JPH11287412A - Internal melt furnace - Google Patents

Internal melt furnace

Info

Publication number
JPH11287412A
JPH11287412A JP10088550A JP8855098A JPH11287412A JP H11287412 A JPH11287412 A JP H11287412A JP 10088550 A JP10088550 A JP 10088550A JP 8855098 A JP8855098 A JP 8855098A JP H11287412 A JPH11287412 A JP H11287412A
Authority
JP
Japan
Prior art keywords
ash
melting
combustion
melt
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.)
Granted
Application number
JP10088550A
Other languages
Japanese (ja)
Other versions
JP3982048B2 (en
Inventor
Michinori Narisawa
道則 成澤
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP08855098A priority Critical patent/JP3982048B2/en
Publication of JPH11287412A publication Critical patent/JPH11287412A/en
Application granted granted Critical
Publication of JP3982048B2 publication Critical patent/JP3982048B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To enhance melt treatment capacity by a method wherein a molten slug reservoir of an ash melt part bottom is deepened to generate a quantity of molten slug and incinerated ash is completely molten. SOLUTION: In an internal melt furnace to melt by the combustion generation heat of a combustible content in ash serving as a main melt heat source, the internal melt furnace 1 consists of a combustion part 2, an ash melt part 3, and a slug cooling part 8. The combustion part 2 comprises an incinerated ash storage tank 6; and a furnace bed 5 connected to the lower part of the incinerated ash storage tank 6 and provided at a bottom with a combustion air nozzle 4. The ash melt part 3 is formed in a horizontal cylindrical state and the furnace bed 5 of the combustion part 2 is connected in the direction of a tangential line to one end of the bottom of the ash melt part 3 and an assist device 9 is connected in the tangential line direction of the ash melt part 3. A swirl flow of combustion gas 10 is formed in the ash melt part 3 and the molten slug reservoir 3a for molten slug 13 is formed in the bottom of the ash melt part 3. In a so formed internal part melt furnace 1, a horizontal cylindrical assist melt part 14 having a radius smaller than that of the ash melt part 3 and provided at a lower end with a gutter part 15 is interposed between the ash melt part 3 and a slug cooling part 8.

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、都市ごみ焼却炉や
各種焼却装置等から排出される未燃分を含んだ焼却灰な
どを溶融処理する内部溶融炉に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an internal melting furnace for melting incinerated ash and the like containing unburned components discharged from municipal waste incinerators and various incinerators.

【0002】[0002]

【従来の技術】都市ごみ、下水汚泥等の各廃棄物は、焼
却施設で焼却処理され、生じた焼却灰や煤塵は、従来埋
め立て処分されていた。しかし、埋立処分地枯渇の問題
や有害重金属類の溶出による地下水汚染の問題があるた
め、溶融による減量・減容化と無害化の必要性が高まっ
ている。
2. Description of the Related Art Waste such as municipal solid waste and sewage sludge has been incinerated in an incineration facility, and the resulting incinerated ash and dust have been conventionally disposed of in landfills. However, due to the problem of depletion of landfill sites and the problem of groundwater pollution due to elution of harmful heavy metals, the necessity of weight reduction, volume reduction and detoxification by melting is increasing.

【0003】このような背景から、ごみ焼却炉でごみを
焼却する際、ごみを抑制燃焼(ガス化熱分解)して焼却
灰の中に未燃分を残し、この未燃分を含む焼却灰を下流
側の灰溶融炉で燃焼させ、その燃焼発生熱を灰の主溶融
熱源とすることによって、外部から供給される熱量を減
少させる内部溶融炉が提案され、一部で実処理が行われ
ている。
[0003] From such a background, when incinerating refuse in a refuse incinerator, the refuse is suppressed and burned (gasification and pyrolysis) to leave unburned ash in the incinerated ash, and the incinerated ash containing the unburned ash is contained. Is burned in the ash melting furnace on the downstream side, and an internal melting furnace that reduces the amount of heat supplied from the outside by using the heat generated by the combustion as the main heat source of ash has been proposed. ing.

