Stamenković, Olivera

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  • Stamenković, Olivera (17)

Author's Bibliography

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 . .
9
8

Kinetic modeling of the biodiesel production from sunflower oil over corn cob ash

Kostić, Milan; Đorđević, Biljana; Pavlović, Stefan; Miladinović, Marija R.; Stamenković, Olivera

(Leskovac : Faculty of Technology, 2023)

TY  - CONF
AU  - Kostić, Milan
AU  - Đorđević, Biljana
AU  - Pavlović, Stefan
AU  - Miladinović, Marija R.
AU  - Stamenković, Olivera
PY  - 2023
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/7352
AB  - The investigation of reaction kinetics is crucial for practical implications in process equipment design and scaling up. In this study, a kinetic analysis of the methanolysis of a blend of radish and castor oil catalyzed by calcium oxide was carried out. The objectives were to propose a comprehensive model for describing the kinetics of this methanolysis reaction and determine its activation energy. The methanolysis was conducted in a batch reactor under atmospheric pressure with the following reaction conditions: a radish-to-castor oil blend mass ratio of 1:1, a methanol-to-oil molar ratio of 12:1, a catalyst amount of 5% of the oil blend weight, and reaction temperatures of 
30 C, 45 C, and 60 C. The model involving the changing reaction mechanism and the triacylglycerol (TAG) mass transfer limitation was first simplified to a pseudo-first order model regarding TAGs and fatty acid methyl esters, which was then used to calculate the apparent reaction rate constant. A good agreement between the calculated and experimental values of the TAG conversion degree was proved by a low mean relative percentage deviation of ±6.1% (based on 66 data), thus validating the applied simple kinetic model. A positive effect of the reaction temperature on the apparent reaction rate constant was observed. Using the Arrhenius equation, the activation energy of methanolysis was determined to be 46.12 kJ/mol. The obtained value of activation energy is much lower than values of activation energy determined for the calcium oxide-catalyzed methanolysis of single oil feedstocks, such as soybean, canola, Jatropha, and waste frying oils. The lower activation energy suggests the potential for enhanced efficiency and feasibility of utilizing this blend as a feedstock for biodiesel production compared to the individual oily feedstocks previously studied.
PB  - Leskovac : Faculty of Technology
C3  - Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia
T1  - Kinetic modeling of the biodiesel production from sunflower oil over corn cob ash
SP  - 129
EP  - 130
UR  - https://hdl.handle.net/21.15107/rcub_cer_7352
ER  - 
@conference{
author = "Kostić, Milan and Đorđević, Biljana and Pavlović, Stefan and Miladinović, Marija R. and Stamenković, Olivera",
year = "2023",
abstract = "The investigation of reaction kinetics is crucial for practical implications in process equipment design and scaling up. In this study, a kinetic analysis of the methanolysis of a blend of radish and castor oil catalyzed by calcium oxide was carried out. The objectives were to propose a comprehensive model for describing the kinetics of this methanolysis reaction and determine its activation energy. The methanolysis was conducted in a batch reactor under atmospheric pressure with the following reaction conditions: a radish-to-castor oil blend mass ratio of 1:1, a methanol-to-oil molar ratio of 12:1, a catalyst amount of 5% of the oil blend weight, and reaction temperatures of 
30 C, 45 C, and 60 C. The model involving the changing reaction mechanism and the triacylglycerol (TAG) mass transfer limitation was first simplified to a pseudo-first order model regarding TAGs and fatty acid methyl esters, which was then used to calculate the apparent reaction rate constant. A good agreement between the calculated and experimental values of the TAG conversion degree was proved by a low mean relative percentage deviation of ±6.1% (based on 66 data), thus validating the applied simple kinetic model. A positive effect of the reaction temperature on the apparent reaction rate constant was observed. Using the Arrhenius equation, the activation energy of methanolysis was determined to be 46.12 kJ/mol. The obtained value of activation energy is much lower than values of activation energy determined for the calcium oxide-catalyzed methanolysis of single oil feedstocks, such as soybean, canola, Jatropha, and waste frying oils. The lower activation energy suggests the potential for enhanced efficiency and feasibility of utilizing this blend as a feedstock for biodiesel production compared to the individual oily feedstocks previously studied.",
publisher = "Leskovac : Faculty of Technology",
journal = "Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia",
title = "Kinetic modeling of the biodiesel production from sunflower oil over corn cob ash",
pages = "129-130",
url = "https://hdl.handle.net/21.15107/rcub_cer_7352"
}
Kostić, M., Đorđević, B., Pavlović, S., Miladinović, M. R.,& Stamenković, O.. (2023). Kinetic modeling of the biodiesel production from sunflower oil over corn cob ash. in Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia
Leskovac : Faculty of Technology., 129-130.
https://hdl.handle.net/21.15107/rcub_cer_7352
Kostić M, Đorđević B, Pavlović S, Miladinović MR, Stamenković O. Kinetic modeling of the biodiesel production from sunflower oil over corn cob ash. in Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia. 2023;:129-130.
https://hdl.handle.net/21.15107/rcub_cer_7352 .
Kostić, Milan, Đorđević, Biljana, Pavlović, Stefan, Miladinović, Marija R., Stamenković, Olivera, "Kinetic modeling of the biodiesel production from sunflower oil over corn cob ash" in Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia (2023):129-130,
https://hdl.handle.net/21.15107/rcub_cer_7352 .

Optimization of the heterogeneously catalysed methanolysis of plum kernel oil in the presence of menthol-based deep eutectic solvent

Đorđević, Biljana; Pavlović, Stefan; Kostić, Milan; Stamenković, Olivera

(Leskovac : Faculty of Technology, 2023)

TY  - CONF
AU  - Đorđević, Biljana
AU  - Pavlović, Stefan
AU  - Kostić, Milan
AU  - Stamenković, Olivera
PY  - 2023
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/7353
AB  - Waste plum kernels from the fruit processing industry might be a valuable oil source  for biodiesel production which use can reduce the biodiesel production cost. The  application of green cosolvents, like deep eutectic solvents (DESs), in the alcoholysis  reaction can improve the oil conversion rate. This study reports on the optimization the plum kernel oil methanolysis over 35CaO/ZP (35% CaO supported on a fly ash-based  zeolite) in the presence of triethanolamine:menthol (TEOA:M, 2:1 mol/mol) DES as  cosolvent. The reactions were carried out in a 250 mL batch magnetic stirred reactor  (900 rpm) with a reflux condenser under atmosferic pressure and at 60 °C. The effect  of the catalyst amount (2-10% based on the oil mass), TEOA:M DES amount (1-9%  based on the oil mass) and methanol:oil molar ratio (6:1-12:1 mol/mol) on the fatty acid  methyl esters (FAMEs) content was analyzed according to a Box-Behnken design. The  obtained experimental data of the FAME content were modeled by a second-order  polynomial equation and the response surface methodology was used for determining  the optimal reaction conditions for achieving the highest FAME content. According to  the analysis of variance (ANOVA), the catalyst amount had the most significant  influence on the FAME content, followed by the TEOA:M DES amount and the  methanol:oil molar ratio. By analyzing the second-order polynomial equation, it can be  concluded that the catalyst amount and TEOA:M DES amount have a positive effect on  the FAME content. The maximum FAME content (99.67%) was achieved under the  following optimal reaction conditions: catalyst amount of 8% (based on the oil mass),  TEOA:M DES amount of 4.8% (based on the oil mass), and methanol:oil molar ratio of  6.1:1.
PB  - Leskovac : Faculty of Technology
C3  - Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia
T1  - Optimization of the heterogeneously catalysed methanolysis of plum kernel oil in the presence of menthol-based deep eutectic solvent
SP  - 128
EP  - 129
UR  - https://hdl.handle.net/21.15107/rcub_cer_7353
ER  - 
@conference{
author = "Đorđević, Biljana and Pavlović, Stefan and Kostić, Milan and Stamenković, Olivera",
year = "2023",
abstract = "Waste plum kernels from the fruit processing industry might be a valuable oil source  for biodiesel production which use can reduce the biodiesel production cost. The  application of green cosolvents, like deep eutectic solvents (DESs), in the alcoholysis  reaction can improve the oil conversion rate. This study reports on the optimization the plum kernel oil methanolysis over 35CaO/ZP (35% CaO supported on a fly ash-based  zeolite) in the presence of triethanolamine:menthol (TEOA:M, 2:1 mol/mol) DES as  cosolvent. The reactions were carried out in a 250 mL batch magnetic stirred reactor  (900 rpm) with a reflux condenser under atmosferic pressure and at 60 °C. The effect  of the catalyst amount (2-10% based on the oil mass), TEOA:M DES amount (1-9%  based on the oil mass) and methanol:oil molar ratio (6:1-12:1 mol/mol) on the fatty acid  methyl esters (FAMEs) content was analyzed according to a Box-Behnken design. The  obtained experimental data of the FAME content were modeled by a second-order  polynomial equation and the response surface methodology was used for determining  the optimal reaction conditions for achieving the highest FAME content. According to  the analysis of variance (ANOVA), the catalyst amount had the most significant  influence on the FAME content, followed by the TEOA:M DES amount and the  methanol:oil molar ratio. By analyzing the second-order polynomial equation, it can be  concluded that the catalyst amount and TEOA:M DES amount have a positive effect on  the FAME content. The maximum FAME content (99.67%) was achieved under the  following optimal reaction conditions: catalyst amount of 8% (based on the oil mass),  TEOA:M DES amount of 4.8% (based on the oil mass), and methanol:oil molar ratio of  6.1:1.",
publisher = "Leskovac : Faculty of Technology",
journal = "Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia",
title = "Optimization of the heterogeneously catalysed methanolysis of plum kernel oil in the presence of menthol-based deep eutectic solvent",
pages = "128-129",
url = "https://hdl.handle.net/21.15107/rcub_cer_7353"
}
Đorđević, B., Pavlović, S., Kostić, M.,& Stamenković, O.. (2023). Optimization of the heterogeneously catalysed methanolysis of plum kernel oil in the presence of menthol-based deep eutectic solvent. in Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia
Leskovac : Faculty of Technology., 128-129.
https://hdl.handle.net/21.15107/rcub_cer_7353
Đorđević B, Pavlović S, Kostić M, Stamenković O. Optimization of the heterogeneously catalysed methanolysis of plum kernel oil in the presence of menthol-based deep eutectic solvent. in Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia. 2023;:128-129.
https://hdl.handle.net/21.15107/rcub_cer_7353 .
Đorđević, Biljana, Pavlović, Stefan, Kostić, Milan, Stamenković, Olivera, "Optimization of the heterogeneously catalysed methanolysis of plum kernel oil in the presence of menthol-based deep eutectic solvent" in Book of abstracts - 15th international symposium „Novel technologies and sustainable development“,  October, 20-21, 2023, Leskovac, Serbia (2023):128-129,
https://hdl.handle.net/21.15107/rcub_cer_7353 .

