Separation and regeneration method of catalyst for preparing DL-methionine through catalytic hydrolysis
A catalytic hydrolysis and catalyst technology, applied in the field of methionine production, can solve the problems of high processing cost, difficult catalyst regeneration and recovery, etc., and achieve the effect of high activity, high maintenance cost and optimized separation
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Embodiment 1
[0026] Pass the ammonium methionine (2-amino-4-methylthioammonium butyrate) hydrolyzate containing solid cerium oxide catalyst into the plate and frame filter, and keep it under the saturation pressure condition of 30°C to realize closed thermo-solid separation , to obtain a wet solid cerium oxide catalyst, the aminonitrile content A in the hydrolyzed solution is ≤0.1%, then the wet solid cerium oxide catalyst is passed through a tank type sedimentation separator for sedimentation separation to obtain the oxidized Cerium catalyst.
Embodiment 2
[0028] Pass the ammonium methionine (2-amino-4-methylthioammonium butyrate) hydrolyzate containing solid cerium oxide catalyst into the belt filter, and keep the temperature at 80°C under saturated pressure to achieve closed thermo-solid separation , to obtain a wet solid cerium oxide catalyst, the aminonitrile content A in the hydrolyzed solution is 0.1%<A≤0.3%, then the wet solid cerium oxide catalyst is washed by solvent beating and then passed into a tower sedimentation separator After sedimentation and separation, the catalyst is passed into a tower scrubber for further countercurrent washing with a solvent, and the activated cerium oxide catalyst is separated and obtained.
Embodiment 3
[0030] Pass the ammonium methionine (2-amino-4-methylthioammonium butyrate) hydrolyzate containing solid cerium oxide catalyst into the centrifuge, keep the temperature at 80°C under saturated pressure conditions to realize closed thermosetting separation, and obtain Wet solid cerium oxide catalyst, the aminonitrile content A in the hydrolyzate is 0.3%<A≤2%, then the wet solid cerium oxide catalyst is washed by solvent beating and then passed into a centrifugal sedimentation separator for sedimentation separation After that, it is passed into the butterfly countercurrent scrubber for further solvent countercurrent washing, and the washed solid cerium oxide catalyst enters the fluidized fluidized bed for regeneration with air. When the regeneration temperature reaches 300 ° C, the regeneration residence time is 10 minutes, and the activated cerium oxide catalyst is obtained. Cerium oxide catalyst.
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