2014
DOI: 10.1016/j.jestch.2014.04.002
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Transesterification of used cooking oil over alkali metal (Li, Na, K) supported rice husk silica as potential solid base catalyst

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Cited by 81 publications
(66 citation statements)
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“…% KOH/AC for WFO, 9:1, 120 minutes and 600 rpm, respectively. As shown in Figure 3(c), the lower temperatures (30-50 C) were accompanied by lower conversion, which could be ascribed to the higher viscosity of the oil at lower temperatures, causing lower mass transfer resistance among oil-methanol-catalyst phases Fadhil et al, 2016b;Hindryawati et al, 2014;Takase et al, 2014;Zabeti et al, 2009). The conversion yield increased with increasing the reaction temperature and reached the maximum value at 65 C. On the other hand, the reaction temperatures higher than 65 C reduced the methyl ester yield due the evaporation and forming bubbles of methanol, which might inhibit the interface interaction (Al-Jammal, Al-Hamamre, & Alnaief, 2016;Encinar et al, 2010;Takase et al, 2014).…”
Section: Optimization Of Transesterification Parametersmentioning
confidence: 96%
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“…% KOH/AC for WFO, 9:1, 120 minutes and 600 rpm, respectively. As shown in Figure 3(c), the lower temperatures (30-50 C) were accompanied by lower conversion, which could be ascribed to the higher viscosity of the oil at lower temperatures, causing lower mass transfer resistance among oil-methanol-catalyst phases Fadhil et al, 2016b;Hindryawati et al, 2014;Takase et al, 2014;Zabeti et al, 2009). The conversion yield increased with increasing the reaction temperature and reached the maximum value at 65 C. On the other hand, the reaction temperatures higher than 65 C reduced the methyl ester yield due the evaporation and forming bubbles of methanol, which might inhibit the interface interaction (Al-Jammal, Al-Hamamre, & Alnaief, 2016;Encinar et al, 2010;Takase et al, 2014).…”
Section: Optimization Of Transesterification Parametersmentioning
confidence: 96%
“…Furthermore, WFO is a virgin oil and was not subjected to any thermal treatment in opposition to WCO which was subjected to the frying process at a higher temperature leading to significant changes in the chemical composition. It was observed that conduction of the reaction at durations longer than the optimum period reduced the methyl ester which may be due to the hydrolysis of some of the esters to their corresponding free fatty acids (Fadhil et al, 2016a(Fadhil et al, , 2016bHindryawati et al, 2014).…”
Section: Optimization Of Transesterification Parametersmentioning
confidence: 99%
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“…The use of non-edible oils from seeds of rubber, jatropha, castor, linseed, moringa oleifera, cotton, karanja, neem and tobacco plants are being proposed to avert any impending fuel-food crisis [1,2,[13][14][15][16][17][18][19]. Raw material accounts for about 60-90% of the production cost of biodiesel and producing biodiesel from these feedstock will ultimately reduce its consumer's price [1,14,[20][21][22]. In consideration of nature of all these plants, rubber tree had less investigation on its potentials and in many sub-Saharan Africa (SSA) countries, it stands to be only a source of latex.…”
Section: Introductionmentioning
confidence: 99%
“…Salah satu sumber energi yang dapat digunakan sebagai bahan bakar alternatif adalah biodiesel (Hindryawati et al, 2014). Biodiesel merupakan mono-alkil ester yang berasal dari asam lemak yang terbuat dari minyak tumbuh-tumbuhan atau lemak hewan sehingga ramah lingkungan.…”
Section: Latar Belakangunclassified