JPS604722B2 - Exhaust smoke purification method and device - Google Patents
Exhaust smoke purification method and deviceInfo
- Publication number
- JPS604722B2 JPS604722B2 JP51097694A JP9769476A JPS604722B2 JP S604722 B2 JPS604722 B2 JP S604722B2 JP 51097694 A JP51097694 A JP 51097694A JP 9769476 A JP9769476 A JP 9769476A JP S604722 B2 JPS604722 B2 JP S604722B2
- Authority
- JP
- Japan
- Prior art keywords
- flue gas
- water
- condensed water
- pressure difference
- exhaust 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.)
- Expired
Links
Landscapes
- Treating Waste Gases (AREA)
- Separation Of Particles Using Liquids (AREA)
Description
【発明の詳細な説明】
本発明は排煙の浄化方法及びその装置にかかわり、更に
詳しくは各種燃焼装置等の排煙中に含まれる粉じんのほ
かに微細な水溶性塩類、その他有害物質をも除去する方
法及びその装置にかかわる。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and device for purifying flue gas, and more specifically, it also removes fine water-soluble salts and other harmful substances in addition to dust contained in flue gas from various combustion devices. It concerns the removal method and device.
従釆、排煙浄化を目的として各種の方法、装置が提案さ
れて来た。Various methods and devices have been proposed for the purpose of purifying flue gas.
最近は公害対策上、燃焼排ガスの脱じん及び脱硫を同時
に行うものが多く、この場合の排ガス処理には一般に緑
式処理が採用されているが、処理後の排ガス中にはJI
SZ斑雌で測定される「‘まいじん」として【ィ’本来
の粉じん(非水溶性)【ロー 同伴ミスト中の溶解塩(
ナトリウム塩、カルシウム塩などの水溶性塩類)が含ま
れており、特に‘o’‘まこれを機械的に除くことは困
難で、このため排煙規制値を満足し得ないものが多かっ
た。Recently, in order to prevent pollution, many combustion exhaust gases are dedusted and desulfurized at the same time, and green treatment is generally adopted for exhaust gas treatment in this case, but after treatment, the exhaust gas contains JI
The ``dust'' measured in the SZ Spotted Female is ``inherent dust (water-insoluble) ``dissolved salts in the entrained mist (
Water-soluble salts such as sodium salts and calcium salts) are contained, and it is difficult to remove them mechanically, especially 'o'', and for this reason, many of them fail to meet the smoke emission regulation values.
従来の装置で排ガス洗浄に海水又は苛性ソーダ並びに石
灰類を使用した時は、洗浄後の排ガス中に水落性塩類の
微粒子の存在が避け難く、これが湿式ガス洗浄装置の最
大の欠陥であり、この塩類を除去する為に、更に湿式電
気集じん機の採用を考慮せざるを得ないのが実情であっ
た。When conventional equipment uses seawater, caustic soda, and lime for cleaning exhaust gas, it is difficult to avoid the presence of fine particles of salts in the exhaust gas after cleaning, and this is the biggest drawback of wet gas cleaning equipment. In order to remove the dust, it was necessary to consider the use of a wet electrostatic precipitator.
しかも溢式電気集じん機使用に際しては装置の腐食、ス
ケール付着等操業上の問題があり、設備費高と相まって
、特に中小容量の排ガス処理には通さなかった。従来、
空気中水分の凝縮が除じんに大きな効果を表すことは知
られていたが、本発明者は特に水落性塩類の超微粒子が
この凝縮水分に捕捉されるという知見に基づき種々研究
の結果、排ガスの流路に擬風機を設け、排ガスの流れに
対して8E風機の前方に加湿装置及び後方に凝縮水分雛
装置を設け、更に加湿装置の前方及び凝縮水分離装置の
後方の少なくとも一方に絞りを設けることにより、擬風
機の前後の圧力差を利用して排ガス中の飽和水分を凝縮
させ、排風機の下流でこの凝縮水を除去することにより
、高度の除じん効果を得ることができた。Furthermore, when using an overflow type electrostatic precipitator, there are operational problems such as corrosion of the device and scale adhesion, which, combined with high equipment costs, makes it unsuitable for waste gas treatment of small to medium capacity in particular. Conventionally,
It has been known that the condensation of moisture in the air has a great effect on dust removal, but the inventor of the present invention has conducted various studies based on the knowledge that ultrafine particles of water-soluble salts are captured in this condensed moisture, and has found that A fan is installed in the flow path of the exhaust gas, a humidifier is installed in front of the 8E fan and a condensed water filtration device is installed behind the 8E fan, and a throttle is installed in front of the humidifier and at least one of the rear of the condensed water separator. By installing this, the saturated water in the exhaust gas is condensed using the pressure difference before and after the fan, and this condensed water is removed downstream of the fan, resulting in a highly effective dust removal effect.
