34results about How to "Good shape selectivity" patented technology

The invention provides a catalytic cracking catalyst and a preparation method thereof, wherein the catalyst comprises 15-65% of natural minerals, 10-60% of an oxide, and 25-75% of a Y type molecular sieve and a phosphorus-containing and supported-metal-containing MFI-structure molecular sieve, wherein the n(SiO2) / n(Al2O3) of the phosphorus-containing and supported-metal-containing MFI-structure molecular sieve is more than 18 and less than 70, the Al distribution parameter D is more than or equal to 0.6 and is less than or equal to 0.85, the volume of the mesopores accounts for 50-80% of the total pore volume, the volume of the mesopores with the pore size of 2-20 nm accounts for more than 85% of the total mesopore volume, the amount of the strong acid accounts for 50-80% of the total acidamount, a ratio of the acid B to the acid L is 7-30, the phosphorus content is 1-15 wt%, and the supported metal content is 0.1-5 wt%. The preparation method comprises: carrying out mixing beating onthe phosphorus-containing and supported-metal-containing MFI-structure molecular sieve, the Y type molecular sieve, the natural minerals and an inorganic oxide binder, and carrying out spray drying.According to the present invention, the catalytic cracking catalyst has the high low-carbon olefin yield in the catalytic cracking of petroleum hydrocarbons.

The invention relates to a catalytic cracking catalyst and a preparation method thereof, wherein the catalyst comprises 15-65% of natural minerals, 10-30% of an oxide, and 25-75% of a Y-type molecularsieve and a phosphorus-containing and supported metal-containing IMF structural molecular sieve, the Al distribution parameter D of the phosphorus-containing and supported metal-containing IMF structural molecular sieve is more than or equal to 0.6 and is less than or equal to 0.85, the volume of mesopores accounts for 50-80% of the total volume of pores, the volume of pores with a pore size of 2-20 nm accounts for more than 85% of the total volume of mesopores, the strong acid accounts for 50-80%, a ratio of an acid B to an acid L is 7-30, the phosphorus content is 0.1-15 wt%, and the supported metal content is 0.1-5 wt%. The preparation method comprises: carrying out mixing beating on the phosphorus-containing and supported metal-containing IMF structural molecular sieve, the Y-type molecular sieve, the natural minerals and an inorganic oxide binder, and carrying out spray drying. According to the present invention, with the application of the catalytic cracking catalyst in catalytic cracking of petroleum hydrocarbons, the yield of low-carbon olefins is high.

The invention provides a catalytic cracking catalyst and a preparation method thereof, wherein the catalyst comprises 15-65% of natural minerals, 10-60% of an oxide, and 25-75% of a Y type molecular sieve and a phosphorus-containing IMF-structure molecular sieve, wherein the n(SiO2) / n(Al2O3) of the phosphorus-containing IMF-structure molecular sieve is more than 18 and less than 70, the phosphoruscontent is 1-15 wt%, the Al distribution parameter D is more than or equal to 0.6 and is less than or equal to 0.85, the volume of the mesopores accounts for 40-70% of the total pore volume, the volume of the mesopores with the pore size of 2-20 nm accounts for more than 85% of the total mesopore volume, the amount of the strong acid accounts for 45-75% of the total acid amount, and a ratio of the acid B to the acid L is 8-30. According to the present invention, the catalytic cracking catalyst has high low-carbon olefin yield and high BTX yield in the catalytic cracking of petroleum hydrocarbons.

The invention discloses a toluene and methanol alkylation catalyst and a preparation method and application thereof. A catalyst carrier contains a hydrogen-type ZSM-48 molecular sieve and a modified element which comprises one or several of lanthanum, magnesium, phosphorus and silicon, the content (in percentage by weight ) of the hydrogen-type ZSM-48 molecular sieve in the carrier is 10wt%-90wt%, and preferably 20wt%-80wt%; the modified element contains one or several of lanthanum, magnesium, phosphorus and silicon and is calculated according to oxides, and the modified element accounts for 0.05%-60% of the weight of the carrier, and preferably 0.5%-40%. The catalyst is used for an alkylation reaction of toluene and methanol, and has the characteristics that the conversion rate of the toluene is high, the selectivity of paraxylene is high, and the like.