JPH0529400U - Incubator - Google Patents

Incubator

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Publication number
JPH0529400U
JPH0529400U JP8578791U JP8578791U JPH0529400U JP H0529400 U JPH0529400 U JP H0529400U JP 8578791 U JP8578791 U JP 8578791U JP 8578791 U JP8578791 U JP 8578791U JP H0529400 U JPH0529400 U JP H0529400U
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JP
Japan
Prior art keywords
draft tube
culture
tank
stirring blade
accelerating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP8578791U
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Japanese (ja)
Other versions
JP2519058Y2 (en
Inventor
弘三 永易
学 政本
泰彦 今井
Original Assignee
食品産業超高圧利用技術研究組合
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Priority to JP1991085787U priority Critical patent/JP2519058Y2/en
Publication of JPH0529400U publication Critical patent/JPH0529400U/en
Application granted granted Critical
Publication of JP2519058Y2 publication Critical patent/JP2519058Y2/en
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    • 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
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02Stirrer or mobile mixing elements

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

Abstract

(57)【要約】 (修正有) 【目的】 菌体、細胞等を培養液中で効率よく培養す
る。とくに、高粘度の培養液を高い気液接触効率で混合
することを目的とする。 【構成】 回転するドラフトチューブ10の上部に下降
流加速用攪拌翼20を設け、ドラフトチューブ10の下
部近傍に底部液排出加速用攪拌翼22を設け、ドラフト
チューブ10の外底部又は内部に散気管24、46を設
ける。さらには、ドラフトチューブ10の外周部に、回
転することにより上向きの力が生じる突起物28、44
を設ける。
(57) [Summary] (Correction) [Purpose] Efficiently cultivate cells, cells, etc. in culture medium. In particular, the purpose is to mix a highly viscous culture solution with high gas-liquid contact efficiency. [Structure] A stirring blade 20 for accelerating a downward flow is provided on an upper portion of a rotating draft tube 10, a stirring blade 22 for accelerating a bottom liquid is provided near a lower portion of the draft tube 10, and an air diffuser is provided on an outer bottom portion or inside of the draft tube 10. 24 and 46 are provided. Further, on the outer peripheral portion of the draft tube 10, the protrusions 28, 44 that generate an upward force by rotating.
To provide.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は、菌体、細胞等を培養液中で効率よく培養する装置、とくに、高粘度 の培養液を高い気液接触効率で混合する培養装置に関するものである。 The present invention relates to an apparatus for efficiently culturing cells, cells and the like in a culture solution, and more particularly to a culture apparatus for mixing a highly viscous culture solution with high gas-liquid contact efficiency.

【0002】[0002]

【従来の技術】[Prior Art]

従来の培養装置の主流は、槽内に菌体、細胞等を加えた培養液を満たし、攪拌 機により攪拌するとともに、槽下方から空気等のガスを吹き込んで、培養液を循 環させて気液接触を行なうことにより反応を進行させる、いわゆる通気攪拌方式 であった。しかし、培養の種類によっては、攪拌による強いせん断力で菌体又は 細胞へ大きな影響を与える場合がある。さらに、設置面積を小さくする必要もあ り、縦型(塔型)培養槽の各種培養系への適用が検討されだしている。 塔型培養槽の主流は、ドラフトチューブを槽内に設け、槽内に菌体、細胞等を 加えた培養液を満たし、槽下方から空気等のガスを吹き込んで、培養液を循環さ せて気液接触を行なう気泡塔方式であった。 The main stream of conventional culture equipment is to fill the tank with a culture solution containing cells, cells, etc., stir it with a stirrer, and blow gas such as air from below the tank to circulate the culture solution. It was a so-called aeration and stirring method in which the reaction was allowed to proceed by contacting with the liquid. However, depending on the type of culture, strong shearing force due to agitation may have a large effect on cells or cells. Furthermore, there is a need to reduce the installation area, and application of vertical type (tower type) culture tanks to various culture systems is being studied. The mainstream of a tower culture tank is to install a draft tube inside the tank, fill the tank with a culture solution containing cells, cells, etc., and blow gas such as air from below the tank to circulate the culture solution. It was a bubble column system in which gas-liquid contact was performed.

