JPH062808A - Slag tap type coal combustion unit - Google Patents

Slag tap type coal combustion unit

Info

Publication number
JPH062808A
JPH062808A JP18758592A JP18758592A JPH062808A JP H062808 A JPH062808 A JP H062808A JP 18758592 A JP18758592 A JP 18758592A JP 18758592 A JP18758592 A JP 18758592A JP H062808 A JPH062808 A JP H062808A
Authority
JP
Japan
Prior art keywords
combustion chamber
slag
primary
primary combustion
coal
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.)
Withdrawn
Application number
JP18758592A
Other languages
Japanese (ja)
Inventor
Mitsuhiro Irino
光博 入野
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 JP18758592A priority Critical patent/JPH062808A/en
Publication of JPH062808A publication Critical patent/JPH062808A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE:To perform a substantial complete removal of slag from combustion gas. CONSTITUTION:A plurality of feeding holes 3 in which coal and primary air 1 are fed into a vertical primary combustion chamber 2 in a tangential direction are arranged at the upper part of a wall 4 of the primary combustion chamber and combustion gas 5 swirls and flows downward. A cyclone inner cylinder 16 communicating with a secondary combustion chamber 7 is arranged at the upper part within the primary combustion chamber 2 and at the same time its lower part 17 is expanded in a tapered form, thereby combustion gas flowing in a downward swirled direction is directed to strike against the side wall 4 by the tapered expanded part 17 as indicated by a symbol 5a, reversed as indicated by a symbol 5b and then the combustion gas is flowed into the cyclone inner cylinder 16 of high temperature.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、石炭焚きのガスタービ
ン発電プラントやMHD(磁気流体)発電プラントで用
いられるスラグタップ式石炭燃焼器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a slag tap type coal combustor used in a coal-fired gas turbine power plant or MHD (magnetic fluid) power plant.

【0002】[0002]

【従来の技術】スラグタップ式石炭燃焼器はスラッギン
グ式石炭ガス化炉とも称されているが、その従来例とし
て図5〜図7に示すようなものがあり、図5はその全体
構成を示す断面図、図6及び図7はそれぞれ図5のVI
−VI線及びVII−VII線に沿う断面図である。
2. Description of the Related Art A slag tap type coal combustor is also called a slagging type coal gasifier, and there are conventional slag tap type coal gasifiers as shown in FIGS. 5 to 7, and FIG. The cross-sectional views, and FIGS. 6 and 7 are VI of FIG.
It is sectional drawing which follows the -VI line and the VII-VII line.

【0003】図5において、石炭と1次空気1を縦型の
1次燃焼室2内に図6で示すように接線方向で投入する
複数個(本例では4個)の投入孔3は、従来、1次燃焼
室2の側壁4の下部に設けられている。したがって、こ
れらの投入孔3から1次燃焼室2内に接線方向で投入さ
れた石炭と1次空気1による燃焼ガス5は、1次燃焼室
2内を上向きに旋回しながら流れ、その遠心力にてスラ
グ6が分離され、それから1次燃焼室2の頂部上に設け
られている2次燃焼室7に流れて、図7に示すように複
数個(本例では4個)の投入孔8から投入された2次空
気9にて2次燃焼し、その後排出口10から図示してい
ないガスタービンやMHD発電機等に供給される。一
方、燃焼ガス5から分離されたスラグ6は、1次燃焼室
2の底部11に設けられているスラグタップ孔12か
ら、水だめ13内の水14中に落下して急冷され、細か
い粒状となって水だめ13の底部にたまり、その後適宜
取出口15から取出される。
In FIG. 5, a plurality of (four in this example) charging holes 3 for charging coal and primary air 1 in a vertical type primary combustion chamber 2 in a tangential direction as shown in FIG. Conventionally, it is provided below the side wall 4 of the primary combustion chamber 2. Therefore, the combustion gas 5 generated by coal and the primary air 1 tangentially injected into the primary combustion chamber 2 through these injection holes 3 flows upward in the primary combustion chamber 2 while swirling upward, and the centrifugal force thereof is generated. The slag 6 is separated from the slag 6 and then flows into the secondary combustion chamber 7 provided on the top of the primary combustion chamber 2, and as shown in FIG. Secondary combustion is carried out with the secondary air 9 introduced from the above, and then it is supplied from the exhaust port 10 to a gas turbine, an MHD generator or the like not shown. On the other hand, the slag 6 separated from the combustion gas 5 falls into the water 14 in the sump 13 from the slag tap hole 12 provided in the bottom portion 11 of the primary combustion chamber 2 and is rapidly cooled to form fine particles. After that, it accumulates at the bottom of the sump 13 and is then taken out through the outlet 15 as appropriate.

【0004】[0004]

【発明が解決しようとする課題】ところで、上記した従
来のスラグタップ式石炭燃焼器にあっては、次のような
問題があった。 (1)1次燃焼室2内に投入された石炭と1次空気1に
よる燃焼ガス5は、上向き旋回流として上昇しているた
め、1次燃焼室2の側壁4の内面を液膜状で流下するス
ラグ6の重力による流下を防げる。 (2)このスラグ6が1次燃焼室2の側壁4の内面に沿
って下向きに流下する際、1次燃焼室2の側壁4の下方
部から投入された石炭と1次空気1のジェット流にて壁
での流下膜が切断され、1次燃焼室2内に飛散する。 (3)石炭と1次空気1による燃焼ガス5は常に上昇流
であることから、1次燃焼室2のガス流に乗った小粒径
のスラグ6′については、遠心力作用が小さいために重
力分離が十分に行われない。
The conventional slag tap type coal combustor described above has the following problems. (1) Since the combustion gas 5 generated by the coal and the primary air 1 charged into the primary combustion chamber 2 is rising as an upward swirling flow, the inner surface of the side wall 4 of the primary combustion chamber 2 is formed into a liquid film. It is possible to prevent gravity from flowing down the slag 6. (2) When the slag 6 flows downward along the inner surface of the side wall 4 of the primary combustion chamber 2, the jet flow of coal and the primary air 1 injected from the lower part of the side wall 4 of the primary combustion chamber 2 At the wall, the falling film is cut and scattered in the primary combustion chamber 2. (3) Since the combustion gas 5 of coal and the primary air 1 is always an upward flow, the centrifugal force action is small for the slag 6'having a small particle size and riding on the gas flow in the primary combustion chamber 2 Gravitational separation is not sufficient.

【0005】そして、これら3つの原因によって、従来
のスラグタップ式石炭燃焼室におけるスラグ除去率は8
0〜90%程度に留っており、石炭焚きのガスタービン
発電のためには、石炭燃焼器の後流側にスラグ除去装置
を特別に設けて、スラグを燃焼ガス中から再度除去する
必要があった。
Due to these three causes, the slag removal rate in the conventional slag tap type coal combustion chamber is 8%.
It remains around 0 to 90%, and for the coal-fired gas turbine power generation, it is necessary to specially install a slag removing device on the downstream side of the coal combustor to remove the slag from the combustion gas again. there were.

【0006】本発明は、このような従来技術の課題を解
決するためになされたもので、石炭と1次空気による燃
焼ガス中からスラグをほぼ完全に除去できるようにした
スラグタップ式石炭燃焼器を提供することを目的とす
る。
[0006] The present invention has been made to solve the problems of the prior art, and is a slag tap type coal combustor capable of almost completely removing slag from the combustion gas of coal and primary air. The purpose is to provide.

【0007】[0007]

【課題を解決するための手段】上記の課題を解決するた
めに、本発明は、縦型の1次燃焼室を備えるスラグタッ
プ式石炭燃焼器において、石炭と1次空気を上記1次燃
焼室内に接線方向で投入する複数個の投入孔を1次燃焼
室の側壁上部に設け、かつ上記1次燃焼室の頂部上に設
けた2次燃焼室に連らなる高温サイクロン内筒を1次燃
焼室内の上部に設けると共に、この高温サイクロン内筒
の下部をテーパ状に拡大したものである。
In order to solve the above problems, the present invention provides a slag tap type coal combustor having a vertical primary combustion chamber, in which coal and primary air are fed into the primary combustion chamber. A plurality of injection holes for tangential injection are provided in the upper side wall of the primary combustion chamber, and a high temperature cyclone inner cylinder connected to the secondary combustion chamber provided on the top of the primary combustion chamber is used for primary combustion. It is provided in the upper part of the room, and the lower part of the high temperature cyclone inner cylinder is enlarged in a tapered shape.

【0008】[0008]

【作用】上記の手段によれば、石炭と1次空気は1次燃
焼室内にその側壁上部から接線方向で投入されて、その
燃焼ガスは1次燃焼室の側壁と高温サイクロン内筒との
間を下向きに旋回しながら流れ、これにより、1次燃焼
室の側壁内面に沿うスラグの流下が促進されると共に、
石炭と1次空気のジェット流による流下スラグの切断、
飛散が防止される。
According to the above-mentioned means, the coal and the primary air are tangentially injected into the primary combustion chamber from the upper portion of the side wall thereof, and the combustion gas is generated between the sidewall of the primary combustion chamber and the high temperature cyclone inner cylinder. While swirling downward, which facilitates the flow of slag along the inner surface of the side wall of the primary combustion chamber,
Cutting down slag with coal and primary air jet stream,
Scattering is prevented.

【0009】そして、この下向きに旋回して流れる燃焼
ガスは、それから、高温サイクロン内筒下部のテーパ拡
大部によって1次燃焼室の側壁に衝突するように流れ、
スラグの衝突分離が行われる。その後、燃焼ガスは反転
して、高温サイクロン内筒に流入して2次燃焼室に流れ
るが、該反転により流速零の断面が形成されて、スラグ
の重力分離が十分に行われ、小粒径のスラグも確実に除
去されるので、燃焼ガスからスラグがほぼ完全に除去さ
れる。
The combustion gas that swirls downwards then flows so as to collide with the side wall of the primary combustion chamber by the taper expansion portion at the lower portion of the high temperature cyclone inner cylinder.
Collision separation of slag is performed. After that, the combustion gas is reversed and flows into the high temperature cyclone inner cylinder and flows into the secondary combustion chamber. By the reversal, a cross section with a zero flow velocity is formed, and gravity separation of the slag is sufficiently performed, and a small particle size is obtained. Since the slag of is also reliably removed, the slag is almost completely removed from the combustion gas.

【0010】[0010]

【実施例】以下図1〜図4を参照して、本発明の実施例
について詳細に説明する。図1は本発明に係るスラグタ
ップ式石炭燃焼器の一実施例を示す断面図、図2,図3
及び図4はそれぞれ図1のII−II線.III−II
I線及びIV−IV線に沿う断面図であり、図5〜図7
に示したものと同一の部分には同一の符号を付して、重
複する説明は省略する。
Embodiments of the present invention will be described in detail below with reference to FIGS. FIG. 1 is a sectional view showing an embodiment of a slag tap type coal combustor according to the present invention, FIG. 2 and FIG.
And FIG. 4 are respectively the lines II-II of FIG. III-II
It is sectional drawing which follows the I line and the IV-IV line, and is FIGS.
The same parts as those shown in are denoted by the same reference numerals, and overlapping description will be omitted.

【0011】図1〜図4において、石炭と1次空気1を
縦型の1次燃焼器2内に接線方向で投入する複数個(本
例では4個)の投入孔3は、従来によれば1次燃焼室2
の側壁4の下部に設けられていたが(図5参照)、本発
明によれば、1次燃焼室2の側壁4の上部に設けられて
いる。また、本発明によれば、1次燃焼室2の頂部上に
設けられている2次燃焼室7に連らなる高温サイクロン
内筒16が1次燃焼室2内の上部に設けられていると共
に、この高温サイクロン内筒16の下部17はテーパ状
に拡大されている。
1 to 4, a plurality of (4 in this example) charging holes 3 for charging coal and primary air 1 into a vertical type primary combustor 2 in a tangential direction are different from the conventional ones. If the primary combustion chamber 2
Although it was provided at the lower portion of the side wall 4 of the primary combustion chamber 2 (see FIG. 5), it is provided at the upper portion of the sidewall 4 of the primary combustion chamber 2 according to the present invention. Further, according to the present invention, the high temperature cyclone inner cylinder 16 connected to the secondary combustion chamber 7 provided on the top of the primary combustion chamber 2 is provided at the upper portion of the primary combustion chamber 2 as well. The lower portion 17 of the high temperature cyclone inner cylinder 16 is enlarged in a tapered shape.

【0012】このような構成によれば、石炭と1次空気
1は1次燃焼室2内にその側壁4の上部から接線方向で
投入されて、その燃焼ガス5は1次燃焼室2の側壁4と
高温サイクロン内筒16との間を下向きに旋回しながら
流れ、これにより、1次燃焼室2の側壁4の内面に沿う
スラグ6の流下が促進されると共に、石炭と1次空気1
のジェット流による流下スラグ6の切断、飛散が防止さ
れる。
According to this structure, the coal and the primary air 1 are introduced into the primary combustion chamber 2 from the upper portion of the side wall 4 in the tangential direction, and the combustion gas 5 thereof is the side wall of the primary combustion chamber 2. 4 and the high temperature cyclone inner cylinder 16 while swirling downward, which promotes the flow down of the slag 6 along the inner surface of the side wall 4 of the primary combustion chamber 2 and the coal and the primary air 1
The falling slag 6 is prevented from being cut and scattered by the jet flow of.

【0013】そして、この下向きに旋回して流れる燃焼
ガス5は、それから、高温サイクロン内筒16の下部の
テーパ拡大部17によって1次燃焼室2の側壁4に符号
5aで示すように衝突するように流れ、スラグ6の衝突
分離が行われる。その後、燃焼ガス5は符号5bで示す
ように反転して、高温サイクロン内筒16に流入して符
号5cで示すように2次燃焼室7に流れるが、該反転に
より流速零の断面が形成されて、スラグ6の重力分離が
十分に行われ、小粒径のスラグ6′も確実に除去される
ので、燃焼ガス5からスラグ6がほぼ完全に除去され、
これにより100%近くスラグが除去された燃焼ガス
(スラグがほとんどないことから、スラグフリー燃焼ガ
スと称することができる)5dとなって、2次燃焼室7
の排出口10から図示していないガスタービンやMHD
発電機等に供給される。
The combustion gas 5 swirling downwardly then collides with the side wall 4 of the primary combustion chamber 2 by the taper expanding portion 17 at the lower part of the high temperature cyclone inner cylinder 16 as indicated by reference numeral 5a. And the collision separation of the slag 6 is performed. After that, the combustion gas 5 is inverted as shown by the reference numeral 5b, flows into the high temperature cyclone inner cylinder 16 and flows into the secondary combustion chamber 7 as shown by the reference numeral 5c. As a result, the slag 6 is sufficiently separated by gravity, and the slag 6'having a small particle size is also surely removed, so that the slag 6 is almost completely removed from the combustion gas 5,
As a result, the combustion gas from which slag has been removed by almost 100% (which can be referred to as slag-free combustion gas because there is almost no slag) becomes 5d, and the secondary combustion chamber 7
From the exhaust port 10 of the gas turbine or MHD (not shown)
It is supplied to generators.

【0014】なお、高温サイクロン円筒16は、例えば
燃焼器及びサイクロン内筒冷却水18を投入する管19
をコイル状に形成し、その表面を断熱材で覆うことによ
り構成することができる。
The high-temperature cyclone cylinder 16 includes, for example, a pipe 19 for introducing a combustor and cyclone inner cylinder cooling water 18.
Can be formed into a coil shape and the surface thereof can be covered with a heat insulating material.

【0015】[0015]

【発明の効果】以上述べたように、本発明によれば、縦
型の1次燃焼室を備えるスラグタップ式石炭燃焼器にお
いて、石炭と1次空気の投入孔を1次燃焼室の側壁上部
に設けると共に、1次燃焼室内の上部に高温サイクロン
内筒を設けることによって、1次燃焼室の側壁を膜状と
なって下向きに流れるスラグの流下を促進する方向の下
向き旋回流を生じさせると共に、石炭と1次空気の投入
孔を1次燃焼室の側壁下部に設置していた時に生じてい
た流下スラグの、石炭と1次空気のジェット流による切
断、飛散を防止することが可能となる。そして、高温サ
イクロン内筒の設置にて生じる燃焼ガスの反転によっ
て、流速零断面での燃焼ガス中の小粒径スラグの重力分
離を可能とし、更に高温サイクロン内筒下部のテーパ拡
大部によって燃焼ガスの燃焼室側壁への衝突によるスラ
グの衝突分離を可能とし、全体として100%近いスラ
グ除去率の達成が可能となる。
As described above, according to the present invention, in a slag tap type coal combustor having a vertical type primary combustion chamber, the injection holes for coal and primary air are provided on the upper side wall of the primary combustion chamber. And a high temperature cyclone inner cylinder is provided in the upper part of the primary combustion chamber to generate a downward swirling flow in a direction that promotes the downward flow of the slag flowing downward in the form of a film on the side wall of the primary combustion chamber. , It is possible to prevent cutting and scattering of the falling slag generated by the injection flow of coal and primary air at the lower part of the side wall of the primary combustion chamber due to the jet flow of coal and primary air. . Then, by reversing the combustion gas generated by installing the high temperature cyclone inner cylinder, it is possible to gravity separate the small particle size slag in the combustion gas at the zero flow velocity cross section, and further the combustion gas is increased by the taper expansion part at the lower part of the high temperature cyclone inner cylinder. It is possible to separate the slag by collision with the side wall of the combustion chamber, and it is possible to achieve a slag removal rate close to 100% as a whole.

