水远敏2,
万佩佩2,
李伟成3,
高迎新3,
戚伟康4,,
1.华航环境发展有限公司,北京 100071
2.达斯玛环境科技股份有限公司,北京 100089
3.中国科学院生态环境研究中心,环境水质学国家重点实验室,北京 100085
4.北京工业大学,城镇污水深度处理与资源化利用技术国家工程实验室,北京 100124
作者简介: 郭进(1982—),女,硕士,工程师。研究方向:水污染控制。E-mail:piero98@sohu.com.
通讯作者: 戚伟康,qiweikang10@163.com
中图分类号: X703
Enhanced SMD process in treating organic sulfur compounds and para-ester manufacturing wastewater by micro-electric field-ZVI-UBF
GUO Jin1,,SHUI Yuanmin2,
WAN Peipei2,
LI Weicheng3,
GAO Yingxin3,
QI Weikang4,,
1.Huahang Environmental Developed Co. Ltd., Beijing 100071, China
2.Dasmart Environmental Science and Technologies Co. Ltd., Beijing 100089, China
3.State Key Laboratory of Environmental Aquatic Chemistry, Research Center for Eco-Environmental Sciences, Chinese Academy of Science, Beijing 100085, China
4.National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Beijing University of Technology, Beijing 100124, China
Corresponding author: QI Weikang,qiweikang10@163.com
CLC number: X703
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摘要:有机硫化合物对位酯生产废水具有COD高、含硫酸盐和有机硫高以及碳硫比低的特点,针对单一厌氧反应器在处理废水时只能在较低COD容积负荷(OLR)下运行的问题,在提高有机硫对位脂生产废水产甲烷反硝化效能的基础上,采用微电场-零价铁联合方式处理该类废水。实验结果表明:OLR(以COD计)为6.67 g·(L·d)?1,进水COD为20 000 mg·L?1时,复合床的COD去除率为70%,产甲烷率为1.41 L·(L·d)?1,反硝化率为87%,对位脂降解率为74%;在COD/
关键词: 微电场-零价铁-UBF/
有机硫化合物/
对位脂生产废水/
COD/$ {\rm{TSO}}_4^{2 - } $/
同步产甲烷反硝化
Abstract:Organic sulfur(s) compounds and para-ester manufacturing wastewater was characterized as high COD, rich sulfate and organic S compounds and low C/S ratio. Single anaerobic reactor treating this kind of wastewater can only run at low COD loading rate (OLR), then the micro-electric field - zero-valent-iron (ZVI) joint system was used to treat it based on the enhancing effect of methanogenesis and denitrification from organic S compounds and para-ester manufacturing wastewater. The experimental result indicated that the compound bed could remove 70% of COD, achieve 1.41 L·(L·d)?1 of methane production rate, 87% of denitrification efficiency and 74% para-ester degradation efficiency at COD organic load rating (OLR) up to 6.67 g·(L·d)?1 and influent COD of 20 000 mg·L?1. At COD/
Key words:micro-electric field-zero-valent-iron (ZVI)-UBF/
organic sulfur compound/
para-ester manufacturing wastewater/
COD/$ {\rm{TSO}}_4^{2 - } $ ratio/
simultaneous methanogenesis and denitrification process.
