JP3522083B2 - Method and apparatus for controlling rotary kiln incinerator - Google Patents

Method and apparatus for controlling rotary kiln incinerator

Info

Publication number
JP3522083B2
JP3522083B2 JP12612297A JP12612297A JP3522083B2 JP 3522083 B2 JP3522083 B2 JP 3522083B2 JP 12612297 A JP12612297 A JP 12612297A JP 12612297 A JP12612297 A JP 12612297A JP 3522083 B2 JP3522083 B2 JP 3522083B2
Authority
JP
Japan
Prior art keywords
rotary kiln
incinerator
kiln
furnace
outlet
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 - Fee Related
Application number
JP12612297A
Other languages
Japanese (ja)
Other versions
JPH10318677A (en
Inventor
一弘 東村
聰 和田
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP12612297A priority Critical patent/JP3522083B2/en
Publication of JPH10318677A publication Critical patent/JPH10318677A/en
Application granted granted Critical
Publication of JP3522083B2 publication Critical patent/JP3522083B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Incineration Of Waste (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明はロータリーキルン
式焼却炉の制御方法及びその装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a rotary kiln type incinerator control method and apparatus.

【0002】[0002]

【従来の技術】ゴミ焼却設備としてロータリーキルンを
備えた焼却設備が知られている。この種焼却の一例とし
て図2に示すように、ゴミ投入口1をロータリーキルン
2の一端に設け、このキルン2の他端にストーカ炉3を
設けてなるロータリーキルン式焼却炉4が知られてい
る。
2. Description of the Related Art An incinerator equipped with a rotary kiln is known as a refuse incinerator. As an example of this kind of incineration, as shown in FIG. 2, a rotary kiln incinerator 4 is known in which a dust inlet 1 is provided at one end of a rotary kiln 2 and a stoker oven 3 is provided at the other end of the kiln 2.

【0003】即ち、上記焼却炉4において、投入口1か
らロータリーキルン2内に投入された処理物は、キルン
自身の回転によって炉内で転動あるいは滑動させられ
る。一方、ロータリーキルン2は出口側が僅かに低くな
る傾斜を持たせて設置されるので、その回転運動によっ
て処理物は少しづつ投入口1から出口側2Aへと搬送さ
れその間に燃焼空気と反応して焼却される。
That is, in the incinerator 4, the processed material charged into the rotary kiln 2 from the charging port 1 is rolled or slid in the furnace by the rotation of the kiln itself. On the other hand, since the rotary kiln 2 is installed with an inclination such that the outlet side is slightly lowered, the rotary motion thereof causes the processed material to be gradually conveyed from the input port 1 to the outlet side 2A and reacts with the combustion air in the meantime to be incinerated. To be done.

【0004】従って、上記ロータリーキルン式焼却炉で
は、処理物の燃焼速度に応じてキルン2の終端に達する
までに処理物が燃え尽きるよう、回転数を操作して処理
物のキルン内での滞留時間を調節し、さらに、最終的に
ストーカ炉3で後燃焼を行うので、極めて焼却性の高い
処理が可能となる。
Therefore, in the above rotary kiln type incinerator, the number of rotations is manipulated so that the residence time in the kiln is controlled by operating the rotation speed so that the treatment material burns out by the end of the kiln 2 according to the burning speed of the treatment object. Since it is adjusted, and after-burning is finally performed in the stoker furnace 3, it is possible to perform treatment with extremely high incineration.

【0005】このように上記焼却炉4はキルン2とスト
ーカ炉の、それぞれの炉が持つ特性が発揮できるように
構成されているため、感染性医療廃棄物、廃プラスチッ
ク、廃油、廃液、汚泥など殆どの産業廃棄物の処理が可
能である利点を有する。
As described above, since the incinerator 4 is constructed so that the characteristics of the kiln 2 and the stoker furnace can be exhibited, infectious medical waste, waste plastic, waste oil, waste liquid, sludge, etc. It has the advantage that most industrial waste can be treated.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上記処
理物のキルン内での滞留時間は、ロータリーキルンの回
転数の操作量よりも、クリンカ付着により生じるキルン
表面の摩擦状況の影響を強く受ける。
However, the residence time of the treated material in the kiln is more affected by the frictional condition of the kiln surface caused by clinker adhesion than the manipulated variable of the rotational speed of the rotary kiln.

【0007】従って、ロータリーキルンの運転を数十日
といった長期間連続運転していくとクリンカ付着により
処理物は次第に流動しにくくなり、送り性能は徐々に小
さくなっていく。
Therefore, when the rotary kiln is continuously operated for a long period of time, such as several tens of days, the processed material gradually becomes hard to flow due to the clinker adhesion, and the feeding performance gradually decreases.

