JPS62217010A - Gas pressure atomizing burner - Google Patents

Gas pressure atomizing burner

Info

Publication number
JPS62217010A
JPS62217010A JP5696386A JP5696386A JPS62217010A JP S62217010 A JPS62217010 A JP S62217010A JP 5696386 A JP5696386 A JP 5696386A JP 5696386 A JP5696386 A JP 5696386A JP S62217010 A JPS62217010 A JP S62217010A
Authority
JP
Japan
Prior art keywords
gas
nozzle
oil
mixing
mixing chamber
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
JP5696386A
Other languages
Japanese (ja)
Inventor
Shuichi Kishida
岸田 修一
Mitsuyasu Nakajima
中嶋 三泰
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.)
JFE Steel Corp
Toho Gas Co Ltd
Original Assignee
Kawasaki Steel 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 Kawasaki Steel Corp, Toho Gas Co Ltd filed Critical Kawasaki Steel Corp
Priority to JP5696386A priority Critical patent/JPS62217010A/en
Publication of JPS62217010A publication Critical patent/JPS62217010A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To realize higher turn-down ratio at low atomizing medium ratio and small gas heat input ratio with no necessity of the flow control of gas by a structure wherein the passing cross section of the primary mixing chamber of fuel oil and gas is throttled into that of a mixing nozzle. CONSTITUTION:In a burner 10, oil, which flows in a fuel supply passage 15 and through an oil nozzle 17 as indicated with an arrow A, and atomizing fuel gas, which flows in a gas passage 16 and through a gas nozzle 18, respectively enter a primary mixing chamber 19. Next, the passing cross section toward a mixing nozzle is abruptly throttled in taper so as to develop the agitation due to the change of stream lines. Thus, the separation of liquid stream and air stream, which occurred so far, is prevented from developing and the mixing is accelerated in a mixing nozzle 20 and the jetting from a jet 21 under highly atomized state is realized. The position, at which the mixing chamber 19 is throttled to the nozzle 20, is set at the rear of a point, at which the oil nozzle 17 communicates with the mixing chamber 19.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、中間混合型ガス圧噴霧燃焼器に関する。[Detailed description of the invention] [Industrial application field] FIELD OF THE INVENTION The present invention relates to an intermediate mixing gas pressure atomizing combustor.

〔従来の技術] 都市ガス等の比較的高圧の燃料ガスを霧化媒体として燃
料油を噴霧するガス圧噴霧燃焼方法が。
[Prior Art] A gas pressure atomization combustion method uses relatively high-pressure fuel gas such as city gas as an atomization medium to atomize fuel oil.

例えば特開昭511−149521号公報等に示されて
いる。このガス圧噴霧燃焼方法は、従来の蒸気噴霧や高
圧空気噴霧燃焼に比較し、(a)燃料ガスの先行燃焼に
より燃料油の気化が促進されて燃焼性能が向上し、低0
2、低NOx燃焼がOI俺となること、(b)低温度の
蒸気もしくは高圧空気を炉内に送り込まずに済むので炉
の熱効率が向上すること、(C)低燃焼負荷でも、霧化
媒体比率が大きいため燃焼性が損なわれず、ターンダウ
ン比を大きくとれること等の利点がある。
For example, it is shown in Japanese Patent Laid-Open No. 511-149521. Compared to conventional steam spray or high-pressure air spray combustion, this gas pressure spray combustion method has the following advantages: (a) Pre-combustion of fuel gas promotes vaporization of fuel oil, improves combustion performance, and reduces CO2 emissions.
2. Low NOx combustion becomes OI, (b) the thermal efficiency of the furnace is improved because there is no need to feed low temperature steam or high pressure air into the furnace, (c) even at low combustion loads, the atomization medium Since the ratio is large, combustibility is not impaired and there are advantages such as a large turndown ratio.

