JPH04129799U - Aeration stirring device - Google Patents

Aeration stirring device

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Publication number
JPH04129799U
JPH04129799U JP4412591U JP4412591U JPH04129799U JP H04129799 U JPH04129799 U JP H04129799U JP 4412591 U JP4412591 U JP 4412591U JP 4412591 U JP4412591 U JP 4412591U JP H04129799 U JPH04129799 U JP H04129799U
Authority
JP
Japan
Prior art keywords
stirring
air
fermenter
rotating shaft
stirring blade
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.)
Pending
Application number
JP4412591U
Other languages
Japanese (ja)
Inventor
健治 山村
康平 三木
守 三島
Original Assignee
住友重機械工業株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 住友重機械工業株式会社 filed Critical 住友重機械工業株式会社
Priority to JP4412591U priority Critical patent/JPH04129799U/en
Publication of JPH04129799U publication Critical patent/JPH04129799U/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02Stirrer or mobile mixing elements
    • C12M27/08Stirrer or mobile mixing elements with different stirrer shapes in one shaft or axis
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/06Nozzles; Sprayers; Spargers; Diffusers

Landscapes

  • 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】 【目的】 高粘性発酵液でも気泡の微細化を促進して高
い酸素供給と撹拌混合が得られ、発酵生産性の向上を図
ることができる通気撹拌装置を提供すること。 【構成】 発酵槽1の底壁の内面に沿った形状の底面を
有した平板状の撹拌翼4の下側部であって、その回転円
周に近接した位置に空気吐出孔6が開口したシングルノ
ズル5を設けている。シングルノズル5の空気吐出孔6
から吐出される空気を撹拌翼4の回転時に上方からはた
けるように複数個の突起物7を回転軸2から放射状に設
けている。
(57) [Summary] [Purpose] To provide an aeration stirring device capable of promoting the miniaturization of air bubbles even in a highly viscous fermented liquid to obtain high oxygen supply and stirring and mixing, thereby improving fermentation productivity. [Structure] Air discharge holes 6 are opened at the lower side of a flat stirring blade 4 having a bottom surface shaped along the inner surface of the bottom wall of the fermenter 1, at a position close to its rotational circumference. A single nozzle 5 is provided. Air discharge hole 6 of single nozzle 5
A plurality of protrusions 7 are provided radially from the rotating shaft 2 so that the air discharged from the stirring blades 4 is flapped from above when the stirring blades 4 rotate.

Description

【考案の詳細な説明】[Detailed explanation of the idea]

【0001】0001

【産業上の利用分野】[Industrial application field]

この考案は、化学、薬品、食品工業等で通気を必要とする高粘性発酵液の通気 撹拌装置に関するものである。 This idea is designed to aerate highly viscous fermented liquids that require aeration in the chemical, pharmaceutical, and food industries. This relates to a stirring device.

【0002】0002

【従来の技術】[Conventional technology]

従来、発酵液を通気撹拌する装置として、図4に示すようなものがある。21は 発酵液Fを入れた発酵槽、22は回転軸、23は回転軸22に上下2段に設けられたデ ィスクタービン翼、25は回転軸22の駆動用モータ、26は平板状邪魔板、27はリン グ状のスパージャ、28は空気供給用チューブを示す。この装置においては、モー タ25によって回転されるディスクタービン翼23による発酵液Fの撹拌中に、図示 しない空気源からチューブ28を介して送られる空気がスパージャ27から吐出され 、この空気の吐出により発酵液F中に気泡が生じると、この気泡が高速で回転す るディスクタービン翼23で破砕されて細分化され、発酵液F中に酸素が溶解、供 給される。 Conventionally, there is a device shown in FIG. 4 as a device for aerating and stirring a fermentation liquid. 21 is A fermentation tank containing fermentation liquid F, 22 is a rotating shaft, and 23 is a device provided on the rotating shaft 22 in two stages, upper and lower. disk turbine blade, 25 is a motor for driving the rotating shaft 22, 26 is a flat baffle plate, 27 is a link 28 indicates a tube for air supply. In this device, the mode During the stirring of the fermentation liquid F by the disk turbine blades 23 rotated by the Air sent through tube 28 from a source that does not discharge air from sparger 27 When air bubbles are generated in the fermentation liquid F due to this air discharge, these air bubbles rotate at high speed. The disk turbine blades 23 crush and finely divide the fermentation liquid, and oxygen is dissolved and provided in the fermentation liquid F. be provided.

