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Catalytic cracking sulfur reducing additive, preparation method thereof, and method for reducing sulfur content in catalytic cracking gasoline

A sulfur-reducing additive and catalytic cracking technology, which is applied in catalytic cracking, chemical instruments and methods, physical/chemical process catalysts, etc., can solve problems such as lower gasoline yield, reduced gasoline production efficiency, catalytic cracking catalyst poisoning, etc., to achieve Effects of increasing gasoline yield, reducing sulfur content, and increasing yield

Active Publication Date: 2016-06-01
CNOOC HUIZHOU PETROCHEM CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the catalyst has the effect of reducing sulfur, the introduced vanadium will cause catalytic cracking catalyst poisoning
[0010] It can be seen that although there are currently existing sulfur-reducing additives that can reduce the sulfur content in FCC gasoline, which can reduce the sulfur content in FCC gasoline, the use of existing sulfur-reducing additives will also reduce the yield of gasoline. Some even have poisoning effects on catalytic cracking catalysts, reducing the efficiency of gasoline production in the catalytic cracking process

Method used

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  • Catalytic cracking sulfur reducing additive, preparation method thereof, and method for reducing sulfur content in catalytic cracking gasoline

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preparation example Construction

[0018] The present invention provides a kind of preparation method of catalytic cracking sulfur reducing additive, and this method comprises the following steps:

[0019] (1) The molecular sieve, clay, pseudoboehmite and alumina sol are mixed and beaten for the first time to obtain the first slurry;

[0020] (2) mixing and beating the first slurry and the titanium-containing compound for the second time to obtain a second slurry;

[0021] (3) Drying and calcining the second slurry in sequence.

[0022] According to the present invention, in step (1), on a dry basis, relative to 100 parts by weight of the catalytic cracking sulfur reduction additive, the amount of the molecular sieve used is 25-45 parts by weight, preferably 30-40 parts by weight part; the consumption of the clay is 20-60 parts by weight, preferably 30-40 parts by weight; the consumption of the pseudo-boehmite is 10-20 parts by weight, preferably 12-18 parts by weight; the aluminum sol The amount used is 2-15...

Embodiment 1

[0052] This example is used to illustrate the preparation method of the catalytic cracking sulfur reducing additive of the present invention.

[0053] (1) 700.0 grams of REY molecular sieve slurry with a solid content of 30% by weight, 179.4 grams of pseudoboehmite, 192.7 grams of alumina sol and 325.0 grams of halloysite were added to the beating tank in sequence, mixed and beaten for 30 minutes to obtain the first slurry A1;

[0054] (2) Mix and beat the solution formed by the first slurry A1, 280.8 grams of tetrabutyl titanate and 59.0 grams of water for 20 minutes to obtain the second slurry B1;

[0055] (3) The second slurry B1 is spray-dried and roasted in sequence, washed with hot water, and then dried to obtain the sulfur-reducing additive SAC-1; the spray-drying temperature is 450°C; the roasting temperature is 500°C, and the roasting time is 1 hour .

[0056] Wherein, according to the calculation of the feeding amount, it is known that the content of titanium oxide ...

Embodiment 2

[0058] This example is used to illustrate the preparation method of the catalytic cracking sulfur reducing additive of the present invention.

[0059] (1) Add 700.0 grams of slurry consisting of 95 weight percent REY molecular sieves and 5 weight percent USY molecular sieves, 179.4 grams of pseudo-boehmite, 192.7 grams of aluminum sol and 257.1 grams of kaolin into the beating tank in sequence, with a solid content of 30% by weight, Mix and beat for 30 minutes to obtain the first slurry A2.

[0060] (2) The first slurry A2 was mixed with a solution formed by 199.8 g of tetrabutyl titanate and 42.0 g of water for beating, and the second slurry B2 was obtained after 30 minutes.

[0061] (3) The second slurry B2 is spray-dried and roasted in sequence, washed with hot water, and then dried to obtain the sulfur-reducing additive SAC-2; the spray-drying temperature is 450°C; the roasting temperature is 500°C, and the roasting time is 1 hour .

[0062] Wherein, according to the cal...

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Abstract

The invention discloses a preparation method for a catalytic cracking sulfur-reducing auxiliary agent, a catalytic cracking sulfur-reducing auxiliary agent prepared by the preparation method, and a method for reducing sulfur content in catalytic cracking gasoline by using the catalytic cracking sulfur-reducing auxiliary agent. With the provided catalytic cracking sulfur-reducing auxiliary agent, the sulfur content of the gasoline can be reduced; meanwhile, yield of the catalytic cracking gasoline is increased.

Description

technical field [0001] The invention relates to a catalytic cracking sulfur reducing additive, a preparation method of the catalytic cracking sulfur reducing additive, and a method for reducing sulfur content in catalytic cracking gasoline by using the catalytic cracking sulfur reducing additive. Background technique [0002] At present, air environmental protection regulations are becoming increasingly stringent. In order to meet the regulatory requirements on automobile exhaust emissions, it has become an important issue for my country's petroleum refining industry to greatly reduce the sulfur content in gasoline. In the processing technology of producing gasoline and diesel in my country, the catalytic cracking process is the core process. More than 70% of gasoline and more than 30% of diesel in China come from catalytic cracking process. This makes reducing the sulfur content in gasoline obtained from the catalytic cracking process the primary task of reducing the sulfu...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/10C10G11/00
Inventor 宋家庆孔劼琛姚小强徐向宇徐振领吴青
Owner CNOOC HUIZHOU PETROCHEM CO LTD