JPH11304137A - Treatment of exhaust gas of ash melting furnace and ash melting furnace - Google Patents
Treatment of exhaust gas of ash melting furnace and ash melting furnaceInfo
- Publication number
- JPH11304137A JPH11304137A JP10114820A JP11482098A JPH11304137A JP H11304137 A JPH11304137 A JP H11304137A JP 10114820 A JP10114820 A JP 10114820A JP 11482098 A JP11482098 A JP 11482098A JP H11304137 A JPH11304137 A JP H11304137A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- combustion chamber
- secondary combustion
- melting furnace
- ash
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
Landscapes
- Chimneys And Flues (AREA)
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、下水汚泥、都市ご
み及び産業廃棄物などの焼却灰及び事業用火力発電プラ
ント等の燃焼炉から排出される焼却灰を溶融する灰溶融
炉の排ガス処理方法及び灰溶融炉に関するものである。The present invention relates to an exhaust gas treatment method for an ash melting furnace for melting incinerated ash such as sewage sludge, municipal solid waste and industrial waste, and incinerated ash discharged from a combustion furnace such as a commercial thermal power plant. And an ash melting furnace.
【0002】[0002]
【従来の技術】従来より、下水汚泥、都市ごみ及び産業
廃棄物などの焼却灰(粉体無機物)は、その資源化、減
容化及び無害化を図るために、例えば、図4に示すよう
な竪型旋回灰溶融炉51によって溶融され、スラグとし
て取り出されている。このような灰溶融炉51では、そ
の炉内に燃料(重油等)52、焼却灰53及び空気54
を接線方向へ向けて吹き込み、バーナなどを用いて燃焼
させており、燃焼された焼却灰は溶融されてスラグ55
となる。そして、この溶融スラグ55は、灰溶融炉51
の下部のスラグタップ(図示せず)から重力によって落
下され、図示しない下方の水冷槽(水砕スラグ)やコン
ベア(空冷スラグ)へ投入されて取り出される。また、
灰溶融炉51の炉内で発生した排ガス56は、ガス出口
から上部の二次燃焼室57へ導かれ、この二次燃焼室5
7内で燃焼された後、二次燃焼室出口より排ガスダクト
58に排出され、該排ガスダクト58を介して熱交換器
59及び排ガス処理設備に導かれる。2. Description of the Related Art Conventionally, incinerated ash (powder inorganic substance) such as sewage sludge, municipal solid waste and industrial waste has been used, for example, as shown in FIG. It is melted by a simple vertical swirling ash melting furnace 51 and taken out as slag. In such an ash melting furnace 51, a fuel (heavy oil or the like) 52, incineration ash 53, and air 54
Is burned in a tangential direction and burned using a burner or the like.
Becomes The molten slag 55 is supplied to the ash melting furnace 51.
Is dropped by a gravity from a lower slag tap (not shown), and is put into a lower water cooling tank (granulated slag) or a conveyor (air cooled slag) (not shown) to be taken out. Also,
The exhaust gas 56 generated in the furnace of the ash melting furnace 51 is guided from a gas outlet to an upper secondary combustion chamber 57, and the secondary combustion chamber 5
After being burned in 7, it is discharged from the secondary combustion chamber outlet to an exhaust gas duct 58, and guided to a heat exchanger 59 and an exhaust gas treatment facility via the exhaust gas duct 58.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、上述し
た従来の竪型旋回灰溶融炉51の排ガス処理方法では、
炉内から熱交換器59に導かれる排ガス56の温度が1
300〜1500゜Cであり、排ガス56中の溶融飛灰
が液状となっているので、排ガス56中の溶融飛灰60
が排出の途中で二次燃焼室57の出口部、排ガスダクト
58の内部及び熱交換器59のフィン部に付着して成長
することが起こり、これによって排ガスダクト58等の
閉塞や熱交換器59の性能ダウンを招くという問題があ
った。したがって、溶融飛灰60が排ガスダクト58等
に付着成長した場合には、その度に設備を停止して清掃
を行う必要があるので、生産性の向上を図ることが困難
であった。However, in the above-mentioned conventional exhaust gas treatment method of the vertical swirling ash melting furnace 51,
The temperature of the exhaust gas 56 guided from the furnace to the heat exchanger 59 is 1
300 to 1500 ° C., and the molten fly ash in the exhaust gas 56 is in a liquid state.
