Application of a compact trickle-bed bioreactor for the removal of odor and volatile organic compounds emitted from a wastewater treatment plant
A compact trickle-bed bioreactor (CTBB) was tested for the removal of volatile organic compounds (VOCs) and hydrogen sulphide (H 2 S) present in the exhaust air of a wastewater treatment plant. At gas-flow rates varying between 2.0 and 30.0 m 3 /h and for specific pollutant loads up to 20 g/(m 3 ·h)...
- Autores:
-
Kasperczyk, Damian
Urbaniec, Krzysztof
Barbusinski, Krzysztof
Rene, Eldon
Colmenares Quintero, Ramón Fernando
- Tipo de recurso:
- Article of journal
- Fecha de publicación:
- 2023
- Institución:
- Universidad Cooperativa de Colombia
- Repositorio:
- Repositorio UCC
- Idioma:
- OAI Identifier:
- oai:repository.ucc.edu.co:20.500.12494/50631
- Acceso en línea:
- https://doi.org/https://doi.org/10.1016/j.jenvman.2019.01.106
https://www.sciencedirect.com/science/article/pii/S0301479719301215?via%3Dihub
https://hdl.handle.net/20.500.12494/50631
- Palabra clave:
- AIR POLLUTANT
ARTICLE
BIODEGRADATION
BIOREACTOR
BIOREACTORS
CONCENTRATION (COMPOSITION)
CONCENTRATION (PARAMETER)
EFFICIENCY MEASUREMENT
EXHAUST GAS
FLOW RATE
FRAGRANCE
GAS FLOW
HYDROGEN SULFIDE
MICROBIAL ACTIVITY
NONHUMAN
ODOR
ODOR CONTROL
ODORANTS
POLLUTANT REMOVAL
PSEUDOMONAS FLUORESCENS
THIOBACILLUS
THIOL DERIVATIVE
VOLATILE ORGANIC COMPOUND
VOLATILE ORGANIC COMPOUNDS
WASTE WATER
WASTE WATER MANAGEMENT
WASTE WATER TREATMENT PLANT
WASTEWATER TREATMENT PLANT
- Rights
- openAccess
- License
- http://purl.org/coar/access_right/c_abf2
Summary: | A compact trickle-bed bioreactor (CTBB) was tested for the removal of volatile organic compounds (VOCs) and hydrogen sulphide (H 2 S) present in the exhaust air of a wastewater treatment plant. At gas-flow rates varying between 2.0 and 30.0 m 3 /h and for specific pollutant loads up to 20 g/(m 3 ·h), removal efficiencies for H 2 S and VOC were >95%. The CTBB was designed for a maximum H 2 S concentration of ~200 ppm and removal efficiencies >97% were noticed. VOC concentrations were in the range of 25–240 ppm v and the removal efficiency was in the range of 85–99%. Possible consequences of an excessive pollutant overload and the time required for regenerating the microbial activity and reviving stable process conditions in the CTBB were also investigated. An increase in the H 2 S concentration from 400 to 600 ppm v for a few hours caused bioreactor poisoning; however, when original H 2 S concentrations were restored, stable CTBB operation was ascertained within 3 h. © 2019 Elsevier Ltd |
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