【0004】この内部溶融炉は、焼却灰中に含まれる未
燃分の燃焼熱および灯油バーナなどの助燃装置の熱によ
り炉内を高温に保ち、炉壁からの輻射熱や炉内のガスか
らの対流伝熱により焼却灰を溶融する。溶融スラグは、
連続出滓され、下流側に設けられたスラグ冷却部に落下
して急冷固化されて水冷スラグとなった後、コンベヤに
よりスラグピットに搬送される。焼却灰中の未燃分を燃
焼させる空気は、蒸気や内部溶融炉出口排ガスなどによ
り加熱された後、高温空気として燃焼空気ノズルに供給
される。また、この内部溶融炉の溶融部に面する炉壁
は、飛灰などが付着して生じる溶損を抑えるために水冷
壁構造にしてある。
[0004] In this internal melting furnace, the inside of the furnace is kept at a high temperature by the heat of combustion of the unburned portion contained in the incineration ash and the heat of a combustion assist device such as a kerosene burner, and the radiant heat from the furnace walls and the gas from the furnace gas are used. Melt incineration ash by convective heat transfer. The molten slag is
The slag is continuously discharged, falls into a slag cooling section provided on the downstream side, is rapidly cooled and solidified into water-cooled slag, and is then conveyed to a slag pit by a conveyor. The air that burns the unburned components in the incineration ash is heated by steam or exhaust gas from the internal melting furnace, and then supplied to the combustion air nozzle as high-temperature air. The furnace wall facing the melting portion of the internal melting furnace has a water-cooled wall structure in order to suppress melting damage caused by fly ash and the like.

【0005】しかしながら、上記内部溶融炉では、ごみ
焼却炉から排出される灰の量と溶融炉で溶融処理する灰
の量がバランスしないと、溶融炉側において灰量過多に
より溶融スラグ中に未溶融の灰が混入することがある。
[0005] However, in the above internal melting furnace, if the amount of ash discharged from the refuse incinerator and the amount of ash to be melted in the melting furnace are not balanced, unmelted slag in the molten slag due to excessive ash on the melting furnace side. Ash may be mixed.

【0006】そこで本願出願人は、これらの問題を解決
するために、溶融炉側において灰量過多による未溶融灰
の混入が生じても湯溜めによって灰を溶融し、また、旋
回流により燃焼ガスの炉内滞留時間を長くして炉内の燃
焼効率を高めることにより溶融処理能力の向上を図るよ
うにした内部溶融炉を創案し、特許出願した(特願平9
−224791(未公開))。
In order to solve these problems, the applicant of the present application melts the ash by means of a water pool even if unmelted ash is mixed due to an excessive amount of ash on the melting furnace side, and generates combustion gas by a swirling flow. Of an internal melting furnace designed to improve the melting processing capacity by increasing the residence time in the furnace and increasing the combustion efficiency in the furnace, and filed a patent application (Japanese Patent Application No. Hei 9 (1998) -108).
-224791 (not disclosed)).

【0007】図6および図7は、特願平9−22479
1に掲載された内部溶融炉に関するもので、図6はその
断面図であり、図7は図6のA−A矢視図である。図に
おいて、1は燃焼部2と灰溶融部3とからなる内部溶融
炉である。燃焼部2は、焼却灰貯槽6と、焼却灰貯槽6
の下部に連接され、底部に燃焼空気ノズル4を有する炉
床5と、焼却灰貯槽6中の焼却灰12を炉床5へ押し出
すプッシャ7とからなる。灰溶融部3は、横向きの円筒
状をしており、燃焼部2の炉床5が灰溶融部3底部の一
端に接線方向に接続され、灰溶融部3の他端はスラグ冷
却部8に連接され、灰溶融部3上部の一端の接線方向に
助燃装置9が接続されている。灰溶融部3内には燃焼ガ
ス10の旋回流11を形成し、灰溶融部3底部に溶融ス
ラグ13の湯溜め3aを形成している。
FIGS. 6 and 7 show Japanese Patent Application No. 9-22479.
1 relates to the internal melting furnace, FIG. 6 is a sectional view thereof, and FIG. 7 is a view taken along the line AA of FIG. In the figure, reference numeral 1 denotes an internal melting furnace including a combustion section 2 and an ash melting section 3. The combustion unit 2 includes an incineration ash storage tank 6 and an incineration ash storage tank 6.
And a pusher 7 that pushes out the incineration ash 12 in the incineration ash storage tank 6 to the hearth 5. The ash fusion part 3 has a laterally cylindrical shape, and the hearth 5 of the combustion part 2 is tangentially connected to one end of the bottom of the ash fusion part 3, and the other end of the ash fusion part 3 is connected to the slag cooling part 8. An auxiliary combustion device 9 is connected in a tangential direction of one end of the upper part of the ash fusion part 3 which is connected. A swirling flow 11 of the combustion gas 10 is formed in the ash fusion part 3, and a pool 3 a of the molten slag 13 is formed at the bottom of the ash fusion part 3.

