JPH0258971B2 - - Google Patents
Info
- Publication number
- JPH0258971B2 JPH0258971B2 JP61160584A JP16058486A JPH0258971B2 JP H0258971 B2 JPH0258971 B2 JP H0258971B2 JP 61160584 A JP61160584 A JP 61160584A JP 16058486 A JP16058486 A JP 16058486A JP H0258971 B2 JPH0258971 B2 JP H0258971B2
- Authority
- JP
- Japan
- Prior art keywords
- drum
- gas
- partition wall
- circumferential surface
- rotating drum
- 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
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
- B01F23/2331—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
- B01F23/23313—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements through a separate conduit substantially parallel with the stirrer axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
- B01F23/2331—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
- B01F23/2331—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
- B01F23/23314—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements through a hollow stirrer element
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/25—Mixers with both stirrer and drive unit submerged in the material being mixed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/94—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with rotary cylinders or cones
- B01F27/941—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with rotary cylinders or cones being hollow, perforated or having special stirring elements thereon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/116—Stirrers shaped as cylinders, balls or rollers
- B01F27/1161—Stirrers shaped as cylinders, balls or rollers having holes in the surface
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Gas Separation By Absorption (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は気液接触装置に係り、特に多孔円筒型
回転ドラムを有する気液接触装置において、気泡
径を均等化させるように改良した装置に関する。Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a gas-liquid contact device, and more particularly to a gas-liquid contact device having a porous cylindrical rotating drum, which is improved so as to equalize the bubble diameter. .
[従来の技術]
多孔ドラムを槽体内に水没可能に設け、このド
ラム内に気体を加圧供給すると共に該ドラムを回
転させて、ドラム周面より気泡を液中に噴出させ
るようにした気液接触装置が知られている(例え
ば特公昭52−21991、同52−22953)。[Prior Art] A gas-liquid device in which a porous drum is provided in a tank body so as to be submerged in water, and gas is supplied under pressure into the drum and the drum is rotated to eject air bubbles into the liquid from the circumferential surface of the drum. Contact devices are known (for example, Japanese Patent Publications No. 52-21991 and No. 52-22953).
このような多孔円筒ドラムによる気液接触方式
には、該ドラムをその軸心方向が略鉛直方向にな
るように設置する縦型のものと、ドラムを水平方
向に設置する横型とがある。前者の縦型のもの
(例えば、前記特公昭52−21991)は、後者の横型
のものに比べ、ドラムの枢支機構が簡便であり、
小型小容量仕様に特に好適であるという特長を有
している。 Such a gas-liquid contact system using a porous cylindrical drum includes a vertical type in which the drum is installed so that its axial direction is substantially vertical, and a horizontal type in which the drum is installed horizontally. The former vertical type (for example, the above-mentioned Japanese Patent Publication No. 52-21991) has a simpler drum pivot mechanism than the latter horizontal type.
It has the feature of being particularly suitable for small size and small capacity specifications.
[発明が解決しようとする問題点]
ところが、従来の縦型回転ドラム方式の気液接
触装置においては、ドラム側周面の開口から噴出
される気泡径がドラムの上下でかなり異なり、気
泡径のばらつきが大きくなるという問題があつ
た。[Problems to be Solved by the Invention] However, in the conventional vertical rotating drum type gas-liquid contact device, the diameter of the bubbles ejected from the openings on the peripheral surface of the drum differs considerably between the top and bottom of the drum. There was a problem that the dispersion became large.
即ち、ドラム上部へは、下部に比べ小さな水圧
(液圧)が加えられるので、気体が多量に噴出し
て気泡径が大きくなり易く、逆にドラム下部から
噴出される気泡は小径化し易いのである。 In other words, since a smaller water pressure (hydraulic pressure) is applied to the upper part of the drum than to the lower part, a large amount of gas is ejected and the bubble diameter tends to increase, and conversely, the bubbles ejected from the lower part of the drum tend to become smaller in diameter. .
