JPH01310202A - Construction of furnace for partial combustion of coal - Google Patents
Construction of furnace for partial combustion of coalInfo
- Publication number
- JPH01310202A JPH01310202A JP14013888A JP14013888A JPH01310202A JP H01310202 A JPH01310202 A JP H01310202A JP 14013888 A JP14013888 A JP 14013888A JP 14013888 A JP14013888 A JP 14013888A JP H01310202 A JPH01310202 A JP H01310202A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- partial combustion
- slag
- coal
- combustion furnace
- 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.)
- Granted
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
- Solid-Fuel Combustion (AREA)
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、石炭部分燃焼炉の構造に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to the structure of a coal partial combustion furnace.
石炭部分燃焼炉は、一般産業珀浦焚きボイラの燃料転換
(重油−石炭)を目的に開発が進められているもので、
第4図に示す如く円筒状の炉1に、接線方向のダクト2
から燃焼用空気と微粉炭を投入し、高速旋回させ乍ら予
熱バーナ3により短時間に部分燃焼させ、投入した微粉
炭の灰を炉底の排出口4より溶融灰として排出し、灰の
少ないガスをボイラ燃焼室5内で2段燃焼用の空気によ
り燃焼させようとするものである。(先行技術文献とし
て、例えば第8凹
演集がある。)
〔発明が解決しようとする課題〕
然し乍ら、上記の石炭部分燃焼炉の構造では、脱灰率に
限界があるので、脱灰率の向上を図ることのできる石炭
部分燃焼炉の出現が望まれている。The coal partial combustion furnace is being developed for the purpose of fuel conversion (heavy oil - coal) for general industrial Kahura-fired boilers.
As shown in Fig. 4, a tangential duct 2 is connected to a cylindrical furnace 1.
Combustion air and pulverized coal are input from the furnace, and while they are swirled at high speed, they are partially combusted in a short time by the preheating burner 3, and the ash of the input pulverized coal is discharged as molten ash from the outlet 4 at the bottom of the furnace, resulting in less ash. The purpose is to combust gas in the boiler combustion chamber 5 using air for two-stage combustion. (As a prior art document, there is, for example, the 8th Concave Collection.) [Problems to be Solved by the Invention] However, in the structure of the above-mentioned coal partial combustion furnace, there is a limit to the deashing rate. It is hoped that a coal partial combustion furnace will be developed that can improve the performance.
本発明は上記実情に鑑みなされたもので、脱灰率の向上
を図ることができると共に、ガスとスラグを良好に分離
できる石炭部分燃焼炉の構造を提供することを目的とす
るものである。The present invention was made in view of the above circumstances, and an object of the present invention is to provide a structure of a coal partial combustion furnace that can improve the deashing rate and can satisfactorily separate gas and slag.
上記課題を解決するための本発明の石炭部分燃焼炉の構
造は、横型石炭部分燃焼炉の出口側を絞り込んで縦型石
炭部分燃焼炉に接線方向から接続し、縦型石炭部分燃焼
炉の中高部に環状のスラグ溜りを設け、そのスラグ溜り
の内周壁に前記横型石炭部分燃焼炉側の位置でスラグ溢
流口を設け、そのスラグ溢流口の下側にスラグ切断装置
を設け、縦型石炭部分燃焼炉の上面中央にガスダクトを
設けて成るものである。The structure of the coal partial combustion furnace of the present invention for solving the above problems is such that the outlet side of the horizontal coal partial combustion furnace is narrowed down and connected to the vertical coal partial combustion furnace from the tangential direction. An annular slag pool is provided in the section, a slag overflow port is provided on the inner circumferential wall of the slag pool at a position on the side of the horizontal coal partial combustion furnace, and a slag cutting device is provided below the slag overflow port. A gas duct is installed in the center of the upper surface of a coal partial combustion furnace.
前記横型石炭部分燃焼炉及び縦型石炭部分燃焼炉の炉体
は、共に水冷壁構造で、内面に耐火材が取付けられてい
ることが好ましい。It is preferable that the furnace bodies of the horizontal coal partial combustion furnace and the vertical coal partial combustion furnace both have a water-cooled wall structure, and a refractory material is attached to the inner surface.
また前記ガスダクトは、水冷壁構造であることが好まし
い。Further, it is preferable that the gas duct has a water-cooled wall structure.
さらに縦型石炭部分燃焼炉の下端に延設された胴部は、
ドラグチエンコンベヤ水槽に浸漬されていることが好ま
しい。Furthermore, the body extending to the lower end of the vertical coal partial combustion furnace is
It is preferable that the drag chain conveyor is immersed in a water tank.
