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US5281128A Expired / Lapsed US ⏱️ 0.0 years remaining

Multistage process for combusting fuel mixtures

Assignee: Kawasaki Motors Ltd
•
Filing: 1990-11-26
•
Granted: 1994-01-25
•
Expires: 2010-11-26
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Abstract

Abstract This invention is a combustion process having a series of stages in which the fuel is stepwise combusted using specific catalysts and catalytic structures and, optionally, a final homogeneous combustion zone. The choice of catalysts and the use of specific structures, including those employing integral heat exchange, results in a catalyst support which is stable due to its comparatively low temperature and yet the product combustion gas is at a temperature suitable for use in a gas turbine, furnace, boiler, or the like, but has low NOx content.

Inventors

  • 👤 Ralph A. Dalla Betta
  • 👤 Kazunori Tsurumi
  • 👤 Nobuyasu Ezawa

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 11:50
CPC Classifications
F; F23; F23C; F23C13/00; F23C6/00; F23C6/04; F23C6/045; F23C2900/00; F23C2900/13002

Claims Analysis

Total Claims: 41
Claim 1
Independent Claim 253 words
A process for combusting fuel mixtures comprising the steps of: a. mixing an oxygen-containing gas with a fuel to form a combustible mixture, b. contacting the combustible mixture in a first zone with a first zone combustion catalyst comprising palladium at reaction conditions sufficient to combust at least a portion but not all of the fuel and produce a first zone combustion catalyst temperature no greater than about 940° C., c. contacting the partially combusted gas from the first zone in a second zone with a second combustion catalyst comprising palladium on a support having integral heat exchange surfaces in which a surface supporting said second zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a further portion but not all of the fuel and produce a second zone combustion catalyst temperature of no greater than about 940° C., and contacting the partially combusted gas from the second zone in a third zone with a third zone combustion catalyst comprising platinum on a support having integral heat exchange in which a surface supporting said third zone catalyst is in heat exchange relationship with a surface not supporting a catalyst and both such surfaces are in contact with partially combusted gas at reaction conditions sufficient to combust at least a further portion of the fuel and produce a third zone combustion catalyst temperature no greater than about 1050° C.
Claim 2
Dependent Claim 253 words
A process for combusting fuel mixtures comprising the steps of: a. mixing an oxygen-containing gas with a fuel to form a combustible mixture, b. contacting the combustible mixture in a first zone with a first zone combustion catalyst comprising palladium at reaction conditions sufficient to combust at least a portion but not all of the fuel and produce a first zone combustion catalyst temperature no greater than about 940° C., c. contacting the partially combusted gas from the first zone in a second zone with a second combustion catalyst comprising palladium on a support having integral heat exchange surfaces in which a surface supporting said second zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a further portion but not all of the fuel and produce a second zone combustion catalyst temperature of no greater than about 940° C., and contacting the partially combusted gas from the second zone in a third zone with a third zone combustion catalyst comprising platinum on a support having integral heat exchange in which a surface supporting said third zone catalyst is in heat exchange relationship with a surface not supporting a catalyst and both such surfaces are in contact with partially combusted gas at reaction conditions sufficient to combust at least a further portion of the fuel and produce a third zone combustion catalyst temperature no greater than about 1050° C.
Claim 3
Dependent Claim 24 words
The process of claim 1 where the combustible mixture is introduced into the first zone at a temperature of at least about 325° C.
Claim 4
Dependent Claim 24 words
The process of claim 2 where the combustible mixture is introduced into the first zone at a temperature between 325° C. and 372° C.
Claim 5
Dependent Claim 24 words
The process of claim 1 where the bulk temperature of the gas leaving the first zone is between about 500° C. and 650° C.
Claim 6
Dependent Claim 17 words
The process of claim 4 where the first zone combustion catalyst comprises palladium on a metallic support.
Claim 7
Dependent Claim 23 words
The process of claim 1 where the first zone combustion catalyst additionally contains one or more Group IB metals or Group VIII metals.
Claim 8
Dependent Claim 16 words
The process of claim 6 where the first zone combustion catalyst additionally contains silver or platinum.
Claim 9
Dependent Claim 19 words
The process of claim 1 where the first zone combustion catalyst comprises a support having integral heat exchange surfaces.
Claim 10
Dependent Claim 24 words
The process of claim 1 where the bulk temperature of the gas leaving the second zone is between about 750° C. and 800° C.
Claim 11
Dependent Claim 23 words
