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Sulfur modified porous iron oxide catalyst, preparation method therefor and application of sulfur modified porous iron oxide catalyst

An iron oxide and catalyst technology, applied in the field of environmental pollution remediation and inorganic materials, can solve the problems of loss of catalytic effect, narrow pH operating range, increased operating cost, etc., and achieve the effects of high reaction rate, large specific surface area and strong dispersibility

Active Publication Date: 2016-03-23
安联环境科技集团有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] ① Narrow pH operating range: Fenton reagent has a better treatment effect in the range of pH 2.0 to 6.0, and the best activity is reflected at pH 2.8; at higher pH, such as when pH is greater than 6.0, Fenton reagent The effect of Fe is greatly reduced due to iron accumulation and precipitation, and in the presence of oxygen, Fe 2+ will be oxidized to Fe 3+ , thus forming iron oxides to settle down and lose their catalytic effect; since the pH of most wastewater is greater than 6.0, it is necessary to pre-adjust the acidity of the wastewater and add acidic reagents, thus increasing the operating cost;
[0010] ② Fenton cannot completely mineralize organic matter. In most cases, due to the tendency of iron aggregation and sedimentation, the intermediate products of degradation can be combined with Fe 3+ It forms a stable complex and can compete with the generation of OH. It is difficult to use Fenton's reagent to degrade organic pollutants. The mineralization degree is difficult to exceed 60%.

Method used

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  • Sulfur modified porous iron oxide catalyst, preparation method therefor and application of sulfur modified porous iron oxide catalyst
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  • Sulfur modified porous iron oxide catalyst, preparation method therefor and application of sulfur modified porous iron oxide catalyst

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Experimental program
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Effect test

Embodiment 1

[0036] A sulfur-modified porous iron oxide catalyst is prepared by the following method: (1) 1.8 g of oxalic acid is dissolved in 50 mL of water to prepare an oxalic acid solution with a concentration of 0.4 mol / L, and the heating process is heated to 60° C. in a water bath. (2) Under magnetic stirring, add 0.01 mol of sodium thiosulfate to the above-mentioned oxalic acid solution, stir for 5 min and mix evenly, dropwise add 50 mL of a solution containing 0.02 mol of ferrous sulfate, and continue to stir the reaction Immediately after 30min, ice bath for 30min to obtain a yellow suspension; (3) filter the above-mentioned yellow suspension, and then dry it in a blast drying oven at 80° C. until the moisture is dried to obtain a yellow sulfur-modified oxyoxalate Iron precursor; the above precursor is calcined in a muffle furnace, and heated to 300°C at a heating rate of 4°C / min for 60min to obtain a sulfur-modified porous iron oxide catalyst.

[0037] The electron scanning elect...

Embodiment 2

[0039] A sulfur-modified porous iron oxide catalyst is prepared by the following method: (1) Dissolving 0.02 mol of oxalic acid in 50 mL of water to prepare an oxalic acid solution, heating it to 60° C. in a water bath, and performing magnetic stirring during the heating process to make the oxalic acid completely (2) Under magnetic stirring, add 0.01 mol of sodium thiosulfate to the above-mentioned oxalic acid solution, stir to dissolve the sodium thiosulfate completely, and add dropwise 50 mL containing 0.02 mol Fe(NO) after mixing evenly. 3 ) 2 The solution obtained was a yellow suspension, and the reaction was continued to be stirred for 10 minutes, followed by an ice bath for 10 minutes; (3) the above-mentioned yellow suspension was vacuum filtered and washed, and then dried in a blast drying oven at 100 ° C until the water was dried to obtain The yellow granular sulfur-modified ferrous oxalate precursor was calcined in a muffle furnace and heated to 300 °C for 60 min at a...

Embodiment 3

[0045] A sulfur-modified porous iron oxide catalyst is prepared by the following method: (1) Dissolving 0.02 mol of oxalic acid in 50 mL of water to prepare an oxalic acid solution, heating it to 60° C. in a water bath, and performing magnetic stirring during the heating process to make the oxalic acid completely (2) Under magnetic stirring, add 0.01 mol of sodium thiosulfate to the above-mentioned oxalic acid solution, stir to dissolve the sodium thiosulfate completely, and add 50 mL of Fe(NO) containing 0.02 mol dropwise after mixing evenly. 3 ) 2 The solution obtained was a yellow suspension, and the reaction was continued to be stirred for 10 minutes, followed by an ice bath for 10 minutes; (3) the above-mentioned yellow suspension was vacuum filtered and washed, and then dried in a blast drying oven at 100 ° C until the water was dried to obtain The yellow granular sulfur-modified ferrous oxalate precursor was calcined in a muffle furnace, and heated to 300°C at a heating...

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Abstract

The invention belongs to the field of environmental pollution remediation and inorganic materials and particularly relates to a sulfur modified porous iron oxide catalyst, a preparation method therefor and application of the sulfur modified porous iron oxide catalyst. A main ingredient of the porous iron oxide catalyst is iron oxide, and a sulfide of iron coexists. The preparation method comprises the steps: dissolving oxalic acid in water so as to prepare an oxalic acid solution, carrying out heating in water bath, and carrying out stirring while carrying out heating until the oxalic acid is completely dissolved; and adding a sulfur compound solution into the oxalic acid solution, carrying out uniform mixing, then, dropwise adding a ferrous salt solution into the mixture, continuing to carry out stirring until the reaction is thorough, then, carrying out ice bath immediately so as to obtain a yellow suspension, carrying out filtrating, then, carrying out drying treatment so as to obtain a yellow sulfur-modified ferrous oxalate precursor, and then, carrying out calcination, thereby obtaining the sulfur modified porous iron oxide catalyst. The sulfur modified porous iron oxide catalyst can be used for effectively activating hydrogen peroxide and persulfate in sewage water with the pH value of 3-10 and efficiently removing toxic or refractory organic pollutants from the water.

Description

technical field [0001] The invention belongs to the field of environmental pollution remediation and inorganic materials, and particularly relates to a sulfur-modified porous iron oxide catalyst and a preparation method and application thereof. Background technique [0002] my country is a big water-deficient country, and environmental pollution, especially water pollution, will further reduce the available water resources and restrict my country's economic and social development. Common sewage treatment methods include physical method, chemical method and microbial method. Physical methods can only achieve the transfer of pollutants, but cannot eliminate their environmental hazards. Biological method is the most common sewage treatment method, but its treatment cycle is long, and the treatment effect of industrial wastewater containing a large amount of highly toxic and refractory organic pollutants is not good. The advanced oxidation technology based on hydroxyl radicals...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/043B01J35/10C02F1/72C02F101/30C02F101/34
CPCC02F1/725B01J23/745B01J27/043C02F2101/30C02F2101/345B01J35/19B01J35/615
Inventor 杜江坤鲍建国
Owner 安联环境科技集团有限公司
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