Assembly and method for reducing nitrogen oxides, carbon monoxide and hydrocarbons in exhausts of internal combustion engines
View Patent ↗An assembly and method for reducing nitrogen oxides, carbon monoxide and hydrocarbons in exhausts of internal combustion engines, wherein the exhaust is acted upon in a first stage catalytic converter. A first portion of the first stage catalytic converter output is cooled and a second portion of the catalytic converter output is not cooled. The cooled and not cooled exhausts are united and directed to a second stage catalytic converter. Air is injected into a selected one of (1) the not cooled exhaust prior to the juncture thereof with the cooled exhaust, and (2) the combined cooled and not cooled exhausts after the juncture thereof.
1. A method of operating a catalytic system for reducing emissions from a rich burn spark-ignited engine, comprising:
controlling intake air and fuel (AFR) to produce first exhaust gases substantially free of oxygen;
passing said first exhaust gases into a first-stage catalyst chamber containing a three-way catalyst (TWC) operating above 800° F., which minimizes NOx content by reducing NOx (to N 2 and O 2 );
passing exhaust gases exiting from the first-stage catalyst chamber to an inter-stage cooling chamber having
a) cooling means, and cooling by-pass means, which are used to adjust gas temperature to a controlled Tmix =390 -520° F., and
b) secondary air injection means, which enriches the oxygen content to about 0.25- 1.0%;
passing exhaust gases exiting from the inter-stage cooling chamber to a second-stage catalyst chamber containing a catalyst that minimizes CO content by oxidizing CO to CO 2 .
2. The method of claim 1 , wherein the engine is a stationary engine in combined heat and power (CHP) application.
3. The method of claim 2 , wherein Tmix =390-420° F.
4. The method of claim 2 , wherein the AFR is provided using a gaseous fuel/air mixer, a computer controlled fuel valve, and gaseous fuel is provided to the fuel/air mixer at atmospheric pressure.
5. The method of claim 4 , wherein said gaseous fuel is Natural Gas.
6. The method of claim 2 , wherein emissions of NOx exiting the first stage catalyst chamber are less than 3.7 ppm (at 15% O 2 ), and emissions of CO exiting the second stage catalyst chamber are less than 8.9 ppm (at 15% O 2 ), said emissions based on time-average data taken over an extended interval.
7. The method of claim 1 , wherein the inter-stage cooling chamber provides for injection of water.