【0008】[0008]

【発明が解決しようとする課題】しかしながら、上記特
願平9−224791に掲載された内部溶融炉では、湯
溜めが溶融部底部の円弧面に沿って形成されるため、溶
融スラグの深さが浅く、未溶融灰を溶融するには必ずし
も十分ではない。
However, in the internal melting furnace disclosed in Japanese Patent Application No. Hei 9-224791, the depth of the molten slag is reduced because the pool is formed along the arc surface at the bottom of the molten portion. It is shallow and not always sufficient to melt unmolten ash.

【0009】本発明は、上記のような問題点を解決する
ために創案されたもので、溶融炉底部の湯溜めを深く形
成するとともに、水冷壁構造部分の面積を小さく抑える
ようにした内部溶融炉を提供することを目的とするもの
である。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and has an internal melting device in which a water pool at the bottom of a melting furnace is formed deep and an area of a water cooling wall structure portion is reduced. It is intended to provide a furnace.

【0010】[0010]

【課題を解決するための手段】上記目的を達成するた
め、本発明によれば、未燃分やRDFを含んだ焼却灰
を、灰中の可燃分の燃焼発生熱を主溶融熱源として溶融
する内部溶融炉であって、該内部溶融炉は、燃焼部と灰
溶融部とスラグ冷却部とからなり、燃焼部は、焼却灰貯
槽と、焼却灰貯槽の下部に連接され底部に燃焼空気ノズ
ルを有する炉床と、焼却灰貯槽中の焼却灰を炉床へ押し
出すプッシャとからなり、灰溶融部は、横向きの円筒状
をしており、前記燃焼部の炉床が灰溶融部底部の一端に
接線方向に接続され、灰溶融部の一端の接線方向に助燃
装置が接続されていて、灰溶融部内に燃焼ガスの旋回流
を形成し、灰溶融部底部に溶融スラグの湯溜めを形成し
た内部溶融炉において、灰溶融部とスラグ冷却部との間
に、灰溶融部よりも半径が小さく、下端にとい部を有
し、かつ、とい部底面と灰溶融部底面とを同一面となる
ようにした横向き円筒状の補助溶融部を介在させた内部
溶融炉が提供される。なお、RDFとはごみ固形化燃料
である。
According to the present invention, in order to achieve the above object, incinerated ash containing unburned components and RDF is melted using the heat generated by combustion of the combustible components in the ash as a main heat source of fusion. An internal melting furnace, which includes a combustion section, an ash melting section, and a slag cooling section, and the combustion section is connected to an incineration ash storage tank and a lower portion of the incineration ash storage tank, and has a combustion air nozzle at a bottom portion. Hearth, and a pusher that pushes out the incineration ash in the incineration ash storage tank to the hearth, the ash melting part has a cylindrical shape in a horizontal direction, and the hearth of the combustion part is at one end of the bottom of the ash melting part. A tangential connection, an auxiliary combustion device is connected tangentially to one end of the ash fusion part, a swirling flow of combustion gas is formed in the ash fusion part, and a molten slag pool is formed at the bottom of the ash fusion part. In the melting furnace, a half of the ash melting part is located between the ash melting part and the slag cooling part. Small, has a trough portion at the lower end, and an internal melting furnace is interposed lateral cylindrical auxiliary melting portion was formed to be flush with the trough bottom face and the ash melting portion bottom is provided. Note that RDF is a solidified fuel.

