Inhibition by fatty acids during fermentation of pre-treated waste activated sludge.

Fermentation of waste activated sludge produces volatile fatty acids (VFAs), which can be used as the carbon sources for numerous biological processes. However, product inhibition can limit extent of fermentation to VFAs. In this study, product inhibition during fermentation of waste activated sludge pre-treated by a thermal hydrolysis process (THP-WAS) was investigated. Product inhibition was confirmed as spiking reactors with high levels of a mix of VFAs prevented fermentation taking place. Various inhibition models were trialled and it was found that a threshold model (based on thermodynamics) provided the best fit between model and data. This is the first time that threshold type inhibition has been shown for a mixed substrate, mixed population system. Batch fermentations carried out with THP-WAS of different dilutions were used to evaluate the impact of different organic loadings. The threshold VFA concentration for the systems studied was determined to be 17±1gCOD(VFA)L(-1). Inhibition was shown to be due to the presence of a combination of VFAs containing 2-6 carbon atoms each. When evaluated individually, by spiking individual VFAs, all VFAs except for acetate had the same impact at this threshold; acetate being approximately 50% as inhibitory as the other organic acids (COD basis). Based on this, a weighted model could be proposed to better represent the data. Strategies to improve overall yield could be increased production of acetate, or dilution to below the inhibitory level.

[1]  Orhan Yenigün,et al.  Two‐phase anaerobic digestion processes: a review , 2002 .

[2]  P. Elefsiniotis,et al.  Anaerobic acidogenesis of primary sludge: The role of solids retention time , 1994, Biotechnology and bioengineering.

[3]  F. Morgan-Sagastume,et al.  Production of volatile fatty acids by fermentation of waste activated sludge pre-treated in full-scale thermal hydrolysis plants. , 2011, Bioresource technology.

[4]  Glen T. Daigger,et al.  Wastewater solids fermentation for volatile acid production and enhanced biological phosphorus removal , 1995 .

[5]  J. Lester,et al.  Anaerobic acidogenesis of a complex wastewater: II. Kinetics of growth, inhibition, and product formation , 1988, Biotechnology and bioengineering.

[6]  A. E. Greenberg,et al.  Standard methods for the examination of water and wastewater : supplement to the sixteenth edition , 1988 .

[7]  P. Reichert AQUASIM-a tool for simulation and data analysis of aquatic systems , 1994 .

[8]  Determination of the critical concentration of inhibitory products in a repeated fed-batch culture , 1992 .

[9]  K. Kakimoto,et al.  Studies on Anaerobic Digestion Mechanism: Influence of Pretreatment Temperature on Biodegradation of Waste Activated Sludge , 1997 .

[10]  D J Batstone,et al.  Estimation of hydrolysis parameters in full-scale anerobic digesters. , 2009, Biotechnology and bioengineering.

[11]  A.J.C.M. Matthijsen,et al.  Product inhibition in the acid forming stage of the anaerobic digestion process , 1982 .

[12]  M. Madigan,et al.  Brock Biology of Microorganisms , 1996 .

[13]  Charles J. Banks,et al.  The effect of volatile fatty acid additions on the anaerobic digestion of cellulose and glucose in batch reactors , 2005 .

[14]  M A M Reis,et al.  Strategies for the development of a side stream process for polyhydroxyalkanoate (PHA) production from sugar cane molasses. , 2007, Journal of biotechnology.

[15]  S. Pavlostathis,et al.  Kinetics of Anaerobic Treatment , 1991 .

[16]  R. Cord-Ruwisch,et al.  Experimental evidence for the need of thermodynamic considerations in modelling of anaerobic environmental bioprocesses , 1997 .

[17]  H. Siegrist,et al.  The IWA Anaerobic Digestion Model No 1 (ADM1). , 2002, Water science and technology : a journal of the International Association on Water Pollution Research.