Device and method for catalytic tail chlorine dehydrogenation and catalyst regeneration by adopting metal oxides
A catalyst and oxide technology, applied in catalyst regeneration/reactivation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of complex procedures and high operating costs, and achieve the effect of improving stability and improving industrial efficiency.
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Embodiment 1
[0056] The components of industrial tail chlorine are: H 2 , 3.97%; Cl 2 , 72.85%; O 2 , 9.93%; N 2 , 13.25%.
[0057] Copper oxide powder is used as catalyst. The catalyst packing height is 0.35m, the reaction temperature is 70°C, and the apparent operating gas velocity Uf=0.3m / s. When the tail chlorine is dehydrogenated under this condition, the hydrogen conversion rate can reach 75.56%. The mass concentration of polyvinyl alcohol solution is 0.5%, the microwave reaction temperature is 180°C, and the reaction time is 5min. The residence time of the catalyst in the reaction fluidized bed is 4h, and the regeneration time of the catalyst is 3h.
Embodiment 2
[0059] The components of industrial tail chlorine are: H 2 , 3.05%; Cl 2 , 72.36%; O 2 , 10.31%; N 2 , 14.25%.
[0060] Copper oxide particles are used as the catalyst. The catalyst packing height is 0.45m, the reaction temperature is 130°C, and the apparent operating gas velocity Uf=0.35m / s. When tail chlorine is dehydrogenated under this condition, the hydrogen conversion rate can reach 81.76%. The mass concentration of polyvinyl alcohol solution is 1%, the microwave reaction temperature is 160°C, and the reaction time is 3min. The residence time of the catalyst in the reaction fluidized bed is 4.5h, and the regeneration time of the catalyst is 3h.
Embodiment 3
[0062] The components of industrial tail chlorine are: H 2 , 3.97%; Cl 2 , 72.85%; O 2 , 9.93%; N 2 , 13.25%.
[0063] Cobalt oxide powder is used as catalyst. The catalyst packing height is 0.45m, the reaction temperature is 130°C, and the apparent operating gas velocity Uf=0.35m / s. Under this condition, when the tail chlorine is dehydrogenated, the hydrogen conversion rate can reach 87.33%. The mass concentration of polyvinyl alcohol solution is 0.5%, the microwave reaction temperature is 180°C, and the reaction time is 5min. The residence time of the catalyst in the reaction fluidized bed is 4.5h, and the regeneration time of the catalyst is 2.5h.
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