A direct methanol fuel cell membrane electrode for improving catalyst utilization and its preparation method
A methanol fuel cell and utilization rate technology, applied in fuel cells, battery electrodes, circuits, etc., can solve the problems of large electrochemical reaction resistance of electrodes, catalyst inoperability, and proton inability to transfer, etc., so as to reduce preparation costs and improve utilization rate , Highly hydrophilic effect
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Embodiment 1
[0059] according to figure 2 The process and process shown are used to prepare direct methanol fuel cell electrodes and membrane electrodes with improved catalyst utilization, and conduct discharge tests. The main steps are as follows:
[0060] (1) Preparation of electrodes
[0061] Carbon paper containing polytetrafluoroethylene (PTFE) is used as a diffusion layer, and a microporous layer 2 containing PTFE is coated on the hydrophobic diffusion layer, wherein the content of polytetrafluoroethylene is 15 wt.%. A microporous layer 3 containing Nafion is coated on the outer microporous layer, wherein the content of Nafion is 30wt.%. Prepare the appropriate proportion of catalyst slurry, using isopropanol as solvent. Use PtRu / C as a catalyst on the anode side and Pt / C as a catalyst on the cathode side, and spray catalyst slurry on the microporous layer 3 containing Nafion to form a catalyst layer.
[0062] (2) Treatment of proton exchange membrane
[0063] The membrane was e...
Embodiment 2
[0069] The direct methanol fuel cell membrane electrode of the catalyst utilization rate of the present invention is tested under the conditions of high concentration methanol and dry oxygen. First, a double microporous layer electrode was prepared according to the same procedure as in Example 1.
[0070] The obtained membrane electrode assembly and sealing air cushion were assembled in a single cell and then tested. The test conditions were: cell operating temperature 60°C, normal pressure, anode fuel 2M methanol (flow rate 3ml min -1 ), the cathode air intake is dry oxygen (the flow rate is 199ml min -1 ). The limiting current density can reach 500.21mA cm -2 , the maximum power density reaches 76.29mW cm -2 , Example 2 increased by 41.01% compared to Comparative Example 2.
Embodiment 3
[0072] The direct methanol fuel cell membrane electrode of the catalyst utilization rate of the present invention is tested under the conditions of low concentration of methanol and humidified oxygen. First, a double microporous layer electrode was prepared according to the same procedure as in Example 1.
[0073] The obtained membrane electrode assembly and sealing air cushion were assembled in a single cell and then tested. The test conditions were: cell operating temperature 60°C, normal pressure, anode fuel 0.5M methanol (flow rate 3ml min -1 ), the cathode air intake is humidified oxygen (relative humidity is 60%, flow rate is 199ml min -1 ). The limiting current density can reach 135.05mA cm -2 , the maximum power density reaches 29.12mW cm -2 , Compared with Comparative Example 3, Example 3 has improved by 97.38%.
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