JPH04110501A - Pressurized fluidized-bed boiler - Google Patents
Pressurized fluidized-bed boilerInfo
- Publication number
- JPH04110501A JPH04110501A JP22646390A JP22646390A JPH04110501A JP H04110501 A JPH04110501 A JP H04110501A JP 22646390 A JP22646390 A JP 22646390A JP 22646390 A JP22646390 A JP 22646390A JP H04110501 A JPH04110501 A JP H04110501A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- fluidized bed
- evaporator
- tubes
- tube
- 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
- 238000002485 combustion reaction Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 239000002184 metal Substances 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
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]
本発明は加圧流動床ボイラ、特にその伝熱管の配置に関
する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a pressurized fluidized bed boiler, and in particular to the arrangement of heat exchanger tubes thereof.
(従来の技術)
第2図は加圧流動床ボイラ複合発電プラントの一例を示
す系統図である。加圧流動床ボイラは、石炭を燃料とし
、かつプラントとして高効率が期待できる。しかしなが
ら現時点においては、100MW級の実証プラントが本
年運転開始するという段階に過ぎない。将来の大容量商
用プラントにおいては、蒸発器、過熱器、再熱器等の伝
熱面積が非常に大きくなるので、これを加圧流動床ボイ
ラ火炉内に収め、更にこの火炉を収める耐圧容器をいか
に小さくまとめるかが1つの課題となる。また、象、速
起動時における再熱器管および過熱器管の焼損を防止す
るための配慮も必要となるが、従来はこれらに対する対
策がなかった。(Prior Art) FIG. 2 is a system diagram showing an example of a pressurized fluidized bed boiler combined power generation plant. A pressurized fluidized bed boiler uses coal as fuel and is expected to be highly efficient as a plant. However, at present, we are only at the stage where a 100 MW class demonstration plant is scheduled to begin operation this year. In future large-capacity commercial plants, the heat transfer area of evaporators, superheaters, reheaters, etc. will become extremely large, so these will be housed in a pressurized fluidized bed boiler furnace, and a pressure-resistant container to house this furnace will also be installed. One challenge is how to make it as small as possible. In addition, consideration must be given to preventing burnout of the reheater tube and superheater tube during quick start-up, but conventionally there were no measures against this.
本発明は、大容量の加圧流動床ボイラにおいて、これを
コンパクトにまとめ、かつ急速起動時に過熱器ならびに
再熱器のチューブの焼損を防止する対策を提案すること
を目的とする。SUMMARY OF THE INVENTION The present invention aims to provide a measure for making a large-capacity pressurized fluidized bed boiler compact and preventing the tubes of the superheater and reheater from burning out during rapid startup.
(課題を解決するための手段)
本発明は、前記従来の#J題を解決するために、流動床
内に蒸発器管および過熱器管を設け、加圧下で気泡型流
動床を形成して燃焼する流動床ボイラにおいて、上記蒸
発器管を設ける炉と上記過熱器管を設ける炉とを別体と
し、それら別体の炉を同一の横置型耐圧容器内ムこ収容
したことを特徴とする加圧流動床ボイラ;ならびに
流動床内に蒸発器管、過熱器管および再熱器管を設け、
加圧下で気泡形流動床を形成して燃焼する流動床ボイラ
において、上記蒸発器管を設ける炉と上記過熱器管およ
び上記再熱器管を設ける炉とを別体とし、それら別体の
炉を同一の横置型耐圧容器内に収容したことを特徴とす
る加圧流動床ボイラを提案するものである。(Means for Solving the Problems) In order to solve the conventional problem #J, the present invention provides an evaporator tube and a superheater tube in a fluidized bed to form a bubble-type fluidized bed under pressure. A combustion fluidized bed boiler, characterized in that the furnace in which the evaporator tube is installed and the furnace in which the superheater tube is installed are separate, and the separate furnaces are housed in the same horizontal pressure vessel. a pressurized fluidized bed boiler; and an evaporator tube, a superheater tube and a reheater tube within the fluidized bed;
In a fluidized bed boiler that burns by forming a bubble-type fluidized bed under pressure, a furnace in which the evaporator tube is provided and a furnace in which the superheater tube and the reheater tube are provided are separate, and the furnace is a separate furnace. This paper proposes a pressurized fluidized bed boiler characterized in that both are housed in the same horizontal pressure vessel.
