Catalytic cracking catalyst containing modified molecular sieve and preparation method of catalytic cracking catalyst

A catalytic cracking and molecular sieve technology, applied in molecular sieve catalysts, catalytic cracking, physical/chemical process catalysts, etc., can solve problems such as unfavorable heavy metals, large particles of rare earth precipitates, unfavorable uniform dispersion, etc.

Inactive Publication Date: 2016-05-11
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

It has been found that the ion exchange between rare earth ions and cations such as sodium of the molecular sieve, and migration into the molecular sieve can improve the activity and stability of the molecular sieve, but once the ion-exchanged rare earth contacts with vanadium, it is easy to break away from the framework structure of the molecular sieve and form rare earth vanadate. On the contrary, the structural stability of the molecular sieve is deteriorated; and the rare earth existing in the form of an independent phase can be used to trap heavy metals in the catalytic cracking reaction process and play an anti-heavy metal role due to the difference in the location and state of existence.
Therefore, the above-mentioned rare earth molecular sieve prepared by rare earth ion exchange does not contain rare earth in independent phase, so its ability to resist heavy metal pollution is insufficient
[0010] The rare earth-containing Y-type molecular sieve prepared by the precipitation method, even if a rare earth precipitate is formed and contains a separate phase of rare earth, the particles of the rare earth precipitate are large, which is not conducive to uniform dispersion on the surface of the molecular sieve, and is not conducive to effective contact with heavy metals. , Capture heavy metals in time

Method used

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  • Catalytic cracking catalyst containing modified molecular sieve and preparation method of catalytic cracking catalyst
  • Catalytic cracking catalyst containing modified molecular sieve and preparation method of catalytic cracking catalyst
  • Catalytic cracking catalyst containing modified molecular sieve and preparation method of catalytic cracking catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0053] 16g of citric acid, 4g of ethylene glycol, 54g of yttrium nitrate and 128g of ammonium oxalate were simultaneously added to the self-made yttrium-containing Y-type molecular sieve slurry Y-1, and stirred at a temperature of 55°C for 20 minutes. Filtration, washing, and calcination of the filter cake at 600° C. and 100% water vapor atmosphere for 2 hours to obtain the modified molecular sieve Z-1 of the present invention.

[0054] Add 600 g (dry basis) of molecular sieve Z-1 into 1.2 L of deionized water, and perform sand milling to obtain molecular sieve slurry Z-1J. Mix 619g of alumina sol, 1499g of kaolin, and 2.2L of water for beating, then add molecular sieve slurry Z-1J, continue stirring for 30 minutes, homogenize, spray dry and form, roast, wash with water, and dry to obtain catalyst C-1 of the present invention.

Embodiment 2

[0056] Mix and beat 798g (dry basis) REUSY molecular sieve, 16g (dry basis) ZSM-5 molecular sieve, and water according to the weight ratio of molecular sieve (dry basis): water = 1:3 to form a molecular sieve slurry, add 110g ethylenediaminetetra Acetic acid, 104 mL of rare earth nitrate, and ammonia water were used to adjust the pH value of the molecular sieve slurry in the range of 7.5 to 8.0, then 23 g of ethanol was added, and stirred at room temperature (25° C.) for 30 minutes. Filter, wash, and dry the filter cake at 200°C. The modified molecular sieve Z-2 of the present invention is obtained.

[0057] 600g (dry basis) of molecular sieve Z-2 was added into 1.2L of deionized water, and subjected to sand milling to obtain molecular sieve slurry Z-2J. Mix 619g of alumina sol, 1513g of diatomaceous earth, and 2.2L of water for beating, then add molecular sieve slurry Z-2J, continue to stir for 30 minutes, spray dry after homogenization, roast, wash, and dry to obtain cataly...

Embodiment 3

[0059] Mix 798g (dry basis) REUSY molecular sieve and water according to the weight ratio of molecular sieve (dry basis): water = 1:3 to form a slurry, add 155g urea and 85g lanthanum nitrate in sequence, stir at room temperature (25°C), and use ammonia water Adjust the pH value of the molecular sieve slurry in the range of 6.5-7.0, then add 14 g of ethylene glycol, and continue stirring for 1.5 hours at room temperature (25° C.). Dry at 250°C. The modified molecular sieve Z-3 of the present invention is obtained.

[0060] Add 600 g (dry basis) of molecular sieve Z-3 into 1.2 L of deionized water, and perform sand milling to obtain molecular sieve slurry Z-3J. Mix 1054g kaolin, 587g pseudo-boehmite, and 2.2L water for beating, add 60mL hydrochloric acid, stir for 1 hour, then add molecular sieve slurry Z-3J, stir for 15min, then add 515g aluminum sol, continue stirring for 30min to form a gel, homogeneous Afterwards, it is formed by spray drying, calcined, washed with water,...

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Abstract

The invention relates to a catalytic cracking catalyst containing modified molecular sieve and a preparation method of the catalytic cracking catalyst. The catalytic cracking catalyst with the mass being 100% comprises, 10-55% of modified molecular sieve by dry basis, 10-80% of clay by dry basis, 0-40% of inorganic oxide in terms of its oxide and 5-40% of binder in terms of its oxide. The preparation method of the modified molecular sieve includes: mixing molecular sieve slurry, compound solution containing metal ions of element periodic table IIIB, precipitator and organic complexing agent and/or dispersing agent, stirring under 5-100 DEG C for at least 10 minutes to obtain mixed slurry of molecular sieve and precipitation containing metal of the element periodic table IIIB, drying, and roasting or not to obtain the molecular sieve modified by the elements of the element periodic table IIIB. The catalytic cracking catalyst is good in activity stability and heavy metal pollution resistance.

Description

technical field [0001] The invention relates to a catalytic cracking catalyst, in particular to a catalytic cracking catalyst with excellent activity stability and anti-heavy metal pollution performance. Background technique [0002] Crude oil is increasingly heavy and inferior. Efficient processing of heavy oil and blending of residual oil has become an urgent need for refiners to improve processing capacity and obtain higher profits. Catalytic cracking is the most important process of heavy oil processing. Due to its significant advantages such as high conversion efficiency of heavy oil, good product quality, non-hydrogenation and low operating pressure, it occupies a pivotal position in the process of processing heavy oil in refineries. It is the refinery's profit main source of . According to statistics, there are currently about 420 sets of catalytic cracking units in the world. The largest single set of catalytic cracking units has reached 10 million tons per year, wi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/08B01J29/80B01J29/70C10G11/05
Inventor 高雄厚孙书红郑云锋黄校亮李晓艳王林曹庚正刘从华潘志爽丁伟王栋滕秋霞
Owner PETROCHINA CO LTD
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