Process for improving the catalytic activity of catalyst systems for reductive amination of aliphatic cyanoaldehydes to aliphatic diamines
A technology for the reduction of aldehydes to amines and catalytic activity, which can be used in chemical instruments and methods, preparation of reductive alkylation, preparation of amino compounds, etc., and can solve the problems of short catalyst life and low yield
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Embodiment 1
[0053] A reactor mixture was prepared by combining crude cyanaldehyde (where the cyanaldehyde contained 85-90 wt% cyanaldehyde) and t-butanol (t-butanol) to obtain a crude cyanaldehyde concentrate of approximately 70 wt%. The mixture was passed through a bed of sodium carbonate. The reactor tube was charged with 7.0 g of BASF Co-0179T catalyst and diluted with 100 grit (150 μm) SiC (silicon carbide) fines. The temperature of the reactor was raised to 250°C. Under continuous hydrogen flow, the temperature of the reactor was maintained at 250°C for 14 hours, then the temperature was lowered to about less than 80°C. Once the temperature of the reactor was lowered to less than 80°C, an excess flow of ammonia (approximately 3-5 times the desired set point as described below) was introduced into the reactor. The temperature and pressure are then changed to the desired set points, ie about 100°C and about 1400 psig. After at least one hour, reduce the ammonia rate to the desired s...
Embodiment 2
[0055] A reactor mixture was prepared by combining crude cyanaldehyde (where the cyanaldehyde contained 85-90 wt% cyanaldehyde) and t-butanol (t-butanol) to obtain a crude cyanaldehyde concentrate of approximately 70 wt%. The mixture was passed through a bed of sodium carbonate. The reactor tube was charged with 7.0 g of BASF Co-0179T catalyst and diluted with 100 grit (150 μm) SiC (silicon carbide) fines. The temperature of the reactor was raised to 233°C. Under continuous hydrogen flow, the temperature of the reactor was maintained at 233°C for 14 hours, then the temperature was lowered to about less than 80°C. Once the temperature of the reactor is lowered to less than 80 °C. An excess flow of ammonia (approximately 3-5 times the desired set point as described below) is then introduced into the reactor. The temperature and pressure are then changed to the desired set points, ie about 100°C and about 2000 psig. After at least one hour, reduce the ammonia rate to the desi...
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