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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

Active Publication Date: 2012-07-11
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the shortcomings of the crystallization unit, such as long operation process, many equipment, large material loss, and high labor intensity, more piperidinol products are taken away by the crystallization mother liquor after the two crystallization processes, which will inevitably reduce the single-cycle yield of the product, and the product per ton The consumption of acetone is relatively large

Method used

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  • Separation and purification method and device for extracting and purifying piperidinol product from piperidone hydrogenation reaction solution
  • Separation and purification method and device for extracting and purifying piperidinol product from piperidone hydrogenation reaction solution
  • Separation and purification method and device for extracting and purifying piperidinol product from piperidone hydrogenation reaction solution

Examples

Experimental program
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Effect test

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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Abstract

The invention discloses a separation and purification method and a device for extracting and purifying a piperidinol product from piperidone hydrogenation reaction solution, and the method comprises the following steps: (a) leading piperidinol crude product raw material solution into a feed inlet of a piperidone recovery distillation column, discharging light components of piperidone, acetonine and the like from the top of the piperidone recovery distillation column, then condensing by a recovery condenser, leading part of the light components to return and simultaneously extracting part of the light components as a piperidone product; and (b) sending the materials extracted from the bottom part of the piperidone recovery distillation column into the feed inlet of a piperidinol rectification column, extracting gas phase piperidinol from the top of the piperidinol rectification column, condensing the gas phase piperidinol by the condenser, then leading one part to return, simultaneously extracting the other part as a product, heating stillage residue part discharged from the bottom of the piperidinol rectification column by a reboiler at the bottom of the piperidinol rectification column, then forming the gas phase, returning into the column and simultaneously discharging one part as waste liquid. The adoption of the method can obtain the high-purity piperidinol product (above 99.5% by weight) at one time and recover the piperidone product.

Description

technical field [0001] The invention relates to a separation and purification method for purifying piperidinol products from a piperidone hydrogenation reaction solution, and also relates to a separation and purification device for purifying piperidinol products from a piperidone hydrogenation reaction solution. Background technique [0002] Such as figure 1 Shown traditional piperidinol (2,2,6,6-tetramethyl-4-piperidinol) production technique is to use acetone as basic raw material earlier, obtain piperidone after reaction, then piperidone (2,2,6,6-Tetramethyl-4-piperidone) is hydrogenated to obtain the crude piperidinol, which is a mixture of components such as piperidinol, piperidone and acetonin involved in the present invention. After the solution is simply removed from alcohol (at this time, the mass percentage of piperidinol is about 90%), the first crystallization is carried out to obtain 95%-97% of piperidinol. Then, after secondary crystallization, more than 99.5...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07D211/46B01D3/14
Inventor 冯惠生徐世昌任新单纯
Owner TIANJIN UNIV