Method for purifying diacid dimethyl esters by plate distillation separation

A technology of dimethyl dibasic acid and dimethyl succinate, which is applied in the field of separation and purification of organic mixtures, can solve the problems of high production cost, complex production process and large investment in equipment, and reduce energy consumption and product quality. The effect of stable and uniform quality and simplified process flow

Active Publication Date: 2012-05-02
WEIFANG YUANLI CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Dibasic acid dimethyl ester is a mixture obtained by esterification of mixed diacid, a by-product of adipic acid production, and methanol. In addition to the three esters, there are a certain amount of light components and heavy components in the mixture. To obtain a higher purity For three esters, it is necessary to separate the various components. The traditional distillation separation device and distillation method can separate five mixtures and obtain three pure products. At least four distillation towers are required, one tower separates and removes light components, and the tower The bottom material enters the second tower, the top of the second tower is separated and purified to obtain dimethyl succinate, the bottom material of the second tower enters the third tower, the top of the third tower is separated and purified to obtain dimethyl glutarate, and the bottom material of the third tower enters the fourth tower, the top of the four towers is separated and purified to obtain dimethyl adipate, and the bottom of the four towers is heavy components. Therefore, the traditional production process has complex production processes, large equipment investment, and high production costs.

Method used

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  • Method for purifying diacid dimethyl esters by plate distillation separation
  • Method for purifying diacid dimethyl esters by plate distillation separation

Examples

Experimental program
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Effect test

Embodiment 1

[0021] The raw material dimethyl mixed diacid passes through three distillation towers connected in series in sequence, and first enters the first distillation tower connected in series. The pressure inside the first distillation tower is 20kPa, the gas phase temperature at the top of the tower is 95°C, and the temperature at the bottom of the tower is 115°C. ℃, the light component is separated from the top of the first distillation tower, and the bottom material enters the second distillation tower. The bottom of the second distillation tower is vertically equipped with a partition to divide the lower cavity of the second distillation tower into The first tower chamber on one side and the second tower chamber on the other side, and the material inlet of the second distillation tower is located below the top of the partition, the pressure inside the second distillation tower is 18kPa, and the gas phase temperature at the top of the tower is 100°C , the temperature at the bottom...

Embodiment 2

[0023] Dimethyl mixed diacid as the raw material passes through three distillation towers connected in series, and first enters the first distillation tower connected in series. The internal pressure of the first distillation tower is 22kPa, the gas phase temperature at the top of the tower is 100°C, and the temperature at the bottom of the tower is 120°C. ℃, the light component is separated from the top of the first distillation tower, and the bottom material enters the second distillation tower. The bottom of the second distillation tower is vertically equipped with a partition to divide the lower cavity of the second distillation tower into The first tower chamber on one side and the second tower chamber on the other side, and the material inlet of the second distillation tower is located below the top of the partition, the pressure inside the second distillation tower is 19kPa, and the gas phase temperature at the top of the tower is 105°C , the temperature at the bottom of...

Embodiment 3

[0025] The raw material mixed diacid dimethyl ester passes through three distillation towers connected in series in turn, and first enters the first distillation tower connected in series. The pressure inside the first distillation tower is 23kPa, the gas phase temperature at the top of the tower is 105°C, and the temperature at the bottom of the tower is 130°C. ℃, the light component is separated from the top of the first distillation tower, and the bottom material enters the second distillation tower. The bottom of the second distillation tower is vertically equipped with a partition to divide the lower cavity of the second distillation tower into The first tower chamber on one side and the second tower chamber on the other side, and the material inlet of the second distillation tower is located below the top of the partition, the pressure inside the second distillation tower is 20kPa, and the gas phase temperature at the top of the tower is 110°C , the temperature at the bot...

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Abstract

The invention discloses a method for purifying diacid dimethyl esters by plate distillation separation. The distillation separation is successively finished in three series-wound distillation towers. The bottom of a second distillation tower is vertically provided with a separator plate, which divides the bottom cavity into a first tower chamber and a second tower chamber. A material inlet of the second distillation tower is positioned below the top of the separator plate. The method provided by the invention comprises the following steps of: mixing a raw material with diacid dimethyl esters, allowing the mixture to enter into the first distillation tower, separating a light component out from the top of first distillation tower, allowing the material at the tower bottom to enter into the second distillation tower, separating 1,4-succinic acid dimethyl ester out from the top of the distillation tower, separating 1,5-dimethyl glutarate out from the bottom of the second tower chamber of the second distillation tower, allowing the material at the tower bottom of the first tower chamber of the second distillation tower to enter into the third distillation tower, separating 1,6-adipic acid dimethyl ester out from the top of the third distillation tower, and discharging a heavier component in the raw material from the tower bottom. Starting with the first distillation tower, the temperature of the distillation towers successively rises and the pressure successively reduces.

Description

technical field [0001] The invention relates to the technical field of separation and purification of organic mixtures, in particular to a method for preparing 1,4-dimethyl succinate, 1,5-dimethyl glutarate and 1,6- Dimethyl adipate method. Background technique [0002] Dimethyl 1,4-succinate, dimethyl 1,5-glutarate and dimethyl 1,6-hexanedioate are all important chemical raw materials. [0003] Dimethyl 1,4-succinate is mainly used in food spices, in the preparation of fruit and fruit wine flavors and in the pharmaceutical industry, and in the synthesis of light stabilizers, high-grade paints, fungicides, and pharmaceutical intermediates, etc.; 1 , Dimethyl 5-glutaric acid is mainly used in organic synthesis; dimethyl 1,6-adipate can be used as a raw material for synthetic intermediates, medicines, and spices, as a plasticizer and high-boiling solvent, or as nylon acid The main component of dimethyl ester can also be used as a raw material for hydrogenation to produce 1,6...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C67/54C07C69/40C07C69/42C07C69/44
Inventor 杨辉刘修华谭立文秦国栋张建梅牛庆娟孙文刚
Owner WEIFANG YUANLI CHEM
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