Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

A kind of synthetic process of n-butyl acetate

A technology for the synthesis of n-butyl acetate, which is applied to the preparation of carboxylic acid esters, chemical instruments and methods, and the preparation of organic compounds to achieve the effect of reducing energy consumption

Inactive Publication Date: 2016-08-24
CHINA UNIV OF PETROLEUM (EAST CHINA)
View PDF7 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Although the use of the solid acid catalyst and the application of the reactive distillation tower process have effectively improved the selectivity of the esterification reaction, the conversion rate of acetic acid and the separation purity of the product, the problem of high energy consumption in the rectification tower still exists, so it is necessary to reduce the Process energy consumption, improve the energy utilization rate of the rectification process

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • A kind of synthetic process of n-butyl acetate
  • A kind of synthetic process of n-butyl acetate
  • A kind of synthetic process of n-butyl acetate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Example 1: Such as figure 1 As shown, the differential pressure thermal coupling reaction distillation atmospheric column (1) rectification zone (|) theoretical plate number is 5, reaction zone (II) theoretical plate number is 20, and vacuum column (2) theoretical plate number is 10 , The feed n-butanol is fed from the 6th theoretical plate (counted from top to bottom) in the atmospheric column (1), and the acetic acid is fed from the 10th theoretical plate with a molar ratio of 1:1. The flow rate and mass fraction of each incoming and outgoing stream are shown in Table 1. The temperature at the top of the atmospheric tower is 90.6℃, the temperature in the reaction zone is 91.6-116.6℃, the temperature of the phase separator is 50℃, and the temperature at the bottom of the vacuum tower is 78.0℃ , The operating pressure of the vacuum tower is 0.02MPa. The conversion rate of acetic acid is 98.39%. For the calculation of energy consumption, the same acetic acid conversion r...

Embodiment 2

[0018] Example 2: Such as figure 1 As shown, the feed composition, the molar ratio of feed n-butanol to acetic acid, the feed position and the number of theoretical plates in each zone are the same as in Example 1, and the operating pressure of the vacuum tower is 0.01 MPa. The flow rate and mass fraction of each incoming and outgoing stream are shown in Table 2. The top temperature of the atmospheric tower is 91.1℃, the temperature of the reaction zone is 91.8~118.3℃, the temperature of the phase separator is 50℃, and the temperature of the bottom of the vacuum tower is 61.6℃ . The conversion rate of acetic acid is 97.93%. For the calculation of energy consumption, the same conversion rate of acetic acid and product separation requirements are met. The heat load of the reboiler in the conventional reactive distillation process is 1925.663 kW. The top steam of the pressure column provides the heat source, so the energy consumption of only the compressor is 888.418kW, which can...

Embodiment 3

[0022] Example 3: Such as figure 1 As shown, the feed composition, the molar ratio of feed n-butanol to acetic acid, and the number of theoretical plates in each zone are the same as in Example 1. The feed n-butanol and acetic acid enter the atmospheric column from the sixth theoretical plate at the same time, and the vacuum column is operated The pressure is 0.03MPa. The flow rate and mass fraction of each incoming and outgoing stream are shown in Table 3. The top temperature of the atmospheric tower is 90.5℃, the temperature of the reaction zone is 92.5-116.1℃, the temperature of the phase separator is 50℃, and the bottom temperature of the vacuum tower is 83.2℃ . The conversion rate of acetic acid is 97.50%. For the calculation of energy consumption, the same acetic acid conversion rate and product separation requirements are met. The heat load of the reboiler in the conventional reactive distillation process is 1907.444kW. The top steam of the compression tower provides t...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention provides a process for synthesizing n-butyl acetate, in particular relates to a novel process for synthesizing n-butyl acetate by utilizing a pressure-difference thermal-coupling reaction rectification column. The process device comprises a pressure-difference thermal-coupling reaction rectification column atmospheric column, a vacuum column, a compressor, a heat exchanger, a pump and a phase separator. Raw materials n-butyl alcohol and acetic acid perform an esterification reaction in the vacuum column reaction section of the pressure-difference thermal-coupling reaction rectification column to generate the n-butyl acetate, the compressor is arranged between the vacuum column and the atmospheric column, steam extracted from the top of the vacuum column is pressurized through the compressor and enters the bottom of the atmospheric column, a reboiler at the bottom of the vacuum column is heated by potential heat of the steam at the top of the atmospheric column to perform thermal coupling between two columns, so that great energy-saving in the rectification process can be realized, the advantages of the pressure-difference thermal-coupling rectification column and a reaction rectification column can be played sufficiently, the esterification reaction and refining of the target product can be realized at the same time. According to the process, over 97 percent of acetic acid and over 99 mass percent of the high-purity product can be obtained.

Description

Technical field: [0001] The present invention relates to a synthetic process method for n-butyl acetate, in particular to a novel process method for synthesizing n-butyl acetate using a reactive distillation tower and differential pressure thermal coupling technology, which can complete the synthesis of n-butyl acetate and product separation, and Compared with conventional reactive distillation equipment, it can save more than 50% energy. Background technique: [0002] N-Butyl acetate is an important chemical raw material. It is often used as an organic solvent, dehydrating agent, and extractant. It is widely used in chemical, pharmaceutical, leather, plastic and perfume industries. At present, the production of n-butyl acetate is mostly batch and continuous production processes using concentrated sulfuric acid as a catalyst. These process methods are relatively mature in application and simple in operation, but they also have many defects. First, liquid concentrated sulfuric ac...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C07C69/14C07C67/08C07C67/54
CPCY02P20/10
Inventor 孙兰义李军王俊马占华刘雪暖李青松
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products