JPH07260357A - Ash-melting furnace apparatus - Google Patents

Ash-melting furnace apparatus

Info

Publication number
JPH07260357A
JPH07260357A JP5082494A JP5082494A JPH07260357A JP H07260357 A JPH07260357 A JP H07260357A JP 5082494 A JP5082494 A JP 5082494A JP 5082494 A JP5082494 A JP 5082494A JP H07260357 A JPH07260357 A JP H07260357A
Authority
JP
Japan
Prior art keywords
ash
burner
furnace
exhaust
side wall
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
JP5082494A
Other languages
Japanese (ja)
Inventor
Sho Yasuoka
省 安岡
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.)
Tokyo Gas Co Ltd
Original Assignee
Tokyo Gas 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 Tokyo Gas Co Ltd filed Critical Tokyo Gas Co Ltd
Priority to JP5082494A priority Critical patent/JPH07260357A/en
Publication of JPH07260357A publication Critical patent/JPH07260357A/en
Pending legal-status Critical Current

Links

Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Abstract

PURPOSE:To realize the compactification of a furnace, suppress the generation of NOx and homogenize a melt by providing a burner in an opening of a side wall of a furnace body and an exhaust-discharge outlet in an opening of another side wall and arranging a melt chamber in a bottom wall from which the melt overflows to the exhaust-discharge outlet. CONSTITUTION:A furnace body 1 is provided with a burner 2 in an opening of a side wall 3 and an exhaust-discharge outlet 5 in an opening in another side wall 4. The furnace body 1 is further provided in a bottom wall thereof with a melt chamber 6 from which the melt overflows to the exhaust-discharge outlet 5. Ash preliminarily mixed with air or oxygen is fed together with fuel and is made to burn by the burner 2 while being circulated in a slewing device 7. Combustion gas is made to diffuse in an opening 9 and flat flame 11 is formed and circulation flow is simultaneously formed in the interior 10 of the furnace. Part of particles of the ash are made to move along an incline ceiling wall 8 before being allowed to fall into the melt chamber 6. Thus, the atmosphere within the furnace 10 is stirred and the melting of the ash and the homogenization of the melt are facilitated.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、灰溶融炉装置に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ash melting furnace apparatus.

【0002】[0002]

【従来の技術】焼却灰等の成分中には揮発成分が含まれ
ており、これは高温で発泡するため、ガス抜きをする必
要がある。従来は、バーナにより焼却灰の表面から順次
溶融して行く方法であり、この方法を実行するための装
置として、傾斜反射炉、旋回溶融炉、電気溶融炉等の種
々のものがある。
2. Description of the Related Art Ingredients such as incinerated ash contain volatile components, which are foamed at a high temperature and must be degassed. Conventionally, it is a method of sequentially melting from the surface of the incineration ash by a burner, and there are various devices such as an inclined reverberation furnace, a swirling melting furnace, an electric melting furnace, etc. for performing this method.

【0003】[0003]

【発明が解決するための課題】前記した炉では、ダスト
が排気等により外部へ飛散することが多い。また、溶融
を輻射伝熱のみに依存しているため、灰表面の面積等の
必要性から設備が大型化せざるを得なかった。また、電
気溶融炉では、ダストの飛散は抑えられるものの、溶融
エネルギコストが非常に高く、且つ電極等の消耗が激し
いため、操業コストの面で大きな課題があった。
DISCLOSURE OF THE INVENTION In the above-mentioned furnace, dust is often scattered to the outside due to exhaust gas or the like. In addition, since the melting depends only on the radiative heat transfer, the facility has to be increased in size due to the necessity of the area of the ash surface and the like. Further, in the electric melting furnace, although the scattering of dust can be suppressed, the melting energy cost is very high, and the electrodes and the like are consumed so much that there is a big problem in terms of operating cost.

【0004】[0004]

【課題を解決するための手段】前記課題を解決するため
に、本発明は、炉体側壁にバーナを開口させ、そのバー
ナとは反対側の炉体側壁下部に排気兼排出口を構成し、
炉底には前記排気兼排出口へ溶湯がオーバーフローする
溶湯室を設けたことを特徴とする灰溶融装置を提供する
ものである。
In order to solve the above-mentioned problems, according to the present invention, a burner is opened in a side wall of a furnace body, and an exhaust / exhaust port is formed in a lower part of the side wall of the furnace body opposite to the burner.
The ash melting apparatus is provided with a molten metal chamber at the bottom of the furnace, the molten metal overflowing into the exhaust / exhaust port.

