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, the method 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;
introducing the dissociated halogen gas to the flue gas stream to allow the dissociated halogen gas to react with mercury present in the flue gas stream at a temperature in the range of about 60° C.-400° C., the dissociated halogen gas introduced to 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:
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;
introducing the dissociated halogen gas to the flue gas stream to allow the dissociated halogen gas to react with mercury present in the flue gas stream at a temperature in the range of about 60° C.-400° C., the dissociated halogen gas introduced at least one location to 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 (CaO, CaSiO3), 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 mercury control system for a coal combustion system comprising:
a coal combustor;
a pollutant control device comprising a particulate control device including at least one of an electrostatic precipitator, a fabric filter, and a scrubber;
a halogen dissociation unit having an activation energy source for generating a dissociated halogen gas therein, the halogen dissociation unit in communication with a flue gas stream of the coal combustion system located downstream of the coal combustor, the halogen dissociation unit configured to expose the dissociated halogen gas to mercury present in the flue gas stream allowing the dissociated halogen gas to react with the mercury at a temperature in the range of about 60° C.-400° C. for capture by the pollutant control device; and
a device for injecting carbon particulates.
20. The mercury control system of claim 19 , wherein the halogen dissociation unit has a configuration for dissociating at least one of dissociated allyl iodide, dissociated allyl chloride, dissociated allyl bromide, and combinations thereof.
21. The mercury control system of claim 19 , further comprising a photolysis lamp for exposing the dissociated halogen gas to light.