JP2002267154A - Boiler device - Google Patents

Boiler device

Info

Publication number
JP2002267154A
JP2002267154A JP2001062186A JP2001062186A JP2002267154A JP 2002267154 A JP2002267154 A JP 2002267154A JP 2001062186 A JP2001062186 A JP 2001062186A JP 2001062186 A JP2001062186 A JP 2001062186A JP 2002267154 A JP2002267154 A JP 2002267154A
Authority
JP
Japan
Prior art keywords
boiler
evaporator
air
temperature
heater
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
Application number
JP2001062186A
Other languages
Japanese (ja)
Inventor
Kazuyuki Maruishi
和幸 丸石
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP2001062186A priority Critical patent/JP2002267154A/en
Publication of JP2002267154A publication Critical patent/JP2002267154A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Air Supply (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce unburnt matters in ash and achieve a highly efficient operation by more raising the temperature of combustion air of a boiler. SOLUTION: A boiler device having a heater 6 relatively little in temperature change due to heat absorption is provided with an air duct evaporator 9 connected in parallel with the heater 6. The temperature of the combustion air supplied from an air preheater 2 is raised through the air duct evaporator 9 to supply the combustion air to a boiler wind box 3. The air duct evaporator 9 has its inlet/outlet connected to the heater 6 by communicating pipes 8. Flow rate is adjusted by valves 10 disposed in the communicating pipes.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明はボイラ装置に関わ
り、特に石炭焚きボイラの灰中未燃分を低減するのに好
適なボイラ装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a boiler, and more particularly to a boiler suitable for reducing unburned ash in coal-fired boilers.

【0002】[0002]

【従来の技術】従来のボイラ装置を図2に示す。押込フ
ァン1より送られる空気は、空気予熱器2にて約300
°℃程度に加熱され、ウインドボックス3に送られる。
ウインドボックス3より送られた燃焼用空気は、火炉4
にて燃料と共に燃焼し、過熱器5、蒸発器6、節炭器7
を通過し、空気予熱器2にて熱回収され、煙突に送られ
る。
2. Description of the Related Art FIG. 2 shows a conventional boiler apparatus. The air sent from the pushing fan 1 is approximately 300
It is heated to about ° C and sent to the wind box 3.
The combustion air sent from the wind box 3 is supplied to the furnace 4
Combustion with fuel at, superheater 5, evaporator 6, economizer 7
And heat is recovered by the air preheater 2 and sent to the chimney.

【0003】従来のボイラ装置は、空気予熱器2にて加
熱された燃焼用空気を直接にウインドボックス3に供給
する系統を備えたものである。
[0003] The conventional boiler apparatus has a system for directly supplying combustion air heated by the air preheater 2 to the wind box 3.

【0004】[0004]

【発明が解決しようとする課題】上記従来技術は、空気
予熱器2のみの加熱であるので、灰中未燃分の低減に有
効な燃焼用空気の温度上昇に関しての配慮がされていな
かった。
In the above prior art, since only the air preheater 2 is heated, no consideration has been given to a rise in the temperature of combustion air that is effective in reducing unburned ash in ash.

【0005】本発明の目的は、前記燃焼用空気の温度を
更に上昇させることにより、灰中未燃分の低減を図り、
より高効率の運用を可能にすることにある。
An object of the present invention is to further reduce the unburned ash content by further increasing the temperature of the combustion air.
The purpose is to enable more efficient operation.

【0006】[0006]

【課題を解決するための手段】前記課題を解決するため
に、本発明は主として次のような構成を採用する。熱吸
収による温度変化の比較的少ない加熱器を有するボイラ
装置であって、前記加熱器と並列接続された風道蒸発器
を設け、空気予熱器から送られた燃焼用空気を前記風道
蒸発器を通し温度上昇させてボイラウインドボックスに
送給するボイラ装置。
In order to solve the above problems, the present invention mainly employs the following configuration. A boiler device having a heater having a relatively small temperature change due to heat absorption, comprising a wind path evaporator connected in parallel with the heater, wherein the combustion air sent from an air preheater is supplied to the air path evaporator. A boiler device that raises the temperature through the boiler and feeds it to the boiler wind box.

【0007】[0007]

【発明の実施の形態】本発明の実施形態に係るボイラ装
置について図1を用いて以下説明する。図1は、本発明
の実施形態に係るボイラ装置における概略的な煙風道系
統及び流体経路を示す図であり、1は押込ファン、2は
空気予熱器、3はウインドボックス、4は火炉・ケー
ジ、5は過熱器、6は蒸発器、7は節炭器、8は連絡
管、9は風道蒸発器、10はバルブ、11は汽水分離
器、をそれぞれ表す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A boiler device according to an embodiment of the present invention will be described below with reference to FIG. FIG. 1 is a diagram showing a schematic flue duct system and a fluid path in a boiler apparatus according to an embodiment of the present invention, wherein 1 is a push-in fan, 2 is an air preheater, 3 is a wind box, 4 is a furnace and Cage, 5 is a superheater, 6 is an evaporator, 7 is a economizer, 8 is a connecting pipe, 9 is an airway evaporator, 10 is a valve, and 11 is a steam separator.

【0008】図1の(1)において、押込ファン1より
送られる燃焼用空気は、空気予熱器2にて約300℃程
度に加熱され、更に、風道蒸発器9にて更に加熱され
る。高温の燃焼空気は、火炉4にて燃料と共に燃焼し、
過熱器5、蒸発器6、節炭器7を通過し空気予熱器2に
て熱回収され、煙突に送られる。以上が押込ファンから
の空気の一連の流れである。
In FIG. 1A, the combustion air sent from the pushing fan 1 is heated to about 300 ° C. by an air preheater 2 and further heated by an airway evaporator 9. The high-temperature combustion air is burned together with the fuel in the furnace 4,
After passing through the superheater 5, the evaporator 6, and the economizer 7, heat is recovered by the air preheater 2 and sent to the chimney. The above is a series of flows of the air from the pushing fan.

【0009】図1の(2)にボイラ水の流動経路を示す
が、蒸発器6と風道蒸発器9の接続関係は図示のとおり
である。風道蒸発器9は蒸発器6の出入口と連絡管8に
より接続されており、バルブ10で流量調整する。そし
て、風道蒸発器9は蒸発器6入口より取り出した飽和蒸
気(約400〜420℃)を熱源としている。風道蒸発
器9を通過した流体は、汽水分離器入口11に戻され
る。
FIG. 1 (2) shows the flow path of the boiler water. The connection relationship between the evaporator 6 and the wind path evaporator 9 is as shown. The airway evaporator 9 is connected to the entrance and exit of the evaporator 6 by a communication pipe 8, and the flow rate is adjusted by a valve 10. The wind path evaporator 9 uses saturated steam (about 400 to 420 ° C.) taken out from the inlet of the evaporator 6 as a heat source. The fluid that has passed through the airway evaporator 9 is returned to the brackish water separator inlet 11.

【0010】以上のように、押込ファン1より送られる
空気は、空気予熱器2にて約300℃程度に加熱された
後、ウインドボックス3に投入される前に、蒸発器6入
口より取り出した飽和蒸気(約400〜420℃)を熱
源とした風道蒸発器9にて更に加熱される。この際、空
気予熱器2にて約300℃程度に加熱された燃焼用空気
は、風道蒸発器9にて更に20〜30℃加熱される。
As described above, the air sent from the pushing fan 1 is heated to about 300 ° C. by the air preheater 2 and then taken out from the inlet of the evaporator 6 before being put into the wind box 3. The air is further heated by an airway evaporator 9 using saturated steam (about 400 to 420 ° C.) as a heat source. At this time, the combustion air heated to about 300 ° C. by the air preheater 2 is further heated by the airway evaporator 9 to 20 to 30 ° C.

【0011】ボイラに投入される燃焼空気温度は、高温
である程、灰中未燃分は低減される特性を持っており、
これにより高効率の運用が可能となる。図4に示したよ
うに燃焼用空気温度を20℃上昇させると約10〜15
%程度の灰中未燃分が低下する特性となり、ボイラの高
効率運転が可能となる。
[0011] The higher the temperature of the combustion air charged to the boiler, the lower the unburned ash content in the ash is,
This enables highly efficient operation. As shown in FIG. 4, when the temperature of the combustion air is increased by 20 ° C., about 10 to 15
%, The unburned matter in the ash is reduced, and the boiler can be operated with high efficiency.

【0012】ここで、燃焼空気温度の上昇は、ボイラ伝
面調整によるボイラ出口ガス温度上昇によっても可能で
あるが、この場合にはボイラ効率は低下する。しかし、
本発明では、空気予熱器出口側の空気を加熱することか
ら、ガス温度上昇によるボイラ効率低下もなく、効率向
上が可能となる。
Here, the temperature of the combustion air can be increased by increasing the temperature of the gas at the boiler outlet by adjusting the boiler transmission surface, but in this case, the boiler efficiency is reduced. But,
In the present invention, since the air on the outlet side of the air preheater is heated, the efficiency can be improved without a decrease in the boiler efficiency due to an increase in the gas temperature.

【0013】図3に或るプラントのP−I線図を示す
が、図示するように、圧力・温度域の特性上、蒸発器で
の昇温は、5〜7℃と少ないことから風道蒸発器を通過
した流体との温度差も小さくなる。ここで、蒸発器6を
通過する流体(水・蒸気)は、熱吸収してエンタルピが
上昇しても、温度変化が少ない特徴があることから、風
道蒸発器9を通過して蒸発器出口に戻る流体との温度差
も少なくボイラ特性への影響も殆どないと云える。
FIG. 3 shows a P-I diagram of a certain plant. As shown in the drawing, the temperature rise in the evaporator is as small as 5 to 7 ° C. due to the characteristics of the pressure and temperature range. The temperature difference with the fluid that has passed through the evaporator is also small. Here, the fluid (water / steam) passing through the evaporator 6 has a characteristic that the temperature change is small even if the enthalpy rises due to heat absorption. It can be said that there is little temperature difference with the fluid returning to boiler and there is almost no influence on the boiler characteristics.

【0014】[0014]

【発明の効果】本発明によれば、灰中未燃分の低減が可
能となり、また、空気予熱器出口側の空気を加熱するこ
とから、ガス温度上昇によるボイラ効率低下もなく効率
向上が可能となる。
According to the present invention, it is possible to reduce the unburned portion in the ash and to heat the air at the outlet side of the air preheater, thereby improving the efficiency without lowering the boiler efficiency due to a rise in gas temperature. Becomes

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

【図1】本発明の実施形態に係るボイラ装置における概
略的な煙風道系統及び流体経路を示す図である。
FIG. 1 is a diagram showing a schematic flue duct system and a fluid path in a boiler device according to an embodiment of the present invention.

【図2】従来技術における概略的な煙風道系統及び流体
経路を示す図である。
FIG. 2 is a diagram showing a schematic flue duct system and a fluid path in the prior art.

【図3】プラントのP−I線図の一例を示す図である。FIG. 3 is a diagram showing an example of a PI diagram of a plant.

【図4】空気温度と灰中未燃分との関係を示す図であ
る。
FIG. 4 is a diagram showing a relationship between air temperature and unburned ash content.

【符号の説明】[Explanation of symbols]

1 押込ファン 2 空気予熱器 3 ウインドボックス 4 火炉・ケージ 5 過熱器 6 蒸発器 7 節炭器 8 連絡管 9 風道蒸発器 10 バルブ 11 汽水分離器 DESCRIPTION OF SYMBOLS 1 Push fan 2 Air preheater 3 Wind box 4 Furnace / cage 5 Superheater 6 Evaporator 7 Energy saving device 8 Communication tube 9 Airway evaporator 10 Valve 11 Steam separator

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 熱吸収による温度変化の比較的少ない加
熱器を有するボイラ装置であって、 前記加熱器と並列接続された風道蒸発器を設け、 空気予熱器から送られた燃焼用空気を前記風道蒸発器を
通し温度上昇させてボイラウインドボックスに送給する
ことを特徴とするボイラ装置。
1. A boiler device having a heater having a relatively small temperature change due to heat absorption, comprising a wind path evaporator connected in parallel with the heater, wherein a combustion air sent from an air preheater is supplied. A boiler device, wherein the temperature is increased through the wind path evaporator and is supplied to a boiler wind box.
【請求項2】 請求項1に記載のボイラ装置において、 前記風道蒸発器は、前記加熱器とその出入口を連絡管で
接続され、前記連絡管に設置されたバルブで流量調整さ
れることを特徴とするボイラ装置。
2. The boiler device according to claim 1, wherein the air path evaporator is connected to the heater and its inlet and outlet by a connecting pipe, and the flow rate is adjusted by a valve installed in the connecting pipe. Boiler equipment characterized.
JP2001062186A 2001-03-06 2001-03-06 Boiler device Pending JP2002267154A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001062186A JP2002267154A (en) 2001-03-06 2001-03-06 Boiler device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001062186A JP2002267154A (en) 2001-03-06 2001-03-06 Boiler device

Publications (1)

Publication Number Publication Date
JP2002267154A true JP2002267154A (en) 2002-09-18

Family

ID=18921363

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001062186A Pending JP2002267154A (en) 2001-03-06 2001-03-06 Boiler device

Country Status (1)

Country Link
JP (1) JP2002267154A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007205188A (en) * 2006-01-31 2007-08-16 Hitachi Engineering & Services Co Ltd Energy saving installation using waste heat
CN104864380A (en) * 2015-05-14 2015-08-26 张国银 Vertical fuel oil and fuel gas steam boiler
CN104913499A (en) * 2015-04-30 2015-09-16 张国银 Vertical type fuel oil and fuel gas normal pressure hot water boiler
JP2020528535A (en) * 2017-07-27 2020-09-24 スミトモ エスエイチアイ エフダブリュー エナージア オサケ ユキチュア Method of preheating combustion gas in fluidized bed boiler equipment and fluidized bed boiler equipment

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007205188A (en) * 2006-01-31 2007-08-16 Hitachi Engineering & Services Co Ltd Energy saving installation using waste heat
JP4554527B2 (en) * 2006-01-31 2010-09-29 株式会社日立エンジニアリング・アンド・サービス Energy-saving equipment using waste heat
CN104913499A (en) * 2015-04-30 2015-09-16 张国银 Vertical type fuel oil and fuel gas normal pressure hot water boiler
CN104864380A (en) * 2015-05-14 2015-08-26 张国银 Vertical fuel oil and fuel gas steam boiler
JP2020528535A (en) * 2017-07-27 2020-09-24 スミトモ エスエイチアイ エフダブリュー エナージア オサケ ユキチュア Method of preheating combustion gas in fluidized bed boiler equipment and fluidized bed boiler equipment

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