【0005】また、本発明は、バーナは、燃焼用空気又
は酸素と灰との予混合気を旋回させ、平面火炎を形成す
る旋回器を保持させたことを特徴とする第1項記載の灰
溶炉融装置を提供するものである。
Further, according to the present invention, the burner swirls combustion air or a premixed air of oxygen and ash to hold a swirler for forming a flat flame. A furnace melting apparatus is provided.

【0006】また本発明は、炉体の天井はバーナから排
気兼排出口に向けてやや下降させた傾斜天井壁に構成し
たことを特徴とする請求項1記載の灰溶融装置を提供す
るものである。
Further, the present invention provides the ash melting apparatus according to claim 1, characterized in that the ceiling of the furnace body is constituted by an inclined ceiling wall slightly lowered from the burner toward the exhaust / exhaust port. is there.

【0007】[0007]

【作用】空気又は酸素と予混合した灰は、バーナに供給
されて旋回器を介して噴出し、同時に燃料ガスがバーナ
に供給されると、前記予混合気と燃料ガスは旋回しなが
らバーナに於いて燃焼を開始する。しかして、燃焼ガス
は、開口部に於いて急速に拡大しつつ平面火炎を形成し
ながら、炉内で図中矢印の如く循環流を形成する。そし
て、同時に、火炎中で溶解を開始した灰の粒子は開口部
周囲の側壁を移動して、一部は側壁下側から溶湯室へと
流れるが、他の一部は、傾斜天井壁へと移動しつつ雫と
して溶湯室へ落下する。天井壁は、前記した通り、傾斜
構成しているので、溶湯の一部は壁面にそって移動しつ
つ輻射伝熱と対流伝熱をうけながら溶融均質化されて溶
融室へと落下する。溶湯室内で完全に溶融均質化された
後、溶湯はオーバーフローして排気兼排出口から排出さ
れる。かかる際、炉内では、前記した通り、図中矢印で
示すような循環流が形成されており、これにより炉内雰
囲気は攪拌されて灰の溶融及び均質化を促進する。
The ash premixed with air or oxygen is supplied to the burner and ejected through the swirler. At the same time, when the fuel gas is supplied to the burner, the premixed gas and the fuel gas swirl to the burner. Combustion starts there. Then, the combustion gas forms a plane flame while rapidly expanding at the opening and forms a circulating flow in the furnace as indicated by an arrow in the figure. At the same time, the ash particles that have started to dissolve in the flame move on the side wall around the opening, and part of the ash particles flow from the lower side of the side wall to the molten metal chamber, while the other part moves to the inclined ceiling wall. While moving, it drops as a drop into the molten metal chamber. Since the ceiling wall is inclined as described above, a part of the molten metal is melted and homogenized while moving along the wall surface while undergoing radiative heat transfer and convective heat transfer and falls into the melting chamber. After being completely melted and homogenized in the molten metal chamber, the molten metal overflows and is discharged from the exhaust / discharge port. At this time, as described above, a circulating flow is formed in the furnace as shown by the arrow in the figure, whereby the atmosphere in the furnace is agitated to promote melting and homogenization of ash.

【0008】[0008]

【実施例】符号1は炉体であって、2は炉体1の側壁3
に開口部9に開口させたバーナである。そのバーナ2の
反対側の側壁4の下部には、排気兼排出口5を構成し、
炉底には前記排気兼排出口5へ溶湯がオーバーフローす
る溶湯室6を構成する。バーナ2は、燃焼用空気又は酸
素と灰との予混合気を旋回させる旋回器7を保持させ
る。また、炉体1の天井は、バーナ2から排気兼排出口
5へとやや下降させた傾斜天井壁8に構成する。その天
井壁8の角度、即ち、図中θは、溶湯の流れ状態を勘案
しながら10〜45度の範囲でよい。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Reference numeral 1 is a furnace body, and 2 is a side wall 3 of the furnace body 1.
It is a burner opened at the opening 9. An exhaust / exhaust port 5 is formed in the lower portion of the side wall 4 opposite to the burner 2,
At the bottom of the furnace, a molten metal chamber 6 is formed in which the molten metal overflows into the exhaust / exhaust port 5. The burner 2 holds a swirler 7 that swirls combustion air or a premixed air of oxygen and ash. Further, the ceiling of the furnace body 1 is constituted by an inclined ceiling wall 8 slightly lowered from the burner 2 to the exhaust / exhaust port 5. The angle of the ceiling wall 8, that is, θ in the figure, may be in the range of 10 to 45 degrees in consideration of the flow state of the molten metal.

