JP3365584B2 - Ash melting method and equipment - Google Patents
Ash melting method and equipmentInfo
- Publication number
- JP3365584B2 JP3365584B2 JP20576394A JP20576394A JP3365584B2 JP 3365584 B2 JP3365584 B2 JP 3365584B2 JP 20576394 A JP20576394 A JP 20576394A JP 20576394 A JP20576394 A JP 20576394A JP 3365584 B2 JP3365584 B2 JP 3365584B2
- Authority
- JP
- Japan
- Prior art keywords
- ash
- melting
- furnace
- melted
- flame
- 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
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、灰溶融方法及び装置に
関するものである。FIELD OF THE INVENTION The present invention relates to an ash melting method and apparatus.
【0002】[0002]
【従来技術】従来の燃焼式灰溶融炉は、バーナ火炎と炉
内壁の輻射加熱により灰の層の表面から溶融させる表面
溶融炉と、灰を全量燃焼用空気またはこの流れの中に混
ぜ、火炎中並びに炉内壁に付着させて溶融させる旋回溶
融炉等の2つの大きなタイプがある。2. Description of the Related Art A conventional combustion-type ash melting furnace is a surface melting furnace that melts from the surface of a layer of ash by a burner flame and radiant heating of the inner wall of the furnace, and the total amount of ash is mixed with combustion air or this flow to produce flame There are two major types, such as swirl melting furnaces, which melt by adhering to the inside and inside walls of the furnace.
【0003】[0003]
【発明が解決する課題】前記した表面溶融炉は、灰は
その表面しか溶融せず、すぐ下の灰の層が断熱層となり
周囲または下部の炉体構造を熱と浸食から守る働きがあ
る。炉内では輻射加熱により、灰の層の表面だけを溶
融する方式であるため、負荷を大きくとれず、結果とし
て大型となり、効率も低い。一般に火炎温度も高くな
り、NOxも高い等々の課題がある。また前記した旋回
溶融炉は、火炎並びに溶融途中の灰粒子を炉内壁に直
接ぶつける方式であるために、炉内の損傷が激しい。こ
のタイプの溶融炉は燃焼ガス並びに灰の流れのコースが
固定化されやすく、このコースの炉内壁は頻繁にメンテ
ナンスが必要となる。全量の灰を火炎または燃焼ガス
中に混ぜ込むこの方式では、熱源単位を向上させるには
大量の灰を火炎中に混合する必要があるが、この際火炎
の維持や燃焼制御が難しくなり未燃分の発生などを招く
等々の課題がある。In the surface melting furnace described above, the ash melts only on its surface, and the ash layer immediately below serves as a heat insulating layer to protect the surrounding or lower furnace body structure from heat and erosion. Since only the surface of the ash layer is melted by radiant heating in the furnace, a large load cannot be taken, resulting in a large size and low efficiency. Generally, there are problems such as high flame temperature and high NOx. Further, since the swirling melting furnace described above is a method of directly hitting the flame and ash particles in the middle of melting on the inner wall of the furnace, the damage in the furnace is severe. In this type of melting furnace, the course of combustion gas and ash flow is likely to be fixed, and the furnace inner wall of this course requires frequent maintenance. In this method of mixing all the amount of ash into the flame or combustion gas, it is necessary to mix a large amount of ash into the flame in order to improve the heat source unit, but at this time it is difficult to maintain the flame and control combustion, and unburned There are problems such as the generation of minutes.
【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、本発明は溶融すべき灰の一部を燃料、空気等の支燃
剤と共に灰溶融バーナで燃焼させて溶融粒子として火炎
と共に、炉内に投入した溶融すべき灰中に高速で噴出さ
せ、前記炉内の灰の深部まで熱を伝達させて炉内の灰の
溶融を促進することを特徴とする灰溶融方法を提供する
ものである。In order to solve the above-mentioned problems, the present invention burns a part of ash to be melted together with a combustion-supporting agent such as fuel and air in an ash-melting burner to form a molten particle together with a flame in a furnace. is ejected at high speed into the ash in to be melted was charged within, it is provided a ash melting method characterized by facilitating the melting of ash deep ash by transferring heat in the furnace of the furnace is there.
【0005】また、本発明は、炉における溶融すべき灰
を投入する主灰供給部の下方に傾斜溶融部を構成し、こ
の傾斜溶融部に対向する炉体壁に灰溶融バーナを設置
し、この灰溶融バーナ側に、溶融すべき灰の一部を燃
料、空気等の支燃剤に混入させる予混合灰供給部を設
け、予混合灰を燃料、空気等の支燃剤と共に前記灰溶融
バーナにより燃焼させて溶融粒子として火炎と共に、炉
内に投入した溶融すべき灰中に高速で噴出させる構成と
したことを特徴とする灰溶融装置を提供するものであ
る。The present invention also relates to the ash to be melted in the furnace.
The inclined melting section is constructed below the main ash supply section where
Installed ash melting burner on the furnace wall facing the inclined melting part of
Then, burn part of the ash to be melted to the ash melting burner side.
Installed a premixed ash supply unit that mixes with fuel, air, and other combustion-supporting agents.
Fusing the premixed ash with fuel, air and other combustion-supporting agents
Burned by a burner to form molten particles together with the flame, the furnace
With a configuration that ejects at high speed into the ash that is to be melted and is to be melted
The present invention provides an ash melting device characterized by
It
【0006】[0006]
【作用】灰溶融バーナから溶融すべき灰の一部を溶融粒
子として火炎と共に炉内に投入した溶融すべき灰中に高
速で噴出させる。火炎と共に高速で吹き出された前記灰
溶融バーナ側からの予混合灰の溶融粒子(溶融完了のも
のや溶融途中の物も含む)は直進性に優れ、その保有熱
と運動エネルギーにより、燃焼噴流となって効果的に炉
内の灰層表面を叩き、深部まで熱を伝え、溶融を促進す
る。前記炉内の灰層に入り込んだ溶融粒子は周囲の炉内
灰が溶融を開始するきっかけ(核)となり、また表面の
残った溶融粒子は、まだ粉末状の炉内灰表面からの灰の
飛散を防止する。更に、炉内灰層の表面は、火炎と炉内
からの輻射加熱が加わり、上記の効果により溶融が促進
される。前記灰溶融バーナ側からの予混合灰の混合割合
は灰の材質や燃料の性質、炉体構造により異なる。一般
に低カロリーの燃料や燃えにくい燃料では、火炎の安定
性から灰の予混合率を50%以下に抑える。Function: A portion of the ash to be melted from the ash melting burner is jetted at high speed as molten particles into the ash to be melted introduced into the furnace together with the flame. The ash blown out at high speed with the flame
The molten particles of premixed ash (including those that have been melted and those that are in the process of being melted ) from the side of the melting burner are excellent in straightness, and the heat and kinetic energy possessed by them make it a combustion jet and the furnace effectively
It strikes the surface of the ash layer inside and transfers heat to deep parts to promote melting. Molten particles melt particles entering into the ash layer around the furnace <br/> ash remaining the trigger (nucleus), and also the surface to initiate melting of the furnace, the still powdery furnace ash surface Prevent the scattering of ash. Furthermore, the surface of the furnace ash layer, joined by radiant heat from the flame and furnace, melting accelerated by the effect
To be done . The mixing ratio of the premixed ash from the ash melting burner side varies depending on the material of the ash, the property of the fuel, and the structure of the furnace body. Generally, for low-calorie fuels and non-flammable fuels, the ash premixing ratio is suppressed to 50% or less because of flame stability.
【0007】[0007]
【実施例】符号1は炉体であって、2は主灰供給部であ
る。3は主灰供給部2の下部に設けた傾斜溶融部であ
る。この傾斜溶融部3の対向壁に灰溶融バーナ4を設置
し、その灰溶融バーナ4には燃料供給部5、空気等の支
燃剤供給部6及び予混合灰供給部7を設け、前記傾斜溶
融部3の下部には完全溶融部12を構成する。8はプッ
シャー、9は排出部である。場合によっては、前記予混
合灰供給部7を設けずに、燃料に溶融すべき灰の一部を
混入したり、支燃剤に溶融すべき灰の一部を混入しても
よい。EXAMPLES Reference numeral 1 is a furnace body , and 2 is a main ash supply section . Reference numeral 3 denotes an inclined melting section provided below the main ash supply section 2 . An ash melting burner 4 is installed on the opposite wall of the inclined melting section 3, and the ash melting burner 4 is provided with a fuel supply section 5, a combustion-supporting agent supply section 6 such as air, and a premixed ash supply section 7. A complete melting portion 12 is formed below the portion 3. 8 is a pusher, and 9 is a discharge part. In some cases, the premix
A part of the ash to be melted may be mixed into the fuel or a part of the ash to be melted may be mixed into the combustion supporting agent without providing the combined ash supply unit 7.