【0003】0003

【考案が解決しようとする課題】[Problem that the idea aims to solve]

ところで、前記のような従来の装置においては、発酵槽21内の発酵液Fの粘度 が発酵の経過とともに高くなると、撹拌混合が不十分となることがある。このよ うな高粘性発酵液の撹拌混合が不十分の場合には、撹拌効果を上げるために撹拌 翼としてディスクタービン翼23に代えて、発酵槽21の底壁の内面に沿った形状の 底面を有する平板状のアンカー翼やゲート翼などを用いればよいが、酸素供給の 側面から見ると、これらアンカー翼やゲート翼は低速回転で使用されること、ま た比較的大きな翼であることのため、通気した気泡を物理的に微細化して酸素供 給効果を高める機能をもっていないという問題点があった。 そこでこの考案は、前記のような従来の問題点を排除し、高粘性発酵液でも気 泡の微細化を促進して高い酸素供給と撹拌混合が得られ、発酵生産性の向上を図 ることができる通気撹拌装置を提供することを目的とする。 By the way, in the conventional apparatus as described above, the viscosity of the fermentation liquid F in the fermenter 21 If the amount increases over the course of fermentation, stirring and mixing may become insufficient. This way If stirring and mixing of the highly viscous fermented liquid is insufficient, stir to increase the stirring effect. Instead of the disk turbine blade 23 as a blade, a blade shaped along the inner surface of the bottom wall of the fermenter 21 is used. A plate-shaped anchor blade or gate blade with a bottom surface may be used, but the oxygen supply Viewed from the side, these anchor blades and gate blades are used at low speeds, or Because the blades are relatively large, the air bubbles are physically made finer to provide oxygen. The problem was that it did not have a function to enhance the supply effect. Therefore, this invention eliminates the conventional problems mentioned above and allows even highly viscous fermented liquid to be air-filled. Promotes the miniaturization of bubbles to achieve high oxygen supply and agitation, improving fermentation productivity. The purpose of the present invention is to provide an aeration stirring device that can provide ventilation.

【0004】0004

【課題を解決するための手段】[Means to solve the problem]

前記目的を達成するため、この考案は、前記のような通気撹拌装置において、 撹拌翼の下側部であって、その回転円周に近接した位置に空気吐出孔が開口した 通気管を設け、この通気管の空気吐出孔から吐出される空気を撹拌翼の回転時に 上方からはたけるように複数個の突起物を回転軸から放射状に設けている。 In order to achieve the above object, this invention provides the above-mentioned aeration stirring device, The air discharge hole is located on the lower side of the stirring blade, close to its rotating circumference. A ventilation pipe is provided, and the air discharged from the air discharge hole of this ventilation pipe is pumped when the stirring blade rotates. A plurality of protrusions are provided radially from the rotating shaft so as to flap from above.

【0005】[0005]

【作用】[Effect]

前記構成により、通気管の空気吐出孔から発酵槽内へ吐出される空気は、撹拌 翼の回転時に該翼とともに回転する複数個の突起物により、該突起物が吐出孔を 通過する都度に吐出孔の上方ではたかれ、これにより気泡は微細化される。 With the above configuration, the air discharged into the fermenter from the air discharge hole of the ventilation pipe is stirred. When the blade rotates, a plurality of protrusions rotate together with the blade, and the protrusion opens the discharge hole. Each time it passes, it flutters above the discharge hole, thereby making the bubbles finer.

【0006】[0006]

【実施例】【Example】

図1はこの考案の一実施例を示す通気撹拌装置の概略図、図2は図1のA−A 線に沿う一部省略の横断平面図、図3は撹拌翼及び回転軸に対する突起物の取付 関係を示す斜視図である。図1,2,3において1は発酵液Fを入れた円筒形の 発酵槽で、発酵槽1内の中心部には下端が底壁付近まで延在する回転軸2が軸受 で回転可能に支持されて設けられている。発酵槽1の頂壁から突出した回転軸2 には駆動用のモータ3が接続されている。回転軸2には発酵槽1の底壁の内面に 沿った形状の底面を有し、高粘性の発酵液Fの撹拌混合に適している平板状の撹 拌翼4が取付けられている。 Fig. 1 is a schematic diagram of an aeration stirring device showing an embodiment of this invention, and Fig. 2 is an A-A diagram of Fig. 1. A partially omitted cross-sectional plan view along the line, Figure 3 shows the attachment of protrusions to the stirring blade and rotating shaft. FIG. 3 is a perspective view showing the relationship. In Figures 1, 2, and 3, 1 is a cylindrical container containing fermentation liquid F. In the fermenter, a rotary shaft 2 with a lower end extending to near the bottom wall is mounted in the center of the fermenter 1. It is rotatably supported. A rotating shaft 2 protruding from the top wall of the fermenter 1 A driving motor 3 is connected to. The rotary shaft 2 has an inner surface of the bottom wall of the fermenter 1 A flat plate type stirrer with a contoured bottom surface and suitable for stirring and mixing highly viscous fermentation liquid F. A stirring blade 4 is attached.

