JPS5844317Y2 - heating rotary furnace - Google Patents

heating rotary furnace

Info

Publication number
JPS5844317Y2
JPS5844317Y2 JP9490880U JP9490880U JPS5844317Y2 JP S5844317 Y2 JPS5844317 Y2 JP S5844317Y2 JP 9490880 U JP9490880 U JP 9490880U JP 9490880 U JP9490880 U JP 9490880U JP S5844317 Y2 JPS5844317 Y2 JP S5844317Y2
Authority
JP
Japan
Prior art keywords
rotating body
processed
cylinder
mixing cylinder
rotary furnace
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
JP9490880U
Other languages
Japanese (ja)
Other versions
JPS5719397U (en
Inventor
尚男 北野
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP9490880U priority Critical patent/JPS5844317Y2/en
Publication of JPS5719397U publication Critical patent/JPS5719397U/ja
Application granted granted Critical
Publication of JPS5844317Y2 publication Critical patent/JPS5844317Y2/en
Expired legal-status Critical Current

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  • Drying Of Solid Materials (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Incineration Of Waste (AREA)

Description

【考案の詳細な説明】 この考案は、被処理物を加熱することにより、所望の化
学反応を起こさせたり、または被処理物を乾燥若しくは
焼却処理したりするための加熱回転炉に関する。
[Detailed Description of the Invention] This invention relates to a heating rotary furnace for causing a desired chemical reaction or drying or incineration of an object by heating the object.

従来、この種回転炉として、粘稠性の高い被処理物が筒
状回転体内壁に付着することにより起こる熱伝導の低下
等の弊害を防止するため、回転体内に内部逆送装置を備
えたものは知られている。
Conventionally, this type of rotary furnace was equipped with an internal reverse feed device inside the rotary body in order to prevent adverse effects such as a decrease in heat conduction caused by highly viscous processed materials adhering to the wall of the cylindrical rotary body. Things are known.

この逆送装置は、回転体内において加熱処理されて粘稠
性が低下し粉末又は顆粒状化した被処理物を回転体の入
口側に逆送し、該被処理物を外部から回転体内に送り込
まれる未加熱の被処理物に混合させて、未加熱の被処理
物の粘稠性を低下させて、被処理物が回転体内面に極力
付着しないようにするためのものである。
This reverse feeding device transports the processed material, which has been heat-treated in the rotating body to reduce its viscosity and become powder or granules, to the inlet side of the rotating body, and feeds the processed material from the outside into the rotating body. It is mixed with the unheated processed material to reduce the viscosity of the unheated processed material and prevent the processed material from adhering to the inner surface of the rotating body as much as possible.

然し乍ら、前記の工夫にも拘らず、従来の回転炉には、
次の如き欠点があった。
However, despite the above-mentioned innovations, conventional rotary furnaces have
It had the following drawbacks.

即ち、回転体内に送り込まれた未加熱の被処理物と逆送
された加熱処理途中の被処理物とは、回転体内面に別個
に落下し、回転体内を前方に向かって移動する間に、混
合されるものであったから、回転体内を所定距離移動し
ない限り、両者の十分な混合は行われなかった。
That is, the unheated workpiece sent into the rotating body and the workpiece that is being heated and sent back fall separately onto the inner surface of the rotating body, and while moving forward inside the rotating body, Since they were mixed together, sufficient mixing of the two was not achieved unless the two were moved a predetermined distance within the rotating body.

従って、回転体の入口近くの内面に被処理物が付着する
のを所期の目的の通りに防止することは出来ないという
欠点があった。
Therefore, there is a drawback that it is not possible to prevent the object to be treated from adhering to the inner surface near the inlet of the rotating body as intended.

この考案は、上記欠点を解決すると共に、反応効率や処
理効率を高めることのできる加熱回転炉を提供すること
を目的とするものである。
The purpose of this invention is to provide a heating rotary furnace that can solve the above-mentioned drawbacks and improve reaction efficiency and treatment efficiency.

以下に、この考案を図面に示す実施例に基づいて説明す
る。
This invention will be explained below based on embodiments shown in the drawings.

なお、この明細書において、前とは第1図右側を、後と
は同図左側をいう。
In this specification, the front refers to the right side in FIG. 1, and the rear refers to the left side in the same figure.

第1図に示す如く、燃焼炉1内に、軸心を前方下り傾斜
となるようにして、筒体回転体2が回転自在に嵌められ
ており、該回転体2の全長は図示された長さの倍程ある
と共に、その前後部は燃焼炉1より前後方向に稍々突出
しており、更に、同前端には処理完了の被処理物のため
の排出口を有する前端鏡板(図示略)が取付けられ、他
方、同後端には大きな貫通孔3を有する後端鏡板4が取
付けられている。
As shown in FIG. 1, a cylindrical rotating body 2 is rotatably fitted into a combustion furnace 1 with its axis slanting forward and downward, and the total length of the rotating body 2 is the length shown in the figure. Its front and rear parts protrude slightly from the combustion furnace 1 in the front-rear direction, and there is also a front head plate (not shown) at the front end that has a discharge port for the processed material. On the other hand, a rear end mirror plate 4 having a large through hole 3 is attached to the rear end.

前記貫通孔3に前端部が嵌まり込むかたちで、回転体2
内の加熱ガスの排出口5を有する固定ジャケット6が設
けられた、該固定ジャケット6の後壁には、これを貫通
して回転体2内に突出した被処理物供給筒7が設けられ
、該供給筒7内には、粘稠性の高い被処理物を正確に回
転体2内に供給するためのスクリューコンベア8が収め
られている。
The rotating body 2 is inserted into the through hole 3 with its front end fitted into the through hole 3.
A fixed jacket 6 having a heating gas outlet 5 therein is provided, and a workpiece supply cylinder 7 extending through the fixed jacket 6 and protruding into the rotating body 2 is provided on the rear wall of the fixed jacket 6. A screw conveyor 8 is housed within the supply cylinder 7 for accurately feeding a highly viscous workpiece into the rotating body 2.

前記回転体2の前後方向中央部には、被処理物を回転体
2の後半部2aを溜めるための環状堰9が設けられ、該
環状堰9より後方の回転体2の部分、即ち後半部2a内
には、内部逆送装置10が設けられている。
An annular weir 9 is provided at the center of the rotary body 2 in the front-rear direction for storing the object to be processed in the rear half 2a of the rotary body 2. An internal reversing device 10 is provided within 2a.

該逆送装置10の逆送筒11は、所要本の支持棒12を
介して、その軸心を回転体2の軸心と一致させるように
して回転体2に固定されており、該逆送筒11内には、
1条以上の逆送用スクリューコンベア13が固着されて
おり、該スクリューコンベア13は、回転体2が第2図
において時計方向に回転することにより、それと共に回
転し逆送筒11内に入った被処理物を逆送するためのも
のである。
The reverse feed tube 11 of the reverse feed device 10 is fixed to the rotating body 2 via a required number of support rods 12 so that its axis coincides with the axis of the rotating body 2. Inside the tube 11,
One or more threads of a reverse feed screw conveyor 13 are fixed, and as the rotating body 2 rotates clockwise in FIG. This is for transporting the processed material back.

前記逆送筒11の入口端(前端)には、開口部14を有
する円錐状壁15が固着され、鉄壁15の開口部14の
周縁には、第2図に示す如く、掬い上げダクト16が接
続され、その先端部は回転体2に固着されている。
A conical wall 15 having an opening 14 is fixed to the inlet end (front end) of the reverse feed cylinder 11, and a scooping duct 16 is provided around the periphery of the opening 14 of the iron wall 15, as shown in FIG. The distal end thereof is fixed to the rotating body 2.

該掬い上げダクト16は、第2図に示す如く、回転体2
の回転方向に対して先となる方の壁に掬い上げ口17を
有すると共に、該掬い上げ口17に被処理物が円滑に入
り込むように回転方向側に向かって傾斜している。
The scooping duct 16 is connected to the rotating body 2 as shown in FIG.
A scooping opening 17 is provided on the wall facing forward in the rotational direction, and the scooping opening 17 is inclined toward the rotational direction so that the object to be processed can smoothly enter the scooping opening 17.

逆送筒11の出口端(後端)には、光拡がりラッパ状の
混合筒18が、前記供給筒7を囲繞するかたちで設けら
れ、該混合筒18と逆送筒11との境には段部19が形
成されている。
At the outlet end (rear end) of the reverse feed tube 11, a light spreading trumpet-shaped mixing tube 18 is provided to surround the supply tube 7, and at the boundary between the mixing tube 18 and the reverse feed tube 11, A stepped portion 19 is formed.

前記混合筒18のテーパー状拡開の程度、長さ等は、被
処理物の粘稠度、回転体2の軸心の傾斜角度、回転体2
の回転速度等を勘案して、要するに、未加熱の被処理物
と加熱処理途中の被処理物とが、混合攪拌されるに十分
な時間、混合筒18内に滞留し得るように調節決定され
る。
The degree of tapered expansion, length, etc. of the mixing cylinder 18 depends on the viscosity of the material to be processed, the inclination angle of the axis of the rotating body 2, and the rotating body 2.
In short, the adjustment is made by taking into consideration the rotational speed of the mixing cylinder 18, etc., so that the unheated workpiece and the workpiece that is undergoing heat treatment can remain in the mixing cylinder 18 for a sufficient time to be mixed and stirred. Ru.

この実施例では、前記混合筒18の出口端の外径を大き
くして、可及的に回転体2に近づけて、被処理物が混合
筒18から回転体2内面に落下した際に発生する飛散ダ
ストを極力少くして、加熱ガス内に混入するダスト量を
少くしている。
In this embodiment, the outer diameter of the outlet end of the mixing cylinder 18 is increased to bring it as close to the rotating body 2 as possible, so that the problem occurs when the material to be processed falls from the mixing cylinder 18 onto the inner surface of the rotating body 2. Scattered dust is minimized to reduce the amount of dust mixed into the heated gas.

以下に、前記回転炉の作用について説明する。The operation of the rotary furnace will be explained below.

運転開始時から定常運転状態になるまでは、回転体2内
の状態、例えば回転体2内に運転停止した際の被処理物
が残留しているとか、回転体2内が全くの空であるとか
の状態に応じて、粘稠性の低い粉末又は顆粒化した被処
理物を、スクリューコンベア8又は該コンベア8を抜き
取って供給能力の高い別個のコンベアによって回転体2
内に供給する。
From the start of operation until the steady state of operation is reached, the condition inside the rotating body 2 is determined, for example, if the object to be processed remains in the rotating body 2 when the operation was stopped, or if the inside of the rotating body 2 is completely empty. Depending on the situation, the powder with low viscosity or the granulated material to be processed is transferred to the rotary body 2 by the screw conveyor 8 or by a separate conveyor with a high supply capacity after extracting the conveyor 8.
supply within.

このような過渡的な運転を経て定常運転状態に至った後
、スクリューコンベア8に粘稠性の高い被処理物を供給
すると、回転体2内に突出した供給筒7の前端から未加
熱の被処理物が混合筒18内に落下する。
After such a transient operation reaches a steady state of operation, when a highly viscous material is fed to the screw conveyor 8, unheated material flows from the front end of the supply tube 7 protruding into the rotating body 2. The processed material falls into the mixing cylinder 18.

ところが、混合筒18の内面下部は、逆送された被処理
物、即ち、すでに加熱処理されて粘稠性の低下した粉末
又は顆粒状等の被処理物によって被覆されたようになっ
ているので、未加熱の被処理物はその上に落下して、は
とんど混合筒18の内面に付着することはない。
However, the lower inner surface of the mixing cylinder 18 is coated with the processed material that has been sent back, that is, the processed material that has already been heat-treated and whose viscosity has decreased, such as powder or granules. , the unheated material to be processed falls onto it and rarely adheres to the inner surface of the mixing cylinder 18.