The process of claim 1 where the second zone combustion catalyst additionally contains one or more Group IB metals or Group VIII metals.
Claim 12
Dependent Claim 16 words
The process of claim 10 where the second zone combustion catalyst additionally contains silver or platinum.
Claim 13
Dependent Claim 24 words
The process of claim 1 where the bulk temperature of the gas leaving the third zone is between about 850° C. and 1050° C.
Claim 14
Dependent Claim 24 words
The process of claim 12 where the bulk temperature of the gas leaving the third zone is between about 850° C. and 1050° C.
Claim 15
Dependent Claim 23 words
The process of claim 1 where the oxygen-containing gas is air and is compressed to a pressure of 0.0 to 35 atms (gauge).
Claim 16
Dependent Claim 32 words
The process of claim 1 where the first zone combustion catalyst comprising palladium on a metallic support additionally comprises a barrier layer covering at least a portion of the palladium containing catalyst.
Claim 17
Dependent Claim 12 words
The process of claim 15 where the barrier layer comprises aluminum oxide.
Claim 18
Dependent Claim 43 words
The process of claim 1 additionally comprising the step of oxidizing any remaining unoxidized fuel in a fourth zone to produce a gas having a temperature greater than that of the gas leaving the third zone but no greater than about 1700° C.
Claim 19
Dependent Claim 294 words
A process for combusting fuel mixtures to produce a low NO x gas comprising the steps of: a. contacting a combustible mixture of a fuel and air in a first zone with a first zone combustion catalyst comprising palladium on a support at reaction conditions sufficient to combust at least a portion but not all of the fuel and produce a partially combusted gas both at a bulk and localized temperature no greater than about 800° C., b. contacting the partially combusted gas from the first zone in a second zone with a second zone combustion catalyst comprising palladium on a support having integral heat exchange surfaces in which a surface supporting said second zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a portion but not all of the fuel and produce a partially combusted gas at a bulk temperature greater than the bulk temperature of the gas leaving the first zone but not greater than about 900° C., and c. contacting the partially combusted gas from the second zone in a third zone with a third zone combustion catalyst comprising platinum on a support having integral heat exchange surfaces in which a surface supporting said third zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a portion of the fuel and produce a low NO x gas both at a bulk and localized temperature greater than the bulk temperature of the gas leaving the second stage but less than about 1200° C.
Claim 20
Dependent Claim 294 words
A process for combusting fuel mixtures to produce a low NO x gas comprising the steps of: a. contacting a combustible mixture of a fuel and air in a first zone with a first zone combustion catalyst comprising palladium on a support at reaction conditions sufficient to combust at least a portion but not all of the fuel and produce a partially combusted gas both at a bulk and localized temperature no greater than about 800° C., b. contacting the partially combusted gas from the first zone in a second zone with a second zone combustion catalyst comprising palladium on a support having integral heat exchange surfaces in which a surface supporting said second zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a portion but not all of the fuel and produce a partially combusted gas at a bulk temperature greater than the bulk temperature of the gas leaving the first zone but not greater than about 900° C., and c. contacting the partially combusted gas from the second zone in a third zone with a third zone combustion catalyst comprising platinum on a support having integral heat exchange surfaces in which a surface supporting said third zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a portion of the fuel and produce a low NO x gas both at a bulk and localized temperature greater than the bulk temperature of the gas leaving the second stage but less than about 1200° C.
Claim 21
Dependent Claim 24 words
The process of claim 18 wherein the combustible mixture is introduced into the first zone at a temperature of at least about 325° C.
Claim 22
Dependent Claim 24 words
The process of claim 19 where the combustible mixture is introduced into the first zone at a temperature between 325° C. and 375° C.
Claim 23
Dependent Claim 23 words
The process of claim 18 where the bulk temperature of the gas leaving the first zone is no greater than about 550° C.
Claim 24
Dependent Claim 24 words
The process of claim 21 where the bulk temperature of the gas leaving the first zone is between about 500° C and 600° C.
Claim 25
Dependent Claim 16 words
The process of claim 18 where the first zone combustion catalyst support is ceramic or metal.
Claim 26
Dependent Claim 14 words
The process of claim 23 where the first zone combustion catalyst support is metal.
Claim 27
Dependent Claim 24 words
The process of claim 18 wherein the bulk temperature of the gas leaving the second zone is between about 700° C. and 800° C.
Claim 28
Dependent Claim 16 words
