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Heavy oil hydrotreating catalyst and use thereof

A heavy oil hydrogenation and catalyst technology, which is applied in heavy oil hydrogenation catalyst and heavy oil hydrogenation field, can solve the problem of catalyst surface active center reduction and achieve good hydrodesulfurization effect

Active Publication Date: 2016-07-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is to provide a new catalyst with high metal content which cannot avoid the aggregation of active metals, which leads to the reduction of active centers on the surface of the catalyst. Heavy oil hydrotreating catalyst with better desulfurization, denitrification effect and carbon residue conversion performance and its application

Method used

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  • Heavy oil hydrotreating catalyst and use thereof
  • Heavy oil hydrotreating catalyst and use thereof
  • Heavy oil hydrotreating catalyst and use thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] The pseudo-boehmite dry rubber powder RPB90 produced by 1 kilogram of Changling Catalyst Factory and the turmeric powder of 30 grams are mixed uniformly. ) in 1.1 liters of aqueous solution, mixed evenly, continued kneading on a twin-screw extruder to form a plastic body, extruded into a trilobal strip of ф1.1 mm, dried at 120°C for 3 hours, and then roasted at 600°C for 3 hours to obtain Boron-containing shaped alumina carrier Z1. The physical and chemical results of the determination of Z1 are shown in Table 1.

Embodiment 2

[0048] The pseudo-boehmite dry rubber powder RPB100 produced by 1 kilogram of Changling Catalyst Factory is mixed with 30 gram of turnip powder, at room temperature this mixture is mixed with boron trioxide 20g, nitric acid 25 milliliters (mass fraction 65%) Mix 1.2 liters of the aqueous solution of the solution evenly, continue kneading on the twin-screw extruder to form a plastic body, and extrude it into a butterfly-shaped strip of ф1.1 mm. After the wet strip is dried at 110°C for 2 hours, it is roasted at 700°C for 3 hours to obtain boron-containing Shaped alumina support Z2. The physical and chemical results of the determination of Z2 are shown in Table 1.

Embodiment 3

[0051] Weigh 150g of the Z1 carrier and place it in the hydration kettle, add 450g of deionized water, seal the hydration kettle and put it in the oven, heat it with a programmed temperature rise, and control the heating rate to 10°C·min -1 , the treatment temperature is 80° C., and the treatment time is 12 hours. After the completion of the hydrothermal treatment, the alumina was filtered, and then dried at 120° C. for 3 hours to obtain a hydrothermally treated alumina carrier.

[0052] Take 100 grams of carrier Z1 after heat treatment in water, and use 220 milliliters containing MoO 3 170 g / L, NiO 30 g / L mixed solution of ammonium molybdate and nickel nitrate was impregnated for 1 hour, filtered, dried at 120°C for 2 hours, and calcined at 410°C for 4 hours to obtain catalyst C1. Calculated by oxide and based on the load on the surface of the unit carrier, the content of molybdenum oxide and nickel oxide in catalyst C1 is measured by X-ray fluorescence spectrometer, and whe...

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Abstract

The present invention provides a heavy oil hydrotreating catalyst which comprises a boron-containing forming alumina carrier, metal component molybdenum and metal component cobalt or nickel; by calculation of oxide on the basis of the total weight of the boron-containing forming alumina carrier as a reference, the content of boron in the boron-containing forming alumina carrier is 0.5-5 weight%; by calculation of oxide on the basis of the unit carrier surface loading amount as a reference, the content of the metal component molybdenum in the catalyst is 4.8mumol / m<2> to 9.0mumol / m<2>, the content of the metal component cobalt or nickel in the catalyst is 1.5 mumol / m<2> to 4.0 mumol / m<2>; and when the catalyst is characterized by XRD, no MoO3 characteristic peak appears at diffraction angle 2 theta of 26-degree + / -2-degree. Compared with conventional heavy oil hydrotreating catalysts, the heavy oil hydrotreating catalyst has better hydrodesulfurization, denitrification and carbon residue removal effects when used in heavy oil hydrotreating.

Description

technical field [0001] The invention relates to a heavy oil hydrogenation treatment catalyst and a heavy oil hydrogenation treatment method using the heavy oil hydrogenation treatment catalyst. Background technique [0002] Heavy oil processing, especially the deep processing of residual oil, not only helps to improve the utilization rate of crude oil, alleviate the tense trend of energy supply, but also reduce environmental pollution and realize efficient and clean utilization of energy. [0003] Heavy oil is enriched with impurities such as sulfur, nitrogen, metals, and carbon residues in crude oil. These impurities have serious adverse effects on subsequent processing and product properties, so they must be removed. Since impurities such as sulfur and nitrogen in heavy oil are mostly enriched in macromolecular polycyclic aromatic hydrocarbons, it is difficult to remove them. Therefore, catalysts for related reactions such as desulfurization, denitrogenation, and carbon re...

Claims

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Application Information

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IPC IPC(8): B01J23/883B01J23/882B01J35/10B01J32/00C10G45/08
Inventor 胡大为杨清河张轩曾双亲刘佳孙淑玲戴立顺
Owner CHINA PETROLEUM & CHEM CORP