Evaluation of anaerobic digestion post-treatment options using an integrated model-based approach. (1st June 2019)

• Record Type: Journal Article
• Authors: Flores-Alsina, X.; Feldman, H.; Monje, V.T.; Ramin, P.; Kjellberg, K.; Jeppsson, U.; Batstone, D.J.; Gernaey, K.V.
• Is Part Of: Water research. Volume 156(2019)
• Page Start: 264
• Page End: 276
• Publication Date: 2019-06-01
• Subjects: Anammox -- Bacterial competition -- Biofilms -- Industrial wastewater -- Physico chemical modelling; Water -- Pollution -- Research -- Periodicals; 363.7394
• DOI: 10.1016/j.watres.2019.02.035
• Languages: English
• ISSNs: 0043-1354

Abstract

Abstract: The objective of this paper is to present the main results of an engineering-research project dealing with model-based evaluation of waste streams treatment from a biotech company. This has been extensively done in domestic treatment systems, but is equally important, and with different challenges in industrial wastewater treatment. A new set of biological (activated sludge, anaerobic digestion), physicochemical (aqueous phase, precipitation, mass transfer) process models and model interfaces are required to describe removal of organics in an upflow anaerobic sludge blanket (UASB) reactor plus either traditional nitrification/denitrification (A1 ) or partial nitritation (PN)/anammox (ANX) (A2 ) processes. Model-based analysis shows that option A1 requires a decrease in digestion energy recovery (Erecovery ) in order to have enough organic substrate for subsequent post NO3 reduction treatment (95 kWh.kg N −1 ). In contrast, A2 in an aerobic granular sludge reactor allows for higher UASB conversion since N removal is carried out autotrophically. The study also reveals that the addition of an aerated pre-treatment unit prior to the PN/ANX (A2 ) reactor promotes COD and H2 S oxidation, CO2 and CH4 stripping, a pH increase (up to 8.5) and a reduction of the risk of intra-granular precipitation as well as sulfide inhibition. Simulations indicate clear differences regarding the microbial distribution/abundance within the biofilm in A2 when comparing the two operational modes. Final results show the effects of different loading and operational conditions; dissolved oxygen (DO), Total Suspended Solids (TSSop ), energy recovery (Erecovery ); on the overall process performance; N removal, aeration energy (Eaeration ), net energy production (Erecovery ); using response surfaces, highlighting the need of integrated approaches to avoid sub-optimal outcomes. The study shows the benefits of virtual plant simulation and demonstrates the potential of model-based evaluation when process engineers in industry have to decide between competing options. Graphical abstract: Image 1 Highlights: A plant-wide model comprised of a UASB reactor and two post-treatment alternatives is developed. All process units (conventional/biofilm) are simulated sequentially. Synergies and trade-offs between are analysed in detail. Pre-treatment alternatives affect granule structure and properties in PN/ANX systems. Integrated approaches avoid sub-optimal outcomes.