JPS6370007A - Gas burner in fluidized bed - Google Patents

Gas burner in fluidized bed

Info

Publication number
JPS6370007A
JPS6370007A JP21343086A JP21343086A JPS6370007A JP S6370007 A JPS6370007 A JP S6370007A JP 21343086 A JP21343086 A JP 21343086A JP 21343086 A JP21343086 A JP 21343086A JP S6370007 A JPS6370007 A JP S6370007A
Authority
JP
Japan
Prior art keywords
gas
fluidized bed
burner
air
combustion
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
JP21343086A
Other languages
Japanese (ja)
Inventor
Tsuneo Watabe
恒夫 渡部
Teruyuki Yokobayashi
横林 照之
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 Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP21343086A priority Critical patent/JPS6370007A/en
Publication of JPS6370007A publication Critical patent/JPS6370007A/en
Pending legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

PURPOSE:To provide a gas burner, installed in a bed, which performs uniform combustion on the wide plane of a fluidized bed, is durable to the continuous use for a long time, improves economical efficiency, and facilitates maintenance and inspection, by a method wherein the gas burner is provided with a gas fuel feed pipe, installed in a fluidized bed, a burner branch pipe, branched from the gas fuel feed pipe and extended in a flat surface manner in parallel to an air dispersion plate, and gas injection nozzles, situated in a dispersed manner on the upper surface of the branch pipe. CONSTITUTION:Air for combustion fed in an air box 5 is fed through an air injection nozzle 7 to a fluidized bed 2. Gas fuel is fed to the fluidized bed 2 through a gas fuel feed pipe 9, a burner branch pipe 11, and a gas injection nozzle 12, and is externally mixed with the air for combustion for combustion. In case multi-fuel combustion is effected by using gas and coal, coal is fed in the fluidized bed 2 through a coal feed pipe 8. Gas burnt in the fluidized bed 2 and an air tower 3 passes a heat transfer part situated at the rear part of a boiler, and is exhausted as exhaust gas to the outside of the boiler. By arranging the gas injection nozzle 12 as shown in Fig., the gas can be uniformly burnt on the wide surface of the fluidized bed. In a large boiler, a plurality of burners 10 are arranged in juxtaposition, and combustion on a wide area is practicable.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 流動層を用いた燃焼装置に係り、特に石炭、ガス混焼可
能な流il?l1層内ガスバーナに関する。
[Detailed Description of the Invention] [Industrial Field of Application] This invention relates to a combustion device using a fluidized bed, particularly a fluid bed capable of co-combusting coal and gas. Regarding the l1 in-layer gas burner.

〔従来の技術〕[Conventional technology]

流動層燃焼装置は、固体燃料を流動媒体と共に流動させ
ながら燃焼させる構造となっており、気体燃料あるいは
液体燃料を主燃料として使用する構造ではない。また現
状、燃焼装置の起動点火は。
A fluidized bed combustion apparatus has a structure in which solid fuel is combusted while flowing together with a fluidized medium, and does not use gaseous fuel or liquid fuel as the main fuel. Also, at present, the startup ignition of the combustion equipment.

油を燃やす熱風炉あるいは油を燃料とする層上バーナに
よるのが一般的である。流動層内で燃焼を行う層内バー
ナとしては、 実開昭56−75513、 実開昭58−148410、 実開昭58−148411、 実開昭58−148412号の各公報に記載のものがあ
るが、いずれも小型で起動用バーナとして考案されたも
のである。第8図に実開昭56−75513号記載の層
内点火バーナ装置を示す。
Generally, an oil-burning hot air furnace or an oil-fueled bed burner is used. In-bed burners that perform combustion in a fluidized bed include those described in the following publications: Utility Model Application No. 56-75513, Utility Model Application No. 58-148410, Utility Model Application No. 58-148411, and Utility Model Application No. 58-148412. However, all of them are small and were devised as starting burners. FIG. 8 shows an in-bed ignition burner device described in Japanese Utility Model Application No. 56-75513.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

