4.7 Article

One-pot conversion of highly acidic waste cooking oil into biodiesel over a novel bio-based bi-functional catalyst

期刊

FUEL
卷 283, 期 -, 页码 -

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ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2020.118914

关键词

Biodiesel; Waste cooking oil; Heterogeneous catalyst; Activated carbon; Simultaneous esterification transesterification

资金

  1. Canada Research Chairs Program

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A KOH/corncobs-derived activated carbon (AC) heterogeneous catalyst was developed for single stage biodiesel production from highly acidic waste vegetable oil, showing activity in both esterification and transesterification reactions. Optimal conditions of sulfuric acid to raw corn cobs ratio, activation temperature, reaction time, catalyst loading, and temperature were identified to achieve a high yield of 97.8% meeting ASTM standards. The catalyst exhibited stability for up to five successive uses in esterification but easily leached KOH and became inactive in transesterification.
We developed a KOH/corncobs-derived activated carbon (AC) heterogeneous catalyst for the single stage biodiesel production from highly acidic waste vegetable oil, which was active in both the esterification and transesterification reactions. Among the different AC preparation conditions tested, a sulfuric acid to raw corn cobs (volume/weight) ratio of 5:1, activation temperature and time of 600 degrees C for 1 h were selected as the best conditions. The specific surface area (SSA) was 627 m(2)/g but among all the samples, the highest SSA was however 1131 m(2)/g. The main factors affecting the simultaneous esterification-transesterification were investigated with a full factorial design combined with response surface methodology via central composite design. The optimum conditions were 1 h reaction time, 18:1 methanol:oil molar ratio, 1 wt% catalyst loading and 45 degrees C temperature, at which the yield was 97.8%. The biodiesel obtained, in such conditions, matched the ASTM standards. The catalyst was stable for up to five successive times to catalyze esterification, but KOH leached easily and the catalyst became inactive in the transesterification.

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