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

High-purity tert-butyl alcohol online recovery technology for continuously producing potassium tert-butoxide

A technology of potassium tert-butoxide and tert-butanol, applied in the field of preparation of potassium tert-butoxide, which can solve the problems of low production efficiency, high production cost, difficulty in transportation and storage, etc.

Pending Publication Date: 2020-04-21
江苏天泽新材料有限公司
View PDF4 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, the mainstream method for domestic manufacturers to produce potassium tert-butoxide is to use tert-butanol to react with potassium metal, which requires the use of a large amount of active potassium metal, which is poor in safety, has a risk of explosion, and is not easy to transport and store
At the same time, metal potassium is expensive, making the production cost higher
[0004] Potassium tert-butoxide is also prepared by using potassium hydroxide aqueous solution and tert-butanol as the reaction raw materials. However, due to the dissolution and ionization equilibrium of the tert-butanol-potassium hydroxide-water system, it is a strongly reversible reaction system, which cannot spontaneously change from hydrogen to hydrogen. Potassium oxide is converted into potassium tert-butoxide, otherwise potassium tert-butoxide will react immediately to form potassium hydroxide when it meets water, and water must be removed from the system quickly
In order to solve this technical problem, there is a technical route for producing potassium tert-butoxide by azeotropic reaction rectification. The process of combining reaction and azeotropic distillation on the interface and a packed column with a large specific surface area are used as a process route for the preparation of potassium tert-butoxide. The technical difficulties of online recycling have led to the failure of this technical route to be widely used
In order to solve the technical problem of on-line recovery in the technical route of producing potassium tert-butoxide by azeotropic reaction distillation, it is usually necessary to enter the third component to realize the recovery of water in the reaction system and the problem of high energy consumption for recovery. The announcement number is CN206033617U The utility model patent proposed a production device of potassium tert-butoxide, including: a reaction kettle, which is connected to the pervaporation membrane separation unit through a delivery pump and a heater in turn; the intercepting side of the pervaporation membrane separation unit The outlet is connected to the reaction kettle; the permeate side of the pervaporation membrane separation unit is equipped with a vacuum pump and a permeate condenser, and the outlet of the permeate condenser is also connected with a permeate tank and a permeate pump; the process requires a pervaporation membrane High, need to face the problem of frequent replacement and maintenance, resulting in low production efficiency and further increase in production costs

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
  • High-purity tert-butyl alcohol online recovery technology for continuously producing potassium tert-butoxide
  • High-purity tert-butyl alcohol online recovery technology for continuously producing potassium tert-butoxide
  • High-purity tert-butyl alcohol online recovery technology for continuously producing potassium tert-butoxide

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0102] Embodiment 1: In the settling tank DECANTER, pre-inject cyclohexane 1100Kg as base material, tert-butanol 300Kg, then carry out tert-butanol and cyclohexane feed in the azeotropic reaction rectification column COLUMN1, cyclohexane 192Kg, 768Kg of tert-butanol, under the heating action of the azeotropic reactive distillation column COLUMN1, heated until the top temperature of the azeotropic reactive distillation column COLUMN1 is controlled at 65°C, and the temperature of the bottom of the tower is controlled at 85°C; tert-butanol and cyclohexane The binary azeotropic gas phase PG enters the settling tank DECANTER after cooling, and through the settling separation of the light phase and heavy phase of the settling tank DECANTER, the light phase separation liquid LT composed of tert-butanol and cyclohexane is refluxed to the azeotropic reaction The rectification tower COLUMN1 circulates for five hours to ensure a stable reflux balance between the azeotropic reaction rectif...

