2016
DOI: 10.1016/j.proeng.2016.06.606
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Process Optimization for Biodiesel Production from Waste Frying Oil over Montmorillonite Clay K-30

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Cited by 18 publications
(11 citation statements)
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“…Due to the demonstrated and promising results of using clay for biodiesel production, Jaimasith and Phiyanalinmat (2007) selected it as a catalyst. In a recent study, Ayoub et al, (2016) have demonstrated that montmorillonite clay K-30 is an effective catalyst for the biodiesel production from waste frying oil. Using response surface methodology,…”
Section: Accepted Manuscriptmentioning
confidence: 99%
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“…Due to the demonstrated and promising results of using clay for biodiesel production, Jaimasith and Phiyanalinmat (2007) selected it as a catalyst. In a recent study, Ayoub et al, (2016) have demonstrated that montmorillonite clay K-30 is an effective catalyst for the biodiesel production from waste frying oil. Using response surface methodology,…”
Section: Accepted Manuscriptmentioning
confidence: 99%
“…These variables are the reaction time (minutes), reaction temperature ( o C), amount of catalyst (wt%) and oil/methanol ratio. Ayoub et al (2016) studied the effect of these four controlling variables on the biodiesel production in 30 experimental runs. Commercial clay catalyst montmorillonite K-30 (in powdered form) has been utilized in the experimental work because it has several advantages such as safe to handle, reusable, inexpensive and can act as a general acid or base.…”
Section: Accepted Manuscriptmentioning
confidence: 99%
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“…The amphoteric montmorillonite clay K‐30 was used as solid base catalysts for transesterification of waste frying palm oil and methanol . The results showed a high yield of 78.4 %, under conditions of 12:1 methanol/waste oil with 3 wt % of montmorillonite clay K‐30 catalyst, reaction time of 180 min at 90 °C.…”
Section: Heterogeneous Catalystsmentioning
confidence: 99%
“…The tryglycerides react with an alcohol, usually methanol, in the presence of a basic catalyst to give alchyl esters, biodiesel, and glicerol [5,14,15]. The chemical reaction takes place in a batch stirred reactor at temperatures between 60-70 • C for a time of 60 min [5,[16][17][18]. The correct operation of the batch reactor is essential to reach a high yield of the transesterification reaction.…”
Section: Introductionmentioning
confidence: 99%