JPH042846B2 - - Google Patents
Info
- Publication number
- JPH042846B2 JPH042846B2 JP58245405A JP24540583A JPH042846B2 JP H042846 B2 JPH042846 B2 JP H042846B2 JP 58245405 A JP58245405 A JP 58245405A JP 24540583 A JP24540583 A JP 24540583A JP H042846 B2 JPH042846 B2 JP H042846B2
- Authority
- JP
- Japan
- Prior art keywords
- flame
- burner
- fuel
- auxiliary combustion
- coke
- 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 - Lifetime
Links
Description
【発明の詳細な説明】
この発明は微細コークス等の難燃性燃料を燃焼
させるに好適なバーナ装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a burner device suitable for burning flame-retardant fuel such as fine coke.
最近の燃料事情の変化に伴ない、大型ボイラに
おいても、その燃料を石油(例えば重油)から石
油ボイラの構造のまゝ安価な燃料である石油コー
クスへ転換して発電コストを下げることが考えら
れた。しかしこのような石油コークスの燃焼は着
火性、火炎の保持の点からしてその実現はきわめ
て困難であつた。発明者等はこれを実現すべく、
種々実験を重ね、石油コークス燃焼に適するバー
ナを開発することができた。その構造については
実願昭58−162051号でさきに出願した。この場合
石油コークスは、あらかじめ所定の粒径の微粒に
粉砕され、バーナに気流輸送される。また石油コ
ークスの性状は、燃料比(固定炭素/揮発分)が
7〜9.5と高く着火や保炎ができない為、重油火
炎等の着火保炎性のよい火炎を微粉コークスバー
ナの中央に形成させながら、微粉コークスを完全
燃焼させる方式を採用した。 With recent changes in the fuel situation, it has become possible to reduce power generation costs by converting the fuel used in large boilers from petroleum (for example, heavy oil) to petroleum coke, which is an inexpensive fuel that retains the structure of petroleum boilers. Ta. However, such combustion of petroleum coke has been extremely difficult to achieve in terms of ignitability and flame retention. In order to realize this, the inventors and others
After conducting various experiments, we were able to develop a burner suitable for burning petroleum coke. The structure was previously filed in Utility Application No. 162051/1983. In this case, the petroleum coke is pulverized in advance into fine particles of a predetermined particle size and transported by pneumatic flow to the burner. In addition, petroleum coke has a high fuel ratio (fixed carbon/volatile content) of 7 to 9.5, making it difficult to ignite and hold the flame. Therefore, a flame with good ignition and flame holding properties, such as a heavy oil flame, is formed in the center of the pulverulent coke burner. However, we adopted a method that completely burns fine coke.
第1図は発明者等の実験に際して使用したバー
ナの一例で微粉コークスを燃焼させるバーナを示
す。先ずバーナの起動に当つては点火トーチ5に
よつて重油バーナ4から噴射する重油に着火させ
燃焼させる。一方図示しない微粉機により粉砕さ
れた石油コークスは気流輸送されて、エルボ9、
微粉コークスバーナ2を経て炉中7に噴射され、
重油火炎14と接触することにより着火し、微粉
石油コークス火炎15を形成する。なお図中符号
3はインペラ、13は二次空気、12は三次空気
である。 FIG. 1 shows an example of a burner used in experiments by the inventors, which burns fine coke. First, when starting the burner, the ignition torch 5 ignites the heavy oil injected from the heavy oil burner 4 and causes it to burn. On the other hand, petroleum coke pulverized by a pulverizer (not shown) is transported by air flow to the elbow 9,
The fine coke is injected into the furnace 7 through the burner 2,
When it comes into contact with the heavy oil flame 14, it ignites and forms a pulverized petroleum coke flame 15. In the figure, reference numeral 3 represents an impeller, 13 represents secondary air, and 12 represents tertiary air.
第2図及び第3図は重油火炎14と微粉石油コ
ークス火炎15の形成状態を示す図であり、助燃
料たる重油火炎14を中心としてこれを包囲する
ように微粉石油コークス火炎15が形成される。
この形式のバーナにおいては微粉コークスは主と
して重油火炎14の輻射によつて着火、燃焼する
ことになるが、重油火炎14は微粉コークス火炎
15によつて酸素を消費し、O2分圧の低い空気
によつて燃焼を行なうことになる。このため重油
火炎温度が相対的に低く、コークスの燃焼時間が
長くなつたり、未燃分の発生量が増加する等の事
態が生じる。 FIGS. 2 and 3 are diagrams showing how the heavy oil flame 14 and the pulverized petroleum coke flame 15 are formed, and the pulverized petroleum coke flame 15 is formed to surround the heavy oil flame 14, which is the auxiliary fuel. .
In this type of burner, the fine coke is ignited and burned mainly by the radiation of the heavy oil flame 14, but the heavy oil flame 14 consumes oxygen by the fine coke flame 15, and the air with a low O 2 partial pressure Combustion will be carried out by As a result, the heavy oil flame temperature is relatively low, resulting in situations such as a longer coke combustion time and an increased amount of unburned matter.