【0008】主灰供給部2から灰10を投入する一方、
灰溶融バーナ4には予混合灰供給部7から溶融すべき灰
の一部が、また燃料供給部5及び支燃剤供給部6から
は、それぞれ、燃料ガス及び空気等が灰溶融バーナ4に
導入されると、バーナ4に於いて燃焼が開始して、前記
予混合灰供給部7から供給された予混合灰は溶融粒子と
なって火炎11と共に前記炉体1内の灰10中に高速で
噴出する。高速で吹き出された前記予混合灰の溶融粒子
(溶融完了のものや溶融途中の物も含む)は直進性に優
れ、その保有熱と運動エネルギーにより、燃焼噴流とな
って効果的に灰10層表面を叩き、深部まで熱を伝え、
溶融を促進する。灰10層に入り込んだ溶融粒子は周囲
の灰10が溶融を開始するきっかけ(核)となり、また
表面の残った溶融粒子は、まだ粉末状の灰10表面から
の灰の飛散を防止する。更に、灰10層の表面は、火炎
11と炉内からの輻射加熱が加わり、上記の効果により
溶融が促進される。前記予混合灰供給部7から供給され
た予混合灰の混合割合は灰の材質や燃料の性質、炉体1
構造により異なる。一般に低カロリーの燃料等では火炎
の安定性から灰の予混合比率を50%以下に抑える。While the ash 10 is charged from the main ash supply unit 2,
The ash to be melted from the premixed ash supply unit 7 is supplied to the ash melting burner 4.
Part, also from the fuel supply unit 5 and the combustion-supporting agent supply unit 6, respectively, the fuel gas and air or the like is introduced into the ash melting burner 4, the start of the combustion at the burner 4, wherein
The premixed ash supplied from the premixed ash supply unit 7 becomes molten particles and is jetted at high speed into the ash 10 in the furnace body 1 together with the flame 11. The molten particles of the premixed ash blown out at high speed (including those that have been melted and those that are in the process of being melted ) have excellent straightness, and due to the heat and kinetic energy that they possess, they become a combustion jet.
Effectively beating the ash 10 layer surface, transferring heat to the deep I,
Promotes melting. The molten particles that have entered the ash 10 layer serve as a trigger (nucleus) for the surrounding ash 10 to start melting, and the molten particles that remain on the surface prevent the ash from scattering from the surface of the ash 10 which is still powdery. Further, the surface of the ash 10 layer is heated by the flame 11 and radiant heating from the inside of the furnace, and the melting is promoted by the above effect. It is supplied from the premixed ash supply unit 7.
The mixing ratio of the premixed ash depends on the material of the ash, the properties of the fuel, the furnace body 1
It depends on the structure. Generally, in the case of low-calorie fuel, etc., the premixing ratio of ash is suppressed to 50% or less for stability of flame.
【0009】一般に材料を火炎中に混ぜる場合は、吸熱
により火炎温度が下がるため、バーナ自体はNOxの低
減対策を施さない汎用の物で構わない。ただし、よりN
Oxの低減を求めるには低NOxバーナを使用すること
ができる。この場合灰粒子を含んだ火炎の運動量を維持
するには高速で吹き出す低NOxバーナが必要となる
が、一般のそれらは流速が遅いため当方式には不向きで
ある。この方式に有効なバーナは「燃料炉内直接噴射」
を利用したもので、流速を上げるほどNOxの低減効果
があるため、そのときは本発明の特徴である運動エネル
ギーも維持できる。灰溶融炉用のバーナ構造の例を図2
に示す。NOxの低減原理は主に火炎温度を下げること
である。しかし、限られたスペース内での短い火炎内で
材料をしっかりと溶融させたいときは、これと反対に火
炎温度を上げ気味にする必要も出てくる。火炎中で完全
溶融する割合をどう設定するか、また予混合割合をどう
設定するかなどにより、最適な火炎の状態を選択しなけ
ればならないことは言うまでもない。場合によって支燃
剤として酸素を使用してもよい。In general, when the materials are mixed in the flame, the flame temperature is lowered by the heat absorption, so that the burner itself may be a general-purpose one without the NOx reduction measures. However, more N
A low NOx burner can be used to seek Ox reduction. In this case, a low NOx burner that blows out at high speed is required to maintain the momentum of the flame containing ash particles, but these are generally unsuitable for this system because the flow velocity is slow. The burner effective for this method is "direct injection in the fuel furnace".
Since the NOx reduction effect is obtained as the flow velocity is increased, the kinetic energy, which is a feature of the present invention, can be maintained at that time. Fig. 2 shows an example of a burner structure for an ash melting furnace.
Shown in. The principle of NOx reduction is mainly to lower the flame temperature. However, when it is desired to melt the material in a short flame within a limited space, the flame temperature must be raised to the contrary. It goes without saying that the optimum flame state must be selected depending on how to set the ratio of complete melting in the flame and how to set the premixing ratio. In some cases, oxygen may be used as a combustion support agent.
