Multi-phase chiral metal catalyst and its production
A metal catalyst and catalyst technology, applied in the direction of catalyst activation/preparation, carbon monoxide reaction preparation, catalyst carrier, etc., can solve the problems of heterogeneous hydrogen chiral formylation catalyst and related technology research, and achieve the effect of maintaining catalytic performance
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Embodiment 1
[0042] (1), 10.0 g of acid-washed, alcohol-washed, roasted silicon oxide (180 mesh, main pore diameter 9.7 nm) was vacuum activated at 180 ° C for 3 hours, and about 20 ml of rhodium chloride aqueous solution (containing 0.25 mg of chlorine hydrate Rhodium chloride), impregnated by incipient wetness method in ultrasonic vibration for 4 hours, and vacuum rotary evaporation to remove excess water. The obtained catalyst precursor was dried in a vacuum drying oven at 100° C. for about 24 hours, and then calcined in a quartz sample tube furnace at 300° C. for 3 hours to obtain the catalyst precursor. (2) Take 0.05g of the aforementioned catalyst precursor and reductively activate it in hydrogen (50ml / min) at 400°C for 3 hours. After the temperature drops to room temperature, introduce 3.2mg of chiral phosphine ligand (R)-BINAP under the protection of argon 5ml of toluene solution modification. Catalyst A modified in situ with chiral ligands was obtained.
Embodiment 2
[0044] The same as in Example 1, except that step (3) is added, after soaking at 60° C. for 3 hours, hydrogen purging is carried out to evaporate the solvent to obtain chiral pre-modified catalyst B.
Embodiment 3
[0046] Same as Example 1, except that the mesoporous carrier in step (1) is replaced with 3.4nm MCM-41. Catalyst C modified in situ with chiral ligands was obtained.
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