【0007】 5はシングルノズル(通気管)で、撹拌翼4の下側部であって、その回転円周 に近接した位置に先端の空気吐出孔6が開口するように設けられている。シング ルノズル5には槽外に設置した図示しないコンプレッサ等の空気源から空気が供 給されるようになっている。7は撹拌翼4の底面近くの回転軸2に一部のものが 撹拌翼4の底面に沿うように放射状に設けられた突起物で、シングルノズル5の 空気吐出孔6から吐出される空気を撹拌翼4の回転時に上方からはたけるように なっている。突起物7は発酵槽1の底壁の内面に沿った湾曲状を呈しているが、 必ずしもこのような形状でなくともよい。また、回転軸2に対する突起物7の取 付位置や個数も図示したものに限定されず、これらは実施に際して任意にその設 計を変更、修正することができる。[0007] Reference numeral 5 denotes a single nozzle (vent pipe), which is located on the lower side of the stirring blade 4 and whose rotational circumference is An air discharge hole 6 at the tip is provided to open at a position close to. Thing Air is supplied to the nozzle 5 from an air source such as a compressor (not shown) installed outside the tank. They are now being paid. 7 is a part of the rotating shaft 2 near the bottom of the stirring blade 4. These are protrusions provided radially along the bottom surface of the stirring blades 4, and are used for the single nozzle 5. The air discharged from the air discharge hole 6 is blown out from above when the stirring blade 4 rotates. It has become. The protrusion 7 has a curved shape along the inner surface of the bottom wall of the fermenter 1, It does not necessarily have to have such a shape. Also, the attachment of the protrusion 7 to the rotating shaft 2 The location and number of attachments are not limited to what is shown in the diagram, and these can be set arbitrarily during implementation. You can change and modify the meter.

【0008】 前記のような装置は、通常、一定の撹拌速度、かつ一定の通気量で連続的に運 転される。この運転の際に、シングルノズル5の吐出孔6から吐出された空気は 、撹拌翼4の回転時に該翼とともに回転する複数個の突起物7により、該突起物 が吐出孔6を通過する都度に吐出孔6の上方ではたかれ、これにより気泡は微細 化される。[0008] Such equipment is usually operated continuously at a constant agitation rate and a constant aeration rate. be transferred. During this operation, the air discharged from the discharge hole 6 of the single nozzle 5 is , a plurality of protrusions 7 that rotate together with the stirring blade 4 when the stirring blade 4 rotates, the protrusion Every time the gas passes through the discharge hole 6, it is fluttered above the discharge hole 6, and as a result, fine air bubbles are be converted into

【0009】 この実施例装置の効果を確認するため、下記条件で酸素溶解速度の比較を行な った。 通気撹拌条件 槽容積:2リットル(内径130mm) 通気量:2リットル/min 液:水道水及びカルボキシメチルセルロース(CMC)水溶液 液温:30℃ 通気撹拌方法 対照装置:図3に示す撹拌翼で突起物7の付いていない翼(翼巾= 70mm、翼高=145mm、1枚翼)、4枚の邪魔板、シングルノズルによ る通気。 この実施例装置:図3に示す突起物7付き撹拌翼4(翼巾=70mm、 翼高=145mm、1枚翼、6個の突起物7、突起物7の直径110mm)、4 枚の邪魔板、シングルノズルによる通気。 酸素溶解速度の測定結果を液側酸素移動容量係数KLa(h▲上付-1▼)で表 1に示す。尚、KLaは亜硫酸ソーダ法により測定した。[0009] In order to confirm the effectiveness of this example device, we compared the oxygen dissolution rate under the following conditions. It was. Aeration stirring conditions Tank volume: 2 liters (inner diameter 130mm) Airflow rate: 2 liters/min Liquid: tap water and carboxymethyl cellulose (CMC) aqueous solution Liquid temperature: 30℃ Aeration stirring method Control device: The stirring blade shown in Fig. 3 without the protrusion 7 (blade width = 70mm, blade height = 145mm, 1 blade), 4 baffle plates, single nozzle ventilation. This embodiment device: stirring blade 4 with protrusion 7 shown in FIG. 3 (blade width = 70 mm, Wing height = 145 mm, 1 blade, 6 protrusions 7, diameter of protrusions 7 110 mm), 4 Ventilation with two baffle plates and a single nozzle. The measurement results of the oxygen dissolution rate are expressed as the liquid side oxygen transfer capacity coefficient KLa (h▲superscript-1▼). Shown in 1. In addition, KLa was measured by the sodium sulfite method.

