Jovanović, Dušan

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  • Jovanović, Dušan (2)
  • Jovanović, Dušan M. (2)
Projects

Author's Bibliography

Biodiesel synthesis using K2CO3/Al-O-Si aerogel catalysts

Lukić, Ivana; Krstić, Jugoslav; Glišić, Sandra; Jovanović, Dušan; Skala, Dejan

(Serbian Chemical Society, Belgrade, 2010)

TY  - JOUR
AU  - Lukić, Ivana
AU  - Krstić, Jugoslav
AU  - Glišić, Sandra
AU  - Jovanović, Dušan
AU  - Skala, Dejan
PY  - 2010
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/1600
AB  - In this study, catalysts for fatty acid methyl esters (FAME or biodiesel) synthesis with K2CO3 as the active component on an alumina/silica support were synthesized using the sol-gel method, which was followed by drying the 'dense' wet gels with supercritical carbon dioxide to obtain the aerogels. The prepared catalysts were characterized by XRD analysis, FTIR spectroscopy and N2 physisorption at 77 K, and tested in the methanolysis of sunflower oil. The effects of reaction variables, such as reaction time, temperature and methanol to oil molar ratio, on the yield of FAME were investigated. The aerogel catalysts with K2CO3 as the active component on an alumina/silica support exhibited good activity in the methanolysis of sunflower oil. The leaching of potassium when the catalyst was in contact with pure methanol under the working conditions of methanolysis was also tested in this study, indicating that it occurred only at higher temperatures, while at lower ones, it was negligible.
AB  - U ovom radu katalizator za sintezu metil estara masnih kiselina (MEMK ili biodizel) sa K2CO3 kao aktivnom komponentom na alumosilikatnom nosaču sintetizovan je sol-gel metodom nakon čega je dobijeni gel sušen uz prisustvo natkritičnog ugljen dioksida da bi se dobio aerogel. Za karakterizaciju sintetizovanih katalizatora korišćene su metode XRD, FTIR i N2 fizisorpcija na 77 K i katalizatori su testirani u reakciji metanolize suncokretovog ulja. Katalizator je testiran u reakciji metanolize suncekrotovog ulja i sintezi MEMK. Ispitan je uticaj različitih parametara kao što su vreme, temperatura i molarni odnos metanol : ulje na prinos MEMK. Aerogel katalizator sa K2CO3 kao aktivnom komponentom na alumosilikatnom nosaču pokazao je dobru katalitičku aktivnost u reakciji metanolize suncokretovog ulja. Izluživanje kalijuma u kontaktu sa metanolom na radnim uslovima metanolize takođe je testirano u ovom radu, pokazujući da ono postoji na višim temperaturama, dok je na nižim zanemarljivo.
PB  - Serbian Chemical Society, Belgrade
T2  - Journal of the Serbian Chemical Society
T1  - Biodiesel synthesis using K2CO3/Al-O-Si aerogel catalysts
T1  - Sinteza biodizela katalizovana alumosilikatnim aerogelom sa K2Co3
EP  - 801
IS  - 6
SP  - 789
VL  - 75
UR  - https://hdl.handle.net/21.15107/rcub_technorep_1600
ER  - 
@article{
author = "Lukić, Ivana and Krstić, Jugoslav and Glišić, Sandra and Jovanović, Dušan and Skala, Dejan",
year = "2010",
abstract = "In this study, catalysts for fatty acid methyl esters (FAME or biodiesel) synthesis with K2CO3 as the active component on an alumina/silica support were synthesized using the sol-gel method, which was followed by drying the 'dense' wet gels with supercritical carbon dioxide to obtain the aerogels. The prepared catalysts were characterized by XRD analysis, FTIR spectroscopy and N2 physisorption at 77 K, and tested in the methanolysis of sunflower oil. The effects of reaction variables, such as reaction time, temperature and methanol to oil molar ratio, on the yield of FAME were investigated. The aerogel catalysts with K2CO3 as the active component on an alumina/silica support exhibited good activity in the methanolysis of sunflower oil. The leaching of potassium when the catalyst was in contact with pure methanol under the working conditions of methanolysis was also tested in this study, indicating that it occurred only at higher temperatures, while at lower ones, it was negligible., U ovom radu katalizator za sintezu metil estara masnih kiselina (MEMK ili biodizel) sa K2CO3 kao aktivnom komponentom na alumosilikatnom nosaču sintetizovan je sol-gel metodom nakon čega je dobijeni gel sušen uz prisustvo natkritičnog ugljen dioksida da bi se dobio aerogel. Za karakterizaciju sintetizovanih katalizatora korišćene su metode XRD, FTIR i N2 fizisorpcija na 77 K i katalizatori su testirani u reakciji metanolize suncokretovog ulja. Katalizator je testiran u reakciji metanolize suncekrotovog ulja i sintezi MEMK. Ispitan je uticaj različitih parametara kao što su vreme, temperatura i molarni odnos metanol : ulje na prinos MEMK. Aerogel katalizator sa K2CO3 kao aktivnom komponentom na alumosilikatnom nosaču pokazao je dobru katalitičku aktivnost u reakciji metanolize suncokretovog ulja. Izluživanje kalijuma u kontaktu sa metanolom na radnim uslovima metanolize takođe je testirano u ovom radu, pokazujući da ono postoji na višim temperaturama, dok je na nižim zanemarljivo.",
publisher = "Serbian Chemical Society, Belgrade",
journal = "Journal of the Serbian Chemical Society",
title = "Biodiesel synthesis using K2CO3/Al-O-Si aerogel catalysts, Sinteza biodizela katalizovana alumosilikatnim aerogelom sa K2Co3",
pages = "801-789",
number = "6",
volume = "75",
url = "https://hdl.handle.net/21.15107/rcub_technorep_1600"
}
Lukić, I., Krstić, J., Glišić, S., Jovanović, D.,& Skala, D.. (2010). Biodiesel synthesis using K2CO3/Al-O-Si aerogel catalysts. in Journal of the Serbian Chemical Society
Serbian Chemical Society, Belgrade., 75(6), 789-801.
https://hdl.handle.net/21.15107/rcub_technorep_1600
Lukić I, Krstić J, Glišić S, Jovanović D, Skala D. Biodiesel synthesis using K2CO3/Al-O-Si aerogel catalysts. in Journal of the Serbian Chemical Society. 2010;75(6):789-801.
https://hdl.handle.net/21.15107/rcub_technorep_1600 .
Lukić, Ivana, Krstić, Jugoslav, Glišić, Sandra, Jovanović, Dušan, Skala, Dejan, "Biodiesel synthesis using K2CO3/Al-O-Si aerogel catalysts" in Journal of the Serbian Chemical Society, 75, no. 6 (2010):789-801,
https://hdl.handle.net/21.15107/rcub_technorep_1600 .
20
27

