JPH08285262A - Device and method to feed waste tires into combustion furnace - Google Patents

Device and method to feed waste tires into combustion furnace

Info

Publication number
JPH08285262A
JPH08285262A JP8242095A JP8242095A JPH08285262A JP H08285262 A JPH08285262 A JP H08285262A JP 8242095 A JP8242095 A JP 8242095A JP 8242095 A JP8242095 A JP 8242095A JP H08285262 A JPH08285262 A JP H08285262A
Authority
JP
Japan
Prior art keywords
waste tires
combustion furnace
reaction tube
tip
hot air
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
JP8242095A
Other languages
Japanese (ja)
Inventor
Minoru Asanuma
稔 浅沼
Takeshi Furukawa
武 古川
Tsutomu Shikada
勉 鹿田
Takeshi Konishi
武史 小西
Ichiro Ueno
一郎 上野
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP8242095A priority Critical patent/JPH08285262A/en
Publication of JPH08285262A publication Critical patent/JPH08285262A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE: To provided a feeding device and method by which waste tires can be constantly fed into a combustion furnace, and a stable combustion can be ensured. CONSTITUTION: Waste tires 1 are fed to a reactor by a charging hopper 2. The fed waste tires 1 are first crushed and mixed by a crushing blade 4 to be evened. Then, the reactor is tapered in toward the tip, the waste tires 1 are compressed, and of which the volumes are reduced while being continuously transferred to the tip. Also, the compressed and volume-reduced waste tires 1 work as a sealing member in order to prevent a pyrolytic gas generated at the tip of the reactor from reversing. The waste tires 1 being transferred to the tip of the reactor are heated to raise the temperature by hot air 7 from the outside of the reactor, and are dehydrated and thermally decomposed and become a flammable pyrolytic gas and pyrolytic residue 8. Further, these are charged in a combustion furnace 6 by the hot air 7.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は廃タイヤを燃焼炉へ供給
し、処理する装置及び方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and method for supplying and treating waste tires to a combustion furnace.

【0002】[0002]

【従来の技術】自動車の生産量の増加に伴って、廃タイ
ヤの排出量は増加傾向にあり、社会状況、環境面から廃
タイヤの処理方法は問題となっている。一般的な処理方
法として、そのままの状態で焼却炉に処理する方法があ
るが、かさ高い形状および都市ごみ等に比べ発熱量が高
いことから部分的に焼却炉にホットスポットが発生し、
炉壁耐火物を破損して炉の寿命を短くするという問題が
ある。このような問題点を解決するために、廃タイヤの
専焼炉を設置するあるいは事前に廃タイヤを粉砕・減容
化処理、乾燥処理等の予備処理装置を設け燃焼炉へ供給
する方法がある。
2. Description of the Related Art Along with the increase in automobile production, the amount of waste tires discharged tends to increase, and the method of treating waste tires has become a problem from the social and environmental viewpoints. As a general treatment method, there is a method of treating it in the incinerator as it is, but due to its bulky shape and high calorific value compared to municipal waste, hot spots partially occur in the incinerator,
There is a problem that the furnace wall refractory is damaged to shorten the life of the furnace. In order to solve such a problem, there is a method in which a dedicated burning furnace for waste tires is installed or a waste tire is supplied in advance to a combustion furnace by providing a pretreatment device for crushing / volume reduction treatment, drying treatment and the like.

【0003】特開昭58−222185号公報には燃焼
ガス排出管と残渣カ−ボン燃焼のオフガス排出管を設
け、乾留炉を少なくとも2炉併設させた廃タイヤ乾留炉
が開示されている。
Japanese Unexamined Patent Publication (Kokai) No. 58-222185 discloses a waste tire dry distillation furnace in which a combustion gas exhaust pipe and an off gas exhaust pipe for residual carbon combustion are provided, and at least two dry distillation furnaces are provided side by side.

