Impacts of retrofitting analysis on first generation ethanol production: process design and techno-economics
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  • 作者:Karthik Rajendran ; Sreevathsava Rajoli…
  • 关键词:Process design ; Retrofitting analysis ; Ethanol ; Aspen plus ; Techno ; economic analysis
  • 刊名:Bioprocess and Biosystems Engineering
  • 出版年:2015
  • 出版时间:February 2015
  • 年:2015
  • 卷:38
  • 期:2
  • 页码:389-397
  • 全文大小:1,734 KB
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  • 作者单位:Karthik Rajendran (1)
    Sreevathsava Rajoli (1)
    Oliver Teichert (2)
    Mohammad J. Taherzadeh (1)

    1. Swedish Centre for Resource Recovery, University of Bor?s, 50190, Bor?s, Sweden
    2. Lantm?nnen Agroetanol AB, 60238, Norrk?ping, Sweden
  • 刊物类别:Chemistry and Materials Science
  • 刊物主题:Chemistry
    Biotechnology
    Industrial Chemistry and Chemical Engineering
    Industrial and Production Engineering
    Waste Management and Waste Technology
    Waste Water Technology, Water Pollution Control, Water Management and Aquatic Pollution
    Food Science
  • 出版者:Springer Berlin / Heidelberg
  • ISSN:1615-7605
文摘
More than half of the bioethanol plants in operation today use corn or grains as raw materials. The downstream processing of mash after fermentation to produce ethanol and distiller grains is an energy-demanding process, which needs retrofitting for optimization. In addition, the fluctuation in the ethanol and grain prices affects the overall profitability of the plant. For this purpose, a process simulation was performed in Aspen Plus? based on an existing industrial plant located in Sweden. The simulations were compared using different scenarios including different concentrations of ethanol, using the stillage for biogas production to produce steam instead of distiller grains as a by-product, and altering the purity of the ethanol produced. Using stillage for biogas production, as well as utilizing the steam, reduced the overall energy consumption by 40?% compared to the plant in operation. The fluctuations in grain prices had a high impact on the net present value (NPV), where grain prices greater than 349 USD/ton reached a zero NPV. After 20?years, the plant in operation producing 41,600 tons ethanol/year can generate a profit of 78 million USD. Compared to the base case, the less purified ethanol resulted in a lower NPV of 30 million USD.

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