JPH11325444A - Burner type swirling melting furnace - Google Patents

Burner type swirling melting furnace

Info

Publication number
JPH11325444A
JPH11325444A JP12835498A JP12835498A JPH11325444A JP H11325444 A JPH11325444 A JP H11325444A JP 12835498 A JP12835498 A JP 12835498A JP 12835498 A JP12835498 A JP 12835498A JP H11325444 A JPH11325444 A JP H11325444A
Authority
JP
Japan
Prior art keywords
burner
melting furnace
furnace
swirling
fuel
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.)
Withdrawn
Application number
JP12835498A
Other languages
Japanese (ja)
Inventor
Masao Taguma
昌夫 田熊
Hiroki Honda
裕姫 本多
Izuru Ishikawa
出 石川
Akihisa Goda
聡央 郷田
Sueo Yoshida
季男 吉田
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP12835498A priority Critical patent/JPH11325444A/en
Publication of JPH11325444A publication Critical patent/JPH11325444A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To strengthen a swirling flame with a simplified structure. SOLUTION: A burner type swirling melting furnace 1 includes a cylindrical heat resistant wall with a burner 5 provided on the wall. The burner 5 is fixed at an angle where an infection direction of the burner 5 makes contact with a tangential line of a virtual circle 7 having a predetermined radius in a furnace 6. The burner 5 has a triple structure, in which it includes a core tube provided most thereinside for injecting incineration ash together with air, an inner tube provided around the periphery of the former for injecting a fuel, and an outer tube provided on the periphery of the former core tube for supplying air into the furnace 6. The melting furnace 1 uses the integral burner 5 to effectually form a swirling flame.

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、各種廃棄物の焼却
灰、例えば下水汚泥等の焼却灰を溶融してスラグ化する
バーナ式旋回溶融炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a burner-type rotary melting furnace for melting incinerated ash of various kinds of waste, for example, incinerated ash such as sewage sludge to form slag.

【0002】[0002]

【従来の技術】下水処理焼却灰を溶融処理し、これを資
源化し、リサイクルするニーズが高まっており、特に既
設焼却炉から生じる焼却灰の溶融炉の建設ニーズが増加
している。このような背景のもと、下水汚泥焼却設備で
は一般に発電設備を付設していないので、電力を使用す
るプラズマ溶融炉よりも、燃料を使用するバーナ式溶融
炉のニーズが高い。図5及び図6は、従来のバーナ式旋
回溶融炉における、バーナの取付状態を示す水平方向断
面図である。図5に示すように、断面が円形の溶融炉3
1は、壁部32に一対のバーナ33,34を設けてい
る。バーナ33は、重油等の燃料と燃焼用空気を炉内3
7に噴射できる構造であり、他方のバーナ34は、焼却
灰の粉体及び燃焼用の空気を噴射できる構造になってい
る。また、図6に示す溶融炉31は、壁部32に4個の
バーナ35,36を配設し、一対のバーナ35は、焼却
灰、空気、燃料を炉内37に噴射できる構造であり、他
の一対のバーナ36は、焼却灰を噴射できる構造になっ
ている。
2. Description of the Related Art There is an increasing need to melt sewage incineration ash, to recycle it, and to recycle it. In particular, there is an increasing need to construct a melting furnace for incineration ash generated from existing incinerators. Against this background, sewage sludge incineration facilities generally do not have a power generation facility, so there is a greater need for burner-type melting furnaces that use fuel than plasma melting furnaces that use electric power. FIGS. 5 and 6 are horizontal cross-sectional views showing a mounted state of a burner in a conventional burner type rotary melting furnace. As shown in FIG. 5, the melting furnace 3 having a circular cross section
In 1, a pair of burners 33 and 34 are provided on a wall 32. The burner 33 converts fuel such as heavy oil and combustion air into the furnace 3.
7, and the other burner 34 has a structure capable of injecting incinerated ash powder and combustion air. In addition, the melting furnace 31 shown in FIG. 6 has four burners 35 and 36 disposed on the wall 32, and the pair of burners 35 has a structure capable of injecting incineration ash, air, and fuel into the furnace 37. The other pair of burners 36 has a structure that can inject incineration ash.