このように気泡径がばらつくと、それだけ気液
接触効果も低下するという問題が生ずる。 When the bubble diameter varies in this way, a problem arises in that the gas-liquid contact effect is reduced accordingly.
[問題点を解決するための手段]
本発明は、縦型回転ドラムを備えた気液接触装
置において、ドラム内の天蓋から仕切壁をドラム
内周面との間に間隔があくように垂設すると共
に、この仕切壁の下部に仕切壁の内外を連通する
連通部を設けた。そして、この仕切壁とドラム内
周面との間には、この間の部分を上昇する気体に
通過圧損を付与するための絞りを設けた。[Means for Solving the Problems] The present invention provides a gas-liquid contact device equipped with a vertical rotating drum, in which a partition wall is vertically disposed from a canopy inside the drum so as to leave a space between it and the inner peripheral surface of the drum. At the same time, a communication section was provided at the bottom of the partition wall to communicate between the inside and outside of the partition wall. A throttle was provided between the partition wall and the inner circumferential surface of the drum to impart pressure loss to the gas rising in the space between the partition wall and the inner peripheral surface of the drum.
なお、気体の供給管はドラム底部の中央部より
ドラム内に装入される。 Note that the gas supply pipe is inserted into the drum from the center of the bottom of the drum.
[作用]
本発明の気液接触装置において、気体供給管か
らドラム内の中央の室内に供給される気体は、仕
切壁下部の連通部を回り込んで該仕切壁とドラム
内周面との間を上昇する。そして、このドラム周
面に設けられた開口から順次に噴出する。この
際、ドラムは回転されており、開口から噴出され
た気体は剪断作用等を受けて微小な気泡となる。[Function] In the gas-liquid contact device of the present invention, the gas supplied from the gas supply pipe into the central chamber of the drum goes around the communication part at the bottom of the partition wall and flows between the partition wall and the inner circumferential surface of the drum. rise. Then, they are sequentially ejected from openings provided on the circumferential surface of this drum. At this time, the drum is being rotated, and the gas ejected from the openings is subjected to a shearing action and becomes minute bubbles.
而して、本発明においては、仕切壁とドラム内
周面との間に絞りが設けられており、この部分を
上昇する気体は絞りの通過圧損により上方に到る
程小なる圧力(静圧)を保有するようになる。そ
のため、液圧(ヘツド)の小さいドラム側周面の
上部程、低い圧力で気体が噴出されるようになる
ので、ドラムの上下で略々同一気体噴出量とな
り、気泡が均一径化する。 Therefore, in the present invention, a throttle is provided between the partition wall and the inner circumferential surface of the drum, and the gas rising in this area is caused to rise upward due to the pressure loss passing through the throttle (static pressure). ). Therefore, gas is ejected at a lower pressure toward the upper part of the drum side circumferential surface where the liquid pressure (head) is lower, so that the amount of gas ejected is approximately the same on the upper and lower sides of the drum, and the bubbles have a uniform diameter.
[実施例] 以下図面を参照して実施例について説明する。[Example] Examples will be described below with reference to the drawings.
第1図は本発明の実施例に係る気液接触装置の
構成を示す正面要部断面図である。 FIG. 1 is a front sectional view showing the main part of the configuration of a gas-liquid contact device according to an embodiment of the present invention.
符号10は槽体であつて、支柱12を介して設
けられた台座14にモータ16が固設されてい
る。モータ16は、その回転軸16aが鉛直方向
となるように設置されており、回転軸16aの下
端には円筒形の回転ドラム18がナツト20によ
つて取り付けられている。ドラム18は有蓋有底
であり、回転軸心が鉛直方向となつている。 Reference numeral 10 denotes a tank body, and a motor 16 is fixed to a pedestal 14 provided via a support 12. The motor 16 is installed so that its rotating shaft 16a is vertical, and a cylindrical rotating drum 18 is attached to the lower end of the rotating shaft 16a with a nut 20. The drum 18 has a lid and a bottom, and its axis of rotation is in the vertical direction.