【0011】本発明の他の実施形態によれば、未燃分や
RDFを含んだ焼却灰を、灰中の可燃分の燃焼発生熱を
主溶融熱源として溶融する内部溶融炉であって、該内部
溶融炉は、燃焼部と灰溶融部とスラグ冷却部とからな
り、燃焼部は、焼却灰貯槽と、焼却灰貯槽の下部に連接
され底部に燃焼空気ノズルを有する炉床と、焼却灰貯槽
中の焼却灰を炉床へ押し出すプッシャとからなり、灰溶
融部は、横向きの円筒状をしており、前記燃焼部の炉床
が灰溶融部底部の一端に接線方向に接続され、灰溶融部
の他端はスラグ冷却部に連接され、灰溶融部の一端の接
線方向に助燃装置が接続されていて、灰溶融部内に燃焼
ガスの旋回流を形成し、灰溶融部底部に溶融スラグの湯
溜めを形成した内部溶融炉において、灰溶融部の中間
に、下端に開口を有するリングを内嵌した内部溶融炉が
提供される。
According to another embodiment of the present invention, there is provided an internal melting furnace for melting incinerated ash containing unburned components and RDF using heat generated by combustion of combustible components in the ash as a main melting heat source. The internal melting furnace is composed of a combustion part, an ash melting part, and a slag cooling part.The combustion part is connected to a lower part of the incineration ash storage tank, a hearth having a combustion air nozzle at a bottom part, and an incineration ash storage tank. A pusher that pushes out the incinerated ash to the hearth, the ash melting part has a laterally cylindrical shape, and the hearth of the combustion part is tangentially connected to one end of the bottom of the ash melting part, The other end of the section is connected to the slag cooling section, and a combustion assist device is connected in a tangential direction of one end of the ash melting section, forming a swirling flow of combustion gas in the ash melting section, and forming a swirl flow of the molten slag at the bottom of the ash melting section. An opening at the lower end in the middle of the ash melting part in an internal melting furnace with a water pool formed Internal melting furnace fitted in the ring is provided.

【0012】次に本発明の作用を説明する。ごみ焼却炉
から排出される未燃分を含んだ焼却灰は、プッシャによ
り焼却灰貯槽から燃焼部の炉床へ押し出される。押し出
された焼却灰は、炉床上で燃焼空気ノズルから噴出され
る高温の空気により未燃分が燃焼して、その熱により溶
融されて溶融スラグとなり、炉床から下流側の灰溶融部
へ流下する。この溶融スラグ中には、完全に溶融しない
未溶融の灰分が含まれており、燃焼部からの燃焼ガス中
には飛灰が含まれているが、灰溶融部内には燃焼部から
の燃焼ガスと助燃装置からの燃焼ガスにより旋回流が形
成されていて、その旋回流によって未溶融の灰分と飛灰
は灰溶融部の円筒状の炉内壁に沿って旋回しながら溶融
する。このとき、未溶融の灰が固まった状態で押し出さ
れても底部にとい部を有する小径の補助燃焼部や下端に
開口を有するリングを内嵌したので溶融スラグの流下が
制限され、灰溶融部底部には多量の溶融スラグが溜まっ
ており、灰は溶融スラグに触れて溶融する。また、燃焼
ガスは円筒状の灰溶融部内を旋回するので、炉内滞留時
間が長くなり、灰を完全に溶融することができ、溶融処
理能力が向上する。補助燃焼部やリングの下流側では炉
壁に溶融スラグがほとんど付着しないので水冷壁の必要
がなく、損失熱量も少ない。溶融スラグはスラグ冷却部
中に落ちて急冷固化する。
Next, the operation of the present invention will be described. The incinerated ash containing unburned matter discharged from the refuse incinerator is pushed out of the incinerated ash storage tank by the pusher to the hearth of the combustion section. The extruded incineration ash burns unburned components by the high-temperature air jetted from the combustion air nozzles on the hearth, and is melted by the heat to form molten slag, which flows down from the hearth to the ash melting part on the downstream side. I do. This molten slag contains unmelted ash that is not completely melted, and fly ash is contained in the combustion gas from the combustion part, but the combustion gas from the combustion part is contained in the ash fusion part. A swirling flow is formed by the combustion gas from the combustion assist device and the unmelted ash and fly ash are melted while swirling along the cylindrical inner wall of the ash melting portion by the swirling flow. At this time, even if the unmelted ash is extruded in a solidified state, the flow of the molten slag is limited because the small-diameter auxiliary combustion portion having a shank at the bottom and a ring having an opening at the lower end are internally fitted, and the ash melting portion A large amount of molten slag is stored at the bottom, and the ash comes into contact with the molten slag and melts. Further, since the combustion gas swirls in the cylindrical ash melting portion, the residence time in the furnace is lengthened, the ash can be completely melted, and the melting processing ability is improved. Since molten slag hardly adheres to the furnace wall on the downstream side of the auxiliary combustion section and the ring, there is no need for a water cooling wall, and the heat loss is small. The molten slag falls into the slag cooling section and solidifies rapidly.