[発明が解決しようとする問題点] しかしながら、このガス圧噴霧燃焼による燃焼負荷の調
節は、一般には、(イ)ガス圧一定制御または(ロ)ガ
スー油定差圧制御にて油側の流量制御によりなされるが
、いずれの場合でも、低燃焼負荷では、ガス専焼として
、ガス側のみの流量制御でターンダウン比を大きくとる
ものである。
[Problems to be Solved by the Invention] However, the combustion load by this gas pressure spray combustion is generally controlled by (a) constant gas pressure control or (b) constant gas-oil differential pressure control to control the flow rate on the oil side. This is done through control, but in any case, at low combustion loads, gas-only combustion is performed and a large turndown ratio is achieved by controlling the flow rate only on the gas side.

一般に噴霧燃焼器は大別して第5図に示す3つの型式、
すなわち、(A)内部混合型、(B)中間混合型、およ
び(C)外部混合型がある。これらの特徴は第4表に示
すように一長一短であるが、ターンダウン特性から見れ
ば、内部混合型の場合は、低燃焼負荷になって油/ガス
の流量比、圧力比が小さくなる(油圧がガス圧に比べて
低くなる)と油側に脈動が′生じ、場合よってはガスの
油ノズル側への逆流現象を生じることもあり、高ターン
ダウン比を実現するバーナとしては不向きである。その
意中間混合型の場合、低燃焼負荷での油の脈動や逆流も
なく都合が良いのであるが。
In general, spray combustors can be roughly divided into three types, as shown in Figure 5.
That is, there are (A) internal mixing type, (B) intermediate mixing type, and (C) external mixing type. These characteristics have advantages and disadvantages as shown in Table 4, but from the viewpoint of turndown characteristics, internal mixing type has a low combustion load and the oil/gas flow ratio and pressure ratio are small (hydraulic (lower than the gas pressure), pulsations occur on the oil side, and in some cases, a backflow phenomenon of gas toward the oil nozzle side may occur, making it unsuitable for a burner that achieves a high turndown ratio. However, in the case of a medium-mixing type, there is no oil pulsation or backflow at low combustion loads, which is convenient.

良好な霧化特性を維持するためには霧化媒体比率を小さ
くできない欠点を有していた。すなわち、中間混合型噴
霧燃焼器の場合、霧化媒体比率は比較的大きく(従来の
中間混合型噴霧燃焼器の場合、定格燃焼負荷時で気/液
質量流量比W G/W L・0.10〜0.15が実用
上のド限であり、これは例えば[根矢ら 船舶技術研究
所報告12−1 (S50.l )P、IJに示される
ような気/液流量比と噴霧液滴粒径の関係から一般的で
ある)、このため低燃焼負荷でのガス専焼時にガス側に
流量制御機能をもたせて、所望のターンダウン比を実現
させる必要があった。
In order to maintain good atomization characteristics, the atomization medium ratio cannot be reduced. That is, in the case of an intermediate mix type spray combustor, the atomizing medium ratio is relatively large (in the case of a conventional intermediate mix type spray combustor, the gas/liquid mass flow rate ratio W G/W L・0. 10 to 0.15 is the practical limit, and this is based on the air/liquid flow rate ratio and spray liquid as shown in [Neya et al., Ship Engineering Research Institute Report 12-1 (S50.l) P, IJ]. For this reason, it was necessary to provide a flow rate control function on the gas side to achieve the desired turndown ratio during gas-only combustion under low combustion load.

したがって、ガス側に流量制御弁や流量計等の計装機器
を必要とし、また空燃比制御系にもガス流量に応じた必
要空気量の演算装置が必要である。さらに、燃料ガスと
して天然ガス系都市ガスを使用し、燃料油として安価な
C重油を用いる場合など、霧化媒体の流量比率の大きな
噴霧燃焼器を用いてガス圧噴霧燃焼を行なうには、経済
的効果が得られなくなるなどの問題があった。
Therefore, instrumentation equipment such as a flow rate control valve and a flow meter is required on the gas side, and an air-fuel ratio control system also requires a calculation device for calculating the required air amount according to the gas flow rate. Furthermore, when using natural gas-based city gas as the fuel gas and inexpensive C heavy oil as the fuel oil, it is economical to perform gas pressure atomization combustion using a spray combustor with a large flow rate ratio of the atomization medium. There were problems such as the inability to obtain desired effects.