而して、逆送された被処理物と未加熱の被処理物とは、
ラッパ状の混合筒18の回転、即ち、回転体2の回転に
伴って、混合筒18内面を、混合されながら後方に移動
し、十分に混合された状態で、回転体2の内面に落下す
る。
Therefore, the processed material that has been sent back and the unheated processed material are
As the trumpet-shaped mixing cylinder 18 rotates, that is, as the rotating body 2 rotates, the inner surface of the mixing cylinder 18 moves backward while being mixed, and falls onto the inner surface of the rotating body 2 in a sufficiently mixed state. .

この回転体2の内面に落下した被処理物は、その内面に
はほとんど付着しない状態になっているので、回転体2
の回転に伴って、その内面に付着することなく、従って
燃焼炉1からの熱を効率よく吸収しながら、前方にスム
ーズに移動して行く。
The object to be processed that has fallen onto the inner surface of the rotating body 2 is hardly attached to the inner surface, so the rotating body 2
As it rotates, it smoothly moves forward without adhering to its inner surface, thus efficiently absorbing heat from the combustion furnace 1.

そして、環状堰9の位置近くまで前進した被処理物の一
部は、第2図に示す如く、回転体2の回転に伴って掬い
上げ口17、掬い上げダクト16、円錐状壁15を経て
、逆送筒11に送り込まれ、逆送用スクリューコンベア
13の作用により、混合筒18に逆送される。
Then, as shown in FIG. 2, a part of the material to be treated that has advanced close to the position of the annular weir 9 passes through the scooping opening 17, the scooping duct 16, and the conical wall 15 as the rotating body 2 rotates. , is fed into the reverse feed cylinder 11, and is fed back to the mixing cylinder 18 by the action of the reverse screw conveyor 13.

逆送された被処理物は、前記の如く、再び回転体2の内
面に落下する。
The object to be processed that has been sent back falls onto the inner surface of the rotating body 2 again as described above.

他方、被処理物の残りは、環状堰9を越えて更に前方に
進みつ・、加熱処理されて、回転体2の前端に至り、所
定の手段により回転体2外に排出される。
On the other hand, the remainder of the material to be treated passes further forward beyond the annular weir 9, is heated, reaches the front end of the rotating body 2, and is discharged from the rotating body 2 by a predetermined means.

定常運転状態にあっては、以上の作用が連続的に繰り返
されるものである。
In a steady state of operation, the above actions are repeated continuously.

なお、年に1乃至2回程しか運転を停止することはない
が、その際にはスクリューコンベア8による被処理物の
供給を停止した後、回転炉の運転を所定時間続行した後
停止し、要すれば、所定手段により回転体2内の被処理
物を回転体2から排出する。
Although the operation is only stopped once or twice a year, in that case, after stopping the supply of the material to be processed by the screw conveyor 8, the operation of the rotary furnace is continued for a predetermined period of time and then stopped. Then, the object to be processed inside the rotating body 2 is discharged from the rotating body 2 by a predetermined means.

以上の説明から明かなように、この考案の回転炉は被処
理物が回転体2の内面に付着することを防止出来るのみ
ならず、被処理物を循環させて処理効率や反応効率も高
めることが出来るものであるから、被処理物が粘稠性の
高いものに限定されないことは勿論である。
As is clear from the above explanation, the rotary furnace of this invention not only prevents the objects to be treated from adhering to the inner surface of the rotating body 2, but also improves processing efficiency and reaction efficiency by circulating the objects. Of course, the material to be treated is not limited to highly viscous materials.

また、掬い上げダクト16の数は、−任意である。Further, the number of scooping ducts 16 is - arbitrary.

