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US2910343A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for catalytically reducing nitrogen oxides in industrial stack gases

Assignee: EIDP Inc
•
Filing: 1955-12-08
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Granted: 1959-10-27
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Expires: 1975-12-08
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Abstract

Abstract <PICT:0829581/III/1> Noxious gases containing nitrogen oxide fumes are made innocuous by producing a gas free from nitrogen oxides and hydrogen cyanide by adding a reducing gas and passing the resulting mixture first over a noble metal catalyst then over a heterogeneous gas phase reduction catalyst, the catalysis being conducted at 100 DEG C. to 1000 DEG C., preferably 500-1000 DEG C. Reducing gases may be natural gas, methane, ethane, propane, butane, or mixtures thereof alone or with hydrogen, oil or coke oven hydrocarbon gas, or hydrogen alone. 40% H2 may be used with an alkane, and the presence of H2 renders preheating of the catalyst layer unnecessary. The gases treated may be those containing NO, N2O and/or NO2, from the HNO3 oxidation of cyclic alkanones or cyclic alkanols or from the oxidation of NH3 to HNO3. A mixture of natural gas and air enters catalyst converter 1 through inlet manifold 7 and is ignited by spark plug 9. The resulting gas flame is passed through catalyst bed 2, which is divided into at least two layers with, or without a gas permeable partition 2a, until the desired temperature is attained. The air feed is discontinued, the gas containing nitrogen oxides after passing through preheater 10, or not, enters converter 1 at 6 and natural gas, with or without H2, enters through distributer 4. Steam or nitrogen enters through inlet manifold 7 and gas, wherein the nitrogen oxides have been converted to N2, and containing CO2 and H2O is withdrawn from outlet 8 through heat exchanger 10 to stack. The temperature is controlled by the extent of preheating, by the amount of steam, or nitrogen used, and by water jacket 3, in response to indications of thermocouple in well 11. The first catalyst is a thin layer of gold, ruthenium, iridium, platinum, rhodium or palladium, or mixtures thereof, as gauzes, or mats, or supported on alumina, infusorial earth or kieselguhr. The second catalyst is nickel on alumina or nickel aluminate, copper chromite, copper impregnated alumina, or oxides of metals, such as titanium, calcium, cerium, zirconium, aluminium, thorium, tin, tungsten, molybdenum, niobium, chromium, manganese, zinc, copper, cobalt, nickel and iron, particularly mixed oxides of copper and chromium and of nickel and chromium. The nickel on alumina is prepared by precipitating basic nickel carbonate with ammonium carbonate or bicarbonate on alumina hydrate, dried and calcined to convert nickel salt to oxide and dehydrate the alumina, the nickel oxide is reduced to nickel, and the mixture of nickel and alumina is mixed with a volatilizable lubricant, e.g. high melting wax, pelleted, heated to 500 DEG C. in O2, and finally heated to 1050 DEG C.

Inventors

  • 👤 Childers Eugene
  • 👤 Ellis Charles William
  • 👤 Ryan Donald James

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 07:26
CPC Classifications
F; F01; F01N; F01N3/00; F01N3/08; F01N3/10; F01N3/18; F01N3/20; F01N3/2006; F01N3/2046; B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8621; B01D53/8625; B01D53/8628; F01N3/02; F01N3/0205; F01N3/2033; F01N3/206; F01N3/2066; F01N3/24; F01N3/38; F23; F23B; F23B7/00; F23J; F23J11/00; F01N2240/00; F01N2240/02; F01N2260/00; F01N2260/02; F01N2260/024; F01N2610/00; F01N2610/03; F01N2610/04; F23B2700/00; F23B2700/023; Y; Y02; Y02C; Y02C20/00; Y02C20/10; Y02T; Y02T10/00; Y02T10/10; Y02T10/12

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 151 words
IN A PROCESS FOR THE DISPOSAL OF A STACK GAS CONTAINING NITROGEN OXIDE FUMES IN ORDER TO PRODUCE A STACK GAS WHICH IS SUBSTANTIALLY FREE FROM NITROGEN OXIDES AND HYDROGEN CYANIDE AND CAN BE DISCHARGED SAFELY INTO THE ATMOSPHERE WITHOUT ANY DETRIMENTAL EFFECT ON THE ENVIRONMENT, THE STEPS WHICH COMPRISE ADDING A REDUCING GAS TO A NOCUOUS GAS CONTAINING A NITROGEN OXIDE, PASSIN THE RESULTING GASEOUS MIXTURE AT A SPACE VELOCITY OF AT LEAST 25,000 RECIPROCAL HOURS, SPT PER CUBIC FOOT OF CATALYST OVER A PLATINUM ON ALUMINA CATALYST AND THEREAFTER OVER A NICKEL CATALYST SUPORTED ON ALUMINA AT A TEMPERATURE OF 100* C. TO 1000* C., THE NOBLE CATALYST BEING DISPOSED IN A BED HAVING A DEPTH LESS THAN ABOUT ONE-HALF THE DEPTH OF THE NICKEL ON ALUMINA BED, CONTROLLING THE TEMPERATURE AND THEREBY REDUCING THE NITROGEN OXIDE TO NITROGEN AND FINALLY DISCHARGING THE RESULTING EFFUENT GAS INTO THE ATMOSPHERE.
Claim 2
Dependent Claim 151 words
IN A PROCESS FOR THE DISPOSAL OF A STACK GAS CONTAINING NITROGEN OXIDE FUMES IN ORDER TO PRODUCE A STACK GAS WHICH IS SUBSTANTIALLY FREE FROM NITROGEN OXIDES AND HYDROGEN CYANIDE AND CAN BE DISCHARGED SAFELY INTO THE ATMOSPHERE WITHOUT ANY DETRIMENTAL EFFECT ON THE ENVIRONMENT, THE STEPS WHICH COMPRISE ADDING A REDUCING GAS TO A NOCUOUS GAS CONTAINING A NITROGEN OXIDE, PASSIN THE RESULTING GASEOUS MIXTURE AT A SPACE VELOCITY OF AT LEAST 25,000 RECIPROCAL HOURS, SPT PER CUBIC FOOT OF CATALYST OVER A PLATINUM ON ALUMINA CATALYST AND THEREAFTER OVER A NICKEL CATALYST SUPORTED ON ALUMINA AT A TEMPERATURE OF 100* C. TO 1000* C., THE NOBLE CATALYST BEING DISPOSED IN A BED HAVING A DEPTH LESS THAN ABOUT ONE-HALF THE DEPTH OF THE NICKEL ON ALUMINA BED, CONTROLLING THE TEMPERATURE AND THEREBY REDUCING THE NITROGEN OXIDE TO NITROGEN AND FINALLY DISCHARGING THE RESULTING EFFUENT GAS INTO THE ATMOSPHERE.

References Cited (Backward Citations)

US1962485A Cited
GB476684A Cited
GB693775A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1962-10-26 1963-04-27 1963-10-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1966-10-26 1967-04-27 1967-10-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1970-10-26 1971-04-27 1971-10-27 $7700.00 Window Closed / Lapsed

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