JP2002139212A - Powder melting burner - Google Patents

Powder melting burner

Info

Publication number
JP2002139212A
JP2002139212A JP2000335098A JP2000335098A JP2002139212A JP 2002139212 A JP2002139212 A JP 2002139212A JP 2000335098 A JP2000335098 A JP 2000335098A JP 2000335098 A JP2000335098 A JP 2000335098A JP 2002139212 A JP2002139212 A JP 2002139212A
Authority
JP
Japan
Prior art keywords
nozzle
gas
powder
gaseous fuel
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.)
Granted
Application number
JP2000335098A
Other languages
Japanese (ja)
Other versions
JP4550989B2 (en
Inventor
Koichiro Kanefuji
▲紘▼一郎 金藤
Shuji Hirose
秀志 広瀬
Shinichi Miyake
新一 三宅
Susumu Yamada
進 山田
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.)
Daido Steel Co Ltd
Japan Oxygen Co Ltd
Nippon Sanso Corp
Toho Gas Co Ltd
Original Assignee
Daido Steel Co Ltd
Japan Oxygen Co Ltd
Nippon Sanso Corp
Toho 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 Daido Steel Co Ltd, Japan Oxygen Co Ltd, Nippon Sanso Corp, Toho Gas Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP2000335098A priority Critical patent/JP4550989B2/en
Publication of JP2002139212A publication Critical patent/JP2002139212A/en
Application granted granted Critical
Publication of JP4550989B2 publication Critical patent/JP4550989B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To realize a flame having the shape that becomes bold from the neighbourhood of a tip end of a burner. SOLUTION: A powder melting burner 10 comprises a gas fuel nozzle 12 for injecting a gas fuel such as town gas from its center toward an outer periphery, a primary combustion assist gas nozzle 14 for injecting primary combustion assist gas employing oxygen as a chief ingredient, and a powder nozzle 16 for injecting powder together with carrying gas and a secondary combustion assist gas nozzle 18 for injecting secondary combustion assist gas employing oxygen as a chief ingredient, all being arranged in this order concentrically. A spacer 26 is concentrically disposed inside the gas fuel nozzle 12, and a nozzle hole 12a opened at a tip end of the gas fuel nozzle 12 is set to be annular. More specifically, a gas fuel is injected from the nozzle hole 12a of the gas fuel nozzle 12 annularly.

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】この発明は、細粒や微粒状ご
み焼却残渣、下水汚泥やその焼却残渣、セラミック粉体
等の粉体を火炎中で溶融するのに用いられ、酸素を支燃
ガスの主成分とする粉体溶融バーナに関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is used for melting powders such as fine and fine particulate incineration residues, sewage sludge and its incineration residues, and ceramic powder in a flame, and converts oxygen into a combustion supporting gas. The present invention relates to a powder melting burner containing as a main component.

【0002】[0002]

【従来の技術】前記粉体溶融バーナとして、例えば特開
平10−244187号公報に記載のものが存在する。
この公報に開示される粉体溶融バーナは、その中心部か
ら外周部に向かい、燃料用ノズル、酸素を主成分とする
1次支燃ガス用ノズル、粉体と搬送気体との固気混合物
用ノズルおよび酸素を主成分とする2次支燃ガス用ノズ
ルが、この順で同心円状に配置されている。
2. Description of the Related Art As the powder melting burner, there is one disclosed in, for example, JP-A-10-244187.
The powder melting burner disclosed in this publication has a fuel nozzle, a primary combustion supporting gas nozzle containing oxygen as a main component, and a solid-gas mixture of powder and a carrier gas. The nozzle and the nozzle for the secondary combustion supporting gas containing oxygen as a main component are arranged concentrically in this order.

【0003】[0003]

【発明が解決しようとする課題】前述した従来の粉体溶
融ノズルの構造では、粉体は燃料用ノズルや1次支燃ガ
ス用ノズルの外周から供給されるので、粉体の溶融を確
実かつ速やかに行なうには、バーナ先端部近くの火炎径
を太くし、粉体が火炎から外れずに接触時間を長くし得
る、直進性のある火炎を形成することが強く望まれる。
しかし、前記燃料用ノズルのノズル孔は円形の単孔であ
り、直進性のある火炎を形成し得るものの、バーナ先端
部近くから太くなる火炎は形成できなかった。
In the above-described conventional structure of the powder melting nozzle, the powder is supplied from the outer periphery of the fuel nozzle or the primary combustion supporting gas nozzle, so that the powder can be reliably melted. In order to carry out the process promptly, it is strongly desired to increase the diameter of the flame near the tip of the burner so as to form a flame having a straight traveling property that can increase the contact time without the powder coming off the flame.
However, although the nozzle hole of the fuel nozzle is a circular single hole and can form a straight flame, it cannot form a thick flame near the tip of the burner.

