JPS63176989A - Rotary kiln - Google Patents

Rotary kiln

Info

Publication number
JPS63176989A
JPS63176989A JP505587A JP505587A JPS63176989A JP S63176989 A JPS63176989 A JP S63176989A JP 505587 A JP505587 A JP 505587A JP 505587 A JP505587 A JP 505587A JP S63176989 A JPS63176989 A JP S63176989A
Authority
JP
Japan
Prior art keywords
rotary kiln
rotary
inclination angle
cylinder
rotating cylindrical
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.)
Granted
Application number
JP505587A
Other languages
Japanese (ja)
Other versions
JPH0262796B2 (en
Inventor
清治 道前
天宮 明
遠藤 憲明
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.)
Daido Netsugaku Kk
Doumae Chikuro Kogyo Kk
Original Assignee
Daido Netsugaku Kk
Doumae Chikuro Kogyo Kk
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 Daido Netsugaku Kk, Doumae Chikuro Kogyo Kk filed Critical Daido Netsugaku Kk
Priority to JP505587A priority Critical patent/JPS63176989A/en
Publication of JPS63176989A publication Critical patent/JPS63176989A/en
Publication of JPH0262796B2 publication Critical patent/JPH0262796B2/ja
Granted legal-status Critical Current

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Landscapes

  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明はロータリーキルン(回転炉)に関する。[Detailed description of the invention] Industrial applications The present invention relates to a rotary kiln.

さらに詳しくは、本発明は傾斜角度を自在に変えること
ができる回転円筒体部からなるロータリーキルンに関す
る。
More specifically, the present invention relates to a rotary kiln comprising a rotating cylindrical body portion whose inclination angle can be freely changed.

ロータリーキルンは、水平面に対してわずかに傾斜した
回転円筒体内に被処理物を投入し、円筒の一端または中
間部からの熱風あるいは火炎によフ投人材料の高温処理
を行う装置である。ロータリーキルンは一般に処理温度
が高く、回転円筒体を保護するため円筒内面に耐火材を
内張ジし、被処理物が円筒体の回転により、内部を転動
しながら傾斜円筒体の下端部に向かって進む間に供給さ
れた熱エネルギーにより被処理物を加熱処理することを
特色としている。また、ロータリーキルンは、構造が比
較的単純であると共に、所定の安定した処理条件下での
連続操業を特徴としている。
A rotary kiln is a device in which a material to be treated is put into a rotating cylinder slightly inclined with respect to the horizontal plane, and the material is subjected to high-temperature treatment using hot air or flame from one end or the middle of the cylinder. Rotary kilns generally have high processing temperatures, and in order to protect the rotating cylinder, the inner surface of the cylinder is lined with a refractory material. The feature is that the object to be treated is heat-treated using the thermal energy supplied while the process progresses. Further, rotary kilns are characterized by a relatively simple structure and continuous operation under predetermined and stable processing conditions.

従来の技術 ロータリーキルンは乾燥、燃焼、焼却、焼結などの熱処
理や熱加工に広く利用されているが、その形状、同速、
加熱方式などにより種々に分類される。形状から分類す
ると、円筒胴体がキルンのほぼ全長にわたり同一径で形
成される単胴型と、胴体が2種類以上の異なった径で形
成される複胴型と、単胴が並列に配置され両者がフード
で連接された二段又は多段型に分けられる。
Conventional technology Rotary kilns are widely used for heat treatment and thermal processing such as drying, combustion, incineration, and sintering, but their shape, speed,
They are classified into various types depending on the heating method, etc. Classified based on shape, there are single-barrel types, in which the cylindrical body is formed with the same diameter over almost the entire length of the kiln, double-barrel types, in which the cylinder bodies are formed with two or more different diameters, and double-barrel types, in which the single-barrel bodies are arranged in parallel. It can be divided into two-stage or multi-stage types connected by a hood.

従来の二段型ロータリーキルンの一例を第1図に示す。An example of a conventional two-stage rotary kiln is shown in FIG.

このロータリーキルンはそれぞれ所定の傾斜角度をもっ
て並列に配置された2つの固定傾斜回転円筒体lOが連
結フード16によって連接されている。回転円筒体の傾
斜角度は変えることができない構成になっている。
This rotary kiln includes two fixed inclined rotary cylinders 1O arranged in parallel at predetermined inclination angles and connected by a connecting hood 16. The inclination angle of the rotating cylindrical body cannot be changed.

単胴型、複胴型あるいは多段型のいずれにしても、従来
のロータリーキルンは傾斜角度が固定されている。ロー
タリーキレンの処理速度は、処理高度を一定とした場合
、その回転数と傾斜角度によって決まる。従って、傾斜
角度が固定されている従来のロータリーキルンでは、被
処理物の種顧、性質及び量が変わった場合、最適の処理
速度で処理することができない。例えば、高流動性の液
体の処理効率が低く、円筒体内張りの耐火物全損傷する
恐れのある被処理物質については別の装置で燗雑な前卯
埋を行う必要があった。
Regardless of whether it is a single-shell type, a multi-shell type, or a multi-stage type, a conventional rotary kiln has a fixed inclination angle. The processing speed of a rotary cleaner is determined by its rotational speed and inclination angle, assuming that the processing altitude is constant. Therefore, a conventional rotary kiln with a fixed inclination angle cannot process at an optimum processing speed when the type, nature, and quantity of the material to be processed changes. For example, the treatment efficiency of highly fluid liquids is low, and for materials to be treated that may damage all the refractories lining the cylinder, it is necessary to perform complicated pre-burying using a separate device.

傾斜角度が固定されかつ連続式である従来のロータリー
キルンでは、廃酸、廃アルカリ土類金属化合物、等を含
む汚泥廃棄物を処理すると、回転円筒体内面に汚泥が粘
着したり、あるいは大きな玉状の塊りを形成する傾同が
あり、これら廃棄物の熱処理が極めて困難であった。こ
の種の被処理物は、ロータリーキルンに替わる伸の装置
!全選択するか、あるいは特殊な前処理装置を設ける必
要があった。
In conventional rotary kilns, which have a fixed inclination angle and are continuous, when processing sludge waste containing waste acids, waste alkaline earth metal compounds, etc., the sludge sticks to the inner surface of the rotating cylinder or forms large beads. These wastes tend to form clumps, making heat treatment of these wastes extremely difficult. This type of processing material is a perfect alternative to a rotary kiln! It was necessary to either select all or install special pre-processing equipment.

問題点を解決するための手段 本発明は、上記に鑑みてなされたものであって、ロータ
リーキルンの構造の単純性、被処理物の種類、性質、処
理速度、等の負荷変動に対する順応性、温度制御の容易
性、熱効率を含む経済性を生かし、なおかつ高流動性液
体および耐火物を損傷する恐れのある物質も処理可能に
することによりロータリーキルンの適用範囲全拡大する
ために、少なくとも2つの回転田筒体全フードを介して
連結し、その内少なくとも1つの回転円筒体の傾斜角度
を可変としたロータリーキルンを提供せんとするもので
ある。
Means for Solving the Problems The present invention has been made in view of the above-mentioned problems. At least two rotary fields will be installed in order to expand the range of applications of rotary kilns by taking advantage of their economical benefits, including ease of control and thermal efficiency, while also being able to process highly fluid liquids and substances that can damage refractories. It is an object of the present invention to provide a rotary kiln in which all cylinders are connected via a hood and the inclination angle of at least one of the rotating cylinders is variable.

本発明は、少なくとも2つの回転円筒体をフードを介し
て連結し、その内少なくとも1つの回転円筒体の傾斜角
度を可変としたことを特徴とするロータリーキルンに関
する、 作用 処理温度が一定の場合、ロータリーキルンの処理速度は
その回転数と傾斜角度によって決まる。
The present invention relates to a rotary kiln characterized in that at least two rotating cylindrical bodies are connected via a hood, and the inclination angle of at least one of the rotating cylindrical bodies is variable. The processing speed of is determined by its rotation speed and inclination angle.

しかしながら、従来のロータリーキルンは流動性の高い
物質の処理は通常の回転数および傾斜色度では制御が困
難であって、著しく熱効率を低下させる場合が多いため
、普通は他の装置を使用している。このような場合にも
、負荷変動に対するJIB応性の優れた本発明のロータ
リーキルンによれば、可変傾斜回転円筒体の形状を樽の
ように中窪みとし、#〕ぼ水平に維持して被処理物を十
分に加熱処理した後、後続の固定傾斜回転円筒体に移送
して処理すれば、容積に対する処理量が増加して高い熱
効率を得ると共に、被処理物が浴としての機能をもって
、耐火物の高度変化及び被処理物の重力による損傷を著
しく低減することができる。
However, in conventional rotary kilns, processing of highly fluid substances is difficult to control with normal rotational speed and gradient chromaticity, and thermal efficiency is often significantly reduced, so other equipment is usually used. . Even in such a case, according to the rotary kiln of the present invention, which has excellent JIB response to load fluctuations, the shape of the variable tilt rotating cylinder is made into a hollow shape like a barrel, and the workpiece is maintained almost horizontally. If the material is sufficiently heat-treated and then transferred to the following fixed inclined rotary cylinder for treatment, the throughput per volume increases and high thermal efficiency is obtained. Damage caused by altitude changes and gravity of the object to be processed can be significantly reduced.

耐火物に対して侵食性の強い被処理物質に対しては、同
様に可変傾斜回転円筒体音はぼ水平に保ち、予め侵食防
止剤を供給して保護浴全形放させ、そこに被処理′@ヲ
供給して適温で十分に反応させることができる、そして
一旦保護浴を生成させた後は連続的に保護剤と被処理物
を供給することができる。この場合にも、制御温度が異
なる可変傾斜回転円筒体と固定傾斜回転円筒体を連結す
ることによって、高温ガスの一部を相互に利用したり、
他のカスを供給したりして熱効率を著しく高めることが
できる。
For materials to be treated that are highly corrosive to refractories, the variable tilt rotating cylinder should be kept nearly horizontal, an anti-erosion agent should be supplied in advance, the entire protective bath should be released, and the material to be treated should be placed there. The protective agent and the material to be treated can be supplied continuously to allow a sufficient reaction to occur at an appropriate temperature. In this case as well, by connecting a variable tilt rotating cylinder and a fixed tilt rotating cylinder with different control temperatures, a part of the high temperature gas can be used mutually.
Thermal efficiency can be significantly increased by supplying other waste.

さらに、可変傾斜回転円筒体と固定傾斜円筒体を直列に
連結し、各連結部において材料の供給、雰囲気ガスの調
整を行なうことによって、酸化、遣元、等の反応を反応
速度に応じて効率良くかつ自由に進行させることができ
る。
Furthermore, by connecting the variable tilt rotary cylinder and the fixed tilt cylinder in series, and by supplying materials and adjusting the atmospheric gas at each connection, reactions such as oxidation and oxygenation can be carried out efficiently depending on the reaction rate. It can be progressed well and freely.

実施例 第2図に本発明によるロータリーキルンの側面図を示す
。このロータリーキル/は操業中に傾斜角度を自在に変
えることができる可変傾斜回転円筒体20と、該円筒体
に直列に連結され、傾斜角度が固定されている固定傾斜
回転円筒体10からなる。可変傾斜回転円筒体20と固
定傾斜円筒体10との連結部には、図示されていないけ
れども材料、空気、ガスなど全供給するノズルが設置さ
れている。12は固定傾斜円筒体の支持装置、15は駆
動装置、14は排出口部、15はガスシール・フードで
ある。21は被処理物の供給口部、該部にはガス送入バ
ーナが設けられているが図示されていない、22は可変
傾斜回転円筒体20の支持装置、25は駆動装置、21
4はガスシール・フードそして25は可変傾斜回転円筒
体20を傾斜させる油圧式傾動装置である。図の幽霊線
は可変傾斜回転円筒体の傾斜角変更位置を示す。
Embodiment FIG. 2 shows a side view of a rotary kiln according to the present invention. This rotary kill machine consists of a variable tilt rotary cylindrical body 20 whose tilt angle can be freely changed during operation, and a fixed tilt rotary cylinder 10 which is connected in series to the cylinder and whose tilt angle is fixed. Although not shown, a nozzle for supplying all materials, air, gas, etc. is installed at the joint between the variable tilt rotating cylinder 20 and the fixed tilt cylinder 10. 12 is a support device for the fixed inclined cylinder, 15 is a drive device, 14 is an exhaust port, and 15 is a gas seal hood. Reference numeral 21 denotes a supply port of the material to be treated, this part is provided with a gas feed burner (not shown), 22 is a support device for the variable tilt rotation cylinder 20, 25 is a drive device, 21
4 is a gas seal hood, and 25 is a hydraulic tilting device for tilting the variable tilt rotary cylindrical body 20. The ghost line in the figure indicates the tilt angle changing position of the variable tilt rotating cylinder.

