JPH044021A - High-temperature exhaust gas denitrification device - Google Patents
High-temperature exhaust gas denitrification deviceInfo
- Publication number
- JPH044021A JPH044021A JP2103001A JP10300190A JPH044021A JP H044021 A JPH044021 A JP H044021A JP 2103001 A JP2103001 A JP 2103001A JP 10300190 A JP10300190 A JP 10300190A JP H044021 A JPH044021 A JP H044021A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- temperature
- denitrification
- cooling
- temperature exhaust
- 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
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- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ガスタービン等から排出される高温の燃焼ガ
スの脱硝装置に係り、特に高温排ガスに、直接冷却用気
体を混合処理して、脱硝反応に好適な温度に冷却制御し
て脱硝効率の向上をはかる脱硝装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a denitrification device for high-temperature combustion gas discharged from a gas turbine or the like, and in particular, the present invention relates to a denitrification device for high-temperature combustion gas discharged from a gas turbine, etc. The present invention relates to a denitrification device that improves denitrification efficiency by controlling cooling to a temperature suitable for denitrification reactions.
最近の原子力発電の伸びに伴ない、火力発電はベースロ
ード用から負荷調整用へと移行する傾向にある。特に、
ガスタービンによる発電は、起動、停止が容易で迅速に
行えることから、シーズン火力用等としてガスタービン
単独で使用するケースもあり、排ガス温度が600〜7
00℃程度の高温になる。With the recent growth in nuclear power generation, there is a tendency for thermal power generation to shift from base load use to load adjustment use. especially,
Power generation using a gas turbine is easy and quick to start and stop, so there are cases where the gas turbine is used alone for seasonal thermal power, etc., and the exhaust gas temperature is 600-700℃.
The temperature will be as high as 00℃.
しかし、環境規制は年々厳しくなり、当然に窒素酸化物
(NOx)も規制値内に納める必要がある。However, environmental regulations are becoming stricter year by year, and it is natural that nitrogen oxides (NOx) must also be kept within regulatory limits.
第7図に、従来の高温排ガス脱硝システムの一例を示す
。すなわち、ガスタービンの排ガス出口部に、直接脱硝
反応器3を配置して排ガスの脱硝処理を行うシステムで
ある。FIG. 7 shows an example of a conventional high-temperature exhaust gas denitrification system. That is, this is a system in which the denitrification reactor 3 is placed directly at the exhaust gas outlet of the gas turbine to perform denitrification treatment on the exhaust gas.
一般に、脱硝触媒の性能は第6図(a)に示すごとく、
350℃前後で使用する場合が最も良く、高温に耐える
触媒はど、脱硝性能が低下する傾向にある。そのため、
高温排ガスを直接脱硝処理する場合には、第6図(b)
に示すごとく、脱硝温度が上昇するにしたがって、大量
の触媒が必要となってくる。Generally, the performance of the denitrification catalyst is as shown in Figure 6(a).
It is best to use the catalyst at around 350°C; catalysts that can withstand high temperatures tend to have lower denitrification performance. Therefore,
When directly denitrifying high-temperature exhaust gas, Fig. 6(b)
As shown in Figure 2, as the denitrification temperature increases, a large amount of catalyst becomes necessary.
このため、高温排ガスの脱硝方式として、水とアンモニ
アを注入して排ガスの高温領域を抑制し、脱硝触媒の耐
久性と脱硝性能の向上をはかる方法(特開平L−119
330号公報)あるいは高温排ガス中に冷却水をスプレ
ーして排ガス温度を最適温度に制御する装置(実開平1
−80617号公報)などが提案されている。For this reason, as a denitrification method for high-temperature exhaust gas, a method is proposed in which water and ammonia are injected to suppress the high-temperature region of the exhaust gas and to improve the durability and denitrification performance of the denitrification catalyst (Japanese Patent Application Laid-Open No. 1999-11991).
No. 330) or a device that sprays cooling water into high-temperature exhaust gas to control the exhaust gas temperature to the optimum temperature (Utility Model Publication No. 1
-80617) and the like have been proposed.
上述したごとく、従来の高温排ガスに対する脱硝システ
ムは、経済性を無視し多量の触媒を充填することにより
脱硝可能としたり、場合によっては、全く脱硝処理が不
可能となるケースもしばしば見られた。As mentioned above, conventional denitrification systems for high-temperature exhaust gas have often been able to perform denitrification by filling a large amount of catalyst, ignoring economic efficiency, or in some cases, have been unable to perform denitrification treatment at all.
また、高温排ガス系に水とアンモニアを注入したり、ま
た冷却水をスプレーして高温の排ガス温度の低下をはか
る方式は、冷却水を排ガス中に均等に混合して排ガスの
温度を適温に、しかも均一に降下させることがむつかし
く、生成する排水の処理にも問題があった。In addition, methods to lower the temperature of high-temperature exhaust gas by injecting water and ammonia into the high-temperature exhaust gas system or spraying cooling water are methods that evenly mix cooling water into the exhaust gas to maintain the appropriate temperature of the exhaust gas. Moreover, it was difficult to lower the wastewater uniformly, and there were also problems in treating the wastewater produced.
本発明の目的は、上記従来技術における問題点を解消す
るものであって、高温の排ガスに冷却用の空気あるいは
水蒸気などを導入して、排ガスの温度を使用する触媒に
おける脱硝性能が最も高い温度領域に均一に冷却して、
充填触媒量を低減すると共に、従来脱硝処理が不可能で
あった高温排ガスの脱硝を可能とし、かつ脱硝効率の高
い高温排ガスの脱硝装置を提供することにある。An object of the present invention is to solve the above-mentioned problems in the prior art, and to achieve the highest denitrification performance in a catalyst using the temperature of the exhaust gas by introducing cooling air or steam into the high-temperature exhaust gas. Cool the area evenly,
It is an object of the present invention to provide a denitrification device for high-temperature exhaust gas that can reduce the amount of catalyst charged, can denitrify high-temperature exhaust gas that has conventionally been impossible to denitrate, and has high denitrification efficiency.
上記本発明の目的を達成するために、ガスタービン等よ
り排出される高温の燃焼排ガスの出口部に、高温排ガス
と常温の冷却用空気などを十分に混合させる混合器を設
け、上記排ガスの温度を所定の温度範囲に均一に降下さ
せ、後流に設けられている脱硝反応器へ導入される排ガ
ス温度を最適な脱硝温度にまで、あらかじめ低下させて
脱硝処理を行うものである。In order to achieve the above object of the present invention, a mixer is provided at the outlet of high-temperature combustion exhaust gas discharged from a gas turbine or the like to sufficiently mix the high-temperature exhaust gas with room temperature cooling air, etc., and the temperature of the exhaust gas is The denitrification process is performed by uniformly lowering the temperature of the exhaust gas to a predetermined temperature range, and by lowering the temperature of the exhaust gas introduced into the denitrification reactor provided downstream to the optimal denitrification temperature in advance.
本発明は、ガスタービンなどより排出される高温の燃焼
排ガス系に、排ガス中のN0x(窒素酸化物)を触媒の
もとでアンモニアと反応させて無害なN2(窒素)に変
換する脱硝反応器を備えた高温排ガス脱硝装置において
、上記脱硝反応器の前流の高温排ガス系に、大気を吸引
もしくは加圧して導入して排ガスと混合させる混合器を
設け、排ガス温度を使用する触媒の脱硝反応効率の高い
温度範囲に冷却制御する手段を設けた高温排ガス脱硝装
置である。The present invention provides a denitrification reactor for high-temperature combustion exhaust gas systems discharged from gas turbines, etc., which reacts NOx (nitrogen oxides) in the exhaust gas with ammonia under a catalyst to convert it into harmless N2 (nitrogen). In a high-temperature exhaust gas denitrification device equipped with a high-temperature exhaust gas denitrification system, a mixer is installed in the high-temperature exhaust gas system upstream of the denitrification reactor to suck or pressurize atmospheric air and mix it with the exhaust gas. This is a high-temperature exhaust gas denitrification device equipped with means for controlling cooling to a highly efficient temperature range.
本発明における高温排ガスの冷却制御手段は、高温排ガ
ス系にベンチュリ機構を設け、該ベンチュリ機構によっ
て大気を直接吸引混合して排ガス温度を冷却制御する手
段、またはファンもしくはコンプレッサにより大気を吸
引昇圧して高温排ガス系に導入して排ガスと混合させ、
排ガス温度を冷却制御する手段、あるいは高温排ガス系
にベンチュリ機構を設けて大気を直接吸引混合する手段
と、ファンもしくはコンプレッサにより大気を昇圧して
導入し排ガスと混合させる手段とを併用することにより
、排ガス温度を冷却制御することができる。さらに、本
発明の高温排ガスの冷却制御手段は、高温排ガス系に水
蒸気を導入して混合し排ガス温度を冷却制御することも
できる。The cooling control means for high-temperature exhaust gas in the present invention includes means for providing a venturi mechanism in the high-temperature exhaust gas system and controlling the temperature of the exhaust gas by directly sucking and mixing the atmosphere with the venturi mechanism, or by sucking and pressurizing the atmosphere using a fan or compressor. Introduced into the high-temperature exhaust gas system and mixed with exhaust gas,
By using a combination of means for cooling and controlling the exhaust gas temperature, or means for directly sucking and mixing atmospheric air by providing a venturi mechanism in the high-temperature exhaust gas system, and means for increasing the pressure of atmospheric air using a fan or compressor and introducing it and mixing it with the exhaust gas, The exhaust gas temperature can be controlled by cooling. Furthermore, the high-temperature exhaust gas cooling control means of the present invention can also cool and control the exhaust gas temperature by introducing and mixing water vapor into the high-temperature exhaust gas system.
そして、本発明の高温排ガスの冷却制御手段において、
該冷却制御手段の冷却用流体の供給系に。And, in the high temperature exhaust gas cooling control means of the present invention,
In the cooling fluid supply system of the cooling control means.
排ガス温度を制御するための流体の流量制御ダンパおよ
び流量制御弁を設け、排ガス温度を冷却制御する手段を
有するものであり、また冷却制御手段の冷却用流体の供
給系に、脱硝反応用のアンモニアを注入混合する手段を
設け、上記冷却用流体中にアンモニアを混合させて排ガ
ス温度を冷却制御することもできる。It is equipped with a fluid flow control damper and a flow control valve for controlling the exhaust gas temperature, and has means for cooling and controlling the exhaust gas temperature, and also has ammonia for denitrification reaction in the cooling fluid supply system of the cooling control means. It is also possible to provide a means for injecting and mixing ammonia into the cooling fluid to control the exhaust gas temperature by cooling.
脱硝反応器への排ガス入口ガス温度を均一に低下させて
、使用する触媒の最も脱硝能力の高い温度範囲に制御し
て脱硝処理を行うため、少ない充填触媒量で、高い効率
で脱硝反応を達成することが可能となる。The temperature of the exhaust gas inlet to the denitrification reactor is uniformly lowered and the denitrification process is performed by controlling it to the temperature range where the catalyst used has the highest denitrification ability, achieving highly efficient denitrification reactions with a small amount of catalyst charged. It becomes possible to do so.
以下に本発明の一実施例を挙げ1図面を引用しながらさ
らに詳細に説明する。第1図に1本発明の脱硝装置にお
ける脱硝システムの一例を示す。Hereinafter, one embodiment of the present invention will be described in more detail with reference to one drawing. FIG. 1 shows an example of the denitrification system in the denitrification apparatus of the present invention.
図に示すごとく、ガスタービン1の出口部に、常温の大
気等を混合する混合器2を設け、処理ガス温度を脱硝反
応の最適温度に低下させた後、脱硝反応器3へ導入して
、排ガス中のNOxを脱硝させる方式である。As shown in the figure, a mixer 2 is installed at the outlet of the gas turbine 1 to mix atmospheric air at room temperature, and after the temperature of the treated gas is lowered to the optimum temperature for the denitrification reaction, it is introduced into the denitrification reactor 3. This method removes NOx from exhaust gas.
