JP2003083509A - Boiler for performing recirculation combustion of exhaust gas - Google Patents

Boiler for performing recirculation combustion of exhaust gas

Info

Publication number
JP2003083509A
JP2003083509A JP2001275781A JP2001275781A JP2003083509A JP 2003083509 A JP2003083509 A JP 2003083509A JP 2001275781 A JP2001275781 A JP 2001275781A JP 2001275781 A JP2001275781 A JP 2001275781A JP 2003083509 A JP2003083509 A JP 2003083509A
Authority
JP
Japan
Prior art keywords
combustion
exhaust gas
amount
gas recirculation
boiler
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.)
Granted
Application number
JP2001275781A
Other languages
Japanese (ja)
Other versions
JP4672932B2 (en
Inventor
Shigeru Kuroki
茂 黒木
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.)
SAMSON CO Ltd
Original Assignee
SAMSON CO Ltd
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 SAMSON CO Ltd filed Critical SAMSON CO Ltd
Priority to JP2001275781A priority Critical patent/JP4672932B2/en
Publication of JP2003083509A publication Critical patent/JP2003083509A/en
Application granted granted Critical
Publication of JP4672932B2 publication Critical patent/JP4672932B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To realize both prevention of generation of photochemical smog and maintenance of high efficiency of a boiler. SOLUTION: The boiler 1 is provided with combustion air amount regulators 8, 9 which regulate a supply amount of combustion air supplied to a combustion device 3 and an exhaust gas circulation passage 5 through which exhaust gas after combustion is circulated to the combustion device. The boiler 1 enables recirculation combustion of the exhaust gas. In the boiler 1, an exhaust gas circulation amount regulator 6 which regulates an amount of the exhaust gas circulating to the combustion chamber is installed and a switch of operation and suspension of recirculation of the exhaust gas is kept possible. In the case that the photochemical smog does not generate, the recirculation combustion of the exhaust gas is not operated and the supply amount of the combustion air is made an amount of air for an EGR suspension state. In the case that the photochemical smog generates, the recirculation combustion of the exhaust gas is operated and the supply amount of the combustion air is made an amount of air for an EGR operation state.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は必要に応じて排ガス再循
環燃焼を行うボイラに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a boiler which performs exhaust gas recirculation combustion as required.

【0002】[0002]

【従来の技術】火炎の燃焼を行うと、光化学スモッグの
原因となるNOx(窒素酸化物)が発生し、NOxは太
陽の強い紫外線を受けると光化学反応を起こしてオゾン
などの光化学オキシダントになる。日差しが強く、気温
が高く、風の弱い日の日中には、光化学オキシダントの
濃度が高まり、光化学オキシダントがたまって白くもや
がかかったようになったものが光化学スモッグであり、
光化学スモッグは健康被害を引き起こすことがある。大
気の汚染が著しくなった場合、都道府県知事はその事態
を周知するとともに、ばい煙排出者や自動車使用者に対
し、ばい煙排出量の減少や自動車運行を制限することの
協力を求めることになっている(大気汚染防止法第23
条)。参考として東京都における注意報発令基準と緊急
時協力工場・事業場への措置を図3に示す。
2. Description of the Related Art When a flame is burned, NOx (nitrogen oxide) which causes photochemical smog is generated. When NOx receives strong ultraviolet rays from the sun, NOx undergoes a photochemical reaction to become a photochemical oxidant such as ozone. During the daytime when the sun is strong, the temperature is high, and the wind is weak, the concentration of the photochemical oxidant increases, and the photochemical oxidant accumulates in a white mist, which is photochemical smog.
Photochemical smog can cause health problems. When the air pollution becomes significant, the prefectural governor will be informed of the situation and ask the smokers and car users to cooperate in reducing the smoke emissions and restricting vehicle operation. Yes (Air Pollution Control Law No. 23
Article). For reference, Figure 3 shows the standards for issuing warnings and measures for emergency cooperation factories and business establishments in Tokyo.