【0003】上記の溶融炉31では、炉内37にある一
定の径を有する仮想円38を設定し、両図において、バ
ーナの火炉内噴出方向軸線39が、その仮想円38に接
するように、各バーナ33〜36が配置されている。こ
のような構成により、バーナー33〜36から炉内37
へ噴射される燃料と燃焼用空気は、軸線39に沿って炉
内37に噴射されて安定した旋回燃焼火炎を形成し、焼
却灰を燃焼・溶融する。
In the melting furnace 31 described above, an imaginary circle 38 having a certain diameter is set in the furnace 37, and in both figures, an axis 39 of the burner in the furnace is directed in such a manner as to contact the imaginary circle 38. Each burner 33-36 is arranged. With such a configuration, the inside of the furnace 37 is connected to the burners 33 to 36.
The fuel and the combustion air injected into the furnace 37 are injected into the furnace 37 along the axis 39 to form a stable swirling combustion flame and burn and melt the incineration ash.

【0004】[0004]

【発明が解決しようとする課題】このように、従来のバ
ーナ式旋回溶融炉では、焼却灰、燃料、空気をそれぞれ
異なるバーナによって、炉内に噴射することが多かっ
た。また、複数本のバーナを用いた方が、スムーズな旋
回火炎を得ることができるという見解があった。しか
し、バーナを複数本使用すると旋回はスムーズに形成さ
れるものの、バーナ1本当たりの燃料等の流量が減り、
旋回力は必ずしも最良の状態ではない。更に、焼却灰、
燃料、空気を供給する設備が複数箇所となるため、溶融
炉構造が大型、複雑化し、建設コストが高価になってい
た。本発明は上記課題に鑑みてなされたもので、簡単な
構造で旋回火炎を強くすることができるバーナ式旋回溶
融炉を提供することを目的とする。
As described above, in the conventional burner-type swirling melting furnace, incineration ash, fuel, and air are often injected into the furnace by different burners. In addition, there was a view that the use of a plurality of burners can provide a smooth turning flame. However, when multiple burners are used, the swirl is formed smoothly, but the flow rate of fuel and the like per burner decreases,
The turning force is not always in the best condition. Furthermore, incineration ash,
Since there are a plurality of facilities for supplying fuel and air, the structure of the melting furnace is large and complicated, and the construction cost is high. The present invention has been made in view of the above problems, and an object of the present invention is to provide a burner-type swirling melting furnace that can strengthen a swirling flame with a simple structure.

【0005】[0005]

【課題を解決するための手段】本発明は、上記目的を達
成するために、円筒体の炉本体に対してその内周面に沿
う方向にバーナを設けてなるバーナ式旋回溶融炉におい
て、上記バーナを焼却灰と燃料と燃焼空気を同時に供給
可能な一体型バーナとし、同一体型バーナを上記炉本体
の一箇所に設けたものである。本明細書において、焼却
灰は、下水汚泥焼却灰に限らず、各種の焼却灰を意味
し、単に灰と称することもある。また、上記バーナは、
中心部から灰及び搬送空気を供給し、その外周から燃
料、更にその外周から燃焼空気を供給可能な三重構造と
することが好ましい。
In order to achieve the above object, the present invention provides a burner-type swirling melting furnace comprising a cylindrical furnace body provided with a burner in a direction along an inner peripheral surface thereof. The burner is an integrated burner capable of simultaneously supplying incineration ash, fuel and combustion air, and a single-body burner is provided at one location of the furnace body. In this specification, incineration ash is not limited to sewage sludge incineration ash, but means various types of incineration ash, and may be simply referred to as ash. The burner is
It is preferable to have a triple structure in which ash and carrier air are supplied from the center, fuel is supplied from the outer periphery, and combustion air is further supplied from the outer periphery.

【0006】[0006]

【発明の実施の形態】以下、本発明の実施の形態による
バーナ式旋回溶融炉について、図面を参照しながら説明
する。図1は、バーナ式旋回溶融炉1とこれに付帯する
二次燃焼室2及びスラグ抜き室3を示す。溶融炉1は円
筒状の耐熱性壁部4を備え、壁部には実質的に1個のバ
ーナ5を設けている。図2に示すようにバーナ5は、炉
内6における所定径を有する仮想円7に対しその接線方
向に、バーナ5の噴射方向が、向くように固定されてい
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a burner-type swirling melting furnace according to an embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows a burner-type swirling melting furnace 1 and a secondary combustion chamber 2 and a slag removal chamber 3 attached thereto. The melting furnace 1 has a cylindrical heat-resistant wall portion 4, and the wall portion is provided with substantially one burner 5. As shown in FIG. 2, the burner 5 is fixed such that the injection direction of the burner 5 is directed tangentially to a virtual circle 7 having a predetermined diameter in the furnace 6.

