Oleochemical processing | Transesterification | Transesterification for FAME production | Pyrolysis oil (2.7125 m3/hour) | Oil from Camelina, Oil from Ethiopian Mustard seed | | 83 |
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 |
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 | 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 |
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 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 | 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 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 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 |
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 |
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 |
Oleochemical processing | Polycondensation | Polycondensation for alkyd resins production | Pyrolysis oil (2.7125 m3/hour) | | | 90 |
Oleochemical processing | Polyamidation | Polyamidation for polyamide production | Pyrolysis oil (2.7125 m3/hour) | | | 91 |
Direct combustion of solid biomass | Domestic pellet burners for heat | Pellet boiler for heat | Heat (0.02 MWth) | Stemwood from final fellings originating from nonconifer trees, Stemwood from final fellings originating from conifer trees, Sawdust from sawmills from nonconifers, Sawdust from sawmills from conifers | Level 9, System ready for full scale deployment | 33 |
Oleochemical processing | Oxidative cleavage | Oxidative cleavage for carboxylic acids production | Pyrolysis oil (2.7125 m3/hour) | | | 95 |
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 | 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 |
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 |
Oleochemical processing | Intermolecular condensation | Intermolecular condensation for oligormers production | Pyrolysis oil (2.7125 m3/hour) | | | 88 |
Oleochemical processing | Hydrolysis | Hydrolysis for short chain fatty acids production | Pyrolysis oil (2.7125 m3/hour) | | | 92 |
Oleochemical processing | Hydrogenation | Hydrogenation for fatty alcohols production | Pyrolysis oil (2.7125 m3/hour) | | | 87 |
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 |
Extraction of fibers | Hemp fiber processing for pulp and paper | Hemp fiber processing for pulp and paper | Pyrolysis oil (2.7125 m3/hour) | | | 100 |
Extraction of fibers | Hemp fiber processing for composite material | Hemp fiber processing for composite material | Pyrolysis oil (2.7125 m3/hour) | | | 98 |
Extraction of fibers | Hemp fiber processing for agro textile | Hemp fiber processing for agro textile | Pyrolysis oil (2.7125 m3/hour) | | | 99 |
Oleochemical processing | Heat polymerisation | Heat polymerisation for blown/stand oil production | Pyrolysis oil (2.7125 m3/hour) | | | 89 |
Direct combustion of solid biomass | Waste incinerators with energy recovery | Grate fired waste incinerator | Power (10 MWe), Heat (25 MWth) | Hazardous post consumer wood, Non hazardous post consumer wood, Biowaste as part of integrally collected municipal waste: Biodegradable waste of not separately collected municipal waste (excluding textile and paper) | Level 9, System ready for full scale deployment | 32 |
Direct combustion of solid biomass | Fixed bed combustion for heat | Grate boiler with wood chips for heat | Heat (15 MWth) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Non hazardous post consumer wood, Residues from further woodprocessing, Bark residues from pulp and paper industry | Level 9, System ready for full scale deployment | 29 |
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