この発明の目的は上述した問題点を除去し、燃
焼効率が高く未燃分の発生量を低減し得るバーナ
装置を提供することにある。 An object of the present invention is to provide a burner device that eliminates the above-mentioned problems and has high combustion efficiency and can reduce the amount of unburned matter generated.
要するにこの発明は、難燃性微粉燃料の噴出流
れを旋回流れにする手段をもち、複数のノズルを
偏り位置させて助燃ノズル組を形成し、難燃性微
粉燃料の噴霧流れを分断するように複数の該助燃
ノズル組を相互に離隔配置したことを特徴とする
難燃性燃料用バーナ装置である。 In short, the present invention has a means for turning the ejected flow of the flame-retardant pulverized fuel into a swirling flow, and forms a auxiliary combustion nozzle set by arranging a plurality of nozzles at biased positions, so as to divide the sprayed flow of the flame-retardant pulverized fuel. This burner device for flame-retardant fuel is characterized in that a plurality of auxiliary combustion nozzle sets are arranged at a distance from each other.
以下この発明の実施例を図面により説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第4図ないし第6図はこの発明の第1の実施例
を示す。図中微粉コークスバーナ2の内部には中
心軸線をほぼ同一とするように助燃料たる重油を
噴射する重油バーナ4が配置してある。この重油
バーナ4の先端部には、各々3個のバーナノズル
20が二組に分かれて配置してある。これにより
重油バーナ4から噴射する重油は二組に分かれて
噴射され、重油火炎14a,14bを形成する。
一方微粉石油コークスは微粉コークスバーナ2の
出口においてスワラ21によつて旋回力が与えら
れ炉内に噴射し微粉コークス火炎15を形成す
る。微粉コークス自体は旋回力が与えられている
ため、第6図の如く分割された火炎14a,14
bの間に回り込み、これらの火炎と十分に接触す
る。このため微粉コークスは短時間で着火しかつ
燃焼するため燃焼性は向上し、未燃分の発生率は
低下する。つまり分割火炎とすることにより重油
火炎と微粉コークスとの接触の機会が増加し、か
つ火炎表面積が増加し、重油火炎と直接接触しな
い微粉コークスも強い輻射熱によりきわめて短時
間で着火、燃焼する。 4 to 6 show a first embodiment of the invention. In the figure, inside the pulverulent coke burner 2, a heavy oil burner 4 for injecting heavy oil as auxiliary fuel is arranged so that the central axes thereof are substantially the same. At the tip of the heavy oil burner 4, three burner nozzles 20 are arranged in two groups. As a result, the heavy oil injected from the heavy oil burner 4 is divided into two groups and injected, forming heavy oil flames 14a and 14b.
On the other hand, the pulverized petroleum coke is given a swirling force by the swirler 21 at the outlet of the pulverized coke burner 2, and is injected into the furnace to form a pulverized coke flame 15. Since the fine coke itself is given a swirling force, the divided flames 14a, 14 as shown in FIG.
b, and makes full contact with these flames. For this reason, fine coke ignites and burns in a short time, improving combustibility and reducing the rate of unburned matter. In other words, by creating a split flame, the chances of contact between the heavy oil flame and the fine coke increase, and the flame surface area increases, and even the fine coke that does not come into direct contact with the heavy oil flame can be ignited and burned in an extremely short time due to strong radiant heat.
第7図及び第8図は別の実施例を示す。 7 and 8 show another embodiment.
符号22は助燃用燃料として気体燃料(LNG、
LPG等)を噴射するガスバーナであり、第8図
の如く微粉コークスバーナ2の外周部に対して3
本づつ二組に分けて対向配置しておく。各ガスバ
ーナに対しては例えば2個づつノズル用管理材軸
心より半径方向にガスを噴出するノズルを形成し
ておき、各ガスバーナ火炎23が全体として同一
方向に旋回するようノズルの形成位置を定めてお
く。これにより微粉コークスバーナ2から噴射し
た微粉コークスはガスバーナ火炎23と良好に混
合し短時間で着火燃焼する。なおこの場合、微粉
コークスエバーナ2内にスワラを配置し、微粉コ
ークス自体に対しても旋回力を与えるよう構成し
てもよい。またこのバーナ22の燃料を第1の実
施例の如く重油等の液体燃料に変更してもよい
し、反対に第4図のバーナを気体燃料用バーナと
して利用してもよい。 Reference numeral 22 indicates gaseous fuel (LNG,
This is a gas burner that injects LPG, etc.), and as shown in Figure 8, it is a gas burner that injects
Divide the books into two groups and place them facing each other. For each gas burner, for example, two nozzles that eject gas in the radial direction from the axis of the nozzle management material are formed, and the nozzle formation positions are determined so that the flame 23 of each gas burner as a whole turns in the same direction. I'll keep it. As a result, the fine coke injected from the fine coke burner 2 mixes well with the gas burner flame 23 and ignites and burns in a short time. In this case, a swirler may be arranged in the fine coke burner 2 to apply swirling force to the fine coke itself. Further, the fuel of this burner 22 may be changed to liquid fuel such as heavy oil as in the first embodiment, or conversely, the burner shown in FIG. 4 may be used as a gaseous fuel burner.