Adsorption of Pb2+, Cd2+ and Sr2+ ions onto natural and acid-activated sepiolites

Lazarević, Slavica; Janković-Častvan, Ivona; Jovanović, Dušan; Milonjić, Slobodan K.; Janaćković, Đorđe; Petrović, Rada

(Elsevier Science Bv, Amsterdam, 2007)

TY  - JOUR
AU  - Lazarević, Slavica
AU  - Janković-Častvan, Ivona
AU  - Jovanović, Dušan
AU  - Milonjić, Slobodan K.
AU  - Janaćković, Đorđe
AU  - Petrović, Rada
PY  - 2007
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/1157
AB  - The adsorption mechanisms of Ph2+, Cd2+ and Sr2+ ions on natural sepiolite and the influence of acid treatment on the adsorption capacity of sepiolite were investigated. The point of zero charge pH(pzc), is 7.4 +/- 0.1 for natural sepiolite and 6.9 +/- 0.1 for partially acid-activated sepiolite. The shift of the pH(pzc) of sepiolites toward lower pH values in solutions of Ph2+ and Cd2+ ions indicates that specific adsorption of these cations on natural and acid-activated sepiolites occurred, which was more pronounced for Pb2+ ions than for Cd2+ ions. There was no shift of the pH(pzc) in Solution containing Sr2+ ions, suggesting that specific adsorption of this cation did not occur. The affinity for ion exchange with the Mg2+ ions from the sepiolite structure was the highest for Pb2+ ions, then Cd2+, whereas the affinity for Sr2+ ions was negligible. The adsorption isotherms suggest that the sequence of the efficiency of the sepiolites adsorption is Ph2+ gt Cd2+ gt Sr2+. The retention of Pb2+ and Cd2+ ions by sepiolite occurs dominantly by specific adsorption and exchange of Mg2+ ions from the sepiolite structure. The concentration in the external outer sphere of the Stem layer by electrostatic forces is the dominant mechanism for the retention of Sr2+ ions on the surface of sepiolites. Despite increases in the surface areas upon acid activation, improvements in the adsorption were not observed, as a result of the decreasing number of Mg-OH groups, as main centers for specific adsorption, and the number of Mg2+ ions available for ion exchange with Pb2+, Cd2+ and Sr2+ ions. The removal of Mg-OH groups from the sepiolite also resulted in a decrease in the point of zero charge and an increase of the relative surface acidity, from 2.6 +/- 0.1 for the natural to 6.4 +/- 0.1 for the acid-activated sepiolite.
PB  - Elsevier Science Bv, Amsterdam
T2  - Applied Clay Science
T1  - Adsorption of Pb2+, Cd2+ and Sr2+ ions onto natural and acid-activated sepiolites
EP  - 57
IS  - 1-2
SP  - 47
VL  - 37
DO  - 10.1016/j.clay.2006.11.008
ER  - 
@article{
author = "Lazarević, Slavica and Janković-Častvan, Ivona and Jovanović, Dušan and Milonjić, Slobodan K. and Janaćković, Đorđe and Petrović, Rada",
year = "2007",
abstract = "The adsorption mechanisms of Ph2+, Cd2+ and Sr2+ ions on natural sepiolite and the influence of acid treatment on the adsorption capacity of sepiolite were investigated. The point of zero charge pH(pzc), is 7.4 +/- 0.1 for natural sepiolite and 6.9 +/- 0.1 for partially acid-activated sepiolite. The shift of the pH(pzc) of sepiolites toward lower pH values in solutions of Ph2+ and Cd2+ ions indicates that specific adsorption of these cations on natural and acid-activated sepiolites occurred, which was more pronounced for Pb2+ ions than for Cd2+ ions. There was no shift of the pH(pzc) in Solution containing Sr2+ ions, suggesting that specific adsorption of this cation did not occur. The affinity for ion exchange with the Mg2+ ions from the sepiolite structure was the highest for Pb2+ ions, then Cd2+, whereas the affinity for Sr2+ ions was negligible. The adsorption isotherms suggest that the sequence of the efficiency of the sepiolites adsorption is Ph2+ gt Cd2+ gt Sr2+. The retention of Pb2+ and Cd2+ ions by sepiolite occurs dominantly by specific adsorption and exchange of Mg2+ ions from the sepiolite structure. The concentration in the external outer sphere of the Stem layer by electrostatic forces is the dominant mechanism for the retention of Sr2+ ions on the surface of sepiolites. Despite increases in the surface areas upon acid activation, improvements in the adsorption were not observed, as a result of the decreasing number of Mg-OH groups, as main centers for specific adsorption, and the number of Mg2+ ions available for ion exchange with Pb2+, Cd2+ and Sr2+ ions. The removal of Mg-OH groups from the sepiolite also resulted in a decrease in the point of zero charge and an increase of the relative surface acidity, from 2.6 +/- 0.1 for the natural to 6.4 +/- 0.1 for the acid-activated sepiolite.",
publisher = "Elsevier Science Bv, Amsterdam",
journal = "Applied Clay Science",
title = "Adsorption of Pb2+, Cd2+ and Sr2+ ions onto natural and acid-activated sepiolites",
pages = "57-47",
number = "1-2",
volume = "37",
doi = "10.1016/j.clay.2006.11.008"
}
Lazarević, S., Janković-Častvan, I., Jovanović, D., Milonjić, S. K., Janaćković, Đ.,& Petrović, R.. (2007). Adsorption of Pb2+, Cd2+ and Sr2+ ions onto natural and acid-activated sepiolites. in Applied Clay Science
Elsevier Science Bv, Amsterdam., 37(1-2), 47-57.
https://doi.org/10.1016/j.clay.2006.11.008
Lazarević S, Janković-Častvan I, Jovanović D, Milonjić SK, Janaćković Đ, Petrović R. Adsorption of Pb2+, Cd2+ and Sr2+ ions onto natural and acid-activated sepiolites. in Applied Clay Science. 2007;37(1-2):47-57.
doi:10.1016/j.clay.2006.11.008 .
Lazarević, Slavica, Janković-Častvan, Ivona, Jovanović, Dušan, Milonjić, Slobodan K., Janaćković, Đorđe, Petrović, Rada, "Adsorption of Pb2+, Cd2+ and Sr2+ ions onto natural and acid-activated sepiolites" in Applied Clay Science, 37, no. 1-2 (2007):47-57,
https://doi.org/10.1016/j.clay.2006.11.008 . .
198
165
218

The sorption of lead, cadmium and strontium from aqueous solutions on sepiolite

Lazarević, Slavica; Janković-Častvan, Ivona; Ilić, Miloje M.; Jovanović, Dušan M.; Janaćković, Đorđe; Petrović, Rada

(Association of Chemical Engineers of Serbia, 2006)

TY  - JOUR
AU  - Lazarević, Slavica
AU  - Janković-Častvan, Ivona
AU  - Ilić, Miloje M.
AU  - Jovanović, Dušan M.
AU  - Janaćković, Đorđe
AU  - Petrović, Rada
PY  - 2006
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/964
AB  - The results of the characterization and the sorption properties of sepiolite from the locality Slovići are presented in this paper. X-Ray diffraction analysis, infrared spectroscopy and differential thermal analysis revealed sepiolite as the main phase and small amounts of magnesite as an impurity. The specific surface area of sepiolite, determined by nitrogen adsorption and by applying the BET equation was found to be 339 m2/g. The point of zero charge was determined by the batch equilibration method, under different conditions, and the shift in the point of zero charge, in the presence of Pb2+, Cd2+ and Sr2+ ions, was investigated. It was determined that the point of zero charge changed with modification of the solid/liquid ratio and by washing the powder, which indicated that under the investigated conditions some dissolution of the sepiolite and impurities took place also influencing the position of the point of zero charge. In the presence of Pb2+, Cd2+ and Sr2"1" ions, the point of zero charge was shifted toward lower pH values denoting specific ion sorption. The greatest shift and, therefore the largest specific sorption, appeared in the case of Pb2+ ions, somewhat less with Cd2+, and the least with Sr2"1" ions. The adsorption isotherms were determined for the Pb2+, Cd2+ and Sr2+ ions, as well as the amounts of these ions that were removed from aqueous media by the ion exchange of Mg2+ ions from the sepiolite structure, depending on the equilibrium ion concentrations. In the case of ion exchange, as in the case of specific sorption, the affinity of sepiolite for the investigated ions can be presented in the following order Pb2+  gt  Cd2+  gt  Sr2"1". For the removal of Sr2"1" ions from aqueous media by sepiolite, a third mechanism is important probably, the ion exchange of exchangeable ions from the sepiolite structure channels. As the result of the action of all the sorption mechanisms sepiolite is removes mostly Pb2+ ions, then Cd2+ and least of all Sr2"1" ions from the aqueous media.
AB  - U radu su prikazani rezultati karakterizacije i određivanja sorpcionih svojstava sepiolita sa lokaliteta Slovići. Određena je tačka nultog naelektrisanja sepiolita pri različitim uslovima i ispitano pomeranje tačke nultog naelektrisanja u prisustvu jona Pb2+, CcF+ I Sr2+. Utvrđeno je da se tačka nultog naelektrisanja menja sa promenom odnosa čvrsto/tečno i ispiranjem praha. U prisustvu jona Pb2+, Cd2+ i Sr2+, tačka nultog naelektrisanja se pomera ka nižim pH vrednostima, što ukazuje na specifičnu sorpciju jona. Određene su adsorpcione izoterme za jone Pb2+, Cd2+ i Sr2+ i količine ovih jona koji se jonski izmenjuju sa Mg2+ jonima iz strukture sepiolita u zavisnosti od ravnotežne koncentracije jona. Najveći afinitet sepiolit ima prema jonima Pb2+, nešto manji prema jonima Cd i najmanji za Sr2+ jone, kako u slučaju specifične sorpcije tako i u slučaju jonske izmene Mg2+ jona iz strukture sepiolita.
PB  - Association of Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - The sorption of lead, cadmium and strontium from aqueous solutions on sepiolite
T1  - Sorpcija jona olova, kadmijuma i stroncijuma iz vodenih rastvora na sepiolitu
EP  - 22
IS  - 1-2
SP  - 15
VL  - 60
DO  - 10.2298/HEMIND0602015L
ER  - 
@article{
author = "Lazarević, Slavica and Janković-Častvan, Ivona and Ilić, Miloje M. and Jovanović, Dušan M. and Janaćković, Đorđe and Petrović, Rada",
year = "2006",
abstract = "The results of the characterization and the sorption properties of sepiolite from the locality Slovići are presented in this paper. X-Ray diffraction analysis, infrared spectroscopy and differential thermal analysis revealed sepiolite as the main phase and small amounts of magnesite as an impurity. The specific surface area of sepiolite, determined by nitrogen adsorption and by applying the BET equation was found to be 339 m2/g. The point of zero charge was determined by the batch equilibration method, under different conditions, and the shift in the point of zero charge, in the presence of Pb2+, Cd2+ and Sr2+ ions, was investigated. It was determined that the point of zero charge changed with modification of the solid/liquid ratio and by washing the powder, which indicated that under the investigated conditions some dissolution of the sepiolite and impurities took place also influencing the position of the point of zero charge. In the presence of Pb2+, Cd2+ and Sr2"1" ions, the point of zero charge was shifted toward lower pH values denoting specific ion sorption. The greatest shift and, therefore the largest specific sorption, appeared in the case of Pb2+ ions, somewhat less with Cd2+, and the least with Sr2"1" ions. The adsorption isotherms were determined for the Pb2+, Cd2+ and Sr2+ ions, as well as the amounts of these ions that were removed from aqueous media by the ion exchange of Mg2+ ions from the sepiolite structure, depending on the equilibrium ion concentrations. In the case of ion exchange, as in the case of specific sorption, the affinity of sepiolite for the investigated ions can be presented in the following order Pb2+  gt  Cd2+  gt  Sr2"1". For the removal of Sr2"1" ions from aqueous media by sepiolite, a third mechanism is important probably, the ion exchange of exchangeable ions from the sepiolite structure channels. As the result of the action of all the sorption mechanisms sepiolite is removes mostly Pb2+ ions, then Cd2+ and least of all Sr2"1" ions from the aqueous media., U radu su prikazani rezultati karakterizacije i određivanja sorpcionih svojstava sepiolita sa lokaliteta Slovići. Određena je tačka nultog naelektrisanja sepiolita pri različitim uslovima i ispitano pomeranje tačke nultog naelektrisanja u prisustvu jona Pb2+, CcF+ I Sr2+. Utvrđeno je da se tačka nultog naelektrisanja menja sa promenom odnosa čvrsto/tečno i ispiranjem praha. U prisustvu jona Pb2+, Cd2+ i Sr2+, tačka nultog naelektrisanja se pomera ka nižim pH vrednostima, što ukazuje na specifičnu sorpciju jona. Određene su adsorpcione izoterme za jone Pb2+, Cd2+ i Sr2+ i količine ovih jona koji se jonski izmenjuju sa Mg2+ jonima iz strukture sepiolita u zavisnosti od ravnotežne koncentracije jona. Najveći afinitet sepiolit ima prema jonima Pb2+, nešto manji prema jonima Cd i najmanji za Sr2+ jone, kako u slučaju specifične sorpcije tako i u slučaju jonske izmene Mg2+ jona iz strukture sepiolita.",
publisher = "Association of Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "The sorption of lead, cadmium and strontium from aqueous solutions on sepiolite, Sorpcija jona olova, kadmijuma i stroncijuma iz vodenih rastvora na sepiolitu",
pages = "22-15",
number = "1-2",
volume = "60",
doi = "10.2298/HEMIND0602015L"
}
Lazarević, S., Janković-Častvan, I., Ilić, M. M., Jovanović, D. M., Janaćković, Đ.,& Petrović, R.. (2006). The sorption of lead, cadmium and strontium from aqueous solutions on sepiolite. in Hemijska industrija
Association of Chemical Engineers of Serbia., 60(1-2), 15-22.
https://doi.org/10.2298/HEMIND0602015L
Lazarević S, Janković-Častvan I, Ilić MM, Jovanović DM, Janaćković Đ, Petrović R. The sorption of lead, cadmium and strontium from aqueous solutions on sepiolite. in Hemijska industrija. 2006;60(1-2):15-22.
doi:10.2298/HEMIND0602015L .
Lazarević, Slavica, Janković-Častvan, Ivona, Ilić, Miloje M., Jovanović, Dušan M., Janaćković, Đorđe, Petrović, Rada, "The sorption of lead, cadmium and strontium from aqueous solutions on sepiolite" in Hemijska industrija, 60, no. 1-2 (2006):15-22,
https://doi.org/10.2298/HEMIND0602015L . .

Hydrodesulfurization of light gas oil: Kinetic determination in a batch reactor

Skala, Dejan; Orlović, Aleksandar; Marković, Branislav; Tarlecki-Barićević, Ana; Jovanović, Dušan M.

(Association of Chemical Engineers of Serbia, 2002)

TY  - JOUR
AU  - Skala, Dejan
AU  - Orlović, Aleksandar
AU  - Marković, Branislav
AU  - Tarlecki-Barićević, Ana
AU  - Jovanović, Dušan M.
PY  - 2002
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/484
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.
AB  - Ispitivanja aktivnosti novog (svežeg) i regenerisanog katalizatora tipa Cyanamid HDS 20C je realizovano u ovom radu u laboratorijskom šaržnom reaktoru (2 dm3). Smanjena aktivnost regenerisanog u odnosu na svež katalizator povezana je promenom izračunate konstante brzine reakcije desulfurizacije lakog gasnog ulja. U cilju određivanja konstante brzine merena je konverzija sumpornih jedinjenja i određivana kinetika procesa HDS primenom integralne metode. Lako gasno ulje različitog porekla (iz nafte Ural REB sa 0,92 mas% sumpora i nafte "Kikinda" sa vojvođanskih izvora sa 0,092 mas%) je korišćeno u ovim ispitivanjima. Određena je konstanta brzine i energija aktivacije procesa HDS pod pretpostavkom da je u pitanju pseudo reakcija I reda. Dobijene brojne vrednosti su upoređene sa objavljenim rezultatima u literaturi koji se odnose na HDS čistih model jedinjenja (tiofen, benzotiofen, dibenzotiofen i supstituisani deri-vati ovih jedinjenja). Utvrđeno je da postoji samo mala razlika u određenoj prividnoj konstanti brzine (tj. i aktivnosti) za svež i regenerisan katalizator na 300°C, koja postaje sve veća kako se proces izvodi na višim temperaturama (350°C). Ovako ponašanje regenerisanog katalizatora može se objasniti činjenicom da LGU u svom sastavu ima pored slabije reaktivnih sumpornih jedinjenja aromatskog tipa (benzo i dibenzotiofeni) i izvestan udeo jedinjenja tipa sulfida, disulfida i tiofena koji su mnogo reaktivniji. Takav odnos manje i više reaktivnih jedinjenja sumpora utiče na ukupan efekat HDS i potrebu da katalizator poseduje potrebnu aktivnost kako bi se tek na višim temperaturama ostvarila željena konverzija sumpornih jedinjenja aromatskog tipa. Ponovljeni eksperimenti pod istim uslovima ukazuju da postoji razlika između brzina deaktivacije svežeg i regenerisanog katalizatora kao i da se brzine deaktivacije može dovesti u vezu sa objavljenim rezultatima iz literature. Međutim, uočeni efekti deaktivacije katalizatora i podaci koji se mogu iskoristiti nisu bili dovoljni da se detaljno prouči i definiše brzina deaktivacije katalizatora.
PB  - Association of Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - Hydrodesulfurization of light gas oil: Kinetic determination in a batch reactor
T1  - Hidrodesulfurizacija lakog gasnog ulja
EP  - 532
IS  - 12
SP  - 529
VL  - 56
DO  - 10.2298/HEMIND0212529S
ER  - 
@article{
author = "Skala, Dejan and Orlović, Aleksandar and Marković, Branislav and Tarlecki-Barićević, Ana and Jovanović, Dušan M.",
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., Ispitivanja aktivnosti novog (svežeg) i regenerisanog katalizatora tipa Cyanamid HDS 20C je realizovano u ovom radu u laboratorijskom šaržnom reaktoru (2 dm3). Smanjena aktivnost regenerisanog u odnosu na svež katalizator povezana je promenom izračunate konstante brzine reakcije desulfurizacije lakog gasnog ulja. U cilju određivanja konstante brzine merena je konverzija sumpornih jedinjenja i određivana kinetika procesa HDS primenom integralne metode. Lako gasno ulje različitog porekla (iz nafte Ural REB sa 0,92 mas% sumpora i nafte "Kikinda" sa vojvođanskih izvora sa 0,092 mas%) je korišćeno u ovim ispitivanjima. Određena je konstanta brzine i energija aktivacije procesa HDS pod pretpostavkom da je u pitanju pseudo reakcija I reda. Dobijene brojne vrednosti su upoređene sa objavljenim rezultatima u literaturi koji se odnose na HDS čistih model jedinjenja (tiofen, benzotiofen, dibenzotiofen i supstituisani deri-vati ovih jedinjenja). Utvrđeno je da postoji samo mala razlika u određenoj prividnoj konstanti brzine (tj. i aktivnosti) za svež i regenerisan katalizator na 300°C, koja postaje sve veća kako se proces izvodi na višim temperaturama (350°C). Ovako ponašanje regenerisanog katalizatora može se objasniti činjenicom da LGU u svom sastavu ima pored slabije reaktivnih sumpornih jedinjenja aromatskog tipa (benzo i dibenzotiofeni) i izvestan udeo jedinjenja tipa sulfida, disulfida i tiofena koji su mnogo reaktivniji. Takav odnos manje i više reaktivnih jedinjenja sumpora utiče na ukupan efekat HDS i potrebu da katalizator poseduje potrebnu aktivnost kako bi se tek na višim temperaturama ostvarila željena konverzija sumpornih jedinjenja aromatskog tipa. Ponovljeni eksperimenti pod istim uslovima ukazuju da postoji razlika između brzina deaktivacije svežeg i regenerisanog katalizatora kao i da se brzine deaktivacije može dovesti u vezu sa objavljenim rezultatima iz literature. Međutim, uočeni efekti deaktivacije katalizatora i podaci koji se mogu iskoristiti nisu bili dovoljni da se detaljno prouči i definiše brzina deaktivacije katalizatora.",
publisher = "Association of Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "Hydrodesulfurization of light gas oil: Kinetic determination in a batch reactor, Hidrodesulfurizacija lakog gasnog ulja",
pages = "532-529",
number = "12",
volume = "56",
doi = "10.2298/HEMIND0212529S"
}
Skala, D., Orlović, A., Marković, B., Tarlecki-Barićević, A.,& Jovanović, D. M.. (2002). Hydrodesulfurization of light gas oil: Kinetic determination in a batch reactor. in Hemijska industrija
Association of Chemical Engineers of Serbia., 56(12), 529-532.
https://doi.org/10.2298/HEMIND0212529S
Skala D, Orlović A, Marković B, Tarlecki-Barićević A, Jovanović DM. Hydrodesulfurization of light gas oil: Kinetic determination in a batch reactor. in Hemijska industrija. 2002;56(12):529-532.
doi:10.2298/HEMIND0212529S .
Skala, Dejan, Orlović, Aleksandar, Marković, Branislav, Tarlecki-Barićević, Ana, Jovanović, Dušan M., "Hydrodesulfurization of light gas oil: Kinetic determination in a batch reactor" in Hemijska industrija, 56, no. 12 (2002):529-532,
https://doi.org/10.2298/HEMIND0212529S . .
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