SORBENTS FOR REMOVAL OF MERCURY

• US 20160339385A1
• Filed: 05/20/2016
• Published: 11/24/2016
• Est. Priority Date: 05/20/2015
• Status: Active Application

• Current Assignee: Calgon Carbon Corporation (Kuraray Company Limited)
• Original Assignee: Calgon Carbon Corporation (Kuraray Company Limited)
• Inventors: MIMNA, Richard A., TRAMPOSCH, Walter G.
• Application Number:
  US15/160,605
• Publication Number:
  US 20160339385A1
• Time in Patent Office: Days
• US Class Current: 1/1
• CPC Class Codes: B01D 2251/108 Halogens or halogen compounds
• CPC Class Codes: B01D 2251/30 Alkali metal compounds
• CPC Class Codes: B01D 2251/40 Alkaline earth metal or magnesium compounds
• CPC Class Codes: B01D 2253/102 Carbon
• CPC Class Codes: B01D 2257/602 Mercury or mercury compounds
• CPC Class Codes: B01D 53/64 Heavy metals or compounds thereof, e.g. mercury
• CPC Class Codes: B01D 53/83 with moving reactants

Abstract

Methods and systems for reducing mercury emissions from fluid streams are provided herein, as are adsorbent materials having high volumetric iodine numbers.

Claims

1. A method for mercury removal comprising:

injecting an alkaline agent into a flue gas stream; and

injecting a sorbent comprising an adsorptive material having a volumetric iodine number of greater than 300 mg/cc and an oxidizing agent into the flue gas stream.

2. The method of claim 1, wherein the alkaline agent is selected from the group consisting of calcium carbonate, calcium oxide, calcium hydroxide;

magnesium carbonate, magnesium hydroxide, magnesium oxide, sodium carbonate, sodium bicarbonate, trisodium hydrogendicarbonate dihydrate, and combinations thereof.

3. The method of claim 1, wherein the alkaline agent has a surface area of greater than 100 m²/g.

4. The method of claim 1, wherein the alkaline agent is injected upstream of the sorbent.

5. The method of claim 1, wherein the alkaline agent is injected downstream of the sorbent.

6. The method of claim 1, wherein the alkaline agent injection is co-located with that of the sorbent.

7. The method of claim 1, wherein the alkaline agent and the sorbent are co-injected as a blend.

8. The method of claim 1, wherein the adsorptive material is selected from the group consisting of activated carbon, reactivated carbon, graphite, graphene carbon black, zeolite, silica, silica gel, clay, and combinations thereof.

9. The method of claim 1, wherein the adsorptive material has a volumetric iodine number of about 350 mg/cc to about 800 mg/cc determined as the product of the gravimetric iodine number determined using standard test method ASTM D-4607 and the apparent density of the activated carbon as determined using standard test method ASTM D-2854.

10. The method of claim 1, wherein the adsorptive material has a gravimetric iodine number of about 500 mg/g to about 1500 mg/g determined using standard test method ASTM D-4607.

11. The method of claim 1, wherein the oxidizing agent is selected from the group consisting of chlorine, bromine, iodine, hydrogen bromide, ammonium bromide, ammonium chloride, calcium hypochlorite, calcium hypobromite, calcium hypoiodite, calcium chloride, calcium bromide, calcium iodide, magnesium chloride, magnesium bromide, magnesium iodide, sodium chloride, sodium bromide, sodium iodide, potassium tri-chloride, potassium tri-bromide, potassium tri-iodide, and combinations thereof.

12. The method of claim 1, wherein the sorbent is an impregnated adsorbent.

13. The method of claim 1, wherein the sorbent is an admixture.

14. The method of claim 1, wherein the oxidizing agent comprises about 5 wt. % to about 50 wt. % of the sorbent.

15. The method of claim 1, wherein the sorbent further comprises a nitrogen source.

16. The method of claim 10, wherein the nitrogen source is selected from the group consisting of ammonium containing compounds, ammonia containing compounds, amines containing compounds, amides containing compounds, imines containing compounds, quaternary ammonium containing compounds, and combinations thereof.

17. The method of claim 10, wherein the nitrogen source comprises about 5 wt. % to about 50 wt. % of the sorbent.

18. The method of claim 1, wherein the sorbent has a mean particle diameter of about 1 μ

m to about 30 μ

m.

19. The method of claim 1, wherein injecting the alkaline agent is carried out at a feed rate of about 500 lb/hr to about 6000 lb/hr.

20. The method of claim 1, wherein injecting the sorbent is carried out at a feed rate of about 5 lbs/hr to about 10 lbs/hr.