JPH085002A - Natural circulation type water tube boiler facility - Google Patents

Natural circulation type water tube boiler facility

Info

Publication number
JPH085002A
JPH085002A JP13316494A JP13316494A JPH085002A JP H085002 A JPH085002 A JP H085002A JP 13316494 A JP13316494 A JP 13316494A JP 13316494 A JP13316494 A JP 13316494A JP H085002 A JPH085002 A JP H085002A
Authority
JP
Japan
Prior art keywords
exhaust gas
flow passage
gas flow
denitration device
natural circulation
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
Application number
JP13316494A
Other languages
Japanese (ja)
Inventor
Akira Fujisawa
明 藤澤
Hideki Teragakinai
秀樹 寺垣内
Hisashi Honda
寿 本田
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.)
IHI Corp
IHI Packaged Boiler Co Ltd
Original Assignee
IHI Corp
IHI Packaged Boiler 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 IHI Corp, IHI Packaged Boiler Co Ltd filed Critical IHI Corp
Priority to JP13316494A priority Critical patent/JPH085002A/en
Publication of JPH085002A publication Critical patent/JPH085002A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00Methods of steam generation characterised by form of heating method
    • F22B1/02Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • F22B1/1807Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines using the exhaust gases of combustion engines
    • F22B1/1815Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines using the exhaust gases of combustion engines using the exhaust gases of gas-turbines

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chimneys And Flues (AREA)

Abstract

PURPOSE:To contrive the miniaturization of a facility as well as making of the facility in one unit by a method wherein nitrogen oxide is removed from high-temperature exhaust gas, supplied into a lower side exhaust gas flow passage, through a high-temperature denitrification device, then, the exhaust gas is guided into an upper side exhaust gas flow passage in the form of turning back and is discharged into atmosphere through a natural circulation type water tube boiler and a feed water preheater. CONSTITUTION:The inside of a casing 19 is partitioned into lower and upper side exhaust gas flow passages 21, 22 by a partitioning plate 20 while exhaust gas, introduced from an exhaust gas supplying port 17 connected to an exhaust gas supplying duct 1a, is conducted into the upper side exhaust gas flow passage 22 through the lower side exhaust gas flow passage 21 in the form of turning back. A high-temperature denitrification device 12 is provided in the lower side exhaust gas flow passage 21 of the casing 19 while a natural circulation type water tube boiler 11 is arranged at the downstream side of the high-temperature denitrification device 12 so that boiler tubes 4 penetrate through the partitioning plate 20. On the other hand, a medium-temperature denitrification device 13 is provided at the turning back part 23 between both of flow passages 21, 22 while a feed water preheater 14 is provided in the upper side exhaust gas flow passage 22 at the downstream side of the water tube boiler 11 respectively and a changeover damper 16 is provided in a communicating unit 24, communicating the flow passage 21 with the flow passage 22.

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、自然循環式水管ボイラ
設備に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a natural circulation type water pipe boiler facility.

【0002】[0002]

