JPH10339407A - Combustion apparatus - Google Patents
Combustion apparatusInfo
- Publication number
- JPH10339407A JPH10339407A JP15115097A JP15115097A JPH10339407A JP H10339407 A JPH10339407 A JP H10339407A JP 15115097 A JP15115097 A JP 15115097A JP 15115097 A JP15115097 A JP 15115097A JP H10339407 A JPH10339407 A JP H10339407A
- Authority
- JP
- Japan
- Prior art keywords
- air
- pressure air
- stage combustion
- pressure
- low
- 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
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 172
- 239000003245 coal Substances 0.000 claims abstract description 7
- 238000001035 drying Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 17
- 230000000630 rising effect Effects 0.000 description 10
- 238000010586 diagram Methods 0.000 description 9
- 230000001174 ascending effect Effects 0.000 description 7
- 230000002093 peripheral effect Effects 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
Landscapes
- Air Supply (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は燃焼装置に係り、特
に二段燃焼により低NOx燃焼を行うのに未燃分を低減
するのに好適な燃焼装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combustion apparatus, and more particularly to a combustion apparatus suitable for performing low NOx combustion by two-stage combustion and reducing unburned components.
【0002】[0002]
【従来の技術】低NOx燃焼のため二段燃焼システムが
広く適用されている。図10に微粉炭燃焼ボイラにおけ
る一般的な二段燃焼システムの空気系統を示す。微粉炭
を乾燥及び搬送するための一次空気は、一次空気ファン
1によって供給される。一次空気は空気予熱器2によっ
て所定の温度まで温められた後微粉炭機(ミル)3に導
入され、微粉炭を乾燥させると共にバーナ4を通して火
炉5へ搬送する。2. Description of the Related Art Two-stage combustion systems are widely applied for low NOx combustion. FIG. 10 shows an air system of a general two-stage combustion system in a pulverized coal combustion boiler. Primary air for drying and conveying the pulverized coal is supplied by a primary air fan 1. After the primary air is heated to a predetermined temperature by the air preheater 2, it is introduced into a pulverized coal machine (mill) 3, where the pulverized coal is dried and conveyed to a furnace 5 through a burner 4.
【0003】一方、燃焼用空気(二次空気)は押込空気
ファン6によって供給される。二次空気は空気予熱器2
で所定の温度まで温められた後、風道7を通してバーナ
用風箱9及び二段燃焼用風箱12に供給され、バーナ4
及び二段燃焼用空気投入口13から火炉に導入される。
二段燃焼システムにおいては、バーナ4から供給される
一次空気と二次空気の総量は一般に理論空気流量より少
なく、完全燃焼に必要な残りの空気は過剰に供給する空
気分も加えて二段燃焼用空気投入口13から供給され
る。On the other hand, combustion air (secondary air) is supplied by a forced air fan 6. Secondary air is air preheater 2
After being warmed to a predetermined temperature in the burner 4, it is supplied to the burner wind box 9 and the two-stage combustion wind box 12 through the wind path 7,
And it is introduce | transduced into a furnace from the air inlet 13 for two-stage combustion.
In the two-stage combustion system, the total amount of the primary air and the secondary air supplied from the burner 4 is generally smaller than the theoretical air flow rate, and the remaining air required for complete combustion is the two-stage combustion in addition to the excess air supply. It is supplied from the air inlet 13.
【0004】従って、バーナ4から供給される空気流量
による燃焼ガス中には未燃分が生じており、未燃分の完
全燃焼を促進するためには、二段燃焼用空気を火炉内で
十分に混合させる必要がある。この目的のために、二段
燃焼用風箱12の圧力はバーナ用風箱9の圧力より高く
して二段燃焼用空気の投入速度を速くすることが一般に
行われている。その結果、図10において、バーナ用風
箱9には、風道7から高圧で供給された高圧空気をバー
ナ用空気ダンパ8によって圧力を低めた低圧空気が供給
される。このようなバーナ用空気ダンパ8による圧力損
失はすなわち、それがエネルギー損失となる。[0004] Therefore, unburned components are generated in the combustion gas due to the flow rate of the air supplied from the burner 4, and in order to promote complete combustion of the unburned components, the two-stage combustion air is sufficiently supplied in the furnace. Must be mixed. To this end, it is common practice to increase the pressure of the two-stage combustion air box 12 by making the pressure of the two-stage combustion air box 12 higher than the pressure of the burner wind box 9. As a result, in FIG. 10, low-pressure air is supplied to the burner wind box 9 by reducing the pressure of the high-pressure air supplied from the wind path 7 at a high pressure by the burner air damper 8. Such a pressure loss due to the burner air damper 8 is an energy loss.