【表1】 前記結果から、突起物7を付けることにより酸素供給(溶解)性能が高くなる ことが明らかである。[Table 1] From the above results, it is clear that adding the protrusions 7 improves the oxygen supply (dissolution) performance.

【0010】 尚、前記実施例においては通気管としてシングルノズル5を示したが、ほかに 例えばリング状のスパージャのようなものでもよい。ただし、スパージャの場合 には空気吐出孔から吐出される空気を突起物7ではたけるようにする必要がある 。0010 In addition, although the single nozzle 5 was shown as the ventilation pipe in the above embodiment, other For example, it may be a ring-shaped sparger. However, in the case of sparger It is necessary to make the protrusion 7 blow the air discharged from the air discharge hole. .

【0011】[0011]

【考案の効果】[Effect of the idea]

この考案は前記のような構成からなるので、気泡の細分化機能が低いアンカー 翼やゲート翼などのような高粘性発酵液の撹拌に適した撹拌翼でも、気泡微細化 の効果が得られる。したがって、高粘性発酵液でも高い酸素供給と撹拌混合を得 ることができ、従来、低下しがちだった発酵生産性の向上を図ることができると いう優れた効果がある。 This device has the above-mentioned configuration, so it is an anchor with a low ability to subdivide bubbles. Even stirring blades suitable for stirring highly viscous fermented liquid, such as blades and gate blades, can reduce air bubbles into fine particles. The effect of this can be obtained. Therefore, high oxygen supply and stirring mixing can be achieved even with highly viscous fermentation liquid. This makes it possible to improve fermentation productivity, which has tended to decline in the past. It has an excellent effect.

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

【図1】この考案の一実施例を示す通気撹拌装置の概略
図である。
FIG. 1 is a schematic diagram of an aeration stirring device showing an embodiment of this invention.

【図2】図1のA−A線に沿う一部省略の横断平面図で
ある。
FIG. 2 is a partially omitted cross-sectional plan view taken along line A-A in FIG. 1;

【図3】同上の撹拌翼及び回転軸に対する突起物の取付
関係を示す斜視図である。
FIG. 3 is a perspective view showing the attachment relationship of the protrusion to the stirring blade and the rotating shaft.

【図4】従来の例を示す通気撹拌装置の概略図である。FIG. 4 is a schematic diagram of a conventional aeration stirring device.

【符号の説明】[Explanation of symbols]

1 発酵槽 2 回転軸 3 モータ 4 撹拌翼 5 シングルノズル 6 空気吐出孔 7 突起物 1 Fermenter 2 Rotating axis 3 motor 4 Stirring blade 5 Single nozzle 6 Air discharge hole 7 Protrusions

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 発酵槽と、この発酵槽内の中心部に設け
られた回転軸と、この回転軸に発酵槽の底壁の内面に沿
った形状の底面を有して取付けられ、発酵槽内の発酵液
を撹拌する平板状の撹拌翼とを具えた通気撹拌装置にお
いて、撹拌翼の下側部であって、その回転円周に近接し
た位置に空気吐出孔が開口した通気管を設け、この通気
管の空気吐出孔から吐出される空気を撹拌翼の回転時に
上方からはたけるように複数個の突起物を回転軸から放
射状に設けたことを特徴とする通気撹拌装置。
Claim 1: A fermenter, a rotating shaft provided in the center of the fermenter, and a bottom surface shaped along the inner surface of the bottom wall of the fermenter, the rotary shaft being attached to the rotating shaft, In an aeration stirring device equipped with a flat stirring blade that stirs the fermented liquid inside, a ventilation pipe with an air discharge hole is provided at a position near the rotational circumference of the stirring blade on the lower side of the stirring blade. An aeration stirring device characterized in that a plurality of protrusions are provided radially from a rotating shaft so that the air discharged from the air discharge hole of the ventilation pipe is flapped from above when the stirring blade rotates.
JP4412591U 1991-05-16 1991-05-16 Aeration stirring device Pending JPH04129799U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4412591U JPH04129799U (en) 1991-05-16 1991-05-16 Aeration stirring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4412591U JPH04129799U (en) 1991-05-16 1991-05-16 Aeration stirring device

Publications (1)

Publication Number Publication Date
JPH04129799U true JPH04129799U (en) 1992-11-27

Family

ID=31924332

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4412591U Pending JPH04129799U (en) 1991-05-16 1991-05-16 Aeration stirring device

Country Status (1)

Country Link
JP (1) JPH04129799U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010253372A (en) * 2009-04-23 2010-11-11 Ihi Corp Gas-liquid stirrer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010253372A (en) * 2009-04-23 2010-11-11 Ihi Corp Gas-liquid stirrer

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