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Sulfate radical modified iridium-based methane combustion catalyst as well as preparation and application thereof

A combustion catalyst, iridium-based methane technology, applied in the direction of physical/chemical process catalysts, combustion methods, combustion types, etc., can solve the problems of unexamined catalyst water resistance, poor activity, and reduced catalytic activity, so that the synthesis process is simple and feasible control, good water resistance, good reproducibility

Pending Publication Date: 2021-07-16
FUZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

CN110075831A Ir / TiO is synthesized by loading Ir with equal volume impregnation method with titanium dioxide as carrier 2 Catalyst, under the condition of lower space velocity (30000mL∙h -1 ∙g cat -1 ) has high low-temperature activity, but the water resistance of the catalyst was not investigated
CN111686723A is active component with bimetallic containing iridium, and titanium dioxide or zirconium dioxide is carrier, wherein zirconium dioxide supports bimetallic containing iridium and shows poor activity (Ir-Pt / ZrO 2 the T 99 575 ℃), and Ir-Pt / TiO 2 Insufficient water resistance (adding 10% water vapor, the catalytic activity is reduced by 35%)

Method used

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  • Sulfate radical modified iridium-based methane combustion catalyst as well as preparation and application thereof
  • Sulfate radical modified iridium-based methane combustion catalyst as well as preparation and application thereof
  • Sulfate radical modified iridium-based methane combustion catalyst as well as preparation and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Weigh ZrOCl 2 ∙8H 2 O and (NH 4 ) 2 SO 4 (10:1 by molar ratio) was dissolved in 140 mL deionized water and stirred for 20 min to obtain a mixed solution. Transfer the mixed solution into a hydrothermal reaction kettle with a volume of 200 mL, place it in a forced air drying oven, raise the temperature to 100 °C at a rate of 5 °C / min and keep it for 12 h, and then increase the temperature to 100 °C at a rate of 5 °C / min. Incubate at 200°C for 12 h. After the hydrothermal kettle was naturally cooled to room temperature, the hydrothermal product was washed with deionized water until no Cl was detected. - . Then put the obtained precipitate in an oven, set the temperature at 60°C for 20 hours, after the drying is completed, transfer it to a crucible in a muffle furnace, heat up to 800°C at a rate of 120°C / h and roast for 5 hours, and naturally cool down to obtain ZrO 2 carrier. ZrO 2 The carrier was ground to powder, and 2.0 g powdered ZrO was weighed 2 Carrier, ...

Embodiment 2

[0026] Take ZrO(NO 3 ) 2 and (NH 4 ) 2 SO 4 (The molar ratio is 6:1) was dissolved in 140 mL deionized water, stirred for 20 min to obtain a mixed solution. Transfer the mixed solution into a hydrothermal reaction kettle with a volume of 200 mL, place it in a forced air drying oven, raise the temperature to 100 °C at a rate of 5 °C / min and keep it for 10 h, and then increase the temperature to 100 °C at a rate of 5 °C / min. Incubate at 200°C for 20 h. After the hydrothermal kettle was naturally cooled to room temperature, the hydrothermal product was transferred to a centrifuge cup, and the hydrothermal product was washed with deionized water until no Cl was detected. - . Then put the obtained precipitate in an oven, set the temperature at 60°C for 20 hours, after the drying is completed, transfer it to a crucible in a muffle furnace, heat up to 800°C at a rate of 60°C / h and bake for 6 hours, then cool down naturally get ZrO 2 carrier. ZrO 2 Carrier ground to powder, ...

Embodiment 3

[0028] Take Zr(NO 3 ) 4 and (NH 4 ) 2 SO 4(4:1 by molar ratio) was dissolved in 140 mL deionized water, stirred for 20 min to obtain a mixed solution. Transfer the mixed solution into a hydrothermal reaction kettle with a volume of 200 mL, place it in a forced air drying oven, raise the temperature to 100 °C at a rate of 5 °C / min and keep it for 20 h, and then increase the temperature to 100 °C at a rate of 5 °C / min. Incubate at 200°C for 15 h. After the hydrothermal kettle was naturally cooled to room temperature, the hydrothermal product was transferred to a centrifuge cup, and the hydrothermal product was washed with deionized water until no Cl was detected. - . Then put the obtained precipitate in an oven, set the temperature at 60°C for 20 h, after the drying is completed, transfer it to a crucible in a muffle furnace, heat up to 800°C at a rate of 180°C / h and bake for 4 h, then cool down naturally get ZrO 2 carrier. ZrO 2 Carrier ground to powder, weigh 2.0g po...

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PUM

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Abstract

The invention discloses a sulfate radical modified iridium-based methane combustion catalyst as well as a preparation method and application thereof, and belongs to the field of energy and environment catalysis. The catalyst comprises an active component and a carrier, the active component is mainly an iridium oxide, and the carrier is sulfate radical modified zirconium dioxide. The sulfate radical modified zirconium dioxide is obtained through a hydrothermal method and heat treatment and serves as the carrier, active components are loaded through an impregnation method, and the sulfate radical modified iridium-based methane combustion catalyst is obtained through drying and high-temperature activation treatment. The catalyst has relatively high methane combustion activity under the conditions of low-concentration methane (0.1-2%) and normal pressure and low temperature (300-400 DEG C), also has good water resistance and excellent hydrothermal stability, and can be suitable for low-concentration methane treatment systems of coal seam tail gas or oil field associated tail gas and the like.

Description

technical field [0001] The invention belongs to the field of energy and environmental catalysis, and in particular relates to a sulfate-modified iridium-based methane combustion catalyst and a preparation method and application thereof. Background technique [0002] During the mining of coal mines and oil fields, there will be a large amount of coalbed methane and oilfield associated gas. Due to technical constraints, a large part of oilfield associated gas (or coalbed methane) containing low-concentration methane is evacuated. The greenhouse effect of methane is 25 times that of carbon dioxide. The direct discharge of a large amount of coal seam tail gas and associated tail gas from oil fields not only wastes energy but also imposes a burden on the environment. Due to the low concentration of methane, it cannot be directly recycled, and the traditional methane combustion temperature is usually above 1400 ° C, so that the nitrogen in the air participates in the reaction at h...

Claims

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Application Information

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IPC IPC(8): B01J27/055F23G7/07
CPCB01J27/055F23G7/07
Inventor 詹瑛瑛康亮陈崇启蔡国辉江莉龙
Owner FUZHOU UNIV