【0008】この送り性能の低下を防ぐために、従来で
はキルンの回転数を大きくする操作が行われているが、
回転数の上下限値の巾は予め決まっており、従って、処
理物の送り性能がある一定基準以下になれば、その時点
で炉の運転を停止してキルン内のクリンカを除去しなけ
ればならない。
In order to prevent the deterioration of the feeding performance, an operation of increasing the rotation speed of the kiln has been conventionally performed.
The range of the upper and lower limits of the number of revolutions is predetermined, so if the feed performance of the processed material falls below a certain standard, the operation of the furnace must be stopped at that point to remove the clinker in the kiln. .

【0009】従って、ロータリーキルンを備えた焼却炉
の連続可能な運転日数は他の焼却炉、例えばストーカ炉
や流動床炉等に比べて短い欠点があった。一方、クリン
カ除去作業を行うには、炉を安全な温度まで下げる必要
があり、冷却時間として通常は2〜3日を要し、その後
に除去作業を行うためその間焼却処理が完全に滞る問題
もあった。
Therefore, the incinerator equipped with the rotary kiln has a drawback that the number of continuous operating days is shorter than that of other incinerators such as a stoker furnace and a fluidized bed furnace. On the other hand, in order to perform the clinker removal work, it is necessary to lower the temperature of the furnace to a safe temperature, and it usually takes 2 to 3 days as a cooling time, and since the removal work is performed after that, there is a problem that the incineration process is completely delayed during that time. there were.

【0010】この発明は、上記問題点を解消することを
目的としてなされたものであり、クリンカの発生、成長
があっても焼却物の送り速度を一定以上に保つことを可
能として長時間連続運転を可能にするロータリーキルン
式焼却炉の制御方法及びその装置を得ることを目的とし
てなされたものである。
The present invention has been made for the purpose of solving the above problems, and it is possible to maintain the feed rate of the incinerated material at a certain level or higher even if clinker is generated or grown, and continuously operate for a long time. The object of the present invention is to obtain a method and an apparatus for controlling a rotary kiln incinerator that enables the above.

【0011】[0011]

【課題を解決するための手段】請求項1のロータリーキ
ルン式焼却炉の制御方法は、ロータリーキルンを備えた
焼却装置において、連続処理時間の経過と共にロータリ
ーキルンの出口部の高さを次第に低くして投入口から出
口部への下降傾斜を大きくしていくことを特徴とするも
のである。
According to a first aspect of the present invention, there is provided a rotary kiln-type incinerator control method, wherein in an incinerator having a rotary kiln, the height of the outlet of the rotary kiln is gradually lowered as the continuous processing time elapses. It is characterized by increasing the descending inclination from the to the exit.

【0012】従って、キルンの回転数が上限に至っても
上記下降傾斜により焼却物の送り性能が維持されるた
め、クリンカの堆積があっても燃焼の継続が可能とな
る。請求項2のロータリーキルン式焼却炉の制御装置
は、ロータリーキルンを備えた焼却装置において、ロー
タリーキルンを回転自在に支持する架台を、前記ロータ
リーキルンの投入口側端を支点として水平軸周囲に回動
可能に支持し、前記架台の出口側端底部であって炉の熱
影響の少ない部位に、前記架台を上下動可能に支持する
駆動装置を設けたことを特徴とするものである。
Therefore, even if the number of rotations of the kiln reaches the upper limit, the descending inclination maintains the feeding performance of the incinerated matter, so that the combustion can be continued even if the clinker is accumulated. The control device for a rotary kiln type incinerator according to claim 2, wherein in a incinerator including a rotary kiln, a pedestal that rotatably supports the rotary kiln is supported rotatably around a horizontal axis with an end on the inlet side of the rotary kiln as a fulcrum. Further, a drive device for supporting the gantry so as to be movable up and down is provided at a bottom end portion of the gantry on the outlet side, which is less affected by heat in the furnace.

【0013】この装置は、請求項1の方法を実施する装
置であって、ロータリーキルンの傾斜角を調節可能に支
持したものである。
This device is a device for carrying out the method according to the first aspect of the present invention, in which the tilt angle of the rotary kiln is adjustable.

【0014】[0014]

【発明の実施の形態】次に、この発明の一実施の形態を
説明する。図1はロータリーキルンを備えた焼却炉の側
面図である。
BEST MODE FOR CARRYING OUT THE INVENTION Next, an embodiment of the present invention will be described. FIG. 1 is a side view of an incinerator equipped with a rotary kiln.

【0015】図1において、1はゴミ投入口、2はロー
タリーキルンを示す。このゴミ焼却炉4はロータリーキ
ルン2にストーカ炉3が連接され、ストーカ炉3の灰出
口に灰の分級機3Aが設けられている。
In FIG. 1, 1 is a dust input port and 2 is a rotary kiln. In this refuse incinerator 4, a stoker furnace 3 is connected to a rotary kiln 2, and an ash classifier 3A is provided at the ash outlet of the stoker furnace 3.