【0003】火炎を燃焼するボイラは、運転を行えばN
Oxが発生するが、上記の通りNOxは環境に悪影響を
与えるため、NOx発生量を低減する努力が行われてい
る。NOx発生量を削減する手段の1つとして排ガス再
循環燃焼がある。NOxは高温で燃焼すると多量に発生
し、燃焼温度が低いと発生量は少なくなる。燃焼用空気
に排ガスを混合すると、排ガスは酸素量が少ないために
燃焼用空気の酸素濃度が低下し、酸素濃度の低い燃焼用
空気で燃焼を行うと火炎の局所的な高温域がなくなり、
火炎温度の低下によってNOx発生量は減少する。ただ
し、燃焼に必要な酸素量は変わらないため、排ガス再循
環燃焼時には酸素濃度が低くなっている分だけ燃焼用空
気供給量を増やす必要があり、燃焼用空気量を多くすれ
ば排ガスとともに排出される熱量が多くなるため、ボイ
ラの効率は低下することになる。
Boilers that burn flames have N
Although Ox is generated, NOx has an adverse effect on the environment as described above, so efforts are being made to reduce the amount of NOx generated. Exhaust gas recirculation combustion is one of the means for reducing the NOx generation amount. When NOx is burned at a high temperature, a large amount of NOx is generated, and when the combustion temperature is low, the generated amount is small. When the exhaust gas is mixed with the combustion air, the oxygen concentration of the exhaust gas is low because the exhaust gas has a small amount of oxygen, and when the combustion air having a low oxygen concentration is used for combustion, the local high temperature region of the flame disappears.
The NOx generation amount decreases as the flame temperature decreases. However, since the amount of oxygen required for combustion does not change, it is necessary to increase the combustion air supply amount as much as the oxygen concentration is low during exhaust gas recirculation combustion.If the combustion air amount is increased, it will be discharged together with the exhaust gas. Since the amount of heat generated is large, the efficiency of the boiler will decrease.

【0004】NOx発生量を抑制する手段がないボイラ
の場合、光化学オキシダント濃度上昇によってNOx発
生量の削減が必要になったとしても、ボイラの運転をカ
ットすることでしかNOxの発生量を減らすことができ
ない。しかしボイラの運転をカットするということは、
蒸気を使用するシステム全体の操業をカットすることに
なるため、NOx発生量を削減するために運転をカット
することは容易ではなかった。
In the case of a boiler having no means for suppressing the NOx generation amount, even if it is necessary to reduce the NOx generation amount due to an increase in the photochemical oxidant concentration, the NOx generation amount can be reduced only by cutting the operation of the boiler. I can't. However, cutting the operation of the boiler means
Since the operation of the entire system using steam is cut, it is not easy to cut the operation to reduce the NOx generation amount.

【0005】[0005]

【発明が解決しようとする課題】本発明が解決しようと
する課題は、光化学スモッグの発生を防ぐこととボイラ
の効率を高く保つことを両立することにある。
The problem to be solved by the present invention is to prevent the generation of photochemical smog and keep the efficiency of the boiler high.

【0006】[0006]

【課題を解決するための手段】請求項1に記載の発明
は、燃料と燃焼用空気を供給して燃焼を行う燃焼装置、
燃焼装置へ燃焼用空気を供給する送風機、燃焼装置へ供
給する燃焼用空気の供給量を調節する燃焼用空気量調節
装置、燃焼後の排ガスを燃焼装置へ循環させる排ガス循
環路を設け、排ガス再循環燃焼を可能としているボイラ
であって、燃料供給量に対応した酸素量を供給するよう
に燃焼用空気供給量を調節しているボイラにおいて、燃
焼装置へ循環する排ガス量を調節する排ガス循環量調節
装置を設け、排ガス循環量調節装置によって排ガス再循
環の実施と停止の切り換えを可能とし、前記の燃焼用空
気量調節装置には、排ガス再循環を実施しない場合での
燃焼用空気供給量であるEGR停止時用風量と、排ガス
再循環を実施する場合での燃焼用空気供給量であるEG
R実施時用風量を設定しておき、排ガス再循環停止時に
はEGR停止時用風量に基づいて燃焼用空気量の調節を
行い、排ガス再循環実施時にはEGR実施時用風量に基
づいて燃焼用空気量の調節を行うことを特徴とする。
According to a first aspect of the present invention, there is provided a combustion device for supplying fuel and combustion air to perform combustion.
An air blower that supplies combustion air to the combustion device, a combustion air amount adjustment device that adjusts the supply amount of combustion air that is supplied to the combustion device, and an exhaust gas circulation path that circulates the exhaust gas after combustion to the combustion device Exhaust gas circulation amount that adjusts the amount of exhaust gas that circulates to the combustion device in a boiler that enables circulating combustion and that adjusts the combustion air supply amount to supply the oxygen amount that corresponds to the fuel supply amount A control device is provided, and it is possible to switch between execution and stop of exhaust gas recirculation by the exhaust gas circulation amount control device.The above-mentioned combustion air amount control device uses the combustion air supply amount when exhaust gas recirculation is not performed. An EGR stop air flow rate and an EG that is the combustion air supply rate when exhaust gas recirculation is performed
The amount of air for R execution is set, the amount of combustion air is adjusted based on the amount of air for EGR stop when exhaust gas recirculation is stopped, and the amount of combustion air is based on the amount of air for EGR execution during exhaust gas recirculation. It is characterized by performing adjustment of.

