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Spinel oxide catalyst for coal-fired 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. , Unsatisfactory purification effect and other problems, achieve significant redox performance and thermal stability, improve service life, load and load position are precisely controllable

Active Publication Date: 2019-04-05
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 for coal-fired flue gas purification. The catalyst is of a layered structure and consists of a carrier, an intermediate component and a kernel componentin sequence from outside to inside, wherein the kernel component is a metal oxide of a spinel structure. The invention further discloses a preparation method of the catalyst. Active components of thecatalyst disclosed by the invention show a multilayer distribution inside the carrier; layered reactions of different pollutants on the surface of the catalyst and in a bulk phase are realized by using different migration and diffusion rules of various exhaust gas ingredients in the various layers of active components of the catalyst and the carrier structure, so that the problem of efficient cooperative control of various pollutants in a complex system of coal-fired flue gas with coexisting pollutants such as NOx, Hg0 abd PAHs is solved.

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 Applications(China)
IPC IPC(8): B01J23/755B01J23/78B01J23/86B01J23/889B01J35/10F23G7/07
CPCF23G7/07B01J23/755B01J23/78B01J23/864B01J23/8892B01J35/612B01J35/613B01J35/647
Inventor 竺新波
Owner NINGBO UNIV