Integrated electrical power and chemical production using fuel cells
US-2016351931-A1 · Dec 1, 2016 · US
US11831057B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11831057-B2 |
| Application number | US-201917416334-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 18, 2019 |
| Priority date | Dec 18, 2018 |
| Publication date | Nov 28, 2023 |
| Grant date | Nov 28, 2023 |
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A method of integrating a fuel cell with a steam methane reformer is provided. The system includes at least one fuel cell including an anode and a cathode, and a steam methane reformer including a syngas stream, and a flue gas stream. The method includes introducing at least a portion of the flue gas stream to the cathode, thereby producing a CO2 depleted flue gas stream and introducing a hydrocarbon containing stream to the anode, thereby producing an electrical energy output and a carbon dioxide and hydrogen containing stream from the fuel cell.
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What is claimed is: 1. A method of integrating a fuel cell with a steam methane reformer, comprising; at least one fuel cell 100 comprising an anode 104 and a cathode 103 , a steam methane reformer 114 comprising a syngas stream 305 , and a flue gas stream 101 , the method comprising; a) introducing at least a portion of the flue gas stream 101 to the cathode 103 , thereby producing a CO2 depleted flue gas stream 112 b) introducing a hydrocarbon containing stream 303 to the anode 104 , thereby producing an electrical energy output 107 and a carbon dioxide and hydrogen containing stream 307 from the fuel cell 100 , c) separating a hydrogen-rich stream 306 from the carbon dioxide and hydrogen containing stream 307 , thereby producing a carbon dioxide rich stream 111 , d) combining the hydrogen-rich stream 306 with the syngas stream 305 , thereby producing a combined syngas stream, and e) introducing the combined syngas stream into a hydrogen separation device 115 , thereby producing a second high purity hydrogen stream 116 . 2. The method of claim 1 , wherein the hydrocarbon containing stream 303 is natural gas. 3. The method of claim 1 , wherein the hydrocarbon containing stream is desulfurized prior to introduction into the anode 104 . 4. The method of claim 1 , wherein the carbon dioxide and hydrogen containing stream 307 passes through a water-gas shift reactor 108 between steps b) and c). 5. The method of claim 1 , wherein the syngas stream 305 has passed through a water-gas shift reactor 108 prior to step d).
Reforming processes, e.g. autothermal, partial oxidation or steam reforming · CPC title
followed by reaction of water vapour with carbon monoxide · CPC title
by diffusion · CPC title
Direct internal reforming at the anode of the fuel cell · CPC title
Removal of carbon monoxide or carbon dioxide · CPC title
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