Reactive distillation-vapor permeation coupling process for polyoxymethylene dimethyl ether synthesis
A technology of polyoxymethylene dimethyl ether and reactive distillation, which is applied in the preparation of organic compounds, chemical industry, sustainable manufacturing/processing, etc., and can solve problems such as complex product components, complicated separation process, and high energy consumption
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Embodiment 1
[0060] The method of the present invention is used for the polyoxymethylene dimethyl ether process of methylal and water-containing paraformaldehyde reaction under acidic conditions, and methylal and water-containing paraformaldehyde are obtained from the polyoxymethylene dimethyl ether reaction rectification tower respectively The two liquid-phase feed ports on the reaction section enter into the polyoxymethylene dimethyl ether reactive distillation column, and the methylal feed port is below the water-containing paraformaldehyde feed port. The mass ratio of formaldehyde to methylal in the raw material paraformaldehyde of the polyoxymethylene dimethyl ether reactive distillation column is 3, the working pressure of the polyoxymethylene dimethyl ether reactive distillation column is an absolute pressure of 6 atm, and the catalyst adopts Acidic resin, catalyst consumption is 200kg / m 3 , The height of the catalytic packing in the reaction section is 2.5 meters, the height of the...
Embodiment 2
[0063] The method of the present invention is used for the reaction system polyoxymethylene dimethyl ether process of methylal and water-containing paraformaldehyde under acidic conditions, and methylal and water-containing paraformaldehyde are obtained from the polyoxymethylene dimethyl ether reaction rectification tower respectively The two liquid-phase feed ports on the reaction section enter into the polyoxymethylene dimethyl ether reactive distillation column, and the methylal feed port is below the water-containing paraformaldehyde feed port. The mass ratio of formaldehyde to methylal in the raw material paraformaldehyde of the polyoxymethylene dimethyl ether reactive distillation column is 4.5, the working pressure of the polyoxymethylene dimethyl ether reactive distillation column is 7 atm absolute pressure, and the catalyst adopts Acidic molecular sieve, catalyst consumption is 100kg / m 3 , There are 15 catalytic trays in the reaction section, 25 trays in the rectifica...
Embodiment 3
[0066] The method of the invention is used in the process of preparing polyoxymethylene dimethyl ether by reacting methylal and water-containing gas-phase formaldehyde under acidic conditions. Methylal and water-containing gas-phase formaldehyde enter the polyoxymethylene dimethyl ether reactive distillation tower from the liquid-phase feed port and the gas-phase feed port on the polyoxymethylene dimethyl ether reactive distillation tower respectively, and formaldehyde The aldehyde feed port is above the water-containing vapor phase formaldehyde feed port. The mass ratio of formaldehyde to methylal in the raw material gas phase formaldehyde of the polyoxymethylene dimethyl ether reactive distillation column is 0.6, the working pressure of the polyoxymethylene dimethyl ether reactive distillation column is an absolute pressure of 2 atm, and the catalyst adopts acidic Resin, catalyst consumption is 300kg / m 3 The height of the catalytic packing in the reaction section is 4 meter...
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Abstract
Description
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Application Information
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