Adheres to the outlet of the secondary combustion chamber 57, the inside of the exhaust gas duct 58 and the fin of the heat exchanger 59 during the discharge, and grows. However, there is a problem that the performance is deteriorated. Therefore, when the molten fly ash 60 adheres to and grows on the exhaust gas duct 58 and the like, it is necessary to stop and clean the apparatus each time, and it has been difficult to improve the productivity.
【0004】本発明はこのような実状に鑑みてなされた
ものであって、その目的は、排ガス中にキャリオーバさ
れた溶融飛灰の排ガスダクト等への付着を防止し、長期
安定運転を行うことが可能な灰溶融炉の排ガス処理方法
及び灰溶融炉を提供することにある。The present invention has been made in view of such circumstances, and an object of the present invention is to prevent molten fly ash carried over in exhaust gas from adhering to an exhaust gas duct or the like and to perform long-term stable operation. It is an object of the present invention to provide an exhaust gas treatment method for an ash melting furnace and an ash melting furnace capable of performing the above.
【0005】[0005]
【課題を解決するための手段】上記従来技術の有する課
題を解決するため、本発明においては、焼却灰を溶融す
る灰溶融炉の排ガス処理方法において、前記灰溶融炉の
上部に排ガスを燃焼させる二次燃焼室を設け、この二次
燃焼室内に排ガスを導いて急冷し、該排ガス中の液状溶
融飛灰を瞬時に固体化して排出している。また、本発明
は、焼却灰を溶融する灰溶融炉において、該灰溶融炉の
上部に排ガスを燃焼させる二次燃焼室を設けると共に、
この二次燃焼室内に排ガスを急冷する急冷手段を設けて
いる。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems of the prior art, the present invention relates to a method for treating exhaust gas in an ash melting furnace for melting incinerated ash, wherein the exhaust gas is burned in the upper part of the ash melting furnace. A secondary combustion chamber is provided, and the exhaust gas is introduced into the secondary combustion chamber and quenched, and the liquid molten fly ash in the exhaust gas is instantaneously solidified and discharged. Further, the present invention provides, in an ash melting furnace for melting incineration ash, a secondary combustion chamber for burning exhaust gas at an upper portion of the ash melting furnace,
A quenching means for quenching the exhaust gas is provided in the secondary combustion chamber.
【0006】[0006]
【発明の実施の形態】以下、本発明を図示の実施の形態
に基づいて詳細に説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail based on illustrated embodiments.
【0007】図1は本発明の実施の形態に係る竪型旋回
灰溶融炉を示す概念図、図2は図1のA部を拡大して示
す断面図、図3はその旋回灰溶融炉が適用される設備の
一部概要を示す説明図である。本実施の形態の灰溶融炉
1は、図1〜図3に示す如く、耐火材(レンガ、キャス
タ)によって有底円筒状に形成された炉本体2を有して
おり、同炉本体2の底部には、大径の炉内3で溶融され
たスラグ4を重力により落下させて排出するスラグタッ
プ(図示せず)が設けられている。FIG. 1 is a conceptual view showing a vertical swirling ash melting furnace according to an embodiment of the present invention, FIG. 2 is a sectional view showing an enlarged part A of FIG. 1, and FIG. It is an explanatory view showing a partial outline of equipment to be applied. The ash melting furnace 1 of the present embodiment has a furnace main body 2 formed in a cylindrical shape with a bottom by a refractory material (brick, caster) as shown in FIGS. At the bottom, a slag tap (not shown) for dropping the slag 4 melted in the large-diameter furnace 3 by gravity and discharging the slag 4 is provided.