次に本発明実施の一例を示す図面により詳細説明する。Next, a detailed explanation will be given with reference to drawings showing an example of the implementation of the present invention.
絞り1及び1′は流略における排ガスの流れを抑制する
ものであって、例えば、オリフイス、ベンチュリー管、
ダンパー、バルフ、コックその他各種形式のものを採択
使用することができる。この絞りは次に述べる加湿装置
2の前方、又は凝縮水分離装置4の後方の少なくとも何
れか一方に設けられる必要があり、場合によっては両方
に設けることができる。なお本発明において前方及び後
方とは排ガスの流れの上流を前方、下流を後方とする。
絞り1,1′は9E風機3の駆動により排風機の前後に
高い圧力差を生じさせるために設けたものであって、そ
の絞りの程度は使用目的によって任意に設定する。加湿
装置2は排風磯前排ガスに充分な湿度を与え、好ましく
は水蒸気飽和となすためのもので、種々の加湿装置が採
択されるが蒸気噴射、水の階霧などが好適であって排風
機の前方に設け、絞り1を排風機の前方に設ける場合は
絞り1が加湿装置と同位置若しくは加湿装置の直前に位
置する如く設置するのが好ましい。The throttles 1 and 1' are for suppressing the flow of exhaust gas in the flow, and are, for example, orifices, venturi tubes, etc.
Various types of dampers, valves, cocks, etc. can be adopted and used. This throttle needs to be provided at least either in front of the humidifying device 2, which will be described below, or in the rear of the condensed water separation device 4, and in some cases, it can be provided in both. In the present invention, the term "front" and "rear" refer to the upstream side of the exhaust gas flow as the front side, and the downstream side of the exhaust gas flow as the rear side.
The throttles 1 and 1' are provided to generate a high pressure difference between the front and rear sides of the exhaust fan by driving the 9E wind fan 3, and the degree of the throttle is set arbitrarily depending on the purpose of use. The humidifying device 2 is used to give sufficient humidity to the exhaust gas in front of the exhaust shore, preferably to saturate it with water vapor. Various humidifying devices can be used, but steam injection, water mist, etc. are suitable, and an exhaust gas is used. When the diaphragm 1 is installed in front of the exhaust fan, it is preferable to install the diaphragm 1 at the same position as the humidifier or just in front of the humidifier.
9E風機3は排ガスを移送するとともに、排風機の前後
に高い圧力差を生ぜしめるためのものであって、ファン
、ブロアーその他各種の排風機を使用することができる
。The 9E blower 3 is used to transport exhaust gas and create a high pressure difference between the front and rear sides of the blower, and a fan, a blower, or any other type of blower may be used.
凝縮水分雛装置4は9E風機3の後方に設けられ、排風
機3の加圧効果により発生した排ガス中の凝縮水分を分
離除去することにより、排ガス中の微細な粉じん(非水
溶性)及び同伴ミスト中の水縁性塩類を同時に除去する
ものであって、通常使用される遠心式又は慣性式ミスト
除去装置から任意に選択使用することができる。The condensed moisture extraction device 4 is installed behind the 9E fan 3, and separates and removes the condensed moisture in the exhaust gas generated by the pressurizing effect of the exhaust fan 3, thereby removing fine dust (water-insoluble) and entrained particles in the exhaust gas. The water-related salts in the mist are removed at the same time, and any commonly used centrifugal or inertial mist removal device can be used.
