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Metal modified foamed ceramic ozone catalyst and preparation method thereof

A technology of foam ceramics and metal modification, which is applied in the direction of metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, physical/chemical process catalysts, etc. Catalyst activity and stability, transfer performance and other issues are greatly affected, to achieve the effect of mass transfer, light weight and good mechanical properties

Inactive Publication Date: 2021-11-02
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

At present, heterogeneous ozone oxidation catalysts mainly support transition metals Fe, Cu, Ni, Mn, Ce and their oxides on the carrier, but the combination between the active component and the carrier is not firm, the dispersion is low, and it is easy to dissolve. Severely limits catalyst activity and stability
In a traditional fixed-bed reactor, the reactor bed is composed of randomly packed regular particles or special-shaped particle catalysts. The reactant flow passes through the bed in a flow and permeation manner and undergoes a chemical reaction. There is a large pressure drop in the application, flow The resistance is large, and the transfer performance is greatly affected by the bed height

Method used

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  • Metal modified foamed ceramic ozone catalyst and preparation method thereof
  • Metal modified foamed ceramic ozone catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] (1) Soak alumina foam ceramics with a diameter of 45 mm and a thickness of 15 mm in 0.1 mol / L sodium hydroxide and 0.1 mol / L hydrochloric acid for 12 hours to remove surface oil and impurities, and rinse repeatedly with deionized water until neutral , place it in a blast drying oven to dry at 120°C, then raise the temperature to 500°C at a rate of 5°C / min, keep it warm for 4 hours, and let it cool down to room temperature naturally for use.

[0040](2) Immerse the washed, roasted and cooled alumina foam carrier in the aluminum sol, pull it out at a constant speed, and blow off excess liquid. Then dry at 120°C for 3h, bake at 550°C for 4h and cool down. The above process is repeated three times to increase the thickness of the coating.

[0041] (3) Immerse the alumina foam ceramics coated with the transition layer in 0.3mol / L cerium nitrate solution for 6h, put the alumina foam ceramic carrier adsorbed with cerium nitrate into a drying oven and dry at 120°C for 8h. The...

Embodiment 2

[0043] In step (3), the alumina foam ceramics coated with the transition layer was immersed in 0.3 mol / L ferric nitrate solution for 6 hours, and the alumina foam ceramic carrier adsorbed with ferric nitrate was placed in a drying oven at 120° C. for 8 hours to dry.

[0044] The dried samples were placed in a muffle furnace to be calcined at 500°C at a heating rate of 5°C / min and held for 4 hours to obtain an iron-modified alumina foam ceramic catalyst. Other preparation steps are as in Example 1.

Embodiment 3

[0046] In step (3), the alumina foam ceramics coated with the transition layer was immersed in 0.3 mol / L manganese nitrate solution for 6 hours, and the alumina foam ceramic carrier adsorbed with ferric nitrate was placed in a drying oven at 120° C. for 8 hours.

[0047] The dried samples were placed in a muffle furnace to be calcined at 500°C at a heating rate of 5°C / min and held for 4 hours to obtain a manganese-modified alumina foam ceramic catalyst. Other preparation steps are as in Example 1.

[0048] The catalysts prepared in Examples 1-3 of the present invention were used in the ozone catalytic degradation experiment to evaluate the performance of the catalysts. The experiment was carried out in a plexiglass reactor. Ozone entered the reactor from the bottom of the reactor through the aeration head and mixed with wastewater. The ozone gas phase concentration was 10mg / L, and the reaction temperature was 25°C; the catalyst dosage was 40g / L; the initial TOC was The 40ppm ...

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Abstract

The invention belongs to the technical field of catalysts, provides a metal modified foamed ceramic ozone catalyst and a preparation method thereof, and aims to prepare an efficient, stable and economical catalytic ozonation catalyst for advanced treatment of wastewater. The preparation method comprises the following steps: taking reticular foamed ceramic with a three-dimensional porous structure as a carrier, coating aluminum sol to form a gamma-Al2O3 transition coating, and loading metal oxides such as iron, copper, manganese, cerium and the like by adopting an impregnation method. The material has a high internal surface area and a large pore volume, the huge pore structure and the inner surface of the material provide more attachment sites for metal active components, and the open pore structure can enhance the mass transfer effect of liquid and gas phases, shorten the diffusion path and reduce the flow resistance. The catalyst provided by the invention strengthens the catalytic reaction process on the two scales of catalytic activity surface and catalytic kinetics, and has a good catalytic ozonation effect.

Description

technical field [0001] The invention belongs to the technical field of catalysts, in particular to a method for preparing a metal-modified foam ceramic ozone catalyst. Background technique [0002] Ozone oxidation technology has been widely used in the field of water treatment, but due to its oxidation selectivity and low ozone utilization rate, the popularization and application of ozone oxidation technology has been severely limited. Ozone catalytic oxidation technology is to introduce a catalyst into the traditional single ozone system, increase the oxidation potential of ozone in the system, accelerate the generation of hydroxyl radicals ( OH), an active species with stronger oxidation ability than ozone molecules, and achieve the rapid removal of organic pollutants. Purpose. Ozone catalytic technology is considered to have the most application potential in sewage treatment applications due to the rapid reaction of oxidative degradation of organic matter and low treatme...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/745B01J23/34B01J23/10C02F1/72C02F1/78C02F101/34
CPCB01J23/10B01J23/745B01J23/34B01J23/002C02F1/78C02F1/725C02F2101/345C02F2209/20C02F2209/44
Inventor 陈硕赵洋全燮于洪涛
Owner DALIAN UNIV OF TECH