【0008】また、上記炉本体2の炉内3には、図示し
ない燃料タンクから燃料(重油等)5が供給され、図示
しない焼却灰ホッパから焼却灰6が供給されると共に、
後述の熱交換器等から燃焼空気7が供給されるようにな
っており、これら燃料5、焼却灰6及び燃焼空気7は、
図示しないバーナによって炉内3で旋回しながら燃焼さ
れてスラグ4を溶融するように構成されている。そし
て、灰溶融炉1の下方には、矢印で示すように、重力に
より落下させたスラグ4を回収する図外のコンベアなど
が設置されている。一方、炉本体2の頂部には、炉内3
で発生した排ガス8を上方から排出するため、小径のガ
ス出口9が設けられている。灰溶融炉1の上部には、ガ
ス出口9と連通して、排ガス8を燃焼させる二次燃焼室
10が設けられている。A fuel (heavy oil or the like) 5 is supplied from a fuel tank (not shown) to the inside 3 of the furnace main body 2, and incineration ash 6 is supplied from an incineration ash hopper (not shown).
Combustion air 7 is supplied from a heat exchanger or the like described later, and these fuel 5, incineration ash 6, and combustion air 7
The slag 4 is melted while being swirled in the furnace 3 by a burner (not shown) to melt the slag 4. Below the ash melting furnace 1, as shown by an arrow, an unillustrated conveyor for collecting the slag 4 dropped by gravity is installed. On the other hand, the inside of the furnace 3
A small-diameter gas outlet 9 is provided for discharging the exhaust gas 8 generated in the above from above. Above the ash melting furnace 1, a secondary combustion chamber 10 that communicates with the gas outlet 9 and burns the exhaust gas 8 is provided.
【0009】上記二次燃焼室10の側壁上部には、排ガ
スダクト11の一端部が接続され、該排ガスダクト11
の他端部は熱交換器12に接続されており、炉内3で発
生した排ガス8は、二次燃焼室10及び排ガスダクト1
1を介して熱交換器12に導かれるようになっている。
また、二次燃焼室10内の出口部付近の頂部10aに
は、空気13にて霧状の水(粒径が100μm以下)1
4を噴射する急冷手段の水噴霧ノズル15が下方へ向け
て設けられ、該水噴霧ノズル15から水14を噴霧する
ことにより二次燃焼室10内の排ガス8を急冷するよう
に構成されている。この水噴霧ノズル15は、図2に示
す如く、空気13及び水14の二流体方式であり、先細
りの空気供給パイプ16と該空気供給パイプ16の内部
に配設される先細りの水供給パイプ17とによって形成
された二重構造になっている。One end of an exhaust gas duct 11 is connected to the upper part of the side wall of the secondary combustion chamber 10.
The other end is connected to a heat exchanger 12, and the exhaust gas 8 generated in the furnace 3 is discharged from the secondary combustion chamber 10 and the exhaust gas duct 1.
1 to the heat exchanger 12.
On the top 10 a near the outlet in the secondary combustion chamber 10, water 13 (particle size: 100 μm or less) is atomized by air 13.
The water spray nozzle 15 of the quenching means for injecting the water 4 is provided downward, and is configured to quench the exhaust gas 8 in the secondary combustion chamber 10 by spraying water 14 from the water spray nozzle 15. . As shown in FIG. 2, the water spray nozzle 15 is a two-fluid system of air 13 and water 14, and has a tapered air supply pipe 16 and a tapered water supply pipe 17 disposed inside the air supply pipe 16. And a double structure formed by
【0010】しかも、上記二次燃焼室10の頂部10a
であって、水噴霧ノズル15の周囲には、空気13の通
過が可能なセラミックフォーム18が設けられており、
該セラミックフォーム18から空気13を二次燃焼室1
0内に吹き込むことにより、排ガス8中の溶融飛灰が同
二次燃焼室10の内壁面に付着しないようになってい
る。また、空気供給パイプ16及び水供給パイプ17
は、それぞれ図示しない圧縮ポンプや水供給タンクなど
に接続されている。In addition, the top 10a of the secondary combustion chamber 10
Around the water spray nozzle 15, a ceramic foam 18 through which air 13 can pass is provided,
The air 13 is supplied from the ceramic foam 18 to the secondary combustion chamber 1.