【0016】そして、ロータリーキルン2を回転自在に
支持する架台5を、前記ロータリーキルンの投入口側端
を支点5Aとして水平軸(図の紙背方向)周囲に回動可
能に支持し、前記架台5の出口側端底部5Bであって炉
2、3の熱影響の少ない部位に、前記架台5を矢印Pで
示すように上下動可能に支持する駆動装置6を設けて構
成されている。
The pedestal 5 for rotatably supporting the rotary kiln 2 is rotatably supported around the horizontal axis (paper spine direction in the figure) with the end on the inlet side of the rotary kiln as a fulcrum 5A, and the exit of the gantry 5 A drive device 6 for supporting the gantry 5 so as to be movable up and down as shown by an arrow P is provided at a side end bottom portion 5B where heat is less affected by the furnaces 2 and 3.

【0017】上記駆動装置6は図示のようにシリンダピ
ストンからなる油圧装置のほか、テコ或いはラックピニ
ヨンなどからなるリンク装置などが使用される。また図
において、5Cはロータリーキルン2を回転自在に支持
する駆動ロール、或いは空転支持ロールを示す。
As the drive device 6, a hydraulic device composed of a cylinder piston as shown in the drawing, and a link device composed of a lever or a rack and pinion are used. Further, in the figure, 5C indicates a drive roll for rotatably supporting the rotary kiln 2 or an idling support roll.

【0018】つぎに制御方法について説明する。投入口
1からロータリーキルン2へ焼却物を投入すれば、既述
のようにキルン自身の回転によって炉内で転動あるいは
滑動させられ、傾斜によって少しづつ投入口1から出口
側2Aへと搬送されその間に燃焼空気と反応して焼却さ
れる。
Next, the control method will be described. If the incinerator is charged into the rotary kiln 2 from the charging port 1, it is rolled or slid in the furnace by the rotation of the kiln itself as described above, and is gradually conveyed from the charging port 1 to the outlet side 2A by the inclination, while Is incinerated by reacting with combustion air.

【0019】長時間連続焼却によりクリンカが発生堆積
し、これにともなって処理物の送り速度が低下した場
合、当初はロータリーキルン2の回転数を上昇させ送り
速度を補償するが、回転数上昇が上限に達し回転数によ
る調整が出来なくなった場合、駆動装置6を駆動しロー
タリーキルン2の傾斜角を大きくする。
When a clinker is generated and accumulated due to continuous incineration for a long time, and the feed rate of the processed material is reduced accordingly, the rotation speed of the rotary kiln 2 is initially increased to compensate the feed speed, but the increase in the rotation speed is the upper limit. When it becomes impossible to adjust the rotation speed, the driving device 6 is driven to increase the inclination angle of the rotary kiln 2.

【0020】従って、この傾斜角の増加により送り速度
が保たれ、さらに運転継続が可能となる。なお、上記に
おいて回転速度の調節後、傾斜角の調節を実施する場合
を説明したが、回転速度と傾斜角の調節を同時に平行し
て実施してもよく、さらに傾斜角の調節の後に回転速度
の調節を実施してもよい。
Therefore, the feed rate is maintained by the increase in the inclination angle, and the operation can be continued. Although the case where the tilt angle is adjusted after adjusting the rotation speed has been described above, the rotation speed and the tilt angle may be adjusted in parallel at the same time, and the rotation speed may be adjusted after the tilt angle is adjusted. May be adjusted.

【0021】[0021]

【発明の効果】以上説明したようにこの発明の方法によ
れば、ロータリーキルンで処理物を焼却する場合、クリ
ンカの発生による送り速度の低下を回転数の増加以外に
ロータリーキルンの傾斜角の増加によっても調整出来る
ようにしたため、従来を上回るクリンカ堆積量であって
もそのまま燃焼が継続可能となり、長期間の連続処理が
可能となる効果を有する。
As described above, according to the method of the present invention, when incinerating an object to be processed in the rotary kiln, the decrease in the feed rate due to the occurrence of clinker is caused by the increase in the tilt angle of the rotary kiln in addition to the increase in the rotation speed. Since the amount of clinker can be adjusted, combustion can be continued as it is even if the amount of clinker accumulated exceeds the conventional amount, and continuous treatment for a long period of time can be performed.

【図面の簡単な説明】[Brief description of drawings]

【図1】この発明の一実施の形態を示す断面図である。FIG. 1 is a sectional view showing an embodiment of the present invention.

【図2】従来例を示す断面図である。FIG. 2 is a sectional view showing a conventional example.

