JPH0443691Y2 - - Google Patents
Info
- Publication number
- JPH0443691Y2 JPH0443691Y2 JP1987146783U JP14678387U JPH0443691Y2 JP H0443691 Y2 JPH0443691 Y2 JP H0443691Y2 JP 1987146783 U JP1987146783 U JP 1987146783U JP 14678387 U JP14678387 U JP 14678387U JP H0443691 Y2 JPH0443691 Y2 JP H0443691Y2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- coal
- cyclone
- combustion chamber
- cyclone body
- 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
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は、ボイラ火炉などの工業炉を炉本体と
し、この炉本体の前炉として微粉炭、微粉オイル
コークスなどの固体燃料(以下、単に石炭とい
う)を燃焼用旋回空気により燃焼する、予燃焼室
を備えたサイクロン石炭燃焼装置に関するもので
ある。[Detailed explanation of the invention] [Field of industrial application] The present invention uses an industrial furnace such as a boiler furnace as a furnace body, and a solid fuel such as pulverized coal or pulverized oil coke (hereinafter simply referred to as This invention relates to a cyclone coal combustion device equipped with a pre-combustion chamber that burns coal (referred to as coal) using swirling air for combustion.
従来から、ボイラ火炉などの工業炉において
は、炉本体に前炉としてサイクロン石炭燃焼装置
を設けて石炭を部分燃焼させるようにしたものが
知られている。このような前炉を備えた工業炉
は、燃焼効果が優れたものであることから、広く
用いられている。
BACKGROUND ART Conventionally, industrial furnaces such as boiler furnaces have been known in which a cyclone coal combustion device is provided as a forehearth in the furnace body to partially burn coal. Industrial furnaces equipped with such forehearths are widely used because of their excellent combustion effects.
上記の従来型のサイクロン石炭燃焼装置の構造
を示すものとして、たとえば先に提案した実開昭
60−76717号公報に示されるように、微粉炭と空
気とをサイクロン石炭燃焼装置内に供給するとと
もに、これらを高速旋回流として効果的に混合し
て燃焼させることにより、微粉炭を部分燃焼させ
る構造のものが開示されている。すなわち、第3
図に示すように、ボイラ火炉などの火炉1の側壁
にサイクロン石炭燃焼装置2を横方向に取り付
け、このサイクロン石炭燃焼装置に石炭投入口
3、空気供給口4および燃焼ガスを火炉へ導くガ
ス導通口5を設け、サイクロン石炭燃焼装置2の
内部に、この装置2内で発生する燃焼ガスを通過
させ溶融スラグをせき止めるためのスラグバツフ
ル6を設けるとともに、スラグバツフルの燃焼ガ
ス上流側に下向きのスラグ流下口7を設けたサイ
クロン石炭燃焼装置が記載されている。8はスラ
グタンク、10は燃焼室、11はバイパスライ
ン、12は火炎である。 As an illustration of the structure of the conventional cyclone coal combustion equipment mentioned above, for example,
As shown in Publication No. 60-76717, pulverized coal is partially combusted by supplying pulverized coal and air into a cyclone coal combustion device and effectively mixing and combusting them as a high-speed swirling flow. structure is disclosed. That is, the third
As shown in the figure, a cyclone coal combustion device 2 is installed laterally on the side wall of a furnace 1 such as a boiler furnace, and this cyclone coal combustion device has a coal input port 3, an air supply port 4, and a gas conductor for guiding combustion gas to the furnace. A slag butthole 6 is provided inside the cyclone coal combustion device 2 for passing combustion gas generated in the device 2 and damming up molten slag, and a downward slag flow port is provided on the upstream side of the slag buttful for combustion gas. 7 is described. 8 is a slag tank, 10 is a combustion chamber, 11 is a bypass line, and 12 is a flame.
