JP2006299010A - External heating rotary kiln - Google Patents

External heating rotary kiln

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Publication number
JP2006299010A
JP2006299010A JP2005119879A JP2005119879A JP2006299010A JP 2006299010 A JP2006299010 A JP 2006299010A JP 2005119879 A JP2005119879 A JP 2005119879A JP 2005119879 A JP2005119879 A JP 2005119879A JP 2006299010 A JP2006299010 A JP 2006299010A
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JP
Japan
Prior art keywords
rotary kiln
spiral
dust
inner cylinder
external heating
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Pending
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JP2005119879A
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Japanese (ja)
Inventor
Haruyuki Ono
治之 小野
Hirotsugu Noguchi
博嗣 野口
Akira Nishizawa
章 西澤
Shinji Hara
真二 原
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Kurimoto Ltd
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Kurimoto Ltd
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Publication date
Application filed by Kurimoto Ltd filed Critical Kurimoto Ltd
Priority to JP2005119879A priority Critical patent/JP2006299010A/en
Publication of JP2006299010A publication Critical patent/JP2006299010A/en
Pending legal-status Critical Current

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  • Muffle Furnaces And Rotary Kilns (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)
  • Coke Industry (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide an external heating rotary kiln to prevent the deposition of dust, suppress the lowering of thermal efficiency and the variation of carbonization, increase the quality of carbonized product and enable efficient operation by scraping up the dust transported with hot air. <P>SOLUTION: A combustible waste is carbonized by dry distillation to form a carbonized material and the gas generated by the dry distillation is used as a heat source of an external heating rotary kiln 10. The dust deposited in a heating zone 18 is scraped up toward the exhaust port 21 and discharged at need by forming a spiral lifter 16 on the outer circumference of an inner cylinder 11 or forming a plurality of spiral lifters at intervals on the outer circumference of the inner cylinder. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

この発明は、可燃性廃棄物を乾留して炭化物を生成し、乾留時に発生した乾留ガスを熱源とする外熱式ロータリーキルンに関する。   The present invention relates to an externally heated rotary kiln that produces carbonized carbon by combusting combustible waste and uses a carbonized gas generated during carbonization as a heat source.

可燃性廃棄物を乾留し、ここで発生する乾留ガスを、直接または間接に熱源とする外熱式ロータリーキルンを設置した廃棄物処理システムの一例を図4に示す。この図において、破砕・細断して圧縮減容した(以下、「減容処理した」という)可燃性廃棄物を図示しない定量供給手段により外熱式ロータリーキルン50の内筒51に投入し、この外熱式ロータリーキルン50で乾留され、炭化された可燃性廃棄物は図示しない炭化物冷却手段に送り出され、乾留域で発生した乾留ガスは、脱臭炉Xで燃焼・脱臭され、外熱式ロータリーキルンの加熱ゾーン58に熱風として供給される。   FIG. 4 shows an example of a waste treatment system in which combustible waste is carbonized and an externally heated rotary kiln in which the carbonized gas generated here is directly or indirectly used as a heat source is installed. In this figure, combustible waste that has been crushed and shredded and reduced in volume (hereinafter referred to as “volume reduction treatment”) is put into the inner cylinder 51 of the external heating type rotary kiln 50 by a quantitative supply means (not shown). The combustible waste carbonized and carbonized in the external heating rotary kiln 50 is sent to a carbide cooling means (not shown), and the carbonization gas generated in the carbonization zone is burned and deodorized in the deodorizing furnace X to heat the external heating rotary kiln. The zone 58 is supplied as hot air.

ここで、これまで一般的に採用されてきた外熱式ロータリーキルンとして特許文献1を挙げることができる。   Here, patent document 1 can be mentioned as an external heating type rotary kiln generally employ | adopted until now.

特開2001−131556号公報(課題解決のための手段および図1)JP 2001-131556 A (Means for solving problems and FIG. 1)

上記外熱式ロータリーキルンにおいて、発生した乾留ガスを熱源とするときは、熱風中にダストが混在し、外熱式ロータリーキルンの加熱ゾーンに上記ダストが堆積し、その結果、熱効率が低下し、ダストが偏って堆積したときに乾留ムラが生じて炭化状態にバラツキが生じ、炭化物の品位が低下することになる。   In the external heating rotary kiln, when the generated dry distillation gas is used as a heat source, dust is mixed in the hot air, and the dust accumulates in the heating zone of the external heating rotary kiln. When it is deposited unevenly, dry distillation unevenness occurs and the carbonization state varies, and the quality of the carbide decreases.

