JP2003210932A - Equipment for dust collection deodorization - Google Patents
Equipment for dust collection deodorizationInfo
- Publication number
- JP2003210932A JP2003210932A JP2002015396A JP2002015396A JP2003210932A JP 2003210932 A JP2003210932 A JP 2003210932A JP 2002015396 A JP2002015396 A JP 2002015396A JP 2002015396 A JP2002015396 A JP 2002015396A JP 2003210932 A JP2003210932 A JP 2003210932A
- Authority
- JP
- Japan
- Prior art keywords
- dust collecting
- perforated plate
- gas supply
- supply path
- polluted gas
- 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.)
- Granted
Links
Landscapes
- Treating Waste Gases (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、汚染された気体を
浄化するための装置に関し、特に粉塵,煤煙,臭気など
の汚染物質を含んだ気体について集塵脱臭を行うための
装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for purifying contaminated gas, and more particularly to a device for collecting and deodorizing gas containing pollutants such as dust, soot and odor.
【0002】[0002]
【従来の技術】従来の集塵脱臭装置としては図5に示す
ようなものがあり、その装置本体100は圧縮機102により
加圧された煤煙を含む気体を煙管104により放出管106へ
導いて、同放出管106から水槽108内へ放出するようにな
っていて、放出管106の頂部には多数の小孔106aが均一
に形成されている。そして、水槽108内に設置した超音
波振動子110から発振される超音波により上記煤煙を含
む気体を処理して、同煤煙を水槽108内の吸収水により
吸収除去することが行われている。2. Description of the Related Art As a conventional dust collecting and deodorizing device, there is one as shown in FIG. 5, and its device main body 100 guides a gas containing soot smoke pressurized by a compressor 102 to a discharge pipe 106 by a smoke pipe 104. The discharge pipe 106 is discharged into the water tank 108, and a large number of small holes 106a are uniformly formed at the top of the discharge pipe 106. Then, the gas containing the soot and smoke is processed by the ultrasonic waves oscillated from the ultrasonic transducer 110 installed in the water tank 108, and the soot and smoke is absorbed and removed by the absorbed water in the water tank 108.
【0003】しかしながら、上述のような従来の装置で
は放出管106の上面に多数の均一な小孔106aが形成され
ているので、放出管106の煙管104に近い側では気泡が多
数形成されるが、煙管104から離隔した側では気泡が僅
かしか形成されず、全体として圧力損失が大きくなり、
超音波エネルギーが有効に利用されないという不具合が
ある。また、多数の小孔106aを有する放出管106の製作
のためのコストの増大を招くという不具合もある。However, in the conventional device as described above, since many uniform small holes 106a are formed on the upper surface of the discharge pipe 106, many bubbles are formed on the side of the discharge pipe 106 near the smoke pipe 104. On the side separated from the smoke tube 104, only a few bubbles are formed, resulting in a large pressure loss as a whole,
There is a problem that ultrasonic energy is not effectively used. In addition, there is a problem that the cost for manufacturing the discharge pipe 106 having a large number of small holes 106a increases.
【0004】[0004]
【発明が解決しようとする課題】そこで本発明は、汚染
気体を通す多孔板の小孔群の配置を適切に且つ安価に行
えるようにするとともに、同小孔群に対する超音波発生
器の配置も適切に行えるようにして、効率のよい集塵脱
臭作用を低コストで実現できるようにした装置を提供す
ることを課題とする。Therefore, the present invention makes it possible to appropriately and inexpensively arrange the small hole group of the perforated plate through which the contaminated gas passes, and also to arrange the ultrasonic generator for the small hole group. An object of the present invention is to provide an apparatus that can be appropriately performed and can realize an efficient dust collecting and deodorizing action at low cost.
【0005】[0005]
【課題を解決するための手段】前述の課題を解決するた
め、本発明の集塵脱臭装置は、塵埃,煤煙,臭気などの
汚染物質を含んだ汚染気体について集塵脱臭処理を行う
べく処理用液体を収容したタンク本体が、同タンク本体
の頂壁から垂下された隔壁により汚染気体供給経路と汚
染気体処理部とに分割されて、上記汚染気体供給経路の
上部に汚染気体供給口が設けられるとともに、上記汚染
気体処理部の上部に処理済み気体回収口が設けられ、上
記隔壁の下端縁と上記タンク本体の底面との間に上記の
汚染気体供給経路と汚染気体処理部との連通路が形成さ
れて、上記汚染気体処理部に上記隔壁の下端縁から上記
タンク本体の側壁へ到る多孔板が設けられるとともに、
同多孔板の下方から同多孔板へ向けて超音波を放射する
超音波発生器が設けられ、上記多孔板における孔径が、
上記汚染気体供給経路から遠ざかるにつれて増大するよ
うに設定されていることを特徴としている。In order to solve the above-mentioned problems, the dust collecting and deodorizing apparatus of the present invention is designed to perform a dust collecting and deodorizing process on a pollutant gas containing pollutants such as dust, soot and odor. The tank body containing the liquid is divided into a polluted gas supply path and a polluted gas treatment section by a partition wall hanging from the top wall of the tank body, and a polluted gas supply port is provided above the polluted gas supply path. Along with the above, a treated gas recovery port is provided in the upper portion of the contaminated gas treatment section, and a communication path between the contaminated gas supply path and the contaminated gas treatment section is provided between the lower edge of the partition wall and the bottom surface of the tank body. Formed, the contaminated gas treatment unit is provided with a perforated plate extending from the lower end edge of the partition wall to the side wall of the tank body,
An ultrasonic wave generator that emits ultrasonic waves from the lower side of the perforated plate to the perforated plate is provided, and the hole diameter in the perforated plate is
It is characterized in that it is set so as to increase as the distance from the contaminated gas supply path increases.
【0006】また本発明の集塵脱臭装置は、上記多孔板
が、上記汚染気体供給経路から遠ざかるにつれて漸次上
方へ向かい傾斜するように配置されていることを特徴と
している。Further, the dust collecting deodorizing apparatus of the present invention is characterized in that the perforated plate is arranged so as to gradually incline upward as it goes away from the polluted gas supply path.