【0004】[0004]

【発明の目的】そこで発明者は、前記課題の解決策を求
めて種々模索したところ、前述した火炎径が太くならな
い原因は、単孔からは燃料が円柱状に噴出されるため、
その中心部の燃料と外周から供給される1次支燃ガスと
が離間しており、バーナ先端部近くでの1次支燃ガスと
燃料全体との混合が速やかに行なわれず、酸化反応によ
る膨張力が弱いためであることが確認された。すなわ
ち、燃料用バーナの先端から噴出される燃料の全体を1
次支燃ガスに近づけることで、燃料と1次支燃ガスとの
混合が速やかに行なわれ、酸化反応による膨張力を大き
くし、従ってバーナ先端部近くでの火炎径を太くし得る
ことが判った。
Accordingly, the inventor of the present invention has sought various solutions for the above-mentioned problems, and found that the reason why the flame diameter is not increased is that fuel is ejected from a single hole in a cylindrical shape.
The fuel at the center and the primary supporting gas supplied from the outer periphery are separated from each other, and the primary supporting gas and the entire fuel near the tip of the burner are not mixed promptly, and expansion due to oxidation reaction occurs. It was confirmed that the strength was weak. In other words, the entire amount of fuel ejected from the tip of the fuel burner is 1
It can be seen that, by bringing the fuel closer to the secondary combustion supporting gas, the fuel and the primary combustion supporting gas are mixed quickly, the expansion force due to the oxidation reaction is increased, and the flame diameter near the burner tip can be increased. Was.

【0005】本発明は、前述した従来の技術が内在して
いる欠点に鑑み、これを好適に解決するべく提案された
ものであって、バーナ先端部近くから太くなる形状の火
炎を実現し、粉体を確実かつ速やかに溶融できる粉体溶
融バーナを提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been proposed in view of the above-mentioned drawbacks of the prior art, and has been proposed in order to solve the problem in a favorable manner. An object of the present invention is to provide a powder melting burner that can surely and quickly melt powder.

【0006】[0006]

【課題を解決するための手段】前述した課題を解決し、
所期の目的を好適に達成するため、本発明に係る粉体溶
融バーナは、中心部から外周部に向かい、気体燃料用ノ
ズル、酸素を主成分とする1次支燃ガス用ノズル、粉体
を搬送気体と共に噴出する粉体用ノズル、酸素を主成分
とする2次支燃ガス用ノズルが、この順で同心円状に配
置されると共に、前記気体燃料用ノズルから気体燃料を
略円環状に噴出するよう構成したことを特徴とする。
[MEANS FOR SOLVING THE PROBLEMS]
In order to suitably achieve the intended purpose, the powder melting burner according to the present invention is provided with a gas fuel nozzle, a primary combustion supporting gas nozzle mainly containing oxygen, And a nozzle for a secondary combustion supporting gas containing oxygen as a main component are arranged concentrically in this order, and the gaseous fuel is supplied from the gaseous fuel nozzle in a substantially annular shape. It is characterized in that it is configured to squirt.

【0007】[0007]

【発明の実施の形態】次に、本発明に係る粉体溶融バー
ナにつき、好適な実施例を挙げて、添付図面を参照しな
がら以下説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, a powder melting burner according to the present invention will be described below with reference to the accompanying drawings by way of preferred embodiments.

【0008】[0008]

【第1実施例】図1は、第1実施例に係る粉体溶融バー
ナ10を示すものであって、その中心部から外周部に向
かい、都市ガス等の気体燃料を噴出する気体燃料用ノズ
ル12、酸素を主成分とする1次支燃ガスを噴出する1
次支燃ガス用ノズル14、粉体を搬送気体と共に噴出す
る粉体用ノズル16および酸素を主成分とする2次支燃
ガスを噴出する2次支燃ガス用ノズル18が、この順で
夫々独立した流路で同心円状に配置されている。また、
1次支燃ガス用ノズル14のノズル先端、粉体用ノズル
16のノズル先端および2次支燃ガス用ノズル18のノ
ズル先端は、同一面上に臨むよう設定されるのに対し、
気体燃料用ノズル12のノズル先端は、外側に位置する
1次支燃ガス用ノズル14のノズル先端よりも所定長さ
だけ後退するよう位置決めしてある。なお、粉体溶融バ
ーナ10の最外部には、冷却水が循環供給される冷却筒
20が設けられている。
First Embodiment FIG. 1 shows a powder melting burner 10 according to a first embodiment, and a gas fuel nozzle for ejecting a gas fuel such as a city gas from a central portion to an outer peripheral portion thereof. 12. Inject primary combustion supporting gas mainly composed of oxygen 1
The nozzle 14 for the next combustion support gas, the nozzle 16 for the powder that ejects the powder together with the carrier gas, and the nozzle 18 for the secondary combustion gas that ejects the secondary combustion gas containing oxygen as a main component are respectively in this order. They are arranged concentrically in independent flow paths. Also,
The nozzle tip of the primary support gas nozzle 14, the nozzle tip of the powder nozzle 16, and the nozzle tip of the secondary support gas nozzle 18 are set to face the same plane.
The nozzle tip of the gas fuel nozzle 12 is positioned so as to be retracted by a predetermined length from the nozzle tip of the primary combustion supporting gas nozzle 14 located outside. A cooling cylinder 20 to which cooling water is circulated and supplied is provided at the outermost part of the powder melting burner 10.

