| Project: | Carotenoids from spent coffee grounds |
| Description: | Production of carotenoids from the hydrolysis and fermentation of spent coffee grounds from the HoReCa sector |
| Quantity | Unit | Functional unit description |
|---|---|---|
| 1 | g | Production of 1 gram of carotenoids from spent coffee grounds. |
| Quantity | Unit | Description |
|---|---|---|
| 1250 | g | Spent coffee grounds sourced from the HoReCa sector |
| 12.5 | kg | Process water for hydrolysis and fermentation stages |
| 125 | g | Sulfuric acid used for the acid hydrolysis process |
| 90 | g | Sodium hydroxide used for pH neutralization of hydrolysate |
| 20 | g | Nutrient supplements including yeast extract and mineral salts |
| Quantity | Unit | Description |
|---|---|---|
| 1249 | g | Solid coffee ground residue remaining after hydrolysis and fermentation stages. |
| 12.735 | kg | Liquid wastewater containing neutralized salts and dissolved organic nutrients. |
| Quantity | Unit | Description |
|---|---|---|
| 1.15 | kWh | Pre-treatment including drying and milling of spent coffee grounds |
| 1.85 | kWh | Thermal energy for heating and agitation during acid hydrolysis |
| 3.2 | kWh | Energy for sterilization and bioreactor operation during fermentation |
| 0.95 | kWh | Downstream processing including centrifugation and carotenoid extraction |
| Quantity | Unit | Description |
|---|---|---|
| 0 | kWh | No energy produced |
| Quantity | Unit | Description |
|---|---|---|
| 0.46 | Kg CO2eq | Pre-treatment including drying and milling of spent coffee grounds |
| 0.74 | Kg CO2eq | Thermal energy for heating and agitation during acid hydrolysis |
| 1.28 | Kg CO2eq | Energy for sterilization and bioreactor operation during fermentation |
| 0.38 | Kg CO2eq | Downstream processing including centrifugation and carotenoid extraction |
| 0 | Kg CO2eq | No CO2eq emitted directly |
| Quantity | Unit | Description |
|---|---|---|
| 0 | Kg CO2eq | No energy produced |
| 0 | Kg CO2eq | No CO2eq absorbed |