流動層ボイラは元来固体燃料を使用するボイラとして計
画されているが、近時、製鉄所等で発生する高炉ガス、
転炉ガス、コークス炉ガスや、化学プラン1−で発生す
る可燃性ガスを流動層ボイラで、石炭と混焼したいとい
う要求がある。これに対し、前記の各公報に記載のバー
ナは、前述のように起動用のバーナであり、流動層内の
局部を加熱することはできても、流動層の広い平面で全
体的に燃焼させることおよび石炭との長時間にわたるガ
ス混焼については配慮されておらず、熱風炉なしで起動
させる為の層内バーナにとどまっていた。
Fluidized bed boilers were originally planned as boilers that used solid fuel, but in recent years, blast furnace gas generated in steel plants, etc.
There is a demand for co-firing converter gas, coke oven gas, and flammable gas generated in chemical plan 1- with coal in a fluidized bed boiler. On the other hand, the burners described in each of the above-mentioned publications are startup burners as mentioned above, and although they can heat a local area within the fluidized bed, they burn the entire fluidized bed over a wide plane. However, no consideration was given to the long-term co-firing of gas with coal, and it was limited to an in-bed burner that could be started without a hot blast furnace.

又、第9図に示すように、流動層ボイラの風箱5内にバ
ーナ枝管11を設け、空気分散板6に設けた空気噴出ノ
ズル7の内部に、前記バーナ枝管11から分散したガス
ノズル枝管16を前記空気噴出ノズルの頂部を貫通させ
て配設し、空気噴出ノズルの頂部に、ガス噴出用の細孔
を設けたガス噴出ノズル12をキャップ状に設けてなる
ガス燃焼用のバーナの考案も行われている。しかしなが
ら、この構造では、空気分散板6とバーナ枝管11との
相対的な温度差(200〜350℃)による平面(水平
)方向の伸び差と熱応力について配慮されておらず、ガ
スノズル枝管16が破損する問題がある。これを避ける
為、ガスノズル技管取付部にベローズを用いろ方法もあ
るが、ガス噴出ノズルは、100〜200m、m、ピッ
チの基盤目状に設置されるため、例えば10m角の炉の
場合、10000〜2500個ものベローズが必要とな
り、経済性、接続部の点検保守性に問題があった。
Further, as shown in FIG. 9, a burner branch pipe 11 is provided in the wind box 5 of the fluidized bed boiler, and gas nozzles dispersed from the burner branch pipe 11 are installed inside the air jet nozzle 7 provided in the air distribution plate 6. A burner for gas combustion, in which a branch pipe 16 is arranged to pass through the top of the air jet nozzle, and a cap-shaped gas jet nozzle 12 having a gas jet pore is provided at the top of the air jet nozzle. is also being devised. However, this structure does not take into consideration the difference in elongation in the plane (horizontal) direction and thermal stress due to the relative temperature difference (200 to 350°C) between the air distribution plate 6 and the burner branch pipe 11, and the gas nozzle branch pipe There is a problem that 16 is damaged. In order to avoid this, there is a method of using bellows at the gas nozzle pipe attachment part, but since gas jet nozzles are installed in a base pattern with a pitch of 100 to 200 m, for example, in the case of a 10 m square furnace, As many as 10,000 to 2,500 bellows were required, which caused problems in terms of economy and ease of inspection and maintenance of the connection.

本発明の課題は、流動層の広い平面で均等に燃焼し、長
時間連続使用に耐え、経済的で点検保守も容易な層内設
置のガスバーナを提供することにある。
An object of the present invention is to provide a gas burner installed in a bed that burns evenly over a wide flat surface of a fluidized bed, can withstand continuous use for a long time, is economical, and is easy to inspect and maintain.

〔問題点を解決するための手段〕[Means for solving problems]

上記目的は、ガス燃料供給管を、火炉側壁又は空気分散
板を貫通して流動層内へ配設し、流動層内で前記ガス燃
料供給管から分岐し、空気分散板に平行な、平面的に広
がるバーナ枝管と、該バーナ枝管の上面に、平均的に分
散して配置されたガス噴出ノズルから成る流動層内ガス
バーナを設けることにより達成される。
The above object is to install a gas fuel supply pipe through the furnace side wall or the air distribution plate into the fluidized bed, branch from the gas fuel supply pipe within the fluidized bed, and form a planar structure parallel to the air distribution plate. This is achieved by providing a gas burner in a fluidized bed consisting of a burner branch pipe extending over the area and gas ejection nozzles arranged evenly distributed on the upper surface of the burner branch pipe.

