Preparation method of silicon-based catalytic cracking catalyst
A catalytic cracking and catalyst technology, applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of poor stability of acid silica sol, difficulty in storage, easy loss of fluidity, etc., to achieve rapid diffusion, The effect of increasing solid content and reducing production cost
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Embodiment 1
[0046] In the reaction tank with water bath heating, add 2.3kg water, 714g aluminum sol (solid content 21% by weight), add 909g activated alumina (solid content 66% by weight) under stirring, then slowly add hydrochloric acid and carry out peptization, Stir for 1h. The initial pH value of sodium-type alkaline silica sol (30% by weight of silicon dioxide content) is 9.60. Weigh 1000 g of alkaline silica sol, add 9 ml of concentrated hydrochloric acid (concentration 37% by mass) under stirring conditions, and stir evenly to obtain the pH value 3.0 hydrochloric acid modified alkaline silica sol; 1.28kg of REHY molecular sieve with a solid content of 82% by weight plus 1.92kg of water for beating and dispersion, adding 3% oxalic acid relative to the dry basis of the molecular sieve and relative to the dry basis of the catalyst RE 2 o 3 1.0% rare earth solution by mass, wherein oxalic acid is pre-dissolved in water, a 1:1 diluted aqueous solution of the rare earth solution and th...
Embodiment 2
[0048] In a reaction tank with water bath heating, add 2.3kg of water, add 1045g of activated alumina (solid content 66% by weight) under stirring, then slowly add hydrochloric acid for peptization, stir for 1h, add 571g of aluminum sol (solid content 21% by weight) weight%). The initial pH value of sodium-type alkaline silica sol (silicon dioxide content 30% by weight) is 9.60. Weigh 1000 g of alkaline silica sol, add 8 ml of concentrated hydrochloric acid (concentration 37 mass %) under stirring conditions, and stir evenly to obtain the pH value 3.5 hydrochloric acid modified alkaline silica sol; 1.28kg of REHY molecular sieve with a solid content of 82% by weight plus 1.92kg of water for beating and dispersion, adding 3% oxalic acid relative to the dry basis of the molecular sieve and relative to the dry basis of the catalyst RE 2 o 3 1.0% rare earth solution by mass, wherein oxalic acid is pre-dissolved in an appropriate amount of water, and a 1:1 diluted aqueous solutio...
Embodiment 3
[0050] In a reaction tank with water bath heating, add 2.3 kg of water, add 1000 g of activated alumina (solid content: 66% by weight) under stirring, then slowly add hydrochloric acid for peptization, and stir for 1 h. The initial pH value of sodium-type alkaline silica sol (30% by weight of silica content) is 9.60. Weigh 1000 g of alkaline silica sol, add 7 ml of concentrated hydrochloric acid (concentration: 37% by mass) under stirring conditions, and stir evenly to obtain the pH value 3.8 hydrochloric acid modified alkaline silica sol; 1.28kg of REHY molecular sieves with a solid content of 82% by weight plus 1.92kg of water for beating and dispersion, adding 3% oxalic acid relative to the dry basis of the molecular sieve and relative to the dry basis of the catalyst RE 2 o 3 1.0% rare earth solution by mass, wherein oxalic acid is pre-dissolved in an appropriate amount of water, and a 1:1 diluted aqueous solution of the rare earth aqueous solution and the precipitant amm...
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