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US5208205A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalyst system for converting emissions of a lean-burn engine

Assignee: Ford Global Technologies LLC
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Filing: 1991-10-07
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Granted: 1993-05-04
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Expires: 2011-10-07
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Abstract

Abstract A catalyst system for attaining high conversions of NO, HC, and CO in a fuel-lean emission flow (i.e., containing SO 2 , H 2 O, H 2 , and considerable excess oxygen), the system comprising: (a) a first stage reducing catalyst for treating the nitric oxide emissions, the catalyst containing highly acidic gamma alumina (i.e., with a pH pzc of less than 3); (b) means for injecting gaseous or liquid reductants into the emission stream prior to entering said first stage catalyst, said first stage catalyst temperature being selected to be in the range of 550°-650° C.; and (c) an oxidation catalyst effective for treating the effluent from the first stage catalyst. Another aspect of this invention is a method of treating the exhaust gas from a fuel-lean emission flow from a fossil-fueled internal combustion engine having a redox ratio of 0.02-0.09, the method comprising: (a) injecting a gaseous or liquid HC or oxygenated HC reductant into the emission stream at a location where the stream is within the temperature range of 550°-650° C.; (b) immediately exposing the injected stream to a first stage catalyst containing acidic gamma alumina with a pH pzc of less than 3; and (c) exposing the effluent from the first stage catalyst to an oxidation catalyst that is effective in ensuring that the NO, HC, and CO in the emissions are each converted to at least 80%.

Inventors

  • 👤 Somasundaram Subramanian
  • 👤 Robert J. Kudla
  • 👤 Mohinder S. Chattha

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 08:21
CPC Classifications
F; F01; F01N; F01N3/00; F01N3/08; F01N3/10; F01N3/18; F01N3/20; F01N3/206; F01N3/2066; B; B01; B01D; B01D53/00; B01D53/34; B01D53/92; B01D53/94; B01D53/9459; B01J; B01J21/00; B01J21/02; B01J21/04; F01N13/00; F01N13/009; B01D2251/00; B01D2251/20; B01D2251/208; B01D2251/21; B01D2255/00; B01D2255/10; B01D2255/102; B01D2255/1023; B01D53/9404; B01D53/9409; B01D53/9413; B01D53/9418; B01D53/944; F01N2610/00; F01N2610/03; Y; Y02; Y02T; Y02T10/00; Y02T10/10; Y02T10/12

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 126 words
A catalyst system for attaining high conversion of NO x , HC, and CO contained in the emission flow from a lean-burn internal combustion engine, the system comprising: (a) a first stage catalyst for treating nitric oxide in said emission flow, said first stage catalyst consisting of highly acidic gamma alumina having a pH pzc of less than 3; (b) means for distributing a gaseous or liquid NO x reductant into said emission stream prior to entering said first stage catalyst when the latter is at a temperature range of 550°-650° C., said reductant being selected from the group consisting of alkanes, alkenes, alkynes, aromatics, alcohols, aldehydes, ketones, ethers, and esters; and (c) an oxidizing catalyst effective for treating the effluent from said first stage catalyst.
Claim 2
Dependent Claim 126 words
A catalyst system for attaining high conversion of NO x , HC, and CO contained in the emission flow from a lean-burn internal combustion engine, the system comprising: (a) a first stage catalyst for treating nitric oxide in said emission flow, said first stage catalyst consisting of highly acidic gamma alumina having a pH pzc of less than 3; (b) means for distributing a gaseous or liquid NO x reductant into said emission stream prior to entering said first stage catalyst when the latter is at a temperature range of 550°-650° C., said reductant being selected from the group consisting of alkanes, alkenes, alkynes, aromatics, alcohols, aldehydes, ketones, ethers, and esters; and (c) an oxidizing catalyst effective for treating the effluent from said first stage catalyst.
Claim 3
Dependent Claim 33 words
The catalyst system as in claim 1, in which said means for distributing is an injector effective to introduce said NO x reductant in an amount of 100-5000 ppm of said emission flow.
Claim 4
Dependent Claim 22 words
The catalyst system as in claim 1, in which the ratio of reductant to NO x is in the range of 0.1-10.0.
Claim 5
Dependent Claim 22 words
The catalyst system as in claim 1, in which the oxygen content of said emission flow is in the range of 1.5-10%.
Claim 6
Dependent Claim 37 words
The catalyst system as in claim 1, in which the acidic alumina is characterized by strong acid centers resulting in strong Lewis or Bronsted acidity. such alumina generally having a point of zero charge less than 3.
Claim 7
Dependent Claim 24 words
The catalyst system as in claim 1, in which said emission flow contains SO 2 , H 2 , H 2 O, and CO.
Claim 8
Dependent Claim 43 words
The catalyst system as in claim 1, in which said acidic alumina is obtained by acidification of alumina with acids (HCl, H 2 SO 4 , HF, H 3 PO 4 ) or salts (AlF 3 , AlCl 3 , NH 4 F).
Claim 9
Dependent Claim 20 words
The system as in claim 1, in which said means for distributing comprises a mechanical apparatus for spraying said reductant.
Claim 10
Dependent Claim 53 words
The catalyst system as in claim 1, in which said means for distributing is a device effective to inject an amount of reductant in accordance with the variance of the instantaneous content of NO x in the exhaust stream by use of one or more sensors and a microprocessor of the sensor signal.
Claim 11
Dependent Claim 24 words
The catalyst system as in claim 9, in which said sensor provides a direct measurement of the NO x content of the exhaust stream.
Claim 12
Dependent Claim 23 words
The catalyst system as in claim 1, in which said oxidation catalyst is a base metal oxide or a supported noble metal catalyst.
Claim 13
Dependent Claim 29 words
The catalyst system as in claim 9, in which said microprocessor indirectly estimates the NO x content of the exhaust stream based on the operating conditions of the engine.

References Cited (Backward Citations)

US4087384A Cited
US4111848A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1996-05-03 1996-11-02 1997-05-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2000-05-03 2000-11-02 2001-05-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2004-05-03 2004-11-02 2005-05-04 $7700.00 Window Closed / Lapsed

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