposed in the culture tank, the solid-liquid separation means can be washed and sterilized simultaneously with the culture tank, There is no need to provide an independent cleaning or sterilization mechanism in the solid-liquid separation means. Therefore, the semi-continuous culture apparatus of the present invention can separate the cells from the culture solution with a simple configuration, and can reduce the risk of contamination.

本発明の半連続培養装置において、前記フィルタは0.001〜1.0mmの範囲の孔径の細孔を備えることが好ましい。前記フィルタは細孔の孔径が1.0mmを超えると前記菌体を十分に分離できなくなる。また、前記フィルタの細孔の孔径を0.001mm未満とすることはコストも含め技術的に難しい。   In the semi-continuous culture apparatus of the present invention, the filter preferably includes pores having a pore diameter in the range of 0.001 to 1.0 mm. If the pore diameter of the filter exceeds 1.0 mm, the cells cannot be sufficiently separated. Further, it is technically difficult to make the pore diameter of the filter smaller than 0.001 mm including the cost.

また、本発明の半連続培養装置は、前記第1の濾過手段が限外濾過膜を備えると共に、前記培養液供給手段の途中に配設され精密濾過膜を備える第2の濾過手段と、前記濾液循環手段の途中に配設され精密濾過膜を備える第3の濾過手段とを備えることが好ましい。   The semi-continuous culture apparatus of the present invention is characterized in that the first filtration means includes an ultrafiltration membrane, and the second filtration means includes a microfiltration membrane disposed in the middle of the culture solution supply means, It is preferable to include a third filtration means provided in the middle of the filtrate circulation means and provided with a microfiltration membrane.

本発明の半連続培養装置は、前記培養液供給手段の途中に精密濾過膜を備える第2の濾過手段が配設されていることにより、前記培養液から前記菌体をさらに完全に分離することができる。   The semi-continuous culture apparatus of the present invention further completely separates the cells from the culture solution by disposing a second filtration unit having a microfiltration membrane in the middle of the culture solution supply unit. Can do.

この結果、前記培養液供給手段により実質的に前記菌体を含まない前記培養液を前記第1の濾過手段に供給することができる。このとき、前記第1の濾過手段は前記限外濾過膜を備えていることにより、実質的に前記菌体を含まない前記培養液を濾過して、濾物として前記生成物を効率よく回収することができる。   As a result, the culture solution substantially free of the cells can be supplied to the first filtration unit by the culture solution supply unit. At this time, since the first filtration means includes the ultrafiltration membrane, the culture solution substantially free of the cells is filtered, and the product is efficiently recovered as a filtrate. be able to.

さらに、本発明の半連続培養装置は、前記濾液循環手段の途中に精密濾過膜を備える第3の濾過手段が配設されていることにより、前記濾液に混入する雑菌等を分離除去することができ、前記培養槽におけるコンタミネーションを確実に防止することができる。   Furthermore, the semi-continuous culture apparatus of the present invention can separate and remove germs and the like mixed in the filtrate by providing a third filtration means having a microfiltration membrane in the middle of the filtrate circulation means. It is possible to reliably prevent contamination in the culture tank.

本発明の半連続培養装置の構成を示すシステム構成図。The system block diagram which shows the structure of the semi-continuous culture apparatus of this invention. 図1に示すスピンフィルタの構成を一部破断して示す斜視図。FIG. 2 is a perspective view showing a partially broken configuration of the spin filter shown in FIG. 1.

次に、添付の図面を参照しながら本発明の実施の形態についてさらに詳しく説明する。   Next, embodiments of the present invention will be described in more detail with reference to the accompanying drawings.

図1に示すように、本実施形態の半連続培養装置1は、培養液2を収容し培養液2中で菌を培養する培養槽3と、培養槽3内に配設され、培養液2から菌体を分離する固液分離手段としてのスピンフィルタ4と、培養液2から菌が産生した生成物を回収する第1の濾過手段としての限外濾過膜装置5を備えている。スピンフィルタ4は限外濾過膜装置5に培養液2を供給する培養液供給手段としての培養液導管6に接続されており、培養液導管6は途中に配設された第2の濾過手段としての精密濾過膜装置7を介して限外濾過膜装置5に接続されている。   As shown in FIG. 1, the semi-continuous culture apparatus 1 of the present embodiment contains a culture solution 2 and a culture vessel 3 for culturing bacteria in the culture solution 2, and is disposed in the culture vessel 3. A spin filter 4 as a solid-liquid separation means for separating bacterial cells from the culture medium, and an ultrafiltration membrane device 5 as a first filtration means for recovering a product produced by the bacteria from the culture solution 2. The spin filter 4 is connected to a culture fluid conduit 6 as a culture fluid supply means for supplying the culture fluid 2 to the ultrafiltration membrane device 5, and the culture fluid conduit 6 serves as a second filtration means disposed in the middle. Is connected to the ultrafiltration membrane device 5 through the microfiltration membrane device 7.

