From: Cultivation of microalgae for biofuel production: coupling with sugarcane-processing factories
Parameter/description | Value | References |
---|---|---|
Assumed depth of pond (m) | 0.30 | [8] |
Assumed dimensions of a pond (m) | 10, 100, and 0.30 for width, length, and depth, respectively | |
Fraction of area occupied by the PBRs (%) | 0.10 | [8] |
Temperature (°C) | 29.70 | Characteristics of the wastewater |
pH | 6.60 | Characteristics of the wastewater |
Algae growth rate/productivity (g/m2/day) | 25 | |
Mixing velocity in the pond (cm/s) | 25 | |
Electricity demand by paddle wheel (kW/ha) | 2 | [8] |
Electricity demand to pump WW to pond (kWh/L) | 2.40 × 10-5 | [23] |
Electricity demand to pump from pond to bio-flocculation (kWh/L) | 4.80 × 10-5 | |
Electricity demand for recycle pump (kWh/L) | 2.50 × 10-5 | |
Electricity consumption for flue gas injection (kWh/kg CO2) | 2.22 × 10-2 | [24] |
% of flue gases captured | 90 | Estimated |
CO2 utilization (% converted to algae) | 85 | |
CO2 required for algal growth (g CO2/g algae dry) | 1.92 | From the microalgae composition |
TN required for algal growth (g N/g algae dry) | 0.09 | From the microalgae composition |
TP required for algal growth (g P/g algae dry) | 1.28 × 10-2 | From the microalgae composition |
TN reduction (%) | 95 | |
TP reduction (%) | 80 | [8] |
Water loss by evaporation (m/day) | 6.91 × 10-3 | Average evaporation rate data for Metahara [27] |
Algae oil content (wt.%) | 30 | |
Culture density (g/L) | 0.50 (0.10–2) | |
Ratio of total pond area to total facility foot print (%) | 84 | [29] |