このドラム18は、その側周面に多数の開口2
2が設けられ、この開口22の外周側には気体噴
出ノズル24が突設されている。なお本実施例で
は、開口22は桝目形に配列されている。 This drum 18 has a large number of openings 2 on its side circumferential surface.
2 is provided, and a gas jet nozzle 24 is provided protruding from the outer peripheral side of this opening 22. In this embodiment, the openings 22 are arranged in a grid pattern.
槽体10の底面には、台座26が固設され、こ
の台座26から気体供給管28が立ち上げられて
いる。この気体供給管28は、ドラム18の底板
18aを貫通してドラム18内の上部近傍にまで
達している。また、ドラム底板18bには、この
気体供給管28を挿通する開口が設けられている
のであるが、この開口の縁部には摺動部材30が
設けられ、ドラム18の回転時におけるドラム1
8下端の枢支をなすようになつている。 A pedestal 26 is fixed to the bottom surface of the tank body 10, and a gas supply pipe 28 is raised from this pedestal 26. This gas supply pipe 28 penetrates the bottom plate 18a of the drum 18 and reaches near the top inside the drum 18. Further, the drum bottom plate 18b is provided with an opening through which the gas supply pipe 28 is inserted, and a sliding member 30 is provided at the edge of this opening, so that when the drum 18 rotates, the drum 18 is rotated.
8 It is designed to form a pivot at the lower end.
符号32は仕切壁であつて、本実施例ではドラ
ム18よりも小径円筒状のものであり、ドラム1
8の天蓋部18bから垂設されている。この仕切
壁32は、ドラム18よりも高さの小さいもので
あり、該仕切壁32の下端とドラム底板18aと
の間には連通部34が形成されている。また、仕
切壁32とドラム18内周面との間には、この間
を上昇する気体流に通過圧損を与えて、気体が上
方に到る程小なる圧力を保有するようにするため
の絞り36が多段に設けられている。なお、前記
気体供給管28の下部は、T字状になつており、
フレキシブルチユーブ38が接続されている。 Reference numeral 32 denotes a partition wall, which in this embodiment has a cylindrical shape with a smaller diameter than the drum 18.
The canopy part 18b of No. 8 is vertically installed. This partition wall 32 is smaller in height than the drum 18, and a communication portion 34 is formed between the lower end of the partition wall 32 and the drum bottom plate 18a. Further, between the partition wall 32 and the inner circumferential surface of the drum 18, there is a throttle 36 for giving a passing pressure loss to the gas flow rising therebetween, so that the gas maintains an extremely small pressure upward. are arranged in multiple stages. Note that the lower part of the gas supply pipe 28 is T-shaped,
A flexible tube 38 is connected.
かかる構成の気液接触装置において、フレキシ
ブルチユーブ38及び気体供給管28を通して気
体を回転ドラム18内に供給すると共にモータ1
6を回転させると、気体は仕切壁32の下端の連
通部34を回り込んで該仕切壁32とドラム18
内周との間を上昇し、順次ノズル24から噴出さ
れる。そして、ドラム18の回転によつて受ける
剪断作用によつて細かく分断され微細気泡とな
る。 In the gas-liquid contact device having such a configuration, gas is supplied into the rotating drum 18 through the flexible tube 38 and the gas supply pipe 28, and the motor 1
6 is rotated, the gas flows around the communication part 34 at the lower end of the partition wall 32 and between the partition wall 32 and the drum 18.
The liquid rises between the inner circumference and is sequentially ejected from the nozzle 24. Then, due to the shearing action caused by the rotation of the drum 18, it is finely divided into fine bubbles.