〔作用〕[Effect]

流動層内の広い平面に分散配置されたガス噴出ノズルか
ら噴出した燃料ガスは、燃焼用空気と早期に均等な混合
を行い、流動層内の広い平面で均等に燃焼する。
The fuel gas ejected from gas ejection nozzles distributed over a wide plane within the fluidized bed mixes quickly and evenly with combustion air, and is evenly combusted over a wide plane within the fluidized bed.

バーナが、空気分散板あるいは火炉側壁に固定されてい
るのは、ガス燃料供給管が空気分散板あるいは火炉側壁
を貫通している部分のみであり、バーナの空気分散板と
平行な方向の熱による伸びは、空気分散板の熱による伸
びと無関係である。
The burner is fixed to the air distribution plate or the furnace side wall only in the part where the gas fuel supply pipe penetrates the air distribution plate or the furnace side wall. The elongation is independent of the thermal elongation of the air distribution plate.

また、流動媒体が冷えた状態で流動層内のガスバーナに
点火しようとする時、流動層上面がガス噴出ノズルに接
近するまで流動層高を下げると、流動層上部の空塔部分
が、バーナ点火時の燃焼空間となる。バーナに点火、燃
焼させると周辺の流動媒体の温度が、次第に上昇し、流
動媒体内での燃焼が可能となる。
In addition, when trying to ignite a gas burner in the fluidized bed when the fluidized medium is cold, if the height of the fluidized bed is lowered until the top surface of the fluidized bed approaches the gas jet nozzle, the empty column above the fluidized bed will ignite the burner. It becomes a burning space of time. When the burner is ignited and combusted, the temperature of the surrounding fluid medium gradually rises, allowing combustion within the fluid medium.

〔実施例〕〔Example〕

以下、第1図〜第4図により本発明の一実施例を説明す
る。
An embodiment of the present invention will be described below with reference to FIGS. 1 to 4.

第1図は本発明による流動層内ガスバーナを装備したボ
イラの側断面図を示し、該ボイラは、火炉1と、該火炉
の上部に設けた空塔3と、前記火炉の下部に設けた流動
層2と、該流動層の底部をなす空気分散板6と、該空気
分散板に接して空気分散板の下方に設けられた風箱5と
、前記空気分散板の流動層側に設けられ、空気分散板の
流動層側と風箱側を連通ずる多数の空気噴出ノズル7と
、前記風箱5と前記空気分散板6を貫通して設けられ、
空気分散板6の上面に開孔を有する石炭供給管8と、前
記風箱5と前記空気分散板6を貫通して設けられ、流動
層2内に達しているガス燃料供給管9と、流動層内で該
ガス燃料供給管9から分岐し、空気分散板6に平行に平
面的に広がる格子状の枠をなすバーナ枝管11と、該バ
ーナ枝管11の上面に上方に向けて、管軸方向に沿って
設けられ、ガス噴出孔が、空気噴出ノズル7の空気噴出
孔とほぼ同じ水平面上に設けられているガス噴出ノズル
12を有している。
FIG. 1 shows a side sectional view of a boiler equipped with a gas burner in a fluidized bed according to the present invention. a layer 2, an air distribution plate 6 forming the bottom of the fluidized bed, a wind box 5 provided below the air distribution plate in contact with the air distribution plate, and provided on the fluidized bed side of the air distribution plate, A large number of air jet nozzles 7 that communicate the fluidized bed side and the wind box side of the air distribution plate, and are provided to penetrate the wind box 5 and the air distribution plate 6,
A coal supply pipe 8 having an opening on the upper surface of the air distribution plate 6, a gas fuel supply pipe 9 provided through the wind box 5 and the air distribution plate 6 and reaching into the fluidized bed 2, A burner branch pipe 11 branches from the gas fuel supply pipe 9 within the layer and forms a lattice-like frame that spreads in parallel with the air distribution plate 6, and a burner branch pipe 11 extends upward from the upper surface of the burner branch pipe 11. The gas ejection nozzle 12 is provided along the axial direction and has a gas ejection hole provided on substantially the same horizontal plane as the air ejection hole of the air ejection nozzle 7 .

