Abstract

Process liquid recirculation initially stimulated one-phase anaerobic digestion of alfalfa silage in two semi-continuously fed and stirred tank reactors. Thus, with increased pH, alkalinity and stability it was possible to increase the organic loading rate to 3 g VS L-1 d(-1), as compared to 2.25 g VS L-1 d(-1) in a control reactor without recirculation. However, the recirculation of liquid eventually caused an accumulation of organic and inorganic substances, leading to an inhibition of hydrolysis and methanogenesis. This inhibition of microbial activity was prevented in one of the processes by replacing 50% of the recirculated process liquid with water during the second half of the operation period. A multiple linear regression model of principal components using seven input variables explained the variance in output variables nearly as well as the original model using all 23 measured input variables. The results show that it is necessary to adjust the degree of liquid recirculation to reach an optimal process. (c) 2005 Elsevier Ltd. All rights reserved

Keywords

Anaerobic digestion; Biogas; Energy crops; Liquid recirculation; Methane; Multiple linear regression; Silage; Specific methanogenic activity

Published in

Bioresource Technology
2007, Volume: 98, number: 1, pages: 104-111
Publisher: ELSEVIER SCI LTD

SLU Authors

• Nordberg, Åke

  • Department of Molecular Sciences, Swedish University of Agricultural Sciences
    

• Stenberg, Bo

  • Department of Soil and Environment, Swedish University of Agricultural Sciences
    

UKÄ Subject classification

Renewable Bioenergy Research


Publication identifier

DOI: https://doi.org/10.1016/j.biortech.2005.11.027

Permanent link to this page (URI)

https://res.slu.se/id/publ/9197