JPH0379906A - Cyclone for circulating fluidized bed boiler - Google Patents
Cyclone for circulating fluidized bed boilerInfo
- Publication number
- JPH0379906A JPH0379906A JP21503589A JP21503589A JPH0379906A JP H0379906 A JPH0379906 A JP H0379906A JP 21503589 A JP21503589 A JP 21503589A JP 21503589 A JP21503589 A JP 21503589A JP H0379906 A JPH0379906 A JP H0379906A
- Authority
- JP
- Japan
- Prior art keywords
- cyclone
- heat transfer
- solid particles
- inner cylinder
- 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
- 239000002245 particle Substances 0.000 claims abstract description 43
- 239000007787 solid Substances 0.000 claims abstract description 25
- 238000004140 cleaning Methods 0.000 claims abstract description 9
- 238000002485 combustion reaction Methods 0.000 abstract description 7
- 230000003628 erosive effect Effects 0.000 abstract description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000006210 lotion Substances 0.000 description 1
- 238000013020 steam cleaning Methods 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
- 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、循環流動層ボイラのサイクロンに関し、特に
ボイラ後流における伝熱面のクリーニング装置を不要か
らしたサイクロンの構造に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a cyclone for a circulating fluidized bed boiler, and more particularly to a cyclone structure that eliminates the need for a cleaning device for the heat transfer surface downstream of the boiler.
従来の技術 従来の循環流動層ボイラを第3図に例示する。Conventional technology A conventional circulating fluidized bed boiler is illustrated in FIG.
第3図において、参照符号lは燃焼炉、2はサイクロン
、3は伝熱面、5は空気又は蒸気クリーニング装置をそ
れぞれ示している。In FIG. 3, reference numeral 1 represents a combustion furnace, 2 represents a cyclone, 3 represents a heat transfer surface, and 5 represents an air or steam cleaning device.
このような循環流動層ボイラにおいて、燃焼炉!から飛
び出した固体粒子はサイクロン2で浦果されるが、サイ
クロン2で捕集されない固体粒子は後流の伝熱面3に付
着して、伝熱効率を低下させるようになる。従来では、
伝熱面直上に空気又は蒸気式クリーニング装置5を設け
、空気又は蒸気を伝熱面3に直接噴射することで伝熱面
5を清掃し、伝熱効率を回復させるようにしている。In such a circulating fluidized bed boiler, the combustion furnace! The solid particles that fly out are collected by the cyclone 2, but the solid particles that are not collected by the cyclone 2 adhere to the downstream heat transfer surface 3, reducing heat transfer efficiency. Conventionally,
An air or steam type cleaning device 5 is provided directly above the heat transfer surface, and air or steam is directly injected onto the heat transfer surface 3 to clean the heat transfer surface 5 and restore heat transfer efficiency.
発明が解決しようとする課題
サイクロンによって捕集される固体粒子の粒子径には限
界があり、限界粒子径以下の粒子は後流の伝熱面3へ飛
散されることになるが、この粒子径の小さな固体粒子は
伝熱面3に付着し易いといった性質を有している。Problems to be Solved by the Invention There is a limit to the particle size of solid particles collected by a cyclone, and particles below the limit particle size will be scattered to the heat transfer surface 3 in the wake; The small solid particles have a property of easily adhering to the heat transfer surface 3.
この伝熱面3への固体粒子の付着により低下する伝熱面
の伝熱効率を回復するため、空気又は蒸気式クリーニン
グ装置5が設けられているが、このような装置は設備が
大規模になるだけでなく、クリーニング装置が高流速で
固体粒子を巻き込むことによる伝熱面3のエロージョン
対策が必要であり、しかもボイラの制御に与える外乱し
大きいものになっている。In order to restore the heat transfer efficiency of the heat transfer surface, which decreases due to the adhesion of solid particles to the heat transfer surface 3, an air or steam type cleaning device 5 is provided, but such a device requires large-scale equipment. In addition, it is necessary to take measures against erosion of the heat transfer surface 3 due to solid particles being drawn in by the cleaning device at a high flow rate, and furthermore, the disturbance to the control of the boiler is large.
本発明は上記事情にかんがみてなされたもので、上記の
ようなりリーニング装置の機能を有し、したがってその
ようなりリーニング装置を不要とし、クリーニング装置
使用により必要であったエロージョン対策及びボイラ制
御に与える外乱れをなくすことができる指環流動層ボイ
ラのサイクロンを提供することを目的とする。The present invention has been made in view of the above circumstances, and has the function of a leaning device as described above, thus eliminating the need for such a leaning device, and providing benefits to erosion countermeasures and boiler control that were necessary when using a cleaning device. An object of the present invention is to provide a cyclone for a ring fluidized bed boiler that can eliminate external turbulence.
