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A kind of solid base catalyst and preparation method thereof

A technology of solid base catalyst and catalyst quality, which is applied in the direction of catalyst carrier, molecular sieve catalyst, chemical instruments and methods, etc., which can solve the problem that the mechanical strength of the catalyst cannot meet the requirements of the catalyst, the low resistance to metal and non-hydrocarbon impurities, and the poor stability of the catalyst at high temperature low yield of dry gas and coke, excellent high-temperature hydrothermal stability, and high conversion rate of heavy oil

Active Publication Date: 2021-12-03
CNOOC TIANJIN CHEM RES & DESIGN INST +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] The solid base catalyst disclosed in patent CN109663585A is used in the field of biodiesel preparation, and the catalyst particles are prepared by grinding method, and the mechanical strength of the catalyst cannot meet the requirements of industrial cracking units for the catalyst
Although CN107115853A and CN101755036 introduce basic centers into catalytic cracking reactions, the catalysts have poor high-temperature stability, low resistance to metal and non-hydrocarbon impurities, and cannot stably process full-fraction residues and oils with high residual carbon content for a long period of time. Super heavy oil such as sand bitumen
However, the existing solid base catalysts generally have poor stability problems. For example, hydrotalcite solid base catalysts gradually transform into low-activity spinel structures under high temperature conditions, and it is difficult to process low-quality heavy oil with high carbon residues. Therefore, it is necessary to develop a Inferior heavy oil alkali catalysts with excellent structural properties have good application prospects

Method used

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  • A kind of solid base catalyst and preparation method thereof
  • A kind of solid base catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0067] (1) The selection of the silica carrier is the same as that of the comparative example.

[0068] (2) Pore thickening treatment: the silica carrier is first modified by silicon in the gel synthesis stage, and the silica carrier gel is first replaced with ethanol to replace the water in the gel, and then the ethanol solution containing ethyl orthosilicate Replacement, and finally replace the ethanol solution with water, and dry at 120°C to obtain a silicon-modified silica carrier. The mass proportion of the modified component in the silica carrier is 1.5wt%.

[0069] (3) Transition metal doping: Doping the transition metal with manganese, using 0.1mol / L manganese nitrate dilute solution to treat silicon-modified silica carrier, dissolving with dilute sulfuric acid to adjust pH=3, washing and drying to obtain manganese-modified A permanent silica carrier, manganese forms a bond with silicon in the carrier, and the mass ratio of manganese to the silica carrier is 0.25wt%. ...

Embodiment 2

[0074] (1) The silicon-aluminum composite oxide carrier is selected, and the BET specific surface area is measured to be 583m 2 / g, average pore diameter 4.9nm, pore volume 0.68cm 3 / g, mesopore volume 0.65 cm 3 / g, the proportion of mesoporous pore volume (more than 2nm pore volume) is 95.59%.

[0075] (2) Pore thickening treatment: the silicon-aluminum composite oxide carrier is first modified with titanium in the gel synthesis stage, and the silicon-aluminum composite oxide carrier gel is first replaced with ethanol to replace the water in the gel, and then with titanium tetrachloride The ethanol solution was replaced, and finally the ethanol solution was replaced with water, and finally dried at 120°C to obtain a titanium-modified silicon-aluminum composite oxide carrier. The mass ratio of the modified component titanium dioxide to the silicon-aluminum composite oxide carrier was 1.5wt %.

[0076] (3) Transition metal doping: Doping the transition metal with manganese, ...

Embodiment 3

[0081] (1) The silicon-aluminum composite oxide carrier is selected, and the BET specific surface area is measured to be 556m 2 / g, average pore diameter 5.6nm, pore volume 0.72cm 3 / g, mesopore volume 0.71 cm 3 / g, the proportion of mesoporous pore volume (more than 2nm pore volume) is 98.61%.

[0082] (2) The channel thickening treatment is the same as in Example 2.

[0083] (3) Transition metal doping is the same as in Example 2.

[0084] (4) The surface modification treatment is the same as in Example 2.

[0085] (5) The preparation of the microsphere catalyst by the integrated method of spray drying is the same as in Example 2.

[0086] (6) Catalyst evaluation and product analysis are the same as in Comparative Example 1.

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Abstract

The invention discloses a solid base catalyst and a preparation method thereof. The solid base catalyst of the present invention consists of active components, auxiliary agents, forming aids and solid base catalyst carriers. The solid base catalyst support is a highly mesoporous catalytic support. The solid base catalyst support has undergone pore thickening treatment, transition metal doping, and surface modification treatment to improve the hydrothermal stability of the catalyst and eliminate some polar centers. Reduce the catalyst's ability to adsorb polycyclic aromatic hydrocarbons and non-hydrocarbon impurities in heavy oil, and increase the life of the catalyst. The invention also provides a preparation method of the solid base catalyst to prepare microsphere, strip and spherical catalysts, which are used in reaction processes such as fluidized bed catalytic cracking, fixed bed and moving bed. The solid base catalyst of the present invention has a coke yield of less than 10wt% and a selectivity of low-carbon olefins in liquefied gas greater than 80% during the catalytic cracking process of heavy oil and residual oil with a residual carbon content greater than 10wt%.

Description

technical field [0001] The invention relates to a solid base catalyst and a preparation method. Background technique [0002] The research on solid base catalyst materials and solid base catalytic reactions has achieved rapid development. The use of solid base catalysts in the fields of biodiesel production, olefin isomerization, and heavy oil conversion and utilization has become a research hotspot. Base catalysts with stable and reliable performance and their preparation methods are key technologies. [0003] With the depletion of light oil resources worldwide, the trend of heavy crude oil in the world has made refineries increasingly desire to convert heavy residue oil into light and high-priced products, especially the heavy and inferior crude oil in my country. The trend is more obvious. The common technology for converting heavy oil into light oil is catalytic cracking, and catalytic cracking units occupy an important position in my country's oil refining industry. Du...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/34B01J21/08B01J32/00B01J35/10B01J21/12B01J29/03C10G11/02C10G11/04C10G11/05C10G11/18
CPCB01J23/34B01J21/08B01J21/12B01J29/0341C10G11/02C10G11/04C10G11/05C10G11/18B01J2229/186B01J35/617B01J35/635B01J35/647B01J35/615
Inventor 吴青李滨郭春垒臧甲忠孙振海何鸣元范景新郭健靳凤英宫毓鹏
Owner CNOOC TIANJIN CHEM RES & DESIGN INST
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