JPS6342722A - Humidifying and atomizing device for powder - Google Patents
Humidifying and atomizing device for powderInfo
- Publication number
- JPS6342722A JPS6342722A JP61186563A JP18656386A JPS6342722A JP S6342722 A JPS6342722 A JP S6342722A JP 61186563 A JP61186563 A JP 61186563A JP 18656386 A JP18656386 A JP 18656386A JP S6342722 A JPS6342722 A JP S6342722A
- Authority
- JP
- Japan
- Prior art keywords
- medium
- reactive agent
- humidifying
- powder
- dry powder
- 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
Links
- 239000000843 powder Substances 0.000 title claims abstract description 24
- 238000002156 mixing Methods 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 abstract description 7
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 239000000376 reactant Substances 0.000 description 24
- 239000007789 gas Substances 0.000 description 14
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 230000001473 noxious effect Effects 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 238000003805 vibration mixing Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は1例えば有害ガス除去装置の反応剤の循環使用
に適用される反応効率増加の為の反応剤の処理等に適用
されて好適な粉体の加湿微粒化装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention is suitable for application, for example, to the treatment of reactants for increasing reaction efficiency, which is applied to the recycling of reactants in harmful gas removal equipment. This invention relates to a humidifying and atomizing device for powder.
都市ごみ焼却プラント等から排出される有害ガス(例え
ば塩化水素)を除去するには9反応剤(消石灰等)を空
気輸送等により、比較的温度の低い(150〜450℃
)ガス中に吹込んで排ガス中の有害ガスと反応剤を反応
させて有害ガスを除去している。To remove harmful gases (e.g. hydrogen chloride) emitted from municipal waste incineration plants, etc., reactants (slaked lime, etc.) are transported by air to relatively low temperatures (150 to 450°C).
) Noxious gases are removed by blowing into the gas and reacting with the noxious gases in the exhaust gas.
従来方法においては気体と固体の反応であるため9反応
剤の排ガス中の反応は反応剤がガス中に吹込まれた瞬時
に完了してしまい、その後はあまり反応率はトからなか
った。In the conventional method, since the reaction is between a gas and a solid, the reaction of the nine reactants in the exhaust gas was completed the moment the reactants were blown into the gas, and the reaction rate was not very high after that.
その反応率をLげるためには反応剤に湿り気を持たせ(
ガスが反応剤に良く吸着する)又微粉にして(ガスと反
応剤との接触面積がふえる)その反応剤を排ガス中に吹
込めば良いということがわかってきた。なお排ガス中に
吹込まれた反応剤は飛灰と混合するが、そのまま捨てる
ことはせず1回収されて(回収された時は高温の反応剤
になっている。)反応効率が悪くなる壕で再度使用され
る。In order to increase the reaction rate, the reactant must be moistened (
It has become clear that the reactant can be pulverized (the gas adsorbs well on the reactant) or pulverized (the contact area between the gas and the reactant is increased) and then blown into the exhaust gas. Note that the reactant injected into the exhaust gas mixes with the fly ash, but it is not thrown away as is, but is collected once (it is a high-temperature reactant when recovered) in a trench where the reaction efficiency deteriorates. used again.
以トから本発明は反応剤を減温加湿し、かつ微粉にする
装置を提供するものである。From the above, the present invention provides an apparatus for cooling and humidifying a reactant and pulverizing it into fine powder.
本発明は1粒状の減温加湿媒体と乾き粉体とを混合し、
後流側で両者を分離する振動混合スクリーン装置と1分
離された減温加湿媒体を一旦水槽に落したのち水切りし
て前記振動混合スクリーン装置の上流側に供給する液温
加湿媒体循環供給装置と1分離された加湿微粉の搬送装
置と、乾き粉体を前記振動混合スクリーン装置の上流側
に供給する乾き粉体定量供給装置とから成ることを特徴
とする。The present invention mixes a granular temperature-reducing humidifying medium and dry powder,
A vibrating mixing screen device that separates the two on the downstream side; and a liquid temperature humidifying medium circulation supply device that drops the separated temperature-reduced humidifying medium into a water tank, drains it, and supplies it to the upstream side of the vibrating mixing screen device. The present invention is characterized in that it consists of a transport device for the separated humidified fine powder, and a dry powder constant supply device that supplies the dry powder to the upstream side of the vibrating mixing screen device.