【0007】請求項2に記載の発明は、前記の排ガス再
循環燃焼を行うボイラにおいて、ボイラ燃焼時の燃焼量
は高燃焼と低燃焼の2段階で制御するものであり、EG
R停止時用風量には排ガス再循環停止時における高燃焼
用風量及び低燃焼用風量を設定し、EGR実施時用風量
には排ガス再循環実施時における高燃焼用風量及び低燃
焼用風量を設定しておき、EGR停止時用風量の設定風
量はEGR実施時用風量の設定風量より少なくなるよう
に設定したことを特徴とする。
According to a second aspect of the present invention, in the boiler that performs the exhaust gas recirculation combustion, the combustion amount during boiler combustion is controlled in two stages of high combustion and low combustion.
For R stop air volume, set high combustion air volume and low combustion air volume when exhaust gas recirculation is stopped, and set EGR implementation air volume for high combustion and low combustion air volume when exhaust gas recirculation is implemented. The set air volume for the EGR stop air volume is set to be smaller than the set air volume for the EGR execution air volume.

【0008】請求項3に記載の発明は、前記の排ガス再
循環燃焼を行うボイラにおいて、燃焼用空気供給量調節
装置は、EGR停止時用風量を設定した第1ダンパと、
EGR実施時用風量を設定した第2ダンパからなり、排
ガス再循環停止時には、第2ダンパを開いた状態で固定
して燃焼量に応じて第1ダンパの開度を調節することで
燃焼用空気供給量を調節し、排ガス再循環実施時には、
第1ダンパを開いた状態で固定して燃焼量に応じて第2
ダンパの開度を調節することで燃焼用空気供給量の調節
を行うことを特徴とする。
According to a third aspect of the present invention, in the boiler for performing the exhaust gas recirculation combustion, the combustion air supply amount adjusting device includes a first damper for setting an EGR stop time air amount,
It consists of a second damper that sets the air flow rate for EGR execution, and when the exhaust gas recirculation is stopped, the second damper is fixed in the open state and the opening of the first damper is adjusted according to the combustion amount to burn the combustion air. Adjust the supply amount, and when recirculating exhaust gas,
The first damper is fixed in the open state and the second damper is used according to the combustion amount.
It is characterized in that the supply amount of combustion air is adjusted by adjusting the opening degree of the damper.

【0009】請求項4に記載の発明は、前記の排ガス再
循環燃焼を行うボイラにおいて、光化学スモッグが発生
する気象条件下では排ガス再循環を実施し、光化学スモ
ッグの発生しない気象条件下では排ガス再循環を実施し
ないことを特徴とする。
According to a fourth aspect of the present invention, in the boiler for performing the exhaust gas recirculation combustion, exhaust gas recirculation is carried out under weather conditions where photochemical smog is generated, and exhaust gas recirculation is carried out under weather conditions where photochemical smog is not generated. It is characterized by not performing circulation.

【0010】[0010]

【発明の実施の形態】本発明の一実施例を図面を用いて
説明する。図1は一実施例におけるボイラ1のフロー
図、図2はそのタイムチャートである。ボイラ1は内部
に燃焼室(図示せず)を設けており、燃焼室上部に燃焼
装置3を設ける。燃焼装置3には燃焼用空気供給路7を
接続し、燃焼用空気供給路7の他端には送風機10を接
続する。送風機10は取り込んだ空気を加圧し、燃焼用
空気供給路7を通して燃焼装置3へ送り込む。ボイラ1
の下部には、燃焼室内から燃焼後の排ガスを取り出す排
気通路4を設け、排気通路4の途中に排気通路4から分
岐させた排ガス循環路5を接続し、排ガス循環路5の他
端は、送風機10が空気の取り込みを行っている管に接
続する。排ガス循環路5の途中に排ガス循環量調節装置
としてEGRダンパ6、燃焼用空気供給路7の途中には
燃焼用空気量調節装置として第1ダンパ8及び第2ダン
パ9を設ける。送風機10、EGRダンパ6、第1ダン
パ8、第2ダンパ9の作動を制御する給気制御装置2を
設け、給気制御装置2は各装置と信号線で接続してお
く。
DETAILED DESCRIPTION OF THE INVENTION An embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a flow chart of the boiler 1 in one embodiment, and FIG. 2 is its time chart. The boiler 1 is provided with a combustion chamber (not shown) inside, and a combustion device 3 is provided above the combustion chamber. A combustion air supply passage 7 is connected to the combustion device 3, and a blower 10 is connected to the other end of the combustion air supply passage 7. The blower 10 pressurizes the taken-in air and sends it to the combustion device 3 through the combustion air supply passage 7. Boiler 1
An exhaust passage 4 for taking out exhaust gas after combustion from the combustion chamber is provided in the lower part of the exhaust gas, and an exhaust gas circulation passage 5 branched from the exhaust passage 4 is connected in the middle of the exhaust passage 4, and the other end of the exhaust gas circulation passage 5 is The blower 10 is connected to the pipe taking in air. An EGR damper 6 as an exhaust gas circulation amount adjusting device is provided in the middle of the exhaust gas circulation path 5, and a first damper 8 and a second damper 9 as combustion air amount adjusting devices are provided in the middle of the combustion air supply path 7. An air supply control device 2 for controlling the operation of the blower 10, the EGR damper 6, the first damper 8, and the second damper 9 is provided, and the air supply control device 2 is connected to each device by a signal line.

【0011】ボイラ1の燃焼装置3は、燃料と燃焼用空
気の供給を受けて燃焼を行う。ボイラ燃焼時の燃焼量
は、高燃焼と低燃焼の2段階で制御するものであれば、
高燃焼用燃料及び高燃焼用空気の供給量と、低燃焼用燃
料及び低燃焼用空気の供給量を設定しておき、燃料及び
燃焼用空気の供給量を制御することで燃焼量を制御す
る。燃焼用空気量の調節は、燃焼用空気供給路7の流路
面積を調節する第1ダンパ8及び第2ダンパ9によって
行う。第1ダンパ8には排ガス再循環を実施していない
場合において、高燃焼用風量となる開度と、低燃焼用風
量となる開度を設定しておき、第2ダンパ9には排ガス
再循環を実施している場合において、高燃焼用風量とな
る開度と、低燃焼用風量となる開度を設定しておく。
The combustion device 3 of the boiler 1 is supplied with fuel and combustion air to perform combustion. If the amount of combustion during boiler combustion is controlled in two stages, high combustion and low combustion,
The supply amount of high combustion fuel and high combustion air and the supply amount of low combustion fuel and low combustion air are set in advance, and the combustion amount is controlled by controlling the supply amounts of fuel and combustion air. . The amount of combustion air is adjusted by the first damper 8 and the second damper 9 that adjust the flow passage area of the combustion air supply passage 7. When exhaust gas recirculation is not carried out for the first damper 8, an opening for high air volume for combustion and an opening for low air volume for combustion are set, and the exhaust gas recirculation for the second damper 9 is made. In the case where is performed, the opening degree that provides the high combustion air volume and the opening degree that provides the low combustion air volume are set.

【0012】排ガス再循環燃焼の実施は、排ガス循環路
5の流路面積を全開と全閉の2点で制御するEGRダン
パ6を開くことで行う。EGRダンパ6を全閉にしてい
る場合、排ガスが送風機10へ流れることはないため、
送風機10が供給する空気はボイラ外部から取り込んだ
通常空気のみとなる。EGRダンパ6を全開にすると、
排気通路4の排ガスが排ガス循環路5を通過することが
できるようになるため、送風機10へ向かう排ガスの流
れが生じ、送風機10が供給する空気は、外部から取り
込んだ通常空気と排気通路4から取り込んだ排ガスを混
合した酸素濃度の低い空気となる。EGRダンパ6を全
開にしている場合が排ガス再循環実施時であり、EGR
ダンパ6を全閉としている場合が排ガス再循環停止時と
なる。
The exhaust gas recirculation combustion is carried out by opening the EGR damper 6 which controls the flow passage area of the exhaust gas circulation passage 5 at two points of full opening and full closing. When the EGR damper 6 is fully closed, exhaust gas does not flow to the blower 10,
The air supplied by the blower 10 is only the normal air taken in from the outside of the boiler. When the EGR damper 6 is fully opened,
Since the exhaust gas in the exhaust passage 4 can pass through the exhaust gas circulation passage 5, a flow of the exhaust gas toward the blower 10 is generated, and the air supplied by the blower 10 is supplied from the outside through the normal air and the exhaust passage 4. It becomes air with a low oxygen concentration, which is a mixture of the taken-in exhaust gas. The case where exhaust gas recirculation is performed is when the EGR damper 6 is fully opened.
When the damper 6 is fully closed, the exhaust gas recirculation is stopped.

【0013】EGRダンパ6の操作は給気制御装置2に
よって行い、給気制御装置2は、排ガス再循環停止時に
は第1ダンパ8によって燃焼用空気供給量の調節を行
い、排ガス再循環実施時には第2ダンパ9によって燃焼
用空気供給量の調節を行う。排ガス再循環を実施するか
否かは、給気制御装置2への入力によって切り換えるこ
とができるようにしておく。
The EGR damper 6 is operated by the air supply control device 2. The air supply control device 2 adjusts the combustion air supply amount by the first damper 8 when the exhaust gas recirculation is stopped, and when the exhaust gas recirculation is carried out. The amount of combustion air supplied is adjusted by the two dampers 9. Whether or not to carry out exhaust gas recirculation can be switched by an input to the air supply control device 2.