限外濾過膜装置5は培養槽3にその濾液を循環させる濾液循環手段としての濾液導管8を備えており、濾液導管8は途中に配設された第3の濾過手段としての精密濾過膜装置9を介して培養槽3に接続されている。   The ultrafiltration membrane device 5 includes a filtrate conduit 8 as a filtrate circulation means for circulating the filtrate in the culture tank 3, and the filtrate conduit 8 is a microfiltration membrane device as a third filtration means disposed in the middle. 9 is connected to the culture tank 3 through 9.

培養槽3は、槽外の上部に設けられたモータ10から垂下されるシャフト11とシャフト11に取着された攪拌羽根12により、培養液2を攪拌することができるようになっている。   The culture tank 3 can stir the culture solution 2 by a shaft 11 suspended from a motor 10 provided at an upper portion outside the tank and a stirring blade 12 attached to the shaft 11.

スピンフィルタ4は、図2に示すように、中空シャフト13を備えており、中空シャフト13に間隔を存して外嵌された複数の円形の枠体4aと、枠体4aの外周縁に沿って配設されて中空円筒状に形成されたフィルタ4bとを備えている。また、フィルタ4bの上下は蓋体4c,4dにより密封されている。フィルタ4bは、例えば、パンチングメタル、セラミックス、樹脂等により形成され、0.001〜1.0mmの範囲の孔径の細孔を備えている。   As shown in FIG. 2, the spin filter 4 includes a hollow shaft 13, and a plurality of circular frames 4 a that are externally fitted to the hollow shaft 13 at intervals, and along the outer peripheral edge of the frame 4 a. And a filter 4b formed in a hollow cylindrical shape. The upper and lower sides of the filter 4b are sealed by lids 4c and 4d. The filter 4b is formed of, for example, punching metal, ceramics, resin, or the like, and includes pores having a pore diameter in the range of 0.001 to 1.0 mm.

中空シャフト13は培養槽3外の上部でロータリージョイント14を介して培養液導管6に接続されると共に、ロータリージョイント14の下方に設けられたプーリ15がモータ16の回転軸に接続されている。   The hollow shaft 13 is connected to the culture medium conduit 6 via the rotary joint 14 at the upper part outside the culture tank 3, and a pulley 15 provided below the rotary joint 14 is connected to the rotating shaft of the motor 16.

限外濾過膜装置5は限外濾過膜17を備えており、限外濾過膜17により培養液2を濾過して、濾物として前記菌が産生した生成物、例えば酵素が濃縮された濃縮液を得る。限外濾過膜17は、例えば、分画分子量が5000〜30000の範囲であり、中空糸膜モジュールを構成している。前記濃縮液は、限外濾過膜装置5に備えられた濃縮液導管18を介して後工程に供給される。一方、限外濾過膜17の濾液は濾液導管8により限外濾過膜装置5から排出される。   The ultrafiltration membrane device 5 includes an ultrafiltration membrane 17. The culture solution 2 is filtered by the ultrafiltration membrane 17, and the product produced by the bacterium as a filtrate, for example, a concentrated solution in which an enzyme is concentrated. Get. For example, the ultrafiltration membrane 17 has a molecular weight cut-off in the range of 5000 to 30000, and constitutes a hollow fiber membrane module. The concentrated liquid is supplied to a subsequent process through a concentrated liquid conduit 18 provided in the ultrafiltration membrane device 5. On the other hand, the filtrate of the ultrafiltration membrane 17 is discharged from the ultrafiltration membrane device 5 through the filtrate conduit 8.

