Method for producing oxalate by coupling carbon monoxide(CO)
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 selectivity of oxalate ester and low utilization rate of nitrite ester, so as to avoid thermal or catalytic decomposition , the effect of good technical effect
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Embodiment 1
[0020] Using CO and methyl nitrite as raw materials, wherein the molar ratio of CO and methyl nitrite is 1.2:1, palladium-supported alumina is used as a catalyst, and the weight content of metal palladium is 1.5% based on the weight of the carrier. The CO and methyl nitrite raw materials first enter the crystallizer, remove water and alcohol at a temperature of -20°C, and the obtained effluent I enters a coupling reactor at a reaction temperature of 120°C and a reaction pressure of -0.05MPa. Airspeed is 1000 hours -1 Contact with a palladium-containing catalyst under certain conditions to generate a reaction effluent containing dimethyl oxalate. The reaction results are: the single-pass conversion rate of CO is 62.3%, and the selectivity of dimethyl oxalate is 98.2%.
Embodiment 2
[0022] Using CO and methyl nitrite as raw materials, wherein the molar ratio of CO to methyl nitrite is 1.5:1, palladium-supported alumina is used as a catalyst, and the weight content of metal palladium is 0.5% based on the weight of the carrier. The CO and methyl nitrite raw materials first enter the crystallizer, remove water and alcohol at a temperature of -10°C, and the obtained effluent I enters the coupling reactor at a reaction temperature of 130°C and a reaction pressure of 0.05MPa. Speed is 2000 hours -1 Contacting with a palladium-containing catalyst under certain conditions produces a reaction effluent containing dimethyl oxalate, and the reaction results are: the single-pass conversion rate of CO is 55.4%, and the selectivity of dimethyl oxalate is 97.9%.
Embodiment 3
[0024] Using CO and ethyl nitrite as raw materials, wherein the molar ratio of CO to ethyl nitrite is 1:1, palladium-loaded ZSM-5 molecular sieve is used as catalyst (Si / Al molar ratio is 550:1), and the carrier weight As a benchmark, the weight content of metal palladium is 0.8%, CO and ethyl nitrite raw materials first enter the cooler, remove water and alcohol under the condition of temperature-8 ° C, and the effluent I obtained enters the coupling reactor and reacts The temperature is 140°C, the reaction pressure is 0.1MPa, and the reaction space velocity is 3000 hours -1 Contact with a palladium-containing catalyst under certain conditions to generate a reaction effluent containing diethyl oxalate. The reaction results are: the single-pass conversion rate of CO is 66.4%, and the selectivity of diethyl oxalate is 99.1%.
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