【0003】 従来、特開昭63−251077号公報には、培養槽内部に、軸流羽根車を設 けた円筒(ドラフトチューブ)を設置し、羽根車を回転させることにより、培養 液を吸い上げ、上部から外周部へ流下させたことで酸素を培養液に与え培養させ る装置が記載されている。また、円筒を軸流羽根車の外周と一体化して、羽根車 とともに円筒を回転させることも記載されている。 また、特開昭55−15718号公報には、ドラフトチューブ上半分にスリッ トを付け、その内部に、気体を液体中に拡散させるためのスパージャーを設け、 さらに、ドラフトチューブ最下端に、液体をチューブ外へ排出させる軸流インペ ラーを備えた培養装置が記載されている。Conventionally, in Japanese Patent Laid-Open No. 63-251077, a cylinder (draft tube) provided with an axial flow impeller is installed inside a culture tank, and the impeller is rotated to suck up a culture solution. It describes an apparatus that feeds oxygen to the culture medium for culturing by flowing it down from the upper part to the outer peripheral part. It is also described that the cylinder is integrated with the outer circumference of the axial flow impeller and the cylinder is rotated together with the impeller. Further, in JP-A-55-15718, a slit is attached to the upper half of the draft tube, and a sparger for diffusing gas into the liquid is provided therein, and further, a liquid is provided at the lowermost end of the draft tube. There is described a culture device equipped with an axial flow impeller that discharges water outside the tube.

【0004】[0004]

【考案が解決しようとする課題】[Problems to be solved by the device]

しかし、上記の従来技術においては、麹菌の液体培養のごとき、好気性培養で 、かつ高粘度条件となる液体発酵には、十分に対応できなかった。 また、特開昭63−251077号公報記載の培養装置では、酸素供給が培養 液落下による気体(空気)巻き込みにのみ依存するため、酸素供給速度に限界が あり、高粘度条件下でも高い酸素供給が必要な麹菌培養等での対応は難しい。 また、特開昭55−15718号公報記載の培養装置では、通常の培養におい ては、高い酸素供給能力を発揮できるが、粘度が上昇した場合、槽全体の流動を 均一にすることは困難となり、酸素の供給能力も低下し、同じく麹菌等の培養に は適さなくなる。 一般に培養槽としてよく使用されている攪拌槽形式であると、高粘度になると 、攪拌翼部分のみが攪拌され、槽全体を均一に攪拌するためには、特殊な攪拌翼 形状の設置と、強大な攪拌動力が必要となる。 上記の攪拌槽形式で槽全体を均一にするため、強力に攪拌を実施する場合、麹 菌等の糸状菌では、機械的なせん断により菌体がダメージを受けやすい。 本考案は、上記の諸点に鑑みなされたもので、高粘度の培養液であっても均一 に混合することができ、気液接触効率が高く、かつ、菌体へのダメージの少ない 培養装置を提供することを目的とするものである。 However, the above-mentioned conventional techniques cannot sufficiently cope with liquid fermentation such as liquid culture of Aspergillus oryzae, which is aerobic culture and has a high viscosity condition. Further, in the culture device described in JP-A-63-251077, the oxygen supply depends only on the entrainment of gas (air) due to the dropping of the culture solution, so the oxygen supply rate is limited, and the high oxygen supply is achieved even under high viscosity conditions. It is difficult to respond to the koji mold culture that requires Further, in the culture device described in JP-A-55-15718, a high oxygen supply capacity can be exhibited in ordinary culture, but when the viscosity increases, it becomes difficult to make the flow of the whole tank uniform. Also, the oxygen supply capacity is reduced, and it becomes unsuitable for culturing koji mold. With the stirring tank type that is commonly used as a culture tank, when the viscosity becomes high, only the stirring blade section is stirred, and in order to uniformly stir the entire tank, a special stirring blade shape must be installed and A strong stirring power is required. In order to make the whole tank uniform in the above stirring tank type, when strongly stirring is performed, filamentous fungi such as koji mold are likely to be damaged by mechanical shearing. The present invention has been made in view of the above points, and provides a culture apparatus capable of uniformly mixing even a high-viscosity culture solution, having high gas-liquid contact efficiency and less damage to bacterial cells. It is intended to be provided.

【0005】[0005]

【課題を解決するための手段】[Means for Solving the Problems]

上記の目的を達成するために、本考案の培養装置は、図面を参照して説明すれ ば、上下端が開放されたドラフトチューブ10を、縦型培養槽12内に槽側壁1 4、槽底壁16及び槽蓋18との間に間隙が生じるように設置した培養装置にお いて、 ドラフトチューブ10内の上部に設けられた下降流加速用攪拌翼20と、 ドラフトチューブ10の下部近傍に設けられた底部液排出加速用攪拌翼22と 、 ドラフトチューブ10の外底部又は内部に設けられた散気管24、46と、 ドラフトチューブ10を回転させる回転軸26と、 を備えたことを特徴としている。 上記の培養装置において、下降流加速用攪拌翼20の回転軸と、底部液排出加 速用攪拌翼22の回転軸と、ドラフトチューブ10回転用の回転軸26とを共用 するように構成するのが望ましい。 また、ドラフトチューブ10の外周部に、ドラフトチューブが回転することに より上向きの力が生じるような形状の突起物28、44を設けるのが望ましい。 In order to achieve the above object, the culture device of the present invention comprises a draft tube 10 whose upper and lower ends are opened in a vertical culture tank 12, a tank side wall 14 and a tank bottom. In a culture device installed so that a gap is created between the wall 16 and the tank lid 18, a downflow accelerating stirring blade 20 provided in an upper part of the draft tube 10 and a lower part of the draft tube 10 are provided. A bottom blade discharge acceleration stirring blade 22 provided therein; diffuser tubes 24 and 46 provided at an outer bottom portion or inside of the draft tube 10; and a rotary shaft 26 for rotating the draft tube 10. .. In the above-mentioned culture device, the rotating shaft of the stirring blade 20 for accelerating the downflow, the rotating shaft of the stirring blade 22 for accelerating the bottom liquid, and the rotating shaft 26 for rotating the draft tube 10 are configured to be shared. Is desirable. Further, it is desirable to provide, on the outer peripheral portion of the draft tube 10, projections 28 and 44 having a shape such that an upward force is generated by the rotation of the draft tube.

【0006】[0006]

【作用】[Action]

培養槽12内に同心円状に設置されたドラフトチューブ10を、槽外部の駆動 装置(図示せず)で回転させると同時に、下降流加速用攪拌翼20及び底部液排 出加速用攪拌翼22を回転させ、培養液の下向きの流れを加速させるとともに、 ドラフトチューブ内の液体をドラフトチューブ外へ加速しながら排出する。培養 液への酸素供給は、ドラフトチューブ外底部に円周状に設置された散気管24か ら上向きに空気を噴出し、外周部の培養液の上昇流を加速させながら行なわれる 。 また、散気管46がドラフトチューブ内に設置されている場合は、散気管46 から下向きに空気を噴出し、ドラフトチューブ内の培養液の下降流を加速させな がら空気が混合される。 さらに、ドラフトチューブ外周部に突起物28、44を設けている場合は、回 転するドラフトチューブにより、外周部の培養液の上昇流が加速される。 The draft tube 10 installed concentrically in the culture tank 12 is rotated by a drive device (not shown) outside the tank, and at the same time, the stirring blade 20 for accelerating the downward flow and the stirring blade 22 for accelerating the bottom liquid discharge are set. Rotate to accelerate the downward flow of the culture solution and discharge the liquid in the draft tube while accelerating it out of the draft tube. Oxygen is supplied to the culture medium by blasting air upward from the air diffuser 24 circumferentially installed on the outer bottom of the draft tube to accelerate the upward flow of the culture medium in the outer peripheral portion. When the air diffuser 46 is installed in the draft tube, air is jetted downward from the air diffuser 46 to mix the air while accelerating the downward flow of the culture solution in the draft tube. Furthermore, when the protrusions 28 and 44 are provided on the outer peripheral portion of the draft tube, the rotating draft tube accelerates the upward flow of the culture solution in the outer peripheral portion.