Embodiment 2

[0106] Embodiment 2: In the settling tank DECANTER, pre-inject cyclohexane 1100Kg as base material, tert-butanol 300Kg, then carry out tert-butanol and cyclohexane feed in the azeotropic reaction rectification column COLUMN1, cyclohexane 192Kg, 768Kg of tert-butanol, under the heating action of the azeotropic reactive distillation column COLUMN1, heated until the top temperature of the azeotropic reactive distillation column COLUMN1 is controlled at 65°C, and the temperature of the bottom of the tower is controlled at 85°C; tert-butanol and cyclohexane The binary azeotropic gas phase PG enters the settling tank DECANTER after cooling, and through the settling separation of the light phase and heavy phase of the settling tank DECANTER, the light phase separation liquid LT composed of tert-butanol and cyclohexane is refluxed to the azeotropic reaction The rectification tower COLUMN1 circulates for five hours to ensure a stable reflux balance between the azeotropic reaction rectif...

Embodiment 3

[0110] Embodiment 3: In the settling tank DECANTER, pre-inject cyclohexane 1100Kg as base material, tert-butanol 300Kg, then carry out tert-butanol and cyclohexane feed in the azeotropic reaction rectification column COLUMN1, cyclohexane 192Kg, 768Kg of tert-butanol, under the heating action of the azeotropic reactive distillation column COLUMN1, heated until the top temperature of the azeotropic reactive distillation column COLUMN1 is controlled at 65°C, and the temperature of the bottom of the tower is controlled at 85°C; tert-butanol and cyclohexane The binary azeotropic gas phase PG enters the settling tank DECANTER after cooling, and through the settling separation of the light phase and heavy phase of the settling tank DECANTER, the light phase separation liquid LT composed of tert-butanol and cyclohexane is refluxed to the azeotropic reaction The rectification tower COLUMN1 circulates for five hours to ensure a stable reflux balance between the azeotropic reaction rectif...

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 discloses a high-purity tert-butyl alcohol online recovery technology for continuously producing potassium tert-butoxide. The high-purity tert-butyl alcohol online recovery technology comprises the following operation steps: S401) transferring a heavy-phase separation liquid in a settling tank into a tert-butyl alcohol rectifying tower through a tert-butyl alcohol recovery pump; S402) evaporating and rectifying tert-butyl alcohol in the heavy-phase separation liquid under the heating action of the tert-butyl alcohol rectifying tower to form a tert-butyl alcohol gas phase of whichthe purity is not lower than 80%, extracting the tert-butyl alcohol gas phase from the tower top of the tert-butyl alcohol rectifying tower, and extracting purified water of which the purity is not lower than 99% from the tower bottom of the tert-butyl alcohol rectifying tower; and S403) cooling the tert-butyl alcohol gas phase extracted in step S4020), allowing the cooled tert-butyl alcohol gasphase to enter the settling tank, and allowing a mixed solution of tert-butyl alcohol and cyclohexane to form a light-phase separation solution of the settling tank under the settling separation action of the light phase and the heavy phase of the settling tank. The online recovery technology realizes clean, environment-friendly, efficient, continuous and stable production process of potassium tert-butoxide, no excess material is consumed in the whole production process, and no waste water or waste residues are generated.

Description

technical field [0001] The invention belongs to the preparation technology of potassium tert-butoxide, in particular to an on-line recovery process of high-purity tert-butanol for continuous production of potassium tert-butoxide. Background technique [0002] Potassium tert-butoxide is an important organic base, which is much more basic than sodium hydroxide and potassium hydroxide. Due to (CH 3 ) 3 The inductive effect of CO-three methyl groups makes it more basic and active than other potassium alkoxides, so it is a good catalyst and is widely used in various organic synthesis fields such as chemical industry, medicine, and pesticides In, for example, transesterification, condensation, rearrangement, polymerization, ring opening and preparation of heavy metal orthoesters, etc. Specifically, potassium tert-butoxide can be used to catalyze Michael addition reaction, Pinacol rearrangement reaction and Ramberg-Backlund rearrangement reaction, to prepare condensing agent of ...

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): C07C29/70C07C29/80C07C29/76C07C31/12C07C31/30
CPCC07C29/70C07C29/80C07C29/76
Inventor 黄辉
Owner 江苏天泽新材料有限公司
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