Dynamic halogenation of sorbents for the removal of mercury from flue gases
A halogen-containing gas is injected into a flowing transport air/sorbent stream at a point close to the point where the sorbent and transport air first mix to maximize the residence time available for the halogen-containing compound to be adsorbed onto the sorbent surface prior to the sorbent being injected into a flue gas containing mercury. This process maximizes the benefit and utilization of the halogen-containing reagent by placing it exactly where it is needed to facilitate elemental mercury removal—on the surface of the sorbent. The sorbent particles with their loading of adsorbed halogen-containing reagent enter the flue gas with a high reactivity for the removal of elemental mercury.
1 . A method of removing a portion of the elemental mercury in a flue gas created during a combustion process, comprising:
providing four streams, wherein the first stream comprises a halogen containing reagent, the second stream comprises a sorbent, the third stream comprises conveyance air, and the fourth stream comprises a flue gas containing elemental mercury;
combining the first, second, and third streams wherein the halogen containing reagent is adsorbed onto the sorbent;
injecting the combined stream into the fourth stream;
adsorbing the elemental mercury onto the sorbent; and
removing the sorbent from the fourth stream.
2 . The method according to claim 1 , wherein the flue gas is created during the combustion of at least one of a fossil fuel and municipal solid waste.
3 . The method according to claim 2 , wherein the fossil fuel comprises coal.
4 . The method according to claim 1 , wherein the halogen containing agent comprises at least one of chlorine, bromine, iodine or fluorine and halide derivatives thereof.
5 . The method according to claim 1 , wherein the sorbent comprises a carbonaceous sorbent.
6 . The method according to claim 5 , wherein the carbonaceous sorbent comprises at least one of powdered activated carbon, carbons and chars produced from coal and other organic materials, and unburned carbon produced by a combustion process.
7 . The method according to claim 1 , wherein the first and second streams are combined at a temperature between about 0 C. and about 50 C.
8 . The method according to claim 1 , wherein the first, second and third streams are first combined just prior to injection of the combined stream into the fourth stream.
9 . The method according to claim 1 , wherein the combined stream is injected into the fourth stream at a location where the temperature of the fourth stream is below about 175 C.
10 . The method according to claim 1 , further comprising the step of adsorbing a substantial portion of oxidized mercury present in the flue gas in addition to the elemental mercury in the fourth stream.
11 . The method according to claim 1 , further comprising the step of using a fabric filter to remove the sorbent from the fourth stream.
12 . The method according to claim 1 , further comprising the step of using an electrostatic precipitator to remove the sorbent from the fourth stream.
13 . The method according to claim 1 , wherein the fourth stream is provided with up to about 4 moles of halogen per million moles of flue gas, and at least about 0.1 pounds of sorbent per million cubic feet of flue gas.