【0007】さらに本発明の集塵脱臭装置は、上記多孔
板の傾斜角度が3〜7度の範囲に設定されていることを
特徴としている。Further, the dust collecting and deodorizing apparatus of the present invention is characterized in that the angle of inclination of the perforated plate is set in the range of 3 to 7 degrees.
【0008】上述の本発明の集塵脱臭装置では、塵埃,
煤煙,臭気などの汚染物質を含んだ汚染気体を上記汚染
気体供給口から圧入するか、または上記処理済み気体回
収口から吸引することにより、同汚染気体は、上記多孔
板を通過しながら上記超音波発生器からの超音波により
集塵脱臭作用を受けるが、その際、上記多孔板における
多数の小孔の孔径が、上記汚染気体供給経路から遠ざか
るにつれて増大するように設定されているので、同多孔
板における上記汚染気体の通過が一様に行われて、上記
超音波による塵埃などの液中への捕捉および臭気物質の
分解も効率よく一様に行われるようになる。In the above dust collecting and deodorizing apparatus of the present invention, dust,
By polluting the pollutant gas containing pollutants such as soot and odor from the pollutant gas supply port or by sucking it from the treated gas recovery port, the pollutant gas passes through the perforated plate and becomes superabundant. The ultrasonic waves from the sound wave generator are subjected to dust collecting and deodorizing action, but at that time, the hole diameters of the large number of small holes in the perforated plate are set so as to increase as the distance from the contaminated gas supply path increases. The contaminated gas is uniformly passed through the perforated plate, and the ultrasonic waves are efficiently and uniformly trapped in the liquid such as dust and decomposed the odorous substance.
【0009】また、上記多孔板が上記気体供給経路から
遠ざかるにつれて漸次上方へ向かい傾斜するように配置
されることにより、上記多孔板における小孔の孔径の分
布と相まって、同多孔板を通過する気体の流れが一様に
なり、これにより集塵脱臭作用が効率よく適切に行われ
るようになる。Further, since the perforated plate is arranged so as to gradually incline upward as it goes away from the gas supply path, the gas passing through the perforated plate is coupled with the distribution of the hole diameters of the small holes in the perforated plate. Becomes uniform, which enables the deodorizing action of dust collection to be efficiently and properly performed.
【0010】そして、実験の結果に基づき上記多孔板の
傾斜角度が3〜7度の範囲に設定されると、上記集塵脱
臭作用が一層効率よく行われる。When the inclination angle of the perforated plate is set within the range of 3 to 7 degrees based on the result of the experiment, the dust collecting and deodorizing action is performed more efficiently.
【0011】さらに本発明の集塵脱臭装置は、上記多孔
板が、上記汚染気体供給経路から遠ざかるにつれて孔径
を段階的に大きくするように、複数段階に孔径を設定さ
れていることを特徴としている。Further, the dust collecting and deodorizing apparatus of the present invention is characterized in that the perforated plate has a plurality of stepped hole diameters so that the hole diameters gradually increase as the distance from the contaminated gas supply path increases. .
【0012】また本発明の集塵脱臭装置は、上記多孔板
が、上記汚染気体供給経路から遠ざかるにつれて孔径を
大きくするように3段階に孔径を設定されて、その孔径
の割合が上記気体供給経路に近いものから順に1:2:
4となるように設定されていることを特徴としている。Further, in the dust collecting and deodorizing apparatus of the present invention, the perforated plate is set in three stages of hole diameters such that the hole diameter increases as the distance from the polluted gas supply route increases, and the ratio of the hole diameters is the gas supply route. 1: 2:
The feature is that it is set to 4.
【0013】さらに本発明の集塵脱臭装置は、上記多孔
板の孔の総面積が、同多孔板の平面の総面積の5〜15
%となるように設定されていることを特徴としている。Further, in the dust collecting and deodorizing apparatus of the present invention, the total area of the holes of the perforated plate is 5 to 15 of the total area of the plane of the perforated plate.
It is characterized by being set to be%.
【0014】上述のように、上記多孔板が、上記汚染気
体供給経路から遠ざかるにつれて孔径を段階的に大きく
するように、複数段階に孔径を設定されていると、その
製作時には各段階ごとに同じ孔径で孔明け作業が行える
ので、装置全体としての性能を極力維持しながら、その
製造コストを節減できるようになる。As described above, when the perforated plate has a plurality of stepped hole diameters so that the hole diameter increases stepwise as it moves away from the contaminated gas supply path, the same for each step at the time of manufacture. Since the boring operation can be performed with the hole diameter, the manufacturing cost can be reduced while maintaining the performance of the entire apparatus as much as possible.
【0015】そして、上記孔径の大きさの段階が3段階
とされて、その孔径の割合が上記気体供給経路に近いも
のから順に1:2:4となるように設定されていると、
その製造コストの低減および装置全体としての性能の維
持が適切に行われるようになる。If the size of the hole diameter is set to three, and the ratio of the hole diameter is set to 1: 2: 4 in order from the one closer to the gas supply path,
The manufacturing cost can be reduced and the performance of the entire device can be maintained appropriately.
【0016】さらに、上記多孔板における孔の総面積
が、同多孔板の平面の総面積の5〜15%となるように
設定されていると、上記の各孔を汚染気体が通過しなが
ら上記超音波発生器からの超音波により受ける塵埃の分
離捕捉や臭気物質の分解処理が的確に行われるようにな
る。Further, when the total area of the holes in the perforated plate is set to be 5 to 15% of the total area of the plane of the perforated plate, the polluted gas passes through each of the above holes while the contaminated gas passes through the holes. The separation and capture of dust received by the ultrasonic waves from the ultrasonic generator and the decomposition processing of odorous substances can be performed accurately.
【0017】また本発明の集塵脱臭装置は、上記汚染気
体供給経路に汚染気体を圧送して供給する手段が接続さ
れたり、上記汚染気体処理部の上部における上記処理済
み気体回収口に気体吸引手段が接続されたりすることに
よって、装置全体としての作動が的確に行われる。Further, in the dust collecting and deodorizing apparatus of the present invention, means for feeding the polluted gas by pressure feed to the polluted gas supply path is connected, or gas is sucked into the treated gas recovery port in the upper part of the polluted gas treatment section. The operation of the entire apparatus is properly performed by connecting the means.
【0018】そして、上記超音波発生器が、その超音波
の周波数を19.5〜29kHzに設定されることによ
り、上記多孔板における孔径の大きさおよび配置の状態
と相まって、汚染気体についての集塵脱臭作用が適切に
行われる。By setting the ultrasonic wave frequency of the ultrasonic wave generator to 19.5 to 29 kHz, the size and arrangement of the hole diameter in the perforated plate, together with the state of the polluted gas, are collected. The dust deodorizing action is properly performed.
【0019】さらに、上記汚染気体供給経路に、オゾン
ガスまたはオゾン水を供給するオゾン供給手段が接続さ
れたり、同オゾン供給手段として上記汚染気体供給経路
内に垂下されたオゾン供給管の下端開口の位置を、上記
タンク本体における上記隔壁の下端縁と同タンク本体の
底面との中間のレベルに設定されたりすることにより、
処理液体中への上記のオゾンガスまたはオゾン水の供給
が適切に行われて、汚染気体についてのオゾンによる殺
菌作用が的確に行われるようになる。Further, an ozone supply means for supplying ozone gas or ozone water is connected to the polluted gas supply path, or a position of a lower end opening of an ozone supply pipe hung in the polluted gas supply path as the ozone supply means. By setting it at an intermediate level between the bottom edge of the partition wall of the tank body and the bottom surface of the tank body,
The ozone gas or ozone water is appropriately supplied to the treatment liquid, and the sterilizing action of ozone on the polluted gas is properly performed.
【0020】さらに、上記汚染気体供給経路内へ油を気
化させて供給する手段が設けられると、この油の気化し
たガスが、汚染気体中の塵埃や煤煙を捕捉して効率よく
処理液体中へ分離するようになる。Further, when a means for vaporizing and supplying the oil into the polluted gas supply path is provided, the vaporized gas of the oil captures dust and soot in the polluted gas and efficiently transfers it into the treated liquid. It comes to separate.
【0021】[0021]
【発明の実施の形態】以下、図面により本発明の実施形
態について説明すると、図1は本発明の第1実施形態と
しての集塵脱臭装置の縦断面図、図2は図1の装置にお
ける多孔板の平面図であり、図3は本発明の第2実施形
態としての集塵脱臭装置の縦断面図、図4は本発明の第
3実施形態としての集塵脱臭装置の縦断面図である。BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a vertical cross-sectional view of a dust collecting and deodorizing apparatus as a first embodiment of the present invention, and FIG. It is a top view of a board, Drawing 3 is a longitudinal section of a dust collecting deodorizing device as a 2nd embodiment of the present invention, and Drawing 4 is a longitudinal sectional view of a dust collecting deodorizing device as a 3rd embodiment of the present invention. .
【0022】まず本発明の第1実施形態としての集塵脱
臭装置について説明すると、図1に示すように、塵埃,
煤煙,臭気などの汚染物質を含んだ汚染気体について集
塵脱臭処理を行えるように、清水または石鹸水などの処
理用液体Bを収容したタンク本体10が、同タンク本体10
の頂壁から垂下された隔壁10aにより汚染気体処理部12
と汚染気体供給経路16とに分割されており、汚染気体供
給経路16の上部には汚染気体Aの供給口16aが設けら
れ、汚染気体処理部12の上部には処理済み気体回収口22
が設けられている。そして、隔壁10aの下端縁10bとタ
ンク本体10の底面10cとの間には汚染気体供給経路16と
汚染気体処理部12との連通路10dが形成されている。First, a dust collecting and deodorizing apparatus as a first embodiment of the present invention will be described. As shown in FIG.
The tank body 10 containing the processing liquid B such as fresh water or soap water is the same as the tank body 10 so that the dust collecting and deodorizing process can be performed on the polluted gas containing pollutants such as soot and odor.
By the partition wall 10a hanging from the top wall of the
And a contaminated gas supply path 16 are provided, a contaminated gas A supply port 16a is provided above the contaminated gas supply path 16, and a treated gas recovery port 22 is provided above the contaminated gas processing unit 12.
Is provided. A communication path 10d between the polluted gas supply path 16 and the polluted gas processing unit 12 is formed between the bottom edge 10b of the partition wall 10a and the bottom surface 10c of the tank body 10.
【0023】また、汚染気体処理部12には、隔壁10aの
下端縁10bからタンク本体10の側壁へ到る多孔板18が設
けられるとともに、同多孔板18の下方から同多孔板18へ
向けて超音波を放射する超音波発生器20が設けられ、同
超音波発生器20は底壁開口14に嵌合固定されている。Further, the polluted gas treatment section 12 is provided with a perforated plate 18 extending from the lower end edge 10b of the partition wall 10a to the side wall of the tank body 10, and from below the perforated plate 18 toward the perforated plate 18. An ultrasonic wave generator 20 that emits ultrasonic waves is provided, and the ultrasonic wave generator 20 is fitted and fixed to the bottom wall opening 14.
【0024】多孔板18における多数の小孔26の各孔径
は、汚染気体供給経路16から遠ざかるにつれて増大する
ように形成されているが、本実施形態では特に3段階に
わたって段階的に孔径を大きくするように、各段階の小
孔26a,26b,26cの孔径が設定されており、汚染気体
供給経路16に近いものから順に孔径の割合が1:2:4
となるように、3種類の孔径2mmφ,4mmφ,8m
mφが用いられている。The hole diameters of the large number of small holes 26 in the perforated plate 18 are formed so as to increase as the distance from the polluted gas supply passage 16 increases, but in the present embodiment, the hole diameter is increased stepwise particularly in three steps. As described above, the hole diameters of the small holes 26a, 26b, and 26c at each stage are set, and the hole diameter ratio is 1: 2: 4 in order from the one closer to the polluted gas supply path 16.
3 types of hole diameter 2mmφ, 4mmφ, 8m
mφ is used.
【0025】そして、多孔板18における孔26a,26b,
26cの総面積は、同多孔板18の平面の総面積の5〜15
%となるように設定されている。The holes 26a, 26b in the perforated plate 18 are
The total area of 26c is 5 to 15 of the total area of the plane of the perforated plate 18.
It is set to be%.
【0026】さらに、多孔板18は、汚染気体供給経路16
から遠ざかるにつれて漸次上方へ向かい傾斜するように
配置されていて、その水平面25となす傾斜角度αは3〜
7度の範囲に設定されている。Further, the perforated plate 18 is provided with a polluted gas supply path 16
It is arranged so as to gradually incline upward with increasing distance from, and the inclination angle α with the horizontal plane 25 is 3 to.
It is set in the range of 7 degrees.
【0027】本装置のタンク本体10において、その汚染
気体供給経路16の上部の汚染気体供給口16aに、汚染気
体Aを圧入するための図示しないブロワーのごとき気体
圧入手段が接続されるか、あるいは処理済み気体回収口
22に、気体吸引手段としてのブロワー24が接続される
が、上記の気体圧入手段および気体吸引手段を共に備え
るようにしてもよい。In the tank body 10 of the present apparatus, a gas press-in means such as a blower (not shown) for pressurizing the pollutant gas A is connected to the pollutant gas supply port 16a in the upper part of the polluted gas supply path 16, or Treated gas recovery port
Although a blower 24 as a gas suction means is connected to 22, a gas suction means and a gas suction means described above may be provided together.
【0028】汚染気体処理部12には処理用液体Bの液面
34のレベルを計測する液面検出センサー11が設けられて
おり、同センサー11からの検出信号に基づき、液面が所
要のレベルに保たれるように制御器13からの制御信号に
よってブロワー24の制御が行われたり、タンク15からの
処理用液体の補充が行われたりするようになっている。The contaminated gas processing section 12 has a liquid level of the processing liquid B.
A liquid level detection sensor 11 for measuring the level of 34 is provided, and based on the detection signal from the sensor 11, the blower 24 of the blower 24 is controlled by a control signal from the controller 13 so that the liquid level is maintained at a required level. The control is performed and the processing liquid is replenished from the tank 15.
【0029】また、超音波発生器20から放出される超音
波の周波数は19.5〜29kHzに設定されている。The frequency of the ultrasonic waves emitted from the ultrasonic generator 20 is set to 19.5 to 29 kHz.
【0030】上述の第1実施形態の集塵脱臭装置では、
塵埃,煤煙,臭気などの汚染物質を含んだ汚染気体Aを
汚染気体供給口16aから図示しないブロワーで圧入する
か、または処理済み気体回収口22からブロワー24により
吸引することによって、同汚染気体Aは、多孔板18を通
過しながら超音波発生器20からの超音波により集塵脱臭
作用を受けるが、その際、多孔板18における多数の小孔
26が、3段階の孔径をもつ小孔26a,26b,26cとし
て、汚染気体供給経路16から遠ざかるにつれて孔径を増
大するように設定されているので、同多孔板18における
汚染気体Aの通過が一様に行われて、上記超音波による
塵埃などの液中への捕捉および臭気物質の分解も効率よ
く一様に行われるようになる。In the dust collecting and deodorizing device of the first embodiment described above,
A pollutant gas A containing pollutants such as dust, soot, and odor is pressed into the pollutant gas supply port 16a by a blower (not shown) or sucked from the treated gas recovery port 22 by the blower 24. Is subjected to a dust collecting and deodorizing action by the ultrasonic waves from the ultrasonic generator 20 while passing through the perforated plate 18. At that time, a large number of small holes in the perforated plate 18 are
Since 26 is set as small holes 26a, 26b, and 26c having a three-step hole diameter so that the hole diameter increases as the distance from the polluted gas supply path 16 increases, the passage of the polluted gas A through the perforated plate 18 is reduced. In this way, the ultrasonic waves can be efficiently and uniformly captured in the liquid such as dust and decomposed the odorous substance.
【0031】また、多孔板18が、汚染気体供給経路16か
ら遠ざかるにつれて漸次上方へ向かい傾斜するように配
置されることにより、多孔板18における小孔の孔径の分
布と相まって、同多孔板18を通過する気体の流れが一様
になり、これにより集塵脱臭作用が効率よく適切に行わ
れるようになる。そして、実験の結果に基づき多孔板18
の傾斜角度が3〜7度の範囲に設定されると、上記集塵
脱臭作用が一層効率よく行われる。Further, since the perforated plate 18 is arranged so as to gradually incline upward as it goes away from the polluted gas supply path 16, the perforated plate 18 is combined with the pore size distribution of the small holes in the perforated plate 18. The flow of the gas passing therethrough becomes uniform, so that the deodorizing action of dust collection can be efficiently and appropriately performed. Then, based on the result of the experiment, the perforated plate 18
When the inclination angle of is set in the range of 3 to 7 degrees, the dust collecting deodorizing action is more efficiently performed.
【0032】前述のように、多孔板18は、汚染気体供給
経路16から遠ざかるにつれて小孔26の孔径を段階的に大
きくした複数段階の小孔26a,26b,26cとして各孔径
を設定されているので、その製作時には各段階ごとに同
じ孔径で孔明け作業が行えるので、装置全体としての性
能を極力維持しながら、その製造コストを節減できるよ
うになる。そして、上記孔径の大きさの段階が3段階と
されて、その孔径の割合が汚染気体供給経路16に近いも
のから順に1:2:4となるように設定されていると、
その製造コストの低減および装置全体としての性能の維
持が適切に行われるようになる。As described above, the perforated plate 18 has a plurality of stages of small holes 26a, 26b, and 26c in which the diameters of the small holes 26 are gradually increased with increasing distance from the polluted gas supply passage 16. Therefore, at the time of manufacturing, since it is possible to perform the drilling work with the same hole diameter at each stage, it is possible to reduce the manufacturing cost while maintaining the performance of the entire apparatus as much as possible. Then, if the size of the hole diameter is set to three levels, and the ratio of the hole diameter is set to 1: 2: 4 in order from the one closer to the polluted gas supply path 16,
The manufacturing cost can be reduced and the performance of the entire device can be maintained appropriately.