而して、本実施例では、絞り36が多段に設け
られており、該絞りを通過する際の圧損により、
仕切壁32とドラム18内周面との間を上昇する
気体は、上部に流れ込む程保有圧力が低下する。
そのため、この絞り36の開度を適宜調整してお
くことに、各ノズル24におけるドラム18内外
における水圧と気体圧との差をほぼ均等なものと
することができる。これにより、各ノズル24か
ら単位時間当り等量の気体を噴出させることが可
能となり、各ノズル24から発生する気泡径が均
等化する。 In this embodiment, the throttles 36 are provided in multiple stages, and due to the pressure loss when passing through the throttles,
The pressure of the gas rising between the partition wall 32 and the inner peripheral surface of the drum 18 decreases as it flows upward.
Therefore, by appropriately adjusting the opening degree of the throttle 36, the difference between the water pressure and the gas pressure inside and outside the drum 18 in each nozzle 24 can be made almost equal. This makes it possible to eject an equal amount of gas from each nozzle 24 per unit time, and the diameters of bubbles generated from each nozzle 24 are made equal.
なお、本実施例装置の運転開始前の状態にあつ
ては、ドラム18内には液体が入つている。この
液体は、装置の運転開始に伴つて気体供給管から
供給される気体に押されると共に、ドラム18の
回転遠心力によつて、ドラム18外に排出され
る。 Note that before the apparatus of this embodiment starts operating, the drum 18 contains liquid. This liquid is pushed by the gas supplied from the gas supply pipe when the apparatus starts operating, and is also discharged out of the drum 18 by the rotational centrifugal force of the drum 18.
上記実施例では、ノズル24を突設しているの
で、ドラム18と共に回る液体の速度が小さくな
つた箇所で気体が噴出されるようなり、それだけ
噴出気体の剪断効果が高く、気泡が微細になると
いう効果がある。即ち、ドラム18を回転させる
と、ドラム18の側周に接している液体もドラム
18と共に回転するが、ドラム18の表面から遠
ざかるにつれて液体の速度は低下してくる。 In the above embodiment, since the nozzle 24 is provided in a protruding manner, the gas is ejected at a point where the speed of the liquid rotating together with the drum 18 is reduced, which increases the shearing effect of the ejected gas and makes the bubbles finer. There is an effect. That is, when the drum 18 is rotated, the liquid in contact with the side circumference of the drum 18 also rotates with the drum 18, but the speed of the liquid decreases as it moves away from the surface of the drum 18.
従つて、ノズル24の先端では、ドラム18の
表面に比べ、液体との相対速度差が大きくなり、
噴出される気体に大きな剪断力を作用させること
が可能となるのである。 Therefore, the relative velocity difference between the tip of the nozzle 24 and the liquid is larger than that at the surface of the drum 18.
This makes it possible to apply a large shearing force to the ejected gas.
また、上記実施例では、ドラム底板18aが摺
動部材30を介して気体供給管28に枢支される
構成となつており、ドラム18が上下2箇所の支
持となり、安定した回転が行なえるという効果が
ある。但し、本発明では、ドラム底板は必須では
なく、有蓋無底のドラムとしても良い。この場
合、ドラム下端にスポークを半径方向に延設し、
このスポークの先端に、気体供給管28に遊嵌す
るボス部材を固設せしめるようにしても良い。 Further, in the above embodiment, the drum bottom plate 18a is configured to be pivotally supported by the gas supply pipe 28 via the sliding member 30, and the drum 18 is supported in two places, upper and lower, and stable rotation can be performed. effective. However, in the present invention, the drum bottom plate is not essential, and a drum with a lid and no bottom may be used. In this case, spokes are installed radially at the bottom end of the drum,
A boss member that loosely fits into the gas supply pipe 28 may be fixed to the tip of the spoke.