Utilization of waste plum stones as a source of oil and catalyst for biodiesel production

Miladinović, Marija; Pavlović, Stefan; Banković-Ilić, Ivana; Kostić, Milan; Stamenković, Olivera; Veljković, Vlada

(Association of Chemical Engineers of Serbia, 2023)

TY  - JOUR
AU  - Miladinović, Marija
AU  - Pavlović, Stefan
AU  - Banković-Ilić, Ivana
AU  - Kostić, Milan
AU  - Stamenković, Olivera
AU  - Veljković, Vlada
PY  - 2023
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/7206
AB  - Possibilities of using waste plum stones in biodiesel production were investigated. The plum kernels were used as a source to obtain oil by the Soxhlet extraction method, while the whole plum stones, the plum stone shells that remained after the crashing, and the plum kernel cake that remained after the oil extraction, were burned off to obtain ashes. The collected ashes were characterized by elemental composition, porosity, and base strength and tested for catalytic activity in transesterification of esterified plum kernel oil. Dominant elements were potassium, calcium, and magnesium at different contents in the three obtained ashes. The most active catalyst was the plum stone shell ash, so the effect of temperature (40, 50, and 60°C) on the reaction rate was investigated. The reaction rate constant increased with the reaction temperature with the activation energy value of 58.8 kJ mol-1. In addition, the plum stone shell ash can be reused as a catalyst after recalcination.
AB  - U ovom radu istraživana je mogućnost korišćenja otpadnih koštica šljive u proizvodnji biodizela. Jezgra  šljive su iskorišćena kao sirovina za dobijanje ulja primenom Soxhlet-ove metode ekstrakcije. Cele  koštice, ljuske koštica šljive i pogača dobijena nakon ekstrakcije ulja iz jezgra šljive spaljeni su da bi se  dobio pepeo, koji je korišćen kao katalizator. Dobijene tri vrste sakupljenog pepela su najpre  okarakterisane u pogledu hemijskog sastava, poroznosti i baznosti, a zatim je testirana katalitička  aktivnost u transesterifikaciji esterifikovanog ulja koštica šljive. Dominantni elementi u pepelu, kao što  su kalijum, kalcijum i magnezijum, imali su različit sadržaj u sve tri vrste pepela. Najveću katalitičku  aktivnost pokazao je pepeo koštica šljive, zbog čega je dalje istraživan uticaj temperature (40, 50 i 60 °C)  na brzinu reakcije katalizovane ovim pepelom. Konstanta brzine reakcije povećavala se sa porastom  temperature reakcije, a vrednost energije aktivacije je 58,8 kJ mol-1 . Pored toga, pepeo koštica šljive  može se ponovo koristiti kao katalizator nakon rekalcinacije.
PB  - Association of Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - Utilization of waste plum stones as a source of oil and catalyst for biodiesel production
T1  - Korišćenje otpadnih koštica šljive kao izvora ulja i katalizatora za  proizvodnju biodizela
VL  - 77
IS  - 1
SP  - 39
EP  - 52
DO  - 10.2298/HEMIND221113009M
ER  - 
@article{
author = "Miladinović, Marija and Pavlović, Stefan and Banković-Ilić, Ivana and Kostić, Milan and Stamenković, Olivera and Veljković, Vlada",
year = "2023",
abstract = "Possibilities of using waste plum stones in biodiesel production were investigated. The plum kernels were used as a source to obtain oil by the Soxhlet extraction method, while the whole plum stones, the plum stone shells that remained after the crashing, and the plum kernel cake that remained after the oil extraction, were burned off to obtain ashes. The collected ashes were characterized by elemental composition, porosity, and base strength and tested for catalytic activity in transesterification of esterified plum kernel oil. Dominant elements were potassium, calcium, and magnesium at different contents in the three obtained ashes. The most active catalyst was the plum stone shell ash, so the effect of temperature (40, 50, and 60°C) on the reaction rate was investigated. The reaction rate constant increased with the reaction temperature with the activation energy value of 58.8 kJ mol-1. In addition, the plum stone shell ash can be reused as a catalyst after recalcination., U ovom radu istraživana je mogućnost korišćenja otpadnih koštica šljive u proizvodnji biodizela. Jezgra  šljive su iskorišćena kao sirovina za dobijanje ulja primenom Soxhlet-ove metode ekstrakcije. Cele  koštice, ljuske koštica šljive i pogača dobijena nakon ekstrakcije ulja iz jezgra šljive spaljeni su da bi se  dobio pepeo, koji je korišćen kao katalizator. Dobijene tri vrste sakupljenog pepela su najpre  okarakterisane u pogledu hemijskog sastava, poroznosti i baznosti, a zatim je testirana katalitička  aktivnost u transesterifikaciji esterifikovanog ulja koštica šljive. Dominantni elementi u pepelu, kao što  su kalijum, kalcijum i magnezijum, imali su različit sadržaj u sve tri vrste pepela. Najveću katalitičku  aktivnost pokazao je pepeo koštica šljive, zbog čega je dalje istraživan uticaj temperature (40, 50 i 60 °C)  na brzinu reakcije katalizovane ovim pepelom. Konstanta brzine reakcije povećavala se sa porastom  temperature reakcije, a vrednost energije aktivacije je 58,8 kJ mol-1 . Pored toga, pepeo koštica šljive  može se ponovo koristiti kao katalizator nakon rekalcinacije.",
publisher = "Association of Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "Utilization of waste plum stones as a source of oil and catalyst for biodiesel production, Korišćenje otpadnih koštica šljive kao izvora ulja i katalizatora za  proizvodnju biodizela",
volume = "77",
number = "1",
pages = "39-52",
doi = "10.2298/HEMIND221113009M"
}
Miladinović, M., Pavlović, S., Banković-Ilić, I., Kostić, M., Stamenković, O.,& Veljković, V.. (2023). Utilization of waste plum stones as a source of oil and catalyst for biodiesel production. in Hemijska industrija
Association of Chemical Engineers of Serbia., 77(1), 39-52.
https://doi.org/10.2298/HEMIND221113009M
Miladinović M, Pavlović S, Banković-Ilić I, Kostić M, Stamenković O, Veljković V. Utilization of waste plum stones as a source of oil and catalyst for biodiesel production. in Hemijska industrija. 2023;77(1):39-52.
doi:10.2298/HEMIND221113009M .
Miladinović, Marija, Pavlović, Stefan, Banković-Ilić, Ivana, Kostić, Milan, Stamenković, Olivera, Veljković, Vlada, "Utilization of waste plum stones as a source of oil and catalyst for biodiesel production" in Hemijska industrija, 77, no. 1 (2023):39-52,
https://doi.org/10.2298/HEMIND221113009M . .
1
1

Transesterification of used cooking sunflower oil catalyzed by hazelnut shell ash

Miladinović, Marija M.; Krstić, Jugoslav; Zdujić, Miodrag V.; Veselinović, Ljiljana M.; Veljović, Đorđe; Banković-Ilić, Ivana B.; Stamenković, Olivera; Veljković, Vlada B.

(Elsevier, 2022)

TY  - JOUR
AU  - Miladinović, Marija M.
AU  - Krstić, Jugoslav
AU  - Zdujić, Miodrag V.
AU  - Veselinović, Ljiljana M.
AU  - Veljović, Đorđe
AU  - Banković-Ilić, Ivana B.
AU  - Stamenković, Olivera
AU  - Veljković, Vlada B.
PY  - 2022
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/4868
AB  - Hazelnut shell ash was investigated as a new base catalyst for the transesterification of used cooking sunflower oil to biodiesel. To understand its catalytic properties, the prepared ash was characterized by EDX, XRD, TGA/DTA, Hg porosimetry, N2 physisorption, FE-SEM, and basic strength measurements. The effects of the catalyst loading in the range of 1–5% of the oil weight and the methanol-to-oil molar ratio of 6:1–18:1 on the kinetics of the fatty acid methyl esters synthesis were established. Moreover, the leaching and reusability of the catalyst were assessed. The obtained results revealed that hazelnut shell ash was mostly composed of K, Ca, and Mg. The highest ester content (98%) was achieved at the catalyst loading of 5%, the methanol-to-oil molar ratio of 12:1, and the reaction time of 10 min. The contribution of homogeneous catalysis because of the catalyst leaching was confirmed but did not determine the overall reaction rate. The catalyst can be reused after the recalcination at 800 °C for 2 h achieving the high methyl esters content (>96%) in 30 min after three subsequent runs. The overall reaction followed the pseudo-first-order kinetics with respect to triacylglycerols. A linear relationship between the apparent reaction rate constant and the catalyst loading and the methanol-to-oil molar ratio was determined. The determined value of the reaction rate constant was 0.0576 dm6/(min•mol2).
PB  - Elsevier
T2  - Renewable Energy
T1  - Transesterification of used cooking sunflower oil catalyzed by hazelnut shell ash
VL  - 183
SP  - 103
EP  - 113
DO  - 10.1016/j.renene.2021.10.071
ER  - 
@article{
author = "Miladinović, Marija M. and Krstić, Jugoslav and Zdujić, Miodrag V. and Veselinović, Ljiljana M. and Veljović, Đorđe and Banković-Ilić, Ivana B. and Stamenković, Olivera and Veljković, Vlada B.",
year = "2022",
abstract = "Hazelnut shell ash was investigated as a new base catalyst for the transesterification of used cooking sunflower oil to biodiesel. To understand its catalytic properties, the prepared ash was characterized by EDX, XRD, TGA/DTA, Hg porosimetry, N2 physisorption, FE-SEM, and basic strength measurements. The effects of the catalyst loading in the range of 1–5% of the oil weight and the methanol-to-oil molar ratio of 6:1–18:1 on the kinetics of the fatty acid methyl esters synthesis were established. Moreover, the leaching and reusability of the catalyst were assessed. The obtained results revealed that hazelnut shell ash was mostly composed of K, Ca, and Mg. The highest ester content (98%) was achieved at the catalyst loading of 5%, the methanol-to-oil molar ratio of 12:1, and the reaction time of 10 min. The contribution of homogeneous catalysis because of the catalyst leaching was confirmed but did not determine the overall reaction rate. The catalyst can be reused after the recalcination at 800 °C for 2 h achieving the high methyl esters content (>96%) in 30 min after three subsequent runs. The overall reaction followed the pseudo-first-order kinetics with respect to triacylglycerols. A linear relationship between the apparent reaction rate constant and the catalyst loading and the methanol-to-oil molar ratio was determined. The determined value of the reaction rate constant was 0.0576 dm6/(min•mol2).",
publisher = "Elsevier",
journal = "Renewable Energy",
title = "Transesterification of used cooking sunflower oil catalyzed by hazelnut shell ash",
volume = "183",
pages = "103-113",
doi = "10.1016/j.renene.2021.10.071"
}
Miladinović, M. M., Krstić, J., Zdujić, M. V., Veselinović, L. M., Veljović, Đ., Banković-Ilić, I. B., Stamenković, O.,& Veljković, V. B.. (2022). Transesterification of used cooking sunflower oil catalyzed by hazelnut shell ash. in Renewable Energy
Elsevier., 183, 103-113.
https://doi.org/10.1016/j.renene.2021.10.071
Miladinović MM, Krstić J, Zdujić MV, Veselinović LM, Veljović Đ, Banković-Ilić IB, Stamenković O, Veljković VB. Transesterification of used cooking sunflower oil catalyzed by hazelnut shell ash. in Renewable Energy. 2022;183:103-113.
doi:10.1016/j.renene.2021.10.071 .
Miladinović, Marija M., Krstić, Jugoslav, Zdujić, Miodrag V., Veselinović, Ljiljana M., Veljović, Đorđe, Banković-Ilić, Ivana B., Stamenković, Olivera, Veljković, Vlada B., "Transesterification of used cooking sunflower oil catalyzed by hazelnut shell ash" in Renewable Energy, 183 (2022):103-113,
https://doi.org/10.1016/j.renene.2021.10.071 . .
9
6

Biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing

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

(Elsevier, 2022)

TY  - JOUR
AU  - Krstić, Jugoslav
AU  - Nježić, Zvonko B.
AU  - Kostić, Milan D.
AU  - Marić, Boško D.
AU  - Šimurina, Olivera D.
AU  - Stamenković, Olivera
AU  - Veljković, Vlada
PY  - 2022
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/5402
AB  - A solid catalyst was prepared from waste filter cake (WFC) from a sugar beet processing plant and used, after calcination at 900 °C within 2 h, for biodiesel production from rapeseed oil and methanol. The calcined WFC (CFC) catalyst was characterized by XRF, FTIR, XRD, TGA/DTG, TPDe, TPD-CO2, SEM, N2 physisorption, and Hg porosimetry. The CFC is a CaO-based catalyst with a rigid, sustainable macroporous structure with the largest particles of 2.0 × 0.5 µm, a specific surface area of 7.3 m2/g, and a basicity of 0.27 mmol/g. It provides high conversion of 97.9% in 1 h at the methanol-to-oil molar ratio of 9:1, the temperature of 60 °C, and the catalyst loading of 10% of the oil mass. Its catalytic efficiency is comparable to the WFC-based nanocatalysts and CaO-based catalysts from natural sources. CFC was reused twice with a negligible decrease in catalytic activity, ensuring a FAME content above 97% in 1 h. The biodiesel produced from rapeseed oil over the CFC catalyst has good fuel properties that fulfill most of EN 14214. Therefore, WFC is a promising source of a low-cost, highly active, basic, and environmentally friendly CFC catalyst, which could reduce biodiesel production costs. From this point of view, this catalyst has great potential for developing the process at the commercial level.
PB  - Elsevier
T2  - Process Safety and Environmental Protection
T1  - Biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing
VL  - 168
SP  - 463
EP  - 473
DO  - 10.1016/j.psep.2022.10.021
ER  - 
@article{
author = "Krstić, Jugoslav and Nježić, Zvonko B. and Kostić, Milan D. and Marić, Boško D. and Šimurina, Olivera D. and Stamenković, Olivera and Veljković, Vlada",
year = "2022",
abstract = "A solid catalyst was prepared from waste filter cake (WFC) from a sugar beet processing plant and used, after calcination at 900 °C within 2 h, for biodiesel production from rapeseed oil and methanol. The calcined WFC (CFC) catalyst was characterized by XRF, FTIR, XRD, TGA/DTG, TPDe, TPD-CO2, SEM, N2 physisorption, and Hg porosimetry. The CFC is a CaO-based catalyst with a rigid, sustainable macroporous structure with the largest particles of 2.0 × 0.5 µm, a specific surface area of 7.3 m2/g, and a basicity of 0.27 mmol/g. It provides high conversion of 97.9% in 1 h at the methanol-to-oil molar ratio of 9:1, the temperature of 60 °C, and the catalyst loading of 10% of the oil mass. Its catalytic efficiency is comparable to the WFC-based nanocatalysts and CaO-based catalysts from natural sources. CFC was reused twice with a negligible decrease in catalytic activity, ensuring a FAME content above 97% in 1 h. The biodiesel produced from rapeseed oil over the CFC catalyst has good fuel properties that fulfill most of EN 14214. Therefore, WFC is a promising source of a low-cost, highly active, basic, and environmentally friendly CFC catalyst, which could reduce biodiesel production costs. From this point of view, this catalyst has great potential for developing the process at the commercial level.",
publisher = "Elsevier",
journal = "Process Safety and Environmental Protection",
title = "Biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing",
volume = "168",
pages = "463-473",
doi = "10.1016/j.psep.2022.10.021"
}
Krstić, J., Nježić, Z. B., Kostić, M. D., Marić, B. D., Šimurina, O. D., Stamenković, O.,& Veljković, V.. (2022). Biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing. in Process Safety and Environmental Protection
Elsevier., 168, 463-473.
https://doi.org/10.1016/j.psep.2022.10.021
Krstić J, Nježić ZB, Kostić MD, Marić BD, Šimurina OD, Stamenković O, Veljković V. Biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing. in Process Safety and Environmental Protection. 2022;168:463-473.
doi:10.1016/j.psep.2022.10.021 .
Krstić, Jugoslav, Nježić, Zvonko B., Kostić, Milan D., Marić, Boško D., Šimurina, Olivera D., Stamenković, Olivera, Veljković, Vlada, "Biodiesel production from rapeseed oil over calcined waste filter cake from sugar beet processing" in Process Safety and Environmental Protection, 168 (2022):463-473,
https://doi.org/10.1016/j.psep.2022.10.021 . .
1
6
6

Modeling the biodiesel production using the wheat straw ash as a catalyst

Veličković, Ana; Avramović, Jelena M.; Kostić, Milan; Krstić, Jugoslav; Stamenković, Olivera; Veljković, Vlada B.

(Belgrade : Association of the Chemical Engineers of Serbia, 2021)

TY  - JOUR
AU  - Veličković, Ana
AU  - Avramović, Jelena M.
AU  - Kostić, Milan
AU  - Krstić, Jugoslav
AU  - Stamenković, Olivera
AU  - Veljković, Vlada B.
PY  - 2021
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/4844
AB  - Wheat straw ash (WSA) was investigated as a new catalyst in biodiesel production from sunflower oil. The catalyst was characterized by temperature-programmed decomposition, X-ray powder diffraction, Hg porosimetry, N2 physisorption, and scanning electron microscopy - energy dispersive X-ray spectroscopy methods. The methanolysis reaction was tested in the temperature range of 55–65 oC, the catalyst loading range 10–20 % of the oil weight, and the methanol-to-oil molar ratio range 18 : 1–24 : 1. The reaction conditions of the sunflower oil methanolysis over WSA were optimized by using the response surface methodology in combination with the historical experimental design. The optimum process conditions ensuring the highest fatty acid methyl esters (FAME) content of 98.6 % were the reaction temperature of 60.3 oC, the catalyst loading of 11.6 % (based on the oil weight), the methanol-to-oil molar ratio of 18.3 :1, and the reaction time of 124 min. The values of the statistical criteria, such as coefficients of determination (R2 = 0.811, R2pred = 0.789, R2adj = 0.761) and the mean relative percent deviation (MRPD) value of 10.6 % (66 data) implied the acceptability and precision of the developed model. The FAME content after 4 h of reaction under the optimal conditions decreased to 37, 12, and 3 %, after the first, second, and third reuse, respectively.
AB  - Pepeo pšenične slame (PPS) je korišćen kao katalizator u proizvodnji biodizela iz sunco-kretovog ulja. Karakterizacija katalizatora je izvršena primenom metoda tempera-turski programiranom razgradnjom (temperature-programmed decomposition, TPDe), rentgenskom difrakcijom (X-ray diffraction, XRD), Hg porozimetrijom, N2 fizi-sorpcijom i skenirajućom elektronskom mikrosopijom sa energo-disperzivnom spek-trometrijom (scanning electron microscopy and energy dispersive X-ray spectroscopy, SEM-EDS). Reakcija metanolize istraživana je pri sledećim reakcionim uslovima: tem-peraturni opseg 55-65 °C; količina katalizatora 10-20 % (računato na masu ulja) i opseg molskog odnosa methanol : ulje 18 : 1 – 24 : 1. Optimizacija reakcionih uslova izvršena je metodologijom površine odziva u kombinaciji sa istorijskim eksperimentalnim planom. Maksimalni prinos metil estara masnih kiselina (MEMK) od 98,6 % postignut je pri sledećim optimalnim reakcionim uslovima: temperatura 60,3 oC, količina katalizatora 11,6 % (računato na masu ulja), molski odnos methanol : ulje 18,3 : 1 i vreme trajanja reakcije 124 min. Vrednosti koeficijenata determinacije (R2 = 0,811, R2pred = 0,789, R2adj = 0,761) i srednjeg relativnog odstupanja (10,6 %, 66 podataka) ukazali su na prihvatljivost i pouzdanost razvijenog modela. Sadržaj MEMK nakon 4 h reakcije pri optimalnim uslovima smanjen je na 37, 12 i 3 % nakon prve, druge i treće upotrebe katalizatora, redom.
PB  - Belgrade : Association of the Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - Modeling the biodiesel production using the wheat straw ash as a catalyst
T1  - Pepeo pšenične slame kao katalizator u proizvodnji biodizela
VL  - 75
IS  - 5
SP  - 257
EP  - 276
DO  - 10.2298/HEMIND210526028V
ER  - 
@article{
author = "Veličković, Ana and Avramović, Jelena M. and Kostić, Milan and Krstić, Jugoslav and Stamenković, Olivera and Veljković, Vlada B.",
year = "2021",
abstract = "Wheat straw ash (WSA) was investigated as a new catalyst in biodiesel production from sunflower oil. The catalyst was characterized by temperature-programmed decomposition, X-ray powder diffraction, Hg porosimetry, N2 physisorption, and scanning electron microscopy - energy dispersive X-ray spectroscopy methods. The methanolysis reaction was tested in the temperature range of 55–65 oC, the catalyst loading range 10–20 % of the oil weight, and the methanol-to-oil molar ratio range 18 : 1–24 : 1. The reaction conditions of the sunflower oil methanolysis over WSA were optimized by using the response surface methodology in combination with the historical experimental design. The optimum process conditions ensuring the highest fatty acid methyl esters (FAME) content of 98.6 % were the reaction temperature of 60.3 oC, the catalyst loading of 11.6 % (based on the oil weight), the methanol-to-oil molar ratio of 18.3 :1, and the reaction time of 124 min. The values of the statistical criteria, such as coefficients of determination (R2 = 0.811, R2pred = 0.789, R2adj = 0.761) and the mean relative percent deviation (MRPD) value of 10.6 % (66 data) implied the acceptability and precision of the developed model. The FAME content after 4 h of reaction under the optimal conditions decreased to 37, 12, and 3 %, after the first, second, and third reuse, respectively., Pepeo pšenične slame (PPS) je korišćen kao katalizator u proizvodnji biodizela iz sunco-kretovog ulja. Karakterizacija katalizatora je izvršena primenom metoda tempera-turski programiranom razgradnjom (temperature-programmed decomposition, TPDe), rentgenskom difrakcijom (X-ray diffraction, XRD), Hg porozimetrijom, N2 fizi-sorpcijom i skenirajućom elektronskom mikrosopijom sa energo-disperzivnom spek-trometrijom (scanning electron microscopy and energy dispersive X-ray spectroscopy, SEM-EDS). Reakcija metanolize istraživana je pri sledećim reakcionim uslovima: tem-peraturni opseg 55-65 °C; količina katalizatora 10-20 % (računato na masu ulja) i opseg molskog odnosa methanol : ulje 18 : 1 – 24 : 1. Optimizacija reakcionih uslova izvršena je metodologijom površine odziva u kombinaciji sa istorijskim eksperimentalnim planom. Maksimalni prinos metil estara masnih kiselina (MEMK) od 98,6 % postignut je pri sledećim optimalnim reakcionim uslovima: temperatura 60,3 oC, količina katalizatora 11,6 % (računato na masu ulja), molski odnos methanol : ulje 18,3 : 1 i vreme trajanja reakcije 124 min. Vrednosti koeficijenata determinacije (R2 = 0,811, R2pred = 0,789, R2adj = 0,761) i srednjeg relativnog odstupanja (10,6 %, 66 podataka) ukazali su na prihvatljivost i pouzdanost razvijenog modela. Sadržaj MEMK nakon 4 h reakcije pri optimalnim uslovima smanjen je na 37, 12 i 3 % nakon prve, druge i treće upotrebe katalizatora, redom.",
publisher = "Belgrade : Association of the Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "Modeling the biodiesel production using the wheat straw ash as a catalyst, Pepeo pšenične slame kao katalizator u proizvodnji biodizela",
volume = "75",
number = "5",
pages = "257-276",
doi = "10.2298/HEMIND210526028V"
}
Veličković, A., Avramović, J. M., Kostić, M., Krstić, J., Stamenković, O.,& Veljković, V. B.. (2021). Modeling the biodiesel production using the wheat straw ash as a catalyst. in Hemijska industrija
Belgrade : Association of the Chemical Engineers of Serbia., 75(5), 257-276.
https://doi.org/10.2298/HEMIND210526028V
Veličković A, Avramović JM, Kostić M, Krstić J, Stamenković O, Veljković VB. Modeling the biodiesel production using the wheat straw ash as a catalyst. in Hemijska industrija. 2021;75(5):257-276.
doi:10.2298/HEMIND210526028V .
Veličković, Ana, Avramović, Jelena M., Kostić, Milan, Krstić, Jugoslav, Stamenković, Olivera, Veljković, Vlada B., "Modeling the biodiesel production using the wheat straw ash as a catalyst" in Hemijska industrija, 75, no. 5 (2021):257-276,
https://doi.org/10.2298/HEMIND210526028V . .
5

Valorization of walnut shell ash as a catalyst for biodiesel production

Miladinović, Marija R.; Zdujić, Miodrag; Veljović, Đorđe; Krstić, Jugoslav; Banković-Ilić, Ivana B.; Veljković, Vlada B.; Stamenković, Olivera

(Elsevier, 2020)

TY  - JOUR
AU  - Miladinović, Marija R.
AU  - Zdujić, Miodrag
AU  - Veljović, Đorđe
AU  - Krstić, Jugoslav
AU  - Banković-Ilić, Ivana B.
AU  - Veljković, Vlada B.
AU  - Stamenković, Olivera
PY  - 2020
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3217
AB  - The catalytic activity of the walnut shell ash was investigated in the biodiesel production by the sunflower oil methanolysis. The catalyst was characterized by the TG-DTA, XRD, Hg porosimetry, N2 physisorption, SEM, and Hammett method. In addition, the effects of the catalyst loading and the methanol-to-oil molar ratio on the methyl esters synthesis were tested at the reaction temperature of 60 °C. The walnut shell ash provided a very fast reaction and a high FAME content (over 98%). As the reaction occurred in the absence of triacylglycerols mass transfer limitation, the pseudo-first-order model was employed for describing the kinetics of the reaction. The catalyst was successfully reused four times after the regeneration of the catalytic activity by recalcination at 800 °C.
PB  - Elsevier
T2  - Renewable Energy
T1  - Valorization of walnut shell ash as a catalyst for biodiesel production
VL  - 147
SP  - 1033
EP  - 1043
DO  - 10.1016/j.renene.2019.09.056
ER  - 
@article{
author = "Miladinović, Marija R. and Zdujić, Miodrag and Veljović, Đorđe and Krstić, Jugoslav and Banković-Ilić, Ivana B. and Veljković, Vlada B. and Stamenković, Olivera",
year = "2020",
abstract = "The catalytic activity of the walnut shell ash was investigated in the biodiesel production by the sunflower oil methanolysis. The catalyst was characterized by the TG-DTA, XRD, Hg porosimetry, N2 physisorption, SEM, and Hammett method. In addition, the effects of the catalyst loading and the methanol-to-oil molar ratio on the methyl esters synthesis were tested at the reaction temperature of 60 °C. The walnut shell ash provided a very fast reaction and a high FAME content (over 98%). As the reaction occurred in the absence of triacylglycerols mass transfer limitation, the pseudo-first-order model was employed for describing the kinetics of the reaction. The catalyst was successfully reused four times after the regeneration of the catalytic activity by recalcination at 800 °C.",
publisher = "Elsevier",
journal = "Renewable Energy",
title = "Valorization of walnut shell ash as a catalyst for biodiesel production",
volume = "147",
pages = "1033-1043",
doi = "10.1016/j.renene.2019.09.056"
}
Miladinović, M. R., Zdujić, M., Veljović, Đ., Krstić, J., Banković-Ilić, I. B., Veljković, V. B.,& Stamenković, O.. (2020). Valorization of walnut shell ash as a catalyst for biodiesel production. in Renewable Energy
Elsevier., 147, 1033-1043.
https://doi.org/10.1016/j.renene.2019.09.056
Miladinović MR, Zdujić M, Veljović Đ, Krstić J, Banković-Ilić IB, Veljković VB, Stamenković O. Valorization of walnut shell ash as a catalyst for biodiesel production. in Renewable Energy. 2020;147:1033-1043.
doi:10.1016/j.renene.2019.09.056 .
Miladinović, Marija R., Zdujić, Miodrag, Veljović, Đorđe, Krstić, Jugoslav, Banković-Ilić, Ivana B., Veljković, Vlada B., Stamenković, Olivera, "Valorization of walnut shell ash as a catalyst for biodiesel production" in Renewable Energy, 147 (2020):1033-1043,
https://doi.org/10.1016/j.renene.2019.09.056 . .
87
31
92

Valorization of walnut shell ash as a catalyst for biodiesel production

Miladinović, Marija R.; Zdujić, Miodrag; Veljović, Đorđe; Krstić, Jugoslav; Banković-Ilić, Ivana B.; Veljković, Vlada B.; Stamenković, Olivera

(Elsevier, 2020)

TY  - JOUR
AU  - Miladinović, Marija R.
AU  - Zdujić, Miodrag
AU  - Veljović, Đorđe
AU  - Krstić, Jugoslav
AU  - Banković-Ilić, Ivana B.
AU  - Veljković, Vlada B.
AU  - Stamenković, Olivera
PY  - 2020
UR  - http://dais.sanu.ac.rs/123456789/6903
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3319
AB  - The catalytic activity of the walnut shell ash was investigated in the biodiesel production by the sunflower oil methanolysis. The catalyst was characterized by the TG-DTA, XRD, Hg porosimetry, N2 physisorption, SEM, and Hammett method. In addition, the effects of the catalyst loading and the methanol-to-oil molar ratio on the methyl esters synthesis were tested at the reaction temperature of 60 °C. The walnut shell ash provided a very fast reaction and a high FAME content (over 98%). As the reaction occurred in the absence of triacylglycerols mass transfer limitation, the pseudo-first-order model was employed for describing the kinetics of the reaction. The catalyst was successfully reused four times after the regeneration of the catalytic activity by recalcination at 800 °C.
PB  - Elsevier
T2  - Renewable Energy
T1  - Valorization of walnut shell ash as a catalyst for biodiesel production
VL  - 147
SP  - 1033
EP  - 1043
DO  - 10.1016/j.renene.2019.09.056
ER  - 
@article{
author = "Miladinović, Marija R. and Zdujić, Miodrag and Veljović, Đorđe and Krstić, Jugoslav and Banković-Ilić, Ivana B. and Veljković, Vlada B. and Stamenković, Olivera",
year = "2020",
abstract = "The catalytic activity of the walnut shell ash was investigated in the biodiesel production by the sunflower oil methanolysis. The catalyst was characterized by the TG-DTA, XRD, Hg porosimetry, N2 physisorption, SEM, and Hammett method. In addition, the effects of the catalyst loading and the methanol-to-oil molar ratio on the methyl esters synthesis were tested at the reaction temperature of 60 °C. The walnut shell ash provided a very fast reaction and a high FAME content (over 98%). As the reaction occurred in the absence of triacylglycerols mass transfer limitation, the pseudo-first-order model was employed for describing the kinetics of the reaction. The catalyst was successfully reused four times after the regeneration of the catalytic activity by recalcination at 800 °C.",
publisher = "Elsevier",
journal = "Renewable Energy",
title = "Valorization of walnut shell ash as a catalyst for biodiesel production",
volume = "147",
pages = "1033-1043",
doi = "10.1016/j.renene.2019.09.056"
}
Miladinović, M. R., Zdujić, M., Veljović, Đ., Krstić, J., Banković-Ilić, I. B., Veljković, V. B.,& Stamenković, O.. (2020). Valorization of walnut shell ash as a catalyst for biodiesel production. in Renewable Energy
Elsevier., 147, 1033-1043.
https://doi.org/10.1016/j.renene.2019.09.056
Miladinović MR, Zdujić M, Veljović Đ, Krstić J, Banković-Ilić IB, Veljković VB, Stamenković O. Valorization of walnut shell ash as a catalyst for biodiesel production. in Renewable Energy. 2020;147:1033-1043.
doi:10.1016/j.renene.2019.09.056 .
Miladinović, Marija R., Zdujić, Miodrag, Veljović, Đorđe, Krstić, Jugoslav, Banković-Ilić, Ivana B., Veljković, Vlada B., Stamenković, Olivera, "Valorization of walnut shell ash as a catalyst for biodiesel production" in Renewable Energy, 147 (2020):1033-1043,
https://doi.org/10.1016/j.renene.2019.09.056 . .
87
31
94

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 .

Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst

Marinković, Dalibor; Miladinović, Marija R.; Avramović, Jelena M.; Krstić, Ivan; Stanković, Miroslav; Stamenković, Olivera; Jovanović, Dušan M.; Veljković, Vlada B.

(Oxford : Pergamon-Elsevier Science Ltd, 2018)

TY  - JOUR
AU  - Marinković, Dalibor
AU  - Miladinović, Marija R.
AU  - Avramović, Jelena M.
AU  - Krstić, Ivan
AU  - Stanković, Miroslav
AU  - Stamenković, Olivera
AU  - Jovanović, Dušan M.
AU  - Veljković, Vlada B.
PY  - 2018
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/2301
AB  - Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 particles were conducted in batch stirred and packed-bed tubular reactors at 60 degrees C. The proposed three-parameter kinetic model describing the overall reaction with a variable mechanism was successfully applied to both batch and continuous reactions. The process optimization was done using the response surface methodology combined with a central composite design. The obtained optimal catalyst concentration, methanol-to-oil molar ratio and reaction time for the batch reaction were 0.55% (CaO to the oil), 9:1 and 5.22 h, respectively. In the continuous process, the catalyst was highly active stable and slightly leachable during 30 h. The deactivation of the catalyst was due to massive deposition of the organic molecules from the reaction mixture, which sheltered the catalytically active sites on the catalyst surface.
PB  - Oxford : Pergamon-Elsevier Science Ltd
T2  - Energy Conversion and Management
T1  - Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst
VL  - 163
SP  - 122
EP  - 133
DO  - 10.1016/j.enconman.2018.02.048
ER  - 
@article{
author = "Marinković, Dalibor and Miladinović, Marija R. and Avramović, Jelena M. and Krstić, Ivan and Stanković, Miroslav and Stamenković, Olivera and Jovanović, Dušan M. and Veljković, Vlada B.",
year = "2018",
abstract = "Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 particles were conducted in batch stirred and packed-bed tubular reactors at 60 degrees C. The proposed three-parameter kinetic model describing the overall reaction with a variable mechanism was successfully applied to both batch and continuous reactions. The process optimization was done using the response surface methodology combined with a central composite design. The obtained optimal catalyst concentration, methanol-to-oil molar ratio and reaction time for the batch reaction were 0.55% (CaO to the oil), 9:1 and 5.22 h, respectively. In the continuous process, the catalyst was highly active stable and slightly leachable during 30 h. The deactivation of the catalyst was due to massive deposition of the organic molecules from the reaction mixture, which sheltered the catalytically active sites on the catalyst surface.",
publisher = "Oxford : Pergamon-Elsevier Science Ltd",
journal = "Energy Conversion and Management",
title = "Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst",
volume = "163",
pages = "122-133",
doi = "10.1016/j.enconman.2018.02.048"
}
Marinković, D., Miladinović, M. R., Avramović, J. M., Krstić, I., Stanković, M., Stamenković, O., Jovanović, D. M.,& Veljković, V. B.. (2018). Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst. in Energy Conversion and Management
Oxford : Pergamon-Elsevier Science Ltd., 163, 122-133.
https://doi.org/10.1016/j.enconman.2018.02.048
Marinković D, Miladinović MR, Avramović JM, Krstić I, Stanković M, Stamenković O, Jovanović DM, Veljković VB. Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst. in Energy Conversion and Management. 2018;163:122-133.
doi:10.1016/j.enconman.2018.02.048 .
Marinković, Dalibor, Miladinović, Marija R., Avramović, Jelena M., Krstić, Ivan, Stanković, Miroslav, Stamenković, Olivera, Jovanović, Dušan M., Veljković, Vlada B., "Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst" in Energy Conversion and Management, 163 (2018):122-133,
https://doi.org/10.1016/j.enconman.2018.02.048 . .
21
14
21

Supplementary material for: "Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst"

Marinković, Dalibor; Miladinović, Marija R.; Avramović, Jelena M.; Krstić, Ivan; Stanković, Miroslav; Stamenković, Olivera; Jovanović, Dušan M.; Veljković, Vlada B.

(Elsevier, 2018)

TY  - DATA
AU  - Marinković, Dalibor
AU  - Miladinović, Marija R.
AU  - Avramović, Jelena M.
AU  - Krstić, Ivan
AU  - Stanković, Miroslav
AU  - Stamenković, Olivera
AU  - Jovanović, Dušan M.
AU  - Veljković, Vlada B.
PY  - 2018
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/4490
AB  - Supplementary material for: Marinković, D., Miladinovic, M. R., Avramović, J. M., Krstic, I. B., Stanković, M., Stamenković, O., Jovanović, D. M.,& Veljković, V. B. (2018). Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst. Energy Conversion and Management, 163, 122-133. https://doi.org/10.1016/j.enconman.2018.02.048
PB  - Elsevier
T2  - Energy Conversion and Management
T1  - Supplementary material for: "Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst"
UR  - https://hdl.handle.net/21.15107/rcub_cer_4490
ER  - 
@misc{
author = "Marinković, Dalibor and Miladinović, Marija R. and Avramović, Jelena M. and Krstić, Ivan and Stanković, Miroslav and Stamenković, Olivera and Jovanović, Dušan M. and Veljković, Vlada B.",
year = "2018",
abstract = "Supplementary material for: Marinković, D., Miladinovic, M. R., Avramović, J. M., Krstic, I. B., Stanković, M., Stamenković, O., Jovanović, D. M.,& Veljković, V. B. (2018). Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst. Energy Conversion and Management, 163, 122-133. https://doi.org/10.1016/j.enconman.2018.02.048",
publisher = "Elsevier",
journal = "Energy Conversion and Management",
title = "Supplementary material for: "Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst"",
url = "https://hdl.handle.net/21.15107/rcub_cer_4490"
}
Marinković, D., Miladinović, M. R., Avramović, J. M., Krstić, I., Stanković, M., Stamenković, O., Jovanović, D. M.,& Veljković, V. B.. (2018). Supplementary material for: "Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst". in Energy Conversion and Management
Elsevier..
https://hdl.handle.net/21.15107/rcub_cer_4490
Marinković D, Miladinović MR, Avramović JM, Krstić I, Stanković M, Stamenković O, Jovanović DM, Veljković VB. Supplementary material for: "Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst". in Energy Conversion and Management. 2018;.
https://hdl.handle.net/21.15107/rcub_cer_4490 .
Marinković, Dalibor, Miladinović, Marija R., Avramović, Jelena M., Krstić, Ivan, Stanković, Miroslav, Stamenković, Olivera, Jovanović, Dušan M., Veljković, Vlada B., "Supplementary material for: "Kinetic modeling and optimization of sunflower oil methanolysis catalyzed by spherically-shaped CaO/gamma-Al2O3 catalyst"" in Energy Conversion and Management (2018),
https://hdl.handle.net/21.15107/rcub_cer_4490 .

Synthesis and characterization of spherically-shaped CaO/gamma-Al2O3 catalyst and its application in biodiesel production

Marinković, Dalibor; Avramović, Jelena M.; Stanković, Miroslav; Stamenković, Olivera; Jovanović, Dušan M.; Veljković, Vlada B.

(Oxford : Pergamon-Elsevier Science Ltd, 2017)

TY  - JOUR
AU  - Marinković, Dalibor
AU  - Avramović, Jelena M.
AU  - Stanković, Miroslav
AU  - Stamenković, Olivera
AU  - Jovanović, Dušan M.
AU  - Veljković, Vlada B.
PY  - 2017
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/2255
AB  - Loading CaO onto spherically-shaped gamma-Al2O3 support was applied for the preparation of a cost-effective and environmentally-friendly heterogeneous catalyst for biodiesel production. Physico-chemical, textural and morphological characterization was performed using optical emission spectroscopy (ICP OES), Hg-porosimetry, N-2 physisorption, scanning electron microscopy (FESEM), X-ray diffraction (XRPD), Fourier transform infrared spectroscopy (ATR FTIR) and Hammett indicators. The effects of catalyst preparation conditions (different precursor salts and calcination temperatures) on the catalyst activity, and the reaction conditions (methanol-to-oil molar ratio and catalyst loading) on the reaction rate and esters yield were studied. In addition, catalyst stability was investigated. The most active catalyst was derived from the nitrate precursor after calcination at 475 degrees C (inert atmosphere). Under mild reaction conditions (60 degrees C, 5 h, 900 rpm, methanol-to-oil molar ratio of 12:1 and catalyst loading (CaO wt% to the oil) of 0.5%), the equilibrium ester content of 94.3% was obtained in the methanolysis of sunflower oil in a batch reactor. The catalyst remained sufficiently active in two consecutive cycles without any pretreatment. Mechanical erosion caused by stirring and massive deposition of organic molecules from the reaction mixture caused the decrease of catalytic activity while CaO leaching was negligible.
PB  - Oxford : Pergamon-Elsevier Science Ltd
T2  - Energy Conversion and Management
T1  - Synthesis and characterization of spherically-shaped CaO/gamma-Al2O3 catalyst and its application in biodiesel production
VL  - 144
SP  - 399
EP  - 413
DO  - 10.1016/j.enconman.2017.04.079
ER  - 
@article{
author = "Marinković, Dalibor and Avramović, Jelena M. and Stanković, Miroslav and Stamenković, Olivera and Jovanović, Dušan M. and Veljković, Vlada B.",
year = "2017",
abstract = "Loading CaO onto spherically-shaped gamma-Al2O3 support was applied for the preparation of a cost-effective and environmentally-friendly heterogeneous catalyst for biodiesel production. Physico-chemical, textural and morphological characterization was performed using optical emission spectroscopy (ICP OES), Hg-porosimetry, N-2 physisorption, scanning electron microscopy (FESEM), X-ray diffraction (XRPD), Fourier transform infrared spectroscopy (ATR FTIR) and Hammett indicators. The effects of catalyst preparation conditions (different precursor salts and calcination temperatures) on the catalyst activity, and the reaction conditions (methanol-to-oil molar ratio and catalyst loading) on the reaction rate and esters yield were studied. In addition, catalyst stability was investigated. The most active catalyst was derived from the nitrate precursor after calcination at 475 degrees C (inert atmosphere). Under mild reaction conditions (60 degrees C, 5 h, 900 rpm, methanol-to-oil molar ratio of 12:1 and catalyst loading (CaO wt% to the oil) of 0.5%), the equilibrium ester content of 94.3% was obtained in the methanolysis of sunflower oil in a batch reactor. The catalyst remained sufficiently active in two consecutive cycles without any pretreatment. Mechanical erosion caused by stirring and massive deposition of organic molecules from the reaction mixture caused the decrease of catalytic activity while CaO leaching was negligible.",
publisher = "Oxford : Pergamon-Elsevier Science Ltd",
journal = "Energy Conversion and Management",
title = "Synthesis and characterization of spherically-shaped CaO/gamma-Al2O3 catalyst and its application in biodiesel production",
volume = "144",
pages = "399-413",
doi = "10.1016/j.enconman.2017.04.079"
}
Marinković, D., Avramović, J. M., Stanković, M., Stamenković, O., Jovanović, D. M.,& Veljković, V. B.. (2017). Synthesis and characterization of spherically-shaped CaO/gamma-Al2O3 catalyst and its application in biodiesel production. in Energy Conversion and Management
Oxford : Pergamon-Elsevier Science Ltd., 144, 399-413.
https://doi.org/10.1016/j.enconman.2017.04.079
Marinković D, Avramović JM, Stanković M, Stamenković O, Jovanović DM, Veljković VB. Synthesis and characterization of spherically-shaped CaO/gamma-Al2O3 catalyst and its application in biodiesel production. in Energy Conversion and Management. 2017;144:399-413.
doi:10.1016/j.enconman.2017.04.079 .
Marinković, Dalibor, Avramović, Jelena M., Stanković, Miroslav, Stamenković, Olivera, Jovanović, Dušan M., Veljković, Vlada B., "Synthesis and characterization of spherically-shaped CaO/gamma-Al2O3 catalyst and its application in biodiesel production" in Energy Conversion and Management, 144 (2017):399-413,
https://doi.org/10.1016/j.enconman.2017.04.079 . .
62
41
65

Modeling and optimization of sunflower oil methanolysis over quicklime bits in a packed bed tubular reactor using the response surface methodology

Miladinović, Marija R.; Stamenković, Olivera; Banković, Predrag; Milutinović Nikolić, Aleksandra; Jovanović, Dušan M.; Veljković, Vlada B.

(Oxford : Pergamon-Elsevier Science Ltd, 2016)

TY  - JOUR
AU  - Miladinović, Marija R.
AU  - Stamenković, Olivera
AU  - Banković, Predrag
AU  - Milutinović Nikolić, Aleksandra
AU  - Jovanović, Dušan M.
AU  - Veljković, Vlada B.
PY  - 2016
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1949
AB  - The effect of the residence time (i.e. liquid flow rate through the reactor), methanol-to-oil molar ratio and reaction temperature on the fatty acid methyl esters (FAMEs) content at the output of a continuous packed bed tubular reactor was modeled by the response surface methodology (RSM) combined with the 3(3) full factorial design (FFD) with replication or the Box-Behnken design (BBD) with five center points. The methanolysis of sunflower oil was carried out at the residence time of 1.0, 1.5 and 2.0 h, the methanol-to-oil molar ratios of 6:1, 12:1 and 18:1 and the reaction temperature of 40, 50 and 60 degrees C under the atmospheric pressure. Based on the used experimental designs, the model equations containing only linear and two-factor interaction terms were developed for predicting the FAME content, which were validated through the use of the unseen data. Applying the analysis of variance (ANOVA), all three factors were shown to have a significant influence on the FAME content. Acceptable statistical predictability and accuracy resulted from both designs since the values of the coefficient of determination were close to unity while the values of the mean relative percentage deviation were relatively low ( LT +/- 10%). In addition, both designs predicted the maximum FAME content of above 99%, which agreed closely with the actual FAME content (98.8%). The same optimal reaction temperature (60 degrees C) and residence time (2.0 h) were determined by both designs while the BBD model suggested a slightly lower methanol-to oil molar ratio (12.2:1) than the 3(3) FFD model (12.8:1). Since the BBD realization involved three times smaller number of experimental runs, thus requiring lower costs, less labor and shorter time than the 33 FFD, it could be recommended for the optimization of biodiesel production processes.
PB  - Oxford : Pergamon-Elsevier Science Ltd
T2  - Energy Conversion and Management
T1  - Modeling and optimization of sunflower oil methanolysis over quicklime bits in a packed bed tubular reactor using the response surface methodology
VL  - 130
SP  - 25
EP  - 33
DO  - 10.1016/j.enconman.2016.10.020
ER  - 
@article{
author = "Miladinović, Marija R. and Stamenković, Olivera and Banković, Predrag and Milutinović Nikolić, Aleksandra and Jovanović, Dušan M. and Veljković, Vlada B.",
year = "2016",
abstract = "The effect of the residence time (i.e. liquid flow rate through the reactor), methanol-to-oil molar ratio and reaction temperature on the fatty acid methyl esters (FAMEs) content at the output of a continuous packed bed tubular reactor was modeled by the response surface methodology (RSM) combined with the 3(3) full factorial design (FFD) with replication or the Box-Behnken design (BBD) with five center points. The methanolysis of sunflower oil was carried out at the residence time of 1.0, 1.5 and 2.0 h, the methanol-to-oil molar ratios of 6:1, 12:1 and 18:1 and the reaction temperature of 40, 50 and 60 degrees C under the atmospheric pressure. Based on the used experimental designs, the model equations containing only linear and two-factor interaction terms were developed for predicting the FAME content, which were validated through the use of the unseen data. Applying the analysis of variance (ANOVA), all three factors were shown to have a significant influence on the FAME content. Acceptable statistical predictability and accuracy resulted from both designs since the values of the coefficient of determination were close to unity while the values of the mean relative percentage deviation were relatively low ( LT +/- 10%). In addition, both designs predicted the maximum FAME content of above 99%, which agreed closely with the actual FAME content (98.8%). The same optimal reaction temperature (60 degrees C) and residence time (2.0 h) were determined by both designs while the BBD model suggested a slightly lower methanol-to oil molar ratio (12.2:1) than the 3(3) FFD model (12.8:1). Since the BBD realization involved three times smaller number of experimental runs, thus requiring lower costs, less labor and shorter time than the 33 FFD, it could be recommended for the optimization of biodiesel production processes.",
publisher = "Oxford : Pergamon-Elsevier Science Ltd",
journal = "Energy Conversion and Management",
title = "Modeling and optimization of sunflower oil methanolysis over quicklime bits in a packed bed tubular reactor using the response surface methodology",
volume = "130",
pages = "25-33",
doi = "10.1016/j.enconman.2016.10.020"
}
Miladinović, M. R., Stamenković, O., Banković, P., Milutinović Nikolić, A., Jovanović, D. M.,& Veljković, V. B.. (2016). Modeling and optimization of sunflower oil methanolysis over quicklime bits in a packed bed tubular reactor using the response surface methodology. in Energy Conversion and Management
Oxford : Pergamon-Elsevier Science Ltd., 130, 25-33.
https://doi.org/10.1016/j.enconman.2016.10.020
Miladinović MR, Stamenković O, Banković P, Milutinović Nikolić A, Jovanović DM, Veljković VB. Modeling and optimization of sunflower oil methanolysis over quicklime bits in a packed bed tubular reactor using the response surface methodology. in Energy Conversion and Management. 2016;130:25-33.
doi:10.1016/j.enconman.2016.10.020 .
Miladinović, Marija R., Stamenković, Olivera, Banković, Predrag, Milutinović Nikolić, Aleksandra, Jovanović, Dušan M., Veljković, Vlada B., "Modeling and optimization of sunflower oil methanolysis over quicklime bits in a packed bed tubular reactor using the response surface methodology" in Energy Conversion and Management, 130 (2016):25-33,
https://doi.org/10.1016/j.enconman.2016.10.020 . .
30
24
32

Calcium oxide as a promising heterogeneous catalyst for biodiesel production: Current state and perspectives

Marinković, Dalibor; Stanković, Miroslav; Velickovic, Ana V; Avramović, Jelena M.; Miladinović, Marija R.; Stamenković, Olivera; Veljković, Vlada B.; Jovanović, Dušan M.

(Oxford : Pergamon-Elsevier Science Ltd, 2016)

TY  - JOUR
AU  - Marinković, Dalibor
AU  - Stanković, Miroslav
AU  - Velickovic, Ana V
AU  - Avramović, Jelena M.
AU  - Miladinović, Marija R.
AU  - Stamenković, Olivera
AU  - Veljković, Vlada B.
AU  - Jovanović, Dušan M.
PY  - 2016
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1956
AB  - The present paper is an overview of the recent progress in the development of various CaO-based catalysts suitable for biodiesel production. The mechanism, kinetics and optimization of transesterification reaction over these catalysts are first considered. Then, the practical application of CaO-based catalysts is discussed with a special stress on leaching and reusability of these catalysts. Also, various continuous reactor systems currently in use for biodiesel production are appraised. In addition to it, purification of crude biodiesel and the ecological aspects of using CaO-based catalysts are considered. Finally, the potentials of CaO-based catalysts for heterogeneous catalysis for biodiesel production are emphasized to assess the future perspectives of their use. This review might help in selecting suitable CaO-based catalysts and the optimum reaction conditions for biodiesel production.
PB  - Oxford : Pergamon-Elsevier Science Ltd
T2  - Renewable & Sustainable Energy Reviews
T1  - Calcium oxide as a promising heterogeneous catalyst for biodiesel production: Current state and perspectives
VL  - 56
SP  - 1387
EP  - 1408
DO  - 10.1016/j.rser.2015.12.007
ER  - 
@article{
author = "Marinković, Dalibor and Stanković, Miroslav and Velickovic, Ana V and Avramović, Jelena M. and Miladinović, Marija R. and Stamenković, Olivera and Veljković, Vlada B. and Jovanović, Dušan M.",
year = "2016",
abstract = "The present paper is an overview of the recent progress in the development of various CaO-based catalysts suitable for biodiesel production. The mechanism, kinetics and optimization of transesterification reaction over these catalysts are first considered. Then, the practical application of CaO-based catalysts is discussed with a special stress on leaching and reusability of these catalysts. Also, various continuous reactor systems currently in use for biodiesel production are appraised. In addition to it, purification of crude biodiesel and the ecological aspects of using CaO-based catalysts are considered. Finally, the potentials of CaO-based catalysts for heterogeneous catalysis for biodiesel production are emphasized to assess the future perspectives of their use. This review might help in selecting suitable CaO-based catalysts and the optimum reaction conditions for biodiesel production.",
publisher = "Oxford : Pergamon-Elsevier Science Ltd",
journal = "Renewable & Sustainable Energy Reviews",
title = "Calcium oxide as a promising heterogeneous catalyst for biodiesel production: Current state and perspectives",
volume = "56",
pages = "1387-1408",
doi = "10.1016/j.rser.2015.12.007"
}
Marinković, D., Stanković, M., Velickovic, A. V., Avramović, J. M., Miladinović, M. R., Stamenković, O., Veljković, V. B.,& Jovanović, D. M.. (2016). Calcium oxide as a promising heterogeneous catalyst for biodiesel production: Current state and perspectives. in Renewable & Sustainable Energy Reviews
Oxford : Pergamon-Elsevier Science Ltd., 56, 1387-1408.
https://doi.org/10.1016/j.rser.2015.12.007
Marinković D, Stanković M, Velickovic AV, Avramović JM, Miladinović MR, Stamenković O, Veljković VB, Jovanović DM. Calcium oxide as a promising heterogeneous catalyst for biodiesel production: Current state and perspectives. in Renewable & Sustainable Energy Reviews. 2016;56:1387-1408.
doi:10.1016/j.rser.2015.12.007 .
Marinković, Dalibor, Stanković, Miroslav, Velickovic, Ana V, Avramović, Jelena M., Miladinović, Marija R., Stamenković, Olivera, Veljković, Vlada B., Jovanović, Dušan M., "Calcium oxide as a promising heterogeneous catalyst for biodiesel production: Current state and perspectives" in Renewable & Sustainable Energy Reviews, 56 (2016):1387-1408,
https://doi.org/10.1016/j.rser.2015.12.007 . .
3
266
180
279

A kinetic study of quicklime-catalyzed sunflower oil methanolysis

Miladinović, Marija R; Krstić, Jugoslav; Tasic, Marija B; Stamenković, Olivera; Veljković, Vlada B.

(Inst Chemical Engineers, Rugby, 2014)

TY  - JOUR
AU  - Miladinović, Marija R
AU  - Krstić, Jugoslav
AU  - Tasic, Marija B
AU  - Stamenković, Olivera
AU  - Veljković, Vlada B.
PY  - 2014
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1438
AB  - The quicklime-catalyzed sunflower oil methanolysis was studied at mild reaction conditions. Quicklime (calcined at 550 degrees C for 4h) in amounts of 1.0, 2.5, 5.0 and 10.0% (based on the oil weight) and different molar ratios of methanol-to-oil (6:1, 12:1 and 18:1) were employed to investigate their influence on the methyl esters content and the kinetics of the methanolysis reaction. The optimal methanol-to-oil molar ratio and quicklime amount for achieving the highest fatty acid methyl esters content were established to be 12:1 and 5% (based on the oil weight), respectively. The sigmoidal kinetics of quicklime-catalyzed methanolysis reaction was described by a model which included the changing mechanism of the reaction and the triacylglycerols mass transfer limitation. The kinetic parameters were determined and correlated with the process variables. A good agreement between the kinetic model and the experimental data for all applied reaction conditions was observed.
PB  - Inst Chemical Engineers, Rugby
T2  - Chemical Engineering Research & Design
T1  - A kinetic study of quicklime-catalyzed sunflower oil methanolysis
VL  - 92
IS  - 9
SP  - 1740
EP  - 1752
DO  - 10.1016/j.cherd.2013.11.023
ER  - 
@article{
author = "Miladinović, Marija R and Krstić, Jugoslav and Tasic, Marija B and Stamenković, Olivera and Veljković, Vlada B.",
year = "2014",
abstract = "The quicklime-catalyzed sunflower oil methanolysis was studied at mild reaction conditions. Quicklime (calcined at 550 degrees C for 4h) in amounts of 1.0, 2.5, 5.0 and 10.0% (based on the oil weight) and different molar ratios of methanol-to-oil (6:1, 12:1 and 18:1) were employed to investigate their influence on the methyl esters content and the kinetics of the methanolysis reaction. The optimal methanol-to-oil molar ratio and quicklime amount for achieving the highest fatty acid methyl esters content were established to be 12:1 and 5% (based on the oil weight), respectively. The sigmoidal kinetics of quicklime-catalyzed methanolysis reaction was described by a model which included the changing mechanism of the reaction and the triacylglycerols mass transfer limitation. The kinetic parameters were determined and correlated with the process variables. A good agreement between the kinetic model and the experimental data for all applied reaction conditions was observed.",
publisher = "Inst Chemical Engineers, Rugby",
journal = "Chemical Engineering Research & Design",
title = "A kinetic study of quicklime-catalyzed sunflower oil methanolysis",
volume = "92",
number = "9",
pages = "1740-1752",
doi = "10.1016/j.cherd.2013.11.023"
}
Miladinović, M. R., Krstić, J., Tasic, M. B., Stamenković, O.,& Veljković, V. B.. (2014). A kinetic study of quicklime-catalyzed sunflower oil methanolysis. in Chemical Engineering Research & Design
Inst Chemical Engineers, Rugby., 92(9), 1740-1752.
https://doi.org/10.1016/j.cherd.2013.11.023
Miladinović MR, Krstić J, Tasic MB, Stamenković O, Veljković VB. A kinetic study of quicklime-catalyzed sunflower oil methanolysis. in Chemical Engineering Research & Design. 2014;92(9):1740-1752.
doi:10.1016/j.cherd.2013.11.023 .
Miladinović, Marija R, Krstić, Jugoslav, Tasic, Marija B, Stamenković, Olivera, Veljković, Vlada B., "A kinetic study of quicklime-catalyzed sunflower oil methanolysis" in Chemical Engineering Research & Design, 92, no. 9 (2014):1740-1752,
https://doi.org/10.1016/j.cherd.2013.11.023 . .
41
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Prethodna studija opravdanosti sa generalnim projektom procesa i postrojenja - Poluindustrijsko postrojenje za sintezu biodizela iz suncokretovog ulja i metanola u koloni sa pakovanim slojem negašenog kreča kao katalizatorom

Popović, Zoran; Marinković, Dalibor; Nešić, Gordana; Veljković, Vlada B.; Stamenković, Olivera

(Univerzitet u Beogradu, Naučna ustanova, Institut za hemiju, tehnologiju i metalurgiju, 2014)

TY  - GEN
AU  - Popović, Zoran
AU  - Marinković, Dalibor
AU  - Nešić, Gordana
AU  - Veljković, Vlada B.
AU  - Stamenković, Olivera
PY  - 2014
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3753
AB  - Tехничко решење дефинише континуални поступак добијања FAME на бази уља
сунцокрета применом комерцијалног негашеног креча као катализатора у реактору са
непокретним слојем катализатора и раздвајање метилестарске и метанолно-глицеролне фазе
у гравитационом сепаратору.
PB  - Univerzitet u Beogradu, Naučna ustanova, Institut za hemiju, tehnologiju i metalurgiju
T1  - Prethodna studija opravdanosti sa generalnim projektom procesa i postrojenja - Poluindustrijsko postrojenje za sintezu biodizela iz suncokretovog ulja i metanola u koloni sa pakovanim slojem negašenog kreča kao katalizatorom
UR  - https://hdl.handle.net/21.15107/rcub_cer_3753
ER  - 
@misc{
author = "Popović, Zoran and Marinković, Dalibor and Nešić, Gordana and Veljković, Vlada B. and Stamenković, Olivera",
year = "2014",
abstract = "Tехничко решење дефинише континуални поступак добијања FAME на бази уља
сунцокрета применом комерцијалног негашеног креча као катализатора у реактору са
непокретним слојем катализатора и раздвајање метилестарске и метанолно-глицеролне фазе
у гравитационом сепаратору.",
publisher = "Univerzitet u Beogradu, Naučna ustanova, Institut za hemiju, tehnologiju i metalurgiju",
title = "Prethodna studija opravdanosti sa generalnim projektom procesa i postrojenja - Poluindustrijsko postrojenje za sintezu biodizela iz suncokretovog ulja i metanola u koloni sa pakovanim slojem negašenog kreča kao katalizatorom",
url = "https://hdl.handle.net/21.15107/rcub_cer_3753"
}
Popović, Z., Marinković, D., Nešić, G., Veljković, V. B.,& Stamenković, O.. (2014). Prethodna studija opravdanosti sa generalnim projektom procesa i postrojenja - Poluindustrijsko postrojenje za sintezu biodizela iz suncokretovog ulja i metanola u koloni sa pakovanim slojem negašenog kreča kao katalizatorom. 
Univerzitet u Beogradu, Naučna ustanova, Institut za hemiju, tehnologiju i metalurgiju..
https://hdl.handle.net/21.15107/rcub_cer_3753
Popović Z, Marinković D, Nešić G, Veljković VB, Stamenković O. Prethodna studija opravdanosti sa generalnim projektom procesa i postrojenja - Poluindustrijsko postrojenje za sintezu biodizela iz suncokretovog ulja i metanola u koloni sa pakovanim slojem negašenog kreča kao katalizatorom. 2014;.
https://hdl.handle.net/21.15107/rcub_cer_3753 .
Popović, Zoran, Marinković, Dalibor, Nešić, Gordana, Veljković, Vlada B., Stamenković, Olivera, "Prethodna studija opravdanosti sa generalnim projektom procesa i postrojenja - Poluindustrijsko postrojenje za sintezu biodizela iz suncokretovog ulja i metanola u koloni sa pakovanim slojem negašenog kreča kao katalizatorom" (2014),
https://hdl.handle.net/21.15107/rcub_cer_3753 .