Table 1.
Technology Stage | Process | Amount | Unit |
---|---|---|---|
Input | |||
Plum waste | Transportation and cutting | 5000 | kg/km |
Pressurized hot water pretreatment | Water | 700 | L |
Cellulose | 38.4 | kg | |
Hemicellulose | 26.8 | kg | |
Lignin | 28.6 | kg | |
Others (ash + protein) | 6.2 | kg | |
Electricity (Parr reactor) | 71.0 | kWh | |
SSF process | Cellulose | 31.5 | kg |
Hemicellulose | 1.36 | kg | |
Lignin | 23.3 | kg | |
Enzymes | 51.37 | kg | |
Nutrients and yeast | 35.23 | kg | |
Inoculum + L. rhamnoses | 3.52 | kg | |
Water | 297 | L | |
Electricity | 250 | kWh | |
Lactic acid purification | Ammonium sulfate | 10.0 | kg |
Butanol | 50.0 | L | |
Polymerization and microwave | Lactic acid | 29.2 | kg |
SnCl2 | 11.68 | kg | |
o-xylene | 38.54 | kg | |
Electricity (microwave) | 100.0 | kWh | |
Output | |||
Pressurized hot water pretreatment (liquid phase) | Hemicellulose | 18 | kg |
By-products | 17 | kg | |
Water | 600 | kWh | |
Pressurized hot water pretreatment (solid phase) | Cellulose | 31.5 | kg |
Hemicellulose | 1.36 | kg | |
Lignin | 23.3 | kg | |
SSF process | Lactic acid | 29.2 | L |
Waste | 423.28 | L | |
Lactic acid purification | Waste | 60.0 | L |
Polymerization and microwave | SnCl2 | 10.2 | kg |
Waste | 52.62 | kg | |
PLA | 26.8 | kg |