本文選題：青霉素生產(chǎn)廢水 + Fenton試劑��； 參考：《山西大學》2015年碩士論文

【摘要】：青霉素生產(chǎn)廢水水質(zhì)成分復雜,CODcr濃度高,硫酸鹽濃度高,水量波動大,難降解,處理水長期存在不達標的問題。本研究采用Fenton試劑氧化法、Cu/Fe催化還原法、曝氣鐵碳微電解法、臭氧氧化法對青霉素生產(chǎn)廢水生化處理后的出水進行了深度處理研究,以期為青霉素生產(chǎn)廢水的深度處理提供參考。采用了Fenton試劑氧化法、Cu/Fe催化還原法、曝氣鐵碳微電解法、臭氧氧化法這4種方法,考察了4種方法的影響因素對處理效果的影響。結果表明,Fenton試劑氧化法的最佳條件是H202(質(zhì)量分數(shù)30%)投加量為100ml/L, Fe~(2+)和H202配比(摩爾比)為1/10,pH值為3.0,反應時間為0.5h,在最佳條件下CODcr去除率達到89.7%,BOD5去除率達到36.4%,NH3-N去除率達到98.8%；Cu/Fe催化還原法的最佳條件是反應溫度為25℃,銅鐵總投加量為60.00g/L,銅鐵投加比例為1：4,廢水pH為4.5,反應時間為1h,在最佳條件下CODcr去除率達到64.2%,BOD5去除率達到47.1%,NH3-N去除率達到97.8%；曝氣鐵碳微電解法的最佳條件是曝氣時間為2.0h,鐵炭投加量為66.67g/L,鐵碳比1：1,曝氣量為0.25L/min,初始pH值為4.0,在最佳條件下,CODcr去除率達到58.7%,BOD5去除率達到42.2%,NH3-N去除率達到99.2%；臭氧氧化法的最佳條件是通氣時間為20min,臭氧通入量為6.67g/L,反應溫度為30℃,廢水pH為10.0,在最佳條件下,CODcr去除率可達60.7%,BOD5去除率可達47.9%,NH3-N去除率達到96.8%。研究結果顯示,4種方法中Fenton試劑氧化法處理效果最好,出水COD_(cr)為22.5mg/L,達到《GB 8978-1996))中的一級排放標準。
[Abstract]:The water quality of penicillin wastewater is characterized by high concentration of CODcr, high concentration of sulfate, large fluctuation of water quantity and difficulty of degradation. The problem of water treatment is not up to standard for a long time. In this paper, the advanced treatment of effluent from penicillin production wastewater after biochemical treatment was studied by Fenton reagent oxidation method and catalytic reduction of Cu / Fe, aerated iron-carbon microelectrolysis and ozone oxidation. In order to provide a reference for the advanced treatment of penicillin production wastewater. The Fenton reagent oxidation method Cu- / Fe catalytic reduction method, aerated iron-carbon micro-electrolysis method and ozone oxidation method were used. The influence factors of the four methods on the treatment effect were investigated. The results show that the optimum conditions of Fenton reagent oxidation method are that the dosage of H2022 (30wt%) is 100ml / L, Feb2) and the molar ratio of H202 (molar ratio) is 1 / 10 (pH = 3.0), the reaction time is 0.5 h, and the removal rate of CODcr reaches 89.7BOD5 and the removal rate of NH _ 3-N reaches 98.8wt%. The optimum conditions are as follows: (1) the ratio of H _ (20) to H _ (20) is 100 ml / L, and the molar ratio of H _ (202) to H _ (202) is 3.0% and 0.5 h respectively. The optimum conditions for Cu- / Fe catalytic reduction are as follows: the reaction temperature is 25 鈩，

本文編號：2043953