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JPH0330042B2 - - Google Patents
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JPH0330042B2 - - Google Patents

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Publication number
JPH0330042B2
JPH0330042B2 JP56076416A JP7641681A JPH0330042B2 JP H0330042 B2 JPH0330042 B2 JP H0330042B2 JP 56076416 A JP56076416 A JP 56076416A JP 7641681 A JP7641681 A JP 7641681A JP H0330042 B2 JPH0330042 B2 JP H0330042B2
Authority
JP
Japan
Prior art keywords
fluidized bed
reheater
superheater
steam
fluidized
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 - Lifetime
Application number
JP56076416A
Other languages
Japanese (ja)
Other versions
JPS57192701A (en
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to JP7641681A priority Critical patent/JPS57192701A/en
Publication of JPS57192701A publication Critical patent/JPS57192701A/en
Publication of JPH0330042B2 publication Critical patent/JPH0330042B2/ja
Granted legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Description

【発明の詳細な説明】 本発明は流動層ボイラ装置に係り、特に蒸気原
動機におけるサーマルシヨツクを極力少くした流
動層ボイラ装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fluidized bed boiler apparatus, and more particularly to a fluidized bed boiler apparatus in which thermal shock in a steam engine is minimized.

流動層ボイラは、低品位の石炭等の燃料を良好
に燃焼せしめ、また伝熱コイルへの伝熱特性が高
いことから、エネルギー危機の現在において、発
電所等の各方面に多く採用されている。
Fluidized bed boilers are widely used in various fields such as power plants in the current energy crisis because they can burn low-grade coal and other fuels well and have high heat transfer characteristics to heat transfer coils. .

しかし、流動層ボイラにおいては、流動用媒体
の量が蒸気発生量の増大に伴つて増大し、流動媒
体が被焼却物の燃焼に適する温度まで昇温するに
要する時間が増大し、起動に際しての過熱器また
は再熱器の焼損防止等、起動および正常運転に入
つてからの制御に関する種々の問題が提起されて
いる。また流動媒体の量の増大に伴う起動時間お
よび制御に際しての時間遅れ、助燃燃料量の増大
という問題がある。さらにまた流動層ボイラの総
伝熱量は流動層中に配置されている伝熱コイルの
総伝熱面積で決まるため、ボイラの蒸発量を自由
に調節することが難しいという問題がある。
However, in a fluidized bed boiler, the amount of fluidizing medium increases as the amount of steam generated increases, and the time required for the fluidizing medium to heat up to a temperature suitable for burning the materials to be incinerated increases. Various problems have been raised regarding startup and control after normal operation, such as prevention of burnout of the superheater or reheater. Further, there are problems such as a delay in start-up time and control due to an increase in the amount of fluidized medium, and an increase in the amount of auxiliary fuel. Furthermore, since the total heat transfer amount of a fluidized bed boiler is determined by the total heat transfer area of the heat transfer coils arranged in the fluidized bed, there is a problem that it is difficult to freely adjust the evaporation amount of the boiler.

上記問題を解決するため、流動層室を複数の部
屋に分割し、その任意の部屋数を流動化させるこ
とにより、種々の負荷に対応した運転を行うこと
が提案されている。
In order to solve the above problem, it has been proposed to divide the fluidized bed chamber into a plurality of chambers and fluidize any number of the chambers to perform operation corresponding to various loads.

しかしながら、上記方法においては、通常、過
熱器と再加熱器が異なる流動層室(単数また複
数)に配置されるため、過熱器および再熱器で加
熱された蒸気の温度が異なり、蒸気原動機(ター
ビン)に入つたときにサーマルシヨツクを生じ、
タービンに損傷を生じる恐れがある。
However, in the above method, the superheater and reheater are usually arranged in different fluidized bed chamber(s), so the temperature of the steam heated in the superheater and reheater is different, and the steam prime mover ( generates a thermal shock when entering the turbine),
Damage to the turbine may occur.

本発明の目的は、過熱器および再熱器の発生蒸
気の温度差を極力少くし、蒸気原動機に与えるサ
ーマルシヨツクを低減する流動層ボイラ装置を提
供することにある。
An object of the present invention is to provide a fluidized bed boiler apparatus that minimizes the temperature difference between the steam generated in a superheater and a reheater and reduces thermal shock on a steam engine.

本発明は、複数の流動層室に区画された流動炉
を有する流動層ボイラ装置において、過熱器およ
び再熱器を同一流動層室内に配置し、同一条件で
加熱するようにしたことを特徴とする。
The present invention is characterized in that in a fluidized bed boiler apparatus having a fluidized furnace divided into a plurality of fluidized bed chambers, a superheater and a reheater are arranged in the same fluidized bed chamber and heated under the same conditions. do.

以下、本発明を図面によりさらに詳細に説明す
る。
Hereinafter, the present invention will be explained in more detail with reference to the drawings.

第1図は、本発明の一実施例を示す流動層ボイ
ラ装置の要部断面図である。図において、流動層
ボイラ1は、隔壁2により2室に区画されたエア
ボツクス3Aおよび3Bと、その上部の多孔板4
Aおよび4Bと、該多孔板上に形成された流動媒
体と燃料の流動層5Aおよび5Bと、上記各流動
層内に配置された過熱器6A,6Bおよび再熱器
7A,7Bからなる。流動層5A,5Bは、送風
機9からダンパ10A,10B、エアボツクス3
A,3Bおよび多孔板4A,4Bを通して吹込ま
れる空気により流動媒体(砂、灰分等)と燃料
(石炭その他固形可燃物)が流動化することによ
つて形成される。なお、炉上部には蒸発器8が設
けられている。ボイラ内のドラムおよび蒸発器8
で発生した蒸気は、過熱器6A,6Bに導入さ
れ、ここで過熱された後蒸気原動機(図示せず)
に導びかれる。また再熱器7A,7Bは、蒸気原
動機で一旦膨張して温度低下した蒸気を加熱する
もので、それぞれ端部は蒸気原動機に接続され、
再加熱によつて発生した高温過熱蒸気は再び蒸気
原動機に供給される。
FIG. 1 is a sectional view of a main part of a fluidized bed boiler apparatus showing one embodiment of the present invention. In the figure, a fluidized bed boiler 1 includes air boxes 3A and 3B divided into two chambers by a partition wall 2, and a perforated plate 4 above the air boxes 3A and 3B.
A and 4B, fluidized beds 5A and 5B of fluidized medium and fuel formed on the perforated plates, superheaters 6A and 6B and reheaters 7A and 7B arranged in each of the fluidized beds. Fluidized beds 5A and 5B are connected to air blower 9, dampers 10A and 10B, and air box 3.
It is formed by fluidizing a fluid medium (sand, ash, etc.) and fuel (coal or other solid combustible material) by air blown through A, 3B and the perforated plates 4A, 4B. Note that an evaporator 8 is provided in the upper part of the furnace. Drum and evaporator in the boiler 8
The steam generated in
be guided by The reheaters 7A and 7B heat the steam whose temperature has been lowered by expanding once in the steam engine, and each end is connected to the steam engine.
The high-temperature superheated steam generated by reheating is again supplied to the steam motor.

上記実施例によれば、過熱器6Aと再熱器7A
を同じ流動層室5A内に、また過熱器6Bと再熱
器7Bを他の同じ流動層室5B内に配置したの
で、それぞれ同一条件で加熱することができ、過
熱器および再熱器からそれぞれ蒸気原動機へ供給
される過熱蒸気の温度差をなくし、サーマルシヨ
ツクを著しく低減することができる。
According to the above embodiment, the superheater 6A and the reheater 7A
are placed in the same fluidized bed chamber 5A, and the superheater 6B and reheater 7B are placed in the same fluidized bed chamber 5B, so they can be heated under the same conditions, and the superheater and reheater can each It is possible to eliminate the temperature difference in superheated steam supplied to the steam engine, and to significantly reduce thermal shock.

上記実施例においては、流動層室は、エアボツ
クスのみ区画され、流動層5A,5Bは特に仕切
られていないが、必要に応じて隔壁で仕切ること
ができる。
In the above embodiment, the fluidized bed chamber is divided only by the air box, and the fluidized beds 5A and 5B are not particularly partitioned, but they can be partitioned by partition walls if necessary.

以上、本発明によれば、過熱器と再熱器を同一
流動層室内に配置したので、種々の負荷に対応し
て流動層室を運転する場合においても蒸気原動機
に入る過熱蒸気の温度差がほとんどなくなり、サ
ーマルシヨツクによる蒸気原動機の歪み、損傷等
の発生を防止することができる。
As described above, according to the present invention, since the superheater and the reheater are arranged in the same fluidized bed chamber, even when operating the fluidized bed chamber in response to various loads, the temperature difference of the superheated steam entering the steam prime mover can be reduced. It is possible to prevent distortion and damage to the steam motor due to thermal shock.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、本発明の一実施例を示す流動層ボイ
ラ装置の主要部を示す断面図である。 1……流動層ボイラ、3A,3B……エアボツ
クス、5A,5B……流動層、6A,6B……過
熱器、7A,7B……再熱器。
FIG. 1 is a sectional view showing the main parts of a fluidized bed boiler device showing one embodiment of the present invention. 1... Fluidized bed boiler, 3A, 3B... Air box, 5A, 5B... Fluidized bed, 6A, 6B... Superheater, 7A, 7B... Reheater.

Claims (1)

【特許請求の範囲】[Claims] 1 複数の流動層室に区画された流動炉を有する
流動層ボイラ装置において、過熱器および再熱器
を同一流動室内に配置したことを特徴とする流動
層ボイラ装置。
1. A fluidized bed boiler device having a fluidized furnace divided into a plurality of fluidized bed chambers, characterized in that a superheater and a reheater are arranged in the same fluidized bed chamber.
JP7641681A 1981-05-22 1981-05-22 Fluid bed boiler device Granted JPS57192701A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7641681A JPS57192701A (en) 1981-05-22 1981-05-22 Fluid bed boiler device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7641681A JPS57192701A (en) 1981-05-22 1981-05-22 Fluid bed boiler device

Publications (2)

Publication Number Publication Date
JPS57192701A JPS57192701A (en) 1982-11-26
JPH0330042B2 true JPH0330042B2 (en) 1991-04-26

Family

ID=13604603

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7641681A Granted JPS57192701A (en) 1981-05-22 1981-05-22 Fluid bed boiler device

Country Status (1)

Country Link
JP (1) JPS57192701A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60101501U (en) * 1983-12-19 1985-07-11 バブコツク日立株式会社 fluidized bed boiler

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5829326Y2 (en) * 1976-06-23 1983-06-27 エヌオーケー株式会社 flexible membrane body

Also Published As

Publication number Publication date
JPS57192701A (en) 1982-11-26

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