Method for preparing methyl ethyl carbonate by adopting pipeline continuous reactor
A technology of ethyl methyl carbonate and pipeline reactor, applied in the purification/separation of carbonate/haloformate, preparation of carbon dioxide or inorganic carbonate, organic chemistry, etc., can solve the problem of long synthesis route and high energy consumption , the conversion rate of reactants and the low selectivity of products, etc., to achieve the effect of short time consumption, low energy consumption and low cost
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Embodiment 1
[0045] 1. Pipeline continuous catalytic reaction: carbon dioxide, methanol, and ethanol react under the conditions of high-temperature and high-pressure catalysts (main components: aluminum oxide, zirconium phosphate, cerium oxide, and nickel) to finally generate ethyl methyl carbonate;
[0046] 1) 99% CO from CO2 storage tank 2 After pressurization, it is added from the middle and lower part of the pipeline reactor, and the raw materials methanol and ethanol (mass ratio 0.9:1.1) are mixed according to the proportion and then pumped from the middle and upper part of the pipeline reactor.
[0047] 2) CO 2 : The mass ratio of methanol and ethanol mixed alcohol (including methanol and ethanol returned to the pipeline after being separated from the top of the T3 tower) is 3:2.
[0048] 3) The operating pressure of the pipeline reactor is 4Mpa, and the reaction temperature is 120°C. The inside of the pipeline reactor is filled with fillers and catalysts (composed of aluminum oxide...
Embodiment 2
[0062] 1. Pipeline continuous catalytic reaction: carbon dioxide, methanol, and ethanol react under the conditions of high-temperature and high-pressure catalysts (main components: aluminum oxide, zirconium phosphate, cerium oxide, and nickel) to finally generate ethyl methyl carbonate;
[0063] 1) 99% CO from CO2 storage tank 2 After pressurization, it is added from the middle and lower part of the pipeline reactor, and the raw materials methanol and ethanol (mass ratio 1.2:1.5) are mixed according to the proportion and then pumped from the middle and upper part of the pipeline reactor.
[0064] 2) CO 2 : The mass ratio of methanol and ethanol mixed alcohol (including methanol and ethanol returned to the pipeline after being separated from the top of the T3 tower) is 5:3.
[0065] 3) The operating pressure of the pipeline reactor is 5Mpa, and the reaction temperature is 150°C. The inside of the pipeline reactor is filled with fillers, catalysts (composed of aluminum oxide, z...
Embodiment 3
[0075] 1. Pipeline continuous catalytic reaction: carbon dioxide, methanol, and ethanol react under the conditions of high-temperature and high-pressure catalysts (main components: aluminum oxide, zirconium phosphate, cerium oxide, and nickel) to finally generate ethyl methyl carbonate;
[0076] 1) 99% CO from CO2 storage tank 2 After pressurization, it is added from the middle and lower part of the pipeline reactor, and the raw materials methanol and ethanol (mass ratio 0.9:1.5) are mixed according to the proportion and then pumped from the middle and upper part of the pipeline reactor.
[0077] 2) CO 2 : The mass ratio of methanol and ethanol mixed alcohol (including methanol and ethanol returned to the pipeline after being separated from the top of the T3 tower) is 4:2.
[0078] 3) The operating pressure of the pipeline reactor is 3Mpa, and the reaction temperature is 90°C. The inside of the pipeline reactor is filled with fillers and catalysts (composed of aluminum oxide,...
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