JPS5854166Y2 - Water sprinkler type defoaming device - Google Patents

Water sprinkler type defoaming device

Info

Publication number
JPS5854166Y2
JPS5854166Y2 JP18003578U JP18003578U JPS5854166Y2 JP S5854166 Y2 JPS5854166 Y2 JP S5854166Y2 JP 18003578 U JP18003578 U JP 18003578U JP 18003578 U JP18003578 U JP 18003578U JP S5854166 Y2 JPS5854166 Y2 JP S5854166Y2
Authority
JP
Japan
Prior art keywords
water
liquid
tower
water sprinkling
defoaming device
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
Application number
JP18003578U
Other languages
Japanese (ja)
Other versions
JPS5599712U (en
Inventor
義郎 安東
育三 前野
Original Assignee
住友精密工業株式会社
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 住友精密工業株式会社 filed Critical 住友精密工業株式会社
Priority to JP18003578U priority Critical patent/JPS5854166Y2/en
Publication of JPS5599712U publication Critical patent/JPS5599712U/ja
Application granted granted Critical
Publication of JPS5854166Y2 publication Critical patent/JPS5854166Y2/en
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 この考案は、発泡性の強い液体(以下、泡沫液という)
から発生する泡沫を散水により破壊し処理する散水型の
消泡装置に関する。
[Detailed explanation of the invention] This invention is a highly foaming liquid (hereinafter referred to as foaming liquid).
This invention relates to a water sprinkling type defoaming device that destroys and disposes of foam generated from water by sprinkling water.

このような消泡装置は、例えばオゾンによる水処理設備
等に使用される。
Such defoaming devices are used, for example, in water treatment equipment using ozone.

第1図は消泡装置を排水のオゾン処理の際に生じる未反
応の余剰オゾン(以下、排オゾンという)に対して適用
した例である。
FIG. 1 shows an example in which a defoaming device is applied to unreacted surplus ozone (hereinafter referred to as exhaust ozone) generated during ozone treatment of wastewater.

オゾン処理の対象となる排水はそれ自身発泡性があるか
、あるいはオゾンと反応して発泡性物質を生成する場合
が多い。
The wastewater to be ozonated often has foaming properties itself or reacts with ozone to produce foaming substances.

したがって排オゾンも多くの場合、泡沫を伴ない後段の
排オゾン分解装置に侵入して分解剤の性能を劣化させる
Therefore, exhaust ozone also often enters the downstream exhaust ozone decomposition device accompanied by foam, deteriorating the performance of the decomposer.

そこで従来は第1図に示すように、排オゾンを含有する
泡沫液を導入管1で処理塔2内へ取入れ、これに塔内上
方の散水ノズル3から清水を噴射して泡沫を破壊した後
、液分がら分離した排オゾンを塔上部の放出管4より取
出し、液分は噴射水とともにサイフオンブレーカ−等の
排水管5により逐次塔外へ排出させる。
Therefore, conventionally, as shown in Fig. 1, a foamy liquid containing exhaust ozone is introduced into a treatment tower 2 through an introduction pipe 1, and fresh water is injected into it from a water spray nozzle 3 located above the tower to destroy the foam. The waste ozone separated from the liquid component is taken out from the discharge pipe 4 at the top of the tower, and the liquid component is sequentially discharged to the outside of the tower through a drain pipe 5 such as a siphon breaker together with the jet water.

ところがこの場合、清水の圧力は必ずしも一定とは限ら
ず散水の勢力も安定とは言えなかった。
However, in this case, the pressure of the fresh water was not necessarily constant, and the force of the water sprinkling was also not stable.

しかも上記泡沫液は、前段のオゾン処理反応塔(図示せ
ず)内におけるフローテーション効果により53分を多
量に含有する。
Moreover, the foamed liquid contains a large amount of 53% due to the flotation effect in the ozonation reaction tower (not shown) at the previous stage.

このため塔外へ排出される水液中に53分が濃縮された
形で混入し、これをそのまま河川等へ放流することは環
境衛生上好ましくない。
For this reason, 53 min is mixed in a concentrated form in the aqueous liquid discharged outside the tower, and it is unfavorable from an environmental hygiene standpoint to discharge this as it is into a river or the like.

