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Catalyst for low-molecular straight-chain paraffin isomerization in Fischer-Tropsch synthesis

A technology of straight-chain alkanes and Fischer-Tropsch synthesis, which is applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, catalyst activation/preparation, etc., and can solve the problem of small specific surface area and adsorption of pure zirconia Increased capacity and surface acidity, weak surface acidity, etc.

Active Publication Date: 2019-04-16
CHINA UNIV OF PETROLEUM (EAST CHINA)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, pure zirconia has disadvantages such as small specific surface area and weak surface acidity, and is not suitable for industrial production. Some researchers choose to dope metal atoms containing p or d orbitals in zirconia (such as Ti, Ce, Al, Si etc.), the introduction of different metal atoms will cause different changes to the properties of ZrO2, such as the introduction of metal atoms Ti will increase the specific surface area of ​​the composite oxide carrier, thereby improving the catalytic activity of the catalyst; the introduction of rare earth metal atoms such as Ce will improve The thermal stability and oxygen storage capacity of the support; the introduction of metal atoms containing acidic sites such as Al will increase the adsorption capacity and surface acidity of the composite oxide support

Method used

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  • Catalyst for low-molecular straight-chain paraffin isomerization in Fischer-Tropsch synthesis

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0013] (1) The calculated amount of Al(NO 3 ) 3 9H 2 O, zirconium salt (zirconium-aluminum ratio 1:1), lanthanum salt is dissolved in deionized water, (the concentration of zirconium 0.4mol / L, the content of lanthanum 2wt%) drips ammonia water under vigorous stirring and adjusts pH value to be 10;

[0014] (2) Put the mixture into a hydrothermal kettle at 180°C for 24 hours of hydrothermal reaction, wash with water until there is no Cl- and it is neutral;

[0015] (3) Dry the filter cake obtained by washing at 120°C to obtain tetragonal Al 2 o 3 -ZrO 2 carrier.

[0016] (4) Dissolve the zirconium-based composite oxide carrier prepared in step (3) in an aqueous solution of ammonium metatungstate, stir for 6 hours, age for 24 hours, air-dry at 80°C, and roast at 800°C for 4 hours to obtain a W mass fraction of 15%. WO 3 / Al 2 o 3 -ZrO 2 powder;

[0017] (5) WO obtained in step (4) 3 / Al 2 o 3 -ZrO 2 The powder was dispersed in an aqueous solution of nickel nitrate...

Embodiment 2

[0019] The operation steps are the same as in Example 1, except that in step (5), the WO obtained in step (4) is modified. 3 / Al 2 o 3 -ZrO 2 The powder was dispersed in an aqueous solution of nickel nitrate, stirred for 6 hours, aged for 24 hours, air-dried at 80°C and calcined at 500°C for 4 hours to obtain Ni-WO with a mass fraction of Ni of 4%. 3 / Al 2 o 3 -ZrO 2 Catalyst, named Catalyst B. Catalyst performance and product octane number are shown in Table 1;

Embodiment 3

[0021] The operation steps are the same as in Example 1, except that in step (5), the WO obtained in step (4) is modified. 3 / Al 2 o 3 -ZrO 2 The powder was dispersed in an aqueous solution of nickel nitrate, stirred for 6 hours, aged for 24 hours, air-dried at 80°C and calcined at 500°C for 4 hours to obtain Ni-WO with a mass fraction of Ni of 6%. 3 / Al 2 o 3 -ZrO 2 Catalyst, named Catalyst C. Catalyst performance and product octane number are shown in Table 1;

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Abstract

The invention discloses a catalyst for low-molecular straight-chain paraffin (nC5-nC8) isomerization in Fischer-Tropsch synthesis and a preparation method and application thereof for solving the problems of low activity, poor stability and low conversion rate of an existing catalyst for low-molecular straight-chain paraffin isomerization in Fischer-Tropsch synthesis. In the preparation method, anAl2O3-ZrO2 composite oxide carrier is prepared with a coprecipitation method, a lanthanum salt is added to increase the proportion of the zirconia tetragonal phase and regulate the Al2O3 content to maintain the acidity of the catalyst, then a Ni-WO3 / Al2O3-ZrO2 catalyst is prepared with an equivalent-volume impregnation method, and thus the catalyst for low-molecular straight-chain paraffin isomerization in Fischer-Tropsch synthesis is obtained, wherein Al2O3-ZrO2 serves as the carrier of the catalyst, and the active metal components of the catalyst include 1-5 wt% of Ni, 10-15 wt% of W and 0.5-2.5 wt% of La. The catalyst has high isomerization activity and selectivity, and good repeatability and catalytic stability; besides, the reaction temperature is low, and the isomerization activity of low-molecular straight-chain paraffin can be maintained at a high temperature.

Description

technical field [0001] The invention belongs to the technical field of catalyst preparation, and in particular relates to a catalyst for Fischer-Tropsch synthesis of low-molecular linear alkane isomerization, a preparation method and an application thereof. Background technique [0002] As the requirements for environmental protection are getting higher and higher, the sulfur content can be reduced to less than 10 μg / g and the olefin content can be reduced to less than 24v% by hydrodesulfurization and olefin reduction of gasoline. Although the content of olefins and aromatics in gasoline is gradually reduced, its octane number is also greatly reduced. To reduce sulfur and olefins with little or no loss of octane, selective hydrocracking or isomerization is required. Hydroisomerization is particularly important for increasing the octane number of gasoline. The RON of isoparaffins is much higher than that of normal paraffins with the same carbon number. For example, nC 6 T...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/888B01J37/02B01J37/03C10G45/60
CPCC10G45/60B01J23/002B01J23/888B01J37/0201B01J37/0207B01J37/031
Inventor 刘东门卓武师楠吕毅军黄恪朱超张亚东
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)
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