Transition metal phosphide hydrofined catalyst and preparation method thereof
A transition metal, hydrorefining technology, applied in the direction of physical/chemical process catalysts, chemical instruments and methods, chemical/physical processes, etc., can solve the problems of low phosphide dispersion, reduced catalyst activity, and unsatisfactory conditions. Achieve high hydrofining reactivity, small interaction, and improve performance
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Embodiment 1
[0023] Weigh 1.63g of nickel nitrate (Ni(NO 3 ) 2 ·6H 2 O) and 0.73 g of diammonium hydrogen phosphate ((NH 4 ) 2 HPO 4 ) were dissolved in deionized water respectively, then the two were mixed, adjusted with concentrated nitric acid to dissolve the precipitate, and an equal volume was impregnated into 3.0 g of mesoporous carbon (the pore volume of mesoporous carbon was 2.0 mL / g, and the specific surface area was 1500 m 2 / g, pore diameter is 5nm). Immerse for 10 hours, then dry at 120°C and bake at 200°C for 3 hours. 0.11g TiCl 4 The aqueous solution of the above sample was added dropwise, immersed for 10 hours, then dried at 120°C for 10 hours, and calcined at 200°C for 3 hours to obtain a catalyst precursor.
[0024] 1g of the catalyst precursor was placed in the constant temperature zone of the reactor, and both ends were supported by quartz sand. Reduction with hydrogen at 150°C for 2 hours, then heated to 500°C at a rate of 2°C / min, constant temperature for 3 hou...
Embodiment 2
[0026] With 0.43g of Ce(NO 3 ) 4 Instead of 0.11g TiCl in Example 1 4 , the composition is shown in Table 1, and other steps are the same as in Example 1.
Embodiment 3
[0028] Replace nickel nitrate of 1.63g and the diammonium hydrogen phosphate of 0.73g in embodiment 1 with the cobalt nitrate of 2.61g and the diammonium hydrogen phosphate of 1.18g, with 0.85g TiCl 4 Instead of 0.11g TiCl in Example 1 4 , the composition is shown in Table 1, and other steps are the same as in Example 1.
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