JPH0639217Y2 - Cyclone type coal combustor - Google Patents

Cyclone type coal combustor

Info

Publication number
JPH0639217Y2
JPH0639217Y2 JP2477789U JP2477789U JPH0639217Y2 JP H0639217 Y2 JPH0639217 Y2 JP H0639217Y2 JP 2477789 U JP2477789 U JP 2477789U JP 2477789 U JP2477789 U JP 2477789U JP H0639217 Y2 JPH0639217 Y2 JP H0639217Y2
Authority
JP
Japan
Prior art keywords
combustion chamber
flow
slag
partition wall
combustor
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
Application number
JP2477789U
Other languages
Japanese (ja)
Other versions
JPH02122911U (en
Inventor
要三良 岩藤
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 JP2477789U priority Critical patent/JPH0639217Y2/en
Publication of JPH02122911U publication Critical patent/JPH02122911U/ja
Application granted granted Critical
Publication of JPH0639217Y2 publication Critical patent/JPH0639217Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、石炭だきMHD(Magnet Hydro Dynamics)発電
用、噴流床式石炭ガス化炉用、石炭だきガスタービン用
等のサイクロン式石炭燃焼器に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is a cyclone type coal combustor for coal-fired MHD (Magnet Hydro Dynamics) power generation, for a spouted bed type coal gasifier, for a coal-fired gas turbine, etc. Regarding

〔従来の技術〕[Conventional technology]

第4図に従来技術によるサイクロン式の石炭燃焼器の構
成概念図を示す。
FIG. 4 shows a conceptual diagram of the structure of a cyclone type coal combustor according to the prior art.

燃焼器頭部の石炭吹き込みノズル2から第1段燃焼室1
内へ噴射される燃料13は、燃焼室胴部の内壁面に添って
切線方向に開口して設けられたサイクロンノズル8から
吹き込まれる酸化剤(酸素又は高温空気)12の強力な旋
回流によって拡散混合され燃焼し、燃焼反応によって生
成する残渣(石炭スラグ)は気流の遠心力作用によって
燃焼室の内壁面へたゝきつけられ、後部隔壁4で堰止め
られ、下部に設けられたスラグ流出口9からスラグポッ
ト11へ流れ込み燃焼室内から系外へ分離捕集され、スラ
グ14として排出される。石炭スラグが除去された高温の
燃焼ガスは、後部隔壁4の中央部に設けられた堰7で形
成される出口7Aを通って第2段燃焼室5へ導入される。
なお、15は第2段燃焼室5から排出される高温ガスであ
る。
1st stage combustion chamber 1 from coal injection nozzle 2 of the combustor head
The fuel 13 injected into the interior is diffused by the strong swirling flow of the oxidant (oxygen or high temperature air) 12 blown from the cyclone nozzle 8 provided along the inner wall surface of the combustion chamber body along the cut line direction. The residue (coal slag) that is mixed and burned and produced by the combustion reaction is urged against the inner wall surface of the combustion chamber by the centrifugal force of the air flow, blocked by the rear partition wall 4, and the slag outlet 9 provided in the lower part. Flows into the slag pot 11 from the combustion chamber, is separated and collected outside the system from the combustion chamber, and is discharged as slag 14. The high-temperature combustion gas from which the coal slag has been removed is introduced into the second-stage combustion chamber 5 through the outlet 7A formed by the weir 7 provided in the central portion of the rear partition wall 4.
In addition, 15 is a high temperature gas discharged from the second stage combustion chamber 5.

〔考案が解決しようとする課題〕 次世代の石炭利用技術の実用化への課題としては、周知
のように、燃焼残渣(石炭スラグ)を、燃焼室内ででき
る限り高い効率で除去し高温クリーンガスを製造する燃
焼器を玉成することが重要とされており、各方面で研究
開発が進められている。
[Problems to be solved by the invention] It is well known that the practical use of the next-generation coal utilization technology is to remove combustion residues (coal slag) in the combustion chamber as efficiently as possible to obtain a high-temperature clean gas. It is important to make a combustor that manufactures, and research and development is progressing in various fields.

