4.6 Article

Optimization of Hydrolysis-Acidogenesis Phase of Swine Manure for Biogas Production Using Two-Stage Anaerobic Fermentation

Journal

PROCESSES
Volume 9, Issue 8, Pages -

Publisher

MDPI
DOI: 10.3390/pr9081324

Keywords

two-stage anaerobic digestion; biomethane; swine manure; operational time; response surface methodology (RSM)

Funding

  1. Taiwan's Ministry of Science and Technology [MOST 108-2221-E-035-056, 108-2221-E-035 -036 -MY3, 109-2221-E-035-028]

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Through response surface methodology, the optimization of operational period and initial operational pH for hydrolysis and acidogenesis of swine manure at 35 degrees C in batch operation mode was conducted. The optimal condition resulted in peak volatile acid production, methane production rate, and methane yield. The two-stage anaerobic system showed higher biogas production efficiency compared to a single-stage system, with similar dominant methane-producing species.
The traditional pig manure wastewater treatment in Taiwan has been low in methane production efficiency due to unstable influent concentration, wastewater volume, and quality. Two-stage anaerobic systems, in contrast, have the advantage of buffering the organic loading rate in the first stage (hydrolysis-acidogenesis phase), allowing a more constant feeding rate to the second stage (methanogenesis phase). Response surface methodology was applied to optimize the operational period (0.5-2.0 d) and initial operational pH (4-10) for hydrolysis and acidogenesis of the swine manure (total solid 5.3%) at 35 degrees C in batch operation mode. A methanogenesis verification experiment with the optimal condition of operational period 1.5 d and pH 6.5 using batch operation resulted in peak volatile acid production 7 g COD/L, methane production rate (MPR) 0.3 L-CH4/L-d, and methane yield (MY) 92 mL-CH4/g-CODre (chemical oxygen demand removed). Moreover, a two-stage system including a hydrolysis-acidogenesis reactor with the optimal operating condition and a methanogenesis reactor provided an average MPR 163 mL/L-d and MY 38 mL/g volatile solids, which values are 60% higher than those of a single-stage system; both systems have similar dominant methane-producing species of Firmicutes and Bacteroidetes with each having around 30%-40%. The advantages of a two-stage anaerobic fermentation system in treating swine manure for biogas production are obvious.

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