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Application of sulfur poisoning palladium catalyst as catalyst for removing organic pollutants in water body

A technology of organic pollutants and palladium catalysts, applied in the field of water treatment, can solve the problems of safety risks, lack of resource utilization methods, and high recycling costs

Pending Publication Date: 2021-12-31
UNIV OF SCI & TECH OF CHINA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this method not only has high recycling costs but also has safety risks
Therefore, compared to catalyst regeneration, direct recycling of such sulfur-poisoned catalysts may be a more economically feasible strategy, but there is still a lack of suitable resource utilization pathways.

Method used

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  • Application of sulfur poisoning palladium catalyst as catalyst for removing organic pollutants in water body
  • Application of sulfur poisoning palladium catalyst as catalyst for removing organic pollutants in water body
  • Application of sulfur poisoning palladium catalyst as catalyst for removing organic pollutants in water body

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0115] (1) Sulfur-poisoned nano-palladium catalysts include Pd 4 S, the mass content of sulfur in the sulfur-poisoned nano-palladium catalyst is 8%;

[0116] Weigh 20 mg of dry sulfur-poisoned nano-palladium catalyst solids, add 20 mL of n-hexane for ultrasonic dispersion for 30 minutes, then add 180 mg of titanium dioxide particles as a carrier, and ultrasonically disperse for 10 minutes to ensure that the added titanium dioxide particles and sulfur-poisoned nano-palladium catalysts are mixed evenly, and then stir for 6 hours. The sulfur-poisoned nano-palladium catalyst is fully adsorbed on the surface of titanium dioxide particles. After standing for several minutes, remove the supernatant, and dry at 50° C. to obtain supported catalyst 1 (Pd loaded on a titania carrier). 4 S catalyst).

[0117] (2) Sulfur-poisoned nano-palladium catalysts include Pd 16 S 7 and Pd 4 S, where Pd 16 S 7 and Pd 4 The mass content of S is respectively 44% and 56%, and the mass content of...

Embodiment 2

[0122] In 0.1mmol / L 4-chlorophenol (4-CP) organic waste water (solvent is water), add PMS (the addition amount of PMS is 0.25mmol / L), add the boric acid buffer salt (boric acid buffering salt) that pH value is 7.4 The addition amount of salt is 5mmol / L), and the pH value is 6~7 during the control reaction, then add the supported catalyst 1 of embodiment 1 (the addition amount of supported catalyst is 0.25g / L), stir reaction 40min under normal temperature, Get the treated water body.

[0123] The supported catalyst 1 is replaced by supported catalyst 2, pure palladium catalyst or other common commercial catalysts (such as commercial tricobalt tetroxide, separate titanium dioxide substrate, carbon nanotubes, graphene oxide, 0.025g / L Co 2+ ), the rest of the steps and parameters are the same as the above operations, and the water body is processed. The removal efficiency of 4-CP in the treated water is as follows Figure 4 shown. Figure 4 It is a comparison chart of the remov...

Embodiment 3

[0125] In 0.1mmol / L 4-chlorophenol (4-CP) organic waste water, add PMS (the addition amount of PMS is 0.25mmol / L), add the boric acid buffer salt that pH value is 7.4, pH value is 4 during control reaction , then add the supported catalyst 1 of Example 1 (the addition amount of the supported catalyst 1 is 0.25g / L), and stir and react for 40min at room temperature to obtain the treated water body.

[0126] In 0.1mmol / L 4-chlorophenol (4-CP) organic waste water, add PMS (the addition amount of PMS is 0.25mmol / L), add the boric acid buffer salt that pH value is 7.4, pH value is 4 during control reaction , then add the supported catalyst 2 of Example 1 (the addition amount of the supported catalyst 2 is 0.25g / L), stir and react at room temperature for 40min, and obtain the treated water body.

[0127] In 0.1mmol / L 4-chlorophenol (4-CP) organic waste water, add PMS (the addition amount of PMS is 0.25mmol / L), add the boric acid buffer salt that pH value is 7.4, pH value is 4 during ...

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Abstract

The invention relates to the technical field of water treatment, in particular to application of a sulfur poisoning palladium catalyst as a catalyst for removing organic pollutants in a water body. According to the invention, the sulfur poisoning palladium catalyst can be used as a catalyst for removing the organic pollutants in the water body, and the sulfur poisoning palladium catalyst is matched with peroxymonosulfate to effectively degrade the organic pollutants in the water body, so that the organic pollutants in the water body are effectively removed. The sulfur poisoning palladium catalyst activated PMS has the advantages of high organic pollutant removal efficiency, good cycle stability and wide pH application range, and can be used for treating various organic pollutants, including various phenolic compounds and other electron-rich organic pollutants. Compared with noble metal catalysts such as Pd and the like, the sulfur poisoning palladium catalyst belongs to wastes, so that the water treatment cost can be reduced and resource waste is avoided by recycling the sulfur poisoning palladium catalyst. The material has high catalytic selectivity and strong ion interference resistance, and is not easily influenced by water quality characteristics (such as chloride ions, nitrate ions and bicarbonate ions), and toxic disinfection by-products are not easy to generate.

Description

technical field [0001] The invention relates to the technical field of water treatment, in particular to the application of a sulfur-poisoned palladium catalyst as a catalyst for removing organic pollutants in water bodies. Background technique [0002] In recent years, Fenton-like advanced oxidation technology based on permonosulfate (PMS) has been increasingly applied in water treatment and soil remediation. This type of technology is mainly to generate highly oxidative active sulfate radicals (SO 4 ·- ), can achieve efficient removal of a variety of refractory pollutants, but in practical applications, it is susceptible to interference from coexisting ions (such as chloride ions, bicarbonate ions) and natural organic matter in the environment, and it may also react with halide ions Formation of carcinogenic bromates and other halogenated disinfection by-products. The advanced oxidation technology based on non-free radical pathway can solve the above problems to a large...

Claims

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Application Information

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IPC IPC(8): C02F1/72C02F1/461C02F1/467B01J27/043C02F101/34C02F101/36
CPCC02F1/725C02F1/4672C02F1/46109B01J27/043C02F2101/36C02F2101/345C02F2001/46142Y02W10/37
Inventor 李文卫司洋郭智妍张爱勇柳后起
Owner UNIV OF SCI & TECH OF CHINA