第5図は、上記従来技術のサイクロン式石炭燃焼器にお
ける燃焼器内の高温燃焼ガスの流れと燃焼器内壁面に添
って流動する溶融スラグの流れ模様を示したものであ
る。図に示すように、燃焼室胴部の内壁面に添って切線
方向に開口して設けられたサイクロンノズル8から吹出
される酸化剤(酸素又は高温空気)12は、燃焼室内壁面
の軸方向断面に対して、サイクロンノズルから15度〜20
度の広り角(α)で広がり、燃焼室内周壁に添って軸方
向に螺旋状のリブ流れイを生ずる。一方、燃焼火炎中の
残渣は溶融ミスト状で酸化剤の旋回渦流による遠心力作
用で燃焼室内壁面にたゝきつけられ、内周壁面の軸方向
のリブ流れイに添って後流へ押し流され、後流側下部の
スラグ流出口9からスラグポット11内へ流下する。こゝ
で前記のリブ流れイに乗って隔壁面に衝突した一部の溶
融スラグが、隔壁4中央部の高温ガスの出口7Aに向って
流れる主流ガスに誘引され、隔壁部の堰7を乗り越え、
後流へのキャリオーバーを生じ、スラグ除去性能を低下
させる欠点があった。
FIG. 5 shows the flow of the high temperature combustion gas in the combustor and the flow pattern of the molten slag flowing along the inner wall surface of the combustor in the above-mentioned conventional cyclone type coal combustor. As shown in the figure, the oxidizer (oxygen or high temperature air) 12 blown out from the cyclone nozzle 8 provided along the inner wall surface of the combustion chamber body along the cutting line is an axial cross section of the combustion chamber wall surface. Against, from the cyclone nozzle 15 degrees ~ 20
It spreads at a widening angle (α) and generates a spiral rib flow B in the axial direction along the peripheral wall of the combustion chamber. On the other hand, the residue in the combustion flame is in the form of molten mist and is pushed against the inner wall surface of the combustion chamber by the centrifugal force of the swirling vortex flow of the oxidizer, and is pushed to the wake along the axial rib flow a of the inner wall surface. It flows down into the slag pot 11 from the slag outlet 9 at the lower part of the wake side. Here, a part of the molten slag that has collided with the partition wall surface by riding on the rib flow a is attracted by the mainstream gas flowing toward the high temperature gas outlet 7A in the central portion of the partition wall 4, and gets over the weir 7 of the partition wall. ,
There is a drawback that carry-over to the wake occurs and the slag removal performance is deteriorated.

本考案は、このような溶融スラグの溢流現象を防止しよ
うとするものである。
The present invention is intended to prevent such an overflow phenomenon of molten slag.

〔課題を解決するための手段〕[Means for Solving the Problems]

本考案は、燃焼室内に旋回気流を形成させ、石炭を溶融
状態で旋回流の遠心力作用によって燃焼器内壁面に分離
し系外へ排出するサイクロン式石炭燃焼器において、燃
焼ガス流れの下流側の燃焼室の隔壁面に、燃焼室内の旋
回流れに沿ったガイドベーンを設けた。
The present invention is a cyclone type coal combustor in which a swirling airflow is formed in a combustion chamber, and coal is separated into inner walls of a combustor by a centrifugal force action of the swirling flow in a molten state and discharged to the outside of the system. Guide vanes along the swirl flow in the combustion chamber were provided on the partition wall surface of the combustion chamber.

〔作用〕[Action]

本考案では、燃焼室の後流側の隔壁の面に衝突した旋回
する主流のガス流れは、隔壁面から突出したガイドベー
ンの側面に衝突して乱れとなり、隔壁面において旋回流
と軸心に向う流れが消去され、流れの淀み渦部が隔壁面
のコーナー部に生ずる。従って、燃焼室の内壁面に沿う
リブ流れに押し流されて来る溶融スラグの流れは、隔壁
のコーナー部に形成される淀み渦域に塞じ込められ、隔
壁に沿って下方へ流れ、隔壁面での気流の求心力作用に
よる溶融スラグのキャリーオーバーが阻止される。
In the present invention, the swirling main-stream gas flow that collides with the surface of the partition wall on the wake side of the combustion chamber collides with the side surface of the guide vane protruding from the partition surface to become turbulent, and the swirl flow and the axial center are formed on the partition surface. The flow on the other side is erased, and a stagnation vortex portion of the flow occurs at the corner portion of the partition wall surface. Therefore, the flow of the molten slag, which is pushed by the rib flow along the inner wall surface of the combustion chamber, is confined in the stagnation vortex region formed at the corner of the partition wall, flows downward along the partition wall, and at the partition wall surface. Carryover of molten slag due to the centripetal force of the air flow is prevented.

また、隔壁面の中間域に衝突する溶融スラグは、旋回流
れに沿ったガイドベーンの側面に衝突してガイドベーン
に沿って外側へ向って流動して隔壁コーナー部の淀み渦
域へ流れ込み、隔壁に沿って下流へ流れ、同様に隔壁面
での気流の求心力作用による溶融スラグのキャリーオー
バーが阻止される。
Further, the molten slag colliding with the intermediate area of the partition wall surface collides with the side surface of the guide vane along the swirling flow, flows outward along the guide vane, flows into the stagnation vortex region of the partition wall corner, and Along the wall, the carry-over of the molten slag due to the centripetal force of the air flow on the partition surface is prevented.

以上のように、本考案によれば溶融スラグのキャリーオ
ーバーが防止され、燃焼器の性能が向上する。
As described above, according to the present invention, carryover of molten slag is prevented, and the performance of the combustor is improved.

〔実施例〕 本考案の一実施例を第1図ないし第3図によって説明す
る。
[Embodiment] An embodiment of the present invention will be described with reference to FIGS.

本実施例に係るサイクロン式石炭燃焼器は、石炭(微粉
炭、微粉炭・水混合燃料(CWM)、又は微粉炭・油混合
燃料(COM))バーナ2、燃焼室ヘッド3、第1燃焼室
1、第1燃焼室の後流側の隔壁4、第1燃焼室1の下部
に設けられたスラグ流下口9、同スラグ流下口9に接続
されたスラグポット11及び上記隔壁4に接続して下流側
に設けられた第2燃焼室5で構成され、燃焼室ヘッド3
には補助酸化剤を吹き込むスワラー10を内装し、第1燃
焼室の胴部には胴壁に内接して接線方向に開口し酸化剤
(高温空気)を吹き込むサイクロンノズル8を設けてい
る。上記隔壁4の上流面には、サイクロンノズル8によ
る第1燃焼室1内の旋回流れに沿って傾いた3個のガイ
ドベーン6を放射状に配設し、更に隔壁4の中央には、
ガスの流出口7Aを形成する同筒状の堰7を設けている。
The cyclone type coal combustor according to the present embodiment includes a coal (pulverized coal, pulverized coal / water mixed fuel (CWM) or pulverized coal / oil mixed fuel (COM)) burner 2, a combustion chamber head 3, a first combustion chamber. 1, a partition wall 4 on the downstream side of the first combustion chamber, a slag downflow port 9 provided in the lower portion of the first combustion chamber 1, a slag pot 11 connected to the slag flowdown port 9 and the partition wall 4 It is composed of the second combustion chamber 5 provided on the downstream side, and includes the combustion chamber head 3
A swirler 10 for injecting an auxiliary oxidant is installed inside, and a cyclone nozzle 8 for injecting an oxidant (high temperature air) is provided in the body of the first combustion chamber so as to be inscribed in the body wall and open in the tangential direction. On the upstream surface of the partition wall 4, three guide vanes 6 inclined along the swirling flow in the first combustion chamber 1 by the cyclone nozzle 8 are radially arranged, and further in the center of the partition wall 4,
A cylindrical weir 7 that forms a gas outlet 7A is provided.

