Mixing assessment of an industrial anaerobic digestion reactor using CFD

被引:14
作者
Abyaneh, Ehsan Zamani [1 ]
Zarghami, Reza [1 ]
Kruehne, Ulrich [2 ]
Grundtvig, Rosinha [2 ]
Ramin, Pedram [2 ]
Mostou, Navid [1 ]
机构
[1] Univ Tehran, Coll Engn, Proc Design & Simulat Res Ctr, Sch Chem Engn, POB 11155, Tehran, Iran
[2] Tech Univ Denmark, Proc & Syst Engn Ctr PROSYS, Dept Chem & Biochem Engn, Bldg 229, DK-2800 Lyngby, Denmark
关键词
CFD; Mixing; Anaerobic digestion; Dead zone; RTD; Acknowledgements The authors wish to thank Kasper Kjellberg (Senior Technology Manager; Novozymes) who kindly provided the geometry dimensions and process details; The authors also gratefully acknowledge the Technical University of Denmark; Copenhagen; Denmark for the partial support of this study; FLOW PATTERN VISUALIZATION; FULL-SCALE; STIRRED-TANK; MODEL; SIMULATION; BEHAVIOR; SYSTEMS; DESIGN;
D O I
10.1016/j.renene.2022.04.147
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A computational fluid dynamic model was developed for an industrial anaerobic digestion reactor to assess its mixing efficiency. The mixing was evaluated by inspecting different parameters, including velocity patterns, dead zones and residence time distribution (RTD). Single-phase simulations were conducted considering and neglecting the presence of solids content and its effect on the viscosity of the slurry. The fluid was considered Newtonian in the absence of solids and non-Newtonian when solids were present. Dead zones were observed in both mixing and expanded sludge bed sections. These zones comprised, respectively, 49 vol % and 10 vol % of the mixing section and the expanded sludge bed section. The formation of the dead zones can be attributed to inefficiency of the mixing section in pumping flow upward into the middle of the reactor, especially, near the internal circulation pipe. Hence, a modification considering the discussed reasons would be beneficial to avoid the formation of dead zones. In addition, a compartment model representing the RTD is proposed, in which different patterns of plug flow, continuous mixed zones, dead volumes and recycle flow are considered.(c) 2022 Elsevier Ltd. All rights reserved.
引用
收藏
页码:537 / 549
页数:13
相关论文
共 46 条
[1]   Application of CFD methods to an anaerobic digester: The case of Ontinyent WWTP, Valencia, Spain [J].
Amparo Lopez-Jimenez, P. ;
Escudero-Gonzalez, Juan ;
Montoya Martinez, Tatiana ;
Fajardo Montanana, Vicente ;
Gualtieri, Carlo .
JOURNAL OF WATER PROCESS ENGINEERING, 2015, 7 :131-140
[2]  
[Anonymous], 1998, Verification and validation in computational science and engineering
[3]   Anaerobic digestion of seven different sewage sludges: A biodegradability and modelling study [J].
Astals, S. ;
Esteban-Gutierrez, M. ;
Fernandez-Arevalo, T. ;
Aymerich, E. ;
Garcia-Heras, J. L. ;
Mata-Ahiarez, J. .
WATER RESEARCH, 2013, 47 (16) :6033-6043
[4]   Estimation of Hydrolysis Parameters in Full-Scale Anerobic Digesters [J].
Batstone, D. J. ;
Tait, S. ;
Starrenburg, D. .
BIOTECHNOLOGY AND BIOENGINEERING, 2009, 102 (05) :1513-1520
[5]   Industrial applications of the IWA anaerobic digestion model No. 1 (ADM1) [J].
Batstone, DJ ;
Keller, J .
WATER SCIENCE AND TECHNOLOGY, 2003, 47 (12) :199-206
[6]  
Batstone DJ, 2002, WATER SCI TECHNOL, V45, P65
[7]   The impact of temperature on the rheological behaviour of anaerobic digested sludge [J].
Baudez, J. C. ;
Slatter, P. ;
Eshtiaghi, N. .
CHEMICAL ENGINEERING JOURNAL, 2013, 215 :182-187
[8]   Computational fluid dynamics modelling of sewage sludge mixing in an anaerobic digester [J].
Bridgeman, J. .
ADVANCES IN ENGINEERING SOFTWARE, 2012, 44 (01) :54-62
[9]   CFD simulation of anaerobic digester with variable sewage sludge rheology [J].
Craig, K. J. ;
Nieuwoudt, M. N. ;
Niemand, L. J. .
WATER RESEARCH, 2013, 47 (13) :4485-4497
[10]   Euler-Lagrange Computational Fluid Dynamics simulation of a full-scale unconfined anaerobic digester for wastewater sludge treatment [J].
Dapelo, D. ;
Bridgeman, J. .
ADVANCES IN ENGINEERING SOFTWARE, 2018, 117 :153-169