上述の如く構成された本発明の石炭部分燃焼炉によると
、横型石炭部分燃焼炉で高速旋回し乍ら部分燃焼して得
た高温ガスは絞り込まれた出口より縦型石炭部分燃焼炉
に接線方向より高速で吹き込まれ、大きな旋回力で旋回
し乍ら上面中央のガスダクトより流出する。また横型石
炭部分燃焼炉で溶融したスラグは前記高温ガスに伴われ
て炉底を流動し、絞り込まれた出口より縦型石炭部分燃
焼炉に接線方向より流入し、中高部のスラグ溜りを廻っ
て内周壁に設けられた溢流口より流下する。According to the coal partial combustion furnace of the present invention configured as described above, the high temperature gas obtained by partial combustion while rotating at high speed in the horizontal coal partial combustion furnace is tangentially transferred to the vertical coal partial combustion furnace from the narrowed outlet. It is blown in at a higher speed and flows out from the gas duct in the center of the upper surface while rotating with a large swirling force. In addition, the slag melted in the horizontal coal partial combustion furnace flows along the bottom of the furnace accompanied by the high-temperature gas, flows tangentially into the vertical coal partial combustion furnace from the narrowed outlet, and circulates around the slag pool in the middle and high part. It flows down from the overflow port provided on the inner peripheral wall.
溢流口より流下するスラグが固化した場合には、スラグ
切断装置により切断落下せしめられる。When the slag flowing down from the overflow port solidifies, it is cut and dropped by a slag cutting device.
溢流口より流下したスラグは、縦型石炭部分燃焼炉の下
方にドラグチエンコンベヤ水槽が備わっている場合は、
水槽で冷却固化された上、ドラグチエンコンベヤにより
搬出される。If the vertical coal partial combustion furnace is equipped with a drag chain conveyor water tank, the slag flowing down from the overflow port will be
After being cooled and solidified in a water tank, it is transported out by a drag chain conveyor.
本発明による石炭部分燃焼炉の構造の一実施例を第1図
及び第2図によって説明すると、1oは横型石炭部分燃
焼炉で、円筒状の炉体11の一端側の接線方向にダクト
12が設けられている。ダクト12は1次空気と微粉炭
を投入するノズル12a、2次空気を投入するノズル1
2bが交互に四段スリット状に設けられている。炉体1
1の一端面中央には予熱バーナ13が設けられ、他端の
出口14側は絞り込まれて縦型石炭部分燃焼炉15に接
線方向から接続されている。縦型石炭部分燃焼炉15内
の中高部の前記横型石炭部分燃焼炉IOの炉底よりも低
い位置に環状のスラグ溜り16が設けられ、そのスラグ
溜り16の内周壁leaに前記横型石炭部分燃焼炉IO
側の位置でスラグ溢流口17が設けられている。このス
ラグ溢流口17の下側にはスラグ切断装置18が設けら
れている。スラグ切断装置18は、縦型石炭部分燃焼炉
15の炉体19を摺動可能に貫通したロッド20の先端
にカッター21を固設し、ロッド20の基端を炉外に設
置したシリンダー22のピストンロッド23の先端に継
手24を介して連結して成るものである。縦型石炭部分
燃焼炉15の上面中央にはガスダクト25がその基端が
貫通接続されて設けられている。An embodiment of the structure of a coal partial combustion furnace according to the present invention will be described with reference to FIGS. 1 and 2. 1o is a horizontal coal partial combustion furnace, and a duct 12 is installed in the tangential direction of one end side of a cylindrical furnace body 11. It is provided. The duct 12 has a nozzle 12a that inputs primary air and pulverized coal, and a nozzle 1 that inputs secondary air.
2b are provided alternately in a four-stage slit shape. Furnace body 1
A preheating burner 13 is provided at the center of one end surface of the fuel cell 1, and the outlet 14 side of the other end is narrowed and connected tangentially to a vertical coal partial combustion furnace 15. An annular slag sump 16 is provided at a middle and high part of the vertical coal partial combustion furnace 15 at a position lower than the bottom of the horizontal coal partial combustion furnace IO. Furnace IO
A slag overflow port 17 is provided at a side position. A slag cutting device 18 is provided below the slag overflow port 17. The slag cutting device 18 has a cutter 21 fixed to the tip of a rod 20 that slidably penetrates the furnace body 19 of the vertical coal partial combustion furnace 15, and a cylinder 22 with the base end of the rod 20 installed outside the furnace. It is connected to the tip of the piston rod 23 via a joint 24. A gas duct 25 is provided at the center of the upper surface of the vertical coal partial combustion furnace 15, with its base end being connected through the gas duct 25.
