Gasification system for preparing cyclohexanone oxime in caprolactam by Beckmann gas phase rearrangement
A technology of gasification system and caprolactam, which is applied in the field of chemical production system, can solve the problems of economic loss, coking and denaturation of cyclohexanone oxime, and achieve the effect of reducing economic loss
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Embodiment 1
[0048] A certain alcohol solution of cyclohexanone oxime is heated to 110°C in the high-pressure batching tank 1, and it is pressed into the gasification tower 2 under high pressure together with high-pressure nitrogen and atomized through the nozzle. At the same time, a large amount of hot nitrogen enters the gasification tower 2 and heats the atomized cyclohexanone oxime alcohol solution droplets to 210°C for gasification, and then the material enters the fluidized bed heater 3 for secondary heating until the reaction The temperature is 350°C, and then the material is condensed to 60°C through the condenser 4 to liquefy it, and then collected in the material collection tank 5, and part of the unliquefied alcohol is further condensed and collected through the partial condenser 6 . After the operation is completed, the hot air at 500°C is passed into the system for charcoal burning.
[0049] The evaluation results of cyclohexanone oxime coking in this example are shown in Tab...
Embodiment 2
[0051] A certain alcohol solution of cyclohexanone oxime is heated to 140°C in the high-pressure batching tank 1, and it is pressed into the gasification tower 2 under the action of high pressure together with high-pressure nitrogen and atomized through the nozzle. At the same time, a large amount of hot nitrogen enters the gasification tower 2 and heats the atomized cyclohexanone oxime alcohol solution droplets to 230 ° C for gasification, and then the material enters the fluidized bed heater 3 for secondary heating until the reaction The temperature is 360°C, and then the material is condensed to 60°C through the condenser 4 to be liquefied, and then collected in the material collection tank 5, and part of the unliquefied alcohol is further condensed and collected through the partial condenser 6 . After the operation is completed, the hot air at 500°C is passed into the system for charcoal burning.
[0052] The evaluation results of cyclohexanone oxime coking in this exampl...
Embodiment 3
[0054] A certain alcohol solution of cyclohexanone oxime is heated to 180°C in the high-pressure batching tank 1, and it is pressed into the gasification tower 2 under the action of high pressure together with high-pressure nitrogen and atomized through the nozzle. At the same time, a large amount of hot nitrogen enters the gasification tower 2 and heats the atomized cyclohexanone oxime alcohol solution droplets to 240 ° C for gasification, and then the material enters the fluidized bed heater 3 for secondary heating until the reaction The temperature is 380°C, and then the material is condensed to 60°C through the condenser 4 to liquefy it, and then collected in the material collection tank 5, and part of the unliquefied alcohol is further condensed and collected through the partial condenser 6 . After the operation is completed, the hot air at 500°C is passed into the system for charcoal burning.
[0055] The evaluation results of cyclohexanone oxime coking in this example ...
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