JPH07265660A - Apparatus for vaporizing aqueous ammonia solution - Google Patents

Apparatus for vaporizing aqueous ammonia solution

Info

Publication number
JPH07265660A
JPH07265660A JP6060431A JP6043194A JPH07265660A JP H07265660 A JPH07265660 A JP H07265660A JP 6060431 A JP6060431 A JP 6060431A JP 6043194 A JP6043194 A JP 6043194A JP H07265660 A JPH07265660 A JP H07265660A
Authority
JP
Japan
Prior art keywords
ammonia
tube
ammonia water
waste gas
exhaust gas
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
JP6060431A
Other languages
Japanese (ja)
Other versions
JP3358862B2 (en
Inventor
Osamu Naito
内藤  治
Toshihiko Imamoto
敏彦 今本
Atsushi Morii
淳 守井
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP06043194A priority Critical patent/JP3358862B2/en
Publication of JPH07265660A publication Critical patent/JPH07265660A/en
Application granted granted Critical
Publication of JP3358862B2 publication Critical patent/JP3358862B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To unnecessitate a waste gas fan and an ammonia soln. vaporizer and to simplify an apparatus by installing a tube for vaporizing an ammonia soln. in a waste heat recovering boiler on the upper stream side of a denitration reactor. CONSTITUTION:Many heat exchangers 11 are arranged in a waste heat recovering boiler 12 using waste gas from a gas turbine, etc., a denitration reactor 1 contg. a catalyst is interposed between the heat exchangers 11 and NOx in waste gas is reduced to harmless nitrogen and water. At this time, a meandering tube 4 for vaporizing an ammonia soln. is disposed on the upper stream side of most of the heat exchangers 11 and the reactor 1, and many ammonia injecting nozzles 5 are fixed in the rear end part of the tube 4. An ammonia soln. allowed to flow in the tube 4 is gradually heated by heat exchange with waste gas on the outside of the tube 4, the concn. rises and the ammonia soln. is converted into gaseous ammonia and steam by vaporization. The gaseous ammonia and steam spout out of the nozzles 5 and are introduced into the reactor 1 after mixing with the waste gas.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は排ガスの脱硝用のアンモ
ニア水気化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ammonia water vaporizer for denitration of exhaust gas.

【0002】[0002]

【従来の技術】従来の排ガス脱硝用アンモニア水気化装
置を図5によって説明する。アンモニア水を気化させる
ために、別置きアンモニア水気化器6を設置し、アンモ
ニア水のアトマイズ用媒体とアンモニア水とを混合して
該アンモニア水気化器6内にアトマイズ用ノズル8より
噴霧した後、脱硝反応器1に導かれる排ガスから分岐し
た一部の排ガス中で気化させてアンモニア注入ノズル5
から注入しているため、排ガスファン7、別置きアンモ
ニア水気化器6等が必要ある。なお、図5中、9はアン
モニア水タンク、10はアンモニア水ポンプを示す。
2. Description of the Related Art A conventional ammonia water vaporizer for exhaust gas denitration will be described with reference to FIG. In order to vaporize the ammonia water, a separately installed ammonia water vaporizer 6 is installed, and a medium for atomizing the ammonia water and the ammonia water are mixed and sprayed from the atomizing nozzle 8 into the ammonia water vaporizer 6; Ammonia injection nozzle 5 is vaporized by vaporizing in a part of the exhaust gas branched from the exhaust gas guided to the denitration reactor 1.
Since it is injected from above, an exhaust gas fan 7, a separate ammonia water vaporizer 6 and the like are required. In addition, in FIG. 5, 9 shows an ammonia water tank, and 10 shows an ammonia water pump.

【0003】[0003]

【発明が解決しようとする課題】上述したように、従来
法においては、アンモニア水を気化させるためには、気
化しやすいようにまずアトマイズ用媒体と混合して小さ
いアンモニア水滴として噴霧し、その噴霧されたアンモ
ニア水滴に熱を加えて気化させている。その場合、熱源
として、排ガス系より排ガスを抽出する排ガスファンの
設置並びにアトマイズ用ノズルを備えた別置きアンモニ
ア水気化器の設置が必要となり、系統が複雑であるとい
う問題がある。本発明は上記技術水準に鑑み、従来技術
の問題点を解決できる脱硝用アンモニア水の気化装置を
提供しようとするものである。
As described above, in the conventional method, in order to vaporize the ammonia water, it is first mixed with the atomizing medium so as to be easily vaporized and then sprayed as small ammonia water droplets. The ammonia droplets thus formed are heated to be vaporized. In that case, as a heat source, it is necessary to install an exhaust gas fan for extracting exhaust gas from an exhaust gas system and a separate ammonia water vaporizer equipped with an atomizing nozzle, which causes a problem that the system is complicated. In view of the above technical level, the present invention aims to provide a denitration ammonia water vaporizer capable of solving the problems of the prior art.

