Production of NO from N.sub.2 O
AssigneeE. I. Du Pont de Nemours and Company
InventorsRonald A. Reimer, Colin S. Slaten
Life of this patent
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Abstract
A Process for the conversion of N.sub.2 O to NO by heating a gas stream containing N.sub.2 O by contact with a heated heat exchange surface to a temperature of about 400.degree. to 700 degrees C., and then heating the gas to a temperature of about 850 degrees C. while the gas is not in contact with a heated heat exchange surface, and spontaneously and decomposing the N.sub.2 O and recovering NO.
Claims7
A process for the production and recovery of NO from a gas stream prepared by the decomposition of N.sub.2 O contained in a gas stream, which comprises (a) heating a first gas stream containing the N.sub.2 O to a temperature between about 400 and 700 degrees C. by contacting said N.sub.2 O containing stream with a heated heat-exchange surface, (b) then passing the stream into a zone where is it out of contact with a heated heat-exchange surface while raising the stream temperature to about 850 degrees C., by combining the stream with a heated second gas stream or by injecting and combusting a combustible gas in the stream, (c) decomposing the N.sub.2 O in the stream spontaneously and exothermally to form NO, N.sub.2 and O.sub.2, while the temperature in the stream is raised to at least about 1000 degrees C., (d) rapidly cooling the gas stream now containing NO and (e) recovering the NO formed.
A process for the production and recovery of NO from a gas stream prepared by the decomposition of N.sub.2 O contained in a gas stream, which comprises (a) heating a first gas stream containing the N.sub.2 O to a temperature between about 400 and 700 degrees C. by contacting said N.sub.2 O containing stream with a heated heat-exchange surface, (b) combusting a combustible second gas stream, (c) then combining the first and second gas streams in a zone where the combined stream is out of contact with a heated heat-exchange surface, the temperature and volume of the second gas stream being sufficient to raise the temperature of the combined stream to 850 degrees C., (d) decomposing the N.sub.2 O in the combined stream spontaneously and exothermally to form NO, N.sub.2 and O.sub.2, while the temperature in the combined stream is raised to at least about 1000 degrees C., (e) rapidly cooling the gas stream now containing NO and (f) recovering the NO formed.
A process for the production and recovery of NO from a gas stream prepared by the decomposition of N.sub.2 O contained in a gas stream, which comprises (a) heating a first gas stream containing the N.sub.2 O to a temperature between about 400 and 700 degrees C. by contacting said N.sub.2 O containing stream with a heated heat-exchange surface, (b) injecting a combustible second gas stream into the first gas stream, (c) igniting the combustible second gas stream as it is injected directly into the first gas stream thereby heating the entire combined steam to a temperature of a least 850 degrees C. at which temperature the N.sub.2 O in the combined stream decomposes spontaneously and exothermally to form NO, N.sub.2, and O.sub.2, and the temperature of the combined stream is raised to at least about 1000 degrees C. (d) rapidly cooling the gas stream now containing NO and (e) recovering the NO formed.
Dependencies are inferred from the claim text.