また、上記状態にならないようにするためには、定期的にダストを除去する必要があり、そのためには外熱式ロータリーキルンを停止しなければならず生産性の低下と熱効率の低下に繋がる。   Moreover, in order not to become the said state, it is necessary to remove dust regularly, For that purpose, an external heating type rotary kiln must be stopped, and it leads to the fall of productivity and the fall of thermal efficiency.

上記従来技術の問題に鑑みこの発明は、外熱式ロータリーキルンの加熱ゾーンに、熱風と共に運び込まれたダストを、ロータリーキルンの回転とともに掻き集めるようにして熱効率の低下を抑え、かつ、可燃性廃棄物の炭化状態のバラツキを防止するとともに、装置を停止することなく掻き集められたダストを随時装置外に排出できる外熱式ロータリーキルンを提供することを課題とする。   In view of the above-described problems of the prior art, the present invention suppresses a decrease in thermal efficiency by collecting dust carried together with hot air into the heating zone of the externally heated rotary kiln so as to suppress the decrease in thermal efficiency. It is an object of the present invention to provide an externally heated rotary kiln capable of preventing variation in the carbonized state and discharging dust scraped up to the outside of the apparatus at any time without stopping the apparatus.

上記課題を解決するためにこの発明は、可燃性廃棄物を乾留して炭化物を生成し、乾留時に発生した乾留ガスを熱源とする外熱式ロータリーキルンにおいて、内筒の外周面にスパイラルリフタを配設し、外筒の要所に、加熱ゾーン内に堆積するダストの排出口を設けたものであり、具体的には、上記スパイラルリフタは、連続した螺旋翼、または内筒表面の螺旋軌道上に多数の分断翼を複数個配設したものであり、加熱ゾーン内に堆積するダストを上記スパイラルリフタの推力により、上記ダスト排出口に向けて掻き集められるようにしたものである。   In order to solve the above-described problems, the present invention provides a carbide lifter by carbonizing combustible waste, and arranging a spiral lifter on the outer peripheral surface of the inner cylinder in an external heating type rotary kiln using a carbonization gas generated during carbonization as a heat source. Provided, and a discharge port for dust accumulated in the heating zone is provided at a point of the outer cylinder. Specifically, the spiral lifter is provided on a continuous spiral blade or on the spiral orbit of the inner cylinder surface. A plurality of dividing blades are arranged, and dust accumulated in the heating zone is scraped toward the dust discharge port by the thrust of the spiral lifter.

上記の如く構成するこの発明によれば、外熱式ロータリーキルンの加熱ゾーンに熱風と共に送り込まれたダストは、絶えずダスト排出口に向けて掻き集められ、随時装置外に排出されるので熱効率の低下を来すことなく、また、熱伝導が均一になってバラツキのない乾留・炭化が進み、品位の高い炭化物を得ることができる。   According to the present invention configured as described above, the dust sent together with the hot air into the heating zone of the externally heated rotary kiln is constantly scraped toward the dust discharge port and is discharged to the outside of the device at any time. In addition, the heat conduction becomes uniform and the carbonization and carbonization without variation proceed, and a high-quality carbide can be obtained.

次にこの発明の実施の形態を、図面を参照しながら説明する。   Next, embodiments of the present invention will be described with reference to the drawings.

図1は実施例1で、外熱式ロータリーキルン10の内筒11には、その両端に支持環12が一体的に設けられ、この支持環12を介して支持ローラー13に支持され、内筒11にはギヤー14が一体的に嵌められ、このギヤー14にピニオン15が噛み合って所定の速度で回転するようになっている。   FIG. 1 shows a first embodiment in which an inner cylinder 11 of an external heating type rotary kiln 10 is integrally provided with support rings 12 at both ends thereof, and is supported by a support roller 13 via the support rings 12. A gear 14 is integrally fitted to the gear 14, and a pinion 15 is engaged with the gear 14 so as to rotate at a predetermined speed.

上記内筒11の外周面には、中央から外側に向けて反対巻きのスパイラルリフタ16を一体的に設け、その外側に外筒17が全体を覆うように配置され、上記内筒11と外筒17との間に熱風が通過する加熱ゾーン18を形成している。   On the outer peripheral surface of the inner cylinder 11, a spiral lifter 16 that is wound in an opposite direction from the center toward the outside is integrally provided, and an outer cylinder 17 is disposed outside the outer cylinder 17 so as to cover the whole. The inner cylinder 11 and the outer cylinder A heating zone 18 through which hot air passes is formed.

