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Pypocholoride decomposition catalyst

A hypochlorite and catalyst technology, which is applied in the field of hypochlorite decomposition catalyst, can solve the problem of low catalytic activity of the catalyst and achieve high decomposition efficiency

Active Publication Date: 2022-07-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Catalytic decomposition of hypochlorite is mainly to generate oxygen and corresponding salts. Patent CN102886268A has prepared a sodium hypochlorite catalyst loaded with nickel, copper and manganese on cement. Although the surface area of ​​the catalyst is increased, its catalytic activity is still low

Method used

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  • Pypocholoride decomposition catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] (1) Impregnate 1000g of the above alumina pellets with an equal volume of 0.4mol / L cerium nitrate solution, dry at 80°C for 10h, and then calcinate at 450°C for 4h;

[0029] (2) Impregnate the alumina pellets obtained in step (1) with an equal volume of sodium hydroxide solution with a concentration of 0.3 mol / L, and vacuum dry at 60°C for 12 hours;

[0030] (3) The amount of cobalt, nickel and hypochlorous acid is calculated as 0.1:1:1.1 Cobalt nitrate, nickel nitrate and hypochlorous acid are prepared into a mixed solution, and the total mass of cobalt, nickel and hypochlorous acid in the solution The concentration was 0.6 mol / L, the pH of the solution was adjusted to 5.0 with sodium hydroxide, and the alumina pellets obtained in step (2) were impregnated with equal volume, dried at 80 °C for 12 h, and then calcined at 150 °C for 4 h to obtain catalyst C1.

Embodiment 2

[0032] (1) Impregnate 1000g alumina pellets with an equal volume of 0.4mol / L cerium nitrate solution, dry at 80°C for 12h, and bake at 450°C for 4h after drying;

[0033] (2) Impregnate the alumina pellets obtained in step (1) with an equal volume of sodium hydroxide solution with a concentration of 0.3 mol / L, and vacuum dry at 60°C for 12 hours;

[0034] (3) Calculate the mass of cobalt, nickel and hypochlorous acid as 0.2:1:1.2. Mix cobalt nitrate, nickel nitrate and hypochlorous acid into a mixed solution, and the total mass concentration of cobalt, nickel and hypochlorous acid in the solution 0.6mol / L, the pH of the solution was adjusted to 5.0 with sodium hydroxide, the alumina pellets obtained in step (2) were impregnated with equal volume, dried at 80°C for 12h, and then calcined at 150°C for 4h to obtain catalyst C2.

Embodiment 3

[0036] (1) Impregnate 1000g alumina pellets with an equal volume of 0.4mol / L cerium nitrate solution, dry at 80°C for 12h, and bake at 450°C for 4h after drying;

[0037] (2) Impregnate the alumina pellets obtained in step (1) with an equal volume of sodium hydroxide solution with a concentration of 0.3 mol / L, and vacuum dry at 60°C for 12 hours;

[0038] (3) Calculate the mass of cobalt, nickel and hypochlorous acid as 0.3:1:1.3. Mix cobalt nitrate, nickel nitrate and hypochlorous acid into a mixed solution, and the total mass concentration of cobalt, nickel and hypochlorous acid in the solution Alumina pellets obtained in step (2) were impregnated with equal volume, dried at 80°C for 12h, and then calcined at 150°C for 4h to obtain catalyst C3.

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Abstract

The pypocholoride decomposition catalyst is prepared by the following steps: (1) loading cerium on a carrier by an impregnation method, drying and roasting; (2) impregnating a product obtained in the step (1) with a sodium hydroxide or potassium hydroxide solution, and carrying out vacuum drying; and (3) dipping the product in the step (2) in a mixed solution of cobalt salt, nickel salt and hypochlorous acid, drying and roasting to obtain the catalyst. The catalyst provided by the invention takes cerium as an auxiliary agent to play a role in effectively capturing hypochlorite, and takes nickel and cobalt as active components to timely decompose hypochlorite. In the preparation process of the catalyst, the cerium component is firstly loaded, then the nickel and the cobalt are loaded by an in-situ co-precipitation reaction method, and the active component and the auxiliary agent are uniformly dispersed and can be well matched, so that the cerium can be decomposed in time by the nickel and the cobalt while capturing the chlorate, and the decomposition efficiency of the catalyst is high.

Description

technical field [0001] The present invention relates to the technical field of catalysts, in particular to a hypochlorite decomposition catalyst. Background technique [0002] Hypochlorous acid has strong oxidizing properties and is widely used in chemical synthesis, oxidative degradation, oxidative disinfection and other fields. However, hypochlorous acid has a pungent odor and is easily converted into highly toxic chlorine gas under acidic conditions, which has a greater impact on the environment. . However, in industrial production, the wastewater containing chlorine tail gas treated with lye contains a large amount of sodium hypochlorite, and the solution after the application of hypochlorous acid has hypochlorous acid residues. These solutions have pungent odor and strong oxidizing property. In case of acid, it is easy to release chlorine gas, resulting in secondary pollution. Hypochlorous acid and sodium hypochlorite have poor stability and are easily decomposed into...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83B01J37/02B01J37/08B01J37/03C02F1/72C02F101/12
CPCB01J23/83B01J23/002B01J37/0201B01J37/088B01J37/035B01J37/082C02F1/725B01J2523/00C02F2101/12B01J2523/31B01J2523/3712B01J2523/845B01J2523/847
Inventor 程晓东马和旭马传军郭宏山
Owner CHINA PETROLEUM & CHEM CORP