本発明は、ガス4F崖時のガス側の流量制御装置を必要
としない程度に霧化媒体であるガス入熱比率を小さくし
た中間混合型噴霧燃焼器を提供し。
The present invention provides an intermediate mixing type spray combustor in which the heat input ratio of gas, which is an atomization medium, is reduced to such an extent that a flow rate control device on the gas side at the time of a gas 4F cliff is not required.

低霧化媒体比率でガス側の流量制御なしに高ターンダウ
ン比を容易に実現することを目的とするものである。
The purpose is to easily realize a high turndown ratio at a low atomizing medium ratio without controlling the flow rate on the gas side.

c問題点を解決するための手段】 本発明は、燃料油を供給する油ノズルと、燃料ガスを供
給するガスノズルとを混合ノズルに連通し、燃料油と燃
料ガスを混合状態で噴出する噴射孔を混合ノズルの先端
に形成してなる中間混合型ガス圧噴霧燃焼器において、
燃料油と燃料ガスの混合部に1次混合室を形成し、1次
混合室から混合ノズルに対する通過断面を絞るようにし
たものである。
Means for Solving Problems c] The present invention provides an injection hole that communicates an oil nozzle for supplying fuel oil and a gas nozzle for supplying fuel gas with a mixing nozzle, and injects fuel oil and fuel gas in a mixed state. In an intermediate mixing type gas pressure spray combustor formed at the tip of a mixing nozzle,
A primary mixing chamber is formed in the fuel oil and fuel gas mixing section, and the passage cross section from the primary mixing chamber to the mixing nozzle is narrowed.

[作用] 本発明によれば、燃料油は油ノズルを通り、ll化用の
燃料ガスはガスノズルを通り、それぞれ1次混合室に導
かれて相互に混合される。さらに、燃料油と燃料ガスは
、1次混合室から混合ノズルに導かれる際に、通過断面
を絞ったことによる流線の変向効果と流れの攪拌効果に
より、液流と気流の分離傾向を防ぐことができ、混合ノ
ズルで混合を促進され、噴出孔から高度に微粒化された
状態で噴出可能とされる。これにより、ガス専焼時のガ
ス側の流量制御装置を必要としない程度に霧化媒体であ
るガス入熱比率を小さくした噴霜燃焼気を嬶供し、低霧
化媒体比率でガス側の流量制御なしに高ターンダウン比
を容易に実現することがof能となる。
[Operation] According to the present invention, the fuel oil passes through the oil nozzle, and the fuel gas for 1I formation passes through the gas nozzle, and are guided to the primary mixing chamber and mixed with each other. Furthermore, when the fuel oil and fuel gas are led from the primary mixing chamber to the mixing nozzle, the tendency of separation between the liquid flow and the air flow is reduced due to the effect of changing the direction of the streamlines and the stirring effect of the flow due to the narrowed passage cross section. The mixture is promoted by the mixing nozzle, and can be ejected from the ejection hole in a highly atomized state. This provides blast combustion air with a low heat input ratio of gas, which is an atomizing medium, to the extent that a flow rate control device on the gas side is not required during gas-only combustion, and the flow rate on the gas side can be controlled with a low atomizing medium ratio. It becomes possible to easily realize a high turndown ratio without the need for a high turndown ratio.

[実施例] 第1図は、本発明の一実施例に係る中間混合型ガス圧噴
霧燃焼器を示す断面図である。
[Embodiment] FIG. 1 is a sectional view showing an intermediate mixing type gas pressure spray combustor according to an embodiment of the present invention.

