JP2002166257A - Cooling method for heat decomposition residue generated from heat decomposition furnace and cooling device for the heat decomposition residue - Google Patents

Cooling method for heat decomposition residue generated from heat decomposition furnace and cooling device for the heat decomposition residue

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Publication number
JP2002166257A
JP2002166257A JP2000403826A JP2000403826A JP2002166257A JP 2002166257 A JP2002166257 A JP 2002166257A JP 2000403826 A JP2000403826 A JP 2000403826A JP 2000403826 A JP2000403826 A JP 2000403826A JP 2002166257 A JP2002166257 A JP 2002166257A
Authority
JP
Japan
Prior art keywords
cooling
residue
pyrolysis residue
pyrolysis
steel ball
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
JP2000403826A
Other languages
Japanese (ja)
Inventor
Keiichi Muramoto
恵一 村本
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.)
Taiyo Machinery Co Ltd
Original Assignee
Taiyo Machinery 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 Taiyo Machinery Co Ltd filed Critical Taiyo Machinery Co Ltd
Priority to JP2000403826A priority Critical patent/JP2002166257A/en
Publication of JP2002166257A publication Critical patent/JP2002166257A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a cooling method and a cooling device for heat decomposition residue which has a good efficiency in cooling the heat decomposition residue and is capable of proceed simultaneous separation of char from other residue upon the reuse of the char in the residue generated from the heat decomposition in a heat decomposition furnace. SOLUTION: The cooling method comprises: To mix a large number of a small diametrical steel balls 1 with the highly heated residue A generated by heat decomposition of trash, or the like, and to make the cooling of the residue A by transfer of the heat of the heat decomposition residue A to the steel balls 1, and then to separate the steel balls 1 from the heat decomposition residue A so as to residue the balls 1 for repeating the initial process after they are cooled down.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する分野】本発明は、主にゴミ等の熱分解に
より発生した熱分解残渣を冷却し、その熱分解残渣のチ
ャー(炭化物)を再利用するための熱分解残渣の冷却を
行うための熱分解炉からの熱分解残渣の冷却方法と熱分
解残渣の冷却装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to cooling a pyrolysis residue mainly generated by pyrolysis of refuse and the like, and cooling the pyrolysis residue for recycling the char (carbide) of the pyrolysis residue. The present invention relates to a method for cooling a thermal decomposition residue from a thermal decomposition furnace and a device for cooling a thermal decomposition residue.

【0002】[0002]

【従来の技術】最近、都市ゴミ等の焼却処理の方向とし
て、ダイオキシン発生問題等から、ゴミを直接に燃焼さ
せずに、熱分解させて可燃ガスとチャーとを取り出す熱
分解炉が多様される方向にある。こうした熱分解炉から
取り出される熱分解残渣は、500℃前後の高温であ
り、そのチャーを分離し、取り出して再利用すためには
冷却が必要である。
2. Description of the Related Art Recently, pyrolysis furnaces for extracting flammable gas and char by pyrolysis without directly burning garbage due to problems such as dioxin generation have been diversified as the direction of incineration of municipal garbage. In the direction. The pyrolysis residue taken out of such a pyrolysis furnace has a high temperature of around 500 ° C., and requires cooling to separate its char, take it out, and reuse it.

【0003】ゴミ焼却炉のボトム灰等の冷却について
は、これに直接に散水して冷却しても大して問題はない
が、熱分解炉から出る熱分解残渣は、そのチャー(炭化
物)を再利用(主に燃料)するため、これに直接散水す
る方式を採ることは、塊を形成したり、また、水分含有
率が上がることで再利用に不都合であり、これまでは、
熱分解残渣の冷却方法として、回転ドラム冷却方式と、
その搬出、移送系の振動コンベ等において、間接冷却
(水冷)方式を採用していた。
[0003] Regarding the cooling of bottom ash and the like in a garbage incinerator, there is no problem even if water is directly sprayed on the bottom ash, but the pyrolysis residue from the pyrolysis furnace reuses its char (carbide). (Mainly fuel), it is inconvenient to reuse water directly by adopting the method of watering because it forms lumps and increases the water content.
As a cooling method of the pyrolysis residue, a rotating drum cooling method,
An indirect cooling (water-cooling) system was adopted for the vibration conveyor of the carrying-out and transfer system.

