Method for producing oxalic ester by CO coupling
An oxalate ester and coupling technology, which is applied in the direction of carbon monoxide or formate reaction preparation, organic chemistry, etc., can solve the problems of low single-pass conversion rate of raw materials and low selectivity of oxalate ester
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Embodiment 1
[0025]Using CO and methyl nitrite as raw materials, wherein the molar ratio of CO and methyl nitrite is 1.2:1, the high-gravity rotating bed reactor is loaded with palladium-loaded alumina catalyst, based on the carrier, the weight content of palladium Both are 1.5%. CO and methyl nitrite raw materials enter the rotary bed reactor to contact with the catalyst. At a reaction temperature of 100°C, the reaction pressure is -0.01MPa; The result of the reaction is: the single pass conversion rate of CO is 62.3%, and the selectivity of dimethyl oxalate is 97.2%.
Embodiment 2
[0027] Using CO and methyl nitrite as raw materials, wherein the molar ratio of CO to methyl nitrite is 1.5:1, the high-gravity rotating bed reactor is loaded with palladium-loaded alumina catalyst, based on the carrier, the weight content of palladium Both are 0.5%, CO and methyl nitrite raw materials enter the rotating bed reactor to contact with the catalyst, at a reaction temperature of 150°C, and a reaction pressure of -0.06MPa; under the condition of the rotating speed of the rotor of the high gravity rotating bed reactor being 2000rpm, its The result of the reaction is: the single-pass conversion rate of CO is 55.4%, and the selectivity of dimethyl oxalate is 97.9%.
Embodiment 3
[0029] Using CO and ethyl nitrite as raw materials, wherein the molar ratio of CO to ethyl nitrite is 1:1, a palladium-loaded ZSM-5 molecular sieve catalyst (Si / Al molar ratio of 150 : 1), taking the carrier as a benchmark, the weight content of palladium is 0.8%, CO and ethyl nitrite raw materials enter the rotating bed reactor to contact with the catalyst, at the reaction temperature of 120 ° C, the reaction pressure is -0.02MPa; Under the condition that the rotating speed of the rotor of the bed reactor is 5000 rpm, the reaction result is as follows: the single-pass conversion rate of CO is 66.4%, and the selectivity of diethyl oxalate is 98.1%.
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