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Pervaporation-normal pressure rectification integrated process for separating dimethyl carbonate and methanol

A technology of dimethyl carbonate and atmospheric distillation, which is applied to the preparation of organic carbonates, the separation/purification of hydroxyl compounds, the purification/separation of carbonates/haloformates, etc., to reduce energy consumption and simplify production The effect of low process and operation cost

Active Publication Date: 2015-02-25
JIANGSU JIUMO HIGH TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the pervaporation-distillation integrated process still needs to be improved in the production process of dimethyl carbonate. For example, most of the high-concentration by-product methanol will still be added to the reactive distillation column as a reactant. On the premise of maintaining the quality of dimethyl ester products, further simplify the production process, thereby reducing more energy consumption and reducing operating costs, and there is still innovation work to be done

Method used

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  • Pervaporation-normal pressure rectification integrated process for separating dimethyl carbonate and methanol

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Experimental program
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Effect test

Embodiment 1

[0024] like figure 1 As shown, the azeotropic mixture of dimethyl carbonate and methanol is obtained at the top of reactive distillation column 1, the temperature is 64°C, the content of dimethyl carbonate is 30% (by mass fraction, the same below), and the content of methanol is 70% . The azeotropic mixture first enters the buffer tank 2, and then is transported to the pervaporation membrane system 4 by the liquid delivery pump 3 at 40°C, and contacts with the polydimethylsiloxane-polyvinylidene fluoride composite membrane. The pervaporation membrane system 4 includes a membrane module, a condenser and a vacuum pump, and the downstream side of the membrane is evacuated by a vacuum pump to maintain a vacuum degree of 100Pa. Due to the difference in pervaporation membrane selectivity for methanol and dimethyl carbonate adsorption, the pervaporation process breaks the methanol-dimethyl carbonate azeotropic equilibrium, and the retentate side is condensed by the condenser to obta...

Embodiment 2

[0026] like figure 1As shown, the azeotropic mixture of dimethyl carbonate and methanol is obtained at the top of the reactive distillation column 1, and the temperature is 64°C. The azeotropic mixture first enters the buffer tank 2, and then uses the liquid delivery pump 3 to transport to In the pervaporation membrane system 4, it is in contact with polydimethylsiloxane-polyvinylidene fluoride-nano titanium dioxide composite membrane. The pervaporation membrane system 4 includes a membrane module, a condenser and a vacuum pump, and the downstream side of the membrane is evacuated by a vacuum pump to maintain a vacuum degree of 2000Pa. Due to the difference in pervaporation membrane selectivity for methanol and dimethyl carbonate adsorption, the pervaporation process breaks the methanol-dimethyl carbonate azeotropic equilibrium, and the retentate side is condensed by the condenser to obtain a concentration of dimethyl carbonate of 10.3 wt% feed liquid a, feed liquid b with a ...

Embodiment 3

[0028] The azeotropic mixture of dimethyl carbonate and methanol is obtained at the top of the reactive distillation column 1, and the temperature is 64°C. The azeotropic mixture first enters the buffer tank 2, and then is transported to the pervaporation membrane by the liquid delivery pump 3 at 20°C In system 4, contact with a polydimethylsiloxane-silica-zirconia support layer composite membrane that is preferentially permeable to methanol. The pervaporation membrane system 4 includes a membrane module, a condenser and a vacuum pump, and the downstream side of the membrane is evacuated by a vacuum pump to maintain a vacuum degree of 10100 Pa. Due to the difference in pervaporation membrane selectivity for methanol and dimethyl carbonate adsorption, the pervaporation process breaks the methanol-dimethyl carbonate azeotropic equilibrium, and the retentate side is condensed by the condenser to obtain a concentration of dimethyl carbonate of 48.4 wt% feed liquid a, feed liquid b...

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Abstract

The invention provides a pervaporation-normal pressure rectification integrated process for separating dimethyl carbonate and methanol. The process is characterized in that when the azeotropic solution of dimethyl carbonate and methanol obtained in a reactive rectification tower passes through a pervaporation membrane system and due to the difference of the adsorption permselectivity of a pervaporation membrane to components, the methanol-dimethyl carbonate azeotropic bottleneck is effectively broken, the low-concentration side dimethyl carbonate liquid is returned to the reactive rectification tower for cyclic separation, while the high-concentration side dimethyl carbonate liquid is conveyed to a normal pressure rectification tower and separated by the normal pressure rectification tower to obtain the dimethyl carbonate product having the quality purity of more than 99.6% at the bottom of the tower, and the methanol-dimethyl carbonate azeotropic liquid obtained at the top of the tower is mixed with the azeotropic liquid of the reactive rectification tower for next cyclic separation. According to the pervaporation-normal pressure rectification integrated process for separating dimethyl carbonate and methanol, the quality of the dimethyl carbonate product is improved at low energy consumption and the production process and equipment are simplified; the process has the advantages of simplicity and convenience in operation, economic efficiency, adjustability, high integrity and the like.

Description

technical field [0001] The invention relates to a process for the integrated separation of dimethyl carbonate and methanol by pervaporation-atmospheric rectification, and belongs to the technical field of dimethyl carbonate separation. Background technique [0002] Dimethyl Carbonate (Dimethyl Carbonate, referred to as DMC) is a green chemical product that meets the requirements of modern "clean technology" and is environmentally friendly. It is also an important organic synthesis intermediate and starting material. Phenols, alcohols, amines, hydrazines, and esters react to synthesize many compounds with special properties; secondly, DMC has excellent solubility properties, and can be used as a low-toxicity solvent and cleaning agent in the fields of medicine, coatings, batteries, etc.; in addition, DMC The oxygen content reaches 53.3%. As a gasoline additive, it can increase the octane number of gasoline, improve combustion efficiency, and reduce exhaust pollution. [0003...

Claims

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Application Information

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IPC IPC(8): C07C31/04C07C29/76C07C69/96C07C68/06C07C68/08
CPCC07C68/06C07C68/08C07C69/96Y02P20/10
Inventor 丁晓斌南江普杜运平曹明明
Owner JIANGSU JIUMO HIGH TECH CO LTD
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