【0013】[0013]

【発明の実施の形態】以下、本発明の好ましい実施形態
について、図面に基づいて説明する。図1ないし図3
は、本発明の一実施形態を示すものであり、図1は本発
明による内部溶融炉の斜視図である。図2は図1の側面
図であり、図3は図2のB−B矢視図である。なお、図
6および図7で説明した内部溶融炉と共通する部材につ
いては、同じ符号を用いて説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below with reference to the drawings. 1 to 3
1 shows an embodiment of the present invention, and FIG. 1 is a perspective view of an internal melting furnace according to the present invention. FIG. 2 is a side view of FIG. 1, and FIG. 3 is a view taken in the direction of arrows BB in FIG. Members common to the internal melting furnace described with reference to FIGS. 6 and 7 will be described using the same reference numerals.

【0014】図において、1は未燃分を含んだ焼却灰1
2を溶融処理する内部溶融炉である。この内部溶融炉1
は、燃焼部2と灰溶融部3とスラグ冷却部8とから構成
されている。
In the figure, reference numeral 1 denotes incinerated ash 1 containing unburned components.
2 is an internal melting furnace for melting processing. This internal melting furnace 1
Is composed of a combustion section 2, an ash melting section 3, and a slag cooling section 8.

【0015】燃焼部2は、焼却灰貯槽6と、この焼却灰
貯槽6の下部に連接され底部に燃焼空気ノズル4を配設
した炉床5と、焼却灰貯槽6中の焼却灰12を炉床5へ
押し出すプッシャ7とから構成されている。また、燃焼
空気ノズル4は、多数の空気孔を有しており複数本配設
されている。
The combustion section 2 includes an incineration ash storage tank 6, a hearth 5 connected to a lower portion of the incineration ash storage tank 6 and having a combustion air nozzle 4 disposed at the bottom, and an incineration ash 12 in the incineration ash storage tank 6. And a pusher 7 for extruding the floor 5. Further, the combustion air nozzle 4 has a large number of air holes, and a plurality of combustion air nozzles are provided.

【0016】灰溶融部3は、横向きの円筒状をしてお
り、灰溶融部3の底部の一端は上記炉床5に接続されて
いる。3aは灰溶融部3の底部に形成した溶融スラグ1
3の湯溜めである。灰溶融部3の一端の接線方向に昇温
バーナやプラズマなどの助燃装置9が接続されている。
10は燃焼ガスであり、11は燃焼ガス10の旋回流で
ある。13は溶融スラグであり、13aはスラグ冷却部
8内で冷却された冷却スラグでる。
The ash fusion part 3 has a cylindrical shape in a horizontal direction, and one end of the bottom of the ash fusion part 3 is connected to the hearth 5. 3a is a molten slag 1 formed at the bottom of the ash fusion portion 3.
It is the third pool. An auxiliary burner 9 such as a heating burner or plasma is connected in a tangential direction at one end of the ash melting portion 3.
10 is a combustion gas, and 11 is a swirling flow of the combustion gas 10. Reference numeral 13 denotes a molten slag, and 13a denotes a cooling slag cooled in the slag cooling unit 8.

【0017】14は灰溶融部3の一端とスラグ冷却部8
のスラグ排出部16との間に介在した補助溶融部で、灰
溶融部3よりも半径が小さく、下端に凹状のとい部15
を有している。また、この補助溶融部14は、とい部1
5の底面と灰溶融部3の底面とが同一平面になるように
している。
Reference numeral 14 denotes one end of the ash melting section 3 and the slag cooling section 8
The auxiliary melting portion interposed between the slag discharging portion 16 and the slag discharging portion 16. The auxiliary melting portion has a smaller radius than the ash melting portion 3 and has a concave shank
have. Further, the auxiliary melting part 14 is
5 and the bottom surface of the ash fusion part 3 are made to be on the same plane.

【0018】17はスラグ排出部16の中間に設けた排
ガス排出管である。
Reference numeral 17 denotes an exhaust gas discharge pipe provided in the middle of the slag discharge section 16.

