Reactor with plate-shaped catalytic membrane for direct conversion of microalgae into biofuels
US-2024026387-A1 · Jan 25, 2024 · US
US11866690B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11866690-B2 |
| Application number | US-202017019392-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 14, 2020 |
| Priority date | Sep 13, 2019 |
| Publication date | Jan 9, 2024 |
| Grant date | Jan 9, 2024 |
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A method includes containing an algae media within a contactor, introducing a stream of natural gas comprising up to 80 wt % carbon dioxide (CO 2 ) into the contactor, contacting the natural gas on the algae media and thereby allowing the algae media to consume CO 2 from the natural gas, and discharging a stream of natural gas comprising 2 wt % or less CO 2 from the contactor.
Opening claim text (preview).
The invention claimed is: 1. A method, comprising: containing an algae media within a contactor; introducing a stream of natural gas comprising up to 80 wt % carbon dioxide (CO 2 ) and having a fluid pressure in a range of 500 psig to 2000 psig into the contactor; maintaining the fluid pressure within the contactor in the range; contacting the natural gas on the algae media and thereby allowing the algae media to consume CO 2 from the natural gas; and discharging a stream of natural gas comprising 2 wt % or less CO 2 from the contactor at a fluid pressure in the range into a pressurized pipeline. 2. The method of claim 1 , wherein the contactor comprises an algae photobioreactor. 3. The method of claim 1 , wherein containing the algae media within the contactor comprises: circulating the algae media into the contactor from an algae photobioreactor; and returning the algae media to the algae photobioreactor after contacting the natural gas on the algae media within the contactor. 4. The method of claim 3 , wherein the algae photobioreactor comprises an enclosed reactor. 5. The method of claim 1 , further comprising conveying the stream of natural gas discharged from the contactor to a power plant for combustion. 6. The method of claim 1 , further comprising: generating oxygen (O 2 ) with the algae media; stripping at least a portion of the O 2 with the natural gas within the contactor and thereby discharging a stream of natural gas enriched with O 2 from the contactor; and using the stream of natural gas enriched with O 2 in an oxygen-requiring process. 7. The method of claim 6 , wherein the oxygen-requiring process comprises at least one of syngas production and oxycombustion for power production. 8. A method, comprising: introducing a stream of natural gas having a fluid pressure in a range of 500 psig to 2000 psig into an algae photobioreactor (PBR) containing an algae media; generating oxygen (O 2 ) with the algae media; stripping at least a portion of the O 2 with the natural gas within the PBR; discharging a stream of natural gas enriched with O 2 from the PBR at the fluid pressure in the range; and using the stream of natural gas enriched with O 2 in an oxygen-requiring process. 9. The method of claim 8 , wherein the natural gas comprises up to 80 wt % carbon dioxide (CO 2 ), and wherein generating the O 2 with the algae media comprises: contacting the natural gas on the algae media; and consuming at least a portion of the CO 2 from the natural gas with the algae media. 10. The method of claim 8 , wherein using the stream of natural gas enriched with O 2 in an oxygen-requiring process comprises: conveying the stream of natural gas enriched with O 2 to a combustion power plant; and combusting the stream of natural gas enriched with O 2 in the combustion power plant to generate power. 11. The method of claim 8 , wherein using the stream of natural gas enriched with O 2 in an oxygen-requiring process comprises: conveying the stream of natural gas enriched with O 2 to a partial oxidation system; and generating a syngas product in the partial oxidation system with the stream of natural gas enriched with O 2 . 12. The method of claim 8 , wherein the algae photobioreactor comprises an enclosed reactor. 13. The method of claim 8 , wherein using the stream of natural gas enriched with O 2 in an oxygen-requiring process is preceded by dehydrating the stream of natural gas enriched with O 2 . 14. A method, comprising: introducing a stream of a high-carbon dioxide (CO 2 ) concentration gas with a fluid pressure in a range of 500 psig to 2000 psig into a contactor containing an algae media, wherein the high-CO 2 concentration gas comprising at a natural gas having up to 80 wt % CO 2 ; contacting the high-CO 2 concentration gas on the algae media and thereby allowing the algae media to consume CO 2 from the high-CO 2 concentration gas; and discharging a stream of gas comprising 2 wt % or less CO 2 from the contactor at the fluid pressure in a range of 500 psig to 2000 psig into a pressurized pipeline. 15. The method of claim 14 , wherein the contactor comprises an algae photobioreactor. 16. The method of claim 14 , wherein containing the algae media within the contactor comprises: circulating the algae media into the contactor from an algae photobioreactor; and returning the algae media to the algae photobioreactor after contacting the natural gas on the algae media within the contactor. 17. The method of claim 14 , further comprising conveying the stream of gas discharged from the contactor to a power plant for combustion. 18. The method of claim 14 , further comprising: generating oxygen (O 2 ) with the algae media; stripping at least a portion of the O 2 with the high-CO 2 concentration gas within the contactor and thereby discharging a stream of gas enriched with O 2 from the contactor; and using the stream of gas enriched with O 2 in an oxygen-requiring process.
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