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Preparation method of ozone oxidation catalyst for treating coal gasification wastewater

A technology for coal gasification wastewater and ozone oxidation, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve difficult recovery, impurity dissolution and low catalytic efficiency and other problems, to achieve the effect of simple preparation method, diverse application methods and high catalytic activity

Active Publication Date: 2018-01-12
POTEN ENVIRONMENT GRP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

It can solve technical problems such as organic pollutants in ozone decomposed water, catalysts are easily oxidized and decomposed by ozone, low strength, easy to break, impurities are leached out, catalytic efficiency is low, and difficult to recycle. However, the catalyst components of the invention are complex, difficult to prepare, and unsuitable for industrialization. application

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] The mass ratio of 20% NiAl-LDH, 20% CoAl-LDH, 20% NiFe-LDH, 10% CuAl-LDH, 10% ZnAl-LDH, 10% MgFe-LDH, 10% MgAl -The calcination temperature and calcination time of LDH in the muffle furnace were respectively set as 450°C, 2h; 450°C, 4h; 550°C, 4h; 350°C, 2h; 500°C, 4h; 430°C, 2h; 4h. The prepared ozonation catalyst is obtained by grinding and pulverizing the dried and fluffy catalyst precursor components after roasting and uniformly mixing them together. The dosage of the catalyst in the ozone catalytic oxidation experiment was set to 11g / L.

[0030] Take 1000ml of water sample, and continuously aerate the ozone reaction, the ozone flow rate is 0.7L / min, the reaction time is 40min, and the pH value is 7.8. Wastewater initial water quality index: COD Cr It is 136.7mg / L, the chromaticity is 400 times, and the turbidity is 0.80NTU; the water quality COD after treatment Cr The removal rate of chroma is 98.0%, the removal rate of chroma is 99.0%, and the removal rate of ...

Embodiment 2

[0033] Put 20% NiAl-LDH, 20% CoAl-LDH, 30% NiFe-LDH, 10% CuAl-LDH, 10% ZnAl-LDH, 10% MgFe-LDH in the muffle furnace The calcination temperature and calcination time were set as 450℃, 5h; 450℃, 4h; 550℃, 4h; 400℃, 3h; 500℃, 6h; 430℃, 4h. The ozonation catalyst is obtained by grinding and pulverizing the dried and fluffy catalyst precursor components evenly and then mixing them together. The dosage of the catalyst in the ozone catalytic oxidation experimental system was set at 20g / L.

[0034] Take 1000ml of water sample, and continuously aerate the ozone reaction, the ozone flow rate is 0.6L / min, the reaction time is 30min, and the pH value is 8.1. Wastewater initial water quality index: COD Cr It is 132.6mg / L, the chromaticity is 400 times, and the turbidity is 0.85NTU; the water quality COD after treatment Cr The removal rate of chroma is 92.7%, the removal rate of chroma is 99.0%, and the removal rate of turbidity is 82.4%.

[0035] The catalyst that has been used or used...

Embodiment 3

[0037] Put 20% NiAl-LDH, 30% CoAl-LDH, 20% NiFe-LDH, 10% CuAl-LDH, 10% ZnAl-LDH, 10% MgFe-LDH in the muffle furnace The calcination temperature and calcination time were set as 450℃, 3h; 450℃, 4h; 550℃, 4h; 550℃, 5h; 500℃, 4h; 430℃, 5h. The ozone catalyst is obtained by grinding and pulverizing the dried and fluffy catalyst precursor components evenly after roasting and mixing them together. The dosage of the catalyst in the ozone catalytic oxidation system is set to 18g / L.

[0038] Take 1000ml of water sample, and continuously aerate the ozone reaction, the ozone flow rate is 0.5L / min, the reaction time is 60min, and the pH value is 8.6. Wastewater initial water quality index: COD Cr It is 128.1mg / L, the chromaticity is 400 times, and the turbidity is 0.83NTU; the water quality COD after treatment Cr The removal rate of 93.1%, the removal rate of color is 99.0%, and the removal rate of turbidity is 86.1%.

[0039] The catalyst that has been used or used many times is drie...

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Abstract

The invention relates to a method for preparing an ozone oxidation catalyst for treating coal gasification wastewater, wherein hydrotalcite is selected as the catalyst precursor, and the mass ratio of the hydrotalcite is: 0-50% NiAl-LDH, 0-50% CoAl ‑LDH, 0~50% NiFe‑LDH, 0~30% CuAl‑LDH, 0~30% ZnAl‑LDH, 0~30% MgFe‑LDH, 0~30% MgAl‑LDH, the sum of mass ratio is After 100% hydrotalcite materials of each component are roasted separately, they are ground, pulverized and mixed evenly to obtain an ozone oxidation catalyst. The catalyst prepared by the invention is a multi-component composite metal oxide, has high catalytic activity, avoids the problem that the active components of the existing ozone oxidation catalyst are easily dissolved, and has simple preparation method, environmental friendliness, strong applicability and wide application range.

Description

technical field [0001] The invention relates to the technical field of industrial wastewater treatment, in particular to a preparation method of an ozone oxidation catalyst for treating coal gasification wastewater. Background technique [0002] Coal is the main energy source in my country, and coal chemical industry projects are developing rapidly. However, the ecological environment in the areas where coal resources are mainly distributed is fragile, engineering-type water shortages are serious, and water resources are seriously insufficient. The composition of coal chemical wastewater produced by different processes such as Lurgi furnace, Winkler furnace, Texaco coal-water slurry gasification, multi-nozzle coal-water slurry gasification furnace, and Shell dry coal powder pressure gasification furnace is very different. Large, the wastewater produced by these gasification processes has high content of oil, phenol, ammonia and cyanide, especially the fixed bed gasification ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/80C02F1/78
Inventor 乔瑞平耿翠玉陈广升
Owner POTEN ENVIRONMENT GRP