Mercury control using moderate-temperature dissociation of halogen compounds
A system and method is provided for the removal of mercury from flue gas. Effective removal of mercury is obtained by oxidation of elemental mercury, with highly reactive halogen species derived from dissociation of halogen compounds at moderate temperatures brought into contact with the flue gas with or without the addition of carbon.
1. A method of removing mercury from a flue gas stream of a coal combustion system having a combustor and a pollutant control device comprising:
generating a dissociated halogen gas from a reactive precursor at a temperature in the range of about 60° C.-400° C. by providing activation energy to the reactive precursor;
reacting the dissociated halogen gas with mercury present in the flue gas stream at a temperature in the range of about 60° C.-400° C., the dissociated halogen gas reacted with mercury in the flue gas stream at least one location downstream from the combustor and upstream of the pollutant control device;
injecting particulates into the flue gas stream; and
capturing the mercury using the pollutant control device.
2. The method of claim 1 , wherein the dissociated halogen gas oxidizes the mercury present in the flue gas stream.
3. The method of claim 1 , wherein the dissociated halogen gas transforms the mercury present in the flue gas stream into a particulate-associated form.
4. The method of claim 1 , wherein the mercury is captured using at least one of a particulate control device such as an electrostatic precipitator, fabric filter, and scrubber.
5. The method of claim 1 , wherein the dissociated halogen gas comprises a gas of at least one of allyl iodide, allyl chloride, allyl bromide, and any combination thereof.
6. The method of claim 1 , wherein the dissociated halogen gas comprises at least one of organic di- and polyhalides including fluorocarbons, and inorganic non-metal halides with low decomposition temperatures.
7. The method of claim 1 , wherein the particulates are comprised of at least one of activated carbon or alkaline compounds (CaO, CaSiO3).
8. The method of claim 1 , further comprising exposing the precursor halogen gas to light from a photolysis lamp.
9. A method of removing mercury from a flue gas stream of a coal combustion system having a combustor and a pollutant control device, the method comprising:
providing activation energy to a reactive precursor generating a dissociated halogen gas at a temperature in the range of about 60° C. to about 400° C.;
reacting the dissociated halogen gas with mercury present in the flue gas stream at a temperature in the range of about 60° C. to about 400° C., the dissociated halogen gas reacted with the mercury at least one location of the flue gas stream downstream from the combustor and upstream of the pollutant control device;
injecting particulates into the flue gas stream, the particulates comprised of at least one of activated carbon, alkaline compounds, or any combination thereof; and
capturing the mercury using the pollutant control device.
10. The method of claim 9 , wherein the dissociated halogen gas oxidizes the mercury present in the flue gas stream.
11. The method of claim 9 , wherein the dissociated halogen gas transforms the mercury present in the flue gas stream into a particulate-associated form.
12. The method of claim 9 , wherein the mercury is captured using at least one of a particulate control device such as an electrostatic precipitator, fabric filter and/or scrubber.
13. The method of claim 9 , wherein the dissociated halogen gas comprises a gas of at least one of allyl iodide, allyl chloride, allyl bromide, and combinations thereof.
14. The method of claim 9 , wherein the dissociated halogen gas comprises at least one of organic di- and polyhalides including fluorocarbons, and inorganic non-metal halides with low decomposition temperatures.
15. The method of claim 9 , wherein the dissociated halogen gas comprises an organic chemical compound.
16. The method of claim 9 , wherein the point of injection of the reactive precursor into a duct is at the appropriate temperature corresponding to the dissociation temperature of the reactive precursor and below the decomposition temperature of oxidized mercury.
17. The method of claim 16 , wherein the reactive precursor is injected at least one location into the duct prior to an electrostatic precipitator device at a temperature in the range of about 320° C.-420° C.
18. The method of claim 16 , wherein sulfuryl chloride is injected at least one location into the duct prior to an electrostatic precipitator, a fabric filter, and a scrubber at a temperature in the range of about 100° C.-400° C.
19. A method of removing mercury from a flue gas stream of a coal combustion system having a combustor and a pollutant control device comprising:
providing activation energy to a reactive precursor generating a dissociated halogen gas from the reactive precursor at a temperature in the range of about 60° C.-400° C.;
reacting the dissociated halogen gas with mercury present in the flue gas stream at a temperature in the range of about 60° C.-400° C., the dissociated halogen gas reacted with mercury in the flue gas stream at least one location downstream from the combustor and upstream of the pollutant control device;
injecting particulates into the flue gas stream; and
capturing the mercury using the pollutant control device.