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

【図1】本発明に係るスラグタップ式石炭燃焼器の一実
施例を示す断面図である。
FIG. 1 is a sectional view showing an embodiment of a slag tap type coal combustor according to the present invention.

【図2】図1のII−II線断面図である。FIG. 2 is a sectional view taken along line II-II of FIG.

【図3】図1のIII−III線断面図である。FIG. 3 is a sectional view taken along line III-III in FIG.

【図4】図1のIV−IV線断面図である。FIG. 4 is a sectional view taken along line IV-IV in FIG.

【図5】従来のスラグタップ式石炭燃焼器を示す断面図
である。
FIG. 5 is a cross-sectional view showing a conventional slag tap type coal combustor.

【図6】図5のVI−VI線断面図である。6 is a sectional view taken along line VI-VI of FIG.

【図7】図5のVII−VII線断面図である。7 is a sectional view taken along line VII-VII in FIG.

【符号の説明】[Explanation of symbols]

1 石炭と1次空気 2 1次燃焼室 3 投入孔 4 側壁 5 燃焼ガス 6 スラグ 7 2次燃焼室 8 投入孔 9 2次空気 10 排出口 11 底部 12 スラグタップ孔 13 水だめ 14 水 15 スラグ取出口 16 高温サイクロン内筒 17 テーパ拡大部 18 冷却水 19 管 1 Coal and primary air 2 Primary combustion chamber 3 Input hole 4 Side wall 5 Combustion gas 6 Slag 7 Secondary combustion chamber 8 Input hole 9 Secondary air 10 Discharge port 11 Bottom 12 Slag tap hole 13 Sump 14 Water 15 Slag removal Outlet 16 High temperature cyclone inner cylinder 17 Taper expansion part 18 Cooling water 19 Pipe

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】縦型の1次燃焼室を備えるスラグタップ式
石炭燃焼器において、石炭と1次空気を上記1次燃焼室
内に接線方向で投入する複数個の投入孔を1次燃焼室の
側壁上部に設け、かつ上記1次燃焼室の頂部上に設けた
2次燃焼室に連らなる高温サイクロン内筒を1次燃焼室
内の上部に設けると共に、この高温サイクロン内筒の下
部をテーパ状に拡大したことを特徴とするスラグタップ
式石炭燃焼器。
1. A slag tap type coal combustor having a vertical type primary combustion chamber, wherein a plurality of injection holes for introducing coal and primary air into the primary combustion chamber in a tangential direction are provided in the primary combustion chamber. A high temperature cyclone inner cylinder connected to the secondary combustion chamber provided on the upper portion of the side wall and on the top of the primary combustion chamber is provided on the upper portion of the primary combustion chamber, and the lower portion of the high temperature cyclone inner cylinder is tapered. A slag tap type coal combustor characterized by being expanded to.
JP18758592A 1992-06-22 1992-06-22 Slag tap type coal combustion unit Withdrawn JPH062808A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18758592A JPH062808A (en) 1992-06-22 1992-06-22 Slag tap type coal combustion unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18758592A JPH062808A (en) 1992-06-22 1992-06-22 Slag tap type coal combustion unit

Publications (1)

Publication Number Publication Date
JPH062808A true JPH062808A (en) 1994-01-11

Family

ID=16208686

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18758592A Withdrawn JPH062808A (en) 1992-06-22 1992-06-22 Slag tap type coal combustion unit

Country Status (1)

Country Link
JP (1) JPH062808A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106642082A (en) * 2016-12-08 2017-05-10 哈尔滨工业大学 Small-sized cyclone-melting pulverized coal furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106642082A (en) * 2016-12-08 2017-05-10 哈尔滨工业大学 Small-sized cyclone-melting pulverized coal furnace
CN106642082B (en) * 2016-12-08 2019-04-09 哈尔滨工业大学 A kind of small cyclones melting coal-powder boiler

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