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Technological method for separating and refining butyl butyrate by using partition plate tower

A technology of butyl butyrate and partition tower, which is applied in the technical field of separating and refining butyl butyrate by using partition tower, which can solve the difficulty of increasing the separation of butyl butyrate, affect the purity of butyl butyrate, increase the residence time, etc. problem, to achieve the effect of improving thermodynamic efficiency, low thermodynamic efficiency and reducing the number

Active Publication Date: 2020-05-05
TIANJIN BOHUA YONGLI CHEM IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

If the crude butyl butyrate adopts the traditional multi-tower separation process, it usually needs to go through 2 to 3 rectification tower systems to complete the rectification operation of butyl butyrate. The residence time at high temperature leads to an increase in side reactions and the generation of by-products such as C8 and C12 esters. In this case, the difficulty of butyl butyrate separation is increased and the purity of butyl butyrate products is affected.
To solve this problem, it is necessary to increase equipment investment, heighten the tower body or increase subsequent rectification equipment, etc., but this will cause problems such as large equipment investment, large floor area, complicated operation, and high energy consumption.

Method used

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  • Technological method for separating and refining butyl butyrate by using partition plate tower

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0037] Example 1: the mass concentration of butyl butyrate in the crude product butyl butyrate is 93%, the feed rate is 15L / h, the number of theoretical plates in the public rectification section is 12, and the number of theoretical plates in the pre-fractionation section and the main column is 8 , the number of theoretical plates in the common stripping section is 5, the feed position is at the second theoretical plate in the pre-fractionation section of the partition tower, the reflux ratio is 6, and the distribution ratio of the reflux liquid between the feed section on both sides of the partition and the side line outlet section is 3. The operating pressure at the top of the partition tower is -73kPa, and the operating temperature at the top of the tower is 111°C. The overhead fraction is condensed and enters the reflux tank, and analyzed by gas chromatography, the mass concentration of n-butyraldehyde is 50.4%, the mass concentration of n-butanol is 6.8%, and the mass conc...

example 2

[0039] Example 2: Butyrate mass concentration is 89% in the crude product butyl butyrate, feed rate is 19L / h, and public rectifying section theoretical plate number is 15, and pre-fractionation section and main column theoretical plate number are 11, The number of theoretical plates in the common stripping section is 8, the feed position is at the sixth theoretical plate in the pre-fractionation section of the partition tower, the reflux ratio is 9, and the distribution ratio of the reflux liquid between the feed section on both sides of the partition and the side line discharge section is 5, The operating pressure at the top of the partition column is -81kPa, and the operating temperature at the top of the column is 108°C. The overhead fraction is condensed and enters the reflux tank. After chromatographic analysis, the mass concentration of n-butyraldehyde is 53.6%, the mass concentration of n-butanol is 6.3%, and the mass concentration of isobutyraldehyde is 10.5%. The buty...

example 3

[0040] Example 3: the mass concentration of butyl butyrate in the crude product butyl butyrate is 85%, the feed rate is 20L / h, the number of theoretical plates in the public rectification section is 18, and the number of theoretical plates in the pre-fractionation section and the main column is 14 , the number of theoretical plates in the common stripping section is 11, the feed position is at the 10th theoretical plate in the pre-fractionation section of the partition tower, the reflux ratio is 3, and the distribution ratio of the reflux liquid in the feed section on both sides of the partition and the side line discharge section is 7. The operating pressure at the top of the partition tower is -77kPa, and the operating temperature at the top of the tower is 114°C. The overhead fraction is condensed and enters the reflux tank. After chromatographic analysis, the mass concentration of n-butyraldehyde is 56.4%, the mass concentration of n-butanol is 6.9%, and the mass concentrat...

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Abstract

The invention relates to a technological method for separating and refining butyl butyrate by using a partition plate tower. The method comprises the following steps: arranging a partition plate in the middle of a butyl butyrate rectifying tower body, and dividing the butyl butyrate rectifying tower into a public rectifying section A, a public stripping section D, and a pre-fractionation section Band a side discharge section C on two sides of the partition plate; enabling the crude butyl butyrate to enter a pre-fractionation section through a crude preheater; arranging a liquid collector above the partition plate, descending liquid above the partition plate is collected and guided into a liquid distributor, and the allowing liquid distributor to distribute the liquid above the partition plate to a pre-fractionation section and a side line discharging section on the two sides of the partition plate; connecting the tower kettle reboiler to the bottom of the public stripping section D; and connecting a butyl butyrate rectifying tower side extraction pipeline to the shell pass gas phase inlet of the crude preheater. According to the technological method for separating and refining butyl butyrate, the mass concentration of butyl butyrate is 99% or above. The process has the characteristics of low process energy consumption, low equipment investment and the like, and has a wide application prospect.

Description

technical field [0001] The invention relates to a process method for separating and refining butyl butyrate by using a partition tower, in particular to obtain high-concentration butyl butyrate by rectifying crude butyl butyrate by using a partition tower. Background technique [0002] Although rectification technology has been widely used because of its mature technology, problems such as excessive equipment investment and high energy consumption for separation cannot be avoided in application, and it can no longer meet the requirements of energy-saving and efficient modern distillation technology. Thermocouple distillation is a complex distillation method, which can reduce the irreversible effective energy loss in the process, thereby reducing the energy consumption of the process. The clapboard column is also called a thermally coupled rectification column or a dividing wall rectification column. It is a completely thermally coupled rectification column. The internal spa...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C69/24C07C67/48C07C67/54C07C67/52
CPCC07C67/48C07C67/54C07C67/52C07C69/24Y02P20/10
Inventor 杨志波刘宇娜李治水李云辉张波李越苗淳
Owner TIANJIN BOHUA YONGLI CHEM IND
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