By blowing the gas into the inside 0, the molten fly ash in the exhaust gas 8 does not adhere to the inner wall surface of the secondary combustion chamber 10. In addition, the air supply pipe 16 and the water supply pipe 17
Are connected to a compression pump, a water supply tank, and the like (not shown).
【0011】なお、上記熱交換器12の下流側には、排
ガス処理設備が設けられている。すなわち、熱交換器1
2を経た排ガス8は、図3に示す如く、遠心力により灰
19を分離捕集するサイクロン(集じん装置)20に送
られる共に、苛性ソーダ及び水による処理を行って排水
する排煙処理塔21に送られ、ファン22を介して煙突
23から大気に排出されるようになっている。An exhaust gas treatment facility is provided downstream of the heat exchanger 12. That is, the heat exchanger 1
As shown in FIG. 3, the exhaust gas 8 that has passed through 2 is sent to a cyclone (dust collection device) 20 that separates and collects the ash 19 by centrifugal force, and is treated with caustic soda and water, and is then discharged into a flue gas treatment tower 21. And is discharged from the chimney 23 to the atmosphere via the fan 22.
【0012】このような旋回灰溶融炉1を使用して排ガ
ス8を処理するには、炉内3に供給された焼却灰6をバ
ーナ(図示せず)の火炎により旋回させながら燃焼して
溶融する。溶融されたスラグ4は、図示しないスラグタ
ップから重力により落下して図外のコンベヤなどに排出
されて回収される。一方、炉内3で発生した排ガス8
は、炉本体2のガス出口9より二次燃焼室10に導か
れ、この二次燃焼室10内で燃焼される。そして、二次
燃焼室10の上部に導かれた排ガス8は、図1及び図2
に示す如く、水噴霧ノズル15から噴霧された水14に
よって急冷され、当該排ガス8中にキャリオーバされた
液状溶融飛灰は瞬時に固体化される。すなわち、ガス出
口9の温度が1500゜Cの排ガス8中では、溶融飛灰
が液状となっているが、排ガス8を急冷してその温度を
850゜Cにすると、灰融点の温度1350゜よりも5
00゜C低くなるため、液状溶融飛灰は瞬時に固体化さ
れることになる。In order to treat the exhaust gas 8 using the swirling ash melting furnace 1, the incineration ash 6 supplied to the furnace 3 is burned and melted while being swirled by the flame of a burner (not shown). I do. The molten slag 4 is dropped by a gravity from a slag tap (not shown) and discharged to a conveyor or the like (not shown) to be collected. On the other hand, the exhaust gas 8 generated in the furnace 3
Is guided from the gas outlet 9 of the furnace body 2 to the secondary combustion chamber 10 where it is burned. The exhaust gas 8 guided to the upper part of the secondary combustion chamber 10 is shown in FIGS.
As shown in (1), the liquid molten fly ash rapidly cooled by the water 14 sprayed from the water spray nozzle 15 and carried over in the exhaust gas 8 is instantaneously solidified. That is, in the exhaust gas 8 at a temperature of the gas outlet 9 of 1500 ° C., the molten fly ash is in a liquid state, but when the exhaust gas 8 is rapidly cooled to 850 ° C., the temperature of the ash melting point becomes 1350 ° C. Also 5
Since the temperature is lowered by 00 ° C., the liquid molten fly ash is instantaneously solidified.
