JP3071171B2 - Swirling type ash melting furnace - Google Patents

Swirling type ash melting furnace

Info

Publication number
JP3071171B2
JP3071171B2 JP10071555A JP7155598A JP3071171B2 JP 3071171 B2 JP3071171 B2 JP 3071171B2 JP 10071555 A JP10071555 A JP 10071555A JP 7155598 A JP7155598 A JP 7155598A JP 3071171 B2 JP3071171 B2 JP 3071171B2
Authority
JP
Japan
Prior art keywords
slag
burner
furnace
molten slag
melting furnace
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.)
Expired - Fee Related
Application number
JP10071555A
Other languages
Japanese (ja)
Other versions
JPH11270832A (en
Inventor
正人 遠藤
康一 山口
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP10071555A priority Critical patent/JP3071171B2/en
Publication of JPH11270832A publication Critical patent/JPH11270832A/en
Application granted granted Critical
Publication of JP3071171B2 publication Critical patent/JP3071171B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、廃棄物などの焼却
灰を旋回させつつバーナで溶融し、溶融スラグ化する旋
回流式灰溶融炉の改良に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in a swirling type ash melting furnace in which incinerated ash such as waste is swirled and melted by a burner to form molten slag.

【0002】[0002]

【従来の技術】ごみ焼却灰、下水汚泥焼却灰などの最終
処分方法として、従来は主として埋め立てが行われてい
たが、最近ではこれらの焼却灰を高温で溶融してスラグ
化し、大幅な減容化を図るとともに重金属の流出を防止
し、さらに得られたスラグを原料として透水性ブロック
や路盤材などとして資源化する方法が普及しつつある。
2. Description of the Related Art As a final disposal method for refuse incineration ash, sewage sludge incineration ash, etc., landfills have conventionally been mainly used. In addition, a method of preventing outflow of heavy metals while at the same time utilizing the obtained slag as a raw material as a permeable block or a roadbed material, and the like, is becoming widespread.

【0003】この目的のために、従来から図4に示すよ
うな旋回流式灰溶融炉が用いられている。この従来の旋
回流式灰溶融炉は、傾斜させた旋回溶融部1に焼却灰を
接線方向から吹き込み、旋回させながら主バーナ2で溶
融させ、溶融スラグを燃焼ガスとともに下方の炉本体3
に導き、その底部中心に設けられた湯口4から流出させ
る一方、燃焼ガスは炉本体3の上部排気口5から排ガス
処理設備に送られる構造となっている。また6は補助バ
ーナ、7は湯口バーナ、8はスラグコンベヤである。
[0003] For this purpose, a swirling flow ash melting furnace as shown in Fig. 4 has conventionally been used. In this conventional swirling type ash melting furnace, incineration ash is blown tangentially into an inclined swirling melting part 1 and melted by a main burner 2 while being swirled.
And the fuel gas is discharged from a gate 4 provided at the center of the bottom, while the combustion gas is sent from an upper exhaust port 5 of the furnace body 3 to an exhaust gas treatment facility. 6 is an auxiliary burner, 7 is a sprue burner, and 8 is a slag conveyor.

【0004】このような旋回流式灰溶融炉では、溶融ス
ラグを安定して流出させるために、必ず炉内圧を大気圧
よりも高い正圧にしなければならない。また湯口4を適
度に加熱するために、湯口4の下部にも排ガス吸引口9
を設けて炉内から燃焼ガスの一部を吸引している。その
結果、旋回溶融部1で完全に溶融しなかった飛灰の一部
が燃焼ガスに乗って湯口4に達し、スラグコンベヤ8に
取り出される溶融スラグの表面にダストとなって付着す
ることがあった。このようなダストの付着は、溶融スラ
グを透水性ブロックや路盤材などとして商品化する場合
には商品価値を低下させる原因となる。
[0004] In such a swirling flow ash melting furnace, the furnace pressure must always be set to a positive pressure higher than the atmospheric pressure in order to stably discharge the molten slag. In order to heat the gate 4 appropriately, an exhaust gas suction port 9 is also provided below the gate 4.
And a part of the combustion gas is sucked from the furnace. As a result, a part of the fly ash that has not been completely melted in the swirl melting part 1 may reach the gate 4 on the combustion gas and may adhere to the surface of the molten slag taken out to the slag conveyor 8 as dust. Was. Such adhesion of dust causes a reduction in commercial value when the molten slag is commercialized as a water-permeable block or a roadbed material.

【0005】[0005]

【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決して、溶融スラグを安定して流出させる
ことができ、しかも溶融スラグの表面にダストが付着す
ることのない旋回流式灰溶融炉を提供するためになされ
たものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned conventional problems, and enables the molten slag to flow out stably without causing dust to adhere to the surface of the molten slag. The purpose of the present invention is to provide a ash melting furnace.

【0006】[0006]

【課題を解決するための手段】上記の課題を解決するた
めになされた本発明は、焼却灰を旋回させつつバーナで
溶融し、溶融スラグとして炉外に取り出す旋回流式灰溶
融炉において、バーナの燃焼排ガスが流れる炉本体の側
方に、溶融スラグ流動用の開口を備えたガス分離壁を介
してスラグ箱を設け、バーナの燃焼排ガスの流れ方向
対して、溶融スラグの流動方向を異ならせるとともに、
そのガス分離壁によって前記燃焼排ガスを遮断し、前記
スラグ箱は内部にバーナを設け、スラグ箱内の圧力を炉
本体の圧力よりも高く維持したことを特徴とするもので
ある。具体的には、前記スラグ箱において、溶融スラグ
を滞留時間を持って外部に流出するようにすることが好
ましい。
Has been made to solve the above problems, there is provided a means for solving the present invention, while turning the ash melted by a burner, in the swirling flow type ash melting furnace taken out of the furnace as a molten slag, the burner Side of the furnace body where the flue gas from the furnace flows
Through a gas separation wall with openings for the flow of molten slag.
And a slag box is installed in the burner's combustion exhaust gas flow direction .
In contrast, Rutotomoni with different flow Direction of molten slag,
The flue gas is blocked by the gas separation wall,
The slag box has a burner inside, and the pressure inside the slag box is
It is characterized in that the pressure is maintained higher than the pressure of the main body . Specifically, in the slag box, the molten slag
Is preferably discharged outside with a residence time .

【0007】本発明の旋回流式灰溶融炉では、溶融スラ
グを燃焼ガスとは異なる方向に導き、ガス分離壁で遮断
て炉外に取り出すようにしたので、燃焼ガスに乗って
飛来するダストが溶融スラグの表面に付着しにくい。特
に炉本体の側方に、溶融スラグ流動用の開口を備えたガ
ス分離壁を介してスラグ箱を設けた構造を採用し、その
内部にバーナを設け、スラグ箱内の圧力を炉本体の圧力
よりも高く維持したので、全くダストの付着のない溶融
スラグを取り出すことができる。
[0007] In the swirling flow type ash melting furnace of the present invention is-out guide in a different direction to the molten slag combustion gases, blocking gas separating wall
Since they were taken out to the outside of the furnace and, the dust flying aboard the combustion gas hardly adheres to the surface of the molten slag. In particular, a structure in which a slag box is provided on the side of the furnace body via a gas separation wall with an opening for flowing molten slag ,
A burner is installed inside, and the pressure in the slag box is
Since the slag was maintained at a higher level , a molten slag with no dust attached can be taken out.

【0008】[0008]

【発明の実施の形態】以下に本発明の好ましい実施の形
態を示す。図1は本発明の旋回流式灰溶融炉の概略的な
斜視図、図2はそのA−A断面図、図3はそのB−B断
面図である。これらの図中、1は焼却灰が接線方向に吹
き込まれる旋回溶融部、2は旋回溶融部1に設けられた
主バーナ、3はこの旋回溶融部1で溶融されたスラグが
燃焼排ガスとともに流入する炉本体、5は炉本体3の直
上に設けられた上部排気口であり、これらは図4に示し
た従来の旋回流式灰溶融炉と同様のものである。しかし
本発明では、この炉本体3の側方にスラグ箱10を設け
て、バーナの燃焼排ガスの流れ方向と、溶融スラグの流
動方向とを異ならせてある。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below. FIG. 1 is a schematic perspective view of a swirling type ash melting furnace of the present invention, FIG. 2 is a sectional view taken along line AA, and FIG. 3 is a sectional view taken along line BB. In these figures, reference numeral 1 denotes a swirling melting portion into which incineration ash is blown in a tangential direction, 2 denotes a main burner provided in the swirling melting portion 1, and 3 denotes a slag melted in the swirling melting portion 1 flows in with the flue gas. Furnace bodies 5 and 5 are upper exhaust ports provided directly above the furnace body 3 and are the same as those of the conventional swirling type ash melting furnace shown in FIG. However, in the present invention, the slag box 10 is provided on the side of the furnace main body 3 so that the flow direction of the combustion exhaust gas from the burner is different from the flow direction of the molten slag.

