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Author:

Li, X. (Li, X..) (Scholars:李星) | Peng, Y. (Peng, Y..) | He, Y. (He, Y..) | Ma, B. (Ma, B..) | Zhao, J. (Zhao, J..) (Scholars:赵京)

Indexed by:

Scopus PKU CSCD CSSCI

Abstract:

The effects of six feeding modes in treating anaerobic digester (AD) supernatant and domestic sewage were investigated using shortcut nitrification sequencing batch reactor (SBR) by anaerobic-aerobic-anoxic (AOA) processes. Batch experiments were incubated at 20.0℃ in domestic sewage-AD supernatant (24:1) media, and the ratio of ammonia oxidizing bacteria (AOB) was 7.34%. AD supernatant was injected at the beginning of the anaerobic or aerobic phase and dosed two or three times during the aerobic phase, hereafter referred to as SBR-a, SBR-b, SBR-c, SBR-d, SBR-e and SBR-f. Soluble chemical oxygen demand (SCODCr), PO43--P and NH4+-N concentrations were also determined in the present study. The results showed that adding AD supernatant had no effect on removal of organic matter at various feeding modes. However, removal of PO43--P was low when AD supernatant was treated in AOA-SBR combined with domestic sewage. In fact, phosphate loading rate (PLR) increased by 104.88%. Concentrations of PO43--P in the effluents were also higher than 2.0 mg/L in all experimental conditions, which could have been the limitation of the AOA-SBR system. Specific nitrite production rate (SNPR) in dosing AD supernatant was significantly higher than that of AOA-SBR, but only in the treatment of domestic sewage, which indicated that the addition of AD supernatant helped stabilize shortcut nitrification. Adding AD supernatant at the beginning of the anaerobic phase in AOA-SBR attained the best results, with increases in specific ammonia uptake rate (SAUR) (0.1680 g/(g·d)), SNPR (0.1363 g/(g·d)), and simultaneous nitrification denitrification (SND) rate to 26.64 %. © 2016, Editorial Department of Molecular Catalysis. All right reserved.

Keyword:

Anaerobic digester supernatant; Biological nitrogen removal; Domestic sewage; Sequencing batch reactor; Shortcut nitrification

Author Community:

  • [ 1 ] [Li, X.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, College of Environmental and Energy Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 2 ] [Peng, Y.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, College of Environmental and Energy Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 3 ] [He, Y.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, College of Environmental and Energy Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 4 ] [Ma, B.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, College of Environmental and Energy Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 5 ] [Zhao, J.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, College of Environmental and Energy Engineering, Beijing University of Technology, Beijing, 100124, China

Reprint Author's Address:

  • [Peng, Y.]Key Laboratory of Beijing for Water Quality Science and Water Environment Recovery Engineering, College of Environmental and Energy Engineering, Beijing University of TechnologyChina

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Source :

Research of Environmental Sciences

ISSN: 1001-6929

Year: 2016

Issue: 5

Volume: 29

Page: 746-752

Cited Count:

WoS CC Cited Count:

SCOPUS Cited Count:

ESI Highly Cited Papers on the List: 0 Unfold All

WanFang Cited Count:

Chinese Cited Count:

30 Days PV: 0

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