【0009】前記1次支燃ガス用ノズル14は、先端側
ノズル22と、その外周囲部に配置された基端側ノズル
24(粉体ノズルをも形成する)とで構成されており、先
端側ノズル22のガス流路と基端側ノズル24のガス流
路とは、両ノズル22,24の接合部において先端側ノ
ズル22に穿設されて略接線方向に延在する複数の支燃
ガス用旋回手段としての孔22aで連通されている(図
3参照)。すなわち1次支燃ガスは、基端側ノズル24
のガス流路から複数の孔22aを介して先端側ノズル2
2のガス流路へ流れる際に旋回流が与えられ、該1次支
燃ガスは旋回しつつノズル先端から噴出されるよう構成
してある。そして、このように1次支燃ガスを旋回する
ことで、前記気体燃料用ノズル12から噴出される気体
燃料との混合を促すと共に、粉体用ノズル16から噴出
される粉体と火炎との接触も促すようになっている。な
お、先端側ノズル22におけるノズル先端部のガス流路
は、その中心軸線方向に絞り込まれると共に、ノズル先
端で開口するノズル孔14aは円形の単孔に設定してあ
る。
The primary combustion supporting gas nozzle 14 comprises a distal nozzle 22 and a proximal nozzle 24 (which also forms a powder nozzle) disposed on the outer periphery thereof. The gas flow path of the side nozzle 22 and the gas flow path of the base side nozzle 24 are formed by a plurality of combustion supporting gases that are formed in the front end side nozzle 22 at the joint of the two nozzles 22 and 24 and extend substantially in a tangential direction. (See FIG. 3). That is, the primary combustion supporting gas is supplied to the base side nozzle 24.
From the gas flow path through the plurality of holes 22a.
A swirling flow is given when flowing to the second gas flow path, and the primary combustion supporting gas is ejected from the nozzle tip while swirling. By swirling the primary combustion supporting gas in this way, mixing with the gaseous fuel ejected from the gaseous fuel nozzle 12 is promoted, and the powder and the flame ejected from the powdery nozzle 16 are mixed. It also encourages contact. The gas flow path at the nozzle tip of the tip side nozzle 22 is narrowed in the direction of the central axis, and the nozzle hole 14a opened at the nozzle tip is set as a single circular hole.

【0010】前記粉体用ノズル16のノズル先端で開口
するノズル孔16aは、図2に示すように、前記1次支
燃ガス用ノズル14のノズル孔14aを囲む円環状に設
定されている。また粉体用ノズル16のノズル先端部に
おける粉体流路は、その中心軸線方向に絞り込まれてお
り、粉体はノズル孔16aから軸中心に向けて斜めに噴
出されるよう構成される。
The nozzle hole 16a opening at the nozzle tip of the powder nozzle 16 is formed in an annular shape surrounding the nozzle hole 14a of the primary combustion supporting gas nozzle 14, as shown in FIG. The powder flow path at the nozzle tip of the powder nozzle 16 is narrowed in the central axis direction, and the powder is obliquely ejected from the nozzle hole 16a toward the axial center.

【0011】前記2次支燃ガス用ノズル18のノズル先
端には、前記粉体用ノズル16のノズル孔16aを囲む
所要径の円周上に、図2に示す如く、周方向に所定間隔
離間して複数のノズル孔18aが開口している。各ノズ
ル孔18aに連通するガス流路は軸線方向に沿って延在
し(図1参照)、2次支燃ガスは各ノズル孔18aから軸
線方向に沿って直進するよう噴出される。
At the nozzle tip of the secondary combustion supporting gas nozzle 18, on a circumference of a required diameter surrounding the nozzle hole 16 a of the powder nozzle 16, as shown in FIG. Thus, a plurality of nozzle holes 18a are opened. The gas flow passage communicating with each nozzle hole 18a extends along the axial direction (see FIG. 1), and the secondary combustion supporting gas is ejected from each nozzle hole 18a so as to go straight along the axial direction.

