JPH08303953A - Rotary kiln - Google Patents

Rotary kiln

Info

Publication number
JPH08303953A
JPH08303953A JP11145795A JP11145795A JPH08303953A JP H08303953 A JPH08303953 A JP H08303953A JP 11145795 A JP11145795 A JP 11145795A JP 11145795 A JP11145795 A JP 11145795A JP H08303953 A JPH08303953 A JP H08303953A
Authority
JP
Japan
Prior art keywords
rotary
treated article
rotation
time
rotary cylinder
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
JP11145795A
Other languages
Japanese (ja)
Inventor
Teruyuki Nishiura
照行 西浦
Akira Hashimoto
彰 橋本
Yasuhiko Shiyouji
易彦 庄司
Shigeru Hanaoka
茂 花岡
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP11145795A priority Critical patent/JPH08303953A/en
Publication of JPH08303953A publication Critical patent/JPH08303953A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE: To make it possible to control residual time without changing the time and enhance throughput per unit time even when the supply of treated articles is unstable by installing a spiral groove continued with the inner surface of a rotary cylindrical body and forcing the cylindrical body to repeat its normal and reversal turning. CONSTITUTION: A heater 1 is partitioned in several sections and controlled so that single temperature adjustment may be available. A rotary cylinder 2 is heated with the heater 1 and provided with a spiral groove continued with the inner surface. A treated article is continuously charged into the continuous inside groove from one end 3 of the rotary cylinder where the treated article is moved in the direction of the other end in the radial groove by turning the rotary cylinder 2. The rotary speed and the rotary direction of the rotary cylinder 2 is arbitrarily controllable. When the rotary direction is in a normal mode, the treated article is moved in the other end direction while the treated article is returned when the rotary direction is in a reversal mode, which makes it possible to prolong the rotation time longer than the inversion time, thereby moving the treated article to in the direction of the other end 4 and discharge the treated article from a discharge opening in continuous mode.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、粉体・粒体等を連続的
に乾燥・焼成をするためのロータリーキルンに関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a rotary kiln for continuously drying and firing powder, granules and the like.

【0002】[0002]

【従来の技術】一般に、ロータリーキルンは衆知のよう
に外部から熱される構造を有した円筒体を水平に対して
やや傾斜して設置し、そしてこれを同位置で回転させな
がら傾斜された円筒体の高い方から被処理物を円筒体中
に投入し、回転にしたがって次第に低い方に移動させて
排出するまでの間に、加熱する構成となっている。
2. Description of the Related Art In general, a rotary kiln has a cylindrical body having a structure that is heated from the outside, as is known in the art, and is installed at a slight inclination with respect to the horizontal, and the cylindrical body is inclined while rotating at the same position. The object to be treated is charged into the cylindrical body from the higher side, and is gradually heated to the lower side in accordance with the rotation and heated until it is discharged.

【0003】[0003]

【発明が解決しようとする課題】このようなロータリー
キルンを使用して加熱を行う場合、回転する円筒体への
被処理物の充填量は15〜18%が一般的である。この
理由は円筒体内を通過する材料速度が、回転する円筒体
の傾斜角度、投入量、回転数等によって決定されるため
である。投入材料が円筒体内を通過する時間、すなわち
被処理物の滞留時間は上記と同様な因子によって決定さ
れる。
When heating is performed using such a rotary kiln, the filling amount of the object to be treated in the rotating cylindrical body is generally 15 to 18%. The reason for this is that the material velocity passing through the cylindrical body is determined by the inclination angle of the rotating cylindrical body, the input amount, the number of rotations, and the like. The time for the input material to pass through the cylinder, that is, the residence time of the material to be treated, is determined by the same factors as above.

【0004】また、円筒体の傾斜角度を0゜とした場
合、被処理物の滞留時間は次の(数1)で求められる。
When the inclination angle of the cylindrical body is 0 °, the residence time of the object to be treated is calculated by the following (Equation 1).

【0005】[0005]

【数1】 [Equation 1]

【0006】但し(数1)中、τは滞留時間(min)、N
は回転数(rpm)、βは材料安息角(゜)、Fは材料供給量
(kg/min)、Lは円筒体長(m)、ρSは材料嵩密度(kg/m3) Dは円筒体内径(m)をそれぞれ示す。
However, in (Formula 1), τ is the residence time (min), N
Is the number of revolutions (rpm), β is the angle of repose of the material (°), and F is the material supply amount.
(kg / min), L is the cylinder length (m), ρS is the material bulk density (kg / m 3 ), and D is the cylinder inner diameter (m).

【0007】したがって滞留時間は、回転する円筒体の
傾斜角度を0゜にした場合、回転数と材料供給量の関係
できまる。もし滞留時間を長くしようとすると、所定回
転数では材料供給量を下げればならなく、その分処理能
力が低下する。また材料供給量を増やすためには回転数
を下げなければならず、この場合は加熱効率がおちる。
円筒体に傾斜角度をつけた場合も同様である。連続的に
投入された材料が回転する円筒体内で分散して処理時間
の異なるものが混合することもある。また、材料供給量
が一定しないと円筒体内での滞留時間の変化が生じ均一
な加熱処理ができないという課題があった。
Therefore, the residence time can be determined by the relationship between the number of revolutions and the material supply amount when the tilting angle of the rotating cylinder is 0 °. If an attempt is made to lengthen the residence time, the material supply amount must be reduced at a predetermined rotation speed, and the processing capacity will be reduced accordingly. Further, in order to increase the material supply amount, the number of rotations must be decreased, and in this case, the heating efficiency drops.
The same applies when the cylinder is inclined. In some cases, the continuously charged materials are dispersed in the rotating cylinder to mix materials having different processing times. Further, if the material supply amount is not constant, there is a problem that the residence time in the cylinder changes and uniform heat treatment cannot be performed.

【0008】[0008]

【課題を解決するための手段】上記課題を解決するため
に本発明は、外部から加熱されるとともに内面に連続す
る螺旋状の溝を有して回転する円筒体(ロータリー円
筒)であって、被処理物はこのロータリー円筒の一端
(供給口)からその内部の連続する螺旋状の溝内に供給
され、ロータリー円筒の正転、逆転のくり返しにより被
処理物は連続する螺旋状の溝内を移動する。ここでのロ
ータリー円筒の回転数、回転方向は任意に制御でき、回
転方向が一方(正転)の時被処理物は円筒の他端(排出
口)の方向に移動し、回転方向が反対(逆転)の時は処
理物は供給口に戻る。従ってこの正転の時間の方が逆転
の時間よりも長く設定することにより、混合物は全体と
して排出口の方向に移動する。このように正転と逆転を
1サイクルとしくり返すことにより、被処理物はロータ
リーキルンの供給口から排出口へと移動する。
In order to solve the above-mentioned problems, the present invention provides a cylindrical body (rotary cylinder) which is heated from the outside and has a spiral groove which is continuous on the inner surface and rotates. The object to be processed is supplied from one end (supply port) of the rotary cylinder into the continuous spiral groove inside the rotary cylinder, and the object to be processed passes through the continuous spiral groove by the forward and reverse rotation of the rotary cylinder. Moving. The number of rotations and the direction of rotation of the rotary cylinder can be arbitrarily controlled. When the rotation direction is one (normal rotation), the object to be processed moves toward the other end (exhaust port) of the cylinder, and the rotation direction is opposite ( In the case of (reverse rotation), the processed product returns to the supply port. Therefore, by setting the forward rotation time longer than the reverse rotation time, the mixture as a whole moves toward the discharge port. By repeating normal rotation and reverse rotation as one cycle in this manner, the object to be processed moves from the supply port to the discharge port of the rotary kiln.

【0009】[0009]

【作用】このように本発明ではロータリー円筒の内面に
連続する螺旋状の溝を有しており、この溝内の有効体積
を大きくすることにより被処理物の充填量も多くでき、
溝内の充填量が変化しても、すなわち被処理物の投入量
が変化しても滞留時間は一定になる。
As described above, in the present invention, the inner surface of the rotary cylinder has a continuous spiral groove, and by increasing the effective volume in this groove, the filling amount of the object to be treated can be increased,
The residence time becomes constant even if the filling amount in the groove changes, that is, the input amount of the object to be processed changes.

【0010】また連続する螺旋状の溝内を被処理物が順
次移動する構成により、供給時間が異なる被処理物が混
ざることのないように処理できる。さらに被処理物の表
面層と中央部分の温度差も回転数が速いほど小さくな
る。ところが回転数が速いと被処理物は速くロータリー
円筒中を移動するため、所定の温度キープ時間を得るた
めには連続する溝のピッチを小さくするか、または長い
ロータリー円筒が必要になる。
Further, since the objects to be processed are successively moved in the continuous spiral groove, the objects to be processed having different supply times can be processed without being mixed. Further, the temperature difference between the surface layer and the central portion of the object to be treated also decreases as the rotation speed increases. However, when the rotation speed is high, the object to be processed moves quickly in the rotary cylinder, so that the pitch of continuous grooves is made small or a long rotary cylinder is required to obtain a predetermined temperature keeping time.

【0011】本発明のキルンではロータリー円筒の回転
数とともに回転方向も任意に制御できるので、円筒の回
転方向が正転の時には被処理物が供給口の反対側(排出
口)に移動し、回転方向が逆転の時には被処理物は供給
口に戻される。従ってこの正転の時間の方が逆転の時間
よりも長く設定することにより被処理物全体は排出口の
方向に移動することになる。このことから正転、逆転の
時間差を変えることによって、円筒体中での滞留時間を
任意に制御することができる。
In the kiln of the present invention, the rotation direction as well as the rotation direction of the rotary cylinder can be controlled arbitrarily, so that when the rotation direction of the cylinder is forward, the object to be processed moves to the side opposite to the supply port (discharge port) and rotates. When the direction is reversed, the object to be processed is returned to the supply port. Therefore, by setting the forward rotation time longer than the reverse rotation time, the entire object to be processed moves toward the discharge port. Therefore, the residence time in the cylindrical body can be arbitrarily controlled by changing the time difference between forward rotation and reverse rotation.

【0012】[0012]

【実施例】以下、図面とともに本発明の実施例を説明す
る。図1は、本発明のロータリーキルンを示し、1は加
熱ヒーターである。この加熱ヒーターはいくつかのゾー
ンに区切られ、それぞれ単独で温度を調整できるように
制御されている。2はこのヒーター1により加熱され内
面に連続する螺旋状の溝を有して回転するロータリー円
筒を示す。図2はロータリー円筒2とヒーター1を図1
のA−A′線に切った断面図を示す。被処理物は3に示
すロータリー円筒の一端(供給12)から内部の連続す
る溝内に投入する。ロータリー円筒の回転により被処理
物は連続する螺旋状の溝内を他端4の方向に移動する。
このロータリー円筒の回転数、回転方向は任意に制御で
き、その回転方向が正転の時被処理物は他端方向に移動
し、回転方向が逆転の時には被処理物は供給口側に戻
る。従って正転の時間の方が逆転の時間より長くなるよ
うに設定することで被処理物は全体として他端4の方向
に移動し、連続的に排出口から排出される。このロータ
リーキルンを使用した処理物の円筒中での滞留時間は以
下の(数2)で求められる。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows a rotary kiln of the present invention, and 1 is a heater. This heater is divided into several zones, each of which is controlled so that its temperature can be adjusted independently. Reference numeral 2 denotes a rotary cylinder which is heated by the heater 1 and has a spiral groove which is continuous on the inner surface and rotates. FIG. 2 shows a rotary cylinder 2 and a heater 1.
A sectional view taken along line AA ′ of FIG. The object to be processed is put into a continuous groove inside from one end (supply 12) of the rotary cylinder shown in FIG. The object to be processed moves in the direction of the other end 4 in the continuous spiral groove by the rotation of the rotary cylinder.
The rotation speed and rotation direction of the rotary cylinder can be controlled arbitrarily. When the rotation direction is forward, the object to be processed moves toward the other end, and when the rotation direction is reverse, the object to be processed returns to the supply port side. Therefore, by setting the forward rotation time to be longer than the reverse rotation time, the object as a whole moves toward the other end 4 and is continuously discharged from the discharge port. The residence time in the cylinder of the processed material using this rotary kiln is calculated by the following (Equation 2).

【0013】[0013]

【数2】 [Equation 2]

【0014】但し(数2)中、τは滞留時間(h)、P
nは連続した螺旋状の溝数、Nは回転数(rpm)、T1
は正転時間(min)、tは正転時間と逆転時間との差
(min)、Tsは1サイクル時間(min)をそれぞ
れ示す。
However, in (Equation 2), τ is the residence time (h), P
n is the number of continuous spiral grooves, N is the number of revolutions (rpm), T1
Represents the forward rotation time (min), t represents the difference between the normal rotation time and the reverse rotation time (min), and Ts represents one cycle time (min).

【0015】このように回転数、または正転時間と逆転
時間の差を任意に設定することにより被処理物のロータ
リー円筒体中での滞留時間を自由にコントロールするこ
とができる。
As described above, by arbitrarily setting the rotation speed or the difference between the normal rotation time and the reverse rotation time, the residence time of the object to be processed in the rotary cylinder can be freely controlled.

【0016】[0016]

【発明の効果】以上説明したように、本発明のロータリ
ーキルンでは、回転する円筒体の内面に連続した螺旋状
の溝を設けて、円筒体に正転・逆転をくり返させること
により、被処理物の供給が不安定でも滞留時間は変わら
ず、また滞留時間を任意に制御可能とすることにより十
分な熱処理が施すことができ、単位時間当りの処理量を
大幅に向上させることができた。
As described above, in the rotary kiln of the present invention, a continuous spiral groove is provided on the inner surface of the rotating cylinder, and the cylinder is repeatedly rotated in the normal direction and the reverse direction. The residence time did not change even when the supply of the material was unstable, and by allowing the residence time to be controlled arbitrarily, a sufficient heat treatment could be performed, and the throughput per unit time could be greatly improved.

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

【図1】本発明の実施例におけるロータリーキルンの説
明図
FIG. 1 is an explanatory view of a rotary kiln according to an embodiment of the present invention.

【図2】図1のA−A′線に沿った断面図FIG. 2 is a sectional view taken along the line AA ′ of FIG.

【符号の説明】[Explanation of symbols]

1 加熱ヒーター 2 連続した螺旋状の溝を有したロータリー円筒 3 供給口 4 排出口 1 heating heater 2 rotary cylinder with continuous spiral groove 3 supply port 4 discharge port

───────────────────────────────────────────────────── フロントページの続き (72)発明者 花岡 茂 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Shigeru Hanaoka 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】外部から加熱されるとともに内面に連続す
る螺旋状の溝を有して回転する円筒体からなり、その回
転方向が定期的に正転、逆転をくり返すことを特徴とす
るロータリーキルン。
1. A rotary kiln characterized by comprising a cylindrical body which is heated from the outside and has a continuous spiral groove on its inner surface and which rotates, and the direction of rotation thereof periodically repeats normal rotation and reverse rotation. .
【請求項2】被加熱材料が回転する円筒体の一端から内
部に供給され、連続する螺旋状の溝内での前進、後退を
繰り返し順次移動しながら加熱処理されるものであっ
て、円筒体の正転逆転の1サイクルにおいて正転時の総
回転数を逆転時のそれよりも多く設定することによっ
て、被加熱材料を円筒の他端から排出することを特徴と
した請求項1記載のロータリーキルンを用いた加熱処理
方法。
2. A material to be heated is supplied from one end of a rotating cylindrical body to the inside thereof, and is heated while repeatedly moving forward and backward in a continuous spiral groove. 2. The rotary kiln according to claim 1, wherein the material to be heated is discharged from the other end of the cylinder by setting the total number of revolutions during forward rotation in one cycle of forward rotation and reverse rotation to be higher than that during reverse rotation. A heat treatment method using.
JP11145795A 1995-05-10 1995-05-10 Rotary kiln Pending JPH08303953A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11145795A JPH08303953A (en) 1995-05-10 1995-05-10 Rotary kiln

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11145795A JPH08303953A (en) 1995-05-10 1995-05-10 Rotary kiln

Publications (1)

Publication Number Publication Date
JPH08303953A true JPH08303953A (en) 1996-11-22

Family

ID=14561723

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11145795A Pending JPH08303953A (en) 1995-05-10 1995-05-10 Rotary kiln

Country Status (1)

Country Link
JP (1) JPH08303953A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005089664A (en) * 2003-09-19 2005-04-07 Takuma Co Ltd Pyrolysis drum unit
JP2006343041A (en) * 2005-06-09 2006-12-21 Tsukishima Kikai Co Ltd Heat treatment method for fluid, and heat treatment apparatus for fluid
CN101966584A (en) * 2010-11-18 2011-02-09 宁波百琪达自动化设备有限公司 Hydrogenation furnace for hydrogenating rare earth alloy powder
CN103743226A (en) * 2014-01-15 2014-04-23 合肥国轩高科动力能源股份公司 Rotary lithium battery powder oven
CN104776715A (en) * 2015-04-19 2015-07-15 郴州福鑫有色金属有限公司 Rotary kiln
JP2017117561A (en) * 2015-12-22 2017-06-29 信越化学工業株式会社 Rotary type cylindrical furnace, and method for manufacturing negative electrode active material for nonaqueous electrolyte secondary battery
CN107388260A (en) * 2017-07-14 2017-11-24 光大环境科技(中国)有限公司 Control method and control system for counter current rotary kiln system
JP2018200140A (en) * 2017-05-26 2018-12-20 株式会社東芝 Thermal decomposition furnace
CN109520286A (en) * 2018-11-06 2019-03-26 长兴新亚环保机械科技有限公司 A kind of industrial furnace convenient for heat dissipation

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005089664A (en) * 2003-09-19 2005-04-07 Takuma Co Ltd Pyrolysis drum unit
JP2006343041A (en) * 2005-06-09 2006-12-21 Tsukishima Kikai Co Ltd Heat treatment method for fluid, and heat treatment apparatus for fluid
JP4674803B2 (en) * 2005-06-09 2011-04-20 月島機械株式会社 Fluid heat treatment method and fluid heat treatment apparatus
CN101966584A (en) * 2010-11-18 2011-02-09 宁波百琪达自动化设备有限公司 Hydrogenation furnace for hydrogenating rare earth alloy powder
CN103743226A (en) * 2014-01-15 2014-04-23 合肥国轩高科动力能源股份公司 Rotary lithium battery powder oven
CN104776715A (en) * 2015-04-19 2015-07-15 郴州福鑫有色金属有限公司 Rotary kiln
JP2017117561A (en) * 2015-12-22 2017-06-29 信越化学工業株式会社 Rotary type cylindrical furnace, and method for manufacturing negative electrode active material for nonaqueous electrolyte secondary battery
JP2018200140A (en) * 2017-05-26 2018-12-20 株式会社東芝 Thermal decomposition furnace
CN107388260A (en) * 2017-07-14 2017-11-24 光大环境科技(中国)有限公司 Control method and control system for counter current rotary kiln system
CN109520286A (en) * 2018-11-06 2019-03-26 长兴新亚环保机械科技有限公司 A kind of industrial furnace convenient for heat dissipation

Similar Documents

Publication Publication Date Title
JPH08303953A (en) Rotary kiln
US3905757A (en) Apparatus and method for distributing material being processed over a furnace hearth floor
US5997289A (en) Rotary calciner with mixing flights
US2680084A (en) Hydraulic conveying
RU2146793C1 (en) Method of and device for charging loose material into rotating hearth furnace
US3035303A (en) Extrusion of organic thermoplastic polymeric materials
JP2011038653A (en) External heat type rotary furnace and core tube thereof
WO2005095878A1 (en) Method and device for pulse heat treatment of bulk materials
US4149845A (en) Rabbles and material handling systems utilizing the same
US5908291A (en) Continuous cross-flow rotary kiln
JP3396986B2 (en) Powder heat treatment furnace
JPH0424392Y2 (en)
JP4674803B2 (en) Fluid heat treatment method and fluid heat treatment apparatus
JPH07234073A (en) Heat treating furnace
JPH06306495A (en) Method for granulating raw material for sintering
JPH10148471A (en) Cylindrical rotary type dryer
CA1090123A (en) Split flow material handling system
US3160402A (en) Apparatus for the roasting of pellets
JPH09329391A (en) Horizontal rotation type heating device
SU1571380A1 (en) Rotary furnace
SU483997A1 (en) The method of processing dispersed materials
JPS63176989A (en) Rotary kiln
KR101879094B1 (en) Online stirrer for throughput enlargement of powder sample in belt type furnace
JPH0642876A (en) Indirect heating type rotary heating furnace
JP2016121860A (en) Rotary kiln