TY - JOUR
T1 - Statistical optimization of biodiesel production from waste cooking oil using CaO as catalyst in a Robinson-Mahoney type reactor
AU - Soria-Figueroa, Erick
AU - Mena-Cervantes, Violeta Y.
AU - García-Solares, Montserrat
AU - Hernández-Altamirano, Raúl
AU - Vazquez-Arenas, Jorge
N1 - Publisher Copyright:
© 2020 Elsevier Ltd
PY - 2020/12/15
Y1 - 2020/12/15
N2 - This study presents a statistical optimization conducted with operating variables affecting the biodiesel production using calcium oxide (CaO, industrial grade) as heterogeneous catalyst, and waste cooking oil as triglyceride source. The experiments are carried out in a commercial Robinson-Mahoney reactor (600 cm3) using a fixed catalytic basket to analyze the advantages (e.g. optimal contact between phases, facile catalyst recovery, heat transfer) and challenges of this design upon the establishing of a bench-scale transesterification process. As a pretreatment, the catalyst was calcined at 700 °C for 2 h. A Box-Behnken design (BBD) is used to account for the catalyst dosage (3,6 and 9 wt%), particle size (1.18, 1.41 and 2 mm) and the methanol-oil molar ratio (6, 9 and 12), at fixed temperature of 60 °C, stirring of 700 rpm and reaction time of 2 h. Reaction conversions greater than 98.5% w/w of triglycerides into methyl esters were achieved for the optimized conditions estimated through the BBD at 8.75% w/w catalyst dosage, 2 mm of particle size and 8.72:1 of methanol-oil molar ratio.
AB - This study presents a statistical optimization conducted with operating variables affecting the biodiesel production using calcium oxide (CaO, industrial grade) as heterogeneous catalyst, and waste cooking oil as triglyceride source. The experiments are carried out in a commercial Robinson-Mahoney reactor (600 cm3) using a fixed catalytic basket to analyze the advantages (e.g. optimal contact between phases, facile catalyst recovery, heat transfer) and challenges of this design upon the establishing of a bench-scale transesterification process. As a pretreatment, the catalyst was calcined at 700 °C for 2 h. A Box-Behnken design (BBD) is used to account for the catalyst dosage (3,6 and 9 wt%), particle size (1.18, 1.41 and 2 mm) and the methanol-oil molar ratio (6, 9 and 12), at fixed temperature of 60 °C, stirring of 700 rpm and reaction time of 2 h. Reaction conversions greater than 98.5% w/w of triglycerides into methyl esters were achieved for the optimized conditions estimated through the BBD at 8.75% w/w catalyst dosage, 2 mm of particle size and 8.72:1 of methanol-oil molar ratio.
KW - Biodiesel
KW - Box-Behnken design
KW - Calcium oxide
KW - Heterogeneous catalysis
KW - Robinson-Mahoney reactor
UR - http://www.scopus.com/inward/record.url?scp=85088962393&partnerID=8YFLogxK
U2 - 10.1016/j.fuel.2020.118853
DO - 10.1016/j.fuel.2020.118853
M3 - Artículo
AN - SCOPUS:85088962393
SN - 0016-2361
VL - 282
JO - Fuel
JF - Fuel
M1 - 118853
ER -