Abstract
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,
49volume % and 10volume % 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.
Original language | English |
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Journal | Renewable Energy |
Volume | 192 |
Pages (from-to) | 537-549 |
ISSN | 0960-1481 |
DOIs | |
Publication status | Published - 2022 |
Keywords
- CFD
- mixing
- Anaerobic digestion
- Dead zone
- RTD