Method to reduce mercury, acid gas, and particulate emissions
View Patent ↗A waste gas is contacted with a mercury removal agent to remove mercury and a flue gas conditioning agent to alter a resistivity and/or cohesivity of particulates. The flue gas conditioning agent can be substantially free of SO 3 and/or comprise more than about 25 wt. % SO 3 , and/or the mercury removal agent can be substantially unaffected by the flue gas conditioning agent. An amount of mercury removed from the waste gas in the presence of the flue gas conditioning agent can be the same or more than that removed from the waste gas in the absence of the flue gas conditioning agent. An amount of the acid gas removed, by an acid gas removal agent, from the waste gas in the presence of the flue gas conditioning agent can be the same or more than that removed from the waste gas in the absence of the flue gas conditioning agent.
1. A method, comprising:
receiving a contaminated waste gas comprising particulates, an acid gas, and mercury;
contacting the waste gas with a mercury removal agent to remove or cause the removal of mercury from the waste gas and a flue gas conditioning agent to alter at least one of a resistivity and cohesivity of the particulates; and
removing at least most of the mercury and particulates from the waste gas to produce a treated gas, wherein at least one of the following is true:
(i) the flue gas conditioning agent is substantially free of SO 3 , wherein an amount of mercury removed from the waste gas in the presence of the flue gas conditioning agent is at least the same as an amount of mercury removed from the waste gas in the absence of the flue gas conditioning agent;
(ii) the flue gas conditioning agent comprises more than about 25 wt. % SO 3 and the mercury removal agent is substantially unaffected by the flue gas conditioning agent, wherein an amount of mercury removed from the waste gas in the presence of the flue gas conditioning agent is at least the same as an amount of mercury removed from the waste gas in the absence of the flue gas conditioning agent; and
(iii) wherein the waste gas is contacted with an acid gas removal agent to remove or cause the removal of the acid gas from the waste gas and wherein an amount of the acid gas removed from the waste gas in the presence of the flue gas conditioning agent is at least the same as an amount of the acid gas removed from the waste gas in the absence of the flue gas conditioning agent.
2. The method of claim 1 , wherein (i) is true, wherein the mercury removal agent comprises one or more of a halogen and activated carbon, and wherein the flue gas conditioning agent contains no more than about 1 wt. % SO 3 .
3. The method of claim 2 , wherein the flue gas conditioning agent is one or more of the flue gas conditioning agents sold under the tradenames ATI-2001™ and/or RESPond™, an alkali metal, alkaline earth metal, or rare earth nitrite, an alkali metal, alkaline earth metal, or rare earth nitrate, ammonium nitrite, and ammonium nitrate.
4. The method of claim 3 , wherein the flue gas conditioning agent comprises one or more of sodium nitrite, sodium nitrate, lithium nitrite, lithium nitrate, barium nitrite, barium nitrate, cerium nitrite, cerium nitrate, ammonium nitrite and ammonium nitrate.
5. The method of claim 2 , wherein the mercury removal agent is contacted with the waste gas upstream of an air preheater and wherein the flue gas conditioning agent is contacted with the waste gas downstream of the air preheater.
6. The method of claim 2 , wherein the mercury removal agent is contacted with the waste gas at a first location downstream of a second location where the flue gas conditioning agent is contacted with the waste gas, wherein a static mixer is positioned in the waste gas between the first and second locations, and wherein a distance between the first and second locations is at least about 10 feet.
7. The method of claim 1 , wherein (ii) is true and wherein the mercury removal agent comprises one or more of ammonium halide, amine halide, and quaternary ammonium halide.
8. The method of claim 7 , wherein the mercury removal agent is contacted with the waste gas upstream of an air preheater and wherein the flue gas conditioning agent is contacted with the waste gas downstream of the air preheater.
9. The method of claim 7 , wherein the mercury removal agent is contacted with the waste gas at a first location downstream of a second location where the flue gas conditioning agent is contacted with the waste gas and wherein a distance between the first and second locations is at least about 10 feet.
10. The method of claim 1 , wherein (iii) is true and wherein the acid gas removal agent is one or more of trona, a bicarbonate, and a hydroxide.
11. The method of claim 10 , wherein the acid gas removal agent is contacted with the waste gas upstream of a preheater.
12. The method of claim 10 , wherein the acid gas removal agent is contacted with the waste gas downstream of a preheater.
13. The method of claim 1 , wherein (i) and (iii) are true and wherein the acid gas removal agent is contacted with the waste gas upstream of where the mercury removal agent is contacted with the waste gas stream.
14. The method of claim 13 , wherein both the acid gas removal agent and mercury removal agent are contacted with the waste gas stream upstream of an air preheater and wherein the flue gas conditioning agent is contacted with the waste gas stream downstream of the air preheater.
15. The method of claim 13 , wherein both the acid gas removal agent and mercury removal agent are contacted with the waste gas stream downstream of an air preheater and wherein the flue gas conditioning agent is contacted with the waste gas stream downstream of the air preheater.
16. The method of claim 13 , wherein the acid gas removal agent is contacted with the waste gas upstream of an air preheater, wherein the mercury removal agent is contacted with the waste gas stream downstream of an air preheater, and wherein the flue gas conditioning agent is contacted with the waste gas stream downstream of the air preheater.
17. The method of claim 13 , wherein the mercury removal agent is contacted with the waste gas upstream of an air preheater, wherein the acid gas removal agent is contacted with the waste gas stream downstream of an air preheater, and wherein the flue gas conditioning agent is contacted with the waste gas stream downstream of the air preheater.
18. A method, comprising:
receiving a contaminated waste gas comprising particulates, SO 2 , and mercury;
contacting the waste gas with a carbon sorbent to remove or cause the removal of mercury from the waste gas and a flue gas conditioning agent to improve an ability of an electrostatic precipitator to remove the particulates; and
removing at least most of the mercury and particulates from the waste gas to produce a treated gas, wherein at least one of the following is true:
(i) wherein the flue gas conditioning agent does not diminish or otherwise inhibit mercury sorption by the carbon sorbent; and
(ii) wherein the waste gas is contacted with a dry sorbent injection (“DSI”) sorbent for SO 2 control and wherein the flue gas conditioning agent does not react or otherwise interact with the DSI sorbent.
19. The method of claim 18 , wherein the flue gas conditioning agent is substantially free of SO 3 and wherein the carbon sorbent is activated carbon.
20. The method of claim 18 , wherein (i) is true, wherein the carbon sorbent comprises activated carbon and is contacted with the waste gas upstream of an air preheater, and wherein the flue gas conditioning agent is contacted with the waste gas downstream of the air preheater.
21. The method of claim 18 , wherein (i) is true, wherein the carbon sorbent is contacted with the waste gas at a first location downstream of a second location where the flue gas conditioning agent is contacted with the waste gas, and wherein a distance between the first and second locations is at least about 10 feet.
22. The method of claim 18 , wherein (ii) is true.
23. The method of claim 22 , wherein the DSI sorbent is contacted with the waste gas upstream of an air preheater.
24. The method of claim 22 , wherein the DSI sorbent is contacted with the waste gas downstream of a preheater.
25. The method of claim 18 , wherein (i) and (ii) are true and wherein the DSI sorbent is contacted with the waste gas upstream of where the carbon sorbent is contacted with the waste gas stream.
26. The method of claim 18 , wherein (i) and (ii) are true, wherein both the DSI sorbent and carbon sorbent are contacted with the waste gas stream upstream of an air preheater, and wherein the flue gas conditioning agent is contacted with the waste gas stream downstream of the air preheater.
27. The method of claim 18 , wherein (i) and (ii) are true, wherein both the DSI sorbent and carbon sorbent are contacted with the waste gas stream downstream of an air preheater, and wherein the flue gas conditioning agent is contacted with the waste gas stream downstream of the air preheater.
28. The method of claim 18 , wherein (i) and (ii) are true, wherein the DSI sorbent is contacted with the waste gas upstream of an air preheater, wherein the carbon sorbent is contacted with the waste gas stream downstream of an air preheater, and wherein the flue gas conditioning agent is contacted with the waste gas stream downstream of the air preheater.
29. The method of claim 18 , wherein (i) and (ii) are true, wherein the carbon sorbent is contacted with the waste gas upstream of an air preheater, wherein the DSI sorbent is contacted with the waste gas stream downstream of an air preheater, and wherein the flue gas conditioning agent is contacted with the waste gas stream downstream of the air preheater.