【0014】第1ダンパ8に設定しているダンパ開度
は、排ガス再循環を行っていない通常の酸素濃度をもっ
た空気で燃焼を行う場合での、低燃焼用風量と高燃焼用
風量分の開度に設定し、第2ダンパ9に設定しているダ
ンパ開度は、排ガス再循環を行うことで酸素濃度の低下
している空気で燃焼を行う場合での、低燃焼用風量と高
燃焼用風量分の開度に設定する。燃焼量が大きければ燃
焼に必要な酸素量は大きくなり、燃焼量が小さければ燃
焼に必要な酸素量は小さくなるため、低燃焼用風量と高
燃焼用風量では高燃焼用風量の方が大きくなるように開
度を大きくする。燃焼量が同じ場合には燃焼に必要な酸
素量は同じであるが、酸素濃度が低ければ一定量の燃焼
用空気に含まれている酸素量が少なくなるため、燃焼用
空気供給量は多くする必要となる。そのため、第1ダン
パ8に設定している低燃焼用開度及び高燃焼用開度よ
り、第2ダンパ9に設定している低燃焼用開度及び高燃
焼用開度の方が燃焼用空気供給量が多くなるようにして
おく。
The damper opening set for the first damper 8 corresponds to a low combustion air volume and a high combustion air volume when combustion is performed with air having a normal oxygen concentration without exhaust gas recirculation. Is set to the second damper 9 and the damper opening set to the second damper 9 is set to a low combustion air volume and a high combustion amount in the case of performing combustion with air having a reduced oxygen concentration by performing exhaust gas recirculation. Set the opening for the combustion air volume. The larger the amount of combustion, the larger the amount of oxygen required for combustion, and the smaller the amount of combustion, the smaller the amount of oxygen required for combustion. Therefore, for low and high combustion air volumes, the high combustion air volume is larger. To increase the opening. If the amount of combustion is the same, the amount of oxygen required for combustion is the same, but if the oxygen concentration is low, the amount of oxygen contained in a certain amount of combustion air will decrease, so the amount of combustion air supplied will be increased. Will be needed. Therefore, the low-combustion opening and the high-combustion opening set in the second damper 9 are lower than the low-combustion opening and the high-combustion opening set in the first damper 8. Make sure that the supply is large.

【0015】図2はEGRダンパ6、第1ダンパ8、第
2ダンパ9による風量調節の例を示したタイムチャート
である。最初は給気制御装置2には排ガス再循環を行わ
ないとの設定を行っており、排ガス再循環停止時の状態
から始まっている。排ガス再循環を行わずに燃焼を行う
場合、EGRダンパ6は全閉、第2ダンパ9は全開に固
定しておき、燃焼量に応じて第1ダンパ8の開度を変更
することで燃焼用空気供給量の調節を行う。この場合、
EGRダンパ6を閉じているために排気通路4の排ガス
が送風機10内に入ることはなく、送風機10からは通
常の酸素濃度を持った燃焼用空気が送られる。第2ダン
パ9は全開で固定しておき、第1ダンパ8は燃焼量によ
って開度を調節するため、第1ダンパ8で調節した風量
が燃焼装置3へ送られる燃焼用空気供給量となる。
FIG. 2 is a time chart showing an example of air volume adjustment by the EGR damper 6, the first damper 8 and the second damper 9. Initially, the air supply control device 2 is set so that exhaust gas recirculation is not performed, and it starts from the state when exhaust gas recirculation is stopped. When performing combustion without exhaust gas recirculation, the EGR damper 6 is fixed to be fully closed and the second damper 9 is fixed to be fully open, and the opening degree of the first damper 8 is changed according to the combustion amount for combustion. Adjust the air supply. in this case,
Since the EGR damper 6 is closed, the exhaust gas in the exhaust passage 4 does not enter the blower 10, and the blower 10 sends combustion air having a normal oxygen concentration. The second damper 9 is fixed in a fully opened state, and the opening of the first damper 8 is adjusted by the combustion amount. Therefore, the air volume adjusted by the first damper 8 becomes the combustion air supply amount sent to the combustion device 3.

【0016】給気制御装置2へ排ガス再循環燃焼実施の
入力を行うと、給気制御装置2はEGRダンパ6を全閉
から全開に移動させ、第1ダンパ8は全開とし、第2ダ
ンパ9は燃焼量に合った開度に変更する。EGRダンパ
6を開くと、送風機10が排気通路4の排ガスを吸引す
ることになるため、送風機10から燃焼装置3へ送る燃
焼用空気の酸素濃度は低下する。排ガス再循環燃焼を実
施している場合、第1ダンパ8は全開で固定しておき、
第2ダンパ9は燃焼量によって開度を調節する。そのた
め、第2ダンパ9で調節した風量が燃焼装置3へ送られ
る燃焼用空気供給量となり、第2ダンパ9の設定開度は
第1ダンパ8の設定開度よりも、酸素濃度が低下してい
る分だけ大きくしているため、排ガス再循環停止時より
燃焼用空気供給量が多くなる。
When the exhaust gas recirculation combustion execution is input to the air supply control device 2, the air supply control device 2 moves the EGR damper 6 from fully closed to fully open, the first damper 8 is fully opened, and the second damper 9 is opened. Changes to an opening that matches the amount of combustion. When the EGR damper 6 is opened, the blower 10 sucks the exhaust gas in the exhaust passage 4, so that the oxygen concentration of the combustion air sent from the blower 10 to the combustion device 3 decreases. When performing exhaust gas recirculation combustion, the first damper 8 should be fully open and fixed,
The second damper 9 adjusts the opening according to the amount of combustion. Therefore, the air volume adjusted by the second damper 9 becomes the combustion air supply amount sent to the combustion device 3, and the set opening degree of the second damper 9 has a lower oxygen concentration than the set opening degree of the first damper 8. Since the amount is increased as much as there is, the supply amount of combustion air becomes larger than when the exhaust gas recirculation is stopped.