【0012】前記気体燃料用ノズル12におけるノズル
先端部の内側には、図1に示す如く、断面円形のスペー
サ26が同心状に配置され、気体燃料用ノズル12のノ
ズル先端で開口するノズル孔12aは、該スペーサ26
によって円環状となるよう構成される。すなわち、気体
燃料用ノズル12のノズル孔12aからは、気体燃料が
円環状に噴出されるようになっている。なお、スペーサ
26の外周には、周方向に所定間隔で離間して複数の保
持部材28が配設され、これら保持部材28によってス
ペーサ26の外周と気体燃料用ノズル12の内周との間
が等間隔に保持されて、燃料流路を確保するよう構成さ
れる。またスペーサ26の基端(ノズル先端とは反対側)
に、図示しない調整手段に接続する調整用シャフト30
が連結され、該シャフト30を軸線方向に前後動するこ
とによって、気体燃料用ノズル12に対してスペーサ2
6を位置調整し得るよう構成してある。
As shown in FIG. 1, a spacer 26 having a circular cross section is concentrically arranged inside the nozzle tip of the gas fuel nozzle 12, and a nozzle hole 12a opening at the nozzle tip of the gas fuel nozzle 12. Is the spacer 26
It is comprised so that it may become annular. That is, the gaseous fuel is ejected from the nozzle hole 12a of the gaseous fuel nozzle 12 in an annular shape. A plurality of holding members 28 are arranged on the outer circumference of the spacer 26 at predetermined intervals in the circumferential direction, and the distance between the outer circumference of the spacer 26 and the inner circumference of the gas fuel nozzle 12 is maintained by these holding members 28. It is configured to be kept at equal intervals to secure a fuel flow path. The base end of the spacer 26 (the side opposite to the nozzle tip)
The adjusting shaft 30 connected to adjusting means (not shown)
The shaft 30 is moved back and forth in the axial direction, so that the spacer 2
6 can be adjusted in position.

【0013】[0013]

【第1実施例の作用】次に、前述した第1実施例に係る
粉体溶融バーナの作用につき説明する。前記気体燃料用
ノズル12、1次支燃ガス用ノズル14、粉体用ノズル
16および2次支燃ガス用ノズル18に、夫々対応して
気体燃料、1次支燃ガス、粉体と搬送気体および2次支
燃ガスを供給することで、各支燃ガスによって気体燃料
および粉体が燃焼される。このとき、気体燃料用ノズル
12のノズル孔12aから噴出される気体燃料は円環状
となり、気体燃料用ノズル12の外側に位置する1次支
燃ガス用ノズル14のノズル孔14aから噴出される1
次支燃ガスに対して気体燃料の全体が物理的に近接す
る。これにより、バーナ先端部近くから気体燃料と1次
支燃ガスとの混合が促進され、酸化反応による膨張力が
大きくなり、従ってバーナ先端部近くから火炎径は太く
なる。また、気体燃料は軸線に沿って直進するよう噴出
されるから、前記粉体用ノズル16のノズル孔16aか
ら噴出される粉体は、火炎から外れることなく長い時間
に亘って接触し、該粉体の溶融が確実かつ速やかに行な
われる。
Next, the operation of the powder melting burner according to the first embodiment will be described. The gas fuel nozzle 12, the primary combustion supporting nozzle 14, the powder nozzle 16 and the secondary combustion supporting nozzle 18 correspond to the gas fuel, the primary combustion supporting gas, the powder and the carrier gas, respectively. The gas fuel and the powder are burned by each supporting gas by supplying the secondary supporting gas. At this time, the gaseous fuel ejected from the nozzle hole 12a of the gaseous fuel nozzle 12 becomes annular, and is ejected from the nozzle hole 14a of the primary combustion supporting gas nozzle 14 located outside the gaseous fuel nozzle 12.
The whole gaseous fuel is physically close to the next supporting gas. As a result, the mixing of the gaseous fuel and the primary combustion supporting gas is promoted near the burner tip, the expansion force due to the oxidation reaction is increased, and the flame diameter is increased near the burner tip. Further, since the gaseous fuel is ejected so as to travel straight along the axis, the powder ejected from the nozzle hole 16a of the powder nozzle 16 comes into contact with the flame for a long time without coming off the flame, and The body melts reliably and quickly.

【0014】なお、図示例ではスペーサ26の先端と気
体燃料用ノズル12のノズル先端とは同一面上に臨むよ
う位置決めされているが、前記調整用シャフト30によ
りスペーサ26を軸線方向に前後動することで、その先
端を気体燃料用ノズル12のノズル先端に対して前方に
突出したり後退させる。これにより、気体燃料用ノズル
12のノズル孔12aから噴出させる気体燃料の状態
を、燃焼条件に応じて変化させ、最適な燃焼を行なわせ
ることができる。
In the illustrated example, the tip of the spacer 26 and the nozzle tip of the gaseous fuel nozzle 12 are positioned so as to face the same plane, but the adjusting shaft 30 moves the spacer 26 back and forth in the axial direction. This causes the tip to protrude forward or recede with respect to the nozzle tip of the gaseous fuel nozzle 12. Thereby, the state of the gaseous fuel ejected from the nozzle hole 12a of the gaseous fuel nozzle 12 can be changed in accordance with the combustion conditions, and optimal combustion can be performed.

