초록 ▼

The present disclosure relates to an apparatus and method for increasing the level of hydrogen produced in an exhaust gas recirculation pathway within an internal combustion engine. A hydrocarbon water gas shift reformer is positioned in series with a water gas shift reformer within the exhaust gas

The present disclosure relates to an apparatus and method for increasing the level of hydrogen produced in an exhaust gas recirculation pathway within an internal combustion engine. A hydrocarbon water gas shift reformer is positioned in series with a water gas shift reformer within the exhaust gas recirculation pathway to improve the yield of hydrogen and to improve the relative efficiency of both catalytic procedures.

대표청구항 ▼

1. A method to process exhaust gas expelled from at least one cylinder of a plurality of cylinders of an internal combustion engine, the method comprising: (a) providing an internal combustion engine having an intake manifold wherein the engine includes an exhaust gas recirculation pathway containin

1. A method to process exhaust gas expelled from at least one cylinder of a plurality of cylinders of an internal combustion engine, the method comprising: (a) providing an internal combustion engine having an intake manifold wherein the engine includes an exhaust gas recirculation pathway containing a hydrocarbon steam reformer including a steam reformation catalyst and a water gas shift reformer including a water gas shift catalyst wherein said water gas shift reformer is serially coupled downstream of said hydrocarbon steam reformer;(b) introducing hydrocarbon fuel and air into one or more cylinders of the engine;(c) operating the engine such that internal combustion occurs in one or more cylinders of the engine and generating an untreated exhaust gas in one or more cylinders of the engine and expelling said untreated exhaust gas from said one or more cylinders wherein the untreated exhaust gas contains: (1) unreacted hydrocarbon fuel and water; or (2) water and no hydrocarbon fuel;(d) determining a level of hydrocarbon in said untreated exhaust gas with a hydrocarbon sensor;(e) based on said level of hydrocarbon determined by said hydrocarbon sensor, i) in the case that the untreated exhaust gas contains unreacted hydrocarbon and water, optionally introducing additional hydrocarbon to the untreated exhaust gas and ii) when said untreated exhaust gas contains water and no hydrocarbon, introducing hydrocarbon to the untreated exhaust gas to provide a treated exhaust gas, wherein both the untreated and treated exhaust gas contain hydrocarbon and water,wherein said level of hydrocarbon is set in the range of 1.0% to 5.0% by volume;(f) introducing the untreated and/or treated exhaust gas into the hydrocarbon steam reformer and reacting the hydrocarbon and water in the untreated and/or treated exhaust gas in the presence of the steam reformation catalyst at a temperature of 400° C. to 800° C. and outputting an exhaust gas containing increased levels of carbon monoxide and hydrogen, and wherein said hydrogen in said exhaust gas output after said reaction in said water gas shift reformer is at a level of 2.0% by volume to 10.0% by volume;(g) introducing the exhaust gas output from step (e) to said water gas shift reformer and reacting the carbon monoxide and water in said exhaust gas output in the presence of the water gas shift catalyst and forming carbon dioxide and hydrogen; and(h) introducing said exhaust gas output to said intake manifold of said engine. 2. The method of claim 1 wherein the hydrogen gas in said untreated exhaust gas is at a level of 0.1% by volume to 6% by volume. 3. The method of claim 1 wherein said steam reformation catalyst in said hydrocarbon steam reformer is maintained at said temperature of 400° C. to 800° C. exclusively by generation of heat from said internal combustion engine. 4. The method of claim 1 wherein said engine includes a cylinder block and said hydrocarbon steam reformer is positioned at a distance of 3.0 inches to 24.0 inches from said cylinder block. 5. The method of claim 1 wherein operating the engine such that internal combustion occurs in one or more cylinders of the engine further comprises operating the engine such that at least one of the cylinders of the engine is a dedicated exhaust gas recirculation (D-EGR) cylinder. 6. The method of claim 1 wherein expelling the untreated exhaust gas from the cylinders of the engine includes expelling the untreated exhaust gas from the dedicated exhaust gas recirculation cylinder and the untreated exhaust gas expelled from the dedicated exhaust gas recirculation cylinder is introduced to said hydrocarbon steam reformer followed by said water gas shift reformer. 7. The method of claim 1 wherein at least one cylinder of said internal combustion engine is a dedicated exhaust gas recirculation (D-EGR) cylinder, wherein 90% to 100% by volume of the exhaust gas expelled from the dedicated EGR cylinder is recirculated in said exhaust gas recirculation pathway containing said hydrocarbon steam reformer and said water gas shift reformer connected in series. 8. The method of claim 1 wherein said internal combustion engine includes a turbine and said exhaust gas recirculation pathway comprises a high-pressure exhaust gas recirculation system wherein a portion of said exhaust gas is taken upstream of the turbine and said exhaust gas is recirculated. 9. The method of claim 1 wherein said internal combustion engine includes a turbine and said exhaust gas recirculation pathway comprises a low-pressure exhaust recirculation system wherein a portion of said exhaust gas is taken downstream of the turbine and said exhaust gas is recirculated. 10. The method of claim 1 wherein said hydrocarbon fuel comprises methane and said water gas shift reaction comprises: CH4+H2O→CO+3H2. 11. The method of claim 10 wherein said steam reformation catalyst is at a temperature of 500° C. to 800° C. 12. The method of claim 11 wherein said temperature of 500° C. to 800° C. is maintained exclusively by generation of heat from said internal combustion engine. 13. The method of claim 1 wherein said water gas shift reaction is conducted at a temperature of 300° C. to 500° C.