Table 3 Estimated costs involved in the synthesis of 1% Cu-doped BiVO4.
Item | Quantity (per batch) | Unit cost (RM) | Total cost (RM) | Notes |
|---|---|---|---|---|
Raw materials | ||||
Bi(NO3)3·5H2O | 3.3954 g | RM 2.38/g | 8.08 | Bi source |
NH4VO3 | 0.8189 g | RM 1.25/g | 1.02 | V source |
CuSO4·5H2O | 0.101 g | RM 2.75/g | 0.28 | Cu dopant source |
Total raw material cost | 9.38 | |||
Synthesis process | ||||
Hydrothermal heating (180 °C) | 1.5 kWh × 15 h = 22.5 kWh | RM 0.24 per kWh* | 5.40 | Energy cost for autoclave operation |
Deionized water | 200 mL | RM 0.01/mL | 2.00 | For dissolving reagents and washing catalyst |
Ethanol (for washing) | 20 mL | RM 0.11/mL | 2.20 | For catalyst washing |
Drying | 1.5 kWh × 12 h = 18.0 kWh | RM 0.24 per kWh* | 4.32 | Energy cost for oven operation |
Calcination | 3.0 kWh × 4 h = 12.0 kWh | RM 0.24 per kWh* | 2.88 | Energy cost for box furnace operation |
Total synthesis cost | 16.80 | |||
Equipment depreciation | ||||
Teflon-lined autoclave usage | – | – | 0.20 | Based on estimated equipment depreciation per batch |
Centrifuge/filtration setup | – | – | 0.10 | Equipment for recovery and filtration |
Total equipment cost | 0.30 | |||
Overall cost | 26.48 | Per batch (3.5 g photocatalyst yield) | ||