Method and system for controlling mercury emissions from coal-fired thermal processes
View Patent ↗The present disclosure is directed to the use of elemental or speciated iodine and bromine to control total mercury emissions.
1. A method, comprising:
combusting, in a thermal unit, a halogen-containing and mercury-containing carbonaceous feed material to form a mercury-containing gas stream, the mercury-containing gas stream also comprising a halogen and particulates from the carbonaceous feed material;
separating, in at least one of an electrostatic precipitator and baghouse, at least a portion of the mercury, halogen, and particulates from the mercury-containing gas stream;
after separating, contacting, in a scrubber, a chemical agent with the mercury-containing gas stream to enhance removal of residual mercury from the mercury-containing gas stream, wherein the chemical agent comprises a halogen and wherein the halogen in the chemical agent comprises iodine; and
after contacting, removing, by the scrubber, at least part of the halogen and the residual mercury from the mercury-containing gas stream.
2. The method of claim 1 , wherein the scrubber is a wet scrubber, wherein the carbonaceous feed material is coal, wherein the halogen in the carbonaceous feed material is at least one of iodine and bromine, and wherein the chemical agent is soluble in a scrubbing solution of the wet scrubber.
3. The method of claim 2 , wherein a total dissolved mercury concentration in the scrubbing solution is relatively low and wherein no more than about 20% of the mercury in the mercury-containing gas stream is dissolved in the scrubbing solution.
4. The method of claim 1 , wherein the chemical agent is introduced directly into the scrubber.
5. The method of claim 1 , wherein the chemical agent is introduced into the gas stream upstream of an air preheater and the scrubber.
6. The method of claim 1 wherein the scrubber is upstream of a particulate control device and wherein the particulate control device is a electrostatic precipitator and/or baghouse.
7. The method of claim 1 , wherein the chemical agent is carried by or part of a reactive surface agent.
8. The method of claim 7 , wherein the reactive surface agent comprises one or more of a zeolite, silica, silica alumina, alumina, gamma-alumina, activated alumina, acidified alumina, amorphous or crystalline aluminosilicate, amorphous silica alumina, ion exchange resin, clay, a transition metal sulfate, porous ceramic, porous carbonaceous material, wherein the carbonaceous material compromise coal ash, unburned carbon, charcoal, char, coke, carbon black, activated carbon, other hydrocarbon and coal derivatives, and other forms of carbon, trona, alkali metal bicarbonates, alkali metal bisulfate, alkali metal bisulfite, alkali metal sulfide, elemental sulfur, limestone, hydrated or slaked lime, circulating fluidized bed ash, fluidized catalytic cracker (FCC) fine, fumed silicate, metal oxide particle or powder, re-milled or fine fraction fly ash, bottom ash, fluidized bed combustor ash, and mixtures thereof.
9. The method of claim 1 , wherein the chemical agent is a mercury active agent.
10. The method of claim 9 , wherein the mercury active agent further comprises one or more of zinc or potassium bromide, calcium, sodium or potassium bromate, iodide salts including sodium, calcium, magnesium, zinc or potassium iodide, calcium, sodium or potassium iodate, diatomic bromine, diatomic elemental halogens, hydrogen bromide, and other bromine-containing compounds.
11. The method of claim 1 , wherein the halogen further comprises bromine.
12. The method of claim 1 , wherein the mercury-containing carbonaceous feed material comprises iodine and wherein the iodine is introduced with the feed material prior to combustion.
13. A method, comprising:
combusting, in a thermal unit, a halogen-containing and mercury-containing carbonaceous feed material to form a mercury-containing gas stream, the mercury-containing gas stream also comprising a halogen and particulates from the carbonaceous feed material;
separating, in at least one of an electrostatic precipitator and baghouse, at least a portion of the mercury, halogen, and particulates from the mercury-containing gas stream;
after separating, contacting, a chemical agent with the mercury-containing gas stream in a scrubber to enhance removal of residual mercury from the mercury-containing gas stream, wherein the chemical agent comprises a halogen and wherein the halogen in the chemical agent comprises iodine and at least one of chlorine and bromine; and
after contacting, removing, by the scrubber, at least part of the halogen and mercury from the mercury-containing gas stream.
14. The method of claim 13 , wherein the carbonaceous feed material is coal, wherein the halogen in the carbonaceous feed material is at least one of iodine and bromine, wherein the scrubber is a wet scrubber and wherein the chemical agent is soluble in a scrubbing solution of the wet scrubber.
15. The method of claim 14 , wherein a total dissolved mercury concentration in the scrubbing solution is relatively low and wherein no more than about 20% of the mercury in the mercury-containing gas stream is dissolved in the scrubbing solution.
16. The method of claim 13 , wherein the chemical agent is introduced directly into the scrubber.
17. The method of claim 13 , wherein the chemical agent is introduced into the gas stream upstream of an air preheater and the scrubber.
18. The method of claim 13 , wherein the scrubber is upstream of a particulate control device and wherein the particulate control device is a electrostatic precipitator and/or baghouse.
19. The method of claim 13 , wherein the chemical agent is carried by or part of a reactive surface agent.
20. The method of claim 19 , wherein the reactive surface agent comprises one or more of a zeolite, silica, silica alumina, alumina, gamma-alumina, activated alumina, acidified alumina, amorphous or crystalline aluminosilicate, amorphous silica alumina, ion exchange resin, clay, a transition metal sulfate, porous ceramic, porous carbonaceous material, wherein the carbonaceous material comprises coal ash, unburned carbon, charcoal, char, coke, carbon black, activated carbon, other hydrocarbon and coal derivatives, and other forms of carbon, trona, alkali metal bicarbonates, alkali metal bisulfate, alkali metal bisulfate, alkali metal sulfide, elemental sulfur, limestone, hydrated or slaked lime, circulating fluidized bed ash, fluidized catalytic cracker (FCC) fine, fumed silicate, metal oxide particle or powder, re-milled or fine fraction fly ash, bottom ash, fluidized bed combustor ash, and mixtures thereof.
21. The method of claim 13 , wherein the chemical agent is a mercury active agent.
22. The method of claim 21 , wherein the mercury active agent comprises one or more of zinc or potassium bromide, calcium, sodium or potassium bromate, iodide salts including sodium, calcium, magnesium, zinc or potassium iodide, calcium, sodium or potassium iodate, diatomic bromine, diatomic elemental halogens, hydrogen bromide, and other bromine-containing compounds.
23. The method of claim 13 , wherein the halogen further comprises bromine.
24. A method, comprising:
combusting, in a thermal unit, an iodine-containing and mercury-containing feed material to generate a mercury-containing gas stream, wherein the mercury-containing gas stream also comprises iodine and particulates from the feed material;
separating, in at least one of an electrostatic precipitator and baghouse, at least a portion of the mercury, iodine, and particulates from the mercury-containing gas stream;
after separating, contacting, within a scrubber, the mercury-containing gas stream with additional iodine to enhance removal of residual mercury from the mercury-containing gas stream; and
after contacting, removing, by the scrubber, at least part of the iodine and the mercury from the mercury-containing gas stream.
25. The method of claim 24 , wherein the additional iodine is introduced into the mercury-containing gas stream downstream of a thermal unit that combusts the feed material.
26. The method of claim 25 , wherein the additional iodine is introduced downstream of a preheater and wherein the feed material comprises coal.
27. The method of claim 24 , wherein the additional iodine is introduced directly into the scrubber.