【0007】[0007]

【実施例】【Example】

以下、図面を参照して本考案の好適な実施例を詳細に説明する。ただし、この 実施例に記載されている構成機器の形状、その相対配置などは、とくに特定的な 記載がない限りは、本考案の範囲をそれらのみに限定する趣旨のものではなく、 単なる説明例にすぎない。 実施例1 図1において、10は上下端が開放された円筒状のドラフトチューブで、円筒 状の縦型培養槽12内に、槽側壁14、槽底壁16及び槽蓋18との間に間隙が 生じるように同心円状に設置される。 ドラフトチューブ10内の上部には、下降流加速用攪拌翼20が設けられ、ド ラフトチューブ10の下側には、底部液排出加速用攪拌翼22が設けられる。ド ラフトチューブ10の外底部には、散気管24が設けられる。26は回転軸で、 ドラフトチューブ10、下降流加速用攪拌翼20及び底部液排出加速用攪拌翼2 2を回転させるためのものである。 ドラフトチューブ10の外周部には、ドラフトチューブが回転することにより 上向きの力が生じるような形状の、スパイラル状又は傾斜板状の突起物28が設 けられている。また、ドラフトチューブ10の上部には、複数のスリット30が 設けられている。このスリット30は、液面がスリット30近辺まで下降したと きに、液をドラフトチューブ10内に流入させるためのものである。32、34 はドラフトチューブ10と回転軸26を連結するための連結具、36は邪魔板、 38は培養液入口、40は液出口、42は排気口である。 Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the drawings. However, unless otherwise specified, the shapes of the components and the relative arrangements of the constituent devices described in this embodiment are not intended to limit the scope of the present invention thereto, but are merely explanatory examples. Nothing more. Example 1 In FIG. 1, reference numeral 10 denotes a cylindrical draft tube having open upper and lower ends, and a space is provided in a cylindrical vertical culture tank 12 between a tank side wall 14, a tank bottom wall 16 and a tank lid 18. Are installed concentrically so that A stirring blade 20 for accelerating the descending flow is provided in the upper portion of the draft tube 10, and a stirring blade 22 for accelerating the bottom liquid discharge is provided below the draft tube 10. An air diffuser 24 is provided on the outer bottom of the draft tube 10. Reference numeral 26 denotes a rotating shaft for rotating the draft tube 10, the descending flow accelerating stirring blade 20 and the bottom liquid discharge accelerating stirring blade 22. On the outer peripheral portion of the draft tube 10, there is provided a spiral or inclined plate-like protrusion 28 having a shape in which an upward force is generated by the rotation of the draft tube. Further, a plurality of slits 30 are provided on the upper portion of the draft tube 10. The slit 30 is for allowing the liquid to flow into the draft tube 10 when the liquid surface descends to the vicinity of the slit 30. Reference numerals 32 and 34 are connecting tools for connecting the draft tube 10 and the rotary shaft 26, 36 is a baffle plate, 38 is a culture solution inlet, 40 is a solution outlet, and 42 is an exhaust port.

【0008】 実施例2 本実施例は、連続した突起物を代わりに、図2に示すように、不連続の突起物 44を設けたものである。他の構成は図1の場合と同様である。Embodiment 2 In this embodiment, instead of a continuous projection, a discontinuous projection 44 is provided as shown in FIG. Other configurations are similar to those in the case of FIG.