【0004】[0004]

【発明が解決しようとする課題】上述した熱分解残渣の
冷却方式では、時間を要したり、間接冷却手段であるが
ために高価についたり、冷却効率的についても、設備コ
スト的にについても不利であった。また、熱分解炉から
取り出された熱分解残渣は、チャー(炭化物)と、ゴミ
に混入されている種々の不燃物(金属物を含む)が混在
しており、両者が塊となって一体化していたりすること
が多いので、単に自然冷却や間接冷却を行っても、いづ
れ両者を分離して取り出すための工程が必要がある。
The above-mentioned cooling method of the pyrolysis residue requires time, is expensive due to the indirect cooling means, has disadvantages in terms of cooling efficiency and equipment cost. Met. In addition, the pyrolysis residue taken out of the pyrolysis furnace contains char (carbide) and various non-combustible substances (including metal substances) mixed in the garbage, and both are integrated into a lump. Therefore, a process for separating and taking out both of them is required even if only natural cooling or indirect cooling is performed.

【0005】本発明は、こうした従来技術の問題点に鑑
み、熱分解炉からの熱分解残渣のチャーの再利用に際
し、その熱分解残渣を冷却する方法として、冷却効率に
優れ、同時にチャーと他の残渣との分離をも同時進行さ
せることのできる新たな熱分解炉からの熱分解残渣の冷
却方法と熱分解残渣の冷却装置を提供することを目的と
する。
[0005] In view of the problems of the prior art, the present invention provides a method of cooling the pyrolysis residue upon reusing the pyrolysis residue from the pyrolysis furnace, which is excellent in cooling efficiency and at the same time as the char and other methods. It is an object of the present invention to provide a method for cooling a pyrolysis residue from a new pyrolysis furnace and a cooling device for the pyrolysis residue, which can simultaneously proceed with separation of the pyrolysis residue.

【0006】[0006]

【課題を解決するための手段】本発明にかかる熱分解炉
からの熱分解残渣の冷却方法は、上記目的を達成するた
めに、ゴミ等の熱分解により得られた高温の熱分解残渣
を冷却する熱分解炉からの熱分解残渣の冷却方法であっ
て、前記高温の熱分解残渣Aに多数の小径の鋼球1を付
加して混合し、前記鋼球1と前記熱分解残渣Aとの接触
によって熱分解残渣A中のチャーA1の塊をほぐし、ま
た、他の残渣A2との分離を図りながら該熱分解残渣A
の熱を前記鋼球1に伝播せしめる工程、前記鋼球1と熱
分解残渣Aとを分離する工程、及び前記鋼球1を冷却し
て後に再び前記当初の工程に用いる還流工程、からな
る、という手段を講じたものである。
According to the present invention, there is provided a method for cooling a pyrolysis residue from a pyrolysis furnace according to the present invention. A method of cooling a pyrolysis residue from a pyrolysis furnace, wherein a number of small-diameter steel balls 1 are added to and mixed with the high-temperature pyrolysis residue A, and the steel balls 1 and the pyrolysis residue A are mixed. By contact, the lump of the char A1 in the pyrolysis residue A is loosened, and the pyrolysis residue A is separated from the other residue A2 while being separated.
A step of transmitting the heat of the steel ball 1 to the steel ball 1, a step of separating the steel ball 1 and the pyrolysis residue A, and a refluxing step of cooling the steel ball 1 and then using it again in the initial step. That is the means to take.

【0007】本発明の方法において、前記鋼球1が、直
径1ミリ乃至3ミリであることが好ましい。
In the method of the present invention, the steel ball 1 preferably has a diameter of 1 mm to 3 mm.

【0008】本発明にかかる熱分解炉からの熱分解残渣
の冷却装置は、上記目的を達成するために、多数の小径
の鋼球1と、前記高温の熱分解残渣Aに前記鋼球1を付
加して混合する振動ドラム2と、前記鋼球1と熱分解残
渣Aとを分離する分離手段3と、前記鋼球1を冷却する
冷却手段4と、冷却された前記鋼球1を前記振動ドラム
2に還流する移送手段5とからなる、という手段を講じ
たものである。
[0008] In order to achieve the above object, the apparatus for cooling a pyrolysis residue from a pyrolysis furnace according to the present invention includes a number of small-diameter steel balls 1 and the steel balls 1 on the high-temperature pyrolysis residue A. A vibrating drum 2 to be added and mixed; separating means 3 for separating the steel ball 1 and the pyrolysis residue A; cooling means 4 for cooling the steel ball 1; And a transfer means 5 for returning to the drum 2.