【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。火炎温度が数十度から数百度下がり、N
Oxの発生が抑えられる。予混合させた灰は、伝熱効
果の高い火炎中で効果的に溶融される。表面部分にお
いてもこの衝撃加熱により、溶融が促進され、と合わ
せて高効率の溶融が実現する。粒子を含んだ火炎は直
進性に優れるため、表面溶融時に必要とされる灰層表面
のヒートスポットが作りやすい。(一般に表面溶融の場
合、溶融を積極的に開始する温度の高い部分を持ったほ
うが良い。)従来の表面溶融炉の特徴である下部の未
溶融灰層による炉体の保護の機能も維持できる。全体
の伝熱効果が高いため、同一容積当たりの負荷を上げる
事ができ、より高効率の溶融及び装置のコンパクト化が
可能となる。As described above, the present invention has the following effects. Flame temperature drops from tens to hundreds of degrees, N
Generation of Ox is suppressed. The premixed ash is effectively melted in a flame having a high heat transfer effect. This impact heating also promotes melting at the surface portion, and together with this, highly efficient melting is realized. Since the flame containing particles is excellent in straightness, a heat spot on the surface of the ash layer, which is required when the surface is melted, is easily formed. (Generally, in the case of surface melting, it is better to have a high temperature part that actively starts melting.) The function of protecting the furnace body by the lower unmelted ash layer, which is a feature of conventional surface melting furnaces, can be maintained. . Since the overall heat transfer effect is high, it is possible to increase the load per unit volume, and it is possible to achieve more efficient melting and downsizing of the device .
【0011】[0011]
【図面の簡単な説明】[Brief description of drawings]
【図1】全体の断面的説明図である。FIG. 1 is an overall cross-sectional explanatory view.
【図2】灰溶融バーナの説明図である。FIG. 2 is an explanatory view of an ash melting burner.
1 炉体 2 主灰供給部 3 傾斜溶融部 4 灰溶融バーナ 5 燃料供給部 6 支燃剤供給部 7 予混合灰供給部 8 プッシャー 9 排出部 10 灰 11 火炎1 Furnace Body 2 Main Ash Supply Section 3 Gradient Melting Section 4 Ash Melting Burner 5 Fuel Supply Section 6 Combustion Agent Supply Section 7 Premixed Ash Supply Section 8 Pusher 9 Discharge Section 10 Ash 11 Flame
フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F23G 5/00 115 F27B 3/20 F23J 1/00 Front page continued (58) Fields surveyed (Int.Cl. 7 , DB name) F23G 5/00 115 F27B 3/20 F23J 1/00
Claims (2)
支燃剤と共に灰溶融バーナで燃焼させて溶融粒子として
火炎と共に、炉内に投入した溶融すべき灰中に高速で噴
出させ、前記炉内の灰の深部まで熱を伝達させて炉内の
灰の溶融を促進することを特徴とする灰溶融方法。1. A part of the ash to be melted is burned by an ash melting burner together with a combustion-supporting agent such as fuel and air to be ejected at high speed into the ash to be melted, together with a flame as molten particles, A method for melting ash, characterized in that heat is transferred to a deep portion of the ash in the furnace to accelerate melting of the ash in the furnace .
灰供給部の下方に傾斜溶融部を構成し、この傾斜溶融部
に対向する炉体壁に灰溶融バーナを設置し、この灰溶融
バーナ側に、溶融すべき灰の一部を燃料、空気等の支燃
剤に混入させる予混合灰供給部を設け、予混合灰を燃
料、空気等の支燃剤と共に前記灰溶融バーナにより燃焼
させて溶融粒子として火炎と共に、炉内に投入した溶融
すべき灰中に高速で噴出させる構成としたことを特徴と
する灰溶融装置。2. A main for charging ash to be melted in a furnace
An inclined melting section is formed below the ash supply section.
Install an ash melting burner on the wall of the furnace facing the
A part of the ash to be melted is burnt to the burner side, such as fuel and air.
A premixed ash supply unit that mixes with the agent is provided to burn the premixed ash.
Combustion with the ash-melting burner together with fuel and air
Melted into the furnace together with the flame as molten particles
An ash melting device characterized in that the ash is ejected at high speed into ash to be discharged .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20576394A JP3365584B2 (en) | 1994-08-30 | 1994-08-30 | Ash melting method and equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20576394A JP3365584B2 (en) | 1994-08-30 | 1994-08-30 | Ash melting method and equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0868517A JPH0868517A (en) | 1996-03-12 |
| JP3365584B2 true JP3365584B2 (en) | 2003-01-14 |
Family
ID=16512269
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20576394A Expired - Fee Related JP3365584B2 (en) | 1994-08-30 | 1994-08-30 | Ash melting method and equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3365584B2 (en) |
-
1994
- 1994-08-30 JP JP20576394A patent/JP3365584B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0868517A (en) | 1996-03-12 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |