JPH024103A - Particle quantity control method inside fluidized bed boiler - Google Patents
Particle quantity control method inside fluidized bed boilerInfo
- Publication number
- JPH024103A JPH024103A JP15216888A JP15216888A JPH024103A JP H024103 A JPH024103 A JP H024103A JP 15216888 A JP15216888 A JP 15216888A JP 15216888 A JP15216888 A JP 15216888A JP H024103 A JPH024103 A JP H024103A
- Authority
- JP
- Japan
- Prior art keywords
- cyclone
- particles
- level
- gas
- fluidized bed
- 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.)
- Pending
Links
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、粒子貯槽内の粒子のレベルを簡単に調整でき
る流動層ボイラ内粒子量調節方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for adjusting the amount of particles in a fluidized bed boiler, which allows the level of particles in a particle storage tank to be easily adjusted.
第2図に示す如く、従来の流動層ボイラは、供給管3か
ら燃焼室1に燃料a及び補給固形物すを投入すると共に
流動層ノズル2から空気Cを導入して燃焼を行ない、そ
の燃焼ガスd及び粒子eを通路4を経てサイクロン5に
導入し、当該サイクロン5にて燃焼ガスdと粒子eとの
分離を行なっている。As shown in FIG. 2, in the conventional fluidized bed boiler, fuel a and supplementary solid matter are introduced into the combustion chamber 1 from the supply pipe 3, and air C is introduced from the fluidized bed nozzle 2 to perform combustion. Gas d and particles e are introduced into a cyclone 5 through a passage 4, and the cyclone 5 separates the combustion gas d and particles e.
このサイクロン5で分離された燃焼ガスdはサイクロン
出口9及び通路10を経て集塵器11に流入し、この集
塵器11にて燃焼ガスd中の微粒子e′をさらに分離し
たあと、微粒子e“のみを微粒子排出口13から排出し
、微粒子e。The combustion gas d separated by the cyclone 5 flows into the dust collector 11 through the cyclone outlet 9 and the passage 10, and the dust collector 11 further separates the fine particles e' in the combustion gas d. "Only the particulate matter e is discharged from the particulate discharge port 13, and the particulate matter e.
を除いた燃焼ガスdを通路12から放出している。The combustion gas d except for the combustion gas d is released from the passage 12.
一方、サイクロン5で分離された粒子eはサイクロン5
の下部のサイクロン粒子排出口6を通って粒子貯槽7内
に貯留されたあと、通路8を経て前記燃焼室1内に戻さ
れる。On the other hand, particles e separated by cyclone 5 are
After passing through a cyclone particle outlet 6 at the bottom of the cyclone particle outlet 6 and being stored in a particle storage tank 7, the particles are returned to the combustion chamber 1 through a passage 8.
この流動層ボイラでは、前記燃焼室1に投入される燃料
a及び補給固形物すと、サイクロン出口9から排出され
る燃焼ガスd及び微粒子e′とのバランスにより粒子貯
槽7内の粒子eのレベルLは上昇したり下降したりする
ため、従来は下部排出口14又は上部排出口15より粒
子eを抜き出したり、燃焼室1に投入する補給固彫物す
を増加することにより粒子貯槽7内の粒子eのレベルL
を調整している。In this fluidized bed boiler, the level of particles e in the particle storage tank 7 is determined by the balance between the fuel a and the supplementary solids introduced into the combustion chamber 1, and the combustion gas d and particulates e' discharged from the cyclone outlet 9. Since L rises and falls, conventionally, the particles in the particle storage tank 7 are removed by extracting the particles e from the lower discharge port 14 or the upper discharge port 15, or by increasing the number of replenishing solid particles fed into the combustion chamber 1. level L of e
are being adjusted.
ところで、微粒子排出口13から排出される微粒子e″
は粒子の粒が非常に小さいから取扱い及び処理が容易で
あり、かつ、利用価値があるのに対し、上部排出口15
や下部排出口14からの排出物の中には粗粒子も混入し
、取扱い及び処理が難かしく、その利用も困難である。By the way, the particulates e″ discharged from the particulate discharge port 13
Since the particles are very small, they are easy to handle and process, and have utility value, whereas the upper discharge port 15
Also, coarse particles are mixed in the discharge from the lower discharge port 14, making it difficult to handle and dispose of, and also difficult to utilize.