【0009】本発明の装置において、前記鋼球1が、直
径1ミリ乃至3ミリであるのが好ましい。
In the apparatus of the present invention, the steel ball 1 preferably has a diameter of 1 to 3 mm.

【0010】本発明の装置において、前記分離手段3が
磁気吸着機3aであるのが好ましい。
In the apparatus of the present invention, it is preferable that the separating means 3 is a magnetic attraction machine 3a.

【0011】本発明の装置において、前記冷却手段4が
前記鋼球1が通過する筒状体4aと、該筒状体4aの周
囲に設けられた水冷ジャケット4bとからなる間接水冷
方式であるのが好ましい。
In the apparatus of the present invention, the cooling means 4 is of an indirect water cooling type comprising a cylindrical body 4a through which the steel balls 1 pass and a water cooling jacket 4b provided around the cylindrical body 4a. Is preferred.

【0012】[0012]

【発明の実施の形態】本発明の方法において、前記高温
の熱分解残渣Aに多数の小径の鋼球1を付加して混合す
る手段としては、適宜の手段を用いてよく、例えば、実
施例の如き、鋳物砂を落とすのに用いる振動ドラム、或
いはロータリーキルンが好ましい。前述した振動ドラム
には、通常、ドラム本体を冷却する手段を備えているの
で、これによっても熱分解残渣Aの間接冷却効果が望め
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In the method of the present invention, as a means for adding a large number of small-diameter steel balls 1 to the high-temperature pyrolysis residue A and mixing them, any suitable means may be used. And a vibrating drum or a rotary kiln used to remove foundry sand. Since the above-mentioned vibrating drum is usually provided with a means for cooling the drum main body, an effect of indirect cooling of the pyrolysis residue A can be expected also by this means.

【0013】また、振動ドラムであれば、鋳物砂を落と
すのに必要な振動を発生するので、前記鋼球1と前記熱
分解残渣Aとの接触によって熱分解残渣A中のチャーA
1の塊をほぐし、また、他の残渣A2との分離を図りな
がら該熱分解残渣Aの熱を前記鋼球1に伝播せしめるの
に好適である。そして、前記鋼球1と熱分解残渣Aとを
分離する工程として、鋼球1のみを熱分解残渣Aから分
離する場合には、適宜の手段、例えば、実施例の如く磁
気吸着機を用いることでチャーA1との分離は容易に図
ることが可能である。
In the case of a vibrating drum, the vibration required for dropping the foundry sand is generated. Therefore, the contact between the steel ball 1 and the pyrolysis residue A causes the formation of the char A in the pyrolysis residue A.
It is suitable to spread the heat of the pyrolysis residue A to the steel ball 1 while loosening the lump and separating it from the other residue A2. When only the steel ball 1 is separated from the pyrolysis residue A in the step of separating the steel ball 1 from the pyrolysis residue A, appropriate means, for example, a magnetic adsorber as in the embodiment is used. Thus, separation from the char A1 can be easily achieved.

【0014】唯、熱分解残渣Aには、チャーA1の他に
ゴミ等に含まれていた不燃性の異物(金属製品、陶器
等)であるその他の残渣A2がそのまま残っているの
で、何れこれらも分離してやる必要があり、こうした工
程を、鋼球1の分離工程と同時に行うか、或いはその前
後に行うか、また、鋼球1の分離工程とチャーA1の分
離工程と異物であるその他の残渣A2の分離工程との三
つの工程に分けて行うかは適宜選択してよい。
However, in the pyrolysis residue A, in addition to the char A1, other residues A2, which are nonflammable foreign substances (metal products, pottery, etc.) contained in dust and the like, remain as they are. It is necessary to separate these steps simultaneously with or before or after the step of separating the steel ball 1, or to separate the step of separating the steel ball 1 and the step of separating the char A1 from the other residue that is a foreign substance. Whether to perform the separation into three steps of the separation step of A2 may be appropriately selected.