この発明を実施することにより助燃用燃料によ
る火炎を複数に分割するため石油コークス等の難
燃性燃料と助燃用燃料火炎とが十分に接触し、難
燃性燃料は短時間で着火燃焼し、未燃分の発生量
が大幅に低下すると共に、バーナの制御性を向上
させることができる。 By carrying out this invention, the flame caused by the auxiliary fuel is divided into a plurality of parts, so that the flame retardant fuel such as petroleum coke and the auxiliary fuel flame come into sufficient contact, and the flame resistant fuel ignites and burns in a short time. The amount of unburned matter generated can be significantly reduced, and the controllability of the burner can be improved.
第1図は発明者等の実験に使用したバーナの一
例で微粉コークスバーナの断面図、第2図は第1
図のバーナの燃焼状態を示す模式図、第3図は第
2図の−線による断面図、第4図はこの発明
の一実施例に係るバーナ装置の燃料噴射部断面
図、第5図は第4図の−線による重油バーナ
正面図、第6図は第4図の−線による断面
図、第7図は第2の実施例を示すバーナ装置の燃
料噴射部断面図、第8図は第7図の−線によ
る断面図である。
2……微粉コークスバーナ、4……重油バー
ナ、14a,14b,23……助燃用燃料分割火
炎、20……重油バーナノズル、22……ガスバ
ーナ。
Figure 1 is a cross-sectional view of a fine coke burner, which is an example of a burner used in the inventors' experiments, and Figure 2 is a cross-sectional view of a fine coke burner.
3 is a sectional view taken along the - line in FIG. 2, FIG. 4 is a sectional view of the fuel injection part of a burner device according to an embodiment of the present invention, and FIG. FIG. 4 is a front view of the heavy oil burner taken along the - line in FIG. 4, FIG. 6 is a sectional view taken along the - line in FIG. FIG. 7 is a sectional view taken along the - line in FIG. 7; 2...Fine powder coke burner, 4...Heavy oil burner, 14a, 14b, 23... Fuel split flame for auxiliary combustion, 20...Heavy oil burner nozzle, 22... Gas burner.
Claims (1)
手段をもち、複数のノズルを偏り位置させて助燃
ノズル組を形成し、難燃性微粉燃料の噴霧流れを
分断するように複数の該助燃ノズル組を相互に離
隔配置したことを特徴とする難燃性燃料用バーナ
装置。 2 前記ノズルをノズル用管部材の軸心より半径
方向に助燃燃料を噴出する複数のノズルとし、該
ノズル用管部材を複数本を並列かつ偏り位置させ
一の助燃ノズル組を形成し、該助燃ノズル組を相
互に離隔配置したことを特徴とする特許請求の範
囲第1項記載の難燃性燃料用バーナ装置。 3 前記助燃ノズル組をガス燃焼用の助燃ノズル
組とすることを特徴とする特許請求の範囲第2項
記載の難燃性燃料用バーナ装置。[Scope of Claims] 1. It has a means for turning the ejected flow of the flame-retardant pulverized fuel into a swirling flow, and forms an auxiliary combustion nozzle set by arranging a plurality of nozzles in uneven positions to divide the sprayed flow of the flame-retardant pulverized fuel. A burner device for flame-retardant fuel, characterized in that a plurality of auxiliary combustion nozzle sets are arranged at a distance from each other. 2. The nozzles are a plurality of nozzles that eject auxiliary combustion fuel in a radial direction from the axis of the nozzle tube member, and a plurality of the nozzle tube members are arranged in parallel and offset to form one auxiliary combustion nozzle set, and the auxiliary combustion A burner device for flame-retardant fuel according to claim 1, characterized in that the nozzle sets are arranged at a distance from each other. 3. The burner device for flame-retardant fuel according to claim 2, wherein the auxiliary combustion nozzle set is a auxiliary combustion nozzle set for gas combustion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24540583A JPS60140012A (en) | 1983-12-28 | 1983-12-28 | Burner device for incombustible fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24540583A JPS60140012A (en) | 1983-12-28 | 1983-12-28 | Burner device for incombustible fuel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60140012A JPS60140012A (en) | 1985-07-24 |
| JPH042846B2 true JPH042846B2 (en) | 1992-01-21 |
Family
ID=17133159
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24540583A Granted JPS60140012A (en) | 1983-12-28 | 1983-12-28 | Burner device for incombustible fuel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60140012A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5412243Y2 (en) * | 1974-09-07 | 1979-05-30 |
-
1983
- 1983-12-28 JP JP24540583A patent/JPS60140012A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60140012A (en) | 1985-07-24 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |