JP2671991B2 - Fluidized bed combustion equipment - Google Patents

Fluidized bed combustion equipment

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Publication number
JP2671991B2
JP2671991B2 JP63077055A JP7705588A JP2671991B2 JP 2671991 B2 JP2671991 B2 JP 2671991B2 JP 63077055 A JP63077055 A JP 63077055A JP 7705588 A JP7705588 A JP 7705588A JP 2671991 B2 JP2671991 B2 JP 2671991B2
Authority
JP
Japan
Prior art keywords
ash
fluidized bed
combustion
bed furnace
unburned
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 - Fee Related
Application number
JP63077055A
Other languages
Japanese (ja)
Other versions
JPH01252806A (en
Inventor
正彦 田辺
茂伸 高田
Original Assignee
バブコツク日立株式会社
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 by バブコツク日立株式会社 filed Critical バブコツク日立株式会社
Priority to JP63077055A priority Critical patent/JP2671991B2/en
Publication of JPH01252806A publication Critical patent/JPH01252806A/en
Application granted granted Critical
Publication of JP2671991B2 publication Critical patent/JP2671991B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は流動層燃焼装置に係り、特に石炭や石油コー
クスなどの固形燃料を使用し、主燃焼流動層炉(MBC)
から排出された未燃灰を燃焼させるための流動層炉(CB
C)を設置した流動層燃焼装置に関する。
Description: TECHNICAL FIELD The present invention relates to a fluidized bed combustion apparatus, and in particular, uses a solid fuel such as coal or petroleum coke, and a main combustion fluidized bed furnace (MBC).
Fluidized bed furnace (CB) for burning unburned ash discharged from
C) Installed fluidized bed combustor.

〔従来の技術〕[Conventional technology]

第2図により従来技術を説明する。主燃焼流動層炉1
で燃焼した石炭などの固形燃料の燃焼灰は、飛散灰とな
って燃焼ガスとともに排出され、節炭器15、マルチサイ
クロン3、脱硝装置4、空気予熱器5、バグフィルタ6
にて捕集され、燃焼ガスは22に示すように外部に排出さ
れる。上記飛散灰中には多くの未燃分を含むので、再度
燃焼炉にて燃焼させ装置の熱効率の向上が図られてい
る。すなわち、上記飛散灰の大部分(約70〜90%)はマ
ルチサイクロン3で捕集されるので、ここで捕集された
灰と節炭器15で捕集された灰は灰タンク7に集められ、
灰排出機17、17′から適量が取出されブロア8、8′か
らの空気によりエゼクタ13、13′、層内吹込用灰流管
9、9′を介して主燃焼流動層炉1および未燃灰燃焼炉
(Carbon burn up Cell(CBC))2の流動層18、18′中
に灰ノズル10、10′を経て吹込まれる。なお、脱硝装置
4、空気予熱器5、バグフィルタ6で捕集された燃焼灰
は灰コンベア12でサイロに運ばれセメント原料その他の
用途に使用される。
The prior art will be described with reference to FIG. Main combustion fluidized bed furnace 1
Combustion ash of solid fuels such as coal burned in the form of fly ash is discharged together with the combustion gas, and the economizer 15, multi-cyclone 3, denitration device 4, air preheater 5, bag filter 6
And the combustion gas is discharged to the outside as shown at 22. Since the fly ash contains a large amount of unburned components, it is burned again in the combustion furnace to improve the thermal efficiency of the device. That is, since most of the fly ash (about 70 to 90%) is collected by the multi-cyclone 3, the ash collected here and the ash collected by the economizer 15 are collected in the ash tank 7. The
A proper amount is taken out from the ash dischargers 17 and 17 ', and the air from the blowers 8 and 8'through the ejectors 13 and 13', the ash flow pipes 9 and 9'for in-layer injection, and the main combustion fluidized bed furnace 1 and unburned air. It is blown into the fluidized beds 18, 18 'of the ash combustion furnace (Carbon burn up Cell (CBC)) 2 through the ash nozzles 10, 10'. The combustion ash collected by the denitration device 4, the air preheater 5, and the bag filter 6 is carried to a silo by the ash conveyor 12 and used as a cement raw material or other purposes.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

上記従来技術においては、MBC,CBCの流動層の空気室
を多室形(マルチセル)にして負荷の大小に応じ運転す
るセル数を増減する場合、休転セルへの灰ノズルや灰流
管へ流動層中の流動媒体が逆流して閉塞する事故が発生
する。ブロアがトリプ事故で停止した場合も同様であ
る。これは灰ノズルが吹込む流動層部の圧力が約1000〜
1500mm水柱と高圧であるためで、灰流管の空気圧が低下
すると流動媒体が灰ノズル内へ逆流するからである。こ
のように灰ノズルや灰流管が閉塞した場合は、灰タンク
中の未燃灰を燃焼できないという問題があった。
In the above-mentioned conventional technology, when the air chamber of the fluidized bed of MBC, CBC is made into a multi-chamber type (multi-cell) and the number of cells to be operated is increased or decreased according to the size of the load, the ash nozzle to the idle cell or the ash flow pipe An accident occurs in which the fluid medium in the fluidized bed flows backward and is blocked. The same applies when the blower stops due to a trip accident. This is because the pressure of the fluidized bed part blown by the ash nozzle is about 1000 ~
This is because the pressure is 1500 mm of water and the pressure is high, and when the air pressure in the ash flow pipe decreases, the flowing medium flows back into the ash nozzle. When the ash nozzle and the ash flow pipe are blocked in this way, there is a problem that unburned ash in the ash tank cannot be burned.

〔課題を解決するための手段〕[Means for solving the problem]

上記した問題点は、主燃焼流動層炉と該流動層炉から
排出された未燃灰を燃焼させる未燃灰燃焼流動層炉とを
備え、主燃料流動層炉から排出された飛散灰を捕集する
装置と、捕集された飛散灰を貯蔵する灰タンクを有する
流動層燃焼装置において、前記灰タンクの飛散灰を前記
主燃焼流動層炉と未燃灰燃焼流動層炉の、流動媒体層中
に供給する灰供給装置を設けるとともに、少なくとも一
方の空塔部へ前記飛散灰を供給する灰供給装置を設けた
ことを特徴とする流動層燃焼装置により解決される。
The problems described above include a main combustion fluidized bed furnace and an unburned ash combustion fluidized bed furnace that burns unburned ash discharged from the fluidized bed furnace, and collects fly ash discharged from the main fuel fluidized bed furnace. In a fluidized bed combustion device having a collecting device and an ash tank for storing the collected fly ash, the fly ash of the ash tank is a fluidized medium bed of the main combustion fluidized bed furnace and the unburned ash burning fluidized bed furnace. The fluidized bed combustion apparatus is characterized in that an ash supply device for supplying the fly ash is provided to at least one of the empty columns while providing an ash supply device for supplying the ash to the inside.

〔実施例〕〔Example〕

本発明の実施例を第1図に示す。第2図で説明した従
来技術と同一部分については同一符号で示しており、そ
の動作は同一であるので再度の説明は省略する。本実施
例が第2図の従来技術と相違している点は、MBCおよびC
BCの流動層中への灰の供給路である灰流管9、9′およ
び灰ノズル10、10′が閉塞した場合に備え、灰タンク7
と灰コンベア12を継ぐ灰タンクオーバフロー管11を設け
たところにある。
FIG. 1 shows an embodiment of the present invention. The same parts as those of the conventional technique described in FIG. This embodiment is different from the prior art in FIG. 2 in that MBC and C
The ash tank 7 is provided in case the ash flow pipes 9 and 9'and the ash nozzles 10 and 10 ', which are ash supply passages into the BC fluidized bed, are closed.
An ash tank overflow pipe 11 that connects the ash conveyor 12 and the ash conveyor 12 is provided.

灰ノズル10、10′、灰流管9、9′などが閉塞した場
合は弁11aを開き、灰タンクオーバフロー管11を経て灰
コンべア12に、灰タンク7中の灰が流入する。灰コンベ
ア12に供給された飛散灰は、灰コンベアの下に設けた灰
排出機20により切出され、エゼクタ21を介し、押込通風
機14の出口風道より分岐した空気によって、層上吹込用
灰流管16を経て、MBC、CBCの流動層上部の空塔部19、1
9′のいずれか、あるいは両方に吹込まれる。
When the ash nozzles 10 and 10 ', the ash flow pipes 9 and 9', etc. are closed, the valve 11a is opened and the ash in the ash tank 7 flows into the ash conveyor 12 through the ash tank overflow pipe 11. The fly ash supplied to the ash conveyor 12 is cut out by an ash ejector 20 provided below the ash conveyor, and through the ejector 21, by the air branched from the outlet air passage of the forced draft fan 14, for the upper layer blowing. After passing through the ash flow pipe 16, the empty tower section 19, 1 above the fluidized bed of MBC and CBC
It is blown into either or both of 9 '.

〔発明の効果〕〔The invention's effect〕

本発明によれば、MBC、CBCの流動層中への灰の供給路
が閉塞した場合でも、灰タンクオーバーフロー管、灰コ
ンベア、層上吹込用灰流管を経て飛散灰をMBCあるいはC
BCの空塔部に供給し、未燃灰の燃焼を続行し装置の燃焼
効率を維持することができる。
According to the present invention, even if the ash supply path to the fluidized bed of the MBC and CBC is blocked, the fly ash is MBC or C through the ash tank overflow pipe, the ash conveyor, and the ash flow pipe for in-layer blowing.
It is possible to maintain the combustion efficiency of the equipment by supplying it to the empty tower section of BC and continuing the combustion of unburned ash.

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

第1図は、本発明の一実施例を示す装置系統図、第2図
は、従来技術の説明図である。 1……主燃焼流動層炉、2……未燃灰燃焼流動層炉、3
……マルチサイクロン、4……脱硝装置、5……空気予
熱器、6……バグフィルタ、7……灰タンク、8……ブ
ロア、9、9′……層内吹込用灰流管、10、10′……灰
ノズル、11……灰タンクオーバフロー管、12……灰コン
ベア、13……エゼクタ、14……押込通風機、15……節炭
器、16……層上吹込用灰流管、17……灰排出機、18、1
8′……流動層、19、19′……空塔部、20……灰コンベ
ア下灰排出機、21……灰コンベア下エゼクタ。
FIG. 1 is a system diagram showing an embodiment of the present invention, and FIG. 2 is an explanatory diagram of a conventional technique. 1 ... Main combustion fluidized bed furnace, 2 ... Unburnt ash combustion fluidized bed furnace, 3
…… Multi cyclone, 4 …… Denitration device, 5 …… Air preheater, 6 …… Bag filter, 7 …… Ash tank, 8 …… Blower, 9,9 ′ …… Internal layer blowing ash flow tube, 10 , 10 '... Ash nozzle, 11 ... Ash tank overflow pipe, 12 ... Ash conveyor, 13 ... Ejector, 14 ... Push fan, 15 ... Economizer, 16 ... Layer-up ash flow Tube, 17 ... ash ejector, 18, 1
8 '... fluidized bed, 19, 19' ... empty tower section, 20 ... ash conveyor under ash ejector, 21 ... ash conveyor under ejector.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】主燃焼流動層炉と該流動層炉から排出され
た未燃灰を燃焼させる未燃灰燃焼流動層炉とを備え、主
燃料流動層炉から排出された飛散灰を捕集する装置と、
捕集された飛散灰を貯蔵する灰タンクを有する流動層燃
焼装置において、前記灰タンクの飛散灰を前記主燃焼流
動層炉と未燃灰燃焼流動層炉の、流動媒体層中に供給す
る灰供給装置を設けるとともに、少なくとも一方の空塔
部へ前記飛散灰を供給する灰供給装置を設けたことを特
徴とする流動層燃焼装置。
1. A main combustion fluidized bed furnace and an unburned ash combustion fluidized bed furnace that burns unburned ash discharged from the fluidized bed furnace, and collects fly ash discharged from the main fuel fluidized bed furnace. Device to
In a fluidized bed combustion device having an ash tank for storing collected fly ash, fly ash of the ash tank is supplied to the fluidized medium bed of the main combustion fluidized bed furnace and the unburned ash combustion fluidized bed furnace. A fluidized bed combustion apparatus comprising a supply device and an ash supply device for supplying the fly ash to at least one of the empty columns.
JP63077055A 1988-03-30 1988-03-30 Fluidized bed combustion equipment Expired - Fee Related JP2671991B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63077055A JP2671991B2 (en) 1988-03-30 1988-03-30 Fluidized bed combustion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63077055A JP2671991B2 (en) 1988-03-30 1988-03-30 Fluidized bed combustion equipment

Publications (2)

Publication Number Publication Date
JPH01252806A JPH01252806A (en) 1989-10-09
JP2671991B2 true JP2671991B2 (en) 1997-11-05

Family

ID=13623101

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63077055A Expired - Fee Related JP2671991B2 (en) 1988-03-30 1988-03-30 Fluidized bed combustion equipment

Country Status (1)

Country Link
JP (1) JP2671991B2 (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5946412A (en) * 1982-09-09 1984-03-15 Kawasaki Heavy Ind Ltd Recombustion method for unburnt carbon in fluidized boiler
JPS61144309U (en) * 1985-02-28 1986-09-05
JPH0629641B2 (en) * 1985-04-17 1994-04-20 バブコツク日立株式会社 Fluidized bed boiler control method
JPS62258911A (en) * 1986-04-30 1987-11-11 Kawasaki Heavy Ind Ltd Method of combustion in fluidized bed

Also Published As

Publication number Publication date
JPH01252806A (en) 1989-10-09

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