JPH0824548A - Air purifier - Google Patents

Air purifier

Info

Publication number
JPH0824548A
JPH0824548A JP16258994A JP16258994A JPH0824548A JP H0824548 A JPH0824548 A JP H0824548A JP 16258994 A JP16258994 A JP 16258994A JP 16258994 A JP16258994 A JP 16258994A JP H0824548 A JPH0824548 A JP H0824548A
Authority
JP
Japan
Prior art keywords
air
water
heat exchanger
duct
gas diffuser
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
JP16258994A
Other languages
Japanese (ja)
Inventor
Hisanori Yato
久典 矢藤
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electronics Corp
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 Matsushita Electronics Corp filed Critical Matsushita Electronics Corp
Priority to JP16258994A priority Critical patent/JPH0824548A/en
Publication of JPH0824548A publication Critical patent/JPH0824548A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide an air purifier enabling to efficiently remove various contamination substances without using chemicals. CONSTITUTION:This device is provided with a contamination substance collection room 1 for discharging contaminated air fed into a gas diffuser 7 through a suction duct 9 into water through fine vent holes 13 of the gas diffuser 7, a water condensation room 3 provided with a heat exchanger 16, an air duct 5 for recovering air of which a contamination component is removed in the water in the inside of the contamination substance collection room 1 and introducing it into the water condensation room 3, and a water discharge pipe 6 for circulating waste water from the contamination substance collection room 1, and the water discharge pipe 6 is heat-exchangeably connected to a heat exchanger 16 and the purified air is taken out by an exhaust duct 17 through the heat exchanger 16.

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、半導体素子等の精密機
器の製造現場や、医療現場などのクリーンルーム内で各
種薬品から発生した腐食性の有害ガスを浄化したり、ク
リーンルームに供給される空気中に浮遊する窒素酸化
物、亜硫酸ガス等の汚染物質を除去するのに適した空気
浄化装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention purifies corrosive harmful gas generated from various chemicals in a clean room such as a manufacturing site of precision equipment such as semiconductor devices or a medical field, and supplies air to the clean room. The present invention relates to an air purification device suitable for removing contaminants such as nitrogen oxides and sulfurous acid gas suspended therein.

【0002】[0002]

【従来の技術】空気浄化装置には種々の形式のものがあ
るが、その多くは、化学反応、化学中和反応、触媒作用
または物理的吸着作用を利用して空気中の汚染物質をと
り除くものである。
2. Description of the Related Art There are various types of air purifiers, most of which remove pollutants from the air by utilizing chemical reaction, chemical neutralization reaction, catalytic action or physical adsorption action. Is.

【0003】[0003]

【発明が解決しようとする課題】このため、薬剤やケミ
カルフィルタなどを不可欠とするのみならず、これらを
定期的に交換しなければならないので、多額の維持費を
必要とした。また、除去できる汚染物質の種類や量が限
定されるという課題もあった。
For this reason, not only chemicals and chemical filters are indispensable, but also these must be replaced regularly, so a large amount of maintenance cost is required. There is also a problem that the types and amounts of contaminants that can be removed are limited.

【0004】したがって本発明の目的は、薬剤を使用す
ることなく多種の汚染物質を効率よく除去できる空気浄
化装置を提供することにある。
Therefore, it is an object of the present invention to provide an air purifying device which can efficiently remove various pollutants without using chemicals.

【0005】[0005]

【課題を解決するための手段】本発明によると、上述し
た目的を達成するために、吸気ダクトを通じてガス拡散
器に送り込まれた汚染空気をガス拡散器の微細な通気孔
を通じて水中に放出させる汚染物質捕集室と、熱交換器
を設けた水分凝集室と、汚染物質捕集室内の水中で汚染
成分を除去された空気を回収して水分凝集室に導くエア
ダクトと、汚染物質捕集室の排水を流通させる排水パイ
プと、浄化された空気をとり出す排気ダクトとを備え、
前記排水パイプは前記熱交換器に熱的に結合され、前記
熱交換器を通過した空気が前記排気ダクトに導かれるこ
とを特徴とする空気浄化装置が提供される。
According to the present invention, in order to achieve the above-mentioned object, polluted air fed into a gas diffuser through an intake duct is discharged into water through fine ventilation holes of the gas diffuser. The substance collection chamber, the moisture coagulation chamber provided with a heat exchanger, the air duct for collecting the air from which pollutant components have been removed in the water in the pollutant collection chamber and guiding it to the moisture coagulation chamber, and the pollutant collection chamber Equipped with a drainage pipe for circulating wastewater and an exhaust duct for taking out purified air,
An air purification apparatus is provided, wherein the drainage pipe is thermally coupled to the heat exchanger, and the air passing through the heat exchanger is guided to the exhaust duct.

