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• W350345162 abstract "This thesis is an exploration into the technical and economic issues related to a syngas fermenting biorefinery producing 50 metric tons per day of hydrogen gas and 12 metric tons per day of PHA, a biodegradable plastic. In addition, an optimization study on the bioreactor is performed by varying reactor diameter and stirring speed. The analysis assumed switchgrass costing $55/Mg as feedstock, and the bacterium Rhodospirillum rubrum to ferment the syngas. With a hydrogen market value of $1.90/kg assumed, 95% pure PHA was determined producible for approximately $2.05/kg. Grassroots capital for the biorefinery was estimated to be $55 million, with annual operating costs at $8.3 million. For a constant volumetric mass transfer coefficient of 0.05 s the optimum reactor size was a 14.8 m diameter being stirred at 0.6 rev/s. Producing PHA by this method was found to be less expensive than processes using sugar fermentation." @default.
• W350345162 created "2016-06-24" @default.
• W350345162 creator A5023651894 @default.
• W350345162 date "2018-08-13" @default.
• W350345162 modified "2023-09-25" @default.
• W350345162 title "A techno-economic analysis of syngas fermentation for the production of hydrogen and polyhydroxyalkanoate" @default.
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• W350345162 doi "https://doi.org/10.31274/rtd-180813-15834" @default.
• W350345162 hasPublicationYear "2018" @default.
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