ガス圧噴霧燃焼器10は、相互に2重管構造を形成する
オイルガン外管11とオイルガン内管12の先端部に、
7トマイザ(バーナチップ)13を配設している。すな
わち、7トマイザ13は、上記外管11とアトマイザ1
3の両者に螺合するキャップ14によって外管11と結
合するとともに、内管12に直接的に螺合している。こ
こで、外管11と内管12の間には燃料油供給通路15
が形成され、内管12には燃料ガス供給通路16が形成
されている。
The gas pressure spray combustor 10 includes an oil gun outer pipe 11 and an oil gun inner pipe 12, each of which has a double-pipe structure.
7 tomizers (burner chips) 13 are provided. That is, the 7 tomizer 13 includes the outer tube 11 and the atomizer 1.
It is connected to the outer tube 11 by a cap 14 that is screwed onto both of the tubes 3 and 3, and is directly screwed onto the inner tube 12. Here, a fuel oil supply passage 15 is provided between the outer pipe 11 and the inner pipe 12.
is formed, and a fuel gas supply passage 16 is formed in the inner tube 12.

アトマイザ13には、燃料油供給通路15に連通ずる油
ノズル17.燃料ガス供給通路16に連通ずるガスノズ
ル1B、1次混合室19、混合ノズル20が形成されて
いる。すなわち、燃焼器10は、燃料油を供給する油ノ
ズル17と、燃料ガスを供給するガスノズル18とを1
次混合室19に應・通し、その後方において急激に径を
絞ったテーパー状通過部22(テーパー角θ2)を経て
混合ノズル20を形成し、燃料油と燃料ガスを混合状態
で噴出する噴出孔21を混合ノズル20の先端に形成し
ている。なお、主ガスノズル18.1次混合室19、混
合ノズル20は、アトマイザ13の軸芯部に形成され、
油ノズル17は軸芯に対しある角度(入射角θ1)で1
次混合室19に連通している。
The atomizer 13 includes an oil nozzle 17 that communicates with the fuel oil supply passage 15. A gas nozzle 1B communicating with the fuel gas supply passage 16, a primary mixing chamber 19, and a mixing nozzle 20 are formed. That is, the combustor 10 has one oil nozzle 17 that supplies fuel oil and one gas nozzle 18 that supplies fuel gas.
The mixture nozzle 20 is formed through a taper-shaped passage portion 22 (taper angle θ2) whose diameter is rapidly narrowed behind the mixing chamber 19, and an ejection hole through which fuel oil and fuel gas are ejected in a mixed state. 21 is formed at the tip of the mixing nozzle 20. The main gas nozzle 18, the primary mixing chamber 19, and the mixing nozzle 20 are formed in the axial center of the atomizer 13,
The oil nozzle 17 is 1 at a certain angle (incident angle θ1) with respect to the axis.
It communicates with the next mixing chamber 19.

次に、上記実施例の作用について説明する。Next, the operation of the above embodiment will be explained.

