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AU2002228791A1 - Selective catalytic reduction of no, enabled by side stream urea decomposition - Google Patents

Selective catalytic reduction of no, enabled by side stream urea decomposition

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Publication number
AU2002228791A1
AU2002228791A1AU2002228791AAU2879102AAU2002228791A1AU 2002228791 A1AU2002228791 A1AU 2002228791A1AU 2002228791 AAU2002228791 AAU 2002228791AAU 2879102 AAU2879102 AAU 2879102AAU 2002228791 A1AU2002228791 A1AU 2002228791A1
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AU
Australia
Prior art keywords
urea
flue gas
side stream
scr
stream
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.)
Abandoned
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AU2002228791A
Inventor
John M. Boyle
Paul G. Carmignani
William E. Cummings Jr.
Piers De Havilland
William H Sun
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.)
Fuel Tech Inc
Original Assignee
Fuel Tech Inc
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
Family has litigation
First worldwide family litigation filedlitigationCriticalhttps://patents.darts-ip.com/?family=22948481&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=AU2002228791(A1)"Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Fuel Tech IncfiledCriticalFuel Tech Inc
Publication of AU2002228791A1publicationCriticalpatent/AU2002228791A1/en
Abandonedlegal-statusCriticalCurrent

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Abstract

A preferred process arrangement utilizes the enthalpy of the flue gas, which can be supplemented if need be, to convert urea ( 30 ) into ammonia for SCR. Urea ( 30 ), which decomposes at temperatures above 140 ° C., is injected ( 32 ) into a flue gas stream split off ( 28 ) after a heat exchanger ( 22 ), such as a primary superheater or an economizer. Ideally, the side stream would gasify the urea without need for further heating; but, when heat is required it is far less than would be needed to heat either the entire effluent ( 23 ) or the urea ( 30 ). This side stream, typically less than 3% of the flue gas, provides the required temperature and residence time for complete decomposition of urea ( 30 ). A cyclonic separator can be used to remove particulates and completely mix the reagent and flue gas. This stream can then be directed to an injection grid ( 37 ) ahead of SCR using a blower ( 36 ). The mixing with the flue gas is facilitated due to an order of magnitude higher mass of side stream compared to that injected through the AIG in a traditional ammonia-SCR process.
AU2002228791A2000-12-012001-12-03Selective catalytic reduction of no, enabled by side stream urea decompositionAbandonedAU2002228791A1 (en)

Applications Claiming Priority (3)

Application NumberPriority DateFiling DateTitle
US25061800P2000-12-012000-12-01
US602506182000-12-01
PCT/US2001/046415WO2002043837A1 (en)2000-12-012001-12-03Selective catalytic reduction of no, enabled by side stream urea decomposition

Publications (1)

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AU2002228791A1true AU2002228791A1 (en)2002-06-11

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Application NumberTitlePriority DateFiling Date
AU2002228791AAbandonedAU2002228791A1 (en)2000-12-012001-12-03Selective catalytic reduction of no, enabled by side stream urea decomposition

Country Status (15)

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US (1)US7090810B2 (en)
EP (1)EP1339479B1 (en)
JP (1)JP2004514828A (en)
KR (1)KR20020081294A (en)
CN (2)CN101066520B (en)
AT (1)ATE355883T1 (en)
AU (1)AU2002228791A1 (en)
CA (1)CA2397923C (en)
CZ (1)CZ305419B6 (en)
DE (1)DE60127164T2 (en)
ES (1)ES2278806T3 (en)
MX (1)MXPA02007703A (en)
PT (1)PT1339479E (en)
TW (1)TWI228054B (en)
WO (1)WO2002043837A1 (en)

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Also Published As

Publication numberPublication date
JP2004514828A (en)2004-05-20
DE60127164T2 (en)2008-01-10
CN101066520B (en)2010-06-16
EP1339479B1 (en)2007-03-07
KR20020081294A (en)2002-10-26
DE60127164D1 (en)2007-04-19
TW200407189A (en)2004-05-16
MXPA02007703A (en)2004-09-10
ATE355883T1 (en)2007-03-15
CA2397923C (en)2007-08-07
US7090810B2 (en)2006-08-15
US20040057887A1 (en)2004-03-25
TWI228054B (en)2005-02-21
CN1419471A (en)2003-05-21
WO2002043837A1 (en)2002-06-06
CZ305419B6 (en)2015-09-09
ES2278806T3 (en)2007-08-16
CZ2003218A3 (en)2003-12-17
HK1111648A1 (en)2008-08-15
CA2397923A1 (en)2002-06-06
EP1339479A4 (en)2004-11-24
PT1339479E (en)2007-05-31
CN101066520A (en)2007-11-07
EP1339479A1 (en)2003-09-03
CN1314475C (en)2007-05-09

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