Carbon dioxide conversion to hydrocarbon fuel via syngas production cell harnessed from solar radiation

1. A process for converting carbon dioxide to hydrocarbon fuels using solar energy, the process comprising the steps of:

receiving direct sunlight with a plurality of heliostats and reflecting the direct sunlight from the heliostats as reflected sunlight onto a tower receiver, wherein the reflected sunlight heats a heat transfer fluid in the tower receiver;

converting a water stream to a generated steam stream in a steam generator, wherein the heat transfer fluid provides heat to the steam generator;

feeding the generated steam stream to a steam turbine, wherein the steam turbine converts thermal energy in the generated steam stream to mechanical energy to drive an electric generator to generate electricity;

heating a fuel feed stream by transferring thermal energy from the heat transfer fluid to create a heated fuel feed stream, such that the heated fuel feed stream reaches a temperature of between 650° C. and 800° C.;

feeding the heated fuel feed stream to a syngas production cell, wherein the heated fuel feed stream comprises carbon dioxide and water, wherein the carbon dioxide is captured from a fuel gas stream, wherein the syngas production cell comprises a solid oxide electrolyzer cell, wherein the solid oxide electrolyzer cell comprises a porous cathode, the solid oxide electrolyte, and a porous anode;

converting the carbon dioxide and water in the heated fuel feed stream to carbon monoxide and hydrogen in the syngas production cell to produce a syngas stream, wherein the syngas production cell comprises a solid oxide electrolyte;

feeding the syngas stream to a catalytic reactor, wherein the catalytic reactor operates in the presence of a catalyst; and

converting the syngas stream to a hydrocarbon fuel stream in the catalytic reactor.

2. The process as claimed in claim 1 , wherein the step of converting the carbon dioxide and water in the heated fuel feed stream to carbon monoxide and hydrogen in the syngas production cell further comprises the steps of:

supplying the electricity to the porous cathode of the solid oxide electrolyzer cell;

contacting the porous cathode with the heated fuel feed stream;

reducing the carbon dioxide to create carbon monoxide and oxygen ions, wherein the oxygen ions pass through the porous cathode to the solid oxide electrolyte;

reducing the water to create hydrogen and oxygen ions, wherein the oxygen ions pass through the porous cathode to the solid oxide electrolyte;

diffusing the oxygen ions through the solid oxide electrolyte to the porous anode; and

releasing electrons from the oxygen ions at the porous anode, such that oxygen molecules are formed to create an oxygen stream.

3. The process as claimed in claim 1 , further comprising the step of:

feeding the hydrocarbon fuel to a power plant for consumption.

4. A process for converting carbon dioxide to hydrocarbon fuels using solar energy, the process comprising the steps of:

receiving direct sunlight with a plurality of heliostats and reflecting the direct sunlight from the heliostats as reflected sunlight onto a tower receiver, wherein the reflected sunlight heats a heat transfer fluid in the tower receiver;

converting a water stream to a generated steam stream in a steam generator, wherein the heat transfer fluid provides heat to the steam generator;

feeding the generated steam stream to a steam turbine, wherein the steam turbine converts thermal energy in the generated steam stream to mechanical energy to drive an electric generator to generate electricity;

heating a fuel feed stream by transferring thermal energy from the heat transfer fluid to create a heated fuel feed stream, such that the heated fuel feed stream reaches a temperature of between 650° C. and 800° C.;

feeding the heated fuel feed stream to a syngas production cell, wherein the heated fuel feed stream comprises carbon dioxide and water, wherein the carbon dioxide is captured from a fuel gas stream, wherein the syngas production cell comprises a solid oxide electrolyzer cell, wherein the solid oxide fuel cell comprises a porous anode, the solid oxide electrolyte, and a porous cathode;

converting the carbon dioxide and water in the heated fuel feed stream to carbon monoxide and hydrogen in the syngas production cell to produce a syngas stream, wherein the syngas production cell comprises a solid oxide electrolyte;

feeding the syngas stream to a catalytic reactor, wherein the catalytic reactor operates in the presence of a catalyst; and

converting the syngas stream to a hydrocarbon fuel stream in the catalytic reactor.

5. The process as claimed in claim 4 , wherein the step of converting the carbon dioxide and water in the heated fuel feed stream to carbon monoxide and hydrogen in the syngas production cell further comprises the steps of:

adding a gaseous hydrocarbon to the heated fuel feed stream;

feeding the heated fuel feed stream to the porous anode of the solid oxide fuel cell;

reforming the water and the gaseous hydrocarbon in the heated fuel feed stream to create carbon monoxide and hydrogen;

reforming the carbon dioxide and the gaseous hydrocarbon in the heated fuel feed stream to create carbon monoxide and hydrogen;

reducing oxygen from an oxygen supply on the porous cathode of the solid oxide fuel cell to generate oxygen ions;

diffusing the oxygen ions through the solid oxide electrolyte to the porous anode;

oxidizing the hydrogen at the porous anode with the oxygen ions to create water and electrons;

oxidizing the methane at the porous anode with the oxygen ions to create carbon monoxide, hydrogen, and electrons; and

supplying the electrons to an electrical substation, wherein the electrical substation is configured to combine the electrons from the syngas production cell with the electricity generated by the electric generator.

6. The process as claimed in claim 5 , wherein the gaseous hydrocarbon comprises methane.