Details
Original language | English |
---|---|
Pages (from-to) | 8-15 |
Number of pages | 8 |
Journal | Journal of Environmental Management |
Volume | 220 |
Early online date | 10 May 2018 |
Publication status | Published - 15 Aug 2018 |
Abstract
At an Austrian soft drink company, an expanded granular sludge bed reactor for anaerobic wastewater treatment was inoculated with sludge from paper and food industries. Detailed online monitoring and laboratory examinations were carried out during startup and subsequent phases, which included a period of inhibition after ca. 80 days during which reactor degradative performance diminished suddenly, following a period of increased effluent VFA. After dosing iron chloride (FeCl2) and micronutrients and reducing organic loading to startup levels, the reactor eventually reached efficient operation (>85% COD degradation) after a gradual recovery phase. In this work performance data both at lab and full scale are elaborated along startup, adaptation, pre-inhibition, recovery and stable phases, and correlated between scales. High rate anaerobic treatment of soft drink industry wastewater was successful in terms of COD removal efficiency and final effluent COD (∼300 mg l−1), with a startup period (including inhibition) of ca. 5 months.
Keywords
- EGSB reactor, Granular sludge, Methanogenic inhibition, Re-commissioning, Reactor startup
ASJC Scopus subject areas
- Environmental Science(all)
- Environmental Engineering
- Environmental Science(all)
- Waste Management and Disposal
- Environmental Science(all)
- Management, Monitoring, Policy and Law
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In: Journal of Environmental Management, Vol. 220, 15.08.2018, p. 8-15.
Research output: Contribution to journal › Article › Research › peer review
}
TY - JOUR
T1 - High-rate anaerobic treatment of wastewater from soft drink industry
T2 - Methods, performance and experiences
AU - Cuff, Graham
AU - Turcios, Ariel E.
AU - Mohammad-pajooh, Ehsan
AU - Kujawski, Olaf
AU - Weichgrebe, Dirk
AU - Rosenwinkel, Karl Heinz
N1 - © 2018 Elsevier Ltd. All rights reserved.
PY - 2018/8/15
Y1 - 2018/8/15
N2 - At an Austrian soft drink company, an expanded granular sludge bed reactor for anaerobic wastewater treatment was inoculated with sludge from paper and food industries. Detailed online monitoring and laboratory examinations were carried out during startup and subsequent phases, which included a period of inhibition after ca. 80 days during which reactor degradative performance diminished suddenly, following a period of increased effluent VFA. After dosing iron chloride (FeCl2) and micronutrients and reducing organic loading to startup levels, the reactor eventually reached efficient operation (>85% COD degradation) after a gradual recovery phase. In this work performance data both at lab and full scale are elaborated along startup, adaptation, pre-inhibition, recovery and stable phases, and correlated between scales. High rate anaerobic treatment of soft drink industry wastewater was successful in terms of COD removal efficiency and final effluent COD (∼300 mg l−1), with a startup period (including inhibition) of ca. 5 months.
AB - At an Austrian soft drink company, an expanded granular sludge bed reactor for anaerobic wastewater treatment was inoculated with sludge from paper and food industries. Detailed online monitoring and laboratory examinations were carried out during startup and subsequent phases, which included a period of inhibition after ca. 80 days during which reactor degradative performance diminished suddenly, following a period of increased effluent VFA. After dosing iron chloride (FeCl2) and micronutrients and reducing organic loading to startup levels, the reactor eventually reached efficient operation (>85% COD degradation) after a gradual recovery phase. In this work performance data both at lab and full scale are elaborated along startup, adaptation, pre-inhibition, recovery and stable phases, and correlated between scales. High rate anaerobic treatment of soft drink industry wastewater was successful in terms of COD removal efficiency and final effluent COD (∼300 mg l−1), with a startup period (including inhibition) of ca. 5 months.
KW - EGSB reactor
KW - Granular sludge
KW - Methanogenic inhibition
KW - Re-commissioning
KW - Reactor startup
UR - http://www.scopus.com/inward/record.url?scp=85046706816&partnerID=8YFLogxK
U2 - 10.1016/j.jenvman.2018.05.015
DO - 10.1016/j.jenvman.2018.05.015
M3 - Article
C2 - 29753988
AN - SCOPUS:85046706816
VL - 220
SP - 8
EP - 15
JO - Journal of Environmental Management
JF - Journal of Environmental Management
SN - 0301-4797
ER -