JP5131597B2 - Operation control method of heat storage combustion type exhaust gas purification device - Google Patents
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- 238000002485 combustion reaction Methods 0.000 title claims description 73
- 238000005338 heat storage Methods 0.000 title claims description 58
- 238000000746 purification Methods 0.000 title claims description 41
- 238000000034 method Methods 0.000 title claims description 16
- 238000004519 manufacturing process Methods 0.000 claims description 15
- 230000001172 regenerating effect Effects 0.000 claims description 15
- 238000010926 purge Methods 0.000 claims description 14
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 238000003860 storage Methods 0.000 description 7
- 239000000446 fuel Substances 0.000 description 4
- 239000012855 volatile organic compound Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
Description
本発明は蓄熱燃焼式排ガス浄化装置の運転制御方法に関する。さらに詳しくは、蓄熱燃焼式排ガス浄化装置が備えられている生産設備が生産準備等により一時停止し、揮発性有機化合物(Volatile Organic Compounds:以下、VOCという)を含む排ガスが排気されないあいだに、この排ガス浄化装置の運転を処理運転から待機運転に切替えて制御する運転制御方法に関する。 The present invention relates to an operation control method for a heat storage combustion type exhaust gas purification device. More specifically, while the production facility equipped with the heat storage combustion type exhaust gas purification device is temporarily stopped due to production preparation or the like, the exhaust gas containing volatile organic compounds (hereinafter referred to as VOC) is not exhausted. The present invention relates to an operation control method for controlling the operation of an exhaust gas purifier from a processing operation to a standby operation.
従来より、図7に示されるように、内部に第1の蓄熱体1aを配設した蓄熱室1を有する第1塔と第2の蓄熱体2aを配設した蓄熱室2を有する第2塔とを並列に配設し、各蓄熱体1a、2aの上部を共通の燃焼室3にした構造からなる本体と、各蓄熱体1a、2aの下方にそれぞれ接続されている入口ダンパ4a、5aおよび出口ダンパ4b、5bと、入口ダンパ4a、5aに接続される排ガス供給管6aと、出口ダンパ4b、5bに接続される処理済みの浄化ガス排気管6bと、前記排ガス供給管6aにおける入口ダンパ4a、5aの上流位置に接続される送風機7と、排ガス供給管6aから生産設備に延びる吸引ライン8に接続される、排ガスの吸引と遮断を切替える吸引遮断ダンパ9および冷風取入ダンパ10と、各ダンパの切替および燃焼室の温度を制御する制御装置Aとを備える蓄熱燃焼式排ガス浄化装置(Regenerative Thermal Oxidizer:RTO)がある(たとえば特許文献1)。また、前記燃焼室3には、バーナ11と温度を監視する温度センサ12が設けられている。 Conventionally, as shown in FIG. 7, a first tower having a heat storage chamber 1 having a first heat storage body 1a disposed therein and a second tower having a heat storage chamber 2 having a second heat storage body 2a disposed therein. Are arranged in parallel, and a main body having a structure in which the upper portions of the heat storage bodies 1a and 2a are formed as a common combustion chamber 3, and inlet dampers 4a and 5a connected to the lower sides of the heat storage bodies 1a and 2a, respectively. Outlet dampers 4b and 5b, exhaust gas supply pipe 6a connected to inlet dampers 4a and 5a, treated purified gas exhaust pipe 6b connected to outlet dampers 4b and 5b, and inlet damper 4a in the exhaust gas supply pipe 6a 5a, a blower 7 connected to the upstream position of the exhaust gas supply pipe 6a, a suction line 8 extending from the exhaust gas supply pipe 6a to the production facility, and a suction shut-off damper 9 and a cold air intake damper 10 for switching between exhaust gas suction and shut-off, Switching the damper Fine combustion chamber regenerative-combustion exhaust gas purifying apparatus and a control device A to control the temperature of (Regenerative Thermal Oxidizer: RTO) is (for example, Patent Document 1). The combustion chamber 3 is provided with a burner 11 and a temperature sensor 12 for monitoring the temperature.
この蓄熱燃焼式排ガス浄化装置では、第1の蓄熱体1aを通過させた排ガスを対象成分分解に必要な温度に保持されている燃焼室3内で高温燃焼分解処理し、燃焼後の浄化ガスを第2の蓄熱体2aを通過させる。そして、このとき、浄化ガスからの熱は第2の蓄熱体2aへ蓄熱され、冷却された浄化ガスを外気に排出させている。 In this heat storage combustion type exhaust gas purification apparatus, the exhaust gas that has passed through the first heat storage body 1a is subjected to high-temperature combustion decomposition treatment in the combustion chamber 3 that is maintained at a temperature necessary for target component decomposition, and the purified gas after combustion is treated. The 2nd thermal storage body 2a is allowed to pass through. At this time, the heat from the purified gas is stored in the second heat storage body 2a, and the cooled purified gas is discharged to the outside air.
従来の蓄熱燃焼式排ガス浄化装置において、吸引ライン8側の生産設備における被処理製品の段取り替えなどにより該浄化装置の昇温運転モードから生産設備の排ガス処理指令までの時間(ガス処理準備段階の時間)が長くなる場合や、排ガス処理指令後のガス処理運転の途中に生産設備における製品取替えなどにより一時停止した場合に、VOCを含む排ガスが排気されないあいだ、蓄熱燃焼式排ガス浄化装置は待機運転モードとなる。 In a conventional heat storage combustion type exhaust gas purification device, the time from the temperature raising operation mode of the purification device to the exhaust gas treatment command of the production facility (e.g., in the gas treatment preparation stage) by changing the product to be treated in the production facility on the suction line 8 side. The thermal storage combustion exhaust gas purifier is in standby operation when exhaust gas containing VOC is not exhausted when the time is long or when the gas treatment operation is temporarily stopped due to product replacement in the production facility after the exhaust gas treatment command. It becomes a mode.
なお、待機運転モードとは、吸引ライン8側からのVOCを含む排ガスをいつでも処理できるように、第1塔と第2塔に設置された蓄熱体1a、2aの熱的平衡を維持しつつ燃焼室3を所定温度(約800〜850℃)以上に維持する運転である。この待機運転モードでは、吸引ライン8側の排ガス経路が前記吸引遮断ダンパ9により遮断されるため、冷風取入ダンパ10から大気を取り入れるようにしている。 In the standby operation mode, combustion is performed while maintaining thermal equilibrium between the heat storage elements 1a and 2a installed in the first tower and the second tower so that exhaust gas containing VOC from the suction line 8 side can be treated at any time. In this operation, the chamber 3 is maintained at a predetermined temperature (about 800 to 850 ° C.) or higher. In this standby operation mode, the exhaust gas path on the suction line 8 side is blocked by the suction cutoff damper 9, so that the air is taken in from the cold air intake damper 10.
たとえば、図8に示されるように、自動運転の入力に基づき昇温運転モードが選択される(ステップS1)と、冷風取入ダンパを開かれる(ステップS2)。
そして、表1に示されるように、塔切替用第1ダンパサイクル運転と送風機の昇温運転風量の設定が行われるとともに、バーナが運転する(ステップS3)。
For example, as shown in FIG. 8, when the temperature raising operation mode is selected based on the automatic operation input (step S1), the cold air intake damper is opened (step S2).
Then, as shown in Table 1, the first damper cycle operation for tower switching and the setting of the temperature raising operation air volume of the blower are performed, and the burner is operated (step S3).
この第1ダンパサイクル運転では、第1塔と第2塔の入口ダンパと出口ダンパの開閉動作がパターン1とパターン2を交互に繰り返される。すなわち、図10に示されるように、第1塔の入口ダンパ4aと第2塔の出口ダンパ5bが開状態に切り替わるとともに第1の出口ダンパ4bと第2の入口ダンパ5aが閉状態に切り替わるパターン1と、第1塔の入口ダンパ4aと第2塔の出口ダンパ5bが閉状態に切り替わるとともに第1の出口ダンパ4bと第2の入口ダンパ5aが開状態に切り替わるパターン2とを交互に繰り返す。なお、図10における矢印Xは気流方向を示している。 In the first damper cycle operation, the opening and closing operations of the inlet damper and the outlet damper of the first tower and the second tower are repeated alternately in pattern 1 and pattern 2. That is, as shown in FIG. 10, a pattern in which the inlet damper 4a of the first tower and the outlet damper 5b of the second tower are switched to the open state and the first outlet damper 4b and the second inlet damper 5a are switched to the closed state. 1 and the pattern 2 in which the inlet damper 4a of the first tower and the outlet damper 5b of the second tower are switched to the closed state and the first outlet damper 4b and the second inlet damper 5a are switched to the open state are alternately repeated. In addition, the arrow X in FIG. 10 has shown the airflow direction.
ついで、燃焼室内の温度、たとえば850度の設定値に到達したか否かが判定される(ステップS4)。
この判定に基づいて、燃焼室の温度が設定値未満であると判断されると、再度判定を行い、燃焼室の温度が設定値以上であると判断されると、排ガス処理指令の入力を受信し、生産設備の処理運転モードが選択される(ステップS5)。
Next, it is determined whether or not a temperature in the combustion chamber, for example, a set value of 850 degrees has been reached (step S4).
Based on this determination, if it is determined that the temperature of the combustion chamber is lower than the set value, the determination is made again. If it is determined that the temperature of the combustion chamber is equal to or higher than the set value, the input of the exhaust gas treatment command is received. Then, the processing operation mode of the production facility is selected (step S5).
これに対して、たとえば生産設備における被処理製品の段取り替えに時間がかかり、排ガス処理指令が入力されない場合には、待機運転モードが選択される。 On the other hand, for example, when it takes time to change the product to be processed in the production facility and no exhaust gas treatment command is input, the standby operation mode is selected.
この待機運転モードが選択されると、図9に示されるように、送風機の待機運転風量が設定されたのち、運転中のバーナを停止し、消火させる温度が設定値に到達しているか否かが判定される(ステップS6、S7)。 When this standby operation mode is selected, as shown in FIG. 9, after the standby operation air volume of the blower is set, whether or not the temperature at which the burner during operation is stopped and the fire extinguishing reaches the set value is determined. Is determined (steps S6 and S7).
この判定に基づいて、温度が設定値未満であると判断されると、再度判定を行う。
そして、判定に基づいて、設定値以上であると判断されると、バーナを停止する(ステップ8)。
If it is determined that the temperature is lower than the set value based on this determination, the determination is performed again.
And if it is judged that it is more than a set value based on judgment, a burner will be stopped (Step 8).
ついで、バーナが停止されると、今度は燃焼室内を所定温度以上に維持するために、バーナを運転して再度着火させる温度が設定値、たとえば850℃に到達しているか否かが判定される(ステップ9)。 Next, when the burner is stopped, it is determined whether or not the temperature at which the burner is operated and ignited again reaches a set value, for example, 850 ° C., in order to maintain the combustion chamber at a predetermined temperature or higher. (Step 9).
この判定に基づいて、再度着火させる温度が設定値を越えて満たしていると判断されると、再度判定を行う。
そして、判定に基づいて、温度が設定値以下であると判断されると、バーナを運転する(ステップ10)。
その後、排ガス処理指令の入力信号を取得するまで、前述したステップ3〜4とタイミングを合わせてステップ7からステップ10を繰り返す。
If it is determined that the temperature to be ignited again exceeds the set value based on this determination, the determination is performed again.
If it is determined that the temperature is equal to or lower than the set value based on the determination, the burner is operated (step 10).
Thereafter, steps 7 to 10 are repeated in synchronism with steps 3 to 4 described above until an input signal of the exhaust gas treatment command is acquired.
従来の蓄熱燃焼式排ガス浄化装置における待機運転時は、冷風取入ダンパにより大気を導入するため、バーナ再着火温度の設定値の判定(ステップ9)に基づいて、燃焼室内を所定温度以上に維持しようすると、バーナで助燃する必要がある。
このため、ステップ9を繰り返す判定にかかる時間が長いと、バーナの運転時間が長くなることから、バーナの使用時間が長くなりバーナの寿命が短くなりやすいとともに、バーナの燃料消費量を削減することが難しい。
During standby operation in a conventional heat storage combustion exhaust gas purification device, the atmosphere is introduced by a cold air intake damper, so the combustion chamber is maintained at a predetermined temperature or higher based on determination of the set value of the burner reignition temperature (step 9). If you try, you will need to use a burner to help.
For this reason, if the time taken to repeat step 9 is long, the burner operation time becomes long, so the burner usage time is long, the burner life is likely to be shortened, and the fuel consumption of the burner is reduced. Is difficult.
そこで、本発明は、叙上の事情に鑑み、待機運転時における燃焼室のバーナの寿命の確保および燃料消費量の低減を図る蓄熱燃焼式排ガス浄化装置の運転制御方法を提供することを目的とする。 Therefore, in view of the above circumstances, the present invention has an object to provide an operation control method for a regenerative combustion exhaust gas purification device that ensures the life of a burner in a combustion chamber and reduces fuel consumption during standby operation. To do.
本発明の蓄熱燃焼式排ガス浄化装置の運転制御方法は、蓄熱体を配設した蓄熱室を有する塔を複数並列に配設し、各蓄熱体の上部をバーナが設けられる共通の燃焼室にした構造からなる本体と、各蓄熱体の下方にそれぞれ接続されている入口ダンパおよび出口ダンパと、該入口ダンパに接続される排ガス供給管と、該出口ダンパに接続される処理済みの浄化ガス排気管と、前記排ガス供給管における入口ダンパの上流位置に接続される送風機と、排ガス供給管から生産設備に延びる吸引ラインに接続される、排ガスの吸引と遮断を切替える吸引遮断ダンパおよび冷風取入ダンパと、各ダンパの切替および燃焼室の温度を制御する制御装置とを備える蓄熱燃焼式排ガス浄化装置において、塔切替用第1ダンパサイクル運転を有する運転モードを排ガス処理指令に基づいて待機運転モードに切替えて制御する運転制御方法であって、前記排ガス処理指令に基づいて切替えられた待機運転モードに少なくとも、隣接する塔の入口ダンパと出口ダンパが順次開状態に切り替わると他の塔の入口ダンパと出口ダンパが閉状態に切り替わるパターンを繰り返す塔切替用第2ダンパサイクル運転を行う工程を含むことを特徴としている。 In the operation control method of the heat storage combustion exhaust gas purification apparatus of the present invention, a plurality of towers having heat storage chambers provided with heat storage bodies are arranged in parallel, and the upper part of each heat storage body is made a common combustion chamber provided with a burner. A main body having a structure, an inlet damper and an outlet damper connected to each of the heat storage members, an exhaust gas supply pipe connected to the inlet damper, and a treated purified gas exhaust pipe connected to the outlet damper A blower connected to the upstream position of the inlet damper in the exhaust gas supply pipe, and a suction shut-off damper and a cold air intake damper that are connected to a suction line extending from the exhaust gas supply pipe to the production facility and that switch between suction and shut-off of the exhaust gas A regenerative combustion-type exhaust gas purification apparatus comprising a control device that controls the switching of each damper and the temperature of the combustion chamber, and has an operation mode having a first damper cycle operation for tower switching. An operation control method for controlling by switching to a standby operation mode based on a gas treatment command, wherein at least an entrance damper and an outlet damper of adjacent towers are sequentially opened in the standby operation mode switched based on the exhaust gas treatment command It is characterized by including a step of performing a tower switching second damper cycle operation that repeats a pattern in which the inlet damper and outlet damper of another tower are switched to a closed state when switched to.
本発明によれば、待機運転中の第2ダンパサイクル運転により、大気を塔内の蓄熱体に通さないで排出する制御を行っているので、燃焼室のバーナにて助燃する時間を低減することができる。 According to the present invention, since the second damper cycle operation during the standby operation is performed to discharge the atmosphere without passing through the heat storage body in the tower, the time for supporting the combustion with the burner in the combustion chamber is reduced. Can do.
これにより、待機運転時におけるバーナの寿命の確保および燃料消費量の低減を図ることができる。 Thereby, the lifetime of the burner during standby operation can be ensured and the fuel consumption can be reduced.
本発明は、蓄熱室の数により2塔式や、3塔式、多塔式がある蓄熱燃焼式排ガス浄化装置に適用することができる。2塔式の蓄熱燃焼式排ガス浄化装置が最も構造が単純で、小型にすることができる。 The present invention can be applied to a heat storage combustion type exhaust gas purifying apparatus having a two-tower type, a three-tower type, or a multi-tower type depending on the number of heat storage chambers. The two-column heat storage combustion exhaust gas purification device has the simplest structure and can be made compact.
以下、添付図面に基づいて本発明の蓄熱燃焼式排ガス浄化装置の運転制御方法を説明する。本発明に適用される一実施の形態にかかわる蓄熱燃焼式排ガス浄化装置は、基本的な構造として図7に示される蓄熱燃焼式排ガス浄化装置と同じであるが、制御装置Aに代えて制御装置Bが用いられている点で異なっている。 Hereinafter, the operation control method of the regenerative combustion type exhaust gas purification apparatus of the present invention will be described based on the attached drawings. The regenerative combustion exhaust gas purification apparatus according to an embodiment applied to the present invention is the same as the regenerative combustion exhaust gas purification apparatus shown in FIG. The difference is that B is used.