なお、上記実施例では仕切板32は上下に等径
であるが、必ずしもこれに限定されない。例え
ば、下方程小径化する形状のものなども採用で
き、この場合には圧損を付与するための絞り36
を省略することが可能となる。また円筒形でなく
とも良く、6角形、8角形等の多角形としても良
い。 In the above embodiment, the partition plates 32 have the same diameter at the top and bottom, but the diameter is not necessarily limited to this. For example, it is also possible to adopt a shape that becomes smaller in diameter toward the bottom, and in this case, the orifice 36 to provide pressure loss
can be omitted. Moreover, it does not have to be cylindrical, but may be polygonal such as hexagonal or octagonal.
[効果]
以上の通り、本発明によれば均一な径の微細気
泡を発生させることが可能で、気液接触効率が高
い気液接触装置が提供される。[Effects] As described above, according to the present invention, a gas-liquid contact device is provided that is capable of generating microbubbles with a uniform diameter and has high gas-liquid contact efficiency.
本発明の気液接触装置は、各種水処理装置や、
養殖魚槽への空気や酸素の供給装置、あるいは気
液接触反応装置、ガス吸収装置、湿式集塵装置、
ガス脱硫装置など各種装置として極めて好適に適
用可能である。 The gas-liquid contact device of the present invention can be used in various water treatment devices,
Equipment for supplying air and oxygen to aquaculture fish tanks, gas-liquid contact reaction equipment, gas absorption equipment, wet dust collectors,
It can be extremely suitably applied to various devices such as gas desulfurization equipment.
第1図は本発明の実施例装置の縦断面図であ
る。
10……槽体、18……回転ドラム、22……
開口、24……ノズル、28……気体供給管、3
2……仕切壁。
FIG. 1 is a longitudinal sectional view of an apparatus according to an embodiment of the present invention. 10... Tank body, 18... Rotating drum, 22...
Opening, 24... Nozzle, 28... Gas supply pipe, 3
2... Partition wall.
Claims (1)
して設置された有蓋でかつ側周面に多数の気体噴
出口を有する回転ドラムと、該回転ドラムの天蓋
部より垂設された該回転ドラムよりも小径筒状の
仕切壁と、該仕切壁下部に設けられた仕切壁内外
部の連通部と、該仕切壁外周面と回転ドラム内周
面との間に配設された、上昇気体に通過圧損を付
与するための絞りと、前記回転ドラムの底板中央
より該回転ドラム内に挿入された気体供給管と、
を有する気液接触装置。1. A tank body, a rotary drum with a lid installed in the tank body with the axial direction in a substantially vertical direction and having a large number of gas ejection ports on the side circumferential surface, and a rotary drum installed vertically from the canopy of the rotary drum. A cylindrical partition wall having a diameter smaller than that of the rotating drum, a communication portion between the inside and outside of the partition wall provided at the lower part of the partition wall, and a partition wall disposed between the outer circumferential surface of the partition wall and the inner circumferential surface of the rotating drum. a throttle for imparting a passing pressure drop to the rising gas; a gas supply pipe inserted into the rotating drum from the center of the bottom plate of the rotating drum;
A gas-liquid contact device with
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61160584A JPS6316034A (en) | 1986-07-08 | 1986-07-08 | Gas-liquid contact apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61160584A JPS6316034A (en) | 1986-07-08 | 1986-07-08 | Gas-liquid contact apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6316034A JPS6316034A (en) | 1988-01-23 |
| JPH0258971B2 true JPH0258971B2 (en) | 1990-12-11 |
Family
ID=15718116
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61160584A Granted JPS6316034A (en) | 1986-07-08 | 1986-07-08 | Gas-liquid contact apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6316034A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4990166A (en) * | 1989-06-08 | 1991-02-05 | Babich William F | Gas stream purifying equipment |
| JPH0751198Y2 (en) * | 1990-04-10 | 1995-11-22 | 宇部興産株式会社 | Gas-liquid contact device |
-
1986
- 1986-07-08 JP JP61160584A patent/JPS6316034A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6316034A (en) | 1988-01-23 |
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