A simple kinetic model applied to anaerobic digestion of cow manure.

A simple model of anaerobic degradation in a continuous stirred digester is presented. The hydrolysis of cow manure was modelled as consisting of two fractions, one rapidly degradable and the other more slowly degradable, and both processes were represented by first-order kinetics in a two-substrate first-order (TSFO) model. The fractions were separated by water flushing. Biomethane potential (BMP) tests were performed to determine the hydrolysis constant and biodegradability of each fraction. The hydrolysis constants of the rapidly and slowly degradable fractions were 0.278 and 0.069 d-1, respectively. Coupled with a simple anaerobic digestion model, the TSFO model was used to simulate the digester behaviour and predict methane production. Experiments in a 3.0 L digester were used to determine the decay constant and yield values and to validate the model. Two solid loads (2.9 and 4.4 gVS/L.d) were applied to the digester, and the dynamics of both biodegradable fractions, the non-biodegradable fraction and the microorganism concentration were reproduced by the model. These results approximate the actual biodegradable solids removal to within 85%. A parametric sensitivity study was performed, and the results show that the hydrolysis constant mainly influences the biodegradable fractions and that the decay and yield parameters mainly influence the microorganism concentration.

Microbiota adaptation after an alkaline pH perturbation in a full-scale UASB anaerobic reactor treating dairy wastewater.

The aim of this study was to understand how the microbial community adapted to changes, including a pH perturbation, occurring during the start-up and operation processes in a full-scale methanogenic UASB reactor designed to treat dairy wastewater. The reactor performance, prokaryotic community, and lipid degradation capacity were monitored over a 9-month period. The methanogenic community was studied by mcrA/mrtA gene copy-number quantification and methanogenic activity tests. A diverse prokaryotic community characterized the seeding sludge as assessed by sequencing the V4 region of the 16S rRNA gene. As the feeding began, the bacterial community was dominated by Firmicutes, Synergistetes, and Proteobacteria phyla. After an accidental pH increase that affected the microbial community structure, a sharp increase in the relative abundance of Clostridia and a decrease in the mcrA/mrtA gene copy number and methanogenic activity were observed. After a recovery period, the microbial population regained diversity and methanogenic activity. Alkaline shocks are likely to happen in dairy wastewater treatment because of the caustic soda usage. In this work, the plasticity of the prokaryotic community was key to surviving changes to the external environment and supporting biogas production in the reactor.

Integrated anaerobic treatment of dairy industrial wastewater and sludge.

Performance parameters were studied in an alternative full-scale dairy effluent treatment system comprising two anaerobic sludge-blanket reactors in parallel arrangement with upward flow, internal fat-separation by flotation, external lamella settler and floated material digester. Reactors were initially inoculated with flocculent sludge and granulated in a high-load stage. Using loading rates up to a maximum 5.5 kg COD/m(3) x d-hydraulic residence time of 17 hours- reactor efficiency was found to remain stable around 90% of COD. Average sludge digester efficiency using a loading rate of 3.5 kgVS/m(3) x d with a lipid content of 47% of COD amounted to 78% of VS (87% of lipid removal). LCFA inhibition as assayed using palmitate was found to depend not only on the palmitate concentration but also on the palmitate-to-biomass concentration ratio.

Assessment on the performance of a series of two UASB reactors compared against one of the same total volume using Anaerobic Digestion Model No 1 (ADM1).

The ADM1 is applied to simulate the behaviour of an Upflow Anaerobic Sludge Blanket Reactor (UASB) treating blood powder (spray dried blood meal) wastewater. Considering a completely mixed liquid phase, the model is defined by a set of differential equations which can be numerically solved. Experimental data allows validating the output of the model which is then used for performing numerous simulations. A single reactor is compared to a series of two identical reactors of half the volume each. For the same total hydraulic retention time, the series reaches an outlet concentration 74% inferior to that of the single reactor. Furthermore, for the same total conversion the volume required by the series is 43% of that of the single reactor.