Catalytic anode with conductive polymer intercalation and preparation method and application thereof
By growing conductive polymer organic matter on nickel foam and electrodepositing, a catalytic anode with conductive polymer intercalation was prepared, which solved the problems of poor stability and low OER activity of catalytic electrodes in the direct electrolytic seawater hydrogen production system, and achieved efficient and stable seawater electrolysis hydrogen production, reducing the cost of hydrogen production.
Patent Information
- Application Number
- CN202510287764.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-03-11
- Publication Date
- 2025-05-23
- Estimated Expiration
- 2045-03-11
AI Technical Summary
In the prior art, the direct electrolytic seawater hydrogen production system has poor catalytic electrode stability, low OER activity, high proportion of side reaction ClER, and poor mechanical stability under industrial-grade high current density, resulting in low hydrogen production efficiency, high electrolytic energy consumption, and poor operating stability.
The conductive polymer organic matter was grown on the foam nickel foam by chemical deposition, and a mixed solution containing a nickel nitrate aqueous solution and a ferric nitrate aqueous solution for electrodeposition was prepared to prepare a catalytic anode with a conductive polymer intercalation.
The interaction between the catalyst and the current collector is improved, the OER activity of the electrode is enhanced, the damage of chloride ions to the electrolytic system is reduced, the catalytic stability and catalytic activity of direct electrolysis of seawater is significantly improved, and the cost of hydrogen production is reduced.
Smart Images

Figure CN120026366A_ABST
Abstract
Claims
1. A method for preparing a catalytic anode having a conductive polymer intercalation layer, characterized in that: The steps include: Step 1: growing a conductive high molecular organic substance on nickel foam by chemical deposition to prepare an electrode; Step 2: preparing a mixed solution containing an aqueous nickel nitrate solution and an aqueous ferric nitrate solution as an electrolyte, transferring the solution to a three-electrode electrolytic cell, using the electrode prepared in step 1 as a cathode of the electrolytic cell and a platinum wire electrode as an anode of the electrolytic cell to perform electrodeposition; Step 3: Take out the nickel foam after electrodeposition, wash it, remove the surface moisture, and obtain a catalytic anode with a conductive polymer intercalation layer.
2. The method for preparing a catalytic anode having a conductive polymer intercalation layer according to claim 1, characterized in that: In step 1, the conductive high molecular organic substance is selected from any one of 3-carboxypyrrole, sodium dodecyl sulfate, and ethylenediaminetetraacetic acid.
3. The method for preparing a catalytic anode having a conductive polymer intercalation layer according to claim 1, characterized in that: In step 1, the electrode is prepared by: The conductive high molecular organic matter is dissolved in deionized water to prepare a solution, and then the cleaned foamed nickel is immersed in the solution without stirring. After being placed for a period of time, it is taken out and washed to remove surface moisture to obtain the electrode.
4. The method for preparing a catalytic anode having a conductive polymer intercalation layer according to claim 3, characterized in that: The mass volume ratio (g / mL) of the conductive high molecular organic matter to the deionized water is 1:5-100.
5. The method for preparing a catalytic anode with a conductive polymer intercalation layer according to claim 1, characterized in that: In step 2, the molar ratio of the nickel nitrate aqueous solution to the iron nitrate aqueous solution is 1:1, and the volume ratio is 10:1-1:
10.
6. The method for preparing a catalytic anode with a conductive polymer intercalation layer according to claim 1, characterized in that: In step 2, the electrodeposition is performed at a potential of -1.5 V vs. RHE. The electrodeposition includes two times of electrodeposition. After the first electrodeposition for 6 min, the electrode is taken out, and after removing the surface bubbles, the electrodeposition is performed again for 6 min to form a more uniform catalyst layer.
7. The method for preparing a catalytic anode with a conductive polymer intercalation layer according to claim 1, characterized in that: In step 2, the mixed solution also includes an aqueous solution of chromium nitrate.
8. The method for preparing a catalytic anode with a conductive polymer intercalation layer according to claim 7, characterized in that: The concentration of the chromium nitrate aqueous solution is the same as that of the nickel nitrate aqueous solution or the ferric nitrate aqueous solution, and the volume ratio of the chromium nitrate aqueous solution to the nickel nitrate aqueous solution or the ferric nitrate aqueous solution is 1-4:
2.
9. A catalytic anode with a conductive polymer intercalation layer prepared by the preparation method according to any one of claims 1 to 8.
10. Use of the catalytic anode with a conductive polymer intercalation layer as claimed in claim 9 in a hydrogen production system by electrolysis of seawater.
Citation Information
Patent Citations
Oxygen evolution reaction catalyst for seawater electrolysis as well as preparation method and application of oxygen evolution reaction catalyst
CN115181994A
Anion-regulated hydroxyl sulfide electrolyzed water catalyst as well as preparation method and application thereof
CN117888122A
PPy / NiCo-LDH / NF composite material and preparation method and application thereof
CN119425806A
Hospital management system and method for hospital management based on beacon
KR102651993B1