Separation and purification method and device for extracting and purifying piperidinol product from piperidone hydrogenation reaction solution
A technology of hydrogenation reaction and purification method, applied in fractionation, organic chemistry and other directions, can solve the problems of reducing the single-cycle yield of products, long operation process of crystallization unit, large consumption of acetone, etc., to reduce the amount of residual heat coking, The effect of reducing labor intensity of workers and improving product yield
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Embodiment 1
[0029] Heat the crude piperidinol raw material liquid to 70°C and feed it into the feed port in the middle of the piperidone recovery distillation tower 1. Light components such as piperidone and acetonin are discharged from the top of the piperidone recovery distillation tower and passed through Recovery condenser 3 condenses and partly refluxes and simultaneously partially extracts as piperidone product; the operating pressure at the top of the described piperidone recovery distillation tower is -0.090MPa (absolute pressure, the same below), and the pressure between the top and the bottom of the tower is Pressure difference is 2kPa; (b) the material that recovers from the bottom of described piperidone rectifying tower is sent into the middle part feed port of piperidinol rectifying tower 4, and is extracted at the top of described piperidinol rectifying tower tower Gas-phase piperidinol is discharged, and the gas-phase piperidinol is partially refluxed after being condensed ...
Embodiment 2
[0032]Heat the crude piperidinol raw material liquid to 72°C and feed it into the feed port in the middle of the piperidone recovery distillation tower 1. Light components such as piperidone and acetonin are discharged from the top of the piperidone recovery distillation tower and passed through Recovery condenser 3 condenses and partly refluxes and simultaneously partly extracts as piperidone product; the operating pressure at the top of the described piperidone recovery distillation tower is 0.01MPa (absolute pressure), and the pressure difference between the top and the bottom of the tower is 1kPa (b) The material extracted from the bottom of the piperidone recovery distillation tower is sent to the middle feed port of the piperidine alcohol rectification tower 4, and the gas phase piperidine is extracted at the top of the piperidine alcohol rectification tower Alcohol, the gaseous piperidine alcohol is partially refluxed after being condensed by the condenser, and the other...
Embodiment 3
[0035] Heat the piperidinol crude raw material liquid to 68°C and feed it into the feed port in the middle of the piperidone recovery distillation tower 1. Light components such as piperidone and acetonin are discharged from the top of the piperidone recovery distillation tower and passed through Recovery condenser 3 condenses and partly refluxes and simultaneously partially extracts as piperidone product; the operating pressure at the top of the described piperidone recovery distillation tower is 0.040MPa (absolute pressure), and the pressure difference between the top and the bottom of the tower is 3kPa (b) The material extracted from the bottom of the piperidone recovery distillation tower is sent to the middle feed port of the piperidine alcohol rectification tower 4, and the gas phase piperidine is extracted at the top of the piperidine alcohol rectification tower Alcohol, the gaseous piperidine alcohol is partially refluxed after being condensed by the condenser, and the ...
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