【0009】 実施例3 本実施例は、図3に示すように、ドラフトチューブ10内に下向きに空気を噴 出する散気管46を設けたものである。図3では、一例として、回転軸26を中 空状とし、この中空部に空気を供給して、散気管46から下向きに噴出するよう にしている。この散気管46は、底部の散気管の代わりに設けてもよく、又は両 者を設けてもよい。他の構成は図1の場合と同様である。Embodiment 3 In this embodiment, as shown in FIG. 3, an air diffuser 46 for ejecting air downward is provided in the draft tube 10. In FIG. 3, as an example, the rotary shaft 26 is hollow, and air is supplied to this hollow portion so that the air is ejected downward from the air diffusing pipe 46. This air diffuser 46 may be provided in place of the bottom air diffuser or both may be provided. Other configurations are similar to those in the case of FIG.

【0010】[0010]

【考案の効果】[Effect of the device]

本考案は、上記のように構成されているので、つぎのような効果を奏する。 (1) 高濃度菌体培養時等の高粘度(非ニュートン流体)に対しても、槽内全 体が均一に混合でき、気液接触効率が高くなる。 (2) ドラフトチューブ内の上部に下降流加速用攪拌翼を設けるとともに、ド ラフトチューブの下部近傍に底部液排出加速用攪拌翼を設けているので、効率よ く培養液を循環させることができる。 (3) ドラフトチューブの外周部にスパイラル状の連続又は不連続の突起物を 設ける場合は、培養液がドラフトチューブの外周部でスパイラル状に流動し、こ のため、菌体が一部自己増粒し、菌体の高濃度化が促進される。また、ドラフト チューブの回転エネルギーで液体を主に流動させるため、菌体へのダメージが少 ない。 Since the present invention is configured as described above, it has the following effects. (1) Even for high viscosity (non-Newtonian fluid) during high-concentration cell culture, the whole tank can be uniformly mixed, and the gas-liquid contact efficiency becomes high. (2) Since the stirring blade for accelerating the downflow is provided in the upper part of the draft tube and the stirring blade for accelerating the bottom liquid discharge is provided near the lower part of the draft tube, the culture solution can be circulated efficiently. .. (3) When a spiral continuous or discontinuous projection is provided on the outer periphery of the draft tube, the culture fluid spirally flows on the outer periphery of the draft tube, which causes some bacterial cells to self-proliferate. Granules are promoted to increase the concentration of bacterial cells. Also, since the liquid mainly flows by the rotational energy of the draft tube, there is little damage to the cells.

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

【図1】本考案の一実施例を示す培養装置の縦断面説明
図である。
FIG. 1 is an explanatory longitudinal sectional view of a culture device showing an embodiment of the present invention.

【図2】本考案の他の実施例を示す培養装置の縦断面説
明図である。
FIG. 2 is a vertical cross-sectional explanatory view of a culture device showing another embodiment of the present invention.

【図3】本考案のさらに他の実施例を示す培養装置の縦
断面説明図である。
FIG. 3 is a vertical cross-sectional explanatory view of a culture device showing still another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 ドラフトチューブ 12 培養槽 14 槽側壁 16 槽底壁 18 槽蓋 20 下降流加速用攪拌翼 22 底部液排出加速用攪拌翼 24 散気管 26 回転軸 28 突起物 30 スリット 36 邪魔板 44 突起物 46 散気管 10 Draft Tube 12 Culture Tank 14 Tank Side Wall 16 Tank Bottom Wall 18 Tank Lid 20 Downflow Acceleration Stirring Blade 22 Bottom Liquid Discharge Acceleration Stirring Blade 24 Diffuser Tube 26 Rotating Shaft 28 Projection 30 Slit 36 Baffle Plate 44 Projection 46 Dispersion trachea

