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 | 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 |
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 |
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 |
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 |
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 | Polycondensation | Polycondensation for alkyd resins production | Pyrolysis oil (2.7125 m3/hour) | | | 90 |
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 |
Oleochemical processing | Intermolecular condensation | Intermolecular condensation for oligormers production | Pyrolysis oil (2.7125 m3/hour) | | | 88 |
Oleochemical processing | Esterification | Esterification for fatty esters production | Pyrolysis oil (2.7125 m3/hour) | | | 96 |
Oleochemical processing | Amines via nitrile route | Nitrile route to fatty aminesproduction | Pyrolysis oil (2.7125 m3/hour) | | | 86 |
Oleochemical processing | Oxidative cleavage | Oxidative cleavage for carboxylic acids production | Pyrolysis oil (2.7125 m3/hour) | | | 95 |
Oleochemical processing | Olefin metathesis | Olefin metathesis for chemical building blocks production | Pyrolysis oil (2.7125 m3/hour) | | | 94 |
Oleochemical processing | Amidation | Amidation for fatty amines production | Pyrolysis oil (2.7125 m3/hour) | | | 97 |
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 | 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 |
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 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 | 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 | 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 | 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 | 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 |
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