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A kind of hydrogenation reforming catalyst and preparation method thereof

A hydrogenation modification and catalyst technology, applied in the fields of physical/chemical process catalysts, organic compound/hydride/coordination complex catalysts, chemical instruments and methods, etc.

Active Publication Date: 2017-01-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When the catalyst is used for diesel hydro-upgrading, although the freezing point of the diesel fraction can be lowered and the cetane number of the modified diesel can be increased, the diesel yield is still low below 97%.

Method used

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  • A kind of hydrogenation reforming catalyst and preparation method thereof
  • A kind of hydrogenation reforming catalyst and preparation method thereof
  • A kind of hydrogenation reforming catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0088] Weigh 18g 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 this wetting solution I to impregnate 300g of the S1 carrier, then perform 10h of curing, and after drying at 120°C for 3h, the prepared sample is designated as B1.

[0089] The above-mentioned B1 sample was spray-impregnated with an equal volume of impregnating solution containing Mo, Ni, and P (the first impregnating solution). After the spray-immersing, it was directly dried at 120°C for 3 hours and roasted at 480°C for 2 hours. The obtained sample was designated as Z1 .

[0090]Weigh 15g of tartaric acid, stir and dissolve in 45g of water to prepare a wetting solution. Spray and soak the wetting solution II evenly on Z1 for 15 minutes. After spraying and immersing in wetting solution II, dry at 100°C for 2 hours, impregnate the above-mentioned carrier with an equal volume of imp...

Embodiment 2

[0092] Weigh 24g of polyethylene glycol 1000, stir and dissolve in measured water to prepare wetting solution I. Use this wetting solution I to impregnate 300g of S2 carrier in an equal volume, then perform 5h of curing, and after drying at 120°C for 3h, the prepared sample is designated as B2.

[0093] Spray and impregnate the B2 sample with an equal volume of impregnating solution (first impregnating solution) containing Mo, Ni, and P. After spraying, divide the obtained sample into three 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 marked as Z2; the second sample is cured for 1h, dried at 120°C for 3h, and roasted at 480°C for 2h, and the sample obtained is marked as Z3; the third sample is cured for 3h, dried at 120°C for 3h, and roasted at 480°C After 2h, the prepared sample was designated as Z4.

[0094] Weigh 1.0 g of malic acid, stir and dissolve in 6 g of ethanol to prepare wetting ...

Embodiment 3

[0096] Weigh 4g of polyethylene glycol 8000, stir and dissolve in the measured aqueous solution to prepare wetting solution I. Impregnate 200g of S3 carrier with equal volume of this wetting solution I, then perform 5h of curing, and after drying at 120°C for 3h, the prepared sample is designated as B3.

[0097] The B3 sample was spray-impregnated with an equal volume of impregnation solution containing Mo, Ni, and P (the first immersion solution), and dried directly at 120°C for 3 hours. The obtained sample was designated as Z5.

[0098] Weigh 7g 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 the Z5 for 25 minutes. The above sample was impregnated with an equal volume of impregnation solution containing Mo, Co, and P (the second impregnation solution). After the impregnation, it was cured for 1 hour and dried at 120°C for 3 hours. The obtained catalyst was designated as C7....

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Abstract

A catalyst for hydrogenation modification and a preparing method thereof are disclosed. In the catalyst, a carrier comprises aluminum oxide and a molecular sieve, active metal components are Mo, Co and Ni, distribution situations of concentrations of the active metal components in the cross section of each catalyst particle are that Co0 / Co1<Co<1 / 2> / Co1<1, Ni0 / Ni1>Ni<1 / 2> / Ni1>1, Ni0 / Mo0>Ni<1 / 2> / Mo<1 / 2>>Ni1 / Mo1 and Co0 / Mo0<Co<1 / 2> / Mo<1 / 2><Co1 / Mo1, and the catalyst comprises an organic compound. The preparing method includes dipping with a solution containing an absorbent I by saturated dipping or excessive dipping, dipping with a solution containing the active metal Mo and the active metal Ni, drying, calcinating, dipping with an absorbent II comprising one or more of organic carboxylic acids and salts thereof by unsaturated dipping, and loading the active metal Mo and the active metal Co by dipping or loading the Mo, the Co and the organic compound by dipping. The catalyst is used in a diesel oil hydrogenation modification process, has deep hydrodesulfurization activity, and can improve comprehensive properties such as the cetane number under the circumstance that a high diesel oil yield is maintained.

Description

technical field [0001] The invention relates to a hydrogenation upgrading catalyst and a preparation method thereof, in particular to a hydrogenation upgrading catalyst suitable for diesel oil upgrading and a preparation method thereof. Background technique [0002] For clean diesel production, existing technologies mainly include hydrorefining and medium-pressure hydroupgrading technologies. Hydrofining can reduce the sulfur content of modified diesel, but it has limited ability to improve cetane number and lower T95 temperature. Medium-pressure hydro-upgrading uses a hydro-upgrading catalyst containing molecular sieves (Y-type molecular sieves or β molecular sieves) to properly crack aromatics in diesel oil, while reducing the content of sulfur and nitrogen impurities in diesel oil, and improving diesel cetane Comprehensive performance such as value. However, if the current hydrogenation upgrading catalyst is used to improve the comprehensive performance of diesel oil (s...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/34C10G45/12
Inventor 温德荣杨占林唐兆吉姜虹王继锋魏登凌
Owner CHINA PETROLEUM & CHEM CORP