JPS6342722A - Humidifying and atomizing device for powder - Google Patents

Humidifying and atomizing device for powder

Info

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
Application number
JP61186563A
Other languages
Japanese (ja)
Inventor
Narimoto Tomizawa
富澤 成元
Hiroshi Fukushima
寛 福島
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP61186563A priority Critical patent/JPS6342722A/en
Publication of JPS6342722A publication Critical patent/JPS6342722A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently perform the treatment of a reactive agent for enhancing reaction efficiency by allowing a desuperheating and humidifying medium to once fall in a water tank and thereafter draining it and feeding it together with dry powder to a vibratory mixing screen device and separating both and carrying dry powder. CONSTITUTION:A dry reactive agent 9 and a treating medium 10 are introduced into receiving parts A, B, C of a vibrating conveyer 1. In a mixing part D, the width of a draff is enlarged and the layer thickness is made thin and simultaneously the reactive agent 9 is mixed with the medium 10 and the surface of the medium is coated with the reactive agent 9. In the vibrating screen part E, the reactive agent coated on the surface of the medium is peeled in a particulate shape by collision or the like and passed through a screen 2 and the medium 10 is discharged to a water tank 7 and quantitatively scraped up with a scraper 6, drained and thereafter fed to a vibrating conveyer 1.

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.

〔従来の技術〕[Conventional technology]

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.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

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.

〔問題点を解決するための手段〕[Means for solving problems]

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.

〔作用〕[Effect]

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.

〔実施例〕〔Example〕

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.

〔発明の効果〕〔Effect of the invention〕

(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.

【図面の簡単な説明】[Brief explanation of the drawing]

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)

【特許請求の範囲】[Claims]  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、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:
JP61186563A 1986-08-08 1986-08-08 Humidifying and atomizing device for powder Pending JPS6342722A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (1)

* Cited by examiner, † Cited by third party
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

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