ただし櫨過式ミスト除去装置は目詰りを起すのでこの場
合適当ではない。本装置は上記のような構成を有するも
のであるから、排風機3を駆動するときは前方から流れ
てくる排ガス6は絞り1で流れが抑制されるとともに排
風機3により後方に強制的に移送されるので、絞り1と
aE風機3の間は減圧状態となり、ついでこの間に設け
られた加湿装置2によって水蒸気で飽和せしめられる。However, a filter-type mist removal device is not suitable in this case because it causes clogging. Since this device has the above configuration, when the exhaust fan 3 is driven, the exhaust gas 6 flowing from the front is suppressed by the throttle 1 and is forcibly transferred to the rear by the exhaust fan 3. As a result, the space between the aperture 1 and the aE fan 3 is reduced in pressure, and is then saturated with water vapor by the humidifying device 2 provided between the aperture 1 and the aE fan 3.
水蒸気で飽和された排ガスは排風機3により送り出され
た後は昇庄して元の圧力状態に戻り、又は凝縮水分隣菱
贋4や他の絞り1′その他の流路阻害物によって元の圧
力よりは更に昇圧された状態となる。このようにして排
風機の前方で減圧状態で水蒸気飽和とされた排ガスは排
風機の後方では昇庄されて水蒸気過飽和の状態になり、
瞬時に水分の凝縮が起る。After the exhaust gas saturated with water vapor is sent out by the exhaust fan 3, it is elevated and returns to the original pressure state, or the original pressure is reduced by the condensed water pipe 4, other throttles 1', and other flow path obstructions. The voltage is further increased. In this way, the exhaust gas that is reduced in pressure and saturated with water vapor in front of the exhaust fan is elevated and becomes supersaturated with water vapor at the rear of the exhaust fan.
Moisture condensation occurs instantly.
この排ガスを続いて凝縮水分離装置4に通すときは、発
生した凝縮水が排ガスから分離される。When this exhaust gas is subsequently passed through the condensed water separator 4, the generated condensed water is separated from the exhaust gas.
その際凝縮水に付着した形で非水溶性粉じんが、又凝縮
水に溶解した形で水溶性塩類が凝縮水と共に除去される
。凝縮水の発生量が多い程、目的とする除じん効果が向
上するが、凝縮水の発生量はSE風機前後の圧力差が大
きい程、又排ガス温度が高い程多い。At this time, water-insoluble dust adhering to the condensed water and water-soluble salts dissolved in the condensed water are removed together with the condensed water. The greater the amount of condensed water generated, the better the desired dust removal effect will be, but the greater the pressure difference before and after the SE blower, or the higher the exhaust gas temperature, the greater the amount of condensed water generated.
本発明者の実施例では、海水洗浄塔と中圧ベンチュリー
スクラバ−を備えた実際の焼却炉排ガス処理装置で、絞
り1並びに加湿装置2として中圧ベンチュリースクラバ
ーを採用し、排風機3の前後の圧力差が50物吻水柱(
擬風磯前−45仇吻水柱、後十5仇肌水柱)、排ガス温
度35〜40℃、乾き排ガス通過量20000Nで/日
のとき下記の如き結果が得られた。第1表
尚凝縮水分雛装置4には特殊の慣性型(ユーロホルム
ミスト ェリミネーター;日本碍子製)を用い通過凝縮
水の高率除去を行わせた。In the embodiment of the present inventor, in an actual incinerator exhaust gas treatment equipment equipped with a seawater washing tower and a medium-pressure venturi scrubber, medium-pressure venturi scrubbers are adopted as the throttle 1 and the humidifying device 2, and the The pressure difference is 50 mm water column (
The following results were obtained when the exhaust gas temperature was 35 to 40° C., and the amount of dry exhaust gas passing was 20,000 N/day. Table 1 The condensed water broiler device 4 has a special inertial type (Euroform).
A mist eliminator (manufactured by Nippon Insulator) was used to remove condensed water at a high rate.
分離除去された凝縮水の性状は次の如きものであった。
第2表凝縮水の色は未燃炭素の微粒子を含む為に黒く、
又海水中の塩化ナトリウムが溶けた状態で含まれ、海水
と変らない位に塩からいものであった。The properties of the separated condensed water were as follows.
