JPH03114515U - - Google Patents

Info

Publication number
JPH03114515U
JPH03114515U JP1990023640U JP2364090U JPH03114515U JP H03114515 U JPH03114515 U JP H03114515U JP 1990023640 U JP1990023640 U JP 1990023640U JP 2364090 U JP2364090 U JP 2364090U JP H03114515 U JPH03114515 U JP H03114515U
Authority
JP
Japan
Prior art keywords
exhaust gas
gas purification
plant
purification device
denitrification
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
JP1990023640U
Other languages
Japanese (ja)
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 filed Critical
Priority to JP1990023640U priority Critical patent/JPH03114515U/ja
Publication of JPH03114515U publication Critical patent/JPH03114515U/ja
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Landscapes

  • Exhaust Gas After Treatment (AREA)

Description

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

第1図は本考案の一実施例を示すコジエネプラ
ント用排ガス浄化装置の概略図、第2図はCO除
去触媒の温度特性を示す線図、第3図はCO除去
触媒のNH酸化の温度特性を示す線図、第4図
はNH注入モル比と脱硝率の関係を示す線図、
第5図は排ガス温度と脱硝率との関係を示す線図
、第6図は全負荷時の排熱回収ボイラ内の温度分
布を示す線図、第7図は負荷変化時の排熱回収ボ
イラ内の温度分布を示す線図、第8図は従来のコ
ジエネプラント用排ガス浄化装置概略図である。 1……排熱回収ボイラ、2……排ガス流、3…
…過熱器、4a,4b……蒸発器、5……アンモ
ニア注入装置、6……脱硝装置、7……節炭器、
8……煙突、9……ガスタービン、10……蒸気
タービン、11……CO除去装置。
Fig. 1 is a schematic diagram of an exhaust gas purification device for a CODIENE plant showing an embodiment of the present invention, Fig. 2 is a diagram showing the temperature characteristics of the CO removal catalyst, and Fig. 3 is a diagram showing the temperature characteristics of the CO removal catalyst for NH3 oxidation. A diagram showing the temperature characteristics; Figure 4 is a diagram showing the relationship between the NH3 injection molar ratio and the denitrification rate;
Figure 5 is a diagram showing the relationship between exhaust gas temperature and denitrification rate, Figure 6 is a diagram showing the temperature distribution inside the exhaust heat recovery boiler at full load, and Figure 7 is a diagram showing the exhaust heat recovery boiler when the load changes. FIG. 8 is a schematic diagram of a conventional exhaust gas purification device for a COGENE plant. 1...Exhaust heat recovery boiler, 2...Exhaust gas flow, 3...
...Superheater, 4a, 4b... Evaporator, 5... Ammonia injection device, 6... Denitrification device, 7... Carbon saver,
8...Chimney, 9...Gas turbine, 10...Steam turbine, 11...CO removal device.

Claims (1)

【実用新案登録請求の範囲】 1 ガスタービンの排ガスから熱を回収する排熱
回収ボイラの内部に、過熱器、蒸発器、節炭器、
脱硝装置およびCO除去装置が収納され、かつ前
記蒸発器が2分割されて、その中間部に前記脱硝
装置が配置されたコジエネプラント用排ガス浄化
装置において、 前記2分割された蒸発器の中間部で、かつ排ガ
スの流れに沿つて前記脱硝装置の後流側に、前記
CO除去装置を配置したことを特徴とするコジエ
ネプラント用排ガス浄化装置。 2 請求項1記載のコジエネプラント用排ガス浄
化装置において、 前記脱硝装置の出口NOx濃度を15%Oz換
算で15ppmvd以下に、出口NH濃度を1
5%O換算で25ppmvd以下にそれぞれ設
定したことを特徴とするコジエネプラント用排ガ
ス浄化装置。
[Scope of Claim for Utility Model Registration] 1. A superheater, evaporator, energy saver,
In an exhaust gas purification device for a COGENE plant, in which a denitrification device and a CO removal device are housed, the evaporator is divided into two, and the denitration device is arranged in the middle portion, the middle portion of the two divided evaporators. An exhaust gas purification device for a cogeneration plant, characterized in that the CO removal device is disposed downstream of the denitrification device along the flow of exhaust gas. 2. The exhaust gas purification device for a CODIE plant according to claim 1, wherein the NOx concentration at the outlet of the denitrification device is set to 15 ppmvd or less in terms of 15% Oz, and the NH3 concentration at the outlet is set to 1.
An exhaust gas purification device for a COZIENE plant, characterized in that each is set to 25 ppmvd or less in terms of 5% O2 .
JP1990023640U 1990-03-08 1990-03-08 Pending JPH03114515U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1990023640U JPH03114515U (en) 1990-03-08 1990-03-08

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1990023640U JPH03114515U (en) 1990-03-08 1990-03-08

Publications (1)

Publication Number Publication Date
JPH03114515U true JPH03114515U (en) 1991-11-25

Family

ID=31526621

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1990023640U Pending JPH03114515U (en) 1990-03-08 1990-03-08

Country Status (1)

Country Link
JP (1) JPH03114515U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011522987A (en) * 2008-05-15 2011-08-04 ジョンソン、マッセイ、インコーポレイテッド Emission reduction device used with heat recovery steam generator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011522987A (en) * 2008-05-15 2011-08-04 ジョンソン、マッセイ、インコーポレイテッド Emission reduction device used with heat recovery steam generator

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