2015
DOI: 10.1016/j.egypro.2015.07.143
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Novel Technology for Bio-diesel Production from Cooking and Waste Cooking Oil by Microwave Irradiation

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Cited by 55 publications
(14 citation statements)
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“…Priambodo et al. () obtained a 93% biodiesel conversion efficiency for WCO using commercial strontium oxide (SrO), 40 to 180 seconds of reaction time, a reaction temperature of around 80°C, a 6:1 methanol‐to‐oil ratio, and a microwave power output of 1000 watts (W). Wang, Lee, and Chen () investigated microwave‐ and reflux‐assisted transesterification in methanol with alkali‐loaded low‐aluminum ( Al) Zeolite Beta as a catalyst and obtained a final conversion yield of more than 90% within an hour of reflux reaction.…”
Section: Biodiesel Production From Waste Cooking Oilsmentioning
confidence: 99%
“…Priambodo et al. () obtained a 93% biodiesel conversion efficiency for WCO using commercial strontium oxide (SrO), 40 to 180 seconds of reaction time, a reaction temperature of around 80°C, a 6:1 methanol‐to‐oil ratio, and a microwave power output of 1000 watts (W). Wang, Lee, and Chen () investigated microwave‐ and reflux‐assisted transesterification in methanol with alkali‐loaded low‐aluminum ( Al) Zeolite Beta as a catalyst and obtained a final conversion yield of more than 90% within an hour of reflux reaction.…”
Section: Biodiesel Production From Waste Cooking Oilsmentioning
confidence: 99%
“…SathyaSelvabala et al (2011) melakukan proses dua tahap untuk menghasilkan biodiesel dari minyak nyamplung menggunakan katalis asam padat dimodifikasi zeolite untuk langkah pretreatment diikuti oleh reaksi transesterifikasi berkatalis KOH. Penggunaan microwave dilakukan oleh Priambodo et al (2015) pada reaksi transesterifikasi minyak goreng segar dan minyak goreng bekas. Faktor utama yang mempengaruhi proses transesterifikasi adalah rasio molar metanol terhadap minyak, jumlah katalis dan waktu reaksi.…”
Section: Kajian Pustaka Dan Perumusan Hipotesisunclassified
“…The activity of base catalysts is higher than that of acid catalysts for both homogeneous and heterogeneous catalysts, and the reaction occurs under milder conditions. However, base catalysts cause the problem of a side saponification reaction that occurs in the presence of FFA [ 15 ]. The heterogeneous base and acid catalysts are much easier to separate from the product, and allow the performance of continuous processes or reuse of the catalysts in batch regimes [ 16 , 17 ].…”
Section: Introductionmentioning
confidence: 99%