前記横型石炭部分燃焼炉lOの炉体11及び縦型石炭部
分燃焼炉15の炉体19は、共に水冷壁構造で、内面に
耐火材2Bが取付けられている。また前記ガスダクト2
5も水冷壁構造となっている。The furnace body 11 of the horizontal coal partial combustion furnace IO and the furnace body 19 of the vertical coal partial combustion furnace 15 both have a water-cooled wall structure, and a refractory material 2B is attached to the inner surface. In addition, the gas duct 2
5 also has a water-cooled wall structure.
縦型石炭部分燃焼炉15の下端に延設された胴部27は
、第3図に示す如くドラグチエンコンベヤ28を有する
水槽(ドラグチエンコンベヤケーシング)29に浸漬さ
れ、ドラグチエンコンベヤ28がスラグの流下位置に位
置している。The body 27 extending from the lower end of the vertical coal partial combustion furnace 15 is immersed in a water tank (drag chain conveyor casing) 29 having a drag chain conveyor 28, as shown in FIG. It is located downstream.
上記構造の実施例の石炭部分燃焼炉の運転について説明
すると、横型石炭部分燃焼炉IOに、接線方向のダクト
12のノズル12aから1次空気と微粉炭が吹き込まれ
、ノズル12bから2次空気が吹き込まれ、高速旋回し
乍ら、起動時に予熱バーナ13により昇熱されている横
型石炭部分燃焼炉IO内で部分燃焼せしめられる。この
部分燃焼により発生した高温ガスは絞り込まれた出口1
4より縦型石炭部分燃焼炉15に第2図の矢印の如く接
線方向より高速で吹き込まれ、高温ガス中の溶融スラグ
のミストは周壁に当り耐火材26にったってスラグ溜り
16に入り、スラグミストの少ないガスは大きな旋回力
で旋回し乍ら上面中央のガスダクト25より流出する。To explain the operation of the coal partial combustion furnace of the embodiment with the above structure, primary air and pulverized coal are blown into the horizontal coal partial combustion furnace IO from the nozzle 12a of the duct 12 in the tangential direction, and secondary air is blown from the nozzle 12b. The coal is blown in, and while rotating at high speed, it is partially combusted in the horizontal coal partial combustion furnace IO, which is heated by the preheating burner 13 at the time of startup. The high temperature gas generated by this partial combustion is narrowed down to the outlet 1.
The molten slag mist in the high-temperature gas hits the peripheral wall, runs along the refractory material 26, enters the slag pool 16, and slag The gas with less mist flows out from the gas duct 25 at the center of the upper surface while swirling with a large swirling force.
また横型石炭部分燃焼炉IOで溶融したスラグは前記高
温ガスに伴われて炉底を流動し、絞り込まれた出口14
より縦型石炭部分燃焼炉15に第2図の矢印の如く接線
方向より流入し、中高部のスラグ溜り1Gに流下して、
該スラグ溜り16を矢印の如く廻って、内周壁18aに
設けられたスラグ溢流口17より流下する。流下したス
ラグは、第1図グチエンコンベヤ28の駆動により搬出
される。溢流口17より流下するスラグは固化すると堆
積して次第にスラグ溜り16の内周壁leaに囲まれた
スラグ流下孔16bが狭くなるので、適宜スラグ溢流口
17より垂れ下って固化したスラグを第1図に示される
スラグ切断装置18により切断する。即ち、シリンダー
22を作動し、ピストンロッド23に連結されたロッド
20を前進摺動させて、先端に固設されたカッター21
にて垂れ下って固化したスラグを切断して水槽29中の
ドラグチエンコンベヤ28上に落下させる。Further, the slag melted in the horizontal coal partial combustion furnace IO flows through the bottom of the furnace accompanied by the high temperature gas, and flows through the narrowed outlet 14.
The slag flows into the vertical coal partial combustion furnace 15 from the tangential direction as shown by the arrow in FIG.
The slag flows around the slag pool 16 as shown by the arrow and flows down from the slag overflow port 17 provided on the inner circumferential wall 18a. The slag that has flowed down is carried out by driving the groove conveyor 28 in FIG. When the slag flowing down from the overflow port 17 solidifies, it accumulates and the slag flow hole 16b surrounded by the inner circumferential wall lea of the slag reservoir 16 becomes narrower. The slag is cut by a slag cutting device 18 shown in FIG. That is, the cylinder 22 is operated, the rod 20 connected to the piston rod 23 is slid forward, and the cutter 21 fixed at the tip is moved forward.
The hanging and solidified slag is cut and dropped onto a drag chain conveyor 28 in a water tank 29.
