JPS6354414B2 - - Google Patents
Info
- Publication number
- JPS6354414B2 JPS6354414B2 JP56012167A JP1216781A JPS6354414B2 JP S6354414 B2 JPS6354414 B2 JP S6354414B2 JP 56012167 A JP56012167 A JP 56012167A JP 1216781 A JP1216781 A JP 1216781A JP S6354414 B2 JPS6354414 B2 JP S6354414B2
- Authority
- JP
- Japan
- Prior art keywords
- mixture
- oxygen
- suction opening
- sludge
- retention container
- 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
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
- B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
- B01F23/2323—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
- B01F23/23231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit
-
- 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
- B01F23/234—Surface aerating
-
- 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
- B01F23/234—Surface aerating
- B01F23/2341—Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere
- B01F23/23413—Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere using nozzles for projecting the liquid into the gas atmosphere
-
- 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
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/45—Mixing liquids with liquids; Emulsifying using flow mixing
- B01F23/454—Mixing liquids with liquids; Emulsifying using flow mixing by injecting a mixture of liquid and gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Description
【発明の詳細な説明】
本発明は混合装置、特に汚水処理あるいは化学
処理などにおいて2相以上の成分を含む混合体を
効果的に撹拌混合することのできる混合装置に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a mixing device, and particularly to a mixing device that can effectively stir and mix a mixture containing components of two or more phases in sewage treatment or chemical treatment.
2相以上の液体あるいは気体と液体との分散ま
たは撹拌混合を行うことが各種の処理工程におい
て必要とされ、例えば廃水、廃液などの汚水に酸
素を供給して汚水を活性化させる汚水処理工程、
また化学処理における乳化や反応、溶解時におけ
る2相以上の液体及び気体と液体との混合として
周知である。 Dispersion or agitation mixing of two or more phases of liquid or gas and liquid is required in various treatment processes, such as sewage treatment processes in which oxygen is supplied to wastewater, waste liquid, etc. to activate the wastewater,
It is also well known as a liquid of two or more phases or a mixture of a gas and a liquid during emulsification, reaction, or dissolution in chemical processing.
従来、前述した撹拌混合はポンプによる混合あ
るいは静止型ミキサによる混合などが一般的であ
るが、これら混合装置によつても、未混合のもの
が生し、このために混合効率が著しく低下し、ま
た未混合の気体あるいは液体成分の量が所定量以
上に達すると爆発その他の危険が発生するなどの
問題があつた。 Conventionally, the above-mentioned agitation mixing has generally been carried out using a pump or a static mixer, but even with these mixing devices, unmixed materials are produced, which significantly reduces the mixing efficiency. Furthermore, if the amount of unmixed gas or liquid components exceeds a predetermined amount, there is a problem that an explosion or other danger may occur.
本発明は上記従来の課題に鑑みなされたもので
あり、この目的は、未混合成分を再び混合作用に
供することによつて混合効率を改善し、効果的な
混合作用を行うことのできる改良された混合装置
を提供することにある。 The present invention has been made in view of the above-mentioned conventional problems, and the object thereof is to improve the mixing efficiency by subjecting the unmixed components to the mixing action again, and to provide an improved method capable of performing an effective mixing action. The object of the present invention is to provide a mixing device that has the following characteristics.
上記目的を達成するために、本発明は、2相以
上の成分を含む混合体が導入され、これらの成分
を少なくとも上相および下相として保持する密閉
型滞留容器と、該滞留容器内に設けられ混合体を
滞留容器に導くための導入管と、を有し、前記導
入管は、その側部に設けられ上相内に開口した吸
入開口と、該吸入開口近傍に設けられ混合体が下
方に向けて噴射される噴射ノズルと、この噴射ノ
ズルを取り囲み下相内にまで伸びるとともに下方
に向けて開口する筒体と、を含み、噴射ノズルか
ら混合体を噴射することによつて滞留容器の上部
に残つた未混合の上相の成分を吸入開口から導入
管に吸入し、再混合に供するとともに、この再結
合した混合体を下相内に導入することによつて混
合体を下相内において下方に向けて拡散させるこ
とを特徴とする。 In order to achieve the above object, the present invention provides a closed retention container into which a mixture containing components of two or more phases is introduced and retains these components as at least an upper phase and a lower phase; an inlet pipe for guiding the mixture into the retention container, the inlet pipe having a suction opening provided on the side thereof and opening into the upper phase, and a suction opening provided near the suction opening so that the mixture is directed downwardly. a cylinder body that surrounds the injection nozzle, extends into the lower phase, and opens downward, and the mixture is injected from the injection nozzle into the retention vessel. The components of the unmixed upper phase remaining in the upper part are sucked into the inlet pipe through the suction opening and subjected to remixing, and the recombined mixture is introduced into the lower phase, thereby causing the mixture to flow into the lower phase. It is characterized by being diffused downward at.
