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US4045540A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the synthesis of ammonium nitrite

Assignee: Honeywell International Inc
•
Filing: 1976-03-10
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Granted: 1977-08-30
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Expires: 1996-03-10
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Abstract

Abstract Ammonium nitrite is commercially produced by contacting a gaseous stream containing nitric oxide, nitrogen dioxide and oxygen with an aqueous solution containing a basically reacting ammonium compound in an absorption system. However, at normal production rates, serious problems have been encountered because of the emission of unreacted nitric oxide which causes pollution of the atmosphere. It has now been found that by adding controlled supplemental quantities of nitrogen dioxide to the absorption system, nitrogen oxide emission is substantially reduced.

Inventors

  • 👤 Richard Ross Hertzog

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 04:35
CPC Classifications
C; C01; C01C; C01C1/00; C01C1/24; C01B; C01B21/00; C01B21/20; C01B21/50

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 156 words
In a process for producing ammonium nitrite by the absorption of a gas containing nitric oxide, nitrogen dioxide, oxygen and at least 65 percent by volume of inert gas in an absorption system with an aqueous absorbing solution containing a basically reacting ammonium compound selected from the group consisting of ammonium carbonate, ammonium bicarbonate, ammonium hydroxide and mixtures thereof, employing entering gas with at least 2.0 mol ratio of nitric oxide:nitrogen dioxide and employing absorbing solution having normality of at least 0.01 with respect to the basically reacting ammonium compound, the improvement which comprises adding supplemental nitrogen dioxide to said gas being absorbed in the absorption system in amount sufficient to maintain a nitric oxide:nitrogen dioxide mol ratio between 0.8 and 1.0 in the exiting gas, said supplemental nitrogen dioxide being added to said gas when the absorption of nitrogen oxides is 50 to 95 percent complete based on the nitrogen oxides in the entering gas.
Claim 2
Dependent Claim 156 words
In a process for producing ammonium nitrite by the absorption of a gas containing nitric oxide, nitrogen dioxide, oxygen and at least 65 percent by volume of inert gas in an absorption system with an aqueous absorbing solution containing a basically reacting ammonium compound selected from the group consisting of ammonium carbonate, ammonium bicarbonate, ammonium hydroxide and mixtures thereof, employing entering gas with at least 2.0 mol ratio of nitric oxide:nitrogen dioxide and employing absorbing solution having normality of at least 0.01 with respect to the basically reacting ammonium compound, the improvement which comprises adding supplemental nitrogen dioxide to said gas being absorbed in the absorption system in amount sufficient to maintain a nitric oxide:nitrogen dioxide mol ratio between 0.8 and 1.0 in the exiting gas, said supplemental nitrogen dioxide being added to said gas when the absorption of nitrogen oxides is 50 to 95 percent complete based on the nitrogen oxides in the entering gas.
Claim 3
Dependent Claim 14 words
The process of claim 1 wherein said basically reacting ammonium compound is ammonium bicarbonate.
Claim 4
Dependent Claim 20 words
The process of claim 1 wherein said basically reacting ammonium compound is a mixture of ammonium bicarbonate and ammonium carbonate.
Claim 5
Dependent Claim 35 words
The process of claim 1 wherein sufficient supplemental nitrogen dioxide is added to said absorption system to maintain a nitric oxide:nitrogen dioxide mol ratio between 0.9 and 1.0 in the gas exiting said absorption system.
Claim 6
Dependent Claim 33 words
The process of claim 4 wherein said supplemental nitrogen dioxide is added when the absorption of nitrogen oxides is 60 to 90 percent complete based on the nitrogen oxides in said entering gas.

References Cited (Backward Citations)

US1061630A Cited
US1070070A Cited
US2805123A Cited
US2797144A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-29 1981-02-28 1981-08-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-29 1985-02-28 1985-08-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-29 1989-02-28 1989-08-30 $7700.00 Window Closed / Lapsed

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