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

Method and equipment for separating propionaldehyde-water-acetic acid mixed liquid by combining azeotropic distillation and extraction distillation by saliferous mixed extracting agent

A technology of mixed extraction agent and azeotropic distillation, which is applied in separation methods, distillation separation, chemical instruments and methods, etc., can solve the problems of high energy consumption, high energy consumption in the separation process, complicated separation process, etc., and achieve low energy consumption , high product purity and simple process steps

Inactive Publication Date: 2009-09-30
滨海火炬科技有限公司
View PDF0 Cites 19 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Since propionaldehyde forms azeotrope with acetic acid, formaldehyde and water, the mixed product is separated by azeotropic distillation, and the reflux ratio (R) is controlled at about 10:1, which not only consumes a lot of energy, but also can only obtain about 98% of propionate. aldehyde
At present, in order to obtain high-purity propionaldehyde, more than 99% of propionaldehyde can be obtained by using calcium oxide to dry and dehydrate, and then re-distilled. However, the separation process consumes a lot of energy, and a large amount of waste liquid needs to be treated. The separation process of this method is complicated.

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 and equipment for separating propionaldehyde-water-acetic acid mixed liquid by combining azeotropic distillation and extraction distillation by saliferous mixed extracting agent
  • Method and equipment for separating propionaldehyde-water-acetic acid mixed liquid by combining azeotropic distillation and extraction distillation by saliferous mixed extracting agent
  • Method and equipment for separating propionaldehyde-water-acetic acid mixed liquid by combining azeotropic distillation and extraction distillation by saliferous mixed extracting agent

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Embodiment 1, azeotropic rectification and extractive rectification combined process and experimental device refer to respectively figure 1 , figure 2 , where 1 is the raw material storage tank, 2 is the pump, 3 is the glass rotameter, 4 is the sampler of the tower kettle, 5 is the electric heating mantle, 6 is the tower kettle, 7 is the thermometer of the tower kettle, 8 is the solvent storage tank, and 9 is the Pump, 10 is a glass rotameter, 11 is a glass fiber cotton and jacket, 12 is a filler, 13 is a sampler at the top of the tower, 14 is a return port, 15 is a thermometer at the top of the tower, 16 is an electromagnetic rod, and 17 is a condenser. Propionaldehyde-acetic acid-water mixture was analyzed by SP-6800 chromatograph, the composition is shown in Table 2, and the composition in the table is the mass content. After the raw material solution is subjected to azeotropic distillation, 98% of propionaldehyde can be obtained, and at the same time, a small amo...

Embodiment 2

[0029] Embodiment 2 is basically the same as Embodiment 1, but has the following changes:

[0030] The feed rate ratio containing sulfolane and glycerin mixed solvent (extractant) of step (2) is 1:1.5;

[0031] In the mixed solvent containing salt sulfolane and glycerin, the mass content of salt is 15%, and the volume ratio of sulfolane and glycerin is 1:1;

[0032] Described salt is sodium acetate.

Embodiment 3

[0033] Embodiment 3 is basically the same as Embodiment 1, but has the following changes:

[0034] The feed rate ratio containing sulfolane and glycerol mixed solvent (extractant) of step (2) is 1:0.5;

[0035] In the mixed solvent of salt-containing sulfolane and glycerin, the mass content of salt is 10%;

[0036] Described salt is potassium acetate.

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 method and equipment for separating propionaldehyde-water-acetic acid mixed liquid by combining azeotropic distillation and extraction distillation by saliferous mixed extracting agent. The steps are as follows: (1) performing azeotropic distillation to propionaldehyde-water-acetic acid mixed liquid, and obtaining about 98 percent of propionaldehyde at the top of an extracting and rectifying tower; (2) extracting and separating the about 98 percent of propionaldehyde by the mixed solvent of saliferous sulfolane and glycerin, obtaining over 99.8 percent of propionaldehyde at the top of the extracting and rectifying tower, and flowing out the saliferous mixed extracting agent from a tower kettle; (3) processing the saliferous mixed extracting agent by a regeneration tower and respectively obtaining 98 percent of propionaldehyde, aqueous solution containing acid and distillate containing the extracting solvent at the top of the regeneration tower; (4) returning 98 percent of propionaldehyde into a material tank of an azeotrope tower for circulation use; and (5) dewatering the aqueous solution containing acid, returning the distillate containing the extracting solvent to a mixed solvent storage tank and circularly using the saliferous mixed extracting agent. The invention has simpler process steps, high product purity, circular utilization of the mixed extracting solvent, no waste liquid emission in the production process and low energy consumption.

Description

technical field [0001] The present invention relates to an extractive distillation process of a salt-containing mixed extractant, in particular to a process for separating propionaldehyde-acetic acid-water and propionaldehyde-acetic acid systems through azeotropic rectification and salt-containing mixed extractant extractive distillation. In particular, it relates to a salt-containing mixed solvent for extraction and rectification separation of propionaldehyde and a combined separation process of azeotropic rectification and salt-containing mixed solvent. The invention will also provide equipment for use in this method. Background technique [0002] Propionaldehyde is an important organic raw material, which can be used in a series of organic synthesis. It is the raw material for producing alkyd resin, high-efficiency and low-toxicity pesticide herbicide, insecticide, fungicide, rubber accelerator, etc. The organic products made from it are widely used in coatings, plastic...

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 Applications(China)
IPC IPC(8): C07C45/82C07C47/02B01D3/00
Inventor 顾正桂
Owner 滨海火炬科技有限公司
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