以上の次第で、この考案によれば、内部逆送装置の逆送
筒の出口端に、光拡がりラッパ状の混合筒が、回転体内
に突出した被処理物供給筒を囲繞するかたちで設けられ
ているものであるがら、混合筒内において、未加熱の被
処理物と加熱されて粉末又は顆粒状化した被処理物とが
十分に混合攪拌されて、即ち、粘稠性の低下した状態と
なって、回転体内面に落下するものであるから、従来の
回転炉に比較して、回転体内面に付着する被処理物の量
を極めて少なくすることが出来る。
Based on the above, according to this invention, a light spreading trumpet-shaped mixing cylinder is provided at the outlet end of the reverse transport cylinder of the internal reverse transport device so as to surround the processing material supply cylinder protruding into the rotating body. However, in the mixing cylinder, the unheated processed material and the heated powdered or granulated processed material are sufficiently mixed and stirred, that is, the viscosity is reduced. Since the material falls onto the inner surface of the rotating body, the amount of material to be treated that adheres to the inner surface of the rotating body can be extremely reduced compared to conventional rotary furnaces.

また、未加熱の被処理物が、混合筒の内面の加熱処理さ
れた被処理物の上に落下するものであるから、被処理物
が混合筒内面に付着することもほとんどない。
Further, since the unheated material to be processed falls onto the heat-treated material on the inner surface of the mixing cylinder, the material to be processed hardly adheres to the inner surface of the mixing cylinder.

更に、混合筒内で被処理物と既加熱の被処理物とを予混
合して、回転体内に供給するものであるから、回転体で
の処理効率や反応効率を高めることが出来る。
Furthermore, since the material to be treated and the heated material to be treated are premixed in the mixing cylinder and then supplied into the rotating body, the processing efficiency and reaction efficiency in the rotating body can be improved.

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

図面はこの考案の実施例を示すものであって、第1図は
要部縦断面図、第2図は第1図II−II線断面図であ
る。 2・・・・・・筒状回転体、7・・・・・・被処理物供
給筒、10・・・・・・内部逆送装置、11・・・・・
・逆送筒、18・・・・・・混合筒。
The drawings show an embodiment of this invention, in which FIG. 1 is a vertical cross-sectional view of a main part, and FIG. 2 is a cross-sectional view taken along the line II--II in FIG. 1. 2... Cylindrical rotating body, 7... Processed material supply cylinder, 10... Internal reverse feed device, 11...
・Reverse feed cylinder, 18...Mixing cylinder.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 筒状回転体の人口端部には、被処理物供給筒が回転体内
に突出状態に設けられると共に、前記回転体内の内部逆
送装置の逆送筒の出口端には、光拡がりラッパ状の混合
筒が、前記供給筒を囲繞するかたちで設けられているこ
とを特徴とする加熱回転炉。
At the artificial end of the cylindrical rotating body, a to-be-processed material supply tube is provided to protrude into the rotating body, and at the outlet end of the reverse feeding tube of the internal reverse feeding device within the rotating body, a light spreading trumpet-shaped tube is provided. A heating rotary furnace characterized in that a mixing cylinder is provided to surround the supply cylinder.
JP9490880U 1980-07-04 1980-07-04 heating rotary furnace Expired JPS5844317Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9490880U JPS5844317Y2 (en) 1980-07-04 1980-07-04 heating rotary furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9490880U JPS5844317Y2 (en) 1980-07-04 1980-07-04 heating rotary furnace

Publications (2)

Publication Number Publication Date
JPS5719397U JPS5719397U (en) 1982-02-01
JPS5844317Y2 true JPS5844317Y2 (en) 1983-10-07

Family

ID=29456823

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9490880U Expired JPS5844317Y2 (en) 1980-07-04 1980-07-04 heating rotary furnace

Country Status (1)

Country Link
JP (1) JPS5844317Y2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH047301Y2 (en) * 1985-03-29 1992-02-26
JPH0220608U (en) * 1988-07-18 1990-02-09

Also Published As

Publication number Publication date
JPS5719397U (en) 1982-02-01

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