Catalytic cracking catalyst
A catalytic cracking and catalyst technology, applied in catalytic cracking, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve the problems of reduced catalytic performance, reduced pore volume and specific surface area, low phosphorus utilization efficiency, etc., and achieve high cracking conversion rate and the effect of high yield of low-carbon olefins and high yield of liquefied gas
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[0040] The present invention also provides a preparation method of the catalyst, the method comprising: mixing Y-type molecular sieve, phosphorus-modified ZSM-5 molecular sieve and inorganic binder for beating and spray drying, and optionally performing roasting treatment , to obtain the catalytic cracking catalyst; wherein, the second clay is added or not added in the mixing; on a dry basis, the Y-type molecular sieve, the phosphorus-modified ZSM-5 molecular sieve, the inorganic binder The weight ratio with the second clay is (1-25): (5-50): (1-60): (0-60); the inorganic binder includes phosphorus aluminum inorganic binder and / or other inorganic binders; wherein the phosphorus-modified ZSM-5 molecular sieve is prepared by the following steps: the phosphorus-containing compound solution is contacted with the HZSM-5 molecular sieve, and after drying, external pressure and external It is obtained by carrying out hydrothermal roasting treatment and recovering the product under t...
Embodiment 1-1
[0079] Example 1-1 illustrates the phosphorus-modified ZSM-5 molecular sieve employed in the catalyst of the present invention.
[0080] Get 16.2g diammonium hydrogen phosphate (Tianjin Guangfu Science and Technology Development Co., Ltd., analytically pure, the same below) and dissolve it in 60g deionized water, stir for 0.5h to obtain a phosphorus-containing aqueous solution, add 113g HZSM-5 molecular sieve (Sinopec catalyst company Qilu Provided by the branch company, the relative crystallinity is 91.1%, the silica / alumina molar ratio is 24.1, and the Na 2 The O content is 0.039% by weight and the specific surface area is 353m 2 / g, the total pore volume is 0.177ml / g, the same below), modified by impregnation, impregnated at 20°C for 2 hours, dried in an oven at 110°C, applied external pressure and added water, at 500°C, The phosphorus-modified ZSM-5 molecular sieve sample obtained by treating under 0.5Mpa and 50% water vapor atmosphere for 0.5h is designated as PSZ1-1.
Embodiment 1-2
[0082] Examples 1-2 illustrate phosphorus-modified ZSM-5 molecular sieves employed in the catalysts of the present invention.
[0083] The materials, proportioning, drying and roasting are the same as those in Example 1-1, except that diammonium hydrogen phosphate, HZSM-5 molecular sieve and water are mixed and beaten into a slurry, and the temperature is raised to 100° C. for 2 hours. The obtained phosphorus-modified ZSM-5 molecular sieve sample is denoted as PSZ1-2.
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