Modified molecular sieve capable of improving coking performance
A technology of coking performance and molecular sieve, which is applied in the direction of molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of the limitation of the stability of modified molecular sieves and the inability to fully exert the protective function of P on molecular sieves. , to achieve good heavy oil cracking ability and coke selectivity, large, medium and large pore volume, and good stability
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Embodiment 1
[0058] Get 100 grams (dry basis) NaY molecular sieve (92% of crystallinity, SiO 2 / Al 2 o 3 =4.94), pour into 1000g exchange solution (containing 0.63wt% (NH 4 ) 2 HPO 4 salt and 8.58 wt% NH 4 In the reactor of Cl), exchange at 90°C for 1h, and control the solution pH=3.0~3.5 during the exchange process, filter and wash after the exchange; after roasting at 650°C for 2h in the presence of 100% water vapor, pour the roasted product into Equipped with 1200g exchange solution (containing 0.38wt% RECl 3 and 7.8 wt% NH 4 Cl salt) in a reaction kettle, exchange at 90°C for 1h, and control the pH of the solution during the exchange process=6.0~6.5, filter after exchange, wash, and roast at 660°C for 2h in the presence of 70% water vapor to obtain the present invention Modified molecular sieve A1 that can improve coking performance, containing RE in weight percent 2 o 3 2.52%, P 1.13%, unit cell 2.440nm, crystallinity 49%.
Embodiment 2
[0060] Get 100 grams (dry basis) NaY molecular sieve (88% crystallinity, SiO 2 / Al 2 o 3 =4.78), pour into 900g exchange solution (containing 0.45wt% (NH 4 ) 2 HPO 4 salt and 10wt% (NH 4 ) 2 SO 4 ) in a reaction kettle at 90°C for 1 hour, and at the same time control the solution pH=4.0 to 4.5 during the exchange process, filter and wash after the exchange; after roasting at 650°C for 2 hours in the presence of 100% water vapor, pour the roasted product into the container 1000g exchange solution (containing 0.35wt% RECl 3and 1 wt% NH 4 Cl salt) in a reaction kettle, exchanged at 90°C for 1h, and controlled the solution pH=3.5 to 4.0 during the exchange process, filtered after the exchange, washed, and roasted at 700°C for 1h in the presence of 50% water vapor to obtain the present invention Modified molecular sieve A2 capable of improving coking performance, containing RE in weight percent 2 o 3 1.30%, P 0.58%, unit cell 2.438nm, crystallinity 45%.
Embodiment 3
[0062] Get 100 grams (dry basis) NaY molecular sieve (92% of crystallinity, SiO 2 / Al 2 o 3 =4.94), pour into 500g exchange solution (containing 1.58wt% H 3 PO 4 ) in a reaction kettle at 90°C for 2 hours, while controlling the pH of the solution to 4.0 to 4.5 during the exchange process, filtering and washing after the exchange; roasting at 600°C for 0.5h in the presence of 100% water vapor, pour the roasted product into Equipped with 400g exchange solution (containing 0.55wt% RECl 3 and 10.78wt% (NH 4 ) 2 SO 4 salt) in a reactor, exchanged at 90°C for 0.5h, and controlled the solution pH=6.0 to 6.5 during the exchange process, filtered after the exchange, washed, and roasted at 650°C for 1h in the presence of 100% water vapor to obtain the present invention Modified molecular sieve A3 capable of improving coking performance, containing RE in weight percent 2 o 3 1.44%, P 1.5%, unit cell 2.439nm, crystallinity 53%.
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