Evaluation of the low technology tubular digesters in the production of biogas from slaughterhouse wastewater treatment: Low cost tubular digesters

Abstract

The aim of this research is to identify the operational conditions and performance of low cost tubular digesters producing biogas from the slaughterhouse wastewater treatment. Three full scale sequenced tubular digesters (of more than Failed to parse (syntax error): 8 m^3

each), operating in a slaughterhouse in Cochabamba (Bolivia), have been monitored during one year. The Organic Load Rate (OLR) varied from $0.04$ to $1.13kgSV/m^{3}d$ ($0.04-1.07kgCOD/m^{3}d$), and the Hydraulic Retention Time (HRT) from $3.2$ to $87.4$ days. The passive solar heating design considered drove the slurry temperature to $27^{o}C$, $8^{o}C$ more than mean ambient temperature. The first digester has been filled with soda bottle plastic rings in order to increase the internal effective surface and evaluate, obtaining that an increment in $67\%$ of the internal effective surface, more than doubles the biogas production and enables higher OLRs. A Biogas Production Rate (BPR) peak of Failed to parse (syntax error): 0.2 m^3/m^3d
was observed for Failed to parse (syntax error): OLR = 0.37 kgSV/m^3d

, Failed to parse (syntax error): HRT = 9.7d

and Specific Biogas Production (SBP) = 0.55 m3/kgSV. COD removal achieves values above $70\%$ from $HRT>19$ d. A comparison with other anaerobic digestion technologies demonstrates that low cost tubular digesters with biofilm carriers, are competitive for $OLR<0.5$ kg $COD/m^{3}d$ of biogas production, and for $0.25kgCOD/m^{3}d$, when the focus is on COD removal.