第う図は本発明のもう1つの実施態様金示す模式図であ
って、直列に連結された第1の可変傾斜回転円筒体20
と第2の可変傾斜回転円筒体20からなる。
FIG. 3 is a schematic diagram showing another embodiment of the present invention, in which the first variable inclination rotary cylindrical bodies 20 are connected in series.
and a second variable tilt rotating cylindrical body 20.

実験例 胴直径し5m、排出ロ直径0.7 m、胴長12m。Experimental example The diameter of the trunk is 5m, the diameter of the discharge hole is 0.7m, and the length of the trunk is 12m.

可変傾斜角度0−55度、制御回転数1〜llrpm、
全長5.gmの可変傾斜回転円筒体20に、胴直径15
m、回転数1〜llrpm、全長5mの固定傾斜回転円
筒体10會直列に連結したロータリーキルンを使用し、
可変傾斜回転円筒体20の温度を500℃に維持し、最
初に酸化鉄と酸化アルミニウムを含む汚泥を加熱した後
、ナトリウム塩を多量に含む強塩基性汚泥と前記酸化鉄
・酸化アルミニウムの汚泥を混合し、固定傾斜回転円筒
体10の温度′f:500℃に保シ、前記得られた混合
物を該固定傾斜回転円筒体に移送して、100 K9/
hrの処理速度で直径1〜5cIrLの被処理ボールi
 1000Kg?lたが、ロータリーキルンは円滑に作
動し、耐火物の撰傷は全く観察されなかった。
Variable inclination angle 0-55 degrees, control rotation speed 1-llrpm,
Total length 5. gm variable tilt rotating cylinder 20, body diameter 15
Using a rotary kiln connected in series with 10 fixed inclined rotary cylinders with a rotation speed of 1 to 1 l rpm and a total length of 5 m,
The temperature of the variable tilt rotating cylinder 20 is maintained at 500° C., and after first heating the sludge containing iron oxide and aluminum oxide, the strong basic sludge containing a large amount of sodium salt and the sludge of iron oxide and aluminum oxide are heated. Mix and maintain the temperature 'f of the fixed tilt rotating cylinder 10 at 500° C., transfer the obtained mixture to the fixed tilt rotary cylinder 10 at 100 K9/
Balls to be processed with a diameter of 1 to 5 cIrL at a processing speed of hr
1000Kg? However, the rotary kiln operated smoothly and no damage to the refractory was observed.

発明の効果 本発明により、少なくとも2つの回転円筒体をフードを
介して連結し、その内掛なくとも1つの回転円筒体の傾
斜角度を可変としたため、ロータリーキルンの構造の単
純性、負荷変動に対する順応性、温度制御の容易性、熱
効率を含む経済性を生かし、なおかつ高流動性液体およ
び耐火物を損傷する恐れのある物質も処理可能とするこ
とKよジロータリーキルンの適用範囲全拡大することが
できる。
Effects of the Invention According to the present invention, at least two rotating cylindrical bodies are connected through a hood, and the inclination angle of at least one of the rotating cylindrical bodies is made variable, thereby simplifying the structure of the rotary kiln and adapting it to load fluctuations. The application range of the rotary kiln can be expanded to the full extent by taking advantage of its economic efficiency, ease of temperature control, and thermal efficiency, while also being able to process highly fluid liquids and substances that may damage refractories. .

【図面の簡単な説明】 第1図は従来の二段式ロータリーキル/の側面図、第2
図は本発明によるロータリーキルンの側面図。第5図は
本発明による別の実施態様によるロータリーキルンの側
面図。
[Brief explanation of the drawings] Figure 1 is a side view of a conventional two-stage rotary kill/
The figure is a side view of a rotary kiln according to the present invention. FIG. 5 is a side view of a rotary kiln according to another embodiment of the present invention.

Claims (1)

【特許請求の範囲】 1、少なくとも2つの回転円筒体をフードを介して連結
し、該回転円筒体の少なくとも1つの傾斜角度を可変と
したことを特徴とするロータリーキルン。 2、傾斜角度を自在に変えることができる第1の回転円
筒体20と、該第1の回転円筒体に連結され傾斜角度を
固定した第2の回転円筒体10からなることを特徴とす
る特許請求の範囲第1項に記載のロータリーキルン。 3、傾斜角度を自在に変えることができる第1の回転円
筒体20と、該第1の回転円筒体に連結され傾斜角度を
自在に変えることができる第2の回転円筒体20からな
ることを特徴とする特許請求の範囲第1項に記載のロー
タリーキルン。
Claims: 1. A rotary kiln, characterized in that at least two rotating cylindrical bodies are connected via a hood, and the inclination angle of at least one of the rotating cylindrical bodies is variable. 2. A patent characterized in that it consists of a first rotating cylindrical body 20 whose inclination angle can be freely changed, and a second rotating cylindrical body 10 connected to the first rotating cylindrical body and having a fixed inclination angle. A rotary kiln according to claim 1. 3. It consists of a first rotating cylindrical body 20 whose inclination angle can be freely changed, and a second rotating cylindrical body 20 which is connected to the first rotating cylindrical body and whose inclination angle can be freely changed. A rotary kiln as claimed in claim 1.
JP505587A 1987-01-14 1987-01-14 Rotary kiln Granted JPS63176989A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP505587A JPS63176989A (en) 1987-01-14 1987-01-14 Rotary kiln

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP505587A JPS63176989A (en) 1987-01-14 1987-01-14 Rotary kiln

Publications (2)

Publication Number Publication Date
JPS63176989A true JPS63176989A (en) 1988-07-21
JPH0262796B2 JPH0262796B2 (en) 1990-12-26

Family

ID=11600713

Family Applications (1)

Application Number Title Priority Date Filing Date
JP505587A Granted JPS63176989A (en) 1987-01-14 1987-01-14 Rotary kiln

Country Status (1)

Country Link
JP (1) JPS63176989A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004250260A (en) * 2003-02-19 2004-09-09 Hisashi Ikeda Method and apparatus for firing into cement clinker
WO2005007572A1 (en) * 2003-07-18 2005-01-27 Noriyuki Yamazaki Apparatus and method for producing carbide
JP2006308172A (en) * 2005-04-27 2006-11-09 Takasago Ind Co Ltd Batch type rotary kiln
JP2006308173A (en) * 2005-04-27 2006-11-09 Takasago Ind Co Ltd Batch type rotary kiln

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004250260A (en) * 2003-02-19 2004-09-09 Hisashi Ikeda Method and apparatus for firing into cement clinker
JP4582438B2 (en) * 2003-02-19 2010-11-17 恒 池田 Cement clinker firing method and firing apparatus
WO2005007572A1 (en) * 2003-07-18 2005-01-27 Noriyuki Yamazaki Apparatus and method for producing carbide
JP2006308172A (en) * 2005-04-27 2006-11-09 Takasago Ind Co Ltd Batch type rotary kiln
JP2006308173A (en) * 2005-04-27 2006-11-09 Takasago Ind Co Ltd Batch type rotary kiln

Also Published As

Publication number Publication date
JPH0262796B2 (en) 1990-12-26

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