Plant for the production of carbon, biochar or charcoal for a subsequent thermal gasification into green hydrogen or for further usage.
Design e.g. for sewage sludge with approx. 30% dry substance content. The dry matter content can also be increased by agreement. Exact values will be determined in the course of the preliminary study / planning study.
Version
Plant for the production of carbon, synthesis gas and hydrogen from biological waste materials, tested fermentation products and/or from sewage sludges.
The plant consists of
- preparation tank, agitator, metering device for acids
- steam generator for the production of the needed process steam (electric, alternative: biogas operated)
- two process vessels with heating and agitator for the production of biochar at the quality level of lignite
- vacuum device for the drying of carbon
- filtration system for the filtration of extracted liquids
- export mechanism for the export of carbon
- preparation for the separation of e.g sulphur, phosphorous and nitrogen, filtration is optional
- control and regulation device for the control of the carbonization process
- sensor technology for the process variable (pressure, temperature, position of valve, pH-value, weight)
- grinder for the grinding of carbon
- conveyor for the carbon transport into the entrained flow gasifier
- entrained flow gasifier for the turning of carbon into gas with heating, quantity measurement, measurement of pressure and temperature, export of synthesis gas and slag
- gasification tank
- control and regulation device for the process control of the gasification process
- gas cleaning for the cleaning of the synthesis gas
- gas measuring device for the determining of the substances which are produced within the process
- CO-shift-plant for the reforming of the synthesis gas
- separation device for the separation of CO2
cleaning of hydrogen to 4.0 quality - heat exchanger for heat loss
- pipework within the container
control and regulation device for the plant with access to remote maintenance - container, if needed with induce ventilation and gas detection device
- technical plant documentation, operating instructions, spare parts recommendation with delivery periods, maintenance schedule, CE- approval, TÜV-approval
- H2 transfer station incl. H2 tank (pressure tank 40bar)
incl. compressor for the compression to 40bar
bF H2 300
bf H2 300 | Organic raw material with 30 % dry substrate level | 560 t/a |
|---|---|
Power consumption | 185.000 kWh/a |
Output* hydrogen | 24,2 t/a |
Process heat | 375.000 kWh/a |
CO2 reduction | 250 t/a |
Plant measurements H/W/L in m | 15,0|10,0|8,0 |
bF H2 600
bf H2 600 | Organic raw material with 30 % dry substrate level | 1.120 t/a |
|---|---|
Power consumption | 370.000 kWh/a |
Output* hydrogen | 48,5 t/a |
Process heat | 750.000 kWh/a |
CO2 reduction | 500 t/a |
Plant measurements H/W/L in m | 15,0|10,0|8,0 |
bF H2 1500
bf H2 1500 | Organic raw material with 30 % dry substrate level | 2.800 t/a |
|---|---|
Power consumption | 925.000 kWh/a |
Output* hydrogen | 121,2 t/a |
Process heat | 1.875.000 kWh/a |
CO2 reduction | 1.250 t/a |
Plant measurements H/W/L in m | 15,0|12,0|8,0 |
bF H2 3000
bf H2 3000 | Organic raw material with 30 % dry substrate level | 5.600 t/a |
|---|---|
Power consumption | 1.850.000 kWh/a |
Output* hydrogen | 242,5 t/a |
Process heat | 3.750.000 kWh/a |
CO2 reduction | 2.500 t/a |
Plant measurements H/W/L in m | 18,0|12,0|10,0 |
bF H2 6000
bf H2 6000 | Organic raw material with 30 % dry substrate level | 11.200 t/a |
|---|---|
Power consumption | 3.700.000 kWh/a |
Output* hydrogen | 483,0 t/a |
Process heat | 7.500.000 kWh/a |
CO2 reduction | 5.000 t/a |
Plant measurements H/W/L in m | 20,0|15,0|10,0 |
bF H2 10000
bf H2 10000 | Organic raw material with 30 % dry substrate level | 18.667 t/a |
|---|---|
Power consumption | 6.100.000 kWh/a |
Output* hydrogen | 805,0 t/a |
Process heat | 12.500.000 kWh/a |
CO2 reduction | 8.333 t/a |
Plant measurements H/W/L in m | 23,0|15,0|10,0 |
*Output depending on the plant configuration