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JP2885997B2 - Degassing device - Google Patents
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JP2885997B2 - Degassing device - Google Patents

Degassing device

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Publication number
JP2885997B2
JP2885997B2 JP17859592A JP17859592A JP2885997B2 JP 2885997 B2 JP2885997 B2 JP 2885997B2 JP 17859592 A JP17859592 A JP 17859592A JP 17859592 A JP17859592 A JP 17859592A JP 2885997 B2 JP2885997 B2 JP 2885997B2
Authority
JP
Japan
Prior art keywords
raw water
tower
water tank
inert gas
pipe
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 - Fee Related
Application number
JP17859592A
Other languages
Japanese (ja)
Other versions
JPH0615107A (en
Inventor
俊之 井上
秀夫 東
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ORUGANO KK
Original Assignee
ORUGANO KK
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 ORUGANO KK filed Critical ORUGANO KK
Priority to JP17859592A priority Critical patent/JP2885997B2/en
Publication of JPH0615107A publication Critical patent/JPH0615107A/en
Application granted granted Critical
Publication of JP2885997B2 publication Critical patent/JP2885997B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は水中の溶存酸素を除去す
る脱気装置に関し、更に詳しく述べれば本発明は半導体
製造、ボイラー、医薬製造等で使用される純水の製造の
際等に用いる脱気装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deaerator for removing dissolved oxygen in water, and more particularly to the present invention for use in the production of pure water used in semiconductor production, boilers, pharmaceutical production and the like. It relates to a deaerator.

【0002】[0002]

【従来の技術】従来、純水の製造等においては、ボイラ
ーの腐食防止やバクテリアの発生を防止する等の理由
で、水中の溶存酸素の除去が行われている。
2. Description of the Related Art Conventionally, in the production of pure water, dissolved oxygen in water has been removed for the purpose of preventing corrosion of boilers and generation of bacteria.

【0003】図5は従来の脱気装置の構成の一例を示す
もので、図中50は原水タンクである。原水は流入管5
1から原水タンク50に入り、ここで適宜貯留された
後、送水管52を通って脱気塔53の塔頂に送られる。
なお、54は送水ポンプである。次いで、塔頂に送られ
た原水は脱気塔内を流下する。
FIG. 5 shows an example of the configuration of a conventional deaerator, in which 50 is a raw water tank. Raw water is inflow pipe 5
From 1, the raw water enters a raw water tank 50, where it is appropriately stored, and then sent to the top of a degassing tower 53 through a water pipe 52.
Reference numeral 54 denotes a water pump. Next, the raw water sent to the top of the tower flows down in the degassing tower.

【0004】55は例えば窒素ガス等の不活性ガスの供
給管で、この供給管55から塔底に供給された窒素ガス
は塔53内を通過する際に前記原水と向流的に気液接触
をして、原水中の溶存酸素を除去し、塔頂から廃ガス管
56を通って大気中に放出される。一方、塔内で溶存酸
素を除去された原水は塔底から流出管57を通って取り
出され、処理水となる。なお、58は流出ポンプであ
る。
Reference numeral 55 denotes a supply pipe for supplying an inert gas such as nitrogen gas. The nitrogen gas supplied to the bottom of the tower from the supply pipe 55 is brought into gas-liquid contact with the raw water in a countercurrent manner when passing through the inside of the tower 53. To remove the dissolved oxygen in the raw water, and discharged from the tower through the waste gas pipe 56 to the atmosphere. On the other hand, the raw water from which dissolved oxygen has been removed in the tower is taken out from the tower bottom through the outflow pipe 57 and becomes treated water. Reference numeral 58 denotes an outflow pump.

【0005】この場合低濃度の溶存酸素の処理水を得よ
うとすれば曝気する窒素ガス量を多量にするか、塔高を
高くしたり塔径を大きくして気液反応時間を長くするこ
とが必要であったが、いずれも不経済なものであった。
[0005] In this case, in order to obtain treated water of a low concentration of dissolved oxygen, the amount of nitrogen gas to be aerated must be increased, or the height of the tower or the diameter of the tower must be increased to prolong the gas-liquid reaction time. Were required, but all were uneconomical.

【0006】[0006]

【発明が解決しようとする課題】本発明は上記事情に鑑
みなされたもので、その目的とするところは、塔頂から
放出される窒素ガス等の不活性ガスを有効に利用して、
高効率に原水中の溶存酸素を除去することのできる脱気
装置を提供することにある。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above circumstances, and it is an object of the present invention to effectively utilize an inert gas such as nitrogen gas discharged from a tower top.
An object of the present invention is to provide a deaerator capable of efficiently removing dissolved oxygen in raw water.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に本発明は、脱気処理をする原水を貯留する原水タンク
と、前記原水タンク中の原水を塔頂に供給すると共に塔
底から不活性ガスを供給して塔内で気液接触を行わせる
脱気塔とを有してなる原水中の溶存酸素を除去させる脱
気装置において、塔頂から排出される不活性ガスを前記
原水タンク内の下部側に送給する送給管を備え、塔頂か
ら排出される不活性ガスを原水タンク内の原水中に吹き
込むことにより原水タンク内の原水の溶存酸素を予め低
減させるもので、送給管に不活性ガス送給手段を介装し
てなること、送給手段がエアポンプであること、および
原水タンクへ原水を流入させる流入管に介装したエゼク
タであることを含む。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention provides a raw water tank for storing raw water to be deaerated, supplying the raw water in the raw water tank to the top of the raw water tank, and removing the raw water from the bottom of the tower. A deaerator for removing dissolved oxygen in raw water comprising a degassing tower for supplying an active gas and performing gas-liquid contact in the tower, wherein the inert gas discharged from the top of the raw water tank It is equipped with a feed pipe for feeding to the lower side of the inside, and the inert gas discharged from the top of the tower is blown into the raw water in the raw water tank to reduce the dissolved oxygen of the raw water in the raw water tank in advance. Including that the supply pipe is provided with an inert gas supply means, that the supply means is an air pump, and that the supply pipe is an ejector provided in an inflow pipe for flowing raw water into the raw water tank.

【0008】なお、不活性ガス送給手段としては、上述
のエアポンプやエゼクタに限らず、例えばブロアー等を
使用することもできる。
The inert gas supply means is not limited to the above-described air pump and ejector, but may be, for example, a blower or the like.

【0009】本発明においては、使用済みの不活性ガス
を塔頂からパイプで前記の原水タンクに導入し曝気させ
るもので、この不活性ガス中には少量の酸素を含むが前
記の原水タンクの溶存酸素を減少させるのには問題な
い。
In the present invention, the used inert gas is introduced into the raw water tank through a pipe from the top of the tower and aerated, and the inert gas contains a small amount of oxygen. There is no problem in reducing dissolved oxygen.

【0010】以下、本発明を図面を参照して詳細に説明
する。
Hereinafter, the present invention will be described in detail with reference to the drawings.

【0011】図1は本発明の一実施態様を示すもので、
図中11は原水流入管で、この流入管11を通って溶存
酸素を除去すべき原水が原水タンク12に流入する。タ
ンク12内の原水は送水管13を通り脱気塔14の塔頂
15に流入する。16は送水管13に介装された送水ポ
ンプである。脱気塔14は塔内で気液が充分接触する構
造のものであれば、いずれのものでもよく、例えばラシ
ヒリング等の各種充填材を充填した充填塔、段塔等適宜
採用し得る。
FIG. 1 shows an embodiment of the present invention.
In the figure, reference numeral 11 denotes a raw water inflow pipe through which raw water from which dissolved oxygen is to be removed flows into a raw water tank 12. The raw water in the tank 12 flows through the water pipe 13 into the top 15 of the degassing tower 14. Reference numeral 16 denotes a water supply pump interposed in the water supply pipe 13. The degassing tower 14 may be of any structure as long as gas and liquid are sufficiently contacted in the tower. For example, a packed tower filled with various fillers such as Raschig rings, a column tower, or the like can be appropriately used.

