Table 2.

Results for the 1G autonomous distillery (Reference scenario)

Parameter	Value	Unit
Sugar cane as raw material	165	dry ton/h
Fresh water required	310	m3/h
Ethanol produced	46	m3/h
Vinasse produced	370	m3/h
Bagasse to boiler	74	dry ton/h
Electricity produced	77	MWel
Live steam, 2.5 bar, for evaporators	210	ton/h
Steam, 1.7 bar, required for distillation	160	ton/h
Steam, 1.7 bar, recovered after evaporation	170	ton/h
Total capital cost (including CHP)	117	million US$