Method for preparing diethoxymethane by supported heteropolyacid catalyst
A technology of diethoxymethane and dimethoxymethane, which is applied in the field of preparation of diethoxymethane with supported heteropolyacid catalysts, can solve the problems of excessive consumption, unfavorable large-scale production, and low output, and achieve cheap raw materials Easy to get, good application prospect, high selectivity effect
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Embodiment 1
[0042] In a 200mL autoclave, add 30g dimethoxymethane, 40g ethanol and 3g catalyst, the catalyst is 33%H 3 PW 12 o 40 / SiO 2 , 33%H 4 SiW 12 o 40 / Activated carbon, 33%H 3 PMo 12 o 40 / SBA-15, 33%H 4 SiMo 12 o 40 / MCM-41, 33%H 3 PW 12 o 40 / TiO 2 and 33%H 3 PW 12 o 40 / Al 2 o 3 . The preparation method of load type heteropolyacid uses 33%H 3 PW 12 o 40 / SiO 2 As an example, the preparation process is as follows: use an aqueous solution of phosphotungstic acid with a concentration of 33 mass percent, and use SiO 2 As a carrier, the volume of the impregnating liquid is similar to the pore volume. Mix the two evenly and let it stand at room temperature for 10 hours to obtain a catalyst sample. Dry the sample at 120°C and roast at 350°C for 4 hours to obtain a mass fraction of 33%H 3 PW 12 o 40 / SiO 2 catalyst. Other catalyst preparation procedures are the same as the above process, the difference lies in one or more of the carrier, solvent (ethanol ca...
Embodiment 2
[0047] In a 200mL autoclave, the ratio of the amount of raw material dimethoxymethane and ethanol is 2:1, 1:1, 1:2, 1:3, 1:4 and 3g mass fraction is 33%H 3 PW 12 o 40 / SiO 2 Supported heteropolyacid catalyst, at room temperature with N 2 Replace the air in the kettle three times under the condition of 1.0MPa, so that the remaining air content in the kettle is less than 0.1%, and then pass 2.0MPaN again 2 , let it stand for 30 minutes, and use it to test the leak of the reactor to ensure that the device is airtight and then empty the gas in the kettle. Under the condition of ensuring no air leakage, the temperature was raised under normal pressure, the stirring speed of the reactor was 500 rpm, the reaction temperature was 120°C, the reaction pressure was 3.0 MPa, and the reaction time was 6 hours. The results of controlling the ratio of raw materials are shown in Table 2.
[0048] Table 2. The effect of different raw material ratios on the reaction activity and product sel...
Embodiment 3
[0052] In 200mL autoclave, add 30g dimethoxymethane, 40g ethanol, 3g mass fraction is 33%H 3 PW 12 o 40 / SiO 2 Supported heteropolyacid catalyst, at room temperature with N 2 Replace the air in the kettle three times under the condition of 1.0MPa, so that the remaining air content in the kettle is less than 0.1%, and then pass 2.0MPaN again 2 , let it stand for 30 minutes, and use it to test the leak of the reactor to ensure that the device is airtight and then empty the gas in the kettle. Under the condition of ensuring no air leakage, heat up under normal pressure, the stirring speed of the reactor is 500 rpm, the reaction time is 6 hours, the reaction pressure is 3.0MPa, and the reaction temperatures are 25°C, 40°C, 60°C, and 80°C respectively , 100°C, 120°C, 130°C, 140°C, 150°C, 160°C, the reaction results under different reaction temperature conditions are shown in Table 3.
[0053] Table 3.33%H 3 PW 12 o 40 / SiO 2 Effects of catalysts on the reactivity and produ...
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