Method of removing mercury from exhaust gases of coal fired power plants and associated apparatus
View Patent ↗A method of removing mercury from a coal fired power plant exhaust gas includes passing the exhaust gas through a bulk particle filter to remove coarse particles, introducing powdered activated carbon into the exhaust gas downstream of the bulk particle filter, introducing mercury laden powdered activated carbon containing exhaust gas into a fine particle filter to separate the mercury containing powdered activated carbon from the exhaust gas, separating the powdered activated carbon from the mercury at an elevated temperature in an inert gas environment and recirculating the separating powdered activated carbon into the exhaust gas upstream from the fine particle filter. The desorption is preferably effected at a temperature of about 300 to 500° C. for about 5 to 60 minutes. The method is adapted to remove mercury which may be on the order of about 1 to 1000 ppm to 1 to 10 micrograms/cubic meter of exhaust gas. Corresponding apparatus is provided.
1. A method of removing mercury from a coal fired power plant exhaust gas comprising
passing said exhaust gas through a bulk particle collection device to remove a plurality of coarse particles using a coarse particle filter,
introducing powdered activated carbon into said exhaust gas downstream of said bulk particle collection device,
introducing said powdered activated carbon and said exhaust gas into a fine particle filter to separate mercury containing powdered activated carbon from said exhaust gas,
separating said powdered activated carbon from said mercury at an elevated temperature and in an inert gas environment, and
introducing said powdered activated carbon into said exhaust gas upstream from said fine particle filter.
2. The method of claim 1 including
subsequent to separating said powdered activated carbon from said mercury and said inert gas separating said mercury from said inert gas.
3. The method of claim 2 including separating said powered activated
effecting a carbon from said mercury by desorption of said activated carbon at a temperature of about 300 to 500° C. for about 5 to 60 minutes.
4. The method of claim 3 including effecting said desorption in a continuous process.
5. The method of claim 4 including
after separation of said mercury from said inert gas introducing said inert gas into said exhaust gas upstream of said fine particle filter.
6. The method of claim 3 including
introducing at least a portion of said activated carbon into a combustion chamber of said coal fired process plant.
7. The method of claim 1 including employing said method on said exhaust having about 1 to 1000 ppm of mercury.
8. The method of claim 1 including
recirculating at least a portion of said mercury containing powdered activated carbon into said exhaust gas upstream of said fine particle filter.
9. The method of claim 1 including employing nitrogen as said inert gas.
10. The method of claim 1 including removing ash from said coarse particles in said coarse particle filter.
11. The method of claim 2 including employing said method on mercury containing exhaust gas having mercury in an amount of about 1 to 1000 ppm to about 1–10 micrograms per cubic meter of said exhaust gas.
12. The method of claim 1 including employing in said bulk particle collection device a coarse filter.
13. The method of claim 1 including employing in said bulk particle collection device an electrostatic precipitator.
14. Apparatus for recovering mercury from an exhaust gas from a coal fired power plant comprising
a bulk particle collection device having a coarse particle filter for removing coarse particles from said exhaust gas,
a fine particle filter disposed downstream of said coarse particle filter,
a carbon source for introducing powdered activated carbon into said exhaust gas between said coarse particle filter and said fine particle filter,
said fine particle filter being structured to separate mercury containing powdered activated carbon from said exhaust gas,
a desorption unit for separating said powdered activated carbon from said mercury in an inert gas environment, and
recirculating said powder activated carbon through said exhaust gas between said coarse particle filter and said fine particle filter.
15. The apparatus of claim 14 including
a separation unit for separating mercury from said inert gas received from said desorption unit.
16. The apparatus of claim 14 including
said desorption unit being structured to effect a desorption at a temperature of about 300 to 500° C. for about 5 to 60 minutes.
17. The apparatus of claim 14 including
said desorption unit structured to effect a desorption as a continuous process.
18. The apparatus of claim 15 including
said separation unit being structured to deliver said inert gas to said exhaust gas.
19. The apparatus of claim 14 including
said desorption unit being structured to effect separation of mercury from said powdered activated carbon in mercury amounts of about 1 to 1000 ppm.
20. The apparatus of claim 14 including
said coarse particle filter being structured to remove said coarse particles containing ash from said exhaust gas.
21. The apparatus of claim 14 including
a first conduit for delivering powdered activated carbon from said desorption unit to said exhaust gas intermediate said coarse particle filter and said fine particle filter.
22. The apparatus of claim 14 including
a second conduit for delivering powdered activated carbon separated in said desorption unit to a combustion unit of said coal fired power plant.
23. The apparatus of claim 15 including
said desorption unit being structured to effect separation of mercury from said powdered activated carbon in mercury amounts of about 1 to 1000 ppm to about 1–10 micrograms per cubic foot of said exhaust gas.
24. The apparatus of claim 14 including
said bulk particle collection device having a coarse filter.
25. The apparatus of claim 14 including
said bulk particle collection device having an electrostatic precipitator.