Gasification technologies | Bubbling fluidized bed for syngas production | BFB for syngas | Heat (45 MWth), Methanol (26 m3/hour) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Bark residues from pulp and paper industry, Residues from further woodprocessing, Non hazardous post consumer wood | Level 7, Integrated pilot system demonstrated | 15 |
Gasification technologies | Fixed bed (updraft), direct combustion | Fixed bed, direct combustion | Heat (5 MWth) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Bark residues from pulp and paper industry, Residues from further woodprocessing, Non hazardous post consumer wood | Level 9, System ready for full scale deployment | 13 |
Gasification technologies | Fixed bed (downdraft) for CHP (gas engine) | Fixed bed for CHP | Power (0.05 MWe), Heat (0.1 MWth) | Stemwood from thinnings originating from nonconifer trees, Stemwood from final fellings originating from conifer trees | Level 9, System ready for full scale deployment | 12 |
Gasification technologies | Dual Fluidized bed for syngas production | DFB for syngas | Heat ( MWth), Methane ( m3/hour) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Bark residues from pulp and paper industry, Residues from further woodprocessing, Non hazardous post consumer wood | Level 6, Prototype system verified | 10 |
Gasification technologies | Circulating Fluidized bed for syngas production | CFB for syngas | Heat (45 MWth), Methanol (26 m3/hour) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Bark residues from pulp and paper industry, Residues from further woodprocessing, Non hazardous post consumer wood | Level 7, Integrated pilot system demonstrated | 8 |
Gasification technologies | Bubbling fluidized bed for IGCC | BFB for IGCC | Power (63 MWe), Heat (67 MWth) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Bark residues from pulp and paper industry, Residues from further woodprocessing, Non hazardous post consumer wood | Level 6, Prototype system verified | 14 |
Gasification technologies | Entrained flow for syngas production | Entrained flow for syngas | Heat (45 MWth), Methanol (26 m3/hour) | Black liquor | Level 7, Integrated pilot system demonstrated | 11 |
Gasification technologies | Dual Fluidized bed for CHP (gas engine) | DFB for CHP | Power (5 MWe), Heat (10 MWth) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Bark residues from pulp and paper industry, Residues from further woodprocessing, Non hazardous post consumer wood | Level 9, System ready for full scale deployment | 9 |
Gasification technologies | Bubbling fluidized bed for CHP (gas engine) | BFB for CHP | Power (5 MWe), Heat (8 MWth) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Bark residues from pulp and paper industry, Residues from further woodprocessing, Non hazardous post consumer wood | Level 9, System ready for full scale deployment | 7 |
Gasification technologies | Circulating Fluidized bed for IGCC | CFB for IGCC | Power (63 MWe), Heat (90 MWth) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Bark residues from pulp and paper industry, Residues from further woodprocessing, Non hazardous post consumer wood | Level 7, Integrated pilot system demonstrated | 6 |
Gasification technologies | Circulating Fluidized bed for CHP (gas engine) | CFB for CHP | Power (10 MWe), Heat (15 MWth) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Bark residues from pulp and paper industry, Residues from further woodprocessing, Non hazardous post consumer wood | Level 7, Integrated pilot system demonstrated | 5 |
Oleochemical processing | Olefin metathesis | Olefin metathesis for chemical building blocks production | Pyrolysis oil (2.7125 m3/hour) | | | 94 |
Oleochemical processing | Amines via nitrile route | Nitrile route to fatty aminesproduction | Pyrolysis oil (2.7125 m3/hour) | | | 86 |
Oleochemical processing | Hydrogenation | Hydrogenation for fatty alcohols production | Pyrolysis oil (2.7125 m3/hour) | | | 87 |
Oleochemical processing | Alkali pyrolysis | Alkali pyrolysis for fatty acids production (Sebacic Acid DC10, 2- Octanol) | Pyrolysis oil (2.7125 m3/hour) | Oil from Castor bean | | 81 |
Oleochemical processing | Intermolecular condensation | Intermolecular condensation for oligormers production | Pyrolysis oil (2.7125 m3/hour) | | | 88 |
Oleochemical processing | Heat polymerisation | Heat polymerisation for blown/stand oil production | Pyrolysis oil (2.7125 m3/hour) | | | 89 |
Oleochemical processing | Polyamidation | Polyamidation for polyamide production | Pyrolysis oil (2.7125 m3/hour) | | | 91 |
Oleochemical processing | Oxidative cleavage | Oxidative cleavage for acids production (Azelaic DC9 and Pelargonic acid C9) | Pyrolysis oil (2.7125 m3/hour) | Oil from High oleic acid Safflower | | 82 |
Oleochemical processing | Transesterification | Transesterification for FAME production | Pyrolysis oil (2.7125 m3/hour) | Oil from Camelina, Oil from Ethiopian Mustard seed | | 83 |
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