Catalyst for producing propylene by catalytic cracking of naphtha, preparation method thereof, and method for producing propylene by catalytic cracking of naphtha
A catalytic cracking and catalyst technology is applied in the catalyst field of naphtha catalytic cracking to produce propylene and naphtha catalytic cracking to produce propylene, which can solve the problems of small propylene output and achieve the effect of improving yield
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[0031] According to a preferred embodiment of the present invention, the molecular sieve of the TON structure is a mixture of ZSM-22 zeolite and NU-10 zeolite, and the weight ratio of the two is 2-5:1; the molecular sieve of the MTT structure is ISI- A mixture of 4 zeolite and ZSM-23 zeolite, the weight ratio of the two is 2-5:1.
[0032] In the present invention, the silicon-aluminum atomic molar ratio (Si / Al) of the first molecular sieve may be 0.1-100:1; preferably 30-80:1.
[0033] According to the present invention, preferably, the opening diameter of the pores of the second molecular sieve is 0.65-0.7 nanometers. More preferably, the second molecule is selected from at least one molecular sieve having a structure of AET, AFR, AFS, AFI, BEA, BOG, CFI, CON, GME, IFR, ISV, LTL, MEI, MOR, OFF and SAO kind. Particularly preferably, the second molecular sieve is at least one of Beta, SAPO-5, SAPO-40, SSZ-13, CIT-1, ITQ-7, ZSM-18, mordenite and gmelinite.
[0034] In the pre...
Embodiment 1
[0075] This example is used to illustrate the preparation method of the catalyst provided by the present invention and the method for producing propylene by catalytic cracking of naphtha.
[0076]Prepare the catalyst. Mix 56.2 grams of ZSM-22 molecular sieve (Nanjing Jicang Nano Technology Co., Ltd., Si / Al molar ratio = 30:1) with 56.2 grams of deionized water, and wet ball mill to form a molecular sieve slurry. The particle diameter of the molecular sieve is d 90 = 10 microns, solids content 50% by weight. Add 28.4 grams of aluminum sol (containing 22% by weight of alumina, produced by Sinopec Catalyst Qilu Branch) in the slurry, stir for 10 minutes, add 1.5 grams of polyethylene glycol solution (the weight percent of polyethylene glycol solution is 2% by weight), Stir for 20 minutes to obtain the first active component coating slurry 1.
[0077] The first active component coating slurry 1 is coated with a cordierite honeycomb carrier (the carrier pore density is 100 holes / ...
Embodiment 2
[0082] This example is used to illustrate the preparation method of the catalyst provided by the present invention and the method for producing propylene by catalytic cracking of naphtha.
[0083] (1) Preparation of catalyst.
[0084] Mix 32 grams of ZSM-23 molecular sieve powder (Shanghai Zhuoyue Chemical Co., Ltd., Si / Al molar ratio = 50:1)) with 20 grams of deionized water, and wet ball mill to form a slurry. The particle diameter of the molecular sieve in the slurry is d90 = 8 microns; Add 150 grams of peptized pseudo-boehmite (containing 18% by weight of alumina, the pH value is 2.8, the product of Sinopec Catalyst Qilu Branch Company) in the slurry, and stir for 15 minutes; add 3.2 grams of polyacrylic acid solution (polyacrylic acid solution weight percent 1% by weight), the polyacrylic acid solution was added in an amount of 10% by weight of the molecular sieve, and stirred for 30 minutes to obtain the first active component coating slurry 1.
[0085] The first active...
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