Kostić, Milan

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orcid::0000-0002-2674-6615
  • Kostić, Milan (10)
  • Kostić, Milan D. (2)

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

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

Acceleration of biodiesel production from off-grade oil over waste-based CaO catalyst

Pavlović, Stefan; Kosić, Višnja; Lončarević, Davor; Kostić, Milan; Marinković, Dalibor

(Aachen, Germany : Fuel Science Center, RWTH Aachen University, 2022)

TY  - CONF
AU  - Pavlović, Stefan
AU  - Kosić, Višnja
AU  - Lončarević, Davor
AU  - Kostić, Milan
AU  - Marinković, Dalibor
PY  - 2022
UR  - https://www.fuelcenter.rwth-aachen.de/cms/Fuelcenter/Austausch/Internationale-Konferenz/~rwsva/10-Internationale-Konferenz-2022/?lidx=1
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/5304
AB  - Waste-based CaO was synthesized from chicken eggshell, which calcined form (900 ºC, 5 ºC/min, 4 h) was hydrated (80 ºC, S:L=1:5, 24 h) and rehydrated/calcined (600 ºC, 5 ºC/min, 4 h). The obtained catalyst was characterized (Hg-porosimetry and TPD-CO2) and tested in biodiesel synthesis from off-grade sunflower oil by transesterification to analyse the influence of water addition on reaction intensification. Water content was varied in the range from 1 wt% to 9 wt% by weight of oil. It is shown that water addition positively affects the catalytic activity leading to a reduction in induction time and to faster achievement of the reaction equilibrium (fatty acid methyl esters content > 95%), which for a water content higher than 1 wt% is achieved in 90 min. On the other hand, the equilibrium for the reaction without water addition was achieved considerably later (after 150 min).
PB  - Aachen, Germany : Fuel Science Center, RWTH Aachen University
C3  - Conference report/Book of abstracts-10th International Conference "Fuel Science - From Production to Propulsion"
T1  - Acceleration of biodiesel production from off-grade oil over waste-based CaO catalyst
SP  - 83
EP  - 84
UR  - https://hdl.handle.net/21.15107/rcub_cer_5304
ER  - 
@conference{
author = "Pavlović, Stefan and Kosić, Višnja and Lončarević, Davor and Kostić, Milan and Marinković, Dalibor",
year = "2022",
abstract = "Waste-based CaO was synthesized from chicken eggshell, which calcined form (900 ºC, 5 ºC/min, 4 h) was hydrated (80 ºC, S:L=1:5, 24 h) and rehydrated/calcined (600 ºC, 5 ºC/min, 4 h). The obtained catalyst was characterized (Hg-porosimetry and TPD-CO2) and tested in biodiesel synthesis from off-grade sunflower oil by transesterification to analyse the influence of water addition on reaction intensification. Water content was varied in the range from 1 wt% to 9 wt% by weight of oil. It is shown that water addition positively affects the catalytic activity leading to a reduction in induction time and to faster achievement of the reaction equilibrium (fatty acid methyl esters content > 95%), which for a water content higher than 1 wt% is achieved in 90 min. On the other hand, the equilibrium for the reaction without water addition was achieved considerably later (after 150 min).",
publisher = "Aachen, Germany : Fuel Science Center, RWTH Aachen University",
journal = "Conference report/Book of abstracts-10th International Conference "Fuel Science - From Production to Propulsion"",
title = "Acceleration of biodiesel production from off-grade oil over waste-based CaO catalyst",
pages = "83-84",
url = "https://hdl.handle.net/21.15107/rcub_cer_5304"
}
Pavlović, S., Kosić, V., Lončarević, D., Kostić, M.,& Marinković, D.. (2022). Acceleration of biodiesel production from off-grade oil over waste-based CaO catalyst. in Conference report/Book of abstracts-10th International Conference "Fuel Science - From Production to Propulsion"
Aachen, Germany : Fuel Science Center, RWTH Aachen University., 83-84.
https://hdl.handle.net/21.15107/rcub_cer_5304
Pavlović S, Kosić V, Lončarević D, Kostić M, Marinković D. Acceleration of biodiesel production from off-grade oil over waste-based CaO catalyst. in Conference report/Book of abstracts-10th International Conference "Fuel Science - From Production to Propulsion". 2022;:83-84.
https://hdl.handle.net/21.15107/rcub_cer_5304 .
Pavlović, Stefan, Kosić, Višnja, Lončarević, Davor, Kostić, Milan, Marinković, Dalibor, "Acceleration of biodiesel production from off-grade oil over waste-based CaO catalyst" in Conference report/Book of abstracts-10th International Conference "Fuel Science - From Production to Propulsion" (2022):83-84,
https://hdl.handle.net/21.15107/rcub_cer_5304 .