そこでこの排出液はSS除去装置」三原の凝集沈澱槽、
濾過槽等へ戻され再度35分の除去処理を受けるのが通
例であるが、従来の清水を多量に使用する消泡装置では
、清水のコストが嵩むばかりでなく、SS除去装置の容
量負荷を大きくする欠点があった。
Therefore, this effluent is collected from the SS removal equipment, Mihara's coagulation sedimentation tank,
Normally, it is returned to a filtration tank and subjected to another 35-minute removal process, but with conventional defoaming devices that use a large amount of fresh water, not only does the cost of fresh water increase, but it also increases the capacity load of the SS removal device. There was a drawback to making it bigger.

本考案は、消泡機能を損うことなく上記欠点が解消でき
、性能、経済ともに優れた消泡装置を提供する。
The present invention provides a defoaming device that can eliminate the above drawbacks without impairing the defoaming function and is excellent in both performance and economy.

以下、第2図に掲げる実施例に基づいて本考案を詳細に
説明する。
Hereinafter, the present invention will be explained in detail based on the embodiment shown in FIG.

同図において、1は第1図の1に相当する泡沫液の導入
管であり、同様に2は処理塔、30,32は散水ノズル
、4は気体放出管、5は排出管である。
In the figure, 1 is a foam liquid introduction pipe corresponding to 1 in FIG. 1, 2 is a treatment tower, 30 and 32 are water nozzles, 4 is a gas discharge pipe, and 5 is a discharge pipe.

導入管1は処理塔2頂部に設けられ、泡沫液を塔頂部か
ら落下させることによって塔内の気泡の一部が衝撃破壊
されるよう工夫しである。
The introduction pipe 1 is provided at the top of the treatment tower 2, and is designed so that some of the bubbles in the tower are destroyed by impact by dropping the foam liquid from the top of the tower.

散水ノズル31,3□は、本考案では図示のように2系
列設け、一方のノズル3、が塔内へ導入した泡沫液を循
環させるため、導入液が塔下部の出水口6から加圧ポン
プ7へ送られ、ここから更に手動弁8、液量計9を経て
前記散水ノズル3、に環流するよう設けられる。
In the present invention, the water spray nozzles 31, 3□ are provided in two lines as shown in the figure, and one nozzle 3 circulates the foamy liquid introduced into the tower, so that the introduced liquid is passed from the water outlet 6 at the bottom of the tower to the pressurizing pump. 7, and from there, it is provided so as to be circulated back to the water spray nozzle 3 via a manual valve 8 and a liquid meter 9.

もう一方の散水ノズル32に清水源(図示せず)が手動
弁10を介して接続され、必要に応じて清水も噴射でき
るよう設けられる。
A fresh water source (not shown) is connected to the other water spray nozzle 32 via a manual valve 10, so that fresh water can also be sprayed as needed.

他方、排水管5は例えば第1図に示すようなサイフオン
ブレーカ−形式のものでもよいが、この例では前記加圧
ポンプ7を間欠的に動作させるため、ポンプ7の出側配
管に接続され手動弁11を備える。
On the other hand, the drain pipe 5 may be of the siphon-on-breaker type as shown in FIG. A manual valve 11 is provided.

加圧ポンプ7の間欠動作については後の作用の説明のと
ころで詳しく述べるか′、ポンプを間欠的に動作させる
と電力消費が節減で゛き経済効果を一層増長する。
The intermittent operation of the pressurizing pump 7 will be described in detail later in the explanation of its function, but when the pump is operated intermittently, power consumption can be reduced and the economic effect can be further increased.

−UL記加圧ポンプ7は、間欠動作のため更に処理塔2
に設けた液面計12および13によって制御され、上方
の液面計12で導入液の液面の−L限位NHを検出し、
検出信号がポンプ7の制御器14に人力してポンプ7を
起動するとともに、下方の液面計13で液面の下限位置
りを検出しその検出信号によって加圧ポンプ7が停止す
るよう設けられる。
- Because the UL pressure pump 7 operates intermittently, the processing tower 2
The upper liquid level gauge 12 detects the -L limit NH of the liquid level of the introduced liquid.
A detection signal is manually input to the controller 14 of the pump 7 to start the pump 7, and a lower liquid level gauge 13 detects the lower limit position of the liquid level, and the pressure pump 7 is stopped by the detection signal. .

