Catalyst precursor for synthesizing 1,4-butynediol, catalyst synthesized therefrom and preparation method thereof
A technology of butyne diol and catalyst, which is applied in the preparation of organic compounds, chemical instruments and methods, preparation of hydroxyl compounds, etc., can solve the problem that copper species cannot be converted into active center alkyne copper complexes, poor dispersion of active components, Easy to lose active components and other problems, to achieve the effect of short reaction time, stable product properties, and concentrated pore size distribution
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[0030]The preparation process of the catalyst of the present invention is as follows: Ammonia and Cu, Bi, Al acid salt mixed solutions are continuously sprayed into the impeller 2 rotating at 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 Fall into the reactor from all sides, the generated part of the 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 reactor The overflow port 8 on the top is continuously discharged, and the discharged slurry is the catalyst precursor, which is spray-dried and roasted to obtain the catalyst, wherein the reaction temperature is controlled at 30-40°C, the residence time is 5-20min, and the pH of the slurry discharged from the...
Embodiment 1
[0033] Take 120.8g Cu(NO 3 ) 2 .3H 2 O, 404g Al(NO 3 ) 3 .9H 2 O and 10.4g Bi(NO 3 ) 3 .5H 2 O prepared into 2000mL 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 is spray-dried Obtain catalyst precursor a, and roast the precursor to obtain catalyst A 1 . Among them, the volume fraction of ammonia in the mixed gas is 60%, the atomization nozzle of the liq...
Embodiment 2
[0035] Other conditions are the same as in Example 1, except that the diameter of the nozzle is changed to 12 μm, the volume ratio of the circulation rate of the slurry to the feed rate is 2.5:1, and the pH value of the slurry at the overflow port is 6.5, and the sample taken during the reaction for 1 hour is obtained to obtain the catalyst precursor a 2 and Catalyst A 2 .
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