【0007】図3は、バーナ5の拡大図である。バーナ
5は三重構造であり、径方向の最も内側に空気と焼却灰
を炉内6に噴射する芯管8を設け、その外周に燃料を噴
射する内管9を設け、更に内管9の外周に空気を炉内6
に供給する外管10を設けている。こうしてバーナ5
は、焼却灰の粉体、燃焼用の燃料及び燃焼用の空気を一
体的に噴射することができる。バーナ5には旋回スワラ
11が設けられている。旋回スワラ11の構造は、流体
の流れ方向にある角度をもった多数枚の案内羽根からな
り、バーナ外管が10が壁部4に対して固定され、燃料
及び空気は、旋回スワラ11により、旋回がかけられる
ようになっている。バーナ式旋回溶融炉の他の付帯設備
については、慣用技術が用いられるため、その詳細な構
成は省略する。
FIG. 3 is an enlarged view of the burner 5. The burner 5 has a triple structure. A core pipe 8 for injecting air and incineration ash into the furnace 6 is provided at the innermost side in the radial direction, and an inner pipe 9 for injecting fuel is provided on the outer periphery thereof. Into the furnace 6
Is provided with an outer tube 10 for supplying to the outer tube. Thus burner 5
Can integrally inject incinerated ash powder, combustion fuel and combustion air. The burner 5 is provided with a swirl swirler 11. The structure of the swirling swirler 11 is composed of a number of guide vanes at an angle in the direction of flow of the fluid, the burner outer tube 10 is fixed to the wall 4, and the fuel and air are separated by the swirling swirler 11. A turn can be applied. As for the other auxiliary equipment of the burner-type swirling melting furnace, since a conventional technique is used, a detailed configuration thereof is omitted.

【0008】次に、バーナ式旋回溶融炉の作用について
説明する。溶融炉1が稼働すると、バーナ5の芯管8、
内管9、外管10からそれぞれ焼却灰、燃料、空気が吹
き出される。バーナ5は、一体型バーナであり、初期に
おける旋回火炎の発生は多少遅いが、バーナ5からの噴
出流速が大きいことから、その後より強い旋回がかか
り、安定した旋回燃焼火炎が形成され、焼却灰のスラグ
回収率が向上する。すなわち、芯管から噴射される焼却
灰は、内管9から噴射される燃料に包み込まれるように
噴射され、当該燃料は、その内側にある芯管8からの空
気と、その外側にある外管10からの燃焼用空気により
効率良く燃焼するとともに、昇温し溶融に至る。旋回ス
ワラ11は、芯管8の外側、内管9の外側、及び外管1
0の内側に固定されており、それ自身が回転することは
ないが、内管9内を流れる燃料と外管10内を流れる空
気とに、効率的に旋回をかけることができるしたがっ
て、焼却灰は、約1300〜1600℃の高温、常圧下
で加熱されることにより溶融してスラグ化し、溶融炉1
の下方にあるスラグ抜き室3に流下し、次工程で廃棄又
は再処理される。他方、炉内6で燃焼したガスは、上昇
して二次燃焼室2に導入され、後流側の工程で処理され
たのち排出される。
Next, the operation of the burner type rotary melting furnace will be described. When the melting furnace 1 operates, the core tube 8 of the burner 5,
Incineration ash, fuel and air are blown out from the inner pipe 9 and the outer pipe 10, respectively. The burner 5 is an integrated burner, and the generation of a swirling flame in the initial stage is somewhat slow. However, since the jet flow velocity from the burner 5 is large, a stronger swirl is applied thereafter, and a stable swirling combustion flame is formed. Slag recovery rate is improved. That is, the incineration ash injected from the core pipe is injected so as to be wrapped in the fuel injected from the inner pipe 9, and the fuel is supplied from the air from the core pipe 8 inside the outer pipe and the outer pipe from the outer pipe. Combustion is efficiently carried out by the combustion air from 10 and the temperature is raised to melting. The swirling swirler 11 is provided outside the core tube 8, outside the inner tube 9, and the outer tube 1.
0, and does not rotate by itself, but can efficiently swirl the fuel flowing in the inner pipe 9 and the air flowing in the outer pipe 10, and Is melted into slag by being heated at a high temperature of about 1300 to 1600 ° C. under normal pressure, so that the melting furnace 1
Flows down to the slag removal chamber 3 below, and is discarded or reprocessed in the next step. On the other hand, the gas burned in the furnace 6 rises and is introduced into the secondary combustion chamber 2, and is discharged after being processed in a downstream process.

