2014
DOI: 10.2172/1271650
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Process Design and Economics for the Conversion of Algal Biomass to Biofuels: Algal Biomass Fractionation to Lipid-and Carbohydrate-Derived Fuel Products

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Cited by 57 publications
(137 citation statements)
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“…The stream flows were used for equipment sizing and associated costs. Details are in Davis et al [6], but in summary, this study established that the fractionation approach could achieve a selling price of $4.35 per gallon of gasoline equivalent (GGE) in 2011 dollars for a high-lipid (41 wt%) Scenedesmus feedstock and $5.04/GGE for a lowerlipid (27 wt%) Scenedesmus feedstock if projected improvements in process operating conditions and conversion yields were achieved. Although Davis et al [6] considered ethanol production, the carbohydrate fraction could, in principle, be converted to other fuels or higher value products.…”
Section: Introductionmentioning
confidence: 73%
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“…The stream flows were used for equipment sizing and associated costs. Details are in Davis et al [6], but in summary, this study established that the fractionation approach could achieve a selling price of $4.35 per gallon of gasoline equivalent (GGE) in 2011 dollars for a high-lipid (41 wt%) Scenedesmus feedstock and $5.04/GGE for a lowerlipid (27 wt%) Scenedesmus feedstock if projected improvements in process operating conditions and conversion yields were achieved. Although Davis et al [6] considered ethanol production, the carbohydrate fraction could, in principle, be converted to other fuels or higher value products.…”
Section: Introductionmentioning
confidence: 73%
“…This study presents an LCA of energy use and greenhouse gas emissions for algal biofuels produced via the fractionation process as modeled by Davis et al [6]. The LCA considered all operations in the fuel pathway, including upstream material and energy provisioning operations, cultivation, and final fuel use.…”
Section: Contents Lists Available At Sciencedirectmentioning
confidence: 99%
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“…Conversion of algal biomass to hydrocarbon blendstock has been modeled via a lipid-extraction step to remove the non-lipid component, followed by hydrotreatment of the lipids to generate renewable diesel blendstock (RDB) [34]. In addition, ethanol is produced via fermentation of the non-lipid component and electricity is generated from anaerobic digestion of waste components and combined heat and power system (CHP) ( Figure 5A).…”
Section: Sustainability Considerations For Algal Conversion Processmentioning
confidence: 99%