进水成分变动下ABR-CASS耦合工艺处理制药综合废水的中试研究

廖苗; 樊亚东; 刘诗月; 魏健; 刘洋; 曾萍

doi:10.3969/j.issn.1674-991X.2017.03.042

进水成分变动下ABR-CASS耦合工艺处理制药综合废水的中试研究

doi: 10.3969/j.issn.1674-991X.2017.03.042

廖苗¹,
樊亚东^1,2,
刘诗月^1,3,
魏健¹,
刘洋²,
曾萍¹

^1. 中国环境科学研究院城市水环境科技创新基地,北京 100012
^2. 阿尔伯特大学土木与环境工程系,加拿大阿尔伯特 7-263
^3. 中国地质大学(北京)水资源与环境学院,北京 100083

详细信息

作者简介:
廖苗(1990—),男,硕士研究生,主要研究方向为工业废水污染控制,liaomiao1990 @163.com

中图分类号: X703
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- 被引次数: 0
出版历程
- 收稿日期: 2017-02-03
- 刊出日期: 2017-05-20

Pilot-scale treatment of pharmaceutical comprehensive wastewater by ABR-CASS fed with different batches of influent

^1. Research Institute of Urban Water Environment, Chinese Research Academy of Environmental Sciences, Beijing 100012, China
^2. Department of Civil and Environmental Engineering, University of Alberta, Edmonton, Alberta 7-263, Canada
^3. School of Water Resources and Environment, China University of Geosciences, Beijing 100083, China

摘要

摘要: 采用ABR-CASS耦合工艺在中试反应器中处理某制药厂3批制药综合废水。针对不同进水,ABR和CASS反应器表现出了不同的处理能力。其中,不同成分的3批进水对ABR反应器运行影响不明显。在处理第1批进水的ABR出水时,CASS能够在污泥负荷为0.012 kg/(kg·d)(以MLSS计,全文同)时稳定运行,整个系统对COD的去除率达92.54%,对NH₃-N的去除率达95.77%;而在处理第3批进水的ABR出水时,CASS反应器几乎不能耐受该废水。GC-MS的测定结果表明,与第1批进水相比,第3批进水的ABR出水中存在具有毒性的三正丁胺和对甲基苯酚,可能是造成CASS反应器生物系统崩溃的主要原因。为保证ABR-CASS的稳定运行,需重点考察ABR对原水中关键毒害物的去除能力,从而为CASS提供合适的进水条件。
- 制药废水 /
- ABR-CASS /
- 中试 /
- 进水成分 /
- 毒害物
Abstract: A pilot-scale anaerobic baffled reactor-cyclic activated sludge system (ABR-CASS) reactor was employed to treat three batches of pharmaceutical wastewater from the same pharmaceutical factory. ABR and CASS showed different treatment capabilities to the wastewater. The ABR was almost hardly affected by the components from different batches of pharmaceutical wastewater. However, the influence to CASS was great. CASS could run stably with sludge loading of 0.012 kg COD/(kg MLSS·d) when fed with the first batch of ABR effluent. For the whole system, the overall efficiencies of COD and NH₃-N were 92.54% and 95.77%, separately. However, CASS could not endure the wastewater when fed with the third batch of ABR effluent. GC-MS analysis showed that the toxic compounds of tributylamine and p-methyl phenol from the third batch of ABR effluent might be the main factors caused the crash of CASS. To guarantee stable operation of the whole ABR-CASS system, the elimination capability of ABR on influent key toxic compounds should be concerned to provide suitable influence for CASS operation.
- pharmaceutical wastewater /
- ABR-CASS /
- pilot-scale experiment /
- influent components /
- toxic compounds

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参考文献(36)

