Abstract
Computational fluid dynamic simulations are employed to predict flow characteristics in a continuous auger driven reactor designed for the dilure acid pretreatment of biomass. Slurry containing a high concentration of biomass solids exhibits a high viscosity, which poses unique mixing issues within the reactor. The viscosity increases significantly with a small increase in solids concentration and also varies with temperature. A well-mixed slurry is desirable to evenly distribute acid on biomass, prevent buildup on the walls of the reactor, and provides an uniform final product. Simulations provide flow patterns obtained over a wide range of viscosities and pressure distributions, which may affect reaction rates. Results provide a tool for analyzing sources of inconsistencies in product quality and insight into future design and operating parameters.
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Abbreviations
- c:
-
Newtonian proportionality constant (dimensionless)
- D:
-
Diameter (m)
- F:
-
Volumetric flow rate (m3/s)
- k:
-
Shear rate constant (dimensionless)
- L:
-
Length (m)
- M:
-
Torque (Nm)
- N:
-
Rotation rate (rps)
- P:
-
Pressure (Pa)
- r:
-
Redius (m)
- Re:
-
Reynolds number (dimensionless)
- V:
-
Velocity (m/s)
- γ:
-
Shear rate (/s)
- η:
-
Viscosity (kg/m·s)
- π:
-
Density (kg/m3)
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Berson, R.E., Dasari, R.K. & Hanley, T.R. Modeling of a continuous pretreatment reactor using computational fluid dynamics. Appl Biochem Biotechnol 130, 621–630 (2006). https://doi.org/10.1385/ABAB:130:1:621
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DOI: https://doi.org/10.1385/ABAB:130:1:621