JPH0212136B2 - - Google Patents
Info
- Publication number
- JPH0212136B2 JPH0212136B2 JP60210018A JP21001885A JPH0212136B2 JP H0212136 B2 JPH0212136 B2 JP H0212136B2 JP 60210018 A JP60210018 A JP 60210018A JP 21001885 A JP21001885 A JP 21001885A JP H0212136 B2 JPH0212136 B2 JP H0212136B2
- Authority
- JP
- Japan
- Prior art keywords
- heat transfer
- stirring
- tank
- header
- annular
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F35/93—Heating or cooling systems arranged inside the receptacle
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Accessories For Mixers (AREA)
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は、微生物や細胞を培養するための撹拌
培養や、重合装置等に用いるに好適な高伝熱型撹
拌装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a high heat transfer type stirring device suitable for use in stirring culture for culturing microorganisms and cells, polymerization equipment, etc.
従来、高伝熱型撹拌装置は、撹拌槽本体内にコ
イル状に巻かれた伝熱管を配置し、この伝熱管に
冷媒または熱媒を循環させることによつて、槽内
部の温度を急速に冷却または加温していた。この
種の撹拌装置は、例えば、東京大学出版会によつ
て出版されている合葉修一他の著書である「生物
化学工学」の第313頁に開示されている。
Conventionally, high heat transfer type stirring devices have a coiled heat transfer tube placed inside the stirring tank body, and by circulating a refrigerant or heating medium through the heat transfer tube, the temperature inside the tank can be rapidly increased. It was being cooled or heated. This type of stirring device is disclosed, for example, on page 313 of "Biochemical Engineering" by Shuichi Aiba et al., published by the University of Tokyo Press.
ところで、上述した装置においては、撹拌の効
果を上げるために本体壁にバツフルを設ける場
合、コイル状の伝熱管がバツフルに接触しないよ
うに配置する必要があり、結局伝熱管の伝熱面積
を大きくとることができない。また、コイル状の
伝熱管は、槽の下部から上部にわたつて配設され
るため、本体壁近傍と撹拌軸近傍が分断されてお
り、本体壁の洗浄を十分に行なうことが難しいと
いう問題も残されている。 By the way, in the above-mentioned device, when a baffle is provided on the main body wall to increase the stirring effect, it is necessary to arrange the coiled heat transfer tube so that it does not come into contact with the buffle, which ultimately increases the heat transfer area of the heat transfer tube. I can't take it. In addition, since the coiled heat transfer tube is arranged from the bottom to the top of the tank, the area near the main body wall and the area near the stirring shaft are separated, which poses the problem of making it difficult to thoroughly clean the main body wall. left behind.
本発明の目的は、伝熱面積を大きくすると共
に、バツフル効果により伝熱を効果的に行なうこ
とのできる高伝熱型撹拌装置を提供することであ
る。
An object of the present invention is to provide a high heat transfer type stirring device that can increase the heat transfer area and effectively transfer heat by the buffling effect.
本発明は、撹拌槽内中央部に設けられた撹拌翼
を有する撹拌軸と、該撹拌軸の外周部に位置し撹
拌槽内の上部および下部にそれぞれ設けられた同
芯状の複数の環状ヘツダーと、該上下の複数の環
状ヘツダー間にそれぞれ設けられ、かつ、ヘツダ
ーの円周方向に局部的に集中させて配設された複
数の伝熱管と、上下の複数の環状ヘツダーにそれ
ぞれ独立して設けられた冷媒または熱媒を槽外部
より供給したり抜出すための出入口とを設けたこ
とを特徴とする。
The present invention provides a stirring shaft having stirring blades provided in the center of the stirring tank, and a plurality of concentric annular headers located on the outer periphery of the stirring shaft and provided at the upper and lower parts of the stirring tank, respectively. , a plurality of heat exchanger tubes provided between the plurality of upper and lower annular headers and locally concentrated in the circumferential direction of the header, and a plurality of heat exchanger tubes independently provided in the plurality of upper and lower annular headers. It is characterized by being provided with an inlet/outlet for supplying or extracting the provided refrigerant or heating medium from the outside of the tank.
以下、本発明を具体的な実施例に基づき詳細に
説明する。
Hereinafter, the present invention will be explained in detail based on specific examples.
第1図は本発明の一実施例に係る図で、縦断面
図を示す。また、第2図は第1図のA−A断面図
を示す。これらの図において、1は撹拌槽本体で
あり、8は槽中央部に設けられた撹拌軸である。
また、7a,7bは撹拌軸8に取付けられた撹拌
翼である。2a,2b,2cは、それぞれ槽上部
の環状ヘツダーである。また、3a,3b,3c
は、それぞれ槽下部の環状ヘツダーである。2a
と3aは上下一組の環状ヘツダーであり、同様に
2bと3b、2cと3cもそれぞれ上下一組の環
状ヘツダーである。したがつて、この実施例にお
いては、三組の環状ヘツダーが配置されている。
6aは伝熱管であり、2aと3aとで構成される
環状ヘツダー間に接続される。この伝熱管6aは
環状ヘツダーの周方向に複数配設される。6bも
伝熱管であり、上下の環状ヘツダー2bと3b間
に接続されている。この伝熱管6bも、環状ヘツ
ダーの周方向に複数設けられる。同様に、6cも
伝熱管であり、上下の環状ヘツダー2cと3c間
に接続され、周方向に複数本接続されている。出
入口4aは環状ヘツダー2aと接続され、冷媒ま
たは熱媒をヘツダー2aに供給したり逆にヘツダ
ー側から抜出すために用いられる。出入口4b,
4cも、それぞれ環状ヘツダー2b,2cと接続
され、同様の目的のために使用される。出入口5
aは環状ヘツダー3cと接続され、冷媒または熱
媒をヘツダー3aに供給したり逆にヘツダー側か
ら抜出すために用いられる。出入口5b,5c
も、それぞれ環状ヘツダー3b,3cと接続さ
れ、同様の目的のために使用される。いま、4a
から冷媒(または熱媒)がヘツダー2aに供給さ
れると、冷媒はこのヘツダーの周方向に接続され
た伝熱管内を通つて下部のヘツダー3aに到り、
出入口5aから外部へ取出される。もちろん、逆
の順序で冷媒(または熱媒)を供給しても良い。
他も同様である。槽1の中心部に設けられた撹拌
軸8は、図示しないモータ等により回転駆動さ
れ、撹拌翼7a,7bが槽内の液を撹拌する。こ
のような上下の環状ヘツダー間を複数の伝熱管で
接続した構成により、伝熱面積は従来に較べて飛
躍的に増大し、高伝熱が達成できる。 FIG. 1 is a diagram according to an embodiment of the present invention, and shows a longitudinal cross-sectional view. Moreover, FIG. 2 shows a sectional view taken along the line AA in FIG. 1. In these figures, 1 is the stirring tank main body, and 8 is a stirring shaft provided in the center of the tank.
Moreover, 7a and 7b are stirring blades attached to the stirring shaft 8. 2a, 2b, and 2c are annular headers at the top of the tank, respectively. Also, 3a, 3b, 3c
are the annular headers at the bottom of the tank, respectively. 2a
and 3a are a pair of upper and lower annular headers, and similarly, 2b and 3b, and 2c and 3c are each a pair of upper and lower annular headers. Therefore, in this embodiment, three sets of annular headers are arranged.
A heat transfer tube 6a is connected between the annular headers 2a and 3a. A plurality of heat transfer tubes 6a are arranged in the circumferential direction of the annular header. 6b is also a heat transfer tube and is connected between the upper and lower annular headers 2b and 3b. A plurality of heat transfer tubes 6b are also provided in the circumferential direction of the annular header. Similarly, 6c is also a heat transfer tube, which is connected between the upper and lower annular headers 2c and 3c, and a plurality of tubes are connected in the circumferential direction. The inlet/outlet 4a is connected to the annular header 2a, and is used to supply a refrigerant or a heat medium to the header 2a, and conversely to extract it from the header side. Entrance/exit 4b,
4c is also connected to the annular headers 2b and 2c, respectively, and is used for the same purpose. Doorway 5
A is connected to the annular header 3c, and is used to supply a refrigerant or heat medium to the header 3a, and conversely to extract it from the header side. Entrance/exit 5b, 5c
are also connected to the annular headers 3b and 3c, respectively, and are used for the same purpose. Now 4a
When the refrigerant (or heat medium) is supplied to the header 2a, the refrigerant passes through the heat transfer tubes connected in the circumferential direction of this header and reaches the lower header 3a,
It is taken out from the entrance/exit 5a. Of course, the refrigerant (or heat medium) may be supplied in the reverse order.
The same applies to others. A stirring shaft 8 provided at the center of the tank 1 is rotationally driven by a motor or the like (not shown), and stirring blades 7a and 7b stir the liquid in the tank. With such a configuration in which the upper and lower annular headers are connected by a plurality of heat transfer tubes, the heat transfer area is dramatically increased compared to the conventional method, and high heat transfer can be achieved.
また、この実施例においては、第2図に示すよ
うに、伝熱管6a,6b,6cをヘツダーの円周
方向に局部的に配置している。これにより、マン
ホール9より槽内への液の出入通路を確保すると
共に、撹拌槽の伝熱効果を上げるためのバツフル
効果を与えることを可能としている。 Further, in this embodiment, as shown in FIG. 2, heat exchanger tubes 6a, 6b, and 6c are locally arranged in the circumferential direction of the header. This makes it possible to ensure a path for liquid to enter and exit the tank from the manhole 9, and to provide a buffling effect to improve the heat transfer effect of the stirring tank.
第3図は本発明の他の実施例を示すもので、こ
の例では、伝熱管6a,6b,6cの配置を三角
配列にしている。これにより、撹拌翼7a,7b
により生ずる液の撹拌流れ方向10を均一化し、
槽内の周方向の温度分布の均一化を実現できる。 FIG. 3 shows another embodiment of the present invention, in which heat exchanger tubes 6a, 6b, and 6c are arranged in a triangular arrangement. As a result, the stirring blades 7a, 7b
to homogenize the stirring flow direction 10 of the liquid produced by,
Uniform temperature distribution in the circumferential direction within the tank can be achieved.
