Catalytic reduction of nox

A method comprising:

• (a) passing an exhaust gas from a diesel engine over an oxidation catalyst to provide an adjusted gas stream, the exhaust gas comprising a first content level by volume of NO, a first content level by volume of NO2, and particulate matter, and the adjusted gas stream comprising a second content level by volume of NO that is lower than the first content level of NO, and a second content level by volume of NO2;
• (b) passing the adjusted gas stream through a particulate trap that results in trapping at least a portion of the particulate matter on the particulate trap;
• (c) combusting a portion of the trapped particulate matter in the presence of the adjusted gas stream to reduce a combustion temperature necessary to stop significant accumulation of particulate matter in the particulate trap relative to the combustion temperature of a portion of the particulate matter in the presence of the exhaust gas necessary to stop significant accumulation of particulate matter in the particulate trap, and to create a further adjusted gas stream comprising a third content level by volume of NO and a third content level by volume of NO2 that is lower than the second content level of NO2;
• (d) injecting a reductant fluid comprising urea into the further adjusted gas stream;
• (e) mixing the further adjusted gas stream with the injected reductant fluid to form a further adjusted gas stream mixed with reductant fluid;
• and
• (f) passing the further adjusted gas stream mixed with reductant fluid over an SCR catalyst to provide a final adjusted gas stream comprising a fourth content level by volume of NO and a fourth content level by volume of NO2;
• wherein the second content level of NO2 is sufficiently higher than the first content level of NO2 such that when a portion of the second content-level of NO2 in the adjusted gas stream is consumed during the combustion of the at least a portion of the trapped particulate matter, the resulting third content level of NO2 is still sufficiently high for use with the SCR catalyst to provide the final adjusted gas stream where the total combined volume of the fourth content level of NO and the fourth content level of NO2 is lower than the total combined volume of the first content level of NO and the first content level of NO2, and the total combined volume of the fourth content level of NO and the fourth content level of NO2 is lower relative to the respective total combined volume of NO and NO2 in a final exhaust stream that would result from carrying out steps (b)-(f) starting with the exhaust gas instead of the adjusted gas stream.

A method comprising:

• (a) passing an exhaust gas from a diesel engine over an oxidation catalyst to provide an adjusted gas stream, the exhaust gas comprising a first content level by volume of NO, a first content level by volume of NO2, and particulate matter, and the adjusted gas stream comprising a second content level by volume of NO that is lower than the first content level of NO, and a second content level by volume of NO2;
• (b) passing the adjusted gas stream through a particulate trap that results in trapping at least a portion of the particulate matter on the particulate trap;
• (c) combusting a portion of the trapped particulate matter such that there is no significant accumulation of particulate matter in the particulate trap in the presence of the adjusted gas stream at a combustion temperature that is lower than the temperature necessary to combust the trapped particulate matter in the presence of the exhaust gas such that there is no significant accumulation of particulate matter in the particulate trap, to create a further adjusted gas stream comprising a third content level by volume of NO and a third content level by volume of NO2 that is lower than the second content level of NO2;
• (d) injecting a reductant fluid comprising urea into the further adjusted gas stream;
• (e) mixing the further adjusted gas stream with the injected reductant fluid to form a further adjusted gas stream mixed with reductant fluid;
• and
• (f) passing the further adjusted gas stream mixed with reductant fluid over an SCR catalyst to provide a final adjusted gas stream comprising a fourth content level by volume of NO and a fourth content level by volume of NO2;
• wherein the second content level of NO2 is sufficiently higher than the first content level of NO2 such that when a portion of the second content-level of NO2 in the adjusted gas stream is consumed during the combustion of the at least a portion of the trapped particulate matter, the resulting third content level of NO2 is still sufficiently high for use with the SCR catalyst to provide the final adjusted gas stream where the total combined volume of the fourth content level of NO and the fourth content level of NO2 is lower than the total combined volume of the first content level of NO and the first content level of NO2, and the total combined volume of the fourth content level of NO and the fourth content level of NO2 is lower relative to the respective total combined volume of NO and NO2 in a final exhaust stream that would result from carrying out steps (b)-(f) starting with the exhaust gas instead of the adjusted gas stream;
• and
• wherein the further adjusted gas stream mixed with reductant fluid is at least 225° C. when passed over the SCR catalyst, and the final adjusted gas stream has more than 90% less NOx content by volume and at least 67% less particulate matter content by volume than the exhaust gas.