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 |
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 |
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 |
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 |
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 | 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 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 |
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 | 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 | 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 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 |
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 |
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 |
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 |
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 |
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 |
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 | 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 |
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 |
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 |
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 |
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 |
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 |
Oleochemical processing | Epoxidation | Epoxidation for epoxidized oil production | Pyrolysis oil (2.7125 m3/hour) | | | 93 |
Oleochemical processing | Esterification | Esterification for fatty esters production | Pyrolysis oil (2.7125 m3/hour) | | | 96 |
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 |
Extraction of protein | Extraction of micellar lupin protein, VC example | Extraction of micellar lupin protein | Pyrolysis oil (2.7125 m3/hour) | Lupin seed | | 84 |
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 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 |
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