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Preparation method of non-metal catalyst for efficiently degrading phenol, and catalyst

A non-metallic catalyst and catalyst technology, applied in the direction of chemical instruments and methods, physical/chemical process catalysts, chemical/physical processes, etc., can solve the problems of high treatment costs, secondary pollution, infiltration, etc., and achieve low cost and saving Low energy consumption and low cost

Inactive Publication Date: 2019-12-20
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the catalysts of traditional advanced oxidation technology generally contain metals or metal oxides, and there are disadvantages such as toxic metal penetration, expensive treatment costs and easy to produce secondary pollution to varying degrees.

Method used

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  • Preparation method of non-metal catalyst for efficiently degrading phenol, and catalyst
  • Preparation method of non-metal catalyst for efficiently degrading phenol, and catalyst
  • Preparation method of non-metal catalyst for efficiently degrading phenol, and catalyst

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preparation example Construction

[0026] A kind of preparation method of the non-metallic catalyst of efficient degradation phenol of the present invention, comprises the steps:

[0027] 1) Add 10-40wt.% nitrogen precursor, 10-40wt.% silicon dioxide and 40-60wt.% zinc chloride to 100-500mml aqueous solution according to mass percentage, stir and mix evenly to obtain a suspension solution ;in,

[0028] The nitrogen precursor is more than one of polyaniline, polyacrylonitrile, urea and melamine. The mass ratio of the silicon dioxide to the nitrogen-containing precursor is 0.25˜4:1.

[0029] 2) heating and stirring the obtained suspension at a set temperature and a set time to obtain a nitrogen precursor, silicon dioxide and zinc chloride solid composite; wherein, the set temperature is 50-90°C, The setting time is 5~10h.

[0030] 3) Perform a pyrolysis reaction on the obtained solid compound at a set temperature and a set time to obtain a carbonized compound; wherein, the pyrolysis reaction time is 0.5-4 hour...

Embodiment 1

[0036] (1) Add 0.2g of silicon dioxide, 0.4g of polyacrylonitrile and 0.4g of zinc chloride into 100ml of distilled water at a mass ratio of 0.5:1 to the nitrogen-containing precursor, stir and mix evenly to obtain suspension solution;

[0037] (2) heating and stirring the suspension solution at 50° C. for 5 hours to obtain a solid composite of polyacrylonitrile, silicon dioxide and zinc chloride;

[0038] (3) performing a pyrolysis reaction on the solid composite at 600° C. for 2 hours to obtain a carbonized composite;

[0039] (4) washing the carbonized complex with sodium hydroxide with a concentration of 1M for 4 hours;

[0040] (5) The solution obtained after alkali washing was centrifuged at 10,000 rpm for 10 min, and vacuum-dried at 75° C. to obtain a nitrogen-doped hierarchically porous carbon material, which was the catalyst.

[0041] The SEM image of the prepared metal-free catalyst is shown in figure 1 Shown; The prepared non-metallic catalyst N 2 Adsorption-des...

Embodiment 2

[0043] (1) Add 0.1g of silicon dioxide, 0.4g of polyacrylonitrile and 0.5g of zinc chloride into 100ml of distilled water at a mass ratio of 0.25:1 of silicon dioxide and nitrogen-containing precursor, stir and mix evenly to obtain a suspension solution;

[0044] (2) heating and stirring the suspension solution at 90° C. for 5 hours to obtain a solid composite of polyacrylonitrile, silicon dioxide and zinc chloride;

[0045] (3) performing a pyrolysis reaction on the solid composite at 600° C. for 2 hours to obtain a carbonized composite;

[0046] (4) washing the carbonized complex with sodium hydroxide with a concentration of 1M for 6 hours;

[0047] (5) The solution obtained after alkali washing was centrifuged at 8000 rpm for 10 min, and vacuum-dried at 75° C. to obtain a nitrogen-doped hierarchically porous carbon material, which was the catalyst.

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Abstract

The invention relates to a preparation method of a non-metal catalyst for efficiently degrading phenol. The preparation method comprises the following steps: according to a mass percent ratio, mixing10-40 wt% of a nitrogen precursor, 10-40 wt% of silicon dioxide and 40-60 wt% of zinc chloride into 100-500ml of distilled water, and carrying out uniform mixing by stirring to obtain a suspension solution; heating and stirring the obtained suspension at a set temperature for a set time to obtain a solid compound of the nitrogen precursor, silicon dioxide and zinc chloride; carrying out a pyrolysis reaction on the obtained solid compound at a set temperature for a set time to obtain a carbonized compound; carrying out alkaline washing on the obtained carbonized compound; and centrifuging the solution after alkaline washing, and carrying out vacuum drying to obtain a nitrogen-doped hierarchical-pore carbon material, namely the target catalyst. The specific surface area of the catalyst is 1000 m<2> / g or above. The preparation method has the advantages of simple process, easily obtained raw materials and low cost. The prepared catalyst has high efficiency of catalyzing and degrading phenol at normal temperature, the system temperature does not need to be increased, and energy consumption can be saved.

Description

technical field [0001] The invention relates to a preparation method of a non-metallic catalyst. In particular, it relates to a method for preparing a non-metallic catalyst for efficiently degrading phenol and the catalyst. Background technique [0002] In recent years, with the continuous advancement of my country's industrialization process, the discharge of organic wastewater has become one of the important issues facing us today. Among them, phenol-containing wastewater is the main wastewater produced by the petrochemical industry. Because of its high toxicity and high pollution, it is listed as one of the key harmful wastewater in my country's water pollution control. my country's "Comprehensive Wastewater Discharge Standard" (GB8978-1996) clearly stipulates that phenolic substances are the second type of pollutants, and the discharge standards for primary and secondary wastewater shall not exceed 0.5mg L –1 , the third level standard shall not exceed 2.0mg L –1 . T...

Claims

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Application Information

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IPC IPC(8): B01J27/24B01J21/18C02F1/72B01J35/10C02F101/34
CPCB01J27/24B01J21/18C02F1/725C02F2101/345B01J35/618
Inventor 彭文朝张文
Owner TIANJIN UNIV