しかも、粒子eのレベルLが下る時は補給固形物すを不
必要に多く補給する必要があり、不経済であった。Furthermore, when the level L of particles e drops, it is necessary to replenish an unnecessarily large amount of replenishing solid material, which is uneconomical.
本発明は、上記の如き、従来の問題点を解消するために
なされたものであり、粒子貯槽内の粒子のレベルを節単
に調整できる流動層ボイラ内の粒子量を調節する方法を
提供することを目的としたものである。The present invention has been made in order to solve the conventional problems as described above, and provides a method for adjusting the amount of particles in a fluidized bed boiler that can easily adjust the level of particles in a particle storage tank. The purpose is to
上記目的を達成できる本発明の流動層ボイラ内粒子量調
節方法は、流動層ボイラ内の粒子量を調節するに際し、
燃焼ガスと粒子とを分離するサイクロンの下部に、当該
サイクロンの分離性能を調節する空気又はガスを導入す
ることを特徴とすることを特徴とするものである。The method for adjusting the amount of particles in a fluidized bed boiler of the present invention, which can achieve the above object, includes the following steps when adjusting the amount of particles in a fluidized bed boiler:
This method is characterized in that air or gas is introduced into the lower part of the cyclone that separates combustion gas and particles to adjust the separation performance of the cyclone.
以下、図面を参照して本発明の方法について詳細に説明
する。Hereinafter, the method of the present invention will be explained in detail with reference to the drawings.
第1図は本発明の方法を適用した流動層ボイラの概略図
であり、第2図の従来例とほぼ同様な構成及び機能を有
している。FIG. 1 is a schematic diagram of a fluidized bed boiler to which the method of the present invention is applied, and has substantially the same structure and function as the conventional example shown in FIG.
従って、前述の説明と同じ部分の説明は省略し、図中の
同じ部品はそれぞれ同じ部品番号で示している。Therefore, description of the same parts as in the above description will be omitted, and the same parts in the figures are indicated by the same part numbers.
本発明は、前記サイクロン5の下部に供給管16を取り
付け、この供給管16がら供給される空気又はガスによ
ってサイクロン5の分離性能を調節するのである。In the present invention, a supply pipe 16 is attached to the lower part of the cyclone 5, and the separation performance of the cyclone 5 is adjusted by air or gas supplied from the supply pipe 16.
すなわち、粒子貯槽7内の粒子eのレベルLが上昇する
時は、空気又はガスの導入量を増加するのである。する
と、サイクロン5の分離性能が低下し、サイクロン出口
9から排出される微粒子e゛の量が増加し、粒子貯槽7
内の粒子eのレベルLの上昇が抑制される。That is, when the level L of particles e in the particle storage tank 7 increases, the amount of air or gas introduced is increased. As a result, the separation performance of the cyclone 5 decreases, the amount of fine particles e' discharged from the cyclone outlet 9 increases, and the particle storage tank 7
The increase in the level L of the particles e inside is suppressed.
これとは逆に、前記レベルLが降下する時は、空気また
はガスの供給を減少させる。すると、サイクロン5の分
離性能が向上し、サイクロン出口9から排出される微粒
子e“の量が少なくなり、上記のレベルLの降下が防止
される。Conversely, when the level L falls, the supply of air or gas is reduced. This improves the separation performance of the cyclone 5, reduces the amount of particulates e'' discharged from the cyclone outlet 9, and prevents the drop in level L mentioned above.
すなわち、本発明によれば、供給管16に配設された流
量調整弁17によって空気またはガスの吹き込む量を加
減することによってサイクロン5の分離性能が調節され
、粒子貯槽7内の粒子eのレベルLが簡単に調整される
のである。That is, according to the present invention, the separation performance of the cyclone 5 is adjusted by adjusting the amount of air or gas blown in by the flow rate regulating valve 17 disposed in the supply pipe 16, and the level of particles e in the particle storage tank 7 is adjusted. L can be easily adjusted.
前記粒子貯槽7の粒子e内に含まれる粗粒子は前記通路
8−燃焼室1−通路4−サイクロン5→サイクロン粒子
排出口6を循環するうちに微細化し、サイクロン出口9
より排出可能となるのである。The coarse particles contained in the particles e in the particle storage tank 7 become fine as they circulate through the passage 8 - the combustion chamber 1 - the passage 4 - the cyclone 5 -> the cyclone particle discharge port 6, and then the coarse particles are made fine as they circulate through the passage 8 - the combustion chamber 1 - the passage 4 - the cyclone particle discharge port 6 .
This makes it possible to discharge more easily.
本発明者等は、実験及び検討により燃焼室1からサイク
ロン5に流入するガス量の、例えば、数パーセントの空
気又はガスを供給管16から吹き込むことによって、サ
イクロン出口9より排出する微粒子e°の量を数倍に変
化させ得ることを確認している。Through experiments and studies, the present inventors have found that by blowing air or gas, for example, several percent of the amount of gas flowing into the cyclone 5 from the combustion chamber 1 through the supply pipe 16, the particulates e° discharged from the cyclone outlet 9 can be reduced. It has been confirmed that the amount can be changed several times.
上記のごとく、本発明は、流動層ボイラ内の粒子量を調
節するに際し、燃焼ガスと粒子とを分離するサイクロン
の下部に、当該サイクロンの分離性能を調節する空気又
はガスを導入するもので、粒子貯槽内の粒子のレベルを
簡単に調整できる。As mentioned above, when adjusting the amount of particles in a fluidized bed boiler, the present invention introduces air or gas to the lower part of the cyclone that separates combustion gas and particles to adjust the separation performance of the cyclone. The level of particles in the particle reservoir can be easily adjusted.
また、本発明によれば、処理が難かしく、利用価値のな
い粗粒を含む循環粒子の排出がなく、取扱容易で利用価
値のある微粒子のみが排出されるという利点がある。Further, according to the present invention, there is no discharge of circulating particles including coarse particles that are difficult to process and have no utility value, and only fine particles that are easy to handle and have utility value are discharged.
また、燃焼室に燃料及び補給固形物を投入する際に、そ
の補給固形分を不必要に増加することがないので経済的
な運転ができるという効果がある。Furthermore, when fuel and replenishment solids are introduced into the combustion chamber, the replenishment solid content is not increased unnecessarily, so that economical operation can be achieved.
【図面の簡単な説明】
第1図は本発明の方法を適用した流動層ボイラの概略図
、第2図は従来の流動層ボイラの概略図である。
d・・・燃焼ガス、e・・・粒子、5・・・サイクロン
、11・・・集じん器。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram of a fluidized bed boiler to which the method of the present invention is applied, and FIG. 2 is a schematic diagram of a conventional fluidized bed boiler. d... Combustion gas, e... Particles, 5... Cyclone, 11... Dust collector.
Claims (1)
粒子とを分離するサイクロンの下部に、当該サイクロン
の分離性能を調節する空気又はガスを導入することを特
徴とする流動層ボイラ内粒子量調節方法。The amount of particles in a fluidized bed boiler is characterized in that when adjusting the amount of particles in the fluidized bed boiler, air or gas is introduced into the lower part of a cyclone that separates combustion gas and particles to adjust the separation performance of the cyclone. Adjustment method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15216888A JPH024103A (en) | 1988-06-22 | 1988-06-22 | Particle quantity control method inside fluidized bed boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15216888A JPH024103A (en) | 1988-06-22 | 1988-06-22 | Particle quantity control method inside fluidized bed boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH024103A true JPH024103A (en) | 1990-01-09 |
Family
ID=15534520
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15216888A Pending JPH024103A (en) | 1988-06-22 | 1988-06-22 | Particle quantity control method inside fluidized bed boiler |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH024103A (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6329104A (en) * | 1986-07-21 | 1988-02-06 | Mitsubishi Heavy Ind Ltd | Combustion method for fluidized bed |
-
1988
- 1988-06-22 JP JP15216888A patent/JPH024103A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6329104A (en) * | 1986-07-21 | 1988-02-06 | Mitsubishi Heavy Ind Ltd | Combustion method for fluidized bed |
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