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Application of Iron-Based Catalysts in Catalytic Carbon Dioxide Hydrogenation to Synthesize Light Olefins

A technology for catalyzing carbon dioxide and iron-based catalysts, used in catalysts, carbon compound catalysts, and hydrocarbon production from carbon oxides, etc., can solve problems such as low selectivity, and achieve the effects of simple preparation method, improved life, and stable properties

Active Publication Date: 2022-08-02
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] One of the technical problems to be solved by the present invention is to solve the problem of carbon dioxide hydrogenation synthesis of low-carbon olefin catalysts, to provide a new catalyst for carbon dioxide hydrogenation synthesis of low-carbon olefins, the catalyst has a high CO 2 Conversion and high yield of low carbon olefins, and C 5+ less selective

Method used

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  • Application of Iron-Based Catalysts in Catalytic Carbon Dioxide Hydrogenation to Synthesize Light Olefins

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] Weigh 8.11g of FeCl 3 ·6H 2 O and 2.98g FeCl 2 ·4H 2 Dissolve O in 15 ml of deionized water to make Mixture A. Add 100ml of 3mol / L ammonia water (solution B) to the mixture A at a flow rate of 3ml / min using a constant-flow pump, place it in a 40°C water bath and stir continuously, and age for 2h after the addition is complete. The turbid liquid obtained was filtered and washed until neutral, and then the filter cake was dried in air at 80 °C for 12 h; the dried solid was calcined at 400 °C in air for 4 h to obtain solid C.

[0039] Weigh 2.0g of the above solid C and weigh 0.0524g of KNO 3 and 0.0002g FeSO 4 ·7H 2 O Dissolve it in 2 ml of deionized water to make a mixed solution, immerse the above-mentioned solid C sample in the above-mentioned mixed solution, and mix it evenly. Immersion at room temperature for 12h, drying at 60°C for 12h, roasting at 400°C for 4h, and finally grinding, tableting, crushing, and sieving (20-40 mesh) to obtain an iron-based cataly...

Embodiment 2

[0042] Weigh 2.0g of solid C prepared by the method of Example 1, and weigh 0.052g of KNO 3 and 0.002g FeSO 4 ·7H 2 O Dissolve it in 2 ml of deionized water to make a mixed solution, immerse the above-mentioned solid C sample in the above-mentioned mixed solution, and mix it evenly. Immersion at room temperature for 12h, drying at 60°C for 12h, roasting at 400°C for 4h, and finally grinding, tableting, crushing, and sieving (20-40 mesh) to obtain an iron-based catalyst, wherein the mass content of K is 1%, and the mass of S is 1%. The content is 0.01%, recorded as 1K-0.01S / Fe.

[0043] Catalyst reduction and activation conditions: the reducing gas is pure H 2 , purity>99.9%, space velocity 2000h -1 , the heating rate is 5°C / min, the reduction temperature is 400°C, the pressure is normal pressure, and the reduction time is 6h. Reaction conditions: molar ratio H 2 :CO 2 =3, the space velocity is 2000ml / (g cat h), the pressure is 3MPa, and the temperature is 320°C. The re...

Embodiment 3

[0045] Weigh 2.0g of solid C prepared by the method of Example 1, and weigh 0.052g of KNO 3 and 0.0176g FeSO 4 ·7H 2 O Dissolve it in 2 ml of deionized water to make a mixed solution, immerse the above-mentioned solid C sample in the above-mentioned mixed solution, and mix it evenly. Immersion at room temperature for 12h, drying at 60°C for 12h, roasting at 400°C for 4h, and finally grinding, tableting, crushing, and sieving (20-40 mesh) to obtain an iron-based catalyst, wherein the mass content of K is 1%, and the mass of S is 1%. The content is 0.1%, recorded as 1K-0.1S / Fe.

[0046] Catalyst reduction and activation conditions: the reducing gas is pure H 2 , purity>99.9%, space velocity 2000h -1 , the heating rate is 5°C / min, the reduction temperature is 400°C, the pressure is normal pressure, and the reduction time is 6h. Reaction conditions: molar ratio H 2 :CO 2 =3, the space velocity is 2000ml / (g cat h), the pressure is 3MPa, and the temperature is 320°C. The res...

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Abstract

The invention relates to an iron-based catalyst for synthesizing low-carbon olefins by hydrogenation of carbon dioxide, a preparation method and application thereof, and mainly realizes direct conversion of CO2 onto a single catalyst. 2 Hydrogenation is converted to light olefins, and a high selectivity of light olefins is obtained, while methane and C 5+ selectivity is low. The catalyst used in the present invention includes the following components in parts by mass: a) iron oxides, accounting for 50-99.99%; b) selected from oxides of lithium, sodium, potassium, rubidium and cesium Any one or two or more of them, the fraction of which is 0.001-40%; c) one or both of sulfate and sulfide species are selected, and the fraction of which is 0.001-10%. The catalyst provided by the present invention can directly convert CO 2 Converted to light olefins, CO 2 The conversion rate can reach more than 42%, the selectivity of methane is less than 10%, the carbon-based selectivity of light olefins can reach 44.6%, C 5+ The selectivity is only 27.7%.

Description

technical field [0001] The invention relates to an iron-based catalyst for synthesizing low-carbon olefins by hydrogenation of carbon dioxide, and a preparation method and application thereof. Background technique [0002] In recent years, a large amount of CO 2 The environmental problems caused by the emissions of the CO 2 Not only a greenhouse gas, but also one of the most abundant carbon resources. Utilize CO 2 As a carbon source, a variety of high value-added chemicals and fuels can be synthesized. Low-carbon olefins are one of the most basic raw materials in the chemical industry. At present, the raw materials for the production of low-carbon olefins are mainly derived from petroleum resources. Hydrogen and CO produced by the use of renewable energy such as wind energy, solar energy and surplus nuclear energy to electrolyze water 2 Reaction synthesis of light olefins, not only can achieve CO 2 It also provides a production route that does not rely on petroleum re...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C1/12C07C11/06C07C11/04C07C11/08B01J27/043
CPCC07C1/12B01J27/043C07C2527/043C07C11/06C07C11/04C07C11/08Y02P20/52
Inventor 黄延强梁兵连段洪敏张涛
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI