Transesterification of oil to biodiesel in a continuous tubular reactor with static mixers: Modelling reaction kinetics, mass transfer, scale-up and optimization considering fatty acid composition
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Likozar et al.'s mass balance model for transesterification in a continuous tubular reactor considers the kinetics of glycerides containing different combinations of gadoleic, linoleic, linolenic, oleic, palmitic, and stearic acids.
“Likozar et al. developed a mass balance for the chemical equilibrium, reaction kinetics, and mass transfer required for transesterification in a continuous tubular reactor, a model which considers the kinetics of glycerides containing different combinations of gadoleic, linoleic, linolenic, oleic, palmitic, and stearic acids [17].”
From Effects on Biodiesel Production Caused by Feed Oil Changes in a Continuous Stirred-Tank Reactor (2020) · cites this paper as [17]
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References 24 · Cited by 137
- Authors
- Likozar, B., Pohar, A., & Levec, J.
- Affiliations
- National Institute of Chemistry (SI)
- Corresponding author
- Likozar, Blaž
- ORCID
- Likozar, Blaž
- Venue
- Fuel Processing Technology
- Publisher
- Elsevier BV
- Published
- 2016-02
- Volume
- 142
- Pages
- 326-336
- ISSN
- 0378-3820 (ISSN-L)
- OpenAlex
- W1945481625
- Cited by
- 137
- References
- 24
- Citations by year
- 2026: 3 · 2025: 6 · 2024: 7 · 2023: 7 · 2022: 8 · 2021: 7 · 2020: 24 · 2019: 19 · 2018: 30 · 2017: 14 · 2016: 12
- FWCI
- 9.29
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- Fuel Processing Technology (publishedVersion)
- Funders
- Slovenian Research Agency (ARRS) (P2-0152)
- Topics
- Physical Sciences › Engineering › Biomedical Engineering › Biodiesel Production and Applications
- Physical Sciences › Engineering › Mechanical Engineering › Catalysis and Hydrodesulfurization Studies
- Physical Sciences › Engineering › Biomedical Engineering › Thermochemical Biomass Conversion Processes
- Keywords
- biodiesel production, transesterification, static mixer, continuous tubular reactor, fatty acid methyl esters, fatty acid composition, glycerides, axial dispersion, Peclet number, reaction kinetics, mass transfer, scale-up, process intensification, process economics, waste oil, triglyceride content, temperature effects
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