【0019】次に本発明の実施形態の作用について説明
する。ごみ焼却炉から排出される未燃分を含んだ焼却灰
12は、プッシャ7により焼却灰貯槽6から燃焼部2の
炉床5へ押し出される。押し出された焼却灰12は、炉
床5上で燃焼空気ノズル4から噴出される高温の空気に
より未燃分が燃焼して、その熱により溶融されて溶融ス
ラグ13となり、炉床5から下流側の灰溶融部3へ流下
する。この溶融スラグ13中には、完全に溶融しない未
溶融の灰分が含まれており、燃焼部2からの燃焼ガス中
には飛灰が含まれているが、灰溶融部3内には燃焼部2
からの燃焼ガス10と助燃装置9からの燃焼ガスにより
旋回流11が形成されていて、その旋回流11によって
未溶融の灰分と飛灰は灰溶融部3の円筒状の炉内壁に沿
って旋回しながら溶融する。このとき、未溶融の灰が固
まった状態で押し出されても底部にとい部15を有する
小径の補助燃焼部14や下端に開口を有するリング18
を内嵌したので溶融スラグ13の流下が制限され、灰溶
融部3底部には多量の溶融スラグ13が溜まっており、
灰は溶融スラグ13に触れて溶融する。また、燃焼ガス
10は円筒状の灰溶融部3内を旋回するので、炉内滞留
時間が長くなり、灰を完全に溶融することができ、溶融
処理能力が向上する。補助燃焼部14やリング18の下
流側では炉壁に溶融スラグ13がほとんど付着しないの
で水冷壁の必要がなく、損失熱量も少ない。溶融スラグ
13はスラグ冷却部8中に落ちて急冷固化する。
Next, the operation of the embodiment of the present invention will be described. The incinerated ash 12 containing unburned components discharged from the refuse incinerator is pushed out from the incinerated ash storage tank 6 to the hearth 5 of the combustion unit 2 by the pusher 7. The extruded incineration ash 12 burns unburned components by the high-temperature air jetted from the combustion air nozzle 4 on the hearth 5 and is melted by the heat to form a molten slag 13, which is downstream from the hearth 5. Down to the ash fusion zone 3 The molten slag 13 contains unmelted ash that is not completely melted, and the combustion gas from the combustion section 2 contains fly ash. 2
The swirling flow 11 is formed by the combustion gas 10 from the combustion gas and the combustion gas from the auxiliary combustion device 9, and the unmelted ash and fly ash are swirled along the cylindrical furnace inner wall of the ash melting part 3 by the swirling flow 11. While melting. At this time, even if the unmelted ash is extruded in a solidified state, the small-diameter auxiliary combustion portion 14 having the shaving portion 15 at the bottom and the ring 18 having the opening at the lower end are formed.
, The flow of the molten slag 13 is restricted, and a large amount of the molten slag 13 is accumulated at the bottom of the ash fusion part 3.
The ash touches the molten slag 13 and melts. Further, since the combustion gas 10 swirls in the cylindrical ash melting portion 3, the residence time in the furnace is lengthened, the ash can be completely melted, and the melting processing ability is improved. Since the molten slag 13 hardly adheres to the furnace wall on the downstream side of the auxiliary combustion section 14 and the ring 18, there is no need for a water cooling wall and the amount of heat loss is small. The molten slag 13 falls into the slag cooling section 8 and solidifies rapidly.

【0020】図4および図5は、本発明の他の実施形態
を示すもので、図4は内部溶融炉の側面図であり、図5
は図4のB−B断面図である。図において、18は円筒
状の灰溶融部3内の中間に内嵌したリングで、下端に開
口18aを有しており、溶融スラグ13をリング18の
上流側の灰溶融部3内に多量に滞留させる。なお、他の
構成については、図1ないし図3示した内部溶融炉と同
じであり、重複する説明を省略する。
FIGS. 4 and 5 show another embodiment of the present invention. FIG. 4 is a side view of the internal melting furnace.
FIG. 6 is a sectional view taken along line BB of FIG. 4. In the figure, reference numeral 18 denotes a ring which is fitted in the middle of the cylindrical ash fusion part 3 and has an opening 18a at the lower end, and a large amount of molten slag 13 is introduced into the ash fusion part 3 on the upstream side of the ring 18. Let it stay. The other configuration is the same as that of the internal melting furnace shown in FIGS. 1 to 3, and redundant description will be omitted.

【0021】本発明は、上記実施の形態に限定されるも
のではなく、上記実施形態では、未燃分を含む焼却灰の
溶融について説明したが、未燃分が少ない焼却灰を溶融
する場合には、ごみ固形化燃料(RDF(Refused Deri
ved Full) )を投入して灰の溶融熱源とすることができ
るなど、本発明の要旨を逸脱しない範囲で種々変更し得
ることは勿論である。
The present invention is not limited to the above-described embodiment. In the above-described embodiment, the description has been given of the melting of incinerated ash containing unburned components. Is a solid waste fuel (RDF (Refused Deri)
Of course, various changes can be made without departing from the gist of the present invention, for example, by using ved Full)) as a heat source for melting ash.

