Control of mercury emissions from solid fuel combustion

1. A method for removing mercury from flue gases generated by the combustion of coal, the method comprising:

storing a starter batch of activated carbon in an agglomerated state;

de-agglomerating the starter batch in a separation device to create a contact batch of activated carbon;

injecting the contact batch into contact with the flue gas at a contact location between an economizer and an air preheater, whereupon the activated carbon of the contact batch adsorbs mercury from the flue gas;

transporting the contact batch to the contact location with substantially no intermediate storage of the contact batch following the de-agglomeration of the starter batch to prevent re-agglomeration of the activated carbon prior to injection; and

removing the activated carbon having mercury adsorbed thereon from the flue gas.

2. The method of claim 1 , wherein the transporting occurs in a manner in which, on average, at least ninety percent (90%) of the contact batch is delivered to the contact location in less than five (5) minutes following milling.

3. The method of claim 1 , wherein the separation device reduces the size of the activated carbon in the starter batch such that the activated carbon in the contact batch has a median particle size (d 50 ) less than 15 microns, where d 50 represents 50% of the particles by mass in the entire distribution in the contact batch.

4. The method of claim 3 , wherein the d 50 of the contact batch is less than 8 microns.

5. The method of claim 3 , wherein the d 50 of the contact batch is no more than one-half (½) of a d 50 of the starter batch.

6. The method of claim 3 , wherein the separation device includes at least one of: a jet mill, a ball mill, and a roller mill.

7. The method of claim 1 , further comprising:

depositing at least one of a halogen species and an acidic species on the contact batch prior to disposing the contact batch into contact with the flue gas.

8. The method of claim 1 , wherein the activated carbon adsorbs at least one of elemental mercury and mercury compounds from the flue gas.

9. The method of claim 1 , wherein the temperature of the flue gas at the contact location is between 600° F. and 800° F.

10. The method of claim 1 , wherein the injunction location is upstream of a flue gas side of the air heater and a collection location is at one of a baghouse and an electrostatic precipitator.

11. A method for removing mercury from flue gases generated by the combustion of coal, the method comprising:

milling a starter batch of activated carbon to provide a contact batch of activated carbon having a median particle size (d 50 ) less than 15 microns, where d 50 represents 50% of the particles by mass in the contact batch, the starter batch having a greater median particle size than the contact batch;

injecting the contact batch into contact with the flue gas at a contact location between an economizer and an air preheater, whereupon the activated carbon of the contact batch adsorbs mercury from the flue gas;

transporting the contact batch to the contact location with substantially no intermediate storage of the contact batch following the milling of the starter batch to prevent agglomeration of the activated carbon in the contact batch prior to injection; and

removing the activated carbon having mercury adsorbed thereon from the flue gas at a removal location.

12. The method of claim 11 , wherein the d 50 of the contact batch is less than 8 microns.

13. The method of claim 11 , wherein the transporting occurs in a manner in which, on average, at least ninety percent (90%) of the contact batch is delivered to the contact location in less than five (5) minutes following the milling.

14. The method of claim 11 , further comprising:

depositing at least one of a halogen species and an acidic species on the contact batch prior to disposing the contact batch into contact with the flue gas.

15. A method for removing mercury from flue gases generated by the combustion of coal, the method comprising:

milling a starter batch of activated carbon to provide a contact batch of activated carbon having a median particle size (d 50 ) less than 8 microns, where d 50 represents 50% of the particles by mass in the contact batch, the starter batch having a greater median particle size than the contact batch;

injecting the contact batch into contact with the flue gas at a contact location having a temperature between 600° F. and 800° F., whereupon the activated carbon of the contact batch adsorbs mercury from the flue gas;

transporting the contact batch to the contact location with substantially no intermediate storage of the contact batch following the milling of the starter batch to prevent agglomeration of the activated carbon in the contact batch prior to injection; and

removing the activated carbon having mercury adsorbed thereon from the flue gas at a removal location.

16. The method of claim 15 , wherein the transporting occurs in a manner in which, on average, at least ninety percent (90%) of the contact batch is delivered to the contact location in less than five (5) minutes following the milling.

17. The method of claim 16 , further comprising:

depositing at least one of a halogen species and an acidic species on the contact batch prior to disposing the contact batch into contact with the flue gas.