JPH0222281B2 - - Google Patents
Info
- Publication number
- JPH0222281B2 JPH0222281B2 JP56020946A JP2094681A JPH0222281B2 JP H0222281 B2 JPH0222281 B2 JP H0222281B2 JP 56020946 A JP56020946 A JP 56020946A JP 2094681 A JP2094681 A JP 2094681A JP H0222281 B2 JPH0222281 B2 JP H0222281B2
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- bed
- tube
- superheater
- section
- 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
Links
- 230000008020 evaporation Effects 0.000 claims description 2
- 238000001704 evaporation Methods 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
Description
【発明の詳細な説明】
この発明は流動層ボイラに係り、特に蒸気温度
を良好に制御できる流動層ボイラに関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fluidized bed boiler, and particularly to a fluidized bed boiler that can control steam temperature well.
砂等の流動媒体を流動化させて形成する流動層
中で燃料を燃焼させる流動層炉は燃焼効率が高
く、難燃性の物質でも良好に燃焼できるため最近
各種の分野で利用されている。また流動層内の保
有熱量は非常に高く、伝熱効率は空塔部の4〜5
倍に達するため層中に蒸発管、過熱器管等の伝熱
管を配置して層内の熱を有効に回収する流動層ボ
イラも種々提供されている。しかし、流動層にお
ける燃焼を良好に行うためには供給する燃料の種
類に応じて層温度を適正に保持する必要があり、
一定温度以下に低下すると層内での燃焼が不良と
なつて大量の未燃分が空塔部に飛散することにな
り、反対に層温度が高過ぎると灰分の一部が溶融
して流動化が不良になる等の問題がある。一方流
動層ボイラも他の形式のボイラと同様、蒸気、熱
水を使用する機器の状態により負荷変動が生ずる
が、上述の理由により層温度を変化させてこの負
荷変動に対応することは困難である。このため層
高を調節して過熱器管の一部もしくは全部を層外
に露出させることにより蒸気温度を調節する方法
が提案されたが、過熱器管は層高方向に平行に配
置してあるためわずかな層高の変更により露出面
積が急激に変化してしまい精密な制御は不可能で
あつた。 BACKGROUND ART Fluidized bed furnaces, which burn fuel in a fluidized bed formed by fluidizing a fluidized medium such as sand, have high combustion efficiency and can burn even flame-retardant materials well, so they have recently been used in various fields. In addition, the amount of heat retained in the fluidized bed is extremely high, and the heat transfer efficiency is 4 to 5 in the empty column.
To achieve this, various fluidized bed boilers have been provided in which heat transfer tubes such as evaporator tubes and superheater tubes are arranged in the bed to effectively recover the heat within the bed. However, in order to achieve good combustion in a fluidized bed, it is necessary to maintain the bed temperature appropriately depending on the type of fuel supplied.
If the temperature drops below a certain level, combustion within the bed will fail and a large amount of unburned matter will scatter into the empty column.On the other hand, if the bed temperature is too high, some of the ash will melt and become fluidized. There are problems such as the product becoming defective. On the other hand, fluidized bed boilers, like other types of boilers, experience load fluctuations depending on the conditions of the equipment that uses steam and hot water, but for the reasons mentioned above, it is difficult to respond to these load fluctuations by changing the bed temperature. be. For this reason, a method has been proposed to adjust the steam temperature by adjusting the bed height and exposing part or all of the superheater tubes outside the bed, but the superheater tubes are arranged parallel to the bed height direction. Therefore, even a slight change in layer height causes a sudden change in the exposed area, making precise control impossible.
この発明の目的は上述した問題点を除去し、蒸
気温度を精密に制御できる流動層ボイラを提供す
ることにある。 An object of the present invention is to eliminate the above-mentioned problems and provide a fluidized bed boiler in which steam temperature can be precisely controlled.
要するにこの発明は蒸発管は流動層の比較的下
部に配置し、過熱器管の少なくとも一部を流動層
上層部に斜行部を有する如く配置し、平行配置部
は主たる熱回収部とし、斜行部は温度制御部とし
て精密な制御を行うよう構成し、かつボイラの緊
急停止時には配置高さの少ない平行部と合せて急
激に温度降下させるよう構成したことを特徴とす
るものである。 In short, in this invention, the evaporator tube is arranged relatively lower in the fluidized bed, at least a part of the superheater tube is arranged in the upper part of the fluidized bed so as to have a diagonal section, the parallel arrangement section is the main heat recovery section, and the The row section is configured to perform precise control as a temperature control section, and is characterized by being configured to rapidly drop the temperature in conjunction with the parallel section, which is located at a small height, in the event of an emergency stop of the boiler.
以下この発明の実施例を図面に基づいて説明す
る。 Embodiments of the present invention will be described below based on the drawings.
第1図において、流動層ボイラ本体1内には送
風機4、空気室5および多孔板2を経て供給され
た流動化空気(燃焼用空気)Aにより流動層3が
形成してある。6は流動層3に層内伝熱管として
配置した蒸発管であつて、流動層3の層高方向に
対しほぼ平行となるよう曲折して配置してある。 In FIG. 1, a fluidized bed 3 is formed in a fluidized bed boiler main body 1 by fluidizing air (combustion air) A supplied through a blower 4, an air chamber 5, and a perforated plate 2. Reference numeral 6 denotes an evaporation tube disposed in the fluidized bed 3 as an intrabed heat transfer tube, and is bent so as to be substantially parallel to the bed height direction of the fluidized bed 3.
7は過熱器管であつて、蒸発管6の上部に配置
してあり、蒸気Sの流入側は平行部7aとなつて
おり、出口側は出口端に向つて上昇する斜行部7
bとなつており、斜行部7bの一部が流動層3か
ら露出するよう構成してある。 Reference numeral 7 denotes a superheater tube, which is disposed above the evaporator tube 6, and has a parallel portion 7a on the inflow side of the steam S, and a diagonal portion 7 on the outlet side that rises toward the outlet end.
b, and a portion of the oblique portion 7b is exposed from the fluidized bed 3.
流動層ボイラの運転中蒸気温度を上昇させた場
合には層高H1を増加させて流動層と過熱器管と
の接触面積を増加させることにより行い、反対に
蒸気温度を下降させたい場合には層高H1を減少
させることにより行う。この場合過熱器管7の一
部を斜行させたことにより蒸気温度制御を行う
H2は、平行部の配置高さH3に比較して非常に大
きくとれるので精密な温度制御を行える。ちなみ
に、伝熱効率は空塔部における効率を1とすれば
流動層では4〜5に達し、両者の伝熱効率は大き
く相違するので、斜行部7aにおける層高制御を
行うことにより精密な制御が可能となる。 If you want to increase the steam temperature during operation of a fluidized bed boiler, increase the bed height H1 to increase the contact area between the fluidized bed and the superheater tube, and conversely, if you want to decrease the steam temperature, is performed by decreasing the layer height H1 . In this case, steam temperature control is performed by making a part of the superheater tube 7 run obliquely.
Since H 2 can be much larger than the height H 3 of the parallel portion, precise temperature control can be achieved. By the way, if the efficiency in the empty column section is 1, then in the fluidized bed the heat transfer efficiency reaches 4 to 5, and since the heat transfer efficiency of the two is greatly different, precise control can be achieved by controlling the bed height in the diagonal section 7a. It becomes possible.
次に流動層3の層高制御の具体例を示すと、層
高H1を減少させたい場合には媒体排出管8によ
り流動媒体を排出して貯留槽9に貯留しておき、
層高H1を増加させたい場合には気流輸送管10
により貯留槽9内の流動媒体を気流輸送すること
により行う。 Next, a specific example of bed height control of the fluidized bed 3 is shown. When it is desired to reduce the bed height H 1 , the fluidized medium is discharged through the medium discharge pipe 8 and stored in the storage tank 9.
