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Hemijska IndustrijaVolume 73, Issue 6, 2019, Pages 351-362

Triethanolamine as an efficient cosolvent for biodiesel production by cao-catalyzed sunflower oil ethanolysis: An optimization study(Article)(Open Access)

[Optimizacija proizvodnje biodizela etanolizom suncokretovog ulja: Primena trietanolamina kao efikasnog kosolventa i kalcijum-oksida kao katalizatora]

  • Đokić-Stojanović, D.R.,
  • Todorović, Z.B.,
  • Troter, D.Z.,
  • Stamenković, O.S.,
  • Veselinović, L.M.,
  • Zdujić, M.V.,
  • Manojlović, D.D.,
  • Veljković, V.B.
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  • aZdravlje Actavis, Vlajkova 199, Leskovac, 16000, Serbia
  • bFaculty of Technology, University of Niš, Bulevar Oslobođenja 124, Leskovac, 16000, Serbia
  • cInstitute of Technical Sciences of the Serbian Academy of Sciences and Arts, Knez Mihailova 35, Belgrade, 11000, Serbia
  • dFaculty of Chemistry, University of Belgrade, Studentski trg 12-16, Belgrade, 11000, Serbia
  • eSerbian Academy of Sciences and Arts, Knez Mihailova 35, Belgrade, 11000, Serbia

Abstract

Triethanolamine was applied as an efficient „green“ cosolvent for biodiesel production by CaO-catalyzed ethanolysis of sunflower oil. The reaction was conducted in a batch stirred reactor and optimized with respect to the reaction temperature (61.6-78.4 °C), the ethanol-to-oil molar ratio (7:1-17:1) and the cosolvent loading (3-36 % of the oil weight) by using a rotatable central composite design (RCCD) combined with the response surface methodology (RSM). The optimal reaction conditions were found to be: the ethanol-to-oil molar ratio of 9:1, the reaction temperature of 75 °C and the cosolvent loading of 30 % to oil weight, which resulted in the predicted and actual fatty acid ethyl ester (FAEE) contents of 98.8 % and 97.9±1.3 %, respectively, achieved within only 20 min of the reaction. Also, high FAEE contents were obtained with expired sunflower oil, hempseed oil and waste lard. X-ray diffraction analysis (XRD) was used to understand the changes in the CaO phase. The CaO catalyst can be used without any treatment in two consecutive cycles. Due to the calcium leaching into the product, an additional purification stage must be included in the overall process. © 2019, Association of Chemists and Chemical Engineers of Serbia. All rights reserved.

Author keywords

BiodieselHeterogeneous catalysisTransesterificationXRD

Funding details

Funding sponsor Funding number Acronym
Serbian Academy of Sciences and ArtsSASA
Ministarstvo Prosvete, Nauke i Tehnološkog Razvoja45001,III 45001MPNTR
  • 1

    This work has been funded by the Ministry of Education, Science and Technological Development of the Republic of Serbia (Project III 45001). It is also a part of the Project of the SASA, Serbia.

  • 2

    Acknowledgements: This work has been funded by the Ministry of Education, Science and Technological Development of the Republic of Serbia (Project III 45001). It is also a part of the Project of the SASA, Serbia.

  • ISSN: 0367598X
  • Source Type: Journal
  • Original language: English
  • DOI: 10.2298/HEMIND190822033D
  • Document Type: Article
  • Publisher: Association of Chemists and Chemical Engineers of Serbia

  Veljković, V.B.; Faculty of Technology, University of Niš, Bulevar Oslobođenja 124, Leskovac, Serbia;
© Copyright 2020 Elsevier B.V., All rights reserved.

Cited by 4 documents

Kostić, M.D. , Bijelić, A.B. , Stamenković, O.S.
Kinetics of the used cooking oil transesterification in the presence of slaked lime and the triethanolamine:menthol deep eutectic solvent
(2023) Environmental Progress and Sustainable Energy
Miyuranga, K.A.V. , Arachchige, U.S.P.R. , Balasuriya, B.M.C.M.
Production of Biodiesel in the Presence of Co-Solvents in Transesterification: A Review
(2023) Asian Journal of Chemistry
Veličković, A. , Avramović, J. , Kostić, M.
Modeling the biodiesel production using the wheat straw ash as a catalyst | Pepeo pšenične slame kao katalizator u proizvodnji biodizela
(2021) Hemijska Industrija
View details of all 4 citations
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