Systems and methods for catalyst screens in selective catalytic reduction reactors
A system for use in selective catalytic reduction reactor is disclosed. The system may include a catalyst bed and a screen located close to the catalyst bed in a manner so that flow of flue gas to the catalyst bed contacts the screen before it contacts the catalyst bed. The screen may be adapted to support a weight of at least 400 pounds above the catalyst bed so that the weight is not imposed on the catalyst. The screen may have a plurality of holes across its surface in a manner so that the screen is adapted to change the velocity distribution of the flue gas as it flows through the screen.
1. A system for use in a selective catalytic reduction reactor, the system comprising:
a catalyst bed; and
a screen located at a distance in a range of 1 in. to 12 ft. above the catalyst bed so that flow of flue gas to the catalyst bed contacts the screen or passes through the screen before the flow of flue gas contacts the catalyst bed or passes through the catalyst bed, the screen adapted to support a weight of at least 400 pounds above the catalyst bed so that the weight is not imposed on the catalyst bed, the screen having a plurality of holes across its surface, wherein the screen is adapted to change velocity distribution of the flue gas as it flows through the screen, wherein the screen comprises a flat shape extending from one end of the screen to another end of the screen, the flat shape is defined in a plane perpendicular to the flow of flue gas, and wherein the change in velocity distribution as a result of the screen comprises a 3 to 6% decrease in Root Mean Square (RMS) of overall velocity distribution of the flue gas.
2. The system of claim 1 further comprising:
a duct adapted to channel the flue gas that emanates from a boiler to the selective catalytic reduction reactor.
3. The system of claim 1 , further comprising:
a LPA separator for separating LPA from the flue gas prior to the flue gas contacting the screen.
4. The system of claim 1 , wherein the screen comprises a perforated metal plate.
5. The system of claim 1 , wherein the plurality of holes comprises holes of different sizes arranged in a manner to achieve the change in the velocity distribution of the flue gas.
6. The system of claim 1 , wherein the plurality of holes comprises holes of different sizes are arranged so that holes nearer to the perimeter of the screen are smaller than holes further from the perimeter of the screen.
7. The system of claim 1 , wherein the screen comprises a surface having a roughness of 20 μm or less.
8. The system of claim 1 , wherein the screen is adapted to normalize flue gas flow that has different velocities so that the screen increases the velocity of a section of the flue gas flowing to the screen at a velocity lower than the flue gas's average velocity and decreases the velocity of a section of the flue gas flowing to the screen with a velocity higher than the flue gas's average velocity.
9. The system of claim 1 wherein the ratio of area of holes/area of screen surface is in a range of 45% to 65%.
10. The system of claim 1 , wherein the holes are shaped as a selection from the list consisting of: hexagon, circle, square, rectangular, triangle, pentagon, and combinations thereof.
11. The system of claim 1 , wherein the screen comprises 12 gauge carbon steel.
12. A method for protecting a catalyst bed in a selective catalytic reduction reactor, the method comprising:
disposing a screen at a distance in a range of 1 in. to 12 ft. above the catalyst bed so that flow of flue gas to the catalyst bed contacts the screen or passes through the screen before the flow of flue gas contacts the catalyst bed or passes through the catalyst bed, the screen adapted to withstand a weight of at least 400 pounds without that weight being imposed on the catalyst bed, the screen having a plurality of holes across its surface, wherein the screen comprises a flat shape extending from one end of the screen to another end of the screen;
flowing the flue gas through the screen, wherein the flat shape is defined in a plane perpendicular to the flow of flue gas; and
changing velocity distribution of the flue gas as it flows through the screen, wherein the change in velocity distribution as a result of the screen comprises 3 to 6% decrease in Root Mean Square (RMS) of overall velocity distribution of the flue gas.
13. The method of claim 12 , wherein the screen comprises a perforated metal plate.
14. The method of claim 12 , wherein the screen comprises a surface having a R a of 20 μm.
15. The method of claim 12 , wherein, when the flue gas flow has different velocities, normalizing the flue gas flow comprises increasing the velocity of a section of the flue gas flowing to the screen at a velocity lower than the flue gas's average velocity and decreasing the velocity of a section of the flue gas flowing to the screen with a velocity higher than the flue gas's average velocity.
16. The method of claim 12 , wherein the ratio of area of holes/area of screen surface is in range of 45% to 65%.
17. The method of claim 12 , wherein the holes are shaped as a selection from the list consisting of: hexagon, circle, square, rectangular, triangle, pentagon, and combinations thereof.
18. The method of claim 12 , wherein the screen comprises 12 gauge carbon steel.