Localized mixing of anaerobic plug flow reactors

• Published in: Water research (Oxford) Vol. 204; p. 117588
• Main Authors: Khalil, Charbel Abou, Eraky, Mohamed T., Ghanimeh, Sophia
• Format: Journal Article
• Language: English
• Published: Elsevier Ltd 01.10.2021
• Subjects: Dry anaerobic digestion; Food waste; Innovative mixing; Total solid content; Wastewater; CFD; TAN; WW; AD; AnCSTR; AnPFR; HRT; Wastewater; VOF; TA; Total solid content; Food waste; VFA; FW; PA; Re; Dry anaerobic digestion; OLR; COD; VS; Innovative mixing; TS
• ISSN: 0043-1354; 1879-2448
• DOI: 10.1016/j.watres.2021.117588

•Intermittent mixing that merges hydraulic and biochemical properties.•Design tested under various solid contents ranging from 10 to 22.5.%•Adequate performance observed with feed solid up to 20%.•Solids removal reached up to 92% and methane yield reached 613 ml/g VS.•Digester simulated using computational fluid dynamics. An innovative localized-mixing concept was tested in an Anaerobic Plug Flow Reactor (AnPFR) treating Food Waste (FW) mixed with municipal Wastewater (WW). The proposed concept consists of placing propellers along the shaft of the AnPFR at key points that represent the mid-region of each of the anaerobic digestion stages: hydrolysis, acidogenesis, and methanogenesis. First, the need for and efficiency of localized mixing (the new concept suggested by the authors) were investigated. While the main benefit of localized mixing is the reduction of energy demand associated with (conventional) uniform mixing (i.e., throughout the longitudinal axis), the system can also benefit from synergetic reactions in non-mixed zones. In fact, at a Total Solid (TS) content of 15% (Organic Loading Rate (OLR) of 4.2 g VS.L − 1.d − 1) and a Hydraulic Retention Time (HRT) of 28 days, the mixing pattern was sufficient to maintain stable operation, with high removal rates (up to 96% of solids) and high biogas generation (1128 ± 55 ml.g VSfed−1, of which 68.9% consisted of CH4); but when mixing was halted, the system's performance deteriorated. Second, the loading capacity of the locally-mixed AnPFR was investigated by subjecting it to different TS content (10%, 15%, 20%, and 22.5%, corresponding to OLRs of 2.8, 4.2, 6.3, and 7.9 g VS.L − 1.d − 1, respectively) while operating under the same HRT. It was found that the system can adequately sustain a feed with a maximum TS of 20% while achieving removal rates up to 92% for solids and a CH4 yield of 613 ml.g VSfed−1. The digester was simulated using computational fluid dynamics. The outputs revealed: (1) highest radial mixing at the center of the methanogenesis zone where the propeller is located and (2) low longitudinal mixing before and after the propeller of the methanogenesis stage, implying the presence of sedimentation zones that was visually verified. The former is assumed to favor better dispersion of inhibitors and improved stability, while the latter is expected to provide stagnant areas for enhanced biochemical synergies. [Display omitted]