【0005】また、二段燃焼用空気系統にブーストアッ
プファン10を設ける場合がある。図11は本ブースト
アップファン10を使用した例を示している。風道7か
ら低圧で供給された低圧空気の一部は分岐して二段燃焼
用風箱12への風道に流れ、ブーストアップファン10
によって昇圧された後に二段燃焼用風箱12に供給さ
れ、高圧空気となって二段燃焼用空気投入口13から火
炉5へ導入される。In some cases, a boost-up fan 10 is provided in the two-stage combustion air system. FIG. 11 shows an example in which the boost-up fan 10 is used. A part of the low-pressure air supplied at a low pressure from the wind path 7 branches and flows into the wind path to the two-stage combustion wind box 12, and the boost-up fan 10
After being pressurized, the air is supplied to the two-stage combustion air box 12, becomes high-pressure air, and is introduced into the furnace 5 from the two-stage combustion air inlet 13.
【0006】図11に示す従来例においては、バーナ側
の二次空気系統に抵抗を与えることなく二段燃焼用空気
のみの圧力を高めることができるので、図10の例に比
べてエネルギー損失を抑えることができる。In the conventional example shown in FIG. 11, the pressure of only the two-stage combustion air can be increased without giving any resistance to the secondary air system on the burner side. Can be suppressed.
【0007】しかしながら、二段燃焼用空気は火路に投
入されるため空気予熱器2により昇温されており、容積
流量の増加によるブーストアップファン10の動力が過
大となる。However, the temperature of the two-stage combustion air is increased by the air preheater 2 because it is injected into the fireway, and the power of the boost-up fan 10 becomes excessive due to an increase in the volume flow rate.
【0008】[0008]
【発明が解決しようとする課題】図10の例において
は、バーナ用空気ダンパの圧力損失がそのままエネルギ
ー損失となる。In the example shown in FIG. 10, the pressure loss of the air damper for the burner directly becomes an energy loss.
【0009】また、図11の例においては、バーナ側の
圧力損失によるエネルギー損失は抑えられるが、二段燃
焼用空気の昇圧は空気予熱器2で昇温された後に行われ
るため、容積流量の増加に伴うファン動力の増加が無視
できず、結果的に図10の例におけるエネルギー損失と
大差なくなる。In the example of FIG. 11, energy loss due to pressure loss on the burner side is suppressed, but the pressure of the two-stage combustion air is increased after the temperature is increased by the air preheater 2, so that the volume flow rate is reduced. The increase in fan power accompanying the increase cannot be ignored, and as a result, there is no much difference from the energy loss in the example of FIG.
【0010】[0010]
【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。In order to solve the above problems, the present invention mainly employs the following configuration.
【0011】微粉炭を乾燥してバーナに搬送して燃焼さ
せるための一次空気を微粉炭機に供給する高圧空気供給
系統と、バーナ風箱に前記高圧空気よりも圧力の低い低
圧空気を供給する低圧空気供給系統と、火路内のバーナ
下流側に二段燃焼用空気を投入する手段と、を設けた燃
焼装置において、前記二段燃焼用空気を投入する手段
に、前記高圧空気供給系統および前記低圧空気供給系統
からの高圧空気および低圧空気の一部を供給する系統を
設けた燃焼装置。A high-pressure air supply system for supplying primary air for pulverized coal to be conveyed to a burner for combustion by a burner, and a low-pressure air having a lower pressure than the high-pressure air to a burner wind box. In a combustion device provided with a low-pressure air supply system and a means for charging the two-stage combustion air downstream of the burner in the fire path, the means for charging the two-stage combustion air includes the high-pressure air supply system and A combustion device provided with a system for supplying a part of high-pressure air and low-pressure air from the low-pressure air supply system.
【0012】[0012]
【発明の実施の形態】本発明の実施形態に係る燃焼装置
の空気系統に関する構成を図1に示す。図1において、
1は一次空気ファン、2は空気予熱器、3はミル、4は
バーナ、5は火炉、6は押込空気ファン、7は風道、8
はバーナ用空気ダンパ、9はバーナ用風箱、13は二段
燃焼用空気投入口、21は二段燃焼用高圧側空気供給系
統、22は二段燃焼用高圧空気ダンパ、23は二段燃焼
用高圧側風箱、24は二段燃焼用低圧側空気供給系統、
25は二段燃焼用低圧空気ダンパ、26は二段燃焼用低
圧側風箱、をそれぞれ表す。また、二段燃焼用空気投入
口13は、通常はそれぞれバーナ4の真上に設けられ
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows a configuration relating to an air system of a combustion apparatus according to an embodiment of the present invention. In FIG.
1 is a primary air fan, 2 is an air preheater, 3 is a mill, 4 is a burner, 5 is a furnace, 6 is a forced air fan, 7 is a wind path, 8
Is a burner air damper, 9 is a burner wind box, 13 is a two-stage combustion air inlet, 21 is a two-stage combustion high-pressure air supply system, 22 is a two-stage combustion high-pressure air damper, and 23 is a two-stage combustion. High-pressure side wind box, 24 is a low-pressure side air supply system for two-stage combustion,
25 denotes a low pressure air damper for two-stage combustion, and 26 denotes a low pressure side wind box for two-stage combustion. In addition, the two-stage combustion air inlets 13 are usually provided directly above the burners 4 respectively.
【0013】図1に示す燃焼装置の空気系統の全体構成
は、図10に示す従来技術の空気系統の構成と基礎的な
構成においては類似するが、本発明の実施形態は、以下
説明する技術的事項に特徴がある。Although the overall configuration of the air system of the combustion apparatus shown in FIG. 1 is similar in basic configuration to the configuration of the air system of the prior art shown in FIG. 10, the embodiment of the present invention is based on the technology described below. There is a characteristic in the subject matter.
【0014】一次空気ファン1からの一次空気の一部は
ミル3に供給される前に分岐し、高圧の二段燃焼用空気
として専用の二段燃焼用高圧側空気供給系統21を通し
て二段燃焼用高圧側風箱23に導入される。A part of the primary air from the primary air fan 1 is branched before being supplied to the mill 3 and is subjected to a two-stage combustion through a dedicated two-stage combustion high-pressure air supply system 21 as high-pressure two-stage combustion air. Is introduced into the high pressure side wind box 23.
【0015】一方、押込空気ファン6からの低圧の二次
空気の一部は分岐して二段燃焼用低圧側風箱26に導入
される。高圧側風箱23と低圧側風箱26の各々の空気
流量は二段燃焼用高圧空気ダンパ22及び二段燃焼用低
圧空気ダンパ25によって調整、制御される。On the other hand, part of the low-pressure secondary air from the forced air fan 6 is branched and introduced into the two-stage combustion low-pressure side wind box 26. The air flow rate of each of the high-pressure side wind box 23 and the low-pressure side wind box 26 is adjusted and controlled by the two-stage combustion high-pressure air damper 22 and the two-stage combustion low-pressure air damper 25.
【0016】図2は本実施形態特有の二段燃焼用空気投
入口13周辺の構造を示す。図2に示すように、風箱は
二段燃焼用高圧側風箱23と二段燃焼用低圧側風箱26
に分割されている。二段燃焼用高圧側風箱23には二段
燃焼用高圧側空気供給系統21から、また二段燃焼用低
圧側風箱26には二段燃焼用低圧側空気供給系統24か
ら二段燃焼用空気がそれぞれ供給される。FIG. 2 shows the structure around the two-stage combustion air inlet 13 unique to this embodiment. As shown in FIG. 2, the wind box includes a high-pressure side wind box 23 for two-stage combustion and a low-pressure side wind box 26 for two-stage combustion.
Is divided into The two-stage combustion high pressure side air box 23 is supplied from the two-stage combustion high pressure side air supply system 21, and the two-stage combustion low pressure side wind box 26 is supplied from the two-stage combustion low pressure side air supply system 24. Air is respectively supplied.
【0017】二段燃焼用高圧側空気供給系統21からの
高圧側空気21’は二段燃焼用高圧側風箱23から二段
燃焼用内周空気取入口27を通して二段燃焼用内周空気
供給筒28に導かれた後に火炉5へと投入される。ま
た、二段燃焼用低圧側空気供給系統24からの低圧側空
気24’は二段燃焼用低圧側風箱26から二段燃焼用外
周空気投入口30に設けた二段燃焼用外周空気旋回器2
9によって旋回を与えられた後に火炉5に投入される。The high-pressure side air 21 ′ from the high-pressure side air supply system 21 for the two-stage combustion is supplied from the high-pressure side wind box 23 for the two-stage combustion through the inner-stage air intake 27 for the two-stage combustion. After being guided to the cylinder 28, it is put into the furnace 5. The low-pressure side air 24 ′ from the two-stage combustion low-pressure side air supply system 24 is supplied from the two-stage combustion low-pressure side wind box 26 to the two-stage combustion peripheral air inlet 30 provided at the two-stage combustion peripheral air inlet 30. 2
After being turned by 9, it is put into the furnace 5.
【0018】本実施形態の効果を説明する前に、二段燃
焼を行う燃焼装置における火炉内上昇ガスの流動パター
ンについて図3の(a)、(b)を用いて説明する。バ
ーナ4の噴流は火炉5の中央部で対向する噴流と衝突す
るため、上昇ガス流速は火炉側面から見ると火炉中央部
で最も速くなる。このような現象を特に、図3の(b)
側面図で示している。Before describing the effects of the present embodiment, the flow pattern of the ascending gas in the furnace in a combustion device performing two-stage combustion will be described with reference to FIGS. 3 (a) and 3 (b). Since the jet of the burner 4 collides with the opposing jet at the center of the furnace 5, the rising gas flow velocity becomes the highest at the center of the furnace when viewed from the side of the furnace. In particular, such a phenomenon is illustrated in FIG.
It is shown in a side view.
