Experimental results and simulations based on the Anaerobic Digestion Model No.1 (ADM1) with temperature effects on kinetics were used to evaluate rate limiting steps in sludge bed anaerobic digestion (AD) during load and temperature variations. Simulations were carried out in Aquasim. The model is compared to data from a pilot experiment in a 220 liter AD sludge bed reactor treating diary manure for 16 months of various loads; 0-13 kg COD L −1 d −1 and various temperatures; 25°C, 30°C and 35°C. Methane and CO 2 production were monitored on-line while soluble and particulate organic carbon, pH and volatile fatty acids were measured on regularly collected inlet and effluent samples. Simulated overall soluble and particulate organic carbon removal, methane and CO 2 production, pH and acetate are close to measured values while propionate is underestimated during some transitions. The fit is mainly sensitive to the composition of the feed in terms of relative amounts of lipids, proteins and carbohydrates especially at simultaneously high load and low temperature. During such conditions, the model predicts accumulation of long chained fatty acids (LCFA), suggesting that the degradation of LCFA is the rate-limiting step at low temperatures. This effect is not explained by reduced LCFA solubility at lower temperature. The model predicts that sludge bed AD efficiency on substrates with little or no LCFA is independent of temperature between 25°C and 35°C while LCFA degradation is favoured by higher temperature. Keywords: ADM1, anaerobic digestion, rate limiting, sludge bed, temperature dependence.
INTRODUCTIONAnaerobic digestion (AD) to recover energy as methane from organic wastes can reduce greenhouse gas emissions and contribute to more sustainable waste handling.The Anaerobic Digestion Model No.1 (ADM1) [1] is a common platform of modelling, simulations and understanding AD, developed by the International Water Association (IWA). ADM1 was developed primarily to model digestion of sludge from wastewater treatment plants at standard process temperatures 35°C and 55°C, presumed optimal for respectively meso-and thermophilic digestion.Process heating can consume a large portion of the potential energy of organic wastes, especially in AD of low energy substrates, such as cow manure slurry. Implications of AD at T<35°C to reduce heat losses is therefore studied. ADM1 included temperature effects on kinetic coefficients for the biochemical processes particle disintegration, hydrolysis and substrate uptake reactions (ADM1-T) were developed for this purpose [2]. This model combined with pilot tests is used here to examine temperature effects during a wide range of loadings.Intermediate products are measured to identify rate limiting degradation steps since it is not always obvious what is the rate-limiting step. Disintegration, hydrolysis, propionate degradation and acetoclastic methanogenesis are often considered to be possible rate limiting processes, depending on the feed composition. LCFA degradation may also be...