例えば、650’Cで脱硝反応13に流入する排ガスを
処理する場合は、第6図(b)に示すように、従来は3
50℃処理の触媒量に対し約10倍の脱硝触媒量が必要
であったが、排ガス温度を500℃に低下させることに
より第6図(d)に示すように約2倍の触媒量で安定し
た脱硝が可能となる。For example, when treating exhaust gas flowing into the denitrification reaction 13 at 650'C, as shown in Figure 6(b), conventionally
Approximately 10 times the amount of denitration catalyst was required compared to the amount of catalyst used in the 50°C treatment, but by lowering the exhaust gas temperature to 500°C, the amount of catalyst stabilized at approximately twice the amount as shown in Figure 6 (d). denitrification is possible.
第2図〜第5図は、本発明の高温排ガスの脱硝装置にお
ける大気等の冷却流体を混合し、最適な脱硝反応温度に
制御する場合のプロセスフローを示す具体例であって、
冷却流体の混合手段と排ガス温度制御方式および脱硝用
NH,(アンモニア)の注入位置などの一例を示す。FIGS. 2 to 5 are specific examples showing a process flow when a cooling fluid such as atmospheric air is mixed in the high-temperature exhaust gas denitrification apparatus of the present invention and the denitrification reaction temperature is controlled to the optimum temperature.
An example of the cooling fluid mixing means, the exhaust gas temperature control method, and the injection position of NH and (ammonia) for denitrification is shown.
第2図は、ベンチュリ4を使用し、大気を直接吸引混合
し冷却制御する方式を示す。FIG. 2 shows a method in which a venturi 4 is used to directly suck and mix atmospheric air to control cooling.
第3図は、ファン5により大気を吸引昇圧し、混合器2
に送入して冷却制御する方式を示す。Figure 3 shows air being sucked and pressurized by a fan 5, and a mixer 2
The following shows a method for controlling cooling by feeding
第4図は、圧縮空気6とベンチュリ7を用いて、大気を
吸引昇圧し、混合器2に送入して冷却する制御方式を示
す。FIG. 4 shows a control system in which atmospheric air is sucked and pressurized using compressed air 6 and venturi 7, and is then sent to mixer 2 for cooling.
第5図は、水蒸気8を混合器2に供給し、高温の排ガス
温度を冷却制御する方式を示す。FIG. 5 shows a method of supplying water vapor 8 to the mixer 2 and controlling the temperature of the high-temperature exhaust gas by cooling it.
以上詳細に説明したごとく、本発明の高温排ガス脱硝装
置によれば、高温の排ガス温度を脱硝反応効率の最もよ
い温度範囲に自在に冷却制御することが可能であるので
、少ない触媒の使用量で排ガス中のNOxを高い効率で
脱硝することができる。As explained in detail above, according to the high-temperature exhaust gas denitrification device of the present invention, it is possible to freely control the cooling of the high-temperature exhaust gas to the temperature range that provides the best denitrification reaction efficiency, so it is possible to use a small amount of catalyst. NOx in exhaust gas can be denitrated with high efficiency.
第1図は本発明の実施例において例示した高温排ガス脱
硝装置のシステムフローを示す図、第2図ないし第5図
は本発明の実施例における具体的な実施態様を示す系統
図、第6図(、)は脱硝触媒の排ガス温度と触媒性能(
割合)との関係を示すグラフ、第6図(b)は第6図(
a)に示す触媒を使用した場合の各排ガス温度に対する
触媒充基量(割合)を示すグラフ、第6図(c)は排ガ
ス温度を低下させるために混合した空気増加量に対する
触媒充填量の増加割合を示すグラフ、第6図(d)は第
6図(b)と第6図(c)から算出した合計触媒充填量
(割合)を示すグラフ、第7図は従来の高温排ガス脱硝
装置における脱硝システムフローを示す図である。
1・・・ガスタービン 2・・混合器3・・脱硝反
応器 4・・・ベンチュリ5・・・ファン
6・・・圧縮空気7・・ベンチュリ 8・
・・水蒸気9・・ダンパ 10・・・サイレ
ンサ11・・・制御弁FIG. 1 is a diagram showing a system flow of a high-temperature exhaust gas denitrification device exemplified in an embodiment of the present invention, FIGS. 2 to 5 are system diagrams showing specific embodiments in an embodiment of the present invention, and FIG. (,) is the exhaust gas temperature of the denitrification catalyst and the catalyst performance (
Figure 6(b) is a graph showing the relationship between
A graph showing the amount of catalyst filling (ratio) for each exhaust gas temperature when using the catalyst shown in a), Figure 6(c) shows the increase in the amount of catalyst filling relative to the amount of air mixed to lower the exhaust gas temperature. Figure 6(d) is a graph showing the total catalyst filling amount (ratio) calculated from Figures 6(b) and 6(c). Figure 7 is a graph showing the ratio in a conventional high-temperature exhaust gas denitrification device. It is a figure showing a denitrification system flow. 1... Gas turbine 2... Mixer 3... Denitration reactor 4... Venturi 5... Fan
6...Compressed air 7...Venturi 8.
...Steam 9...Damper 10...Silencer 11...Control valve
Claims (1)
系に、排ガス中のNO_x(窒素酸化物)を触媒のもと
でアンモニアと反応させて無害なN_2(窒素)に変換
する脱硝反応器を備えた高温排ガス脱硝装置において、
上記脱硝反応器の前流の高温排ガス系に、大気を吸引も
しくは加圧して導入して排ガスと混合させる混合器を設
け、排ガス温度を使用する触媒の脱硝反応効率の高い温
度範囲に冷却制御する手段を設けたことを特徴とする高
温排ガス脱硝装置。 2、請求の範囲第1項の高温排ガスの冷却制御手段は、
高温排ガス系にベンチュリ機構を設け、該ベンチュリ機
構によって大気を直接吸引混合して排ガス温度を冷却制
御する手段であることを特徴とする高温排ガス脱硝装置
。 3、請求の範囲第1項の高温排ガスの冷却制御手段は、
ファンもしくはコンプレッサにより大気を吸引昇圧して
高温排ガス系に導入して排ガスと混合させ、排ガス温度
を冷却制御する手段であることを特徴とする高温排ガス
脱硝装置。 4、請求の範囲第1項の高温排ガスの冷却制御手段は、
高温排ガス系にベンチュリ機構を設けて大気を直接吸引
混合する手段と、ファンもしくはコンプレッサにより大
気を昇圧して導入し排ガスと混合させる手段とにより、
排ガス温度を冷却制御することを特徴とする高温排ガス
脱硝装置。 5、請求の範囲第1項の高温排ガスの冷却制御手段は、
高温排ガス系に水蒸気を導入して混合し排ガス温度を冷
却制御する手段であることを特徴とする高温排ガス脱硝
装置。 6、請求の範囲第1項、第2項、第3項、第4項または
第5項記載の排ガス温度の冷却制御手段において、該冷
却制御手段の冷却用流体の供給系に、排ガス温度を制御
するための流体の流量制御ダンパおよび流量制御弁を設
け、排ガス温度を冷却制御する手段を備えたことを特徴
とする高温排ガス脱硝装置。 7、請求の範囲第1項ないし第6項のいずれか1項記載
の排ガス温度の冷却制御手段において、該冷却制御手段
の冷却用流体の供給系に、脱硝反応用のアンモニアを注
入混合する手段を設け、上記冷却用流体中にアンモニア
を混合させて排ガス温度を冷却制御する手段を備えたこ
とを特徴とする高温排ガス脱硝装置。[Claims] 1. In the high-temperature combustion exhaust gas system discharged from a gas turbine, etc., NO_x (nitrogen oxides) in the exhaust gas is converted to harmless N_2 (nitrogen) by reacting with ammonia under a catalyst. In a high-temperature exhaust gas denitrification equipment equipped with a denitrification reactor,
A mixer is installed in the high-temperature exhaust gas system upstream of the denitrification reactor to suck or pressurize atmospheric air and mix it with the exhaust gas, and the temperature of the exhaust gas is controlled to be within a temperature range where the denitrification reaction efficiency of the catalyst used is high. A high-temperature exhaust gas denitrification device characterized by being provided with a means. 2. The high-temperature exhaust gas cooling control means according to claim 1,
A high-temperature exhaust gas denitrification device, characterized in that a venturi mechanism is provided in a high-temperature exhaust gas system, and the venturi mechanism directly sucks and mixes atmospheric air to cool and control the exhaust gas temperature. 3. The high-temperature exhaust gas cooling control means according to claim 1,
A high-temperature exhaust gas denitrification device characterized by being a means for cooling and controlling the exhaust gas temperature by suctioning and pressurizing atmospheric air using a fan or compressor, introducing it into a high-temperature exhaust gas system, and mixing it with the exhaust gas. 4. The high-temperature exhaust gas cooling control means according to claim 1,
By providing a venturi mechanism in the high-temperature exhaust gas system to directly suck and mix the atmosphere, and by using a fan or compressor to increase the pressure of the atmosphere and introduce it and mix it with the exhaust gas,
A high-temperature exhaust gas denitrification device characterized by cooling and controlling exhaust gas temperature. 5. The high-temperature exhaust gas cooling control means according to claim 1,
A high-temperature exhaust gas denitrification device characterized by being a means for introducing and mixing water vapor into a high-temperature exhaust gas system to cool and control the exhaust gas temperature. 6. In the exhaust gas temperature cooling control means according to claim 1, 2, 3, 4 or 5, the exhaust gas temperature is controlled in the cooling fluid supply system of the cooling control means. 1. A high-temperature exhaust gas denitrification device, comprising a fluid flow rate control damper and a flow rate control valve for control, and means for cooling and controlling exhaust gas temperature. 7. In the exhaust gas temperature cooling control means according to any one of claims 1 to 6, means for injecting and mixing ammonia for denitrification reaction into the cooling fluid supply system of the cooling control means. 1. A high-temperature exhaust gas denitrification device comprising: a means for cooling and controlling exhaust gas temperature by mixing ammonia into the cooling fluid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2103001A JPH044021A (en) | 1990-04-20 | 1990-04-20 | High-temperature exhaust gas denitrification device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2103001A JPH044021A (en) | 1990-04-20 | 1990-04-20 | High-temperature exhaust gas denitrification device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH044021A true JPH044021A (en) | 1992-01-08 |
Family
ID=14342437
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2103001A Pending JPH044021A (en) | 1990-04-20 | 1990-04-20 | High-temperature exhaust gas denitrification device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH044021A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009057976A (en) * | 2007-08-31 | 2009-03-19 | General Electric Co <Ge> | Power generation system with exhaust temperature adjustment device and method for controlling the temperature of exhaust gas |
| JP2010144632A (en) * | 2008-12-19 | 2010-07-01 | Ud Trucks Corp | Exhaust emission control device |
| US9644511B2 (en) | 2012-09-06 | 2017-05-09 | Mitsubishi Hitachi Power Systems, Ltd. | Combustion gas cooling apparatus, denitration apparatus including the combustion gas cooling apparatus, and combustion gas cooling method |
| US9890672B2 (en) | 2012-09-06 | 2018-02-13 | Mitsubishi Hitachi Power Systems, Ltd. | Combustion gas cooling apparatus, denitration apparatus having the combustion gas cooling apparatus, and combustion gas cooling method |
| FR3085998A1 (en) * | 2018-09-18 | 2020-03-20 | Psa Automobiles Sa | VEHICLE EXHAUST SYSTEM WITH NEUTRAL GAS COOLING CIRCUIT UPSTREAM OF THE CLEANING DEVICE |
-
1990
- 1990-04-20 JP JP2103001A patent/JPH044021A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009057976A (en) * | 2007-08-31 | 2009-03-19 | General Electric Co <Ge> | Power generation system with exhaust temperature adjustment device and method for controlling the temperature of exhaust gas |
| JP2010144632A (en) * | 2008-12-19 | 2010-07-01 | Ud Trucks Corp | Exhaust emission control device |
| US9644511B2 (en) | 2012-09-06 | 2017-05-09 | Mitsubishi Hitachi Power Systems, Ltd. | Combustion gas cooling apparatus, denitration apparatus including the combustion gas cooling apparatus, and combustion gas cooling method |
| US9890672B2 (en) | 2012-09-06 | 2018-02-13 | Mitsubishi Hitachi Power Systems, Ltd. | Combustion gas cooling apparatus, denitration apparatus having the combustion gas cooling apparatus, and combustion gas cooling method |
| FR3085998A1 (en) * | 2018-09-18 | 2020-03-20 | Psa Automobiles Sa | VEHICLE EXHAUST SYSTEM WITH NEUTRAL GAS COOLING CIRCUIT UPSTREAM OF THE CLEANING DEVICE |
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