【0015】[0015]

【第2実施例】図4は、第2実施例に係る粉体溶融バー
ナ32の要部を示すものであって、基本的な構成は第1
実施例と同一であるから、異なる部分についてのみ説明
する。なお、同一部材には同じ符号を付すものとする。
Second Embodiment FIG. 4 shows a main part of a powder melting burner 32 according to a second embodiment.
Since this embodiment is the same as the embodiment, only different parts will be described. Note that the same members are given the same reference numerals.

【0016】第2実施例の粉体溶融バーナ32では、前
記気体燃料用ノズル12の内側中心部に配置される前記
スペーサ26の外周に、気体燃料用旋回手段としての旋
回羽根34が、周方向に離間して複数螺旋状に配設され
ている。すなわち、気体燃料用ノズル12とスペーサ2
6との間の燃料流路を気体燃料が通過する際に、該燃料
に旋回羽根34により旋回流が与えられ、気体燃料用ノ
ズル12の前記円環状のノズル孔12aから気体燃料は
旋回しつつ噴出されるよう構成される。なお、気体燃料
の旋回方向は、前記1次支燃ガスの旋回方向と同一にな
るよう設定される。また旋回羽根34は、スペーサ26
の外周と気体燃料用ノズル12の内周との間を等間隔に
保持する機能を兼用している。
In the powder melting burner 32 of the second embodiment, swirl vanes 34 as swirl means for gaseous fuel are provided on the outer periphery of the spacer 26 arranged at the center of the gaseous fuel nozzle 12 in the circumferential direction. A plurality of spirals are provided at a distance from each other. That is, the gas fuel nozzle 12 and the spacer 2
When the gaseous fuel passes through the fuel flow path between the gaseous fuel nozzle 6 and the gaseous fuel nozzle 6, a swirling flow is given to the fuel by the swirling blades 34, and the gaseous fuel is swirled from the annular nozzle hole 12a of the gaseous fuel nozzle 12. It is configured to be squirted. The turning direction of the gaseous fuel is set to be the same as the turning direction of the primary supporting gas. The swirl vanes 34
And the function of maintaining the inner periphery of the gas fuel nozzle 12 at equal intervals.

【0017】すなわち、第2実施例の粉体溶融バーナ3
2においても、気体燃料用ノズル12のノズル孔12a
から噴出される気体燃料は、その外周から噴出される1
次支燃ガスに物理的に近接する円環状となるから、第1
実施例と同様にバーナ先端部近くから火炎径を太くで
き、粉体の確実かつ速やかな溶融が達成される。また第
2実施例では、気体燃料を1次支燃ガスと同一方向に旋
回させつつ噴出するので、気体燃料と1次支燃ガスとの
混合がより促進され、更に太い火炎径が得られ、粉体の
速やかな溶融を向上し得る。
That is, the powder melting burner 3 of the second embodiment
2, the nozzle hole 12a of the gas fuel nozzle 12
The gaseous fuel ejected from
Because it becomes an annular shape physically close to the next supporting gas,
As in the embodiment, the flame diameter can be increased from near the tip of the burner, and the powder can be reliably and quickly melted. In the second embodiment, since the gaseous fuel is jetted while being swirled in the same direction as the primary supporting gas, the mixing of the gaseous fuel and the primary supporting gas is further promoted, and a larger flame diameter is obtained. Immediate melting of the powder can be improved.

【0018】[0018]

【第3実施例】図5は、第3実施例に係る粉体溶融バー
ナ36の要部を示すものであって、該第3実施例では、
気体燃料用ノズル38は、先端部で開口する外側管体4
0と、該外側管体40の内側に同心状に配置されると共
に先端部が閉塞された内側管体42とから構成され、両
管体40,42によってノズル先端部に円環状のノズル
孔38aが形成されるようになっている。また内側管体
42の先端部近傍には、その略接線方向に延在する複数
の気体燃料用旋回手段としての孔42aが複数穿設さ
れ、該孔42aを介して両管体40,42が連通するよ
う構成される。すなわち、内側管体42に供給された気
体燃料には、内側管体42から複数の孔42aを介して
外側管体40へ流れる際に旋回流が与えられ、該気体燃
料は旋回しつつノズル先端から円環状に噴出されるよう
構成してある。従って、第3実施例の粉体溶融バーナ3
6においても、前述した第2実施例と同様な作用効果を
奏する。なお符号44は、孔42aの形成位置よりバー
ナ後端側において両管体40,42の間を塞ぐように配
設された逆流防止板であって、該逆流防止板44によっ
て孔42aから噴出した気体燃料の逆流を止めるよう構
成している。
Third Embodiment FIG. 5 shows a main part of a powder melting burner 36 according to a third embodiment. In the third embodiment,
The gas fuel nozzle 38 is connected to the outer tube 4 opening at the tip.
0, and an inner tube 42 concentrically disposed inside the outer tube 40 and having a closed end, and the two tubes 40, 42 form an annular nozzle hole 38a at the nozzle tip. Is formed. In the vicinity of the distal end of the inner pipe 42, a plurality of holes 42a as gaseous fuel swirl means extending in a substantially tangential direction are formed, and both pipes 40, 42 are formed through the holes 42a. It is configured to communicate. That is, the gaseous fuel supplied to the inner tube 42 is given a swirling flow when flowing from the inner tube 42 to the outer tube 40 via the plurality of holes 42a, and the gaseous fuel is swirled while the nozzle tip It is constituted so that it may be spouted in a ring from. Therefore, the powder melting burner 3 of the third embodiment
6 also has the same operation and effect as the above-described second embodiment. Reference numeral 44 denotes a backflow prevention plate disposed so as to close the space between the two pipes 40 and 42 on the rear end side of the burner from the position where the hole 42a is formed, and the backflow prevention plate 44 squirts from the hole 42a. It is configured to stop the backflow of gaseous fuel.

【0019】[0019]

【実験例】気体燃料用ノズルのノズル孔が単孔である従
来例に係る粉体溶融バーナ、第1実施例の粉体溶融バー
ナ10および第2実施例の粉体溶融バーナ32を用い、
バーナ先端部火炎径、燃焼状態、火炎直進性等を測定ま
たは観察した結果を、表1に示す。このときの各条件
は、燃焼量:175kW、燃料:都市ガス13A、支燃
ガス:空気からPAS法で酸素を分離した酸素約93%
の酸素ガス、酸素比m=1.0、とした。なお、粉体用
ノズルからは粉体を噴出させることなく空気を噴出した
状態とした。また、火炎径はバーナ先端から100mm
の位置で測定すると共に、従来例における火炎径を10
0として他を示す。
EXPERIMENTAL EXAMPLE A powder melting burner according to a conventional example in which the nozzle hole of a gas fuel nozzle is a single hole, a powder melting burner 10 of the first embodiment, and a powder melting burner 32 of the second embodiment are used.
Table 1 shows the results of measurement or observation of the burner tip flame diameter, combustion state, flame straightness, and the like. Each condition at this time is as follows: combustion amount: 175 kW, fuel: 13 A of city gas, supporting gas: about 93% of oxygen obtained by separating oxygen from air by the PAS method.
And the oxygen ratio m = 1.0. Note that the powder nozzle was in a state where air was ejected without ejecting the powder. The flame diameter is 100mm from the burner tip.
And the flame diameter in the conventional example was set to 10
Others are shown as 0.

【0020】 [0020]

【0021】表1に示す結果によれば、第1実施例およ
び第2実施例のように、気体燃料を円環状に噴出するこ
とで、バーナ先端部火炎径は従来例に比べて何れも太く
なった。なお、図6(a)は、従来例に係る粉体溶融バー
ナによる実験状態を示すものであって、バーナ先端部近
くでの火炎径は細く、かつ中心部に気体燃料の未燃部分
があることが確認された。これに対し、図6(b)は、第
1実施例に係る粉体溶融バーナによる実験状態を示すも
のであって、バーナ先端部近くでの火炎径は太く、しか
も中心部には気体燃料の未燃部分が生じていないことが
判る。
According to the results shown in Table 1, as in the first embodiment and the second embodiment, the gaseous fuel is ejected in an annular shape, so that the flame diameter at the burner tip is larger than that of the conventional example. became. FIG. 6A shows an experimental state using a powder melting burner according to a conventional example, in which the flame diameter near the burner tip is small, and there is an unburned portion of gaseous fuel in the center. It was confirmed that. On the other hand, FIG. 6B shows an experimental state using the powder melting burner according to the first embodiment, in which the flame diameter near the tip of the burner is large, and the gaseous fuel is in the center. It can be seen that there is no unburned portion.

【0022】なお、各実施例では気体燃料用ノズルのノ
ズル孔を円環状としたが、円環の一部を構成する複数の
弧状のノズル孔を周方向に所定間隔離間して開設し、こ
れらのノズル孔から噴出される気体燃料が略円環状とな
るよう構成したものであってもよい。また、気体燃料に
旋回流を与える手段としては、前述した各実施例の構成
に限定されるものでなく、気体燃料用ノズルの内周面に
螺旋状の溝を設ける等、他の手段を適宜に採用可能であ
る。更に、1次支燃ガスに旋回流を与える手段に関して
も、気体燃料に旋回流を与える手段と同様な手段を採用
し得る。
In each of the embodiments, the nozzle hole of the gas fuel nozzle is formed in an annular shape. However, a plurality of arcuate nozzle holes constituting a part of the annular shape are opened at predetermined intervals in the circumferential direction. The gas fuel ejected from the nozzle hole may be configured to be substantially annular. The means for providing the swirling flow to the gaseous fuel is not limited to the configuration of each of the above-described embodiments, and other means such as providing a spiral groove on the inner peripheral surface of the gaseous fuel nozzle may be used as appropriate. Can be adopted. Further, as for the means for giving the swirling flow to the primary combustion supporting gas, the same means as the means for giving the swirling flow to the gaseous fuel can be adopted.

