Composite carrier catalyst used for glycol and synthesized from hydrogenation of alkyl oxalate, and preparation method thereof
A technology of alkyl oxalate and composite carrier, which is used in catalyst activation/preparation, hydroxyl compound preparation, chemical instruments and methods, etc., to achieve the effects of ensuring thermal stability, improving dispersibility and poor thermal stability
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Embodiment 1
[0024] A kind of preparation method of composite carrier catalyst for hydrogenation of alkyl oxalate to synthesize ethylene glycol, comprises the following steps:
[0025] In the first step, take 22.80g of 25wt% silica sol, dilute it to 200ml with deionized water, adjust the pH value to 3.0, and make solution I;
[0026] In the second step, 4.29g of cerium nitrate was dissolved in 100ml of deionized water, and the pH value was adjusted to 3.0 to form solution II;
[0027] The third step is to dissolve 12.00g urea in 100ml deionized water to form solution III;
[0028] The fourth step is to dissolve 12.08g copper nitrate in 200ml deionized water, adjust the pH value to 3.0, and make solution IV;
[0029] The fifth step is to add solution I, solution II, and solution III together dropwise and mix them, stir vigorously, and age at 90°C for 3 hours, then slowly add solution IV to the mixed solution dropwise, continue to age for 16 hours, and filter and wash to obtain a filter cak...
Embodiment 2
[0035] According to the steps and conditions of Example 1, only the catalyst composition is 25%CuO / 65%SiO 2 -10%B 2 o 3 . Using dimethyl oxalate as raw material, methanol as solvent, at a reaction temperature of 240°C, a reaction pressure of 3.0MPa, and a liquid hourly space velocity of 2.0h -1 , under the condition of hydrogen ester ratio of 200, the conversion rate of dimethyl oxalate is greater than 99.9%, and the selectivity of ethylene glycol is greater than 95%.
Embodiment 3
[0037] According to the steps and conditions of Example 1, only the catalyst composition is 35%CuO / 55%TiO 2 -10% ZrO 2 . Using dimethyl oxalate as raw material, methanol as solvent, at a reaction temperature of 240°C, a reaction pressure of 5.0MPa, and a liquid hourly space velocity of 1.0h -1 , under the condition of hydrogen ester ratio of 160, the conversion rate of dimethyl oxalate is greater than 99.9%, and the selectivity of ethylene glycol is greater than 95%.
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