Super-deep fraction oil hydrodesulphurization catalyst and preparation method thereof

A desulfurization catalyst and deep hydrogenation technology, which is applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve problems such as difficult removal, difficult access to active centers, and decreased reaction rate, so as to improve the pore structure , Avoid the effects of uneven distribution of molecular sieves, increase in pore size and pore volume

Active Publication Date: 2012-11-21
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

4,6-Dimethyldibenzothiophene sulfide is usually the most difficult type of sulfide to remove, because the methyl group next to the sulfur atom creates steric hindrance between the sulfur atom and the active center of the catalyst, Sulfur atoms are not easy to access the active center of the reaction, which leads to a significant decrease in the reaction rate
In the prior art, only emphasis is placed on the type and content of metals and the coordination and cooperation between different metals. How to make the catalyst have a reasonable pore structure and a high content of active metal components to fully play their role, and how to make the acidic components in the catalyst Combined with active metals reasonably, how to make the catalyst have better hydrogenation activity at the same metal content has not been involved

Method used

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  • Super-deep fraction oil hydrodesulphurization catalyst and preparation method thereof
  • Super-deep fraction oil hydrodesulphurization catalyst and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0033] Add 1000mL of water into the dissolution tank, add 26g of nickel chloride to dissolve, and 41.5g of ammonium metatungstate to dissolve in sequence, then add 415ml of aluminum chloride solution, and stir evenly to form a solution. Get 160g ammonium bicarbonate and be made into the aqueous solution that molar concentration is 2.5mol / l. Then the mixed solution, aqueous ammonium bicarbonate solution, and 10% ammonia water as a precipitant are simultaneously and co-flowed into a reaction tank equipped with clean water to form a gel. The pH value of the gel is 8.0, and the temperature of the gel is 50°C. After gel formation, 8 grams of SAPO-11 molecular sieve slurry was added and aged for 2 hours. After aging, filter, add 600ml of clean water and 6.3g of molybdenum trioxide to the filter cake, beat and stir evenly, filter, and dry the obtained filter cake at 80°C for 5 hours, then extrude into strips, wash with clean water for 3 times, and wet the strips at 120 After drying ...

Embodiment 2

[0035] According to the method of Example 1, according to the component content ratio of catalyst B in Table 2, add aluminum chloride, nickel chloride, sodium tungstate, zirconium oxychloride into the solution tank, and stir evenly to form a solution. Take 100g of ammonium bicarbonate to make a solution with a molar concentration of 2.0mol / l. Then the mixed solution, ammonium bicarbonate aqueous solution, and 20% ammonia water as a precipitant are simultaneously and co-flowed into a reaction tank equipped with clean water to form a gel. The pH value of the gel is 7.5, and the gelation temperature is 60°C. After gelation, add 10 grams of SAPO-11 molecular sieve slurry, age for 3 hours, filter after aging, add 600ml of clean water and 8.3g of molybdenum trioxide to the filter cake, beat and stir evenly, filter, and dry the obtained filter cake at 70°C for 7 hours, and then extruded into a strip, washed twice with clean water, dried at 100°C for 8 hours, and calcined at 550°C for...

Embodiment 3

[0037] According to the method of Example 1, according to the component content ratio of catalyst C in Table 1, nickel nitrate, ammonium metatungstate, aluminum chloride, phosphoric acid, water glass were added into the reaction tank, and the solution was made after uniform stirring. Get 120g ammonium oxalate to be made into the solution that molar concentration is 1.8mol / l. Then the mixed solution, ammonium oxalate aqueous solution, and 12% ammonia water as a precipitant are simultaneously and co-flowed into a reaction tank equipped with clean water to form a gel. The pH of the gel is 8.0, and the temperature of the gel is 65°C. After gelling, add 12 grams of SAPO-11 molecular sieve slurry, age for 2 hours, filter after aging, add 600ml of clean water and 8.3g of molybdenum trioxide to the filter cake, beat and stir evenly, filter, and dry the obtained filter cake at 120°C for 1 hours, and then extrude into a strip, dry the wet strip at 130°C for 3 hours, and roast at 600°C f...

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Abstract

The invention discloses a bulk phase super-deep hydrodesulphurization catalyst and a preparation method thereof. The catalyst comprises composite oxide NixWyOz, MoO3, alumina and SAPO-11 molecular sieve. The method comprises the following steps of: adding a proper amount of water-soluble nitrogen-containing compound in the precipitation process of Ni, W and Al, gelling, adding SAPO-11 molecular sieve liquid, ageing, pulping with the MoO3, and molding and activating to obtain the catalyst. The method improves the pore structure of the catalyst to expose more metal active sites on the surface of the catalyst, improves the utilization rate of active metals, and enables the SAPO-11 molecular sieve and the hydrogenation active metals to uniformly and fully contact and well match so as to achieve the effect of super-deep desulphurization of diesel oil. Moreover, because of the increment of aperture and pore volume of the catalyst, the Ni-W high active center is fully utilized, the complex big structural molecules are easier to contact the active center, and particularly the effect when the fraction oil with high macromolecule content is treated is more obvious.

Description

technical field [0001] The invention relates to a distillate oil hydrodesulfurization catalyst and a preparation method thereof, in particular to a bulk phase distillate oil ultra-deep hydrodesulfurization catalyst containing SAPO-11 molecular sieve and a preparation method thereof. Background technique [0002] Since the combustion of sulfur compounds in fuels will cause serious harm to the world's environment and society, the standards for clean fuels formulated by countries around the world have greatly increased the restrictions on sulfur content. The U.S. Environmental Protection Agency has lowered the diesel sulfur content standard to 15ppm in June 2006. Among various desulfurization technologies for diesel, the most mature one is hydrodesulfurization technology. Ways to achieve deep desulfurization include the development of new reactors and new catalysts. Kinetic studies have shown that to reduce the sulfur content of diesel from 500ppm to below 15ppm, the reactor ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/85C10G45/12
Inventor 王海涛冯小萍王继锋徐学军刘东香
Owner CHINA PETROLEUM & CHEM CORP
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