【0015】前記鋼球1を冷却して後に再び前記当初の
工程に用いるための還流工程は、適宜の手段、例えばコ
ンベア移送手段、空気搬送手段、或いは磁気、電気的手
段等の公知の手段を適宜採用して良い。また、前記鋼球
1については、その直径が1ミリ乃至3ミリであること
が好ましいが、一般には、ショットブラストで用いられ
ている鋼球がこれに該当するので、そのままこれを用い
て良い。 しかし、その他に特別にやや大径の鋼球1
(例えば、ベアリング用ボール等)を製造して用いるこ
とも可能である。
The recirculation step for cooling the steel ball 1 and then using it again in the initial step is performed by a suitable means, for example, a conveyer transferring means, a pneumatic conveying means, or a known means such as magnetic or electric means. It may be adopted as appropriate. The steel ball 1 preferably has a diameter of 1 mm to 3 mm, but generally, a steel ball used in shot blasting corresponds to this, so that it may be used as it is. However, other specially large steel balls 1
It is also possible to manufacture and use (for example, bearing balls and the like).

【0016】この鋼球1が熱分解残渣Aに対する熱媒体
(メディア)として用いられることで、熱分解残渣Aか
ら大きな熱量を効率良く吸収して、熱分解残渣Aの温度
を大幅に、概ね、80℃程度に下げることが出来るので
ある。そして、熱の伝播を経た鋼球1を次ぎに冷却する
ことで、この鋼球1を、還流させて、以て、再度、初期
工程の熱分解残渣Aに投入することができる。こうした
鋼球(ショットブラスト用)を熱媒体として利用する考
え方は、本発明独特のものと言える。
Since the steel ball 1 is used as a heating medium (media) for the pyrolysis residue A, a large amount of heat is efficiently absorbed from the pyrolysis residue A, and the temperature of the pyrolysis residue A is largely reduced. It can be lowered to about 80 ° C. Then, by cooling the steel ball 1 which has passed through the heat, the steel ball 1 is refluxed, and thus can be put into the pyrolysis residue A in the initial step again. The idea of using such a steel ball (for shot blast) as a heat medium can be said to be unique to the present invention.

【0017】勿論、上記鋼球1を熱分解残渣Aに投入す
るについて、振動ドラムで行う場合に、熱分解残渣Aに
大して鋼球1が接触し、摩擦することになるので、熱分
解残渣A中のチャーA1の塊をほぐしたり、チャーA1
と他の残渣A2との付着、例えば、金属異物等との付着
からチャーを剥離させることが出来る作用もあり、熱媒
体のみならず、チャーA1の分離を促進する役目も果た
すものである。
Of course, when the steel balls 1 are introduced into the pyrolysis residue A by using a vibrating drum, the steel balls 1 come into contact with the pyrolysis residue A and cause friction. Unravel the lump of Char A1 inside, and Char A1
Has the effect of separating the char from the adhesion with the other residue A2, for example, the adhesion with a metal foreign matter, and also plays a role of promoting the separation of the char A1 as well as the heat medium.

【0018】[0018]

【実施例】本発明にかかる熱分解炉からの熱分解残渣の
冷却方法と熱分解残渣の冷却装置の好適実施例につい
て、図面を参照して以下詳述する。図1及び図2に示す
ように、この熱分解炉13からの熱分解残渣の冷却装置
は、ゴミ等の熱分解により得られた高温の熱分解残渣を
冷却する冷却装置として、多数の小径の鋼球1(図中、
小丸で示す)と、前記高温の熱分解残渣A(図中、点で
示す)に前記鋼球1を付加して振動させながら混合する
振動ドラム2と、前記鋼球1と熱分解残渣Aとを分離す
る分離手段3と、前記鋼球1を冷却する冷却手段4と、
冷却された前記鋼球1を前記振動ドラム2に還流する移
送手段5とからなる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of a method and apparatus for cooling a pyrolysis residue from a pyrolysis furnace according to the present invention will be described in detail below with reference to the drawings. As shown in FIGS. 1 and 2, the cooling device for the pyrolysis residue from the pyrolysis furnace 13 is a cooling device for cooling a high-temperature pyrolysis residue obtained by pyrolysis of dust or the like, and has a large number of small diameters. Steel ball 1 (in the figure,
A vibrating drum 2 for adding the steel ball 1 to the high-temperature pyrolysis residue A (indicated by a dot in the drawing) and mixing while vibrating; and the steel ball 1 and the pyrolysis residue A A cooling means 4 for cooling the steel ball 1,
Transfer means 5 for returning the cooled steel balls 1 to the vibrating drum 2.

