中文题名: | 高硫高浓度抗生素废水处理工艺研究 |
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保密级别: | 2年后公开 |
学科代码: | 083002 |
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学生类型: | 硕士 |
学位: | 工学硕士 |
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学位年度: | 2009 |
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研究方向: | 水污染控制 |
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提交日期: | 2009-06-18 |
答辩日期: | 2009-05-26 |
外文题名: | The Treatment of Sulfate-ridden High-strength Fermentative Industrial Wastewater |
中文摘要: |
高硫型抗生素废水是一种较难处理的高浓度有机废水,寻找经济高效的处理工艺成为近年来的研究重点。本文通过批量培养探讨微好氧(DO≤0.5mg/L)条件处理高硫高浓度抗生素废水的可行性,考察溶氧供给及pH调控对处理效果的影响;通过连续小试考察HRT与进水COD浓度对微好氧工艺污染物去除效果的影响;以臭氧工艺作为生物处理的后续工艺,考察臭氧投加量与调控初始pH对污染物去除效果的影响。结果表明:(1)微好氧和无氧条件下批量培养试验表明:微好氧条件下微生物活性较高,能有效去除COD(去除率为55%);无氧条件下,COD几乎没有变化,MLSS的增长相当缓慢。(2)微好氧连续小试结果表明:当进水COD浓度为13000mg/L,HRT为96h时,COD去除率可达到60%,BOD的去除率为94.4%。提高进水COD浓度(16000mg/L)或缩短水力停留时间(HRT=65h)时,COD的去除率下降,分别为51%和45%。当进水COD浓度为13000mg/L,HRT由96h降至80h时,BOD的去除率降至67%。HRT为96h时,系统出现污泥分层现象,N、P的绝对去除量之比约为1:1。缩短HRT至65h时,N、P的绝对去除量之比约为6:1。试验中进水、曝气柱出水和沉淀柱出水中SO42-浓度,其浓度分别为(7318±415)、(7414±184)、(7338±274)mg/L,方差分析表明三者SO42-浓度没有显著性差异(P>0.842),说明在本研究中并不存在硫酸盐还原作用,(3)臭氧处理结果表明:在臭氧投加量为0-198mg/L时,废水中BOD/COD出现上升(由0.22上升到0.29),继续增加臭氧投加量,BOD/COD下降。臭氧投加量为316mg/L时,COD去除率达到最大(29%),此时,土霉素的去除率为78%。臭氧投加量为806mg/L时,土霉素的去除率接近100%,此时色度去除率达到35.4%。COD的降解速率与土霉素的降解速率不同。
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外文摘要: |
Sulfate-ridden high-strength fermentative industrial wastewater is treated difficultly. This paper attempts to treat the high-sulfur antibiotic wastewater by bacteria, take micro-aerobic (DO=0-0.5mg/L) operating conditions, and discussion on the effect biological treatment of antibiotic wastewater. A lab-scale continuous experiment was designed to investigate the effect of various influent COD Concentrations(13000、16000 mg/L)or HRTs (96、80、65h) on the biological treatment performance of the high-sulfur antibiotic wastewater.The treatment effect of ozone reaction are discussed in the paper by different ozone dosages. The following results were obtained from the experiments:⑴ Batch experiments show oxygen supply had an important effect on bacteria growth and COD removal, DO levels ≤0.5 mg/L, the microorganism grew well while COD removals were 55%, however, without oxygen supply, there was almost no COD removal. ⑵ In the continuous running at low DO levels, it achieved a COD removal of 60%,BOD5 removal of approximately 94.4% in the influent at 96 h HRT and influent COD level of 13000 mg/L. Orange removal decreased when shorten HRT from 96h to 65h or improve the influent COD from 13000 to 16000 mg/L.The ratio between TN and TP removal is different from HRT 96h to 65h. The results show that reduction process of sulfate is not existed under the microaerobic condition.⑶ The obtained results show that the ozonization pretreatment technique can improve the biochemical treatment effect in the ozone dosages of 0-198mg/L.The result of BOD/COD decreased when increased ozone dosage. The highest COD removal is 29% in the ozone dosage of 316mg/L. Oxytetracycline removal is close to 100% in the ozone dosage of 806mg/L,and then color removal is 35.4%.
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参考文献总数: | 104 |
作者简介: | 2006年进入北京师范大学攻读硕士研究生。学习期间,在《环境科学与工程》发表《高硫抗生素废水微好氧处理研究》,申请国家发明专利一项“针对高浓度有机废水的酵母菌低氧SBR工艺”(专利号200510130317.8) |
馆藏号: | 硕083002/0911 |
开放日期: | 2009-06-18 |