風箱5に送給された燃焼用空気は、空気噴出ノズル7を
経て流動WJ2へ供給され、ガス燃料は、ガス燃料供給
管9、バーナ枝管11.ガス噴出ノズル12を経て流動
層2へ供給され、燃焼用空気と外部混合して燃焼する。
The combustion air supplied to the wind box 5 is supplied to the flow WJ2 through the air jet nozzle 7, and the gas fuel is supplied to the gas fuel supply pipe 9, burner branch pipe 11. The gas is supplied to the fluidized bed 2 through the gas jet nozzle 12, mixed externally with combustion air, and combusted.

ガスと石炭を混焼する場合には、石炭は石炭供給管8な
どにより流動層2内へ供給される。流動層2及び空塔3
で燃焼したガスは、ボイラ後部の伝熱部を通過し、排ガ
スとしてボイラ外へ排出される。
When co-firing gas and coal, coal is supplied into the fluidized bed 2 through a coal supply pipe 8 or the like. Fluidized bed 2 and empty column 3
The combusted gas passes through the heat transfer section at the rear of the boiler and is discharged outside the boiler as exhaust gas.

第2図は本発明による流動層内ガスバーナの実施例の斜
視図であり、ガス供給管9、バーナ枝管11、ガス噴出
ノズル12の関連を示している。
FIG. 2 is a perspective view of an embodiment of the fluidized bed gas burner according to the present invention, showing the relationship among the gas supply pipe 9, the burner branch pipe 11, and the gas jet nozzle 12.

ガス噴出ノズルをこのように配置することにより、流動
層の広い面で均一に燃焼することができ、大型のボイラ
にあっては、このバーナ10を複数個並列して装備すれ
ば、広い面積での燃焼が可能である。
By arranging the gas jet nozzles in this way, it is possible to burn uniformly over a wide area of the fluidized bed.In a large boiler, if a plurality of burners 10 are installed in parallel, combustion can be performed over a wide area. combustion is possible.

バーナ枝管11のネジしめ式の押え金具14は、管の管
軸方向の移動を拘束しない構造であって、空気分散板6
とバーナ枝管11の温度差による熱応力の発生を防いで
いる。又、ガス供給管9は、空気分散板6を貫通する個
所でネジ式の取付金具により空気分散板に固定されてお
り、点検保守がきわめて容易である。
The screw-type holding fitting 14 of the burner branch pipe 11 has a structure that does not restrict the movement of the pipe in the pipe axial direction, and the air distribution plate 6
This prevents the occurrence of thermal stress due to the temperature difference between the burner branch pipe 11 and the burner branch pipe 11. Furthermore, the gas supply pipe 9 is fixed to the air distribution plate 6 with screw-type fittings at the point where it passes through the air distribution plate 6, making inspection and maintenance extremely easy.

更に、ガス燃料の噴出位置が流動層2の最下部すなわち
空気分散板6に近接した位置となるので流動層内での燃
焼時間の確保が容易で、十分な層内燃焼が可能である。
Furthermore, since the gas fuel is ejected at the lowest part of the fluidized bed 2, that is, close to the air distribution plate 6, it is easy to secure sufficient combustion time within the fluidized bed, and sufficient combustion within the bed is possible.

バーナ構成部品が空気・ガスの噴出レベルより低い位置
に設置されているので、流動媒体によるバーナ部品の磨
耗が生じない。空気噴出ノズル7およびガス噴出ノズル
12の噴出孔は、第4図に示すように斜め下向きに且つ
各ノズルから放射状に噴出するように構成され、流動層
内の空気とガス燃料の混合を良好にすると共に、炉体止
時に流動媒体がノズルへ漏れこむのを防止している。
Since the burner components are located below the air/gas ejection level, no wear of the burner components by the flowing medium occurs. The ejection holes of the air ejection nozzle 7 and the gas ejection nozzle 12 are configured to emit air diagonally downward and radially from each nozzle, as shown in FIG. 4, to improve the mixing of air and gas fuel in the fluidized bed. At the same time, the fluidized medium is prevented from leaking into the nozzle when the furnace is stopped.

又1本バーナは、火炉側壁や、空気分散板を貫通する部
分が少く、設備費が低順である。
In addition, a single burner has a small amount of penetration through the furnace side wall and air distribution plate, and has a low equipment cost.

本発明による層内ガスバーナの他の実施例を第5図およ
び第6図に示す。バーナ枝管が構成する平面的な枠組み
形状を、放射状にしたものと、百足状にしたものであり
、いずれもほぼ中央にガス燃料供給管を設け、各枝管の
上面に管軸に沿ってガス噴出ノズルを取付けた構造であ
る。
Another embodiment of the in-bed gas burner according to the invention is shown in FIGS. 5 and 6. The planar frame shape of the burner branch pipes is either radial or centipede-shaped.In both cases, a gas fuel supply pipe is installed approximately in the center, and a gas fuel supply pipe is installed on the top surface of each branch pipe along the pipe axis. This structure is equipped with a gas jet nozzle.

気体燃料を用いるバーナの点火を炉の起動状態で安定に
行うことは、冷えた流動媒体が満たされている状態では
困難である。本実施例では第7図に示すように、起動時
は流動層高をガス噴出ノズルの位置まで一時的に低下さ
せてから点火し、流動媒体の温度の上昇に応じて流動媒
体量を増加し、次第に層高を上げて所要のレベルとする
起動方法を採ることにより安定した点火昇温を可能とし
た。
It is difficult to stably ignite a burner using gaseous fuel in the starting state of the furnace when the burner is filled with a cold fluidized medium. In this embodiment, as shown in Fig. 7, at startup, the height of the fluidized bed is temporarily lowered to the position of the gas jet nozzle before ignition, and the amount of fluidized medium is increased as the temperature of the fluidized medium increases. By adopting a startup method that gradually raises the layer height to the required level, stable ignition temperature rise was made possible.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、流動層ボイラにおいて、高炉ガス、コ
ークスガス、転炉ガスと、石炭との混焼が可能となり、
更にLPG等のガスを用いた起動が可能となる。
According to the present invention, co-firing of blast furnace gas, coke gas, converter gas, and coal is possible in a fluidized bed boiler,
Furthermore, startup using gas such as LPG is possible.

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

第1図は本発明の実施例を示す図、第2図は本発明によ
るガスバーナの実施例の斜視図、第3図は第1図の部分
の拡大図、第4図は空気噴出ノズルと本発明によるガス
噴出ノズルの相互の位置を示す図、第5図、第6図は本
発明の他の実施例を示す図、第7図は2本発明を適用し
たボイラの起動時を示す断面図、第8図、第9図は従来
技術の例を示す図である。 1・・・火炉、      2・・・流動層。 5・・・風箱、      6・・・空気分散板、7・
・・空気噴出ノズル、 9・・・ガス燃料供給管、10
・・・流動層内ガスバーナ、 11・・・バーナ枝管、   12・・・ガス噴出ノズ
ル。
Fig. 1 is a diagram showing an embodiment of the present invention, Fig. 2 is a perspective view of an embodiment of the gas burner according to the invention, Fig. 3 is an enlarged view of the part shown in Fig. 1, and Fig. 4 shows an air jet nozzle and a main body. Figures 5 and 6 are diagrams showing the mutual positions of the gas ejection nozzles according to the invention, Figures 5 and 6 are diagrams showing other embodiments of the invention, and Figure 7 is a sectional view showing the start-up of a boiler to which the two inventions are applied. , FIG. 8, and FIG. 9 are diagrams showing examples of the prior art. 1... Furnace, 2... Fluidized bed. 5... Wind box, 6... Air dispersion plate, 7.
...Air jet nozzle, 9...Gas fuel supply pipe, 10
...Fluidized bed gas burner, 11...Burner branch pipe, 12...Gas jet nozzle.

Claims (8)

【特許請求の範囲】[Claims] (1)火炉と、該火炉の下部に設けられた流動層と、該
流動層の底部に設けられた空気分散板と、該空気分散板
に接してその下方に設けられた風箱と、前記空気分散板
に設けられ、前記風箱と前記流動層を連通する空気噴出
ノズルとを有する流動層燃焼装置において、 流動層内に配設したガス燃料供給管と、前記流動層内で
前記ガス燃料供給管から分岐し、空気分散板に平行な、
平面的に広がるバーナ枝管と、該バーナ枝管の上面に分
散して設けられたガス噴出ノズルとを有することを特徴
とする、流動層内ガスバーナ。
(1) a furnace, a fluidized bed provided at the bottom of the furnace, an air distribution plate provided at the bottom of the fluidized bed, a wind box provided in contact with and below the air distribution plate; A fluidized bed combustion apparatus having an air jet nozzle provided on an air distribution plate and communicating the wind box and the fluidized bed, comprising: a gas fuel supply pipe arranged in the fluidized bed; and a gas fuel supply pipe arranged in the fluidized bed; Branching from the supply pipe and parallel to the air distribution plate,
A gas burner in a fluidized bed, characterized in that it has a burner branch pipe that spreads out in a planar manner, and gas ejection nozzles that are distributed and provided on the upper surface of the burner branch pipe.
(2)バーナ枝管を、水平放射状に配置したことを特徴
とする特許請求の範囲第1項に記載の流動層内ガスバー
ナ。
(2) The gas burner in a fluidized bed according to claim 1, wherein the burner branch pipes are arranged horizontally and radially.
(3)バーナ枝管を、百足状に配置したことを特徴とす
る特許請求の範囲第1項に記載の流動層内ガスバーナ。
(3) The gas burner in a fluidized bed according to claim 1, wherein the burner branch pipes are arranged in a centipede shape.
(4)バーナ枝管を、格子状に配置したことを特徴とす
る特許請求の範囲第1項に記載の流動層内ガスバーナ。
(4) The gas burner in a fluidized bed according to claim 1, wherein the burner branch pipes are arranged in a grid pattern.
(5)バーナ枝管を、同心円状に配置したことを特徴と
する特許請求の範囲第1項に記載の流動層内ガスバーナ
(5) The gas burner in a fluidized bed according to claim 1, wherein the burner branch pipes are arranged concentrically.
(6)ガス噴出ノズルに設けたガス噴出孔と、空気噴出
ノズルに設けた空気噴出孔がほぼ同じ水平面にあること
を特徴とする特許請求の範囲第1〜5項のいずれか1項
に記載の流動層内ガスバーナ。
(6) The gas ejection hole provided in the gas ejection nozzle and the air ejection hole provided in the air ejection nozzle are located on substantially the same horizontal plane, according to any one of claims 1 to 5. Fluidized bed gas burner.
(7)ガス噴出ノズルに設けたガス噴出孔が、各ノズル
の中心から見て放射状に設けられ、且つノズル内側から
外側に向け、斜め下方に傾斜していることを特徴とする
特許請求の範囲第1項〜6項のいずれか1項に記載の流
動層内ガスバーナ。
(7) A claim characterized in that the gas ejection holes provided in the gas ejection nozzles are provided radially when viewed from the center of each nozzle, and are inclined obliquely downward from the inside of the nozzle to the outside. The gas burner in a fluidized bed according to any one of Items 1 to 6.
(8)ガス燃料供給管が風箱及び空気分散板を貫通して
設けられていることを特徴とする特許請求の範囲第1〜
7項のいずれか1項に記載の流動層内ガスバーナ。
(8) Claims 1 to 1, characterized in that the gas fuel supply pipe is provided through the wind box and the air distribution plate.
The gas burner in a fluidized bed according to any one of Item 7.
JP21343086A 1986-09-10 1986-09-10 Gas burner in fluidized bed Pending JPS6370007A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21343086A JPS6370007A (en) 1986-09-10 1986-09-10 Gas burner in fluidized bed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21343086A JPS6370007A (en) 1986-09-10 1986-09-10 Gas burner in fluidized bed

Publications (1)

Publication Number Publication Date
JPS6370007A true JPS6370007A (en) 1988-03-30

Family

ID=16639096

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21343086A Pending JPS6370007A (en) 1986-09-10 1986-09-10 Gas burner in fluidized bed

Country Status (1)

Country Link
JP (1) JPS6370007A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS549024A (en) * 1977-06-22 1979-01-23 Mitsubishi Heavy Ind Ltd Fluid layer combustion device
JPS57104086A (en) * 1980-12-18 1982-06-28 Mitsubishi Heavy Ind Ltd Fluidized bed apparatus
JPS6143613B2 (en) * 1978-02-12 1986-09-29 Matsushita Electric Ind Co Ltd

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS549024A (en) * 1977-06-22 1979-01-23 Mitsubishi Heavy Ind Ltd Fluid layer combustion device
JPS6143613B2 (en) * 1978-02-12 1986-09-29 Matsushita Electric Ind Co Ltd
JPS57104086A (en) * 1980-12-18 1982-06-28 Mitsubishi Heavy Ind Ltd Fluidized bed apparatus

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