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A kind of hydrogenation catalyst composition and the method for hydrogenation treatment

A technology of hydrogenation catalyst and composition, which is applied in chemical instruments and methods, chemical/physical processes, organic compound/hydride/coordination complex catalysts, etc., can solve the problems of low catalyst activity and short catalyst life, and achieve Effects of high hydrodesulfurization activity, extended service life, and high hydrodenitrogenation activity

Active Publication Date: 2019-12-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Although the above-mentioned preparation method can improve the hydrogenation performance of the catalyst to a certain extent, further studies have found that the catalysts prepared by the prior art still have the defects of low catalyst activity and short catalyst life.

Method used

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  • A kind of hydrogenation catalyst composition and the method for hydrogenation treatment
  • A kind of hydrogenation catalyst composition and the method for hydrogenation treatment
  • A kind of hydrogenation catalyst composition and the method for hydrogenation treatment

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preparation example Construction

[0028] The present invention provides a hydrogenation catalyst composition, which comprises a hydrogenation catalyst I and a hydrogenation catalyst II; by volume and based on the hydrogenation catalyst composition, the hydrogenation catalyst I The content is 5-95%, preferably 10-80%, more preferably 20-70%; the hydrogenation catalyst I includes a support and a hydrogenation active metal component supported on the support; wherein, the hydrogenation The preparation method of catalyst I comprises:

[0029] (1) load the hydrogenation active metal component and the organic complexing agent on the carrier, and carry out the first drying and roasting to obtain the catalyst precursor; wherein, based on the dry basis weight of the catalyst precursor, the calcining such that the carbon content of the catalyst precursor is 0.01-0.5% by weight, preferably 0.04-0.4% by weight;

[0030] (2) loading an organic complexing agent on the catalyst precursor, and performing second drying without...

specific Embodiment approach

[0038] In a specific embodiment, the compound containing Group VIB metal elements can be selected from at least one of ammonium molybdate, ammonium paramolybdate, ammonium metatungstate, molybdenum oxide and tungsten oxide.

[0039] Another specific embodiment, the compound containing the VIII metal element can be selected from the group VIII metal nitrate, the VIII group metal chloride, the VIII group metal sulfate, the VIII group metal formate , Group VIII metal acetate, Group VIII metal phosphate, Group VIII metal citrate, Group VIII metal oxalate, Group VIII metal carbonate, Group VIII metal Hydroxides of Group VIII metals, Phosphates of Group VIII metals, Phosphides of Group VIII metals, Sulfides of Group VIII metals, Aluminates of Group VIII metals, Group VIII At least one of molybdates of Group VIII metals, tungstates of Group VIII metals and water-soluble oxides of Group VIII metals.

[0040] A preferred specific embodiment, the compound containing the Group VIII meta...

Embodiment 1

[0060] Weigh 54 grams of molybdenum trioxide, 21 grams of basic nickel carbonate, 13 grams of phosphoric acid, and 30 grams of citric acid into 140 grams of deionized water, heat and stir to dissolve to obtain a clear impregnation solution, and impregnate 200 grams of the above solution with saturated impregnation method. Alumina carrier, impregnated for 2 hours, then dried at 120°C for 2 hours, then calcined under the condition of flowing air, the calcined temperature was 360°C, the time was 6 hours, and the air-carrying ratio was 2 liters / (g·hour), the catalyst precursor I-Z-S1 is obtained, and the carbon content is shown in Table 1; 5 grams of ethanol is added to 150 grams of deionized water, stirred to obtain a clear solution, and the saturated impregnation method is used to impregnate I-Z-S1 with the above solution, and impregnate The time was 2 hours, and then dried at 110° C. for 3 hours to obtain catalyst I-1. Based on the total weight of Catalyst I-1 and in terms of ...

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Abstract

The invention relates to a hydrogenation catalyst composition and a hydrogenation treatment method. The hydrogenation catalyst composition includes a hydrogenation catalyst I and a hydrogenation catalyst II; in terms of volume and based on the hydrogenation catalyst composition, the hydrogenation catalyst composition is The content of the hydrogenation catalyst I is 5-95%, and the content of the hydrogenation catalyst II is 5-95%; wherein, the preparation method of the hydrogenation catalyst I includes: (1) adding the hydrogenation active metal component and the organic complexing agent are loaded onto the carrier, and the first drying and roasting are performed to obtain the catalyst precursor; (2) the organic complexing agent is loaded onto the catalyst precursor, and the second drying is performed to obtain the added catalyst precursor. Hydrogen Catalyst I. When the hydrogenation catalyst composition provided by the invention is applied to hydrogenation treatment, it has good activity and long life.

Description

technical field [0001] The present invention relates to a hydrogenation catalyst composition and a method for hydrogenation treatment. Background technique [0002] The increasing awareness of environmental protection and stricter environmental regulations force the refining industry to pay more attention to the development of clean fuel production technology. In the future, vehicle fuels in the market will tend to be "ultra-low sulfur", and fuels that cannot meet emission standards will not be able to enter the market. Hydrogenation technology, as an effective means of desulfurization, is playing an increasingly important role in the production of clean vehicle fuels. Among them, high-efficiency hydrogenation catalysts are the core technology of hydrogenation technology. Therefore, the development of catalysts with higher activity and Selective new hydrogenation catalysts have become one of the most pressing needs of the oil refining industry. [0003] Hydrogenation catal...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/888B01J27/188B01J27/19B01J27/132B01J31/34C10G45/08
CPCC10G45/08B01J23/888B01J23/8885B01J27/132B01J27/188B01J27/19B01J31/34C10G2300/1062C10G2300/1037C10G2300/1077C10G2300/202C10G2300/1022B01J35/19
Inventor 张乐李明丰李会峰聂红丁石刘学芬胡志海李大东
Owner CHINA PETROLEUM & CHEM CORP