Abstract
The treatment of fruit and vegetable waste (FVW) is commonly carried out in continuously stirred tank reactors (CSTR). The high solids and carbohydrate content in FVW cause excessive acidification during anaerobic digestion, affecting reactor stability and methane production. The two-stage process is a possible solution to minimize this issue. To verify the CSTR as a configuration for anaerobic digestion of FVW and to propose alternatives, this study aimed to compare the single-stage with a two-stage process. The experiment evaluated hydraulic retention time of 34, 22, and 16/12 days and organic loading rates of 1.0, 1.5, and 2.0/2.5 kg chemical oxygen demand (COD)/m3·d on methane production. The two-stage system showed better performance than the single stage, resulting in a COD removal of 84% and a methane production rate of 0.459 L CH4/L·d. Furthermore, it was found that the two-stage system can lead to a reduction of 35% in the total reactor volume. In addition, the FVW digestion in a CSTR was compared with the modeling of the FVW liquid and solid fractions digestion. The modeling showed a higher potential for biomethane production with the liquid fraction (FVWL) than with raw FVW. The potential of biomethane production from the solid fraction was equal to the potential with raw FVW. Furthermore, implementing a high-rate reactor system with FVWL could significantly reduce the total volume by 82% compared with the CSTR while also increasing methane productivity.
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