TY - JOUR
T1 - UASB treatment of wastewater with concentrated mixed VFA
AU - Fang, Herbert H.P.
AU - Li, Yu You
AU - Chui, Ho Kwong
PY - 1995/2
Y1 - 1995/2
N2 - The upflow anaerobic-sludge blanket (UASB) process consistently removed 97-99% of chemical oxygen demand (COD) from wastewater containing concentrated mixed volatile fatty acids (VFA) at 37°C at loading rates of up to 24 g-COD/(L·d), corresponding to a food/microorganism ratio of 0.78 g-COD/[g-volatile suspended solids (VSS)·d]. It suggested that, with preacidification, the UASB process can be effective for a wide variety of wastewaters. The COD removal efficiency deteriorated at higher loading rates; there was no butyrate in the effluent, suggesting that butyrate degradation was not a rate-limiting step. Of the COD removed, 92.6% was converted to methane; the rest was converted to granular biomass with an average yield of 0.054 g-VSS/g-COD. The granules had a size of 1−2 mm and settled satisfactorily. Each gram of granule in the reactor was capable of converting a daily maximum of 0.86 g of COD into methane. The granules had a fluffy surface mostly composed of interwound filamentous Methanothrix-Iike bacteria. Syntrophic associations between Methanothrix-. Methanospirillum hungatei-, and Syntrophobacter-Iike bacteria were prevalent in the granule interior. The syntrophic relation between these species was elucidated by thermodynamics.
AB - The upflow anaerobic-sludge blanket (UASB) process consistently removed 97-99% of chemical oxygen demand (COD) from wastewater containing concentrated mixed volatile fatty acids (VFA) at 37°C at loading rates of up to 24 g-COD/(L·d), corresponding to a food/microorganism ratio of 0.78 g-COD/[g-volatile suspended solids (VSS)·d]. It suggested that, with preacidification, the UASB process can be effective for a wide variety of wastewaters. The COD removal efficiency deteriorated at higher loading rates; there was no butyrate in the effluent, suggesting that butyrate degradation was not a rate-limiting step. Of the COD removed, 92.6% was converted to methane; the rest was converted to granular biomass with an average yield of 0.054 g-VSS/g-COD. The granules had a size of 1−2 mm and settled satisfactorily. Each gram of granule in the reactor was capable of converting a daily maximum of 0.86 g of COD into methane. The granules had a fluffy surface mostly composed of interwound filamentous Methanothrix-Iike bacteria. Syntrophic associations between Methanothrix-. Methanospirillum hungatei-, and Syntrophobacter-Iike bacteria were prevalent in the granule interior. The syntrophic relation between these species was elucidated by thermodynamics.
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U2 - 10.1061/(ASCE)0733-9372(1995)121:2(153)
DO - 10.1061/(ASCE)0733-9372(1995)121:2(153)
M3 - Article
AN - SCOPUS:0029239877
SN - 0733-9372
VL - 121
SP - 153
EP - 160
JO - Journal of Environmental Engineering, ASCE
JF - Journal of Environmental Engineering, ASCE
IS - 2
ER -