Method for resource utilization of hexamethylenediamine key intermediate reaction residues
A technology for intermediate and hexamethylene diamine, which is applied in the field of recycling caprolactam, aminocapronitrile, and hexamethylene diamine key intermediate reaction residue resource utilization, can solve the impact of production efficiency and product quality, complex catalyst preparation process and harsh reaction conditions. and other problems to achieve the effect of solving the problem of residue pollution, realizing resource utilization and simple operation
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Embodiment 1
[0028] A method for resource utilization of a hexamethylenediamine key intermediate reaction residue of the present invention comprises the following steps:
[0029] (1) Put the residue and water into the high-pressure reaction kettle at the same time according to the mass ratio of 1:1, and carry out the depolymerization reaction at 100°C under normal pressure. After keeping the temperature at 100°C for 2 hours, cool down and release the pressure to take out the depolymerization reaction solution;
[0030] (2) Dehydrating the depolymerization reaction solution obtained in step (1) under negative pressure; then, performing negative pressure distillation to collect fractions to obtain aminocapronitrile and caprolactam products.
[0031] In the above examples, the high polymer content in the residue in step (1) is 15%; in step (2), when carrying out negative pressure dehydration, the absolute pressure is 1kPa, and the temperature is 100°C; , the absolute pressure is 0.1kPa, and t...
Embodiment 2
[0034] A method for resource utilization of a hexamethylenediamine key intermediate reaction residue of the present invention comprises the following steps:
[0035] (1) Put the residue and water into the high-pressure reaction kettle at the same time according to the mass ratio of 1:10, and carry out the depolymerization reaction at 300°C and 8.5MPa. After keeping the temperature at 300°C for 8 hours, cool down and release the pressure to take out the depolymerization reaction liquid;
[0036] (2) Dehydrating the depolymerization reaction solution obtained in step (1) under negative pressure; then, performing negative pressure distillation to collect fractions to obtain aminocapronitrile and caprolactam products.
[0037] In the above examples, the high polymer content in the residue in step (1) is 90%; in step (2), when carrying out negative pressure dehydration, the absolute pressure is 1.5kPa, and the temperature is 100°C; carry out negative pressure distillation , the abs...
Embodiment 3
[0040] A method for resource utilization of a hexamethylenediamine key intermediate reaction residue of the present invention comprises the following steps:
[0041] (1) the residue, water and catalyst Al 2 o 3 At the same time, put them into the high-pressure reactor respectively, and carry out the depolymerization reaction at 150°C and 0.5MPa. After keeping the temperature at 150°C for 3 hours, cool down and release the pressure to take out the depolymerization reaction liquid;
[0042] (2) Dehydrating the depolymerization reaction solution obtained in step (1) under negative pressure; then, performing negative pressure distillation to collect fractions to obtain aminocapronitrile and caprolactam products.
[0043] In above-mentioned embodiment, in step (1), the polymer content in the residue is 80%, the mass ratio of residue and water is 1:8, residue and Al 2 o 3 The mass ratio is 1:0.01; in step (2), when carrying out negative pressure dehydration, the absolute pressure...
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