Catalyst, preparation method and application as well as reducing activation method of catalyst precursor and preparation method of low carbon olefin

A catalyst and precursor technology, applied in catalyst activation/preparation, preparation of liquid hydrocarbon mixture, hydrocarbon production from carbon oxides, etc., can solve problems such as unfavorable production efficiency, low reaction space velocity, and low selectivity of low-carbon olefins , to achieve high activity stability, high selectivity and high CO conversion

Active Publication Date: 2018-11-02
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When the catalyst is used in a fixed-bed reactor, although a higher conversion rate of CO can be obtained in the reaction of syngas to light olefins, the selectivity of light olefins is still low, and the reaction space velocity is low, which is not conducive to Increase productivity

Method used

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  • Catalyst, preparation method and application as well as reducing activation method of catalyst precursor and preparation method of low carbon olefin
  • Catalyst, preparation method and application as well as reducing activation method of catalyst precursor and preparation method of low carbon olefin
  • Catalyst, preparation method and application as well as reducing activation method of catalyst precursor and preparation method of low carbon olefin

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preparation example Construction

[0069] 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:

[0070] (1) loading the oxide of the Group VIII metal element and / or the precursor of the oxide of the Group VIII metal element on the carrier, and calcining the carrier loaded with the oxide and / or the precursor, obtaining a catalyst precursor;

[0071] (2) Using the method described in the second aspect of the present invention to reductively activate the catalyst precursor.

[0072] 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.

[0073] According to the method described in the fourth aspect ...

Embodiment 1

[0129] (1) Preparation of carrier

[0130] 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.

[0131] 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

[0141] Adopt the same method as Example 1 to prepare the catalyst and prepare low-carbon olefins, the difference is that in step (1), γ-Al 2 o 3 The carrier was prepared by directly impregnating it with the modified zirconium solution without calcination, wherein, based on the total amount of the carrier, the content of Zr was 3% by weight in terms of elements.

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Abstract

The invention discloses a catalyst, a preparation method and application as well as a reducing activation method of a catalyst precursor and a preparation method of low carbon olefin. The invention discloses the catalyst, the preparation method and the application of the catalyst as well as a method for preparing the low carbon olefin by adopting the catalyst. The catalyst contains a carrier and VIII family elements loaded on the carrier; the carrier is aluminum oxide; the valence state of at least partial VIII family metal elements is lower than the highest oxidation state of the metal elements; in a CO2-TPD desorption drawing of the catalyst, a CO2 high-temperature desorption peak exists in a temperature ranging from 300 to 600 DEG C. The catalyst disclosed by the invention can obtain higher CO2 conversion rate even if Fischer-Tropsch synthesis reaction is performed in a high-airspeed fluidized bed reactor under mild reaction conditions; the selectivity of the low carbon olefin can be obviously improved and higher activity stability also can be obtained.

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 method for preparing low-carbon olefins. Background technique [0002] Olefin is an important basic chemical raw material in the production of chemical industry, and it is also a symbol to measure the development level of a country's petrochemical industry. From 1995 to 2010, the world's ethylene demand grew at an average annual rate of 4.1%. At the same time, the world's propylene demand also increased rapidly, with an average annual growth rate of 6.3% from 2000 to 2010. [0003...

Claims

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Application Information

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IPC IPC(8): B01J23/83B01J23/745B01J37/18C10G2/00C07C1/04C07C11/02
CPCB01J23/745B01J23/83B01J37/18C07C1/0435C07C1/044C07C1/0445C10G2/332C10G2/344C10G2300/70C10G2300/703C07C11/02
Inventor晋超吴玉张荣俊夏国富阎振楠侯朝鹏孙霞李明丰
OwnerCHINA PETROLEUM & CHEM CORP