JP2001082735A - Air preheater - Google Patents
Air preheaterInfo
- Publication number
- JP2001082735A JP2001082735A JP25578799A JP25578799A JP2001082735A JP 2001082735 A JP2001082735 A JP 2001082735A JP 25578799 A JP25578799 A JP 25578799A JP 25578799 A JP25578799 A JP 25578799A JP 2001082735 A JP2001082735 A JP 2001082735A
- Authority
- JP
- Japan
- Prior art keywords
- air
- air preheater
- temperature
- preheater
- steam
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ボイラ等の燃焼炉
の空気予熱装置に係り、特に蒸気式空気予熱器と再生式
空気予熱器を備えた空気ダクトの蒸気式空気予熱器出口
の空気ダクト内の出口空気温度の温度差を低減する蒸気
式空気予熱器の出口ダクト構造に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air preheating apparatus for a combustion furnace such as a boiler, and more particularly to an air duct at an outlet of a steam air preheater of an air duct having a steam air preheater and a regenerative air preheater. TECHNICAL FIELD The present invention relates to an outlet duct structure of a steam-type air preheater for reducing a temperature difference between outlet air temperatures in a room.
【0002】[0002]
【従来の技術】図4に示すようにボイラ火炉1で用いる
燃料燃焼用空気は空気ダクト2から蒸気式空気予熱器3
に導入されて熱交換された後、空気ダクト4から再生式
空気予熱器5を通り、ボイラ火炉1に供給される。また
ボイラ燃焼排ガスはボイラ対流部の過熱器6、蒸発器7
及び節炭器8によって熱交換された後、脱硝装置9で脱
硝処理され、その後再生式空気予熱器5に流入し、ボイ
ラ燃焼用空気と熱交換した後、最終的に煙突10から大
気に放出される。2. Description of the Related Art As shown in FIG. 4, fuel combustion air used in a boiler furnace 1 is supplied from an air duct 2 to a steam type air preheater 3.
And heat-exchanged, the air is supplied from the air duct 4 to the boiler furnace 1 through the regenerative air preheater 5. The boiler flue gas is supplied to the superheater 6 and the evaporator 7 in the boiler convection section.
After the heat exchange by the economizer 8, the denitrification treatment is performed by the denitration device 9, then the heat flows into the regenerative air preheater 5, heat exchanges with the boiler combustion air, and finally discharged from the chimney 10 to the atmosphere. Is done.
【0003】ボイラ火炉1に供給される燃焼用空気とし
て、燃焼に適した空気とするために、空気ダクト4から
分岐して再生式空気予熱器5をバイパスするバイパスダ
クト11を通る冷空気と、再生式空気予熱器5を通過し
た熱空気を混合した後、使用している。このとき燃焼用
空気温度を調整するために再生式空気予熱器バイパスダ
クト11に設けられた流量調整ダンパ12を開閉調整す
ることで冷空気流量を調整し、設定した燃焼用空気温度
となるように制御している。In order to make the combustion air supplied to the boiler furnace 1 suitable for combustion, cold air that branches off from an air duct 4 and passes through a bypass duct 11 that bypasses a regenerative air preheater 5; The hot air that has passed through the regenerative air preheater 5 is used after mixing. At this time, in order to adjust the temperature of the combustion air, the flow rate of the cold air is adjusted by opening and closing the flow rate adjustment damper 12 provided in the regenerative air preheater bypass duct 11 so that the combustion air temperature is set. Controlling.
【0004】図3には蒸気式空気予熱器3を挟んで、こ
の前後に設けられている空気ダクト2と空気ダクト4の
拡大図を示す。蒸気式空気予熱器3は、その構造上、上
端から蒸気を供給し、下端からドレンを排出するため、
蒸気式空気予熱器3通過後の空気ダクト4内には図2に
示すようにダクトの上端は高温域、下端は低温域の上端
と下端で温度差のある空気領域(図2の横軸は空気ダク
ト4の横幅方向に長さ)が形成される。FIG. 3 is an enlarged view of the air duct 2 and the air duct 4 provided before and after the steam type air preheater 3 with the steam type air preheater 3 interposed therebetween. Due to its structure, the steam-type air preheater 3 supplies steam from the upper end and discharges drain from the lower end.
In the air duct 4 after passing through the steam-type air preheater 3, as shown in FIG. 2, the upper end of the duct is in a high-temperature region, and the lower end is an air region having a temperature difference between the upper and lower ends of the low-temperature region (the horizontal axis in FIG. (Length in the width direction of the air duct 4).
【0005】空気ダクト4からバイパスダクト11に流
れる空気は、前記温度差をもったまま再生式空気予熱器
5をバイパスし、燃焼用空気として再生式空気予熱器5
を経由した熱空気と合流するので、ボイラ火炉1に導入
する燃焼用空気は前記温度差を持った温度分布のままな
ので、温度計を設置した箇所の燃焼用空気温度と設定し
た燃焼用空気温度とずれが生じる要因となっていた。[0005] The air flowing from the air duct 4 to the bypass duct 11 bypasses the regenerative air preheater 5 while maintaining the above-mentioned temperature difference, and is used as combustion air.
Since the combustion air introduced into the boiler furnace 1 remains at a temperature distribution having the above-mentioned temperature difference, the combustion air temperature at the place where the thermometer is installed and the combustion air temperature set are set. This is the cause of the deviation.
【0006】また、蒸気式空気予熱器3は再生式空気予
熱器5入口の空気温度を上げて低温端メタル温度を高く
するために設けられている。再生式空気予熱器5の低温
端メタル温度は、蒸気式空気予熱器出口空気温度と再生
式空気予熱器出口ガス温度により設定されるが、再生式
空気予熱器5の低温層エレメントが蒸気式空気予熱器3
からの空気のうち、低温域の空気に接触した場合には予
定したエレメント温度よりも低い温度までしか上がら
ず、排ガス中に含まれる硫酸の酸露点以下となり硫酸の
凝縮による再生式空気予熱器5等を構成する機器の腐食
を引き起こす要因となることが問題となっていた。The steam-type air preheater 3 is provided for raising the air temperature at the inlet of the regenerative air preheater 5 to increase the low-temperature end metal temperature. The low-temperature end metal temperature of the regenerative air preheater 5 is set by the steam-type air preheater outlet air temperature and the regenerative air preheater outlet gas temperature. Preheater 3
When the air comes in contact with air in a low temperature range, the temperature rises only to a temperature lower than the expected element temperature, becomes lower than the acid dew point of sulfuric acid contained in the exhaust gas, and the regenerative air preheater 5 by condensation of sulfuric acid. It has been a problem that it may cause corrosion of devices constituting the device.
【0007】[0007]
【発明が解決しようとする課題】上記従来技術では、蒸
気式空気予熱器3の構造上、避けることができない出口
空気温度の不均一が生じる。その空気温度差に起因し
て、再生式空気予熱器5の低温エレメントが腐食する要
因となる。In the above prior art, due to the structure of the steam-type air preheater 3, the inevitable nonuniformity of the outlet air temperature occurs. The difference in air temperature causes corrosion of the low-temperature element of the regenerative air preheater 5.
【0008】本発明の課題は、再生式空気予熱器の低温
端エレメント温度の温度差を低減することを可能にする
ための空気予熱装置を提供することである。[0008] It is an object of the present invention to provide an air preheating apparatus for enabling a temperature difference between the low-temperature end element temperatures of a regenerative air preheater to be reduced.
【0009】[0009]
【課題を解決するための手段】本発明の上記課題は、燃
焼炉の燃料燃焼用空気の流路となる空気ダクトに上流か
ら順に配置された蒸気式空気予熱器と再生式空気予熱器
と、蒸気式空気予熱器出口部の空気ダクトに分岐して設
けられ、再生用空気予熱器をバイパスして燃焼用空気を
燃焼炉に供給するバイパスダクトと、前記蒸気式空気予
熱器出口の空気ダクトに設けた空気攪拌手段を備えた空
気予熱装置により解決される。SUMMARY OF THE INVENTION The object of the present invention is to provide a steam type air preheater and a regenerative type air preheater which are arranged in order from the upstream in an air duct serving as a flow path for fuel combustion air in a combustion furnace. The air duct at the outlet of the steam type air preheater is provided to be branched to the air duct at the outlet of the steam type air preheater, and the bypass duct supplies the combustion air to the combustion furnace by bypassing the regeneration air preheater. The problem is solved by an air preheating device provided with the provided air stirring means.
【0010】[0010]
【作用】蒸気式空気予熱器出口の空気ダクトに流体の混
合を目的とした空気攪拌手段を設けることで、蒸気式空
気予熱器出口における空気温度分布の不均一が低減さ
れ、再生式空気予熱器の低温端エレメント温度も温度差
が低減されて、再生式空気予熱器の低温エレメント等の
腐食を抑制することが可能となる。The non-uniform air temperature distribution at the outlet of the steam-type air preheater is reduced by providing air stirring means for mixing fluid in the air duct at the outlet of the steam-type air preheater. The temperature difference of the low-temperature end element temperature is also reduced, so that corrosion of the low-temperature element and the like of the regenerative air preheater can be suppressed.
【0011】[0011]
【発明の実施の形態】本発明の実施の形態を図面と共に
説明する。ボイラ火炉1に供給される燃焼用空気は、燃
焼に適した空気とするために再生式空気予熱器5をバイ
パスした冷空気と、再生式空気予熱器5を通過した熱空
気を混合させて使用している。このとき燃焼用空気温度
を調整するために再生式空気予熱器バイパスダクト11
に設けられた流量調整ダンパ12を開閉調整することで
冷空気流量を調整し、設定した燃焼用空気温度となるよ
うに制御している。Embodiments of the present invention will be described with reference to the drawings. Combustion air supplied to the boiler furnace 1 is used by mixing cold air that has bypassed the regenerative air preheater 5 and hot air that has passed through the regenerative air preheater 5 in order to make the air suitable for combustion. are doing. At this time, the regeneration air preheater bypass duct 11 is used to adjust the combustion air temperature.
The flow rate of the cold air is adjusted by opening and closing the flow rate adjusting damper 12 provided in the apparatus, and control is performed so that the temperature of the combustion air is set.
【0012】蒸気式空気予熱器3は図3に示すように上
端から供給された蒸気でボイラ燃焼用空気を熱交換する
ためのものである。蒸気式空気予熱器3で蒸気と熱交換
したボイラ燃焼用空気は図2に示すように上端と下端で
約50℃〜90℃程度の温度差が生じ、再生式空気予熱
器5に供給される。The steam type air preheater 3 is for exchanging heat for boiler combustion air with steam supplied from the upper end as shown in FIG. The boiler combustion air that has exchanged heat with steam in the steam type air preheater 3 has a temperature difference of about 50 ° C. to 90 ° C. at the upper end and the lower end as shown in FIG. 2 and is supplied to the regenerative air preheater 5. .
【0013】この温度差をもったまま再生式空気余熱器
をバイパスし、燃焼用空気として合流した場合、冷空気
は上端と下端で約50℃〜90℃程度の温度差を持って
いるため合流後の燃焼用空気温度が不均一となっていた
が、図1に示すように蒸気式空気予熱器出口の空気ダク
ト4に、パンチングプレート、プロペラ、エアフォイル
等で構成される空気攪拌手段13を設置し、蒸気式空気
予熱器出口の空気ダクト4内での温度差を低減すること
で、ボイラ火炉1の燃焼用空気温度の温度差を低減する
ことが可能となる。When the regenerative air preheater is bypassed while having this temperature difference and merged as combustion air, the cold air has a temperature difference of about 50 ° C. to 90 ° C. at the upper end and the lower end. Although the subsequent combustion air temperature was not uniform, as shown in FIG. 1, the air duct 4 at the outlet of the steam-type air preheater was provided with air stirring means 13 composed of a punching plate, a propeller, an air foil, and the like. By installing and reducing the temperature difference in the air duct 4 at the outlet of the steam-type air preheater, the temperature difference in the combustion air temperature of the boiler furnace 1 can be reduced.
【0014】さらに、再生式空気予熱器5は、その低温
エレメントの腐食防止のため低温端エレメント温度を設
定しているが、再生式空気予熱器5の入口空気に温度差
がある場合、再生式空気予熱器5の低温エレメントが蒸
気式空気予熱器3からの低温域の空気に接触した場合に
は予定したエレメント温度よりも低い温度までしか上昇
せず、ガス中に含まれる硫酸の酸露点以下となることに
よって、腐食の要因となっていた。Further, the regenerative air preheater 5 sets a low temperature end element temperature to prevent corrosion of the low temperature element. However, if there is a temperature difference between the inlet air of the regenerative air preheater 5 and the regenerative air preheater 5, When the low-temperature element of the air preheater 5 comes into contact with air in the low-temperature region from the steam-type air preheater 3, the temperature rises only to a temperature lower than the expected element temperature, and is lower than the acid dew point of sulfuric acid contained in the gas. Thus, corrosion was a factor.
【0015】しかし、蒸気式空気予熱器出口ダクト4に
空気攪拌手段13を設けることで再生式空気予熱器入口
空気温度の温度差を低減でき再生式空気予熱器5の低温
エレメントの腐食抑制が可能となる。However, by providing the air agitating means 13 in the steam type air preheater outlet duct 4, the temperature difference between the inlet air temperature of the regenerative air preheater can be reduced and the corrosion of the low temperature element of the regenerative air preheater 5 can be suppressed. Becomes
【0016】[0016]
【発明の効果】本発明によれば、蒸気式空気予熱器出口
ダクトに空気攪拌手段を設けることで、燃焼用空気温度
の温度差を低減でき、さらに再生式空気予熱器の入口空
気温度の温度差を低減することで再生式空気予熱器の低
温エレメント腐食を抑制することが可能となる。According to the present invention, by providing air stirring means at the outlet duct of the steam type air preheater, the temperature difference of the combustion air temperature can be reduced, and the temperature of the inlet air temperature of the regenerative air preheater can be reduced. By reducing the difference, low-temperature element corrosion of the regenerative air preheater can be suppressed.
【図1】 本発明の実施の形態の空気予熱装置の蒸気式
空気予熱器出口の空気ダクト部分の概略図である。FIG. 1 is a schematic view of an air duct portion at an outlet of a steam-type air preheater of an air preheating apparatus according to an embodiment of the present invention.
【図2】 従来技術の空気予熱装置の蒸気式空気予熱器
出口ダクトの空気温度分布を示す図である。FIG. 2 is a diagram showing an air temperature distribution of an outlet duct of a steam-type air preheater of an air preheating apparatus according to the related art.
【図3】 従来技術の空気予熱装置の蒸気式空気予熱器
出口ダクトの概略図である。FIG. 3 is a schematic view of a steam air preheater outlet duct of a prior art air preheating device.
【図4】 ボイラプラントの概略図である。FIG. 4 is a schematic diagram of a boiler plant.
1 ボイラ火炉 2 空気ダ
クト 3 蒸気式空気予熱器 4 空気ダ
クト 5 再生式空気予熱器 6 過熱器 7 蒸発器 8 節炭器 9 脱硝装置 10 煙突 11 再生式空気余熱器バイパスダクト 12 流量
調整ダンパ 13 空気攪拌手段REFERENCE SIGNS LIST 1 boiler furnace 2 air duct 3 steam type air preheater 4 air duct 5 regenerative air preheater 6 superheater 7 evaporator 8 economizer 9 denitrification device 10 chimney 11 regenerative air preheater bypass duct 12 flow control damper 13 air Stirring means
Claims (1)
気ダクトに上流から順に配置された蒸気式空気予熱器と
再生式空気予熱器と、蒸気式空気予熱器出口部の空気ダ
クトに分岐して設けられ、再生用空気予熱器をバイパス
して燃焼用空気を燃焼炉に供給するバイパスダクトと、
前記蒸気式空気予熱器出口の空気ダクトに設けた空気攪
拌手段を備えたことを特徴とする空気予熱装置。1. A steam-type air preheater, a regenerative-type air preheater, and an air duct at an outlet of a steam-type air preheater, which are sequentially arranged from an upstream in an air duct serving as a flow path of fuel combustion air in a combustion furnace. A bypass duct which is provided in a branched manner and bypasses the regeneration air preheater and supplies combustion air to the combustion furnace;
An air preheating device comprising air stirring means provided in an air duct at an outlet of the steam type air preheater.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25578799A JP2001082735A (en) | 1999-09-09 | 1999-09-09 | Air preheater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25578799A JP2001082735A (en) | 1999-09-09 | 1999-09-09 | Air preheater |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2001082735A true JP2001082735A (en) | 2001-03-30 |
Family
ID=17283635
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25578799A Pending JP2001082735A (en) | 1999-09-09 | 1999-09-09 | Air preheater |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2001082735A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102252339A (en) * | 2011-05-12 | 2011-11-23 | 华北电力大学(保定) | System for reducing discharge smoke temperature of power station boiler |
KR101267827B1 (en) | 2009-05-08 | 2013-05-27 | 포스터 휠러 에너지아 오와이 | Thermal power boiler |
CN103672872A (en) * | 2013-01-18 | 2014-03-26 | 北京神雾环境能源科技集团股份有限公司 | Granular fuel boiler with heat accumulation type rotary reversing heater |
CN104061584A (en) * | 2014-07-11 | 2014-09-24 | 岳阳钟鼎热工电磁科技有限公司 | Heat accumulating type slewing air preheater |
CN106402924A (en) * | 2016-10-22 | 2017-02-15 | 无锡翔龙环球科技股份有限公司 | Boiler waste heat recycling and pipe anti-abrasion system |
-
1999
- 1999-09-09 JP JP25578799A patent/JP2001082735A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101267827B1 (en) | 2009-05-08 | 2013-05-27 | 포스터 휠러 에너지아 오와이 | Thermal power boiler |
US9163835B2 (en) | 2009-05-08 | 2015-10-20 | Amec Foster Wheeler Energia Oy | Thermal power boiler |
CN102252339A (en) * | 2011-05-12 | 2011-11-23 | 华北电力大学(保定) | System for reducing discharge smoke temperature of power station boiler |
CN103672872A (en) * | 2013-01-18 | 2014-03-26 | 北京神雾环境能源科技集团股份有限公司 | Granular fuel boiler with heat accumulation type rotary reversing heater |
CN104061584A (en) * | 2014-07-11 | 2014-09-24 | 岳阳钟鼎热工电磁科技有限公司 | Heat accumulating type slewing air preheater |
CN106402924A (en) * | 2016-10-22 | 2017-02-15 | 无锡翔龙环球科技股份有限公司 | Boiler waste heat recycling and pipe anti-abrasion system |
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