Hydrotreating catalyst as well as preparation method and application thereof

A hydrotreating and catalyst technology, applied in catalyst activation/preparation, physical/chemical process catalyst, molecular sieve catalyst, etc., can solve the problems of poor denitrification effect, increase operating cost, and insignificant denitrification effect, and achieve good denitrification effect. Effects of synergistic catalysis, increased content of medium and strong acids, and improved intrinsic activity

Pending Publication Date: 2022-05-10
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0007] CN101590416A discloses a method for preparing a molybdenum-nickel hydrogenation catalyst. The method uses two steps of kneading and impregnation to prepare the catalyst. First, molybdenum oxide, titanium-containing compounds, and phosphorus-containing compounds are added to alumina and/or the precursor of alumina Add nitric acid solution, knead, extrude, dry and roast to obtain aluminum oxide moldings containing titanium, phosphorus and molybdenum, then impregnate nickel-containing phosphoric acid solution, dry and roast to obtain molybdenum-nickel hydrogenation catalysts, However, the catalyst is not effective for refining distillate oil with high nitrogen content
[0008] CN1052501A discloses a hydrorefining catalyst and its preparation m

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  • Hydrotreating catalyst as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0075] Preparation of Hydrotreating Catalyst Support:

[0076] (i) Preparation of Al-SBA-15 molecular sieve

[0077] (1) Preparation of amorphous silica-alumina dry glue A1 and slurry: sodium aluminate solution concentration 20gAl 2 o 3 / L, the concentration of sodium silicate solution is 60gSiO 2 / L, take 0.75L sodium aluminate solution and put it into the gel-forming tank, then add 0.35L sodium silicate solution, control the reaction temperature at 20°C, and feed CO with a concentration of 40v%. 2 gas, CO 2 When the gas accounts for 50% of the total intake, add 0.20L sodium silicate solution while ventilating to control the pH value of the gel to 9.7, then ventilate and stabilize for 20 minutes, filter the slurry and wash it with 65°C deionized water until neutral. The filter cake was beaten with water at a solid-to-liquid volume ratio of 12:1, treated at 120°C under 3.5MPa water vapor pressure for 2 hours, dried at 120°C for 6 hours, crushed and sieved to obtain the amo...

Embodiment 2

[0085] Preparation of Hydrotreating Catalyst Support:

[0086] (i) Preparation of Al-SBA-15 molecular sieve

[0087] (1) Preparation of amorphous silica-alumina dry glue A2: concentration of sodium aluminate solution 30gAl 2 o 3 / L, sodium silicate working solution concentration 90gSiO 2 / L, take 1.25L of sodium aluminate solution and place it in a gel-forming tank, then add 0.65L of sodium silicate solution, control the reaction temperature at 32°C, and feed CO with a concentration of 52v%. 2 Gas, stop when the pH value reaches 9.9, then ventilate and stabilize for 20 minutes, wash until neutral, add water to the filter cake according to the solid-liquid volume ratio of 9:1, and treat it at 130 ° C for 3 hours under 3.9 MPa steam pressure. After drying at 130°C for 8 hours, it was crushed and sieved to obtain the amorphous silica-alumina product A2. The prepared amorphous silica-alumina A2 is mixed with deionized water and beaten to form a slurry; wherein, the mass ratio ...

Embodiment 3

[0095] Preparation of Hydrotreating Catalyst Support:

[0096] (i) Preparation of Al-SBA-15 molecular sieve and slurry

[0097] (1) Preparation of amorphous silica-alumina dry glue A3: concentration of sodium aluminate solution 30gAl 2 o 3 / L, the concentration of sodium silicate solution is 50gSiO 2 / L, put 0.75L sodium aluminate solution into the gel-forming tank, then add 0.12L sodium silicate solution, control the reaction temperature at 23°C, and feed CO with a concentration of 48v%. 2 gas, CO 2 When the gas accounts for 50% of the total intake, add 0.20L sodium silicate solution while ventilating, control the pH value of the gel to be 8.8, then ventilate and stabilize for 20 minutes, filter the slurry and wash it with 75°C deionized water until neutral. The filter cake was beaten with water at a solid-to-liquid volume ratio of 11:1, treated at 120°C under 3.5MPa water vapor pressure for 2 hours, dried at 120°C for 6 hours, crushed and sieved to obtain the amorphous s...

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Abstract

The invention discloses a hydrotreating catalyst as well as a preparation method and application thereof. The preparation method of the hydrotreating catalyst comprises the following steps: (i) preparing an Al-SBA-15 molecular sieve; (ii) aluminum oxide and the Al-SBA-15 molecular sieve prepared in the step (i) are mixed, kneaded and molded, and a hydrotreating catalyst carrier is obtained through drying and roasting; and (iii) impregnating the carrier obtained in the step (ii) with an impregnating solution containing an active metal component and a polyhydroxy compound, and then drying and roasting to obtain the hydrotreating catalyst. The catalyst prepared by the method provided by the invention can deeply remove nitrogen-containing compounds in shale oil, has good hydrogenation performance, meets the quality requirements of subsequent process production, and ensures that the use performance of the cracking catalyst is fully exerted.

Description

technical field [0001] The invention relates to a hydrogenation treatment catalyst and a preparation method thereof, and the catalyst is especially suitable for the shale oil hydrogenation treatment process. Background technique [0002] Among natural resources, oil shale, like petroleum, is mainly produced by algae and other lower plankton through decay and coalification. The shale oil "squeezed" from oil shale through low-carbon distillation and other methods is called "artificial petroleum". After further processing and refining, liquid fuels such as gasoline, kerosene, and diesel can be produced. In the initial stage of oil shale mining, the development of this industry was restricted due to the unqualified technology and the pollution of the environment during the production process. In recent years, with the advancement of technology, this problem has been well solved. It is foreseeable that under the current situation of shortage of oil resources and high oil prices...

Claims

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Application Information

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IPC IPC(8): B01J21/04B01J29/03B01J37/02B01J35/10C10G45/12
CPCB01J21/04B01J29/0341B01J37/0203B01J35/1019B01J35/1038C10G45/12B01J2229/10B01J2229/186C10G2300/202C10G2300/70Y02P20/52
Inventor 杨占林唐兆吉杜艳泽樊宏飞于政敏
Owner CHINA PETROLEUM & CHEM CORP
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