System and method for increasing a carbon monoxide content of syngas produced by a steam methane reformer
US-2019224641-A1 · Jul 25, 2019 · US
US12476267B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12476267-B2 |
| Application number | US-202418417088-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 19, 2024 |
| Priority date | Sep 16, 2020 |
| Publication date | Nov 18, 2025 |
| Grant date | Nov 18, 2025 |
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A fuel cell system includes a fuel cell stack having a plurality of fuel cells that each contain a plurality of fuel electrodes and air electrodes. The system includes a fuel receiving unit connected to the fuel cell stack, which receives a hydrocarbon fuel from a fuel supply. The system includes a fuel exhaust processing unit fluidly coupled to the fuel cell stack by a slip stream, where the fuel exhaust processing unit processes fuel exhaust from the fuel cell stack, and the slip stream is fluidly connected to an exhaust stream flowing from the fuel cell stack. The fuel processing unit removes a first portion of carbon dioxide (CO 2 ) from fuel exhaust within the slip stream, outputs the first portion of CO 2 in a first stream, and outputs a second portion of CO 2 remaining from the fuel exhaust in the slip stream into a second stream, which includes hydrogen.
Opening claim text (preview).
What is claimed is: 1 . A method of extracting carbon dioxide in a fuel cell system, the method comprising: receiving, by a first fluid pathway, fuel exhaust from fuel electrodes of a fuel cell stack, the fuel cell stack comprising a plurality of fuel cells, the plurality of fuel cells comprising air electrodes and the fuel electrodes; receiving, by a second fluid pathway, a first portion of the fuel exhaust from the first fluid pathway; receiving, by a third fluid pathway, a second portion of the fuel exhaust from the first fluid pathway; receiving, by a carbon processing unit, the first portion of the fuel exhaust from the second fluid pathway; removing, by the carbon processing unit, a first portion of carbon dioxide (CO 2 ) from the first portion of the fuel exhaust; outputting, by the carbon processing unit, a remainder of the first portion of the fuel exhaust containing a second portion of CO 2 and hydrogen; receiving, by an air combination unit, the second portion of the fuel exhaust from the third fluid pathway; combining, by the air combination unit, the second portion of the fuel exhaust with air; and providing, by the air combination unit, a mixture of the second portion of the fuel exhaust to the air electrodes within the fuel cell stack. 2 . The method of claim 1 , further comprising exporting, by the carbon processing unit, the first portion of CO 2 . 3 . The method of claim 1 , further comprising recycling the remainder of the first portion of the fuel exhaust to a fuel exhaust stream. 4 . The method of claim 1 , further comprising recycling CO 2 from an air exhaust of the air electrodes through a fluid pathway coupled to the fuel electrodes. 5 . The method of claim 1 , further comprising: receiving, by the air combination unit, air from an ambient air supply; and reacting, by a heater within the air combination unit, residual hydrogen within the remainder of the first portion of the fuel exhaust with the air from the ambient air supply to produce a heated mixture. 6 . The method of claim 5 , further comprising circulating, by the air combination unit, the heated mixture containing reacted fuel exhaust and air to the air electrodes. 7 . The method of claim 1 , further comprising extracting water from the first portion of the fuel exhaust. 8 . The method of claim 1 , further comprising controlling an amount of the first portion of the fuel exhaust within the first fluid pathway. 9 . The method of claim 8 , wherein controlling the amount of the first portion of the fuel exhaust is responsive to at least one operational mode of the fuel cell system. 10 . The method of claim 8 , wherein controlling the amount of the first portion of the fuel exhaust is carried out in real time based on a CO 2 demand. 11 . The method of claim 8 , wherein controlling the amount of the first portion of the fuel exhaust comprises controlling flow of the first portion of the fuel exhaust using at least one of a fan or blower. 12 . The method of claim 8 , wherein controlling the amount of the first portion of the fuel exhaust comprises controlling at least one of a vent or valve. 13 . The method of claim 8 , wherein the amount of the first portion of the fuel exhaust within the first pathway is up to 40% of the fuel exhaust. 14 . The method of claim 7 , wherein extracting water from the first portion of the fuel exhaust comprises cooling, by a cooling component within the carbon processing unit, the first portion of the fuel exhaust. 15 . The method of claim 7 , wherein extracting water from the first portion of the fuel exhaust comprises condensing, by a condenser within the carbon processing unit, the first portion of the fuel exhaust. 16 . The method of claim 1 , wherein removing the first portion of carbon dioxide (CO 2 ) from the first portion of the fuel exhaust is carried out by a plurality of membranes within the carbon processing unit. 17 . The method of claim 1 , wherein the first portion of carbon dioxide (CO 2 ) from the first portion of the fuel exhaust is removed in liquid form. 18 . The method of claim 1 , wherein the first portion carbon dioxide (CO 2 ) from the first portion of the fuel exhaust is removed in gaseous form. 19 . The method of claim 9 , further comprising receiving an input corresponding to a user selection indicating the at least one operational mode. 20 . The method of claim 1 , further comprising, removing H 2 from the first portion of the fuel exhaust.
Direct internal reforming at the anode of the fuel cell · CPC title
comprising carbonates · CPC title
Fuel cells with molten carbonates · CPC title
of fuel cell exhausts · CPC title
Fuel cells · CPC title
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