图1对位酯的化学结构式
Figure1.Chemical structure of para-ester
下载: 全尺寸图片幻灯片
图2微电场-零价铁-UBF实验工艺流程
Figure2.Schematic diagram of the Micro-electric field- zero-valent-iron (ZVI)-UBF
下载: 全尺寸图片幻灯片
图3电场-零价铁-UFB在160 d的连续运行结果
Figure3.Performance of micro-electric field- zero-valent-iron UBF during continuous operation within 160 d
下载: 全尺寸图片幻灯片
图4UBF运行中对位酯进出水浓度
Figure4.Influent and effluent of para-ester concentration during UBF continuous operation
下载: 全尺寸图片幻灯片
图5UBF运行中进出水硝态氮的浓度
Figure5.Influent and effluent of nitrate concentration during UBF continuous operation
下载: 全尺寸图片幻灯片
图6UBF运行中进出水硫酸盐浓度的变化
Figure6.Changes in sulfate concentrations in influent and effluent during UBF continuous operation
下载: 全尺寸图片幻灯片
图7UBF运行中出水硫化物的变化
Figure7.Change of sulfide concentration in effluent during UBF continuous operation
下载: 全尺寸图片幻灯片
表1微电场-零价铁-UFB各个运行阶段的废水成分及COD容积负荷
Table1.Water quality parameters and COD volume load of wastewater inmicro-electric field-ZVI-UBF at different stages
阶段 | 时间/d | COD/ (mg·L?1) | 对位酯/ (mg·L?1) | 硫酸盐/ (mg·L?1) | 有机硫(以 (mg·L?1) | 硝态氮/ (mg·L?1) | OLR/ (g·(L·d)?1) |
Ⅰ | 1~30 | 500 | 100 | 223 | 68.4 | 1.1 | 0.167 |
Ⅰ | 31~45 | 2 000 | 400 | 558 | 273.6 | 4.4 | 0.668 |
Ⅰ | 46~60 | 5 000 | 1 000 | 1 395 | 684 | 11 | 1.67 |
Ⅰ | 61~75 | 10 000 | 2 000 | 2 790 | 1 368 | 22 | 3.34 |
Ⅰ | 76~90 | 15 000 | 3 000 | 4 185 | 2 052 | 33 | 5.01 |
Ⅰ | 91~105 | 20 000 | 4 000 | 5 580 | 2 736 | 44 | 6.68 |
Ⅱ | 106~125 | 20 000 | 4 000 | 10 000 | 2 736 | 44 | 5.01 |
Ⅲ | 126~140 | 20 000 | 4 000 | 20 000 | 2 736 | 44 | 5.01 |
Ⅳ | 141~160 | 20 000 | 4 000 | 10 000 | 2 736 | 44 | 5.01 |
阶段 | 时间/d | COD/ (mg·L?1) | 对位酯/ (mg·L?1) | 硫酸盐/ (mg·L?1) | 有机硫(以 (mg·L?1) | 硝态氮/ (mg·L?1) | OLR/ (g·(L·d)?1) |
Ⅰ | 1~30 | 500 | 100 | 223 | 68.4 | 1.1 | 0.167 |
Ⅰ | 31~45 | 2 000 | 400 | 558 | 273.6 | 4.4 | 0.668 |
Ⅰ | 46~60 | 5 000 | 1 000 | 1 395 | 684 | 11 | 1.67 |
Ⅰ | 61~75 | 10 000 | 2 000 | 2 790 | 1 368 | 22 | 3.34 |
Ⅰ | 76~90 | 15 000 | 3 000 | 4 185 | 2 052 | 33 | 5.01 |
Ⅰ | 91~105 | 20 000 | 4 000 | 5 580 | 2 736 | 44 | 6.68 |
Ⅱ | 106~125 | 20 000 | 4 000 | 10 000 | 2 736 | 44 | 5.01 |
Ⅲ | 126~140 | 20 000 | 4 000 | 20 000 | 2 736 | 44 | 5.01 |
Ⅳ | 141~160 | 20 000 | 4 000 | 10 000 | 2 736 | 44 | 5.01 |
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[1] | 田勇, 刘传玉, 胡永玲, 等. 对位酯的合成技术与生产现状[J]. 化学与粘合, 2011, 33(1): 63-66. doi: 10.3969/j.issn.1001-0017.2011.01.019 |
[2] | 梁诚. 我国染料中间体生产现状与发展趋势[J]. 江苏化工, 2000, 28(Z1): 5-11. |
[3] | 张天永, 夏文娟, 池立峰, 等. 对位酯废水的光催化降解研究[J]. 环境工程学报, 2008, 2(2): 185-188. |
[4] | 徐颖, 陈磊, 周俊晓. Fenton氧化-生化组合工艺处理染料中间体废水[J]. 环境工程学报, 2007, 1(4): 57-60. doi: 10.3969/j.issn.1673-9108.2007.04.013 |
