JPH0449006B2 - - Google Patents
Info
- Publication number
- JPH0449006B2 JPH0449006B2 JP14013888A JP14013888A JPH0449006B2 JP H0449006 B2 JPH0449006 B2 JP H0449006B2 JP 14013888 A JP14013888 A JP 14013888A JP 14013888 A JP14013888 A JP 14013888A JP H0449006 B2 JPH0449006 B2 JP H0449006B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion furnace
- partial combustion
- slag
- coal partial
- 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.)
- Expired
Links
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- Gasification And Melting Of Waste (AREA)
- Solid-Fuel Combustion (AREA)
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、一般産業用油焚きボイラの
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回石炭利用技術研究発表
会講演集がある。)
〔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 oil-fired boilers, and as shown in Figure 4, the cylindrical furnace 1
Combustion air and pulverized coal are input from the tangential duct 2, and are partially combusted in a short time by the preheating burner 3 while rotating at high speed. The aim is to combust the gas with less ash in the boiler combustion chamber 5 using air for two-stage combustion. (As a prior art document, there is, for example, the lecture collection of the 8th Coal Utilization Technology Research Conference.) [Problem to be solved by the invention] However, in the structure of the above coal partial combustion furnace,
Since there is a limit to the deashing rate, there is a desire for a coal partial combustion furnace that can improve the deashing rate.
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 reservoir is provided in the section, and a slag overflow port is provided on the inner peripheral wall of the slag reservoir 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 provided in the center of the upper surface of the vertical 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。 Further, it is preferable that the body extending from the lower end of the vertical coal partial combustion furnace is immersed in the drag chain conveyor 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
を廻つ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 with 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つ
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 a drag chain conveyor water tank is provided below the vertical coal partial combustion furnace, the slag flowing down from the overflow port is cooled and solidified in the water tank before being carried out by the 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図によつて説明すると、10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1
2a、2次空気を投入するノズル12bが交互に
四段スリツト状に設けられている。炉体11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1
5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
10の炉底よりも低い位置に環状のスラグ溜り1
6が設けられ、そのスラグ溜り16の内周壁16
aに前記横型石炭部分燃焼炉10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ツド
20の先端にカツター21を固設し、ロツド20
の基端を炉外に設置したシリンダー22のピスト
ンロツド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. 12 are provided. The duct 12 is a nozzle 1 that injects primary air and pulverized coal.
2a, nozzles 12b for injecting secondary air are provided alternately in a four-stage slit shape. A preheating burner 13 is provided at the center of one end face of the furnace body 11, and the outlet 14 side at the other end is narrowed down to form a vertical coal partial combustion furnace 1.
5 from the tangential direction. An annular slag reservoir 1 is located in 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 10.
6 is provided, and the inner peripheral wall 16 of the slag reservoir 16
A slag overflow port 17 is provided at a position on the horizontal coal partial combustion furnace 10 side. A slag cutting device 18 is provided below the slag overflow port 17. The slag cutting device 18 has a cutter 21 fixed at the tip of a rod 20 that slidably penetrates the furnace body 19 of the vertical coal partial combustion furnace 15.
The proximal end of the piston rod 23 is connected via a joint 24 to the tip of a piston rod 23 of a cylinder 22 installed outside the furnace. 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10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26が取付けられている。
また前記ガスダクト25も水冷壁構造となつてい
る。 The furnace body 11 of the horizontal coal partial combustion furnace 10 and the furnace body 19 of the vertical coal partial combustion furnace 15 both have a water-cooled wall structure, and a refractory material 26 is attached to the inner surface.
Further, the gas duct 25 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10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10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
つたつてスラグ溜り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。また横型石炭部
分燃焼炉10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16に
流下して、該スラグ溜り16を矢印の如く廻つ
て、内周壁16a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図の水層
29内の水中に没して冷却固化された上ドラグチ
エンコンベヤ28上に沈降堆積するので、第3図
の如くドラグチエンコンベヤ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1
6a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より垂れ下つて固化し
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、ピストンロツド23に連結されたロツド20
を前進摺動させて、先端に固設されたカツター2
1にて垂れ下つ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。 To explain the operation of the coal partial combustion furnace of the embodiment of the above structure, primary air and pulverized coal are blown into the horizontal coal partial combustion furnace 10 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 10, 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.