【0019】上記振動ドラム2は、それ自体公知のもの
であり、その詳細説明を省くが、ここでは、その原理図
を図2として参考に示す。 要するに、振動モータ2a
に、より共振バネ2bかい介してドラム本体2cをその
振動中心Oを中心とし揺動させるものであり、2d・2
dは、ベースに支持する防振バネである。 そして、一
般には、その本体2cを水冷するクーリングタワー12
a及びポンプ12b・12からなる冷却手段12を備え
ている。また、図示していないが、この振動ドラム2に
は、供給されてくる熱分解残渣Aが450℃〜500℃
の高温であることで、その熱分解残渣A中のチャー等が
燃焼してしまわないように、不活性ガス、ここでは窒素
ガスが充填されている。
The above-mentioned vibrating drum 2 is known per se, and detailed description thereof will be omitted. Here, a principle diagram thereof is shown as a reference in FIG. In short, the vibration motor 2a
In addition, the drum body 2c is swung about its vibration center O through the resonance spring 2b.
d is an anti-vibration spring supported on the base. In general, the cooling tower 12 that cools the main body 2c with water is used.
a and a cooling means 12 comprising pumps 12b. Although not shown, the supplied thermal decomposition residue A is supplied to the vibrating drum 2 at 450 ° C. to 500 ° C.
Is charged with an inert gas, here a nitrogen gas, so as to prevent the char and the like in the pyrolysis residue A from burning due to the high temperature.

【0020】6は、赤外線温度監視手段であり、振動ド
ラム2からの熱分解残渣A及び鋼球1の出口温度が10
0℃乃至80℃程度に降下しているかどうか検知し、高
ければ鋼球1の供給比率を増加させるよう制御できる構
成とされている。前記鋼球1は、直径1.6ミリのもの
を用いる。 この鋼球1については、その他に、直径1
ミリ〜3ミリのものを用いるのが好ましい。 この鋼球
1は、熱分解残渣Aの2トン/時間に対して40トン/
時間の比率で、定量切り出しで供給される。
Reference numeral 6 denotes an infrared temperature monitoring means for detecting the thermal decomposition residue A from the vibration drum 2 and the outlet temperature of the steel ball 1 at 10
It is configured to detect whether the temperature has dropped to about 0 ° C. to 80 ° C., and to control the supply rate of the steel balls 1 to be increased if the temperature is high. The steel ball 1 has a diameter of 1.6 mm. This steel ball 1 has a diameter of 1
It is preferable to use one having a diameter of 3 mm to 3 mm. This steel ball 1 is 40 tons / hour for 2 tons / hour of the pyrolysis residue A.
It is supplied in quantitative cuts at a ratio of time.

【0021】そして、前記振動ドラム2の出口には、粗
目篩機7が設けられ、チャー等の熱分解残渣A及び鋼球
1は通過させ、残渣中の粗大物、陶器破片や鋳物等の金
属製品片等の未燃物を予め取り出し、粗物処理工程に移
行させるように構成されている。 また、この粗目篩機
7の次ぎには、細目篩機8が設けられ、更に、3mm径
程度以上の小石や小物残渣と鋼球1及びチャー等の残渣
を篩い分ける。
At the outlet of the vibrating drum 2, a coarse sieving machine 7 is provided, through which the pyrolysis residue A such as char and the steel ball 1 are passed, and the coarse substance in the residue, metal fragments such as ceramic fragments and castings. An unburned material such as a product piece is taken out in advance, and the process is shifted to a rough material processing step. In addition to the coarse sieve 7, a fine sieve 8 is provided, and further sieves small pebbles or small residues having a diameter of about 3 mm or more and residues such as steel balls 1 and char.

【0022】上記細目篩機8を出たチャー等の熱分解残
渣A及び鋼球1は前記分離手段3に移行されるが、前記
分離手段3としては、ここでは、二段階の磁気吸着機3
a・3bが用いられている。 これは、固定磁石の周り
を回動自在の円筒に鋼球1させ、チャー等の非磁性体の
熱分解残渣Aを所定位置で落下させ、所定角度回転した
位置で前記磁石が存在しないことで、その位置で鋼球1
が落下し、これにより両者が選別されて取り出される構
成とされているものであり、これ自体も、鋳物砂等の選
別に利用される範囲としては公知の構成のものである。
The pyrolysis residue A such as char and the steel ball 1 which have exited the fine sieving machine 8 are transferred to the separating means 3. The separating means 3 is a two-stage magnetic adsorber 3 here.
a.3b is used. This is because the steel ball 1 is made into a cylinder that is rotatable around a fixed magnet, the pyrolysis residue A of a non-magnetic material such as char is dropped at a predetermined position, and the magnet is not present at a position rotated by a predetermined angle. , Steel ball 1 at that position
Are dropped, whereby the two are separated and taken out, and the structure itself is a known configuration as a range used for sorting casting sand or the like.

【0023】前記冷却手段4は、図1に示す如く、ここ
では、前記鋼球1が通過するチャンバー4aに冷却水が
循環されており、これによって、鋼球1が間接的に冷却
され、80℃から30〜40℃程度、即ち、略常温程度
にまで冷却される方式が採用されている。 前記冷却水
は、パイプライン、タンク4bを介してクーリングタワ
ー4cに繋がれ、ポンプ4e・4fによって循環される
構成とされている。しかし乍ら、こうした間接水冷方式
以外に、鋼球1を直接水中に通過させ、しかる後に高速
のエアーを吹き付けることで、鋼球1を乾燥させて、以
て初期工程に還流させるようにしても良い。
As shown in FIG. 1, the cooling means 4 here circulates cooling water in a chamber 4a through which the steel balls 1 pass, thereby cooling the steel balls 1 indirectly. A method of cooling from about 30 to about 40 ° C., that is, about room temperature is employed. The cooling water is connected to a cooling tower 4c via a pipeline and a tank 4b, and is circulated by pumps 4e and 4f. However, besides such an indirect water cooling method, the steel ball 1 may be dried directly by passing the steel ball 1 directly into water and then blowing high-speed air, thereby returning the steel ball 1 to the initial step. good.

【0024】上記冷却手段4のチャンバー4aを出た鋼
球1は、風選機9に送られ、バグフィルターを介して、
ブロワー10による吸引風によって、鋼球1に付着のチ
ャー等の微粉を吹き飛ばすように構成されている。 勿
論、この風選によっても温度降下が期待でき、殆ど常温
程度へ冷却でき、その後が、メディアタンク11に戻さ
れ、初期の供給状態に至るのである。
The steel ball 1 that has exited the chamber 4a of the cooling means 4 is sent to a wind separator 9 and passes through a bag filter.
The blower 10 is configured to blow off fine powder such as char adhered to the steel ball 1 by the suction wind. Of course, a temperature drop can be expected by this air selection, and the temperature can be almost cooled to about room temperature, and thereafter, it is returned to the media tank 11 to reach an initial supply state.

【0025】本発明のゴミ等の熱分解により得られた高
温の熱分解残渣を冷却する熱分解炉からの熱分解残渣の
冷却方法は、次の工程で実施される。先ず、前記高温の
熱分解残渣に多数の小径の鋼球1を付加して混合し、前
記鋼球1と前記熱分解残渣Aとの接触によって熱分解残
渣A中のチャーA1の塊をほぐし、また、他の残渣A2
との分離を図りながら該熱分解残渣Aの熱を前記鋼球1
に伝播せしめる。次いで、前記鋼球1と熱分解残渣Aと
を分離する。そして、前記鋼球1を冷却して後に再び前
記当初の工程に用いるべく還流させる。
The method for cooling a pyrolysis residue from a pyrolysis furnace for cooling a high-temperature pyrolysis residue obtained by pyrolysis of dust or the like according to the present invention is carried out in the following steps. First, a large number of small-diameter steel balls 1 are added to and mixed with the high-temperature pyrolysis residue, and the lump of char A1 in the pyrolysis residue A is loosened by contact between the steel ball 1 and the pyrolysis residue A, In addition, other residue A2
Heat of the pyrolysis residue A while separating the steel ball 1
To propagate. Next, the steel ball 1 and the pyrolysis residue A are separated. Then, the steel ball 1 is cooled and then refluxed again for use in the initial process.

【0026】上述した熱分解残渣Aの熱を前記鋼球1に
伝播させる場合、熱分解残渣Aの温度を80℃程度に降
下させることができるライン設計を行う。 この場合、
前記鋼球1が、直径1.6ミリであるものを、熱分解残
渣Aとの重量比で、1対20で用いているが、その鋼球
1の直径については、1ミリ乃至3ミリを用いてい良
く、その重量比についても、1対20の範囲とすること
が好ましい。また、鋼球1と熱分解残渣Aとの混合手段
として、上記実施例の振動ドラム2の他にロータリーギ
ルンを用いても実施できる。
When the heat of the above-described pyrolysis residue A is transmitted to the steel ball 1, a line design capable of lowering the temperature of the pyrolysis residue A to about 80 ° C. is performed. in this case,
The steel ball 1 having a diameter of 1.6 mm is used in a weight ratio to the pyrolysis residue A of 1:20, and the diameter of the steel ball 1 is 1 mm to 3 mm. It may be used, and its weight ratio is preferably in the range of 1:20. In addition, as a mixing means of the steel ball 1 and the pyrolysis residue A, a rotary giln can be used in addition to the vibrating drum 2 of the above embodiment.

【0027】[0027]

【発明の効果】本発明の方法及び装置によれば、熱分解
炉からの熱分解残渣を冷却するに際して、鋼球を熱媒体
として利用することで、従来の単純な水冷方式或いは自
然冷却方式に比べて、冷却能率を飛躍的に向上させるこ
とができる利点が有り、合わせて、鋼球と熱分解残渣と
の振動混合により、熱分解残渣のチャーのほぐし、他の
残渣に付着のチャーの分離を同時に進行させることがで
きて、その後のチャーの分離を容易ならしめる利点もあ
る。
According to the method and apparatus of the present invention, when cooling the pyrolysis residue from the pyrolysis furnace, the steel ball is used as a heat medium, thereby reducing the conventional simple water cooling system or natural cooling system. Compared to this, there is an advantage that the cooling efficiency can be dramatically improved. In addition, the vibration mixing of steel balls and the pyrolysis residue dissolves the char of the pyrolysis residue and separates the char adhering to other residues. At the same time, and the subsequent separation of the char is facilitated.

【0028】勿論、鋼球はこれを冷却して初期工程に還
流させる方式であるので、資源再利用の観点からも、コ
スト的に有利であるという利点もある。本発明のその他
の効果は、上記発明の実施の態様の項及び実施例の項に
おいて詳述した通りである。
Of course, since the steel ball is cooled and refluxed to the initial step, there is also an advantage that the cost is advantageous from the viewpoint of resource recycling. Other effects of the present invention are as described in detail in the above-mentioned embodiments and embodiments.

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

【図1】本発明にかかる熱分解炉からの熱分解残渣の冷
却方法に用いる熱分解残渣の冷却装置の概略説明図であ
る。
FIG. 1 is a schematic explanatory view of a device for cooling a pyrolysis residue used in a method for cooling a pyrolysis residue from a pyrolysis furnace according to the present invention.

【図2】本発明にかかる熱分解炉からの熱分解残渣の冷
却方法に用いる振動ドラムの原理図である。
FIG. 2 is a principle view of a vibrating drum used in a method for cooling a pyrolysis residue from a pyrolysis furnace according to the present invention.

【符号の説明】[Explanation of symbols]

1 鋼球 2 振動ドラム 3 分離手段 3a 磁気吸着機 4 冷却手段 5 移送手段 A 熱分解残渣 A1 チャー A2 他の残渣 DESCRIPTION OF SYMBOLS 1 Steel ball 2 Vibration drum 3 Separation means 3a Magnetic adsorption machine 4 Cooling means 5 Transfer means A Pyrolysis residue A1 Char A2 Other residue

