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      Comparative techno‐economic analysis and process design for indirect liquefaction pathways to distillate‐range fuels via biomass‐derived oxygenated intermediates upgrading

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          Abstract

          This paper presents a comparative techno‐economic analysis ( TEA) of five conversion pathways from biomass to gasoline‐, jet‐, and diesel‐range hydrocarbons via indirect liquefaction with a specific focus on pathways utilizing oxygenated intermediates. The four emerging pathways of interest are compared with one conventional pathway (Fischer‐Tropsch) for the production of the hydrocarbon blendstocks. The processing steps of the four emerging pathways include biomass‐to‐syngas via indirect gasification, syngas clean‐up, conversion of syngas to alcohols/oxygenates followed by conversion of alcohols/oxygenates to hydrocarbon blendstocks via dehydration, oligomerization, and hydrogenation. Conversion of biomass‐derived syngas to oxygenated intermediates occurs via three different pathways, producing: (i) mixed alcohols over a MoS 2 catalyst, (ii) mixed oxygenates (a mixture of C 2 + oxygenated compounds, predominantly ethanol, acetic acid, acetaldehyde, ethyl acetate) using an Rh‐based catalyst, and (iii) ethanol from syngas fermentation. This is followed by the conversion of oxygenates/alcohols to fuel‐range olefins in two approaches: (i) mixed alcohols/ethanol to 1‐butanol rich mixture via Guerbet reaction, followed by alcohol dehydration, oligomerization, and hydrogenation, and (ii) mixed oxygenates/ethanol to isobutene rich mixture and followed by oligomerization and hydrogenation. The design features a processing capacity of 2000 tonnes/day (2205 short tons) of dry biomass. The minimum fuel selling prices ( MFSPs) for the four developing pathways range from $3.40 to $5.04 per gasoline‐gallon equivalent ( GGE), in 2011 US dollars. Sensitivity studies show that MFSPs can be improved with co‐product credits and are comparable to the commercial Fischer‐Tropsch benchmark ($3.58/ GGE). Overall, this comparative TEA study documents potential economics for the developmental biofuel pathways via mixed oxygenates. © 2016 Society of Chemical Industry and John Wiley & Sons, Ltd

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          Most cited references44

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          Synthesis of transportation fuels from biomass: chemistry, catalysts, and engineering.

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            Review of fast pyrolysis of biomass and product upgrading

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              Integrated catalytic conversion of gamma-valerolactone to liquid alkenes for transportation fuels.

              Efficient synthesis of renewable fuels remains a challenging and important line of research. We report a strategy by which aqueous solutions of gamma-valerolactone (GVL), produced from biomass-derived carbohydrates, can be converted to liquid alkenes in the molecular weight range appropriate for transportation fuels by an integrated catalytic system that does not require an external source of hydrogen. The GVL feed undergoes decarboxylation at elevated pressures (e.g., 36 bar) over a silica/alumina catalyst to produce a gas stream composed of equimolar amounts of butene and carbon dioxide. This stream is fed directly to an oligomerization reactor containing an acid catalyst (e.g., H ZSM-5, Amberlyst-70), which couples butene monomers to form condensable alkenes with molecular weights that can be targeted for gasoline and/or jet fuel applications. The effluent gaseous stream of CO2 at elevated pressure can potentially be captured and then treated or sequestered to mitigate greenhouse gas emissions from the process.
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                Author and article information

                Journal
                Biofuels, Bioproducts and Biorefining
                Biofuels Bioprod Bioref
                Wiley
                1932-104X
                1932-1031
                January 2017
                September 27 2016
                January 2017
                : 11
                : 1
                : 41-66
                Affiliations
                [1 ] National Renewable Energy Laboratory Golden CO USA
                [2 ] Pacific Northwest National Laboratory Richland WA USA
                Article
                10.1002/bbb.1710
                59400384-1712-404d-921c-b721c7ca1b3b
                © 2017

                http://onlinelibrary.wiley.com/termsAndConditions#am

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