【従来の技術】一般に、自然循環式水管ボイラ設備は、
図2に示される如く、排ガスダクト1途中に、該排ガス
ダクト1より上方に配置された汽水胴2と、該汽水胴2
と相対向して排ガスダクト1より下方に位置するよう配
置された水胴3と、上端が汽水胴2に接続され且つ下端
が排ガスダクト1内を貫通して水胴3に接続され前記排
ガスダクト1の長手方向並びに幅方向に所定の間隔をあ
けて並設された多数の管4と、前記汽水胴2の側部から
排ガスダクト1に沿い排ガス5の流れ方向上流側へ延び
る連絡管6の先端部に接続された上部管寄せ7と、前記
水胴3の底部近傍の側部から排ガスダクト1に沿い排ガ
ス5の流れ方向上流側へ延びる連絡管8の先端部に接続
された下部管寄せ9と、上端が上部管寄せ7に接続され
且つ下端が排ガスダクト1内を貫通して下部管寄せ9に
接続され前記排ガスダクト1の長手方向並びに幅方向に
所定の間隔をあけて並設された多数の管10とを備えた
自然循環式水管ボイラ11を配設し、該自然循環式水管
ボイラ11の管10より上流側における排ガスダクト1
途中に、排ガス5中に含まれる窒素酸化物(NOx)を
除去するための高温脱硝装置12を設けると共に、前記
自然循環式水管ボイラ11の管10と管4の間における
排ガスダクト1途中に、排ガス5中に含まれる窒素酸化
物(NOx)を除去するための中温脱硝装置13を設
け、前記自然循環式水管ボイラ11の管4より下流側に
おける排ガスダクト1途中に、給水予熱器14を設け、
更に、前記高温脱硝装置12の上流側における排ガスダ
クト1と給水予熱器14の下流側における排ガスダクト
1とをバイパスダクト15によって連結し、該バイパス
ダクト15の上流端部に、バイパスダクト15の上流端
部を閉塞して排ガス5を高温脱硝装置12へ導く位置P
1と、高温脱硝装置12の上流側における排ガスダクト
1を閉塞して排ガス5をバイパスダクト15へ導く位置
P2とに切換可能な切換ダンパ16を設けてなる構成を
有している。
2. Description of the Related Art Generally, natural circulation type water pipe boiler equipment is
As shown in FIG. 2, a brackish water cylinder 2 arranged above the exhaust gas duct 1 in the middle of the exhaust gas duct 1 and the brackish water cylinder 2
A water cylinder 3 arranged so as to be opposed to the exhaust gas duct 1 and located below the exhaust gas duct 1, and an upper end connected to the brackish water cylinder 2 and a lower end penetrating the exhaust gas duct 1 and connected to the water cylinder 3 1 of a number of pipes 4 arranged in parallel in the longitudinal direction and the width direction at predetermined intervals, and a connecting pipe 6 extending from the side of the brackish water cylinder 2 along the exhaust gas duct 1 to the upstream side in the flow direction of the exhaust gas 5. The upper header 7 connected to the tip, and the lower header connected to the tip of the connecting pipe 8 extending from the side near the bottom of the water cylinder 3 along the exhaust gas duct 1 to the upstream side in the flow direction of the exhaust gas 5. 9, the upper end is connected to the upper header 7, and the lower end penetrates through the exhaust gas duct 1 and is connected to the lower header 9, which are arranged in parallel in the longitudinal direction and the width direction of the exhaust gas duct 1 with a predetermined interval. Natural circulation type water pipe with a large number of pipes 10 La 11 disposed, discharge at the upstream side of the tubing 10 of the natural circulation water tube boiler 11 gas duct 1
Along the way, a high temperature denitration device 12 for removing nitrogen oxides (NOx) contained in the exhaust gas 5 is provided, and in the middle of the exhaust gas duct 1 between the pipe 10 and the pipe 4 of the natural circulation type water pipe boiler 11, A medium temperature denitration device 13 for removing nitrogen oxides (NOx) contained in the exhaust gas 5 is provided, and a feed water preheater 14 is provided in the exhaust gas duct 1 downstream of the pipe 4 of the natural circulation type water pipe boiler 11. ,
Further, the exhaust gas duct 1 on the upstream side of the high-temperature denitration device 12 and the exhaust gas duct 1 on the downstream side of the feedwater preheater 14 are connected by a bypass duct 15, and the upstream end of the bypass duct 15 is connected to the upstream side of the bypass duct 15. Position P that closes the end and guides the exhaust gas 5 to the high temperature denitration device 12
1 and a position P2 that closes the exhaust gas duct 1 on the upstream side of the high-temperature denitration device 12 and guides the exhaust gas 5 to the bypass duct 15 by providing a switching damper 16.

【0003】蒸気を必要とする場合、切換ダンパ16を
位置P1に切り換えておくと、排ガスダクト1を流れる
高温の排ガス5は、高温脱硝装置12へ導かれ、該高温
脱硝装置12において窒素酸化物が除去された後、自然
循環式水管ボイラ11の管10の間を流れ、前記窒素酸
化物が除去された高温の排ガス5と、自然循環式水管ボ
イラ11の水胴3から連絡管8と下部管寄せ9を介して
管10内に充満しているボイラ水との間で熱交換が行わ
れ、該ボイラ水が加熱されて蒸気化すると共に前記排ガ
ス5の温度が所要温度まで下がる。
When steam is required, if the switching damper 16 is switched to the position P1, the high temperature exhaust gas 5 flowing through the exhaust gas duct 1 is guided to the high temperature denitration device 12, and the high temperature denitration device 12 produces nitrogen oxides. After being removed, the high-temperature exhaust gas 5 that has flowed between the tubes 10 of the natural circulation water tube boiler 11 and has the nitrogen oxides removed, the water cylinder 3 of the natural circulation water tube boiler 11 to the connecting tube 8 and the lower part Heat exchange is performed with the boiler water filling the inside of the pipe 10 via the header 9, the boiler water is heated and vaporized, and the temperature of the exhaust gas 5 is lowered to the required temperature.

【0004】前記管10内において加熱されて蒸気化し
たボイラ水は自然循環により上昇し、上部管寄せ7から
連絡管6を通って汽水胴2へ流入し、又、水胴3内の水
は連絡管8から下部管寄せ9を経て管10内に流入す
る。
The boiler water heated and vaporized in the pipe 10 rises by natural circulation, flows from the upper header 7 through the connecting pipe 6 into the brackish water cylinder 2, and the water in the water cylinder 3 is It flows from the connecting pipe 8 into the pipe 10 through the lower header 9.

【0005】前記所要温度となった排ガス5は、排ガス
ダクト1内を流れて中温脱硝装置13へ流入し、該中温
脱硝装置13において更に窒素酸化物が除去された後、
自然循環式水管ボイラ11の管4の間を流れ、前記窒素
酸化物が除去された所要温度の排ガス5によって管4内
のボイラ水が加熱され、温度が更に低下した排ガス5が
給水予熱器14へ導かれ、該給水予熱器14内の水と熱
交換を行った後、下流の排ガスダクト1から大気へ放出
される。
The exhaust gas 5 having the required temperature flows through the exhaust gas duct 1 and flows into the intermediate temperature denitration device 13, and after further nitrogen oxides are removed in the intermediate temperature denitration device 13,
The boiler water in the pipe 4 is heated by the exhaust gas 5 of the required temperature from which the nitrogen oxides have been removed, flowing between the pipes 4 of the natural circulation type water pipe boiler 11, and the exhaust gas 5 of which the temperature has further decreased is the feed water preheater 14 And is exchanged with the water in the feed water preheater 14 and then discharged to the atmosphere from the exhaust gas duct 1 located downstream.