【0023】[0023]

【発明の効果】以上説明した如く、本発明に係る粉体溶
融バーナでは、気体燃料用バーナから気体燃料を略円環
状に噴出するよう構成したことで、バーナ先端部近くで
の火炎径を太くすることができ、粉体の確実かつ速やか
な溶融を達成し得る。また気体燃料に1次支燃ガスと同
方向の旋回流を与えることで、両者の混合がより促進さ
れ、火炎径を更に太くして粉体の確実かつ速やかな溶融
を更に向上することができる。
As described above, in the powder melting burner according to the present invention, since the gaseous fuel is ejected from the gaseous fuel burner in a substantially annular shape, the flame diameter near the burner tip is increased. And a reliable and rapid melting of the powder can be achieved. In addition, by providing the gaseous fuel with a swirling flow in the same direction as the primary combustion supporting gas, the mixing of the two is further promoted, the flame diameter is further increased, and the reliable and prompt melting of the powder can be further improved. .

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

【図1】本発明の好適な第1実施例に係る粉体溶融バー
ナの要部断面図である。
FIG. 1 is a sectional view of a main part of a powder melting burner according to a preferred first embodiment of the present invention.

【図2】第1実施例に係る粉体溶融バーナの正面図であ
る。
FIG. 2 is a front view of the powder melting burner according to the first embodiment.

【図3】第1実施例に係る粉体溶融バーナの1次支燃ガ
ス用ノズルの断面図である。
FIG. 3 is a sectional view of a nozzle for a primary combustion supporting gas of the powder melting burner according to the first embodiment.

【図4】本発明の好適な第2実施例に係る粉体溶融バー
ナの要部断面図である。
FIG. 4 is a sectional view of a main part of a powder melting burner according to a second preferred embodiment of the present invention.

【図5】本発明の好適な第3実施例に係る粉体溶融バー
ナの要部断面図である。
FIG. 5 is a sectional view of a main part of a powder melting burner according to a third preferred embodiment of the present invention.

【図6】従来例および第1実施例に係る粉体溶融バーナ
での実験例の火炎状態を示す説明図である。
FIG. 6 is an explanatory diagram showing a flame state of an experimental example using the powder melting burner according to the conventional example and the first example.

【符号の説明】[Explanation of symbols]

12 気体燃料用ノズル 14 1次支燃ガス用ノズル 16 粉体用ノズル 18 2次支燃ガス用ノズル 22a 孔(支燃ガス用旋回手段) 34 旋回羽根(気体燃料用旋回手段) 38 気体燃料用ノズル 42a 孔(気体燃料用旋回手段) 12 Gas Fuel Nozzle 14 Primary Combustion Gas Nozzle 16 Powder Nozzle 18 Secondary Combustion Gas Nozzle 22a Holes (Combustion Gas Swirl Means) 34 Swirl Blades (Gas Fuel Swirl Means) 38 Gas Fuel Use Nozzle 42a hole (swirl means for gaseous fuel)

───────────────────────────────────────────────────── フロントページの続き (72)発明者 金藤 ▲紘▼一郎 愛知県名古屋市熱田区六野1丁目2番5号 大同特殊鋼株式会社高蔵製作所内 (72)発明者 広瀬 秀志 愛知県名古屋市熱田区六野1丁目2番5号 大同特殊鋼株式会社高蔵製作所内 (72)発明者 三宅 新一 東京都港区西新橋1丁目16番7号 日本酸 素株式会社内 (72)発明者 山田 進 愛知県名古屋市熱田区桜田町19番18号 東 邦瓦斯株式会社内 Fターム(参考) 3K061 NB03 NB08 3K065 QB10 QC03 4D004 AA36 CA29 CB02 CB34  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Kanto ▲ Hiro ▼ Ichiro 1-2-5 Rokuno, Atsuta-ku, Nagoya City, Aichi Prefecture Daido Steel Co., Ltd. Takakura Works (72) Inventor Hideshi Hirose Nagoya City, Aichi Prefecture 1-2-5, Rokuno, Atsuta-ku Daiko Specialty Steel Co., Ltd. Takakura Works (72) Inventor Shinichi Miyake 1-16-7 Nishi-Shimbashi, Minato-ku, Tokyo Nippon Oxide Corporation (72) Inventor Yamada Susumu Aichi Pref. 19-18 Sakurada-cho, Atsuta-ku, Nagoya-shi F-term in Higashi Kokugas Co., Ltd. (Reference) 3K061 NB03 NB08 3K065 QB10 QC03 4D004 AA36 CA29 CB02 CB34

