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Preparation method of catalyst used for heavy oil cracking

A heavy oil cracking and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, cracking, etc., to achieve the effects of increased output, large specific surface area, and improved quality

Inactive Publication Date: 2017-10-20
WANGJIANG DATANG RESOURCE REGENERATION CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the 1990s, the heavy and inferior quality of crude oil in the world has become increasingly serious. In order to make heavy oil molecules close to the active center of the catalyst and realize the orderly cracking of heavy oil macromolecules, in addition to the general carrier function of the matrix in the heavy oil catalytic cracking catalyst, It is necessary to provide a certain pore structure and active centers. The current catalysts cannot meet the needs and need to be solved urgently.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] A method for preparing a catalyst for heavy oil cracking, comprising the steps of:

[0017] S1. Mix glacial acetic acid and ethanol aqueous solution evenly, add dodecyltrimethoxysilane, heat up and stir, add clay and toluene to continue stirring, heat up to reflux and stir, filter, wash, dry, pulverize, add deionized water and stir, add Diaspore, aluminum sol, beating to obtain the first material;

[0018] S2. Adjust the pH value of the first material system to 0.7-1, stir, adjust the pH value of the system to 5-5.8, and mature to obtain the second material;

[0019] S3, adding molecular sieves to the second material, beating, spray drying, calcining, washing, filtering, and drying to obtain a catalyst for heavy oil cracking.

Embodiment 2

[0021] A method for preparing a catalyst for heavy oil cracking, comprising the steps of:

[0022] S1. Mix 2 parts of glacial acetic acid and 100 parts of ethanol aqueous solution with a concentration of 70wt% in parts by weight, add 1.2 parts of dodecyltrimethoxysilane, heat up to 55°C and stir for 25 minutes, add 20 parts of clay and 100 parts of toluene to continue Stir for 30 minutes, heat up to 125°C and reflux for 4 hours, filter, wash, dry at 60°C, pulverize, add 100 parts of deionized water and stir for 40 minutes at a stirring speed of 600r / min, add 50 parts of diaspore and 40 parts of aluminum sol, and beat 35min, obtain the first material;

[0023] S2. Use hydrochloric acid with a concentration of 30 wt% to adjust the pH value of the first material system to 0.7-1, stir for 50 minutes, use ammonia water to adjust the pH value of the system to 5-5.8, and mature for 10 hours to obtain the second material;

[0024] S3. Add 80 parts of molecular sieves to 200 parts of ...

Embodiment 3

[0026] A method for preparing a catalyst for heavy oil cracking, comprising the steps of:

[0027] S1. Mix 8 parts by weight of glacial acetic acid and 60 parts of 80 wt% ethanol aqueous solution evenly, add 0.4 parts of dodecyltrimethoxysilane, heat up to 75°C and stir for 15 minutes, add 40 parts of clay and 50 parts of toluene to continue Stir for 80 minutes, heat up to 115°C and reflux for 8 hours, filter, wash, dry at 50°C, pulverize, add 150 parts of deionized water and stir for 20 minutes at a stirring speed of 1400r / min, add 40 parts of diaspore and 50 parts of aluminum sol, and beat 15min, obtain the first material;

[0028] S2. Using 40 wt% hydrochloric acid to adjust the pH value of the first material system to 0.7-1, stirring for 40 minutes, using ammonia water to adjust the pH value of the system to 5-5.8, and aging for 20 hours to obtain the second material;

[0029] S3. Add 100 parts of molecular sieve to 100 parts of the second material in parts by weight, bea...

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PUM

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Abstract

The invention discloses a preparation method of a catalyst used for heavy oil cracking. The method comprises the following steps: uniformly mixing glacial acetic acid and an ethanol aqueous solution, adding dodecyltrimethoxysilane, heating the materials and stirring the materials, adding clay and toluene, continuously stirring the materials, heating the materials and performing backflow stirring, performing steps of filtering, washing, drying and crushing, adding deionized water and stirring the materials, adding diaspore and aluminium sol, beating the materials to obtain a first material; adjusting the pH value of a first material system to 0.7-1, stirring the materials, adjusting the pH value of the system to 5-5.8, slaking the material to obtain a second material; adding a molecular sieve in the second material, heating the materials, performing spray drying, calcining the materials, washing the materials, filtering the materials, and drying the material to obtain the catalyst used for heavy oil cracking. The preparation method is characterized in that the specific surface area of the catalyst is large, the appropriate aperture distribution and active center are in favor of diffusion and pre-cracking of heavy oil macromolecules, and the heavy oil cracking capability of the molecular sieve is increased.

Description

technical field [0001] The invention relates to the technical field of heavy oil cracking, in particular to a catalyst preparation method for heavy oil cracking. Background technique [0002] Researches on the processing technology of low-quality heavy oil are very active at home and abroad, mainly in the two fields of decarburization and hydrogenation. Among them, the decarbonization process is relatively mature, and the hydrogenation of low-quality heavy oil mostly adopts the hydrocracking process using catalysts. The macromolecular cracking of heavy oil The catalyst is mainly composed of active component molecular sieve and matrix. The matrix includes two parts: carrier (such as kaolin) and binder (such as aluminum sol, silica sol). The matrix is ​​the main material of catalytic cracking catalyst, accounting for more than 50% of the catalyst components. . In the early catalysts, the substrate was only used as a carrier, which mainly provided physical properties such as g...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J31/26C10G11/05
CPCC10G11/05B01J31/26C10G2300/1037B01J35/633
Inventor 唐来蓉
Owner WANGJIANG DATANG RESOURCE REGENERATION CO LTD