[5] | VAVILIN V A, VASILIEV V B, RYTOV S V, et al. Self-oscillating coexistence of methanogens and sulphate-reducers under hydrogen sulfide inhibition and the pH-regulating effect[J]. Bioresource Technology, 1994, 49(2): 105-119. doi: 10.1016/0960-8524(94)90074-4 |
[6] | 单明娥, 李志良, 李伟成, 等. 厌氧复合床处理有机硫染料中间体-对位脂生产废水[J]. 广州化工, 2017, 45(22): 119-120. |
[7] | 郑伟, 闵长春, 谭春伟. 反相离子抑制色谱法分离对位酯[J]. 化工科技, 2002, 10(4): 34-36. doi: 10.3969/j.issn.1008-0511.2002.04.010 |
[8] | ZHANG Y B, JING Y W, QUAN X, et al. A built-in zero anaerobic reactor to enhance treatment of azo dye wastewater[J]. Water Science and Technology, 2011, 63(4): 741-746. doi: 10.2166/wst.2011.301 |
[9] | ZHANG Y B, LIU Y W, JING Y W, et al. Steady performance of a zero valent iron packed anaerobic reactor for azo dye wastewater treatment under variable influent quality[J]. Journal of Environmental Sciences, 2012, 24(4): 720-727. doi: 10.1016/S1001-0742(11)60803-6 |
[10] | SRILAKSHMI K, REYES S A, JIM A F. Zero valent iron as an electron-donor for methanogenesis and eulfate reduction in anaerobic sludge[J]. Biotechnology and Bioengineering, 2005, 92: 810-819. doi: 10.1002/bit.20623 |
[11] | ZHANG Y B, JING Y W, QUAN X, et al. Performance of a ZVI-UASB reactor for azo dye wastewater treatment[J]. Journal of Chemical Technology and Biotechnology, 2011, 86(2): 199-204. doi: 10.1002/jctb.2485 |
[12] | 孙国鹏, 包南, 黄理辉, 等. 外电场促进生物厌氧与铁床耦合降解活性艳蓝研究[J]. 水处理技术, 2010, 36(12): 42-46. |
[13] | 张鑫, 朱南文, 楼紫阳, 等. 垃圾渗透液的零价铁强化厌氧处理技术[J]. 净水技术, 2013, 32(4): 51-55. doi: 10.3969/j.issn.1009-0177.2013.04.011 |
[14] | DU PREEZ L A, ODENDAAL J P, MAREE J P, et al. Biological removal of sulphate from industrial effluents using producer gas as energy source[J]. Environmental Technology, 1992, 13(9): 875-882. doi: 10.1080/09593339209385222 |
[15] | LI W C, NIU Q G, WU J, et al. Enhanced anaerobic performance and SMD process in treatment of sulfate and organic S-rich TMBA manufacturing wastewater by micro-electric field-zero valent iron-UASB[J]. Journal of Hazardous Materials, 2019, 379(5): 1-8. |
[16] | 刘杏, 刘志刚, 马鲁铭. 催化铁-厌氧微生物耦合技术还原硫酸根的研究[J]. 水处理技术, 2012, 38(5): 70-73. doi: 10.3969/j.issn.1000-3770.2012.05.018 |
[17] | HU Y, JING Z Q, SUDO Y, et al. Effect of influent COD/ |
[18] | 高大文, 彭永臻, 郑庆柱. SBR工艺中短程硝化反硝化的过程控制[J]. 中国给水排水, 2002, 11(18): 13-18. |
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收稿日期:2019-10-19
录用日期:2020-02-17
网络出版日期:2020-08-12
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微电场-零价铁-UBF提高有机硫对位酯生产废水同步产甲烷反硝化效能
郭进1,,水远敏2,
万佩佩2,
李伟成3,
高迎新3,
戚伟康4,,
通讯作者: 戚伟康,qiweikang10@163.com