【0009】スラグ箱10はその底部中央に湯口4を備
えており、またその底面は図3に示すように炉本体3の
底面と同様に傾斜面となっている。このスラグ箱10と
炉本体3との間には、図2に示されるようなガス分離壁
11が設けられている。このガス分離壁11は下部に溶
融スラグ流動用の開口12を備えたものであり、燃焼排
ガスを遮断しつつ溶融スラグのみをスラグ箱10に流入
させることができるようになっている。また、このスラ
グ箱10の天井は湯口バーナ7を設け、スラグ箱10内
の圧力を炉本体の圧力よりも高く維持している。
The slag box 10 has a gate 4 in the center of the bottom, and the bottom surface is an inclined surface like the bottom surface of the furnace body 3 as shown in FIG. A gas separation wall 11 as shown in FIG. 2 is provided between the slag box 10 and the furnace main body 3. The gas separation wall 11 is provided with an opening 12 for flowing molten slag at a lower portion, so that only the molten slag can flow into the slag box 10 while shutting off combustion exhaust gas. In addition, a sprue burner 7 is provided on the ceiling of the slag box 10 to maintain the pressure in the slag box 10 higher than the pressure of the furnace body.

【0010】このように構成された本発明の旋回流式灰
溶融炉は、旋回溶融部1に焼却灰を接線方向に吹き込ん
で旋回させながら、主バーナ2で溶融させ、溶融スラグ
を燃焼ガスとともに下方の炉本体3に導くことは従来と
同様である。しかし本発明の炉では、燃焼ガスは炉本体
3直上に設けられた上部排気口5から排気される一方、
溶融スラグは燃焼ガスとは直角方向に流れ、ガス分離壁
11の開口12からスラグ箱10に流入する。
In the swirling-flow ash melting furnace of the present invention thus constructed, the incineration ash is blown tangentially into the swirling / melting section 1 to be swirled while being melted by the main burner 2, and the molten slag is melted together with the combustion gas. Leading to the lower furnace body 3 is the same as in the prior art. However, in the furnace of the present invention, the combustion gas is exhausted from the upper exhaust port 5 provided immediately above the furnace main body 3,
The molten slag flows in a direction perpendicular to the combustion gas and flows into the slag box 10 from the opening 12 of the gas separation wall 11.

【0011】このようにしてスラグ箱10に流入した溶
融スラグは、スラグ箱10の天井の湯口バーナ7により
更に加熱され、底部中央に設けられた湯口4から取り出
される。旋回流式灰溶融炉では未溶融の飛灰が燃焼ガス
に同伴することが避けられないが、燃焼ガスはガス分離
壁11により遮断されるうえ、湯口バーナ7によりスラ
グ箱10の内部は炉本体3よりもややプラス圧に保たれ
ているため、湯口バーナ7の燃焼ガスはガス分離壁11
の開口12から炉本体3の方向に流れ、炉本体3側から
前記燃焼ガスの流入を阻止する。なお、スラグ箱10
の内部をプラス圧にしたことにより、溶融スラグは安定
して流出する。
The molten slag flowing into the slag box 10 in this way is further heated by the gate burner 7 on the ceiling of the slag box 10 and taken out from the gate 4 provided at the bottom center. In the swirling type ash melting furnace, it is inevitable that unmelted fly ash accompanies the combustion gas. However, the combustion gas is shut off by the gas separation wall 11 and the inside of the slag box 10 is closed by the gate burner 7. 3, the combustion gas of the gate burner 7 is supplied to the gas separation wall 11.
Flows from the opening 12 toward the furnace body 3 to prevent the combustion gas from flowing from the furnace body 3 side. The slag box 10
The molten slag flows out stably due to the positive pressure in the inside.

