Halogen-containing heavy oil hydrogenation catalyst, preparation method thereof and heavy oil hydrotreating method

A heavy oil hydrogenation, halogen-containing technology, applied in catalyst activation/preparation, catalyst carrier, metal/metal oxide/metal hydroxide catalyst, etc. At the same time, there are problems such as bimodal pores, which can achieve the effect of good hydrodemetallization activity, slowing down the formation and growth

Active Publication Date: 2022-05-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The raw material of the alumina carrier is generally pseudo-boehmite. Various methods for preparing phosphorus-containing pseudo-boehmite have been disclosed in the prior art. In terms of controlling the pore distribution and pore volume of alumina by different methods, the prior art The properties of the described pseudo-boehmite and alumina are excellent in some respects, but it is difficult to obtain phosphorus-containing oxides with bimodal pores and large pore volumes and total pore volumes in both pore distributions. aluminum
[0003] At present, with the intensification of the trend of crude oil becoming heavier and inferior, the difficulty of crude oil processing has increased, and higher requirements have been put forward for catalysts for crude oil processing. Further improve

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  • Halogen-containing heavy oil hydrogenation catalyst, preparation method thereof and heavy oil hydrotreating method
  • Halogen-containing heavy oil hydrogenation catalyst, preparation method thereof and heavy oil hydrotreating method
  • Halogen-containing heavy oil hydrogenation catalyst, preparation method thereof and heavy oil hydrotreating method

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preparation example Construction

[0030] The second aspect of the present invention provides a method for preparing a halogen-containing heavy oil hydrogenation catalyst, including the steps of preparing an alumina support with a bimodal pore structure and introducing a hydrogenation active metal into the support, and the hydrogenation active metal is One or more selected from Group VIII metals and Group VIB metals, the amount of the hydrogenation active metal is such that the content of the hydrogenation active metal in the finally obtained catalyst is 0.3-20% by weight; Wherein, the steps for preparing the alumina carrier are as follows:

[0031] (1) Carry out a gelation reaction under the conditions of the simultaneous presence of an aluminum-containing compound and a phosphorus-containing compound to obtain a slurry containing phosphorus-containing alumina hydrate, and the phosphorus-containing compound makes the final carrier, with P 2 o 5 The calculated phosphorus content is 0.1-8.0% by weight;

[0032...

preparation example 1

[0089] (1) Preparation of Al 2 o 3 Concentration is 2L of aluminum sulfate solution of 50g / L, add 5mL concentrated phosphoric acid (concentration 85% by weight, the same below), 9.5g boric acid, obtain the aluminum sulfate solution containing phosphorus, boron element. In a 5-liter reaction tank, the above-mentioned aluminum sulfate solution and an 8% ammonia solution were added in parallel for reaction and precipitation, and then filtered (using XRD to characterize the hydrated aluminum oxide precipitation as an amorphous structure), the reaction temperature was 40 ° C, Control the flow rate of the ammonia solution to make the pH of the reaction system 5.5. In a 5-liter reaction tank, filter cake, deionized water and ammonia water are mixed and beaten. The amount of ammonia water is used to make the pH value of the slurry 8.0. The slurry is aged at 65°C for 60 minutes and filtered, and the filter cake is beaten with deionized water. After washing twice, the filter cake was ...

preparation example 2

[0092] (1) Preparation of Al 2 o 3 Concentration is 90g / L aluminum sulfate solution 2L, add 6mL concentrated phosphoric acid, 51g magnesium sulfate heptahydrate, obtain the aluminum sulfate solution containing phosphorus, magnesium element. In a 5-liter reaction tank, the above-mentioned aluminum sulfate solution containing phosphorus and magnesium elements and the ammonia solution with a concentration of 8% are added in parallel to carry out reaction precipitation, and then filter (the hydrated aluminum oxide precipitation is characterized by XRD as an amorphous structure), The reaction temperature is 45° C., and the flow rate of the ammonia solution is controlled so that the pH of the reaction system is 6.0. In a 5-liter reaction tank, filter cake, deionized water and ammonium bicarbonate were mixed and beaten. The amount of ammonia water was used to make the pH value of the slurry 9.2. The slurry was aged at 40°C for 240 minutes and then filtered. The filter cake was deion...

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Abstract

The invention relates to the field of heavy oil hydrogenation, and discloses a halogen-containing heavy oil hydrogenation catalyst, a preparation method thereof and a heavy oil hydrotreating method. The catalyst contains an alumina carrier with a bimodal pore structure and hydrogenation active metal loaded on the carrier, the carrier contains phosphorus and halogen elements, and by taking the weight of the carrier as a reference, the content of phosphorus in terms of P2O5 is 0.1-8.0 wt%, and the content of halogen in terms of elements is 0.1-6 wt%; characterized by a mercury intrusion method, the first pore distribution of the carrier is mesopores of 3-100 nm, the pore volume V mesopores is 1.0-1.5 mL/g, the second pore distribution of the carrier is macropores of 100-5000 nm, the pore volume V macropores is 1.0-1.8 mL/g, and the total pore volume V total is 2.0-3.3 mL/g. The catalyst is used in the heavy oil hydrotreating process and has good hydrotreating performance.

Description

technical field [0001] The invention relates to the field of heavy oil hydrogenation, in particular to a halogen-containing heavy oil hydrogenation catalyst, a preparation method thereof and a heavy oil hydrogenation treatment method. Background technique [0002] Alumina, especially γ-alumina, is often used as a carrier for the preparation of catalysts because of its good pore structure, specific surface area and thermal stability. In particular, the pore structure of the alumina support is particularly critical to the catalyst performance. The raw material of the alumina carrier is generally pseudo-boehmite. Various methods for preparing phosphorus-containing pseudo-boehmite have been disclosed in the prior art. In terms of controlling the pore distribution and pore volume of alumina by different methods, the prior art The properties of the described pseudo-boehmite and alumina are excellent in some respects, but it is difficult to obtain phosphorus-containing oxides with...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/883B01J23/882B01J23/888B01J37/02B01J37/08B01J21/04B01J32/00B01J35/10B01J37/03B01J37/00C10G45/08
CPCB01J23/883B01J23/882B01J23/888B01J23/002B01J37/0201B01J37/088B01J21/04B01J35/1019B01J35/1047B01J37/031B01J37/082B01J37/0018C10G45/08B01J2523/00B01J2523/31B01J2523/68B01J2523/847B01J2523/845B01J2523/69Y02P20/52
Inventor 孙淑玲杨清河胡大为曾双亲户安鹏王振刘涛
Owner CHINA PETROLEUM & CHEM CORP
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