Supported zirconium sulfate catalyst, preparation method thereof and application thereof in synthesizing ethylene glycol monoethylether acetate or tributyl citrate
A technology of ethylene glycol monoethyl ether and tributyl citrate, applied in the preparation of carboxylate, chemical instruments and methods, preparation of organic compounds, etc., can solve the problem of difficult separation and recovery of catalysts, equipment corrosion, and many side reactions, etc. problems, to achieve the effect of shortening the process flow and production cycle, less usage, and no environmental pollution
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Embodiment 1
[0033] Weigh 1g of zirconium sulfate tetrahydrate, dissolve it in water, add 9g of pretreated activated carbon (see "Summary of the Invention" for the pretreatment method) into the solution, stir at room temperature for 24 hours, heat at 80°C to evaporate the water, and wet The sample was dried at 80°C for 3-5 hours to obtain a supported zirconium sulfate catalyst.
[0034] Reaction material composition:
[0035] Acetic acid 15.6g
[0036] Ethylene glycol monoethyl ether 18g
[0037] Toluene 5g
[0038] Catalyst 0.9g
[0039] Add the above materials into the esterification reactor, heat to 120°C, and react at this temperature for 4 hours, then filter the reaction liquid, recover the catalyst, and rectify the filtrate to obtain the product ethylene glycol monoethyl ether acetic acid ester. The conversion rate of ethylene glycol monoethyl ether is 94.2%, and the selectivity of the target product is 100%.
[0040] The above-mentioned supported zirconium sulfate catalyst is ...
Embodiment 2
[0045]Basically the same as Example 1, but with the following changes: the amount of zirconium sulfate tetrahydrate and activated carbon in the catalyst preparation were 2g and 8g respectively. The conversion rate of ethylene glycol monoethyl ether was 94.9%, and the selectivity of the target product was 100%.
[0046] In the synthetic process step of ethylene glycol monoethyl ether acetate, the mass ratio of ethylene glycol monoethyl ether and acetic acid is 1:1.13 (mol ratio is 1:1.7), and the mass ratio of ethylene glycol monoethyl ether and catalyst is 1: 0.05.
Embodiment 3
[0048] Basically the same as Example 1, but with the following changes: the amount of zirconium sulfate tetrahydrate and activated carbon in the preparation of the catalyst were 3g and 7g respectively. The conversion rate of ethylene glycol monoethyl ether was 95.7%, and the selectivity of the target product was 100%.
[0049] Synthetic process for tributyl citrate:
[0050] Esterification reaction conditions: the mass ratio of citric acid to n-butanol is 1:1.76 (molar ratio is 1:5), and the catalyst is 3% of the total mass of reactants.
[0051] Reaction process:
[0052] Add the prepared catalyst and reaction materials into the esterification reactor at one time according to the above material ratio, heat to the reaction temperature of 110-140°C, and react for 4 hours. After the reaction, filter the mixture in the reactor, recover the catalyst, and react Liquid filtration, neutralize the filtrate with anhydrous sodium carbonate solution, then wash the organic layer with wa...
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