A novel approach to realize SANI process in freshwater sewage treatment - Use of wet flue gas desulfurization waste streams as sulfur source

被引:81
作者
Jiang, Feng [1 ,2 ]
Zhang, Liang [4 ]
Peng, Guo-Liang [1 ]
Liang, Si-Yun [1 ]
Qian, Jin [3 ]
Wei, Li [3 ]
Chen, Guang-Hao [3 ,4 ,5 ]
机构
[1] S China Normal Univ, Sch Chem & Environm, Guangzhou, Guangdong, Peoples R China
[2] Guangdong Prov Key Lab Environm Pollut Control &, Guangzhou, Guangdong, Peoples R China
[3] Hong Kong Univ Sci & Technol, Dept Civil & Environm Engn, Kowloon, Hong Kong, Peoples R China
[4] Sun Yat Sen Univ, SYSU HKUST Res Ctr Innovat Environm Technol, Guangzhou 510275, Guangdong, Peoples R China
[5] Hong Kong Univ Sci & Technol, Adv Water Res & Technol Ctr, FYT Grad Sch, Guangzhou, Guangdong, Peoples R China
基金
中国国家自然科学基金;
关键词
Sludge-minimized sewage treatment process; SANI process; Flue gas desulfurization; Sulfite reduction; Temperature effect; AUTOTROPHIC DENITRIFICATION; SULFATE REDUCTION; NITROGEN REMOVAL; ISOTOPE FRACTIONATION; SLUDGE MINIMIZATION; NITRIFICATION; INTEGRATION; BIOREACTOR; DIOXIDE; SYSTEM;
D O I
10.1016/j.watres.2013.06.051
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
SANI (Sulfate reduction, Autotrophic denitrification and Nitrification Integrated) process has been approved to be a sludge-minimized sewage treatment process in warm and coastal cities with seawater supply. In order to apply this sulfur-based process in inland cold areas, wet flue gas desulfurization (FGD) can be simplified and integrated with SANI process, to provide sulfite as electron carrier for sulfur cycle in sewage treatment. In this study, a lab-scale system of the proposed novel process was developed and run for over 200 days while temperature varied between 30 and 5 degrees C, fed with synthetic FGD wastewaters and sewage. The sulfite-reducing upflow anaerobic sludge bed (SrUASB) reactor, as the major bioreactor of the system, removed 86.9% of organics while the whole system removed 94% of organics even when water temperature decreased to around 10 degrees C. The bactericidal effect of sulfite was not observed in the SrUASB reactor, while thiosulfate was found accumulated under psychrophilic conditions. The sludge yield of the SrUASB reactor was determined to be 0.095 kg VSS/kg COD, higher than of sulfate reduction process but still much lower than of conventional activated sludge processes. The dominant microbes in the SrUASB reactor were determined as Lactococcus spp. rather than sulfate-reducing bacteria, but sulfite reduction still contributed 85.5% to the organic carbon mineralization in this reactor. Ammonia and nitrate were effectively removed in the aerobic and anoxic filters, respectively. This study confirms the proposed process was promising to achieve sludge-minimized sewage treatment integrating with flue gas desulfurization in inland and cold areas. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:5773 / 5782
页数:10
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