Method for recovering catalyst in preparation of cyclohexene by partial hydrogenation of benzene
A recovery method and technology for catalysts, applied in chemical recovery, chemical instruments and methods, catalyst regeneration/reactivation, etc., can solve the problems of increasing the operating cost of the device, fouling of equipment, and the solubility of unstable catalysts, and reduce the Energy consumption and the effect of preventing fouling of equipment
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Embodiment 1
[0019] The reaction mixture after the reaction of the benzene partial hydrogenation reaction system is added to the settler, and after being separated by the settler, the water phase containing the catalyst is returned to the reaction system for recycling, containing cyclohexene, cyclohexane, benzene and other substances The oil phase enters the filter, the oil phase is filtered through the filter, and the obtained filter cake containing the catalyst is returned to the reaction system for recycling, and the oil phase filtrate enters the flash tank for flash evaporation, and the flash pressure is 0.5MPa. Separation of unreacted hydrogen and other residual gases, the oil phase after flash evaporation enters the water washing device, the weight ratio of the water used to the oil phase substance is 1:5, after water washing, the water-soluble substances in the catalyst are removed from the oil phase After extraction, the extract phase is obtained, and the extract phase is returned t...
Embodiment 2
[0022] Add the reaction mixture of the benzene partial hydrogenation reaction system into the settler, and after being separated by the settler, the water phase containing the catalyst is returned to the reaction system for recycling, and the oil containing cyclohexene, cyclohexane, benzene, etc. The phase enters the filter, the oil phase is filtered through the filter, and the obtained filter cake containing the catalyst is returned to the reaction system for recycling, and the oil phase filtrate enters the flash tank for flash evaporation, the flash pressure is 0.4MPa, and the separated Unreacted hydrogen and other residual gases, the oil phase after flash evaporation enters the water washing device, the weight ratio of the water used to the oil phase substance is 1:1, after water washing, the water-soluble substances in the catalyst are extracted from the oil phase , to obtain the extract phase, return the extract phase to the reaction system for recycling, and the obtained ...
Embodiment 3
[0025] Add the reaction mixture of the benzene partial hydrogenation reaction system into the settler, and after being separated by the settler, the water phase containing the catalyst is returned to the reaction system for recycling, and the oil containing cyclohexene, cyclohexane, benzene, etc. The phase enters the filter, the oil phase is filtered through the filter, and the obtained filter cake containing the catalyst is returned to the reaction system for recycling, and the oil phase filtrate enters the flash tank for flash evaporation, the flash pressure is 0.5MPa, and the separated Unreacted hydrogen and other residual gases, the oil phase after flash evaporation enters the water washing device, the weight ratio of the water used to the oil phase substance is 1:10, after water washing, the water-soluble substances in the catalyst are extracted from the oil phase , to obtain the extract phase, return the extract phase to the reaction system for recycling, and the obtained...
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