【0006】[0006]

【作用】本発明においては、汚染空気がガス拡散器の微
細な通気孔を通じて水中に放出されるので、ここで汚染
物質が水に吸収されて払拭される。そして、汚染物質捕
集室から回収された一次浄化空気は、熱交換器を設けた
水分凝集室で二次浄化作用を受ける。とくに一次浄化空
気は高い湿度を有しているが、熱交換器を通過すること
によって低湿度空気となる。しかも、熱交換器は汚染物
質捕集室の排水を利用して冷却されるので、使用する水
を2途に有効利用できる。
In the present invention, the polluted air is discharged into the water through the fine vent holes of the gas diffuser, so that the pollutant is absorbed into the water and wiped off. Then, the primary purified air recovered from the pollutant collection chamber is subjected to the secondary purification action in the moisture aggregation chamber provided with the heat exchanger. Particularly, the primary purified air has a high humidity, but becomes low humidity air by passing through the heat exchanger. Moreover, since the heat exchanger is cooled by using the drainage of the pollutant trap chamber, the water used can be effectively used in two ways.

【0007】[0007]

【実施例】つぎに、本発明の一実施例を、図面を参照し
ながら説明する。
Next, an embodiment of the present invention will be described with reference to the drawings.

【0008】図1に示す空気浄化装置は、汚染物質捕集
室1を設定する第1タンク2と、熱交換型水分凝集室3
を設定する第2タンク4とを備え、第2タンク4はエア
ダクト5および排水パイプ6を介して第1タンク2に連
通している。
The air purification apparatus shown in FIG. 1 includes a first tank 2 for setting a pollutant trap chamber 1 and a heat exchange type water aggregating chamber 3.
And a second tank 4 for setting the above. The second tank 4 communicates with the first tank 2 via an air duct 5 and a drain pipe 6.

【0009】第1タンク2内には、ガス拡散器7および
超純水8が収容されており、ガス拡散器7は吸気ダクト
9に連通している。10は攪拌機、11は給水用パイプ
を示す。ガス拡散器7は図2に示すように、複数に分岐
したパイプ部分12を有し、各パイプ部分12に多数の
微細な通気孔13が散設されている。そして、ガス拡散
器7はそのパイプ部分12が超純水8に没するように、
第1タンク2内に設けられている。また、水質監視モニ
タとしての導電率計14が排水パイプ6に接続されてお
り、給水用パイプ11に接続された電磁開閉弁15が、
導電率計14の出力信号に基づき開閉制御を受けるよう
になっている。
A gas diffuser 7 and ultrapure water 8 are contained in the first tank 2, and the gas diffuser 7 communicates with an intake duct 9. 10 is an agitator and 11 is a water supply pipe. As shown in FIG. 2, the gas diffuser 7 has a plurality of branched pipe portions 12, and a large number of fine ventilation holes 13 are scattered in each pipe portion 12. Then, the gas diffuser 7 has its pipe portion 12 immersed in the ultrapure water 8,
It is provided in the first tank 2. Further, a conductivity meter 14 as a water quality monitor is connected to the drainage pipe 6, and an electromagnetic opening / closing valve 15 connected to the water supply pipe 11 is
Opening / closing control is performed based on the output signal of the conductivity meter 14.

【0010】一方、第2タンク4内には、熱交換器16
が設けられており、熱交換器16に排水パイプ6が熱的
に結合されている。17は浄化空気排出用の排気ダク
ト、18,19は排水管を示す。
On the other hand, in the second tank 4, the heat exchanger 16
Is provided, and the drainage pipe 6 is thermally coupled to the heat exchanger 16. Reference numeral 17 denotes an exhaust duct for discharging purified air, and 18 and 19 denote drain pipes.