本発明によれば、加圧流動床ボイラがコンパクトにまと
まるだけでなく、起動時においても、蒸発器管を設けた
炉の方から起動することにより、他方の炉内に入ってい
る伝熱管(過熱器管、再熱器管)の過熱を防止できる。According to the present invention, not only can the pressurized fluidized bed boiler be made compact, but also when the furnace is started up, the heat exchanger tube installed in the other furnace is started. Prevents overheating of superheater tubes and reheater tubes.
[実施例]
第1図は本発明の一実施例を示す縦断面図である。この
図に示すように、蒸発器管(4)を設けた流動床炉(蒸
発器炉)(2)と過熱器管(5)および再熱器管(6)
を設けた流動床炉(S)I/R1(炉)(3)とが、横
置耐圧容器(])内に独立して別個に配置されている。[Embodiment] FIG. 1 is a longitudinal sectional view showing an embodiment of the present invention. As shown in this figure, a fluidized bed furnace (evaporator furnace) (2) with an evaporator tube (4), a superheater tube (5) and a reheater tube (6)
A fluidized bed furnace (S) I/R1 (furnace) (3) equipped with a fluidized bed furnace (S) I/R1 (furnace) (3) is arranged independently and separately in a horizontal pressure vessel (]).
起動時には、まず蒸発器炉(2)から起動し、蒸気が十
分発生した時点でこれを過熱器管(5)および再熱器管
(6)へ供給する。ここからSR/R11炉(3)の起
動を開始する。At startup, the evaporator furnace (2) is first started, and when enough steam is generated, it is supplied to the superheater tube (5) and the reheater tube (6). From here, start-up of the SR/R11 reactor (3) begins.
なお、蒸発器炉(2)、S)I/R)l炉(3)とも炉
壁は水冷却構造になっているから、SH/R)l炉(3
)の水冷壁には蒸発器炉(2)の起動とともに水を流す
。(ドラムボイラの場合は缶水、モノチューブボイラの
場合は蒸発器炉水冷壁からSH/R)l水冷壁へ、また
はS)I/R)l水冷壁から蒸発器水冷壁へ節炭器出口
水を流す。)また、S)l/RH炉(3)の起動時間を
短縮するため、起動バーナ(7)により単独にヒートア
ップしておく。Note that both the evaporator furnace (2) and the S)I/R)l furnace (3) have a water-cooled furnace wall, so the SH/R)l furnace (3)
) Water is allowed to flow through the water-cooled walls of the evaporator furnace (2) when the evaporator furnace (2) is started. (For drum boilers, can water; for monotube boilers, from the evaporator furnace water-cooled wall to SH/R) l water-cooled wall, or S) I/R) l water-cooled wall to the evaporator water-cooled wall economizer outlet Run water. ) Also, in order to shorten the startup time of the S)l/RH furnace (3), it is heated up independently by a startup burner (7).
もちろん、この時の流動床の温度はチューブメタル温度
の面から制御される。Of course, the temperature of the fluidized bed at this time is controlled from the viewpoint of tube metal temperature.
[発明の効果]
加圧流動床ボイラにおける重要な問題の一つは、耐圧容
器をいかに小さくつくれるがである。特に内径は、容器
重量にある程度比例するので、コストの面から小口径に
選定される必要がある。本発明では、流動床炉を分割し
て横置耐圧容器の内に配置したので、内径を大きくせず
にかつ簡単な構造で、加圧流動床ボイラが樽成できる。[Effects of the Invention] One of the important problems in pressurized fluidized bed boilers is how small the pressure vessel can be made. In particular, the inner diameter is proportional to the weight of the container to some extent, so it is necessary to select a small diameter from the viewpoint of cost. In the present invention, since the fluidized bed furnace is divided and placed inside the horizontal pressure vessel, a pressurized fluidized bed boiler can be constructed without increasing the inner diameter and with a simple structure.