【0009】空気又は酸素と予混合した灰は、空気供給
部12からバーナ2に供給されて旋回器7を介して噴出
し、同時に燃料ガスがバーナ2に供給されると、前記予
混合気と燃料ガスは旋回しながらバーナ2に於いて燃焼
を開始する。しかして、燃焼ガスは、開口部9に於いて
急速に拡大しつつ平面火炎11を形成し、炉内10で図
中矢印の如く循環流を形成する。そして、同時に、火炎
中で溶解を開始した灰の粒子は開口部9周囲の側壁3を
移動して、一部は側壁3の下側から溶湯室6へと流れる
が、他の一部は、傾斜天井壁8へと移動しつつ雫として
側壁4から溶湯室6へと落下する。天井壁8は、前記し
た通り、傾斜構成しているので、溶湯の一部は壁面にそ
って移動しつつ輻射伝熱と対流伝熱をうけながら溶融均
質化されて溶融室6へと落下する。溶湯室6内で完全に
溶融均質化された後、溶湯13はオーバーフローして反
対側の側壁4の下部の排気兼排出口5から排出される。
かかる際、炉内10では、前記した通り、図中矢印で示
すような循環流が形成されており、これにより炉内10
の雰囲気は攪拌されて灰の溶融及び均質化を促進する。
かかる際、バーナ2の空気比は、1.0〜1.5であ
り、また炉内10の温度は、1200〜1600℃であ
る。更に、実操業に際しては、バーナインプット又は空
気比、或は灰の量等を意図的且つ周期的に、例えば、数
秒〜数10秒に変化させて行なうことにより灰やガスの
流れが固定化されない。
The ash premixed with air or oxygen is supplied to the burner 2 from the air supply unit 12 and ejected through the swirler 7, and at the same time when the fuel gas is supplied to the burner 2, the premixed air and the ash are mixed. The fuel gas starts combustion in the burner 2 while swirling. Then, the combustion gas forms a flat flame 11 while rapidly expanding at the opening 9, and forms a circulating flow in the furnace 10 as shown by an arrow in the figure. At the same time, the ash particles that have started to dissolve in the flame move on the side wall 3 around the opening 9 and partly flows from the lower side of the side wall 3 to the molten metal chamber 6, while the other part is While moving to the sloping ceiling wall 8, it drops from the side wall 4 into the molten metal chamber 6 as a drop. Since the ceiling wall 8 is inclined as described above, a part of the molten metal is melted and homogenized while moving along the wall surface while undergoing radiative heat transfer and convective heat transfer and falls into the melting chamber 6. . After being completely melted and homogenized in the molten metal chamber 6, the molten metal 13 overflows and is discharged from the exhaust / exhaust port 5 below the side wall 4 on the opposite side.
At this time, as described above, the circulation flow as shown by the arrow in the drawing is formed in the furnace 10, so that the inside 10
The atmosphere is stirred to promote ash melting and homogenization.
At this time, the air ratio of the burner 2 is 1.0 to 1.5, and the temperature of the furnace 10 is 1200 to 1600 ° C. Further, in actual operation, the flow of ash and gas is not fixed by intentionally and periodically changing the burner input or the air ratio, or the amount of ash, for example, from several seconds to several tens of seconds. .

【0010】[0010]

