Method for decoupled thermo-catalytic pollution control
First Claim
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1. A method of thermocatalytic pollution control comprising the steps of:
- providing a target pollutant having a varying flow rate;
loosely positioning at least one thermocatalytic media in a thermocatalytic reactor, the thermocatalytic reactor having at least one heat source;
rotating the at least one thermocatalytic media to form a fluidized bed;
passing the varying flow rate target pollutant into the fluidized bed of the at least one thermocatalytic media; and
converting the varying flow rate target pollutant that passes through the thermocatalytic media to a selected level of destruction and removal efficiency(DRE).
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Abstract
A new method for design and scale-up of thermocatalytic processes is disclosed. The method is based on optimizing process energetics by decoupling of the process energetics from the DRE for target contaminants. The technique is applicable to high temperature thermocatalytic reactor design and scale-up. The method is based on the implementation of polymeric and other low-pressure drop support for thermocatalytic media as well as the multifunctional catalytic media in conjunction with a novel rotating fluidized particle bed reactor.
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Citations
20 Claims
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1. A method of thermocatalytic pollution control comprising the steps of:
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providing a target pollutant having a varying flow rate;
loosely positioning at least one thermocatalytic media in a thermocatalytic reactor, the thermocatalytic reactor having at least one heat source;
rotating the at least one thermocatalytic media to form a fluidized bed;
passing the varying flow rate target pollutant into the fluidized bed of the at least one thermocatalytic media; and
converting the varying flow rate target pollutant that passes through the thermocatalytic media to a selected level of destruction and removal efficiency(DRE). - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17)
rotating the fluid bed about the at least one heat source.
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3. The method of thermocatalytic pollution control of claim 1, wherein the passing step further includes:
passing the target pollutant from within and through the thermocatalytic media.
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4. The method of thermocatalytic pollution control of claim 1, further comprising the steps of:
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passing the target pollutant into a second thermocatalytic reactor having at least one thermocatalytic media and at least one heat source; and
converting the target pollutant that passes through the thermocatalytic media in the second thermocatalytic reactor to another selected level of destruction and removal efficiency (DRE).
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5. The method of thermocatalytic pollution control of claim 4, further comprising the steps of:
rotating at least one of the first thermocatalytic reactor and the second thermocatalytic reactor.
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6. The method of thermocatalytic pollution control of claim 4, wherein the first thermocatalytic reactor and the second thermocatalytic reactor are in series to one another.
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7. The method of thermocatalytic pollution control of claim 4, wherein the first thermocatalytic reactor and the second thermocatalytic reactor are in parallel to one another.
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8. The method of thermnocatalytic pollution control of claim 1, wherein the one thermocatalytic media includes:
- an elemental composition of Carbon, Oxygen, Hydrogen and Titanium.
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9. The method of thermocatalytic pollution control of claim 1, wherein the one thermocatalytic media includes:
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approximately 1% to approximately 86% by weight Carbon;
approximately 1% to approximately 20% by weight Oxygen;
approximately 7% to approximately 15% by weight Hydrogen; and
approximately 1% to approximately 30% by weight Titanium.
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10. The method of thermocatalytic pollution control of claim 1, wherein the one thermocatalytic media includes:
- an elemental composition of Carbon, Hydrogen, Cadmium and Sulfur.
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11. The method of thermocatalytic pollution control of claim 1, wherein the one thermocatalytic media includes:
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approximately 30% to approximately 86% by weight Carbon;
approximately 6.5% to approximately 14.3% by weight Hydrogen;
approximately 1% to approximately 50% by weight Cadmium; and
approximately 1% to approximately 15% by weight Sulfur.
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12. The method of thermocatalytic pollution control of claim 1, wherein the one thermocatalytic media includes:
an elemental composition of Silicon, Oxygen, and Titanium.
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13. The method of thermocatalytic pollution control of claim 1, wherein the one thermocatalytic media includes:
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approximately 0% to approximately 35% by weight Silicon;
approximately 30% to approximately 60% by weight Oxygen; and
approximately 10% to approximately 60% by weight Titanium.
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14. The method of thermocatalytic pollution control of claim 1, wherein the one thermocatalytic media includes:
- an elemental composition of Silicon, Oxygen, Cadmium and Sulfur.
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15. The method of thermocatalytic pollution control of claim 1, wherein the one thermocatalytic media includes:
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approximately 25% to approximately 55% by weight Silicon;
approximately 30% to approximately 60% by weight Oxygen;
approximately 5% to approximately 35% by weight Cadmium; and
approximately 1% to approximately 10% by weight Sulfur.
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16. The method of thermocatalytic pollution control of claim 1, wherein the heat source includes:
- a high flux light source.
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17. The method of thermocatalytic pollution control of claim 1, wherein the heat source includes:
- a temperature of at least approximately 300°
C. to approximately 400°
C.
- a temperature of at least approximately 300°
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18. A method of high flux photocatalytic pollution control, comprising the steps of:
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providing a target pollutant having a varying flow rate;
loosely positioning thermocatalytic media in a thermocatalytic reactor having at least one heat source;
rotating the loosely positioned thermocatalytic media to form a fluidized bed in the thermocatalytic reactor;
passing varying flow rate target pollutant into the rotating fluidized bed; and
thermocatalytically converting the target pollutant that passes through the rotating fluidized bed to a selected level of destruction and removal efficiency(DRE). - View Dependent Claims (19, 20)
a high flux heat source.
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20. The method of thermocatalytic pollution control of claim 18, wherein the rotating step includes:
rotating the fluidized bed about the at least one heat source.
Specification