Nježić, Zvonko

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Kinetics and optimization of biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing plant

Nježić, Zvonko; Kostić, Milan D.; Marić, Boško D.; Stamenković, Olivera; Šimurina, Olivera D.; Krstić, Jugoslav; Veljković, Vlada B.

(Elsevier, 2023)

TY  - JOUR
AU  - Nježić, Zvonko
AU  - Kostić, Milan D.
AU  - Marić, Boško D.
AU  - Stamenković, Olivera
AU  - Šimurina, Olivera D.
AU  - Krstić, Jugoslav
AU  - Veljković, Vlada B.
PY  - 2023
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/5399
AB  - A low-cost, highly active CaO-based catalyst was prepared from waste filter cake (WFC) from a sugar beet processing factory by calcination in air at 900 °C for 2 h, referred to as the calcined filter cake (CFC). It was used to catalyze the rapeseed oil transesterification with methanol under mild reaction conditions (methanol-to-oil molar ratio of 9:1, catalyst loading of 4–10 %, and reaction temperature of 40–60 °C). Rapeseed oil was characterized regarding the physicochemical properties and fatty acid profile. Low free fatty acid content (about 2.0 mg KOH/g) allowed the direct use of the base CFC catalyst for rapeseed oil transesterification. Rapeseed oil has more unsaturated fatty acids (about 93 %), with oleic acid as the most abundant, than saturated fatty acids (about 7 %). A simplified model combining the changing mechanism of the reaction and the triacylglycerols mass transfer limitation successfully describes the kinetics of transesterification. A good agreement between the model and the experiment was proved by the mean relative percentage deviation for the conversion degree of only ± 7.43 % (based on 42 data). The apparent reaction rate constant follows the Arrhenius equation with the activation energy of 51.9 kJ mol−1. The FAME content higher than 96.5 % can be obtained in wide ranges of the catalyst amount (4–10 %) and the reaction time (about 45–70 min). The following conditions were optimum: the reaction temperature of 59.2 °C, the catalyst loading of 9.1 % (based on the oil weight), and the reaction time of 47 min.
PB  - Elsevier
T2  - Fuel
T1  - Kinetics and optimization of biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing plant
VL  - 334
SP  - 126581
DO  - 10.1016/j.fuel.2022.126581
ER  - 
@article{
author = "Nježić, Zvonko and Kostić, Milan D. and Marić, Boško D. and Stamenković, Olivera and Šimurina, Olivera D. and Krstić, Jugoslav and Veljković, Vlada B.",
year = "2023",
abstract = "A low-cost, highly active CaO-based catalyst was prepared from waste filter cake (WFC) from a sugar beet processing factory by calcination in air at 900 °C for 2 h, referred to as the calcined filter cake (CFC). It was used to catalyze the rapeseed oil transesterification with methanol under mild reaction conditions (methanol-to-oil molar ratio of 9:1, catalyst loading of 4–10 %, and reaction temperature of 40–60 °C). Rapeseed oil was characterized regarding the physicochemical properties and fatty acid profile. Low free fatty acid content (about 2.0 mg KOH/g) allowed the direct use of the base CFC catalyst for rapeseed oil transesterification. Rapeseed oil has more unsaturated fatty acids (about 93 %), with oleic acid as the most abundant, than saturated fatty acids (about 7 %). A simplified model combining the changing mechanism of the reaction and the triacylglycerols mass transfer limitation successfully describes the kinetics of transesterification. A good agreement between the model and the experiment was proved by the mean relative percentage deviation for the conversion degree of only ± 7.43 % (based on 42 data). The apparent reaction rate constant follows the Arrhenius equation with the activation energy of 51.9 kJ mol−1. The FAME content higher than 96.5 % can be obtained in wide ranges of the catalyst amount (4–10 %) and the reaction time (about 45–70 min). The following conditions were optimum: the reaction temperature of 59.2 °C, the catalyst loading of 9.1 % (based on the oil weight), and the reaction time of 47 min.",
publisher = "Elsevier",
journal = "Fuel",
title = "Kinetics and optimization of biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing plant",
volume = "334",
pages = "126581",
doi = "10.1016/j.fuel.2022.126581"
}
Nježić, Z., Kostić, M. D., Marić, B. D., Stamenković, O., Šimurina, O. D., Krstić, J.,& Veljković, V. B.. (2023). Kinetics and optimization of biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing plant. in Fuel
Elsevier., 334, 126581.
https://doi.org/10.1016/j.fuel.2022.126581
Nježić Z, Kostić MD, Marić BD, Stamenković O, Šimurina OD, Krstić J, Veljković VB. Kinetics and optimization of biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing plant. in Fuel. 2023;334:126581.
doi:10.1016/j.fuel.2022.126581 .
Nježić, Zvonko, Kostić, Milan D., Marić, Boško D., Stamenković, Olivera, Šimurina, Olivera D., Krstić, Jugoslav, Veljković, Vlada B., "Kinetics and optimization of biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing plant" in Fuel, 334 (2023):126581,
https://doi.org/10.1016/j.fuel.2022.126581 . .
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Novi tehnološki postupak dobijanja biodizela metanolizom ulja kukuruznih klica u prisustvu pepela kukuruzne kurdeljke kao katalizatora

