Method for producing gasoline alternative fuel and gasoline alternative fuel
US-2024043753-A1 · Feb 8, 2024 · US
US9567268B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9567268-B2 |
| Application number | US-201414316113-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 26, 2014 |
| Priority date | Jun 28, 2013 |
| Publication date | Feb 14, 2017 |
| Grant date | Feb 14, 2017 |
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A quench system and process for cooling high temperature gases is presented. The quench system includes a frustum, or conic, shaped section having an inlet at the smaller end of the quench section and the outlet at the larger end of the quench section. The system includes spray nozzles having openings flush with the wall of the quench section. The process includes spraying a large volume of liquid in small droplets for rapid heat transfer and vaporization of the quench liquid.
Opening claim text (preview).
The invention claimed is: 1. A quench system for high temperature reactor flows, comprising: a quench section having a frustum shape with an inlet, an outlet, and quench section wall; and a plurality of nozzles embedded in the quench section wall; wherein the inlet is at a first end of the frustum shaped quench section and the outlet is at a second end of the frustum shaped quench section, wherein the second end is the same size or larger than the first end, and wherein the quench section has a regular polygonal cross-section, and wherein the nozzles each have an outlet that is flush with the quench section wall, and wherein the quench section has a central axis, and the plurality of nozzles is distributed circumferentially around the quench section wall, and disposed within at least two circular sections where each circular section is oriented perpendicular to the quench section central axis. 2. The quench system of claim 1 wherein the plurality of nozzles comprises several nozzles, with each nozzle comprising a continuous nozzle having an arc length around the circumference and an angle greater than 10 degrees. 3. The quench system of claim 1 further comprising an inlet section is sized and shaped to meld smoothly with a reactor outlet section. 4. The quench system of claim 1 wherein the cross-section of the quench section comprises a regular polygonal shape having at least 6 sides. 5. The quench system of claim 4 wherein the cross-section of the quench section comprises a regular polygonal shape having at least 10 sides. 6. The quench system of claim 1 wherein the cross-section of the quench section comprises a circular shape. 7. The quench system of claim 1 wherein the quench section has a central axis, and the plurality of nozzles comprises at least 4 that lie in a plane that is perpendicular to the central axis of the quench section. 8. The quench system of claim 1 wherein the plurality of nozzles is between 8 and 32 nozzles. 9. The quench system of claim 1 wherein the nozzles are spaced radially around the circumference of the quench section between 15 and 45 degrees. 10. The quench system of claim 1 wherein the plurality of nozzles are distributed circumferentially around the quench section wall, and are disposed in the first half of the quench section from the inlet of the quench section. 11. The quench system of claim 10 wherein the plurality of nozzles are disposed within the first quarter section of the quench section from the inlet. 12. The quench system of claim 1 wherein the at least two circular sections are a first circular section and a second circular section, and the nozzles disposed within the second circular section are offset circumferentially relative to the nozzles disposed within the first circular section. 13. The quench system of claim 1 wherein at least one nozzle of the plurality of nozzles has a shaped orifice for generating a spray having an angle between 30 and 120 degrees. 14. The quench system of claim 1 wherein in at least one nozzle of the plurality of nozzles include an atomizer. 15. The quench system of claim 1 wherein the ratio of the area of the cross-section of the quench section at the outlet to the area of the cross-section of the quench section at the inlet is at least 2. 16. The quench system of claim 1 wherein the length of the quench section to the inlet diameter is a ratio of between 5 and 10.
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