課題を解決するための手段
本発明は、上記目的に対し、流動層式炉内から固体粒子
を含む排ガスをサイクロンに導き、前記固体粒子を排ガ
スから分離して流動層に戻すようにし、又、固体粒子の
混じった排ガスを伝熱面に噴射して清掃を行うようにし
た循環流動層ボイラにおけるサイクロンであって、サイ
クロンの出口に設けられた内筒の高さを可変としたこと
を特徴とする循環流動層ボイラのサイクロンを提供する
ことができる。Means for Solving the Problems The present invention achieves the above object by guiding exhaust gas containing solid particles from inside a fluidized bed furnace to a cyclone, separating the solid particles from the exhaust gas, and returning the solid particles to the fluidized bed. A cyclone for a circulating fluidized bed boiler that cleans the heat transfer surface by injecting exhaust gas mixed with solid particles onto the heat transfer surface, characterized in that the height of the inner cylinder provided at the outlet of the cyclone is variable. A cyclone for a circulating fluidized bed boiler can be provided.
作用
通常、サイクロンの出口には、捕集効率を改善するため
の円筒が設置されているが、この内筒を引き上げること
により、サイクロンの限界捕集粒径を大きくし、サイク
ロン後流に大粒径の粒子を飛散させてやることで、伝熱
面に付着した小粒径の固体粒子を除去するようにしてい
る。Normally, a cylinder is installed at the outlet of the cyclone to improve collection efficiency, but by pulling up this inner cylinder, the limit particle size for collection of the cyclone is increased, and large particles are placed in the wake of the cyclone. By scattering particles with a large diameter, small solid particles attached to the heat transfer surface are removed.
実施例
以下、第1図及び第2図に例示した本発明の好適な実施
例について詳述する。EXAMPLES Below, preferred embodiments of the present invention illustrated in FIGS. 1 and 2 will be described in detail.
第1図は本発明によるサイクロンを含む循環流動層ボイ
ラを示し、第2図は本発明によるサイクロンの要部を示
している。FIG. 1 shows a circulating fluidized bed boiler including a cyclone according to the invention, and FIG. 2 shows the main parts of the cyclone according to the invention.
通常のサイクロン2の出口には、固体粒子の限界捕集粒
径を小さくして捕集効率を改善するための内筒4が設置
されている。この内筒4の長さと限界捕集粒径との間に
は相関があり、内筒4を短かくするに従って限界捕集粒
径は大きくなる。本発明ではこの内筒4は固定せずに、
第2図に示すようにその高さを可変できるように設置し
である。At the outlet of the normal cyclone 2, an inner cylinder 4 is installed to improve the collection efficiency by reducing the critical collection particle size of solid particles. There is a correlation between the length of the inner cylinder 4 and the limit collection particle size, and the shorter the inner cylinder 4 is, the larger the limit collection particle size becomes. In the present invention, this inner cylinder 4 is not fixed;
As shown in Figure 2, it is installed so that its height can be varied.
通常の運転時において、サイクロン2の内筒4は第2図
に破線で示す位置まで降下していて、サイクロン2の捕
集効率の最も高い位置にある。燃焼炉lから飛散した固
体粒子はサイクロン2により捕集され、燃焼炉lに戻さ
れるが、サイクロン2で捕集されない粒径の小さな固体
粒子は後流の伝熱面3に徐々に付着していくことになる
。During normal operation, the inner cylinder 4 of the cyclone 2 is lowered to the position shown by the broken line in FIG. 2, which is the position where the cyclone 2 has the highest collection efficiency. Solid particles scattered from the combustion furnace 1 are collected by the cyclone 2 and returned to the combustion furnace 1, but small solid particles that are not collected by the cyclone 2 gradually adhere to the heat transfer surface 3 in the wake. I'm going to go.
固体粒子の付着により伝熱面3の伝熱効率が低下してき
た時、−時的にサイクロン内筒4をたとえば、第2図に
実線で示す位置まで上昇させる。When the heat transfer efficiency of the heat transfer surface 3 decreases due to the adhesion of solid particles, the cyclone inner cylinder 4 is temporarily raised, for example, to the position shown by the solid line in FIG.
このためサイクロン2の限界捕集粒径が大きくなって、
サイクロン2より放出される排ガスには粒径の大きな固
体粒子が含まれることになる。粒径の大きな固体粒子が
伝熱面3に飛散されると、付着していた粒子が大粒径の
粒子によって除去されるという自掃効果のため、伝熱面
3は清掃される。For this reason, the critical collection particle size of cyclone 2 becomes larger,
The exhaust gas discharged from the cyclone 2 contains solid particles having a large particle size. When large-sized solid particles are scattered onto the heat transfer surface 3, the heat transfer surface 3 is cleaned due to a self-sweeping effect in which the attached particles are removed by the large-sized particles.
伝熱面3が清掃されると、内筒4を再び降下させて、通
常の運転に戻る。Once the heat transfer surface 3 is cleaned, the inner cylinder 4 is lowered again and normal operation is resumed.
発明の効果
本発明では、サイクロン自体が従来の伝熱面クリーニン
グ装置の機能を持つことになるので、空気又は蒸気によ
る大規模なりリーニング装置の設置の必要はなくなり、
空気又は蒸気が高流速で粒子を巻き込んで伝熱面に衝突
することによる二ローションの防止対策が不必要となる
。又、空気又は蒸気を噴射した場合の制御に及ぼす影響
も無視でき、ボイラ運転の信頼性も向上することになる
。Effects of the Invention In the present invention, the cyclone itself has the function of a conventional heat transfer surface cleaning device, so there is no need to install a large-scale cleaning device using air or steam.
Measures to prevent double lotion due to air or steam entraining particles at high flow rates and impinging on the heat transfer surface are no longer necessary. Moreover, the influence on control when air or steam is injected can be ignored, and the reliability of boiler operation is also improved.
【図面の簡単な説明】
第1図は本発明によるサイクロンを含む循環流動層ボイ
ラボイラの構成を示す図、第2図は本発明によるサイク
ロンの要部を拡大して示す図、第3図は従来の循環流動
層ボイラの構成を示す図である。
!・・燃焼炉、2・・サイクロン、3・・伝熱面、4・
・内筒。[Brief Description of the Drawings] Fig. 1 is a diagram showing the configuration of a circulating fluidized bed boiler including a cyclone according to the present invention, Fig. 2 is an enlarged view showing the main parts of the cyclone according to the present invention, and Fig. 3 is a conventional diagram. FIG. 2 is a diagram showing the configuration of a circulating fluidized bed boiler. ! ... Combustion furnace, 2. Cyclone, 3. Heat transfer surface, 4.
・Inner cylinder.
Claims (1)
導き、前記固体粒子を排ガスから分離して流動層に戻す
ようにし、又、固体粒子の混じった排ガスを伝熱面に噴
射して清掃を行うようにした循環流動層ボイラにおける
サイクロンにおいて、サイクロンの出口に設けられた内
筒の高さを可変としたことを特徴とする循環流動層ボイ
ラのサイクロン。Exhaust gas containing solid particles is led from inside the fluidized bed furnace to a cyclone, the solid particles are separated from the exhaust gas and returned to the fluidized bed, and the exhaust gas mixed with solid particles is injected onto the heat transfer surface for cleaning. A cyclone for a circulating fluidized bed boiler, characterized in that the height of an inner cylinder provided at an outlet of the cyclone is variable.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21503589A JPH0379906A (en) | 1989-08-23 | 1989-08-23 | Cyclone for circulating fluidized bed boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21503589A JPH0379906A (en) | 1989-08-23 | 1989-08-23 | Cyclone for circulating fluidized bed boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0379906A true JPH0379906A (en) | 1991-04-04 |
Family
ID=16665676
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21503589A Pending JPH0379906A (en) | 1989-08-23 | 1989-08-23 | Cyclone for circulating fluidized bed boiler |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0379906A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006068498A (en) * | 2004-08-05 | 2006-03-16 | Toshimitsu Sasaki | Chair for infant |
| US8403149B2 (en) | 2005-11-18 | 2013-03-26 | Ricoh Company, Ltd. | Cyclone classifier, flash drying system using the cyclone classifier, and toner prepared by the flash drying system |
-
1989
- 1989-08-23 JP JP21503589A patent/JPH0379906A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006068498A (en) * | 2004-08-05 | 2006-03-16 | Toshimitsu Sasaki | Chair for infant |
| US8403149B2 (en) | 2005-11-18 | 2013-03-26 | Ricoh Company, Ltd. | Cyclone classifier, flash drying system using the cyclone classifier, and toner prepared by the flash drying system |
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