IP Library Granted Patent US 6,914,034
Granted Patent B2
US 6,914,034 · App. 09/940,178 · Granted Jul 5, 2005

Adsorbents for removing heavy metals and methods for producing and using the same

Assignee: Calgon Carbon Corporation
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Quick Facts
Patent No.
US 6,914,034
App. No.
09/940,178
Granted
Jul 5, 2005
Kind
B2
Abstract

Adsorbents for removing anions of a heavy metals comprise a porous carbon in which at least one oxygen-containing compound of iron, copper, and/or aluminum is incorporated. The oxygen-containing compound may be incorporated into the porous carbon by impregnation or dispersion of a suitable precursor of such a compound. The precursor may be further treated to yield the oxygen-containing compound. Such adsorbents are particularly useful for removing arsenic and/or selenium from the environment and may be used in treating drinking water sources.

Claims (51)

1. A carbon adsorbent for use in removing heavy metal anions from a liquid or gas medium comprising a porous carbon having a BET surface area greater than about 100 m 2 /g and having incorporated therein at least one oxygen-containing compound of at least one metal selected from the group consisting of iron (II) and aluminum, or combinations thereof, wherein said adsorbent is capable of interacting with said anions of said heavy metal to lower a concentration of said heavy metal in said liquid or gas.

2. The adsorbent according to claim 1 , wherein said oxygen-containing compound of metal is incorporated into said porous carbon by impregnation or dispersion within said adsorbent.

3. The adsorbent according to claim 1 , wherein said oxygen-containing compound of at least one metal is an oxide or hydroxide.

4. The adsorbent according to claim 1 , wherein said heavy metal is selected from the group consisting of arsenic, selenium and combinations thereof.

5. The adsorbent according to claim 1 , wherein said adsorbent has a micropore volume of greater than about 20 cm 3 /100 g.

6. The adsorbent according to claim 1 , wherein said at least one metal selected from the group consisting of iron (II) and aluminum, or combinations thereof are present at a concentration of up to about 50% by weight of said carbon.

7. An adsorbent for removing heavy metal anions from a liquid or gas medium surrounding said adsorbent, said adsorbent comprising a porous carbon having incorporated therein at least one oxygen-containing compound of at least one metal selected from the group consisting of iron (II) and aluminum or combinations thereof, wherein said metal is present at a concentration in the range from about 0.01 to about 50 percent by weight of said porous carbon; said oxygen-containing compound being selected from the group consisting of oxides, hydroxides and combinations thereof; and said adsorbent having a BET surface area greater than about 100 m 2 /g, wherein said adsorbent is capable of interacting with said anions of said heavy metal to lower a concentration of said heavy metal in said liquid or gas.

8. A method for making a carbon adsorbent for use in removing heavy metal anions from a liquid or gas medium containing said heavy metal, said method comprising the steps of:

(1) providing a porous carbonaceous adsorbent;

(2) impregnating said porous carbonaceous adsorbent with a solution comprising at least one compound of at least one metal selected from the group consisting of iron (II) and aluminum or combinations thereof; and

(3) converting said compound into an oxygen-containing compound of said metal to produce said carbon adsorbent;

wherein said adsorbent is capable of interacting with said anions of said heavy metal to lower a concentration of said heavy metal in said liquid or gas.

9. The method according to claim 8 , wherein said porous carbonaceous adsorbent is an activated carbon.

10. The method according to claim 8 , wherein said compound of said metal is selected from the group consisting of halides, nitrates, sulfates, chlorates, carboxylates having one to five carbon atoms.

11. The method according to claim 8 , wherein said step of converting consists of thermal decomposition or chemical reaction.

12. The method according to claim 8 , wherein said one metal is present at a concentration of up to about 50% by weight of said porous carbonaceous adsorbent.

13. The method according to claim 8 , wherein said oxygen-containing compound is an oxide or hydroxide.

14. The method according to claim 9 , wherein said activated carbon has a BET surface area greater than about 100 m 2 /g and is selected from the group consisting of coal, wood, nut shell, petroleum residue and vegetable-based activated carbons.

15. The method according to claim 9 , wherein said activated carbon is selected from the group consisting of coal, wood, nut shell, petroleum residue, vegetable-based activated carbons and has a micropore volume greater than about 20 cm 3 /100 g of adsorbent.

16. A method for making a carbon adsorbent for use in removing heavy metal anions from a liquid or gas medium, said method comprising the steps of:

(1) pulverizing a carbonaceous material, a binder, and at least one compound of a metal selected from the group consisting of iron (II) and aluminum or combinations thereof to form a powdered mixture;

(2) compacting said powdered mixture into shaped objects;

(3) crushing and screening the shaped objects into a metal-containing particulate material; and

(4) gasifying said metal-containing particulate material to produce said carbon adsorbent;

wherein said adsorbent is capable of interacting with said anions of said heavy metal to lower a concentration of said heavy metal in said liquid or gas.

17. The method according to claim 16 , wherein said carbonaceous material, said binder, and said at least one compound of said metal are pulverized together.

18. The method according to claim 16 , wherein said carbonaceous material, said binder, and said at least one compound of said metal are pulverized separately before said pulverized mixture is made.

19. The method according to claim 16 , wherein said compacting is selected from the group consisting of briquetting, pelletizing, densifying, and extruding.

20. The method according to claim 16 , wherein said gasifying is conducted under an atmosphere comprising an oxygen-containing gas at a temperature in a range from about 900° C. to about 1100° C., for a time sufficient to produce an adsorbent having a BET surface area of at least 100 m 2 /g.

21. The method according to claim 16 further comprising the step of oxidizing said metal-containing particulate material before the step of gasifying.

22. A carbon adsorbent for use in removing heavy metal anions from a liquid or gas medium comprising a porous carbon having a BET surface area greater than about 100 m 2 /g and having incorporated therein iron (III) hydroxide, wherein said adsorbent is capable of interacting with said anions of said heavy metal to lower a concentration of said heavy metal in said liquid or gas.

23. The adsorbent according to claim 22 , wherein said anions comprise oxygen-containing species of said heavy metal.

24. The adsorbent according to claim 23 , wherein said iron (III) hydroxide is incorporated into said porous carbon by impregnation or dispersion within said adsorbent.

25. The adsorbent according to claim 23 , wherein said heavy metal is selected from the group consisting of arsenic, selenium, and combinations thereof.

26. The adsorbent according to claim 23 , wherein said iron (III) is present at a concentration of up to about 50% by weight of said carbon.

27. A method for making a carbon adsorbent for use in removing heavy metal anions from a liquid or gas medium containing said heavy metal anions, said method comprising the steps of:

(1) providing a porous carbonaceous adsorbent;

(2) impregnating said porous carbonaceous adsorbent with a solution comprising at least one compound of iron (III); and

(3) converting said compound into iron (III) hydroxide to produce said carbon adsorbent;

wherein said carbon adsorbent is capable of lowering a concentration of said heavy metal anions in said liquid or gas medium.

28. The method according to claim 27 , wherein said at least one compound of said iron (III) is selected from the group consisting of halides, nitrates, sulfates, chlorates, carboxylates having one to five carbon atoms.

29. A method for making a carbon adsorbent for use in removing heavy metal anions from a liquid or gas medium, said method comprising the steps of:

(1) pulverizing a carbonaceous material, a binder, and at least one compound of iron (III) to form a powdered mixture;

(2) compacting said powdered mixture into shaped objects;

(3) crushing and screening the shaped objects into an iron (III)-containing particulate material; and

(4) gasifying said iron (III)-containing particulate material to produce said carbon adsorbent;

wherein said carbon adsorbent is capable of lowering a concentration of said heavy metal anions in said liquid or gas medium.

30. The method according to claim 29 , wherein said carbonaceous material, said binder, and said at least one compound of said iron (III) are pulverized separately before said mixture is made.

31. The method according to claim 29 , wherein said gasifying is conducted under an atmosphere comprising an oxygen-containing gas at a temperature in a range from about 900° C. to about 1100° C., for a time sufficient to produce an adsorbent having a BET surface area of at least 100 m 2 /g.

32. A carbon adsorbent for use in removing heavy metal anions from a liquid or gas medium comprising a porous carbon having a BET surface area greater than about 100 m 2 /g and having incorporated therein copper hydroxide, wherein said adsorbent is capable of interacting with said anions of said heavy metal to lower a concentration of said heavy metal in said liquid or gas.

33. The adsorbent according to claim 32 , wherein said anions comprise oxygen-containing species of said heavy metal.

Assignments (4)
RELEASE OF SECURITY INTEREST Recorded May 12, 2009
From: JPMORGAN CHASE BANK, N.A.
To: CALGON CARBON CORPORATION
Reel/Frame 022668/0296 →
SECURITY AGREEMENT Recorded Jun 6, 2007
From: CALGON CARBON CORPORATION
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 019382/0937 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 27, 2001
From: VO, TOAN PHAN
To: CALGON CARBON CORPORATION
Reel/Frame 012122/0853 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 27, 2001
From: VO, TOAN PHAN
To: CALGON CARBON CORPORATION
Reel/Frame 012122/0875 →
Continuity (1)
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