| Quantity | Unit | Functional unit description |
|---|---|---|
| 1 | kg | Production of 1 kg of dried bioactive peptides from urban pruning. |
| Quantity | Unit | Description |
|---|---|---|
| 50 | kg | Urban pruning waste biomass |
| 45 | kg | Process water for hydrolysis and fermentation stages |
| 0.02 | kg | Protein-producing yeast culture inoculum |
| 0.5 | kg | Enzymes or acids required for the hydrolysis process |
| Quantity | Unit | Description |
|---|---|---|
| 49 | kg | Residual lignocellulosic biomass from urban pruning hydrolysis. |
| 45 | kg | Wastewater and evaporated process water from drying stages. |
| 0.52 | kg | Spent yeast culture and residual enzymatic materials. |
| Quantity | Unit | Description |
|---|---|---|
| 3.8 | kWh | Electricity for mixing and temperature control during hydrolysis and fermentation. |
| 0.65 | kWh | Electrical energy for pumping systems in ultrafiltration and nanofiltration stages. |
| 4.5 | kWh | Thermal energy required for the concentration of peptides in flash evaporator. |
| 1.2 | kWh | Energy consumption for the final drying stage in the drum drier. |
| Quantity | Unit | Description |
|---|---|---|
| 0 | kWh | No energy produced |
| Quantity | Unit | Description |
|---|---|---|
| 1.558 | Kg CO2eq | Electricity for mixing and temperature control during hydrolysis and fermentation. |
| 0.267 | Kg CO2eq | Electrical energy for pumping systems in ultrafiltration and nanofiltration stages. |
| 1.845 | Kg CO2eq | Thermal energy required for the concentration of peptides in flash evaporator. |
| 0.492 | Kg CO2eq | Energy consumption for the final drying stage in the drum drier. |
| 1.2 | Kg CO2eq | Direct biogenic CO2 emissions from yeast fermentation during protein production |
| Quantity | Unit | Description |
|---|---|---|
| 0 | Kg CO2eq | No energy produced |
| 0 | Kg CO2eq | No CO2eq absorbed |