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Hydrofining catalyst and preparation method thereof

A technology for hydrorefining and catalyst, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of poor dispersion of active components and catalytic denitrification activity not good and other problems, to achieve the effect of improving dispersion, improving stability, and improving desulfurization

Pending Publication Date: 2021-06-18
山西腾茂科技股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] The purpose of the present invention is to overcome the defects of poor dispersion of active components and poor catalytic denitrification activity in the existing hydrogenation catalysts, and provide a hydrogenation refining catalyst and its preparation method

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  • Hydrofining catalyst and preparation method thereof
  • Hydrofining catalyst and preparation method thereof
  • Hydrofining catalyst and preparation method thereof

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preparation example Construction

[0017] A first aspect of the present invention provides a method for preparing a hydrorefining catalyst, the method comprising the following steps:

[0018] (1) Mix the alumina carrier, the compound containing the co-active component and water evenly, adjust the pH value of the obtained slurry to 5-10, stir at room temperature -90°C for 0.5-24 hours, filter and dry, and dry at 550 Calcined at -800°C for 2-5 hours to obtain a composite alumina carrier;

[0019] (2) impregnating the composite alumina carrier with an active metal in an organic solvent, and drying;

[0020] (3) Calcining the product obtained in step (2) under an inert atmosphere at a temperature of 300-700° C. for a time of 0.5-5 hours to obtain a hydrorefining catalyst.

[0021] In some embodiments provided by the present invention, the step (1) is used to prepare a composite alumina support, which can be modified to improve the final performance of the prepared hydrogenation catalyst. Preferably, the specific ...

Embodiment 1

[0042] With 650g alumina (solid content 86wt%, Al 2 o 3 559g), 240mL rare earth chloride solution (rare earth oxide content 250g / L, converted to 60g rare earth oxide), 3200g deionized water, adjust the pH value of the mixture to 5.5 with dilute ammonia water, stir and age at room temperature for 2 hours, filter Afterwards, it was dried at 120° C. for 12 hours, and calcined at 750° C. for 2 hours to obtain a composite alumina carrier. The weight ratio of alumina:rare earth oxide is 1:0.11.

[0043] 339g ferric chloride, 272g ammonium molybdate are dissolved in 800g ethanol (purity 99.9%) and make dipping liquid, gained dipping liquid and above-mentioned composite alumina carrier (with respect to composite alumina carrier, the consumption of iron oxide is 10wt%, The amount of molybdenum oxide is 20wt%) and mixed evenly (the solid-to-liquid weight ratio of composite alumina carrier: organic solvent is 1:2), kept at room temperature for 12h, and then the obtained product was dri...

Embodiment 2

[0045] With 547g alumina (solid content 86wt%, Al 2 o 3 470.4g), 203g magnesium chloride (converted to magnesia 85.5g), and 2000g deionized water are mixed, the pH value of the mixture is adjusted to 7.5 with dilute ammonia water, stirred and aged at 40°C for 1 hour, filtered and dried at 120°C 12 hours, then calcined at 650° C. for 3 hours to obtain a composite alumina carrier. The weight ratio of alumina:magnesia is 1:0.18.

[0046] 280g cobalt nitrate Co(NO 3 ) 2 ·6H 2 0.160g ammonium metatungstate is dissolved in 900g ethanol (purity 99.9%) and makes impregnating liquid, gained impregnating liquid and above-mentioned composite alumina carrier (with respect to composite alumina carrier, the consumption of cobalt oxide is 8wt%, the amount of tungsten oxide The dosage is 15wt%) and mixed evenly (the solid-to-liquid weight ratio of composite alumina carrier: organic solvent is 1:2), kept at room temperature for 8h, then dried the product at 120°C for 6 hours, and baked it...

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Abstract

The invention relates to the field of hydrogenation catalysts. The invention discloses a hydrofining catalyst and a preparation method thereof. The preparation method comprises the following steps: (1) uniformly mixing an alumina carrier, a compound containing an auxiliary active component and water, adjusting the pH value of the obtained slurry to 5-10, conducting stirring at a temperature ranging from room temperature to 90 DEG C for 0.5-24 hours, conducting filtering and drying, and conducting roasting at 550-800 DEG C for 2-5 hours to obtain a composite alumina carrier; (2) impregnating the composite alumina carrier in an organic solvent for loading an active metal, and conducting drying; and (3) roasting the product obtained in the step (2) in an inert atmosphere at 300-700 DEG C for 0.5-5 hours to obtain the hydrofining catalyst. The preparation method can effectively improve the physical and chemical properties of the carrier and significantly improve the dispersity of the active metal on the surface of the catalyst, and is suitable for preparation of hydrodemetallization, hydrodesulfurization and hydroconversion catalysts.

Description

technical field [0001] The invention relates to the field of hydrogenation catalysts, in particular to a method for preparing a hydrorefining catalyst and the prepared hydrorefining catalyst. Background technique [0002] With the increasingly stringent environmental protection regulations, the new diesel standard puts forward stricter requirements on the sulfur mass fraction, aromatic hydrocarbon mass fraction and cetane number in diesel products. The output of catalytic cracking diesel oil accounts for about 30% of the total diesel output. Due to its low cetane number, high mass fraction of sulfur, nitrogen and colloid, the oil product has dark color and poor stability, so it cannot be directly used as diesel oil. Hydrogenation process is one of the most effective means of improving oil quality, and hydrogenation catalyst is the most important and key technology in hydrogenation process. [0003] CN1133723C discloses a distillate oil hydrotreating catalyst and its prepara...

Claims

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Application Information

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IPC IPC(8): B01J23/887B01J23/888B01J35/10C10G45/08
CPCB01J23/8871B01J23/8872B01J23/888C10G45/08B01J35/633B01J35/615
Inventor 许本静柴永明
Owner 山西腾茂科技股份有限公司