4.7 Article

Recovery of pentoses-containing olive stones for their conversion into furfural in the presence of solid acid catalysts

Journal

PROCESS SAFETY AND ENVIRONMENTAL PROTECTION
Volume 143, Issue -, Pages 1-13

Publisher

ELSEVIER
DOI: 10.1016/j.psep.2020.06.033

Keywords

Lignocellulosic biomass; Hemicellulosic liquors; Olive stones; Xylose dehydration; Furfural; Solid acid catalysts

Funding

  1. Spanish Ministry of Economy and Competitiveness [RTI2018-94918-B-C44]
  2. Junta de Andalucia [RNM-1565]
  3. FEDER (European Union) funds [UMA18-FEDERJA-171]
  4. Malaga University
  5. FEDER funds
  6. Spanish MINECO via the concession of a Ramon y Cajal contract [RYC-2015-17109]

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Olive stones were employed as feedstock for furfural production in two stages: 1) autohydrolysis of hemi-cellulosic fraction to recover their pentoses, mainly xylose, and 2) subsequent dehydration of pentoses into furfural. Autohydrolysis step was optimized by using different experimental conditions (temperature: 160-200 degrees C and time: 30-75 min), giving rise to liquors with different xylose concentrations, since hydrolysis was incomplete in some cases. The combined use of a commercial gamma-Al2O3 and CaCl2 led to total hydrolysis of non-hydrolyzed pentosans after autohydrolysis step, and the subsequent dehydration of pentoses into furfural. The maximum values of furfural yield and efficiency were 23 and 96 %, respectively, after only 60 min at 150 degrees C by using liquor obtained by autohydrolysis at 180 degrees C and 30 min (L5.1) as source of pentoses. This liquor, L5.1, provided better catalytic results than other liquors which had shown higher xylose concentration after autohydrolysis, probably due to these latter also exhibited a higher concentration of organic acids; thus, the presence of organic acids, such as acetic and lactic acids, could promote undesired reactions leading to lower furfural yields. Finally, gamma-Al2O3 was more effective for furfural production under these experimental conditions than other solid acid catalysts, such as mesoporous Nb2O5, Nb-doped SBA-15 and Zr-doped HMS silicas, probably due to alumina has a higher density of acid sites. (C) 2020 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.

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