Catalytic cracking catalyst and preparation method thereof

Abstract

The invention relates to a catalytic cracking catalyst and a preparation method. The catalyst contains a cracking activity component, a mesoporous silicon-aluminum material, clay and an adhesive, wherein the cracking activity component comprises a Y-type molecular sieve and an MFI-structure molecular sieve; the Y-type molecular sieve comprises a first Y-type molecular sieve; and the rare-earth content in the first Y-type molecular sieve is 10-25 wt% on the basis of rare-earth oxides, the cell constant is 2.440-2.472nm, the crystallinity is 35-65%, the silicon / aluminum atomic ratio in the framework is 2.5-5.0, and the product of the ratio of 2theta=11.8+ / -0.1 degree peak intensity I1 to 2theta=12.3+ / -0.1 degree peak intensity I2 in an X-ray diffraction pattern and the rare-earth weight percent in the molecular sieve on the basis of rare-earth oxides is greater than 50. The preparation method comprises the following steps: preparing a mixed slurry containing the cracking activity component, mesoporous silicon-aluminum material, adhesive and clay, carrying out spray drying, washing and drying. The catalyst has higher conversion rate and liquefied gas yield, and can reduce the consumption of the molecular sieves in the catalyst, thereby lowering the catalyst production cost.

Description

Background technique [0001] Catalytic cracking (FCC) is an important secondary processing process of crude oil and plays a pivotal role in the refining industry. In the catalytic cracking process, heavy distillates such as vacuum distillate oil or residual oil with heavier components react in the presence of a catalyst and are converted into high value-added products such as liquefied gas, gasoline and diesel. In this process, it is usually necessary to use Catalytic material with high cracking activity. Microporous zeolite catalytic materials are widely used in petroleum refining and processing industries due to their excellent shape-selective catalytic performance and high cracking reaction activity. The Y-type molecular sieve has been the main active component of the catalytic cracking catalyst since it was first used in the 1960s. Especially the Y-type molecular sieve modified by rare earth has a significant effect on improving the acidity and structural stability of the m...

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Problems solved by technology

[0011] In the prior art, regardless of the rare earth Y molecular sieve obtained by the double-cross-two-baking process or the one-cross-one-baking process, the rare earth content in the product is always lower than the total rare earth amount input, such as CN1053808A, CN1069553C, several disclosed in CN1026225C All kinds of rare earth Y molecular sieves have this feature. Even if more rare earth ions are located in the small cages, it is inevitable that some rare earth ions still exist in the supercages, and the rare earth ions in the supercages will be washed in the subsequent washing process. It is backwashed down, resulting in the loss of rare earths, resulting in a decrease in the utilization rate of rare earths

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