Electrocatalyst for proton exchange film fuel cell
A proton exchange membrane and electrocatalyst technology, applied in solid electrolyte fuel cells, fuel cells, battery electrodes, etc., to achieve good thermal stability, strong long-term operating stability, and improved sintering resistance and stability
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preparation Embodiment 1
[0048] Platinum Titanium Carbon (Pt / TiO x / C) (Pt mass percentage 40wt.%, atomic ratio Pt:Ti=5:1) catalyst preparation.
[0049] Carbon black XC-72R is treated with 2N hydrochloric acid and 5N nitric acid solution in advance, after drying at 140°C, weigh 2 grams and disperse with 100ml isopropanol for 30 minutes by ultrasonic oscillation to obtain a carbon slurry, and add ethylene glycol of butyl titanate under stirring solution (containing 482 mg butyl titanate), then dropwise added a mixture of 20 ml isopropanol + 15 ml water + 1 ml nitric acid, stirred for 4 days, titanium was fully hydrolyzed, washed with a large amount of water, and dried to obtain a composite carrier for use. 1.2 g of the prepared composite carrier was ultrasonically vibrated with 200 ml of ethylene glycol for 30 minutes to obtain a carbon slurry. Weigh 2.16g of chloroplatinic acid (containing 0.799g of platinum) and dissolve it in 50ml of ethylene glycol, add it dropwise to the carbon slurry, and after...
preparation Embodiment 2
[0051] Platinum Titanium Carbon (Pt / TiO x / C) (Pt mass percentage 40wt.%, atomic ratio Pt:Ti=1:1) catalyst preparation.
[0052] Other conditions are the same as in Example 1, except that the atomic ratio of Pt and Ti in the catalyst component is changed to 1:1. The platinum metal loading was maintained at 40 wt%. Transmission electron microscopy and X-ray diffraction experimental results show that the catalyst metal particle size and distribution before and after treatment are similar to those in Example 1.
preparation Embodiment 3
[0054] Platinum Titanium Carbon (Pt / TiO x / C) (Pt mass percentage 40wt.%, atomic ratio Pt:Ti=10:1) preparation of catalyst.
[0055] Other conditions are the same as in Example 1, except that the atomic ratio of Pt and Ti in the catalyst component is changed to 10:1. The platinum metal loading was maintained at 40 wt%. Transmission electron microscopy and X-ray diffraction experimental results show that the catalyst metal particle size and distribution before and after treatment are similar to those in Example 1.
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