Claims (3)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 上下端が開放されたドラフトチューブ
(10)を、縦型培養槽(12)内に槽側壁(14)、
槽底壁(16)及び槽蓋(18)との間に間隙が生じる
ように設置した培養装置において、 ドラフトチューブ(10)内の上部に設けられた下降流
加速用攪拌翼(20)と、 ドラフトチューブ(10)の下部近傍に設けられた底部
液排出加速用攪拌翼(22)と、 ドラフトチューブ(10)の外底部又は内部に設けられ
た散気管(24)、(46)と、 ドラフトチューブ(10)を回転させる回転軸(26)
と、 を備えたことを特徴とする培養装置。
1. A draft tube (10) having open upper and lower ends is provided in a vertical culture tank (12) on a side wall (14) of the tank.
In a culture device installed so that a gap is created between the tank bottom wall (16) and the tank lid (18), a downflow accelerating stirring blade (20) provided in the upper part of the draft tube (10), A stirring blade (22) for accelerating the bottom liquid discharge provided near the lower portion of the draft tube (10), air diffusers (24), (46) provided on the outer bottom portion or inside of the draft tube (10), and a draft Rotating shaft (26) for rotating the tube (10)
And a culture device.
【請求項2】 下降流加速用攪拌翼(20)の回転軸
と、底部液排出加速用攪拌翼(22)の回転軸と、ドラ
フトチューブ(10)回転用の回転軸(26)とを共用
するようにしたことを特徴とする請求項1記載の培養装
置。
2. The rotating shaft of the stirring blade (20) for downflow acceleration, the rotating shaft of the stirring blade (22) for accelerating the bottom liquid discharge, and the rotating shaft (26) for rotating the draft tube (10). The culture device according to claim 1, wherein
【請求項3】 ドラフトチューブ(10)の外周部に、
ドラフトチューブが回転することにより上向きの力が生
じるような形状の突起物(28)、(44)を設けたこ
とを特徴とする請求項1又は2記載の培養装置。
3. The outer periphery of the draft tube (10),
The culture device according to claim 1 or 2, further comprising protrusions (28) and (44) each having a shape such that an upward force is generated by rotating the draft tube.
JP1991085787U 1991-09-24 1991-09-24 Incubator Expired - Lifetime JP2519058Y2 (en)

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JP2519058Y2 JP2519058Y2 (en) 1996-12-04

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003507158A (en) * 1999-08-12 2003-02-25 オウトクンプ オサケイティオ ユルキネン Reaching solids from sludge
JP2006510484A (en) * 2002-12-16 2006-03-30 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー Apparatus and method for producing crystals / precipitates / particles
JP2010178734A (en) * 2009-01-08 2010-08-19 Ihi Corp Agitator
KR101340712B1 (en) * 2010-01-20 2013-12-12 에스케이이노베이션 주식회사 Mix apparatus including draft tube

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS545091A (en) * 1977-06-01 1979-01-16 Ranks Hovis Mcdougall Ltd Fermentation promoting method and fermentor
JPH02104276A (en) * 1988-05-11 1990-04-17 Imperial Chem Ind Plc <Ici> Antiseptic culture method and apparatus
JPH032158U (en) * 1989-05-31 1991-01-10

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS545091A (en) * 1977-06-01 1979-01-16 Ranks Hovis Mcdougall Ltd Fermentation promoting method and fermentor
JPH02104276A (en) * 1988-05-11 1990-04-17 Imperial Chem Ind Plc <Ici> Antiseptic culture method and apparatus
JPH032158U (en) * 1989-05-31 1991-01-10

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003507158A (en) * 1999-08-12 2003-02-25 オウトクンプ オサケイティオ ユルキネン Reaching solids from sludge
JP2006510484A (en) * 2002-12-16 2006-03-30 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー Apparatus and method for producing crystals / precipitates / particles
JP2010178734A (en) * 2009-01-08 2010-08-19 Ihi Corp Agitator
KR101340712B1 (en) * 2010-01-20 2013-12-12 에스케이이노베이션 주식회사 Mix apparatus including draft tube

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