IP Library Granted Patent US 7,625,839
Granted Patent B2
US 7,625,839 · App. 11/471,701 · Granted Dec 1, 2009

Activated carbon for use in electric double layer capacitors

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Quick Facts
Patent No.
US 7,625,839
App. No.
11/471,701
Granted
Dec 1, 2009
Kind
B2
Abstract

Activated carbon adapted for electric double layer capacitors is provided, which capacitors can give a large power density per unit volume and which capacitors, even when charge-and-discharge cycle is repeated under a large current or a constant voltage is continuously applied for a long time, undergo less decrease in output density. In particular, the present invention relates to the activated carbon manufactured by carbonization of coconut shell, which has a BET specific surface area of 2000 m 2 /g to 2500 m 2 /g, an average pore diameter of 1.95 nm (19.5 Å) to 2.20 nm (22 Å) and a pore volume of pores having a pore diameter calculated according to a Cranston-Inkley method of 5.0 nm (50 Å) to 30.0 nm (300 Å), of 0.05 cm 3 /g to 0.15 cm 3 /g.

Claims (14)

1. A method of making an activated carbon, which comprises the steps of:

a) pulverizing a coconut shell;

b) carbonizing said coconut shell in an inert atmosphere to produce a coconut shell char; and

c) heat-treating said coconut shell char at a temperature ranging from 900° C. to 1,100° C. in a steam gas atmosphere containing an inert gas selected from the group consisting of nitrogen, argon, and a combustion exhaust gas, wherein the content of steam in said steam gas atmosphere ranges from 30% by volume to 100% by volume,

wherein said activated carbon has a BET specific surface area of 2000 m 2 /g to 2500 m 2 /g, and an average pore diameter of 1.95 nm (19.5 Å) to 2.20 nm (22 Å),

wherein the pore volume of pores having a pore diameter, as calculated according to a Cranston-Inkley method, of 5.0 nm (50 Å) to 30.0 nm (300 Å) is 0.05 cm 3 /g to 0.15 cm 3 /g.

2. The method as claimed in claim 1 , wherein the BET specific surface area is 2000 m 2 /g to 2400 m 2 /g.

3. The method as claimed in claim 1 , wherein the BET specific surface area is 2050 m 2 /g to 2250 m 2 /g.

4. The method as claimed in claim 1 , wherein the pore volume of pores having a pore diameter, calculated according to a Cranston-Inkley method, of 5.0 nm (50 Å) to 30.0 nm (300 Å) is 0.07 cm 3 /g to 0.13 cm 3 /g.

5. The method as claimed in claim 1 , wherein the pore volume of pores having a pore diameter, calculated according to a Cranston-Inkley method, of 5.0 nm (50 Å) to 30.0 nm (300 Å) is 0.08 cm 3 /g to 0.12 cm 3 /g.

6. The method as claimed in claim 1 , wherein the average pore diameter is 2.00 nm to 2.15 nm.

7. The method as claimed in claim 1 , wherein the average pore diameter is 2.02 nm to 2.15 nm.

8. The method as claimed in claim 1 , wherein the heat-treating temperature ranges from 900° C. to 930° C.

9. The method as claimed in claim 1 , wherein the heat-treating is for 125 min. to 150 min.

Assignments (2)
CHANGE OF NAME Recorded Sep 5, 2017
From: MITSUBISHI RAYON CO., LTD.
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 043750/0834 →
MERGER Recorded Sep 4, 2017
From: MITSUBISHI CHEMICAL CORPORATION
To: MITSUBISHI RAYON CO., LTD.
Reel/Frame 043750/0207 →