【0006】前記自然循環式水管ボイラ11の排ガス流
れ方向上流側に位置する管4内のボイラ水は、排ガス流
れ方向下流側と比べ相対的に高温度の排ガス5によって
加熱されつつ前記管4内を上昇すると共に、前記自然循
環式水管ボイラ11の排ガス流れ方向下流側に位置する
管4内のボイラ水は、排ガス流れ方向上流側と比べ相対
的に低温度の排ガス5によって加熱されつつ前記管4内
を下降する形となり、この結果、汽水胴2と水胴3との
間でボイラ水の自然循環が行われ、生成された蒸気が汽
水胴2から取り出される。
The boiler water in the pipe 4 located upstream of the natural circulation type water pipe boiler 11 in the exhaust gas flow direction is heated by the exhaust gas 5 having a relatively higher temperature than in the downstream of the exhaust gas flow direction in the pipe 4. And the boiler water in the pipe 4 located on the downstream side in the exhaust gas flow direction of the natural circulation type water pipe boiler 11 is heated by the exhaust gas 5 having a relatively low temperature as compared with the upstream side in the exhaust gas flow direction, As a result, the boiler water naturally circulates between the steam cylinder 2 and the water cylinder 3, and the generated steam is taken out from the steam cylinder 2.

【0007】一方、運転の都合上、蒸気を必要としない
場合には、切換ダンパ16を位置P2に切り換えると、
高温脱硝装置12の上流側における排ガスダクト1が閉
塞され、排ガス5がバイパスダクト15へ導かれ、前記
高温脱硝装置12から給水予熱器14の間を通過せず
に、迂回する形でバイパスダクト15から下流側の排ガ
スダクト1へ流れて行く。
On the other hand, when steam is not required for the convenience of operation, the switching damper 16 is switched to the position P2,
The exhaust gas duct 1 on the upstream side of the high-temperature denitration device 12 is closed, the exhaust gas 5 is guided to the bypass duct 15, and the bypass duct 15 is bypassed without passing between the high-temperature denitration device 12 and the feedwater preheater 14. To the exhaust gas duct 1 on the downstream side.

【0008】[0008]

【発明が解決しようとする課題】しかしながら、前述の
如き自然循環式水管ボイラ設備では、排ガスダクト1の
上流側から下流側へ向け順次、高温脱硝装置12と、自
然循環式水管ボイラ11の管10と、中温脱硝装置13
と、自然循環式水管ボイラ11の管4と、給水予熱器1
4とを配置しているため、全長が長くなって設備の大型
化が避けられず、設置場所の制約が大きくなると共に、
据え付けに関しても各機器を現地へ搬入し組立る必要が
あり、工数の増加並びにコストアップにつながるという
欠点を有していた。
However, in the natural circulation type water pipe boiler equipment as described above, the high temperature denitration device 12 and the pipe 10 of the natural circulation type water pipe boiler 11 are sequentially arranged from the upstream side to the downstream side of the exhaust gas duct 1. And the medium temperature denitration device 13
And the tube 4 of the natural circulation type water tube boiler 11 and the feed water preheater 1
Since 4 is arranged, the total length becomes long and the size of the equipment cannot be avoided, and the restrictions on the installation place increase, and
With regard to installation, it was necessary to bring each device to the site and assemble it, which had the drawback of increasing the number of man-hours and increasing the cost.

【0009】本発明は、斯かる実情に鑑み、排ガス中に
含まれるNOxを効率よく除去し得、且つ全体として小
型化並びにユニット化を可能として設置場所の制約を小
さくし得、据え付け工数の削減並びにコストダウンを図
り得る自然循環式水管ボイラ設備を提供しようとするも
のである。
In view of the above situation, the present invention can efficiently remove NOx contained in exhaust gas, can be downsized and unitized as a whole, and can reduce restrictions on installation place, and reduce the number of installation steps. Also, the present invention aims to provide a natural circulation type water pipe boiler facility capable of reducing the cost.

【0010】[0010]

