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Distillate oil hydrotreating catalyst and preparation method thereof

A hydrogenation treatment and catalyst technology, applied in the direction of physical/chemical process catalysts, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of not being able to effectively apply heavy distillate oil hydrodesulfurization And other issues

Active Publication Date: 2017-01-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] These prior art hydrotreating catalysts are all conventional hydrodesulfurization catalysts, and cannot be effectively applied to hydrodesulfurization of heavy distillates (especially diesel oil)

Method used

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  • Distillate oil hydrotreating catalyst and preparation method thereof
  • Distillate oil hydrotreating catalyst and preparation method thereof
  • Distillate oil hydrotreating catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0084] Weigh 12g of polyethylene glycol 2000 (that is, polyethylene glycol with a molecular weight of 2000, the same below), stir and dissolve in measured water to prepare wetting solution I. Use the wetting solution I to impregnate 200g of alumina carrier, then perform 10h curing, and after drying at 120°C for 3h, the prepared samples are respectively marked as B1.

[0085] The above-mentioned B1 sample was spray-impregnated with an equal volume of impregnation solution containing W and Ni. After the spray-impregnation, it was directly dried at 120°C for 3 hours and calcined at 480°C for 2 hours. The obtained sample was designated as Z1.

[0086] Weigh 10 g of tartaric acid, stir and dissolve in 30 g of water to prepare a wetting solution. Take the Z1 sample, and spray the wetting solution II evenly on Z1 for 15 minutes. After spraying and immersing in the wetting solution II, dry at 100°C for 2 hours, impregnate the above-mentioned carrier with an equal volume of impregnati...

Embodiment 2

[0088] Weigh 16g of polyethylene glycol 1000, stir and dissolve in measured water to prepare wetting solution I. Use the wetting solution I to impregnate 200g of alumina carrier in equal volume, then perform curing for 5 hours, and dry at 120°C for 3 hours, and the prepared sample is designated as B2.

[0089] Spray and impregnate the B2 sample with an equal volume of impregnation solution containing W and Ni. After the spray impregnation, divide the sample into two parts on average. The first sample is directly dried at 120°C for 3 hours and roasted at 480°C for 2 hours. The obtained sample is designated as Z2; The second sample was cured for 3 hours, dried at 120°C for 3 hours, and roasted at 480°C for 2 hours. The prepared sample was designated as Z3.

[0090] Weigh 1.0 g of malic acid, stir and dissolve in 6 g of ethanol to prepare wetting solution II. Spray and soak the wetting solution II evenly on Z2 for 5 minutes. The above samples were impregnated with equal volumes...

Embodiment 3

[0092] Weigh 7.5g of polyethylene glycol 8000, stir and dissolve in the measured aqueous solution to prepare wetting solution I. Use the wetting solution I to impregnate 300g of alumina carrier in equal volume, then perform curing for 5 hours, and dry at 120°C for 3 hours, and the prepared sample is designated as B3.

[0093] The B3 sample was spray-impregnated with an equal volume of impregnation solution containing W and Ni, dried directly at 120°C for 3 hours, and calcined at 480°C for 2 hours. The obtained sample was designated as Z4.

[0094] Weigh 10.5g each of citric acid and malonic acid, stir and dissolve in 40g water to prepare wetting solution II. Spray and soak the wetting solution II evenly on Z4 for 25 minutes. The above sample was impregnated with an equal volume of impregnation solution containing Mo, Co, and P. After impregnation, it was cured for 1 hour and dried at 120°C for 3 hours. The obtained catalyst was designated as C5.

[0095] Prepare an aqueous s...

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Abstract

The invention discloses a distillate oil hydrotreatment catalyst and a preparation method thereof. The hydrotreatment catalyst comprises an alumina-based carrier and active metal ingredients of Mo, Co, Ni and W. The distribution of the active metal ingredients in the catalyst particles is characterized by comprising Co0 / Co1<Co1 / 2 / Co1<1, Mo0 / Mo1<Mo1 / 2 / Mo1<1, Ni0 / Ni1>Ni1 / 2 / Ni1>1 and W0 / W1>W1 / 2 / W1>1, and preferably, the catalyst particles contain organic matters. The preparation method comprises the following steps of carrying out saturated or excess immersion in an adsorbent I-containing solution, carrying out immersion in a solution containing active metals of W and Ni, carrying out drying and roasting, carrying out unsaturated immersion in an adsorbent II containing one or more of organic carboxylic acids and salts thereof, and carrying out immersion for loading active metals of Mo and Co. The hydrotreatment catalyst has good deep-desulphurization activity and is especially suitable for deep desulphurization of diesel oil.

Description

technical field [0001] The invention relates to a hydroprocessing catalyst and a preparation method thereof, in particular to a hydroprocessing catalyst suitable for deep desulfurization of heavy distillate oil (especially diesel oil) and a preparation method thereof. Background technique [0002] As today's society has higher and higher requirements for the cleanliness of heavy distillate oil (especially diesel oil), the deep hydrodesulfurization technology of heavy distillate oil is becoming more and more important. The sulfur-containing compounds in heavy distillates mainly include aliphatic sulfides, sulfides, dibenzothiophenes, alkylbenzothiophenes, and alkyldibenzothiophenes, among which dibenzothiophenes, dibenzothiophenes, and dibenzothiophenes are difficult to remove. Thiophene compounds such as alkylbenzothiophene and alkyldibenzothiophene, especially 4,6-dimethyldibenzothiophene (4,6-BMDBT) and 2,4,6-trimethyldibenzothiophene Thiophene (2,4,6-BMDBT) sulfur-contai...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/888C10G45/08
Inventor 杨占林姜虹唐兆吉王继锋温德荣魏登凌
Owner CHINA PETROLEUM & CHEM CORP