【発明の効果】本発明は以上の通りであるので、次の諸
効果がある。炉体の独特の構成と旋回流平面火炎を形
成するバーナを使用することにより炉体を大巾にコンパ
クト化できる。火炎中で灰が溶融するため、火炎が冷
却されNOX発生が抑制されると同時に伝熱効果の向上
により省エネが達成できる。天井壁面、各側壁面に於
いて、攪拌する燃焼ガスと灰との摩擦、衝突を繰り返す
ので、輻射加熱と相乗して溶解が促進され、溶湯の均質
化が達成できる。特に側壁に於いて、下方向に向った
灰は溶湯室内の溶湯との接触により吸収され速かに溶融
が完了する。これは雰囲気ガスに混じってダストを飛散
するのを防止できるという大きな効果がある。更に炉
内を燃焼ガスの循環流は溶湯室内の溶湯を高温に保持す
る作用をし、固形分の残留や排出口からの流出を防止す
る。
As described above, the present invention has the following effects. The furnace body can be made extremely compact by using a unique structure of the furnace body and a burner that forms a swirling plane flame. Because ash is melted in the flame, energy saving by improvement at the same time the heat transfer effect the NO X generated flame is cooled is suppressed it can be achieved. On the ceiling wall surface and each side wall surface, friction and collision between the agitated combustion gas and ash are repeated, so that melting is promoted synergistically with radiant heating and homogenization of the molten metal can be achieved. Especially on the side wall, the ash directed downward is absorbed by the contact with the molten metal in the molten metal chamber, and the melting is completed quickly. This has a great effect that it is possible to prevent dust from being scattered by mixing with the atmospheric gas. Further, the circulating flow of the combustion gas in the furnace acts to keep the molten metal in the molten metal chamber at a high temperature, and prevents the solid content from remaining and flowing out from the discharge port.

【0011】[0011]

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

【図1】図1は本発明の断面的説明図である。FIG. 1 is a cross-sectional explanatory view of the present invention.

【符号の説明】[Explanation of symbols]

1 炉体 2 バーナ 3 バーナ側の側壁 4 反対側の側壁 5 排気兼排出口 6 溶湯室 7 旋回器 8 傾斜天井壁 9 開口部 10 炉内 11 平面火炎 12 空気供給部 13 溶湯 1 Furnace Body 2 Burner 3 Side Wall on Burner Side 4 Side Wall on Opposite Side 5 Exhaust and Discharge Port 6 Melt Chamber 7 Swirler 8 Inclined Ceiling Wall 9 Opening 10 Inside Furnace 11 Plane Flame 12 Air Supply Section 13 Molten Metal

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F27B 3/20 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display area F27B 3/20

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 炉体側壁にバーナを開口させ、そのバー
ナとは反対側の炉体側壁下部に排気兼排出口を構成し、
炉底には前記排気兼排出口へ溶湯がオーバーフローする
溶湯室を設けたことを特徴とする灰溶融炉装置。
1. A burner is opened in the side wall of the furnace body, and an exhaust / exhaust port is formed in the lower part of the side wall of the furnace body on the side opposite to the burner.
An ash-melting furnace apparatus characterized in that a molten metal chamber is provided at the bottom of the furnace so that the molten metal overflows to the exhaust / exhaust port.
【請求項2】 バーナは、燃焼用空気又は酸素と灰との
予混合気を旋回させ、平面火炎を形成する旋回器を保持
させたことを特徴とする請求項1記載の灰溶融炉装置。
2. The ash melting furnace apparatus according to claim 1, wherein the burner has a swirler that swirls combustion air or a premixed air of oxygen and ash to form a flat flame.
【請求項3】 炉体の天井はバーナから排気兼排出口に
向けてやや下降させた傾斜天井壁に構成したことを特徴
とする請求項1記載の灰溶融炉装置。
3. The ash melting furnace apparatus according to claim 1, wherein the roof of the furnace body is constructed as an inclined ceiling wall which is slightly lowered from the burner toward the exhaust / exhaust port.
JP5082494A 1994-03-22 1994-03-22 Ash-melting furnace apparatus Pending JPH07260357A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5082494A JPH07260357A (en) 1994-03-22 1994-03-22 Ash-melting furnace apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5082494A JPH07260357A (en) 1994-03-22 1994-03-22 Ash-melting furnace apparatus

Publications (1)

Publication Number Publication Date
JPH07260357A true JPH07260357A (en) 1995-10-13

Family

ID=12869527

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5082494A Pending JPH07260357A (en) 1994-03-22 1994-03-22 Ash-melting furnace apparatus

Country Status (1)

Country Link
JP (1) JPH07260357A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6461145B1 (en) * 1999-02-25 2002-10-08 Stein Heurtey Flat flame burners
KR100391902B1 (en) * 1998-12-23 2003-10-17 주식회사 포스코 Gas burner and method for producing flat flame in annealing furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100391902B1 (en) * 1998-12-23 2003-10-17 주식회사 포스코 Gas burner and method for producing flat flame in annealing furnace
US6461145B1 (en) * 1999-02-25 2002-10-08 Stein Heurtey Flat flame burners

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