【課題を解決するための手段】本発明は、仕切板によっ
て下側排ガス流通路と上側排ガス流通路とに仕切られ、
排ガス供給ダクトに接続される排ガス供給口から導入さ
れる排ガスが、下側排ガス流通路を通り、折り返す形で
上側排ガス流通路を流れ、排ガス排出ダクトに接続され
る排ガス排出口から排出可能となるよう構成したケーシ
ングを備え、該ケーシングの下側排ガス流通路に高温脱
硝装置を設け、該高温脱硝装置の下流側に、上端が汽水
胴に接続され且つ下端が水胴に接続された多数の管を有
する自然循環式水管ボイラを、前記管の上部が前記上側
排ガス流通路内に位置し且つ前記管の下部が前記仕切板
を貫通して前記下側排ガス流通路内に位置するよう配設
し、前記下側排ガス流通路と上側排ガス流通路とを結ぶ
折り返し部分に中温脱硝装置を設け、前記上側排ガス流
通路における前記自然循環式水管ボイラの下流側に給水
予熱器を設け、前記高温脱硝装置の上流側における下側
排ガス流通路と前記給水予熱器の下流側における上側排
ガス流通路とを連通する連通部を前記ケーシング内に形
成し、前記連通部を閉塞し前記排ガス供給口から導入さ
れる排ガスを前記高温脱硝装置へ導く位置と、前記連通
部を開放し且つ高温脱硝装置の上流側における下側排ガ
ス流通路を閉塞して前記排ガス供給口から導入される排
ガスを直接前記排ガス排出口へ導く位置とに切換可能な
切換ダンパを、前記ケーシング内に設けたことを特徴と
するものである。
The present invention is divided into a lower exhaust gas passage and an upper exhaust gas passage by a partition plate,
Exhaust gas introduced from the exhaust gas supply port connected to the exhaust gas supply duct passes through the lower exhaust gas flow passage, flows through the upper exhaust gas flow passage in a folded manner, and can be discharged from the exhaust gas discharge port connected to the exhaust gas discharge duct. A plurality of pipes having a casing configured as described above, provided with a high temperature denitration device in a lower exhaust gas flow passage of the casing, and having an upper end connected to a brackish water cylinder and a lower end connected to a water cylinder on the downstream side of the high temperature denitration device. A natural circulation type water pipe boiler having an upper part of the pipe located in the upper exhaust gas flow passage and a lower part of the pipe penetrating the partition plate and located in the lower exhaust gas flow passage. , A middle temperature denitration device is provided at a folded portion connecting the lower exhaust gas flow passage and the upper exhaust gas flow passage, and a feed water preheater is provided in the upper exhaust gas flow passage on the downstream side of the natural circulation water tube boiler. A communication part that connects the lower exhaust gas flow passage on the upstream side of the high-temperature denitration device and the upper exhaust gas flow passage on the downstream side of the feed water preheater is formed in the casing, and the communication part is closed from the exhaust gas supply port. A position for guiding the introduced exhaust gas to the high-temperature denitration device and the communication part is opened and the lower exhaust gas flow passage on the upstream side of the high-temperature denitration device is closed to directly introduce the exhaust gas introduced from the exhaust gas supply port to the exhaust gas. A switching damper capable of switching to a position leading to the discharge port is provided in the casing.

【0011】[0011]

【作用】従って、切換ダンパを連通部を閉塞する位置に
切り換えておくと、排ガス供給ダクトを流れケーシング
の排ガス供給口から下側排ガス流通路へ供給された高温
の排ガスは、高温脱硝装置へ導かれ、該高温脱硝装置に
おいて窒素酸化物が除去された後、下側排ガス流通路に
おける自然循環式水管ボイラの管の間を流れ、前記窒素
酸化物が除去された高温の排ガスによって管内のボイラ
水が加熱され、所要温度に低下した排ガスが折り返し部
分における中温脱硝装置へ流入し、該中温脱硝装置にお
いて更に窒素酸化物が除去される。
Therefore, when the switching damper is switched to the position where the communication portion is closed, the high temperature exhaust gas supplied from the exhaust gas supply port of the casing to the lower exhaust gas flow passage is guided to the high temperature denitration device. After the nitrogen oxides are removed in the high-temperature denitration device, the water flows between the tubes of the natural circulation type water tube boiler in the lower exhaust gas flow passage, and the boiler water in the tubes is heated by the high-temperature exhaust gas from which the nitrogen oxides have been removed. Is heated and the exhaust gas whose temperature has dropped to the required temperature flows into the intermediate temperature denitration device in the folded portion, and nitrogen oxides are further removed in the intermediate temperature denitration device.

【0012】この後、前記窒素酸化物が除去された所要
温度の排ガスは、折り返す形で上側排ガス流通路へ導か
れ、該上側排ガス流通路における自然循環式水管ボイラ
の管の間を流れ、前記所要温度の排ガスによって管内の
ボイラ水が加熱され、温度が更に低下した排ガスが給水
予熱器へ導かれ、該給水予熱器内の水と熱交換を行った
後、排ガス排出口から排ガス排出ダクトを経て大気へ放
出される。
Thereafter, the exhaust gas at the required temperature from which the nitrogen oxides have been removed is guided to the upper exhaust gas flow passage in a folded manner and flows between the pipes of the natural circulation type water pipe boiler in the upper exhaust gas flow passage, The boiler water in the pipe is heated by the exhaust gas of the required temperature, the exhaust gas with a further lowered temperature is guided to the feed water preheater, and after exchanging heat with the water in the feed water preheater, the exhaust gas discharge duct is connected from the exhaust gas outlet. It is then released into the atmosphere.

【0013】前記自然循環式水管ボイラにおいては、汽
水胴と水胴との間でボイラ水の自然循環が行われ、生成
された蒸気が汽水胴から取り出される。
In the natural circulation water tube boiler, the boiler water is naturally circulated between the steam cylinder and the water cylinder, and the generated steam is taken out from the steam cylinder.