本実施の形態の蓄熱燃焼式排ガス浄化装置は、図1に示されるように、内部に第1の蓄熱体1aを配設した蓄熱室1を有する第1塔T1と第2の蓄熱体2aを配設した蓄熱室2を有する第2塔T2とを並列に配設し、各蓄熱体1a、2aの上部をバーナ3aが設けられる共通の燃焼室3にした構造からなる本体と、各蓄熱体1a、2aの下方にそれぞれ接続されている入口ダンパ4a、5aおよび出口ダンパ4b、5bと、入口ダンパ4a、5aに接続される排ガス供給管6aと、出口ダンパ4b、5bに接続される処理済みの浄化ガス排気管6bと、前記排ガス供給管6aにおける入口ダンパ4a、5aの上流位置に接続される送風機7および冷風導入ダンパ8と、排ガス供給管6aから生産設備に延びる吸引ライン10に接続される、排ガスの吸引と遮断を切替える吸引遮断ダンパ9および冷風導入ダンパ8と、各ダンパの切替および燃焼室の温度を制御する制御装置Bとを備えている。 As shown in FIG. 1, the heat storage combustion exhaust gas purifying apparatus of the present embodiment includes a first tower T1 and a second heat storage body 2a each having a heat storage chamber 1 in which a first heat storage body 1a is disposed. A main body having a structure in which the second tower T2 having the arranged heat storage chamber 2 is arranged in parallel, and the upper part of each heat storage body 1a, 2a is a common combustion chamber 3 provided with a burner 3a, and each heat storage body Inlet dampers 4a and 5a and outlet dampers 4b and 5b connected below 1a and 2a, exhaust gas supply pipe 6a connected to inlet dampers 4a and 5a, and processed to be connected to outlet dampers 4b and 5b, respectively The purified gas exhaust pipe 6b, the blower 7 and the cold air introduction damper 8 connected to the upstream positions of the inlet dampers 4a and 5a in the exhaust gas supply pipe 6a, and the suction line 10 extending from the exhaust gas supply pipe 6a to the production facility. Exclude It includes a suction shutoff damper 9 and the cold air introduction damper 8 switches the suction and blocking of the scan, and a control unit B for controlling the temperature of the switching and the combustion chamber of each damper.
つぎに、本実施の形態における蓄熱燃焼式排ガス浄化装置の運転制御について説明するが、図2に示されるように、昇温運転モード以降の制御(ステップS)は前記図8において説明した制御と同じであることから、説明を省略し、待機運転モード以降について説明する。 Next, the operation control of the regenerative combustion exhaust gas purification apparatus in the present embodiment will be described. As shown in FIG. 2, the control after the heating operation mode (step S) is the same as the control described in FIG. Since it is the same, description is abbreviate | omitted and it demonstrates after standby operation mode.
待機運転モードが選択されると、バーナが停止するとともに塔切替用第2ダンパサイクル運転と送風機の第2ダンパサイクル運転の風量の設定がほぼ同時に行われる(ステップSS1、SS2)。
なお、バーナが停止するとともに塔切替用第2ダンパサイクル運転と送風機の第2ダンパサイクル運転の風量の設定がほぼ同時に行われているが、たとえば前記塔切替用第2ダンパサイクル運転を行うときに、バーナの停止動作と第2ダンパサイクル運転の風量設定動作をタイミングをずらして行うようにすることもできる。
When the standby operation mode is selected, the burner is stopped and the setting of the air volume of the second damper cycle operation for tower switching and the second damper cycle operation of the blower is performed almost simultaneously (steps SS1, SS2).
The burner is stopped and the air volume is set almost simultaneously in the second damper cycle operation for tower switching and the second damper cycle operation for the blower. For example, when the second damper cycle operation for tower switching is performed, Also, the burner stop operation and the air volume setting operation of the second damper cycle operation can be performed at different timings.
この第2ダンパサイクル運転では、図4および表2に示されるように、第1塔T1の入口ダンパ4aと出口ダンパ4bが開状態に切り替わるとともに第2塔T2の入口ダンパ5aと出口ダンパ5bが閉状態に切り替わるパターン1と、第2塔T2の入口ダンパ5aと出口ダンパ5bが開状態に切り替わるとともに第1塔T1の入口ダンパ4aと出口ダンパ4bが閉状態に切り替わるパターン2とを交互に繰り返す。なお、図4における矢印Yは気流方向を示している。 In the second damper cycle operation, as shown in FIG. 4 and Table 2, the inlet damper 4a and the outlet damper 4b of the first tower T1 are switched to the open state, and the inlet damper 5a and the outlet damper 5b of the second tower T2 are The pattern 1 that switches to the closed state and the pattern 2 that switches the inlet damper 5a and the outlet damper 5b of the second tower T2 to the open state and the inlet damper 4a and the outlet damper 4b of the first tower T1 to the closed state are alternately repeated. . In addition, the arrow Y in FIG. 4 has shown the airflow direction.
ついで、燃焼室内を所定温度以上に維持するために、バーナを運転して再度着火させる温度、たとえば780〜800℃の設定値に到達しているか否かが判定される(ステップSS3)。 Next, in order to maintain the combustion chamber at a predetermined temperature or higher, it is determined whether or not a temperature at which the burner is operated and ignited again, for example, a set value of 780 to 800 ° C. has been reached (step SS3).
この判定に基づいて、再度着火させる温度(燃焼室の温度)が設定値を越えていると判断されると、再度判定を行う。
そして、この判定に基づいて、燃焼室の温度が設定値以下であると判断されると、塔切替用第1ダンパサイクル運転と送風機の待機運転の風量の設定が行われるとともに、バーナをほぼ同時に運転する(ステップSS4)。
なお、塔切替用第1ダンパサイクル運転と送風機の待機運転の風量の設定が行われるとともに、バーナをほぼ同時に運転しているが、たとえば塔切替用第1ダンパサイクル運転を行うときに、待機運転の風量設定動作とバーナの運転動作をタイミングをずらして行うようにすることもできる。
Based on this determination, if it is determined that the temperature to be ignited again (combustion chamber temperature) exceeds the set value, the determination is performed again.
Then, based on this determination, if it is determined that the temperature of the combustion chamber is equal to or lower than the set value, the air volume is set for the first damper switching cycle operation for tower switching and the standby operation for the blower, and the burner is set almost simultaneously. Drive (step SS4).
In addition, while setting the air volume of the tower switching first damper cycle operation and the standby operation of the blower, the burner is operated almost simultaneously. For example, when performing the tower switching first damper cycle operation, the standby operation is performed. The air volume setting operation and the burner operation can be performed at different timings.
このときの第1ダンパサイクル運転は、前記図8および表1に示されるように、前記昇温運転モードのときの第1ダンパサイクル運転と同じく、第1塔と第2塔の入口ダンパ4a、5aと出口ダンパ4b、5bの開閉動作がパターン1とパターン2を交互に繰り返す。 As shown in FIG. 8 and Table 1, the first damper cycle operation at this time is the same as the first damper cycle operation in the temperature raising operation mode, and the inlet dampers 4a of the first tower and the second tower, The opening / closing operation of 5a and outlet dampers 4b and 5b repeats pattern 1 and pattern 2 alternately.
ついで、運転中のバーナを停止し、消火させる温度が設定値に到達しているか否かが判定される(ステップSS5)。 Next, it is determined whether or not the operating burner is stopped and the temperature to be extinguished has reached the set value (step SS5).
この判定に基づいて、バーナの消火温度が設定値未満であると判断されると、再度判定を行う。
そして、判定に基づいて、温度が設定値以上であると判断されると、ステップSS2に移行してバーナを停止する。
そして、生産設備の稼動が復帰するまで、前記ステップSS2からステップSS5を繰り返す。
If it is determined that the fire extinguishing temperature of the burner is lower than the set value based on this determination, the determination is performed again.
And if it is judged that temperature is more than a preset value based on judgment, it will shift to Step SS2 and will stop a burner.
The steps SS2 to SS5 are repeated until the operation of the production facility returns.
本実施の形態では、待機運転中の第2ダンパサイクル運転により、大気を塔内の蓄熱体に通さないで排出する制御を行っているので、燃焼室のバーナにて助燃する時間を低減することができる。
これにより、使用しているバーナの寿命を確保し、燃料消費量を低減することから、省エネ運転を達成することができる。
さらに、大気を塔内の蓄熱体に通さないので、蓄熱体を通すための所定風量も必要なくなり、インバータで制御している送風機の回転数を下げて風量を変更することができる。これにより、ここでも回転数を下げることによって省エネ効果が期待できる。
In the present embodiment, the second damper cycle operation during the standby operation is controlled to discharge the atmosphere without passing through the heat storage body in the tower, so that the time for auxiliary combustion with the burner in the combustion chamber is reduced. Can do.
Thereby, since the lifetime of the burner currently used is ensured and fuel consumption is reduced, energy saving operation can be achieved.
Furthermore, since the atmosphere is not passed through the heat storage body in the tower, a predetermined air volume for passing the heat storage body is not necessary, and the air volume can be changed by lowering the rotational speed of the blower controlled by the inverter. Thereby, an energy saving effect can be expected by lowering the rotational speed.
なお、本実施の形態では、吸引ライン8側の生産設備における被処理製品の段取り替えなどにより該浄化装置の昇温運転モードから生産設備の排ガス処理指令までの時間が長くなる場合の待機運転モードについて説明したが、たとえば排ガス処理指令後のガス処理運転の途中に生産設備における製品取替えなどにより一時停止した場合にも適用することができる。ただしこの場合には、ステップSS1の次工程として吸引遮断ダンパを閉じる工程を入れるなど適宜追加変更を行う。 In the present embodiment, the standby operation mode in which the time from the temperature raising operation mode of the purification device to the exhaust gas treatment command of the production facility becomes longer due to, for example, setup change of the product to be treated in the production facility on the suction line 8 side. However, the present invention can also be applied to a case where, for example, the product is temporarily stopped due to product replacement in the production facility during the gas processing operation after the exhaust gas processing command. However, in this case, additional changes are made as appropriate, such as a step of closing the suction shut-off damper as a step subsequent to step SS1.
また、本実施の形態では、2塔式の蓄熱燃焼式排ガス浄化装置について説明したが、本発明は、これに限定されるものではなく、蓄熱室の数により3塔式または多塔式の蓄熱燃焼式排ガス浄化装置に適用することができる。 Further, in the present embodiment, a two-column heat storage combustion type exhaust gas purification device has been described, but the present invention is not limited to this, and a three-column or multi-column heat storage device depending on the number of heat storage chambers. It can be applied to a combustion exhaust gas purification device.
たとえば、図5に示されるように、3塔式の蓄熱燃焼式排ガス浄化装置においては、第1塔T1と第2塔T2に第3塔T3が並列に配設されているとともに、該第1塔T1、第2塔T2および第3塔T3に前記冷風取入ダンパ10に連通するパージ配管21がそれぞれ第1塔パージダンパ22a、第2塔パージダンパ22bおよび第3塔パージダンパ22cを介して接続されている。 For example, as shown in FIG. 5, in a three-column heat storage combustion exhaust gas purification apparatus, a third column T3 is arranged in parallel with the first column T1 and the second column T2, and the first column A purge pipe 21 communicating with the cold air intake damper 10 is connected to the tower T1, the second tower T2, and the third tower T3 via a first tower purge damper 22a, a second tower purge damper 22b, and a third tower purge damper 22c, respectively. Yes.
この3塔式の蓄熱燃焼式排ガス浄化装置は、前記2塔式の蓄熱燃焼式排ガス浄化装置とは異なりパージ配管21を接続する必要があるため、3塔式の蓄熱燃焼式排ガス浄化装置における塔切替用第1ダンパサイクル運転は、図5および表3に示されるように、第1塔T1、第2塔T2および第3塔T3のそれぞれの入口ダンパ4a、5a、23a、出口ダンパ4b、5b、23bおよびパージダンパ22a、22b、22cの切替パターンをパターン1、パターン2およびパターン3を交互に切替えるようにしている。 Unlike the two-tower thermal storage combustion exhaust gas purification apparatus, this three-tower thermal storage combustion exhaust gas purification apparatus needs to be connected to the purge pipe 21, so the tower in the three-tower thermal storage combustion exhaust gas purification apparatus As shown in FIG. 5 and Table 3, the first damper cycle operation for switching is performed in each of the inlet dampers 4a, 5a, 23a, and the outlet dampers 4b, 5b of the first tower T1, the second tower T2, and the third tower T3. , 23b and purge dampers 22a, 22b, and 22c are alternately switched between pattern 1, pattern 2, and pattern 3.
しかしながら、3塔式の蓄熱燃焼式排ガス浄化装置における塔切替用第2ダンパサイクル運転は、パージダンパ22a、22bおよび22cが閉じることから前記2塔式の蓄熱燃焼式排ガス浄化装置の塔切替用第2ダンパサイクル運転と同様に、図6および表4に示されるように、第1塔T1の入口ダンパ4aと出口ダンパ4bが開状態に切り替わるとともに第2塔T2および第3塔T3の入口ダンパ5a、23aと出口ダンパ5b、23bが閉状態に切り替わるパターンとしてのパターン1と、第2塔T2の入口ダンパ5aと出口ダンパ5bが開状態に切り替わるとともに第1塔T1の入口ダンパ4aと出口ダンパ4bおよび第3塔T3の入口ダンパ23aと出口ダンパ23bが閉状態に切り替わるパターンとしてのパターン2と、第3塔T3の入口ダンパ23aと出口ダンパ23bが開状態に切り替わるとともに第1塔T1の入口ダンパ4aと出口ダンパ4bおよび第2塔T2の入口ダンパ5aと出口ダンパ5bが閉状態に切り替わるパターンとしてのパターン3とを繰り返す。 However, in the second tower switching second damper cycle operation in the three-column heat storage combustion exhaust gas purification apparatus, since the purge dampers 22a, 22b and 22c are closed, the second tower switching second operation of the two-column heat storage combustion exhaust gas purification apparatus is performed. Similarly to the damper cycle operation, as shown in FIG. 6 and Table 4, the inlet damper 4a and the outlet damper 4b of the first tower T1 are switched to the open state, and the inlet dampers 5a of the second tower T2 and the third tower T3, 23a and the outlet dampers 5b and 23b are switched to the closed state, and the inlet damper 5a and the outlet damper 5b of the second tower T2 are switched to the open state, and the inlet damper 4a and the outlet damper 4b of the first tower T1 Pattern 2 as a pattern in which the entrance damper 23a and the exit damper 23b of the third tower T3 are switched to the closed state, and the third tower Pattern 3 as a pattern in which the inlet damper 23a and the outlet damper 23b of the third tower are switched to the open state and the inlet damper 4a and the outlet damper 4b of the first tower T1 and the inlet damper 5a and the outlet damper 5b of the second tower T2 are switched to the closed state. And repeat.
