Fischer-Tropsch synthesis iron-based catalyst and preparation method thereof

An iron-based catalyst, Fischer-Tropsch synthesis technology, applied in chemical instruments and methods, physical/chemical process catalysts, chemical elements of heterogeneous catalysts, etc. High Fischer-Tropsch reactivity and other problems, to achieve the effects of excellent selectivity, reduced methane selectivity, and easy control of components

Active Publication Date: 2017-12-12
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, CN101920199 A uses modified silica gel as a carrier to prepare a Fischer-Tropsch cobalt-based catalyst. The preparation method of the catalyst is to use silica gel as a carrier, first use a boron-containing alkaline solution to modify the silica gel carrier, and then use the impregnation method to load the second cobalt. agent and active component Co, the cobalt-based Fischer-Tropsch synthesis catalyst has high Fischer-Tropsch reaction activity, and the carbon number of the product is distributed in C 1 -C 30 between, with C 13 -C 30 The advantage of high selectivity betwe

Method used

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  • Fischer-Tropsch synthesis iron-based catalyst and preparation method thereof
  • Fischer-Tropsch synthesis iron-based catalyst and preparation method thereof
  • Fischer-Tropsch synthesis iron-based catalyst and preparation method thereof

Examples

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Example Embodiment

[0058] Example 1

[0059] (1) Preparation of silica sol pretreated by the precursor of the carrier modifier Ca

[0060] Add 10g of Ca(NO 3 ) 2 ·4H 2 O is dissolved in 50g deionized water, fully dissolved; take SiO 2 12g of alkaline silica sol with a content of 30.5% by weight; at room temperature, the dissolved Ca(NO 3 ) 2 The solution was slowly added dropwise to the continuously vigorously stirred silica sol, and the solution was added within 10 minutes; after continuous stirring and mixing for 30 minutes, ammonia water with a concentration of 5% by weight was slowly added dropwise to the vigorously stirred silica sol until the pH of the system The value is 11, and stirring is continued for 30 minutes to obtain a silica sol pretreated with the precursor of the carrier modifier Ca.

[0061] (2) Preparation of Fe-Tropsch synthesis iron-based catalyst

[0062] Fe(NO 3 ) 3 ·9H 2 O solid 303g and 30g 50wt% Mn(NO 3 ) 2 Add the solution to 750ml deionized water to fully dissolve; place the...

Example Embodiment

[0063] Example 2

[0064] (1) Preparation of silica sol pretreated by the precursor of the carrier modifier Mg

[0065] Add 11g of Mg(NO 3 ) 2 ·6H 2 O is dissolved in 50g deionized water, fully dissolved; take SiO 2 12g of alkaline silica sol with a content of 30.5% by weight; at room temperature, the dissolved Mg(NO 3 ) 2 The solution was slowly added dropwise to the continuously vigorously stirred silica sol, and the solution was added within 10 minutes; after continuous stirring and mixing for 30 minutes, ammonia water with a concentration of 5% by weight was slowly added dropwise to the vigorously stirred silica sol until the pH of the system The value is 11, and stirring is continued for 30 minutes to obtain a silica sol pretreated with a precursor of the carrier modifier Mg.

[0066] (2) Preparation of Fe-Tropsch synthesis iron-based catalyst

[0067] The process of step (2) of Example 1 was repeated to prepare a catalyst, and the obtained catalyst was named Catalyst 2.

Example Embodiment

[0068] Example 3

[0069] (1) Preparation of silica sol pretreated by the precursor of the carrier modifier Zn

[0070] 13g of Zn(NO 3 ) 2 ·6H 2 O is dissolved in 50g deionized water, fully dissolved; take SiO 2 12g alkaline silica sol with a content of 30.5% by weight; at room temperature, the dissolved Zn(NO 3 ) 2 The solution was slowly added dropwise to the continuously vigorously stirred silica sol, and the dripping of the solution was completed within 10 minutes; after continuous stirring and mixing for 30 minutes, 5 wt% ammonia water was slowly added dropwise to the vigorously stirred silica sol until the pH value of the system The value is 11, and the stirring is continued for 30 minutes to obtain a silica sol pretreated with a precursor of the carrier modifier Zn.

[0071] (2) Preparation of Fe-Tropsch synthesis iron-based catalyst

[0072] The process of step (2) of Example 1 was repeated to prepare a catalyst, and the obtained catalyst was named Catalyst 3.

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Abstract

The invention relates to the field of Fischer-Tropsch synthesis, and discloses a Fischer-Tropsch synthesis iron-based catalyst and a preparation method thereof. The catalyst contains a catalytic active component Fe, catalytic aids Mn, Cu, K and Na, a carrier modifying agent M and a carrier SiO2 which match with each other according to a certain ratio, wherein M is at least one of Group IIA, Group IIB and Group IIIA metal elements. The method for preparing the Fischer-Tropsch synthesis iron-based catalyst comprises the following steps: performing a coprecipitation reaction on iron and manganese precursors; performing solid-liquid separation on the coprecipitation reaction product; pulping the obtained solid product; performing mixing with a mixture of copper, potassium and sodium precursors; mixing the obtained mixture with silica sol pretreated by an M precursor; and sequentially performing drying and roasting. The invention also discloses the catalyst prepared by the above method. According to the preparation method, the Fischer-Tropsch synthesis iron-based catalyst having excellent low-carbon olefin selectivity, lower methane selectivity and higher catalytic reaction activity can be obtained.

Description

technical field [0001] The invention relates to the field of Fischer-Tropsch synthesis, in particular to an iron-based catalyst particularly suitable for Fischer-Tropsch synthesis and a preparation method thereof. Background technique [0002] Fischer-Tropsch synthesis is an important way to convert coal and natural gas into liquid fuels or high value-added chemical products. Low-carbon olefins, such as ethylene, propylene, and butene, are important chemical raw materials. At present, they mainly come from the steam cracking process of hydrocarbons such as naphtha or low-molecular hydrocarbons. With the increasing depletion of petroleum resources and With the rise of oil prices, new ways of synthesizing low-carbon olefins from coal have attracted increasing attention. In addition, from a technical and economic point of view, the direct production of low-carbon olefins by Fischer-Tropsch synthesis has broad prospects. At present, the technical development of direct productio...

Claims

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Application Information

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IPC IPC(8): B01J23/889B01J35/10
CPCB01J23/002B01J23/8892B01J35/1014B01J35/1038B01J2523/00B01J2523/842B01J2523/72B01J2523/17B01J2523/13B01J2523/12B01J2523/41B01J2523/23B01J2523/22B01J2523/31B01J2523/27
Inventor 张魁吕毅军胡云剑王鹏程萌武鹏
Owner CHNA ENERGY INVESTMENT CORP LTD
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