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Preparation method and application of a nickel-based multimetal catalyst for carbon dioxide methanation

A multi-metal catalyst, carbon dioxide technology, applied in metal/metal oxide/metal hydroxide catalyst, catalyst activation/preparation, physical/chemical process catalyst, etc., can solve the problems of poor stability, easy coking, low activity, etc. Achieve the effect of high reaction stability, good reactivity and high methane selectivity

Inactive Publication Date: 2021-07-27
FUZHOU UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] The purpose of the present invention is to provide a preparation method and application of a nickel-based multimetal catalyst for carbon dioxide methanation, which is used to improve the problems of low activity, poor stability and easy coking of catalysts currently using Ni as the main active component at low temperatures

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  • Preparation method and application of a nickel-based multimetal catalyst for carbon dioxide methanation
  • Preparation method and application of a nickel-based multimetal catalyst for carbon dioxide methanation
  • Preparation method and application of a nickel-based multimetal catalyst for carbon dioxide methanation

Examples

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Embodiment 1

[0033] A nickel-based multimetal catalyst for carbon dioxide methanation (TiO 2 -Ni-Co-Fe) preparation method: weigh 5g of TiO 2 Roast in a muffle furnace at 500°C for 2h, the heating rate is 2°C / min, take 0.5g of the calcined TiO 2 The sample powder was dispersed in 150ml of deionized water, stirred at a speed of 500r / min for 20min, and then ultrasonicated at a power of 60kHz for 60min. To the dispersed solution, sequentially add Ni(NO 3 ) 2 1ml of aqueous solution, Co(NO 3 ) 2 0.5ml aqueous solution, Fe element content 50mg / ml Fe(NO 3 ) 3 Aqueous solution 0.05ml. After the solution was fully mixed, it was soaked for 0.5 h, and then a NaOH aqueous solution with a concentration of 0.2 mol / L was added dropwise to the solution under stirring conditions to adjust the pH to 10. The precipitate was collected after 3 hours and dried at 60°C. After the dried sample is ground, take 0.2g sample and put it into the fixed bed reactor, and use H 2 For reduction, the temperature ...

Embodiment 2

[0036] A nickel-based multimetal catalyst for carbon dioxide methanation (TiO 2 -Ni-Co-Fe) preparation method: weigh 5g of TiO 2 Roast in a muffle furnace at 500°C for 2h, the heating rate is 2°C / min, take 0.5g of the calcined TiO 2 The sample powder was dispersed in 150ml of deionized water, stirred at a speed of 500r / min for 30min, and then ultrasonicated at a power of 60kHz for 30min and twice. To the dispersed solution, sequentially add Ni(NO 3 ) 2 1.2ml aqueous solution, Co(NO 3 ) 2 1ml of aqueous solution, Fe(NO 3 ) 3 Aqueous solution 0.05ml. After the solution was fully mixed, it was soaked for 1 h, and then NaOH aqueous solution was added dropwise to the solution under stirring condition, and its concentration was 0.2 mol / L to adjust the pH to 7. After 3 hours of precipitation, it was collected and dried at 60°C. After the dried sample is ground, take 0.2g sample and put it into the fixed bed reactor, and use H 2 For reduction, the temperature is controlled a...

Embodiment 3

[0039] A nickel-based multimetal catalyst for carbon dioxide methanation (TiO 2 -Ni-Co-Fe) preparation method: the dried sample powder in Example 2, take 0.2g sample into the fixed bed reactor, use H 2 For reduction, the temperature is controlled at 350°C, the heating rate is 5°C / min, and the reaction space velocity is 7500ml·gcat -1 h -1 . After the reduction is completed, the reaction raw material gas (for CO 2 、H 2 , Ar mixed gas, the volume proportions are 3%, 12%, and 85% respectively), the reaction temperature is 190°C, the heating rate is 2°C / min, and the reaction space velocity is 3000ml·gcat -1 h -1 .

[0040] For the activity evaluation of the catalyst prepared in this example, see Figure 4 Shown in Example 3, methane selectivity in its product > 99%.

[0041] The XRD spectrum of the catalyst sample prepared in this embodiment is shown in figure 1 . It can be seen from the figure that the carrier titanium dioxide and the active component peaks are clearly ...

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Abstract

The invention discloses a preparation method and application of a nickel-based multimetal catalyst for carbon dioxide methanation. The catalyst uses TiO 2 It is the carrier component, Ni, Co, Fe three metals and their oxides are the active components. The catalyst adopts impregnation-co-precipitation synthesis method, and then is dried and reduced to obtain the catalyst. The catalyst is used in an amount of 0.2g, the pressure is a normal atmospheric pressure, the reaction temperature is 150~300°C, and the reaction raw material gas is 3%, 12%, and 85% CO by volume. 2 、H 2 , Ar mixed gas, the reaction uses an intermittent reaction device, the reaction volume is 200~300ml, and the reaction space velocity is 3000ml·gcat ‑1 h ‑1 Catalytic carbon dioxide methanation reaction under certain conditions. The catalyst of the invention has the characteristics of low reaction temperature, good reaction effect, methane selectivity >99%, and small activity attenuation.

Description

technical field [0001] The invention belongs to the technical field of catalysts, and in particular relates to a preparation method and application of a nickel-based multimetal catalyst for carbon dioxide methanation. Background technique [0002] Due to human activities such as the massive burning of bio-fossil fuels, our climate is undergoing drastic changes, atmospheric CO 2 The rising concentration has exceeded the capacity of global oceans and forests to absorb, how to reduce its concentration has become a worldwide research topic. Many researchers regard the conversion and reuse of carbon dioxide as an effective way to solve this problem. Carbon dioxide methanation reaction is an effective way of transformation. [0003] CO 2 (g)+4H 2 (g)→CH 4 (g)+2H 2 O(g)△H Ɵ 298K = -165kJ / mol, △G Ɵ 298K = -113kJ / mol [0004] From a thermodynamic point of view, CO 2 The methanation reaction is restricted by thermodynamic equilibrium, which is not conducive to the forward ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J37/03B01J37/02B01J37/16B01J37/34C07C1/12C07C9/04
Inventor 丁正新李佳伟苏波熊壮龙金林
Owner FUZHOU UNIV