本実施例では、石炭バーナ2噴口から燃焼室内へ噴射さ
れた燃料は、スワラー10及びサイクロンノズル8から供
給される高温空気12と混合され燃焼する。こゝで燃焼室
内には、燃焼室胴壁に切線方向に開口するサイクロンノ
ズル8からの高温空気12によって、高温空気の強力な旋
回流が形成されており、燃焼ガス中の残渣(石炭灰)16
は溶融状態で気流の遠心力作用によって、燃焼室周壁面
に分離され、壁面に添って後流へ押し流され、燃焼室下
部に設けられたスラグポット11の開口部9から流下し、
スラグポット11下部に接続される排出装置によってスラ
グ14として系外へ排出される。一方、石炭灰を分離除去
されたクリーン燃焼ガスは、第2燃焼室5で新な酸化剤
と混合され所定温度の高温燃焼ガス15を製造して、高温
ガスを作動源とする主コンポーネント(MHD 発電チャ
ンネル、ボイラ、ガスタービン等)へ供給する。
In this embodiment, the fuel injected from the injection port of the coal burner 2 into the combustion chamber is mixed with the high temperature air 12 supplied from the swirler 10 and the cyclone nozzle 8 and burned. Here, a strong swirling flow of high-temperature air is formed in the combustion chamber by the high-temperature air 12 from the cyclone nozzle 8 that opens in the cut line direction on the wall of the combustion chamber, and the residue (coal ash) in the combustion gas is formed. 16
Is melted and separated into the peripheral wall of the combustion chamber by the centrifugal force of the air flow, and is pushed backward along the wall and flows down from the opening 9 of the slag pot 11 provided in the lower part of the combustion chamber.
The slag 14 is discharged to the outside of the system by a discharge device connected to the bottom of the slag pot 11. On the other hand, the clean combustion gas from which the coal ash has been separated and removed is mixed with a new oxidizer in the second combustion chamber 5 to produce a high temperature combustion gas 15 at a predetermined temperature, and the main component (MHD) that uses the high temperature gas as an operating source Power generation channel, boiler, gas turbine, etc.).

第3図は、本実施例における第1燃焼室隔壁部の構造及
び流れの作用を示したものである。隔壁4の面に衝突し
た主流ガス流れ(実線)は、壁面上に乱れの境界層を形
成し、旋回方向の流れは突起したガイドベーン6の側面
に衝突して乱れとなり壁面上での旋回流と半径方向の軸
心に向う流れが消去され、隔壁4のコーナー部に流れの
淀み渦域口を生ずる。従って、燃焼室の内周壁面のリブ
流れイに押し流されて来る溶融スラグ16の流は、隔壁4
のコーナー部に形成される流れの淀み渦域口に塞じ込め
られ、隔壁4に沿って流下して第1燃焼室下部のスラグ
流下口9へ流動し、隔壁面での気流の求心力作用による
溶融スラグのキャリオーバーを阻止することができる。
また、隔壁4の面の中間域に衝突する溶融スラグは、旋
回流れに沿って設けられたガイドベーン6の側面に衝突
し、点線で示すようにガイドベーン6に添って外方へ流
動し、隔壁4のコーナー部の淀み渦域口へ流れ同様に隔
壁4に沿って流下してスラグ流下口9へ流れ込む。
FIG. 3 shows the structure and flow action of the first combustion chamber partition wall in this embodiment. The mainstream gas flow (solid line) that collides with the surface of the partition wall 4 forms a turbulent boundary layer on the wall surface, and the flow in the swirling direction collides with the side surface of the protruding guide vane 6 and becomes turbulent, and swirl flow on the wall surface. And the flow toward the radial axis is eliminated, and a flow stagnation vortex opening is formed at the corner of the partition wall 4. Therefore, the flow of the molten slag 16 pushed by the rib flow a on the inner peripheral wall surface of the combustion chamber is
Is confined in the stagnation vortex region mouth of the flow formed in the corner part of the flow path, flows down along the partition wall 4 and flows to the slag flow-down opening 9 in the lower part of the first combustion chamber, and is caused by the centripetal action of the air flow on the partition wall surface. Carryover of molten slag can be prevented.
Further, the molten slag that collides with the intermediate area of the surface of the partition wall 4 collides with the side surface of the guide vane 6 provided along the swirling flow, flows outward along the guide vane 6 as shown by the dotted line, It flows to the stagnation vortex region mouth of the corner portion of the partition wall 4, and likewise flows down along the partition wall 4 and flows into the slag flow-down opening 9.

このようにして、本実施例においては、隔壁堰7からの
製造ガス中へのスラグのキャリオーバーを防止し、燃焼
器の性能向上を達成することができる。
In this way, in this embodiment, the carryover of slag from the partition wall weir 7 into the production gas can be prevented, and the performance of the combustor can be improved.

従来のサイクロン式石炭燃焼器におけるスラグ除去率は
70%ないし80%程度であったが、本実施例によれば90%
以上のスラグ除去率が達成された。
The slag removal rate in a conventional cyclone type coal combustor is
It was about 70% to 80%, but according to this example, 90%
The above slag removal rate was achieved.

〔考案の効果〕[Effect of device]

本考案は、燃焼室の燃焼ガス流れの下流側の隔壁に燃焼
室内の旋回流れに沿ったガイドベーンを設けるという簡
単な構成によって、溶融スラグのキャリーオーバーを防
止してスラグを除去したクリーンな高温の燃焼ガスを得
ることができる。
The present invention has a simple structure in which a guide vane that follows the swirling flow in the combustion chamber is provided in the partition wall on the downstream side of the combustion gas flow in the combustion chamber. Combustion gas can be obtained.

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

第1図は本考案の一実施例の断面図、第2図は第1図に
おけるA−A断面を示す断面図、第3図は本考案は同実
施例の燃焼室における流れの説明図、第4図は従来のサ
イクロン式石炭燃焼器を示す断面図、第5図は従来の同
石炭燃焼器の燃焼室内の流れを示す説明図である。 1…第1段燃焼室、2…石炭バーナ、 3…燃焼室ヘッド、4…隔壁、 5…第2燃焼室、6…ガイドベーン、 7…堰、7A…ガスの流出口、 8…サイクロンノズル、 9…スラグ流下口、10…スワラー、 11…スラグポット、12…酸化剤、 13…石炭、14…スラグ、 15…高温ガス、16…溶融スラグ
FIG. 1 is a sectional view of an embodiment of the present invention, FIG. 2 is a sectional view taken along the line AA in FIG. 1, and FIG. 3 is an explanatory view of a flow in a combustion chamber of the present embodiment, FIG. 4 is a cross-sectional view showing a conventional cyclone type coal combustor, and FIG. 5 is an explanatory view showing a flow in a combustion chamber of the conventional coal combustor. DESCRIPTION OF SYMBOLS 1 ... 1st stage combustion chamber, 2 ... Coal burner, 3 ... Combustion chamber head, 4 ... Partition wall, 5 ... 2nd combustion chamber, 6 ... Guide vane, 7 ... Weir, 7A ... Gas outlet, 8 ... Cyclone nozzle , 9 ... slag downflow port, 10 ... swirler, 11 ... slag pot, 12 ... oxidizer, 13 ... coal, 14 ... slag, 15 ... hot gas, 16 ... molten slag

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】燃焼室内に旋回気流を形成させ、石炭灰を
溶融状態で旋回流の遠心力作用によって燃焼器内壁面に
分離し系外へ排出するサイクロン式石炭燃焼器におい
て、燃焼ガス流れの下流側の燃焼室の隔壁面に燃焼室内
の旋回流れに沿ったガイドベーンを設けたことを特徴と
するサイクロン式石炭燃焼器。
1. A cyclone-type coal combustor in which a swirl flow is formed in a combustion chamber, and coal ash in a molten state is separated into an inner wall surface of the combustor by a centrifugal force action of the swirl flow and discharged to the outside of the system. A cyclone-type coal combustor, characterized in that guide vanes are provided along a swirl flow in the combustion chamber on a partition surface of the downstream combustion chamber.
JP2477789U 1989-03-06 1989-03-06 Cyclone type coal combustor Expired - Lifetime JPH0639217Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2477789U JPH0639217Y2 (en) 1989-03-06 1989-03-06 Cyclone type coal combustor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2477789U JPH0639217Y2 (en) 1989-03-06 1989-03-06 Cyclone type coal combustor

Publications (2)

Publication Number Publication Date
JPH02122911U JPH02122911U (en) 1990-10-09
JPH0639217Y2 true JPH0639217Y2 (en) 1994-10-12

Family

ID=31244929

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2477789U Expired - Lifetime JPH0639217Y2 (en) 1989-03-06 1989-03-06 Cyclone type coal combustor

Country Status (1)

Country Link
JP (1) JPH0639217Y2 (en)

Also Published As

Publication number Publication date
JPH02122911U (en) 1990-10-09

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