【0004】特開平5−296427号公報には廃棄物
をガス化炉内で乾留して、可燃性ガスを生ぜしめ、酸素
を供給しながら、ガス管を介して燃焼炉に導入して燃焼
させる乾留ガス化処理焼却装置が開示されている。
In Japanese Unexamined Patent Publication (Kokai) No. 5-296427, waste is dry-distilled in a gasification furnace to generate a combustible gas, and while supplying oxygen, it is introduced into a combustion furnace through a gas pipe and burned. A dry distillation gasification incinerator is disclosed.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、特開昭
58−222185号公報、特開平5−296427号
公報に開示される技術は連続式ではなく間欠式の処理設
備のため、投入した廃タイヤが完全に処理されるまで次
回の廃タイヤを投入することができない。連続式処理設
備にしようとすると、設備費が高くなる、広い設置面積
が必要となる、メンテナンス等の運転維持費がかかる等
の問題がある。廃タイヤの燃焼性を高めるために廃タイ
ヤを細かくしようとすると、燃焼性は上がるが、粉砕コ
ストがかかり、経済的でなくなる。
However, since the techniques disclosed in JP-A-58-222185 and JP-A-5-296427 are intermittent type treatment equipment rather than continuous type treatment, the waste tires used are The next scrap tire cannot be put in until it is completely processed. If a continuous processing facility is used, there are problems that the facility cost is high, a large installation area is required, and operation and maintenance costs such as maintenance are required. If the waste tire is made finer in order to improve the combustibility of the waste tire, the combustibility increases, but the crushing cost increases, which is not economical.

【0006】本発明は上記問題点を解決するためになさ
れたもので、廃タイヤを予備処理設備なしに連続的に燃
焼炉に供給し、安定した処理方法および装置を提供す
る。
The present invention has been made to solve the above problems, and provides a stable treatment method and apparatus by continuously supplying waste tires to a combustion furnace without pretreatment equipment.

【0007】[0007]

【課題を解決するための手段】本発明は廃タイヤを破砕
・混練、圧縮・減容、脱水・熱分解する機能を持つこと
を特徴とする供給装置および供給装置を用いる廃タイヤ
の焼却炉への供給方法である。
SUMMARY OF THE INVENTION The present invention provides a supply device and a waste tire incinerator using the supply device, which has functions of crushing / kneading, compression / volume reduction, dehydration / pyrolysis of a waste tire. Is the method of supply.

【0008】本発明は、燃焼炉への熱風吹込口に設けら
れた反応筒と、反応筒へ廃タイヤを供給するホッパ−を
有してなり、反応筒は先細りに構成され、反応筒中に
は、廃タイヤを反応筒中に供給し先端に移送する押込装
置、廃タイヤを破砕、混合する破砕装置が設けられ、反
応筒の先端は、内部の廃タイヤが脱水、熱分解される程
度に熱風にて熱せられていることを特徴とする廃タイヤ
供給装置である。さらに本発明の廃タイヤの供給方法
は、上記供給装置を用い、反応筒中央部の温度を廃タイ
ヤの熱分解温度以下、反応筒先端部の温度を前記熱分解
温度550℃以上650℃以下に制御して行なうことを
特徴とする。
The present invention comprises a reaction tube provided at the hot air blowing port to the combustion furnace, and a hopper for supplying waste tire to the reaction tube. The reaction tube is tapered, and the reaction tube is provided in the reaction tube. , A pushing device for supplying the waste tire into the reaction tube and transferring it to the tip, a crushing device for crushing and mixing the waste tire are provided, and the tip of the reaction tube is exposed to hot air to the extent that the waste tire inside is dehydrated and thermally decomposed. It is a waste tire supply device characterized by being heated. Furthermore, the method for supplying a waste tire of the present invention uses the above-mentioned supply device, and the temperature of the central portion of the reaction tube is set to the thermal decomposition temperature of the waste tire or less, and the temperature of the tip of the reaction tube is set to the thermal decomposition temperature of 550 ° C. or more and 650 ° C. or less. It is characterized by being controlled.

【0009】反応筒中央部の温度は廃タイヤの熱分解温
度以下が好ましく、より好ましくは100℃以下であ
る。また、供給装置外套の冷却水によって温度調節する
ことができる。
The temperature at the center of the reaction tube is preferably lower than the thermal decomposition temperature of the waste tire, and more preferably 100 ° C. or lower. Further, the temperature can be adjusted by the cooling water in the outer cover of the supply device.

【0010】廃タイヤは300℃から分解が始まり、4
00℃以上になると急激に分解が進行し、500℃に達
すると加硫ゴムの60%が分解ガス化し、650℃以上
に達するとタイヤの非蒸発成分であるカ−ボンブラック
を残すのみとなる。そのため、反応筒先端部の熱分解部
内の最終的な到達温度は、廃タイヤの熱分解温度以上あ
るいは廃タイヤ中の油分が気化する温度以上であればよ
く、550℃以上650℃以下である。
Waste tires begin to decompose at 300 ° C, and 4
When the temperature rises above 00 ° C, the decomposition progresses rapidly, and when it reaches 500 ° C, 60% of the vulcanized rubber is decomposed and gasified, and when it reaches 650 ° C or higher, only carbon black which is a non-evaporating component of the tire remains. . Therefore, the final temperature reached in the thermal decomposition section at the tip of the reaction tube may be 550 ° C. or higher and 650 ° C. or lower as long as it is the thermal decomposition temperature of the waste tire or higher than the temperature at which the oil content in the waste tire vaporizes.

