blueFLUX H2 – green hydrogen
Plant for the production of carbon, biochar or charcoal for a subsequent thermal gasification into green hydrogen or for further usage.
Design for e.g. sewage sludge with a dry substrate level of 30%. It is possible to increase the dry substrate level upon consultation. Exact data is going to be determined within our preliminary 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 (pressure 10 – 16 bar)
- heating of the added vapour in order to save O2
- 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
- O2-generator for the production of oxygen
- 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
- electrical connection, from installation type bF6000 also gas-powered possible
- 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 |
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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 |
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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 |
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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 |
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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 |
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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 |
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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