燃焼器10において、燃料油は第1図に矢印Aで示すよ
うに燃料油供給通路15かも油ノズル17を通り、また
霧化用の燃料ガスは矢印Bで示すように燃料ガス供給通
路16からガスノズル18を通り、それぞれ1次混合室
19に導かれて相互に混合される。さらに混合ノズル2
0へ導かれる際に、通過断面をテーパー状に急激に絞っ
たことによる流線の変向効果と流れの攪拌効果により、
第2図に示す従来の中間混合型噴霧燃焼器において、比
較的生じやすかった液流31と気流32の分離傾向を防
ぐことができ、混合ノズル20で混合を促進され、噴出
孔21かも高度に微粒化された状態で噴出’al能とさ
れている。なお、1次混合室19から混合ノズル20に
絞る位置は、油ノズル17が1次混合室19に連通ずる
位置より後方にあることが必要であり、適当な混合室長
さが微粒化性能を支配するものである。かくして、本発
明による中間混合型ガス圧噴霧燃焼器による燃料油の微
粒化性能は、従来の中間混合型噴霧燃焼器より低い霧化
媒体比率で良好とすることができ、ガス側の流量制御な
しに高ターンダウン比を実現できる。
In the combustor 10, fuel oil passes through a fuel oil supply passage 15 and an oil nozzle 17 as shown by arrow A in FIG. 1, and fuel gas for atomization passes from a fuel gas supply passage 16 as shown by arrow B. The gases pass through gas nozzles 18 and are each introduced into a primary mixing chamber 19 where they are mixed with each other. Furthermore, mixing nozzle 2
When guided to 0, due to the changing direction of the streamline and the stirring effect of the flow due to the rapid narrowing of the passage cross section into a tapered shape,
In the conventional intermediate mixing type spray combustor shown in FIG. 2, the separation tendency of the liquid flow 31 and the air flow 32, which is relatively easy to occur, can be prevented, the mixing is promoted by the mixing nozzle 20, and the nozzle hole 21 is also It is said that it can be ejected in an atomized state. Note that the position where the primary mixing chamber 19 is squeezed into the mixing nozzle 20 must be located at the rear of the position where the oil nozzle 17 communicates with the primary mixing chamber 19, and the appropriate mixing chamber length governs the atomization performance. It is something to do. Thus, the fuel oil atomization performance of the intermediate-mix gas pressure atomization combustor according to the present invention can be better at a lower atomizing medium ratio than the conventional intermediate-mix gas pressure atomization combustor, without flow control on the gas side. A high turndown ratio can be achieved.

上記実施例による中間混合型ガス圧噴霧燃焼器10を、
燃焼器!25X 10’ kcal/)Ir cr)工
業炉用バーナに適用した。第1表に示すように使用燃料
油はC重油であり、霧化媒体には天然ガス系都市ガス1
3Aを用いた。ガス圧力は 1.5kg/crn’ G
 一定で作動させ、油量を調節することで燃焼負荷を変
更する。
The intermediate mixing type gas pressure atomizing combustor 10 according to the above embodiment includes:
Combustor! 25X 10' kcal/) Ir cr) Applied to an industrial furnace burner. As shown in Table 1, the fuel oil used is C heavy oil, and the atomization medium is natural gas-based city gas.
3A was used. Gas pressure is 1.5kg/crn'G
The combustion load is changed by operating at a constant rate and adjusting the oil amount.

なお、第3図に基づいて燃焼器の具体的な寸法をボせば
、油ノズル17の径0はφ0.8tge 、ガスノズル
18の径Gはφ1.5mm、1次混合室19の径M1は
$ 2.9mm 、混合ノズル20(7)径M2はφ1
.8諺層である。また、油ノズルの入射角θ1はeoI
kである0次に1次混合室19の後方テーパー状通過部
22について種々の絞り形状について霧化特性を調べた
結果、その主なものを第2表に示すが、■のテーパー状
を有する形状(テーパー状通過部22)が最適であるこ
とがわかった。ここで、上記テーパー状通過部22のテ
ーパー角θ2は30度〜60度が好ましく、実施例では
θ2−50度である。さらに第3表に示すように、1次
混合室19から混合ノズル20に絞る位置と油ノズル1
7が1次混合室19に連通ずる位置との関係交は微〜粒
化特性を支配するものであり、本実施例では1文=5.
2m曹とした。
Furthermore, if we specify the specific dimensions of the combustor based on Fig. 3, the diameter 0 of the oil nozzle 17 is φ0.8tge, the diameter G of the gas nozzle 18 is φ1.5mm, and the diameter M1 of the primary mixing chamber 19 is φ0.8tge. $2.9mm, mixing nozzle 20 (7) diameter M2 is φ1
.. There are 8 proverbial layers. Also, the angle of incidence θ1 of the oil nozzle is eoI
As a result of investigating the atomization characteristics of various aperture shapes for the rear tapered passage section 22 of the zero-order primary mixing chamber 19, which is k, the main ones are shown in Table 2. It was found that the shape (tapered passage section 22) was optimal. Here, the taper angle θ2 of the tapered passage portion 22 is preferably 30 degrees to 60 degrees, and in the embodiment is θ2-50 degrees. Further, as shown in Table 3, the position where the oil is squeezed from the primary mixing chamber 19 to the mixing nozzle 20 and the oil nozzle 1
The relationship between 7 and the position communicating with the primary mixing chamber 19 governs the atomization to granulation characteristics, and in this example, 1 sentence = 5.
It was set as 2 m So.