また、4塔式の蓄熱燃焼式排ガス浄化装置の場合には、前記パージ配管は必要なくなることから、塔切替用第2ダンパサイクル運転は、前記第2塔や第3塔の蓄熱燃焼式排ガス浄化装置と同様に、隣接する塔の入口ダンパと出口ダンパが順次開状態に切り替わると他の塔の入口ダンパと出口ダンパが閉状態に切り替わるパターンを繰り返す。 Further, in the case of a 4-tower heat storage combustion exhaust gas purification device, the purge pipe is not necessary, so the second damper cycle operation for tower switching is performed in the heat storage combustion exhaust gas purification of the second tower or the third tower. Similar to the apparatus, when the inlet damper and the outlet damper of the adjacent tower are sequentially switched to the open state, the pattern in which the inlet damper and the outlet damper of the other tower are switched to the closed state is repeated.
B 制御装置
T1 第1塔
T2 第2塔
T3 第3塔
1、2 蓄熱室
1a 第1の蓄熱体
2a 第2の蓄熱体
3 燃焼室
4a、5a、23a 入口ダンパ
4b、5b、23b 出口ダンパ
6a 排ガス供給管
6b 浄化ガス排気管
7 送風機
8 吸引ライン
9 吸引遮断ダンパ
10 冷風取入ダンパ
11 バーナ
12 温度センサ
21 パージ配管
22a、22b、22c パージダンパ
B Control device T1 First tower T2 Second tower T3 Third tower 1, 2 Heat storage chamber 1a First heat storage body 2a Second heat storage body 3 Combustion chambers 4a, 5a, 23a Inlet dampers 4b, 5b, 23b Outlet damper 6a Exhaust gas supply pipe 6b Purified gas exhaust pipe 7 Blower 8 Suction line 9 Suction shut-off damper 10 Cold air intake damper 11 Burner 12 Temperature sensor 21 Purge piping 22a, 22b, 22c Purge damper
Claims (8)
前記排ガス処理指令に基づいて切替えられた待機運転モードに少なくとも、隣接する塔の入口ダンパと出口ダンパが順次開状態に切り替わると他の塔の入口ダンパと出口ダンパが閉状態に切り替わるパターンを繰り返す塔切替用第2ダンパサイクル運転を行う工程を含むことを特徴する蓄熱燃焼式排ガス浄化装置の運転制御方法。 A main body having a structure in which a plurality of towers each having a heat storage chamber provided with a heat storage body are arranged in parallel and the upper part of each heat storage body is a common combustion chamber provided with a burner is connected to the lower side of each heat storage body. An inlet damper and an outlet damper, an exhaust gas supply pipe connected to the inlet damper, a treated purified gas exhaust pipe connected to the outlet damper, and an upstream position of the inlet damper in the exhaust gas supply pipe Connected to a suction line extending from the exhaust gas supply pipe to the production facility, a suction shut-off damper and a cold air intake damper for switching exhaust gas suction and shut-off, and a control device for controlling the switching of each damper and the temperature of the combustion chamber In the heat storage combustion type exhaust gas purification apparatus, the operation mode having the first damper cycle operation for tower switching is switched to the standby operation mode based on the exhaust gas treatment command. A operation control method of,
A tower that repeats a pattern in which the inlet damper and outlet damper of other towers are switched to the closed state when the inlet damper and outlet damper of the adjacent tower are sequentially switched to the open state at least in the standby operation mode switched based on the exhaust gas treatment command An operation control method for a regenerative combustion type exhaust gas purification apparatus, comprising a step of performing a second damper cycle operation for switching.
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