Composite iron-zinc catalyst precursor, catalyst synthesized therefrom, preparation method and application thereof
A technology of catalyst and precursor, which is applied in the field of butadiene-to-butadiene reaction, can solve the problems of reduced catalyst anti-wear performance, reduced catalyst activity, low yield of catalyst butadiene, etc., and achieves short reaction time and improved Effect of selectivity, concentration of pore size distribution
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[0031] The preparation process of the catalyst of the present invention is as follows: ammonia and the acid salt mixed solution of Fe, Zn and M are continuously sprayed into the impeller 2 rotating at a high speed from the feed ports 4 and 5 provided on the impeller cover respectively, and the slurry generated by the reaction is fed by the impeller 2 falls into the reactor, part of the generated slurry enters the circulation pipe 7 through the circulation pipe inlet 6, and the circulating material is sprayed into the high-speed rotating impeller 2 from the circulating material outlet 6 provided on the impeller cover 3, and the generated slurry is discharged from the reaction The overflow port 8 at the top of the device is continuously discharged, and the discharged slurry is filtered, washed, and dried to obtain a catalyst precursor. The catalyst precursor is roasted or shaped to obtain a catalyst, wherein the reaction temperature is controlled at 10-40 ° C, and the residence ti...
Embodiment 1
[0035] Take 666.6g Fe(NO 3 ) 3 .9H 2 O, 392.04g Zn(NO 3 ) 3 .6H 2 O and 49.2g Cr(NO 3 ) 3 .9H 2 O was prepared into 3000mL metal salt solution. The mixed solution of ammonia gas and metal salt is continuously sprayed into the high-speed rotating impeller 2 from the feed ports 4 and 5 provided on the impeller cover respectively, and the slurry generated by the reaction falls into the reactor from around the impeller 2, and the generated part of the slurry Enter the circulation pipe 7 through the circulation pipe inlet 6, and the circulating material enters the high-speed rotating impeller 2 from the circulating material outlet 6 provided on the impeller cover 3, and the slurry generated by the reaction is continuously discharged from the overflow port 8 at the top of the reactor, and then filtered , washed and dried to obtain a catalyst precursor. Among them, the volume fraction of ammonia in the mixed gas is 70%, the atomizing nozzle of the liquid phase feed port, its...
Embodiment 2
[0037] Other conditions are the same as in Example 1, except that the diameter of the nozzle is changed to 18 μm, the circulation rate of the slurry and the volume ratio of the feed amount are 2.5:1, the pH value of the slurry at the overflow port is 7.6, and 49.2g Cr(NO 3 ) 3 .9H 2 O was changed to 35.6gMg(NO 3 ) 2 .6H 2 O, take the sample when reacting for 1h, and obtain the catalyst precursor a 2 and Catalyst A 2 .
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