【0033】さらに、多孔板18における孔の総面積が、
同多孔板18の平面の総面積の5〜15%となるように設
定されていると、上記の各小孔を汚染気体が通過しなが
ら超音波発生器20からの超音波により受ける塵埃の分離
捕捉や臭気物質の分解処理が的確に行われるようにな
る。Furthermore, the total area of the holes in the perforated plate 18 is
If it is set so as to be 5 to 15% of the total area of the plane of the porous plate 18, separation of dust received by ultrasonic waves from the ultrasonic wave generator 20 while contaminated gas passes through each of the above-mentioned small holes. The capture and decomposition of odorous substances will be performed properly.
【0034】また本実施形態の集塵脱臭装置は、汚染気
体供給経路16に汚染気体Aを圧送して供給する手段が接
続されたり、汚染気体処理部12の上部における処理済み
気体回収口22に気体吸引手段としてのブロワー24が接続
されたりすることによって、装置全体としての作動が的
確に行われる。Further, in the dust collecting deodorizing apparatus of this embodiment, means for feeding the polluted gas A by pressure feed to the polluted gas supply path 16 is connected, or to the treated gas recovery port 22 in the upper part of the polluted gas treatment section 12. By connecting a blower 24 as a gas suction means, the operation of the entire apparatus is accurately performed.
【0035】そして、超音波発生器20が、その超音波の
周波数を19.5〜29kHzに設定されることによ
り、多孔板18における小孔の大きさおよび配置の状態と
相まって、汚染気体についての集塵脱臭作用が適切に行
われる。The ultrasonic wave generator 20 sets the frequency of the ultrasonic wave to 19.5 to 29 kHz, which, in combination with the size and arrangement of the small holes in the perforated plate 18, results in The deodorizing action of dust collection is properly performed.
【0036】次に本発明の第2実施形態としての集塵脱
臭装置について説明すると、図3に示すように、この装
置も前述の第1実施形態の装置とほぼ同様に形成されて
おり、図中の同じ符号は同じ部材を示しているが、この
第2実施形態では特に汚染気体供給経路16に、殺菌用の
オゾンガスまたはオゾン水Dを供給するオゾン供給手段
としてのオゾン導入経路30が接続されていて、その下端
開口30aの位置は、隔壁10aの下端縁10bとタンク本体
10の底面10cとの中間のレベルに設定されている。Next, a dust collecting deodorizing apparatus as a second embodiment of the present invention will be described. As shown in FIG. 3, this apparatus is also formed in substantially the same manner as the apparatus of the first embodiment described above. In the second embodiment, an ozone introduction path 30 as an ozone supply means for supplying ozone gas or ozone water D for sterilization is connected to the polluted gas supply path 16 in particular, although the same reference numerals indicate the same members. The lower end opening 30a is located at the lower end edge 10b of the partition wall 10a and the tank body.
It is set to an intermediate level with the bottom surface 10c of the 10.
【0037】上述の第2実施形態では、前述の第1実施
形態と同様の作用効果が得られるほか、さらにオゾンに
よる殺菌作用が行われるので、汚染気体の浄化が一層適
切に行われるようになる。In the above-described second embodiment, in addition to the same effects as the above-described first embodiment, the sterilization effect by ozone is further performed, so that the polluted gas can be purified more appropriately. .
【0038】次に本発明の第3実施形態としての集塵脱
臭装置について説明すると、図4に示すように、この第
3実施形態の場合も前述の第1実施形態の装置とほぼ同
様に形成されて、図4における図1と同じ符号は同じ部
材を示しているが、この第3実施形態では、特に汚染気
体供給経路16内へ油を気化させて供給する手段として、
ヒーター42により油Cを蒸発させるためのオイルタンク
44が設けられている。そして、ヒーター42の制御は、制
御装置13により行われるようになっている。Next, a dust collecting deodorizing device as a third embodiment of the present invention will be described. As shown in FIG. 4, in the case of the third embodiment, the device is formed in substantially the same manner as the device of the first embodiment. The same reference numerals as those in FIG. 1 in FIG. 4 indicate the same members, but in the third embodiment, as means for vaporizing and supplying oil into the polluted gas supply path 16, in particular,
Oil tank for evaporating oil C by heater 42
44 are provided. The heater 42 is controlled by the control device 13.
【0039】上述の第3実施形態の場合も、前述の第1
実施形態と同様の作用効果が得られるほか、油Cの気化
したガスが、汚染気体中の塵埃や煤煙を捕捉して効率よ
く処理液体中へ分離するようになる。Also in the case of the above-mentioned third embodiment, the above-mentioned first
In addition to the same effects and advantages as in the embodiment, the vaporized gas of the oil C captures dust and soot in the contaminated gas and efficiently separates it into the treated liquid.
【0040】このようにして、本発明の各実施形態の集
塵脱臭装置によれば、汚染気体を通す多孔板18の小孔群
の配置を適切に且つ安価に行えるようにするとともに、
同小孔群に対する超音波発生器20の配置も適切に行える
ようにして、効率のよい集塵脱臭装置を低コストで実現
できるようになる。As described above, according to the dust collecting and deodorizing apparatus of the respective embodiments of the present invention, the arrangement of the small hole group of the perforated plate 18 through which the contaminated gas is passed can be appropriately and inexpensively performed.
The ultrasonic generator 20 can be appropriately arranged in the small hole group, and an efficient dust collecting and deodorizing device can be realized at low cost.