【0017】排ガス再循環燃焼を行う目的は、光化学ス
モッグの原因となるNOx発生量を削減することにあ
り、NOx発生量を削減することで光化学オキシダント
濃度の上昇を防止することができる。ところが光化学オ
キシダントは、太陽の強い紫外線を受けることによる光
化学反応によって発生するものであるため、特定の気象
条件下でなければ光化学オキシダント濃度が上昇して光
化学スモッグが発生することはなく、NOx発生量の増
加がそのまま光化学オキシダント濃度の増加に結びつく
ものではない。つまり、ボイラの効率を犠牲にしてもN
Ox発生量を削減することは、光化学スモッグの発生す
る気象条件の場合には有効であるが、光化学スモッグの
発生しにく気象条件の場合には効果がない。
The purpose of the exhaust gas recirculation combustion is to reduce the NOx generation amount that causes photochemical smog. By reducing the NOx generation amount, it is possible to prevent an increase in the photochemical oxidant concentration. However, since photochemical oxidants are generated by photochemical reactions caused by receiving the strong ultraviolet rays of the sun, the photochemical oxidant concentration does not rise and photochemical smog does not occur unless the weather conditions are high, and NOx emission Does not directly lead to an increase in photochemical oxidant concentration. In other words, even if the efficiency of the boiler is sacrificed, N
Reducing the amount of Ox generated is effective under the weather conditions where photochemical smog occurs, but is not effective under the weather conditions where photochemical smog hardly occurs.

【0018】排ガス再循環燃焼の場合、燃焼用空気供給
量を多くする必要があるために排気量が増加し、排気と
ともに排出される熱量が増加するためボイラの効率は低
下する。排ガス再循環燃焼はNOx発生量を削減する効
果を得ることができるが、燃料の有効利用の観点からは
排ガス再循環燃焼を実施しない方がよい。また、効率が
低下すれば燃焼量を多くする必要があるために二酸化炭
素の発生量が増加することになる。二酸化炭素は直接の
公害物質ではないが、地球温暖化の原因となる温室効果
ガスであり、削減すべき対象であるため、二酸化炭素削
減の観点からも排ガス再循環燃焼は実施しない方がよい
ことになる。
In the case of exhaust gas recirculation combustion, it is necessary to increase the amount of combustion air supplied, so that the amount of exhaust gas increases and the amount of heat discharged together with the exhaust gas increases, so the efficiency of the boiler decreases. Exhaust gas recirculation combustion can obtain the effect of reducing the NOx generation amount, but from the viewpoint of effective use of fuel, it is better not to carry out exhaust gas recirculation combustion. In addition, if the efficiency decreases, the amount of carbon dioxide generated increases because it is necessary to increase the amount of combustion. Although carbon dioxide is not a direct pollutant, it is a greenhouse gas that causes global warming and should be reduced. Therefore, from the perspective of reducing carbon dioxide, it is better not to carry out exhaust gas recirculation combustion. become.

【0019】燃焼量に合わせて行う燃焼用空気量の調節
を、排ガス再循実施時と排ガス再循環停止時のそれぞれ
に応じた風量に調節できるようにしておけば、排ガス再
循環燃焼を行う場合も行わない場合にも適正な燃焼を行
うことができ、必要な場合にのみ排ガス再循環燃焼を行
うことができる。光化学オキシダント濃度上昇時には排
ガス再循環燃焼を行うようにすれば、ボイラの運転を削
減しなくともNOx発生量を削減することができ、光化
学スモッグの発生を抑えることができる。逆に、光化学
オキシダント濃度の上昇しない場合には排ガス再循環を
実施しないことで、ボイラの効率を高く保つことがで
き、常時排ガス再循環燃焼を行っているボイラに比べて
燃料消費量が少なくなり、二酸化炭素の発生量も削減す
ることができる。
When exhaust gas recirculation combustion is performed, the amount of combustion air to be adjusted in accordance with the combustion amount can be adjusted so that the air flow rate can be adjusted depending on whether exhaust gas recirculation is performed or when exhaust gas recirculation is stopped. Proper combustion can be performed even when it is not performed, and exhaust gas recirculation combustion can be performed only when necessary. If exhaust gas recirculation combustion is performed when the photochemical oxidant concentration increases, the NOx generation amount can be reduced without reducing the boiler operation, and the photochemical smog can be suppressed. On the contrary, when the photochemical oxidant concentration does not increase, by not performing exhaust gas recirculation, the efficiency of the boiler can be kept high, and the fuel consumption is smaller than that of a boiler that constantly performs exhaust gas recirculation combustion. Also, the amount of carbon dioxide generated can be reduced.