乾き粉体の減温及び加湿の処理は、粉体粒径よりはるか
に大きく(例えばパチンコ王位いの大きさ)、粉体量よ
り多量の減温加湿媒体(例えば鉄球又は鉄球面に穴、溝
をつけたもの)表面の付着水を振動混合により、粉体中
に均一に分散させることにより行う。また振動混合を効
果的に行う為減温加湿媒体層間に粉体が供給されるよう
にする。減温加湿度の調節に、粉体を定量供給とし、減
温加湿媒体の循環量により行う。湿り粉体の微粒化は、
減温加湿媒体間の摩擦と振動スクリーンの作用により、
湿り粉体をスクリーンを通過きせることにより行い、一
方媒体のスクリーン面のタタキ作用により目詰りを防止
する。スクリーンを通過した湿り微粉は空気エジェクタ
により気流搬送され、団粒になることなく、その壕マ用
いられる。Temperature reduction and humidification treatment of dry powder is performed by using a temperature reduction and humidification medium that is much larger than the powder particle size (for example, the size of a pachinko throne) and larger than the amount of powder (for example, an iron ball or a hole in the iron ball surface, Grooved) This is done by uniformly dispersing the water adhering to the surface into the powder using vibration mixing. Further, in order to perform vibrational mixing effectively, the powder is supplied between the layers of the temperature-reducing humidifying medium. To adjust the temperature and humidification, the powder is supplied in a fixed amount and the amount of circulation of the temperature and humidification medium is adjusted. Atomization of wet powder is
Due to the friction between the cooling humidifying medium and the action of the vibrating screen,
This is done by passing wet powder through a screen, while clogging is prevented by the rattling action of the medium on the screen surface. The wet fine powder that has passed through the screen is conveyed by airflow by an air ejector, and is used in the trench without forming into aggregates.
次に本発明装置の一実施例を図面に基づいて説明する。 Next, one embodiment of the device of the present invention will be described based on the drawings.
第1〜2図において、振動コンベア01と振動スクリー
ン02を組合わせ、振動コンベヤ01部は乾き反応剤0
9と処理tn、体10の受入部A、 B、 Cとそれら
の混合部りを有する。受入部A、 B、 Cは乾き反応
剤09を処理媒体層間にはさみ込み、混合部りではトラ
フ巾を拡大して層厚を薄くすると同時に反応剤09が媒
体10と混合され、媒体面が反応剤09でコーティング
される。In Figures 1 and 2, a vibrating conveyor 01 and a vibrating screen 02 are combined, and the vibrating conveyor 01 has no dry reactant.
9, a processing section tn, a receiving section A, B, and C of the body 10, and a mixing section thereof. In the receiving parts A, B, and C, the dry reactant 09 is sandwiched between the layers of the processing medium, and in the mixing part, the trough width is expanded to reduce the layer thickness, and at the same time, the reactant 09 is mixed with the medium 10, and the medium surface is reacted. Coated with agent 09.
微動スクリーン部Eでは媒体面にコーティングされた減
温加湿反応剤がヌクリーンの振動と媒体10同志の衝突
により、微粒状にはがされ。In the micro-movement screen section E, the temperature-reducing and humidifying reactant coated on the medium surface is peeled off into fine particles due to the vibration of NuClean and the collision of the medium 10 with each other.
スクリーン02を通過する。Pass through screen 02.
媒体10は反応剤09をはがされ、振動スクリーン02
網トを移動し、水槽07に排出される。The medium 10 is stripped of the reactant 09 and passed through the vibrating screen 02
The net is moved and discharged into the water tank 07.
水槽07には定量的に媒体10をかきLげる装置06が
取付けられており、水切りされて付着水のみを保有した
媒体10が前記振動コンベヤ024゜流部に、乾き反応
剤09をはさみ込むように2ケ所に分けられて供給され
る。A device 06 for quantitatively scraping the medium 10 is attached to the water tank 07, and the medium 10 that has been drained and retains only attached water is sandwiched with the dry reactant 09 in the flow section of the vibrating conveyor 024°. It is divided into two places and supplied.
微粒化した湿り反応剤は空気エジェクタにより所定の場
所に搬送される。The atomized wetness reactant is conveyed to a predetermined location by an air ejector.
本装置は以」二の構成となっている。This device has the following two configurations.
(1ン滅温加湿媒体間に乾き反応剤を供給するので振動
混合が効果的に行なわれる。(Vibration mixing is effective because the dry reactants are fed between 1 liter of sterilized humidified media.
(2)減温加湿媒体間の摩擦と該媒体のスクリン而への
タタキ作用により、スクリーンの目詰りを防止し、微粒
な湿り反応剤が得られる。(2) Due to the friction between the temperature-reduced humidifying medium and the tapping action of the medium on the screen, clogging of the screen can be prevented and fine particles of the moisturizing reaction agent can be obtained.
(3ン饋粒にした湿り反応剤を排ガス中に連続して供給
出来る。(The wetting reactant can be continuously fed into the exhaust gas in the form of 3 granules.