4 into the vertical partial coal combustion furnace 15 from the tangential direction as shown by the arrow in FIG. 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. Further, the slag melted in the horizontal coal partial combustion furnace 10 flows along the bottom of the furnace accompanied by the high-temperature gas, and flows into the vertical coal partial combustion furnace 15 from the narrowed outlet 14 in the tangential direction as shown by the arrow in FIG. The slag flows down to the slag pool 16 in the middle and high part, goes around the slag pool 16 as shown by the arrow, and reaches the slag overflow port 17 provided in the inner circumferential wall 16a.
flow further down. The slag that has flowed down is immersed in the water in the water layer 29 shown in FIG. 1, where it is cooled and solidified, and then settles and accumulates on the upper drag chain conveyor 28, so that it is carried out by the drive of the drag chain conveyor 28, as shown in FIG. 3. . The slag flowing down from the overflow port 17 solidifies and accumulates on the inner peripheral wall 1 of the slag reservoir 16.
Since the slag flow hole 16b surrounded by the slag flow hole 16b becomes narrower, the slag that hangs down from the slag overflow port 17 and becomes solidified is removed by the slag cutting device 18 shown in FIG.
Cut by. That is, the cylinder 22 is actuated and the rod 20 connected to the piston rod 23 is activated.
By sliding the cutter 2 forward, the cutter 2 fixed at the tip
At step 1, 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, Because it rotates,
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。
10……横型石炭部分燃焼炉、11……炉体、
12……ダクト、12a,12b……ノズル、1
8……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、16b……スラグ流下孔、17……ス
ラグ溢流口、18……スラグ切断装置、19……
炉体、20……ロツド、21……カツター、22
……カツター用エヤシリンダー、23……ピスト
ンロツド、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、29……水
槽(ドラグチエンコンベヤケーシング)。
FIG. 1 is a vertical sectional view showing an embodiment of the structure of a coal partial combustion furnace of the present invention, FIG. 2 is a cross-sectional view taken along the line A-A in FIG. 1, and FIG. 3 is a coal partial combustion furnace of the present invention. FIG. 4 is a cutaway perspective view of a conventional coal partial combustion furnace. 10... Horizontal coal partial combustion furnace, 11... Furnace body,
12...Duct, 12a, 12b...Nozzle, 1
8... Preheating burner, 14... Outlet, 15... Vertical coal partial combustion furnace, 16... Slag pool, 16a...
...Inner peripheral wall, 16b...Slag flow hole, 17...Slag overflow port, 18...Slag cutting device, 19...
Furnace body, 20... Rod, 21... Cutter, 22
... Air cylinder for cutter, 23 ... Piston rod, 24 ... Coupling, 25 ... Gas duct,
26... Refractory material, 27... Body extending downward, 28... Drag chain conveyor, 29... Water tank (drag chain conveyor casing).
Claims (1)
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
がドラグチエ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, and the slag A slag overflow port is provided on the inner peripheral wall of the basin at a position on the horizontal coal partial combustion furnace side, a slag cutting device is provided below the slag overflow port, and a gas duct is provided in the center of the upper surface of the vertical coal partial combustion furnace. The structure of a coal partial combustion furnace consisting of: 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 JPH01310202A (en) | 1989-12-14 |
| JPH0449006B2 true 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) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012247143A (en) * | 2011-05-28 | 2012-12-13 | Masayuki Ono | Natural air-intake combustion equipment |
-
1988
- 1988-06-07 JP JP14013888A patent/JPH01310202A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012247143A (en) * | 2011-05-28 | 2012-12-13 | Masayuki Ono | Natural air-intake combustion equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01310202A (en) | 1989-12-14 |
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| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |