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Preparation method of high-HDS-activity Ni-based non-loading type catalyst

A catalyst, non-supported technology, applied in the direction of chemical instruments and methods, physical/chemical process catalysts, chemical/physical processes, etc., can solve the problem that the active sites cannot be fully exposed, the dispersion is not good, and the active components of non-supported catalysts are too large Intensive and other issues

Inactive Publication Date: 2017-05-10
LIAONING UNIVERSITY OF PETROLEUM AND CHEMICAL TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The main disadvantage of non-supported catalysts is that their active components are too dense and poorly dispersed, resulting in insufficient exposure of active sites, low metal utilization and high cost of use.

Method used

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  • Preparation method of high-HDS-activity Ni-based non-loading type catalyst

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Weigh 11.632 g of nickel nitrate hexahydrate, 5.071 g of ammonium heptamolybdate, and 3.531 g of ammonium metatungstate. Pour 5.071 g of ammonium heptamolybdate and 3.531 g of ammonium metatungstate into a three-necked flask with a capacity of 500 ml, and dissolve them completely with 300 ml of deionized water at 50 °C to obtain solution A. Use ammonia water as the precipitant to adjust the pH of solution A to 9, and heat the temperature of solution A to 90 °C in a water bath. Pour nickel nitrate hexahydrate into a beaker and dissolve in 20 ml deionized water to obtain solution B. Slowly drop solution B into solution A at the same temperature, and it can be seen that a precipitate is gradually formed. After the dropwise addition was completed, nonionic surfactant Tween 60 was added at one time, and its addition amount was 10% of the total mass of the metal compound raw material, i.e. 2.02 g. Afterwards, the solution was stirred at 90 °C for 5 h to fully compound the a...

Embodiment 2

[0021] Weigh 11.632 g of nickel nitrate hexahydrate, 5.071 g of ammonium heptamolybdate, and 3.531 g of ammonium metatungstate. Pour 5.071 g of ammonium heptamolybdate and 3.531 g of ammonium metatungstate into a three-necked flask with a capacity of 500 ml, and dissolve them completely with 300 ml of deionized water at 50 °C to obtain solution A. Use ammonia water as the precipitant to adjust the pH of solution A to 9, and heat the temperature of solution A to 90 °C in a water bath. Pour nickel nitrate hexahydrate into a beaker and dissolve in 20 ml deionized water to obtain solution B. At the same temperature, slowly change solution B and drop it into solution A, and it can be seen that a precipitate is gradually formed. After the dropwise addition was completed, nonionic surfactant Tween 60 was added at one time, and its addition amount was 20% of the total mass of the metal compound raw material, i.e. 4.04 g. Afterwards, the solution was stirred at 90 °C for 5 h to fully...

Embodiment 3

[0023]Weigh 11.632 g of nickel nitrate hexahydrate, 5.071 g of ammonium heptamolybdate, and 3.531 g of ammonium metatungstate. Pour 5.071 g of ammonium heptamolybdate and 3.531 g of ammonium metatungstate into a three-necked flask with a capacity of 500 ml, and dissolve them completely with 300 ml of deionized water at 50 °C to obtain solution A. Use ammonia water as the precipitant to adjust the pH of solution A to 9, and heat the temperature of solution A to 90 °C in a water bath. Pour nickel nitrate hexahydrate into a beaker and dissolve in 20 ml deionized water to obtain solution B. At the same temperature, slowly change solution B and drop it into solution A, and it can be seen that a precipitate is gradually formed. After the dropwise addition was completed, nonionic surfactant Tween 60 was added at one time, and its addition amount was 40% of the total mass of the metal compound raw material, i.e. 6.06 g. Afterwards, the solution was stirred at 90 °C for 5 h to fully ...

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Abstract

The invention discloses a preparation method of a high-HDS-activity Ni-based non-loading type catalyst. The method uses Ni as a co-catalysis ingredient raw material; VIB group metals are selected to be used as active ingredient raw materials; a catalyst particle with the characteristics of nanoscale amorphous structures, good metal dispersibility and developed pore structures can be obtained by a coprecipitation method. The preparation method provided by the invention has the most obvious characteristics that in the catalyst preparation process, surfactants are added; the metal utilization rate of the catalyst is effectively improved; the problems of poor dispersibility and low utilization rate of the non-loading type catalyst are solved; the prepared Ni-based non-loading type catalyst has great specific surface area and developed pore structure, and can provide rich hydrogen desulfurization active sites. Therefore compared with a conventional loading type catalyst, the prepared non-loading type catalyst has the advantage of higher HDS activity. Meanwhile, the preparation method provided by the invention has the advantages that the operation is simple; the conditions are mild; the cost and the energy consumption are low; the method is suitable for mass industrial production.

Description

technical field [0001] The invention belongs to the field of hydrogenation catalysis in industrial catalysis, and in particular relates to a preparation method of a Ni-based non-supported catalyst with high HDS activity. Background technique [0002] With the rapid development of the industrial economy, the world's demand for various oil products is increasing day by day, which makes environmental problems more and more serious for people. With the frequent occurrence of smog weather and acid rain incidents, people's awareness of environmental protection has gradually increased, and the corresponding environmental protection regulations have become more and more stringent. At the same time, domestically produced crude oil is becoming increasingly heavy, and the sulfur content of imported crude oil is increasing, and light crude oil resources are showing a rapid decline. Such contradictions have made oil quality upgrading the focus of public attention. European diesel standa...

Claims

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Application Information

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IPC IPC(8): B01J27/051B01J35/10C10G45/08
CPCC10G45/08B01J27/0515C10G2400/04B01J35/613B01J35/615B01J35/633B01J35/647
Inventor 于隽晨施岩么志伟王海彦王晨马涛倪泽南荣青山蔡耀荣李亚如
Owner LIAONING UNIVERSITY OF PETROLEUM AND CHEMICAL TECHNOLOGY