【0011】[0011]

【作用】投入ホッパ−により廃タイヤが反応筒に供給さ
れる。供給された廃タイヤは、まず破砕刃により、破砕
・混練され、均一化される。次いで反応筒は先細りとな
っており、廃タイヤは連続的に先端に移送されながら圧
縮・減容される。また圧縮・減容された廃タイヤは、反
応筒先端部で発生する熱分解ガスの逆流防止のためのシ
ール材として作用する。反応筒先端部に移送された廃タ
イヤは、反応筒外部からの熱風により昇温・加熱され、
脱水・熱分解され、可燃性の熱分解ガス、熱分解残渣と
なる。さらにこれらは熱風により、燃焼炉に投入され
る。
The waste tire is supplied to the reaction tube by the input hopper. The supplied waste tires are first crushed and kneaded by a crushing blade to be homogenized. Next, the reaction tube is tapered, and the waste tire is continuously transferred to the tip and compressed and reduced in volume. Further, the compressed / reduced waste tire acts as a seal material for preventing backflow of pyrolysis gas generated at the tip of the reaction tube. The waste tire transferred to the tip of the reaction tube is heated and heated by the hot air from the outside of the reaction tube,
Dehydrated and pyrolyzed to form flammable pyrolysis gas and pyrolysis residue. Further, these are introduced into the combustion furnace by hot air.

【0012】[0012]

【実施例】以下に本発明の一実施例を添付図面に基づい
て説明する。図1は本発明の一実施例である装置の正面
概略図である。図1において、1は廃タイヤ、2は投入
ホッパー、3はスクリュー、4は破砕刃、5はモータ
ー、6は燃焼炉、7は熱風、8は熱分解ガスと熱分解残
渣、9は冷却水入口、10は冷却水出口である。
An embodiment of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is a schematic front view of an apparatus according to an embodiment of the present invention. In FIG. 1, 1 is a waste tire, 2 is a charging hopper, 3 is a screw, 4 is a crushing blade, 5 is a motor, 6 is a combustion furnace, 7 is hot air, 8 is pyrolysis gas and pyrolysis residue, and 9 is cooling water. The inlet 10 is a cooling water outlet.

【0013】廃タイヤ1はホッパー2に投入され、反応
筒内に供給される。反応筒内に投入された廃タイヤ1は
破砕刃4により破砕・混練される。次いで廃タイヤ1は
スクリュ−軸の回転により連続的に反応筒中央部、反応
筒先端部に移送される。反応筒は先細りとなっており、
廃タイヤ1は移送されながら、圧縮・減容される。さら
に、熱風7により徐々に昇温加熱され脱水、熱分解をう
け、可燃性の熱分解ガスと熱分解残渣8となる。これら
可燃性の熱分解ガスと熱分解残渣8は熱風7により燃焼
炉6に投入される。
The waste tire 1 is put into the hopper 2 and supplied into the reaction tube. The waste tire 1 put into the reaction tube is crushed and kneaded by the crushing blade 4. Then, the waste tire 1 is continuously transferred to the central portion of the reaction tube and the tip portion of the reaction tube by the rotation of the screw shaft. The reaction tube is tapered,
The waste tire 1 is compressed and reduced in volume while being transported. Further, it is gradually heated and heated by the hot air 7 to undergo dehydration and thermal decomposition to become flammable thermal decomposition gas and thermal decomposition residue 8. The flammable pyrolysis gas and the pyrolysis residue 8 are introduced into the combustion furnace 6 by the hot air 7.

【0014】熱風は窒素等の不活性ガスでもよく、空気
でもよく、酸素富化空気でもよい。熱風が空気あるいは
酸素富化空気である場合、熱分解により発生した熱分解
ガスおよび熱分解残渣と混合され、燃焼バ−ナ−の役目
にもなる。
The hot air may be an inert gas such as nitrogen, air, or oxygen-enriched air. When the hot air is air or oxygen-enriched air, the hot air is mixed with the pyrolysis gas generated by pyrolysis and the pyrolysis residue, and also serves as a combustion burner.

