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https://hdl.handle.net/1822/1525
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Campo DC | Valor | Idioma |
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dc.contributor.author | Pereira, M. A. | - |
dc.contributor.author | Mota, M. | - |
dc.contributor.author | Alves, M. M. | - |
dc.date.accessioned | 2005-05-10T17:04:13Z | - |
dc.date.available | 2005-05-10T17:04:13Z | - |
dc.date.issued | 2002-04 | - |
dc.identifier.citation | “Process biochemistry”. ISSN 1359-5113. 37:9 (2002) 1025-1031. | eng |
dc.identifier.issn | 1359-5113 | - |
dc.identifier.issn | 0032-9592 | - |
dc.identifier.uri | https://hdl.handle.net/1822/1525 | - |
dc.description.abstract | An expanded granular sludge bed (EGSB) reactor and an anaerobic filter (AF), inoculated with granular and suspended sludge, respectively, were operated with an oleic acid-based synthetic effluent. The granular inoculum exhibited a specific methanogenic activity with acetate, ethanol and H2/CO2 as substrates, in average 2–7 times higher than the suspended biomass. Resistance to oleic acid toxicity was ten-fold higher in the granular than in the suspended sludge. Due to the better characteristics of the granular inoculum a faster start-up strategy was adopted in the EGSB than in the AF, being oleic acid fed since the beginning and the co-substrate eliminated on Day 70. In the AF, a co-substrate was fed until Day 150 and oleic acid was introduced only on Day 94. Organic loading rates of 8 and 12 g COD/l d of oleate as the sole carbon source were achieved in the EGSB and AF, with removal efficiencies of 70 and 80%, respectively. At these maximal loads, the average effluent volatile suspended solids were 2.7 and 5.6 g/l in the EGSB and AF, respectively. The methane yield decreased from 280 to 27 l CH4/kg COD-removed in the EGSB and from 362 to 91 l CH4/kg COD-removed in the AF. The possibility of using a faster start-up procedure using a better inoculum was investigated and results suggest that inoculum quality was not, in this case, a dominant factor for the operation of reactors with high LCFA content. | eng |
dc.language.iso | eng | eng |
dc.publisher | Elsevier 1 | eng |
dc.rights | openAccess | eng |
dc.subject | Anaerobic filter | eng |
dc.subject | Expanded granular sludge bed | eng |
dc.subject | Oleic acid | eng |
dc.subject | Long chain fatty acid | eng |
dc.title | Operation of an anaerobic filter and an EGSB reactor for the treatment of an oleic acid-based effluent : influence of inoculum quality | eng |
dc.type | article | eng |
dc.peerreviewed | yes | eng |
oaire.citationStartPage | 1025 | por |
oaire.citationEndPage | 1031 | por |
oaire.citationIssue | 9 | por |
oaire.citationVolume | 37 | por |
dc.identifier.doi | 10.1016/S0032-9592(01)00311-9 | por |
dc.subject.wos | Science & Technology | por |
sdum.journal | Process Biochemistry | por |
Aparece nas coleções: | CEB - Publicações em Revistas/Séries Internacionais / Publications in International Journals/Series |
Ficheiros deste registo:
Ficheiro | Descrição | Tamanho | Formato | |
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2002-18.pdf | 387,3 kB | Adobe PDF | Ver/Abrir |