Kostić, Milan; Đalović, Ivica; Mitrović, Petar; Pavlović, Stefan; Marinković, Dalibor; Nježić, Zvonko; Stamenković, Olivera; Veljković, Vlada B.

(Univerzitet u Nišu -Tehnloški fakultet u Leskovcu, 2019)

TY  - GEN
AU  - Kostić, Milan
AU  - Đalović, Ivica
AU  - Mitrović, Petar
AU  - Pavlović, Stefan
AU  - Marinković, Dalibor
AU  - Nježić, Zvonko
AU  - Stamenković, Olivera
AU  - Veljković, Vlada B.
PY  - 2019
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3809
AB  - Tehničko rešenje pripada oblasti hemijske tehnologije i predstavlja
tehnološki postupak za sintezu metil estara masnih kiselina (MEMK) iz ulja
kukuruznih klica (UKK) primenom pepela dobijenog sagorevanjem kurdeljke
kukuruza kao katalizatora.
PB  - Univerzitet u Nišu -Tehnloški fakultet u Leskovcu
T1  - Novi tehnološki postupak dobijanja biodizela metanolizom ulja kukuruznih klica u prisustvu pepela kukuruzne kurdeljke kao katalizatora
UR  - https://hdl.handle.net/21.15107/rcub_cer_3809
ER  - 
@misc{
author = "Kostić, Milan and Đalović, Ivica and Mitrović, Petar and Pavlović, Stefan and Marinković, Dalibor and Nježić, Zvonko and Stamenković, Olivera and Veljković, Vlada B.",
year = "2019",
abstract = "Tehničko rešenje pripada oblasti hemijske tehnologije i predstavlja
tehnološki postupak za sintezu metil estara masnih kiselina (MEMK) iz ulja
kukuruznih klica (UKK) primenom pepela dobijenog sagorevanjem kurdeljke
kukuruza kao katalizatora.",
publisher = "Univerzitet u Nišu -Tehnloški fakultet u Leskovcu",
title = "Novi tehnološki postupak dobijanja biodizela metanolizom ulja kukuruznih klica u prisustvu pepela kukuruzne kurdeljke kao katalizatora",
url = "https://hdl.handle.net/21.15107/rcub_cer_3809"
}
Kostić, M., Đalović, I., Mitrović, P., Pavlović, S., Marinković, D., Nježić, Z., Stamenković, O.,& Veljković, V. B.. (2019). Novi tehnološki postupak dobijanja biodizela metanolizom ulja kukuruznih klica u prisustvu pepela kukuruzne kurdeljke kao katalizatora. 
Univerzitet u Nišu -Tehnloški fakultet u Leskovcu..
https://hdl.handle.net/21.15107/rcub_cer_3809
Kostić M, Đalović I, Mitrović P, Pavlović S, Marinković D, Nježić Z, Stamenković O, Veljković VB. Novi tehnološki postupak dobijanja biodizela metanolizom ulja kukuruznih klica u prisustvu pepela kukuruzne kurdeljke kao katalizatora. 2019;.
https://hdl.handle.net/21.15107/rcub_cer_3809 .
Kostić, Milan, Đalović, Ivica, Mitrović, Petar, Pavlović, Stefan, Marinković, Dalibor, Nježić, Zvonko, Stamenković, Olivera, Veljković, Vlada B., "Novi tehnološki postupak dobijanja biodizela metanolizom ulja kukuruznih klica u prisustvu pepela kukuruzne kurdeljke kao katalizatora" (2019),
https://hdl.handle.net/21.15107/rcub_cer_3809 .