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Hydrocracking nickel-molybdenum catalyst and preparation method thereof

A hydrocracking and catalyst technology, applied in physical/chemical process catalysts, organic compound/hydride/coordination complex catalysts, chemical instruments and methods, etc., can solve problems such as inapplicability of hydrogenation process, and achieve synthesis cost Low, simple production process, good hydrocracking performance and effect

Active Publication Date: 2018-04-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In the prior art of using nickel and molybdenum metal catalysts at the same time, the catalyst is usually a supported catalyst, which is not suitable for the slurry bed hydrogenation process

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0018] A preparation method for hydrocracking molybdenum-nickel catalyst, comprising the following steps:

[0019] (1) Dissolve and disperse the hexavalent molybdenum source compound with the solvent, add an inorganic acid catalyst, the mass ratio of the inorganic acid catalyst to the hexavalent molybdenum source is (0.05~0.2:1), and then add C1~C5 organic acid at a temperature of 40~150 Reaction under ℃, described solvent is benzene, toluene, water, ethanol or sherwood oil;

[0020] (2) adding C6-C16 organic acid or C6-C16 ester to the product of step (1), and reacting at a temperature of 160-320°C;

[0021] (3) The temperature of the product in step (2) is lowered to 20-80°C, adding nickel-containing inorganic substances, reacting at 50-95°C for 3-10 hours, then raising the temperature to 100-180°C for 1-8 hours;

[0022] (4) separating the product obtained in step (3), removing the solvent phase, washing the oil phase with water, and obtaining the hydrocracking molybdenum-...

Embodiment 1

[0035]15g molybdenum trioxide and 300g water were dissolved and dispersed in the flask, purged with inert gas, 2.5ml hydrochloric acid was added dropwise, and acetic acid was added to react at a temperature of 70°C for 4 hours. The molar ratio of the amount of acetic acid to molybdenum trioxide was 5; The molar ratio of molybdenum oxide to 2-ethylhexanoic acid is 1:9, and heptanoic acid is added to the product of reaction 1) for 5 minutes. After the addition of heptanoic acid is completed, the reaction is carried out at a temperature of 170° C. for 5 hours; The product was cooled to 50°C, nickel sulfate was added according to the molar ratio of nickel sulfate to molybdenum trioxide of 0.3:1, reacted at 80°C for 8 hours, and then reacted at 120°C for 3 hours.

[0036] The product is separated, the solvent phase is removed, the oil phase is washed with water, and the product is collected by distillation under reduced pressure. Carry out metal content analysis, analysis method GB...

Embodiment 2

[0038] 20g molybdic acid and 150g water were dissolved and dispersed in the flask, purged with inert gas, 1.5ml hydrochloric acid was added dropwise, and oxalic acid was added to react for 8 hours at a temperature of 90°C. The molar ratio of oxalic acid consumption to molybdenum trioxide was 3: 1; according to the molar ratio of molybdic acid and heptanoic acid is 1:5, add heptanoic acid to the product of reaction 1), the addition time is 10 minutes, after the addition of heptanoic acid is completed, react at a temperature of 200 ° C for 8 hours; the product Cool down to room temperature, add nickel hydroxide at a molar ratio of nickel hydroxide to molybdic acid of 0.23:1, react at 70°C for 3 hours, and then react at 110°C for 5 hours.

[0039] The product is separated, the solvent phase is removed, the oil phase is washed with water, and the product is collected by distillation under reduced pressure. Carry out metal content analysis, the analysis method is GB / T 17476 equival...

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Abstract

The invention discloses a hydrocracking nickel-molybdenum catalyst and a preparation method thereof. The hydrocracking nickel-molybdenum catalyst is organic nickel-molybdenum salt and contains molybdenum ions, nickel ions and C1-C16 organic anions bonded with the molybdenum ions and the nickel ions, wherein the organic anions contain oxygen atoms, the mole ratio of the nickel ions to the molybdenum ions is (0.05-0.5):1, the valence state distribution of molybdenum in the molybdenum ions is shown as follows: the mole ratio of +4 valent molybdenum ions, +5 valent molybdenum ions and +6 valent molybdenum ions is (0.1-25.0):(10.0-40.0):(45.0-85.0). The provided hydrocracking nickel-molybdenum catalyst has good solubility in heavy oil and good hydrocracking performance and coking inhibition capability. The preparation method of the hydrocracking nickel-molybdenum catalyst adopts a simple process and the synthesis cost is lower.

Description

technical field [0001] The invention relates to a hydrogenation molybdenum-nickel cracking catalyst and a preparation method thereof, more specifically, to a sulfur- and phosphorus-containing nickel-molybdenum-containing organic hydrocracking catalyst and a preparation method thereof. Background technique [0002] Global oil resources are becoming increasingly heavy and inferior. In order to meet the needs of national economic growth and people's living needs, deep processing of heavy oil and improvement of resource utilization have become increasingly concerned issues. Heavy oil processing technology is divided into two categories: decarburization and hydrogenation. In order to further increase the yield of light oil, hydrogenation technology plays an increasingly important role in the field of heavy oil processing. The hydrogenation process includes fixed bed, moving bed, ebullating bed, and slurry bed processes. Among them, the fixed bed hydrogenation technology is the mo...

Claims

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Application Information

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IPC IPC(8): B01J31/04C10G47/02
CPCB01J31/04C10G47/02
Inventor 王红王子军王翠红申海平
Owner CHINA PETROLEUM & CHEM CORP