2002
DOI: 10.1002/1438-9312(200211)104:11<728::aid-ejlt728>3.0.co;2-j
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Kinetics and mechanism of the KOH — catalyzed methanolysis of rapeseed oil for biodiesel production

Abstract: Kinetics and mechanism of the KOHcatalyzed methanolysis of rapeseed oil for biodiesel productionThe reaction of rapeseed oil with methanol catalyzed by KOH is described by a model consisting of two sequences of consecutive competitive reactions. The first sequence expresses the methanolysis of rapeseed oil to methyl esters (biodiesel) whereas the second sequence describes the always present side reaction-saponification of glycerides and methyl esters by KOH. The proposed chemical model is described (after rati… Show more

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Cited by 129 publications
(90 citation statements)
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“…This is due to the fact that the production of ethyl esters is limited by several factors including: water content of bioethanol, the difficult separation of ethyl esters in reaction environments, etc. that is currently Several kinetic studies have been published on transesterification process [10,11,[14][15][16]. The model proposed by Noureddini and Zhu is the most common used, but shows some weaknesses: it does not take into account side reactions that occur like the effect of saponification and water [12,17,18].…”
Section: Experimental Procedures Materialsmentioning
confidence: 99%
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“…This is due to the fact that the production of ethyl esters is limited by several factors including: water content of bioethanol, the difficult separation of ethyl esters in reaction environments, etc. that is currently Several kinetic studies have been published on transesterification process [10,11,[14][15][16]. The model proposed by Noureddini and Zhu is the most common used, but shows some weaknesses: it does not take into account side reactions that occur like the effect of saponification and water [12,17,18].…”
Section: Experimental Procedures Materialsmentioning
confidence: 99%
“…The model proposed by Noureddini and Zhu is the most common used, but shows some weaknesses: it does not take into account side reactions that occur like the effect of saponification and water [12,17,18]. In order to overcome these simplifications, some aspects of the model proposed by Komers are included in our model [11,12]. However, the difficulty of using the Komers model lies on the high number of constant rates (eleven), found for a temperature of 22.75°C and a molar ratio n=2.03.…”
Section: Experimental Procedures Materialsmentioning
confidence: 99%
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“…Prema nekim istraživačima, povratne i direktne reakcije metanolize su reakcije drugog reda [19,20]. Pored uzastopno-paralelnih reakcija, u kinetički model reakcije metanolize uključivana je i ukupna reakcija sinteze MEMK [22,24] ili sporedna reakcija saponifikacije [25]. Zbog kompleksnosti navedenih kinetičkih modela koja zahtevaju složena matematička proračunavanja, novija istraživanja su usmerena ka razvoju jednostavnijih kinetičkih modela, koji dobro opisuju eksperimentalne podatke.…”
Section: Uvodunclassified
“…So me of the few kinetics studies that have been performed in recent times include esterification of free fatty acids in sunflower oil and oleic acid [38][39]. Trans-esterificat ion kinetics of soybean oil with five d ifferent catalysts have also been studied [40].Similarly, Divya and Tyagi [20] reported the study carried out by Ko mers et al; [41] where kinetics and mechanism o f KOH catalyzed methanolysis of rapeseed oil for b iodiesel production was investigated. The first sequence of the reaction expressed the methanolysis of rapeseed oil to biodiesel wh ile the second sequence described the always present side reaction separation of glycerides and biodiesel by KOH.…”
Section: Thermo-kinetics Of Trans-esterificationmentioning
confidence: 99%