Preparation method of bulk cobalt-molybdenum hydrodesulfurization catalyst

A hydrodesulfurization and catalyst technology, applied in the petrochemical field, can solve the problems of large toxic substances, raw material toxicity, and no close contact, and achieve high hydrodesulfurization activity, improved catalytic activity, and close contact effects

Active Publication Date: 2019-04-12
安徽省中知众汇企业管理服务有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the existing synthesis methods of bulk hydrodesulfurization catalysts have the following disadvantages: (1) the raw materials used are highly toxic, and their preparation is complicated, and a large amount of toxic substances will be produced during the production process, which seriously pollutes the environment; (2) the catalyst precursor The cobalt (nickel) molybdenum (tungsten) atoms in the body do not realize the real close contact; (3) The molecular structure and composition of the catalyst precursor are uncertain, which is not conducive to the study of the structure-activity relationship between the active phase and the activity of the catalyst
Therefore, from this point of view, to increase the activity of hydrodesulfurization catalysts, it is necessary to increase the content of type II "Co(Ni)-Mo(W)-S" active phase, which requires that Mo(W) , Co(Ni) atoms are in close contact as much as possible, but the preparation method provided by this patent cannot accurately obtain the molecular structure of the precursor, and cannot prove that there is a true atomic-scale close contact between the active metals

Method used

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  • Preparation method of bulk cobalt-molybdenum hydrodesulfurization catalyst
  • Preparation method of bulk cobalt-molybdenum hydrodesulfurization catalyst
  • Preparation method of bulk cobalt-molybdenum hydrodesulfurization catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0027] (1) Synthesis of precursors

[0028] Dissolve 3.1g of ammonium molybdate in 250ml of water, then add 7.3g of cobalt nitrate, heat, stir and reflux to dissolve; add phosphorous acid to adjust the pH of the system to 4.0, then heat the solution to 60°C and maintain it for 72h to obtain cobalt-molybdenum bimetallic - Oxygen cluster powder crystals;

[0029] figure 1 The spatial structure diagram of the cobalt-molybdenum double metal-oxygen cluster obtained in this example shows that the metal-oxygen cluster is a four-capped Keggin structure, and the cobalt-molybdenum atoms are connected by bridge oxygen bonds Mo-O-Co, and the bond length is about And the cobalt atom is located outside the molybdenum atom cluster, which belongs to the close contact in the true sense, which is conducive to the formation of the active phase; in addition, the cobalt molybdenum atom is more suitable, the cluster volume and the cluster-cluster distance are moderate, and it is suitable as the p...

Embodiment 2

[0042] The preparation process of the catalyst was the same as in Example 1, except that hydrazine sulfate was added during the preparation of the catalyst precursor, and the pH of the solution was adjusted to 5.0. Present embodiment catalyst preparation method is as follows:

[0043] (1) Precursor synthesis

[0044] Dissolve 3.1g of ammonium molybdate in 250ml of water, add 7.3g of cobalt nitrate, heat and stir to reflux to dissolve; add acetic acid to adjust the pH of the system to 5.0, then add 0.7g of hydrazine sulfate, heat the solution to 60°C and maintain it for 72h to obtain Cobalt-molybdenum bimetallic-oxygen cluster powder crystal;

[0045] (2) Mix aluminum hydroxide dry rubber powder and water at a mass ratio of 1:10 to form a slurry at 70°C; then slowly add nitric acid at an acid-to-gel ratio of 1:10 and stir for 30 minutes; then add the cobalt obtained in step (1) Molybdenum bimetallic-oxygen clusters were mixed evenly and extruded into strips; after forming, th...

Embodiment 3

[0052] The catalyst preparation process is the same as in Example 1, except that the cobalt salt used to prepare the catalyst precursor is basic cobalt carbonate, and the obtained precursor is a cobalt-molybdenum bimetallic-oxygen cluster. Present embodiment catalyst preparation method is as follows:

[0053] Dissolve 3.1g of ammonium molybdate in 250ml of water, then add 4.5g of basic cobalt carbonate, heat and stir under reflux to dissolve it; add phosphorous acid to adjust the pH of the system to 4.0, then heat the solution to 60°C and maintain it for 72h to obtain cobalt molybdenum Bimetallic-oxygen cluster powder crystals;

[0054] Mix aluminum hydroxide dry rubber powder and water at a mass ratio of 1:10 to form a slurry at 70°C; then slowly add nitric acid at an acid-to-gel ratio of 1:10 and stir for 30 minutes. Aluminum stone is mixed in a certain proportion and extruded into strips. After forming, it is first dried under infrared lamps, then transferred to an oven a...

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Abstract

The invention provides a preparation method of a bulk cobalt-molybdenum hydrodesulfurization catalyst, which comprises the following steps of: (1) synthesizing a precursor, namely adding cobalt salt into a molybdenum salt solution, heating and refluxing, and adjusting the pH value to 4.0-6.0; heating to 60 DEG C, and maintaining for 48hr to obtain bimetal oxygen clusters; (2) preparing a catalyst:mixing bimetallic-oxygen cluster powder with aluminium hydroxide dry glue powder, molding and activating to obtain the bulk hydrodesulfurization catalyst; the space structure of the bimetal-oxygen clusters obtained by using the method is a four-cap Keggin structure. Cobalt and molybdenum atoms are connected through a bridge oxygen bond Mo-O-Co, and the bond length is shown in the description, thecobalt atom is located outside the molybdenum cluster, which belongs to close contact in real sense, and the sulfurization is beneficial to the generation of an active phase. Cobalt and molybdenum atoms are more suitable, the cluster size and the cluster spacing are moderate, the activation temperature is low, the dibenzothiophene hydrodesulfurization activity is high, and the method can providetheoretical basis for the directional construction of the active phase of the hydrodesulfurization catalyst.

Description

technical field [0001] The invention relates to the petrochemical field, in particular to a preparation method of a high-activity bulk hydrodesulfurization catalyst. Background technique [0002] With the increase in the degree of heavy crude oil and the continuous enhancement of public environmental protection awareness, the pace of upgrading of clean oil standards in my country is gradually accelerating. Hydrodesulfurization is the mainstream technology for the production of ultra-low sulfur clean oil in industry. Improve the hydrodesulfurization catalyst The study of activity has received extensive attention. [0003] The current hydrodesulfurization catalysts are mainly cobalt (nickel) molybdenum (tungsten) catalysts, which can be divided into supported type and bulk type according to the presence or absence of supports. The traditional supported cobalt-molybdenum hydrodesulfurization catalyst improves the catalytic effect by increasing the contact area between the react...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/882B01J37/08B01J37/20C10G45/08
CPCC10G45/08B01J23/882B01J37/082B01J37/20C10G2300/202
Inventor 梁吉雷吴萌萌胡志强宋玉鹤刘慧生韦平和
Owner 安徽省中知众汇企业管理服务有限公司
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