以上の説明で判るように本発明の石炭部分燃焼炉の構造
によれば、横型石炭部分燃焼炉で発生した高温ガスと溶
融スラグが、縦型石炭部分燃焼炉へ接線方向から高速で
投入され、旋回するので、脱灰率が向上する。また溶融
スラグは、縦型石炭部分燃焼炉のスラグ溜りに集められ
、高温ガスの流れとは逆の重力方向にスラグ溢流口より
流下せしめられるので、高温ガスと溶融スラグを良好に
分離できる。As can be seen from the above explanation, according to the structure of the coal partial combustion furnace of the present invention, the high temperature gas and molten slag generated in the horizontal coal partial combustion furnace are fed into the vertical coal partial combustion furnace from a tangential direction at high speed, Since it rotates, the demineralization rate improves. Further, the molten slag is collected in the slag pool of the vertical coal partial combustion furnace and is allowed to flow down from the slag overflow port in the direction of gravity opposite to the flow of the high-temperature gas, so that the high-temperature gas and the molten slag can be separated well.
第1図は本発明の石炭部分燃焼炉の構造の一実施例を示
す縦断面図、第2図は第1図のA−A断面矢視図、第3
図は本発明の石炭部分燃焼炉の全体組立図、第4図は従
来の石炭部分燃焼炉の破断斜視図である。
lO・・・横型石炭部分燃焼炉 11・・・炉 体12
・・・ダクト 12a 、 12b・・・
ノズル13・・・予熱バーナ 14・・・出口
15・・・縦型石炭部分燃焼炉 16・・・スラグ溜り
16a・・・内周壁 113b・・・スラグ
流下孔17・・・スラグ溢流口 18・・・スラ
グ切断装置I9・・・炉 体 20・・・ロ
ッド21・・・カッター
22・・・カッター用エヤシリンダー
23・・・ピストンロッド 24・・・継 手25
・・・ガスダクト 26・・・耐火材27・・
・下方に延設された胴部
28・・・ドラグチエンコンベヤFIG. 1 is a longitudinal cross-sectional view showing an embodiment of the structure of a coal partial combustion furnace of the present invention, FIG.
The figure is an overall assembly diagram of a coal partial combustion furnace of the present invention, and FIG. 4 is a cutaway perspective view of a conventional coal partial combustion furnace. lO...Horizontal coal partial combustion furnace 11...Furnace body 12
...Ducts 12a, 12b...
Nozzle 13...Preheating burner 14...Outlet 15...Vertical coal partial combustion furnace 16...Slag reservoir 16a...Inner peripheral wall 113b...Slag flow hole 17...Slag overflow port 18 ... Slag cutting device I9 ... Furnace body 20 ... Rod 21 ... Cutter 22 ... Cutter air cylinder 23 ... Piston rod 24 ... Joint 25
...Gas duct 26...Fireproof material 27...
・Bottom section 28 extending downward...drag chain conveyor
Claims (1)
部分燃焼炉に接線方向から接続し、縦型石炭部分燃焼炉
の中高部に環状のスラグ溜りを設け、そのスラグ溜りの
内周壁に前記横型石炭部分燃焼炉側の位置でスラグ溢流
口を設け、そのスラグ溢流口の下側にスラグ切断装置を
設け、縦型石炭部分燃焼炉の上面中央にガスダクトを設
けて成る石炭部分燃焼炉の構造。 2)縦型石炭部分燃焼炉の下端に延設された胴部がドラ
グチェンコンベヤ水槽に浸漬されていることを特徴とす
る請求項1記載の石炭部分燃焼炉の構造。[Claims] 1) The outlet side of the horizontal coal partial combustion furnace is narrowed down and connected to the vertical coal partial combustion furnace from the tangential direction, and an annular slag reservoir is provided in the middle and high part of the vertical coal partial combustion furnace. A slag overflow port is provided on the inner peripheral wall of the slag basin at a position on the side of the horizontal coal partial combustion furnace, a slag cutting device is provided below the slag overflow port, and a gas duct is installed in the center of the upper surface of the vertical coal partial combustion furnace. Structure of a coal partial combustion furnace. 2) The structure of a coal partial combustion furnace according to claim 1, wherein the body extending from the lower end of the vertical coal partial combustion furnace is immersed in a drag chain conveyor water tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14013888A JPH01310202A (en) | 1988-06-07 | 1988-06-07 | Construction of furnace for partial combustion of coal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14013888A JPH01310202A (en) | 1988-06-07 | 1988-06-07 | Construction of furnace for partial combustion of coal |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01310202A true JPH01310202A (en) | 1989-12-14 |
| JPH0449006B2 JPH0449006B2 (en) | 1992-08-10 |
Family
ID=15261764
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14013888A Granted JPH01310202A (en) | 1988-06-07 | 1988-06-07 | Construction of furnace for partial combustion of coal |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01310202A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5783362B2 (en) * | 2011-05-28 | 2015-09-24 | 正行 大野 | Natural intake combustion equipment |
-
1988
- 1988-06-07 JP JP14013888A patent/JPH01310202A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0449006B2 (en) | 1992-08-10 |
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