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JPS6363804B2 - - Google Patents
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JPS6363804B2 - - Google Patents

Info

Publication number
JPS6363804B2
JPS6363804B2 JP3290382A JP3290382A JPS6363804B2 JP S6363804 B2 JPS6363804 B2 JP S6363804B2 JP 3290382 A JP3290382 A JP 3290382A JP 3290382 A JP3290382 A JP 3290382A JP S6363804 B2 JPS6363804 B2 JP S6363804B2
Authority
JP
Japan
Prior art keywords
fluidized bed
exhaust gas
inclined plate
fluidized
combustion chamber
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
Application number
JP3290382A
Other languages
Japanese (ja)
Other versions
JPS58148305A (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 JP3290382A priority Critical patent/JPS58148305A/en
Publication of JPS58148305A publication Critical patent/JPS58148305A/en
Publication of JPS6363804B2 publication Critical patent/JPS6363804B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00Fluidised bed combustion apparatus

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Description

【発明の詳細な説明】 本発明は、流動層燃焼装置において燃焼室空塔
部に仕切壁を取付け、ガス排出通路を長くし流動
層から燃焼ガスとともに飛散してきた流動媒体を
燃焼室空塔部において捕集した後再び流動層に戻
して再使用可能にした流動層燃焼装置の流動媒体
飛散防止装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a fluidized bed combustion apparatus in which a partition wall is attached to the cavity of the combustion chamber, the gas discharge passage is lengthened, and the fluidized medium scattered together with the combustion gas from the fluidized bed is removed from the cavity of the combustion chamber. The present invention relates to a fluidized medium scattering prevention device for a fluidized bed combustion apparatus, in which the fluidized medium is collected and returned to the fluidized bed so that it can be reused.

流動層燃焼装置は、燃焼室内の砂等の不活性粉
粒材料よりなる流動媒体を、炉底部から空気を吹
き込むことにより流動化させ、あたかも流体が沸
騰しているかのような状態に活発に運動する流動
層を形成せしめ、該流動層域内に石炭等の燃焼物
質を供給して燃焼せしめる装置でその発生熱量を
流動層域内に配設した伝熱管により熱交換して熱
回収することもでき、該伝熱管内に水を通すと流
動床ボイラとなる。
Fluidized bed combustion equipment fluidizes a fluidized medium made of inert granular material such as sand in a combustion chamber by blowing air from the bottom of the furnace, creating a state in which the fluid moves actively as if it were boiling. A device that forms a fluidized bed and supplies a combustion substance such as coal into the fluidized bed area for combustion, and the generated heat can be exchanged and recovered by heat exchanger tubes disposed within the fluidized bed area. When water is passed through the heat transfer tube, it becomes a fluidized bed boiler.

流動層内に噴射される流動用空気が流動層内で
気泡状を呈し、流動層内を上昇するにつれて膨張
し、流動層界面に達して破裂する。この破裂エネ
ルギーによつて流動層界面の流動媒体粒子が弾か
れ、比較的高い位置まで飛散し、一部は燃焼ガス
とともに燃焼室外に飛散してしまう。この流動媒
体は炉本体の高さ、即ち燃焼室空塔部の高さ
(H1)が第1図に示す如く低くなればなる程燃焼
ガスとともに飛散しやすくなる。流動層燃焼装置
では流動層高(h)を一定に保つ必要がるため第2図
に示す如く燃焼室の高さ(H2)を、該破裂エネ
ルギーによる流動媒体の飛散がない程度に高くす
るか或いは飛散した流動媒体の量を補充しなけれ
ばならない。
The fluidizing air injected into the fluidized bed takes on the shape of bubbles within the fluidized bed, expands as it rises within the fluidized bed, and bursts when it reaches the fluidized bed interface. The fluidized medium particles at the interface of the fluidized bed are repelled by this bursting energy and scattered to a relatively high position, and some of them are scattered outside the combustion chamber along with the combustion gas. The lower the height of the furnace body, that is, the height (H 1 ) of the cavity of the combustion chamber, as shown in FIG. 1, the more easily this fluidized medium will scatter together with the combustion gas. In a fluidized bed combustion device, it is necessary to keep the fluidized bed height (h) constant, so as shown in Figure 2, the height of the combustion chamber (H 2 ) is set high enough to prevent the fluidized medium from scattering due to the bursting energy. Otherwise, the amount of flow medium that has flown out must be replenished.

このため小型化特に炉の高さが制限される流動
層燃焼装置、例えば舶用流動床ボイラや流動床パ
ツケージボイラ等では流動媒体飛散防止対策が必
要となる。
For this reason, it is necessary to take measures to prevent the scattering of fluidized media in fluidized bed combustion apparatuses where the height of the furnace is limited, such as marine fluidized bed boilers and fluidized bed package boilers.

そこで、本発明は流動媒体の飛散防止対策を講
ずることにより、炉高を低く抑えることを目的と
するものである。
Therefore, an object of the present invention is to keep the furnace height low by taking measures to prevent the fluidized medium from scattering.

本発明の実施例を図について説明すると1は流
動床ボイラの燃焼室で、2が流動層。3は燃焼室
空塔部、4が風箱で流動用空気を流動層2の底部
より供給し流動層の流動媒体を浮きあがらせるよ
うに構成する。5は気泡で流動層2の底部におい
ては小さいが、第1図第2図に示す如く流動層内
を上昇するに従つて大きくなり流動層界面におい
て気泡5が破裂し、流動媒体粒子を飛散する。第
3図は本発明を適用した流動層燃焼装置を示した
もので、流動層界面6の上方の囲壁に設けた排ガ
ス排出口7の下方に下端を有し空塔部3内上方に
傾斜せしめた傾斜板8を設け傾斜板8の下端と側
壁との間に間隙11を設けるとともに、傾斜板8
から垂直上方に天井までの間に開口を有する仕切
板9を設け、また空塔部3の天井より垂直に垂下
し傾斜板8までの間に開口を有する仕切板10を
設けて、排ガス排出口7に到るまでの空塔部3上
方に排ガス通路を形成したものである。12は流
動層2内に配設した伝熱管である。第4図は本発
明の他の実施例を示すもので仕切板9,10をそ
れぞれ複数板設け、傾斜板8を谷型に変形したも
のである。即ち、第4図A−A断面を示す第5図
においてわかるように空塔部3の天井から垂下し
た複数の仕切板10,10′、傾斜板8から上方
に複数の仕切板9,9′を設けたもので仕切板
9′は断面くの字型に折曲した形状のものである。
また第4図B−B矢視図である第5図でわかるよ
うに仕切板10の下端を傾斜板8の谷型に合わせ
て突出した形状としたものである。
An embodiment of the present invention will be explained with reference to the figures. 1 is a combustion chamber of a fluidized bed boiler, and 2 is a fluidized bed. Reference numeral 3 denotes an empty tower portion of the combustion chamber, and 4 a wind box configured to supply fluidizing air from the bottom of the fluidized bed 2 to float the fluidized medium in the fluidized bed. The bubbles 5 are small at the bottom of the fluidized bed 2, but grow larger as they rise in the fluidized bed, as shown in Figures 1 and 2, and the bubbles 5 burst at the interface of the fluidized bed, scattering the fluidized medium particles. . FIG. 3 shows a fluidized bed combustion apparatus to which the present invention is applied, which has a lower end below an exhaust gas outlet 7 provided in the surrounding wall above the fluidized bed interface 6, and is inclined upward in the hollow column 3. The inclined plate 8 is provided with a gap 11 between the lower end of the inclined plate 8 and the side wall.
A partition plate 9 having an opening vertically upward from the ceiling to the ceiling is provided, and a partition plate 10 hanging vertically from the ceiling of the tower section 3 and having an opening between the inclined plate 8 and the exhaust gas outlet is provided. 7, an exhaust gas passage is formed above the empty tower section 3. 12 is a heat exchanger tube arranged within the fluidized bed 2. FIG. 4 shows another embodiment of the present invention, in which a plurality of partition plates 9 and 10 are provided, and the inclined plate 8 is deformed into a valley shape. That is, as can be seen in FIG. 5, which shows the cross section taken along line A-A in FIG. The partition plate 9' is bent into a dogleg shape in cross section.
Further, as can be seen in FIG. 5, which is a view taken along the line B--B in FIG. 4, the lower end of the partition plate 10 is shaped to protrude in accordance with the valley shape of the inclined plate 8.

次に本発明の作用について説明すると、流動用
空気が風箱4から流動層2に送り込まれ、流動媒
体を流動化し、ガス気泡5となつて流動層2内を
上昇し、流動層界面6において破裂する。この破
裂エネルギーによつて流動媒体粒子が弾かれて排
ガスとともに上昇し排ガス排出口7から排出され
るが、燃焼室空塔部3にある傾斜板8および仕切
板9によつて通路がはばまれるとともに傾斜板8
下面において排ガスに混合した流動媒体および燃
焼灰は一部分離されて流動層2に落下する。一方
排ガスは仕切板9,10が交互に構成して形成さ
れた通路を通るが、この間において排ガスは上下
に移動しつゝ排ガスと流動媒体とは一層よく分離
され、排ガスは排ガス排出口7から排出される。
仕切板9,10または仕切板9,10,9′,1
0′によつて分離された流動媒体は傾斜板8の上
に落下する。傾斜板8上に落下した流動媒体はそ
の傾斜に沿つて下降し、終には間隙11より流動
層2に返還される。
Next, to explain the operation of the present invention, fluidizing air is sent into the fluidized bed 2 from the wind box 4, fluidizes the fluidized medium, becomes gas bubbles 5, rises in the fluidized bed 2, and reaches the fluidized bed interface 6. Burst. The fluidized medium particles are repelled by this bursting energy, rise together with the exhaust gas, and are discharged from the exhaust gas outlet 7, but the passage is blocked by the inclined plate 8 and partition plate 9 in the cavity 3 of the combustion chamber. The inclined plate 8
The fluidized medium and combustion ash mixed with the exhaust gas on the lower surface are partially separated and fall into the fluidized bed 2. On the other hand, the exhaust gas passes through a passage formed by alternating partition plates 9 and 10, during which time the exhaust gas moves up and down, and the exhaust gas and fluidized medium are further separated, and the exhaust gas is discharged from the exhaust gas outlet 7. It is discharged.
Partition plates 9, 10 or partition plates 9, 10, 9', 1
The flowing medium separated by 0' falls onto the inclined plate 8. The fluidized medium that has fallen onto the inclined plate 8 descends along the inclination, and is finally returned to the fluidized bed 2 through the gap 11.

このように本発明は流動層燃焼装置において燃
焼室空塔部に排ガス排出口の下方に下端を有し空
塔部内に傾斜する傾斜板と、該傾斜板から上方に
天井までの間に開口を有する仕切板と、空塔部天
井より垂下し、上記傾斜板までの間に開口を有す
る仕切板とを交互に配置して排ガス通路を形成す
るとともに、前記傾斜板の下端と燃焼室側壁との
間に間隙を設けたので、流動層界面上に飛散した
流動媒体が排ガスダクトから排出されることなく
傾斜板の作用によつて流動層に還元されるので流
動媒体の消耗を大幅に防止することができるもの
である。従つて砂等の不活性粉粒材料の補給頻度
を著しく減少させ、ひいてはボイラの諸特性を向
上させるばかりでなく流動層ボイラの高さ(H1
を低くおさえることができるので、陸上は勿論、
殊に船用ボイラとして極めて有効なものである。
As described above, the present invention provides a fluidized bed combustion apparatus in which a sloped plate having a lower end below the exhaust gas outlet in the cavity of the combustion chamber and slopes into the cavity, and an opening extending upward from the sloped plate to the ceiling. The exhaust gas passage is formed by alternately arranging partition plates that have an opening, and partition plates that hang down from the ceiling of the tower section and have an opening between them up to the inclined plate, and also form an exhaust gas passage between the lower end of the inclined plate and the side wall of the combustion chamber. Since a gap is provided between the two, the fluidized medium scattered on the fluidized bed interface is returned to the fluidized bed by the action of the inclined plate without being discharged from the exhaust gas duct, thereby greatly preventing consumption of the fluidized medium. It is something that can be done. Therefore, the frequency of replenishment of inert granular materials such as sand can be significantly reduced, which not only improves various boiler characteristics but also reduces the height (H 1 ) of the fluidized bed boiler.
It can be kept low, so it can be used not only on land, but also on land.
It is extremely effective especially as a ship boiler.