本実施例の燃焼負荷特性を第4図にボす、ガス作動圧力
 1.5kg/crn”Gのままでターンダウン比1:
lOが連続的に実現でき、■定格燃焼負荷時のガス入熱
比率−4,8%、■気/液質量流量比W G/W L譚
0.043 、■ガス専焼時の入熱量比−10,0%(
対定格燃焼負荷)となった、これは従来の噴霧燃焼器の
場合のガス作動圧カ一定でのターンダ第 1 表 第3 炎 ラン比 1:5に対し大幅な向上となるものである。さ
らに燃焼範囲のほぼ全域に蕪って低過剰空気燃焼(02
=1%)が実現できた。
The combustion load characteristics of this example are shown in Fig. 4.The turndown ratio is 1:
1O can be achieved continuously, ■Gas heat input ratio at rated combustion load -4.8%, ■Gas/liquid mass flow ratio W G / W L 0.043, ■Heat input ratio during gas-only combustion - 10.0% (
This is a significant improvement over the conventional spray combustor, which has a flame run ratio of 1:5 at a constant gas operating pressure. Furthermore, almost the entire combustion range is covered with low excess air combustion (02
= 1%) was achieved.

本発明によるガス圧噴霜燃焼器を工業炉用バーナに用い
ることにより以ドの効果がある。
By using the gas pressure frost injection combustor according to the present invention in a burner for an industrial furnace, the following effects can be obtained.

■ガス作動圧カ一定もしくは油−ガス差圧一定制御によ
り約1:10程度の高ターンダウン比を得ることができ
、従来、ここまでのターンダウン性を要求される場合に
必要であったガス側の流量制御装置を全く省くことがで
きる。
■A high turndown ratio of about 1:10 can be obtained by controlling the gas operating pressure to a constant level or the oil-gas differential pressure to a constant level, which was previously necessary when high turndown performance was required. A side flow control device can be completely omitted.

■霧化媒体であるガスの入熱比率をドげられるため、安
価なC重油を使用する場合には、油の入熱比率が相対的
に高くなり経済的効果株に優れる。
(2) Since the heat input ratio of the gas which is the atomization medium can be lowered, when using inexpensive C heavy oil, the heat input ratio of the oil becomes relatively high, resulting in excellent economic effects.

[発明の効果] 以上のように、本発明は、燃料油を供給する油ノズルと
、燃料ガスを供給するガスノズルとを混合ノズルに連通
し、燃料油と燃料ガスを混合状態で噴出する噴射孔を混
合ノズルの先端に形成してなる中間混合型ガス圧噴霧燃
焼器において、燃料油と燃料ガスの混合部に1次混合室
を形成、し、1次混合室から混合ノズルに対する通過断
面を絞るようにしたものである。したがって、ガス専焼
時のガス側の流量制御装置を必要としない程度に霧化媒
体であるガス入熱比率を小さくした噴霧燃焼器を提供し
、低霧化媒体比率でガス側の流量制御なしに高ターンダ
ウン比を容易に実現することがl1lf能となる。
[Effects of the Invention] As described above, the present invention provides an injection hole that connects an oil nozzle that supplies fuel oil and a gas nozzle that supplies fuel gas to a mixing nozzle and injects fuel oil and fuel gas in a mixed state. In an intermediate mixing type gas pressure spray combustor formed at the tip of a mixing nozzle, a primary mixing chamber is formed in the mixing part of fuel oil and fuel gas, and the passage cross section from the primary mixing chamber to the mixing nozzle is narrowed. This is how it was done. Therefore, we provide a spray combustor in which the heat input ratio of gas, which is an atomizing medium, is small enough to eliminate the need for a flow rate control device on the gas side during gas-only combustion. Easily realizing a high turndown ratio is an l1lf capability.

