| Treatment in subcritical water | Hydrothermal processing | HTC Hydrothermal carbonisation of biowaste to coal for CHP | Biocoal (2.1 tonnes/hour) | Separately collected biowaste: Biodegradable waste of separately collected municipal waste (excluding textile and paper), Biowaste as part of integrally collected municipal waste: Biodegradable waste of not separately collected municipal waste (excluding textile and paper), Other by-products and residues from food and fruit processing industry | Level 7, Integrated pilot system demonstrated | 74 |
| Treatment in subcritical water | Aqueous Phase Reforming | Aqueous Phase Reforming | Gasoline (5.4 liter/hour) | Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees | Level 5, Laboratory testing integrated system | 27 |
| Torrefaction | Moving bed reactor | Torrefaction and pelletisation (TOP) | Torrefied biomass (10.7 m3/hour) | Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees | Level 9, System ready for full scale deployment | 18 |
| Techniques from pulp and paper industry | Prehydrolysis Kraft process in water phase | Prehydrolysis kraft | Power (76 MWe), Pulp (75 tonnes/hour), Hemicellulose (0 tonnes/hour), Tall oil (3 tonnes/hour), Turpentine (0.4 tonnes/hour) | Stemwood from final fellings originating from nonconifer trees, Stemwood from final fellings originating from conifer trees, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees | Level 9, System ready for full scale deployment | 17 |
| Techniques from pulp and paper industry | Kraft process with LignoBoost process | Kraft process with Lignoboost | Power (28.7 MWe), Lignin (10.1 tonnes/hour), Pulp (75 tonnes/hour), Tall oil (3.3 tonnes/hour), Turpentine (0.4 tonnes/hour) | Stemwood from final fellings originating from nonconifer trees, Stemwood from final fellings originating from conifer trees, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees | Level 9, System ready for full scale deployment | 16 |
| Syngas platform | Fluidised bed gasification for methanol production | Syngas to methanol | Heat (45 MWth), Methanol (41.8 m3/hour) | Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings 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 | 41 |
| Syngas platform | Indirect gasification for SNG production | Producer gas to biomethane | Methane (11850 m3/hour) | Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings 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 | 44 |
| Syngas platform | Fluidised bed gasification for FT-fuels production | Syngas to FT-diesel | Power (1.5 MWe), Heat (26 MWth), FT-diesel (16 m3/hour) | Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings 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 | 52 |
| Oleochemical processing | Hydrolysis | Hydrolysis for short chain fatty acids production | Pyrolysis oil (2.7125 m3/hour) | | | 92 |
| 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 | Polycondensation | Polycondensation for alkyd resins production | Pyrolysis oil (2.7125 m3/hour) | | | 90 |
| Oleochemical processing | Intermolecular condensation | Intermolecular condensation for oligormers production | Pyrolysis oil (2.7125 m3/hour) | | | 88 |
| Oleochemical processing | Olefin metathesis | Olefin metathesis for chemical building blocks production | Pyrolysis oil (2.7125 m3/hour) | | | 94 |
| Oleochemical processing | Oxidative cleavage | Oxidative cleavage for carboxylic acids production | Pyrolysis oil (2.7125 m3/hour) | | | 95 |
| Oleochemical processing | Esterification | Esterification for fatty esters production | Pyrolysis oil (2.7125 m3/hour) | | | 96 |
| Oleochemical processing | Hydrogenation | Hydrogenation for fatty alcohols production | Pyrolysis oil (2.7125 m3/hour) | | | 87 |
| Oleochemical processing | Heat polymerisation | Heat polymerisation for blown/stand oil production | Pyrolysis oil (2.7125 m3/hour) | | | 89 |
| Oleochemical processing | Amines via nitrile route | Nitrile route to fatty aminesproduction | Pyrolysis oil (2.7125 m3/hour) | | | 86 |
| Oleochemical processing | Transesterification | Transesterification for FAME production | Pyrolysis oil (2.7125 m3/hour) | Oil from Camelina, Oil from Ethiopian Mustard seed | | 83 |
| Oleochemical processing | Epoxidation | Epoxidation for epoxidized oil production | Pyrolysis oil (2.7125 m3/hour) | | | 93 |
| 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 | Amidation | Amidation for fatty amines production | Pyrolysis oil (2.7125 m3/hour) | | | 97 |
| 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 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 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 |
| 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 | 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 | 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 | 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 | 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 | 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 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 | 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 |
| Fast pyrolysis | Pyrolysis plus boiler for heat and steam | Residues pyrolysis + CHP plant, value chain example | Power (3.7 MWe), Heat (12.4 MWth) | Cereals straw, Sunflower straw, Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees | Level 6, Prototype system verified | 72 |
| Fast pyrolysis | Pyrolysis oil and diesel engine for electricity | Pyrolysis combustion engine (compression-ignition) | Power (0.25 MWe), Heat (0.25 MWth) | | Level 6, Prototype system verified | 53 |
| Fast pyrolysis | Pyrolysis plus boiler for heat and steam | Pyrolysis oil to steam | Heat (25 MWth) | | Level 9, System ready for full scale deployment | 39 |
| Fast pyrolysis | Pyrolysis plus boiler for heat and steam | Pyrolysis oil to heat | Heat (5 MWth) | | Level 8, System integrated in commercial design | 38 |
| Fast pyrolysis | Pyrolysis oil and diesel engine for electricity | CHP Gas Turbine | Power (1.8 MWe), Heat (4.5 MWth) | | Level 6, Prototype system verified | 63 |
| Fast pyrolysis | Pyrolysis plus boiler for heat and steam | Fast pyrolysis of clean wood | Power (0.33 MWe), Heat (3.2 MWth), Pyrolysis oil (2.667 m3/hour) | Residues from further woodprocessing, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees | Level 8, System integrated in commercial design | 23 |
| Fast pyrolysis | Pyrolysis and hydrogenation for diesel fuel | Pyrolysis oil diesel | Pyrolysis diesel (23.6 m3/hour) | Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees, Sawdust from sawmills from conifers, Sawmill residues: excluding sawdust, conifers, Residues from further woodprocessing | Level 4, Laboratory testing protoype component or process | 40 |
| Fast pyrolysis | Pyrolysis plus boiler for heat and steam | Fast pyrolysis + CHP plant, value chain example | Power (4.13 MWe), Heat (15.24 MWth) | Residues from further woodprocessing, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees | Level 6, Prototype system verified | 70 |
| Fast pyrolysis | Pyrolysis and hydrogenation for diesel fuel | Fast pyrolysis oil thermochemical fractionation to pyrolytic lignin | Pyrolysis oil (2.7125 m3/hour) | Stemwood from final fellings originating from nonconifer trees, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees, SRC Willow, SRC Poplar | | 78 |
| Fast pyrolysis | Pyrolysis plus boiler for heat and steam | Residues pyrolysis + Boiler for heat, value chain example | Power (0.1 MWe), Heat (16.4 MWth) | Cereals straw, Sunflower straw, Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees | Level 7, Integrated pilot system demonstrated | 71 |
| Fast pyrolysis | Pyrolysis plus boiler for heat and steam | Fast pyrolysis + Boiler for heat, value chain example | Power (0.53 MWe), Heat (19.6 MWth) | Residues from further woodprocessing, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees | Level 8, System integrated in commercial design | 67 |
| Fast pyrolysis | Pyrolysis oil and diesel engine for electricity | Fast pyrolysis + Multiple diesel combustion engines, value chain example | Power (5.83 MWe), Heat (8.7 MWth) | Residues from further woodprocessing, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees | Level 6, Prototype system verified | 69 |
| Fast pyrolysis | Pyrolysis plus boiler for heat and steam | Fast pyrolysis of residues | Power (0.1 MWe), Heat (3.4 MWth), Pyrolysis oil (2.7125 m3/hour) | Cereals straw, Sunflower straw, Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees | Level 7, Integrated pilot system demonstrated | 24 |
| Fast pyrolysis | Pyrolysis and hydrogenation for diesel fuel | Co-processing of FPBO in FCC | Pyrolysis oil (2.7125 m3/hour) | Stemwood from final fellings originating from nonconifer trees, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees, SRC Willow, SRC Poplar | | 76 |
| Fast pyrolysis | Pyrolysis plus boiler for heat and steam | Fast pyrolysis + Industrial steam boiler, value chain example | Power (0.66 MWe), Heat (31.4 MWth) | Residues from further woodprocessing, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees | Level 9, System ready for full scale deployment | 68 |
| Fast pyrolysis | Pyrolysis and hydrogenation for diesel fuel | Fast pyrolysis oil thermochemical fractionation to pyrolytic sugars | Pyrolysis oil (2.7125 m3/hour) | Stemwood from final fellings originating from nonconifer trees, Stemwood from thinnings originating from nonconifer trees, Stemwood from thinnings originating from conifer trees, SRC Willow, SRC Poplar | | 77 |
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