A method for improving carbon activity of direct carbon fuel battery
A fuel cell and active technology, applied in the direction of fuel cells, battery electrodes, circuits, etc., can solve the problems of low specific surface, low hydrophilicity, and large ash content of carbon anode, so as to improve performance, reduce hydrophobicity, and increase ratio The effect of surface area
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Embodiment 1
[0015] The carbon anode was treated with HCl, the ratio of acid to carbon was 2:1, the acid concentration was 2M, and the soaking time was 1 h. With NiO as the cathode (obtained from foamed Ni through in-situ oxidation and lithiation), 0.5atm O 2 / CO 2 =1:2 is the oxidizing agent, γ-LiAlO 2 The membrane is an electrolyte carrier diaphragm, and the MCDCFC is prepared. At 700°C and a voltage of 0.75V, the current density reaches 120mA / cm 2 , corresponding to a power density of 90mW / cm 2 .
Embodiment 2
[0017] The carbon anode is treated with HF, the ratio of acid to carbon is 2:1, the concentration of acid is 2M, and the soaking time is 1h. With NiO as the cathode (obtained from foamed Ni through in-situ oxidation and lithiation), 0.5atm O 2 / CO 2 =1:2 is the oxidizing agent, γ-LiAlO 2 The membrane is an electrolyte carrier diaphragm, and the MCDCFC is prepared. At 700 ° C and a voltage of 0.8 V, the current density reaches 130 mA / cm 2 , corresponding to a power density of 104mW / cm 2 .
Embodiment 3
[0019] Using HNO 3 To treat the carbon anode, the ratio of acid to carbon is 2:1, the concentration of acid is 2M, and the soaking time is 1h. With NiO as the cathode (obtained from foamed Ni through in-situ oxidation and lithiation), 0.5atm O 2 / CO 2 =1:2 is the oxidizing agent, γ-LiAlO 2 The membrane is an electrolyte carrier diaphragm, and the MCDCFC is prepared. At 700°C and a voltage of 0.8V, the current density reaches 140mA / cm 2 , corresponding to a power density of 112mW / cm 2 .
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