【0014】一方、運転の都合上、蒸気を必要としない
場合には、切換ダンパを連通部を開放し且つ高温脱硝装
置の上流側における下側排ガス流通路を閉塞する位置に
切り換えると、排ガス供給ダクトを流れケーシングの排
ガス供給口から下側排ガス流通路へ供給された高温の排
ガスは、前記高温脱硝装置から給水予熱器の間を通過せ
ずに、連通部から上側排ガス流通路を経て直接排ガス排
出口へ導かれ、排ガス排出ダクトへ流れて行く。
On the other hand, for the convenience of operation, when steam is not required, the switching damper is switched to a position where the communication portion is opened and the lower exhaust gas flow passage on the upstream side of the high temperature denitration device is closed. The high-temperature exhaust gas that has flowed through the duct from the exhaust gas supply port of the casing to the lower exhaust gas flow passage does not pass between the high-temperature denitration device and the feedwater preheater, but passes directly from the communication section through the upper exhaust gas flow passage to the exhaust gas. It is guided to the exhaust port and flows to the exhaust gas exhaust duct.

【0015】即ち、本発明においては、高温脱硝装置
と、自然循環式水管ボイラと、中温脱硝装置と、給水予
熱器とを直線的に配置するのではなく、ケーシング内に
効率よく収めることが可能となり、全長が長くならず設
備の大型化が避けられ、設置場所の制約が小さくなると
共に、据え付けに関しても各機器をユニットとして搬入
すればよい。
That is, in the present invention, the high temperature denitration device, the natural circulation type water tube boiler, the medium temperature denitration device, and the feed water preheater are not arranged linearly but can be efficiently housed in the casing. Therefore, the total length is not long, the size of the equipment is prevented from being increased, restrictions on the installation place are reduced, and each device may be carried in as a unit for installation.

【0016】[0016]

【実施例】以下、本発明の実施例を図面を参照しつつ説
明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0017】図1は本発明の一実施例であって、図中、
図2と同一の符号を付した部分は同一物を表わしてお
り、排ガス供給ダクト1aに接続される排ガス供給口1
7が下側部に形成され且つ排ガス排出ダクト1bに接続
される排ガス排出口18が上側部に形成されたケーシン
グ19内の所要位置に仕切板20を設けることにより、
前記ケーシング19内に下側排ガス流通路21と上側排
ガス流通路22とを形成し、前記排ガス供給ダクト1a
から排ガス供給口17を経て導入される排ガス5が、下
側排ガス流通路21を通り、折り返す形で上側排ガス流
通路22を流れ、排ガス排出口18から排ガス排出ダク
ト1bへ排出され得るよう構成する。
FIG. 1 shows an embodiment of the present invention.
The parts denoted by the same reference numerals as in FIG. 2 represent the same things, and the exhaust gas supply port 1 connected to the exhaust gas supply duct 1a
By providing the partition plate 20 at a predetermined position in the casing 19 in which the exhaust gas discharge port 18 connected to the exhaust gas discharge duct 1b is formed in the upper part,
A lower exhaust gas flow passage 21 and an upper exhaust gas flow passage 22 are formed in the casing 19, and the exhaust gas supply duct 1a is provided.
The exhaust gas 5 introduced from the exhaust gas supply port 17 through the exhaust gas supply port 17 flows through the lower exhaust gas flow passage 21 and the upper exhaust gas flow passage 22 in a folded manner, and can be discharged from the exhaust gas discharge port 18 to the exhaust gas discharge duct 1b. .

【0018】前記ケーシング19の下側排ガス流通路2
1に高温脱硝装置12を設け、該高温脱硝装置12の下
流側に、上端が汽水胴2に接続され且つ下端が水胴3に
接続された多数の管4を有する自然循環式水管ボイラ1
1を、前記管4の上部が前記上側排ガス流通路22内に
位置し且つ前記管4の下部が前記仕切板20を貫通して
前記下側排ガス流通路21内に位置するよう配設し、前
記下側排ガス流通路21と上側排ガス流通路22とを結
ぶ折り返し部分23に中温脱硝装置13を設け、前記上
側排ガス流通路22における前記自然循環式水管ボイラ
11の下流側に給水予熱器14を設ける。
The lower exhaust gas passage 2 of the casing 19
1 is provided with a high temperature denitration device 12, and on the downstream side of the high temperature denitration device 12, a natural circulation type water pipe boiler 1 having a large number of pipes 4 whose upper end is connected to a brackish water cylinder 2 and whose lower end is connected to a water cylinder 3.
1 is arranged such that the upper portion of the pipe 4 is located in the upper exhaust gas flow passage 22 and the lower portion of the pipe 4 penetrates the partition plate 20 and is located in the lower exhaust gas flow passage 21. A medium temperature denitration device 13 is provided at a folded portion 23 connecting the lower exhaust gas flow passage 21 and the upper exhaust gas flow passage 22, and a feed water preheater 14 is provided in the upper exhaust gas flow passage 22 on the downstream side of the natural circulation water pipe boiler 11. Set up.

【0019】前記高温脱硝装置12の上流側における下
側排ガス流通路21と前記給水予熱器14の下流側にお
ける上側排ガス流通路22とを連通する連通部24を前
記ケーシング19内に形成し、前記連通部24を閉塞し
前記排ガス供給口17から導入される排ガス5を前記高
温脱硝装置12へ導く位置P1と、前記連通部24を開
放し且つ高温脱硝装置12の上流側における下側排ガス
流通路21を閉塞して前記排ガス供給口17から導入さ
れる排ガス5を直接前記排ガス排出口18へ導く位置P
2とに切換可能な切換ダンパ16を、前記ケーシング1
9内に設ける。
A communication portion 24 is formed in the casing 19 for connecting the lower exhaust gas passage 21 on the upstream side of the high temperature denitration device 12 and the upper exhaust gas passage 22 on the downstream side of the feedwater preheater 14 to each other. A position P1 that closes the communication part 24 and guides the exhaust gas 5 introduced from the exhaust gas supply port 17 to the high-temperature denitration device 12, and a lower exhaust gas passageway that opens the communication part 24 and is upstream of the high-temperature denitration device 12. A position P which closes 21 and guides the exhaust gas 5 introduced from the exhaust gas supply port 17 directly to the exhaust gas discharge port 18.
The switching damper 16 that can be switched to
Provided within 9.

【0020】次に、上記実施例の作動を説明する。Next, the operation of the above embodiment will be described.

【0021】蒸気を必要とする場合、切換ダンパ16を
位置P1に切り換えておくと、排ガス供給ダクト1aを
流れケーシング19の排ガス供給口17から下側排ガス
流通路21へ供給された高温の排ガス5は、高温脱硝装
置12へ導かれ、該高温脱硝装置12において窒素酸化
物が除去された後、下側排ガス流通路21における自然
循環式水管ボイラ11の管4の間を流れ、前記窒素酸化
物が除去された高温の排ガス5によって管4内のボイラ
水が加熱され、所要温度に低下した排ガス5が折り返し
部分23における中温脱硝装置13へ流入し、該中温脱
硝装置13において更に窒素酸化物が除去される。
When steam is required, if the switching damper 16 is switched to the position P1, the high temperature exhaust gas 5 supplied to the lower exhaust gas flow passage 21 from the exhaust gas supply port 17 of the casing 19 through the exhaust gas supply duct 1a. Is introduced into the high-temperature denitration device 12 and, after the nitrogen oxides are removed in the high-temperature denitration device 12, flows between the pipes 4 of the natural circulation type water pipe boiler 11 in the lower exhaust gas flow passage 21 to obtain the nitrogen oxides. The boiler water in the pipe 4 is heated by the high-temperature exhaust gas 5 from which the exhaust gas 5 has been removed, and the exhaust gas 5 that has decreased to the required temperature flows into the intermediate-temperature denitration device 13 in the turn-back portion 23, and further nitrogen oxides are generated in the intermediate-temperature denitration device 13. To be removed.

【0022】この後、前記窒素酸化物が除去された所要
温度の排ガス5は、折り返す形で上側排ガス流通路22
へ導かれ、該上側排ガス流通路22における自然循環式
水管ボイラ11の管4の間を流れ、前記所要温度の排ガ
ス5によって管4内のボイラ水が加熱され、温度が更に
低下した排ガス5が給水予熱器14へ導かれ、該給水予
熱器14内の水と熱交換を行った後、排ガス排出口18
から排ガス排出ダクト1bを経て大気へ放出される。
After that, the exhaust gas 5 of the required temperature from which the nitrogen oxides have been removed is folded back to form the upper exhaust gas passage 22.
Is introduced into the upper exhaust gas flow passage 22 and flows between the tubes 4 of the natural circulation water tube boiler 11 in the upper exhaust gas flow passage 22, the boiler water in the tube 4 is heated by the exhaust gas 5 at the required temperature, and the exhaust gas 5 having a further lowered temperature is generated. After being guided to the water supply preheater 14 and exchanging heat with the water in the water supply preheater 14, the exhaust gas discharge port 18
Is discharged to the atmosphere through the exhaust gas discharge duct 1b.

【0023】前記自然循環式水管ボイラ11において
は、下側排ガス流通路21では、排ガス流れ方向上流側
即ち図中左側に位置する管4の温度が、排ガス流れ方向
下流側即ち図中右側に位置する管4の温度より相対的に
高くなる一方、上側排ガス流通路22では、排ガス流れ
方向上流側即ち図中右側に位置する管4の温度が、排ガ
ス流れ方向下流側即ち図中左側に位置する管4の温度よ
り相対的に高くなるが、トータル的には、図中左側に位
置する管4の温度が、図中右側に位置する管4の温度よ
り高くなり、図中左側に位置する管4内のボイラ水が上
昇すると共に、図中右側に位置する管4内のボイラ水が
下降する形となるため、汽水胴2と水胴3との間でボイ
ラ水の自然循環が行われ、生成された蒸気が汽水胴2か
ら取り出される。
In the natural circulation type water pipe boiler 11, in the lower exhaust gas flow passage 21, the temperature of the pipe 4 located on the upstream side in the exhaust gas flow direction, that is, on the left side in the drawing is located on the downstream side in the exhaust gas flow direction, that is, on the right side in the drawing. In the upper exhaust gas flow passage 22, the temperature of the pipe 4 located on the upstream side in the exhaust gas flow direction, that is, on the right side in the figure is located on the downstream side in the exhaust gas flow direction, that is, on the left side in the figure, while being relatively higher than the temperature of the pipe 4. Although the temperature of the pipe 4 is relatively higher than the temperature of the pipe 4, the temperature of the pipe 4 located on the left side of the figure is higher than the temperature of the pipe 4 located on the right side of the figure, and the temperature of the pipe 4 located on the left side of the figure is total. As the boiler water in 4 rises and the boiler water in the pipe 4 located on the right side in the figure descends, natural circulation of boiler water is performed between the brackish water cylinder 2 and the water cylinder 3. The generated steam is taken out from the steam cylinder 2.

【0024】一方、運転の都合上、蒸気を必要としない
場合には、切換ダンパ16を位置P2に切り換えると、
連通部24が開放され且つ高温脱硝装置12の上流側に
おける下側排ガス流通路21が閉塞され、排ガス供給ダ
クト1aを流れケーシング19の排ガス供給口17から
下側排ガス流通路21へ供給された高温の排ガス5は、
前記高温脱硝装置12から給水予熱器14の間を通過せ
ずに、連通部24から上側排ガス流通路22を経て直接
排ガス排出口18へ導かれ、排ガス排出ダクト1bへ流
れて行く。
On the other hand, for the convenience of operation, when the steam is not required, the switching damper 16 is switched to the position P2.
The communication part 24 is opened, the lower exhaust gas flow passage 21 on the upstream side of the high temperature denitration device 12 is closed, and the high temperature supplied through the exhaust gas supply duct 1a from the exhaust gas supply port 17 of the casing 19 to the lower exhaust gas flow passage 21. Exhaust gas 5 of
Without passing between the high temperature denitration device 12 and the feed water preheater 14, it is directly guided from the communication part 24 to the exhaust gas discharge port 18 through the upper exhaust gas flow passage 22 and flows to the exhaust gas discharge duct 1b.

【0025】即ち、本実施例においては、高温脱硝装置
12と、自然循環式水管ボイラ11と、中温脱硝装置1
3と、給水予熱器14とを直線的に配置するのではな
く、ケーシング19内に効率よく収めることが可能とな
り、全長が長くならず設備の大型化が避けられ、設置場
所の制約が小さくなると共に、据え付けに関しても各機
器をユニットとして搬入すればよい。
That is, in this embodiment, the high temperature denitration device 12, the natural circulation type water tube boiler 11 and the medium temperature denitration device 1 are used.
3 and the feedwater preheater 14 can be efficiently housed in the casing 19 instead of being arranged linearly, the total length is not long and the equipment is not upsized, and the restrictions on the installation location are reduced. At the same time, for installation, each device may be carried in as a unit.

【0026】こうして、排ガス5中に含まれるNOxを
効率よく除去し得、且つ全体として小型化並びにユニッ
ト化を可能として設置場所の制約を小さくし得、据え付
け工数の削減並びにコストダウンを図ることができる。
In this way, NOx contained in the exhaust gas 5 can be efficiently removed, the size and unit of the exhaust gas 5 can be reduced as a whole, the restrictions on the installation place can be reduced, and the number of installation steps and the cost can be reduced. it can.

【0027】尚、本発明の自然循環式水管ボイラ設備
は、上述の実施例にのみ限定されるものではなく、本発
明の要旨を逸脱しない範囲内において種々変更を加え得
ることは勿論である。
It should be noted that the natural circulation type water pipe boiler equipment of the present invention is not limited to the above-mentioned embodiment, and various modifications can be made without departing from the scope of the present invention.

【0028】[0028]

【発明の効果】以上、説明したように本発明の自然循環
式水管ボイラ設備によれば、排ガス中に含まれるNOx
を効率よく除去し得、且つ全体として小型化並びにユニ
ット化が可能となり設置場所の制約を小さくし得、据え
付け工数の削減並びにコストダウンを図り得るという優
れた効果を奏し得る。
As described above, according to the natural circulation type water pipe boiler equipment of the present invention, NOx contained in the exhaust gas is reduced.
Can be efficiently removed, and the size and unit can be reduced as a whole, the restrictions on the installation place can be reduced, and the excellent effects that the number of installation steps and the cost can be reduced can be achieved.

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

【図1】本発明の一実施例の側断面図である。FIG. 1 is a side sectional view of an embodiment of the present invention.

【図2】従来例の側断面図である。FIG. 2 is a side sectional view of a conventional example.

【符号の説明】[Explanation of symbols]

1a 排ガス供給ダクト 1b 排ガス排出ダクト 2 汽水胴 3 水胴 4 管 5 排ガス 11 自然循環式水管ボイラ 12 高温脱硝装置 13 中温脱硝装置 14 給水予熱器 16 切換ダンパ 17 排ガス供給口 18 排ガス排出口 19 ケーシング 20 仕切板 21 下側排ガス流通路 22 上側排ガス流通路 23 折り返し部分 24 連通部 P1 位置 P2 位置 1a Exhaust gas supply duct 1b Exhaust gas discharge duct 2 Brackish water cylinder 3 Water cylinder 4 Tube 5 Exhaust gas 11 Natural circulation type water tube boiler 12 High temperature denitration device 13 Medium temperature denitration device 14 Water supply preheater 16 Switching damper 17 Exhaust gas supply port 18 Exhaust gas discharge port 19 Casing 20 Partition plate 21 Lower exhaust gas flow passage 22 Upper exhaust gas flow passage 23 Folded portion 24 Communication portion P1 position P2 position

フロントページの続き (72)発明者 本田 寿 広島県呉市昭和町4番41号 石川島汎用ボ イラ株式会社本社内Continuation of front page (72) Inventor Hisashi Honda, 4-41, Showa-cho, Kure-shi, Hiroshima Ishikawajima general-purpose boiler Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 仕切板によって下側排ガス流通路と上側
排ガス流通路とに仕切られ、排ガス供給ダクトに接続さ
れる排ガス供給口から導入される排ガスが、下側排ガス
流通路を通り、折り返す形で上側排ガス流通路を流れ、
排ガス排出ダクトに接続される排ガス排出口から排出可
能となるよう構成したケーシングを備え、該ケーシング
の下側排ガス流通路に高温脱硝装置を設け、該高温脱硝
装置の下流側に、上端が汽水胴に接続され且つ下端が水
胴に接続された多数の管を有する自然循環式水管ボイラ
を、前記管の上部が前記上側排ガス流通路内に位置し且
つ前記管の下部が前記仕切板を貫通して前記下側排ガス
流通路内に位置するよう配設し、前記下側排ガス流通路
と上側排ガス流通路とを結ぶ折り返し部分に中温脱硝装
置を設け、前記上側排ガス流通路における前記自然循環
式水管ボイラの下流側に給水予熱器を設け、前記高温脱
硝装置の上流側における下側排ガス流通路と前記給水予
熱器の下流側における上側排ガス流通路とを連通する連
通部を前記ケーシング内に形成し、前記連通部を閉塞し
前記排ガス供給口から導入される排ガスを前記高温脱硝
装置へ導く位置と、前記連通部を開放し且つ高温脱硝装
置の上流側における下側排ガス流通路を閉塞して前記排
ガス供給口から導入される排ガスを直接前記排ガス排出
口へ導く位置とに切換可能な切換ダンパを、前記ケーシ
ング内に設けたことを特徴とする自然循環式水管ボイラ
設備。
1. An exhaust gas, which is divided into a lower exhaust gas flow passage and an upper exhaust gas flow passage by a partition plate and is introduced from an exhaust gas supply port connected to an exhaust gas supply duct, passes through the lower exhaust gas flow passage and is folded back. Flows through the upper exhaust gas flow passage at
A casing configured to be discharged from an exhaust gas outlet connected to an exhaust gas discharge duct is provided, a high temperature denitration device is provided in a lower side exhaust gas flow passage of the casing, and a steam turbine is provided with an upper end downstream of the high temperature denitration device. A natural circulation type water pipe boiler having a number of pipes connected to each other and having a lower end connected to a water cylinder, wherein an upper portion of the pipe is located in the upper exhaust gas flow passage and a lower portion of the pipe penetrates the partition plate. Located in the lower exhaust gas flow passage, a middle temperature denitration device is provided at the folded portion connecting the lower exhaust gas flow passage and the upper exhaust gas flow passage, and the natural circulation type water pipe in the upper exhaust gas flow passage A feed water preheater is provided on the downstream side of the boiler, and a communication portion that connects the lower exhaust gas flow passage on the upstream side of the high-temperature denitration device and the upper exhaust gas flow passage on the downstream side of the feed water preheater is provided with the casing. And a position for guiding the exhaust gas introduced from the exhaust gas supply port to the high-temperature denitration device, which is formed in the inside of the exhaust gas, and the lower exhaust gas flow passage on the upstream side of the high-temperature denitration device that opens the communication part. A natural circulation type water pipe boiler facility, characterized in that a switching damper that is capable of switching to a position where the exhaust gas introduced from the exhaust gas supply port is directly guided to the exhaust gas discharge port is provided inside the casing.
JP13316494A 1994-06-15 1994-06-15 Natural circulation type water tube boiler facility Pending JPH085002A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13316494A JPH085002A (en) 1994-06-15 1994-06-15 Natural circulation type water tube boiler facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13316494A JPH085002A (en) 1994-06-15 1994-06-15 Natural circulation type water tube boiler facility

Publications (1)

Publication Number Publication Date
JPH085002A true JPH085002A (en) 1996-01-12

Family

ID=15098189

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13316494A Pending JPH085002A (en) 1994-06-15 1994-06-15 Natural circulation type water tube boiler facility

Country Status (1)

Country Link
JP (1) JPH085002A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002181301A (en) * 2000-12-13 2002-06-26 Samson Co Ltd Exhaust gas boiler preventing overheat
JP2003065530A (en) * 2001-08-22 2003-03-05 Babcock Hitachi Kk Exhaust gas duct structure
JP2008096087A (en) * 2006-10-16 2008-04-24 Ebara Corp Steam boiler device
JP2011069574A (en) * 2009-09-28 2011-04-07 Miura Co Ltd Waste heat boiler and waste heat recovery system
JP2014016124A (en) * 2012-07-10 2014-01-30 Miura Co Ltd Boiler apparatus and cogeneration system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002181301A (en) * 2000-12-13 2002-06-26 Samson Co Ltd Exhaust gas boiler preventing overheat
JP2003065530A (en) * 2001-08-22 2003-03-05 Babcock Hitachi Kk Exhaust gas duct structure
JP4709441B2 (en) * 2001-08-22 2011-06-22 バブコック日立株式会社 Exhaust gas duct structure
JP2008096087A (en) * 2006-10-16 2008-04-24 Ebara Corp Steam boiler device
JP2011069574A (en) * 2009-09-28 2011-04-07 Miura Co Ltd Waste heat boiler and waste heat recovery system
JP2014016124A (en) * 2012-07-10 2014-01-30 Miura Co Ltd Boiler apparatus and cogeneration system

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