【0022】[0022]

【発明の効果】以上述べたように、本発明によれば、灰
溶融部底部の湯溜めに多量の溶融スラグを滞留するよう
にしたので、未燃灰を完全に燃焼することができるとと
もに、水冷壁構造部分の面積を小さく抑えることができ
るなどの優れた効果を奏する。
As described above, according to the present invention, a large amount of molten slag is retained in the sump at the bottom of the ash fusion zone, so that unburned ash can be completely burned. Excellent effects such as the area of the water-cooling wall structure can be reduced.

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

【図1】本発明による内部溶融炉の斜視図である。FIG. 1 is a perspective view of an internal melting furnace according to the present invention.

【図2】図1の側面図である。FIG. 2 is a side view of FIG.

【図3】図2のB−B矢視図である。FIG. 3 is a view taken in the direction of arrows BB in FIG. 2;

【図4】本発明の他の実施形態の内部溶融炉の側面図で
ある。
FIG. 4 is a side view of an internal melting furnace according to another embodiment of the present invention.

【図5】図4のC−C矢視図である。FIG. 5 is a view taken in the direction of the arrows CC in FIG. 4;

【図6】特願平9−224791に掲載された内部溶融
炉の側面断面図である。
FIG. 6 is a side sectional view of an internal melting furnace disclosed in Japanese Patent Application No. 9-224791.

【図7】図6のA−A矢視図である。FIG. 7 is a view on arrow AA of FIG. 6;

【符号の説明】[Explanation of symbols]

1 内部溶融炉 2 燃焼部 3 灰溶融部 3a 湯留め 4 燃焼空気ノズル 5 炉床 6 焼却灰貯槽 7 プッシャ 8 スラグ冷却部 9 助燃装置 10 燃焼ガス 11 旋回流 12 焼却灰 13 溶融スラグ 14 補助溶融部 15 とい部 16 スラグ排出部 17 排ガス排出管 18 リング 18a 開口 DESCRIPTION OF SYMBOLS 1 Internal melting furnace 2 Burning part 3 Ash melting part 3a Hot water 4 Burning air nozzle 5 Hearth 6 Incineration ash storage tank 7 Pusher 8 Slag cooling part 9 Burning aid 10 Combustion gas 11 Swirling flow 12 Burning ash 13 Melting slag 14 Auxiliary melting part 15 Sharp part 16 Slag discharge part 17 Exhaust gas discharge pipe 18 Ring 18a Opening

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI F23G 7/00 103 B09B 3/00 ZAB F23J 1/00 303L ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI F23G 7/00 103 B09B 3/00 ZAB F23J 1/00 303L

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 未燃分やRDFを含んだ焼却灰を、灰中
の可燃分の燃焼発生熱を主溶融熱源として溶融する内部
溶融炉であって、該内部溶融炉は、燃焼部と灰溶融部と
スラグ冷却部とからなり、燃焼部は、焼却灰貯槽と、焼
却灰貯槽の下部に連接され底部に燃焼空気ノズルを有す
る炉床と、焼却灰貯槽中の焼却灰を炉床へ押し出すプッ
シャとからなり、灰溶融部は、横向きの円筒状をしてお
り、前記燃焼部の炉床が灰溶融部底部の一端に接線方向
に接続され、灰溶融部の一端の接線方向に助燃装置が接
続されていて、灰溶融部内に燃焼ガスの旋回流を形成
し、灰溶融部底部に溶融スラグの湯溜めを形成した内部
溶融炉において、灰溶融部とスラグ冷却部との間に、灰
溶融部よりも半径が小さく、下端にとい部を有し、か
つ、とい部底面と灰溶融部底面とを同一面となるように
した横向き円筒状の補助溶融部を介在させたことを特徴
とする内部溶融炉。
1. An internal melting furnace for melting incinerated ash containing unburned components and RDF using heat generated by combustion of combustible components in the ash as a main heat source of fusion, wherein the internal melting furnace comprises a combustion part and an ash. Composed of a melting section and a slag cooling section, the combustion section is an incineration ash storage tank, a hearth connected to the bottom of the incineration ash storage tank and having a combustion air nozzle at the bottom, and extruding incineration ash in the incineration ash storage tank to the hearth. The ash melting portion is formed in a laterally cylindrical shape, and the hearth of the combustion portion is tangentially connected to one end of the ash melting portion bottom, and the ash melting portion is tangentially connected to one end of the ash melting portion. Are connected to each other to form a swirling flow of the combustion gas in the ash melting part and form a pool of molten slag at the bottom of the ash melting part. Radius smaller than the fusion zone, with a sharp end at the lower end, and ash fusion with the bottom of the sharp end An internal melting furnace characterized by interposing a horizontal cylindrical auxiliary melting portion having the same bottom surface as the surface.
【請求項2】 未燃分やRDFを含んだ焼却灰を、灰中
の可燃分の燃焼発生熱を主溶融熱源として溶融する内部
溶融炉であって、該内部溶融炉は、燃焼部と灰溶融部と
スラグ冷却部とからなり、燃焼部は、焼却灰貯槽と、焼
却灰貯槽の下部に連接され底部に燃焼空気ノズルを有す
る炉床と、焼却灰貯槽中の焼却灰を炉床へ押し出すプッ
シャとからなり、灰溶融部は、横向きの円筒状をしてお
り、前記燃焼部の炉床が灰溶融部底部の一端に接線方向
に接続され、灰溶融部の他端はスラグ冷却部に連接さ
れ、灰溶融部の一端の接線方向に助燃装置が接続されて
いて、灰溶融部内に燃焼ガスの旋回流を形成し、灰溶融
部底部に溶融スラグの湯溜めを形成した内部溶融炉にお
いて、灰溶融部の中間に、下端に開口を有するリングを
内嵌したことを特徴とする内部溶融炉。
2. An internal melting furnace for melting incinerated ash containing unburned components and RDF using heat generated by combustion of combustible components in the ash as a main melting heat source. Composed of a melting section and a slag cooling section, the combustion section is an incineration ash storage tank, a hearth connected to the bottom of the incineration ash storage tank and having a combustion air nozzle at the bottom, and extruding incineration ash in the incineration ash storage tank to the hearth. The ash melting part has a cylindrical shape in a horizontal direction, the hearth of the combustion part is tangentially connected to one end of the bottom of the ash melting part, and the other end of the ash melting part is connected to the slag cooling part. In an internal melting furnace in which an auxiliary combustion device is connected in the tangential direction of one end of the ash melting portion and forms a swirling flow of the combustion gas in the ash melting portion, and a molten slag pool is formed at the bottom of the ash melting portion. In the middle of the ash fusion part, a ring with an opening at the lower end is fitted inside Internal melting furnace.
JP08855098A 1998-04-01 1998-04-01 Internal melting furnace Expired - Fee Related JP3982048B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08855098A JP3982048B2 (en) 1998-04-01 1998-04-01 Internal melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08855098A JP3982048B2 (en) 1998-04-01 1998-04-01 Internal melting furnace

Publications (2)

Publication Number Publication Date
JPH11287412A true JPH11287412A (en) 1999-10-19
JP3982048B2 JP3982048B2 (en) 2007-09-26

Family

ID=13945978

Family Applications (1)

Application Number Title Priority Date Filing Date
JP08855098A Expired - Fee Related JP3982048B2 (en) 1998-04-01 1998-04-01 Internal melting furnace

Country Status (1)

Country Link
JP (1) JP3982048B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005106327A1 (en) * 2004-04-29 2005-11-10 Adplatech Corporation Cyclonic plasma pyrolysis system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005106327A1 (en) * 2004-04-29 2005-11-10 Adplatech Corporation Cyclonic plasma pyrolysis system
JP2007534922A (en) * 2004-04-29 2007-11-29 アドプラテック コーポレーション Rotating Plasma Pyrolysis / Melting Furnace (CYCLONIC PLASMACAPYROLYSIS / VITRIFICATIONSYSTEM)
US7665407B2 (en) 2004-04-29 2010-02-23 Adplatech Corporation Cyclonic plasma pyrolysis/vitrification system
JP4719216B2 (en) * 2004-04-29 2011-07-06 アドプラテック コーポレーション Rotating Plasma Pyrolysis / Melting Furnace (CYCLONIC PLASMACAPYROLYSIS / VITRIFICATIONSYSTEM)

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