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

A method for separating sec-butyl acetate from the mixture after the reaction of acetic acid and C4

A technology for sec-butyl acetate and mixtures, applied in the field of separation of unreacted C4, can solve the problems of separation tower operating pressure and separation efficiency, material loss and separation energy consumption, etc., to reduce the possibility of acid on the top of the tower and reduce heating Requirements for heat source, effect of lowering tower top temperature

Active Publication Date: 2016-08-24
HUNAN ZHONGCHUANG CHEM
View PDF6 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the separated C4 light component contains a small amount of acetic acid, the C4 light component needs to be deacidified before being sent out to prevent corrosion of subsequent pipelines and equipment. At the same time, because the separated tower bottom material contains A small amount of C4 light components, this part of C4 light components will be brought into the subsequent separation steps, and will accumulate in the subsequent separation tower, and will affect the operating pressure and separation efficiency of the subsequent separation tower, resulting in unnecessary material loss and separate energy consumption

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 method for separating sec-butyl acetate from the mixture after the reaction of acetic acid and C4
  • A method for separating sec-butyl acetate from the mixture after the reaction of acetic acid and C4

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] The reaction mixture of acetic acid and C4 containing acetic acid, sec-butyl acetate, C4 and C8 hydrocarbons is sent into the de-light component tower at a speed of 10t / h, wherein the content of acetic acid is 6.54wt%, and the content of sec-butyl acetate The content of C4 is 79.62wt%, the content of C4 is 5.57wt%, and the content of C8 hydrocarbon is 8.27wt%. C4 is used as the reflux at the top of the tower, and the other part is extracted as the product. Acetic acid, sec-butyl acetate and C8 hydrocarbons fall into the bottom of the tower, and are sent to the azeotropic distillation column after being extracted from the tower kettle. The operating conditions of the light component removal tower It is: the temperature at the top of the tower is -30°C, the temperature at the bottom of the tower is 100°C, the pressure is normal pressure, the reflux ratio is 20, and the number of theoretical plates is 10; Tower, sec-butyl acetate, water, and C8 hydrocarbons are evaporated ...

Embodiment 2

[0045] The reaction mixture of acetic acid and C4 containing acetic acid, sec-butyl acetate, C4 and C8 hydrocarbons is sent into the light component removal tower at a speed of 10t / h, wherein the content of acetic acid is 12.46wt%, and the content of sec-butyl acetate The content of C4 is 70.65wt%, the content of C4 is 10.73wt%, and the content of C8 hydrocarbon is 6.16wt%. C4 is used as the reflux at the top of the tower, and the other part is extracted as the product. Acetic acid, sec-butyl acetate and C8 hydrocarbons fall into the bottom of the tower, and are sent to the azeotropic distillation column after being extracted from the tower kettle. The operating conditions of the light component removal tower It is: the temperature at the top of the tower is -10°C, the temperature at the bottom of the tower is 110°C, the pressure is normal pressure, the reflux ratio is 1, and the number of theoretical plates is 20; Tower, sec-butyl acetate, water, and C8 hydrocarbons are evapo...

Embodiment 3

[0048] The reaction mixture of acetic acid and C4 containing acetic acid, sec-butyl acetate, C4 and C8 hydrocarbons is sent into the light component removal tower at a speed of 10t / h, wherein the content of acetic acid is 21.58wt%, and the content of sec-butyl acetate The content of C4 is 60.19wt%, the content of C4 is 18.11wt%, and the content of C8 hydrocarbon is 0.12wt%. C4 is used as the reflux at the top of the tower, and the other part is extracted as the product. Acetic acid, sec-butyl acetate and C8 hydrocarbons fall into the bottom of the tower, and are sent to the azeotropic distillation column after being extracted from the tower kettle. The operating conditions of the light component removal tower It is: the temperature at the top of the tower is -20°C, the temperature at the bottom of the tower is 105°C, the pressure is normal pressure, the reflux ratio is 5, and the number of theoretical plates is 30; Tower, sec-butyl acetate, water, and C8 hydrocarbons are evapo...

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 method for separating unreacted C4 from a mixture obtained from reacted acetic acid and C4. The method includes the steps of putting a mixture obtained from reacted acetic acid and C4 in a light component removal column operated at atmospheric pressure, pumping out gasified unreacted C4 light components from the top of the column, putting the gasified unreacted C4 light components in a compressor to be liquefied into a liquid phase, setting part of liquefied C4 as top reflux, extracting the other part of the liquefied C4 as products, and extracting acetic acid, sec-butyl acetate and C8 hydrocarbon which drop to the bottom of the column for further separation. The method for separating unreacted C4 from the mixture obtained from reacted acetic acid and C4 is operated at atmospheric pressure, the temperature of the top and the bottom of the column is reduced, the requirements on heat source of a column bottom reboiler are reduced, the under-pressure operation is changed to atmospheric pressure operation, the C4 light components are separated completely, the liquid compressed through the compressor flows back, the temperature of the top of the column is reduced, the possibility of the acid top of the column is reduced, materials at the bottom of the column do not contain C4 components after separation, and the impact of C4 light components on the fluctuation of separation column operations after the C4 light components are accumulated in a subsequent separation column.

Description

technical field [0001] The invention relates to a method for separating unreacted C4 from a mixture of acetic acid and C4 reacted, in particular to a method for separating unreacted C4 from a mixture of acetic acid and C4 reacted by using an atmospheric distillation column. Background technique [0002] Second-butyl acetate, also known as second-butyl acetate and second-butyl acetate, is one of the four isomers of butyl acetate. It is a colorless, flammable, fruity-flavored liquid. The performance of the isomers is similar, and it has excellent solubility for a variety of synthetic resins and natural resins. Widely used in coatings, inks, adhesives, pesticides, medicines, spices, fine chemicals and oil products and other industries. The existing method for preparing sec-butyl acetate mainly uses C4 olefins as raw materials, and reacts with acetic acid to obtain sec-butyl acetate. This method has a wide source of raw materials and is cheap, good economic benefits, and enviro...

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): C07C69/14C07C67/54C07C9/10C07C9/12C07C11/08C07C11/09C07C11/167C07C7/04B01D3/00
CPCC07C7/04C07C51/44C07C51/46C07C67/54C07C53/08C07C69/14C07C9/10C07C9/12C07C11/08C07C11/09C07C11/167
Inventor 黄能武胡先念刘郁东张小明
Owner HUNAN ZHONGCHUANG CHEM
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