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非均相催化氧化预处理氢化可的松制药废水 被引量:2

PRETREATMENT OF HYDROCORTISONE PHARMACEUTICAL WASTEWATER BY HETEROGENEOUS CATALYTIC OXIDATION
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摘要 化学合成类制药废水浓度高,成分复杂,难生物降解,往往需要进行有效前处理,以满足后续处理要求。采用自制的非均相催化剂CuO-CeO2/AC,催化氧化氢化可的松制药废水。通过扫描电镜、X射线衍射对自制的催化剂的性能进行了表征,研究了pH、催化剂用量、氧化剂用量和反应时间4个因素对废水处理效果的影响,并确定了预处理氢化可的松制药废水的最佳工艺条件。研究结果表明,催化剂成层状分布,形成尖晶石结构,催化剂的活性组分是CuO和CeO2。最佳工艺条件:pH=5,催化剂用量1.5 g/L,H2O2用量15 mL/L,反应时间60 min。出水COD去除率为90%以上,TOC的去除率稳定在85%左右,废水的BOD5/COD从0.066提高到0.335,满足后续生化处理的要求。 Chemical synthetic pharmaceutical wastewater need to be pretreated before the traditional treatment because of its high concentration, complex composition and bad biodegradability. In this study, the heterogeneous catalyst ofCuO-CeOJAC made by ourselves was applied in catalytic oxidation of hydrocortisone pharmaceutical wastewater. The catalyst performance was characterized by scanning electron microscopy (SEM) and X-ray diffraction (XRD). Additionally, the effects of pH, catalyst dosage, oxidant concentration and reaction time on effluent quality were investigated and discussed. The optimum conditions for pretreatment of hydrocortisone pharmaceutical wastewater were determined. The results showed that the morphology of CuO-CeO2/AC catalyst was in layered distribution and maybe formed spinel structure. The catalytic active components were CuO and CeO2. The process parameters were optimized as pH=5, catalyst dosage was 1.5 g/L, H2O2 dosage was 15 mL/L, reaction time was 60 min. Eventually, the removal rate of COD was more than 90%, TOC removal rate was stabilized at about 85% and the BODs/COD ratio increased from 0.066 to 0.335, which met the requirement of the subsequent biological treatment.
机构地区 天津科技大学
出处 《水处理技术》 CAS CSCD 北大核心 2013年第11期96-99,103,共5页 Technology of Water Treatment
基金 科技型中小企业创新基金项目(10C26211200185)
关键词 氢化可的松 制药废水 CuO-CeO2催化剂 催化氧化 hydrocortisone pharmaceutical wastewater CuO-CeO2 catalyst catalytic oxidation
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参考文献15

  • 1贾春燕,陈建新,尹秋响,王静康.氢化可的松的合成研究进展[J].中国抗生素杂志,2007,32(9):525-530. 被引量:7
  • 2Sui Qian, Jun Huang, Shubo Deng, et al. Occurrence and removal of pharmaceuticals, caffeine and DEET in wastewater treatment plants of Beijing, China [J].Water Research010,44:417-426.
  • 3GB21904--2008《化学合成类制药工业水污染物排放标准》[S].北京:中国环境科学出版社,2008.
  • 4Isll Akmehmet Balcloglu, Merihitker. Treatment of pharmaceu- tical wastewater containing antibiotic by 03 and OJI-I202 processes [J].Chemosphere,2003,50:85-95.
  • 5Emad S Elmolla, Malay Chaudhuri. The feasibility of using com- bined Fenton-SBR for antibiotic wastcwater treatment [J].Desalina- tion,2012,285:14-21.
  • 6C Sirtori, A Zapata, I Oiler, et al. Decontamination industrial phar- maceutical wastewater by combining solar photo-Fenton and bio- logical treatment[J].Water Research,2009,43:661-118.
  • 7Sajjad Farhadi, Behnoush Aminzadeh, Ali Torabian, et al. Compar- ison of COD removal fran pharmaceutical wastewater by electro- coagulation,photoelectro0agulation, peroxi-electrocoagulation and peroxi-photoelectrocoagulation processes [J].Journal of Hazardous Materials,2012,219-220:35-42.
  • 8国家环保局科技处,清华大学环境工程系.我国几种工业废水治理技术研究(第三分册)-高浓度有机废水[M].北京:化学工业出版社,1988.
  • 9Glaze W H, Kang J W, Chapin D H. The chemistry of water treatment processes involving ozone, hydrogen peroxide and. ultraviolet radiation[J].Ozone Sci Eng.,1987,9(2):335-342.
  • 10R Alnaizy, A Ackerman. Advanced oxidation of phenolic compounds [J],Advances in Environmental Research,2000,4(3):233-244.

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