本発明によれば、伝熱面積を大きくすると共
に、バツフル効果により伝熱を効果的に行なうこ
とができる。
According to the present invention, it is possible to increase the heat transfer area and to perform heat transfer effectively due to the buffling effect.
第1図および第2図は本発明の一実施例を示す
図、第3図は本発明の他の実施例を示す図であ
る。
1……撹拌槽本体、2a,2b,2c……上部
の環状ヘツダー、3a,3b,3c……上部の環
状ヘツダー、4a,4b,4c……出入口、5
a,5b,5c……出入口、6a,6b,6c…
…伝熱管、7a,7b……撹拌翼、8……撹拌
軸、9……マンホール。
1 and 2 are diagrams showing one embodiment of the invention, and FIG. 3 is a diagram showing another embodiment of the invention. 1... Stirring tank body, 2a, 2b, 2c... Upper annular header, 3a, 3b, 3c... Upper annular header, 4a, 4b, 4c... Entrance/exit, 5
a, 5b, 5c... Entrance/exit, 6a, 6b, 6c...
...Heat transfer tube, 7a, 7b... Stirring blade, 8... Stirring shaft, 9... Manhole.
Claims (1)
撹拌軸と、該撹拌軸の外周部に位置し撹拌槽内の
上部および下部にそれぞれ設けられた同芯状の複
数の環状ヘツダーと、該上下の複数の環状ヘツダ
ー間にそれぞれ設けられ、かつ、ヘツダーの円周
方向に局部的に集中させて配設された複数の伝熱
管と、上下の複数の環状ヘツダーにそれぞれ独立
して設けられた冷媒または熱媒を槽外部より供給
したり抜出すための出入口とを設けたことを特徴
とする高伝熱型撹拌装置。 2 前記伝熱管の配設は、三角配列で局部的にま
とめて構成したことを特徴とする請求項第1項記
載の高伝熱型撹拌装置。[Scope of Claims] 1. A stirring shaft having stirring blades provided at the center of the stirring tank, and a plurality of concentric shafts located at the outer periphery of the stirring shaft and provided at the upper and lower parts of the stirring tank, respectively. an annular header, a plurality of heat transfer tubes each provided between the plurality of upper and lower annular headers and locally concentrated in the circumferential direction of the header, and each of the plurality of upper and lower annular headers. A high heat transfer stirring device characterized by having an independently provided inlet/outlet for supplying or extracting a refrigerant or heat medium from outside the tank. 2. The high heat transfer stirring device according to claim 1, wherein the heat transfer tubes are arranged locally in a triangular arrangement.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60210018A JPS6271523A (en) | 1985-09-25 | 1985-09-25 | High heat transmission type agitating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60210018A JPS6271523A (en) | 1985-09-25 | 1985-09-25 | High heat transmission type agitating apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6271523A JPS6271523A (en) | 1987-04-02 |
| JPH0212136B2 true JPH0212136B2 (en) | 1990-03-19 |
Family
ID=16582459
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60210018A Granted JPS6271523A (en) | 1985-09-25 | 1985-09-25 | High heat transmission type agitating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6271523A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5340577U (en) * | 1976-09-13 | 1978-04-08 |
-
1985
- 1985-09-25 JP JP60210018A patent/JPS6271523A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6271523A (en) | 1987-04-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US20140246182A1 (en) | Heat Transfer Baffle System and Uses Thereof | |
| US4724754A (en) | Apparatus for making molded confections | |
| US4073696A (en) | Apparatus for combined cooling and aeration of biochemical-action vessels | |
| CN107764106A (en) | A kind of rotation blade heat exchanger | |
| CN218821799U (en) | A heat exchanger with good anti-scaling effect | |
| CN108654534A (en) | The energy-efficient reaction kettle of dual coil pipes | |
| JPH0212136B2 (en) | ||
| CN108671865A (en) | The energy-efficient reaction kettle of dual coil pipes being vented using chuck | |
| US1667944A (en) | Agitator | |
| EP0586747A1 (en) | Heat exchanger system with turbulator for particle-in-liquid dispersion | |
| JPH0622422Y2 (en) | Stirrer | |
| JPS60221691A (en) | Condenser | |
| US1793244A (en) | Radiator | |
| US2721730A (en) | Heat exchanger | |
| JP3491229B2 (en) | Multi-tube heat exchanger | |
| KR20040036495A (en) | A High Speed Fermenting and Drying Apparatus | |
| JP3104886B2 (en) | Heat exchanger | |
| CN212142620U (en) | Heat exchanger for reaction kettle | |
| JP2004020096A (en) | Multi-tube type heat transfer agitating device | |
| US3295597A (en) | Heat exchangers | |
| CN224167491U (en) | Polyethylene wax modification reaction kettle | |
| CN213375218U (en) | Manganese sulfate and zinc sulfate evaporative crystallizer | |
| CN217423445U (en) | Heating device for combined air conditioning unit | |
| JPH0416229A (en) | Draft tube type stirring vessel | |
| CN223295283U (en) | Shell-and-tube heat exchanger |