Enhancing efficiencies of oxy-combustion power cycles
A variety of methods and systems are disclosed, including, in one embodiment, a method including introducing fuel and oxygen into a solid oxide fuel cell to generate electric current, a fuel cell oxygen effluent, and a fuel cell exhaust; combusting combustion fuel and an oxygen source in the presence of a working fluid to generate heat and a combustion exhaust, wherein the working fluid comprises carbon dioxide; heating the solid oxide fuel cell with the heat generated by combustion; generating additional electric current from the combustion exhaust with at least one turbine; separating the combustion exhaust to form a carbon dioxide enriched stream and a water enriched stream; and recycling at least a portion of the carbon dioxide enriched stream as the working fluid.
1. A method comprising:
introducing fuel and oxygen into a solid oxide fuel cell to generate electric current, a fuel cell oxygen effluent, and a fuel cell exhaust;
combusting combustion fuel and oxygen of an oxygen source in the presence of a working fluid to generate heat and a combustion exhaust, wherein the working fluid comprises carbon dioxide;
heating the solid oxide fuel cell with the heat generated by combustion;
generating additional electric current from the combustion exhaust with at least one turbine;
separating the combustion exhaust to form a carbon dioxide enriched stream and a water enriched stream;
recycling at least a portion of the carbon dioxide enriched stream as the working fluid; and
generating electric potential between a heat source and a heat sink with one or more thermoelectric generators.
2. The method of claim 1 , further comprising inducing a phase change in one or more phase change materials.
3. The method of claim 2 , wherein the phase change material has a phase change temperature from about 300° C. to about 900° C.
4. The method of claim 2 , wherein the inducing of the phase change material comprises heating the one or more phase change materials with heat from the combustion exhaust or a turbine exhaust.
5. The method of claim 1 , wherein the heat source comprises the combustion exhaust, the fuel cell exhaust, the solid oxide fuel cell, or a combustor.
6. The method of claim 1 , further comprising removing part of the carbon dioxide enriched stream for sequestration, subsurface geological storage, or utilization.
7. The method of claim 6 , wherein the portion of the carbon dioxide enriched stream is pipeline grade carbon dioxide.
8. The method of claim 1 , wherein the oxygen is present in the oxygen source in a concentration from about 90 wt. % to about 100 wt. % by weight of the oxygen source.
9. The method of claim 1 , wherein the combustion fuel comprises hydrogen generated by hydrolysis of water.
10. The method of claim 1 , wherein the oxygen is generated, at least in part, by hydrolysis of water.
11. The method of claim 1 , wherein the combustion fuel comprises the fuel cell exhaust.
12. A system comprising:
a solid oxide fuel cell;
a combustor fluidically coupled to the solid oxide fuel cell;
a turbine directly coupled to the combustor and in thermal communication with the solid oxide fuel cell;
a recuperator energetically coupled to a turbine exhaust of the turbine;
a separator fluidically coupled to the recuperator, wherein the separator is operable to separate carbon dioxide and water;
a first thermoelectric generator in thermal communication with the separated carbon dioxide;
a second thermoelectric generator in thermal communication with the solid oxide fuel cell; and
one or more phase change material in thermal communication with an exhaust.
13. The system of claim 12 , wherein at least one of the thermoelectric generators is in thermal communication with at least one system component selected from the group consisting of the solid oxide fuel cell, the combustor, the turbine, the separator, and any combination thereof.
14. The system of claim 12 , wherein the solid oxide fuel cell, the combustor, or both are in fluidic communication with an oxygen source comprising oxygen in an amount from about 90 wt. % to about 100 wt. %.
15. The system of claim 12 , wherein at least one phase change material is in thermal communication with at least one system component selected from the group consisting of the solid oxide fuel cell, the combustor, the turbine, the separator, and any combination thereof.
16. The system of claim 15 , wherein at least one of the one or more phase change materials has a phase change temperature between about 300° C. and about 900° C.
17. The system of claim 12 , wherein the solid oxide fuel cell, the combustor, or both are in fluidic communication with a fuel source.
18. The system of claim 17 , wherein the fuel source comprises at least one fuel selected from the group consisting of natural gas, coal, hydrogen, propane, methane, butane, pentane, coal gas, liquefied petroleum gas, light fuel oil, heavy fuel oil, solid fuel, gaseous fuel, carbonaceous fuel, kerosene, gasoline, diesel fuel, naphtha, biodiesel, ethanol, charcoal, lignite, petroleum coke, natural gas, compressed natural gas, liquified natural gas, blast furnace gas, coke oven gas, water gas, methanol, nitromethane, jet fuel, JET-A, JP-8, biofuel, syngas, biogas, green hydrogen, pink hydrogen, blue hydrogen, and any combination thereof.