上記加熱ゾーン18には、熱風供給管19が接続され、各熱風供給管19は主管20に繋がり熱風供給源である脱臭炉X(図4参照)に繋がっている。また、外筒17の中央にダスト排出口21が設けられている。なお、上記排出口21は装置の片端に設けてもよく、片端に設ける場合はスパイラルリフタの螺旋方向は一方向となる。   Hot air supply pipes 19 are connected to the heating zone 18, and each hot air supply pipe 19 is connected to a main pipe 20 and connected to a deodorizing furnace X (see FIG. 4) that is a hot air supply source. A dust discharge port 21 is provided at the center of the outer cylinder 17. The discharge port 21 may be provided at one end of the apparatus, and when provided at one end, the spiral direction of the spiral lifter is one direction.

外熱式ロータリーキルン10の内筒11に向けて、減容処理された可燃性廃棄物が、図示しない定量供給装置によってコンスタントに供給され、乾燥・乾留されて炭化が進み、炭化が完了したものは排出口22から排出され、乾留によって発生した乾留ガスは図4に示す脱臭炉Xに送られる。   The combustible waste whose volume has been reduced toward the inner cylinder 11 of the external heating rotary kiln 10 is constantly supplied by a quantitative supply device (not shown), dried and dry-distilled, and carbonized. The dry distillation gas discharged from the discharge port 22 and generated by dry distillation is sent to the deodorizing furnace X shown in FIG.

図2は、図1のA−A矢視図であって、外熱式ロータリーキルン10の内筒11、外筒17、スパイラルリフタ16、熱風排出管23、熱風供給管19、ダスト排出口21が示されている。   2 is an AA arrow view of FIG. 1, and the inner cylinder 11, the outer cylinder 17, the spiral lifter 16, the hot air discharge pipe 23, the hot air supply pipe 19, and the dust discharge port 21 of the external heating rotary kiln 10 are shown. It is shown.

図3は、実施例2の内筒を示し、内筒11の外周面に、中央から両端に向けて反対向きの複数条の仮想螺旋軌道上に多数の分断翼、即ちスパイラルリフタ16aを間欠的に配設されている。この他は、実施例1と同様であるから説明を省略する。   FIG. 3 shows an inner cylinder of the second embodiment, and on the outer peripheral surface of the inner cylinder 11, a large number of divided blades, that is, spiral lifters 16 a are intermittently provided on a plurality of virtual spiral trajectories in opposite directions from the center toward both ends. It is arranged. Since the rest is the same as that of the first embodiment, the description thereof is omitted.

このように構成した実施例2では、加熱ゾーンに堆積したダストは上記スパイラルリフタ16aにより掻き集められ、推力が働いてダスト排出口21(図1,図2参照)に送られるので、随時装置の外へ取り出すことができる。なお、この実施例の場合も排出口を装置の片端に設けることができ、この場合スパイラルリフタ16aは同一方向の螺旋軌道上に配設される。   In Embodiment 2 configured in this manner, the dust accumulated in the heating zone is scraped by the spiral lifter 16a, and thrust is applied to the dust discharge port 21 (see FIGS. 1 and 2). Can be taken out. In this embodiment as well, a discharge port can be provided at one end of the apparatus. In this case, the spiral lifter 16a is disposed on the spiral track in the same direction.

以上説明した通りこの発明によれば、外熱式ロータリーキルンの加熱ゾーンに熱風と共に送り込まれたダストは、連続的、間欠的に設けたスパイラルリフタによって、絶えずダスト排出口に向けて掻き集められ、随時装置の外に排出することができるので、熱効率の低下を来すことなく、また、熱伝導が均一になってバラツキのない乾留・炭化が進み、品位の高い炭化物を得ることができる。また、装置を休止することなく掻き集められたダストを随時排出することができるので生産性が向上し、熱効率を高めることができる。   As described above, according to the present invention, the dust sent together with the hot air into the heating zone of the external heating type rotary kiln is continuously scraped up toward the dust discharge port by the spiral lifter provided continuously and intermittently. Therefore, it is possible to obtain a high-quality carbide without causing a decrease in thermal efficiency, and with uniform heat conduction and non-fluctuation dry distillation / carbonization. In addition, the scraped dust can be discharged at any time without stopping the apparatus, so that productivity is improved and thermal efficiency can be increased.

