Preparation method of 1,4-dioxane produced by dehydrating ethylene glycol
A technology of dioxane and ethylene glycol, applied in 1 field, can solve the problems of repeated use limitation, poor high temperature resistance, etc., and achieve the effects of easy recycling, mild catalytic performance, and broad industrial application prospects.
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Embodiment 1
[0029] Activated carbon was impregnated with KCl, dried at 100 °C for 12 h, and then calcined at 450 °C for 4 h to obtain a catalyst with a loading capacity of 8% KCl / AC.
[0030] The KCl / AC catalyst with a loading of 8% was activated at 300 °C for 2 h.
[0031] In the fixed bed reactor, ethylene glycol is used as the raw material, and the mass space velocity is controlled at 0.3h -1 , the reaction temperature is 200℃, under this condition, ethylene glycol and the activated supported KCl / AC catalyst were reacted for 12 h to obtain 1,4-dioxane.
[0032] Reaction results: The average conversion rate of ethylene glycol was 53%, and the selectivity of 1,4-dioxane was maintained at 60%.
Embodiment 2
[0034] The activated carbon was impregnated with CsCl, dried at 120 °C for 12 h, and then calcined at 450 °C for 4 h to obtain a CsCl / AC catalyst with a loading of 5 wt%.
[0035] The CsCl / AC catalyst with a loading of 5 wt % was activated at 300 °C for 2 h.
[0036] In the fixed bed reactor, ethylene glycol is used as the raw material, and the mass space velocity is controlled at 0.3h -1 , the reaction temperature was 300°C, under this condition, ethylene glycol and the activated CsCl / AC catalyst with a loading of 5% were reacted for 12 h to obtain 1,4-dioxane.
[0037] Reaction results: The average conversion rate of ethylene glycol was 91%, and the selectivity of 1,4-dioxane was maintained at 58%.
Embodiment 3
[0039] Activated carbon was treated with SrCl 2 After impregnation, it was dried at 120 °C for 12 h, and then calcined at 450 °C for 4 h to obtain SrCl with a loading capacity of 15 wt %. 2 / AC Catalyst.
[0040] The catalyst with a loading of 15 wt % was activated at 250 °C for 2 h.
[0041] In the fixed bed reactor, ethylene glycol is used as the raw material, and the mass space velocity is controlled at 0.6h -1 , the reaction temperature is 270 ° C, under this condition, ethylene glycol and activated SrCl with a loading of 15% 2 / AC catalyst for 12 h to obtain 1,4-dioxane.
[0042]Reaction result: The average conversion rate of ethylene glycol is 99%, and the selectivity of 1,4-dioxane is 66%.
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