The process of claim 18 where the second zone combustion catalyst support is metal or ceramic.
Claim 29
Dependent Claim 14 words
The process of claim 26 where the second zone combustion catalyst support is metal.
Claim 30
Dependent Claim 24 words
The process of claim 18 where the bulk temperature of the gas leaving the third zone is between about 850° C. and 1150° C.
Claim 31
Dependent Claim 24 words
The process of claim 25 where the bulk temperature of the gas leaving the third zone is between about 850° C. and 1150° C.
Claim 32
Dependent Claim 16 words
The process of claim 18 where the third stage combustion catalyst support is ceramic or metal.
Claim 33
Dependent Claim 14 words
The process of claim 30 where the third stage combustion catalyst support is metal.
Claim 34
Dependent Claim 31 words
The process of claim 18 where the first zone combustion catalyst comprising palladium on a metallic support additionally comprises an oxide barrier layer covering at least a portion of the palladium.
Claim 35
Dependent Claim 10 words
The process of claim 32 where the barrier comprises zirconia.
Claim 36
Dependent Claim 45 words
The process of claim 18 additionally comprising of the step of oxidizing any remaining unoxidized fluid level in a fourth zone to produce a gas having a temperature greater than that of the gas leaving the third zone but no greater than about 1700° C.
Claim 37
Dependent Claim 44 words
The process of claim 29 additionally comprising the step of oxidizing any remaining unoxidized fluid level in a fourth zone to produce a gas having a temperature greater than that of the gas leaving the third zone but no greater than about 1700° C.
Claim 38
Dependent Claim 302 words
A process for combusting fuel mixtures to produce a low NO x gas comprising the steps of: a. mixing methane and air to product a compressed mixture, b. contacting the compressed mixture in a first zone with a first zone combustion catalyst comprising palladium on a metallic support at reaction conditions sufficient to combust at least a portion but not all of the methane and produce a partially combusted gas at both bulk and localized temperatures no greater than about 800° C., c. contacting the partially combusted gas from the first zone in a second zone with a second zone combustion catalyst comprising palladium on a metallic support having integral heat exchange surfaces in which a surface supporting said second zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a portion but not all of the methane and produce a partially combusted gas at a bulk temperature greater than the bulk temperature of the gas leaving the first zone but no greater than about 900° C., and d. contacting the partially combusted gas from the second zone in a third zone with a third zone combustion catalyst comprising platinum on a metallic support having integral heat exchange surfaces in which a surface supporting said third zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a portion of the methane and produce a low NO x gas at a bulk and a localized temperature greater than the bulk temperature of the gas leaving the second zone but no greater than about 1200° C.
Claim 39
Dependent Claim 302 words
A process for combusting fuel mixtures to produce a low NO x gas comprising the steps of: a. mixing methane and air to product a compressed mixture, b. contacting the compressed mixture in a first zone with a first zone combustion catalyst comprising palladium on a metallic support at reaction conditions sufficient to combust at least a portion but not all of the methane and produce a partially combusted gas at both bulk and localized temperatures no greater than about 800° C., c. contacting the partially combusted gas from the first zone in a second zone with a second zone combustion catalyst comprising palladium on a metallic support having integral heat exchange surfaces in which a surface supporting said second zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a portion but not all of the methane and produce a partially combusted gas at a bulk temperature greater than the bulk temperature of the gas leaving the first zone but no greater than about 900° C., and d. contacting the partially combusted gas from the second zone in a third zone with a third zone combustion catalyst comprising platinum on a metallic support having integral heat exchange surfaces in which a surface supporting said third zone combustion catalyst is in heat exchange relationship with a surface not supporting a catalyst and both surfaces are in contact with the partially combusted gas at reaction conditions sufficient to combust at least a portion of the methane and produce a low NO x gas at a bulk and a localized temperature greater than the bulk temperature of the gas leaving the second zone but no greater than about 1200° C.
Claim 40
Dependent Claim 54 words
The process of claim 36 where the gas from the third zone contains uncombusted methane and additionally comprising the steps of combusting the remaining methane in a fourth zone to produce a gas having a bulk temperature greater than that of the gas leaving the third zone but no greater than about 1700° C.
Claim 41
Dependent Claim 21 words
The processes of claim 37 where the low NO x gas has no more than about five ppm NO x .

References Cited (Backward Citations)

US3969082A Cited
US3870455A Cited
US4088435A Cited
US3970435A Cited
US4270896A Cited
US4118199A Cited
US4019969A Cited
GB1528455A Cited
US4220559A Cited
US4331631A Cited
US4279782A Cited
JPS57210207A Cited
US4414023A Cited
JPS59136140A Cited
JPS6014939A Cited
JPS6014938A Cited
JPS6026211A Cited
JPS6051545A Cited
JPS6051543A Cited
JPS6051544A Cited
JPS6053724A Cited
JPS6054736A Cited
JPS6060424A Cited
JPS6060411A Cited
JPS6066022A Cited
US4731989A Cited
JPS60147243A Cited
JPS60175925A Cited
JPS60196511A Cited
JPS60202745A Cited
JPS60202235A Cited
JPS60200021A Cited
JPS60205116A Cited
JPS60205129A Cited
JPS60205115A Cited
JPS60222145A Cited
JPS60238148A Cited
JPS6133233A Cited
JPS6138627A Cited
US4650782A Cited
JPS61147014A Cited
JPS61209044A Cited
JPS61216734A Cited
JPS61235609A Cited
EP0198948A2 Cited
JPS61237905A Cited
US4711872A Cited
JPS61252408A Cited
JPS61252409A Cited
JPS61259013A Cited
JPS621454A Cited
JPS6241511A Cited
JPS6245343A Cited
JPS6246116A Cited
JPS6249125A Cited
JPS6271535A Cited
JPS6279847A Cited
JPS6280419A Cited
JPS6280420A Cited
JPS6284215A Cited
JPS62112910A Cited
JPS62125210A Cited
JPS62158910A Cited
JPS62216642A Cited
JPS62221445A Cited
JPS62261803A Cited
JPS62289237A Cited
JPS6341720A Cited
EP0266875A1 Cited
US4793797A Cited
JPS63190644A Cited
JPS6380848A Cited
JPS6380849A Cited
JPS6380847A Cited
JPS63213723A Cited
US4849399A Cited
JPS63267804A Cited
US4870824A Cited
JPH01139911A Cited
JPH01210707A Cited
JPH01242151A Cited
JPH0222117A Cited
JPH0252930A Cited
US4893465A Cited
JPH0259045A Cited
JPH02211255A Cited
JPH02213607A Cited
JPH02238206A Cited
JPH02268830A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1997-01-24 1997-07-26 1998-01-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2001-01-24 2001-07-26 2002-01-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2005-01-24 2005-07-26 2006-01-25 $7700.00 Window Closed / Lapsed

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