Table 2 The color of condensed water is black because it contains fine particles of unburned carbon.
It also contained dissolved sodium chloride in seawater, and was as salty as seawater.
本発明の排煙浄化装置を構成する各装置は、既設の排ガ
ス処理設備にも簡単に組み込むことが可能で、既設の除
じん装置の能力を向上させる場合、例えば排出ばいじん
濃度を現状0.2〜0.5夕/Nでから0.2夕/Nで
以下にしたいといった場合に、大きな設備投資をかけず
に実施できる利点がある。Each device constituting the flue gas purification device of the present invention can be easily incorporated into existing exhaust gas treatment equipment, and when improving the capacity of an existing dust removal device, for example, the exhaust dust concentration can be reduced to 0.2 at the current level. This has the advantage that it can be implemented without a large capital investment if you want to reduce it from ~0.5 night/N to 0.2 night/N or less.
多くの場合、設備的には排風機の取替えだけで、又ベン
チュリースクラバーを設置して既に高圧の擬風機を使用
している場合は8E風機後に図面の配置となるように凝
縮水分滋装置を取りつけるだけで効果をあげ得る。なお
海水や苛性ソーダ又は石灰を使用する排ガス洗浄装置は
水溶性塩類のミスト同伴を防ぐ為に排風機3の前に配置
することが必要である。In many cases, the only equipment required is to replace the exhaust fan, or if a Venturi scrubber is installed and a high-pressure artificial fan is already in use, a condensed water draining device is installed after the 8E fan as shown in the drawing. alone can be effective. Note that an exhaust gas cleaning device that uses seawater, caustic soda, or lime must be placed in front of the exhaust fan 3 to prevent water-soluble salts from being entrained in mist.
第1図は本発明実施の場合の構成説明図で1,1′……
絞り、2……加湿装贋、3……9E風機、4....・
・凝縮水分麹装置、5・…・・マノメーター、6,6′
……排ガスを示す。FIG. 1 is an explanatory diagram of the configuration in the case of implementing the present invention. 1, 1'...
Aperture, 2... humidifier, 3... 9E fan, 4. .. .. ..・
・Condensed moisture koji device, 5... Manometer, 6,6'
...Indicates exhaust gas.
Claims (1)
に圧力差発生部を設け、更に排煙の流れに対し該圧力差
発生部の前方及び後方の少くとも一方の流路に絞りを設
けて前方が低圧力部、後方が高圧部となるようにし、低
圧部において給湿することによりほぼ水蒸気飽和状態と
して排煙中の水溶性塩類及び粉塵を捕捉し、次いで高圧
部において水蒸気過飽和状態となつて発生する水分を凝
縮分離することにより、凝縮水とともに水溶性塩類及び
粉塵を分離除去することを特徴とする排煙浄化方法。 2 湿式ガス洗浄装置を通過してきた排煙の流路の一部
に圧力差を発生しうる排風機と、排煙の流れに対し排風
機の前方に加湿装置を、排風機後方に遠心式又は慣性性
式ミスト除去方式による凝縮水分離装置を設け、更に加
湿装置以前及び凝縮水分離装置以降のうち少なくとも一
方に絞り装置を設けたことを特徴とする排煙浄化装置。[Claims] 1. A pressure difference generating section is provided in a part of the flow path of the flue gas that has passed through the wet gas cleaning device, and furthermore, a pressure difference generating section is provided at least in front and behind the pressure difference generating section with respect to the flow of the flue gas. A throttle is provided in one flow path so that the front becomes a low pressure part and the back becomes a high pressure part, and by supplying moisture in the low pressure part, water soluble salts and dust in the flue gas are captured to almost saturate with water vapor, A flue gas purification method characterized in that the moisture generated in a supersaturated state of steam in a high-pressure section is then condensed and separated, thereby separating and removing water-soluble salts and dust together with the condensed water. 2. An exhaust fan that can generate a pressure difference in a part of the flow path of the flue gas that has passed through the wet gas cleaning device, a humidifier in front of the exhaust fan for the flow of exhaust smoke, and a centrifugal or centrifugal type humidifier behind the exhaust fan. 1. A flue gas purification device comprising a condensed water separation device using an inertial mist removal method, and further comprising a throttling device before the humidification device and after the condensed water separation device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51097694A JPS604722B2 (en) | 1976-08-18 | 1976-08-18 | Exhaust smoke purification method and device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51097694A JPS604722B2 (en) | 1976-08-18 | 1976-08-18 | Exhaust smoke purification method and device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5324178A JPS5324178A (en) | 1978-03-06 |
