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Catalytic cracking auxiliary agent and preparation method thereof

A catalytic cracking aid, sodium oxide technology, applied in the directions of catalytic cracking, chemical instruments and methods, cracking, etc., can solve the problems of metal pollution resistance and heavy oil conversion capacity need to be improved, increase the cost of auxiliary agents, and high prices, etc. The effect of reducing production cost, improving production efficiency, and high light oil yield

Active Publication Date: 2013-03-20
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, the best preparation method of the aluminosilicate compound mentioned in ① can be found in US5045519A. This patent uses aluminum alcohol salt as raw material, which is expensive and greatly increases the cost of additives.
[0005] It can be seen that the prior art is trying various methods that can improve the catalytic performance of the auxiliary agent. Although certain results have been obtained and the cracking of heavy oil has been promoted to a certain extent, the existing preparation of catalytic cracking auxiliary agent However, the method still has problems such as high cost, metal pollution resistance and heavy oil conversion ability to be improved.

Method used

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  • Catalytic cracking auxiliary agent and preparation method thereof
  • Catalytic cracking auxiliary agent and preparation method thereof
  • Catalytic cracking auxiliary agent and preparation method thereof

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preparation example Construction

[0022] In the present invention, the non-ion-exchanged mesoporous silica-alumina material can be various mesoporous silica-alumina materials without any ion exchange commonly used in the art. The non-ion-exchanged mesoporous silica-alumina material can be prepared according to conventional methods, and the preparation method can include, for example, neutralizing the aluminum source and alkali solution at room temperature to 85°C to form a gel, and the final pH of the gel is 7 -11; then follow SiO 2 : Al 2 o 3 =1:0.6-9 weight ratio to add silicon source, aging at room temperature to 90°C for 1-10 hours, and then filter. In the present invention, the silica-alumina precipitate obtained after the filtration can be directly used as the non-ion-exchanged mesoporous silica-alumina material, or it can be used as the ion-free mesoporous silica-alumina material after being dried and / or calcined. Exchanged mesoporous silica-alumina materials.

[0023] In the present invention, the ...

Embodiment approach

[0035] According to a preferred embodiment of the present invention, the present invention provides a kind of preparation method of catalytic cracking additive, and this method comprises the following steps:

[0036] (1) Mix and beat the non-ion-exchanged mesoporous silica-alumina material with water to obtain a slurry, and then contact the obtained slurry with an inorganic acid at room temperature to 100°C for at least 0.2 hours to obtain a sodium oxide content of not higher than 0.2% by weight The mesoporous silica-alumina material, wherein the weight ratio of the non-ion-exchanged mesoporous silica-alumina material, water and inorganic acid is 1:5-30:0.03-0.3;

[0037] (2) Mix and beat the mesoporous silica-alumina material obtained in step (1), metal trapping agent, clay and / or heat-resistant inorganic oxide and / or heat-resistant inorganic oxide precursor, and then spray in sequence Dry, wash, filter and dry.

[0038] In the method of the present invention, only the prepa...

preparation Embodiment 1

[0056] The preparation process of the mesoporous silicon-aluminum material SSA-1 is basically the same as that of the mesoporous silicon-aluminum material SA-1 in Example 1 of CN1565733A, except that the ammonium exchange process is replaced by an acid exchange process. The intermediate sediment of SA-1, i.e. the silicon-aluminum precipitate after aging and filtering, is mixed with water in a weight ratio of 1:10, and then the HCl solution (concentration is 10% by weight) is pressed into the sediment (dry basis): HCl=1:0.07 weight ratio was added to the above slurry, contacted at 55°C for 30 minutes, filtered, dried and calcined to obtain a mesoporous silica-alumina material, denoted as SSA-1. The X-ray diffraction spectrum of the sample is shown in figure 1 Curve 2 in . The elemental analysis gravimetric chemical composition of this sample is 0.14Na 2 O·73.6Al 2 o 3 26.1 SiO2 2 .

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Abstract

The invention provides a catalytic cracking auxiliary agent and a preparation method thereof. The catalytic cracking auxiliary agent contains a mesoporous silica alumina material, a metal trapping agent and clay and / or heat-resistant inorganic oxide, wherein the mesoporous silica alumina material is obtained by the following steps of mix-pulping the mesoporous silica alumina material without ion exchange with water to obtain a slurry liquid; and contacting the slurry liquid with an inorganic acid for at least 0.2 hour at a temperature ranging from room temperature to 100 DEG C, so as to make the sodium oxide content in the mesoporous silica alumina material no higher than 0.2 wt%, wherein the weight ratio of the mesoporous silica alumina material without ion exchange, water and the inorganic acid is 1 : 5-30 : 0.03-0.3. The catalytic cracking auxiliary agent has relatively strong heavy oil cracking ability, high light oil yield and good coke selectivity when being used for the catalytic cracking of the heavy oil.

Description

technical field [0001] The invention relates to a catalytic cracking auxiliary agent and a preparation method thereof. Background technique [0002] The continuous rise of crude oil prices has greatly increased the processing costs of refineries. On the one hand, refineries can reduce costs by purchasing low-priced low-quality oil; on the other hand, they can increase economic benefits through deep processing of heavy oil. As an important means of heavy oil processing in refineries, catalytic cracking plays a pivotal role in refineries. It is not only the main means of heavy oil balance and clean fuel production in refineries, but also the focus of energy saving and efficiency enhancement in refineries. Therefore, more and more refineries have shifted their focus to the deep conversion of heavy oil, seeking to increase processing capacity and produce more high value-added products in order to maximize benefits. This means converting as much heavy crude as possible and reduc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/10C10G11/05
Inventor 陈蓓艳沈宁元田辉平黄志青罗一斌欧阳颖宋海涛郑金玉朱玉霞蒋文斌
Owner CHINA PETROLEUM & CHEM CORP
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