【0009】図4は、本実施の形態(実施例)における
一体型バーナ式旋回溶融炉と、従来(比較例)の複数本
のバーナを用いた溶融炉の溶融試験結果を示す。同一条
件下の旋回溶融炉を用いて下水汚泥焼却灰を溶融し、燃
焼空気の吹き込みを変化させた試験を行い、旋回力とス
ラグ回収率を検討した。その結果、溶融炉にバーナを1
本用いて吹き込んだものが、2本用いたものよりスラグ
回収率及びスワール数ともに優れていることが分かっ
た。これらのうちスラグ回収率は、炉内に投入した焼却
灰のうち何%回収されているかを表し、比較例が71%
であったのに対し、本実施例では75%であった。ま
た、実効スワール数は、比較例が6.6であったのに対
し、本実施例では8.3であった。ここで、実効スワー
ル数とは、燃焼ガスの火炉内のある断面における旋回の
強さを示す指数であり、本指数の数値が大きい程、燃焼
ガスの旋回力が大きい、すなわち旋回燃焼火炎渦が安定
して形成されることを意味している。
FIG. 4 shows the results of a melting test of an integrated burner type rotary melting furnace according to the present embodiment (Example) and a melting furnace using a plurality of burners of a conventional (comparative example). The sewage sludge incineration ash was melted using a swirling melting furnace under the same conditions, and a test was performed by changing the blowing of combustion air, and the swirling force and slag recovery rate were examined. As a result, one burner was added to the melting furnace.
It was found that the one blown by using this method was superior in both the slag recovery rate and the number of swirls to that blown by two. Of these, the slag recovery rate indicates what percentage of the incinerated ash charged into the furnace was recovered, and the comparative example was 71%.
On the other hand, it was 75% in this example. The effective swirl number was 6.6 in the comparative example, whereas it was 8.3 in the present example. Here, the effective swirl number is an index indicating the swirling strength of a combustion gas in a certain cross section in the furnace, and the larger the index value is, the larger the swirling force of the combustion gas is, that is, the swirling combustion flame vortex is It means that it is formed stably.

【0010】以上説明したように、本実施の形態によれ
ば、スラグ回収率と旋回燃焼火炎渦が安定して形成され
るようになったので、焼却灰の燃焼効率を向上すること
ができる。また、バーナを一体型(1本)にすること
で、バーナ自体のコストはアップするものの、燃料配管
や空気の配管設備が減ることから溶融炉構造が簡素化
し、炉全体を小型化するとともにコストを下げることが
できる。以上、本発明の実施の形態について説明した
が、勿論、本発明はこれに限定されることなく本発明の
技術的思想に基いて種々の変形が可能である。例えば、
上記実施の形態では、バーナを3重構造にしたが、2重
構造あるいは、4重構造以上であってもよい。また、芯
管8、内管9、外管10から噴射する媒体の種類につい
ても、任意に変更が可能である。
As described above, according to the present embodiment, the slag recovery rate and the swirling combustion flame vortex are formed stably, so that the combustion efficiency of incinerated ash can be improved. Although the cost of the burner itself is increased by integrating the burner (single), the melting furnace structure is simplified because the fuel piping and air piping facilities are reduced, and the size of the entire furnace is reduced and the cost is reduced. Can be lowered. The embodiments of the present invention have been described above. However, the present invention is not limited to the embodiments, and various modifications can be made based on the technical idea of the present invention. For example,
In the above embodiment, the burner has a triple structure, but may have a double structure or a quadruple structure or more. Further, the types of the media ejected from the core tube 8, the inner tube 9, and the outer tube 10 can be arbitrarily changed.

【0011】[0011]

【発明の効果】以上述べたように、円筒体の炉本体に対
してその内周面の接線方向にバーナを設けてなるバーナ
式旋回溶融炉において、前記バーナを灰と燃料と燃焼空
気を同時に供給可能な一体型バーナとし、同一体型バー
ナを前記炉本体の一箇所に設けたので、スラグの回収率
を向上するとともに、溶融炉を小型するとともにコスト
の低減を図ることができる。
As described above, in a burner-type swirling melting furnace in which a burner is provided in a tangential direction of the inner peripheral surface of a cylindrical furnace body, the burner is used to simultaneously convert ash, fuel and combustion air. Since an integrated burner that can be supplied is provided and a single-body burner is provided at one place of the furnace main body, the recovery rate of slag can be improved, and the melting furnace can be reduced in size and cost can be reduced.