【0012】前記塔頂15に送られた原水は、塔内を流
下し、塔底17に至るが、この間に後述する不活性ガス
と気液接触することにより、溶存酸素が原水中から不活
性ガス中に移動し、塔底17に至るまでに溶存酸素は充
分に除去された処理水になる。この処理水は塔底17の
流出管18から流出ポンプ19によって取り出される。
一方、20は不活性ガス供給管で、この供給管を通り、
窒素等の不活性ガスが塔底17に供給され、前記のよう
に塔内を気液接触をしながら塔頂15へ移動する。塔頂
15に至った不活性ガスは原水タンク12内と連通した
送給管21を通り、原水タンク12内の下部側で原水中
に吹き込まれる。22は分散板で、これにより窒素ガス
は原水中に微細な気泡となって吹き込まれ、効率よく原
水中の溶存酸素を除去しながら原水中を上昇し、系外に
放出される。なお、23は液分散機構である。
The raw water sent to the tower top 15 flows down in the tower and reaches the tower bottom 17. During this time, the raw water comes into gas-liquid contact with an inert gas described later, whereby dissolved oxygen is inertized from the raw water. Dissolved oxygen is converted into treated water from which the dissolved oxygen is sufficiently removed before moving into the gas and reaching the bottom 17. This treated water is taken out from an outlet pipe 18 at the bottom 17 by an outlet pump 19.
On the other hand, 20 is an inert gas supply pipe, which passes through this supply pipe,
An inert gas such as nitrogen is supplied to the column bottom 17 and moves to the column top 15 while making gas-liquid contact in the column as described above. The inert gas that has reached the tower top 15 passes through a feed pipe 21 communicating with the inside of the raw water tank 12 and is blown into the raw water at the lower side inside the raw water tank 12. Reference numeral 22 denotes a dispersion plate, whereby nitrogen gas is blown into the raw water as fine bubbles, rises in the raw water while efficiently removing dissolved oxygen in the raw water, and is discharged out of the system. Reference numeral 23 denotes a liquid dispersion mechanism.

【0013】図2は本発明の他の実施態様を示すもので
ある。
FIG. 2 shows another embodiment of the present invention.

【0014】この態様においては、原水流入管11にエ
ゼクタ24が介装されており、また塔頂15に一端を連
結した送給管21の他端は前記エゼクタ24の吸引部に
連結されており、その他の構成は前記実施態様と同じで
あるから、同一部分に同一参照符号を付してその説明を
省略する。
In this embodiment, an ejector 24 is interposed in the raw water inflow pipe 11, and the other end of the feed pipe 21 having one end connected to the top 15 is connected to a suction part of the ejector 24. Since other configurations are the same as those of the above-described embodiment, the same portions are denoted by the same reference numerals and description thereof will be omitted.

【0015】このような構成において、原水が流入管1
1を流れると、エゼクタ24の吸引部が負圧になり、こ
のため脱気塔14内の圧力が減少し、これにより脱気塔
14内における酸素除去効果が高まる。
In such a configuration, the raw water is supplied to the inflow pipe 1.
After flowing through 1, the suction part of the ejector 24 becomes negative pressure, and therefore, the pressure in the degassing tower 14 is reduced, thereby increasing the oxygen removing effect in the degassing tower 14.

【0016】なお、この態様のごとく、不活性ガス送給
手段としてエゼクタを用いる場合は、当該エゼクタ内で
原水と不活性ガスとの気液接触が充分に行われるので、
図2における分散板22を省略してもよい。
When an ejector is used as the inert gas supply means as in this embodiment, gas-liquid contact between the raw water and the inert gas is sufficiently performed in the ejector.
The dispersion plate 22 in FIG. 2 may be omitted.

【0017】図3は本発明の更に他の実施態様を示すも
のである。
FIG. 3 shows still another embodiment of the present invention.

【0018】この態様においては、送給管21にエアポ
ンプ25を介装する以外は、図1に示す実施態様と同様
である。エアポンプ25によって塔頂15の不活性ガス
を原水タンク12に送ることにより、塔内の圧力が減少
し、これにより脱気塔14内における酸素除去効果は高
まる。
This embodiment is the same as the embodiment shown in FIG. 1 except that an air pump 25 is interposed in the feed pipe 21. By sending the inert gas at the tower top 15 to the raw water tank 12 by the air pump 25, the pressure inside the tower is reduced, whereby the oxygen removing effect in the degassing tower 14 is enhanced.