実施例1に係る外熱式ロータリーキルンの正面図Front view of externally heated rotary kiln according to Example 1 図1のA−A矢視図AA arrow view of FIG. 実施例2に係る外熱式ロータリーキルンの内筒の正面図Front view of the inner cylinder of the externally heated rotary kiln according to the second embodiment 廃棄物処理システムの外熱式ロータリーキルン周辺概略図Schematic view of the external heat rotary kiln around the waste treatment system

符号の説明Explanation of symbols

10 外熱式ロータリーキルン
11 内筒
12 支持環
13 支持ローラー
14 ギヤー
15 ピニオン
16 スパイラルリフタ
17 外筒
18 加熱ゾーン
19 熱風供給管
20 主管
21 ダスト排出口
22 排出口(炭化物の)
23 熱風排出管
DESCRIPTION OF SYMBOLS 10 Outer heat type rotary kiln 11 Inner cylinder 12 Support ring 13 Support roller 14 Gear 15 Pinion 16 Spiral lifter 17 Outer cylinder 18 Heating zone 19 Hot air supply pipe 20 Main pipe 21 Dust discharge port 22 Discharge port (of carbide)
23 Hot air discharge pipe

Claims (2)

可燃性廃棄物を乾留して炭化物を生成し、乾留時に発生した乾留ガスを熱源とする外熱式ロータリーキルンにおいて、内筒の外周面にスパイラルリフタを配設し、外筒の要所に、加熱ゾーン内に堆積するダストの排出口を設けたことを特徴とする外熱式ロータリーキルン。   In an externally heated rotary kiln that produces carbonized carbon by combusting combustible waste and using the carbonized gas generated during carbonization as a heat source, a spiral lifter is installed on the outer peripheral surface of the inner cylinder, and heating is performed at the main points of the outer cylinder. An externally heated rotary kiln characterized by providing a discharge port for dust accumulated in the zone. 上記スパイラルリフタは、連続した螺旋翼、または内筒表面の螺旋軌道上に多数の分断翼を複数個配設したものであり、加熱ゾーン内に堆積するダストを上記スパイラルリフタの推力により、上記ダスト排出口に向けて掻き集められるようにしたことを特徴とする請求項1に記載の外熱式ロータリーキルン。   The spiral lifter is a continuous spiral blade or a plurality of divided blades arranged on a spiral orbit on the surface of the inner cylinder, and the dust accumulated in the heating zone is collected by the thrust of the spiral lifter. The externally heated rotary kiln according to claim 1, wherein the externally heated rotary kiln is scraped toward the discharge port.
JP2005119879A 2005-04-18 2005-04-18 External heating rotary kiln Pending JP2006299010A (en)

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JP2005119879A JP2006299010A (en) 2005-04-18 2005-04-18 External heating rotary kiln

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100789703B1 (en) 2007-09-12 2008-01-02 최성철 Waste's carbonization device
JP2008212782A (en) * 2007-02-28 2008-09-18 Mitsubishi Heavy Ind Ltd Kiln furnace and waste gasification system
GB2498631A (en) * 2011-12-14 2013-07-24 Qinetiq Ltd Thermal processing system
JP2015014446A (en) * 2013-07-08 2015-01-22 株式会社東芝 Indirect heating kiln thermal cracking furnace
GB2529053A (en) * 2014-07-03 2016-02-10 Dps Bristol Holdings Ltd Waste processing apparatus
CN106895413A (en) * 2017-04-01 2017-06-27 四川英诺环保设备有限公司 Decomposing machine
EP3410052A1 (en) 2017-05-31 2018-12-05 Hitachi Zosen Corporation Carbonization apparatus
US10421919B2 (en) 2014-07-03 2019-09-24 Pyrocore S.A. Gasifier

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008212782A (en) * 2007-02-28 2008-09-18 Mitsubishi Heavy Ind Ltd Kiln furnace and waste gasification system
KR100789703B1 (en) 2007-09-12 2008-01-02 최성철 Waste's carbonization device
GB2498631A (en) * 2011-12-14 2013-07-24 Qinetiq Ltd Thermal processing system
JP2015014446A (en) * 2013-07-08 2015-01-22 株式会社東芝 Indirect heating kiln thermal cracking furnace
GB2529053A (en) * 2014-07-03 2016-02-10 Dps Bristol Holdings Ltd Waste processing apparatus
US10421919B2 (en) 2014-07-03 2019-09-24 Pyrocore S.A. Gasifier
CN106895413A (en) * 2017-04-01 2017-06-27 四川英诺环保设备有限公司 Decomposing machine
EP3410052A1 (en) 2017-05-31 2018-12-05 Hitachi Zosen Corporation Carbonization apparatus
JP2018203828A (en) * 2017-05-31 2018-12-27 日立造船株式会社 Carbonization apparatus

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