Method And System For Converting A Methane Gas To A Liquid Fuel
A method for converting a methane gas to liquid fuel forms a non-thermal plasma with radicals and directs the plasma over a catalyst to convert the radicals to higher hydrocarbons in liquid form. The method can be performed in a reactor such as a microwave plasma reactor, or a pulsed corona discharge plasma reactor. A system for performing the method includes a methane gas source, a reactant gas source, a reactor and a catalyst.
1 . A method for converting a methane gas to a liquid fuel comprising:
providing a reactor having a reaction chamber;
providing a flow of methane gas and a flow of a reactant gas into the reaction chamber;
providing a catalyst in the reaction chamber;
producing a non-thermal plasma in the reaction chamber to convert the methane gas and the reactant gas into radicals; and
directing the radicals over the catalyst to couple the radicals into hydrocarbons in liquid form.
2 . The method of claim 1 further comprising controlling production of the radicals and coupling of the radicals into the hydrocarbons by controlling the flow rate of the methane gas, the flow rate of the reactant gas, a forward power of the plasma, and a frequency of the plasma.
3 . The method of claim 1 wherein the providing the catalyst step comprises selecting, preparing and dispersing the catalyst to optimize the production of the radicals.
4 . The method of claim 1 wherein the reactor comprises a microwave plasma reactor or a pulsed corona discharge plasma reactor.
5 . The method of claim 1 wherein the methane gas comprises natural gas or bio gas.
6 . The method of claim 1 wherein the radicals comprise C x H y * radicals.
7 . The method of claim 1 wherein the liquid fuel comprises methanol, gasoline (C 5 to C 12 ) or diesel (over C 10 to C 15 ).
8 . The method of claim 1 wherein the flow of the reactant gas comprises CO 2 , O 2 and H 2 O.
9 . The method of claim 1 wherein the catalyst comprises a Co-based catalyst or an Fe-based catalyst.
10 . A method for converting a methane gas to a liquid fuel comprising:
providing a reactor having a reaction chamber;
providing a flow of a methane gas and a flow of reactant gas into the reaction chamber, the reactant gas comprising CO 2 , H 2 O, O 2 or combinations thereof with the flow of the methane gas and the flow of the reactant gas in a ratio selected to provide the liquid fuel with a desired chemical composition;
providing a catalyst in the reaction chamber comprising a Co-based catalyst or an Fe-based catalyst;
producing a non-thermal plasma in the reaction chamber to convert the methane gas and the reactant gas into selected C x H y * radicals;
directing the radicals over the catalyst to couple the radicals into hydrocarbons in liquid form; and
controlling production of the radicals and coupling of the radicals into the hydrocarbons by controlling the flow rate of the methane gas, the flow rate of the reactant gas, a forward power of the plasma, and a frequency of the plasma.
11 . The method of claim 9 further comprising following the directing step, recycling unreacted gases back into the reaction chamber.
12 . The method of claim 9 wherein the flow of the methane gas and the flow of the reactant gas are combined in a ratio to provide the liquid fuel in the form of methanol, gasoline (C 5 to C 12 ) or diesel (over C 10 to C 15 ).
13 . The method of claim 9 wherein a combined flow rate of the methane gas and the reactant gas is from 100-1000 ml/min.
14 . The method of claim 9 wherein the power is from 100-1000 Watts.
15 . The method of claim 9 wherein a pressure in the reaction chamber is from 10-2200 mm Hg.
16 . A system for converting a methane gas to a liquid fuel comprising:
a methane gas source configured to provide a methane gas flow;
a reactant gas source configured to provide a reactant gas flow;
a reactor connected to the methane gas source and the reactant gas source configured to form a non-thermal plasma and produce radicals; and
a catalyst configured to contact the radicals to produce reactions for coupling the radicals into hydrocarbons in liquid form.
17 . The system of claim 16 wherein the reactor comprises a microwave plasma reactor or a pulsed corona discharge plasma reactor.
18 . The system of claim 17 wherein the methane gas comprises natural gas or bio gas.
19 . The system of claim 18 wherein the reactant gas comprises CO 2 , H 2 O, O 2 and combinations thereof with the flow of the methane gas and the flow of the reactant gas in a ratio selected to provide the liquid fuel with a desired chemical composition.
20 . The system of claim 19 wherein the radicals comprise C x H y * radicals.
21 . The system of claim 20 wherein the catalyst comprises a Co-based catalyst or an Fe-based catalyst.