Cod abatement process for electrochemical oxidation
The invention relates to an effluent COD treatment procedure by anodic oxidation combining the use of two different types of anode with a suitable apportionment of current. The first type of anode comprises an anode based on diamond doped-synthetic diamond. The second type of anode comprises an anode with high oxygen overvoltage containing tin and antimony oxides.
1. Device for COD treatment of effluents by anodic oxidation, comprising:
a first electrolyzer equipped with a first type of anode for oxygen evolution, the first anode is an electrode coated with tin and antimony oxides;
at least one second electrolyzer equipped with a second type of anode for oxygen evolution, said second type of anode having higher overvoltage for oxygen evolution than said first type of anode, wherein said second anode is boron-doped diamond electrode,
wherein the first electrolyzer is connected in parallel to the at least one second electrolyzer,
wherein the first electrolyzer and second electrolyzer are configured for simultaneous use in the COD treatment of effluents by anodic oxidation.
2. The device of claim 1 , wherein said at least one second electrolyser has an overall anodic surface lower than said first electrolyser.
3. The device of claim 2 , wherein the ratio between an active surface of said first electrolyser and an active surface of said at least one second electrolyser is between 55:45 and 95:5.
4. The device of claim 1 , wherein the ratio between the electrical current supplied to said first and to said at least one second electrolyser is adjustable.
5. The device of claim 1 , wherein an average faradic yield of higher than 24% is achieved.
6. An effluent COD treatment process comprising
carrying out an anodic oxidation process in a device comprising:
a first electrolyzer equipped with a first type of anode for oxygen evolution, wherein the first anode is an electrode coated with tin and antimony oxides;
at least one second electrolyzer equipped with a second type of anode for oxygen evolution, said second type of anode having higher overvoltage for oxygen evolution than said first type of anode, wherein said second anode is boron-doped diamond electrode,
wherein the first electrolyzer is connected in parallel to the at least one second electrolyzer,
wherein the first electrolyzer and second electrolyzer are configured for simultaneous use in the COD treatment of effluents by anodic oxidation.
7. The process of claim 6 , wherein the ratio between the electrical current supplied to said first electrolyser and to said at least one second electrolyser is between 55:45 and 95:5.
8. The process of claim 6 , wherein an average faradic yield of higher than 24% is achieved with the process.