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 中心部から外周部に向かい、気体燃料用
ノズル、酸素を主成分とする1次支燃ガス用ノズル、粉
体を搬送気体と共に噴出する粉体用ノズル、酸素を主成
分とする2次支燃ガス用ノズルが、この順で同心円状に
配置されると共に、前記気体燃料用ノズルから気体燃料
を略円環状に噴出するよう構成したことを特徴とする粉
体溶融バーナ。
1. A gas fuel nozzle, a primary combustion supporting gas nozzle containing oxygen as a main component, a powder nozzle for ejecting powder together with a carrier gas, and a gas containing oxygen as a main component. A powder melting burner, wherein the nozzles for the secondary combustion supporting gas are arranged concentrically in this order, and the gas fuel nozzle is configured to eject gas fuel from the gas fuel nozzle in a substantially annular shape.
【請求項2】 1次支燃ガスは、前記1次支燃ガス用ノ
ズルに設けた支燃ガス用旋回手段により旋回流が与えら
れて、中心軸線方向に絞り込まれたノズル先端から旋回
しつつ噴出され、また気体燃料は、前記気体燃料用ノズ
ルに設けた気体燃料用旋回手段により1次支燃ガスと同
方向の旋回流が与えられて、気体燃料ノズル先端から旋
回しつつ噴出されるよう構成した請求項1記載の粉体溶
融バーナ。
2. The primary combustion supporting gas is given a swirling flow by a combustion supporting gas swirling means provided on the primary combustion supporting gas nozzle, and swirls from a nozzle tip narrowed in a central axis direction. The gaseous fuel is ejected, and the gaseous fuel swirling means provided in the gaseous fuel nozzle is provided with a swirling flow in the same direction as the primary supporting gas, so that the gaseous fuel is ejected while swirling from the gaseous fuel nozzle tip. The powder melting burner according to claim 1, wherein the burner is constituted.
JP2000335098A 2000-11-01 2000-11-01 Powder melting burner Expired - Lifetime JP4550989B2 (en)

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JP4550989B2 JP4550989B2 (en) 2010-09-22

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7402275B2 (en) * 2004-11-25 2008-07-22 Daido Tokushuko Kabushiki Kaisha Powder body melting burner
JP2009014331A (en) * 2007-06-06 2009-01-22 Jfe Steel Kk Burner lance for charging powdery and granular matter of smelting reduction furnace and manufacturing method of molten metal by smelting reduction
US20100019063A1 (en) * 2006-12-22 2010-01-28 Schroeder Ernst Rotary furnace burner
CN101839479A (en) * 2010-06-28 2010-09-22 天津水泥工业设计研究院有限公司 Powdered coal burner head with high efficiency and low wear
JP2012207817A (en) * 2011-03-29 2012-10-25 Taiyo Nippon Sanso Corp Combustion burner
WO2014148536A1 (en) * 2013-03-21 2014-09-25 大陽日酸株式会社 Combustion burner

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0371236U (en) * 1989-11-16 1991-07-18

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4038876B2 (en) * 1998-05-20 2008-01-30 大同特殊鋼株式会社 Powder melting burner

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0371236U (en) * 1989-11-16 1991-07-18

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7402275B2 (en) * 2004-11-25 2008-07-22 Daido Tokushuko Kabushiki Kaisha Powder body melting burner
US20100019063A1 (en) * 2006-12-22 2010-01-28 Schroeder Ernst Rotary furnace burner
US8393893B2 (en) * 2006-12-22 2013-03-12 Khd Humboldt Wedag Gmbh Rotary furnace burner
DE102006060867B4 (en) * 2006-12-22 2020-07-02 Khd Humboldt Wedag Gmbh Rotary kiln burners
JP2009014331A (en) * 2007-06-06 2009-01-22 Jfe Steel Kk Burner lance for charging powdery and granular matter of smelting reduction furnace and manufacturing method of molten metal by smelting reduction
CN101839479A (en) * 2010-06-28 2010-09-22 天津水泥工业设计研究院有限公司 Powdered coal burner head with high efficiency and low wear
CN101839479B (en) * 2010-06-28 2015-02-25 天津水泥工业设计研究院有限公司 Powdered coal burner head with high efficiency and low wear
JP2012207817A (en) * 2011-03-29 2012-10-25 Taiyo Nippon Sanso Corp Combustion burner
WO2014148536A1 (en) * 2013-03-21 2014-09-25 大陽日酸株式会社 Combustion burner
JP6031591B2 (en) * 2013-03-21 2016-11-24 大陽日酸株式会社 Burning burner
US9586219B2 (en) 2013-03-21 2017-03-07 Taiyo Nippon Sanso Corporation Combustion burner

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