Preparation of bubbling bed hydrotreating catalyst

A hydrotreating and catalyst technology, applied in the refining of hydrocarbon oil, petroleum industry, refining to remove heteroatoms, etc., can solve the problems of harsh catalytic reaction conditions, high pressure drop of the catalyst bed, and short catalyst life cycle, and achieves a high level of performance. Mechanical strength and wear resistance, loss reduction, effect of reducing olefin and aromatic content

Active Publication Date: 2009-03-04
CHINA PETROLEUM & CHEM CORP +1
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  • Description
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  • Application Information

AI Technical Summary

Problems solved by technology

There are the following problems in the hydrotreating of heavy oil products using the fixed bed process: the catalytic reaction conditions will be relatively harsh because the heavy oil products are heavy and contain more mechanical impurities; high-nitrogen raw materials will accelerate catalyst deactivation Very short, the product properties cannot be guaranteed; the pressure drop of the catalyst bed is high;

Method used

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  • Preparation of bubbling bed hydrotreating catalyst
  • Preparation of bubbling bed hydrotreating catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0052] Preparation of modified alumina M-1

[0053] A. Set the concentration to contain 160gAl 2 o 3 / L NaAlO 2 Solution (caustic ratio 1.25-1.5) and concentration 40gAl 2 o 3 / L Al 2 (SO 4 ) 3 The solution was poured into the gel forming device equipped with 1L of bottom water under the condition of stirring, and the temperature was controlled at 60°C and the pH value was 8.5.

[0054] B. After the gelation is completed, age for 0.5-1 hour under stirring conditions.

[0055] C. After aging, the feed liquid is filtered, beaten and washed four times with water, and the ratio of water to filter cake is 30:1.

[0056] D, get 30g magnesium nitrate (Mg(NO 3 ) 2 6H 2 O) add distilled water to dissolve, dilute to 250ml with volumetric flask, be made into magnesium nitrate aqueous solution; Add magnesium nitrate aqueous solution prepared in step C gained slurry and carry out beating, stir for 0.8 hour, filter and dry to obtain magnesium nitrate of the present invention The...

Embodiment 2

[0058] Preparation of modified alumina M-2

[0059] A. Set the concentration to contain 160gAl 2 o 3 / L NaAlO 2 Solution (caustic molar ratio 1.25-1.5) and concentration 40gAl 2 o 3 / L Al 2 (SO 4 ) 3 The solution was poured into the gel forming device equipped with 1L of bottom water under the condition of stirring, and the temperature was controlled at 60°C and the pH value was 8.5.

[0060] B. After the gelation is completed, age for 0.5-1 hour under stirring conditions.

[0061] C. After aging, the feed liquid is filtered, beaten and washed four times with water, and the ratio of water to filter cake is 30:1.

[0062] D, get 84g magnesium chloride MgCl 2 Add distilled water to dissolve, dilute to 250ml with a volumetric flask, and make a magnesium-containing aqueous solution; add the prepared magnesium nitrate aqueous solution to the slurry obtained in step C for beating, stir for 0.5 hours, filter and dry to obtain the magnesium-containing alumina of the present i...

Embodiment 3

[0066] Preparation of ebullating bed hydrogenation catalyst C-1 for stable hydrogenation of heavy oil products of the present invention.

[0067] With 206.6 grams of M-1 and 22 grams of alumina fiber powder (length 30 microns, diameter 6 microns, specific surface 183m 2 / g, pore volume 0.08ml / g) is evenly wetted with 290ml S-1 solution; 0.454ml / g, specific surface area 258m 2 Add 51g aluminum dihydrogen phosphate in / g), add peptizing acid and make adhesive (dry basis 30wt%, acid-aluminum mol ratio is 0.3); , and then put it into a roller compactor, and grind until the paste can be extruded, extruded, dried at 110°C for 4 hours, and roasted at 550°C for 3 hours to obtain catalyst C-1. The physical and chemical properties of the catalyst are listed in Table 2.

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Abstract

The invention discloses a preparation method of a boiling bed hydrotreatment catalyst. During the preparation method of the catalyst, alumina fibers and aluminum dihydrogen phosphate are added, thus improving the mechanical intensity of the catalyst, improving the service life of the catalyst and reducing the product cost. In the method, the aluminum dihydrogen phosphate with better acidity is preferably added into a bond, thus being capable of easing the strong mutual effects between an acid and a refractory porous inorganic oxide as well as the alumina fibers and reducing the loss of pore volumes and specific surface area. Besides, as the aluminum dihydrogen phosphate contains 6 hydroxide radicals, the aluminum dihydrogen phosphate is easy to form a complex compound with metals and is beneficial to improving the mutual effect between a carrier and active metals, thereby improving the activity of the catalyst.

Description

technical field [0001] The invention relates to a preparation method of an ebullating bed hydrogenation treatment catalyst, in particular to a preparation method of an ebullation bed hydrogenation treatment catalyst used for the stable hydrogenation of heavy oil products. Background technique [0002] The catalytic hydrogenation process usually used for heavy oil products is mainly a fixed bed hydrogenation process. Fixed bed reactors are especially suitable for handling lighter and cleaner feeds, such as naphtha, middle distillates, gas oils and ordinary residues. The fixed bed reactor is characterized by smoother operation and easier control. There are the following problems in the hydrotreating of heavy oil products using the fixed bed process: the catalytic reaction conditions will be relatively harsh because the heavy oil products are heavy and contain more mechanical impurities; high-nitrogen raw materials will accelerate catalyst deactivation Very short, the product...

Claims

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Application Information

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IPC IPC(8): C10G45/20C10G45/04
Inventor 刘雪玲王刚王继锋彭绍忠杨占林姜虹
Owner CHINA PETROLEUM & CHEM CORP
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