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 |
Direct combustion of solid biomass | Fixed bed combustion for CHP (steam cycle) | Grate boiler with wood chips 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, Non hazardous post consumer wood, Residues from further woodprocessing, Bark residues from pulp and paper industry | Level 9, System ready for full scale deployment | 30 |
Direct combustion of solid biomass | Fixed bed combustion for heat | Grate boiler with straw for heat | Heat (2 MWth) | Cereals straw, Giant reed (Perennial grass) | Level 9, System ready for full scale deployment | 75 |
Direct combustion of solid biomass | Fixed bed combustion for CHP (steam cycle) | Grate boiler with agrobiomass for CHP | Power (10 MWe), Heat (20 MWth) | Cereals straw, Giant reed (Perennial grass) | Level 9, System ready for full scale deployment | 73 |
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 |
Extraction of fibers | Hemp fiber processing for insulation material, VC example | Fiber processing of hemp to insulation material | Pyrolysis oil (2.7125 m3/hour) | Industrial hemp | | 85 |
Biochemical hydrolysis and fermentation | Fermentation | Fermentation alkaline pretreated | Ethanol (10.2 m3/hour) | | Level 9, System ready for full scale deployment | 56 |
Biochemical hydrolysis and fermentation | Fermentation | Fermentation acid pretreated | Ethanol (7.58 m3/hour) | | Level 9, System ready for full scale deployment | 62 |
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 |
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 | 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 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 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 + 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 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 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 |
Extraction of protein | Extraction of micellar lupin protein, VC example | Extraction of micellar lupin protein | Pyrolysis oil (2.7125 m3/hour) | Lupin seed | | 84 |
Biochemical ethanol and biobased products | Simultaneous saccharification and fermentation | Ethanol from lignocellulose (dilute acid pretreatment), value chain example | Power (13.7 MWe), Ethanol (27.5 m3/hour) | Cereals straw, Maize stover | Level 8, System integrated in commercial design | 65 |
Oleochemical processing | Esterification | Esterification for fatty esters production | Pyrolysis oil (2.7125 m3/hour) | | | 96 |
Oleochemical processing | Epoxidation | Epoxidation for epoxidized oil production | Pyrolysis oil (2.7125 m3/hour) | | | 93 |
Biochemical hydrolysis and fermentation | Enzymatic hydrolysis | Enzymatic hydrolysis alkaline pretreated | Lignin (2.85 tonnes/hour), Glucose (10.75 tonnes/hour), Xylose (7.2 tonnes/hour) | | Level 9, System ready for full scale deployment | 55 |
Biochemical hydrolysis and fermentation | Enzymatic hydrolysis | Enzymatic hydrolysis acid pretreated | Lignin (7.74 tonnes/hour), Glucose (10.75 tonnes/hour), Xylose (2.55 tonnes/hour) | | Level 9, System ready for full scale deployment | 60 |
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 |
Anaerobic digestion | Plug flow digester | Dry Batch Digestion (MSW) | Power (1 MWe), Biogas (700 m3/hour), Methane (420 m3/hour) | Biowaste as part of integrally collected municipal waste: Biodegradable waste of not separately collected municipal waste (excluding textile and paper), Separately collected biowaste: Biodegradable waste of separately collected municipal waste (excluding textile and paper) | Level 9, System ready for full scale deployment | 35 |
Chemical pretreatment | Dilute acid hydrolysis | Dilute acid hydrolysis | Lignin (7.74 tonnes/hour), Hemicellulose (2.83 tonnes/hour), Cellulose (13.4 tonnes/hour) | Cereals straw, Maize stover | Level 9, System ready for full scale deployment | 57 |
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 | 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 |
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 |
Anaerobic digestion | Complete mix digester | Complete mix digester state of the art 2014 | Power (2 MWe), Heat (3.5 MWth), Biogas (505 m3/hour), Methane (278 m3/hour) | Cereals straw, Maize stover, Sugarbeet leaves, Separately collected biowaste: Biodegradable waste of separately collected municipal waste (excluding textile and paper), Unused grassland cuttings (abandoned grassland, managed grasslands not used for feed) | Level 9, System ready for full scale deployment | 2 |
Direct combustion of solid biomass | Direct co-combustion in coal fired power plants | Co-firing in PC | Power (500 MWe) | Sawdust from sawmills from nonconifers, Sawdust from sawmills from conifers, Stemwood from final fellings originating from nonconifer trees, Stemwood from final fellings originating from conifer trees | Level 9, System ready for full scale deployment | 31 |
Direct combustion of solid biomass | Fluidised bed combustion for CHP (steam cycle) | Circulating fluidised bed combustion for CHP (steam cycle) | Power (50 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 9, System ready for full scale deployment | 4 |
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 |
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 | 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 |
Direct combustion of solid biomass | Fluidised bed combustion for CHP (steam cycle) | Bubbling fluidised bed combustion for CHP (steam cycle) | Power (50 MWe), Heat (100 MWth) | Logging residues from final fellings originating from nonconifer trees, Logging residues from final fellings originating from conifer trees, Residues from further woodprocessing, Non hazardous post consumer wood, Bark residues from pulp and paper industry | Level 9, System ready for full scale deployment | 3 |
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 | 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 |
Direct combustion of solid biomass | Domestic residential batch fired stoves for heat | Batch stove for heat | Heat (0.015 MWth) | 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 | 34 |
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 |
Oleochemical processing | Amidation | Amidation for fatty amines production | Pyrolysis oil (2.7125 m3/hour) | | | 97 |
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 |
Chemical pretreatment | Alkaline hydrolysis | Alkaline hydrolysis | Lignin (2.9 tonnes/hour), Hemicellulose (8.0 tonnes/hour), Cellulose (13.4 tonnes/hour) | Cereals straw, Maize stover | Level 7, Integrated pilot system demonstrated | 54 |
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