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A kind of preparation method of highly active and highly antiwear microsphere sulfur transfer agent

A high anti-wear, sulfur transfer agent technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of low sulfur transfer agent activity and ineffectiveness Removal of sulfur oxides and other issues

Active Publication Date: 2016-03-30
BEIJING SJ ENVIRONMENTAL PROTECTION & NEW MATERIAL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The technical problem to be solved by the present invention is that although the sulfur transfer agent prepared by the prior art has high wear resistance, and its coagent has a certain activity, the activity of the sulfur transfer agent is still very low and cannot effectively remove the cracking process. Sulfur-oxygen compounds produced in the medium; and then a preparation method of a high-activity and high-wear-resistant microspherical sulfur transfer agent is proposed

Method used

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  • A kind of preparation method of highly active and highly antiwear microsphere sulfur transfer agent
  • A kind of preparation method of highly active and highly antiwear microsphere sulfur transfer agent

Examples

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Comparison scheme
Effect test

Embodiment 1

[0031] (1) Put 45g of kaolin into 250g, 4wt% phosphoric acid and soak for 12h, take it out and dry it at 100℃ for 5h to obtain a modified binder;

[0032] (2) Add 486g, 30wt% hydrochloric acid to 1223g, 10wt% pseudo-boehmite suspension and mix to obtain a gel, and add 7.6g, 10wt% heavy magnesium oxide suspension to the above gel Mixing to obtain a mixed solution, the added heavy magnesium oxide contains 80wt% of magnesium oxide;

[0033] (3) Add 52g of cerium nitrate, 8g of ammonium metavanadate and 89g, 33wt% of oxalic acid solution to the above-mentioned mixed solution in sequence and then mix to obtain a mixture;

[0034] (4) Add 44 g of the modified binder prepared in step (1) to the above mixture and mix uniformly to obtain a slurry. The slurry is dried at 400°C for 5 hours and then calcined at 600°C for 5 hours to obtain high activity and high Abrasion resistant sulfur transfer agent 1.

Embodiment 2

[0036] (1) Put 50g of Yanggan clay into 100g, 10wt% ammonium phosphate and soak for 14h, take it out and dry at 150℃ for 4h to obtain modified binder;

[0037] (2) Add 700g, 36wt% of nitric acid to 1067g, 12wt% of pseudo-boehmite suspension and mix to obtain a gel, and add 6.8g, 12wt% of heavy magnesium oxide suspension to the above gel Mixing to obtain a mixed solution, the added heavy magnesium oxide contains 90wt% of magnesium oxide;

[0038] (3) Add 58g of cerium sulfate, 54g of ammonium polyvanadate and 197g of 35wt% citric acid solution to the above-mentioned mixed solution in sequence and then mix them to obtain a mixture;

[0039] (4) Add 47 g of the modified binder prepared in step (1) to the above mixture and mix uniformly to obtain a slurry. The slurry is dried at 500°C for 4 hours and then calcined at 700°C for 4 hours to obtain high activity and high Abrasion resistant sulfur transfer agent 2.

Embodiment 3

[0041] (1) Put 47g of bentonite into 125g, 8wt% ammonium hydrogen phosphate soaked for 13h, take it out and dry it at 120℃ for 5h to obtain a modified binder;

[0042] (2) Add 750g, 32wt% of glacial acetic acid to 1138g, 11wt% of pseudo-boehmite suspension and mix to obtain a gel, and add 7.2g, 11wt% of heavy magnesium oxide to the above gel for suspension The liquid is mixed to obtain a mixed liquid, and the added heavy magnesium oxide contains 85% by weight of magnesium oxide;

[0043] (3) Add 32g of cerium chloride, 47g of ammonium polyvanadate and 193g of 34wt% citric acid solution to the above-mentioned mixed solution in sequence, and then mix them to obtain a mixture;

[0044] (4) Add 45g of the modified binder prepared in step (1) to the above mixture and mix uniformly to obtain a slurry. The slurry is dried at 450°C for 4 hours and then calcined at 650°C for 4 hours to obtain high activity and high Abrasion resistant sulfur transfer agent 3.

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Abstract

The invention discloses a method for preparing a microsphere sulfur transfer agent with high activity and high wear resistance. The method comprises the steps: putting an inorganic binder into a phosphoric acid or ammonium phosphate solution, dipping, taking out, and then drying to obtain a modified binder coated with a continuous aluminophosphate layer; and then in a last step of preparing the microsphere sulfur transfer agent, adding the prepared modified binder, then mixing uniformly, drying, and roasting to obtain the sulfur transfer agent. The continuous aluminophosphate coating layer can improve the content of an active component in the sulfur transfer agent, so that the sulfur transfer agent with high adsorption activity is obtained; and in the final roasting step, aluminophosphate is changed into phosphorus pentoxide, so as to improve the wear resistance of the sulfur transfer agent. The microsphere sulfur transfer agent is mainly applicable to a catalytic cracking FCC device, and cooperates with a catalyst for catalytic cracking of heavy oil components; and the microsphere sulfur transfer agent can adsorb sulfur oxides generated in the cracking process, so as to reduce damage of the sulfur oxides to equipment, environment and human health.

Description

Technical field [0001] The invention relates to a method for preparing a microsphere sulfur transfer agent with both high activity and high abrasion resistance, and belongs to the technical field of catalyst preparation. Background technique [0002] With the increase in mining volume, my country’s petroleum reserves are declining and the proportion of heavy oil in the oil is also increasing. Since heavy oil cannot be used directly, it is necessary to carry out catalytic cracking of heavy oil to obtain available light. Quality oil composition. [0003] The FCC unit used in the catalytic cracking of heavy oil is usually composed of a riser and a regenerator. During production, a catalyst catalyzes the heavy oil to undergo high-temperature cracking reaction in the riser. The heavy oil is converted into light oil during the cracking process. At the same time, the catalyst is also coked and deactivated; after that, the deactivated catalyst enters the regenerator for high-temperature re...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J20/12B01J20/28B01J20/30B01J23/22
Inventor 张玮航李丽英樊俐刘振义
Owner BEIJING SJ ENVIRONMENTAL PROTECTION & NEW MATERIAL CO LTD