作者简介: 郭进(1982—),女,硕士,工程师。研究方向:水污染控制。E-mail:piero98@sohu.com 1.华航环境发展有限公司,北京 100071
2.达斯玛环境科技股份有限公司,北京 100089
3.中国科学院生态环境研究中心,环境水质学国家重点实验室,北京 100085
4.北京工业大学,城镇污水深度处理与资源化利用技术国家工程实验室,北京 100124
收稿日期: 2019-10-19
录用日期: 2020-02-17
网络出版日期: 2020-08-12
关键词: 微电场-零价铁-UBF/
有机硫化合物/
对位脂生产废水/
COD/$ {\rm{TSO}}_4^{2 - } $/
同步产甲烷反硝化
摘要:有机硫化合物对位酯生产废水具有COD高、含硫酸盐和有机硫高以及碳硫比低的特点,针对单一厌氧反应器在处理废水时只能在较低COD容积负荷(OLR)下运行的问题,在提高有机硫对位脂生产废水产甲烷反硝化效能的基础上,采用微电场-零价铁联合方式处理该类废水。实验结果表明:OLR(以COD计)为6.67 g·(L·d)?1,进水COD为20 000 mg·L?1时,复合床的COD去除率为70%,产甲烷率为1.41 L·(L·d)?1,反硝化率为87%,对位脂降解率为74%;在COD/$ {\rm{TSO}}_4^{2 - } $ (总硫酸盐)为1.57时,COD去除率、产甲烷率和反硝化率可分别能稳定在60%、1.18 L·(L·d)?1和79%;在COD/$ {\rm{TSO}}_4^{2 - } $ 为0.88时,产甲烷菌受到中等程度的抑制;当COD/$ {\rm{TSO}}_4^{2 - } $ 恢复为1.57时,厌氧系统在7 d后恢复,说明联合系统有很强的恢复能力。综合上述结果,与单一的UBF处理相比,采用微电场-零价铁能显著提高UBF的运行负荷和同步产甲烷反硝化能力,同时也能使反应器承受更低的碳硫比。
English Abstract
Enhanced SMD process in treating organic sulfur compounds and para-ester manufacturing wastewater by micro-electric field-ZVI-UBF
GUO Jin1,,SHUI Yuanmin2,
WAN Peipei2,
LI Weicheng3,
GAO Yingxin3,
QI Weikang4,,
Corresponding author: QI Weikang,qiweikang10@163.com
1.Huahang Environmental Developed Co. Ltd., Beijing 100071, China2.Dasmart Environmental Science and Technologies Co. Ltd., Beijing 100089, China
3.State Key Laboratory of Environmental Aquatic Chemistry, Research Center for Eco-Environmental Sciences, Chinese Academy of Science, Beijing 100085, China
4.National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Beijing University of Technology, Beijing 100124, China
Received Date: 2019-10-19
Accepted Date: 2020-02-17
Available Online: 2020-08-12
Keywords: micro-electric field-zero-valent-iron (ZVI)-UBF/
organic sulfur compound/
para-ester manufacturing wastewater/
COD/$ {\rm{TSO}}_4^{2 - } $ ratio/
simultaneous methanogenesis and denitrification process
Abstract:Organic sulfur(s) compounds and para-ester manufacturing wastewater was characterized as high COD, rich sulfate and organic S compounds and low C/S ratio. Single anaerobic reactor treating this kind of wastewater can only run at low COD loading rate (OLR), then the micro-electric field - zero-valent-iron (ZVI) joint system was used to treat it based on the enhancing effect of methanogenesis and denitrification from organic S compounds and para-ester manufacturing wastewater. The experimental result indicated that the compound bed could remove 70% of COD, achieve 1.41 L·(L·d)?1 of methane production rate, 87% of denitrification efficiency and 74% para-ester degradation efficiency at COD organic load rating (OLR) up to 6.67 g·(L·d)?1 and influent COD of 20 000 mg·L?1. At COD/