Anaerobic Digestion Upgrade Hydrogen
Attribute |
Description |
Standard value |
Unit |
Data type |
|---|---|---|---|---|
|
If set to ‘true’, the technology will be considered in the energy system model (this does not necessarily mean it will be used). Only relevant for optimisation. |
False |
— |
bool |
|
Color for plot |
#90037F |
hex |
str |
|
does the process have a fluidised bed |
False |
— |
bool |
|
methane produced per input |
0.6 |
float |
|
|
Conversion efficiency |
0.3 |
— |
float |
|
Conversion efficiency |
0.8395 |
float |
|
|
maximum output |
inf |
kWh |
float |
|
Carbon-dioxide intensity of technology output (annual average value). |
0.814 |
kg CO2/kWh |
float |
|
Expected lifetime of technology before replacement is required. |
25 |
years |
int |
|
Operation and maintenance cost per consumed carrier unit |
0 |
CHF/kWh |
float |
|
CAPEX cost of technology per unit of capacity. |
1834 |
CHF/kWp |
float |
|
OPEX cost of technology per unit of capacity. |
10 |
CHF/kWp/year |
float |
|
Interest rate for computing levelised costs (if required). |
0.025 |
— |
float |
The relationship between the in- and outflows is given by
The symbols and names of the flows are
|
Inflow Electricity |
|
Inflow H₂ |
|
Outflow Heat |
|
Outflow Gas |
|
Inflow Wet biomass |