2011
DOI: 10.9767/bcrec.6.1.816.31-38
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Fuzzy Modeling to Evaluate the Effect of Temperature on Batch Transesterification of Jatropha Curcas for Biodiesel Production

Abstract:

Biodiesel is an alternative source of fuel that can be synthesized from edible, non-edible and waste oils through transesterification. Firstly Transesterification reaction of Jatropha Curcas oil with butanol in the ratio of 1:25 investigated by using of sodium hydroxide catalyst with mixing intensity of 250 rpm in isothermal batch reactor. Secondly the fuzzy model of the temperature is developed. Performance was evaluated by comparing fuzzy model with the batch kinetic data. Fuzzy models were developed usin… Show more

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Cited by 14 publications
(4 citation statements)
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“…TGA can provide a complete and reliable register of the loss of mass and phase changes thanks to the precise instrumentation used and the uniform heat transfer as the result of a sufficiently small sample size. The raw material that is submitted to pyrolysis in an industrial-scale reactor is a heterogeneous mixture of several plastics with a random distribution of the different components [16], [18]- [22]. It is complicated modeling a stochastic process, far from the deterministic nature of the TGA.…”
Section: Investigation Backgroundmentioning
confidence: 99%
“…TGA can provide a complete and reliable register of the loss of mass and phase changes thanks to the precise instrumentation used and the uniform heat transfer as the result of a sufficiently small sample size. The raw material that is submitted to pyrolysis in an industrial-scale reactor is a heterogeneous mixture of several plastics with a random distribution of the different components [16], [18]- [22]. It is complicated modeling a stochastic process, far from the deterministic nature of the TGA.…”
Section: Investigation Backgroundmentioning
confidence: 99%
“…Details on the modeling of the effect of temperature on transesterification process can be found in the literature. [32][33][34] Moreover, the alcohol-to-oil molar ratio may vary, largely depending on the catalyst percentage (wt%). With a higher catalyst percentage (wt%), the molar ratio is less, and where the catalyst percentage (wt%) is less, the molar ratio is significantly higher; such as, in the methodology described by Krishnamurthy et al, 22 due to having a low catalyst percentage (0.866 wt%), the molar ratio (12.74:1) is found to be higher.…”
Section: Sodiummethoxide (Ch 3 Nao)mentioning
confidence: 99%
“…Reaction temperatures mentioned in Table 3 are based on reaction time and prosperities of scum. Details on the modeling of the effect of temperature on transesterification process can be found in the literature 32–34 . Moreover, the alcohol‐to‐oil molar ratio may vary, largely depending on the catalyst percentage (wt%).…”
Section: Energy From the Dairy Wastementioning
confidence: 99%
“…The effect of temperature at low weight percents is weaker than that at high weight percent of catalyst. This is possibly because the transesterification is a catalytic reaction and goes faster when the basic sites and the contact surface area for reaction increase [25,26].…”
Section: The Effect Of Reaction Temperaturementioning
confidence: 99%