従来の横置型サイクロン石炭燃焼装置は、円筒
型でかつ石炭をサイクロン本体の上流側から軸流
方向に吹き込むか、または接線方向に吹き込み、
燃焼用旋回空気をサイクロン本体の上流側から接
線方向に吹き込むものであるので、サイクロン本
体内における旋回力が不十分であり、また燃焼ガ
スの流れも、石炭・空気吹込み部から下流出口に
向かつてほぼワンスルーで抜けるものであるの
で、滞留時間が短かく燃焼効率がそれ程向上せ
ず、またスラグ捕集率を上昇させるためには、ス
ラグバツフル、スラグスクリーンなどの二次捕集
手段が必要であつた。
Conventional horizontal cyclone coal combustion equipment is cylindrical and blows coal into the cyclone body from the upstream side in an axial direction or in a tangential direction.
Since swirling air for combustion is blown in tangentially from the upstream side of the cyclone body, the swirling force within the cyclone body is insufficient, and the flow of combustion gas is also directed from the coal/air injection section to the downstream outlet. In the past, the slag was passed through almost in one go, so the residence time was short and the combustion efficiency did not improve much, and in order to increase the slag collection rate, secondary collection means such as slag buttfuls and slag screens were required. Ta.
本考案は上記の諸点に鑑みなされたもので、サ
イクロン本体を略円筒型とし、このサイクロン本
体の大径部を火炉の側壁にガス導通口を介して取
り付けるとともに、サイクロン本体の大径部上面
に接線方向に竪型旋回下降流式の予燃焼室を接続
して、予燃焼室に石炭全量と二段燃焼用空気を除
く燃焼用空気全量とを供給して予燃焼し、高温の
燃焼ガスをサイクロン本体の下流端から供給し
て、継続燃焼させるとともに、逆進行の旋回流を
生ぜしめるように構成することにより、高燃焼効
率および高スラグ除去率が達成でき、かつスラグ
の二次捕集手段を設置する必要のないサイクロン
石炭燃焼装置を提供することを目的とするもので
ある。 The present invention was developed in view of the above points.The cyclone body is made into a substantially cylindrical shape, and the large diameter part of the cyclone body is attached to the side wall of the furnace through a gas communication port, and the large diameter part of the cyclone body is attached to the top surface of the large diameter part of the cyclone body. A vertical swirling downflow type pre-combustion chamber is connected in the tangential direction, and the entire amount of coal and the entire amount of combustion air excluding the second-stage combustion air is supplied to the pre-combustion chamber for pre-combustion, and high-temperature combustion gas is produced. High combustion efficiency and high slag removal rate can be achieved by supplying the cyclone from the downstream end of the cyclone body for continuous combustion and generating a reverse swirling flow. The purpose of this invention is to provide a cyclone coal combustion device that does not require the installation of a cyclone coal combustion device.
本考案のサイクロン石炭燃焼装置は、第1図お
よび第2図を参照して説明すれば、略円錐型のサ
イクロン本体15の大径部を、火炉1の側壁に横
方向にガス導通口5を介して取り付け、サイクロ
ン本体15の大径部上面に接線方向に竪型旋回下
降流式の予燃焼室16を接続し、サイクロン本体
15の下面にスラグ流下口7を設け、前記予燃焼
室16の上部に、燃焼に必要な石炭全量を供給す
るための石炭投入口および燃焼用旋回空気供給口
18を設け、前記ガス導通口5内において、予燃
焼室16とサイクロン本体15との接続部の下側
に、予燃焼室16からの旋回ガスをサイクロン本
体15の小径部へ導き、反転させてガス導通口5
へ導くためのバツフル20を設けたことを特徴と
している。
The cyclone coal combustion apparatus of the present invention will be described with reference to FIGS. 1 and 2. The large-diameter portion of the approximately conical cyclone body 15 is connected to the side wall of the furnace 1 with gas inlet 5 in the lateral direction. A vertical swirling downflow type pre-combustion chamber 16 is connected tangentially to the upper surface of the large diameter part of the cyclone main body 15, and a slag flow outlet 7 is provided on the lower surface of the cyclone main body 15. A coal input port for supplying the entire amount of coal necessary for combustion and a swirling air supply port 18 for combustion are provided in the upper part, and in the gas communication port 5, a portion below the connection between the pre-combustion chamber 16 and the cyclone body 15 is provided. On the side, the swirling gas from the pre-combustion chamber 16 is guided to the small diameter part of the cyclone body 15, and then reversed to the gas communication port 5.
It is characterized by the provision of a buttful 20 for guiding.
本考案において、燃焼用旋回空気は予燃焼室の
接線方向に供給する必要があるが、石炭は予燃焼
室の接線方向または軸流方向のいずれでもよい。 In the present invention, the swirling air for combustion needs to be supplied in the tangential direction of the pre-combustion chamber, but the coal may be supplied either in the tangential direction or in the axial direction of the pre-combustion chamber.
予燃焼室16に石炭全量および二段燃焼用空気
を除く燃焼用空気全量を供給し、旋回させながら
予め石炭を予燃焼させ、高温の燃焼ガスを作り出
し、この燃焼ガスをサイクロン本体15の下流端
から供給する。このためサイクロン本体内の壁近
傍を流れる着火石炭粒子および燃焼ガスが、より
強い遠心作用を受けて加速され、燃焼が促進され
るとともに、灰(スラグ)捕集率の向上が促され
る。
The entire amount of coal and the entire amount of combustion air excluding air for second-stage combustion are supplied to the pre-combustion chamber 16, and the coal is pre-combusted while swirling, producing high-temperature combustion gas, and this combustion gas is sent to the downstream end of the cyclone body 15. Supplied from. For this reason, the ignited coal particles and combustion gas flowing near the wall in the cyclone body are accelerated by stronger centrifugal action, promoting combustion and improving the ash (slag) collection rate.
またサイクロン本体内では、バツフル20を設
けたことにより、正逆進行の旋回流が相互に強く
現われ、サイクロン本体内において石炭粒子が十
分に拡散され、かつ石炭粒子のサイクロン本体内
滞留時間が増すことにより、燃焼効率が向上す
る。 In addition, by providing the Batsuful 20 within the cyclone body, the swirling flows of forward and reverse directions appear strongly, and the coal particles are sufficiently diffused within the cyclone body, and the residence time of the coal particles within the cyclone body is increased. This improves combustion efficiency.
以下、第1図および第2図を参照して本考案の
好適な実施例を詳細に説明する。ただしこの実施
例に記載されている構成機器の形状、その相対配
置などは、とくに特定的な記載がない限りは、本
考案の範囲をそれらのみに限定する趣旨のもので
はなく、単なる説明例にすぎない。
Hereinafter, a preferred embodiment of the present invention will be described in detail with reference to FIGS. 1 and 2. However, unless there is a specific description, the shapes of the components described in this example, their relative positions, etc. are not intended to limit the scope of the present invention, but are merely illustrative examples. Only.
15は略円錐型のサイクロン本体で、このサイ
クロン本体15の大径部を火炉1の側壁に横方向
に取り付ける。サイクロン本体15の大径部上面
に接線方向に、略円筒体の下部に略円錐体を連設
した竪型旋回下降流式の予燃焼室16を接続す
る。サイクロン本体15の下面の大径部にスラグ
流下口7を設け、予燃焼室16の上部に、石炭・
一次空気供給口17および燃焼用旋回空気(二次
空気)供給口18を設ける。なお石炭、一次空気
および二次空気を1つの供給口から接線方向に供
給することも可能である。またスラグ流下口7は
小径部に設けることも可能である。5はガス導通
口、10は燃焼室である。 Reference numeral 15 denotes a substantially conical cyclone body, and the large diameter portion of this cyclone body 15 is laterally attached to the side wall of the furnace 1. A vertical swirling downward flow type pre-combustion chamber 16 is connected tangentially to the upper surface of the large diameter portion of the cyclone body 15, which is a substantially cylindrical body with a substantially conical body connected to the lower part thereof. A slag outlet 7 is provided in the large-diameter portion of the lower surface of the cyclone body 15, and coal and
A primary air supply port 17 and a combustion swirling air (secondary air) supply port 18 are provided. It is also possible to supply coal, primary air and secondary air tangentially from one supply port. Further, the slag outlet 7 can also be provided in a small diameter portion. 5 is a gas communication port, and 10 is a combustion chamber.
ガス導通口5内において、予燃焼室16とサイ
クロン本体15との接続部の下側に、予燃焼室1
6からの旋回ガスをサイクロン本体15の小径部
へ導き、反転させてガス導通口5へ導くためのバ
ツフル20が設けられている。 The pre-combustion chamber 1 is located below the connection between the pre-combustion chamber 16 and the cyclone body 15 in the gas communication port 5.
A baffle 20 is provided for guiding the swirling gas from the cyclone body 15 to the small diameter portion of the cyclone body 15, inverting it, and guiding it to the gas communication port 5.
上記のように構成されたサイクロン石炭燃焼装
置おいて、予燃焼室16に微粉炭、一次空気およ
び旋回二次空気を供給して予め微粉体を予燃焼室
内の壁面、火炎およびサイクロン本体からの熱に
より着火させて予燃焼させ、高温の燃焼ガスを作
り出し、この燃焼ガスをサイクロン本体15の下
流端から接線方向に導き、継続燃焼させるととも
に、逆進行旋回流を生ぜしめる。 In the cyclone coal combustion apparatus configured as described above, pulverized coal, primary air and swirling secondary air are supplied to the pre-combustion chamber 16, and the pulverized powder is absorbed from the heat from the wall surface of the pre-combustion chamber, the flame and the cyclone body. The cyclone body 15 is ignited and pre-combusted to produce high-temperature combustion gas, which is guided tangentially from the downstream end of the cyclone body 15 to continue combustion and generate a reverse swirling flow.
高温の燃焼ガスとともに、石炭の未燃部分や灰
の一部がサイクロン本体15内に導入され、小径
部の狭い空間内に流入するので、より強い遠心力
を受けて加速され、燃焼が促進されるとともにス
ラグが効率よく捕集される。さらに燃焼ガスは、
バツフル20により、サイクロン本体15内を反
転して往復するので、石炭粒子の滞留時間が長く
なり、効率よく再燃焼し、灰除去率が向上し、未
燃分が低下する。 Along with the high-temperature combustion gas, the unburned portion of the coal and a portion of the ash are introduced into the cyclone body 15 and flow into the narrow space of the small diameter section, so they are accelerated by stronger centrifugal force and combustion is promoted. At the same time, slag is efficiently collected. Furthermore, the combustion gas
Since the baffle 20 reverses and reciprocates within the cyclone body 15, the residence time of the coal particles becomes longer, the coal particles are efficiently reburned, the ash removal rate is improved, and the amount of unburned particles is reduced.
本考案のサイクロン石炭燃焼装置は上記のよう
に、予燃焼室で予め高温の燃焼ガスを作り出した
後、この燃焼ガスをサイクロン本体の下流端から
接線方向に供給して継続燃焼するように構成され
ているので、燃焼効率が向上し、さらにサイクロ
ン本体は略円錐型になつているので、燃焼ガスの
旋回数が増えて旋回力が強くなり、かつ燃焼ガス
が、バツフルを設けたことにより、反転して往復
するので滞留時間が長くなり、このためスラグの
二次捕集手段を設けることなく、高スラグ除去
率、高燃焼効率を達成することができるという効
果を有している。また燃焼に必要な石炭の全量を
予燃焼室に投入するので、分岐投入が不要とな
り、装置を簡略化することができるという効果が
ある。
As described above, the cyclone coal combustion device of the present invention is configured to generate high-temperature combustion gas in advance in the pre-combustion chamber, and then supply this combustion gas tangentially from the downstream end of the cyclone body for continuous combustion. This improves combustion efficiency, and since the cyclone body is approximately conical, the number of turns of the combustion gas increases, increasing the swirling force. Since the slag is reciprocated, the residence time becomes longer, and this has the effect that a high slag removal rate and high combustion efficiency can be achieved without providing a secondary slag collection means. In addition, since the entire amount of coal required for combustion is charged into the pre-combustion chamber, there is no need to divide the coal into the pre-combustion chamber, thereby simplifying the apparatus.