【0013】次いで、固体化された溶融飛灰を含む排ガ
ス8は、二次燃焼室10のガス出口(図示せず)から排
ガスダクト11を経て熱交換器12に導かれ、該熱交換
器12内を通過しながら、ファン22にて送給された空
気13と熱交換する。温められた空気13は、炉内3及
び二次燃焼室10に供給される。そして、熱交換器12
を通過した排ガス8は、図3に示す如く、サイクロン2
0に送られて灰19を分離し、また、排煙処理塔21に
送られて苛性ソーダ及び水による洗浄処理が行われ、洗
浄水を排出した後、ファン22を介して煙突23から大
気に排出される。Next, the exhaust gas 8 containing the solidified molten fly ash is introduced from a gas outlet (not shown) of the secondary combustion chamber 10 through an exhaust gas duct 11 to a heat exchanger 12, where the heat exchanger 12 While passing through the inside, heat exchange is performed with the air 13 supplied by the fan 22. The heated air 13 is supplied to the inside of the furnace 3 and the secondary combustion chamber 10. And the heat exchanger 12
As shown in FIG. 3, the exhaust gas 8 passing through the
0 to separate the ash 19, and then sent to a flue gas treatment tower 21 where washing treatment with caustic soda and water is performed. After the washing water is discharged, it is discharged to the atmosphere from a chimney 23 via a fan 22. Is done.
【0014】本実施の形態に係る二次燃焼室10内のガ
ス出口部には、排ガス8を急冷する水噴霧ノズル15が
設けられているため、排ガス8中の液状溶融飛灰を瞬時
に固体化させることができ、これによって溶融飛灰が二
次燃焼室10の出口部や排ガスダクト11及び熱交換器
12の内部に付着するのを防止できる。Since a water spray nozzle 15 for rapidly cooling the exhaust gas 8 is provided at the gas outlet in the secondary combustion chamber 10 according to the present embodiment, the liquid molten fly ash in the exhaust gas 8 is instantaneously solidified. This prevents molten fly ash from adhering to the outlet of the secondary combustion chamber 10, the exhaust gas duct 11, and the heat exchanger 12.
【0015】以上、本発明の実施の形態につき述べた
が、本発明は既述の実施の形態に限定されるものではな
く、本発明の要旨を逸脱しない範囲内において種々の変
形及び変更を加え得るものである。例えば、本発明の実
施の形態では、急冷手段として水噴霧ノズル15を設け
たが、排ガス8中の液状溶融飛灰を急冷して確実に固体
化できれば、スプレー方式など他の構造の急冷手段を使
用してもよい。Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and various modifications and changes may be made without departing from the spirit of the present invention. What you get. For example, in the embodiment of the present invention, the water spray nozzle 15 is provided as the quenching means. However, if the liquid molten fly ash in the exhaust gas 8 can be quenched and solidified surely, a quenching means having another structure such as a spray method can be used. May be used.
【0016】[0016]
【発明の効果】上述の如く、本発明に係る灰溶融炉の排
ガス処理方法は、灰溶融炉の上部に排ガスを燃焼させる
二次燃焼室を設け、この二次燃焼室内に排ガスを導いて
急冷し、該排ガス中の液状溶融飛灰を瞬時に固体化して
排出しているので、排ガス中にキャリオーバされた溶融
飛灰が二次燃焼室、排ガスダクト、熱交換器等の内壁面
に付着するのを確実に防止し、長期安定運転を行うこと
ができ、生産性の向上をとコストダウンを図ることがで
きる。As described above, in the method for treating exhaust gas of an ash melting furnace according to the present invention, a secondary combustion chamber for burning exhaust gas is provided at the upper part of the ash melting furnace, and the exhaust gas is guided into the secondary combustion chamber for rapid cooling. Since the molten fly ash in the exhaust gas is solidified and discharged instantaneously, the molten fly ash carried over in the exhaust gas adheres to the inner wall surfaces of the secondary combustion chamber, the exhaust gas duct, the heat exchanger, and the like. , And stable operation can be performed for a long time, thereby improving productivity and reducing costs.