精密濾過膜装置7は精密濾過膜19を備えており、精密濾過膜19により培養液2を濾過して、スピンフィルタ4で分離されなかった菌体を分離し、排出導管20から排出する。精密濾過膜19は、例えば、0.2μmの細孔径を備え中空糸膜モジュールを構成している。また、精密濾過膜装置7には、新たな培地を供給する培地導管21が接続されている。   The microfiltration membrane device 7 includes a microfiltration membrane 19. The culture solution 2 is filtered by the microfiltration membrane 19, so that the cells that have not been separated by the spin filter 4 are separated and discharged from the discharge conduit 20. The microfiltration membrane 19 has a pore diameter of 0.2 μm, for example, and constitutes a hollow fiber membrane module. The microfiltration membrane device 7 is connected to a medium conduit 21 for supplying a new medium.

精密濾過膜装置9は精密濾過膜22を備えており、濾液導管8により培養槽3に循環される濾液中の雑菌等を分離し、排出導管23から排出する。精密濾過膜22は、例えば、0.2μmの細孔径を備え平膜モジュールを構成している。   The microfiltration membrane device 9 includes a microfiltration membrane 22, which separates germs and the like in the filtrate circulated to the culture tank 3 by the filtrate conduit 8 and discharges it from the discharge conduit 23. The microfiltration membrane 22 has a pore size of 0.2 μm, for example, and constitutes a flat membrane module.

次に、本実施形態の半連続培養装置1の作動について説明する。   Next, operation | movement of the semi-continuous culture apparatus 1 of this embodiment is demonstrated.

まず、培養槽3は所定の培養液2を収容するとともに、モータ10によりシャフト11を介して回転される攪拌羽根12により培養液2を攪拌して、培養液2により菌を培養する。前記菌は、酵素等の有用な生成物を産生する菌であればよく特に限定されることはないが、糸状菌等の真菌であって、その菌体が互いに絡み合って菌塊を形成する菌を好適に用いることができる。   First, the culture tank 3 contains a predetermined culture solution 2, and the culture solution 2 is stirred by a stirring blade 12 that is rotated by a motor 10 via a shaft 11, thereby cultivating bacteria with the culture solution 2. The bacterium is not particularly limited as long as it is a bacterium that produces a useful product such as an enzyme, but is a fungus such as a filamentous fungus, and the microbial cells are entangled with each other to form a bacterial mass. Can be suitably used.

前記糸状菌として、例えば、接合菌類、子嚢菌類等の菌を挙げることができ、該糸状菌は不完全菌を含んでいてもよい。前記糸状菌として、具体的には、Aspergillus属菌、Trichoderma属菌、Penicillium属菌、Acremonium属菌、Fusarium属菌等を挙げることができる。   Examples of the filamentous fungus include bacteria such as zygomycetes and ascomycetous fungi, and the filamentous fungus may contain incomplete bacteria. Specific examples of the filamentous fungi include Aspergillus, Trichoderma, Penicillium, Acremonium, and Fusarium.

半連続培養装置1では、培養槽3で前記菌の培養を行いながら、培養液2の一部をスピンフィルタ4、培養液導管6を介して取り出す。このとき、スピンフィルタ4は、モータ16及びプーリ15を介して中空円筒状のフィルタ4bが回転されることにより、培養液2に含まれる菌体を分離する。   In the semi-continuous culture apparatus 1, a part of the culture solution 2 is taken out through the spin filter 4 and the culture solution conduit 6 while culturing the bacteria in the culture tank 3. At this time, the spin filter 4 separates the cells contained in the culture solution 2 by rotating the hollow cylindrical filter 4 b via the motor 16 and the pulley 15.

スピンフィルタ4は、前述のようにしてフィルタ4bが回転されることにより、培養液2がフィルタ4bの表面に対して平行に流動する流れを形成する。この結果、スピンフィルタ4によればクロスフロー濾過を行うことができ、実質的に前記菌体を含まず、前記菌が産生した酵素等の生成物を含む培養液2が中空円筒状のフィルタ4b内部に流入する。   The spin filter 4 forms a flow in which the culture solution 2 flows parallel to the surface of the filter 4b by rotating the filter 4b as described above. As a result, according to the spin filter 4, cross flow filtration can be performed, and the culture solution 2 substantially free of the bacterial cells and containing a product such as an enzyme produced by the fungus is a hollow cylindrical filter 4 b. Flows into the interior.

フィルタ4b内部に流入した培養液2は、中空シャフト13に設けられた図示しない孔部からその内部に流入し、中空シャフト13の内部を通って培養液導管6に導入される。従って、スピンフィルタ4によれば、培養液2が前記糸状菌の菌塊等の菌体を含む場合にも該菌体により目詰まりすることなく、該菌体を分離することができる。   The culture solution 2 that has flowed into the filter 4 b flows into the inside of a hole (not shown) provided in the hollow shaft 13 and is introduced into the culture solution conduit 6 through the hollow shaft 13. Therefore, according to the spin filter 4, even when the culture solution 2 contains microbial cells such as the fungal mass of the filamentous fungus, the microbial cells can be separated without being clogged by the microbial cells.

次に、スピンフィルタ4により前記菌体が分離された培養液2は、培養液導管6を介して精密濾過膜装置7に供給される。精密濾過膜装置7では、精密濾過膜19により培養液2を濾過し、スピンフィルタ4で分離されずにわずかに培養液2に混入している菌体をも分離し、排出導管20から排出する。また、精密濾過膜装置7では、培地導管21から供給される新たな培地を培養液2に溶解すると共に、該培地に含まれる雑菌等を精密濾過膜19により分離する。前記雑菌等は前記菌体と共に排出導管20により廃棄される。   Next, the culture solution 2 from which the cells have been separated by the spin filter 4 is supplied to the microfiltration membrane device 7 through the culture solution conduit 6. In the microfiltration membrane device 7, the culture solution 2 is filtered by the microfiltration membrane 19, and the microbial cells slightly mixed in the culture solution 2 without being separated by the spin filter 4 are also separated and discharged from the discharge conduit 20. . Further, in the microfiltration membrane device 7, a new culture medium supplied from the culture medium conduit 21 is dissolved in the culture solution 2, and germs and the like contained in the culture medium are separated by the microfiltration membrane 19. The miscellaneous bacteria and the like are discarded together with the cells by the discharge conduit 20.

精密濾過膜装置7で濾過された培養液2は、次に、培養液導管6を介して限外濾過膜装置5に供給され、限外濾過膜17により濾過される。この段階の培養液2には菌体は含まれていないが、菌により産生された酵素等の生成物が含まれている。そこで、限外濾過膜17により濾過されることにより、濾物として前記酵素等の生成物が濃縮された濃縮液が得られ、該濃縮液は濃縮液導管18により、バイオエタノール製造工程等の次工程に供給される。   The culture solution 2 filtered by the microfiltration membrane device 7 is then supplied to the ultrafiltration membrane device 5 via the culture solution conduit 6 and filtered by the ultrafiltration membrane 17. The culture solution 2 at this stage does not contain bacterial cells, but contains products such as enzymes produced by the bacteria. Thus, by filtering through the ultrafiltration membrane 17, a concentrated solution in which the product such as the enzyme is concentrated as a filtrate is obtained. Supplied to the process.

一方、限外濾過膜装置5の濾液は、菌体も菌の産生する生成物も含まない培養液2のみであるので、濾液導管8により精密濾過膜装置9を介して培養槽3に循環される。精密濾過膜装置9では、前記濾液としての培養液2は精密濾過膜22で濾過され、雑菌等が濾物として分離される。前記雑菌等の濾物は、排出導管23により廃棄される。   On the other hand, since the filtrate of the ultrafiltration membrane device 5 is only the culture solution 2 that does not contain the cells and the products produced by the bacteria, it is circulated to the culture tank 3 via the microfiltration membrane device 9 by the filtrate conduit 8. The In the microfiltration membrane device 9, the culture solution 2 as the filtrate is filtered through the microfiltration membrane 22, and various germs and the like are separated as filtrate. Filtrate such as bacteria is discarded through the discharge conduit 23.

本実施形態の半連続培養装置1によれば、前述のようにすることにより、糸状菌等の菌塊を形成する菌の場合にもフィルタ4bが目詰まりすることなく、該菌により産生された酵素等の生成物を回収することができる。また、培養槽3から取り出された培養液2は、新たな培地が添加されて培養槽3に循環されるので、前記菌の半連続培養を行うことができる。   According to the semi-continuous culture apparatus 1 of the present embodiment, the filter 4b was produced by the bacteria without clogging even in the case of bacteria forming a bacterial mass such as filamentous fungi, as described above. Products such as enzymes can be recovered. Moreover, since the culture solution 2 taken out from the culture tank 3 is circulated to the culture tank 3 by adding a new medium, semi-continuous culture of the bacteria can be performed.

さらに、本実施形態の半連続培養装置1は培養槽3内にスピンフィルタ4が配設されているので、運転を休止した際等に装置の洗浄、滅菌を行うときには、培養槽3とスピンフィルタ4とを一緒に洗浄、滅菌することができる。   Furthermore, since the spin filter 4 is disposed in the culture tank 3 in the semi-continuous culture apparatus 1 of the present embodiment, the culture tank 3 and the spin filter are used when the apparatus is cleaned and sterilized when the operation is stopped. 4 can be washed and sterilized together.

1…半連続培養装置、 2…培養液、 3…培養槽、 4…スピンフィルタ、 5…限外濾過膜装置、 6…培養液導管、 7…精密濾過膜装置、 8…濾液導管、 9…精密濾過膜装置。   DESCRIPTION OF SYMBOLS 1 ... Semi-continuous culture apparatus, 2 ... Culture solution, 3 ... Culture tank, 4 ... Spin filter, 5 ... Ultrafiltration membrane apparatus, 6 ... Culture solution conduit, 7 ... Microfiltration membrane device, 8 ... Filtrate conduit, 9 ... Microfiltration membrane device.

Claims (3)

培養液を収容すると共に該培養液中で菌を培養する培養槽と、該培養槽から抽出された該培養液を濾過し濾物として該菌が産生した生成物を回収する第1の濾過手段と、該第1の濾過手段の濾液を該培養槽に循環させる濾液循環手段とを備える半連続培養装置において、
該培養槽内に配設された中空円筒状のフィルタを軸回りに回転させることにより、該培養液を該フィルタに対して平行に流動させ、クロスフロー濾過を行うことにより該培養液から菌体を分離する固液分離手段と、該固液分離手段により該菌体が分離された該培養液を該第1の濾過手段に供給する培養液供給手段とを備えることを特徴とする半連続培養装置。
A culture tank for containing the culture solution and culturing the fungus in the culture solution, and a first filtering means for collecting the product produced by the fungus by filtering the culture solution extracted from the culture vessel And a semi-continuous culture apparatus comprising a filtrate circulation means for circulating the filtrate of the first filtration means to the culture tank,
By rotating a hollow cylindrical filter disposed in the culture tank around the axis, the culture fluid is caused to flow in parallel to the filter, and cross-flow filtration is performed, thereby producing bacterial cells from the culture fluid. A semi-continuous culture, comprising: a solid-liquid separation means for separating the culture medium; and a culture liquid supply means for supplying the culture liquid from which the cells have been separated by the solid-liquid separation means to the first filtration means. apparatus.
請求項1記載の半連続培養装置において、前記フィルタは0.001〜1.0mmの範囲の孔径の細孔を備えることを特徴とする半連続培養装置。   The semi-continuous culture apparatus according to claim 1, wherein the filter includes pores having a pore diameter in the range of 0.001 to 1.0 mm. 請求項1又は請求項2記載の半連続培養装置において、前記第1の濾過手段は限外濾過膜を備えると共に、前記培養液供給手段の途中に配設され精密濾過膜を備える第2の濾過手段と、前記濾液循環手段の途中に配設され精密濾過膜を備える第3の濾過手段とを備えることを特徴とする半連続培養装置。   The semi-continuous culture apparatus according to claim 1 or 2, wherein the first filtration means includes an ultrafiltration membrane, and the second filtration includes a microfiltration membrane disposed in the middle of the culture solution supply means. A semi-continuous culture apparatus comprising: means; and third filtration means provided in the middle of the filtrate circulation means and provided with a microfiltration membrane.
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JP2018011530A (en) * 2016-07-19 2018-01-25 株式会社日立製作所 Separation apparatus, culture apparatus, and separation method
WO2018159847A1 (en) 2017-03-03 2018-09-07 富士フイルム株式会社 Cell culture device and cell culture method
US20210163865A1 (en) * 2017-06-30 2021-06-03 Toray Industries, Inc. Production method and production device for chemical by continuous fermentation
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Publication number Priority date Publication date Assignee Title
JP2018011530A (en) * 2016-07-19 2018-01-25 株式会社日立製作所 Separation apparatus, culture apparatus, and separation method
WO2018159847A1 (en) 2017-03-03 2018-09-07 富士フイルム株式会社 Cell culture device and cell culture method
JPWO2018159847A1 (en) * 2017-03-03 2019-06-27 富士フイルム株式会社 Cell culture apparatus and cell culture method
US11725174B2 (en) 2017-03-03 2023-08-15 Fujifilm Corporation Cell culture apparatus and cell culture method
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US20210163865A1 (en) * 2017-06-30 2021-06-03 Toray Industries, Inc. Production method and production device for chemical by continuous fermentation
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