10 - Hydrofaction™ of forestry residues to drop-in renewable transportation fuels
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Cited by (23)
Biomass to biofuels using hydrothermal liquefaction: A comprehensive review
2024, Renewable and Sustainable Energy ReviewsBest practices for bio-crude oil production at pilot scale using continuous flow reactors
2022, 3rd Generation Biofuels: Disruptive Technologies to Enable Commercial ProductionTreatment of hydrothermal liquefaction wastewater with ultrafiltration and air stripping for oil and particle removal and ammonia recovery
2021, Journal of Water Process EngineeringComparative life cycle energy and greenhouse gas footprints of dry and wet torrefaction processes of various biomass feedstocks
2021, Journal of Environmental Chemical EngineeringCitation Excerpt :Some stages have been shown to have a very low impact on overall life cycle GHG emissions and energy consumption of biochar production (via pyrolysis), i.e., farm equipment manufacturing, plant construction and dismantling [20,38]. Plant infrastructure and construction emissions of pyrolysis and hydrothermal liquefaction plants were found to make a very small share of total emissions (less than 1% for both processes) [20,38] and many studies of thermochemical conversion of biomass do not include these emissions [20,39,40]. While environmental impacts such as mineral extraction and ecotoxicity are high for plant construction, decommissioning, and farm equipment manufacturing, they typically are responsible for less than 5% of the total GHG emissions of pellet combustion [41,42].
Integration of hydrothermal liquefaction and carbon capture and storage for the production of advanced liquid biofuels with negative CO<inf>2</inf> emissions
2020, Applied EnergyCitation Excerpt :Since there is no data available on the composition of the aqueous phase produced through hydrotreatment, one component was selected as representative of the organic loading of this phase in order to close the mass balance and minimize atom imbalance across the process. The hydrogen consumption is fixed at 0.04 g/g oil, which is in the range reported in [19], and the total available hydrogen is set as 10 times the required (0.4 g/g oil). The production of other gas phase compounds is determined based on the composition of the gas effluent reported in Table 3 for a larger excess (hydrogen consumption of 1.9% of the initial).