【0015】熱分解により発生した熱分解ガスおよび熱
分解残渣は、熱風により燃焼炉内に投入され燃焼炉内の
みで燃焼されてもよく、熱分解ガスおよび熱分解残渣が
熱風と接触した部分より燃焼を開始してもよい。
The pyrolysis gas and the pyrolysis residue generated by the pyrolysis may be introduced into the combustion furnace by hot air and burned only in the combustion furnace. From the portion where the pyrolysis gas and the pyrolysis residue are in contact with the hot air, Combustion may be initiated.

【0016】熱風による反応筒先端部の加熱方法として
は熱風発生機により熱風を発生し、加熱に用いてもよい
し、燃焼排ガスを加熱に用いてもよい。
As a method of heating the tip of the reaction tube with hot air, hot air may be generated by a hot air generator and used for heating, or combustion exhaust gas may be used for heating.

【0017】本発明装置内の廃タイヤの押し込み装置に
相当する部分の移送方法は、廃タイヤを定常的に移送で
きるものであればよく、スクリュ−の回転による移送、
ピストン式による移送等を挙げることができる。
The method of transferring the portion corresponding to the device for pushing in the waste tire in the apparatus of the present invention may be any method as long as the waste tire can be transferred steadily, such as transfer by rotation of the screw,
The transfer by a piston type can be mentioned.

【0018】実施例1は本発明の装置を5t/dayの
小型燃焼炉に設置し、廃タイヤを1t/dayの割合で
供給し、熱風空気により、乾留、熱分解を行なった場合
である。結果を表1に示す。
Example 1 is a case where the apparatus of the present invention is installed in a small combustion furnace of 5 t / day, waste tires are supplied at a rate of 1 t / day, and carbonization and thermal decomposition are carried out with hot air. The results are shown in Table 1.

【0019】実施例2は熱風空気の代わりに熱風窒素を
用いた場合であり、それ以外は実施例1と同様である。
結果を表1に示す。
The second embodiment is the same as the first embodiment except that hot air nitrogen is used instead of the hot air.
The results are shown in Table 1.

【0020】比較例は本発明の装置を用いず、廃タイヤ
を5t/dayの小型燃焼炉上部から直接投入した場合
である。結果を表1に示す。
A comparative example is a case where a waste tire is directly charged from the upper part of a small combustion furnace of 5 t / day without using the apparatus of the present invention. The results are shown in Table 1.

【0021】[0021]

【表1】 [Table 1]

【0022】表1より、実施例1、2とも未燃炭素、一
酸化炭素の発生量は比較例と比べて少なく、不完全燃焼
することなく、燃焼性は良好であった。又、環境上問題
となる窒素酸化物の発生量も少なく、極めて安定した燃
焼が行なえた。
From Table 1, in Examples 1 and 2, the amounts of unburned carbon and carbon monoxide generated were smaller than those of Comparative Example, incomplete combustion did not occur, and the combustibility was good. In addition, the amount of nitrogen oxide, which is an environmental problem, was small, and extremely stable combustion was possible.

【0023】[0023]

【発明の効果】粉砕、脱水等の予備処理設備の必要もな
く、設備の損耗、破損等の問題もなく、燃焼炉に廃タイ
ヤを供給できる。局部的なホットスポットの発生が抑え
られ、焼却設備において処理できるなど汎用性が高い。
また、廃タイヤをガス状の燃料として燃焼炉に投入する
ことから安定した燃焼炉の操業が可能となる。
EFFECTS OF THE INVENTION Waste tires can be supplied to a combustion furnace without the need for pretreatment equipment such as crushing and dehydration, and without problems such as equipment wear and tear. Generation of local hot spots is suppressed, and it is highly versatile in that it can be processed in an incinerator.
Further, since the waste tire is put into the combustion furnace as a gaseous fuel, stable operation of the combustion furnace becomes possible.

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

【図1】本発明の一実施例を示す図である。FIG. 1 is a diagram showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 廃タイヤ 2 投入ホッパー 3 スクリュー 4 破砕刃 5 モーター 6 燃焼炉 7 熱風 8 熱分解ガス、熱分解残渣 9 冷却水入口 10 冷却水出口 1 Waste tire 2 Input hopper 3 Screw 4 Crushing blade 5 Motor 6 Combustion furnace 7 Hot air 8 Pyrolysis gas, pyrolysis residue 9 Cooling water inlet 10 Cooling water outlet

───────────────────────────────────────────────────── フロントページの続き (72)発明者 小西 武史 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 上野 一郎 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Takeshi Konishi, 1-2, Marunouchi, Chiyoda-ku, Tokyo Japan Steel Pipe Co., Ltd. (72) Ichiro Ueno, 1-2, Marunouchi, Chiyoda-ku, Tokyo Main Steel Pipe Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 廃タイヤを燃焼炉に供給する装置に関
し、燃焼炉への熱風吹込口に設けられた反応筒と、反応
筒へ廃タイヤを供給するホッパ−を有してなり、反応筒
は先細りに構成され、反応筒中には、廃タイヤを反応筒
中に供給し先端に移送する押込装置、廃タイヤを破砕、
混合する破砕装置が設けられ、反応筒の先端は、内部の
廃タイヤが脱水、熱分解される程度に熱風にて熱せられ
ていることを特徴とする廃タイヤの燃焼炉への供給装
置。
1. An apparatus for supplying waste tires to a combustion furnace, comprising a reaction tube provided at a hot air blowing port to the combustion furnace, and a hopper for supplying waste tires to the reaction tube. The taper is configured to be tapered, and the reaction tube has a pushing device for supplying the waste tire into the reaction tube and transferring it to the tip, crushing the waste tire,
A device for supplying waste tires to a combustion furnace, wherein a crushing device for mixing is provided, and the tip of the reaction cylinder is heated by hot air to the extent that the waste tires inside are dehydrated and thermally decomposed.
【請求項2】 請求項1に記載の供給装置を用い、反応
筒中央部の温度を廃タイヤの熱分解温度以下、反応筒先
端部の温度を550℃以上650℃以下に制御して行な
うことを特徴とする廃タイヤの燃焼炉への供給方法。
2. The supply device according to claim 1, wherein the temperature of the central portion of the reaction tube is controlled to be equal to or lower than the thermal decomposition temperature of the waste tire and the temperature of the tip portion of the reaction tube is controlled to 550 ° C. or higher and 650 ° C. or lower. And a method for supplying waste tires to a combustion furnace.
JP8242095A 1995-04-07 1995-04-07 Device and method to feed waste tires into combustion furnace Pending JPH08285262A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8242095A JPH08285262A (en) 1995-04-07 1995-04-07 Device and method to feed waste tires into combustion furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8242095A JPH08285262A (en) 1995-04-07 1995-04-07 Device and method to feed waste tires into combustion furnace

Publications (1)

Publication Number Publication Date
JPH08285262A true JPH08285262A (en) 1996-11-01

Family

ID=13774104

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8242095A Pending JPH08285262A (en) 1995-04-07 1995-04-07 Device and method to feed waste tires into combustion furnace

Country Status (1)

Country Link
JP (1) JPH08285262A (en)

Similar Documents

Publication Publication Date Title
US5186740A (en) Method for preheating scrap iron by pyrolysis of resinous residues contained therein, with total recovery of their energy content and improvement of the steelmaking cycle
US6178899B1 (en) Waste treatment method and waste treatment apparatus
CA1075003A (en) Process and apparatus for the production of combustible gas
US20120210645A1 (en) Multi-ring Plasma Pyrolysis Chamber
JP2000104082A (en) Method and apparatus for producing refuse derived solid fuel
MXPA06012084A (en) Method and apparatus for gasifying waste automotive tires to produce high quality solid carbon and non-condensable synthesis gas.
CN101871649A (en) System for pyrolyzing and burning sludge at low temperature
IE46544B1 (en) Sewage sludge pyrolysis
JP3771887B2 (en) How to use activated sludge
JPH08285262A (en) Device and method to feed waste tires into combustion furnace
JP3713991B2 (en) Waste treatment method and waste treatment facility
JPH11270824A (en) Waste treatment and facility therefor
KR100340263B1 (en) Apparatus and method for the treatment of mixed wastes with high liquid fraction by plasma pyrolysis/gasfication and melting
JP2005003359A (en) Waste processing method and facility
CN218914941U (en) Step-by-step solid waste handles high temperature incinerator
JPS6246117A (en) Gasifying burner for solid combustion matter
CN213480229U (en) Waste pyrolysis pretreatment device
JPH11270823A (en) Equipment and method for waste disposal
CN214009225U (en) Incineration treatment device for combustible industrial solid waste
CN117720938A (en) Organic waste carbonization combustion integrated device
JP2000279916A (en) Waste treatment
CN2758598Y (en) Gasifying incinerator for medical refuse
JPS6318994B2 (en)
JPH09124155A (en) Coal supplying device and supplying method to vertical type furnace
CN117025235A (en) Organic matter material anaerobic pyrolysis system and organic matter material anaerobic pyrolysis method

Legal Events

Date Code Title Description
A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20011113