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  • Wiley  (2)
  • Kim, Hoyong  (2)
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  • Wiley  (2)
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  • 1
    In: Biofuels, Bioproducts and Biorefining, Wiley, Vol. 15, No. 2 ( 2021-03), p. 404-415
    Abstract: Sugar derived from lignocellulosic biomass is an important intermediate product, often used for the production of biofuels and value‐added chemicals. It is therefore essential to understand and reduce the production costs of sugar derived from lignocellulosic biomass. This study evaluates the economic feasibility of a biorefinery producing sugar from lignocellulosic biomass using a combination of autohydrolysis and mechanical refining pretreatment. This biorefinery is self‐sufficient in energy, producing excess electricity for sale. The minimum sugar selling price (MSSP) that achieves a zero net present value is $446/metric ton. The possibility of using the two main by‐products, dissolved hemicellulose and lignin, for the production of high‐value products, xylitol and polyol, is also evaluated. When dissolved hemicellulose is used for xylitol production, the MSSP decreases to $347/metric ton. When lignin is liquefied to produce polyol, the MSSP is further reduced to $342/metric ton. External energy (natural gas) must be purchased if xylitol and polyol are produced. An analysis of capital and operating costs reveals that, although the production of xylitol and polyol incurs additional capital investment, their correspondingly high values outweigh the additional capital costs. Sensitivity analysis results indicate that efficient recovery and recycling of expensive chemicals like acetone and glycerol are key to the success of the biorefinery. Yields of xylitol and polyol also have strong impacts on the process economics. © 2020 Society of Industrial Chemistry and John Wiley & Sons Ltd
    Type of Medium: Online Resource
    ISSN: 1932-104X , 1932-1031
    URL: Issue
    Language: English
    Publisher: Wiley
    Publication Date: 2021
    detail.hit.zdb_id: 2381232-1
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  • 2
    Online Resource
    Online Resource
    Wiley ; 2018
    In:  Biofuels, Bioproducts and Biorefining Vol. 12, No. 3 ( 2018-05), p. 442-452
    In: Biofuels, Bioproducts and Biorefining, Wiley, Vol. 12, No. 3 ( 2018-05), p. 442-452
    Abstract: Feedstock properties are an important factor affecting the process yields and economics of fast‐pyrolysis biorefineries. This study develops a fast‐pyrolysis process model sensitive to feedstock properties based on experimental results. Sixty‐four simulations are run to evaluate the impacts of carbon, ash, and moisture content in biomass feedstocks on process yields and energy consumptions. An economic analysis is conducted for each run to quantify process economics under different feedstock properties. With biomass feedstocks of 48% carbon and 15% moisture, minimum fuel selling price (MFSP) increases from $0.97/L to $1.06/L when ash content increases from 1% to 7%, due to reduced hydrocarbon yields. With biomass feedstocks of 48% carbon and 3% ash content, MFSP increases from $1.03/L to $1.08/L when feedstock moisture increases from 15% to 45% as a consequence of increased energy demand for feedstock drying. The impact of feedstock ash content decreases gradually as ash content increases. Feedstock carbon content has less significant impacts on process economics in this study. © 2018 Society of Chemical Industry and John Wiley & Sons, Ltd
    Type of Medium: Online Resource
    ISSN: 1932-104X , 1932-1031
    URL: Issue
    Language: English
    Publisher: Wiley
    Publication Date: 2018
    detail.hit.zdb_id: 2381232-1
    Location Call Number Limitation Availability
    BibTip Others were also interested in ...
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