【0012】この結果、湯口4からスラグコンベヤ8に
取り出された溶融スラグには全くダストの付着がなく、
この溶融スラグを透水性ブロックや路盤材などとして商
品化する場合にも商品価値を低下させることがない。ま
た溶融スラグは十分な滞留時間を持って流出してくるの
で、内部の気泡が少なくなり、この面でも良質なスラグ
を得ることができる。
As a result, the molten slag taken out from the gate 4 to the slag conveyor 8 has no dust attached thereto,
Even when this molten slag is commercialized as a water-permeable block or a roadbed material, the commercial value is not reduced. Further, since the molten slag flows out with a sufficient residence time, the number of bubbles inside the molten slag is reduced, and a high-quality slag can be obtained in this aspect as well.

【0013】この他、本発明の旋回流式灰溶融炉は最も
浸食されやすいスラグ箱10を炉本体3の側方に設けた
ので、浸食部分のみを交換する作業を簡単に行うことが
できる利点もある。
In addition, since the swirl type ash melting furnace of the present invention has the slag box 10 which is most susceptible to erosion provided on the side of the furnace main body 3, the operation of replacing only the eroded portion can be easily performed. There is also.

【0014】[0014]

【発明の効果】以上に説明したように、本発明の旋回流
式灰溶融炉は溶融スラグを燃焼ガスとは異なる方向に導
いて炉外に取り出すようにしたので、ダストの付着のな
い溶融スラグを取り出すことができ、しかもこの溶融ス
ラグは内部の気泡が少ないから、透水性ブロックや路盤
材などとして商品化する場合にも商品価値を低下させる
ことがない。また本発明の旋回流式灰溶融炉は最も浸食
されやすいスラグ箱のみを簡単に交換することができ
る。
As described above, in the swirling type ash melting furnace of the present invention, the molten slag is guided in a direction different from the combustion gas and is taken out of the furnace. Can be taken out, and since the molten slag has few internal bubbles, the commercial value does not decrease even when commercialized as a water-permeable block or a roadbed material. Further, in the swirling type ash melting furnace of the present invention, only the slag box which is most likely to be eroded can be easily replaced.

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

【図1】本発明の旋回流式灰溶融炉の概略的な斜視図で
ある。
FIG. 1 is a schematic perspective view of a swirling type ash melting furnace of the present invention.

【図2】図1のA−A断面図である。FIG. 2 is a sectional view taken along line AA of FIG.

【図3】図1のB−B断面図である。FIG. 3 is a sectional view taken along the line BB of FIG. 1;

【図4】従来の旋回流式灰溶融炉の断面図である。FIG. 4 is a cross-sectional view of a conventional swirling flow ash melting furnace.

【符号の説明】[Explanation of symbols]

1 旋回溶融部、2 主バーナ、3 炉本体、4 湯
口、5 上部排気口、6補助バーナ、7 湯口バーナ、
8 スラグコンベヤ、9 排ガス吸引口、10スラグ
箱、11 ガス分離壁、12 溶融スラグ流動用の開口
1 swirl melting part, 2 main burner, 3 furnace body, 4 gate, 5 upper exhaust port, 6 auxiliary burner, 7 gate burner,
8 slag conveyor, 9 exhaust gas suction port, 10 slag box, 11 gas separation wall, 12 opening for molten slag flow

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F23J 1/00 F23G 5/00 F23J 1/08 Continuation of front page (58) Field surveyed (Int. Cl. 7 , DB name) F23J 1/00 F23G 5/00 F23J 1/08