【0019】一方、火炉幅方向においては、バーナ直上
の部分で最も速い上昇流速となる。このような現象を特
に、図3の(a)正面図で示している。また、図4に示
すように、二段燃焼用空気はバーナ側から上昇してくる
上昇ガス流によって図4のようにガス流れ下流側である
ところの火炉上部に向けて曲げられるが、図4の(a)
に示すように、二段燃焼用空気噴流の流速が速い程曲げ
られ難く、また、図4の(b)に示すように、二段燃焼
用空気噴流の流速が遅い程曲げられ易い。すなわち、二
段燃焼用空気噴流の流速が最も遅くなる火路の中央付近
においては、バーナ側から上昇してくる上昇ガス流と二
段燃焼用空気の混合が最も悪くなる。したがって、二段
燃焼用空気をより火炉の中央まで供給して混合を促進す
る必要があり、このためには、二段燃焼用空気噴流の流
速を高めること、ひいては高圧の二段燃焼用空気を供給
することが必要となる。On the other hand, in the furnace width direction, the highest ascending flow velocity is obtained immediately above the burner. Such a phenomenon is particularly shown in the front view of FIG. As shown in FIG. 4, the two-stage combustion air is bent toward the upper part of the furnace at the downstream side of the gas flow as shown in FIG. 4 by the rising gas flow rising from the burner side. (A)
As shown in FIG. 4, the higher the flow velocity of the two-stage combustion air jet, the harder it is to bend, and as shown in FIG. 4B, the lower the flow velocity of the two-stage combustion air jet, the easier it is to bend. That is, in the vicinity of the center of the fire path where the flow velocity of the two-stage combustion air jet is the slowest, the mixing of the rising gas flow rising from the burner side and the two-stage combustion air is the worst. Therefore, it is necessary to supply the two-stage combustion air further to the center of the furnace to promote the mixing, and for this purpose, it is necessary to increase the flow velocity of the two-stage combustion air jet, and thus to increase the high-pressure two-stage combustion air. It is necessary to supply.
【0020】したがって、本実施形態によれば、一次空
気ファン1からの高圧空気21’を二段燃焼用高圧側空
気供給系統21から供給しているので、二段燃焼用空気
を火路の中央まで供給することができる。しかしなが
ら、例えば、一次空気ファン1の出口圧力は約1000
mmAqと高く、このような二段燃焼用空気噴流には広
がりがなく、バーナ側からの上昇ガス流との混合は部分
的には良くなるが、すり抜ける部分が生じる場合があ
る。したがって、本実施形態では、さらに前記二段燃焼
用空気投入口13からは、高圧側空気21’とともに低
圧側空気24’を投入する構成としている。Therefore, according to the present embodiment, since the high-pressure air 21 'from the primary air fan 1 is supplied from the high-pressure side air supply system 21 for the two-stage combustion, the two-stage combustion air is supplied to the center of the fire path. Can be supplied up to. However, for example, the outlet pressure of the primary air fan 1 is about 1000
As high as mmAq, such a two-stage combustion air jet has no spread, and the mixing with the rising gas flow from the burner side is partially improved, but there are cases where slip-through portions occur. Therefore, in the present embodiment, the low-pressure side air 24 'is supplied together with the high-pressure side air 21' from the two-stage combustion air supply port 13.
【0021】ここで、図2の実施形態における二段燃焼
用空気の火炉内流動パターンを図5に示す。図5は火路
の側断面図である。内周高圧空気噴流110は高流速且
つ非旋回のため、火炉5の奥行き方向の貫通力が高く火
炉中央部における混合を促進する。一方、外周低圧空気
噴流111は旋回により広がりを有し、内周高圧空気噴
流110の周囲に広がることで、前記内周高圧空気噴流
110により混合されずにすり抜けようとする上昇ガス
との混合に寄与する。すなわち、図3の火路内上昇ガス
の流動パターンに適した二段燃焼用空気の投入が可能と
なる。その結果、エネルギー損失を最小限に抑えて二段
燃焼用空気の混合を効率的に高めることが可能となる。FIG. 5 shows a flow pattern of the two-stage combustion air in the furnace in the embodiment of FIG. FIG. 5 is a side sectional view of a fireway. Since the inner peripheral high-pressure air jet 110 has a high flow velocity and does not swirl, the penetration force in the depth direction of the furnace 5 is high, and the mixing at the center of the furnace is promoted. On the other hand, the outer peripheral low-pressure air jet 111 has a spread due to swirling, and spreads around the inner peripheral high-pressure air jet 110, so that the outer peripheral low-pressure air jet 111 is mixed with the rising gas that tends to slip through without being mixed by the inner peripheral high-pressure air jet 110. Contribute. That is, it is possible to supply the two-stage combustion air suitable for the flow pattern of the rising gas in the fire path in FIG. As a result, it is possible to efficiently increase the mixing of the two-stage combustion air while minimizing the energy loss.
【0022】図1、図2、図6は、高圧空気と低圧空気
とを同心円状に噴出する二段燃焼用空気投入口の例であ
るが、高圧空気と低圧空気とを別々の投入口から噴出す
る例を図6に示す。FIGS. 1, 2 and 6 show examples of two-stage combustion air inlets for ejecting high-pressure air and low-pressure air concentrically. High-pressure air and low-pressure air are supplied from separate inlets. FIG. 6 shows an example of ejection.
【0023】図6は、高圧側および低圧側二段燃焼用空
気投入口の配置例を示す他の実施形態である。バーナ4
の直上に高圧側二段燃焼用空気投入口112を、またバ
ーナとバーナとの間の直上及び側壁14寄りに低圧側二
段燃焼用空気投入口113を設置している。ここで、側
壁寄りに低圧側二段燃焼用空気投入口113を配置した
のは、バーナ真上に高圧側二段燃焼用空気投入口112
を配置したことによるが、これにより側壁側からのすり
抜けが防止できる。また、バーナ真上に高圧側二段燃焼
用空気投入口112を配置することにより、最も上昇速
度が大となるバーナ真上の流速を低下させ混合が促進さ
れる。FIG. 6 shows another embodiment of the arrangement of the high-pressure side and low-pressure side two-stage combustion air inlets. Burner 4
A high-pressure side two-stage combustion air inlet 112 is provided immediately above the burner, and a low-pressure side two-stage combustion air inlet 113 is provided immediately above the burner and near the side wall 14. The reason why the low-pressure side two-stage combustion air inlet 113 is disposed near the side wall is that the high-pressure side two-stage combustion air inlet 112 is located directly above the burner.
Is disposed, but it is possible to prevent slippage from the side wall side. In addition, by disposing the high-pressure-side two-stage combustion air inlet 112 directly above the burner, the flow velocity just above the burner where the ascending speed is the highest is reduced, and the mixing is promoted.
【0024】図7は火路の横断面図であり、図6に示す
二段燃焼用空気投入口の構造例を示す実施形態である。
風箱は二段燃焼用高圧側風箱23と二段燃焼用低圧側風
箱26に分割されている。二段燃焼用高圧側風箱23に
は図1と同様に二段燃焼用高圧側空気供給系統21か
ら、また二段燃焼用低圧側風箱26には図1と同様に二
段燃焼用低圧側空気供給系統24から二段燃焼用空気が
供給される。高圧側二段燃焼用空気投入口203と低圧
側二段燃焼用空気投入口206は火路幅方向に交互に設
置されており、高圧側空気は二段燃焼用高圧側風箱23
から二段燃焼用高圧側空気供給筒202を通して二段燃
焼用高圧側空気投入口203から火炉5へと投入され
る。FIG. 7 is a cross-sectional view of a fire path, and is an embodiment showing a structural example of the two-stage combustion air inlet shown in FIG.
The wind box is divided into a high pressure side wind box 23 for two-stage combustion and a low pressure side wind box 26 for two-stage combustion. The high-pressure side wind box 23 for the two-stage combustion is supplied from the high-pressure side air supply system 21 for the two-stage combustion as in FIG. 1, and the low-pressure side wind box 26 for the two-stage combustion is supplied with the low-pressure The two-stage combustion air is supplied from the side air supply system 24. The high-pressure side two-stage combustion air inlet 203 and the low-pressure side two-stage combustion air inlet 206 are arranged alternately in the width direction of the fire path.
From the high-pressure side air supply cylinder 202 for two-stage combustion, and is introduced into the furnace 5 from the high-pressure side air inlet 203 for two-stage combustion.
【0025】また、低圧側空気は二段燃焼用低圧側風箱
26から二段燃焼用低圧空気旋回器205によって旋回
を与えられた後、二段燃焼用低圧空気投入口206から
火炉5に投入される。本実施形態は火炉幅方向のバーナ
とバーナとの間の距離が長く、図2の実施形態に示す高
圧空気と低圧空気の噴出が同心円状に行われる単一型の
二段燃焼用空気投入口の場合に、低圧側外周空気によっ
てバーナとバーナ間の直上の未燃ガスに対して十分に二
段燃焼用空気を混合できない場合に適しており、二段燃
焼用低圧空気投入口206をバーナとバーナ間の直上部
に設け、二段燃焼用高圧側空気投入口203からの噴流
を補完するように低圧空気を噴出することにより、未燃
ガスのすり抜けを防止し、混合するので未燃分を減少す
ることができる。The low-pressure side air is swirled by the two-stage combustion low-pressure air swirler 205 from the two-stage combustion low-pressure side wind box 26, and is then injected into the furnace 5 through the two-stage combustion low-pressure air inlet 206. Is done. In this embodiment, the distance between the burners in the furnace width direction is long, and a single-type two-stage combustion air inlet in which high-pressure air and low-pressure air are concentrically ejected as shown in the embodiment of FIG. Is suitable for a case where the two-stage combustion air cannot be sufficiently mixed with the unburned gas immediately above the burner due to the low-pressure side outer air, and the two-stage combustion low-pressure air inlet 206 is connected to the burner. It is provided immediately above the burner and blows out low-pressure air so as to complement the jet from the high-pressure side air inlet 203 for two-stage combustion, thereby preventing the unburned gas from slipping through and mixing the unburned gas. Can be reduced.
【0026】図8に燃焼装置の他の実施形態の空気系統
を示す。低圧側空気用風箱303は上段に、高圧側空気
用風箱308は下段に設けられており、押込空気ファン
6からの低圧空気は、空気予熱器2を経由してバーナ用
風箱9への系統から分岐した後、上段AAP(Afte
r Air Port)空気系統301、上段AAP空
気ダンパ302を経由して低圧側空気用風箱303へ供
給される。FIG. 8 shows an air system of another embodiment of the combustion apparatus. The low-pressure air box 303 is provided in the upper part and the high-pressure air box 308 is provided in the lower part. The low-pressure air from the forced air fan 6 passes through the air preheater 2 to the burner box 9. After branching from the system of
r Air Port) The air is supplied to a low-pressure air box 303 via an air system 301 and an upper AAP air damper 302.
【0027】また、一次空気ファン1からの高圧空気
は、空気予熱器2を経由して、ミル3への系統から分岐
した後、下段AAP空気系統306、下段AAP空気ダ
ンパ307を経由して高圧側空気用風箱308から供給
される。各々の空気流量は入口のダンパ302,307
によって調節される。The high-pressure air from the primary air fan 1 passes through the air preheater 2, branches off from the system to the mill 3, and then passes through the lower AAP air system 306 and the lower AAP air damper 307. It is supplied from the side air wind box 308. Each air flow rate is controlled by inlet dampers 302, 307.
Adjusted by.
【0028】本実施形態においては、多段に供給するこ
とで未燃分を含む上昇ガスと二段燃焼用空気とが混合し
て燃焼するのを段階的に行う。ここで、1段で供給する
場合には酸素リッチな状態での燃焼となりNOxが発生
しやすいが、本実施形態では、2段階に分けて供給する
ので、酸素リッチとなるのを抑えられ、低NOx燃焼が
行える。In the present embodiment, the rising gas containing the unburned portion and the two-stage combustion air are mixed and burned stepwise by being supplied in multiple stages. Here, if the supply is performed in one stage, combustion occurs in an oxygen-rich state, and NOx is easily generated. However, in the present embodiment, since the supply is performed in two stages, the oxygen-rich state can be suppressed, and NOx combustion can be performed.
【0029】また、下段に火炉内上昇ガス流に曲げられ
難い高圧側空気を、上段に曲げられ易い低圧側空気を投
入することにより火路中央部の上昇ガス流の流速を抑え
ることができ、未燃分のすり抜けを防止できる。Further, by feeding high-pressure side air which is hardly bent into the ascending gas flow in the furnace at the lower stage and low-pressure side air which is easily bent at the upper stage, the flow velocity of the rising gas flow at the center of the fire path can be suppressed. Unburnable components can be prevented from slipping through.
【0030】図9は二段燃焼用空気の制御方法の実施形
態を示す。ここでは、燃焼負荷100%のときの二段燃
焼空気流量を100%としている。燃焼負荷が高いほど
二段燃焼用空気投入位置における火炉内の上昇ガス流速
は高くなるため、混合性能を確保するためには負荷が高
いほど二段燃焼用空気の貫通力を高める必要がある。ま
た、燃焼負荷が低くなると、火路内の上昇ガスの流速は
遅くなるため、高圧空気量を減少することができる。FIG. 9 shows an embodiment of a method for controlling two-stage combustion air. Here, the two-stage combustion air flow rate when the combustion load is 100% is set to 100%. The higher the combustion load, the higher the ascending gas flow rate in the furnace at the two-stage combustion air input position. Therefore, in order to ensure mixing performance, the higher the load, the higher the penetration force of the two-stage combustion air must be. Further, when the combustion load is reduced, the flow velocity of the ascending gas in the fire path is reduced, so that the amount of high-pressure air can be reduced.
【0031】本実施形態においては、高圧側空気流量が
全二段燃焼用空気流量に占める比率を、負荷が高いほど
高め、50%以下の低負荷においては低圧側空気のみを
供給するように制御している。その結果、全負荷域で二
段燃焼用空気の混合性能を確保すると共に、負荷が下が
ると共に高圧側空気流量を低減して、エネルギー消費の
低減を図っている。また、燃焼負荷に応じて高圧空気と
低圧空気の流量比率を変更するのみならず、それらの流
量そのものを増減している。In this embodiment, the ratio of the high-pressure side air flow rate to the total two-stage combustion air flow rate is increased as the load increases, and only the low-pressure side air is supplied at a low load of 50% or less. doing. As a result, the mixing performance of the two-stage combustion air is ensured in the entire load range, the load is reduced, and the high-pressure side air flow rate is reduced, thereby reducing energy consumption. Further, not only the flow rate ratio between the high-pressure air and the low-pressure air is changed according to the combustion load, but also the flow rate itself is increased or decreased.
【0032】以上説明したように、本発明によれば、二
段燃焼用空気を減圧することなく供給するため、エネル
ギー損失を最小限に抑えて二段燃焼用空気の混合を確保
できる。As described above, according to the present invention, since the two-stage combustion air is supplied without decompression, energy loss can be minimized and mixing of the two-stage combustion air can be ensured.
【0033】[0033]
【発明の効果】本発明によれば、エネルギー損失を最小
限に抑えて二段燃焼用空気の混合を確保できるため、高
効率な燃焼装置を提供することができる。According to the present invention, since the mixing of the two-stage combustion air can be ensured while minimizing the energy loss, a highly efficient combustion apparatus can be provided.
【図1】本発明の実施形態に係る燃焼装置の空気系統を
示す図である。FIG. 1 is a diagram showing an air system of a combustion device according to an embodiment of the present invention.
【図2】本発明の実施形態となる燃焼装置の空気系統に
係る二段燃焼用空気投入口の構造を示す図である。FIG. 2 is a diagram showing a structure of a two-stage combustion air inlet relating to an air system of a combustion device according to an embodiment of the present invention.
【図3】二段燃焼用空気投入位置における火炉内上昇ガ
スの流速分布例を示す図である。FIG. 3 is a diagram showing an example of a flow velocity distribution of ascending gas in a furnace at a two-stage combustion air charging position.
【図4】二段燃焼用空気噴流が火炉内上昇流によって曲
げられる様子を示す説明図である。FIG. 4 is an explanatory view showing a state in which a two-stage combustion air jet is bent by an upward flow in a furnace.
【図5】本発明の実施形態となる燃焼装置の二段燃焼用
空気投入口からの二段燃焼用空気噴流のパターンを示す
図である。FIG. 5 is a view showing a pattern of a two-stage combustion air jet from a two-stage combustion air inlet of the combustion apparatus according to the embodiment of the present invention.
【図6】本発明の他の実施形態に係る二段燃焼用空気投
入口の配置例を示す図である。FIG. 6 is a diagram showing an example of an arrangement of a two-stage combustion air inlet according to another embodiment of the present invention.
【図7】図6における二段燃焼用空気投入口の構造例を
示す図である。7 is a diagram showing a structural example of a two-stage combustion air inlet in FIG.
【図8】本発明の他の実施形態に係る二段燃焼用空気系
統を示す図である。FIG. 8 is a diagram showing a two-stage combustion air system according to another embodiment of the present invention.
【図9】二段燃焼用空気噴流の制御方法を示す図であ
る。FIG. 9 is a diagram showing a method for controlling a two-stage combustion air jet.
【図10】従来技術における空気系統の例を示す図であ
る。FIG. 10 is a diagram showing an example of an air system according to the related art.
【図11】従来技術の空気系統において二段燃焼用空気
系統に昇圧ファンを設けた例を示す図である。FIG. 11 is a diagram showing an example in which a booster fan is provided in a two-stage combustion air system in a conventional air system.
1 一次空気ファン 2 空気予熱器 3 ミル 4 バーナ 5 火炉 6 押込空気ファン 7 風道 8 バーナ用空気ダンパ 9 バーナ用風箱 13 二段燃焼用空気投入口 21 二段燃焼用高圧側空気供給系統 22 二段燃焼用高圧空気ダンパ 23 二段燃焼用高圧側風箱 24 二段燃焼用低圧側空気供給ライン 25 二段燃焼用低圧空気ダンパ 26 二段燃焼用低圧側風箱 27 二段燃焼用内周空気取入口 28 二段燃焼用内周空気供給筒 29 二段燃焼用外周空気旋回器 30 二段燃焼用外周空気投入口 110 内周高圧空気噴流 111 外周低圧空気噴流 112 高圧側二段燃焼用空気投入口 113 低圧側二段燃焼用空気投入口 DESCRIPTION OF SYMBOLS 1 Primary air fan 2 Air preheater 3 Mill 4 Burner 5 Furnace 6 Push-in air fan 7 Wind path 8 Burner air damper 9 Burner wind box 13 Two-stage combustion air inlet 21 High pressure side air supply system for two-stage combustion 22 High-pressure air damper for two-stage combustion 23 High-pressure side wind box for two-stage combustion 24 Low-pressure air supply line for two-stage combustion 25 Low-pressure air damper for two-stage combustion 26 Low-pressure side wind box for two-stage combustion 27 Inner circumference for two-stage combustion Air inlet 28 Two-stage combustion inner air supply tube 29 Two-stage combustion outer air swirler 30 Two-stage combustion outer air inlet 110 Inner high pressure air jet 111 Outer low pressure air jet 112 High pressure side two stage combustion air Inlet 113 Air inlet for low pressure side two-stage combustion
Claims (6)
させるための一次空気を微粉炭機に供給する高圧空気供
給系統と、バーナ風箱に前記高圧空気よりも圧力の低い
低圧空気を供給する低圧空気供給系統と、火路内のバー
ナ下流側に二段燃焼用空気を投入する手段と、を設けた
燃焼装置において、 前記二段燃焼用空気を投入する手段に、前記高圧空気供
給系統および前記低圧空気供給系統からの高圧空気およ
び低圧空気の一部を供給する系統を設けたことを特徴と
する燃焼装置。1. A high-pressure air supply system for supplying primary air to a pulverizer for drying pulverized coal to be conveyed to a burner for combustion, and a low-pressure air having a lower pressure than the high-pressure air is supplied to a burner wind box. A combustion device provided with a low-pressure air supply system to be supplied and a means for charging the two-stage combustion air downstream of the burner in the fire path; A combustion device comprising a system and a system for supplying a part of high-pressure air and low-pressure air from the low-pressure air supply system.