【0019】図4は本発明のまた更に他の実施態様を示
すものである。
FIG. 4 shows still another embodiment of the present invention.

【0020】この態様にあっては、送水ポンプ16の吐
出側とエゼクタ24の原水入口側とが返送管26で連結
され、送水ポンプ16の吐出水の一部がエゼクタ24の
原水入口側へ返送されている。このため、エゼクタ24
を通過する原水量が増加し、エゼクタ24の吸引力を高
め、その結果脱気塔14内の圧力を更に減少させる。こ
れにより、脱気塔14の酸素除去効果を更に高めるもの
である。
In this embodiment, the discharge side of the water supply pump 16 and the raw water inlet side of the ejector 24 are connected by a return pipe 26, and a part of the discharge water of the water supply pump 16 is returned to the raw water inlet side of the ejector 24. Have been. For this reason, the ejector 24
Increases the amount of raw water passing therethrough, increasing the suction force of the ejector 24, and as a result, further reducing the pressure in the degassing tower 14. Thereby, the oxygen removing effect of the degassing tower 14 is further enhanced.

【0021】上記実施態様で示したように、原水タンク
はいくらかの水深があり、窒素ガス等を直接吹き込んだ
のでは水頭分が背圧となって脱気塔にかかるので、ガス
エゼクタを用いて廃窒素ガスを吸引注入するか、エアー
ポンプ等を設置して脱気塔の圧力を大気圧またはそれ以
下にすると処理水の溶存酸素値の低減が更に著しい。
As shown in the above embodiment, the raw water tank has some water depth, and if nitrogen gas or the like is directly blown, the water head becomes back pressure and is applied to the deaeration tower. If the pressure of the degassing tower is reduced to atmospheric pressure or lower by suctioning and injecting nitrogen gas or installing an air pump or the like, the dissolved oxygen value of the treated water is further remarkably reduced.

【0022】[0022]

【実施例】以下、実施例、および比較例により本発明を
具体的に説明する。 (実施例1〜3、比較例1)図1〜3に示す態様(実施
例1〜3)、および図5に示す態様(比較例)を用いて
原水の脱気処理を行った。脱気装置の運転条件を表1に
示した。
The present invention will be specifically described below with reference to examples and comparative examples. (Examples 1 to 3 and Comparative Example 1) Degassing treatment of raw water was performed using the embodiment shown in FIGS. 1 to 3 (Examples 1 to 3) and the embodiment shown in FIG. 5 (Comparative Example). Table 1 shows the operating conditions of the deaerator.

【0023】得られた結果を表2に示した。The results obtained are shown in Table 2.

【0024】[0024]

【表1】 [Table 1]

【0025】[0025]

【表2】 上記実施例より明らかなように残余のN2 ガスを含む廃
ガスを原水タンク内に吹き込むことにより、処理水の溶
存酸素濃度を従来より低減することができ、また、これ
に加えてエゼクタ、エアポンプ等で吸引して塔内圧を下
げた場合には、溶存酸素濃度の低減効果が更に著しい。
[Table 2] As is clear from the above embodiment, by blowing the waste gas containing the residual N 2 gas into the raw water tank, the dissolved oxygen concentration of the treated water can be reduced as compared with the conventional case, and in addition to this, an ejector and an air pump When the internal pressure of the tower is lowered by suction or the like, the effect of reducing the dissolved oxygen concentration is more remarkable.

【0026】[0026]

【発明の効果】本発明によれば、従来と同量の窒素ガス
を使用しても、処理水の溶存酸素濃度の改善効果があ
り、処理水の溶存酸素濃度を一定値に保つならば窒素ガ
ス使用量の削減ができる。
According to the present invention, even if the same amount of nitrogen gas as before is used, there is an effect of improving the dissolved oxygen concentration of the treated water. Gas consumption can be reduced.

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

【図1】本発明の実施態様の一例を示す概略構成図であ
る。
FIG. 1 is a schematic configuration diagram showing an example of an embodiment of the present invention.

【図2】本発明の実施態様の他の例を示す概略構成図で
ある。
FIG. 2 is a schematic configuration diagram showing another example of the embodiment of the present invention.

【図3】本発明の実施態様の更に他の例を示す概略構成
図である。
FIG. 3 is a schematic configuration diagram showing still another example of the embodiment of the present invention.

【図4】本発明の実施態様のまた更に他の例を示す概略
構成図である。
FIG. 4 is a schematic configuration diagram showing still another example of the embodiment of the present invention.

【図5】従来の脱気装置の一例を示す概略構成図であ
る。
FIG. 5 is a schematic configuration diagram showing an example of a conventional deaerator.

【符号の説明】[Explanation of symbols]

11 原水流入管 12 原水タンク 13 送水管 14 脱気塔 15 塔頂 16 送水ポンプ 17 塔底 18 流出管 19 流出ポンプ 20 不活性ガス供給管 21 送給管 22 分散板 23 液分散機構 24 エゼクタ 25 エアポンプ DESCRIPTION OF SYMBOLS 11 Raw water inflow pipe 12 Raw water tank 13 Water pipe 14 Degassing tower 15 Tower top 16 Water pump 17 Tower bottom 18 Outflow pipe 19 Outflow pump 20 Inert gas supply pipe 21 Feed pipe 22 Dispersion plate 23 Liquid dispersion mechanism 24 Ejector 25 Air pump

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 脱気処理をする原水を貯留する原水タン
クと、前記原水タンク中の原水を塔頂に供給すると共に
塔底から不活性ガスを供給して塔内で気液接触を行わせ
る脱気塔とを有してなる原水中の溶存酸素を除去させる
脱気装置において、塔頂から排出される不活性ガスを前
記原水タンク内の下部側に送給する送給管を備え、塔頂
から排出される不活性ガスを原水タンク内の原水中に吹
き込むことにより原水タンク内の原水の溶存酸素を予め
低減させることを特徴とする脱気装置。
1. A raw water tank for storing raw water to be degassed, and raw water in the raw water tank is supplied to the top of the tower and an inert gas is supplied from the bottom of the raw water tank to perform gas-liquid contact in the tower. A deaerator for removing dissolved oxygen in raw water comprising a deaerator and a feed pipe for feeding an inert gas discharged from the top to a lower side in the raw water tank, A degassing device characterized in that dissolved oxygen in raw water in a raw water tank is previously reduced by blowing inert gas discharged from the top into raw water in a raw water tank.
【請求項2】 送給管に不活性ガス送給手段を介装して
なる請求項1記載の脱気装置。
2. The degassing apparatus according to claim 1, wherein an inert gas feeding means is provided in the feeding pipe.
【請求項3】 送給手段がエアポンプである請求項2記
載の脱気装置。
3. The degassing device according to claim 2, wherein the feeding means is an air pump.
【請求項4】 送給手段が原水タンクへ原水を流入させ
る流入管に介装したエゼクタである請求項2記載の脱気
装置。
4. The deaerator according to claim 2, wherein the feeding means is an ejector interposed in an inflow pipe for flowing raw water into the raw water tank.
JP17859592A 1992-07-06 1992-07-06 Degassing device Expired - Fee Related JP2885997B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17859592A JP2885997B2 (en) 1992-07-06 1992-07-06 Degassing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17859592A JP2885997B2 (en) 1992-07-06 1992-07-06 Degassing device

Publications (2)

Publication Number Publication Date
JPH0615107A JPH0615107A (en) 1994-01-25
JP2885997B2 true JP2885997B2 (en) 1999-04-26

Family

ID=16051209

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17859592A Expired - Fee Related JP2885997B2 (en) 1992-07-06 1992-07-06 Degassing device

Country Status (1)

Country Link
JP (1) JP2885997B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5083978B2 (en) * 2008-05-19 2012-11-28 東洋紡エンジニアリング株式会社 Nitrogen deoxygenation equipment

Also Published As

Publication number Publication date
JPH0615107A (en) 1994-01-25

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