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

第1図は本発明の中間混合型ガス圧噴霧燃焼器の一実施
例を示す断面図、第2図は従来の中間混合型ガス圧噴霧
燃焼器内の気液流を示す模式図、第3図は中間混合型ガ
ス圧噴霜燃焼器の関係寸法図、第4図は本発明の中間混
合型ガス圧噴霧燃焼器を用いた工業炉用バーナの燃焼負
荷特性図、第5図は従来の噴霧燃焼器の概要図である。 lO・・・ガス圧噴霜燃焼器、17・・・油ノズル。 18・・・ガスノズル、19・・・1次混合室、20・
・・混合ノズル、21・・・噴出孔。 代理人 弁理士  塩 川 修 治 第 1 図 第2 図 第 3 図 eM−30〜60fi 第4 図 想現負荷(X)
FIG. 1 is a sectional view showing an embodiment of the intermediate mixing type gas pressure spray combustor of the present invention, FIG. 2 is a schematic diagram showing the gas-liquid flow in a conventional intermediate mixing type gas pressure spray combustor, and FIG. The figure shows the related dimensions of the intermediate mix type gas pressure spray combustor, Figure 4 shows the combustion load characteristics of an industrial furnace burner using the intermediate mix type gas pressure spray combustor of the present invention, and Figure 5 shows the conventional FIG. 2 is a schematic diagram of a spray combustor. lO...Gas pressure frost combustor, 17...Oil nozzle. 18... Gas nozzle, 19... Primary mixing chamber, 20...
...Mixing nozzle, 21...Blowout hole. Agent Patent Attorney Osamu Shiokawa 1 Figure 2 Figure 3 Figure eM-30~60fi Figure 4 Imaginary Load (X)

Claims (1)

【特許請求の範囲】[Claims] (1)燃料油を供給する油ノズルと、燃料ガスを供給す
るガスノズルとを混合ノズルに連通し、燃料油と燃料ガ
スを混合状態で噴出する噴射孔を混合ノズルの先端に形
成してなる中間混合型ガス圧噴霧燃焼器において、燃料
油と燃料ガスの混合部に1次混合室を形成し、1次混合
室から混合ノズルに対する通過断面を絞ることを特徴と
するガス圧噴霧燃焼器。
(1) An intermediate area formed by communicating an oil nozzle that supplies fuel oil and a gas nozzle that supplies fuel gas with a mixing nozzle, and forming an injection hole at the tip of the mixing nozzle that ejects fuel oil and fuel gas in a mixed state. A gas pressure spray combustor of mixed type, characterized in that a primary mixing chamber is formed in a mixing section of fuel oil and fuel gas, and a passage cross section from the primary mixing chamber to a mixing nozzle is narrowed.
JP5696386A 1986-03-17 1986-03-17 Gas pressure atomizing burner Pending JPS62217010A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5696386A JPS62217010A (en) 1986-03-17 1986-03-17 Gas pressure atomizing burner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5696386A JPS62217010A (en) 1986-03-17 1986-03-17 Gas pressure atomizing burner

Publications (1)

Publication Number Publication Date
JPS62217010A true JPS62217010A (en) 1987-09-24

Family

ID=13042188

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5696386A Pending JPS62217010A (en) 1986-03-17 1986-03-17 Gas pressure atomizing burner

Country Status (1)

Country Link
JP (1) JPS62217010A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5158726A (en) * 1974-11-13 1976-05-22 Porta Test Mfg BAANA
JPS5941372U (en) * 1982-09-08 1984-03-16 コニカ株式会社 recording device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5158726A (en) * 1974-11-13 1976-05-22 Porta Test Mfg BAANA
JPS5941372U (en) * 1982-09-08 1984-03-16 コニカ株式会社 recording device

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