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】ゴミ等の熱分解により得られた高温の熱分
解残渣を冷却する熱分解炉からの熱分解残渣の冷却方法
であって、 前記高温の熱分解残渣Aに多数の小径の鋼球1を付加し
て混合し、前記鋼球1と前記熱分解残渣Aとの接触によ
って熱分解残渣A中のチャーA1の塊をほぐし、また、
他の残渣A2との分離を図りながら該熱分解残渣Aの熱
を前記鋼球1に伝播せしめる工程、 前記鋼球1と熱分解残渣Aとを分離する工程、及び前記
鋼球1を冷却して後に再び前記当初の工程に用いる還流
工程、からなる、熱分解炉からの熱分解残渣の冷却方
法。
1. A method for cooling a pyrolysis residue from a pyrolysis furnace for cooling a high-temperature pyrolysis residue obtained by pyrolysis of dust or the like, wherein said high-temperature pyrolysis residue A is provided with a plurality of small-diameter steels. The ball 1 is added and mixed, and the mass of the char A1 in the pyrolysis residue A is loosened by the contact between the steel ball 1 and the pyrolysis residue A.
A step of transmitting the heat of the pyrolysis residue A to the steel ball 1 while separating it from the other residue A2; a step of separating the steel ball 1 and the pyrolysis residue A; and cooling the steel ball 1 And a refluxing step to be used again in the initial step, and a method for cooling the pyrolysis residue from the pyrolysis furnace.
【請求項2】前記鋼球1が、直径1ミリ乃至3ミリであ
る、請求項1の熱分解炉からの熱分解残渣の冷却方法。
2. The method for cooling a pyrolysis residue from a pyrolysis furnace according to claim 1, wherein said steel ball 1 has a diameter of 1 mm to 3 mm.
【請求項3】ゴミ等の熱分解により得られた高温の熱分
解残渣を冷却する熱分解残渣の冷却装置であって、 多数の小径の鋼球1と、 前記高温の熱分解残渣Aに前記鋼球1を付加して混合す
る振動ドラム2と、 前記鋼球1と熱分解残渣Aとを分離する分離手段3と、 前記鋼球1を冷却する冷却手段4と、 冷却された前記鋼球1を前記振動ドラム2に還流する移
送手段5とからなる、熱分解残渣の冷却装置。
3. A cooling device for a pyrolysis residue which cools a high-temperature pyrolysis residue obtained by pyrolysis of dust or the like, comprising: a plurality of small-diameter steel balls 1; A vibrating drum 2 for adding and mixing steel balls 1; separating means 3 for separating the steel balls 1 and pyrolysis residue A; cooling means 4 for cooling the steel balls 1; 1. A cooling device for thermal decomposition residues, comprising a transfer means 5 for refluxing 1 to the vibrating drum 2.
【請求項4】前記鋼球1が、直径1ミリ乃至3ミリであ
る、請求項3の熱分解残渣の冷却装置。
4. The cooling apparatus for a pyrolysis residue according to claim 3, wherein said steel ball 1 has a diameter of 1 mm to 3 mm.
【請求項5】前記分離手段3が磁気吸着機3aである、
請求項3又は請求項4の熱分解残渣の冷却装置。
5. The apparatus according to claim 1, wherein the separating means is a magnetic attraction machine.
The cooling device for a pyrolysis residue according to claim 3 or 4.
【請求項6】前記冷却手段4が前記鋼球1が通過する筒
状体4aと、該筒状体4aの周囲に設けられた水冷ジャ
ケット4bとからなる間接水冷方式である、請求項3乃
至請求項5の熱分解残渣の冷却装置。
6. The indirect water cooling system in which the cooling means 4 comprises a cylindrical body 4a through which the steel balls 1 pass, and a water cooling jacket 4b provided around the cylindrical body 4a. The cooling device for a pyrolysis residue according to claim 5.
JP2000403826A 2000-11-30 2000-11-30 Cooling method for heat decomposition residue generated from heat decomposition furnace and cooling device for the heat decomposition residue Pending JP2002166257A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000403826A JP2002166257A (en) 2000-11-30 2000-11-30 Cooling method for heat decomposition residue generated from heat decomposition furnace and cooling device for the heat decomposition residue

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000403826A JP2002166257A (en) 2000-11-30 2000-11-30 Cooling method for heat decomposition residue generated from heat decomposition furnace and cooling device for the heat decomposition residue

Publications (1)

Publication Number Publication Date
JP2002166257A true JP2002166257A (en) 2002-06-11

Family

ID=18867876

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000403826A Pending JP2002166257A (en) 2000-11-30 2000-11-30 Cooling method for heat decomposition residue generated from heat decomposition furnace and cooling device for the heat decomposition residue

Country Status (1)

Country Link
JP (1) JP2002166257A (en)

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