設けると共に前記投入口の内部を複数の流路に分割し、
それぞれの流路に前記高圧空気と前記低圧空気を供給す
る構成としたことを特徴とする燃焼装置。2. The combustion device according to claim 1, wherein an air inlet is provided as means for feeding the two-stage combustion air, and the inside of the inlet is divided into a plurality of flow paths,
A combustion device, wherein the high-pressure air and the low-pressure air are supplied to respective flow paths.
設けると共に前記投入口として、高圧空気用と低圧空気
用にそれぞれ別個に空気投入口を設け、前記空気投入口
にそれぞれ高圧空気と低圧空気を投入する構成としたこ
とを特徴とする燃焼装置。3. The combustion device according to claim 1, wherein an air inlet is provided as a means for feeding the two-stage combustion air, and the inlet is separately charged for high-pressure air and low-pressure air. A combustion device, wherein a port is provided, and high-pressure air and low-pressure air are supplied to the air input port, respectively.
を火炉の幅方向で交互に配置すると共に、 前記高圧空気用投入口をバーナの真上に配置した構成と
したことを特徴とする燃焼装置。4. The combustion device according to claim 3, wherein the high-pressure air inlet and the low-pressure air inlet are alternately arranged in a width direction of the furnace, and the high-pressure air inlet is connected to a burner. A combustion device having a configuration disposed directly above the combustion device.
を火炉の高さ方向に多段に配置した構成としたことを特
徴とする燃焼装置。5. The combustion apparatus according to claim 3, wherein the high-pressure air inlet and the low-pressure air inlet are arranged in multiple stages in the height direction of the furnace. apparatus.
項に記載の燃焼装置において、 前記高圧空気と前記低圧空気の流量の比率、または前記
高圧空気およびまたは前記低圧空気の流量を、燃焼の負
荷に応じて制御することを特徴とする燃焼装置。6. The combustion device according to claim 1, wherein a ratio of a flow rate of the high-pressure air to the low-pressure air, or a flow rate of the high-pressure air and / or the low-pressure air is determined. A combustion device controlled according to a load of the combustion device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15115097A JPH10339407A (en) | 1997-06-09 | 1997-06-09 | Combustion apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15115097A JPH10339407A (en) | 1997-06-09 | 1997-06-09 | Combustion apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10339407A true JPH10339407A (en) | 1998-12-22 |
Family
ID=15512463
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15115097A Pending JPH10339407A (en) | 1997-06-09 | 1997-06-09 | Combustion apparatus |
Country Status (1)
Country | Link |
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JP (1) | JPH10339407A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005003285A (en) * | 2003-06-12 | 2005-01-06 | Nippon Steel Corp | Combustion chamber of waste melting equipment |
JP2016191537A (en) * | 2015-03-31 | 2016-11-10 | Jfeエンジニアリング株式会社 | Stoker type waste incinerator and waste incineration method |
JP2019049384A (en) * | 2017-09-08 | 2019-03-28 | 三菱日立パワーシステムズ株式会社 | Air feeding system of boiler |
-
1997
- 1997-06-09 JP JP15115097A patent/JPH10339407A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005003285A (en) * | 2003-06-12 | 2005-01-06 | Nippon Steel Corp | Combustion chamber of waste melting equipment |
JP2016191537A (en) * | 2015-03-31 | 2016-11-10 | Jfeエンジニアリング株式会社 | Stoker type waste incinerator and waste incineration method |
JP2019049384A (en) * | 2017-09-08 | 2019-03-28 | 三菱日立パワーシステムズ株式会社 | Air feeding system of boiler |
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