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Hydrogenation catalyst and preparation method thereof

A hydrogenation catalyst and hydrogenation activity technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of small catalyst pore size, deactivation, catalyst capacity The metal ability has not been fully utilized and other problems, to achieve the effect of high demetallization rate, hydrogenation demetallization and metal capacity improvement

Active Publication Date: 2012-07-25
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
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Problems solved by technology

[0004] The alumina carrier obtained by the prior art for residual oil hydroprocessing has the technical characteristics of high pore volume and large pore diameter, but for residue oil with a metal content above 150ppm, the pore diameter of the catalyst obtained by the existing technology is still small, due to the existence of diffusion resistance Most of the metal impurities are deposited on the pores of the catalyst, resulting in the rapid deactivation of the catalyst without fully exerting its metal-accommodating capacity. Therefore, effectively increasing the pore size of the catalyst will be the key to the development of inferior residue hydrogenation catalysts

Method used

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

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preparation example Construction

[0012] The present invention provides a method for preparing a hydrogenation catalyst, the method comprising shaping the alumina precursor, drying, calcining, and introducing at least one metal selected from Group VIII and at least one metal selected from Group VIB, wherein, The alumina precursor has a pore volume of 0.8-1.5 ml / g and a pore diameter of 8-40 nm. The calcination condition is 1-6 hours at a temperature of 800-1200° C.

[0013] Under preferred conditions, the calcination condition is 2-4 hours at a temperature of 900-1100°C.

[0014] The precursor of alumina is preferably hydrated alumina. The hydrated alumina is preferably one or more of alumina trihydrate, alumina monohydrate and amorphous aluminum hydroxide. According to the present invention, precursors of alumina which meet the requirements are commercially available.

[0015] According to the method provided by the present invention, molding can be carried out by conventional methods, such as tableting, ba...

Embodiment 1

[0026] 300 grams of pseudo-boehmite dry rubber powder (Changling Catalyst Factory produces PB110) and 10 grams of fenugreek powder are mixed homogeneously, and at room temperature this mixture and the concentration of 360 milliliters are 1% nitric acid aqueous solution, mix homogeneously, After continuing to knead on a twin-screw extruder to form a plastic body, extrude into a trilobal strip of ф1.5mm, dry the wet strip at 120°C for 4 hours, and then calcinate at 1000°C for 3 hours to obtain the carrier Z1. The specific surface area, pore volume and pore size distribution of Z1 were measured, and the results are shown in Table 2.

[0027] The specific surface area, pore volume and pore size distribution of the carrier were measured by BET low temperature nitrogen adsorption method.

Embodiment 2

[0029] Mix 300 grams of pseudo-boehmite dry rubber powder (PB120 produced by Changling Catalyst Factory) and 10 grams of asparagus powder, add 360 milliliters of nitric acid aqueous solution with a concentration of 1%, mix well, and continue kneading on the twin-screw extruder After being plasticized, it was extruded into a butterfly-shaped strip of ф1.1mm, and the wet strip was dried at 120°C for 2 hours, and then calcined at 950°C for 2 hours to obtain the carrier Z3. The specific surface, pore volume and pore size distribution of Z3 were determined in the same manner as in Example 1, and the results are shown in Table 2.

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Abstract

The invention relates to a hydrogenation catalyst and a preparation method thereof, more particularly to a heavy oil-hydrotreating hydrogenation catalyst and a preparation method thereof. The hydrogenation catalyst according to the invention contains alumina carrier, at least one metal selected from Family VIII and at least one metal selected from Family VIB, wherein the alumina carrier has 0.6-1.2 millilitre / gram of pore volume, 80-200 square meter / gram of specific surface and 25-35 nanometers of probable diameter, and the alumina carrier has the following pore distribution: the pore volume of pores with less than 20 nanometers of diameter is smaller than total pore volume by 50%. The hydrogenation catalyst according to the invention has the alumina carrier with larger probable diameter so that the performance of the catalyst in hydrogenation demetallization and metal dissolution is improved.

Description

technical field [0001] The invention relates to a hydrogenation catalyst and a preparation method thereof, in particular to a heavy oil hydrogenation treatment hydrogenation catalyst and a preparation method thereof. Background technique [0002] As the trend of heavy and inferior crude oil in the world continues to intensify, the hydrogenation technology of residual oil has attracted widespread attention. The deep processing of inferior residual oil is not only conducive to improving the utilization rate of crude oil and alleviating the tense trend of energy supply, but also It can also reduce environmental pollution and realize efficient and clean utilization of energy. Compared with distillate oil, in addition to impurities such as sulfur and nitrogen, heavy oil also contains a higher proportion of metal impurities such as Ni and V and asphaltenes. The continuous deposition of these impurities on the surface of the catalyst can easily lead to The pressure drop increased ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/883C10G47/12
Inventor 胡大为杨清河刘滨曾双亲牛传峰邵志才戴立顺聂红刘佳石亚华李大东
Owner CHINA PETROLEUM & CHEM CORP