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Ultra-deep hydrogen desulfurization multi-metal body catalyst with a stratified structure as well as preparation method and application thereof

A bulk catalyst, layered structure technology, applied in catalyst activation/preparation, metal/metal oxide/metal hydroxide catalyst, heterogeneous catalyst chemical elements, etc., can solve environmental unfriendly, environmental pollution, catalyst ratio problems such as small surface area and pore volume, to achieve the effect of high hydrodesulfurization activity, cost reduction, and high dispersion

Active Publication Date: 2014-03-26
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of this kind of synthetic method is that the strong ammonia water is used in the synthetic process, which will pollute the environment.
Since the raw material used in this patent is basic nickel carbonate, which is insoluble in water, the essential reaction of the synthesis process is the replacement reaction between ions and solids, so it is difficult to synthesize catalyst particles with small grains
Chinese patents CN101544904A, CN101153228A, and CN101733120A also disclose a preparation method of a NiMoW three-metal bulk catalyst and its application in ultra-deep desulfurization of diesel oil; although the prepared catalyst shows relatively high activity in ultra-deep desulfurization of diesel oil, the catalyst The specific surface area and pore volume are still small
[0011] (1) The raw materials used are not environmentally friendly;
[0012] (2) catalyst preparation cost is higher;
[0013] (3) The specific surface area, pore volume and activity of the catalyst need to be further improved

Method used

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  • Ultra-deep hydrogen desulfurization multi-metal body catalyst with a stratified structure as well as preparation method and application thereof
  • Ultra-deep hydrogen desulfurization multi-metal body catalyst with a stratified structure as well as preparation method and application thereof

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preparation example Construction

[0047] The preparation method of the present invention is briefly described as follows:

[0048] a) Co-precipitating an aqueous solution of a soluble salt of a Group VIII metal and an aqueous solution of a soluble salt of a +2-valent metal to synthesize a catalyst precursor with a layered structure;

[0049] b) performing anion exchange reaction on the layered structure catalyst precursor slurry and the soluble salt containing at least two VIB group metal anion groups in a mixed solution of surfactant, water and organic solvent.

[0050] In detail, the preparation method of the present invention comprises the following steps:

[0051] a) adding a soluble salt of a VIII group metal and a soluble salt of a +2-valent metal into water to prepare a mixed aqueous solution of soluble salts, then dissolving the alkaline precipitating agent in water to form a solution, and finally adding the alkaline The precipitating agent is added to the mixed aqueous solution of the above-mentioned...

Embodiment 1

[0071] The present embodiment illustrates the preparation of the NiZnMoW bulk catalyst in the present invention:

[0072] a) Weigh nickel nitrate (29.08g, wherein Ni 2+ 0.1mol) and zinc nitrate (1.49g, where Zn 2+ 0.005mol), they were dissolved in 200ml water to form an aqueous solution, and 0.2mol / L NaOH aqueous solution was slowly added dropwise to it to adjust the pH=12, and heated to the reaction temperature to form a light green mixed reaction solution, which was heated at a reaction temperature of 80°C Reflux reaction 25 hours, obtain light green product; The light green product that reaction obtains is filtered and washed, obtains catalyst precursor (being the NiZn-LHS catalyst precursor with layered structure); This catalyst precursor is added in 200ml water, configured as a slurry precursor (a);

[0073] b) Weigh ammonium molybdate (5.4g, wherein Mo 6+ 0.03mol) and ammonium metatungstate (7.2g, where W 6+ 0.03mol), they are dissolved in water (30ml) to form a solu...

Embodiment 2

[0076] The present embodiment illustrates the preparation of the NiZnMoW bulk catalyst in the present invention:

[0077] Use nickel nitrate (29.08g, where Ni 2+ 0.1mol) and zinc nitrate (2.91g, where Zn 2+ 0.01mol) to replace nickel nitrate (29.08g) used in embodiment 1, wherein Ni 2+ 0.1mol) and zinc nitrate (1.49g, where Zn 2+ 0.005mol), prepare multi-metal bulk catalyst (16.4g) in the same manner as described in Example 1, the multi-metal bulk catalyst of synthesis is represented by Cat-B, and the material morphology of this Cat-B catalyst and Cat -A catalyst is similar. The specific surface area of ​​the catalyst determined by low-temperature nitrogen adsorption is 142m 2 / g, the pore volume is 0.42ml / g.

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Abstract

The invention relates to an ultra-deep hydrogen desulfurization multi-metal body catalyst with a stratified structure. In the ultra-deep hydrogen desulfurization multi-metal body catalyst, metals include at last one VIII-group metal, at least one <+2>-valence metal and at least two VIB-group metals. The catalyst is characterized in that, counted by oxides and based on the catalyst, the catalyst comprises the following components by weight percent: 1%-50% of VIII-group metal, 1%-50% of <+2>-valence metals and 5%-60% of two VIB-group metals. The invention further discloses a preparation method and application of the catalyst. The catalyst is applied to the hydrogen desulfurization of diesel distillate containing 4,6-dimethyldibenzothiophene and expresses an ultra-high hydrogen desulfurization activity. According to the catalyst, the ultra-deep desulfurization is realized and the cost of the body catalyst is lowered.

Description

technical field [0001] The invention relates to a multi-metal bulk catalyst for ultra-deep hydrodesulfurization with a layered structure. [0002] The present invention also relates to a method for preparing the above-mentioned catalyst. [0003] The invention also relates to the application of the above-mentioned catalyst in ultra-deep hydrodesulfurization reaction of sulfur-containing compounds. Background technique [0004] Due to the decline of oil reserves, the problem of heavy and inferior oil has become more and more prominent. The high-sulfur crude oil in the world is increasing year by year, and the environmental legislation of various countries has increasingly stringent requirements for limiting the sulfur content in fuel oil. Therefore, the development of ultra-deep processing oil with excellent performance Hydrogen desulfurization catalysts have not only become the core of the field of hydrodesulfurization, but also make hydroprocessing technology more and more...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/888B01J23/889B01J35/10C10G45/08
CPCB01J37/30B01J23/888B01J27/051C10G2400/04B01J37/03C10G45/08B01J35/02B01J23/883B01J23/002B01J23/85B01J23/8885B01J23/8898B01J35/002B01J35/1019B01J35/1038B01J37/20B01J2523/00C10L3/12B01J2523/27B01J2523/68B01J2523/69B01J2523/847B01J2523/72B01J2523/17B01J2523/842B01J2523/22B01J35/1042B01J37/038B01J37/08C10L1/08C10L2200/0446C10L2270/026
Inventor 李灿蒋宗轩陈燕蝶刘铁峰
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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