From: Scale-up of an amoeba-based process for the production of the cannabinoid precursor olivetolic acid
Parameter | Symbol | 1.6-L STR | 7-L STR | 75-L STR | 300-L STR |
---|---|---|---|---|---|
Reactor configurations | |||||
Filling volume [m3] | \({V}_{L}\) | 0.001 | 0.004 | 0.04 | 0.2 |
Reactor diameter [m] | \({D}_{R}\) | 0.11 | 0.16 | 0.3 | 0.6 |
Stirrer diameter [m] | \({d}_{r}\) | 0.044 | 0.064 | 0.135 | 0.196 |
Stirrer height [m] | \({h}_{r}\) | 0.009 | 0.015 | 0.027 | 0.04 |
Number of stirrers | \({S}_{N}\) | 2 | 2 | 2 | 2 |
Maximum local energy dissipation rate [W/kg] | \({\varepsilon }_{max}\) | 3.92 | 3.92 | 3.92 | 3.92 |
Ratio of maximum to specific energy dissipation rate (aerated) | \({\Phi }_{g}\) | 2.36 | 3.02 | 4.58 | 7.83 |
Ratio of maximum to specific energy dissipation rate (unaerated) | \(\Phi\) | 36.54 | 41.45 | 51.75 | 82.86 |
Estimated volumetric gas transfer coefficient [1/h] [25] | \({k}_{L}a\) | 41.7 | 57.6 | 74.3 | 74.1 |
Volumetric power input (aerated) [kW/m3] | \({P}_{g}\) | 1.66 | 1.3 | 0.86 | 0.50 |
Gas velocity [m/s] | \({u}_{g}\) | 5.26 × 10–4 | 9.95 × 10–4 | 2.83 × 10–3 | 3.54 × 10–3 |
Power number | \({P}_{O}\) | 8.26 | 7.6 | 6.5 | 5.56 |
Stirring rate [1/s] | \({n}_{r}\) | 10.83 | 8.88 | 5.41 | 4.29 |