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

Reactive distillation process device and method for synthesis of PODEn (polyoxymethylene dimethyl ethers)

A polymethoxy dimethyl ether, process method technology, applied in chemical instruments and methods, preparation of organic compounds, chemical industry and other directions, can solve the problem of high manufacturing cost, large circulating flow rate, and anhydrous trioxane market. high price problem

Active Publication Date: 2019-08-02
TIANJIN UNIV
View PDF13 Cites 5 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the preparation of existing anhydrous paraformaldehyde requires extraction and multi-step rectification processes, the manufacturing cost is relatively high, the market price of anhydrous paraformaldehyde is relatively high, and the preparation process of polyoxymethylene dimethyl ether is economically limited. Moreover, the reaction in the reactor is still limited by the reaction balance, the reaction conversion rate and target product selectivity are still not high, the flow rate of the circulating stream is relatively large, and the process economy needs to be further improved

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
  • Reactive distillation process device and method for synthesis of PODEn (polyoxymethylene dimethyl ethers)
  • Reactive distillation process device and method for synthesis of PODEn (polyoxymethylene dimethyl ethers)
  • Reactive distillation process device and method for synthesis of PODEn (polyoxymethylene dimethyl ethers)

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0059] The method of the present invention is used for the reaction system polyoxymethylene dimethyl ether process of methylal and paraformaldehyde under acidic conditions, which is the same as the process described in the present invention, including a polyoxymethylene dimethyl ether reactive distillation tower, a Class product refining tower, secondary product refining tower, light component separation tower, methylal mixer, DMM2 mixer. Methylal and paraformaldehyde enter the polyoxymethylene dimethyl ether reactive distillation column from the two liquid-phase feed ports on the reaction section respectively, and the methylal feed port is below the paraformaldehyde feed port . The mass ratio of polyoxymethylene dimethyl ether reactive distillation column raw material paraformaldehyde to methylal is 4.5, the working pressure of polyoxymethylene dimethyl ether reactive distillation column is absolute pressure 4atm, and the top reflux ratio is 0.5, The catalyst is an acidic re...

Embodiment 2

[0062] The method of the present invention is used for the polyoxymethylene dimethyl ether process of methylal and paraformaldehyde reaction under acidic conditions, is identical with the flow process described in the present invention, comprises polyoxymethylene dimethyl ether reactive rectification tower, a Class product refining tower, secondary product refining tower, light component separation tower, methylal mixer, DMM2 mixer. Methylal and paraformaldehyde enter the polyoxymethylene dimethyl ether reactive distillation column from two liquid-phase feed ports on the reaction section respectively, and the methylal feed port is below the paraformaldehyde feed port . The mass ratio of polyoxymethylene dimethyl ether reactive distillation column raw material paraformaldehyde to methylal is 2, the working pressure of polyoxymethylene dimethyl ether reactive distillation column is absolute pressure 2atm, and the top reflux ratio is total reflux , the catalyst is an acidic mole...

Embodiment 3

[0065] The process of using the method of the present invention for the reaction of methylal and gas-phase formaldehyde under acidic conditions to prepare polyoxymethylene dimethyl ether is the same as the process described in the present invention, including a polyoxymethylene dimethyl ether reactive distillation column, a first-stage Product refining tower, secondary product refining tower, light component separation tower, methylal mixer, DMM2 mixer. Methylal and gas-phase formaldehyde enter into the polyoxymethylene dimethyl ether reactive distillation column respectively from the liquid-phase feed port on the reaction section and the gas-phase feed port of the stripping section, and the methylal feed port is at Above the gas phase formaldehyde feed port. The mass ratio of gaseous formaldehyde and methylal in the polyoxymethylene dimethyl ether reactive distillation column raw material is 0.6, the working pressure of the polyoxymethylene dimethyl ether reactive distillatio...

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 reactive distillation process device and method for synthesis of PODEn (polyoxymethylene dimethyl ethers). According to the method, industrial methylal for product chain termination and one or a mixture of two or more of trioxymethylene, paraformaldehyde and gas-phase formaldehyde for product chain propagation are taken as raw materials, no water exits in a reaction system, a PODEn mixed product with multiple degrees of polymerization is obtained through a reaction under the action of an acidic catalyst, a reaction product with the degree of polymerization higher than2 is recovered from the column bottom under the separation action of a PODEn reactive distillation reaction column, and DMM2 with low degree of polymerization and incompletely reacted methylal are recovered from the column top; a product recovered from the column bottom is separated by a production refinery column, a target product DMM3-5 is obtained, DMM2 with low degree of polymerization and DMM6-10 with high degree of polymerization are returned to the PODEn reactive distillation reaction column; incompletely reacted methylal is recycled as a raw material. By use of the characteristic of reactive distillation, excessive methylal is adopted in the reaction process, the conversion rate of formaldehyde substances is substantially increased, and the selectivity and the yield of DMM3-5 are increased.

Description

technical field [0001] The invention belongs to the technical field of chemical production technology and equipment, and relates to polyoxymethylene dimethyl ether, which is a reactive distillation process device and method for synthesizing polyoxymethylene dimethyl ether. Background technique [0002] Polyoxymethylene dimethyl ether is a low-molecular-weight acetal polymer with methoxy as the main chain, and its structural formula is: CH3O(CH2O)nCH3, referred to as DMMn (or PODEn). When n=3~8 (especially 3~5), the substance has a higher cetane number and oxygen content, and there is no sulfur element in the substance, it is a kind of diesel oxygen enhancer with excellent performance, which can Significantly reduce the emission of carbon monoxide and nitrogen oxides in the exhaust of diesel vehicles, without producing sulfur compounds. At the same time, the addition of the substance can improve the combustion performance of diesel without modifying the engine of the vehicle...

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): C07C43/30C07C41/56C07C41/58
CPCC07C41/56C07C41/58C07C43/30Y02P20/10
Inventor 高鑫孟莹李洪李鑫钢从海峰韩振为
Owner TIANJIN UNIV
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