次に作用を説明する。Next, the effect will be explained.

先ず通常の泡沫液を処理する場合、散水ノズル31に係
る手動弁8および11を開き、この状態で処理塔2内に
泡沫液を導入する。
First, when treating a normal foamy liquid, the manual valves 8 and 11 associated with the water spray nozzle 31 are opened, and the foamy liquid is introduced into the treatment tower 2 in this state.

導入液の液面が上限位置Hに達すると、加圧ポンプ7が
起動し塔内の導入液を扱上げてその一部が散水ノズル3
、から塔内に噴射され、扱上げた液の残りは排水管5を
経て装置外へ排出される。
When the liquid level of the introduced liquid reaches the upper limit position H, the pressurizing pump 7 starts to handle the introduced liquid in the tower, and a part of it is sent to the water spray nozzle 3.
The remaining liquid is injected into the tower from , and the remainder of the treated liquid is discharged to the outside of the apparatus through a drain pipe 5.

このとき装置外へ排出される液量が泡沫液の導入量より
多くなるよう前記手動弁8および11を調節しておけば
、塔内の導入液が徐々に)威少し、その液面が下限位置
りまで下がると加圧ポンプ7が停止する。
At this time, if the manual valves 8 and 11 are adjusted so that the amount of liquid discharged outside the device is greater than the amount of foamed liquid introduced, the liquid introduced into the tower will gradually become sluggish, and the liquid level will reach the lower limit. When the pressure pump 7 is lowered to this position, the pressure pump 7 stops.

これによって導入液の液面が再び上昇し、上限位置Hに
到達すると同時に散水が再開される。
As a result, the level of the introduced liquid rises again, and at the same time as reaching the upper limit position H, watering is restarted.

ン このようにして散水が間欠的に繰返されて塔内の導入液
が消泡処理される。
In this way, water sprinkling is repeated intermittently, and the liquid introduced into the column is defoamed.

上記消泡処理は主に散水の物理的な破壊作用によるため
、導入液を循環使用したことによる処理効果の低下は殆
んど認められない。
Since the defoaming treatment described above mainly relies on the physical destructive action of water spraying, there is hardly any decrease in the treatment effect due to the circulating use of the introduced liquid.

それよりも導入液を加圧ポンプ7で扱」二げノズル3□
から強力かつ安定に噴射することによる処理効果の向上
や、導入液を循環使用することによって清水を不用なら
しめ、これによって生じる経済効果のほうがはるかに大
きく、特に実施例に示したように加圧ポンプの間欠動作
と組合せた場合には、水費用、電気料の両面で経費が著
しく節約できる。
Rather, the introduced liquid is handled by the pressure pump 7.
The economic effects of this are far greater, such as improving the treatment effect by powerful and stable spraying from the tank, and eliminating the need for fresh water by circulating the introduced liquid. When combined with intermittent operation of the pump, significant savings can be made in both water and electricity costs.

また、発泡性の特に強い液体を処理したり、導入液が少
なく散水用水の不足する場合は、更に散水ノズル3゜に
接続する手動弁10を開き、清水による散水も合せて行
なう。
In addition, when processing a particularly strong foaming liquid or when the amount of introduced liquid is low and water for sprinkling is insufficient, the manual valve 10 connected to the water sprinkling nozzle 3° is further opened to perform water sprinkling with fresh water.

この場合、必要量の清水が得られるよう手動弁10の開
度を調節するのは勿論であるが、更に手動弁8および1
1も調整して塔内に流入する水液の量が排水量を超えな
いようにする。
In this case, it goes without saying that the opening degree of the manual valve 10 is adjusted to obtain the required amount of fresh water, but also
1 is also adjusted so that the amount of water flowing into the tower does not exceed the amount of drainage.

