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Two-component manganese-based loaded catalyst prepared by using supergravity spray impregnation method and application of catalyst

A supported catalyst, hypergravity technology, applied in catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc. According to the problems of short production cycle and uneven load, it can achieve the effect of promoting uniform adsorption, shortening production cycle and shortening dipping time.

Pending Publication Date: 2019-10-08
ZHONGBEI UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Aiming at the common problems of low dispersion of active components, uneven loading, low loading, and long production cycle in the preparation of supported catalysts by impregnation, the present invention aims to provide a method for preparing two-component manganese by high-gravity spray impregnation. A method and device based on a supported catalyst and used to catalyze the oxidation of nitrobenzene wastewater by ozone, combined with a high-gravity device that can strengthen gas-liquid-solid mass transfer, the prepared supported catalyst has high dispersion of active components, uniform loading, high activity, and production Short cycle time and high catalytic activity

Method used

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  • Two-component manganese-based loaded catalyst prepared by using supergravity spray impregnation method and application of catalyst
  • Two-component manganese-based loaded catalyst prepared by using supergravity spray impregnation method and application of catalyst
  • Two-component manganese-based loaded catalyst prepared by using supergravity spray impregnation method and application of catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0026] Example 1: Using figure 1 Process flow shown, with 1-2 mm spherical γ-Al 2 o 3As a carrier, it was washed repeatedly with deionized water, dried at 105 °C for 4 h, calcined at 300 °C for 4 h, cooled and evenly packed into a rotating packed bed with a filling capacity of 40 g / L. Prepare a mixed solution of copper nitrate and manganese acetate metal salt with a molar ratio of 1:2 at 0.18 mol / L, adjust the pH to 5.0, and put it into the storage tank. The impregnating liquid was sent into the high-gravity rotating packing bed through a circulating pump, the liquid flow rate was 40 L / h, and the rotating speed was set at 600 rpm to make it fully contact with the carrier for impregnation, and the cycle impregnation time was 30 min. Then the hot air was passed for 60 min to take away the moisture on the surface of the catalyst and fix the active components. Take out the catalyst and bake it at 500℃ for 4 h to get Cu-Mn / γ-Al 2 o 3 catalyst.

Embodiment 2

[0027] Example 2: Using figure 1 Process flow shown, with 1-2 mm spherical γ-Al 2 o 3 As a carrier, it was washed repeatedly with deionized water, dried at 105°C for 4 hours, and calcined at 300°C for 4 hours. After cooling, it was evenly packed into a rotating packed bed with a filling capacity of 80 g / L. Prepare a mixed solution of copper nitrate and manganese acetate metal salt with a molar ratio of 1:1 at 0.3 mol / L, adjust the pH to 5.0, and put it into the storage tank. The impregnating liquid was sent into the high-gravity rotating packed bed through a circulating pump, the liquid flow rate was 60 L / h, and the rotating speed was set at 1200 rpm to make it fully contact with the carrier for impregnation, and the cycle impregnation time was 60 min. Then the hot air was passed for 60 min to take away the moisture on the surface of the catalyst and fix the active components. Take out the catalyst and bake it at 700℃ for 3 h to get Cu-Mn / γ-Al 2 o 3 catalyst.

Embodiment 3

[0028] Example 3: Using figure 1 Process flow shown, with 1-2 mm spherical γ-Al 2 o 3 As a carrier, it was washed repeatedly with deionized water, dried at 105 °C for 4 h, calcined at 300 °C for 4 h, cooled and evenly packed into a rotating packed bed with a filling capacity of 50 g / L. Prepare a mixed solution of copper nitrate and manganese acetate metal salt with a molar ratio of 1:4 at 0.15 mol / L, adjust the pH to 5.0, and put it into the storage tank. The impregnating liquid was sent into the high-gravity rotating packing bed through a circulating pump, the liquid flow rate was 60 L / h, and the rotating speed was set at 800 rpm to make it fully contact with the carrier for impregnation, and the cycle impregnation time was 30 min. Then the hot air was passed for 60 min to take away the moisture on the surface of the catalyst and fix the active components. Take out the catalyst and bake it at 500℃ for 4 h to get Cu-Mn / γ-Al 2 o 3 catalyst.

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Abstract

The invention belongs to the technical fields of loaded catalyst preparation and wastewater treatment. Directed at the problems of low active component dispersity, loading ununiformity, low loading amount, long production period and the like in preparation of a loaded catalyst by an impregnation method in the prior art, the invention provides a two-component manganese-based loaded catalyst prepared by using a supergravity spray impregnation method and an application of the catalyst. The two-component manganese-based loaded catalyst is prepared through the following steps: with a cross-flow rotating packed bed as a supergravity device, gamma-Al2O3 as a filling material and a metal salt mixed solution as an impregnation liquid, spraying the impregnation liquid onto the surface of a carrier for impregnation under the action of supergravity, allowing an impregnation liquid to return to a liquid storage tank for cyclic impregnation, blowing off a filling material with hot air, and removingmoisture on the surface of a precursor; and carrying out calcination at a high temperature of 300 to 700 DEG C so as to obtain the two-component manganese-based loaded catalyst. The catalyst preparedby using the method provided by the invention is used as the filling material, and an aeration device is used as a contact reactor, by addition of the above catalyst, a contact reaction between nitrobenzene wastewater and ozone gas is generated under the catalysis of the catalyst; and the catalyst prepared by using the method provided by the invention has the advantages of uniformly-dispersed active component, large specific surface area, high catalytic activity and short production cycle.

Description

technical field [0001] The invention belongs to the technical field of preparation of supported catalysts and wastewater treatment, and in particular relates to a two-component manganese-based supported catalyst prepared by a high-gravity spray staining method and its application. The catalyst is used for heterogeneous catalytic ozone oxidation of nitrobenzene wastewater . Background technique [0002] Heterogeneous catalytic ozone oxidation treatment of organic wastewater, by introducing a solid catalyst, using the adsorption and catalytic properties of the catalyst, catalyzes the decomposition of ozone to generate more OH free radicals, and triggers a series of free radical chain reactions, thereby completely degrading the waste water. refractory organic pollutants. Heterogeneous catalysts have the advantages of high catalytic activity, high mineralization rate of organic matter, no secondary pollution, and easy recycling, so they have attracted extensive attention. At p...

Claims

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Application Information

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IPC IPC(8): B01J23/889B01J37/02B01J37/08C02F1/72C02F1/78C02F101/38
CPCB01J23/8892B01J37/0203B01J37/0207B01J37/082C02F1/725C02F1/78C02F2101/38
Inventor 焦纬洲邵圣娟刘有智
Owner ZHONGBEI UNIV