Orlović, Aleksandar

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orcid::0000-0003-2645-8768
  • Orlović, Aleksandar (4)
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Author's Bibliography

Aerogel Re/Pd-TiO2/SiO2 and Co/Mo-Al2O3/SiO2 catalysts for hydrodesulphurisation of dibenzothiophene and 4,6-dimethyldibenzothiophene

Prokić-Vidojević, Dragana; Glišić, Sandra B.; Krstić, Jugoslav; Orlović, Aleksandar

(Elsevier, 2021)

TY  - JOUR
AU  - Prokić-Vidojević, Dragana
AU  - Glišić, Sandra B.
AU  - Krstić, Jugoslav
AU  - Orlović, Aleksandar
PY  - 2021
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/4239
AB  - Re/Pd-TiO2/SiO2 and Co/Mo-Al2O3/SiO2 aerogel catalysts were synthesized using sol-gel method and supercritical drying in excess solvent, and investigated in the hydrodesulphurisation (HDS) of dibenzothiophene (DBT) and 4,6-dimethyl dibenzothiophene (4,6-DMDBT). The influence of supercritical drying on the final catalytic properties of the materials was determined by parallel synthesis of aerogels and xerogels for Re/Pd-TiO2/SiO2 catalysts. The sol-gel method and supercritical drying were found to result in amorphous aerogels with relatively high degree of uniformity, of both supports and active phases. Corresponding xerogels were found to be similar to aerogels in terms of composition and structure, but characterized by lower specific surface areas. Catalytic activity of Co/Mo-Al2O3/SiO2 aerogel catalysts in HDS of DBT and 4,6-DMDBT has shown no major improvement in comparison to conventional Co/Mo catalyst. On the other hand, Re/Pd-TiO2/SiO2 aerogels, obtained with the addition of mesitylene or without it, achieved 70 % and 64 % higher conversion of 4,6-DMDBT than conventional Co/Mo catalyst, respectively. Increased catalytic activity can be attributed to well dispersed Re and Pd active phases across the catalyst structure, good incorporation of Ti within silica matrix, increased mesopore volumes and high specific surface areas.
PB  - Elsevier
T2  - Catalysis Today
T1  - Aerogel Re/Pd-TiO2/SiO2 and Co/Mo-Al2O3/SiO2 catalysts for hydrodesulphurisation of dibenzothiophene and 4,6-dimethyldibenzothiophene
DO  - 10.1016/j.cattod.2020.11.022
ER  - 
@article{
author = "Prokić-Vidojević, Dragana and Glišić, Sandra B. and Krstić, Jugoslav and Orlović, Aleksandar",
year = "2021",
abstract = "Re/Pd-TiO2/SiO2 and Co/Mo-Al2O3/SiO2 aerogel catalysts were synthesized using sol-gel method and supercritical drying in excess solvent, and investigated in the hydrodesulphurisation (HDS) of dibenzothiophene (DBT) and 4,6-dimethyl dibenzothiophene (4,6-DMDBT). The influence of supercritical drying on the final catalytic properties of the materials was determined by parallel synthesis of aerogels and xerogels for Re/Pd-TiO2/SiO2 catalysts. The sol-gel method and supercritical drying were found to result in amorphous aerogels with relatively high degree of uniformity, of both supports and active phases. Corresponding xerogels were found to be similar to aerogels in terms of composition and structure, but characterized by lower specific surface areas. Catalytic activity of Co/Mo-Al2O3/SiO2 aerogel catalysts in HDS of DBT and 4,6-DMDBT has shown no major improvement in comparison to conventional Co/Mo catalyst. On the other hand, Re/Pd-TiO2/SiO2 aerogels, obtained with the addition of mesitylene or without it, achieved 70 % and 64 % higher conversion of 4,6-DMDBT than conventional Co/Mo catalyst, respectively. Increased catalytic activity can be attributed to well dispersed Re and Pd active phases across the catalyst structure, good incorporation of Ti within silica matrix, increased mesopore volumes and high specific surface areas.",
publisher = "Elsevier",
journal = "Catalysis Today",
title = "Aerogel Re/Pd-TiO2/SiO2 and Co/Mo-Al2O3/SiO2 catalysts for hydrodesulphurisation of dibenzothiophene and 4,6-dimethyldibenzothiophene",
doi = "10.1016/j.cattod.2020.11.022"
}
Prokić-Vidojević, D., Glišić, S. B., Krstić, J.,& Orlović, A.. (2021). Aerogel Re/Pd-TiO2/SiO2 and Co/Mo-Al2O3/SiO2 catalysts for hydrodesulphurisation of dibenzothiophene and 4,6-dimethyldibenzothiophene. in Catalysis Today
Elsevier..
https://doi.org/10.1016/j.cattod.2020.11.022
Prokić-Vidojević D, Glišić SB, Krstić J, Orlović A. Aerogel Re/Pd-TiO2/SiO2 and Co/Mo-Al2O3/SiO2 catalysts for hydrodesulphurisation of dibenzothiophene and 4,6-dimethyldibenzothiophene. in Catalysis Today. 2021;.
doi:10.1016/j.cattod.2020.11.022 .
Prokić-Vidojević, Dragana, Glišić, Sandra B., Krstić, Jugoslav, Orlović, Aleksandar, "Aerogel Re/Pd-TiO2/SiO2 and Co/Mo-Al2O3/SiO2 catalysts for hydrodesulphurisation of dibenzothiophene and 4,6-dimethyldibenzothiophene" in Catalysis Today (2021),
https://doi.org/10.1016/j.cattod.2020.11.022 . .
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Modeling of motor fuel consumption in Serbia with projection to 2025

Marinković, Dalibor; Popović, Zoran; Orlović, Aleksandar; Ristić, Mirjana

(Association of Chemical Engineers of Serbia, 2012)

TY  - JOUR
AU  - Marinković, Dalibor
AU  - Popović, Zoran
AU  - Orlović, Aleksandar
AU  - Ristić, Mirjana
PY  - 2012
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1087
AB  - This study is based on the application of mathematical methods of statistical analysis that can be used to predict the development of motor fuel consumption in the Republic of Serbia. It is based on the linear dependence of consumption growth of motor fuel from the development of gross domestic product per capita, which is then corrected by introducing five additional influencing parameters. The model results indicate that the total consumption of motor fuels in Serbia from 2010 to 2025 will be increased by 26.5%. Individual consumption of motor fuels shows different market tendencies. Diesel fuel consumption expects to continue intensive growth to 2025, even though slightly slower than the achievements in the last decade. The current trend of declining demand for gasoline will be stopped from 2015-2016, then followed by slow growth of demand by 2025. Consumption of liquefied petroleum gasses (LPG) will enter the phase of saturation in 2015.
AB  - Ovaj rad se bazira na primeni metoda matematičke statističke analize koji mogu da posluže za predviđanje razvoja potrošnje motornih goriva u Republici Srbiji. Model je baziran na linearnoj zavisnosti rasta obima potrošnje motornih goriva od razvoja bruto domaćeg proizvoda po glavi stanovnika koja je potom korigovana uvođenjem pet dodatnih uticajnih parametara. Svakom od ovih parametara dodeljen je odgovarajući koeficijent koji odmerava specifični uticaj istog na potrošnju motornih goriva. Rezultati modela ukazuju da će ukupna potrošnja motornih goriva u Srbiji od 2010. do 2025. biti uvećana za 26,5%, sa 2,36 Mt/god na 2,99 Mt/god. Potrošnju dizel goriva očekuje nastavak intenzivnog rasta, doduše nešto usporen u odnosu na ostvarenja u prethodnoj dekadi i do 2025. potrošnja će dostići nivo od blizu 2 Mt. Postojeći trend opadanja tražnje motornih benzina biće zaustavljen 2015-2016, nakon toga sledi spori rast tražnje i do 2025. potrošnja će biti oko 550 Kt. Potrošnja tečnog naftnog gasa (TNG) nakon intenzivnog rasta od 2015. ući će u fazu saturacije, tako da će u periodu 2010-2025. godine zabeležiti mali porast potrošnje - sa 377 na 435 Kt/god.
PB  - Association of Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - Modeling of motor fuel consumption in Serbia with projection to 2025
T1  - Modelovanje potrošnje motornih goriva u Srbiji sa projekcijama do 2025. godine
VL  - 66
IS  - 3
SP  - 413
EP  - 423
DO  - 10.2298/HEMIND110224105M
ER  - 
@article{
author = "Marinković, Dalibor and Popović, Zoran and Orlović, Aleksandar and Ristić, Mirjana",
year = "2012",
abstract = "This study is based on the application of mathematical methods of statistical analysis that can be used to predict the development of motor fuel consumption in the Republic of Serbia. It is based on the linear dependence of consumption growth of motor fuel from the development of gross domestic product per capita, which is then corrected by introducing five additional influencing parameters. The model results indicate that the total consumption of motor fuels in Serbia from 2010 to 2025 will be increased by 26.5%. Individual consumption of motor fuels shows different market tendencies. Diesel fuel consumption expects to continue intensive growth to 2025, even though slightly slower than the achievements in the last decade. The current trend of declining demand for gasoline will be stopped from 2015-2016, then followed by slow growth of demand by 2025. Consumption of liquefied petroleum gasses (LPG) will enter the phase of saturation in 2015., Ovaj rad se bazira na primeni metoda matematičke statističke analize koji mogu da posluže za predviđanje razvoja potrošnje motornih goriva u Republici Srbiji. Model je baziran na linearnoj zavisnosti rasta obima potrošnje motornih goriva od razvoja bruto domaćeg proizvoda po glavi stanovnika koja je potom korigovana uvođenjem pet dodatnih uticajnih parametara. Svakom od ovih parametara dodeljen je odgovarajući koeficijent koji odmerava specifični uticaj istog na potrošnju motornih goriva. Rezultati modela ukazuju da će ukupna potrošnja motornih goriva u Srbiji od 2010. do 2025. biti uvećana za 26,5%, sa 2,36 Mt/god na 2,99 Mt/god. Potrošnju dizel goriva očekuje nastavak intenzivnog rasta, doduše nešto usporen u odnosu na ostvarenja u prethodnoj dekadi i do 2025. potrošnja će dostići nivo od blizu 2 Mt. Postojeći trend opadanja tražnje motornih benzina biće zaustavljen 2015-2016, nakon toga sledi spori rast tražnje i do 2025. potrošnja će biti oko 550 Kt. Potrošnja tečnog naftnog gasa (TNG) nakon intenzivnog rasta od 2015. ući će u fazu saturacije, tako da će u periodu 2010-2025. godine zabeležiti mali porast potrošnje - sa 377 na 435 Kt/god.",
publisher = "Association of Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "Modeling of motor fuel consumption in Serbia with projection to 2025, Modelovanje potrošnje motornih goriva u Srbiji sa projekcijama do 2025. godine",
volume = "66",
number = "3",
pages = "413-423",
doi = "10.2298/HEMIND110224105M"
}
Marinković, D., Popović, Z., Orlović, A.,& Ristić, M.. (2012). Modeling of motor fuel consumption in Serbia with projection to 2025. in Hemijska industrija
Association of Chemical Engineers of Serbia., 66(3), 413-423.
https://doi.org/10.2298/HEMIND110224105M
Marinković D, Popović Z, Orlović A, Ristić M. Modeling of motor fuel consumption in Serbia with projection to 2025. in Hemijska industrija. 2012;66(3):413-423.
doi:10.2298/HEMIND110224105M .
Marinković, Dalibor, Popović, Zoran, Orlović, Aleksandar, Ristić, Mirjana, "Modeling of motor fuel consumption in Serbia with projection to 2025" in Hemijska industrija, 66, no. 3 (2012):413-423,
https://doi.org/10.2298/HEMIND110224105M . .
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Removal of methyl tertiary butyl ether from wastewaters using photolytic, photocatalytic and microbiological degradation processes

Kuburović, Nataša; Todorović, Marija; Raičević, Vera; Orlović, Aleksandar; Jovanović, Ljubinko; Nikolić, Jasmina; Kuburović, Vladimir; Drmanić, Saša; Šolević, Tatjana

(Elsevier B.V., 2007)

TY  - JOUR
AU  - Kuburović, Nataša
AU  - Todorović, Marija
AU  - Raičević, Vera
AU  - Orlović, Aleksandar
AU  - Jovanović, Ljubinko
AU  - Nikolić, Jasmina
AU  - Kuburović, Vladimir
AU  - Drmanić, Saša
AU  - Šolević, Tatjana
PY  - 2007
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/5856
AB  - Contamination of groundwater by methyl tertiary butyl ether (MTBE), that is detected in wastewater of petrochemical industry, is an increasing problem to water supply companies. The subjects of this research were the methods of photolytic, photocatalytic and microbiological degradation of methyl tertiary butyl ether (MTBE) dissolved in wastewaters. The effects of concentrated solar radiation simulated with sodium lamp (SONT UV 400) have been investigated in laboratory experiments. Our result indicated that bacteria Pseudomonas strain CY, isolated from the kerosene, and added alone, was able to gradually degrade MTBE and to decrease its concentration for 93.6% in 12 h. However, the percentage of photolytic degradation decrease in only 4 h was 99.2%. By adding Pseudomonas strain CY after 4 h of light treatment, the degradation was enhanced to 99.55% in additional 5 h. The photocatalytic process was performed in slurry-catalyst reactor with different concentrations of TiO2 catalyst: 5, 0.5 and 0.25 g/L. The MTBE degradation producing carbon dioxide reached 91% in only 150 min, when 5 g/L of catalyst was used.
PB  - Elsevier B.V.
T2  - Desalination
T1  - Removal of methyl tertiary butyl ether from wastewaters using photolytic, photocatalytic and microbiological degradation processes
VL  - 213
IS  - 1-3
SP  - 123
EP  - 128
DO  - 10.1016/j.desal.2006.03.605
ER  - 
@article{
author = "Kuburović, Nataša and Todorović, Marija and Raičević, Vera and Orlović, Aleksandar and Jovanović, Ljubinko and Nikolić, Jasmina and Kuburović, Vladimir and Drmanić, Saša and Šolević, Tatjana",
year = "2007",
abstract = "Contamination of groundwater by methyl tertiary butyl ether (MTBE), that is detected in wastewater of petrochemical industry, is an increasing problem to water supply companies. The subjects of this research were the methods of photolytic, photocatalytic and microbiological degradation of methyl tertiary butyl ether (MTBE) dissolved in wastewaters. The effects of concentrated solar radiation simulated with sodium lamp (SONT UV 400) have been investigated in laboratory experiments. Our result indicated that bacteria Pseudomonas strain CY, isolated from the kerosene, and added alone, was able to gradually degrade MTBE and to decrease its concentration for 93.6% in 12 h. However, the percentage of photolytic degradation decrease in only 4 h was 99.2%. By adding Pseudomonas strain CY after 4 h of light treatment, the degradation was enhanced to 99.55% in additional 5 h. The photocatalytic process was performed in slurry-catalyst reactor with different concentrations of TiO2 catalyst: 5, 0.5 and 0.25 g/L. The MTBE degradation producing carbon dioxide reached 91% in only 150 min, when 5 g/L of catalyst was used.",
publisher = "Elsevier B.V.",
journal = "Desalination",
title = "Removal of methyl tertiary butyl ether from wastewaters using photolytic, photocatalytic and microbiological degradation processes",
volume = "213",
number = "1-3",
pages = "123-128",
doi = "10.1016/j.desal.2006.03.605"
}
Kuburović, N., Todorović, M., Raičević, V., Orlović, A., Jovanović, L., Nikolić, J., Kuburović, V., Drmanić, S.,& Šolević, T.. (2007). Removal of methyl tertiary butyl ether from wastewaters using photolytic, photocatalytic and microbiological degradation processes. in Desalination
Elsevier B.V.., 213(1-3), 123-128.
https://doi.org/10.1016/j.desal.2006.03.605
Kuburović N, Todorović M, Raičević V, Orlović A, Jovanović L, Nikolić J, Kuburović V, Drmanić S, Šolević T. Removal of methyl tertiary butyl ether from wastewaters using photolytic, photocatalytic and microbiological degradation processes. in Desalination. 2007;213(1-3):123-128.
doi:10.1016/j.desal.2006.03.605 .
Kuburović, Nataša, Todorović, Marija, Raičević, Vera, Orlović, Aleksandar, Jovanović, Ljubinko, Nikolić, Jasmina, Kuburović, Vladimir, Drmanić, Saša, Šolević, Tatjana, "Removal of methyl tertiary butyl ether from wastewaters using photolytic, photocatalytic and microbiological degradation processes" in Desalination, 213, no. 1-3 (2007):123-128,
https://doi.org/10.1016/j.desal.2006.03.605 . .
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Hydrodesulfurization of light gas oil - kinetic determination in a batch reactor [Hidrodesulfurizacija lakog gasnog ulja - ispitivanje kinetike HDS u šaržnom reaktoru]

Skala, Dejan; Orlović, Aleksandar; Marković, Bojana; Terlecki-Baričević, Ana V.; Jovanović, D.

(Association of the Chemical Engineers of Serbia, 2002)

TY  - JOUR
AU  - Skala, Dejan
AU  - Orlović, Aleksandar
AU  - Marković, Bojana
AU  - Terlecki-Baričević, Ana V.
AU  - Jovanović, D.
PY  - 2002
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/83
AB  - The performed investigations were directed toward the analysis of the performance and activity of the fresh and regenerated Cyanamid HDS 20C catalyst in a laboratory batch reactor (2 dm3) for the HDS of the diesel fraction (light gas oil, LGO). Testing of the regenerated catalyst was performed with light gas oil (LGO) of different characteristics. The determined values of the reaction rate constant were compared to some published data in the literature for the HDS of specific sulfur compounds as well as the values of the activation energy. The rates of deactivation of the fresh and regenerated catalyst actually existed compared to some other results recently published in the literature. However, such an observed differences were not sufficient to derive a relation which could be used for the determination of the rate of catalyst deactivation.
PB  - Association of the Chemical Engineers of Serbia
T2  - Chemical Industry and Chemical Engineering Quarterly / CICEQ
T1  - Hydrodesulfurization of light gas oil - kinetic determination in a batch reactor [Hidrodesulfurizacija lakog gasnog ulja - ispitivanje kinetike HDS u šaržnom reaktoru]
VL  - 8
IS  - 4
SP  - 529
EP  - 532
UR  - https://hdl.handle.net/21.15107/rcub_cer_83
ER  - 
@article{
author = "Skala, Dejan and Orlović, Aleksandar and Marković, Bojana and Terlecki-Baričević, Ana V. and Jovanović, D.",
year = "2002",
abstract = "The performed investigations were directed toward the analysis of the performance and activity of the fresh and regenerated Cyanamid HDS 20C catalyst in a laboratory batch reactor (2 dm3) for the HDS of the diesel fraction (light gas oil, LGO). Testing of the regenerated catalyst was performed with light gas oil (LGO) of different characteristics. The determined values of the reaction rate constant were compared to some published data in the literature for the HDS of specific sulfur compounds as well as the values of the activation energy. The rates of deactivation of the fresh and regenerated catalyst actually existed compared to some other results recently published in the literature. However, such an observed differences were not sufficient to derive a relation which could be used for the determination of the rate of catalyst deactivation.",
publisher = "Association of the Chemical Engineers of Serbia",
journal = "Chemical Industry and Chemical Engineering Quarterly / CICEQ",
title = "Hydrodesulfurization of light gas oil - kinetic determination in a batch reactor [Hidrodesulfurizacija lakog gasnog ulja - ispitivanje kinetike HDS u šaržnom reaktoru]",
volume = "8",
number = "4",
pages = "529-532",
url = "https://hdl.handle.net/21.15107/rcub_cer_83"
}
Skala, D., Orlović, A., Marković, B., Terlecki-Baričević, A. V.,& Jovanović, D.. (2002). Hydrodesulfurization of light gas oil - kinetic determination in a batch reactor [Hidrodesulfurizacija lakog gasnog ulja - ispitivanje kinetike HDS u šaržnom reaktoru]. in Chemical Industry and Chemical Engineering Quarterly / CICEQ
Association of the Chemical Engineers of Serbia., 8(4), 529-532.
https://hdl.handle.net/21.15107/rcub_cer_83
Skala D, Orlović A, Marković B, Terlecki-Baričević AV, Jovanović D. Hydrodesulfurization of light gas oil - kinetic determination in a batch reactor [Hidrodesulfurizacija lakog gasnog ulja - ispitivanje kinetike HDS u šaržnom reaktoru]. in Chemical Industry and Chemical Engineering Quarterly / CICEQ. 2002;8(4):529-532.
https://hdl.handle.net/21.15107/rcub_cer_83 .
Skala, Dejan, Orlović, Aleksandar, Marković, Bojana, Terlecki-Baričević, Ana V., Jovanović, D., "Hydrodesulfurization of light gas oil - kinetic determination in a batch reactor [Hidrodesulfurizacija lakog gasnog ulja - ispitivanje kinetike HDS u šaržnom reaktoru]" in Chemical Industry and Chemical Engineering Quarterly / CICEQ, 8, no. 4 (2002):529-532,
https://hdl.handle.net/21.15107/rcub_cer_83 .