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 焼却灰を旋回させつつバーナで溶融し、
溶融スラグとして炉外に取り出す旋回流式灰溶融炉にお
いて、バーナの燃焼排ガスが流れる炉本体の側方に、溶
融スラグ流動用の開口を備えたガス分離壁を介してスラ
グ箱を設け、バーナの燃焼排ガスの流れ方向に対して
溶融スラグの流動方向を異ならせるとともに、そのガス
分離壁によって前記燃焼排ガスを遮断し、前記スラグ箱
は内部にバーナを設け、スラグ箱内の圧力を炉本体の圧
力よりも高く維持したことを特徴とする旋回流式灰溶融
炉。
1. An incineration ash is swirled and melted by a burner,
In a swirl-flow ash melting furnace that is taken out of the furnace as molten slag, the ash melts on the side of the furnace body where the combustion exhaust gas from the burner flows.
Slurry through gas separation walls with openings for molten slag flow
The grayed boxes provided, relative to the direction of flow of the combustion exhaust gas of the burner,
Rutotomoni with different flow Direction of the molten slag, the gas
The combustion exhaust gas is blocked by a separation wall, and the slag box is
Is equipped with a burner inside, and the pressure in the slag box is
A swirling flow ash melting furnace characterized by being maintained at a higher force .
【請求項2】 前記スラグ箱において、溶融スラグを滞
留時間を持って外部に流出するようにした請求項1に記
載の旋回流式灰溶融炉。
2. In the slag box, molten slag is accumulated.
2. The method according to claim 1, wherein the liquid flows out with a retention time.
Swirling ash melting furnace.
JP10071555A 1998-03-20 1998-03-20 Swirling type ash melting furnace Expired - Fee Related JP3071171B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10071555A JP3071171B2 (en) 1998-03-20 1998-03-20 Swirling type ash melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10071555A JP3071171B2 (en) 1998-03-20 1998-03-20 Swirling type ash melting furnace

Publications (2)

Publication Number Publication Date
JPH11270832A JPH11270832A (en) 1999-10-05
JP3071171B2 true JP3071171B2 (en) 2000-07-31

Family

ID=13464104

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10071555A Expired - Fee Related JP3071171B2 (en) 1998-03-20 1998-03-20 Swirling type ash melting furnace

Country Status (1)

Country Link
JP (1) JP3071171B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101673983B1 (en) * 2015-08-31 2016-11-08 김윤종 Discharge moisture type dust proof mask

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITBO20030242A1 (en) * 2003-04-23 2004-10-24 Itea Spa PROCEDURE AND PLANT FOR THE TREATMENT OF MATERIALS

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101673983B1 (en) * 2015-08-31 2016-11-08 김윤종 Discharge moisture type dust proof mask

Also Published As

Publication number Publication date
JPH11270832A (en) 1999-10-05

Similar Documents

Publication Publication Date Title
EP0743286B1 (en) Method of melting treatment of incineration fly ash
JPS59180215A (en) Clinker preventive device of municipal waste incinerator
JP3071171B2 (en) Swirling type ash melting furnace
JPH07301490A (en) Melting furnace
JP3678877B2 (en) Ash solidification processing apparatus and melt solidification processing method
JPH0587728B2 (en)
JPH0462312A (en) Device and method for fusion-setting disposal of ash
JPH05141633A (en) Rotary kiln type waste incineration device
KR100355154B1 (en) Incinerator
JP4197289B2 (en) Ash processing equipment
JPH05223235A (en) Apparatus for melting and solidifying ash
JP3643699B2 (en) Furnace and exhaust gas treatment method in the furnace
JPS5918317Y2 (en) Melting furnace with water-cooled spout
JP2625338B2 (en) Ash melting and solidification equipment
JP2003065510A (en) Swirl type melting furnace
JPS6240607B2 (en)
JP4110660B2 (en) Ash melting furnace
JP2597000B2 (en) Burner injection method for rigid swirling flow melting furnace
CA1232755A (en) Method of removal of impure gases at the time of scrap preheating, and equipment for use of same
JPH0391609A (en) Treatment of ash by melting and solidification
JP3088842B2 (en) Melting method of workpiece by swirling flow melting furnace
JPH0561631U (en) Auxiliary fuel supply device to melting furnace
JP3547095B2 (en) Ash melting furnace
JPH06300234A (en) Plasma melting furnace and its slag discharge method
JPS63205190A (en) Melt treatment of waste

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20000509

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080526

Year of fee payment: 8

R371 Transfer withdrawn

Free format text: JAPANESE INTERMEDIATE CODE: R371

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090526

Year of fee payment: 9

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090526

Year of fee payment: 9

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090526

Year of fee payment: 9

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090526

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100526

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110526

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110526

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120526

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130526

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140526

Year of fee payment: 14

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees