Modified molecular sieve capable of improving coking performance
A technology of coking performance and molecular sieve, applied in molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of the stability limitation of modified molecular sieves, the modulation performance not fully exerting the protection function of P on molecular sieves, etc. , to achieve the effect of 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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