【0017】また、本発明に係る灰溶融炉は、灰溶融炉
の上部に排ガスを燃焼させる二次燃焼室を設けると共
に、この二次燃焼室内に排ガスを急冷する水噴霧ノズル
などの急冷手段を設けているので、上記発明と同様の効
果が得られる上、効率的にかつ確実に排ガス中の液状溶
融飛灰を急冷することができる。In the ash melting furnace according to the present invention, a secondary combustion chamber for burning exhaust gas is provided above the ash melting furnace, and quench cooling means such as a water spray nozzle for rapidly cooling the exhaust gas is provided in the secondary combustion chamber. With the provision, the same effect as the above invention can be obtained, and the liquid molten fly ash in the exhaust gas can be rapidly and efficiently cooled.
【図1】本発明の実施の形態に係る竪型旋回灰溶融炉を
示す概念図である。FIG. 1 is a conceptual diagram showing a vertical swirling ash melting furnace according to an embodiment of the present invention.
【図2】図1のA部を拡大して示す断面図である。FIG. 2 is an enlarged sectional view showing a portion A in FIG. 1;
【図3】本発明の実施の形態に係る旋回灰溶融炉が適用
される設備の一部を示す概念図である。FIG. 3 is a conceptual diagram showing a part of equipment to which the swirling ash melting furnace according to the embodiment of the present invention is applied.
【図4】従来の竪型旋回灰溶融炉を示す概念図である。FIG. 4 is a conceptual diagram showing a conventional vertical swirling ash melting furnace.
1 旋回灰溶融炉 2 炉本体 3 炉内 4 スラグ 5 燃料 6 焼却灰 7 燃焼空気 8 排ガス 10 二次燃焼室 11 排ガスダクト 12 熱交換器 13 空気 14 水 15 水噴霧ノズル 16 空気供給パイプ 17 水供給パイプ 18 セラミックフォーム DESCRIPTION OF SYMBOLS 1 Swirling ash melting furnace 2 Furnace main body 3 Furnace 4 Slag 5 Fuel 6 Incineration ash 7 Combustion air 8 Exhaust gas 10 Secondary combustion chamber 11 Exhaust gas duct 12 Heat exchanger 13 Air 14 Water 15 Water spray nozzle 16 Air supply pipe 17 Water supply Pipe 18 ceramic foam
───────────────────────────────────────────────────── フロントページの続き (72)発明者 本多 裕姫 神奈川県横浜市金沢区幸浦一丁目8番地1 三菱重工業株式会社横浜研究所内 (72)発明者 田熊 昌夫 神奈川県横浜市金沢区幸浦一丁目8番地1 三菱重工業株式会社横浜研究所内 (72)発明者 石川 出 神奈川県横浜市金沢区幸浦一丁目8番地1 三菱重工業株式会社横浜研究所内 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Hiroki Honda 1-8-1, Koura, Kanazawa-ku, Yokohama-shi, Kanagawa Prefecture Inside Mitsubishi Heavy Industries, Ltd. Yokohama Research Laboratory (72) Inventor Masao Taguma-ichi Koura, Kanazawa-ku, Yokohama-shi, Kanagawa Mitsubishi Heavy Industries, Ltd. Yokohama Research Laboratory (72) Ishikawa Izukawa, Kanagawa Prefecture, Yokohama City
Claims (3)
方法において、前記灰溶融炉の上部に排ガスを燃焼させ
る二次燃焼室を設け、この二次燃焼室内に排ガスを導い
て急冷し、該排ガス中の液状溶融飛灰を瞬時に固体化し
て排出することを特徴とする灰溶融炉の排ガス処理方
法。1. An exhaust gas treatment method for an ash melting furnace for melting incineration ash, wherein a secondary combustion chamber for burning exhaust gas is provided at an upper portion of the ash melting furnace, and the exhaust gas is introduced into the secondary combustion chamber to be rapidly cooled. An exhaust gas treatment method for an ash melting furnace, comprising instantaneously solidifying and discharging liquid molten fly ash in the exhaust gas.