【符号の説明】[Explanation of symbols]

1…ゴミ投入口 2…ロータリーキルン 3…ストーカ炉 3A…灰分級機 4…ロータリーキルン式焼却炉 5…架台 5A…支点 6…駆動装置 1 ... garbage input port 2 ... Rotary kiln 3 ... stoker furnace 3A ... ash classifier 4 ... Rotary kiln incinerator 5 ... Frame 5A ... fulcrum 6 ... Drive device

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F27B 7/12 F23G 5/20 F27B 7/42 ─────────────────────────────────────────────────── ─── Continuation of front page (58) Fields surveyed (Int.Cl. 7 , DB name) F27B 7/12 F23G 5/20 F27B 7/42

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ロータリーキルンを備えた焼却装置におい
て、連続処理時間の経過と共にロータリーキルンの出口
部の高さを次第に低くして投入口から出口部への下降傾
斜を大きくしていくことを特徴とするロータリーキルン
式焼却炉の制御方法。
1. An incinerator equipped with a rotary kiln, characterized in that the height of the outlet of the rotary kiln is gradually lowered as the continuous processing time elapses, and the descending inclination from the inlet to the outlet is increased. Control method of rotary kiln type incinerator.
【請求項2】ロータリーキルンを備えた焼却装置におい
て、ロータリーキルンを回転自在に支持する架台を、前
記ロータリーキルンの投入口側端を支点として水平軸周
囲に回動可能に支持し、前記架台の出口側端底部であっ
て炉の熱影響の少ない部位に、前記架台を上下動可能に
支持する駆動装置を設けたことを特徴とするロータリー
キルン式焼却炉の制御装置。
2. In an incinerator having a rotary kiln, a pedestal for rotatably supporting the rotary kiln is rotatably supported around a horizontal axis with an end on the inlet side of the rotary kiln as a fulcrum, and an end on the outlet side of the gantry. A control device for a rotary kiln type incinerator, which is provided with a drive device that supports the pedestal so as to be movable up and down, at the bottom of the furnace where there is little heat effect.
JP12612297A 1997-05-16 1997-05-16 Method and apparatus for controlling rotary kiln incinerator Expired - Fee Related JP3522083B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12612297A JP3522083B2 (en) 1997-05-16 1997-05-16 Method and apparatus for controlling rotary kiln incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12612297A JP3522083B2 (en) 1997-05-16 1997-05-16 Method and apparatus for controlling rotary kiln incinerator

Publications (2)

Publication Number Publication Date
JPH10318677A JPH10318677A (en) 1998-12-04
JP3522083B2 true JP3522083B2 (en) 2004-04-26

Family

ID=14927204

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12612297A Expired - Fee Related JP3522083B2 (en) 1997-05-16 1997-05-16 Method and apparatus for controlling rotary kiln incinerator

Country Status (1)

Country Link
JP (1) JP3522083B2 (en)

Also Published As

Publication number Publication date
JPH10318677A (en) 1998-12-04

Similar Documents

Publication Publication Date Title
US6655304B1 (en) Mass fuel combustion system
CA2112740C (en) Process to regulate the quantity of refuse or the depth of the refuse layer on incinerator grates
US5054405A (en) High temperature turbulent gasification unit and method
JP3522083B2 (en) Method and apparatus for controlling rotary kiln incinerator
US3687094A (en) Incinerator apparatus
JP3038129B2 (en) How to incinerate combustibles, especially garbage
JPS59107111A (en) Fluidized-bed type incinerating method of refuse
JP2624912B2 (en) Incinerator combustion control device
JP3580672B2 (en) Stoker type waste incinerator
JP2809585B2 (en) Operation control method of refuse crushing supply device
JP3461372B2 (en) Dust supply device control method
JP3462749B2 (en) Incinerator incineration method
JP3170654B2 (en) Operation control method of dry incineration equipment
JPH11141837A (en) Lateral rotary type incinerator
JPH1163434A (en) Incinerator
JP3744741B2 (en) Incinerator operation control method
JPH11294731A (en) Incineration method of incinerator
JPH0783420A (en) Incinerating method for mixed waste and rotary incinerator
JPH0313705A (en) Full automatic incinerating device
KR0132254B1 (en) Separating apparatus of regenerative material and wastes for incinerator
EP0653517B1 (en) Plant for producing bituminous conglomerate in continuous work cycle
JP3311466B2 (en) Detoxification equipment for refuse incineration dust
JPH0791635A (en) Control of combustion in fluidized-bed incinerator
JPH05180426A (en) Method for afterburning control in incinerator
JP3286853B2 (en) Ash Level Control Method in Stirred Incinerator

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20040106

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20040203

LAPS Cancellation because of no payment of annual fees