INTEGRATED POWER GENERATION AND CHEMICAL PRODUCTION USING FUEL CELLS
In various aspects, systems and methods are provided for operating a molten carbonate fuel cell to reduce or minimize losses due to loss of heat energy. A molten carbonate fuel cell can be operated based on a desired ratio of heat generated by exothermic reactions in the fuel cell relative to heat consumed by endothermic reactions in the fuel cell and any optional integrated endothermic reaction stages.
1 . A method for producing electricity, and hydrogen or syngas, using a molten carbonate fuel cell, the method comprising:
introducing an anode fuel stream comprising reformable fuel into an anode inlet of an anode of a molten carbonate fuel cell;
introducing a cathode inlet stream comprising CO 2 and O 2 into a cathode inlet of a cathode of the molten carbonate fuel cell;
operating the molten carbonate fuel cell to generate electricity at a thermal ratio of about 1.3 or less;
generating an anode exhaust from an anode outlet of the molten carbonate fuel cell; and
separating from the anode exhaust a hydrogen-containing stream, a syngas-containing stream, or a combination thereof.
2 . The method of claim 1 , wherein a CO 2 utilization of the cathode is at least about 50%.
3 . The method of claim 1 , wherein the molten carbonate fuel cell comprises a fuel cell stack.
4 . The method of claim 1 , wherein the molten carbonate fuel cell further comprises one or more integrated endothermic reaction stages.
5 . The method of claim 4 , wherein at least one integrated endothermic reaction stage of the one or more integrated endothermic reaction stages comprises an integrated reforming stage, the anode fuel stream introduced into the anode inlet being passed through the integrated reforming stage prior to entering the anode inlet.
6 . The method of claim 1 , wherein the molten carbonate fuel cell is operated at a voltage V A of about 0.67 Volts or less.
7 . The method of claim 1 , further comprising separating at least one of CO 2 and H 2 O from one or a combination of i) the anode exhaust, ii) the hydrogen-containing stream, and iii) the syngas-containing stream.
8 . The method of claim 1 , wherein the thermal ratio is about 1.15 or less.
9 . The method of claim 1 , wherein the thermal ratio is about 1.0 or less.
10 . The method of claim 1 , wherein the thermal ratio is at least about 0.25.
11 . The method of claim 1 , wherein a temperature at the anode outlet is greater than a temperature at the anode inlet by about 40° C. or less.
12 . The method of claim 1 , wherein a temperature at the anode inlet differs from a temperature at the anode outlet by about 20° C. or less.
13 . The method of claim 1 , wherein a temperature at the anode outlet is less than a temperature at the anode inlet by about 10° C. to about 80° C.
14 . The method of claim 1 , wherein the thermal ratio is about 0.85 or less, the method further comprising supplying heat to the molten carbonate fuel cell to maintain a temperature at the anode outlet that is less than a temperature at the anode inlet by about 5° C. to about 50° C.
15 . The method of claim 1 , wherein less than 10 vol % of H 2 produced in the anode of the molten carbonate fuel cell in a single pass is directly or indirectly recycled to the anode of the molten carbonate fuel cell or the cathode of the molten carbonate fuel cell.
16 . The method of claim 1 , wherein less than 10 vol % of the syngas-containing stream is directly or indirectly recycled to the anode of the molten carbonate fuel cell or the cathode of the molten carbonate fuel cell.
17 . The method of claim 1 , wherein less than 10 vol % of the anode exhaust is directly or indirectly recycled to the anode of the molten carbonate fuel cell or the cathode of the molten carbonate fuel cell.
18 . The method of claim 1 , wherein no portion of the anode exhaust is directly or indirectly recycled to the anode of the molten carbonate fuel cell, directly or indirectly recycled to the cathode of the molten carbonate fuel cell, or a combination thereof.
19 . The method of claim 1 , wherein the syngas-containing stream has a molar ratio of H 2 to CO of about 3.0:1 to about 1.0:1.
20 . The method of claim 1 , wherein the anode exhaust has a molar ratio of H 2 to CO of about 1.5:1 to about 10:1.
21 . The method of claim 20 , wherein the anode exhaust has a molar ratio of H 2 to CO of at least about 3.0:1.