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 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 | 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 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 |
Oleochemical processing | Epoxidation | Epoxidation for epoxidized oil production | Pyrolysis oil (2.7125 m3/hour) | | | 93 |
Oleochemical processing | Amines via nitrile route | Nitrile route to fatty aminesproduction | Pyrolysis oil (2.7125 m3/hour) | | | 86 |
Oleochemical processing | Polyamidation | Polyamidation for polyamide production | Pyrolysis oil (2.7125 m3/hour) | | | 91 |
Oleochemical processing | Hydrolysis | Hydrolysis for short chain fatty acids production | Pyrolysis oil (2.7125 m3/hour) | | | 92 |
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 | 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 | 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 | Esterification | Esterification for fatty esters production | Pyrolysis oil (2.7125 m3/hour) | | | 96 |
Oleochemical processing | Amidation | Amidation for fatty amines production | Pyrolysis oil (2.7125 m3/hour) | | | 97 |
Oleochemical processing | Transesterification | Transesterification for FAME production | Pyrolysis oil (2.7125 m3/hour) | Oil from Camelina, Oil from Ethiopian Mustard seed | | 83 |
Oleochemical processing | Hydrogenation | Hydrogenation for fatty alcohols production | Pyrolysis oil (2.7125 m3/hour) | | | 87 |
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