A kind of preparation method of catalytic cracking flue gas desulfurization auxiliary agent

A desulfurization aid, catalytic cracking technology, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of low transfer rate, low oxidation activity and low reduction activity, etc. Reactivity, longevity effect

Active Publication Date: 2017-02-01
SHENYANG SANJUKAITE CATALYST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the magnesium active component and the cerium active component in the desulfurization aid prepared by the above method are prone to mutual wrapping, and the active center is covered, so the above desulfurization aid is used for catalytic cracking of SO in flue gas. x When the removal treatment is carried out, its oxidation activity and reduction activity are low, and the SO in the flue gas x The transfer rate is low

Method used

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  • A kind of preparation method of catalytic cracking flue gas desulfurization auxiliary agent

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Effect test

Embodiment 1

[0025] This embodiment provides a catalytic cracking flue gas desulfurization aid, which uses alumina as a carrier, magnesium and cerium compounds as active components, based on the weight of the catalyst, the content of magnesium oxide is 35wt%, and the content of cerium oxide is 20wt% %, the rest is alumina.

[0026] The catalytic cracking flue gas desulfurization aid is prepared by the following method:

[0027] (1) 35 parts by weight of granular carrier pseudo-boehmite are fully dispersed in 100ml deionized water, adding mass concentration is 37% hydrochloric acid to adjust the pH to 8 to obtain the first slurry; 30 parts by weight of cerium nitrate with 50ml After deionized water is dissolved, acid is added to adjust the pH value to 7 to obtain the second slurry;

[0028] (2) Mix the first slurry and the second slurry and add 20 parts by weight of aluminum sol, mix evenly, dry at 120°C for 2 hours, and bake at 600°C for 8 hours to obtain a semi-finished product; wherein,...

Embodiment 2

[0031] This embodiment provides a catalytic cracking flue gas desulfurization aid, which uses alumina as a carrier, magnesium, cerium, barium, manganese compounds as active components, based on the weight of the catalyst, the content of magnesium oxide is 35wt%, cerium oxide The content of barium oxide is 15wt%, the content of barium oxide is 2wt%, the content of manganese oxide is 5wt%, and the rest is alumina.

[0032] The catalytic cracking flue gas desulfurization aid is prepared by the following method:

[0033] (1) Fully disperse 35 parts by weight of granular carrier SB powder (the SB powder provided by Beijing Asia-Pacific Aohua Chemical Auxiliary Co., Ltd.) in 100ml deionized water, and add hydrochloric acid with a mass concentration of 37% to adjust the pH value to 8 to obtain The first slurry; after dissolving 22 parts by weight of cerium chloride with 50ml deionized water, adding an acid to adjust the pH value to 7 to obtain the second slurry;

[0034] (2) Mix the...

Embodiment 3

[0037] This embodiment provides a catalytic cracking flue gas desulfurization aid, which uses alumina as a carrier, magnesium, cerium, barium, manganese compounds as active components, based on the weight of the catalyst, the content of magnesium oxide is 35wt%, cerium oxide The content of barium oxide is 15wt%, the content of barium oxide is 2wt%, the content of manganese oxide is 5wt%, and the rest is alumina.

[0038] The catalytic cracking flue gas desulfurization aid is prepared by the following method:

[0039] (1) Fully disperse 30 parts by weight of granular carrier activated alumina powder in 100ml deionized water, add hydrochloric acid with a mass concentration of 37% to adjust the pH value to 8, and obtain the first slurry; After deionized water is dissolved, acid is added to adjust the pH value to 7 to obtain the second slurry;

[0040] (2) Mix the first slurry and the second slurry and add 15 parts by weight of aluminum sol and 5 parts by weight of silica sol, mi...

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Abstract

The invention provides a preparation method of catalytic cracking flue gas desulfurization additive, which is prepared by impregnating the active component cerium ion on the granular carrier under certain conditions, then adding aluminum sol and / or silica sol, drying and roasting Semi-finished products, which are conducive to the better dispersion of the active components on the carrier, and can also form more acid centers in the carrier to improve reactivity; then impregnate the active component magnesium ions on the semi-finished products, dry, The desulfurization aid is obtained after roasting. In the present invention, the active component of cerium ion is impregnated first, and then the active component of magnesium ion is impregnated after adding aluminum sol and / or silica sol, so that the active component of cerium is fully dispersed in the alumina channel. , and make the magnesium active component form a coating outside the cerium active component. When desulfurization is performed, the desulfurization reaction proceeds in layers, the desulfurization activity is high, the transfer rate of SOx in the flue gas is high, and the service life of the desulfurizer is long.

Description

technical field [0001] The invention relates to a preparation method of catalytic cracking flue gas desulfurization additive, which belongs to the technical field of chemical catalysts. Background technique [0002] Catalytic cracking is one of the important processes of petroleum secondary processing. In the process of catalytic cracking, the catalyst is circulated between the reactor and the regenerator. When leaving the reactor, the catalyst contains about 3-10wt% coke. At this time, the deposited coke needs to be burned off in the regenerator with the help of oxygen in the air to restore the catalytic activity of the catalyst and realize the regeneration of the catalyst. [0003] As the content of sulfur and nitrogen heteroatoms in crude oil increases, the sedimentary coke also contains sulfur and nitrogen. When the catalyst is regenerated in the regenerator under oxygen-enriched conditions, the deposited coke and oxygen undergo a combustion reaction to generate regener...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/10B01J23/34B01D53/50B01D53/86
Inventor 陈玲玲单红飞刘聪
Owner SHENYANG SANJUKAITE CATALYST
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