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

第1図第2図は本発明を説明するための従来の
流動床ボイラの断面を示す2例、第3図は本発明
の実施例を示す流動床ボイラの横断面図、第4図
は他の実施例を示す同じく横断面図、第5図は第
4図のA−A断面図、第6図は第4図のB−B線
矢視図である。 1……流動床ボイラ燃焼室、2……流動層、3
……燃焼室空塔部、4……風箱、5……気泡、6
……流動層界面、7……排ガス排出口、8……傾
斜板、9,9′……仕切板、10,10′……仕切
板、11……間隙、12……伝熱管。
FIG. 1 and FIG. 2 are two examples showing cross sections of conventional fluidized bed boilers to explain the present invention, FIG. 3 is a cross sectional view of a fluidized bed boiler showing an embodiment of the present invention, and FIG. 4 is another example. FIG. 5 is a sectional view taken along the line AA in FIG. 4, and FIG. 6 is a sectional view taken along the line BB in FIG. 4. 1...Fluidized bed boiler combustion chamber, 2...Fluidized bed, 3
... Combustion chamber empty tower section, 4 ... Wind box, 5 ... Air bubbles, 6
... Fluidized bed interface, 7 ... Exhaust gas outlet, 8 ... Inclined plate, 9, 9' ... Partition plate, 10, 10' ... Partition plate, 11 ... Gap, 12 ... Heat exchanger tube.

Claims (1)

【特許請求の範囲】[Claims] 1 流動層燃焼装置の燃焼室空塔部上部側壁から
排ガスを排出するものにおいて、側壁に設けた排
ガス排出口の下方に下端を有し空塔部内に上向き
に傾斜する傾斜板と、該傾斜板から垂直上方に配
設し空塔部天井との間に開口を有する仕切板と、
空塔部天井より垂下し上記傾斜板までの間に開口
を有する仕切板とを交互に配置して排ガス通路を
形成するとともに、前記傾斜板の下端と燃焼室側
壁との間に間隙を設けたことを特徴とする流動層
燃焼装置。
1. In a fluidized bed combustion device that discharges exhaust gas from the side wall of the upper part of the cavity in the combustion chamber, an inclined plate having a lower end below the exhaust gas outlet provided in the side wall and sloping upward into the cavity, and the inclined plate a partition plate disposed vertically upward from the ceiling and having an opening between it and the sky tower ceiling;
Exhaust gas passages are formed by alternately arranging partition plates that hang down from the ceiling of the tower section and have openings between them up to the inclined plate, and a gap is provided between the lower end of the inclined plate and the side wall of the combustion chamber. A fluidized bed combustion apparatus characterized by:
JP3290382A 1982-03-01 1982-03-01 Fluidized bed combustion apparatus Granted JPS58148305A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3290382A JPS58148305A (en) 1982-03-01 1982-03-01 Fluidized bed combustion apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3290382A JPS58148305A (en) 1982-03-01 1982-03-01 Fluidized bed combustion apparatus

Publications (2)

Publication Number Publication Date
JPS58148305A JPS58148305A (en) 1983-09-03
JPS6363804B2 true JPS6363804B2 (en) 1988-12-08

Family

ID=12371850

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3290382A Granted JPS58148305A (en) 1982-03-01 1982-03-01 Fluidized bed combustion apparatus

Country Status (1)

Country Link
JP (1) JPS58148305A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5171542A (en) * 1984-03-20 1992-12-15 A. Ahlstrom Corporation Circulating fluidized bed reactor
JPS61161315A (en) * 1985-01-10 1986-07-22 Babcock Hitachi Kk Combustor of fluidized bed furnace
FI86105C (en) * 1985-11-19 1992-07-10 Ahlstroem Oy FOERFARANDE OCH ANORDNING FOER REGLERING AV EN VIRVELBAEDDSREAKTORS FUNKTION.
ATE58220T1 (en) * 1985-12-09 1990-11-15 Ahlstroem Oy CIRCULATION FLUID BED REACTOR, PROCESS FOR SEPARATING SOLIDS FROM FLUE GAS.
US4869207A (en) * 1987-07-13 1989-09-26 A. Ahlstrom Corporation Circulating fluidized bed reactor

Also Published As

Publication number Publication date
JPS58148305A (en) 1983-09-03

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