2022
DOI: 10.1002/bbb.2390
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Non‐catalytic esterification of palm fatty acid distillate with 2‐ethyl hexanol for high purity production of biolubricant ester

Abstract: Palm fatty acid distillate (PFAD), a byproduct of crude palm oil (CPO) refining, is an attractive feedstock for biolubricants due to its inedible nature and the fact that its cost is lower than that of palm oil. Ethylhexyl ester is a novel high‐performance biolubricant synthesized via the non‐catalytic esterification of PFAD with 2‐ethylhexanol (2EH), normally the esterification of PFAD with methanol (MeOH). By substituting a longer carbon chain alcohol for MeOH, the cold flow characteristics, flashpoint, and … Show more

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Cited by 4 publications
(3 citation statements)
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“…Fourier transform infrared (FTIR) analysis was performed using a Spectrum 100 spectrometer with an average of eight scans and 4 cm −1 resolution. The Spectrum 100 spectrometer was supplied by Perkin Elmer (Waltham, MA, USA) 31 . Surface morphology was determined using a scanning electron microscope Hitachi SU‐1015 model from Hitachi, Chiyoda, Tokyo.…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…Fourier transform infrared (FTIR) analysis was performed using a Spectrum 100 spectrometer with an average of eight scans and 4 cm −1 resolution. The Spectrum 100 spectrometer was supplied by Perkin Elmer (Waltham, MA, USA) 31 . Surface morphology was determined using a scanning electron microscope Hitachi SU‐1015 model from Hitachi, Chiyoda, Tokyo.…”
Section: Methodsmentioning
confidence: 99%
“…The Spectrum 100 spectrometer was supplied by Perkin Elmer (Waltham, MA, USA). 31 Surface morphology was determined using a scanning electron microscope Hitachi SU-1015 model from Hitachi, Chiyoda, Tokyo. The imaging was conducted at an accelerating voltage of 15 kV with the primary electron beam current of approximately 120 μA.…”
Section: Characterizationmentioning
confidence: 99%
“…; reaction time, 60 min; and stirring rate, within the range of 84.44 ± 0.8%-95.94 ± 2.1%, with the most productive temperature identified as 70 • C. Reducing the temperature to 60 • C reduced the transformation of FFA as it had a negative impact on the equilibrium of the reaction. When the temperature of the reaction was increased, the reactants acquired sufficient kinetic energy to hasten the mass transfer rate between the PFAD-methanol-catalyst phases; this, therefore, optimised the conversion rate [38,39]. The maximum FFA conversion seen at 70 • C with the use of the Cu 2 S (8%) -FeS (10%) /SiO 2 catalyst reflected the requisite for the increased reaction temperature for the acid catalysis of esterification as opposed to that required for base catalysis [40].…”
Section: Biodiesel Production Reaction Optimisationmentioning
confidence: 99%