| JPS604722B2 true JPS604722B2 (en) | 1985-02-06 |
Family
ID=14199041
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51097694A Expired JPS604722B2 (en) | 1976-08-18 | 1976-08-18 | Exhaust smoke purification method and device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS604722B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017122962A1 (en) * | 2016-01-11 | 2017-07-20 | 손상영 | Droplet generating device and droplet generating method |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6161609A (en) * | 1984-09-03 | 1986-03-29 | Tsuyoshi Aoi | Process for cleaning air to superhigh purity |
| JPS61101223A (en) * | 1984-10-24 | 1986-05-20 | Shinryo Air Conditioning Co Ltd | How to remove atmospheric sea salt particles |
| JP2755082B2 (en) * | 1992-12-25 | 1998-05-20 | 日本鋼管株式会社 | Manufacturing method of hot rolled steel sheet |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS459269Y1 (en) * | 1967-04-19 | 1970-04-30 | ||
| JPS4947147A (en) * | 1972-09-14 | 1974-05-07 |
-
1976
- 1976-08-18 JP JP51097694A patent/JPS604722B2/en not_active Expired
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017122962A1 (en) * | 2016-01-11 | 2017-07-20 | 손상영 | Droplet generating device and droplet generating method |
| CN108602006A (en) * | 2016-01-11 | 2018-09-28 | 孙祥荣 | Drop formation device and drop formation method |
| CN108602006B (en) * | 2016-01-11 | 2021-02-02 | 孙祥荣 | Droplet generating device and droplet generating method |
| US11052343B2 (en) | 2016-01-11 | 2021-07-06 | Sang Young Son | Droplet generating device and droplet generating method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5324178A (en) | 1978-03-06 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105020782B (en) | Air purification method and air purifier | |
| US5965095A (en) | Flue gas humidification and alkaline sorbent injection for improving vapor phase selenium removal efficiency across wet flue gas desulfurization systems | |
| CN108434924A (en) | A kind of flue gas eliminating white smoke system and method | |
| GB1450223A (en) | Pollution control apparatus | |
| CN106621680A (en) | Method and system for deeply removing dust from flue gas after wet desulfurization | |
| US3435593A (en) | Gas cleaning process and apparatus | |
| JPS604722B2 (en) | Exhaust smoke purification method and device | |
| US5284637A (en) | Dry sorbent reactivation process | |
| CN206572625U (en) | Electrostatic spray is combined wet filter system | |
| SE0201227D0 (en) | Method and apparatus for separating dust from a moist gas stream | |
| GB1586623A (en) | Treatment of exhaust gases | |
| CN109078445A (en) | Flue gas ash removal takes off white integrated apparatus | |
| EP0013431A1 (en) | Rod scrubber | |
| US2681121A (en) | Recovery of suspended materials from gases | |
| CN207899175U (en) | A kind of hot investment casting roasting kiln flue purification system | |
| JP7779608B2 (en) | System including two scrubbers connected to an electrostatic precipitator and method for cleaning exhaust gases using the same | |
| JP2000512899A (en) | Method for controlling sulfuric acid aerosol formation in exhaust gas purification systems | |
| CN204693709U (en) | A kind of vehicle-mounted air purification humidifier | |
| RU2792383C1 (en) | Method for cleaning flue gases | |
| CN208905998U (en) | A kind of flue gas ash removal takes off white integrated apparatus | |
| JPH04219116A (en) | Method for cleaning exhaust gas | |
| JPS6097B2 (en) | Combustion exhaust gas purification device | |
| EP3749895B1 (en) | An apparatus for cleaning exhaust smoke | |
| CN105953315A (en) | Air filtering device requiring no consumable | |
| JPS6351924A (en) | Method of removing contaminant |