Technology and device for synthesizing dimethyl carbonate

A technology of dimethyl carbonate and synthesis process, which is applied in the preparation of carbonate/haloformate, carbon monoxide and oxygen, preparation of organic compounds, etc. The problem of high energy consumption in liquid mixing and discharging can achieve the effect of reducing energy consumption, high yield and increasing content.

Active Publication Date: 2019-03-29
潞安化工集团有限公司 +1
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Problems solved by technology

This technique has the following disadvantages: 1) the gas-liquid mixing discharge consumes a lot of energy; 2) the water generated by the reaction stays in the reactor, causing the...

Method used

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  • Technology and device for synthesizing dimethyl carbonate
  • Technology and device for synthesizing dimethyl carbonate
  • Technology and device for synthesizing dimethyl carbonate

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Embodiment 1

[0030] The height of the upper section 1 of the I and No. II reactors of the present invention is 300 millimeters, the height of the middle section 2 is 1200 millimeters, the height of the lower section 3 is 400 millimeters, and the height of the tower kettle 4 is 300 millimeters, and the same diameter of four parts is 80 millimeters. The inlet distributor 5 is located in the middle of the upper section 1, and the outlet distributor 6 is located at 1 / 2 between the inlet distributor 5 and the top of the upper section 1. The opening ratio of the outlet distributor 6 is 15%, and the aperture is 1.5mm. The reaction section of the middle section 2 is divided into upper and lower sections, and the ceramic ball bed (7) is positioned between the two sections and the top of the upper section of the reaction section, and 1600g of Cu / AC catalysts are packed in the catalyst bed 8 in a bulk stacking mode. First add 800g of catalyst to fill up the lower part of the reaction section, then add...

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Abstract

A technology for synthesizing dimethyl carbonate adopts a two-tower continuous reaction, and comprises the following steps: a raw material liquid methanol is fed from the upper part of a gas and liquid distributor of a first reactor, flows out of the gas and liquid distributor and enters the reaction section of a reactor, a raw material gas CO is introduced to the first reactor from the bottom ofthe reaction section of the reactor, O2 is divided into 2-5 passages, O2 in the 2-5 passages except one is distributed in the reaction section of the reactor, a reaction is continuously carried out under the action of a catalyst in the reaction section to generate dimethyl carbonate, a formed mixed liquid A flows into the water separation section of the first reactor, methanol and dimethyl carbonate in the mixed A go through a bottom hydrophobic membrane and continuously downwards flow into a tower bottom to form a mixed liquid B, water permeates a surrounding hydrophilic membrane, and then iscollected and discharged, the mixed liquid B in the bottom of the first reactor enters a second reactor, a crude product is extracted from the bottom of the second reactor, and non-condensable gasesCO, O2 and CO2 obtained after the reactions in the first reactor and the second reactor are discharged from the top of the reactors. The technology has the advantages of simple process, high methanolconversion rate and low energy consumption.

Description

technical field [0001] The invention belongs to a synthesis process and device of dimethyl carbonate Background technique [0002] Dimethyl carbonate (DMC) is an environmentally friendly chemical. It is a colorless transparent liquid at room temperature, miscible with most organic solvents such as alcohols, ketones, esters and ethers, and hardly soluble in water. It has the characteristics of high oxygen content, low vapor pressure, easy volatility and low toxicity. Dimethyl carbonate molecules contain carbonyl and methyl groups, which can replace phosgene as carbonylation reagents, methyl halides and dimethyl sulfate as methylation reagents, and freon and chloroform as solvents. It can be used as an oil additive instead of methyl tert-butyl ether (MTBE), and has broad application prospects. [0003] Since Enichem successfully developed the DMC process in liquid phase oxidative carbonylation of methanol in 1983, the synthesis of DMC by oxidative carbonylation has become a ...

Claims

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Application Information

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IPC IPC(8): C07C68/00C07C69/96B01J8/04
CPCB01J8/0446B01J8/0492B01J8/0496B01J2208/00115C07C68/01C07C69/96
Inventor 郑华艳李忠周龙张国强
Owner 潞安化工集团有限公司
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