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Solid base catalyst and preparation method thereof

A solid base catalyst and catalyst technology, which is applied in the direction of catalyst carrier, molecular sieve catalyst, chemical instrument and method, etc., can solve the problem that the mechanical strength of the catalyst cannot meet the requirements of the catalyst, the ability to resist metal and non-hydrocarbon impurities is low, and it cannot be processed stably for a long time Low dry gas and coke yields, excellent high-temperature hydrothermal stability, and improved hydrothermal stability

Active Publication Date: 2021-10-19
CNOOC TIANJIN CHEM RES & DESIGN INST +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

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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  • Solid base catalyst and preparation method thereof
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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0067] (1) The silica carrier is the same as the contrast.

[0068] (2) Confair thickening treatment: The silicon dioxide carrier performs silicon modification in the synthetic gel stage, and the silicon dioxide carrier gel first uses ethanol to replace moisture in the gel, and then use the ethanol of orthosilatate. Replacement, finally the ethanol solution was replaced with water, and the quality of the silicon modified silicon dioxide carrier was dried at 120 ° C, the mass ratio of the modified component in the silica carrier was 1.5 wt%.

[0069] (3) Transition metal doping: doped transition metal is manganese, treated silicon-modified silicon dioxide carrier with 0.1 mol / L of nitrate dilute solution, dissolved with dilute sulfate, and drying after washing to give manganeseification Sex silicon dioxide support, manganese forming silicon in the carrier is bonded, and manganese is 0.25% by weight in the mass of the silicon dioxide carrier.

[0070] (4) Surface modification trea...

Embodiment 2

[0074] (1) Use a silicone-aluminum compound oxide carrier to measure the BET specific surface area 583m 2 / g, average aperture 4.9 nm, hole is 0.68cm 3 / g, mesh hole, 0.65 cm 3 / g, a mesh hole capacity (greater than 2 nm hole contamination) ratio 95.59%.

[0075] (2) Pore thickening treatment: silicone-aluminum composite oxide carrier first performs titanium modification in the synthetic gel stage, silica aluminum-complex oxide carrier gel first with ethanol to replace moisture, then contain tetrachloride The ethanol solution replacement, finally replaced the ethanol solution with water, and finally dried at 120 ° C to give a titanium-modified silica aluminum-composite oxide carrier, and the quality of the modified component of titanium dioxide in the silica-aluminum composite oxide carrier is 1.5 wt. %.

[0076] (3) Transition metal doping: doped transition metal is manganese, treated with a titanium-modified silica aluminum-aluminum compound oxide vector using 0.1 mol / L of ...

Embodiment 3

[0081] (1) Use a silicone-aluminum compound oxide carrier to measure the BET specific surface area 556m 2 / g, average aperture 5.6 nm, hole is 0.72cm 3 / g, mesh hole, 0.71 cm 3 / g, mesh hole contam (greater than 2 nm pore volume) ratio 98.61%.

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

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

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

[0085] (5) Example 2 for preparing a microsphere catalyst in a spray drying integrated method.

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

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Abstract

The invention discloses a solid base catalyst and a preparation method thereof. The solid base catalyst is composed of an active component, an auxiliary agent, a molding auxiliary agent and a solid base catalyst carrier. The solid base catalyst carrier is a highly mesoporous catalytic carrier, and the solid base catalyst carrier is subjected to pore channel thickening treatment, transition metal doping and surface modification treatment, so that the hydrothermal stability of the catalyst is improved, parts of polar centers are eliminated, the adsorption capacity of the catalyst on polycyclic aromatic hydrocarbon and non-hydrocarbon impurities in heavy oil is reduced, and the service life of the catalyst is prolonged. The invention also provides a preparation method of the solid base catalyst, and microsphere, strip and spherical catalysts are prepared and used for fluidized bed catalytic cracking, fixed bed, moving bed and other reaction processes. When the solid base catalyst is used for treating heavy oil with the residual carbon content larger than 10 wt% and in the residual oil catalytic cracking process, the coke yield is smaller than 10 wt%, and the selectivity of low-carbon olefin in liquefied gas is larger than 80%.

Description

Technical field [0001] The present invention relates to a solid base catalyst and a preparation method. Background technique [0002] Solid alkali catalyst materials and solid base catalytic reaction studies have developed rapidly, using solid base catalysts for biodiesel preparation, olefin isomer, heavy oil conversion utilization and other fields into research hotspots, and the performance stable and reliable base catalyst and preparation method is key technologies. [0003] With the increasing depletion of light oil resources world, the trend of heavy oil in the world has enable refinery to convert heavy residue into light, high-priced products, especially in China's crude oil, inferiorization The trend is more obvious. Common technologies conversion to heavy oil into light oil are catalytic cracks, and catalytic cracking devices occupy an important position in China's refining industry. Catalytic cracking technology has become one of the most important oil secondary processin...

Claims

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Application Information

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Patent Type & Authority Applications(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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