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Preparation and application method of Ce-Zr/molecular sieve Fenton heterogeneous catalyst

A technology of heterogeneous catalyst and application method, which is applied in the preparation and application field of Ce-Zr/molecular sieve Fenton heterogeneous catalyst, can solve the problem of large dosage of chemicals, large sludge, and increase the operation of high-salt and high-COD wastewater treatment equipment Cost and other issues, to achieve the effect of low production cost, easy access, good catalytic activity

Pending Publication Date: 2022-05-10
南京合一环境集团有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to provide a method for preparing and applying Ce-Zr / molecular sieve Fenton heterogeneous catalyst, to solve the problem of large dosage of medicament proposed in the above-mentioned background technology, and a large amount of sludge will be produced at the same time, which needs to be harmless treatment, and increase the operating cost of high-salt and high-COD wastewater treatment equipment

Method used

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  • Preparation and application method of Ce-Zr/molecular sieve Fenton heterogeneous catalyst
  • Preparation and application method of Ce-Zr/molecular sieve Fenton heterogeneous catalyst
  • Preparation and application method of Ce-Zr/molecular sieve Fenton heterogeneous catalyst

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preparation example Construction

[0034] Catalyst preparation steps:

[0035] S1, weigh Ce(NO 3 ) 3 ·6H 2 O, Zr(NO 3 ) 4 ·5H 2 O, under the condition of 40-80 ℃ strong stirring for 10-30 min, dissolve in a certain amount of deionized water to prepare cerium nitrate and zirconium nitrate solution, control the content of cerium nitrate and zirconium nitrate at 0.3%wt-8.0%wt, The molar ratio of Ce to Zr is controlled between (3:1)-(1:5);

[0036] S2. Weigh the purchased molecular sieve raw material with a mass of m3, wash it with deionized water and ethanol alternately with ultrasonic oscillation for 10-60 min at room temperature, and dry the cleaned molecular sieve carrier at 80-120°C for 4-12 h. Take it out for later use, and control the content of active components Ce and Zr at 0.05%wt-2.0%wt;

[0037] S3, slowly add the cerium nitrate and zirconium nitrate solution into the molecular sieve carrier, place it in an ultrasonic oscillation device, shake and impregnate it for 10-120 minutes, and dry the sha...

Embodiment 1

[0039] (1) Weigh 4.328g of Ce(NO 3 ) 3 ·6H 2 O, weigh 4.025g of Zr(NO 3 ) 4 ·5H 2 O, dissolved in 200 mL of deionized water, stirred and dissolved in a water bath at 60°C for 20 min, and prepared as a mixed active solution with cerium nitrate and zirconium nitrate content of about 3.18%;

[0040](2) Weigh 300 g of purchased molecular sieves, wash them with 500 mL of deionized water and 500 mL of ethanol with alternating ultrasonic vibrations for 30 min at room temperature, and dry the cleaned molecular sieves in a drying oven at 90 °C for 8 h. Weigh 200.126g of molecular sieve and place it in a crucible, and slowly add active solutions of cerium nitrate and zirconium nitrate to the crucible filled with molecular sieves step by step, the content of active components Ce and Zr is about 1.11%wt;

[0041] (3) Place the crucible containing the molecular sieve and the active solution in an ultrasonic oscillation device, oscillate and impregnate for 60 min, place the catalyst af...

Embodiment 2

[0043] (1) Weigh 2.167g of Ce(NO 3 ) 3 ·6H 2 O, weigh 4.019g of Zr(NO 3 ) 4 ·5H 2 O, dissolved in 200 mL of deionized water, placed in a water bath at 70°C and stirred for 25 min to form a mixed active solution with cerium nitrate and zirconium nitrate content of about 2.35%;

[0044] (2) Weigh 300 g of purchased molecular sieves, wash them with 500 mL of deionized water and 500 mL of ethanol by alternating ultrasonic oscillation for 30 min at room temperature, and dry the cleaned molecular sieves in a drying oven at 100 °C for 7 h. Weigh 200.008g of molecular sieve and place it in a crucible, and slowly add active solutions of cerium nitrate and zirconium nitrate into the crucible filled with molecular sieves step by step, the content of active components Ce and Zr is about 0.77%wt;

[0045] (3) Place the crucible containing the molecular sieve and the active solution in an ultrasonic oscillation device, oscillate and impregnate for 50 min, place the catalyst after ultra...

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Abstract

The invention discloses a preparation and application method of a Ce-Zr / molecular sieve Fenton heterogeneous catalyst, which comprises preparation of the Ce-Zr / molecular sieve Fenton heterogeneous catalyst from active metals such as Ce and Zr and application of the Ce-Zr / molecular sieve Fenton heterogeneous catalyst in high-salt and high-COD wastewater, the active metals such as Ce and Zr are impregnated in a molecular sieve carrier by an ultrasonic impregnation method, and the Ce-Zr / molecular sieve Fenton heterogeneous catalyst is obtained. Preparing a Ce-Zr / molecular sieve Fenton heterogeneous catalyst; the method comprises the following steps: putting a catalyst sample into wastewater with certain salinity and certain COD (Chemical Oxygen Demand), and degrading and removing COD in the high-salinity wastewater by adding an acid solution, a hydrogen peroxide solution and an alkali solution. According to the preparation and application method of the Ce-Zr / molecular sieve Fenton heterogeneous catalyst, adopted raw materials are low in price and easy to obtain, the production cost of the catalyst is low, the prepared catalyst can be recycled, the number of agents needing to be added into a Fenton reaction system is small compared with a traditional Fenton technology, the amount of generated sludge is small, and the operation cost of the Fenton system is low.

Description

technical field [0001] The invention relates to the technical field of environmental protection wastewater treatment, in particular to a method for preparing and applying a Ce-Zr / molecular sieve Fenton heterogeneous catalyst. Background technique [0002] High-salt and high-COD wastewater has high salt content and complex salt content. High-concentration salt can inhibit the growth of microorganisms and have a certain biological toxicity to microorganisms. Therefore, the biological treatment effect of high-salt and high-COD wastewater is not ideal. COD in wastewater is difficult to be effectively treated by biochemical methods; [0003] Molecular sieve has the characteristics of uniform pore size structure, large specific surface area, high surface polarity, and high stability of skeleton structure. At the same time, the surface of molecular sieve has B acid and L acid. COD in COD is a commonly used catalyst carrier with excellent performance; [0004] At present, high-sal...

Claims

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Application Information

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IPC IPC(8): B01J29/03B01J29/06B01J37/02B01J37/08C02F1/72
CPCB01J29/03B01J29/061B01J37/0201B01J37/088C02F1/722C02F1/725B01J2229/186C02F2305/026C02F2209/08
Inventor 戚绪亮王新孙培军庞欣
Owner 南京合一环境集团有限公司