以下図面に基づいて本発明の好適な実施例を説
明する。 Preferred embodiments of the present invention will be described below based on the drawings.
第1図には都市下水その他の廃水処理工程にお
いて沈澱池からばつき槽へ返送される返送汚泥に
酸素を吹込供給して汚水を活性化させる汚水処理
装置に用いられる混合装置が示され、図示してい
ない沈澱池から返送汚泥が返送導管10,12に
よつてばつき槽へ返送され、両返送導管10,1
2の間に本発明に係る密閉型滞留容器14が設け
られている。滞留容器14を返送導管10,12
に接続する導入及び導出部を除いて気密構造から
成り、実施例における上部に設けられた導入管1
6から2相以上の成分を含む混合体が導入され
る。実施例における混合体は返送導管10から供
給される返送汚泥と、該返送導管10にバルブ1
8から供給される酸素との液体及び気体成分から
成り、返送汚泥中に酸素が混合されて返送汚泥中
のバクテリアが充分に活性化されて汚水処理を行
うことができる。そして、本発明における滞留容
器14は返送汚泥と酸素との処理時間を充分に確
保することができ、すなわち、滞留容器14の流
路断面積は返送導管10,12の面積に比較して
充分大きく設定されているので、返送導管10か
ら供給された活性汚泥と酸素とは滞留容器14内
で充分長い時間滞留し、この滞留時間内で返送汚
泥内への酸素の充分な溶解が行われ、バクテリア
が効果的に活性化されることとなる。 Figure 1 shows a mixing device used in a sewage treatment system that activates sewage by injecting oxygen into returned sludge returned from a settling tank to a dusting tank in urban sewage and other wastewater treatment processes. Return sludge from a settling tank (not shown) is returned to the dusting tank via return conduits 10 and 12, and both return conduits 10 and 1
A closed retention container 14 according to the present invention is provided between the two. The retention container 14 is returned to the return conduits 10, 12.
The inlet pipe 1 has an airtight structure except for the inlet and outlet parts connected to the inlet pipe 1 provided at the upper part in the embodiment.
From 6 onwards, a mixture containing components of two or more phases is introduced. The mixture in the embodiment includes return sludge supplied from a return conduit 10 and a valve 1 in the return conduit 10.
The sludge is composed of liquid and gas components with oxygen supplied from 8, and the oxygen is mixed into the returned sludge, and the bacteria in the returned sludge are sufficiently activated to perform sewage treatment. The retention container 14 according to the present invention can ensure sufficient processing time for the return sludge and oxygen, that is, the flow passage cross-sectional area of the retention container 14 is sufficiently large compared to the area of the return conduits 10 and 12. Since the activated sludge and oxygen supplied from the return conduit 10 remain in the retention container 14 for a sufficiently long time, the oxygen is sufficiently dissolved in the return sludge within this retention time, and bacteria are removed. will be effectively activated.
第1図の実施例において、導入管16はほぼ円
筒形状から成り、その上部開口が返送導管10と
接続され前記返送汚泥と酸素との混合体が導入さ
れるとともに、その下端開口が滞留容器14内に
滞留している混合体内に伸張している。そして、
下端は下方に向けて開口している。実施例の導入
管16はほぼストレートな円筒筒体であり、この
中を返送汚泥が比較的高速度で通過する際に酸素
の溶解が行われる。 In the embodiment shown in FIG. 1, the introduction pipe 16 has a substantially cylindrical shape, and its upper opening is connected to the return pipe 10 to introduce the mixture of return sludge and oxygen, and its lower end opening is connected to the return pipe 10. It extends into the mixture that stays inside. and,
The lower end is open downward. The inlet pipe 16 in the embodiment is a substantially straight cylindrical body, through which oxygen is dissolved as the returned sludge passes at a relatively high speed.
また、本発明においては、前記導入管16の側
部に吸入開口20が設けられ、また該吸入開口2
0の近傍にオリフイスから成る噴射ノズル22が
形成されていることを特徴とし、この結果、導入
管16に導かれた返送汚泥と酸素とが噴射ノズル
22の噴射時に充分に撹拌混合されるとともに、
滞留容器14の上部に残つた未混合の酸素が前記
吸入開口20から導入管16に吸入され再混合に
供されることを特徴とする。すなわち、密閉型滞
留容器14内で前記返送汚泥と酸素とが混合して
いる時、返送汚泥中に溶け込めなかつた未混合の
酸素は返送汚泥液面に上昇し滞留容器14の上部
に溜まる。そして、前述したように、本発明の導
入管16はその側部に吸入開口20が設けられる
とともに、該吸入開口20の近傍に噴射ノズル2
2が設けられていることから、返送汚泥が導入管
16内を高速度で通流する際に吸入開口20の近
傍に溜まつた酸素が導入管16内に引き込まれ、
再び返送汚泥と充分に撹拌混合され、汚泥中に充
分溶け込むことが可能となる。 Further, in the present invention, a suction opening 20 is provided on the side of the introduction pipe 16, and the suction opening 20 is provided at the side of the introduction pipe 16.
It is characterized in that an injection nozzle 22 consisting of an orifice is formed in the vicinity of the injection nozzle 22. As a result, the return sludge introduced into the introduction pipe 16 and oxygen are sufficiently stirred and mixed during injection by the injection nozzle 22,
It is characterized in that the unmixed oxygen remaining in the upper part of the retention container 14 is sucked into the introduction pipe 16 through the suction opening 20 and subjected to remixing. That is, when the return sludge and oxygen are mixed in the closed retention container 14, unmixed oxygen that cannot be dissolved in the return sludge rises to the liquid surface of the return sludge and accumulates in the upper part of the retention container 14. As described above, the introduction pipe 16 of the present invention is provided with a suction opening 20 on the side thereof, and has an injection nozzle 2 in the vicinity of the suction opening 20.
2, when the return sludge flows through the introduction pipe 16 at high speed, the oxygen accumulated near the suction opening 20 is drawn into the introduction pipe 16,
It is sufficiently stirred and mixed with the returned sludge again, making it possible to sufficiently dissolve it into the sludge.
以上のようにして、第1図の実施例によれば、
密閉型滞留容器14内で酸素が効率よく返送汚泥
中に撹拌混合され、未混合の酸素もそのまま捨て
られることなく繰返し返送汚泥と接触混合される
ので、極めて効率よく返送汚泥の活性化を行うこ
とが可能となる。また、混合体は、導入管16の
下端から下方に向けて放出されるので、気泡に滞
留時間が長くなり、混合溶解が促進される。 As described above, according to the embodiment shown in FIG.
Oxygen is efficiently stirred and mixed into the returned sludge in the closed retention container 14, and unmixed oxygen is not discarded as it is but is repeatedly contacted and mixed with the returned sludge, so that the returned sludge can be activated extremely efficiently. becomes possible. Further, since the mixture is discharged downward from the lower end of the introduction pipe 16, the residence time in the bubbles becomes longer, and mixing and dissolution is promoted.
第2図には本発明の第2実施例が示され、第1
図とほぼ同様の構成から成るので同一部材には同
一符号を付して説明を省略する。 A second embodiment of the invention is shown in FIG.
Since the configuration is substantially the same as that shown in the drawings, the same members are given the same reference numerals and explanations will be omitted.
第2図の実施例において特徴的なことは、前記
導入管16の下方に静止型ミキサ24が設けられ
ていることであり、返送汚泥と酸素とがミキサ2
4にて充分に混合撹拌され、混合効率を更に改善
することが可能となる。 A characteristic feature of the embodiment shown in FIG. 2 is that a static mixer 24 is provided below the introduction pipe 16, and the return sludge and oxygen are transferred
4, the mixture is sufficiently mixed and stirred, making it possible to further improve the mixing efficiency.
前述した各実施例においては、返送汚泥の活性
化のために酸素が用いられているが、この酸素は
純酸素でもあるいは空気でもよく、また適宜他の
活性剤例えば純酸素とオゾンとの混合気体、過酸
化水素、次亜塩素酸ソーダあるいは純酸素と凝集
剤との混合剤とすることも可能である。 In each of the above-mentioned embodiments, oxygen is used to activate the returned sludge, but this oxygen may be pure oxygen or air, or other activating agents such as a mixed gas of pure oxygen and ozone may be used as appropriate. , hydrogen peroxide, sodium hypochlorite, or a mixture of pure oxygen and a flocculant.
