Method for preparing SBA(sec-butyl alcohol) through hydrolysis with sec-butyl acetate

A technology of sec-butyl acetate and sec-butanol, which is applied in the fields of hydrolysis preparation, carboxylate/lactone preparation, oxygen-containing compound preparation, etc., can solve the problem that sec-butanol and sec-butyl acetate cannot be separated well, n-butyl Problems such as low conversion rate of olefin per pass and long process

Active Publication Date: 2017-05-10
HUNAN ZHONGCHUANG CHEM
View PDF10 Cites 14 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage is that the single-pass conversion rate of n-butene is low, only about 6%, and the requirements for raw materials are relatively strict. If the n-butene content of the C4 raw material used in the direct hydration process is greater than 90%, it may be directly hydrated to SBA, if the B-B grade fraction with lower n-butene content is directly reacted, the project cost will be increased due to its low conversion rate and high circulation rate, so extractive distillation or molecular sieve separation should be carried out first, and pre-purification should be carri

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
  • Method for preparing SBA(sec-butyl alcohol) through hydrolysis with sec-butyl acetate
  • Method for preparing SBA(sec-butyl alcohol) through hydrolysis with sec-butyl acetate
  • Method for preparing SBA(sec-butyl alcohol) through hydrolysis with sec-butyl acetate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0071] Such as figure 1 Described, the sec-butyl acetate raw material 2 is sent into the first hydrolysis reactor 3 with the speed of 30t / h, wherein, the sec-butyl acetate is a commercially available product purchased, and the industrial purity is 99.68%, and water 1 is added simultaneously, Among them, the molar ratio of water to sec-butyl acetate is 1.05:1, the temperature of the reactor is 60°C, and the reaction pressure is 1.0 MPa. The mixture 4 of sec-butanol, water and sec-butyl acetate obtained through hydrolysis reaction is 34.9 The speed of t / h is sent into the deacidification tower 5, the deacidification tower is a plate tower, the number of theoretical plates is 60, the feed port of the deacidification tower is arranged at the 35th tray, and the top of the deacidification tower is controlled The pressure is normal pressure, the temperature at the top of the tower is 90°C, and the reflux ratio is 2:1. In the deacidification tower, the separated acetic acid falls in...

Embodiment 2

[0074] Such as figure 2 Described, the sec-butyl acetate raw material 2 is sent into the first hydrolysis reactor 3 with the speed of 30t / h, wherein, the sec-butyl acetate is a commercially available product purchased, and the industrial purity is 99.85%, and water 1 is added simultaneously, Among them, the molar ratio of water to sec-butyl acetate is 1.0:1, the temperature of the reactor is 70°C, and the reaction pressure is 0.6MPa. The mixture 4 of sec-butanol, water and sec-butyl acetate obtained through hydrolysis reaction is 34.7 The speed of t / h is sent into the deacidification tower 5, the deacidification tower is a plate tower, the number of theoretical plates is 40, the feed port of the deacidification tower is arranged at the 22nd tray, and the top of the deacidification tower is controlled The pressure is normal pressure, the temperature at the top of the tower is 60°C, and the reflux ratio is 10:1. In the deacidification tower, the separated acetic acid falls int...

Embodiment 3

[0077] Such as image 3 Described, the sec-butyl acetate raw material 2 is sent into the first hydrolysis reactor 3 with the speed of 30t / h, wherein, sec-butyl acetate is a commercially available product purchased, and the industrial purity is 99.57%, and water 1 is added simultaneously, Among them, the molar ratio of water to sec-butyl acetate is 1.2:1, the temperature of the reactor is 80°C, and the reaction pressure is 0.6MPa. The mixture 4 of sec-butanol, water and sec-butyl acetate obtained through hydrolysis reaction is 35.6 The speed of t / h is sent into the deacidification tower 5, the deacidification tower is a plate tower, the number of theoretical plates is 50, the feed inlet of the deacidification tower is arranged at the 30th tray, and the top of the deacidification tower is controlled The pressure is normal pressure, the temperature at the top of the tower is 85°C, and the reflux ratio is 8:1. In the deacidification tower, the separated acetic acid falls into the...

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

A method for preparing sec-butyl alcohol through hydrolysis with SBA(sec-butyl alcohol)comprises steps as follows: (1) SBA is sent to a first hydrolysis reactor to react after being mixed with water; (2) a mixture after the reaction is sent to the lower part of a deacidification tower for separation, and separated acetic acid falls into the tower bottom; (3) a strand of material is extracted out of an SBA enrichment area of the deacidification tower and sent to an SBA refinement tower, an entrainer and water are added, an azeotrope formed by water, sec-butyl acetate and part of SBA is evaporated to the tower top, one part of oil phase is subjected to reflux after condensation layering, the other part returns to a reaction system for recycling with an aqueous phase, most of SBA falls into the tower bottom, and the SBA product is produced from the tower bottom. The SBA separated with the method has the purity of 99% or above, the purity of acetic acid separated by the deacidification tower is 97% or above, the yield of SBA is 70% or above, meanwhile, the method adopts a simple process and is simple to operate, and energy consumption is lower.

Description

technical field [0001] The invention relates to a method for preparing sec-butanol by hydrolysis of sec-butyl acetate. Background technique [0002] Secondary butanol (SBA), also known as second butanol, methyl ethyl carbinol, other butanol, 2-butanol, is a colorless, transparent, flammable liquid with a wine-like smell. SBA is used as a solvent in industry, co-solvent with methanol, can be used as a component to increase the octane number of gasoline, and can also be used to produce plasticizers, mineral dressing agents, herbicides, sec-butyl esters, etc., but the most important application is The production of methyl ethyl ketone accounts for about 90% of the total consumption. At present, the relatively mature methods in the industry include the indirect hydration method of n-butene and the direct hydration method of n-butene. The traditional process for preparing sec-butanol is sulfuric acid indirect hydration, which includes four steps: esterification, hydrolysis, rec...

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
IPC IPC(8): C07C27/00C07C27/30C07C29/09C07C29/82C07C31/12C07C51/09C07C51/46C07C53/08
CPCC07C29/095C07C29/82C07C51/09C07C51/46C07C31/12C07C53/08
Inventor 刘郁东胡先念黄能武李星肖云飞刘良会张小明申文义
Owner HUNAN ZHONGCHUANG CHEM
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products