また炉を分割したことにより、過熱器、再熱器のメタル
温度制御も容易となり、チューブ焼損の問題もな(、起
動時間も短縮できる。Furthermore, by dividing the furnace, it is easier to control the metal temperature of the superheater and reheater, and there is no problem of tube burnout (and startup time can be shortened).
第1図は本発明の一実施例を示す縦断面図である。第2
図は加圧流動床ボイラ複合発電プラントの一例を示す系
統図である。
(1)・・・横置耐圧容器;(2)・・・蒸発器炉;(
3)・・・S)I/RH炉;(4)・・・蒸発器管;(
5)・・・過熱器管;(6)・・・再熱器管;(7)・
・・起動バーナ;
第1図
高)晟螺蚊がス
料 気
料 気
暖FIG. 1 is a longitudinal sectional view showing one embodiment of the present invention. Second
The figure is a system diagram showing an example of a pressurized fluidized bed boiler combined power generation plant. (1)... Horizontal pressure vessel; (2)... Evaporator furnace; (
3)...S) I/RH furnace; (4)...evaporator tube; (
5)... Superheater tube; (6)... Reheater tube; (7).
・・Start burner; Figure 1 high) Air temperature
Claims (1)
で気泡型流動床を形成して燃焼する流動床ボイラにおい
て、上記蒸発器管を設ける炉と上記過熱器管を設ける炉
とを別体とし、それら別体の炉を同一の横置型耐圧容器
内に収容したことを特徴とする加圧流動床ボイラ。 2)流動床内に蒸発器管、過熱器管および再熱器管を設
け、加圧下で気泡形流動床を形成して燃焼する流動床ボ
イラにおいて、上記蒸発器管を設ける炉と上記過熱器管
および上記再熱器管を設ける炉とを別体とし、それら別
体の炉を同一の横置型耐圧容器内に収容したことを特徴
とする加圧流動床ボイラ。[Scope of Claims] 1) A fluidized bed boiler in which an evaporator tube and a superheater tube are provided in a fluidized bed and a bubble-type fluidized bed is formed under pressure and combustion is performed, which includes a furnace provided with the evaporator tube and the superheater tube. 1. A pressurized fluidized bed boiler characterized in that a furnace provided with a vessel is separate, and the separate furnace is housed in the same horizontal pressure vessel. 2) In a fluidized bed boiler in which an evaporator tube, a superheater tube, and a reheater tube are provided in the fluidized bed, and a bubble-type fluidized bed is formed and burned under pressure, a furnace provided with the evaporator tube and the superheater. A pressurized fluidized bed boiler characterized in that a tube and a furnace provided with the reheater tube are separate bodies, and the separate furnaces are housed in the same horizontal pressure vessel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22646390A JPH04110501A (en) | 1990-08-30 | 1990-08-30 | Pressurized fluidized-bed boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22646390A JPH04110501A (en) | 1990-08-30 | 1990-08-30 | Pressurized fluidized-bed boiler |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04110501A true JPH04110501A (en) | 1992-04-13 |
Family
ID=16845496
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22646390A Pending JPH04110501A (en) | 1990-08-30 | 1990-08-30 | Pressurized fluidized-bed boiler |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04110501A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57157920A (en) * | 1981-03-26 | 1982-09-29 | Babcock Hitachi Kk | Solid waste incineration equipment |
-
1990
- 1990-08-30 JP JP22646390A patent/JPH04110501A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57157920A (en) * | 1981-03-26 | 1982-09-29 | Babcock Hitachi Kk | Solid waste incineration equipment |
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