【0004】[0004]

【課題を解決するための手段】本発明は脱硝反応器の上
流側に位置する排熱回収ボイラ内部又は排ガスダクト内
部又はボイラ後部伝熱部煙道内にアンモニア水気化用チ
ューブを設置してなることを特徴とする排ガス脱硝装置
用アンモニア水気化装置である。
According to the present invention, an ammonia water vaporization tube is installed inside the exhaust heat recovery boiler located upstream of the denitration reactor, inside the exhaust gas duct, or inside the flue of the heat transfer section at the rear of the boiler. Is an ammonia water vaporizer for exhaust gas denitration equipment.

【0005】[0005]

【作用】本発明の作用を図4によって説明する。図4に
示すようにアンモニア水気化用チューブ4内を流れるア
ンモニア水は該チューブ4の外側を流れる排ガスと熱交
換して、徐々に加熱され、濃度上昇して気化してアンモ
ニアガスと水蒸気となり、アンモニア注入ノズル5より
噴出し排ガスと混合し脱硝反応器1(図示省略)に導か
れる。
The operation of the present invention will be described with reference to FIG. As shown in FIG. 4, the ammonia water flowing in the ammonia water vaporizing tube 4 exchanges heat with the exhaust gas flowing outside the tube 4, is gradually heated, and the concentration is increased to vaporize into ammonia gas and water vapor, It is ejected from the ammonia injection nozzle 5 and mixed with the exhaust gas to be introduced into the denitration reactor 1 (not shown).

【0006】[0006]

【実施例】以下、本発明の具体例をあげ、本発明の効果
を明らかにする。 (実施例1)本発明の第1実施例を図1によって説明す
る。この実施例はガスタービン、ディ−ゼルエンジン等
(図示省略)の排ガスを使用した排熱回収ボイラ12に
適用したものであって、排熱回収ボイラ12内には多数
の熱交換器(伝熱管)11が配置され、この間に触媒を
用いた脱硝反応器1が設けられていて、排ガス中の窒素
酸化物をアンモニアガスを注入することによって、無害
な窒素と水に還元する態様のものである。前記熱交換器
11及び脱硝反応器1の上流に、蛇行したアンモニア水
気化用チューブ4を備え最終端部に多数のアンモニア注
入ノズル5を設けてある。この気化用チューブ4へはア
ンモニア水(又は、尿素水)を常温にて貯蔵したアンモ
ニア水タンク9より、アンモニア水ポンプ10で昇圧
し、流量を調整弁13にて調整しつつ、導入管14を介
して導入する。アンモニア水は常温のアンモニア水タン
ク9から、アンモニア水ポンプ10により昇圧され又、
流量調整弁13にて流量を調整しつつ排熱回収ボイラ1
2内に設置したアンモニア水気化用チューブ4へ流れ、
気化した後アンモニア注入ノズル5を通じて注入され
る。
EXAMPLES The effects of the present invention will be clarified below with reference to specific examples of the present invention. (Embodiment 1) A first embodiment of the present invention will be described with reference to FIG. This embodiment is applied to an exhaust heat recovery boiler 12 using exhaust gas from a gas turbine, a diesel engine or the like (not shown), and a large number of heat exchangers (heat transfer tubes) are provided in the exhaust heat recovery boiler 12. ) 11 are arranged, and a denitration reactor 1 using a catalyst is provided between them, and nitrogen oxide in exhaust gas is injected into the ammonia gas to reduce harmless nitrogen and water. . A meandering ammonia water vaporization tube 4 is provided upstream of the heat exchanger 11 and the denitration reactor 1, and a large number of ammonia injection nozzles 5 are provided at the final end. To the vaporizing tube 4, the ammonia water tank 9 that stores ammonia water (or urea water) at room temperature raises the pressure with the ammonia water pump 10 and adjusts the flow rate with the adjusting valve 13, while introducing the introducing pipe 14 into the vaporizing tube 4. Introduce through. Ammonia water is pressurized from the ammonia water tank 9 at room temperature by the ammonia water pump 10, and
Exhaust heat recovery boiler 1 while adjusting the flow rate with the flow rate adjusting valve 13.
Flow to the ammonia water vaporization tube 4 installed in 2
After vaporization, it is injected through the ammonia injection nozzle 5.

【0007】(実施例2)本発明の第2実施例を図2
(a),(b)によって説明する。この実施例はボイラ
の排ガスダクト2に設けたもの(図2(a))やガスタ
ービンの排ガスダクト2内に設けた(図2(b))もの
であって、排ガスダクト2の系統には触媒を用いた脱硝
反応器1が設けられていて、排ガス中の窒素酸化物をア
ンモニアガスを注入することによって無害な窒素と水に
還元する態様のものである。前記、脱硝反応器1の上流
に蛇行したアンモニア水気化用チューブ4を備え最終端
部に排ガスダクト内全面にアンモニアガスを噴出する多
数のアンモニア注入ノズル5を設けたものである。な
お、アンモニア水の導入系統については前記実施例1と
同じであるので説明は省略する。
(Second Embodiment) FIG. 2 shows a second embodiment of the present invention.
This will be described with reference to (a) and (b). This embodiment is provided in the exhaust gas duct 2 of the boiler (Fig. 2 (a)) or in the exhaust gas duct 2 of the gas turbine (Fig. 2 (b)). A denitration reactor 1 using a catalyst is provided, and nitrogen oxide in exhaust gas is reduced to harmless nitrogen and water by injecting ammonia gas. The meandering ammonia water vaporization tube 4 is provided upstream of the denitration reactor 1, and a large number of ammonia injection nozzles 5 for ejecting ammonia gas are provided at the final end of the exhaust gas duct. Note that the introduction system of the ammonia water is the same as that of the first embodiment, and therefore the description thereof is omitted.