【0011】吸気ダクト9はクリーンルーム内に連通し
ており、クリーンルーム内の汚れた空気が吸気ダクト9
を通じてガス拡散器7に所定圧力で送り込まれてくる。
この汚染空気は、ガス拡散器7のパイプ部分12の通気
孔13を通じて超純水8中に多数の細かい泡となって放
出される。このようにして汚染空気に広い面積で接触し
た超純水8は、汚染空気中の塩酸、硫酸、硝酸、フッ酸
等の酸性ガスまたはアンモニア等の汚染物質を吸収して
捕集する。
The intake duct 9 communicates with the inside of the clean room, and the dirty air in the clean room is taken in by the intake duct 9.
Through the gas diffuser 7 at a predetermined pressure.
The polluted air is discharged into the ultrapure water 8 as a large number of fine bubbles through the ventilation hole 13 of the pipe portion 12 of the gas diffuser 7. In this way, the ultrapure water 8 that has come into contact with the contaminated air over a wide area absorbs and collects acidic gases such as hydrochloric acid, sulfuric acid, nitric acid, and hydrofluoric acid in the contaminated air or contaminants such as ammonia.

【0012】上述のようにして第1タンク2内で一次浄
化された高湿度の空気は、エアダクト5を通じて第2タ
ンク4内に入り、第2タンク4内の熱交換器16を通過
することによって水分を凝集させる。すなわち、熱交換
器16は排水パイプ6に熱的に結合されており、排水パ
イプ6には第1タンク2からの排水が流通するので、一
次浄化された空気は熱交換器16で冷却され、水分を凝
集させる。このため、汚染物質捕集室1で完全に除去さ
れずに一次浄化空気中に残留した汚染物質が、熱交換型
凝集室3内で凝集水に混入したかたちで捕集され、この
凝集水は排水管19を通じて第2タンク4外に排出され
る。
The high-humidity air primarily purified in the first tank 2 as described above enters the second tank 4 through the air duct 5 and passes through the heat exchanger 16 in the second tank 4. Allow water to agglomerate. That is, since the heat exchanger 16 is thermally coupled to the drainage pipe 6, and the drainage from the first tank 2 flows through the drainage pipe 6, the primary purified air is cooled by the heat exchanger 16. Allow water to agglomerate. For this reason, the pollutants which are not completely removed in the pollutant trap chamber 1 but remain in the primary purified air are trapped in the heat exchange type coagulation chamber 3 in the form of being mixed with the coagulated water. It is discharged to the outside of the second tank 4 through the drainage pipe 19.

【0013】そして、熱交換器16を通過して二次浄化
された低湿度の空気は、排気ダクト17を通じてクリー
ンルーム内に供給される。また、熱交換器16の冷却に
使用された水は、排水管18を通じて排出される。
The low-humidity air that has passed through the heat exchanger 16 and is secondarily purified is supplied into the clean room through the exhaust duct 17. The water used for cooling the heat exchanger 16 is discharged through the drain pipe 18.

【0014】汚染物質捕集室1の排水の汚れは導電率計
14で検出され、導電率計14の指示値が所定範囲を越
えたときに限り、電磁開閉弁15が開かれて第1タンク
2内の超純水8が補充される。このため、第1タンク2
内の超純水8は常に高い純度に維持される。なお、上述
した実施例での超純水8は、半導体素子等の精密機器の
製造現場で多用されている高純度の水であるが、これに
適当な薬剤を混入させることを妨げない。
Contamination of the waste water in the pollutant collection chamber 1 is detected by the conductivity meter 14, and the electromagnetic opening / closing valve 15 is opened to open the first tank only when the value indicated by the conductivity meter 14 exceeds a predetermined range. The ultrapure water 8 in 2 is replenished. Therefore, the first tank 2
The ultrapure water 8 therein is always maintained at a high purity. Although the ultrapure water 8 in the above-described embodiment is high-purity water that is frequently used in the manufacturing site of precision equipment such as semiconductor devices, it does not prevent mixing of a suitable chemical agent.