第1図は本考案のサイクロン石炭燃焼装置の一
実施例を示す断面説明図、第2図は第1図におけ
る−線断面説明図、第3図は従来のサイクロ
ン石炭燃焼装置の一例を示す断面説明図である。
1……火炉、2……サイクロン石炭燃焼装置、
3……石炭投入口、4……空気供給口、5……ガ
ス導通口、6……スラグバツフル、7……スラグ
流下口、8……スラグタンク、10……燃焼室、
11……バイパスライン、12……火炎、15…
…サイクロン本体、16……予燃焼室、17……
石炭・一次空気供給口、18……燃焼用旋回空気
供給口、20……バツフル。
Fig. 1 is an explanatory cross-sectional view showing one embodiment of the cyclone coal combustion device of the present invention, Fig. 2 is an explanatory cross-sectional view taken along the line - in Fig. 1, and Fig. 3 is a cross-sectional view showing an example of the conventional cyclone coal combustion device. It is an explanatory diagram. 1... Furnace, 2... Cyclone coal combustion device,
3...Coal input port, 4...Air supply port, 5...Gas communication port, 6...Slag buttful, 7...Slag outlet, 8...Slag tank, 10...Combustion chamber,
11... Bypass line, 12... Flame, 15...
...Cyclone body, 16... Pre-combustion chamber, 17...
Coal/primary air supply port, 18... Combustion swirling air supply port, 20... Batsuful.
Claims (1)
炉1の側壁に横方向にガス導通口5を介して取り
付け、サイクロン本体15の大径部上面に接線方
向に竪型旋回下降流式の予燃焼室16を接続し、
サイクロン本体15の下面にスラグ流下口7を設
け、前記予燃焼室16の上部に、燃焼に必要な石
炭全量を供給するための石炭投入口および燃焼用
旋回空気供給口18を設け、前記ガス導通口5内
において、予燃焼室16とサイクロン本体15と
の接続部の下側に、予燃焼室16からの旋回ガス
をサイクロン本体15の小径部へ導き、反転させ
てガス導通口5へ導くためのバツフル20を設け
たことを特徴とするサイクロン石炭燃焼装置。 The large diameter portion of the approximately conical cyclone body 15 is attached to the side wall of the furnace 1 laterally through the gas inlet 5, and a vertical swirling downward flow type pre-arrangement is tangentially attached to the upper surface of the large diameter portion of the cyclone body 15. Connect the combustion chamber 16,
A slag flow outlet 7 is provided on the lower surface of the cyclone main body 15, and a coal input port for supplying the entire amount of coal necessary for combustion and a swirling air supply port 18 for combustion are provided in the upper part of the pre-combustion chamber 16. Inside the opening 5, a groove is provided below the connection between the pre-combustion chamber 16 and the cyclone body 15 in order to guide the swirling gas from the pre-combustion chamber 16 to the small diameter part of the cyclone body 15, reverse it, and guide it to the gas communication port 5. A cyclone coal combustion device characterized by being provided with a full 20.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1987146783U JPH0443691Y2 (en) | 1987-09-25 | 1987-09-25 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1987146783U JPH0443691Y2 (en) | 1987-09-25 | 1987-09-25 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6454611U JPS6454611U (en) | 1989-04-04 |
| JPH0443691Y2 true JPH0443691Y2 (en) | 1992-10-15 |
Family
ID=31416592
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1987146783U Expired JPH0443691Y2 (en) | 1987-09-25 | 1987-09-25 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0443691Y2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0833190B2 (en) * | 1987-01-12 | 1996-03-29 | 月島機械株式会社 | Swirl melting furnace |
-
1987
- 1987-09-25 JP JP1987146783U patent/JPH0443691Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6454611U (en) | 1989-04-04 |
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