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Hydrocracking catalyst and preparation method thereof, and method for hydrocracking of heavy feedstock

A hydrocracking and catalyst technology, which is applied in the field of hydrocracking, can solve the problems of high catalyst conversion cost and unsolved carbon deposition problems, and achieve the effects of low coke yield, high product conversion rate and good product selectivity

Active Publication Date: 2022-02-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the catalyst used in this application needs to use noble metals, which makes the conversion cost of the catalyst higher, and does not overcome the carbon deposition problem

Method used

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  • Hydrocracking catalyst and preparation method thereof, and method for hydrocracking of heavy feedstock
  • Hydrocracking catalyst and preparation method thereof, and method for hydrocracking of heavy feedstock

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preparation example Construction

[0033] The second aspect of the present invention provides a method for preparing the above-mentioned hydrocracking catalyst, wherein the method comprises:

[0034] (1) In the presence of an acid, a binder precursor slurry is prepared from an alumina source and a silicon oxide source;

[0035] (2) providing a carrier slurry containing a binder precursor slurry, a silica-alumina molecular sieve and an alkaline metal oxide, and spraying, drying and roasting the carrier slurry to obtain a carrier;

[0036] (3) The carrier is loaded with an active metal compound, then dried and roasted to obtain a catalyst precursor; the active metal compound is a compound containing a metal promoter;

[0037] (4) Reducing the catalyst precursor.

[0038] According to the present invention, in step (1), the alumina source can be the alumina source conventionally used in the art to prepare binders, such as hydrated alumina, alumina sol, boehmite, pseudoboehmite One or more of bauxite, alumina tri...

Embodiment 1

[0077] This example is used to illustrate the hydrocracking catalyst and its preparation method of the present invention.

[0078] (1) USY molecular sieve (purchased from Sinopec Catalyst Qilu Branch Company, dry basis content is 3.8kg), zinc oxide powder (purchased from Headhorse company, purity 99.7%, 0.66kg) and 6.57kg deionized water are mixed, After stirring for 30 minutes, a mixed slurry containing USY molecular sieve and zinc oxide was obtained;

[0079] (2) kaolin (purchased from Suzhou Kaolin Factory S1 series, with a dry basis content of 1.5kg) and pseudoboehmite (purchased from Aluminum Corporation of China Shandong Branch, with a dry basis content of 1.35kg) were stirred and mixed, and then added 5.5kg of deionized water was mixed evenly, and then 500mL of hydrochloric acid (concentration of 30% by weight, purchased from Beijing Chemical Plant) was added to make the pH value of the slurry 3.0, stirred and acidified for 1h, and then heated to 80°C for aging for 2h t...

Embodiment 2

[0084] This example is used to illustrate the hydrocracking catalyst and its preparation method of the present invention.

[0085] (1) PREHY molecular sieve (purchased from Sinopec Catalyst Qilu Branch, the dry basis content is 5.8kg), magnesium oxide powder (purchased from Weifang Lihe Powder Technology Co., Ltd., with a purity of more than 95%, 1.26kg) and 8.6kg deionized water was mixed, and after stirring for 30 minutes, a mixed slurry containing PREHY molecular sieve and magnesium oxide was obtained;

[0086] (2) Expanded perlite (purchased from Mantanghong Abrasives Factory in Gongyi City, with a dry basis content of 2.06kg, 30-60 mesh) and pseudo-boehmite (purchased from China Aluminum Shandong Branch, with a dry basis content of 1.48kg) was stirring and mixing, then added 5.6kg of deionized water and mixed evenly, then added 500mL of hydrochloric acid (concentration of 30% by weight, purchased from Beijing Chemical Plant) to make the pH value of the slurry 3.0, and sti...

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Abstract

The invention relates to the field of hydrocracking, in particular to a hydrocracking catalyst, a preparation method thereof, and a method for hydrocracking heavy raw oil. Described catalyzer comprises the metal promoter of carrier and load; Described carrier is formed by binding agent, silicon-aluminum molecular sieve and basic metal oxide; Wherein, take the total weight of this catalyst as a basis, the content of described silicon-aluminum molecular sieve is 10-65% by weight, the content of the metal accelerator is 1-30% by weight, the content of the basic metal oxide is 0.5-30% by weight, and the content of the binder is 5-50% by weight; The silica-alumina molecular sieve is a silica-alumina molecular sieve with a twelve-membered ring channel structure. The hydrocracking catalyst of the present invention is suitable for producing high-octane gasoline and liquefied gas, has high product conversion rate, good product selectivity, low coke yield, and is suitable for long-term production of low-sulfur high-octane gasoline and liquefied gas. liquefied gas.

Description

technical field [0001] The invention relates to the field of hydrocracking, in particular to a hydrocracking catalyst, a preparation method thereof, and a method for hydrocracking heavy raw oil. Background technique [0002] The existing low-quality catalytic diesel oil is used as light cycle oil in the catalytic cracking unit for re-refining operation to generate gasoline, cracked gas and coke. Although it can be partially converted, the re-refining ratio is large, the selectivity of gasoline is low, coke and dry gas The productive rate is too high, and the economic benefit is low. In recent years, for the purpose of environmental protection and improving economic benefits, many technologies use hydrocracking technology to upgrade low-quality diesel oil. [0003] The existing technologies mainly include the LCO Unicracking process launched by UOP Company to produce high-quality gasoline and low-sulfur diesel by LCO hydrocracking. The raw materials are hydrocracked after hy...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/14B01J29/16C10G47/20
Inventor 于敬川毛安国刘宪龙郭大为
Owner CHINA PETROLEUM & CHEM CORP