Mixed sulfur-iron particles packed reactor for simultaneous advanced removal of nitrogen and phosphorus from secondary effluent

被引:123
|
作者
Wang, Shenghui [1 ]
Liang, Peng [1 ]
Wu, Zhongqin
Su, Fengfeng
Yuan, Lulu
Sun, Yanmei
Wu, Qing
Huang, Xia [1 ]
机构
[1] Tsinghua Univ, Sch Environm, State Key Joint Lab Environm Simulat & Pollut Con, Beijing 100084, Peoples R China
关键词
Secondary effluent; Sulfur-based autotrophic denitrification; Chemical phosphorus precipitation; Sulfuriron particles; Microbial community; DENITRIFICANS GEN. NOV; WASTE-WATER TREATMENT; AUTOTROPHIC DENITRIFICATION; PHOSPHATE REMOVAL; NITRATE REMOVAL; ELEMENTAL-SULFUR; HETEROTROPHIC DENITRIFICATION; SULFATE REDUCTION; GROUNDWATER; BACTERIA;
D O I
10.1007/s11356-014-3370-1
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A mixed sulfur-iron particles packed reactor (SFe reactor) was developed to simultaneously remove total nitrogen (TN) and total phosphorus (TP) of the secondary effluent from municipal wastewater treatment plants. Low effluent TN (<1.5 mg/L) and TP (<0.3 mg/L) concentrations were simultaneously obtained, and high TN removal rate [1.03 g N/(L.d)] and TP removal rate [0.29 g P/(L.d)] were achieved at the hydraulic retention time (HRT) of 0.13 h. Kinetic models describing denitrification were experimentally obtained, which predicted a higher denitrification rate [1.98 g N/(L.d)] of SFe reactor than that [1.58 g N/(L.d)] of sulfur alone packed reactor due to the mutual enhancement between sulfur-based autotrophic denitrification and iron-based chemical denitrification. A high TP removal obtained in SFe reactor was attributed to chemical precipitation of iron particles. Microbial community analysis based on 16S rRNA revealed that autotrophic denitrifying bacteria Thiobacillus and Sulfuricella were the dominant genus, indicating that autotrophic denitrification played important role in nitrate removal. These results indicate that sulfur and iron particles can be packed together in a single reactor to effectively remove nitrate and phosphorus.
引用
收藏
页码:415 / 424
页数:10
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