第1図および第2図は本発明装置の一実施例を示す縦断
立面図及び平面図である。
01・・・摂動コンベヤ、02・・・振動スクリーン。
03・・・エキスパンションジヨイント、04・・・微
粒湿り反応剤とエヤの混合部、 05・・・エジェクタ
。
06・・・媒体かきトげ装置、07・・・水槽、08・
・・乾き反応剤定量供給装置、09・・・反応剤。1 and 2 are a longitudinal sectional elevational view and a plan view showing an embodiment of the apparatus of the present invention. 01... Perturbation conveyor, 02... Vibration screen. 03... Expansion joint, 04... Mixing part of fine moisture reactant and air, 05... Ejector. 06... Medium scraping device, 07... Water tank, 08...
... Dry reactant quantitative supply device, 09... Reactant.
Claims (1)
両者を分離する振動混合スクリーン装置と、分離された
減温加湿媒体を一旦水槽に落したのち水切りして前記振
動混合スクリーン装置の上流側に供給する減温加湿媒体
循環供給装置と、分離された加湿微粉の搬送装置と、乾
き粉体を前記振動混合スクリーン装置の上流側に供給す
る乾き粉体定量供給装置とから成ることを特徴とする粉
体の加湿微粒化装置。A vibrating mixing screen device that mixes granular temperature-reduced humidifying medium and dry powder and separates the two on the downstream side; and a vibrating mixing screen device that mixes the granular temperature-reducing humidifying medium and dry powder and separates the two on the downstream side, and once drops the separated temperature-reducing humidifying medium into a water tank and then drains it. It consists of a temperature-reduced humidifying medium circulation supply device that supplies the upstream side of the device, a conveyance device for the separated humidified fine powder, and a dry powder quantitative supply device that supplies the dry powder to the upstream side of the vibrating mixing screen device. A humidifying and atomizing device for powder, which is characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61186563A JPS6342722A (en) | 1986-08-08 | 1986-08-08 | Humidifying and atomizing device for powder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61186563A JPS6342722A (en) | 1986-08-08 | 1986-08-08 | Humidifying and atomizing device for powder |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6342722A true JPS6342722A (en) | 1988-02-23 |
Family
ID=16190716
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61186563A Pending JPS6342722A (en) | 1986-08-08 | 1986-08-08 | Humidifying and atomizing device for powder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6342722A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5217579A (en) * | 1991-02-21 | 1993-06-08 | Toyota Kagaku Kogyo Kabushiki Kaisha | Distillation system for treating waste organic solvent |
-
1986
- 1986-08-08 JP JP61186563A patent/JPS6342722A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5217579A (en) * | 1991-02-21 | 1993-06-08 | Toyota Kagaku Kogyo Kabushiki Kaisha | Distillation system for treating waste organic solvent |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4319890A (en) | Dry impact capture of aerosol particulates | |
AU692014B2 (en) | Method for separating gaseous pollutants from hot process gases | |
JP2009072730A (en) | Dust collector having powder mixing treatment means and powder mixing treatment method | |
US4446109A (en) | System for dry scrubbing of flue gas | |
JPH0462766B2 (en) | ||
US4317806A (en) | Method and apparatus for dedusting and absorption of contaminating gases being the exhaust gases of waste-incinerating devices and hot-air cupola furnaces | |
CN107789973A (en) | A kind of flue gas of sintering machine dust collecting process and device | |
JPS6342722A (en) | Humidifying and atomizing device for powder | |
US4078041A (en) | Electrofluidized bed gas purification arrangement and method | |
FI83166B (en) | RENINGSMETOD FOER ROEKGASER OCH ANLAEGGNING FOER RENING AV ROEKGASER. | |
JPH01155936A (en) | Apparatus for removing acidic component from waste gas of dust incineration furnace | |
US4229189A (en) | Pollution control apparatus and method | |
JPS60216832A (en) | Purification of waste gas by dry lime process | |
CN106390651A (en) | Integrated tail gas and waste powder treating apparatus of complete set of equipment for regeneration and stirring of asphalt | |
JPS6216169Y2 (en) | ||
EP0095459B1 (en) | Process and system for dry scrubbing of flue gas | |
JP2004150683A (en) | Method and device for transporting refuse incineration fly ash | |
CN214809826U (en) | Desulfurization equipment | |
CN215864641U (en) | Sintering primary mixer dust treatment system based on belt optimization | |
CA2052044C (en) | Method for flyash recycling in a dry so2 scrubber | |
JP3395036B2 (en) | Method and apparatus for removing acid gas from exhaust gas | |
CN207224254U (en) | Fibre cement product process units and integral system | |
AU545580B2 (en) | Process and system for dry scrubbing of flue gas | |
JPS61133122A (en) | Method and device for neutralizing and separating injurious material in flue gas and exhaust gas | |
JPS6327076B2 (en) |