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  4. Fine-tuning key parameters of an integrated reactor system for the simultaneous removal of COD, sulfate and ammonium and elemental sulfur reclamation
 
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Fine-tuning key parameters of an integrated reactor system for the simultaneous removal of COD, sulfate and ammonium and elemental sulfur reclamation

Journal
Journal of Hazardous Materials
Journal Volume
269
Pages
56-67
Date Issued
2014
Author(s)
Yuan Y.
Chen C.
Liang B.
Huang C.
Zhao Y.
Xu X.
Tan W.
Zhou X.
Gao S.
Sun D.
Lee D.  
Zhou J.
Wang A.
DOI
10.1016/j.jhazmat.2013.12.014
URI
https://scholars.lib.ntu.edu.tw/handle/123456789/408445
URL
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84896545774&doi=10.1016%2fj.jhazmat.2013.12.014&partnerID=40&md5=ea25ff9bae28f09ffaabfdde1f5cac7c
Abstract
In this paper, we proposed an integrated reactor system for simultaneous removal of COD, sulfate and ammonium (integrated C-S-N removal system) and investigated the key parameters of the system for a high level of elemental sulfur (S0) production. The system consisted of 4 main units: sulfate reduction and organic carbon removal (SR-CR), autotrophic and heterotrophic denitrifying sulfide removal (A&H-DSR), sulfur reclamation (SR), and aerated filter for aerobic nitrification (AN). In the system, the effects of key operational parameters on production of elemental sulfur were investigated, including hydraulic retention time (HRT) of each unit, sulfide/nitrate (S2--S/NO3--N) ratios, reflux ratios between the A&H-DSR and AN units, and loading rates of chemical oxygen demand (COD), sulfate and ammonium. Physico-chemical characteristics of biosulfur were studied for acquiring efficient S0 recovery. The experiments successfully explored the optimum parameters for each unit and demonstrated 98% COD, 98% sulfate and 78% nitrogen removal efficiency. The optimum HRTs for SR-CR, A&H-DSR and AN were 12h, 3h and 3h, respectively. The reflux ratio of 3 could provide adequate S2--S/NO3--N ratio (approximately 1:1) to the A&H-DSR unit for obtaining maximum sulfur production. In this system, the maximum production of S0 reached 90%, but only 60% S0 was reclaimed from effluent. The S0 that adhered to the outer layer of granules was deposited in the bottom of the A&H-DSR unit. Finally, the microbial community structure of the corresponding unit at different operational stage were analyzed by 16S rRNA gene based high throughput Illumina MiSeq sequencing and the potential function of dominant species were discussed. ? 2013 Elsevier B.V.
Subjects
Aerated nitrification
Denitrifying sulfide removal
Elemental sulfur production
Sulfate reduction and organic carbon removal
Sulfur reclamation
Type
journal article

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