Biodiesel Production From Off-Grade Oil By Transesterification Over Differently Granulated Waste-Based CaO Catalysts

Pavlović, Stefan; Kosić, Višnja; Marinković, Dalibor; Kostić, Milan

(2022)

TY  - CONF
AU  - Pavlović, Stefan
AU  - Kosić, Višnja
AU  - Marinković, Dalibor
AU  - Kostić, Milan
PY  - 2022
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/5307
AB  - The waste fractionated chicken eggshell catalysts were utilized and used in biodiesel production from off-grade sunflower oil. It is confirmed that thermal modification treatment was suitable for conversion of calcite form of eggshell into lime. Fractionation was carried out in the wide particle diameter range from 20 μm. to 100 μm. It is shown that the highest catalytic activity (fatty acid methyl esters content-FAME >96%) was achieved using catalyst obtained from powder faction of >45<63 μm. Important differences in catalytic activity were observed for the boundary fractions (<20 μm, >20<36 μm, and >100 μm), where catalytic activity was greatly reduced. Such behaviour could be explained by mercury intrusion porosimetry results, which indicate the existence of apparent porosity (interparticle and intraparticle) in the mentioned boundary fractions, while in the central fraction (>45<63 μm) the porosity is constant. A poorly-developed system of pores and channels leads to difficult diffusion and inadequate distribution of active centres.
C3  - Proceedings - 2nd International Conference On Green Energy And Environmental Technology
T1  - Biodiesel Production From Off-Grade Oil By Transesterification Over Differently Granulated Waste-Based CaO Catalysts
UR  - https://hdl.handle.net/21.15107/rcub_cer_5307
ER  - 
@conference{
author = "Pavlović, Stefan and Kosić, Višnja and Marinković, Dalibor and Kostić, Milan",
year = "2022",
abstract = "The waste fractionated chicken eggshell catalysts were utilized and used in biodiesel production from off-grade sunflower oil. It is confirmed that thermal modification treatment was suitable for conversion of calcite form of eggshell into lime. Fractionation was carried out in the wide particle diameter range from 20 μm. to 100 μm. It is shown that the highest catalytic activity (fatty acid methyl esters content-FAME >96%) was achieved using catalyst obtained from powder faction of >45<63 μm. Important differences in catalytic activity were observed for the boundary fractions (<20 μm, >20<36 μm, and >100 μm), where catalytic activity was greatly reduced. Such behaviour could be explained by mercury intrusion porosimetry results, which indicate the existence of apparent porosity (interparticle and intraparticle) in the mentioned boundary fractions, while in the central fraction (>45<63 μm) the porosity is constant. A poorly-developed system of pores and channels leads to difficult diffusion and inadequate distribution of active centres.",
journal = "Proceedings - 2nd International Conference On Green Energy And Environmental Technology",
title = "Biodiesel Production From Off-Grade Oil By Transesterification Over Differently Granulated Waste-Based CaO Catalysts",
url = "https://hdl.handle.net/21.15107/rcub_cer_5307"
}
Pavlović, S., Kosić, V., Marinković, D.,& Kostić, M.. (2022). Biodiesel Production From Off-Grade Oil By Transesterification Over Differently Granulated Waste-Based CaO Catalysts. in Proceedings - 2nd International Conference On Green Energy And Environmental Technology.
https://hdl.handle.net/21.15107/rcub_cer_5307
Pavlović S, Kosić V, Marinković D, Kostić M. Biodiesel Production From Off-Grade Oil By Transesterification Over Differently Granulated Waste-Based CaO Catalysts. in Proceedings - 2nd International Conference On Green Energy And Environmental Technology. 2022;.
https://hdl.handle.net/21.15107/rcub_cer_5307 .
Pavlović, Stefan, Kosić, Višnja, Marinković, Dalibor, Kostić, Milan, "Biodiesel Production From Off-Grade Oil By Transesterification Over Differently Granulated Waste-Based CaO Catalysts" in Proceedings - 2nd International Conference On Green Energy And Environmental Technology (2022),
https://hdl.handle.net/21.15107/rcub_cer_5307 .

