JPS5936273Y2 - gas treatment equipment - Google Patents

gas treatment equipment

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Publication number
JPS5936273Y2
JPS5936273Y2 JP18946781U JP18946781U JPS5936273Y2 JP S5936273 Y2 JPS5936273 Y2 JP S5936273Y2 JP 18946781 U JP18946781 U JP 18946781U JP 18946781 U JP18946781 U JP 18946781U JP S5936273 Y2 JPS5936273 Y2 JP S5936273Y2
Authority
JP
Japan
Prior art keywords
substance
reaction section
main reaction
conduit
gas treatment
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
Application number
JP18946781U
Other languages
Japanese (ja)
Other versions
JPS5895230U (en
Inventor
重幸 佐々木
Original Assignee
ガデリウス株式会社
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 ガデリウス株式会社 filed Critical ガデリウス株式会社
Priority to JP18946781U priority Critical patent/JPS5936273Y2/en
Publication of JPS5895230U publication Critical patent/JPS5895230U/en
Application granted granted Critical
Publication of JPS5936273Y2 publication Critical patent/JPS5936273Y2/en
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は粉末状の第1物質と気体状の第2物質とを接触
させ、相互に反応させた後、反応物質を除去するガス処
理装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a gas treatment device that brings a powdered first substance and a gaseous second substance into contact, causes them to react with each other, and then removes the reactant.

従来のガス処理装置では、除去された反応物質中には、
未反応の第1物質が多く含まれており、それらはそのま
ま廃棄されることが多い。
In conventional gas treatment equipment, the removed reactants include:
It contains a large amount of unreacted primary substances, which are often discarded as is.

又、再利用されている場合でも、未反応の第1物質と反
応物質との混合物質いわゆる捕集物質の供給方法や供給
箇所が適切でないために閉塞等の問題が生じ、装置の円
滑な運転に支障を来すこともある。
In addition, even if it is reused, problems such as blockage may occur due to inappropriate supply methods and locations of the mixed substance of unreacted first substance and reactant, so-called collection substance, which may hinder the smooth operation of the equipment. It may also cause problems.

本考案ではかかる欠点をなくするため、捕集物質を再利
用のために連続的に供給出来る装置を備えた新規なるガ
ス処理装置を提供するものである。
In order to eliminate such drawbacks, the present invention provides a new gas processing apparatus equipped with a device capable of continuously supplying collected substances for reuse.

次に図を用いて説明する。Next, it will be explained using figures.

第1図は従来のガス処理装置を示しており、主反応部2
と2次反応部4とで構成されている。
Figure 1 shows a conventional gas treatment device, with main reaction section 2
and a secondary reaction section 4.

第1図において、粉末状の第1物質はブロワ10により
送られて来た圧縮空気により第1物質貯蔵タンク11か
らロータリーフィーダ12を介して定量の第1物質を気
体輸送にて、気体状の第2物質が流れる導管1に供給口
13から供給され第2物質と共に主反応部2に流入する
In FIG. 1, a powdered first substance is produced by transporting a fixed amount of the first substance from a first substance storage tank 11 through a rotary feeder 12 using compressed air sent by a blower 10. The second substance is supplied to the conduit 1 through the supply port 13 and flows into the main reaction section 2 together with the second substance.

ここで、第1物質と第2物質の混合物質の速度は減速さ
れ該混合物質は矢印3に示す流動をしながら第1物質と
第2物質が接触しつつ相互に反応しながらサイクロン形
状の2次反応部4に流入する。
Here, the speed of the mixed substance of the first substance and the second substance is reduced, and the mixed substance flows as shown by arrow 3, and the first substance and the second substance are in contact with each other and react with each other, forming a cyclone shape. Next, it flows into the reaction section 4.

ここで、第1物質と第2物質との混合物質は接触しつつ
、相互に反応しながら下向のらせん流となり反応物質と
未反応の第1物質のある部分は分離された後、導管6を
通り高性能集じん機7及びブロワ8を経て煙突9から大
気に放出される。
Here, the mixed substance of the first substance and the second substance is in contact with each other and reacts with each other, forming a downward spiral flow, and the reactant and a certain portion of the unreacted first substance are separated, and then the conduit 6 The air passes through a high-performance dust collector 7 and a blower 8 before being released into the atmosphere from a chimney 9.

一方、2次反応部4にて捕集された反応物質及び未反応
の第1物質の混合物質いわゆる捕集物質は再利用のため
、ロータリーバルブ5を介して主反応部2の上流側導管
1に供給される。
On the other hand, the mixed substance of the reactant and unreacted first substance collected in the secondary reaction section 4, so-called collected material, is passed through the rotary valve 5 to the upstream conduit 1 of the main reaction section 2 for reuse. supplied to

この場合、導管1に供給された捕集物質は時には導管1
内に滞留し管を閉塞することもある。
In this case, the collection material supplied to conduit 1 is sometimes
It may stay inside the body and block the tube.

この閉塞問題を解決出来る実施例を第2図、第3図及び
第4図に示している。
Examples that can solve this blockage problem are shown in FIGS. 2, 3, and 4.

第2図、第3図及び第4図に示すごとく、2次反応部4
で捕集された捕集物質を第2図では、スクリューコンベ
ア14で、又、第3図では安息角以上の勾配を持ったシ
ュート15で又、第4図ではシュート16の上部より管
17を介して送られて来た圧縮空気を用いて気体輸送に
より、主反応部2の下部の第1物質供給口13の上部に
供給する方法を採用した。
As shown in FIGS. 2, 3 and 4, the secondary reaction section 4
The collected substances are conveyed by a screw conveyor 14 in FIG. 2, by a chute 15 with a slope greater than the angle of repose in FIG. A method was adopted in which the compressed air sent through the main reaction section 2 was supplied to the upper part of the first substance supply port 13 at the lower part of the main reaction part 2 by gas transport.

これらの方法を用いることにより、第1図に示す従来の
方法で問題となった導管1内での捕集物質による閉塞等
が防止出来、且つ、第1物質供給口13の先端部に逆円
錐形状の第1物質拡散錐19を配置することにより空気
輸送された第1物質が導管1で導入された第2物質の気
流に同伴し、充分な接触時間及び接触回数を得ることが
でき、従って反応率を増大する。
By using these methods, it is possible to prevent blockage caused by the collected substances in the conduit 1, which was a problem with the conventional method shown in FIG. By arranging the shaped first substance diffusion cone 19, the air-transported first substance is entrained in the airflow of the second substance introduced through the conduit 1, and sufficient contact time and number of contacts can be obtained. Increase reaction rate.

又、第1物質の供給箇所が第1図に示す主反応部2の上
流側の導管1内の供給口13と同じであっても捕集物質
の供給箇所が第2図、第3図、及び第4図に示す箇所、
即ち、主反応部2の下部であればガス処理装置の性能及
び運転にも何ら影響を及ぼさないことも確認された。
Furthermore, even if the supply point of the first substance is the same as the supply port 13 in the conduit 1 on the upstream side of the main reaction section 2 shown in FIG. and the location shown in Figure 4,
In other words, it was confirmed that the performance and operation of the gas treatment apparatus would not be affected in any way if it was located at the lower part of the main reaction section 2.

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

第1図は従来のガス処理装置の説明図であり、第2図、
第3図、第4図は本考案の実施例を示す説明図である。 尚、図中の主要部の符号は次の通りである。 1・・・・・・導管、2・・・・・・主反応部、3・・
・・・・第1物質と第2物質と捕集物質との混合物質の
流動方向、4・・・・・・2次反応部、5・・・・・・
ロータリーバルブ、6・・・・・・導管、7・・・・・
・高性能集じん機、8・・・・・・ブロワ、9・・・・
・・煙突、10・・・・・・ブロワ、11・・・・・・
第1物質貯蔵タンク、12・・・・・・ロータリーバル
ブ、13・・・・・・第1物質供給口、14・・・・・
・スクリューコンベヤー、15・・・・・・シュート、
16・・・・・・シュート、17・・・・・・管、18
・・・・・・清掃用孔、19・・・・・・逆円錐形状の
第1物質拡散錐。
FIG. 1 is an explanatory diagram of a conventional gas treatment device, and FIG.
FIG. 3 and FIG. 4 are explanatory diagrams showing an embodiment of the present invention. Incidentally, the symbols of the main parts in the figure are as follows. 1... Conduit, 2... Main reaction part, 3...
. . . Flow direction of the mixed substance of the first substance, the second substance, and the collection substance, 4 . . . Secondary reaction section, 5 .
Rotary valve, 6... Conduit, 7...
・High performance dust collector, 8...Blower, 9...
...Chimney, 10...Blower, 11...
First substance storage tank, 12...Rotary valve, 13...First substance supply port, 14...
・Screw conveyor, 15...Chute,
16... Chute, 17... Tube, 18
. . . Cleaning hole, 19 . . . Inverted cone-shaped first substance diffusion cone.

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] (1)粉末状の第1物質と気体状の第2物質とを接触さ
せ、相互に反応させて、未反応の第1物質及び第1物質
と第2物質との反応生成物を除去するガス処理装置に於
て、主反応部とこれに後置する2次反応部より構成され
ること、2次反応部をサイクロン形状とすること、第2
物質を供給する導管に主反応部を接続すること並びに2
次反応部にて捕集された未反応の第1物質を含む物質を
再利用するに際して、該物質を主反応部下部に供給し、
且つ、第1物質の供給を主反応部下部の円錐形状内に供
給することを特徴とするガス処理装置。
(1) A gas that brings a powdered first substance and a gaseous second substance into contact, causes them to react with each other, and removes unreacted first substance and reaction products between the first substance and the second substance. The processing equipment is composed of a main reaction section and a secondary reaction section disposed after it, the secondary reaction section is shaped like a cyclone, and a second reaction section is provided.
connecting the main reaction section to a conduit supplying the substance; and 2.
When reusing the substance containing the unreacted first substance collected in the next reaction part, supplying the substance to the lower part of the main reaction part,
A gas processing apparatus characterized in that the first substance is supplied into a conical shape at the bottom of the main reaction section.
(2)第1物質の供給を主反応部上流側導管内に行うこ
とを特徴とする実用新案登録請求の範囲第1項記載のガ
ス処理装置。
(2) The gas treatment apparatus according to claim 1, wherein the first substance is supplied into the conduit on the upstream side of the main reaction section.
JP18946781U 1981-12-21 1981-12-21 gas treatment equipment Expired JPS5936273Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18946781U JPS5936273Y2 (en) 1981-12-21 1981-12-21 gas treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18946781U JPS5936273Y2 (en) 1981-12-21 1981-12-21 gas treatment equipment

Publications (2)

Publication Number Publication Date
JPS5895230U JPS5895230U (en) 1983-06-28
JPS5936273Y2 true JPS5936273Y2 (en) 1984-10-05

Family

ID=30103362

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18946781U Expired JPS5936273Y2 (en) 1981-12-21 1981-12-21 gas treatment equipment

Country Status (1)

Country Link
JP (1) JPS5936273Y2 (en)

Also Published As

Publication number Publication date
JPS5895230U (en) 1983-06-28

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