Process system for synthesizing hexamethylenediamine key intermediate
A process system and intermediate technology, applied in the field of synthetic hexamethylenediamine key intermediate, 6-aminocapronitrile, can solve the problems affecting the normal operation of the reaction device, affecting the reaction efficiency, reducing the catalyst activity and service life, etc., to improve the Raw material utilization rate and product selectivity, simple process flow, and the effect of reducing surface coking
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Embodiment 1
[0053] Application such as figure 2 Shown process system of the present invention synthesizes hexamethylenediamine key intermediate, and technique comprises the steps:
[0054] (1) The raw material caprolactam and ammonia water with a mass percentage concentration of 25% are transported to the first preheater A101 and the second preheater 2B respectively with a high-pressure pump for preheating. The preheating temperature of caprolactam is 275° C., and the ammonia water The preheating temperature is 450°C, and the preheated caprolactam and ammonia water are passed into the first reactor 3 at a molar ratio of 1:35, and the reaction is carried out at 500°C and 4MPa, and the reaction residence time is 8s; wherein, the first reaction Device 3 is a microchannel reactor;
[0055] (2) Transport the material obtained after the reaction in step (1) to the first separator 5, and carry out gas-liquid separation at 120 ° C. The separated gas phase material ammonia and water are recovere...
Embodiment 2
[0059] Applying the process system of the present invention to synthesize the key intermediate of hexamethylenediamine, the basic process steps are the same as in Example 1, but the difference is that in step (1), the molar ratio of the amount of raw ammonia and caprolactam is 1:1.
[0060] Result analysis method is the same as embodiment 1, specifically see table 1.
Embodiment 3
[0062] The process system of the present invention is used to synthesize the key intermediate of hexamethylenediamine. The basic process steps are the same as those in Example 1, except that in step (1), the molar ratio of raw ammonia water and caprolactam is 50:1.
[0063] Result analysis method is the same as embodiment 1, specifically see table 1.
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