灰溶融炉の上部に排ガスを燃焼させる二次燃焼室を設け
ると共に、この二次燃焼室内に排ガスを急冷する急冷手
段を設けたことを特徴とする灰溶融炉。2. In an ash melting furnace for melting incinerated ash, a secondary combustion chamber for burning exhaust gas is provided above the ash melting furnace, and quenching means for rapidly cooling the exhaust gas is provided in the secondary combustion chamber. An ash melting furnace characterized by the following.
ルからなることを特徴とする請求項2に記載の灰溶融
炉。3. The ash melting furnace according to claim 2, wherein said quenching means comprises a water spray nozzle for spraying water.
Priority Applications (1)
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JP11482098A JP3905635B2 (en) | 1998-04-24 | 1998-04-24 | Ash melting furnace |
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JP11482098A JP3905635B2 (en) | 1998-04-24 | 1998-04-24 | Ash melting furnace |
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JPH11304137A true JPH11304137A (en) | 1999-11-05 |
JP3905635B2 JP3905635B2 (en) | 2007-04-18 |
Family
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JP11482098A Expired - Fee Related JP3905635B2 (en) | 1998-04-24 | 1998-04-24 | Ash melting furnace |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113513760A (en) * | 2021-07-16 | 2021-10-19 | 江门市崖门新财富环保工业有限公司 | Dangerous waste melting and secondary combustion chamber integrated furnace |
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JPS5821729U (en) * | 1981-07-27 | 1983-02-10 | 大阪瓦斯株式会社 | industrial waste melting furnace |
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JPH06265134A (en) * | 1993-03-11 | 1994-09-20 | Kansai Electric Power Co Inc:The | Apparatus and method for recovering value in plasma melting furnace |
JPH08219437A (en) * | 1995-02-15 | 1996-08-30 | Mitsubishi Heavy Ind Ltd | Exhaust gas duct and treating method of high-temperature exhaust gas |
JPH08285245A (en) * | 1995-04-13 | 1996-11-01 | Hitachi Zosen Corp | Electric ash melting furnace facility |
JPH09243049A (en) * | 1996-03-05 | 1997-09-16 | Hitachi Zosen Corp | Exhaust gas cooling apparatus for ash fusing furnace equipment |
JPH10103635A (en) * | 1996-09-25 | 1998-04-21 | Plantec:Kk | Direct connected type incineration ash melting and processing facility and its processing method |
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1998
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Patent Citations (7)
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JPS5821729U (en) * | 1981-07-27 | 1983-02-10 | 大阪瓦斯株式会社 | industrial waste melting furnace |
JPH0630642U (en) * | 1992-09-02 | 1994-04-22 | 株式会社神戸製鋼所 | Nozzle cleaning device for gas cooling chamber |
JPH06265134A (en) * | 1993-03-11 | 1994-09-20 | Kansai Electric Power Co Inc:The | Apparatus and method for recovering value in plasma melting furnace |
JPH08219437A (en) * | 1995-02-15 | 1996-08-30 | Mitsubishi Heavy Ind Ltd | Exhaust gas duct and treating method of high-temperature exhaust gas |
JPH08285245A (en) * | 1995-04-13 | 1996-11-01 | Hitachi Zosen Corp | Electric ash melting furnace facility |
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JPH10103635A (en) * | 1996-09-25 | 1998-04-21 | Plantec:Kk | Direct connected type incineration ash melting and processing facility and its processing method |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN113513760A (en) * | 2021-07-16 | 2021-10-19 | 江门市崖门新财富环保工业有限公司 | Dangerous waste melting and secondary combustion chamber integrated furnace |
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