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Catalyst and its preparation method and application as well as catalyst precursor reduction activation method and preparation method of α-olefin

A catalyst and olefin technology, which can be used in the preparation of liquid hydrocarbon mixtures, chemical instruments and methods, and hydrocarbon production from carbon oxides, etc. Effect

Active Publication Date: 2021-03-12
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

But in this method, the α-olefin content is low

Method used

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  • Catalyst and its preparation method and application as well as catalyst precursor reduction activation method and preparation method of α-olefin
  • Catalyst and its preparation method and application as well as catalyst precursor reduction activation method and preparation method of α-olefin
  • Catalyst and its preparation method and application as well as catalyst precursor reduction activation method and preparation method of α-olefin

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preparation example Construction

[0067] According to a fourth aspect of the present invention, the present invention provides a method for preparing a catalyst, the method comprising the following steps:

[0068] (1) Roasting the carrier loaded with the oxide of the Group VIII metal element and / or the precursor of the oxide of the Group VIII metal element and the compound containing the auxiliary element to obtain a catalyst precursor;

[0069] (2) Using the method described in the second aspect of the present invention to reductively activate the catalyst precursor.

[0070] The reductive activation method has been described in detail above, and will not be described in detail here, and only step (1) will be described in detail here. In the present invention, the term "precursor of an oxide of a Group VIII metal element" refers to a substance capable of forming a complete oxide of a Group VIII metal element under firing conditions.

[0071] According to the method described in the fourth aspect of the prese...

Embodiment 1

[0130] (1) Preparation of carrier

[0131] Take γ-Al 2 o 3 (Sasol product, its specific surface area, pore volume, average pore diameter and particle size distribution are as shown in table 1) 200g, roasted 2 hours in 980 ℃ of air atmospheres, the roasted product was carried out X-ray diffraction analysis (such as figure 1 shown), it is determined that the θ-Al 2 o 3 , its specific surface area, pore volume, average pore size and particle size distribution are shown in Table 1.

[0132] Dissolve zirconium nitrate pentahydrate in 43g deionized water to make a modified zirconium solution, add 100.0g of prepared θ-Al to the modified zirconium solution 2 o 3 , saturated impregnation at 25°C for 2 hours. Then, the impregnated mixture was placed in an oven, and dried in an air atmosphere at 120° C. and normal pressure (1 standard atmospheric pressure, the same below) for 5 hours. The dried material was calcined in an air atmosphere at 400° C. for 3 hours to obtain a carrier. ...

Embodiment 2

[0142] Adopt the same method as in Example 1 to prepare the catalyst and prepare α-olefins, the difference is that in step (1), γ-Al 2 o 3 Instead of roasting, the modified zirconium solution is directly used for saturation impregnation to prepare a carrier, wherein, based on the total amount of the carrier, the content of Zr is 5% by weight in terms of elements.

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Abstract

Catalyst, preparation method and application, catalyst precursor reduction activation method and α-olefin preparation method. The invention discloses a catalyst and its preparation method and application. The invention also discloses a method for preparing α-olefins by using the above-mentioned catalyst. element and optionally a metal element selected from the group consisting of alkali metal elements, alkaline earth metal elements and Group IVB metal elements, the support is alumina, and the valence state of at least some Group VIII metal elements is lower than the highest oxidation state of the metal element Valence state; CO of the catalyst 2 In the ‑TPD desorption diagram, there are desorption peaks in the temperature range of 300‑600 °C. Using the above catalyst for the Fischer-Tropsch synthesis reaction can improve the selectivity for α-olefins and concentrate the carbon number of the α-olefins, while also obtaining an improved CO conversion rate.

Description

technical field [0001] The present invention relates to the technical field of Fischer-Tropsch synthesis, specifically, the present invention relates to a catalyst, and the present invention also relates to a method for reducing and activating a catalyst precursor, a method for preparing a catalyst, and a catalyst prepared by the above-mentioned method. Relating to the application of the above catalyst as a catalyst for Fischer-Tropsch synthesis reaction, the present invention further relates to a preparation method of α-olefin. Background technique [0002] my country's energy resources are rich in coal, rich in natural gas, and short of oil resources. The indirect conversion of coal or natural gas into clean and efficient liquid fuels through Fischer-Tropsch (F-T) synthesis is an important aspect of rational use of resources and a solution to the contradiction between my country's oil supply and demand. main technical approach. The process first converts coal or natural ga...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/887B01J23/889C10G2/00C07C1/04C07C11/02
CPCB01J23/8872B01J23/8892C07C1/041C07C1/044C07C1/0445C10G2/332C10G2/341C10G2300/1088C10G2300/70C07C11/02
Inventor 晋超吴玉夏国富张荣俊阎振楠李明丰侯朝鹏孙霞
Owner CHINA PETROLEUM & CHEM CORP