Preparation of fluid cracking catalyst

A fluidized cracking, catalyst technology, applied in catalytic cracking, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of low hydrogen transfer activity, limited ability to crack macromolecules, catalyst carrier problems such as low cracking activity, to achieve the effect of good light oil selectivity and strong heavy oil macromolecular cracking ability

Inactive Publication Date: 2005-04-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although pseudo-boehmite has certain activity and bonding properties, with the adoption of high-silicon-aluminum ratio molecular sieves with small unit cells, fewer acid centers, and low hydrogen transfer activity, the amount of molecular sieve added to the catalyst has increased significantly. The bonding performance of the binder puts forward higher requirements, so pseudo-boehmite can no longer fully meet this requirement
[0005] The preparation method of the catalytic cracking catalyst disclosed in USP4542118 is to use the aluminum sol with better bonding performance as the binding agent to improve the anti-wear performance of the catalyst. However, because the aluminum sol itself is inert, the aluminum sol is used as the binding agent. The prepared catalyst carrier has low cracking activity and limited ability to crack macromolecules. As a single binder, it will affect the cracking performance of the catalyst

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0031] Take by weighing 88.9 grams of kaolin, make kaolin slurry with 430 milliliters of deionized water, add 4.3 milliliters of concentrated hydrochloric acid of 36% by weight, stir to make the slurry mix evenly, add 20 grams of pseudo-boehmite, add β-alumina trihydrate ( Calculated as hydrated alumina (produced by Shandong Aluminum Plant) 30 grams, then add 16.7 grams of aluminum sol, stir for 1 hour, heat up to 60 ° C, age for 1 hour, finally, add 55.6 grams of ultra-stable molecular sieve USY and stir evenly. The above slurry was dried at 110° C. to obtain catalyst C1 prepared by the method provided by the present invention.

example 2

[0033] Weigh 88.9 grams of kaolin, make kaolin slurry with 430 ml of deionized water, add 50 grams of β-alumina trihydrate, then add 16.7 grams of aluminum sol, stir for 1 hour, and finally add 55.6 grams of ultra-stable molecular sieve USY and stir uniform. Dry the above slurry at 110° C. to obtain catalyst C2 prepared by the method provided by the present invention.

[0034] The compositions of catalysts C1 and C2 prepared in Examples 1 and 2 and comparative catalysts DB1, DB2 and DB3 prepared in Comparative Examples 1, 2 and 3 are listed in Table 1.

[0035]

example 3

[0037] Take 3.85 kg of kaolin and 0.5 kg of montmorillonite (dry weight, produced by Hubei Zhongxiang County Iron Mine Factory), add 16 liters of deionized water, beat for 2 hours, then add 0.5 kg of β-alumina trihydrate, and stir for 0.5 hours , then, add 2.0 kilograms of aluminum sol, continue to stir for 0.5 hours, add 700 milliliters of rare earth chloride solution, finally, add 2.5 kilograms of REHY type molecular sieves (unit cell constant is 2.467 nanometers, rare earth oxide content is 7.8 weight %, Qilu Petrochemical Company Catalyst Factory) and 0.5 kg of ZSM-5 molecular sieve (silicon-aluminum ratio is 60, Qilu Petrochemical Company Catalyst Factory) and stirred evenly. The above slurry was spray-dried to obtain catalyst C3.

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Abstract

During the preparation of fluidizing and cracking catalyst, the cracking catalyst component mixture containing alumina from beta-alumina trihydrate and in 1.5-55 wt% of dried and recovered. The catalyst thus prepared has bulk specific weight and pore volume capable of being regulated in a wide range. Compared with catalyst prepared through available technological process, the catalyst of the present invention has differential reaction activity to light oil raised by 2-11 units and differential reaction activity to heavy oil raised by 0.8-12.9 units.

Description

technical field [0001] The invention relates to a preparation method of a fluidized cracking catalyst. Background technique [0002] Catalytic cracking is an important oil refining process, and catalytic cracking units play a pivotal role in the oil refining industry. In recent years, with the continuous increase in the amount of slag added to raw oil, higher requirements have been put forward for cracking catalysts, that is, they have stronger heavy oil macromolecule cracking ability and better light oil selectivity. [0003] In order to ensure the anti-wear strength of the fluidized cracking catalyst and improve its reaction selectivity, the binders used in the prior art mainly include alumina sol binders, pseudoboehmite binders, composite silica-alumina binders, etc. Binder, composite aluminum-based binder composed of aluminum sol and pseudo-boehmite, etc. [0004] USP4010116 discloses a preparation method of a fluid catalytic cracking catalyst, which proposes to use pe...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J21/04B01J21/16B01J23/10B01J29/08B01J29/18C10G11/18
Inventor 邱中红张万虹王振波李才英
Owner CHINA PETROLEUM & CHEM CORP
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