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Catalytic cracking co-catalyst preparation method

A co-catalyst, catalytic cracking technology, applied in catalytic cracking, physical/chemical process catalyst, molecular sieve catalyst, etc., can solve the problem that the pore structure of the co-catalyst matrix needs to be further improved, and achieve the effect of good diesel selectivity

Active Publication Date: 2013-03-27
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in this method, kaolin microspheres are prepared by conventional methods, and the pore structure of the co-catalyst matrix still needs to be further improved.

Method used

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  • Catalytic cracking co-catalyst preparation method
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  • Catalytic cracking co-catalyst preparation method

Examples

Experimental program
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Effect test

Embodiment 1

[0044] (1) Preparation of in-situ crystallization products from kaolin microspheres

[0045] 3000g of kaolin, based on the mass of kaolin, was added with 9% water glass, 5% pseudoboehmite, 1% auxiliary agent polydimethyldiallylammonium chloride, and deionized water was added to prepare a solid content of 34%. The mixed slurry obtains the kaolin spray microspheres of 3021g. The microspheres were calcined at 970° C. for 1.5 hours to obtain Gaotu microspheres GT-1.

[0046] Take Gaotu microsphere GT-11000g, mix with 537ml water glass, 794ml14wt% sodium hydroxide solution, and 96ml directing agent, stir for 30 minutes, put the mixture into a stainless steel reaction kettle, raise the temperature to 85°C for 6 hours of static crystallization. After the crystallization is completed, the white powder in the solution is removed by settling and washing, and then the filter cake is filtered, washed, and dried to obtain an in-situ crystallization product. As determined by X-ray diffrac...

Embodiment 2

[0054] (1) Preparation of in-situ crystallization products from kaolin microspheres

[0055] With 3000g of kaolin, based on the mass of kaolin, add 5% of water glass, 3% of pseudoboehmite, 2% of auxiliary agent polydimethyldiallylammonium chloride, and add deionized water to prepare a solid content of 36%. The mixed slurry obtained the kaolin spray microspheres of 3106g. The microspheres were calcined at 940°C for 2.5 hours to obtain Gaotu microspheres GT-2.

[0056] Take Gaotu Microsphere GT-21000g, mix with 396ml water glass, 580ml14wt% sodium hydroxide solution, and 65ml directing agent, stir for 30 minutes, put the mixture into a stainless steel reaction kettle, raise the temperature to 96°C for static crystallization for 7 hours. After the crystallization is completed, the white powder in the solution is removed by settling and washing, and then the filter cake is filtered, washed, and dried to obtain an in-situ crystallization product. As determined by X-ray diffractio...

Embodiment 3

[0064] (1) Preparation of in-situ crystallization products from kaolin microspheres

[0065] 3000g of kaolin, based on the mass of kaolin, was added with 3% of water glass, 11% of silica sol, 4% of polydimethyldiallyl ammonium chloride as an auxiliary agent, and deionized water to prepare a mixed slurry with a solid content of 39%. , to obtain 3074g kaolin spray microspheres. A part of the microspheres was calcined at 930° C. for 2.0 hours to obtain Gaotu microspheres GT-3.

[0066] Take Gaotu microsphere GT-31000g, mix with 495ml water glass, 527ml14wt% sodium hydroxide solution, and 121ml directing agent, stir for 30 minutes, put the mixture into a stainless steel reaction kettle, raise the temperature to 91°C for 8h static crystallization. After the crystallization is completed, the white powder in the solution is removed by settling and washing, and then the filter cake is filtered, washed, and dried to obtain an in-situ crystallization product. As determined by X-ray di...

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Abstract

The invention relates to a catalytic cracking co-catalyst preparation method comprising the steps that: (1) an in-situ crystallization product is prepared by using kaolin microspheres, wherein kaolin is adopted as a raw material; deionized water is added, and the mixture is mixed and beaten into slurry; an adhesive and poly dimethyl diallyl ammonium chloride are added; the obtained slurry is prepared into microspheres through spray-drying; the microspheres are calcined, such that calcined microspheres are obtained; the calcined microspheres are mixed with a silicon source, an alkali solution, and a directing agent; hydrothermal crystallization, filtration, washing and drying are carried out, such that the in-situ crystallization product with NaY zeolite content of 5-20% and silica-alumina ratio of 3.5-5.5 is obtained, wherein the dosage of poly dimethyl diallyl ammonium chloride is 1-10% by mass of that of kaolin; (2) the in-situ crystallization product is subjected to exchange and calcination treatment, such that the catalytic cracking co-catalyst is prepared, wherein the in-situ crystallization product is subjected to ammonium salts, rare earth, and magnesium salt exchange, and calcination, such that the catalytic cracking diesel co-catalyst is obtained. Calculated with the weight of the co-catalyst as 100%, the content of sodium oxide is lower than 0.6%, and the co-catalyst contains 0.5-3% of magnesium oxide, and 0.5-5% of rare earth oxide.

Description

technical field [0001] The invention relates to a method for preparing a catalyst composition, in particular to a method for preparing a cocatalyst for catalytic cracking. Background technique [0002] With the change of market demand worldwide, the demand for gasoline and diesel continues to grow, and in recent years the growth rate of diesel demand has always exceeded the growth rate of gasoline. At present, except the United States, the demand for diesel in other parts of the world is greater than that for gasoline. As far as the domestic market is concerned, there is an overall shortage of diesel resources in the refined oil market, and the contradiction between supply and demand is very prominent. Since 1990, the demand for diesel has been much higher than that of gasoline, and has always been increasing. [0003] Diesel mainly includes straight-run diesel and secondary processed diesel. The secondary processing of my country's oil refining industry is mainly based on...

Claims

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Application Information

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IPC IPC(8): B01J29/08C10G11/05
Inventor 高雄厚熊晓云刘宏海王宝杰赵红娟张莉赵晓争曹庚振胡清勋潘志爽柳召永侯凯军刘明霞
Owner PETROCHINA CO LTD