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Spinel oxide catalyst for combustion flue gas purification and preparation method thereof

A spinel oxide and combustion flue gas technology, applied in metal/metal oxide/metal hydroxide catalysts, combustion methods, physical/chemical process catalysts, etc. , wide range of changes, etc., to achieve significant oxidation-reduction performance and thermal stability, and to improve the service life

Active Publication Date: 2021-10-22
NINGBO UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, there are many unsolvable problems in the existing catalytic process: First, there are many kinds of pollutants in the flue gas produced by coal combustion, and the existing catalytic methods are not effective for removing NO x other pollutants, such as CO, PAHs and various heavy metals (such as Hg, As, Pb), etc., the purification effect of various pollutants is not ideal; The range of change is large, which significantly affects the catalyst activity and reaction effect, and it is difficult to ensure the stable discharge of pollutants. Third, there are a large amount of sulfur oxides and alkali metals in the flue gas emitted by coal combustion, which can easily cause catalyst poisoning and deactivation
Researchers at home and abroad have studied the above-mentioned single problem and formed a catalyst formula that can solve the aforementioned single problem based on laboratory research. However, there is no catalyst formula and preparation method that can synergistically solve all the above-mentioned problems in the existing work.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Preparation of SiO by hydrothermal method 2 The protective layer is prepared to have a high specific surface area and expose a highly active crystal plane. 0.15 mol tetrabutyl titanate was dissolved in 0.4 L hydroxypropyl cellulose ethanol solution to obtain a carrier precursor solution. 0.3 mol of zinc nitrate, 0.6 mol of cobalt nitrate and 0.9 mol of citric acid were dissolved in 1L of deionized water at room temperature to obtain a precursor solution for the active core layer. In this embodiment, zinc nitrate and cobalt nitrate, which are relatively cheap and easy to decompose, are used as raw materials for making the active core layer, so that the production cost of the catalyst is relatively low.

[0029] Dissolve 0.1mol of protective layer powder into the precursor solution of the active core layer, add 0.01mol of ethylenediaminetetraacetic acid and 0.01mol of dibutyltin dilaurate, transfer the solution to a hydrothermal kettle, heat to 80°C, and react for 2h to ...

Embodiment 2

[0034] Preparation of SiO by hydrothermal method 2 The protective layer. 0.4 mol tetrabutyl titanate was dissolved in 0.5 L hydroxypropyl cellulose ethanol solution to obtain a carrier precursor solution. 1 mol of nickel sulfate, 3 mol of cobalt sulfate and 5 mol of citric acid were dissolved in 3L of deionized water at room temperature to obtain a precursor solution for the active core layer.

[0035] Dissolve 0.2 mol of protective layer powder into the precursor solution of the active core layer, add 0.01 mol of ethylene dimercaptopropanol and 0.02 mol of dicumyl peroxide, transfer the solution to a hydrothermal kettle, heat to 60°C, and react for 8 hours to obtain First composite colloid.

[0036] The first composite colloid was dissolved in the precursor solution of the carrier, the solution was transferred to a hydrothermal kettle, heated to 90° C., and reacted for 1 hour to obtain the second composite colloid.

[0037] Coating a layer of nano-SiO on the surface of the...

Embodiment 3

[0040] Preparation of SiO by hydrothermal method 2 The protective layer. 0.6 mol of tetrabutyl titanate was dissolved in 1 L of hydroxypropyl cellulose ethanol solution to obtain a carrier precursor solution. 0.9 mol copper chloride, 2.25 mol cobalt chloride and 3.15 mol citric acid were dissolved in 2.5 L deionized water at room temperature to obtain a precursor solution for the active inner core layer.

[0041] Dissolve 0.3mol of protective layer powder into the precursor solution of the active core layer, add 0.03mol of sodium dimercaptopropanesulfonate and 0.05mol of di-tert-butyl peroxide, transfer the solution to a hydrothermal kettle, heat to 95°C, and react 4h, the first composite colloid was obtained.

[0042] The first composite colloid was dissolved in the precursor solution of the carrier, the solution was transferred to a hydrothermal kettle, heated to 65° C., and reacted for 8 hours to obtain the second composite colloid.

[0043] Coating a layer of nano-SiO o...

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Abstract

The invention discloses a spinel oxide catalyst used for the purification of coal-burning flue gas. The catalyst has a layered structure, and from the outside to the inside is a carrier, an intermediate component and an inner core component. The inner core component is The metal oxide with a spinel structure also discloses a preparation method of the catalyst. The active component of the catalyst of the present invention presents a multi-level distribution inside the carrier, and the different migration and diffusion laws of each flue gas component in each active component layer of the catalyst and the carrier structure are used to realize the separation of different pollutants on the surface of the catalyst and in the bulk phase. The layered reaction solves the problem of efficient and coordinated control of multiple pollutants in a complex system where coal-fired flue gas, such as NOx, Hg0 and PAHs, coexists.

Description

technical field [0001] The invention relates to the field of combustion flue gas purification materials, in particular to a spinel oxide catalyst used for combustion flue gas purification and a preparation method thereof. Background technique [0002] According to the International Energy Outlook, global coal consumption will continue to grow slowly at a rate of 0.6% per year (until 2030). my country is a big energy consumer. Under the national conditions of "rich in coal, poor in oil, and low in gas", the primary energy consumption structure is bound to continue to be dominated by coal. Coal-fired flue gas emissions cause air pollution problems. In order to improve the ambient air quality and solve the pollution emission problem of coal-fired power plants, my country has successively promulgated the new version of "Emission Standards of Air Pollutants for Thermal Power Plants" and "Action Plan for Upgrading and Transformation of Coal Power Energy Conservation and Emission ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J23/78B01J23/86B01J23/889B01J35/10F23G7/07
CPCB01J23/755B01J23/78B01J23/864B01J23/8892B01J35/1009B01J35/1014B01J35/1061F23G7/07
Inventor 竺新波
Owner NINGBO UNIV