また、実施例においては返送汚泥と酸素との混
合体が用いられているが、化学処理工程における
2相液体あるいは液体と気体との反応及び溶解あ
るいは乳化などに本発明の装置を利用することも
可能であり、特に比重の異なる例えば油と水をエ
マルジヨン化する場合などにも極めて有効であ
り、比重の小さい成分が滞留容器14の上部に未
混合成分として浮上し、これが再び導入管内に吸
入されて再混合に供されることとなる。 Furthermore, although a mixture of returned sludge and oxygen is used in the examples, the apparatus of the present invention can also be used for reactions, dissolution, or emulsification of two-phase liquids or liquids and gases in chemical treatment processes. This is possible, and is extremely effective especially when emulsifying oil and water, which have different specific gravity, such that components with lower specific gravity float to the top of the retention container 14 as unmixed components, and are sucked into the introduction pipe again. The mixture will then be remixed.
以上説明したように、本発明によれば、2相以
上の成分を含む混合体が極めて効率よく混合さ
れ、また装置を小型化することが可能となる。 As described above, according to the present invention, a mixture containing components of two or more phases can be mixed extremely efficiently, and the apparatus can be downsized.
第1図は本発明に係る混合装置の好適な実施例
を示す概略構成図、第2図は本発明の他の実施例
を示す概略構成図である。
14……密閉型滞留容器、16……導入管、2
0……吸入開口、22……噴射ノズル。
FIG. 1 is a schematic diagram showing a preferred embodiment of a mixing device according to the present invention, and FIG. 2 is a schematic diagram showing another embodiment of the present invention. 14...closed retention container, 16...introduction pipe, 2
0... Suction opening, 22... Injection nozzle.
Claims (1)
れらの成分を少なくとも上相および下相として保
持する密閉型滞留容器と、 該滞留容器内に設けられ混合体を滞留容器に導
くための導入管と、 を有し、 前記導入管は、 その側部に設けられ上相内に開口した吸入開口
と、該吸入開口近傍に設けられ混合体が下方に向
けて噴射される噴射ノズルと、この噴射ノズルを
取り囲み下相内にまで伸びるとともに下方に向け
て開口する筒体と、 を含み、 噴射ノズルから混合体を噴射することによつて
滞留容器の上部に残つた未混合の上相の成分を吸
入開口から導入管に吸入し、再混合に供するとと
もに、この再結合した混合体を下相内に導入する
ことによつて混合体を下相内において下方に向け
て拡散させることを特徴とする混合装置。[Scope of Claims] 1. A closed retention container into which a mixture containing components of two or more phases is introduced and retains these components as at least an upper phase and a lower phase; and a closed retention container provided within the retention container to retain the mixture. an inlet pipe for introducing the mixture into the container, the inlet pipe having a suction opening provided on the side thereof and opening into the upper phase, and a suction opening provided near the suction opening through which the mixture is injected downward. an injection nozzle that surrounds the injection nozzle, extends into the lower phase, and opens downward; The components of the mixed upper phase are sucked into the inlet pipe through the suction opening and subjected to remixing, and the recombined mixture is introduced into the lower phase to direct the mixture downward in the lower phase. A mixing device characterized by diffusion.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56012167A JPS57127428A (en) | 1981-01-29 | 1981-01-29 | Mixer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56012167A JPS57127428A (en) | 1981-01-29 | 1981-01-29 | Mixer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57127428A JPS57127428A (en) | 1982-08-07 |
JPS6354414B2 true JPS6354414B2 (en) | 1988-10-27 |
Family
ID=11797873
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56012167A Granted JPS57127428A (en) | 1981-01-29 | 1981-01-29 | Mixer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS57127428A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0429848Y2 (en) * | 1989-12-26 | 1992-07-20 |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2763518B1 (en) * | 1997-05-26 | 1999-08-20 | Id O Concept | PLANT FOR THE TREATMENT OF FLUIDS SUCH AS BREEDING WATER FOR ANIMALS |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5020018U (en) * | 1973-06-19 | 1975-03-06 | ||
JPS5319170B2 (en) * | 1972-07-28 | 1978-06-19 | ||
JPS5444675A (en) * | 1977-09-12 | 1979-04-09 | Shin Etsu Chem Co Ltd | Production of 3-hydroxy-4-pyrone analog |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56231Y2 (en) * | 1976-07-28 | 1981-01-07 |
-
1981
- 1981-01-29 JP JP56012167A patent/JPS57127428A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5319170B2 (en) * | 1972-07-28 | 1978-06-19 | ||
JPS5020018U (en) * | 1973-06-19 | 1975-03-06 | ||
JPS5444675A (en) * | 1977-09-12 | 1979-04-09 | Shin Etsu Chem Co Ltd | Production of 3-hydroxy-4-pyrone analog |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0429848Y2 (en) * | 1989-12-26 | 1992-07-20 |
Also Published As
Publication number | Publication date |
---|---|
JPS57127428A (en) | 1982-08-07 |
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