4.8 Article

Techno-economic and energetic assessment of an innovative pilot-scale thermosyphon-assisted falling film distillation unit for sanitizer-grade ethanol recovery

Journal

APPLIED ENERGY
Volume 297, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.apenergy.2021.117185

Keywords

Falling film distillation; Two-phase closed thermosyphon; Energy-intensified apparatus; Techno-economic analysis; Ethanol recovery; Sanitizer-grade ethanol

Funding

  1. Coordination for the Improvement of Higher Education Personnel (CAPES) [001]
  2. Petrobras (Petroleo Brasileiro S.A.)
  3. IFSC (Federal Institute for Education, Science and Technology of Santa Catarina)
  4. FAPESC (Santa Catarina State Foundation for Research and Innovation Support)
  5. PoliMi (Politecnico di Milano)
  6. UFSC (Federal University of Santa Catarina)

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The research has developed a novel technology for extracting sanitizer-grade ethanol, and based on experimental data has demonstrated its effectiveness and cost-saving advantages.
The increasing demand for ethanol-based disinfectants due to the COVID-19 pandemic has driven the emergence of innovative strategies to avoid the risk of shortage and reduce production costs. Distillation is well-known as the major energy consumer and cost driver for ethanol recovery in conventional distilleries. Our research team has been developing a novel heat-intensified falling film distillation apparatus assisted by a two-phase closed thermosyphon, patented as Destubcal. Therefore, this study aims to provide a techno-economic and energetic assessment of the pilot-scale thermosyphon-assisted falling film distillation unit applied to recover sanitizergrade ethanol with 70 vol% in alcohol. Performance analysis showed that under a feed flow rate of 14 L/h, a feed temperature of 80 degrees C, and an evaporator temperature of 93 degrees C, the pilot-scale unit reaches the minimum specific thermal energy consumption with the maximum distillate ethanol recovery and energy efficiency (88.5%). The impact of the elements in the capital cost-share showed instrumentation and control (27.8%), and piping and auxiliary equipment (27.6%) as the predominant capital costs, while the cost for major process equipment represents only 6.2% which reveals a low-cost and easy-to-implement technology. The major operating cost-driver is the labor (51.3%) since the pilot-scale unit has a lower capacity than industrial plants. However, the Destubcal unit spends on utility costs about 31.6 $/m(feed)(3), which represents a total saving of 43.8% compared to conventional distilleries. Furthermore, the Destubcal unit saves about 1.78 MJ/kg (46.4%), with 59.2% less column height than a conventional column, being considered techno-economically feasible for sanitizer-grade ethanol recovery.

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