Systems and methods for simultaneous control of carbon dioxide and nitric oxide and generation of nitrous oxide
Systems and methods for simultaneous control of carbon dioxide and nitric oxide and generation of nitrous oxide are provided. In particular, the present invention provides systems and methods utilizing a titania-based photocatalyst to simultaneously control carbon dioxide and nitric oxide levels generated by combustion systems. Additionally, photoreduction of nitric oxide provided by the photocatalyst is used to generate nitrous oxide.
1. A photoreduction system for a fluid stream, the fluid stream including at least carbon dioxide and nitric oxide therein, the photoreduction system comprising:
a catalyst arranged such that the fluid stream flows over a surface region of the catalyst;
a light source configured to illuminate the surface region of the catalyst;
wherein when the light source illuminates the surface region of the catalyst, a concentration of the carbon dioxide and a concentration of the nitric oxide in the fluid stream are reduced as the fluid stream flows over the surface region,
wherein when the concentration of the nitric oxide is reduced as the fluid stream flows over the surface region, nitrous oxide is generated, and
wherein the catalyst comprises copper modified titanium dioxide, and
wherein the fluid stream includes water such that an amount of the nitrous oxide generated is a factor of 4 to 5.46 increase compared to the photoreduction system using a fluid stream having nitric oxide but without water and carbon dioxide, when measured in a photoreactor using operating conditions of carbon dioxide with water at a relative humidity of 70% and having nitric oxide but without water and carbon dioxide, an initial concentration of carbon dioxide ranging between 3.0-4.0% by volume, an initial concentration of nitric oxide ranging between 0.0610-0.0819% by volume, the same mass of the catalyst, and room temperature.
2. The photoreduction system of claim 1 , wherein the titanium dioxide has a band gap energy between 2 and 5 eV.
3. The photoreduction system of claim 1 , wherein a band gap energy of the titanium dioxide is between 2.5 and 4.5 eV.
4. The photoreduction system of claim 1 , wherein a band gap energy of the titanium dioxide is between 3 and 3.5 eV.
5. The photoreduction system of claim 1 , wherein the titanium dioxide comprises a phase selected from the group consisting of anatase, brookite, rutile, and mixtures thereof.
6. The photoreduction system of claim 1 , wherein the phase of the titanium dioxide comprises a mixture of anatase and rutile.
7. The photoreduction system of claim 1 , wherein the copper modified titanium dioxide is formed from reaction of a copper-containing compound and titanium dioxide particles having a mean diameter in a range of 10 to 50 nanometers.
8. The photoreduction system of claim 1 , wherein the copper modified titanium dioxide is formed from reaction of a copper-containing compound and titanium dioxide particles having a mean diameter in a range of 10 to 30 nanometers.
9. The photoreduction system of claim 1 , wherein the copper modified titanium dioxide has a copper content in a range of 0.01 to 5 wt. %.
10. The photoreduction system of claim 1 , wherein the copper modified titanium dioxide has a copper content in a range of 0.1 to 1 wt. %.
11. The photoreduction system of claim 1 , wherein the copper modified titanium dioxide has a copper content in a range of 0.2 to 0.8 wt. %.
12. The photoreduction system of claim 1 , wherein the light source is configured to emit ultraviolet radiation.
13. The photoreduction system of claim 1 , wherein the catalyst consists essentially of copper modified titanium dioxide.
14. The photoreduction system of claim 1 , wherein the conversion of nitric oxide in the fluid stream is greater than 50%.
15. The photoreduction system of claim 1 , wherein the yield of nitrous oxide in the fluid stream is greater than 4%.
16. The photoreduction system of claim 1 , wherein the fluid stream includes flue gas.