【0020】なお、送風機にインバータ回路などを設け
ておき、送風機の回転速度を変更することで燃焼用空気
供給量を調節することも行われており、燃焼用空気量調
節装置は送風機の回転速度を変更するものであっても良
い。この場合には回転速度を、排ガス再循環を実施しな
い場合でのEGR停止時用風量と、排ガス再循環を実施
する場合でのEGR実施時用風量で設定しておき、回転
速度はEGR停止時用の方が低くなるように設定してお
く。実施例のように燃焼量を高燃焼と低燃焼の2段階で
制御する場合には、排ガス再循環実施時での高燃焼用回
転数及び低燃焼用回転数と、排ガス再循環実施時での高
燃焼用回転数及び低燃焼用回転数を設定する。
It is also known that the blower is provided with an inverter circuit or the like and the rotation speed of the blower is changed to adjust the supply amount of combustion air. May be changed. In this case, the rotation speed is set by the EGR stop air volume when exhaust gas recirculation is not executed and the EGR execution air flow when exhaust gas recirculation is executed, and the rotation speed is set when EGR is stopped. It is set so that the one for use is lower. When the combustion amount is controlled in two stages of high combustion and low combustion as in the embodiment, the high combustion rotation speed and the low combustion rotation speed at the time of exhaust gas recirculation and the exhaust gas recirculation at the time of exhaust gas recirculation are executed. Set the high combustion speed and the low combustion speed.

【0021】[0021]

【発明の効果】本発明を実施することによって、光化学
オキシダント濃度の高い場合におけるNOx発生量削減
と、光化学オキシダント濃度の低い場合におけるボイラ
の効率の向上を図ることができる。
By implementing the present invention, it is possible to reduce the NOx generation amount when the photochemical oxidant concentration is high and to improve the efficiency of the boiler when the photochemical oxidant concentration is low.

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

【図1】 本発明の一実施例のフロー図FIG. 1 is a flow chart of an embodiment of the present invention.

【図2】 本発明の一実施例のタイムチャートFIG. 2 is a time chart of an embodiment of the present invention.

【図3】 東京都における注意報発令基準と措置[Figure 3] Warning issuing standards and measures in Tokyo

【符号の説明】[Explanation of symbols]

1 ボイラ 2 給気制御装置 3 燃焼装置 4 排気通路 5 排ガス循環路 6 EGRダンパ 7 燃焼用空気供給路 8 第1ダンパ 9 第2ダンパ 10 送風機 1 boiler 2 Air supply control device 3 Combustion device 4 exhaust passage 5 Exhaust gas circulation 6 EGR damper 7 Combustion air supply path 8 First damper 9 Second damper 10 blower