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

The chicken eggshell calcium oxide ultrasonically dispersed over lignite coal fly ash-based cancrinite zeolite support as a catalyst for biodiesel production

Pavlović, Stefan; Marinković, Dalibor; Kostić, Milan; Lončarević, Davor; Mojović, Ljiljana; Stanković, Miroslav; Veljković, Vlada B.

(Elsevier, 2021)

TY  - JOUR
AU  - Pavlović, Stefan
AU  - Marinković, Dalibor
AU  - Kostić, Milan
AU  - Lončarević, Davor
AU  - Mojović, Ljiljana
AU  - Stanković, Miroslav
AU  - Veljković, Vlada B.
PY  - 2021
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/4035
AB  - Lignite coal fly ash (FA) from a domestic thermal power plant was converted into a pure cancrinite zeolitic material (ZMFA) using a novel, custom-made, rotating autoclave reactor system by a short-term alkali activation process. The obtained ZMFA was used as catalyst support of calcium oxide as an active component derived from waste chicken eggshells (ES). The ZMFA supported calcium oxide catalyst (xCaO/ZMFA) was synthesized by means of the ultrasound-assisted method. The influence of different concentrations of dispersed calcium oxide (x = 5–20 wt%) over ZMFA and thermal treatment at different temperatures (450–600 °C) were studied. The structural and morphological characterization showed that the original cancrinite structure was preserved. The basicity and textural properties indicated the presence of strong active sites in a well-defined pore network suitable for the reactions of bulky organic compounds such as triacylglycerols (TAGs). The highest activity (96.5% of fatty acid methyl esters) in the methanolysis of sunflower oil was achieved with the 20CaO/ZMFA catalyst under reaction conditions: temperature of 60 °C, methanol/oil molar ratio of 12:1, catalyst concentration of 4 wt%, and reaction time of 2 h. It was found that the optimal calcination temperature of the catalyst precursor was 550 °C. At calcination temperatures above 550 °C, the melting of the glassy phase became more intense whereby the molten phase partially reacted with calcium oxide forming the catalytically inactive calcium silicate compounds (wollastonite, larnite, etc.). The rate constants of the two tested kinetic models were correlated with the concentrations of active calcium oxide. The MRPD of both models was low indicating their reliability.
PB  - Elsevier
T2  - Fuel
T1  - The chicken eggshell calcium oxide ultrasonically dispersed over lignite coal fly ash-based cancrinite zeolite support as a catalyst for biodiesel production
VL  - 289
SP  - 119912
DO  - 10.1016/j.fuel.2020.119912
ER  - 
@article{
author = "Pavlović, Stefan and Marinković, Dalibor and Kostić, Milan and Lončarević, Davor and Mojović, Ljiljana and Stanković, Miroslav and Veljković, Vlada B.",
year = "2021",
abstract = "Lignite coal fly ash (FA) from a domestic thermal power plant was converted into a pure cancrinite zeolitic material (ZMFA) using a novel, custom-made, rotating autoclave reactor system by a short-term alkali activation process. The obtained ZMFA was used as catalyst support of calcium oxide as an active component derived from waste chicken eggshells (ES). The ZMFA supported calcium oxide catalyst (xCaO/ZMFA) was synthesized by means of the ultrasound-assisted method. The influence of different concentrations of dispersed calcium oxide (x = 5–20 wt%) over ZMFA and thermal treatment at different temperatures (450–600 °C) were studied. The structural and morphological characterization showed that the original cancrinite structure was preserved. The basicity and textural properties indicated the presence of strong active sites in a well-defined pore network suitable for the reactions of bulky organic compounds such as triacylglycerols (TAGs). The highest activity (96.5% of fatty acid methyl esters) in the methanolysis of sunflower oil was achieved with the 20CaO/ZMFA catalyst under reaction conditions: temperature of 60 °C, methanol/oil molar ratio of 12:1, catalyst concentration of 4 wt%, and reaction time of 2 h. It was found that the optimal calcination temperature of the catalyst precursor was 550 °C. At calcination temperatures above 550 °C, the melting of the glassy phase became more intense whereby the molten phase partially reacted with calcium oxide forming the catalytically inactive calcium silicate compounds (wollastonite, larnite, etc.). The rate constants of the two tested kinetic models were correlated with the concentrations of active calcium oxide. The MRPD of both models was low indicating their reliability.",
publisher = "Elsevier",
journal = "Fuel",
title = "The chicken eggshell calcium oxide ultrasonically dispersed over lignite coal fly ash-based cancrinite zeolite support as a catalyst for biodiesel production",
volume = "289",
pages = "119912",
doi = "10.1016/j.fuel.2020.119912"
}
Pavlović, S., Marinković, D., Kostić, M., Lončarević, D., Mojović, L., Stanković, M.,& Veljković, V. B.. (2021). The chicken eggshell calcium oxide ultrasonically dispersed over lignite coal fly ash-based cancrinite zeolite support as a catalyst for biodiesel production. in Fuel
Elsevier., 289, 119912.
https://doi.org/10.1016/j.fuel.2020.119912
Pavlović S, Marinković D, Kostić M, Lončarević D, Mojović L, Stanković M, Veljković VB. The chicken eggshell calcium oxide ultrasonically dispersed over lignite coal fly ash-based cancrinite zeolite support as a catalyst for biodiesel production. in Fuel. 2021;289:119912.
doi:10.1016/j.fuel.2020.119912 .
Pavlović, Stefan, Marinković, Dalibor, Kostić, Milan, Lončarević, Davor, Mojović, Ljiljana, Stanković, Miroslav, Veljković, Vlada B., "The chicken eggshell calcium oxide ultrasonically dispersed over lignite coal fly ash-based cancrinite zeolite support as a catalyst for biodiesel production" in Fuel, 289 (2021):119912,
https://doi.org/10.1016/j.fuel.2020.119912 . .
2
19
5
15

A CaO/zeolite-based catalyst obtained from waste chicken eggshell and coal fly ash for biodiesel production

Pavlović, Stefan; Marinković, Dalibor; Kostić, Milan; Janković-Častvan, Ivona; Mojović, Ljiljana; Stanković, Miroslav; Veljković, Vlada B.

(Elsevier, 2020)

TY  - JOUR
AU  - Pavlović, Stefan
AU  - Marinković, Dalibor
AU  - Kostić, Milan
AU  - Janković-Častvan, Ivona
AU  - Mojović, Ljiljana
AU  - Stanković, Miroslav
AU  - Veljković, Vlada B.
PY  - 2020
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3423
AB  - The present paper is focused on the development of a new environment-friendly methanolysis catalyst completely
based on waste materials: lignite coal fly ash and chicken eggshells. A novel catalyst based on CaO
supported on a fly ash-based zeolitic material (CaO/FA-ZM) was obtained from a cancrinite-sodalite group
zeolite-like material (vishnevite type) and active CaO by alkali activation in a new miniature autoclave reactor
system and hydration-dehydration. Agitation by rotation of the entire reaction mixture led to a more homogeneous
zeolitic product and saved both time and energy. The obtained catalyst structure corresponds to gismondine
and the crystallographic modification of calcium silicate (α’-dicalcium silicate) with deposited CaO.
The characteristics of the synthesized catalyst were determined using ED-XRF, XRD, FT-IR, SEM, Hg-porosimetry,
N2-physisorption, LDPSA, and Hammett indicators. The CaO/FA-ZM catalyst exhibited a high activity
(97.8% of FAME for only 30 min) and stability (a negligible drop in activity in five consecutive cycles) in the
methanolysis reaction under the optimal reaction conditions (temperature of 60 °C, methanol/oil molar ratio of
6:1, and catalyst concentration of 6 wt%). A kinetic study was performed using two different mechanisms: the
irreversible pseudo-first-order reaction mechanism in two regimes (heterogeneous and homogeneous) and the
changing mechanism combined with the triacylglycerol mass transfer limitation. Both models showed a satisfactory
agreement between the experimental and predicted values of conversion degree (R2 > 0.93), confirming
their validity for the CaO-based heterogeneously catalyzed methanolysis. The values of the activation
energy calculated for both mechanisms were 67.17 and 58.03 kJ mol−1, respectively.
PB  - Elsevier
T2  - Fuel
T1  - A CaO/zeolite-based catalyst obtained from waste chicken eggshell and coal fly ash for biodiesel production
VL  - 267
SP  - 117171
DO  - 10.1016/j.fuel.2020.117171
ER  - 
@article{
author = "Pavlović, Stefan and Marinković, Dalibor and Kostić, Milan and Janković-Častvan, Ivona and Mojović, Ljiljana and Stanković, Miroslav and Veljković, Vlada B.",
year = "2020",
abstract = "The present paper is focused on the development of a new environment-friendly methanolysis catalyst completely
based on waste materials: lignite coal fly ash and chicken eggshells. A novel catalyst based on CaO
supported on a fly ash-based zeolitic material (CaO/FA-ZM) was obtained from a cancrinite-sodalite group
zeolite-like material (vishnevite type) and active CaO by alkali activation in a new miniature autoclave reactor
system and hydration-dehydration. Agitation by rotation of the entire reaction mixture led to a more homogeneous
zeolitic product and saved both time and energy. The obtained catalyst structure corresponds to gismondine
and the crystallographic modification of calcium silicate (α’-dicalcium silicate) with deposited CaO.
The characteristics of the synthesized catalyst were determined using ED-XRF, XRD, FT-IR, SEM, Hg-porosimetry,
N2-physisorption, LDPSA, and Hammett indicators. The CaO/FA-ZM catalyst exhibited a high activity
(97.8% of FAME for only 30 min) and stability (a negligible drop in activity in five consecutive cycles) in the
methanolysis reaction under the optimal reaction conditions (temperature of 60 °C, methanol/oil molar ratio of
6:1, and catalyst concentration of 6 wt%). A kinetic study was performed using two different mechanisms: the
irreversible pseudo-first-order reaction mechanism in two regimes (heterogeneous and homogeneous) and the
changing mechanism combined with the triacylglycerol mass transfer limitation. Both models showed a satisfactory
agreement between the experimental and predicted values of conversion degree (R2 > 0.93), confirming
their validity for the CaO-based heterogeneously catalyzed methanolysis. The values of the activation
energy calculated for both mechanisms were 67.17 and 58.03 kJ mol−1, respectively.",
publisher = "Elsevier",
journal = "Fuel",
title = "A CaO/zeolite-based catalyst obtained from waste chicken eggshell and coal fly ash for biodiesel production",
volume = "267",
pages = "117171",
doi = "10.1016/j.fuel.2020.117171"
}
Pavlović, S., Marinković, D., Kostić, M., Janković-Častvan, I., Mojović, L., Stanković, M.,& Veljković, V. B.. (2020). A CaO/zeolite-based catalyst obtained from waste chicken eggshell and coal fly ash for biodiesel production. in Fuel
Elsevier., 267, 117171.
https://doi.org/10.1016/j.fuel.2020.117171
Pavlović S, Marinković D, Kostić M, Janković-Častvan I, Mojović L, Stanković M, Veljković VB. A CaO/zeolite-based catalyst obtained from waste chicken eggshell and coal fly ash for biodiesel production. in Fuel. 2020;267:117171.
doi:10.1016/j.fuel.2020.117171 .
Pavlović, Stefan, Marinković, Dalibor, Kostić, Milan, Janković-Častvan, Ivona, Mojović, Ljiljana, Stanković, Miroslav, Veljković, Vlada B., "A CaO/zeolite-based catalyst obtained from waste chicken eggshell and coal fly ash for biodiesel production" in Fuel, 267 (2020):117171,
https://doi.org/10.1016/j.fuel.2020.117171 . .
69
32
70

Effects of preparation conditions on the catalytic activity of chicken eggshell catalysts for the transesterification of oils to biodiesel

Pavlović, Stefan; Marinković, Dalibor; Milovanović, Biljana; Kostić, Milan; Gabrovska, Margarita; Nikolova, Dimitrinka; Stanković, Miroslav

(DECHEMA e.V., 2019)

TY  - CONF
AU  - Pavlović, Stefan
AU  - Marinković, Dalibor
AU  - Milovanović, Biljana
AU  - Kostić, Milan
AU  - Gabrovska, Margarita
AU  - Nikolova, Dimitrinka
AU  - Stanković, Miroslav
PY  - 2019
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3434
AB  - Eggshell based catalysts were synthesized by calcination (600 and 900 ºC, 4 h) of raw and rehydration (RH) modified (RH-temperature of 80 ºC, S/L ratio of 1/5, and RH-time of 6 h) eggshell. After RH-treatment, the sample underwent calcination at 600 ºC, 4 h. Obtained catalysts were characterized by XRD, SEM, N2-physisorption, and Hg-porosimetry, whereas the catalytic activity was analyzed in a batch reactor (reaction temperature of 60 ºC, sunflower oil/methanol molar ratio of 1/12, and catalyst concentration of 4 wt.%). The concentration of fatty acid methyl esters (FAMEs) was determined by HPLC. The reaction has reached equilibrium (FAME > 97%) with rehydrated catalyst for 1.5 h, whereas with catalyst calcined at 900 ºC for 4 h.
PB  - DECHEMA e.V.
C3  - 14th EuropaCat – European Congress on Catalysis “Catalysis without Borders”
T1  - Effects of preparation conditions on the catalytic activity of chicken eggshell catalysts for the transesterification of oils to biodiesel
SP  - 643
EP  - 644
UR  - https://hdl.handle.net/21.15107/rcub_cer_3434
ER  - 
@conference{
author = "Pavlović, Stefan and Marinković, Dalibor and Milovanović, Biljana and Kostić, Milan and Gabrovska, Margarita and Nikolova, Dimitrinka and Stanković, Miroslav",
year = "2019",
abstract = "Eggshell based catalysts were synthesized by calcination (600 and 900 ºC, 4 h) of raw and rehydration (RH) modified (RH-temperature of 80 ºC, S/L ratio of 1/5, and RH-time of 6 h) eggshell. After RH-treatment, the sample underwent calcination at 600 ºC, 4 h. Obtained catalysts were characterized by XRD, SEM, N2-physisorption, and Hg-porosimetry, whereas the catalytic activity was analyzed in a batch reactor (reaction temperature of 60 ºC, sunflower oil/methanol molar ratio of 1/12, and catalyst concentration of 4 wt.%). The concentration of fatty acid methyl esters (FAMEs) was determined by HPLC. The reaction has reached equilibrium (FAME > 97%) with rehydrated catalyst for 1.5 h, whereas with catalyst calcined at 900 ºC for 4 h.",
publisher = "DECHEMA e.V.",
journal = "14th EuropaCat – European Congress on Catalysis “Catalysis without Borders”",
title = "Effects of preparation conditions on the catalytic activity of chicken eggshell catalysts for the transesterification of oils to biodiesel",
pages = "643-644",
url = "https://hdl.handle.net/21.15107/rcub_cer_3434"
}
Pavlović, S., Marinković, D., Milovanović, B., Kostić, M., Gabrovska, M., Nikolova, D.,& Stanković, M.. (2019). Effects of preparation conditions on the catalytic activity of chicken eggshell catalysts for the transesterification of oils to biodiesel. in 14th EuropaCat – European Congress on Catalysis “Catalysis without Borders”
DECHEMA e.V.., 643-644.
https://hdl.handle.net/21.15107/rcub_cer_3434
Pavlović S, Marinković D, Milovanović B, Kostić M, Gabrovska M, Nikolova D, Stanković M. Effects of preparation conditions on the catalytic activity of chicken eggshell catalysts for the transesterification of oils to biodiesel. in 14th EuropaCat – European Congress on Catalysis “Catalysis without Borders”. 2019;:643-644.
https://hdl.handle.net/21.15107/rcub_cer_3434 .
Pavlović, Stefan, Marinković, Dalibor, Milovanović, Biljana, Kostić, Milan, Gabrovska, Margarita, Nikolova, Dimitrinka, Stanković, Miroslav, "Effects of preparation conditions on the catalytic activity of chicken eggshell catalysts for the transesterification of oils to biodiesel" in 14th EuropaCat – European Congress on Catalysis “Catalysis without Borders” (2019):643-644,
https://hdl.handle.net/21.15107/rcub_cer_3434 .

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 .