清水による散水を追加することによって、僅かの出費で
従来装置を凌ぐ処理効果をあげることか゛できる。
By adding fresh water sprinkling, it is possible to achieve a treatment effect that exceeds that of conventional equipment at a small expense.

本考案の消泡装置は、上述のとおり安定かつ強力な消泡
ができるばかりでなく経済性にも優れ、装置の維持運転
費用を軽減するとともに、装置外に排出する水液の量が
少ないから、例えば水処理設備の排オゾン処理に使用し
た場合、SS除去装置の容量を小さくできこの方の設備
費、運転費を6下げる効果もある。
As mentioned above, the defoaming device of the present invention not only performs stable and powerful defoaming, but also has excellent economic efficiency, reducing equipment maintenance and operation costs, and reducing the amount of water discharged outside the device. For example, when used for exhaust ozone treatment in water treatment equipment, the capacity of the SS removal device can be reduced, which has the effect of lowering equipment costs and operating costs.

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

第1図は従来の消泡装置の一例を示す系統図、第2図は
本考案梢泡装置の一例を示す系統図である。 図中の記号の説明 1.泡沫液の導入管、2:処理塔、
3□、32:散水ノズル、4:気体放出管、5.排水管
、6:出水口、7:加圧ポンプ、8,10.11 :手
動弁、12.13 :液面計、14:制御器。
FIG. 1 is a system diagram showing an example of a conventional defoaming device, and FIG. 2 is a system diagram showing an example of the foam defoaming device of the present invention. Explanation of symbols in the diagram 1. Foam liquid introduction pipe, 2: treatment tower,
3□, 32: Water nozzle, 4: Gas discharge pipe, 5. Drain pipe, 6: Water outlet, 7: Pressure pump, 8, 10.11: Manual valve, 12.13: Level gauge, 14: Controller.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 処理塔内上方に散水ノズルを備え処理塔内に導入する発
泡性の強い液体を散水により消泡処理する散水型の消泡
装置において、処理塔から取出した前記導入液を循環使
用するための加圧ポンプ7および散水ノズル3、を備え
た循環散水系を設け、上記加圧ポンプで汲上げた導入液
の一部を消泡装置外部に排出し、処理塔内の導入液の液
面レベルに応じて前記ノズルからの散水を間欠的に繰返
し行なうとともに、清水源に接続した散水ノズル3゜を
備えた別の散水系を設けたことを特徴とする散水型消泡
塔。
In a water sprinkling type defoaming device that is equipped with a water spray nozzle in the upper part of the treatment tower and defoams a strongly foaming liquid introduced into the treatment tower by spraying water, a water spraying type defoaming device is used for recycling and reusing the introduced liquid taken out from the treatment tower. A circulation water sprinkling system equipped with a pressure pump 7 and a water sprinkling nozzle 3 is provided, and a part of the introduced liquid pumped up by the pressure pump is discharged to the outside of the defoaming device, and the level of the introduced liquid in the treatment tower is raised to the level of the introduced liquid. A water sprinkling type defoaming tower, characterized in that the water sprinkling from the nozzle is repeated intermittently in response to the above, and is provided with another water sprinkling system equipped with a water sprinkling nozzle 3° connected to a fresh water source.
JP18003578U 1978-12-28 1978-12-28 Water sprinkler type defoaming device Expired JPS5854166Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18003578U JPS5854166Y2 (en) 1978-12-28 1978-12-28 Water sprinkler type defoaming device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18003578U JPS5854166Y2 (en) 1978-12-28 1978-12-28 Water sprinkler type defoaming device

Publications (2)

Publication Number Publication Date
JPS5599712U JPS5599712U (en) 1980-07-11
JPS5854166Y2 true JPS5854166Y2 (en) 1983-12-09

Family

ID=29191707

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18003578U Expired JPS5854166Y2 (en) 1978-12-28 1978-12-28 Water sprinkler type defoaming device

Country Status (1)

Country Link
JP (1) JPS5854166Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5964740B2 (en) * 2012-12-21 2016-08-03 株式会社荏原製作所 Polishing equipment

Also Published As

Publication number Publication date
JPS5599712U (en) 1980-07-11

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