【0041】[0041]
【発明の効果】以上詳述したように、本発明の集塵脱臭
装置によれば次のような効果が得られる。
(1) 塵埃,煤煙,臭気などの汚染物質を含んだ汚染気体
を汚染気体供給経路を通じ圧入するか、または処理済み
気体回収口から吸引することにより、同汚染気体は、多
孔板を通過しながら超音波発生器からの超音波により集
塵脱臭作用を受けるが、その際、上記多孔板における多
数の小孔の孔径が、上記汚染気体供給経路から遠ざかる
につれて増大するように設定されているので、同多孔板
における上記汚染気体の通過が一様に行われて、上記超
音波による塵埃などの液中への捕捉および臭気物質の分
解も効率よく一様に行われるようになる。
(2) 上記多孔板が上記気体供給経路から遠ざかるにつれ
て漸次上方へ向かい傾斜するように配置されることによ
り、上記多孔板における小孔の孔径の分布と相まって、
同多孔板を通過する気体の流れが一様になり、これによ
り集塵脱臭作用が効率よく適切に行われるようになる。
(3) 上記多孔板の傾斜角度が3〜7度の範囲に設定され
ると、上記集塵脱臭作用が一層効率よく行われる。
(4) 上記多孔板が、上記汚染気体供給経路から遠ざかる
につれて孔径を段階的に大きくするように、複数段階に
孔径を設定されていると、その製作時には各段階ごとに
同じ孔径で孔明け作業が行えるので、装置全体としての
性能を極力維持しながら、その製造コストを節減できる
ようになる。
(5) 上記孔径の大きさの段階が3段階とされて、その孔
径の割合が上記気体供給経路に近いものから順に1:
2:4となるように設定されていると、その製造コスト
の低減および装置全体としての性能の維持が適切に行わ
れるようになる。
(6) 上記多孔板における孔の総面積が、同多孔板の平面
の総面積の5〜15%となるように設定されていると、
上記の各孔を汚染気体が通過しながら上記超音波発生器
からの超音波により受ける塵埃の分離や臭気物質の分解
処理が的確に行われるようになる。
(7) 上記汚染気体供給経路に汚染気体を圧送して供給す
る手段が接続されたり、上記汚染気体処理部の上部にお
ける上記処理済み気体回収口に気体吸引手段が接続され
たりすることによって、装置全体としての作動が的確に
行われる。
(8) 上記超音波発生器が、その超音波の周波数を19.
5〜29kHzに設定されることにより、上記多孔板に
おける孔径の大きさおよび配置の状態と相まって、汚染
気体についての集塵脱臭作用が適切に行われる。
(9) 上記汚染気体供給経路に、オゾンガスまたはオゾン
水を供給するオゾン供給手段が接続されたり、同オゾン
供給手段として上記汚染気体供給経路内に垂下されたオ
ゾン供給管の下端開口の位置を、上記タンク本体におけ
る上記隔壁の下端と同タンク本体の底面との中間のレベ
ルに設定されたりすることにより、処理液体中への上記
のオゾンガスまたはオゾン水の供給が適切に行われて、
汚染気体についてのオゾンによる殺菌作用が的確に行わ
れるようになる。
(10) 上記汚染気体供給経路内へ油を気化させて供給す
る手段が設けられると、この油の気化したガスが、汚染
気体中の塵埃や煤煙を捕捉して効率よく処理液体中へ分
離するようになる。
(11) 上記各項により、汚染気体を通す多孔板の小孔群
の配置を適切に且つ安価に行えるようにするとともに、
同小孔群に対する超音波発生器の配置も適切に行えるよ
うにして、効率のよい集塵脱臭装置を低コストで実現で
きるようになる。As described above in detail, according to the dust collecting deodorizing apparatus of the present invention, the following effects can be obtained. (1) By injecting pollutant gas containing pollutants such as dust, soot, odor, etc. through the pollutant gas supply route or sucking it from the treated gas recovery port, the pollutant gas will pass through the perforated plate. It receives dust collecting and deodorizing action by the ultrasonic waves from the ultrasonic generator, but at that time, the hole diameters of a large number of small holes in the perforated plate are set to increase as the distance from the polluted gas supply path increases, The contaminated gas is uniformly passed through the porous plate, and the ultrasonic waves are efficiently and uniformly trapped in the liquid such as dust and decomposed the odorous substance. (2) The perforated plate is arranged so as to incline gradually upward as it goes away from the gas supply path, in combination with the distribution of the pore size of the small holes in the perforated plate,
The flow of gas through the perforated plate becomes uniform, so that the deodorizing action of dust can be efficiently and appropriately performed. (3) When the inclination angle of the perforated plate is set in the range of 3 to 7 degrees, the dust collecting and deodorizing action is more efficiently performed. (4) If the perforated plate is set to have a plurality of stages of hole diameters such that the hole diameter is increased stepwise as it moves away from the polluted gas supply path, the same hole diameter is used for each stage during the manufacturing process. Therefore, the manufacturing cost can be reduced while maintaining the performance of the entire apparatus as much as possible. (5) There are three stages of the size of the pore size, and the ratio of the pore size is closer to the gas supply path in the order of 1:
When the ratio is set to 2: 4, the manufacturing cost can be reduced and the performance of the entire device can be appropriately maintained. (6) When the total area of the holes in the perforated plate is set to be 5 to 15% of the total area of the plane of the perforated plate,
While the contaminated gas passes through each of the above holes, the dust received by the ultrasonic waves from the ultrasonic wave generator and the decomposition process of the odorous substance can be performed accurately. (7) By connecting a means for supplying polluted gas under pressure to the polluted gas supply path, or by connecting a gas suction means to the processed gas recovery port in the upper part of the polluted gas processing section, the device The operation as a whole is accurately performed. (8) The ultrasonic generator sets the frequency of the ultrasonic wave to 19.
