Catalyst for preparing fatty alcohol with low carbon number by catalyzing and hydrolyzing glycerol and preparation method thereof
A catalytic hydrogenolysis and catalyst technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, chemical instrument and method, etc., can solve the problem of strengthening the catalyst, unfavorable effective utilization of glycerin production, and reaction conditions Harsh and other issues
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Embodiment 1
[0044] Using ZrOCl 2 ·8H 2 O aqueous solution and 25-28% ammonia water to prepare zirconium hydroxide by precipitation method. Use (NH 4 ) 6 W 12 o 39 ·xH 2 O solution impregnates the dried and ground zirconium hydroxide, evaporates the impregnating solution to dryness, and then dries the obtained solid at 110°C and roasts at 823°C to obtain a strongly acidic catalyst carrier tungstate-promoted zirconia (WO x / ZrO 2 ). The tungsten content of the support was 15% by weight. Use H 2 PtCl 6 ·6H 2 O, Cu(OH) 2 ·3H 2 O, RhCl 3 ·xH 2 O, Ni(NO 3 ) 2 ·6H 2 O, Co(NO 3 ) 2 ·6H 2 O, NH 4 ReO 4 , IrCl 3 ·xH 2 O, OsCl 3 ·3H 2 O and RuCl 3 ·xH 2 Aqueous solution of O and PdCl 2 The hydrochloric acid solution was impregnated with WO x / ZrO 2 , and then sequentially dried at 110°C and calcined at 823°C to prepare a series of metal-acidic bifunctional catalysts. The metal content in each catalyst was 5 wt%.
[0045] Weigh 0.5g of catalyst, mix it with a certain...
Embodiment 2
[0052] Using RhCl 3 ·xH 2 The catalyst Rh / ZrO 2 , Rh / WO 3 , Rh / SiO 2 , Rh / Al 2 o 3 , Rh / USY, Rh / TiO 2 -SiO 2 and Rh / Al 2 o 3 -SiO 2 , for the catalyst Rh / WO with the highest activity in Example 1 x / ZrO 2 Compare. The Rh content in the prepared catalysts was all 5wt%.
[0053] According to the same method as in Example 1, the activity of the catalyst prepared above on the hydrogenolysis reaction of glycerol was investigated through experiments #11-#17, and the reaction conditions and results are listed in Table 2. The conversion rate of glycerol obtained in Table 2 is significantly lower than that using the strong acid carrier WO x / ZrO 2 Prepared Catalyst Rh / WO x / ZrO 2 response results.
[0054] Table 2 Catalytic activity of Rh catalysts loaded on different supports for glycerol hydrogenolysis reaction
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[0056]
Embodiment 3
[0058] Different acidic supports MoO were prepared by the following two steps x / ZrO 2 、BO x / ZrO 2 、WO x / TiO 2 and WO x / Fe 2 o 3 . 1) Using ZrOCl 2 ·8H 2 O and Fe(NO 3 ) 3 9H 2 Aqueous solution of O and TiCl 4 hydrochloric acid solution, respectively, and 25-28% ammonia water for precipitation reaction to prepare the corresponding metal hydroxide. 2) using (NH 4 ) 6 Mo 7 o 24 4H 2 O, H 3 BO 3 and (NH 4 ) 6 W 12 o 39 ·xH 2 O aqueous solution was impregnated with the obtained metal hydroxide, and the evaporated solid was dried at 110° C. and calcined at different temperatures shown in Table 3 to obtain a catalyst carrier. The contents of molybdenum, boron and tungsten in the prepared carrier are all 15wt%. Using the same method in Example 2, Rh (5wt%) is loaded onto the prepared acidic carrier to prepare the catalyst Rh / MoO x / ZrO 2 , Rh / BO x / ZrO 2 , Rh / WO x / TiO 2 and Rh / WO x / Fe 2 o 3 , for Rh / WO with the highest activity in Example 1 x...
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