2023
DOI: 10.1007/s10532-023-10060-3
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Organic stabilization and methane production under different organic loading rates in UASB treating swine wastewater

Jacineumo Falcão de Oliveira,
Ronaldo Fia,
Ana Flavia Santos Rabelo de Melo
et al.
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Cited by 3 publications
(1 citation statement)
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“…where V r is the useful volume of the reactor (m 3 ), Q is the volumetric flow rate fed to the reactor (m 3 d −1 ), S is the concentration of substrate (kg COD m −3 ), and OLR is the organic loading rate (kg COD m −3 d −1 ). The CH 4 production (BMP) from the AD reactor was calculated from the stoichiometry of the CH 4 formation reaction from 1 g of COD (0.35 NLCH 4 gCOD −1 ) [37,38], also considering an average COD removal efficiency of 85%, represented by the biochemical methane potential (BMP). The operating temperature was set at 20 • C, consistent with the ambient temperature of the study region.…”
Section: Biogas Production Calculationsmentioning
confidence: 99%
“…where V r is the useful volume of the reactor (m 3 ), Q is the volumetric flow rate fed to the reactor (m 3 d −1 ), S is the concentration of substrate (kg COD m −3 ), and OLR is the organic loading rate (kg COD m −3 d −1 ). The CH 4 production (BMP) from the AD reactor was calculated from the stoichiometry of the CH 4 formation reaction from 1 g of COD (0.35 NLCH 4 gCOD −1 ) [37,38], also considering an average COD removal efficiency of 85%, represented by the biochemical methane potential (BMP). The operating temperature was set at 20 • C, consistent with the ambient temperature of the study region.…”
Section: Biogas Production Calculationsmentioning
confidence: 99%