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Comparative Experimental Study Of UV/PS And UV/H2O2 Degradation Of Quinoline In Coal Chemical Wastewater

Posted on:2021-04-13Degree:MasterType:Thesis
Country:ChinaCandidate:K L YuFull Text:PDF
GTID:2381330629482616Subject:Environmental Engineering
Abstract/Summary:PDF Full Text Request
As a typical nitrogen-containing heterocyclic compound,quinoline is widely present in the secondary biochemical effluent of coal chemical industry wastewater.Once discharged into the environmental system,it will have a toxic impact on the environment and humans.Photochemical oxidation technology is widely used in the treatment of nitrogen-containing heterocyclic compounds.At the same time,relevant studies have shown that the combination of transition metal activation technology on the basis of photochemical oxidation technology can improve its effect of degrading pollutants.In this study,ultraviolet light?UV?activated persulfate and hydrogen peroxide?UV/PS and UV/H2O2?two oxidation technologies based on photochemical reaction were used to degrade quinoline.The dosage of oxidant and the initial pH of the solution The effect of the degradation of quinoline was also investigated.The effect of Fe2+on the degradation of quinoline by the two systems was also investigated.Finally,the two oxidation technologies are compared,and the optimal reaction system is selected to measure the rate constant of the reaction between free radicals and quinoline.The research results are as follows:?1?In the UV/PS system,when the initial concentration of quinoline is C0=15mg/L,the ultraviolet light intensity is I0=8.96mW/cm2,and the reaction temperature is 25?,the optimal oxidation conditions are:[PS]:[QL]=20,pH=7,[Fe2+]:[PS]=1:33.After 60minutes of reaction,the removal rate of quinoline was 90.92%,and after 120 minutes of reaction,the removal rate of TOC was 62.33%.?2?In the UV/H2O2 system,when the initial concentration of quinoline is C0=15mg/L,the ultraviolet light intensity is I0=8.96mW/cm2,and the reaction temperature is 25?,the optimal oxidation conditions are:[H2O2]:[QL]=40,pH=7,[Fe2+]:[H2O2]=1:65.After 60 minutes of reaction,the removal rate of quinoline was 90.90%.After 120minutes of reaction,the removal rate of TOC was 65.07%.?3?Comparing the degradation effects of quinoline by the two technologies under their respective optimal reaction conditions,it was found that the degradation rate of quinoline by the Fe2+/UV/PS system was slightly higher than that of Fe2+/UV/H2O2 technology.Controlling other reaction conditions remains the same.When adding the same amount of oxidant or the same amount of Fe2+to the reaction system,it was found that the degradation rate of quinoline by Fe2+/UV/PS is slightly higher than that of Fe2+/UV/H2O2 technology.At the same time,Fe2+/UV/PS consumes less electricity than Fe2+/UV/H2O2,and has a lower economic cost.?4?In the Fe2+/UV/PS system,quenching experiments verify that both SO4and·OH radicals are present in the system.According to the probe compound method,nitrobenzene and benzoic acid are used with the two radicals.The second-order rate constants of the reaction were used to calculate the contents of the two kinds of free radicals,and the rate constants of the reaction between the free radicals and quinoline were measured according to the calculated free radical contents:k·OH,QL=6.86×109M-1·s-1,kSO4-·,QL=8.37×109M-1·s-1.
Keywords/Search Tags:Quinoline, UV/H2O2, UV/PS, Transition metals, Advanced oxidation, Degradation rate constant
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