TY - JOUR
T1 - Micro-oxygenation in upflow anaerobic sludge bed (UASB) reactors using a silicon membrane for sulfide oxidation
AU - Valdés, Freddy
AU - Camiloti, Priscila Rosseto
AU - Bartacek, Jan
AU - Torres-Aravena, Álvaro
AU - Toledo-Alarcón, Javiera
AU - Zaiat, Marcelo
AU - Jeison, David
N1 - Publisher Copyright:
© 2020 by the authors. Licensee MDPI, Basel, Switzerland.
PY - 2020/9
Y1 - 2020/9
N2 - Sulfide produced by sulphate-reducing bacteria in anaerobic reactors can seriously affect biogas quality. Microaeration has become a reliable way to remove sulfide, by promoting its oxidation. However, limited research is available regarding its application in upflow anaerobic sludge bed (UASB) reactors. In this research, silicon membranes were studied as a mechanism to dose oxygen in USAB reactors. Two configurations were tested: the membrane placed inside the reactor or in an external module. Our results show that the external membrane proved to be a more practical alternative, providing conditions for sulfide oxidation. This led to a reduction in its concentration in the liquid effluent and biogas. External membrane configuration achieved a sulfide conversion rate of 2.4 g-S m2 d−1 . Since the membrane was not sulfide-selective, methane losses were observed (about 9%). In addition, excessive oxygen consumption was observed, compared to the stoichiometric requirement. As is the case for many membrane-based systems, membrane area is a key factor determining the correct operation of the system.
AB - Sulfide produced by sulphate-reducing bacteria in anaerobic reactors can seriously affect biogas quality. Microaeration has become a reliable way to remove sulfide, by promoting its oxidation. However, limited research is available regarding its application in upflow anaerobic sludge bed (UASB) reactors. In this research, silicon membranes were studied as a mechanism to dose oxygen in USAB reactors. Two configurations were tested: the membrane placed inside the reactor or in an external module. Our results show that the external membrane proved to be a more practical alternative, providing conditions for sulfide oxidation. This led to a reduction in its concentration in the liquid effluent and biogas. External membrane configuration achieved a sulfide conversion rate of 2.4 g-S m2 d−1 . Since the membrane was not sulfide-selective, methane losses were observed (about 9%). In addition, excessive oxygen consumption was observed, compared to the stoichiometric requirement. As is the case for many membrane-based systems, membrane area is a key factor determining the correct operation of the system.
KW - Membrane
KW - Oxidation
KW - Oxygen
KW - Sulfide
KW - UASB
UR - http://www.scopus.com/inward/record.url?scp=85093944564&partnerID=8YFLogxK
U2 - 10.3390/polym12091990
DO - 10.3390/polym12091990
M3 - Article
AN - SCOPUS:85093944564
SN - 2073-4360
VL - 12
SP - 1
EP - 11
JO - Polymers
JF - Polymers
IS - 9
M1 - 1990
ER -