【0008】(実施例3)次に本発明の第3実施例を図
3によって説明する。この実施例はボイラの後部煙道3
内にアンモニア水気化用チューブ4を設置したものであ
る。ボイラの後部煙道3内には伝熱管11が多数備えら
れているので、アンモニア水気化用チューブ4は伝熱管
11の中間部に設けたものであって、これに接続する排
ガスダクト2には脱硝反応器1が備えられている。な
お、アンモニア水の導入系統については前記実施例1と
同じであるので説明は省略する。
(Embodiment 3) Next, a third embodiment of the present invention will be described with reference to FIG. In this example, the rear flue 3 of the boiler is used.
A tube 4 for vaporizing ammonia water is installed inside. Since a large number of heat transfer tubes 11 are provided in the rear flue 3 of the boiler, the ammonia water vaporization tube 4 is provided in the middle of the heat transfer tube 11, and the exhaust gas duct 2 connected to the tube 4 is provided. A denitration reactor 1 is provided. Note that the introduction system of the ammonia water is the same as that of the first embodiment, and therefore the description thereof is omitted.

【0009】[0009]

【発明の効果】本発明によれば、アンモニア水気化用チ
ューブは脱硝反応器に導かれる排ガスが流れる排熱回収
ボイラ内、もしくは排ガスダクト内もしくはボイラ後部
伝熱部煙道内に容易に設置可能であり、系統は単純とな
り、排ガスファンや別置きアンモニア水気化器が不要と
なり、従来法におけるような装置の複雑性が改善され
る。
According to the present invention, the ammonia water vaporization tube can be easily installed in the exhaust heat recovery boiler in which the exhaust gas guided to the denitration reactor flows, or in the exhaust gas duct or in the heat transfer section flue at the rear of the boiler. Yes, the system is simple, no exhaust gas fan or separate ammonia water vaporizer is required, and the complexity of the device as in the conventional method is improved.

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

【図1】本発明の排熱回収ボイラへの適用例の説明図。FIG. 1 is an explanatory diagram of an application example of the present invention to an exhaust heat recovery boiler.

【図2】本発明のガスダクトへの適用例の説明図。FIG. 2 is an explanatory diagram of an application example of the present invention to a gas duct.

【図3】本発明のボイラへの適用例の説明図。FIG. 3 is an explanatory diagram of an application example of the present invention to a boiler.

【図4】本発明のアンモニア水気化装置の作用の説明
図。
FIG. 4 is an explanatory view of the action of the ammonia water vaporizer of the present invention.

【図5】従来のアンモニア水気化装置の一態様の説明
図。
FIG. 5 is an explanatory view of one mode of a conventional ammonia water vaporizer.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 脱硝反応器の上流側に位置する排熱回収
ボイラ内部又は排ガスダクト内部又はボイラ後部伝熱部
煙道内にアンモニア水気化用チューブを設置してなるこ
とを特徴とする排ガス脱硝装置用アンモニア水気化装
置。
1. An exhaust gas denitration apparatus comprising an ammonia water vaporization tube installed inside an exhaust heat recovery boiler located upstream of a denitration reactor, inside an exhaust gas duct, or inside a flue of a heat transfer section at a rear portion of the boiler. Ammonia water vaporizer.
JP06043194A 1994-03-30 1994-03-30 Ammonia water vaporizer Expired - Lifetime JP3358862B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06043194A JP3358862B2 (en) 1994-03-30 1994-03-30 Ammonia water vaporizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06043194A JP3358862B2 (en) 1994-03-30 1994-03-30 Ammonia water vaporizer

Publications (2)

Publication Number Publication Date
JPH07265660A true JPH07265660A (en) 1995-10-17
JP3358862B2 JP3358862B2 (en) 2002-12-24

Family

ID=13142056

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06043194A Expired - Lifetime JP3358862B2 (en) 1994-03-30 1994-03-30 Ammonia water vaporizer

Country Status (1)

Country Link
JP (1) JP3358862B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007307477A (en) * 2006-05-18 2007-11-29 Babcock Hitachi Kk Ammonia injection device and method for exhaust heat recovery boiler
KR100884657B1 (en) * 2007-06-20 2009-02-23 주식회사 파나시아 Exhaust Gas of High Temperature Denitrifing System and Denitrifing Method using the System

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007307477A (en) * 2006-05-18 2007-11-29 Babcock Hitachi Kk Ammonia injection device and method for exhaust heat recovery boiler
KR100884657B1 (en) * 2007-06-20 2009-02-23 주식회사 파나시아 Exhaust Gas of High Temperature Denitrifing System and Denitrifing Method using the System

Also Published As

Publication number Publication date
JP3358862B2 (en) 2002-12-24

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