If you want to increase the bed height H1 , use the airflow transport pipe 10.
This is carried out by transporting the fluid medium in the storage tank 9 with air current.
ボイラで発生した蒸気を使用する機器の故障等
により流動層ボイラを緊急停止する場合には流動
媒体を排出するが、主たる熱回収部である平行部
7aの配置高さH3は僅かであるため短時間で過
熱器管7全体を層外に露出させることができる。 In the case of emergency shutdown of the fluidized bed boiler due to failure of equipment that uses the steam generated in the boiler, the fluidized medium is discharged, but since the height H 3 of the parallel section 7a, which is the main heat recovery section, is small. The entire superheater tube 7 can be exposed outside the layer in a short time.
なお、以上の説明においては斜行部を有する伝
熱管を過熱器管として説明したが、層内伝熱管と
して過熱器管を配置していない流動層ボイラにあ
つては蒸発管に斜行部を形成することはもとより
可能である。 In the above explanation, the heat exchanger tubes with the skewed section were explained as superheater tubes, but in the case of a fluidized bed boiler in which the superheater tube is not arranged as an intrabed heat exchanger tube, the evaporator tubes have the skewed section. It is of course possible to form.
この発明を実施することにより層高を調節して
蒸気もしくは熱水の温度を精密に制御することが
できる。 By implementing this invention, the temperature of steam or hot water can be precisely controlled by adjusting the bed height.
第1図はこの発明に係る流動層ボイラの断面図
である。
1……流動層ボイラ本体、3……流動層、7…
…過熱器管、7a……平行部、7b……斜行部。
FIG. 1 is a sectional view of a fluidized bed boiler according to the present invention. 1...Fluidized bed boiler main body, 3...Fluidized bed, 7...
...superheater tube, 7a...parallel section, 7b...oblique section.
Claims (1)
と過熱器管とを配置し、蒸発管により蒸気を発生
させるとともに、該発生蒸気を過熱器管により所
望温度に加熱する如くなした流動層ボイラにおい
て、蒸発管は流動層の比較的下部に配置し、かつ
過熱器の少なくとも一部を流動層上層部にて斜行
部を有する如く構成したことを特徴とする流動層
ボイラ。1 An evaporator tube and a superheater tube are arranged in a fluidized bed maintained within a predetermined temperature range, and the evaporator tube generates steam, and the superheater tube heats the generated steam to a desired temperature. 1. A fluidized bed boiler, characterized in that the evaporation tube is disposed relatively below the fluidized bed, and at least a part of the superheater is configured to have a diagonal section in the upper part of the fluidized bed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2094681A JPS57136002A (en) | 1981-02-17 | 1981-02-17 | Fluidized bed boiler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2094681A JPS57136002A (en) | 1981-02-17 | 1981-02-17 | Fluidized bed boiler |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57136002A JPS57136002A (en) | 1982-08-21 |
JPH0222281B2 true JPH0222281B2 (en) | 1990-05-18 |
Family
ID=12041360
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2094681A Granted JPS57136002A (en) | 1981-02-17 | 1981-02-17 | Fluidized bed boiler |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS57136002A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4824597B2 (en) * | 2007-02-19 | 2011-11-30 | 株式会社神戸製鋼所 | Joint mechanism |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5416002A (en) * | 1977-07-07 | 1979-02-06 | Babcock Hitachi Kk | Fluidized heat transmission device |
JPS55131601A (en) * | 1979-03-30 | 1980-10-13 | Babcock Hitachi Kk | Fluidizeddbed boiler |
-
1981
- 1981-02-17 JP JP2094681A patent/JPS57136002A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5416002A (en) * | 1977-07-07 | 1979-02-06 | Babcock Hitachi Kk | Fluidized heat transmission device |
JPS55131601A (en) * | 1979-03-30 | 1980-10-13 | Babcock Hitachi Kk | Fluidizeddbed boiler |
Also Published As
Publication number | Publication date |
---|---|
JPS57136002A (en) | 1982-08-21 |
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