【0015】[0015]

【発明の効果】以上のように本発明によると、汚染空気
を水中に拡散させて汚染空気中に含まれている塩酸、硫
酸、硝酸またはフッ酸等の酸性ガスや、アンモニア等の
汚染物質を、純水を吸着材として除去することができ
る。また、汚染物質捕集室から回収した一次浄化空気を
熱交換型水分凝集室で二次浄化するので、一次浄化では
除去しきれなかった汚染物質を排除でき、しかも、熱交
換器を通じて浄化空気をとり出すので、湿度の低い浄化
空気を効率よくかつ安価にクリーンルーム内に供給する
ことができる。
As described above, according to the present invention, the polluted air is diffused into water and the acidic gas such as hydrochloric acid, sulfuric acid, nitric acid or hydrofluoric acid contained in the polluted air, and pollutants such as ammonia are removed. Pure water can be removed as an adsorbent. In addition, since the primary purified air collected from the pollutant collection chamber is secondarily purified in the heat exchange type moisture coagulation chamber, it is possible to remove pollutants that could not be completely removed by the primary purification, and the purified air is passed through the heat exchanger. Since it is taken out, purified air with low humidity can be efficiently and inexpensively supplied into the clean room.

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

【図1】本発明の一実施例の空気浄化装置の全体構成を
示す側面図
FIG. 1 is a side view showing the overall configuration of an air purification device according to an embodiment of the present invention.

【図2】本発明の一実施例における汚染物質捕集室の斜
視図
FIG. 2 is a perspective view of a pollutant trap chamber according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 汚染物質捕集室 3 熱交換型水分凝集室 5 エアダクト 6 排水パイプ 7 ガス拡散器 8 超純水 9 吸気ダクト 13 通気孔 16 熱交換器 17 排気ダクト 1 Pollutant Collection Chamber 3 Heat Exchange Moisture Coagulation Chamber 5 Air Duct 6 Drain Pipe 7 Gas Diffuser 8 Ultra Pure Water 9 Intake Duct 13 Vent Hole 16 Heat Exchanger 17 Exhaust Duct

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 吸気ダクトを通じてガス拡散器に送り込
まれた汚染空気をガス拡散器の微細な通気孔を通じて水
中に放出させる汚染物質捕集室と、熱交換器を設けた水
分凝集室と、汚染物質捕集室内の水中で汚染物質を除去
された空気を回収して水分凝集室に導くエアダクトと、
汚染物質捕集室の排水を流通させる排水パイプと、浄化
された空気をとり出す排気ダクトとを備え、前記排水パ
イプは前記熱交換器に熱的に結合され、前記熱交換器を
通過した空気が前記排気ダクトに導かれることを特徴と
する空気浄化装置。
1. A pollutant collection chamber for discharging polluted air sent into a gas diffuser through an intake duct into water through fine ventilation holes of the gas diffuser, a water condensation chamber provided with a heat exchanger, and pollution. An air duct that collects air from which pollutants have been removed in the water in the substance collection chamber and guides it to the moisture aggregation chamber,
A drain pipe for circulating the waste water of the pollutant trap chamber, and an exhaust duct for taking out purified air, the drain pipe being thermally coupled to the heat exchanger, the air passing through the heat exchanger. Is introduced into the exhaust duct.
JP16258994A 1994-07-15 1994-07-15 Air purifier Pending JPH0824548A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16258994A JPH0824548A (en) 1994-07-15 1994-07-15 Air purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16258994A JPH0824548A (en) 1994-07-15 1994-07-15 Air purifier

Publications (1)

Publication Number Publication Date
JPH0824548A true JPH0824548A (en) 1996-01-30

Family

ID=15757468

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16258994A Pending JPH0824548A (en) 1994-07-15 1994-07-15 Air purifier

Country Status (1)

Country Link
JP (1) JPH0824548A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103776121A (en) * 2014-02-28 2014-05-07 常州大学 Pressure humidifying device for laboratory pipe system
CN104740953A (en) * 2015-03-03 2015-07-01 苏州华策纺织科技有限公司 Waste-gas treating device of tentering and setting machine
CN106765382A (en) * 2016-12-06 2017-05-31 江门市永成厨具设备有限公司 A kind of combined type fries stove

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103776121A (en) * 2014-02-28 2014-05-07 常州大学 Pressure humidifying device for laboratory pipe system
CN103776121B (en) * 2014-02-28 2016-11-02 常州大学 A kind of damping device with pressure for laboratory tubing
CN104740953A (en) * 2015-03-03 2015-07-01 苏州华策纺织科技有限公司 Waste-gas treating device of tentering and setting machine
CN106765382A (en) * 2016-12-06 2017-05-31 江门市永成厨具设备有限公司 A kind of combined type fries stove

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