[1]	BROOKS B W, TUMER P K, STANLEY J K , et al. Waterborne and sediment toxicity of fluoxetine to select organisms[J]. Chemosphere, 2003,52(1):135-142.
[2]	van der VEN K, KEIL D, MOENS L N , et al. Effects of the antidepressant mianserin in zebrafish:molecular markers of endocrine disruption[J]. Chemosphere, 2006,65(10):1836-1845.
[3]	ESCHER B I, BRAMAZ N, RICHTER M , et al. Comparative ecotoxicological hazard assessment of beta-blockers and their human metabolites using a mode-of-action-based test battery and a QSAR approach[J]. Environmental Science & Technology, 2006,40(23):7402-7408.
[4]	FEMANDEZ C, CARBONELL G, BABIN M . Effects of individual and a mixture of pharmaceuticals and personal-care products on cytotoxicity,EROD activity and ROS production in a rainbow trout gonadal cell line (RTG-2)[J]. Journal of Applied Toxicology, 2013,33(11):1203-1212.
[5]	SHEN R, ANDREWS S A . Demonstration of 20 pharmaceuticals and personal care products (PPCPs) as nitrosamine precursors during chloramine disinfection[J]. Water Research, 2011,45(2):944-952.
[6]	MUNOZ I, GOMEZ M J, MOLINA-DIAZ A , et al. Ranking potential impacts of priority and emerging pollutants in urban wastewater through life cycle impact assessment[J]. Chemosphere, 2008,74(1):37-44.
[7]	TEMES T A, JOSS A, SIEGRIST H . Scrutinizing pharmaceuticals and personal care products in wastewater treatment[J]. Environmental Science & Technology, 2004,38(20):392A-399A.
[8]	CALDWELL D J, MERTENS B, KAPPLER K , et al. A risk-based approach to managing active pharmaceutical ingredients in manufacturing effluent[J]. Environmental Toxicology and Chemistry, 2016,35(4):813-822.
[9]	WANG J L, MAO D Q, MU Q H , et al. Fate and proliferation of typical antibiotic resistance genes in five full-scale pharmaceutical wastewater treatment plants[J]. Science of the Total Environment, 2015,526:366-373.
[10]	SUBEDI B, KANNAN K . Occurrence and fate of select psychoactive pharmaceuticals and antihypertensives in two wastewater treatment plants in New York State, USA[J]. Science of the Total Environment, 2015,514:273-280.
[11]	JEWELL K S, CASTRONOVO S, WICK A , et al. New insights into the transformation of trimethoprim during biological wastewater treatment[J]. Water Research, 2016,88:550-557.
[12]	BINELLI A, MAGNI S, SOAVE C , et al. The biofiltration process by the bivalve D.polymorpha for the removal of some pharmaceuticals and drugs of abuse from civil wastewaters[J]. Ecological Engineering, 2014,71:710-721.
[13]	LEE C O, HOWE K J, THOMSON B M . Ozone and biofiltration as an alternative to reverse osmosis for removing PPCPs and micropollutants from treated wastewater[J]. Water Research, 2012,46(4):1005-1014.
[14]	YU Z, PELDSZUS S, HUCK P M . Adsorption characteristics of selected pharmaceuticals and an endocrine disrupting compound-naproxen, carbamazepine and nonylphenol-on activated carbon[J]. Water Research, 2008,42(12):2873-2882.
[15]	SNYDER S A, ADHAM S, REDDING A M , et al. Role of membranes and activated carbon in the removal of endocrine disruptors and pharmaceuticals[J]. Desalination, 2007,202(1/2/3):156-181.
[16]	聂超, 刘树模, 马伟芳 , 等. Fenton氧化-混凝法预处理噻烷/噻唑制药废水的研究[J]. 环境工程, 2015,33(增刊):39-42. NIE C, LIU S M, MA W F , et al. Research on pretreatment by Fenton and coagulation for 2,5-dihydroxy-dithiane/2-5-nitro-thiazole pharmaceutical wastewater[J]. Environmental Engineering, 2015,33(Suppl):39-42.
[17]	孔明昊 . 臭氧催化氧化深度处理制药园区尾水技术研究[D]. 北京:中国环境科学研究院, 2016.
[18]	TU X, XIAO S H, SONG Y H , et al. Treatment of simulated berberine wastewater by electrochemical process with Pt/Ti anode[J]. Environmental Earth Sciences, 2015,73(9):4957-4966.
[19]	TEMES T A, STUBER J, HERRMANN N , et al. Ozonation:a tool for removal of pharmaceuticals, contrast media and musk fragrances from wastewater[J]. Water Research, 2003,37(8):1976-1982.
[20]	KIM I H, TANAKA H, IWASAKI T , et al. Classification of the degradability of 30 pharmaceuticals in water with ozone, UV and H₂O₂[J]. Water Science and Technology, 2008,57(2):195-200.
[21]	BADAWY M I, WAHAAB R A, EL-KALLINY A S . Fenton-biological treatment processes for the removal of some pharmaceuticals from industrial wastewater[J]. Journal of Hazardous Materials, 2009,167(1/2/3):567-574.
[22]	ZHU L, LÜ M L, DAI X , et al. The stability of aerobic granular sludge under 4-chloroaniline shock in a sequential air-lift bioreactor (SABR)[J]. Bioresource Technology, 2013,140:126-130.
[23]	MORALES G, PESANTE S, VIDAL G . Effects of black liquor shocks on activated sludge treatment of bleached kraft pulp mill wastewater[J]. Journal of Environmental Science and Health Part A Toxic/Hazardous Substances & Environmental Engineering, 2015,50(6):639-645.
[24]	SANDBERG M . Mill case,simulation,and laboratory plant study of black liquor spill effects on a multiple stage biological treatment plant[J]. Canadian Journal of Earth Sciences, 2009,36(5):839-849.
[25]	YANG Q, SHANG H T, WANG J L . Treatment of municipal wastewater by membrane bioreactor:a pilot study[J]. International Journal of Environment and Pollution, 2009,38(3):280-288.
[26]	MEYER T, EDWARDS E A . Anaerobic digestion of pulp and paper mill wastewater and sludge[J]. Water Research, 2014,65:321-349.
[27]	HUANG M H, LI Y M, GU G W . Toxicity reduction of municipal wastewater by anaerobic-anoxic-oxic process[J]. Biomedical and Environmental Sciences, 2010,23(6):481-486.
[28]	GHANIYARI-BENIS S, BORIA R, MONEMIAN S A , et al. Anaerobic treatment of synthetic medium-strength wastewater using a multistage biofilm reactor[J]. Bioresource Technology, 2009,100(5):1740-1745.
[29]	KETHEESAN B, STUCKEY D C . Effects of hydraulic/organic shock/transient loads in anaerobic wastewater treatment: a review[J]. Critical Reviews in Environmental Science and Technology, 2015,45(24):2693-2727.
[30]	BARBER W P, STUCKEY D C . The use of the anaerobic baffled reactor (ABR) for wastewater treatment:a review[J]. Water Research, 1999,33(7):1559-1578.
[31]	沈耀良, 王宝贞 . 循环活性污泥系统CASS处理城市生活废水[J]. 给水排水, 1999,25(11):5-8.
[32]	USEPA. Pollution prevention and toxic[DB/OL]. [2017-02-10]. http://java.epa.gov/chemview.
[33]	化工词典[EB/OL]. [2017-02-20]. http://cheman.chemnet.com/dict/zd.html.
[34]	WANG Y Y, ZHANG Z X, YAN M , et al. Impact of operating conditions on nitrogen removal using cyclic activated sludge technology (CAST)[J]. Journal of Environmental Science and Health: Part A. Toxic/Hazardous Substances & Environmental Engineering, 2010,45(3):370-376.
[35]	LUO W W, JIN X B, YU Y L , et al. Efficient nitrogen removal via simultaneous nitrification and denitrification in a penicillin wastewater biological treatment plant[J]. Environmental Technology, 2014,35(21/22/23/24):2885-2893.
[36]	CHEN Z B, WANG H C, REN N Q , et al. Simultaneous removal and evaluation of organic substrates and NH₃-N by a novel combined process in treating chemical synjournal-based pharmaceutical wastewater[J]. Journal of Hazardous Materials, 2011,197:49-59.