By setting the frequency to 5 to 29 kHz, the dust collecting and deodorizing action with respect to the polluted gas is appropriately performed in combination with the size and arrangement state of the hole diameter in the porous plate. (9) In the polluted gas supply path, an ozone supply means for supplying ozone gas or ozone water is connected, or the position of the lower end opening of the ozone supply pipe hung in the polluted gas supply path as the ozone supply means, By setting it at an intermediate level between the lower end of the partition wall of the tank body and the bottom surface of the tank body, the ozone gas or ozone water is appropriately supplied to the treatment liquid,
The sterilizing action of ozone on the polluted gas is properly performed. (10) When the means for vaporizing and supplying the oil into the polluted gas supply path is provided, the vaporized gas of the oil captures dust and soot in the polluted gas and efficiently separates it into the treated liquid. Like (11) With the above items, it is possible to appropriately and inexpensively arrange the small hole group of the perforated plate through which the contaminated gas is passed,
By appropriately disposing the ultrasonic wave generator in the small hole group, an efficient dust collecting and deodorizing device can be realized at low cost.
【図1】本発明の第1実施形態としての集塵脱臭装置を
概略的に示す縦断面図である。FIG. 1 is a vertical sectional view schematically showing a dust collecting and deodorizing apparatus as a first embodiment of the present invention.
【図2】図1の集塵脱臭装置における多孔板の平面図で
ある。FIG. 2 is a plan view of a perforated plate in the dust collecting and deodorizing apparatus of FIG.
【図3】本発明の第2実施形態としての集塵脱臭装置を
概略的に示す縦断面図である。FIG. 3 is a vertical cross-sectional view schematically showing a dust collecting and deodorizing apparatus as a second embodiment of the present invention.
【図4】本発明の第3実施形態としての集塵脱臭装置を
概略的に示す縦断面図である。FIG. 4 is a vertical sectional view schematically showing a dust collecting and deodorizing apparatus as a third embodiment of the present invention.
【図5】従来の集塵脱臭装置の概略構成を示す縦断面図
である。FIG. 5 is a vertical sectional view showing a schematic configuration of a conventional dust collecting deodorizing apparatus.
10 タンク本体 10a 隔壁 10b 隔壁の下端縁 10c 底面 10d 連通路 11 液面検出センサー 12 汚染気体処理部 13 制御装置 14 底壁開口 15 タンク 16 汚染気体供給経路 16a 汚染気体供給口 18 多孔板 20 超音波発生器 22 処理済み気体回収口 24 ブロワー 25 水平面 26,26a〜26c 小孔 30 オゾン導入経路 30a 下端開口 34 液面 42 ヒーター 44 オイルタンク A 汚染気体 B 処理用液体 C 油 D オゾン水 α 傾斜角度 10 Tank body 10a bulkhead 10b Bottom edge of bulkhead 10c bottom 10d communication passage 11 Liquid level sensor 12 Polluted gas processing unit 13 Control device 14 Bottom wall opening 15 tanks 16 Contamination gas supply route 16a Contaminated gas supply port 18 Perforated plate 20 Ultrasonic generator 22 Treated gas recovery port 24 blower 25 Horizontal 26, 26a-26c Small hole 30 Ozone introduction route 30a Bottom opening 34 Liquid level 42 heater 44 oil tank A polluted gas B Treatment liquid C oil D Ozone water α inclination angle
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 53/74 B01D 53/34 116F 53/77 116Z Fターム(参考) 4D002 AB02 BA02 BA05 BA11 BA14 CA06 DA35 DA51 EA03 GA02 GA03 GB01 GB06 GB20 4D032 AA01 BA01 BA03 BA05 BB05 CA01 CA10 DA02 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) B01D 53/74 B01D 53/34 116F 53/77 116Z F term (reference) 4D002 AB02 BA02 BA05 BA11 BA14 CA06 DA35 DA51 EA03 GA02 GA03 GB01 GB06 GB20 4D032 AA01 BA01 BA03 BA05 BB05 CA01 CA10 DA02
Claims (12)
だ汚染気体について集塵脱臭処理を行うべく処理用液体
を収容したタンク本体が、同タンク本体の頂壁から垂下
された隔壁により汚染気体供給経路と汚染気体処理部と
に分割されて、上記汚染気体供給経路の上部に汚染気体
供給口が設けられるとともに、上記汚染気体処理部の上
部に処理済み気体回収口が設けられ、上記隔壁の下端縁
と上記タンク本体の底面との間に上記の汚染気体供給経
路と汚染気体処理部との連通路が形成されて、上記汚染
気体処理部に上記隔壁の下端縁から上記タンク本体の側
壁へ到る多孔板が設けられるとともに、同多孔板の下方
から同多孔板へ向けて超音波を放射する超音波発生器が
設けられ、上記多孔板における孔径が、上記汚染気体供
給経路から遠ざかるにつれて増大するように設定されて
いることを特徴とする、集塵脱臭装置。1. A tank main body containing a processing liquid for performing a dust collecting and deodorizing process on a pollutant gas containing a pollutant such as dust, soot, and odor is contaminated by a partition wall hanging from a top wall of the tank main body. The partition wall is divided into a gas supply path and a polluted gas processing section, a polluted gas supply port is provided above the polluted gas supply path, and a treated gas recovery port is provided above the polluted gas processing section. Is formed between the bottom edge of the tank body and the bottom surface of the tank body, and a communication path between the polluted gas supply path and the polluted gas treatment section is formed, and the polluted gas treatment section extends from the bottom edge of the partition wall to the side wall of the tank body. A perforated plate is provided, and an ultrasonic wave generator that emits ultrasonic waves from below the perforated plate toward the perforated plate is provided, and the hole diameter in the perforated plate is far from the contaminated gas supply path. The dust collecting and deodorizing device is characterized in that the dust collecting and deodorizing device is set so as to increase with the increase.
て、上記多孔板が、上記汚染気体供給経路から遠ざかる
につれて漸次上方へ向かい傾斜するように配置されてい
ることを特徴とする、集塵脱臭装置。2. The dust collecting deodorizing apparatus according to claim 1, wherein the perforated plate is arranged so as to gradually incline upward as it goes away from the polluted gas supply path. Deodorizing device.
て、上記多孔板の傾斜角度が3〜7度の範囲に設定され
ていることを特徴とする、集塵脱臭装置。3. The dust collecting deodorizing apparatus according to claim 2, wherein the angle of inclination of the perforated plate is set in a range of 3 to 7 degrees.
塵脱臭装置において、上記多孔板が、上記汚染気体供給
経路から遠ざかるにつれて孔径を段階的に大きくするよ
うに、複数段階に孔径を設定されていることを特徴とす
る、集塵脱臭装置。4. The dust collecting and deodorizing apparatus according to claim 1, wherein the perforated plate has a plurality of stages so that the pore size increases stepwise as the distance from the polluted gas supply path increases. A dust collecting and deodorizing device characterized by having a set pore diameter.
て、上記多孔板が、上記汚染気体供給経路から遠ざかる
につれて孔径を大きくするように3段階に孔径を設定さ
れて、その孔径の割合が上記気体供給経路に近いものか
ら順に1:2:4となるように設定されていることを特
徴とする、集塵脱臭装置。5. The dust collecting deodorizing apparatus according to claim 4, wherein the perforated plate is set in three stages of hole diameters such that the hole diameter increases as the distance from the contaminated gas supply path increases, and the ratio of the hole diameters is set. A dust collecting deodorizing device, characterized in that the dust collecting deodorizing device is set so that the gas is closer to the gas supply route in order of 1: 2: 4.
塵脱臭装置において、上記多孔板の孔の総面積が、同多
孔板の平面の総面積の5〜15%となるように設定され
ていることを特徴とする、集塵脱臭装置。6. The dust collecting and deodorizing device according to claim 1, wherein the total area of the holes of the perforated plate is 5 to 15% of the total area of the plane of the perforated plate. The dust collecting and deodorizing device characterized by being set to.
塵脱臭装置において、上記汚染気体供給経路に、汚染気
体を圧送して供給する手段が接続されていることを特徴
とする、集塵脱臭装置。7. The dust collecting and deodorizing apparatus according to claim 1, wherein a means for pumping and supplying the polluted gas is connected to the polluted gas supply path. , Dust collector and deodorizer.
塵脱臭装置において、上記汚染気体処理部の上部におけ
る上記処理済み気体回収口に、気体吸引手段が接続され
ていることを特徴とする、集塵脱臭装置。8. The dust collecting and deodorizing apparatus according to claim 1, wherein a gas suction means is connected to the processed gas recovery port in the upper part of the polluted gas processing unit. A characteristic dust collecting and deodorizing device.
塵脱臭装置において、上記超音波発生器が、その超音波
の周波数を19.5〜29kHzに設定されていること
を特徴とする、集塵脱臭装置。9. The dust collecting deodorizing apparatus according to claim 1, wherein the ultrasonic wave generator has an ultrasonic wave frequency set to 19.5 to 29 kHz. A dust collector and deodorizer.
集塵脱臭装置において、上記汚染気体供給経路に、オゾ
ンガスまたはオゾン水を供給するオゾン供給手段が接続
されていることを特徴とする、集塵脱臭装置。10. The dust collecting and deodorizing apparatus according to claim 1, wherein an ozone supply means for supplying ozone gas or ozone water is connected to the polluted gas supply path. A dust collector and deodorizer.
いて、上記オゾン供給手段が、上記汚染気体供給経路の
上部から同汚染気体供給経路内に垂下されたオゾン供給
管を備えて構成され、同オゾン供給管の下端開口の位置
が、上記隔壁の下端縁と上記タンク本体の底面との中間
のレベルに設定されていることを特徴とする、集塵脱臭
装置。11. The dust collecting deodorizing apparatus according to claim 10, wherein the ozone supply means is provided with an ozone supply pipe hung from the upper part of the polluted gas supply path into the polluted gas supply path. The dust collecting deodorizing device, wherein the position of the lower end opening of the ozone supply pipe is set at a level intermediate between the lower end edge of the partition wall and the bottom surface of the tank body.
の集塵脱臭装置において、上記汚染気体供給経路内へ油
を気化させて供給する手段が設けられたことを特徴とす
る、集塵脱臭装置。12. The dust collecting and deodorizing apparatus according to claim 1, further comprising means for vaporizing and supplying oil into the polluted gas supply path. Dust deodorizer.
Priority Applications (1)
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JP2002015396A JP3717451B2 (en) | 2002-01-24 | 2002-01-24 | Dust collector deodorizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002015396A JP3717451B2 (en) | 2002-01-24 | 2002-01-24 | Dust collector deodorizer |
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JP2003210932A true JP2003210932A (en) | 2003-07-29 |
JP3717451B2 JP3717451B2 (en) | 2005-11-16 |
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JP2002015396A Expired - Fee Related JP3717451B2 (en) | 2002-01-24 | 2002-01-24 | Dust collector deodorizer |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013186829A1 (en) * | 2012-06-11 | 2013-12-19 | 株式会社三育 | Combustion gas processing device |
WO2016029620A1 (en) * | 2014-08-25 | 2016-03-03 | 段洪池 | Air-purification device using liquid reducing agent, and operation and application method therefor |
KR101824372B1 (en) | 2017-12-20 | 2018-03-14 | (주)수일건설엔지니어링 | Dust removal equipment for sewage sludge treatment |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103785221A (en) * | 2014-01-26 | 2014-05-14 | 泰兴市睿济科技有限公司 | Balanced water distribution and clarification tank |
-
2002
- 2002-01-24 JP JP2002015396A patent/JP3717451B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013186829A1 (en) * | 2012-06-11 | 2013-12-19 | 株式会社三育 | Combustion gas processing device |
JPWO2013186829A1 (en) * | 2012-06-11 | 2016-02-01 | 株式会社三育 | Combustion gas processing equipment |
WO2016029620A1 (en) * | 2014-08-25 | 2016-03-03 | 段洪池 | Air-purification device using liquid reducing agent, and operation and application method therefor |
KR101824372B1 (en) | 2017-12-20 | 2018-03-14 | (주)수일건설엔지니어링 | Dust removal equipment for sewage sludge treatment |
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Publication number | Publication date |
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JP3717451B2 (en) | 2005-11-16 |
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