A kind of porous material with high cracking activity and its preparation method
A porous material and cracking activity technology, which is applied in chemical instruments and methods, cracking, catalytic cracking, etc., can solve the problems of increasing filtrate and waste residue treatment costs, high reuse costs, and improvement, to achieve product distribution optimization and strong cracking activity , the effect of a high ratio
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Embodiment 1
[0033] This example illustrates the porous material of the present invention and its preparation.
[0034] Add an appropriate amount of deionized water into the container, heat up to 50°C, and simultaneously crystallize the NaY molecular sieve mother liquor (concentration 55gSiO 2 / L, suspended matter concentration 39mg / L) and sodium metaaluminate solution (102gAl 2 o 3 / L, caustic ratio 2.55) join in the container and carry out continuous reaction and control pH value is 13.8, then concentration is 60gAl 2 o 3 / L Al 2 (SO 4 ) 3 Add the solution to the above slurry, and make the final pH value of the slurry system 9.4, continue to heat up to 80°C and treat for 2 hours, filter and wash the obtained solid precipitate according to the dry basis of the precipitate: ammonium salt: H 2 The weight ratio of O=1:1:10 was exchanged at 60° C. for 0.5 hours. After filtration and washing, the exchange process was repeated once. After filtration, the porous material provided by the pr...
Embodiment 2
[0039] This example illustrates the porous material of the present invention and its preparation.
[0040] Add an appropriate amount of deionized water into the container, heat up to 40°C, and simultaneously crystallize the NaY molecular sieve filtrate (concentration 41gSiO 2 / L, suspended matter concentration 2112mg / L) and sodium metaaluminate solution (159gAl 2 o 3 / L, caustic ratio 1.65) join in the container and carry out continuous reaction and control pH value is 13.6, then concentration is 60gAl 2 o 3 / L Al 2 (SO 4 ) 3 Add the solution to the above slurry, and make the final pH value of the slurry system 10.3, continue to heat up to 60°C and treat for 4 hours, filter and wash the obtained solid precipitate according to the dry basis of the precipitate: ammonium salt: H 2 The weight ratio of O=1:0.4:10 was exchanged at 65° C. for 1 hour, filtered and washed with water, and the exchange process was repeated. After filtering, the porous material provided by the prese...
Embodiment 3
[0045] This example illustrates the porous material of the present invention and its preparation.
[0046] Add an appropriate amount of deionized water in the container, and at room temperature and under vigorous stirring, the NaY molecular sieve crystallization filtrate (concentration 42gSiO 2 / L, suspended matter concentration 630mg / L) and sodium metaaluminate solution (41gAl 2 o 3 / L, caustic ratio 11.5) join in the container and carry out continuous reaction and control pH value is 13.3, then concentration is 60gAl 2 o 3 / L AlCl 3 Add the solution to the above slurry, and make the final pH value of the slurry system 8.6, continue to heat up to 50°C and treat for 8 hours, filter and wash the obtained solid precipitate according to the dry basis of the precipitate: ammonium salt: H 2 The weight ratio of O=1:0.5:10 was exchanged at 55° C. for 0.5 hours. After filtration and washing, the exchange process was repeated once. After filtration, the porous material provided by ...
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