Continuous reforming of diesel fuel for NOx reduction
Raw diesel fuel is reformed to produce partially oxygenated hydrocarbons in the liquid fuel by use of a nonthermal plasma reactor. The reformed diesel fuel is formed by passing a stream of air plasma bubbles through a liquid volume of diesel fuel to strip low molecular weight hydrocarbons from the fuel, while partially oxygenating an abundance of them as a reformate for addition to the exhaust. This reformed diesel fuel is introduced as a sidestream into the exhaust of a diesel engine or other lean-burn power plants as reactants for selective catalytic reduction of nitrogen oxides in the exhaust. Fresh fuel is added to the liquid volume as diesel reformate is stripped from it, and a portion of the stripped fuel is withdrawn from the liquid volume.
1. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides in the exhaust of a lean burn engine or power plant, the method comprising:
continually delivering diesel fuel comprising hydrocarbons to a reformer vessel to maintain a liquid volume of the fuel in the vessel;
bubbling a stream of air plasma up through the liquid volume of fuel to reform some fuel hydrocarbons into oxygenated hydrocarbons and to continually strip oxygenated hydrocarbons and a portion of the fuel hydrocarbons from the liquid volume of fuel into the air plasma;
removing the air plasma stream comprising oxygenated hydrocarbons and fuel hydrocarbons from the vessel and conducting the oxygenated hydrocarbon-containing air plasma stream into exhaust of the lean burn power plant, and
removing stripped diesel fuel from the volume of fuel in the vessel.
2. A method of producing oxygenated hydrocarbons as recited in claim 1 further comprising subjecting the oxygenated hydrocarbon-containing exhaust to a reduction catalyst for reduction of nitrogen oxides by reaction with oxygenated hydrocarbons.
3. A method of producing oxygenated hydrocarbons as recited in claim 1 in which the diesel fuel delivered to the reformer vessel is seeded with an oxygenated hydrocarbon to produce oxygenated hydrocarbons in greater abundance than the seeded amount.
4. A method of producing oxygenated hydrocarbons as recited in claim 1 in which the diesel fuel delivered to the reformer vessel is seeded with ethanol to produce oxygenated hydrocarbons in greater abundance than the seeded amount.
5. A method of producing oxygenated hydrocarbons as recited in claim 1 , further comprising:
generating the air plasma by passing a stream of air through nonthermal alternating passive and active electric fields for the generation of the plasma reactor output stream; and
bubbling a stream of the air plasma up through a liquid volume of fuel.
6. A method of producing oxygenated hydrocarbons as recited in claim 1 further comprising:
generating the air plasma by passing a stream of air through a non-thermal plasma reactor, wherein the non-thermal plasma reactor is a tubular vessel having a reactor space therein for flow-through passage of air, the plasma reactor comprising a high voltage electrode disposed within said reactor space and a ground electrode helically coiled around said tubular vessel in a discretely spaced pattern, thereby providing intertwined helical passive and active electric fields for the generation of the plasma reactor output stream; and
bubbling a stream of the air plasma up through the liquid volume of fuel.
7. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides as recited in claim 1 further comprising:
controlling the rate of delivery of diesel fuel to the reformer vessel to control the amount or composition of oxygenated hydrocarbons in the air plasma stream removed from the reformer vessel.
8. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides as recited in claim 1 and further comprising:
controlling the flow rate of air plasma through the liquid volume of fuel to control the amount or composition of oxygenated hydrocarbons in the air plasma stream removed from the reformer vessel.
9. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides as recited in claim 1 further comprising controlling the temperature of the liquid volume of fuel to control the amount or composition of oxygenated hydrocarbons in the air plasma removed from the reformer vessel.
10. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides as recited in claim 9 comprising controlling the temperature of the liquid fuel in the range of about 100° C. to about 150° C.
11. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides in the exhaust of a diesel engine powering a vehicle, the vehicle having a reservoir of diesel fuel, the method comprising:
continually delivering diesel fuel comprising hydrocarbons to a reformer vessel on the vehicle to maintain a liquid volume of the fuel in the vessel;
bubbling a stream of air plasma up through the liquid volume of fuel to reform some fuel hydrocarbons into oxygenated hydrocarbons and to continually strip oxygenated hydrocarbons and a portion of the fuel hydrocarbons from the liquid volume of fuel into the air plasma;
removing the air plasma stream comprising oxygenated hydrocarbons and fuel hydrocarbons from the vessel and conducting the oxygenated hydrocarbon-containing air plasma stream into exhaust of the diesel engine, and
removing stripped diesel fuel from the volume of fuel in the vessel and delivering the stripped diesel fuel to the engine for combustion or to the diesel fuel reservoir.
12. A method of producing oxygenated hydrocarbons as recited in claim 11 further comprising subjecting the oxygenated hydrocarbon-containing exhaust to a reduction catalyst for reduction of nitrogen oxides by reaction with oxygenated hydrocarbons.
13. A method of producing oxygenated hydrocarbons as recited in claim 11 in which the diesel fuel delivered to the reformer vessel is seeded with an oxygenated hydrocarbon to produce oxygenated hydrocarbons in greater abundance than the seeded amount.
14. A method of producing oxygenated hydrocarbons as recited in claim 11 in which the diesel fuel delivered to the reformer vessel is seeded with ethanol to produce oxygenated hydrocarbons in greater abundance than the seeded amount.
15. A method of producing oxygenated hydrocarbons as recited in claim 11 , further comprising:
generating the air plasma by passing a stream of air through nonthermal alternating passive and active electric fields for the generation of the plasma reactor output stream; and
bubbling a stream of the air plasma up through a liquid volume of fuel.
16. A method of producing oxygenated hydrocarbons as recited in claim 11 further comprising:
generating the air plasma by passing a stream of air through a non-thermal plasma reactor, wherein the non-thermal plasma reactor is a tubular vessel having a reactor space therein for flow-through passage of air, the plasma reactor comprising a high voltage electrode disposed within said reactor space and a ground electrode helically coiled around said tubular vessel in a discretely spaced pattern, thereby providing intertwined helical passive and active electric fields for the generation of the plasma reactor output stream; and
bubbling a stream of the air plasma up through the liquid volume of fuel.
17. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides as recited in claim 11 further comprising:
controlling the rate of delivery of diesel fuel to the reformer vessel to control the amount or composition of oxygenated hydrocarbons in the air plasma stream removed from the reformer vessel.
18. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides as recited in claim 11 and further comprising:
controlling the flow rate of air plasma through the liquid volume of fuel to control the amount or composition of oxygenated hydrocarbons in the air plasma stream removed from the reformer vessel.
19. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides as recited in claim 11 further comprising controlling the temperature of the liquid volume of fuel to control the amount or composition of oxygenated hydrocarbons in the air plasma removed from the reformer vessel.
20. A method of producing oxygenated hydrocarbons for reduction of nitrogen oxides as recited in claim 19 comprising controlling the temperature of the liquid fuel in the range of about 100° C. to about 150° C.