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 燃料と燃焼用空気を供給して燃焼を行う
燃焼装置、燃焼装置へ燃焼用空気を供給する送風機、燃
焼装置へ供給する燃焼用空気の供給量を調節する燃焼用
空気量調節装置、燃焼後の排ガスを燃焼装置へ循環させ
る排ガス循環路を設け、排ガス再循環燃焼を可能として
いるボイラであって、燃料供給量に対応した酸素量を供
給するように燃焼用空気供給量を調節しているボイラに
おいて、燃焼装置へ循環する排ガス量を調節する排ガス
循環量調節装置を設け、排ガス循環量調節装置によって
排ガス再循環の実施と停止の切り換えを可能とし、前記
の燃焼用空気量調節装置には、排ガス再循環を実施しな
い場合での燃焼用空気供給量であるEGR停止時用風量
と、排ガス再循環を実施する場合での燃焼用空気供給量
であるEGR実施時用風量を設定しておき、排ガス再循
環停止時にはEGR停止時用風量に基づいて燃焼用空気
量の調節を行い、排ガス再循環実施時にはEGR実施時
用風量に基づいて燃焼用空気量の調節を行うことを特徴
とする排ガス再循環燃焼を行うボイラ。
1. A combustion device for supplying fuel and combustion air for combustion, a blower for supplying combustion air to the combustion device, and a combustion air amount adjustment for adjusting the supply amount of combustion air supplied to the combustion device. A boiler that enables exhaust gas recirculation combustion by providing an exhaust gas circulation path that circulates the exhaust gas after combustion to the combustion device, and adjusts the combustion air supply amount to supply the oxygen amount corresponding to the fuel supply amount. In the boiler that is being adjusted, an exhaust gas circulation control device is installed to control the amount of exhaust gas that circulates to the combustion device.The exhaust gas circulation control device enables switching between execution and stop of exhaust gas recirculation. The EGR stop air volume, which is the combustion air supply amount when exhaust gas recirculation is not performed, and the EGR air flow amount when combustion gas is supplied, when the exhaust gas recirculation is performed The air flow rate is set, and when the exhaust gas recirculation is stopped, the combustion air volume is adjusted based on the EGR stop air volume, and when the exhaust gas recirculation is performed, the combustion air volume is adjusted based on the EGR execution air volume. A boiler that performs exhaust gas recirculation combustion characterized by performing.
【請求項2】 請求項1に記載の排ガス再循環燃焼を行
うボイラにおいて、ボイラ燃焼時の燃焼量は高燃焼と低
燃焼の2段階で制御するものであり、EGR停止時用風
量には排ガス再循環停止時における高燃焼用風量及び低
燃焼用風量を設定し、EGR実施時用風量には排ガス再
循環実施時における高燃焼用風量及び低燃焼用風量を設
定しておき、EGR停止時用風量の設定風量はEGR実
施時用風量の設定風量より少なくなるように設定したこ
とを特徴とする排ガス再循環燃焼を行うボイラ。
2. The boiler for performing exhaust gas recirculation combustion according to claim 1, wherein the combustion amount during boiler combustion is controlled in two stages, high combustion and low combustion, and the exhaust gas amount for EGR stop is the exhaust gas. Set the high combustion air volume and low combustion air volume at the time of recirculation stop, and set the high combustion air volume and low combustion air volume at the time of exhaust gas recirculation to EGR execution air volume for EGR stop A boiler for performing exhaust gas recirculation combustion, wherein the set air volume of the air volume is set to be smaller than the set air volume of the EGR implementation air volume.
【請求項3】 請求項1または2に記載の排ガス再循環
燃焼を行うボイラにおいて、燃焼用空気供給量調節装置
は、EGR停止時用風量を設定した第1ダンパと、EG
R実施時用風量を設定した第2ダンパからなり、排ガス
再循環停止時には、第2ダンパを開いた状態で固定して
燃焼量に応じて第1ダンパの開度を調節することで燃焼
用空気供給量を調節し、排ガス再循環実施時には、第1
ダンパを開いた状態で固定して燃焼量に応じて第2ダン
パの開度を調節することで燃焼用空気供給量の調節を行
うことを特徴とする排ガス再循環燃焼を行うボイラ。
3. The boiler for performing exhaust gas recirculation combustion according to claim 1, wherein the combustion air supply amount adjusting device includes a first damper for setting an EGR stop air amount and an EG.
It consists of a second damper that sets the air flow rate for R execution, and when the exhaust gas recirculation is stopped, the second damper is fixed in the open state and the opening degree of the first damper is adjusted according to the combustion amount. When the exhaust gas recirculation is carried out by adjusting the supply amount,
A boiler that performs exhaust gas recirculation combustion, wherein the damper is fixed in an open state and the opening amount of the second damper is adjusted according to the combustion amount to adjust the supply amount of combustion air.
【請求項4】 請求項1から3のいずれかに記載の排ガ
ス再循環燃焼を行うボイラにおいて、光化学スモッグが
発生する気象条件下では排ガス再循環を実施し、光化学
スモッグの発生しない気象条件下では排ガス再循環を実
施しないことを特徴とする排ガス再循環燃焼を行うボイ
ラの運転方法。
4. The boiler for exhaust gas recirculation combustion according to any one of claims 1 to 3, wherein exhaust gas recirculation is performed under weather conditions where photochemical smog occurs, and under weather conditions where photochemical smog does not occur. A method for operating a boiler that performs exhaust gas recirculation combustion, characterized in that exhaust gas recirculation is not performed.
JP2001275781A 2001-09-11 2001-09-11 Boiler with exhaust gas recirculation combustion Expired - Fee Related JP4672932B2 (en)

Priority Applications (1)

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JP4672932B2 JP4672932B2 (en) 2011-04-20

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Country Status (1)

Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013088024A (en) * 2011-10-18 2013-05-13 Miura Co Ltd Heat medium boiler
WO2016157925A1 (en) * 2015-03-31 2016-10-06 三浦工業株式会社 Boiler device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2782407B2 (en) * 1993-03-31 1998-07-30 株式会社サムソン Air supply control method for small boiler with exhaust gas recirculation

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013088024A (en) * 2011-10-18 2013-05-13 Miura Co Ltd Heat medium boiler
WO2016157925A1 (en) * 2015-03-31 2016-10-06 三浦工業株式会社 Boiler device

Also Published As

Publication number Publication date
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