Method for producing activated carbon
A method is for producing activated carbon. The method includes: a) mixing a carbonaceous precursor with chemically activating agents to obtain a feedstock mixture; b) producing activated carbon by heating the feedstock mixture under the atmosphere of a physically activating gas; and c) performing suitable post-activation treatment of the produced activated carbon. Step a) includes in sequence the sub-steps of: i. addition of a first chemically activating agent to obtain an impregnated precursor; and ii. addition of a second chemically activating agent to obtain the feedstock mixture. An activated carbon species is obtainable by the method. The activated carbon species may thus be tuned to have a pore size distribution optimized for use in a carbon electrode.
1. A method for producing activated carbon, said method comprising the steps of:
a. mixing a carbonaceous precursor with chemically activating agents to obtain a feedstock mixture;
b. producing activated carbon by heating the feedstock mixture under the atmosphere of a physically activating gas; and
c. performing post-activation treatment of the produced activated carbon via at least one of washing, drying or grinding, wherein step a) comprises in sequence the sub-steps of:
i. addition of a first chemically activating agent to obtain an impregnated precursor; and
ii. addition of a second chemically activating agent to obtain the feedstock mixture;
wherein the first chemically activating agent is selected from the group consisting of MgCl 2 , AlCl 3 , CaCl 2 , FeCl 3 , ZnCl 2 , H 3 PO 4 , P 2 O 5 and H 2 SO 4 , and
wherein the second chemically activating agent is selected from the group consisting of K 2 CO 3 , Na 2 CO 3 , Li 2 CO 3 , KHCO 3 , NaHCO 3 , LiHCO 3 , KOH, NaOH, LiOH and benzyl potassium (C 7 H 7 K).
2. The method according to claim 1 , wherein a mass ratio of the carbonaceous precursor to the first chemically activating agent ranges from 1:10 to 1000:1.
3. The method according to claim 1 , wherein the carbonaceous precursor and the first chemically activating agent are mixed with assistance of a solvent.
4. The method according to claim 1 , wherein the mass ratio of the impregnated precursor and the second chemically activating agent ranges from 1:10 to 1000:1.
5. The method according to claim 1 , wherein the feedstock mixture is introduced into a reactor through a batch feed process.
6. The method according to claim 1 , wherein the feedstock mixture is introduced into a reactor through a continuous feed process.
7. The method according to claim 1 , wherein the physically activating gas is selected from the group consisting of H 2 O, H 2 , O 2 , CO 2 , SO 2 , SO 3 , and NH 3 .
8. The method according to claim 1 , wherein the physically activating agent is introduced into the activation reactor after heating of said activation reactor.
9. The method according to claim 1 , wherein heating is carried out at a temperature ranging from 400 to 1500° C.