Bio-oil fractionation by temperature-swing extraction: Principle and application

Shushil Kumar, Jean-Paul Lange*, Guus van Rossum, Sascha R.A. Kersten

*Corresponding author for this work

Research output: Contribution to journalArticleAcademicpeer-review

24 Citations (Scopus)
55 Downloads (Pure)

Abstract

Bio-oils produced by direct thermal liquefaction often contain heavy components that hinder their utilization as a liquefaction medium. This paper reports a new approach to fractionate the liquefaction bio-oil into a light and a heavy fraction based on solvent extraction and temperature-swing regeneration. This approach is based on hot extraction (T ∼ 70 °C) of the light fraction of the oil with a suitable extraction solvent followed by cold (T ∼ 25 °C) de-mixing of the light fraction and the extraction solvent. In this paper, we (i) illustrate the selection of the extraction solvent and define the solvent properties required, (ii) demonstrate the potential of multistage extraction/regeneration for the bio-oil produced by direct thermal liquefaction, (iii) extend the concept to fractionate a petroleum crude oil, (iv) discuss the theoretical basis of the fractionation using polymer solution theory and, finally, (v) show a low energy requirement of the extraction process by means of process simulation, i.e., an equivalent of ∼1% of the biomass intake.
Original languageEnglish
Pages (from-to)96-104
Number of pages9
JournalBiomass & bioenergy
Volume83
Early online date19 Sept 2015
DOIs
Publication statusPublished - Dec 2015

Keywords

  • Liquefaction
  • Temperature-swing
  • Extraction
  • Bio-oil
  • Biomass
  • Polymer solution theory
  • 2023 OA procedure

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