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Hydrogenation upgrading catalyst and preparation method thereof

A technology for hydrogenation modification and catalyst, which is used in chemical instruments and methods, physical/chemical process catalysts, organic compound/hydride/coordination complex catalysts, etc.

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

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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  • Hydrogenation upgrading catalyst and preparation method thereof
  • Hydrogenation upgrading catalyst and preparation method thereof
  • Hydrogenation upgrading catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0086] Weigh 15g of tartaric acid, stir and dissolve in 45g of water to prepare wetting solution I. Take 300g of the S1 carrier, and spray the wetting solution I evenly on the S1 carrier for 15 minutes. After spraying and immersing in wetting solution I, dry at 100°C for 2 hours, impregnate the above carrier with an equal volume of impregnating solution containing Mo, Co, and P (first impregnating solution), and divide the obtained samples into three parts evenly after impregnating. One sample was not cured, dried at 120°C for 3 hours, roasted at 480°C for 2 hours, and the obtained sample was marked as B1; the second sample was cured for 1 hour, dried at 120°C for 3 hours, and roasted at 480°C for 2 hours, and the obtained sample was marked as B2; The third 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 B3.

[0087] Weigh 6g of polyethylene glycol 2000 (that is, polyethylene glycol with a molec...

Embodiment 2

[0090] Weigh 3 g of malic acid, stir and dissolve in 24 g of ethanol to prepare wetting solution I. Take 300g of the S2 carrier, and spray the wetting solution I evenly on the S2 carrier for 5 minutes. The above-mentioned carrier was impregnated with an equal volume of impregnation solution (first impregnation solution) containing Mo, Co, and P. After impregnation, it was cured for 1 hour, dried at 120°C for 3 hours, and calcined at 480°C for 2 hours. The obtained sample was designated as B4.

[0091] Weigh 24 g of polyethylene glycol 1000, stir and dissolve in measured water to prepare solution II. The sample B4 was impregnated with an equal volume of this solution II, and then cured for 5 hours. After drying at 120°C for 3 hours, the prepared sample was designated as Z4.

[0092]The Z4 sample was spray-impregnated with an equal volume of impregnating solution containing Mo, Ni, and P (the second impregnating solution). After spraying, the sample was divided into three parts...

Embodiment 3

[0094] Weigh 7g each of citric acid and malonic acid, stir and dissolve in 40g water to prepare wetting solution I. Take 200g of the S3 carrier, and spray the wetting solution I evenly on the S3 carrier for 25 minutes. The above-mentioned carrier was impregnated with an equal volume of Mo, Co, and P impregnating solution (the first impregnating solution). After impregnation, it was cured for 1 hour, dried at 120°C for 3 hours, and calcined at 480°C for 2 hours. The obtained sample was designated as B5.

[0095] Weigh 4g of polyethylene glycol 8000, stir and dissolve in the measured aqueous solution to prepare solution II. The sample B5 was impregnated with equal volume of this solution II, and then cured for 5 hours. After drying at 120°C for 3 hours, the prepared sample was designated as Z5.

[0096] The Z5 sample was spray-impregnated with an equal volume of impregnating solution containing Mo, Ni, and P (the second impregnating solution), and dried directly at 120°C for 3 ...

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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 polyol. The preparing method includes dipping the carrier with a wetting solution containing an absorbent I by adopting an unsaturated dipping method, dipping with a solution containing the active metal Mo and the active metal Co, drying, calcinating, dipping with a solution containing an absorbent II that is the polyol by saturated dipping or excessive dipping, dipping with a solution containing the active metal Mo and the active metal Ni, and drying. 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 杨占林唐兆吉姜虹王继锋魏登凌温德荣
Owner CHINA PETROLEUM & CHEM CORP