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

【図1】本発明の実施の形態によるバーナ式旋回溶融炉
の溶融炉とそれに付帯する設備の概略断面図である。
FIG. 1 is a schematic sectional view of a melting furnace of a burner type rotary melting furnace according to an embodiment of the present invention and equipment attached thereto.

【図2】図1におけるX−X線方向の断面図である。FIG. 2 is a cross-sectional view taken along line XX in FIG.

【図3】本発明の実施の形態によるバーナ式旋回溶融炉
のバーナの拡大図である。
FIG. 3 is an enlarged view of a burner of the burner type rotary melting furnace according to the embodiment of the present invention.

【図4】本実施の形態における一体型バーナ式旋回溶融
炉と従来(比較例)の複数のバーナを用いた溶融炉の溶
融試験結果を示す図である。
FIG. 4 is a diagram showing the results of a melting test of an integrated burner type rotary melting furnace according to the present embodiment and a melting furnace using a plurality of conventional burners (comparative example).

【図5】2本のバーナを取付けた従来のバーナ式旋回溶
融炉の概略水平方向断面図である。
FIG. 5 is a schematic horizontal sectional view of a conventional burner-type swirling melting furnace equipped with two burners.

【図6】4本のバーナを取付けた従来のバーナ式旋回溶
融炉の概略水平方向断面図である。
FIG. 6 is a schematic horizontal sectional view of a conventional burner-type swirling melting furnace to which four burners are attached.

【符号の説明】[Explanation of symbols]

1 溶融炉 2 二次燃焼室 3 スラグ抜き室 4 耐熱性壁部 5 バーナ 6 炉内 7 仮想円 8 芯管 9 内管 10 外管 11 旋回スワラ DESCRIPTION OF SYMBOLS 1 Melting furnace 2 Secondary combustion chamber 3 Slag removal chamber 4 Heat resistant wall 5 Burner 6 Furnace 7 Virtual circle 8 Core tube 9 Inner tube 10 Outer tube 11 Rotating swirler

フロントページの続き (72)発明者 郷田 聡央 神奈川県横浜市中区錦町12番地 三菱重工 業株式会社横浜製作所内 (72)発明者 吉田 季男 神奈川県横浜市中区錦町12番地 三菱重工 業株式会社横浜製作所内Continued on the front page (72) Inventor Toshio Goda 12 Nishiki-cho, Naka-ku, Yokohama-shi, Kanagawa Prefecture Mitsubishi Heavy Industries, Ltd. Inside Yokohama Works

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 円筒体の炉本体に対してその内周面に沿
う方向にバーナを設けてなるバーナ式旋回溶融炉におい
て、上記バーナを灰と燃料と燃焼空気を同時に供給可能
な一体型バーナとし、該一体型バーナを上記炉本体の一
箇所に設けたことを特徴とするバーナ式旋回溶融炉。
1. A burner-type swirling melting furnace comprising a cylindrical furnace body provided with a burner in a direction along an inner peripheral surface thereof, wherein said burner is an integrated burner capable of simultaneously supplying ash, fuel and combustion air. Wherein the integrated burner is provided at one location of the furnace main body.
【請求項2】 上記バーナを三重構造とし、中心部から
灰及び搬送空気を供給し、その外周から燃料、更にその
外周から燃焼空気を供給可能としたことを特徴とする請
求項1記載のバーナ式旋回溶融炉。
2. The burner according to claim 1, wherein said burner has a triple structure, wherein ash and carrier air are supplied from a central portion, fuel is supplied from an outer periphery thereof, and combustion air is further supplied from an outer periphery thereof. Swivel melting furnace.
JP12835498A 1998-05-12 1998-05-12 Burner type swirling melting furnace Withdrawn JPH11325444A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12835498A JPH11325444A (en) 1998-05-12 1998-05-12 Burner type swirling melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12835498A JPH11325444A (en) 1998-05-12 1998-05-12 Burner type swirling melting furnace

Publications (1)

Publication Number Publication Date
JPH11325444A true JPH11325444A (en) 1999-11-26

Family

ID=14982755

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12835498A Withdrawn JPH11325444A (en) 1998-05-12 1998-05-12 Burner type swirling melting furnace

Country Status (1)

Country Link
JP (1) JPH11325444A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2018021248A1 (en) * 2016-07-26 2018-08-02 Jfeスチール株式会社 Auxiliary burner for electric furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2018021248A1 (en) * 2016-07-26 2018-08-02 Jfeスチール株式会社 Auxiliary burner for electric furnace

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