Pejanović, Srđan

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  • Pejanović, Srđan (7)
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Author's Bibliography

Experimental study on the ozone absorption accompanied by instantaneous chemical reaction

Đeković-Šević, Milica; Bošković-Vragolović, Nevenka; Garić-Grulović, Radmila; Pejanović, Srđan

(Taylor & Francis Inc, Philadelphia, 2018)

TY  - JOUR
AU  - Đeković-Šević, Milica
AU  - Bošković-Vragolović, Nevenka
AU  - Garić-Grulović, Radmila
AU  - Pejanović, Srđan
PY  - 2018
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/3967
AB  - This work deals with gas absorption accompanied by chemical reaction in a liquid phase. Ozone absorption in potassium indigotrisulfonate solution was investigated in a batch bubble column. Enhancement factor for absorption accompanied by instantaneous chemical reaction in the liquid phase was experimentally determined, as a ratio of the volumetric mass transfer coefficient for the absorption accompanied by reaction to that for pure physical absorption. The influence of (a) the initial concentration of the solute from liquid phase and (b) the ozone concentration in gas phase on the enhancement factor were experimentally examined. The absorption accompanied by instantaneous chemical reaction is a diffusion-controlled process, whose rate depends upon the diffusivities of the absorbing gas and the solute in liquid phase. The influence of these diffusivities was found to be more significant for lower values of the enhancement factor. The rate of ozone absorption was followed by the time change of the solution color, using new method based on the computer program SigmaScan Pro 5 (Systat Software, Inc., San Jose, CA, USA). This investigation is a contribution to the prediction of the ozone consumption in wastewater treatment, in cases when ozone instantaneously reacts with substances present in water.
PB  - Taylor & Francis Inc, Philadelphia
T2  - Chemical Engineering Communications
T1  - Experimental study on the ozone absorption accompanied by instantaneous chemical reaction
EP  - 580
IS  - 5
SP  - 571
VL  - 205
DO  - 10.1080/00986445.2017.1399125
ER  - 
@article{
author = "Đeković-Šević, Milica and Bošković-Vragolović, Nevenka and Garić-Grulović, Radmila and Pejanović, Srđan",
year = "2018",
abstract = "This work deals with gas absorption accompanied by chemical reaction in a liquid phase. Ozone absorption in potassium indigotrisulfonate solution was investigated in a batch bubble column. Enhancement factor for absorption accompanied by instantaneous chemical reaction in the liquid phase was experimentally determined, as a ratio of the volumetric mass transfer coefficient for the absorption accompanied by reaction to that for pure physical absorption. The influence of (a) the initial concentration of the solute from liquid phase and (b) the ozone concentration in gas phase on the enhancement factor were experimentally examined. The absorption accompanied by instantaneous chemical reaction is a diffusion-controlled process, whose rate depends upon the diffusivities of the absorbing gas and the solute in liquid phase. The influence of these diffusivities was found to be more significant for lower values of the enhancement factor. The rate of ozone absorption was followed by the time change of the solution color, using new method based on the computer program SigmaScan Pro 5 (Systat Software, Inc., San Jose, CA, USA). This investigation is a contribution to the prediction of the ozone consumption in wastewater treatment, in cases when ozone instantaneously reacts with substances present in water.",
publisher = "Taylor & Francis Inc, Philadelphia",
journal = "Chemical Engineering Communications",
title = "Experimental study on the ozone absorption accompanied by instantaneous chemical reaction",
pages = "580-571",
number = "5",
volume = "205",
doi = "10.1080/00986445.2017.1399125"
}
Đeković-Šević, M., Bošković-Vragolović, N., Garić-Grulović, R.,& Pejanović, S.. (2018). Experimental study on the ozone absorption accompanied by instantaneous chemical reaction. in Chemical Engineering Communications
Taylor & Francis Inc, Philadelphia., 205(5), 571-580.
https://doi.org/10.1080/00986445.2017.1399125
Đeković-Šević M, Bošković-Vragolović N, Garić-Grulović R, Pejanović S. Experimental study on the ozone absorption accompanied by instantaneous chemical reaction. in Chemical Engineering Communications. 2018;205(5):571-580.
doi:10.1080/00986445.2017.1399125 .
Đeković-Šević, Milica, Bošković-Vragolović, Nevenka, Garić-Grulović, Radmila, Pejanović, Srđan, "Experimental study on the ozone absorption accompanied by instantaneous chemical reaction" in Chemical Engineering Communications, 205, no. 5 (2018):571-580,
https://doi.org/10.1080/00986445.2017.1399125 . .
1

Determination of the ozone volumetric mass transfer coefficient in bubble column with two-fluid nozzle gas distributor

Đeković-Šević, Milica; Bošković-Vragolović, Nevenka; Takić, Ljiljana; Garić-Grulović, Radmila; Pejanović, Srđan

(Association of Chemical Engineers of Serbia, 2015)

TY  - JOUR
AU  - Đeković-Šević, Milica
AU  - Bošković-Vragolović, Nevenka
AU  - Takić, Ljiljana
AU  - Garić-Grulović, Radmila
AU  - Pejanović, Srđan
PY  - 2015
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/2890
AB  - Experimental investigation of gas-liquid mass transfer of ozone in water, in bubble column with two-fluid nozzle gas distributor (BKDM), under different operating conditions, is presented in this work. The main objective was to determine the ozone volumetric mass transfer coefficient, kL a, in calm uniform section of the column, under different values of gas and liquid flow rates. Obtained values of these coefficients were compared with the values in countercurrent bubble column. The critical liquid flowrate, when gas hold up reaches its maximum, was experimentally determined. It was shown that the maximum value of the ozone volumetric mass transfer coefficient is obtained just when liquid flowrate is at its critical value.
AB  - U ovom radu prikazani su rezultati eksperimentalnih ispitivanja prenosa mase gas-tečnost pri ozonizaciji vode u barbotažnoj koloni sa dvofluidnom mlaznicom (BKDM) pod različitim operativnim uslovima. Cilj ovih ispitivanja bio je određivanje vrednosti zapreminskog koeficijenta prenosa mase ozona u vodi, kLa, u mirnoj zoni kolone, pri različitim protocima gasne i tečne faze. U radu je dato i poređenje kLa u BKDM sa vrednostima kLa u klasičnoj protivstrujnoj barbotažnoj koloni sa poroznom pločom tj. fritom. Eksperimentalno je određena vrednost kritičnog protoka tečnosti, pri kojem sadržaj gasa u disperziji, u mirnoj zoni kolone, dostiže svoju maksimalnu vrednost. Rezultati su pokazali da se pri kritičnom protoku tečnosti dobija maksimalna vrednost zapreminskog koeficijenta prenosa mase ozona u vodi.
PB  - Association of Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - Determination of the ozone volumetric mass transfer coefficient in bubble column with two-fluid nozzle gas distributor
T1  - Određivanje zapreminskog koeficijenta prenosa mase ozona u barbotažnoj koloni sa dvofluidnom mlaznicom
EP  - 559
IS  - 5
SP  - 553
VL  - 69
DO  - 10.2298/HEMIND140716075D
ER  - 
@article{
author = "Đeković-Šević, Milica and Bošković-Vragolović, Nevenka and Takić, Ljiljana and Garić-Grulović, Radmila and Pejanović, Srđan",
year = "2015",
abstract = "Experimental investigation of gas-liquid mass transfer of ozone in water, in bubble column with two-fluid nozzle gas distributor (BKDM), under different operating conditions, is presented in this work. The main objective was to determine the ozone volumetric mass transfer coefficient, kL a, in calm uniform section of the column, under different values of gas and liquid flow rates. Obtained values of these coefficients were compared with the values in countercurrent bubble column. The critical liquid flowrate, when gas hold up reaches its maximum, was experimentally determined. It was shown that the maximum value of the ozone volumetric mass transfer coefficient is obtained just when liquid flowrate is at its critical value., U ovom radu prikazani su rezultati eksperimentalnih ispitivanja prenosa mase gas-tečnost pri ozonizaciji vode u barbotažnoj koloni sa dvofluidnom mlaznicom (BKDM) pod različitim operativnim uslovima. Cilj ovih ispitivanja bio je određivanje vrednosti zapreminskog koeficijenta prenosa mase ozona u vodi, kLa, u mirnoj zoni kolone, pri različitim protocima gasne i tečne faze. U radu je dato i poređenje kLa u BKDM sa vrednostima kLa u klasičnoj protivstrujnoj barbotažnoj koloni sa poroznom pločom tj. fritom. Eksperimentalno je određena vrednost kritičnog protoka tečnosti, pri kojem sadržaj gasa u disperziji, u mirnoj zoni kolone, dostiže svoju maksimalnu vrednost. Rezultati su pokazali da se pri kritičnom protoku tečnosti dobija maksimalna vrednost zapreminskog koeficijenta prenosa mase ozona u vodi.",
publisher = "Association of Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "Determination of the ozone volumetric mass transfer coefficient in bubble column with two-fluid nozzle gas distributor, Određivanje zapreminskog koeficijenta prenosa mase ozona u barbotažnoj koloni sa dvofluidnom mlaznicom",
pages = "559-553",
number = "5",
volume = "69",
doi = "10.2298/HEMIND140716075D"
}
Đeković-Šević, M., Bošković-Vragolović, N., Takić, L., Garić-Grulović, R.,& Pejanović, S.. (2015). Determination of the ozone volumetric mass transfer coefficient in bubble column with two-fluid nozzle gas distributor. in Hemijska industrija
Association of Chemical Engineers of Serbia., 69(5), 553-559.
https://doi.org/10.2298/HEMIND140716075D
Đeković-Šević M, Bošković-Vragolović N, Takić L, Garić-Grulović R, Pejanović S. Determination of the ozone volumetric mass transfer coefficient in bubble column with two-fluid nozzle gas distributor. in Hemijska industrija. 2015;69(5):553-559.
doi:10.2298/HEMIND140716075D .
Đeković-Šević, Milica, Bošković-Vragolović, Nevenka, Takić, Ljiljana, Garić-Grulović, Radmila, Pejanović, Srđan, "Determination of the ozone volumetric mass transfer coefficient in bubble column with two-fluid nozzle gas distributor" in Hemijska industrija, 69, no. 5 (2015):553-559,
https://doi.org/10.2298/HEMIND140716075D . .
1
1
1

Modeling the kinetics of essential oil hydrodistillation from plant materials

Milojević, Svetomir; Radosavljević, Dragana B.; Pavićević, Vladimir; Pejanović, Srđan; Veljković, Vlada B.

(Association of Chemical Engineers of Serbia, 2013)

TY  - JOUR
AU  - Milojević, Svetomir
AU  - Radosavljević, Dragana B.
AU  - Pavićević, Vladimir
AU  - Pejanović, Srđan
AU  - Veljković, Vlada B.
PY  - 2013
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/2345
AB  - The present work deals with the modeling of the kinetics of essential oils extraction from plant materials by water and steam distillation. The experimental data were obtained by studying the hydrodistillation kinetics of essential oil from juniper berries. The literature data on the kinetics of essential oils hydrodistillation from different plant materials were also included into the modeling. A physical model based on simultaneous washing and diffusion of essential oil from plant materials were developed to describe the kinetics of essential oils hydrodistillation, and two other simpler models were derived from this physical model assuming either instantaneous washing followed by diffusion or diffusion with no washing (i.e., first-order kinetics). The main goal was to compare these models and suggest the optimum ones for water and steam distillation and for different plant materials. All three models described well the experimental kinetic data on water distillation irrespective of the type of distillation equipment and its scale, the type of plant materials and the operational conditions. The most applicable model is the one involving simultaneous washing and diffusion of the essential oil. However, this model was generally inapplicable for steam distillation of essential oils, except for juniper berries. For this hydrodistillation technique, the pseudo first-order model was shown to be the best one. In a few cases, a variation of the essential oil yield with time was observed to be sigmoidal and was modeled by the Boltzmann sigmoid function.
AB  - Rad se bavi modelovanjem kinetike ekstrakcije etarskog ulja iz biljnih materijala primenom destilacija vodom i vodenom parom. Eksperimentalni podaci dobijeni su proučavanjem kinetike hidrodestilacije etarskog ulja ploda kleke. Literaturni podaci o kinetici hidrodestilacije etarskog ulja iz različitih biljnih materijala su, takođe, uključeni u modelovanje. Za opisivanje kinetike hidrodestilacije etarskog ulja razvijen je fizički model koji je zasnovan na istovremenom ispiranju i difuziji etarskog ulja iz biljnog materijala. Iz ovog modela izvedena su dva prostija modela od kojih je prvi zasnovan na trenutnom ispiranju praćenim difuzijom a drugi na difuziji bez ispiranja (tj.na kinetici prvog reda). Glavni cilj je bio poređenje ovih modela i predlaganje optimalnog za destilacije vodom i vodenom parom I za različite biljne materijale. Sva tri modela opisuju dobro eksperimentalne kinetičke podatke u slučaju destilacije vodom nezavisno od tipa destilatora i njegove veličine, tipa biljnog materijala i procesnih uslova, ali je najbolji model koji uključuje istovremeno ispiranje i difuziju etarskog ulja. Ovaj model je, međutim, neprimenljiv za vodeno-parnu destilaciju etarskog ulja, izuzev za etarsko ulje ploda kleke. Za ovu destilaciju etarskog ulja najbolji je kinetički model pseudo-prvog reda. U slučaju nekoliko biljnih materijala, promena prinosa etarskog ulja sa vremenom je sigmoidna, pa je modelovana Bolcmanovom sigmoidnom funkcijom.
PB  - Association of Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - Modeling the kinetics of essential oil hydrodistillation from plant materials
T1  - Modelovanje kinetike hidrodestilacije etarskog ulja iz biljnih materijala
EP  - 859
IS  - 5
SP  - 843
VL  - 67
DO  - 10.2298/HEMIND121026009M
ER  - 
@article{
author = "Milojević, Svetomir and Radosavljević, Dragana B. and Pavićević, Vladimir and Pejanović, Srđan and Veljković, Vlada B.",
year = "2013",
abstract = "The present work deals with the modeling of the kinetics of essential oils extraction from plant materials by water and steam distillation. The experimental data were obtained by studying the hydrodistillation kinetics of essential oil from juniper berries. The literature data on the kinetics of essential oils hydrodistillation from different plant materials were also included into the modeling. A physical model based on simultaneous washing and diffusion of essential oil from plant materials were developed to describe the kinetics of essential oils hydrodistillation, and two other simpler models were derived from this physical model assuming either instantaneous washing followed by diffusion or diffusion with no washing (i.e., first-order kinetics). The main goal was to compare these models and suggest the optimum ones for water and steam distillation and for different plant materials. All three models described well the experimental kinetic data on water distillation irrespective of the type of distillation equipment and its scale, the type of plant materials and the operational conditions. The most applicable model is the one involving simultaneous washing and diffusion of the essential oil. However, this model was generally inapplicable for steam distillation of essential oils, except for juniper berries. For this hydrodistillation technique, the pseudo first-order model was shown to be the best one. In a few cases, a variation of the essential oil yield with time was observed to be sigmoidal and was modeled by the Boltzmann sigmoid function., Rad se bavi modelovanjem kinetike ekstrakcije etarskog ulja iz biljnih materijala primenom destilacija vodom i vodenom parom. Eksperimentalni podaci dobijeni su proučavanjem kinetike hidrodestilacije etarskog ulja ploda kleke. Literaturni podaci o kinetici hidrodestilacije etarskog ulja iz različitih biljnih materijala su, takođe, uključeni u modelovanje. Za opisivanje kinetike hidrodestilacije etarskog ulja razvijen je fizički model koji je zasnovan na istovremenom ispiranju i difuziji etarskog ulja iz biljnog materijala. Iz ovog modela izvedena su dva prostija modela od kojih je prvi zasnovan na trenutnom ispiranju praćenim difuzijom a drugi na difuziji bez ispiranja (tj.na kinetici prvog reda). Glavni cilj je bio poređenje ovih modela i predlaganje optimalnog za destilacije vodom i vodenom parom I za različite biljne materijale. Sva tri modela opisuju dobro eksperimentalne kinetičke podatke u slučaju destilacije vodom nezavisno od tipa destilatora i njegove veličine, tipa biljnog materijala i procesnih uslova, ali je najbolji model koji uključuje istovremeno ispiranje i difuziju etarskog ulja. Ovaj model je, međutim, neprimenljiv za vodeno-parnu destilaciju etarskog ulja, izuzev za etarsko ulje ploda kleke. Za ovu destilaciju etarskog ulja najbolji je kinetički model pseudo-prvog reda. U slučaju nekoliko biljnih materijala, promena prinosa etarskog ulja sa vremenom je sigmoidna, pa je modelovana Bolcmanovom sigmoidnom funkcijom.",
publisher = "Association of Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "Modeling the kinetics of essential oil hydrodistillation from plant materials, Modelovanje kinetike hidrodestilacije etarskog ulja iz biljnih materijala",
pages = "859-843",
number = "5",
volume = "67",
doi = "10.2298/HEMIND121026009M"
}
Milojević, S., Radosavljević, D. B., Pavićević, V., Pejanović, S.,& Veljković, V. B.. (2013). Modeling the kinetics of essential oil hydrodistillation from plant materials. in Hemijska industrija
Association of Chemical Engineers of Serbia., 67(5), 843-859.
https://doi.org/10.2298/HEMIND121026009M
Milojević S, Radosavljević DB, Pavićević V, Pejanović S, Veljković VB. Modeling the kinetics of essential oil hydrodistillation from plant materials. in Hemijska industrija. 2013;67(5):843-859.
doi:10.2298/HEMIND121026009M .
Milojević, Svetomir, Radosavljević, Dragana B., Pavićević, Vladimir, Pejanović, Srđan, Veljković, Vlada B., "Modeling the kinetics of essential oil hydrodistillation from plant materials" in Hemijska industrija, 67, no. 5 (2013):843-859,
https://doi.org/10.2298/HEMIND121026009M . .
43
32
47

Modelling of the substance transfer in the gas-liquid system with chemical reaction

Mosorinac, T.; Savković-Stevanović, Jelenka B.; Ivanović-Knezević, M.; Pejanović, Srđan; Perunicić, M.; Bošković-Vragolović, Nevenka

(2012)

TY  - JOUR
AU  - Mosorinac, T.
AU  - Savković-Stevanović, Jelenka B.
AU  - Ivanović-Knezević, M.
AU  - Pejanović, Srđan
AU  - Perunicić, M.
AU  - Bošković-Vragolović, Nevenka
PY  - 2012
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/2002
AB  - In this paper substance transfer phenomena in the multistage reactive system were investigated.Substance transfer between liquid and gas phases in a distillation packed column with reactionesterification was examined. Efficiency of substance transfer were examined by HTU-Height of transferunits and volumetric substance transfer coefficients. The esterification reaction of the ethanol andacetic acid was examined. Based on derived mathematical model the total height of transfer units andindividual height of transfer units for the liquid and gas phases were determined. The investigation wasperformed by computer simulation and experiments. Several correlation models for HTU/NTU andsubstance transfer coefficients were studied. The correlations for component transfer were derived inquaternary systems ethanol-ethyl acetate-acetic acid -water.
T2  - Petroleum and Coal
T1  - Modelling of the substance transfer in the gas-liquid system with chemical reaction
EP  - 286
IS  - 3
SP  - 278
VL  - 54
UR  - https://hdl.handle.net/21.15107/rcub_technorep_2002
ER  - 
@article{
author = "Mosorinac, T. and Savković-Stevanović, Jelenka B. and Ivanović-Knezević, M. and Pejanović, Srđan and Perunicić, M. and Bošković-Vragolović, Nevenka",
year = "2012",
abstract = "In this paper substance transfer phenomena in the multistage reactive system were investigated.Substance transfer between liquid and gas phases in a distillation packed column with reactionesterification was examined. Efficiency of substance transfer were examined by HTU-Height of transferunits and volumetric substance transfer coefficients. The esterification reaction of the ethanol andacetic acid was examined. Based on derived mathematical model the total height of transfer units andindividual height of transfer units for the liquid and gas phases were determined. The investigation wasperformed by computer simulation and experiments. Several correlation models for HTU/NTU andsubstance transfer coefficients were studied. The correlations for component transfer were derived inquaternary systems ethanol-ethyl acetate-acetic acid -water.",
journal = "Petroleum and Coal",
title = "Modelling of the substance transfer in the gas-liquid system with chemical reaction",
pages = "286-278",
number = "3",
volume = "54",
url = "https://hdl.handle.net/21.15107/rcub_technorep_2002"
}
Mosorinac, T., Savković-Stevanović, J. B., Ivanović-Knezević, M., Pejanović, S., Perunicić, M.,& Bošković-Vragolović, N.. (2012). Modelling of the substance transfer in the gas-liquid system with chemical reaction. in Petroleum and Coal, 54(3), 278-286.
https://hdl.handle.net/21.15107/rcub_technorep_2002
Mosorinac T, Savković-Stevanović JB, Ivanović-Knezević M, Pejanović S, Perunicić M, Bošković-Vragolović N. Modelling of the substance transfer in the gas-liquid system with chemical reaction. in Petroleum and Coal. 2012;54(3):278-286.
https://hdl.handle.net/21.15107/rcub_technorep_2002 .
Mosorinac, T., Savković-Stevanović, Jelenka B., Ivanović-Knezević, M., Pejanović, Srđan, Perunicić, M., Bošković-Vragolović, Nevenka, "Modelling of the substance transfer in the gas-liquid system with chemical reaction" in Petroleum and Coal, 54, no. 3 (2012):278-286,
https://hdl.handle.net/21.15107/rcub_technorep_2002 .

Material and heat transfer rate in the gas-lquid system

Mosorinac, T.; Ivanović-Knezević, M.; Pejanović, Srđan; Perunicić, M.; Bošković-Vragolović, Nevenka

(2012)

TY  - JOUR
AU  - Mosorinac, T.
AU  - Ivanović-Knezević, M.
AU  - Pejanović, Srđan
AU  - Perunicić, M.
AU  - Bošković-Vragolović, Nevenka
PY  - 2012
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/2006
AB  - In this paper substance transfer rate in the multistage system was investigated. Substance transfer between liquid and gas phases in a distillation packed column with packing was examined. Substance and heat transfer rate were examined and substance transfer coefficients were determined. Efficiency of substance transfer were examined by height of transfer units and volumetric substance transfer coefficients. Based on derived mathematical model the total height of transfer units and individual height of transfer units for the liquid and gas phases were determined. The investigation was performed by computer simulation and experiments. Several correlation models for height of transfer units and substance transfer coefficients were studied.
T2  - WSEAS Transactions on Heat and Mass Transfer
T1  - Material and heat transfer rate in the gas-lquid system
EP  - 121
IS  - 4
SP  - 112
VL  - 6
UR  - https://hdl.handle.net/21.15107/rcub_technorep_2006
ER  - 
@article{
author = "Mosorinac, T. and Ivanović-Knezević, M. and Pejanović, Srđan and Perunicić, M. and Bošković-Vragolović, Nevenka",
year = "2012",
abstract = "In this paper substance transfer rate in the multistage system was investigated. Substance transfer between liquid and gas phases in a distillation packed column with packing was examined. Substance and heat transfer rate were examined and substance transfer coefficients were determined. Efficiency of substance transfer were examined by height of transfer units and volumetric substance transfer coefficients. Based on derived mathematical model the total height of transfer units and individual height of transfer units for the liquid and gas phases were determined. The investigation was performed by computer simulation and experiments. Several correlation models for height of transfer units and substance transfer coefficients were studied.",
journal = "WSEAS Transactions on Heat and Mass Transfer",
title = "Material and heat transfer rate in the gas-lquid system",
pages = "121-112",
number = "4",
volume = "6",
url = "https://hdl.handle.net/21.15107/rcub_technorep_2006"
}
Mosorinac, T., Ivanović-Knezević, M., Pejanović, S., Perunicić, M.,& Bošković-Vragolović, N.. (2012). Material and heat transfer rate in the gas-lquid system. in WSEAS Transactions on Heat and Mass Transfer, 6(4), 112-121.
https://hdl.handle.net/21.15107/rcub_technorep_2006
Mosorinac T, Ivanović-Knezević M, Pejanović S, Perunicić M, Bošković-Vragolović N. Material and heat transfer rate in the gas-lquid system. in WSEAS Transactions on Heat and Mass Transfer. 2012;6(4):112-121.
https://hdl.handle.net/21.15107/rcub_technorep_2006 .
Mosorinac, T., Ivanović-Knezević, M., Pejanović, Srđan, Perunicić, M., Bošković-Vragolović, Nevenka, "Material and heat transfer rate in the gas-lquid system" in WSEAS Transactions on Heat and Mass Transfer, 6, no. 4 (2012):112-121,
https://hdl.handle.net/21.15107/rcub_technorep_2006 .

Diffusion of drugs from hydrogels and liposomes as drug carriers

Pjanović, Rada; Bošković-Vragolović, Nevenka; Veljković-Giga, Jelena; Garić-Grulović, Radmila; Pejanović, Srđan; Bugarski, Branko

(Wiley, Hoboken, 2010)

TY  - JOUR
AU  - Pjanović, Rada
AU  - Bošković-Vragolović, Nevenka
AU  - Veljković-Giga, Jelena
AU  - Garić-Grulović, Radmila
AU  - Pejanović, Srđan
AU  - Bugarski, Branko
PY  - 2010
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/1713
AB  - BACKGROUND: The mass transfer of model drugs Lidocaine hydrochloride and Dihydroquercetin from hydrogels (the usual carriers for topical drugs), and hydrogels containing liposomes, as novel drug vehicles, was studied. Diffusion experiments were performed using a Franz diffusion cell. Experimental data were used to calculate drug diffusion coefficients across membranes, and their effective diffusion coefficients from hydrogels and liposome containing hydrogels. For the first time the diffusion resistance of all drug carriers was determined from corresponding diffusion coefficients. The main aim of this work was the study of drug diffusion coefficients from liposomes and their comparison with related diffusion coefficients from hydrogels to find how liposomes contribute to prolonged and controlled drug release. RESULTS: Drug diffusion coefficients were: 1.38 . 10(-8)-m(2) s(-1) for Lidocaine hydrochloride and 5.96 . 10(-9)m(-2) s(-1) for Dihydroquercetin, while corresponding effective diffusion coefficients from hydrogels were: 7.82 . 10(-10)m(2) s(-1) and 7.98 . 10(-10)m(2) s(-1), respectively. Effective diffusion coefficients from liposome-containing hydrogels were:4.82 . 10(-10)m(2) s(-1) (Lidocaine hydrochloride) and 4.305 . 10(-10)m(2) s(-1) (Dihydroquercetin). Diffusion resistances for the two hydrogels were almost the same. Very similar values of diffusion resistances for all liposome dispersions were obtained. CONCLUSION: Calculated diffusion coefficients and resistances demonstrate that liposomes, as drug carriers, significantly affect diffusion rates. The results obtained could be used whenever diffusion-controlled drug release is required.
PB  - Wiley, Hoboken
T2  - Journal of Chemical Technology and Biotechnology
T1  - Diffusion of drugs from hydrogels and liposomes as drug carriers
EP  - 698
IS  - 5
SP  - 693
VL  - 85
DO  - 10.1002/jctb.2357
ER  - 
@article{
author = "Pjanović, Rada and Bošković-Vragolović, Nevenka and Veljković-Giga, Jelena and Garić-Grulović, Radmila and Pejanović, Srđan and Bugarski, Branko",
year = "2010",
abstract = "BACKGROUND: The mass transfer of model drugs Lidocaine hydrochloride and Dihydroquercetin from hydrogels (the usual carriers for topical drugs), and hydrogels containing liposomes, as novel drug vehicles, was studied. Diffusion experiments were performed using a Franz diffusion cell. Experimental data were used to calculate drug diffusion coefficients across membranes, and their effective diffusion coefficients from hydrogels and liposome containing hydrogels. For the first time the diffusion resistance of all drug carriers was determined from corresponding diffusion coefficients. The main aim of this work was the study of drug diffusion coefficients from liposomes and their comparison with related diffusion coefficients from hydrogels to find how liposomes contribute to prolonged and controlled drug release. RESULTS: Drug diffusion coefficients were: 1.38 . 10(-8)-m(2) s(-1) for Lidocaine hydrochloride and 5.96 . 10(-9)m(-2) s(-1) for Dihydroquercetin, while corresponding effective diffusion coefficients from hydrogels were: 7.82 . 10(-10)m(2) s(-1) and 7.98 . 10(-10)m(2) s(-1), respectively. Effective diffusion coefficients from liposome-containing hydrogels were:4.82 . 10(-10)m(2) s(-1) (Lidocaine hydrochloride) and 4.305 . 10(-10)m(2) s(-1) (Dihydroquercetin). Diffusion resistances for the two hydrogels were almost the same. Very similar values of diffusion resistances for all liposome dispersions were obtained. CONCLUSION: Calculated diffusion coefficients and resistances demonstrate that liposomes, as drug carriers, significantly affect diffusion rates. The results obtained could be used whenever diffusion-controlled drug release is required.",
publisher = "Wiley, Hoboken",
journal = "Journal of Chemical Technology and Biotechnology",
title = "Diffusion of drugs from hydrogels and liposomes as drug carriers",
pages = "698-693",
number = "5",
volume = "85",
doi = "10.1002/jctb.2357"
}
Pjanović, R., Bošković-Vragolović, N., Veljković-Giga, J., Garić-Grulović, R., Pejanović, S.,& Bugarski, B.. (2010). Diffusion of drugs from hydrogels and liposomes as drug carriers. in Journal of Chemical Technology and Biotechnology
Wiley, Hoboken., 85(5), 693-698.
https://doi.org/10.1002/jctb.2357
Pjanović R, Bošković-Vragolović N, Veljković-Giga J, Garić-Grulović R, Pejanović S, Bugarski B. Diffusion of drugs from hydrogels and liposomes as drug carriers. in Journal of Chemical Technology and Biotechnology. 2010;85(5):693-698.
doi:10.1002/jctb.2357 .
Pjanović, Rada, Bošković-Vragolović, Nevenka, Veljković-Giga, Jelena, Garić-Grulović, Radmila, Pejanović, Srđan, Bugarski, Branko, "Diffusion of drugs from hydrogels and liposomes as drug carriers" in Journal of Chemical Technology and Biotechnology, 85, no. 5 (2010):693-698,
https://doi.org/10.1002/jctb.2357 . .
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Diffusion of lidocaine hydrochloride from lipid microparticles

Pjanović, Rada; Stojanović, Radoslava; Šajber, Milana; Veljković, Jelena; Bošković-Vragolović, Nevenka; Pejanović, Srđan

(Association of the Chemical Engineers of Serbia, 2009)

TY  - JOUR
AU  - Pjanović, Rada
AU  - Stojanović, Radoslava
AU  - Šajber, Milana
AU  - Veljković, Jelena
AU  - Bošković-Vragolović, Nevenka
AU  - Pejanović, Srđan
PY  - 2009
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/1454
AB  - Lipid particles, as drug carriers, are of increasing research interest, because a sustained drug release and avoidance of side effects could be achieved by using them. Lidocaine hydrochloride is a very efficient local anesthetic, but it has a short effect. The objective was to prolong the effect of the drug by encapsulating lidocaine hydrochloride in phospholipids microparticles. Two different procedures were used for the preparation of phospholipids microparticles. In both cases, phosphatidylcholine and lysophosphatidylcholine were used for the preparation of microparticles in which 5 % w/w lidocaine hydrochloride solution was encapsulated. The standard Franz diffusion cell was used for the experimental diffusion rate determination. The obtained results show that diffusion rate from microparticles is significantly lower than from the lidocaine hydrochloride solution, which means that this kind of microparticles could be used for the prolonged drug release. There was no much difference in diffusion rates from microparticles obtained by different procedures. That indicates that only the composition of the particles membrane has an influence on the lidocaine hydrochloride release rate.
PB  - Association of the Chemical Engineers of Serbia
T2  - Chemical Industry & Chemical Engineering Quarterly
T1  - Diffusion of lidocaine hydrochloride from lipid microparticles
EP  - 35
IS  - 1
SP  - 33
VL  - 15
DO  - 10.2298/CICEQ0901033P
ER  - 
@article{
author = "Pjanović, Rada and Stojanović, Radoslava and Šajber, Milana and Veljković, Jelena and Bošković-Vragolović, Nevenka and Pejanović, Srđan",
year = "2009",
abstract = "Lipid particles, as drug carriers, are of increasing research interest, because a sustained drug release and avoidance of side effects could be achieved by using them. Lidocaine hydrochloride is a very efficient local anesthetic, but it has a short effect. The objective was to prolong the effect of the drug by encapsulating lidocaine hydrochloride in phospholipids microparticles. Two different procedures were used for the preparation of phospholipids microparticles. In both cases, phosphatidylcholine and lysophosphatidylcholine were used for the preparation of microparticles in which 5 % w/w lidocaine hydrochloride solution was encapsulated. The standard Franz diffusion cell was used for the experimental diffusion rate determination. The obtained results show that diffusion rate from microparticles is significantly lower than from the lidocaine hydrochloride solution, which means that this kind of microparticles could be used for the prolonged drug release. There was no much difference in diffusion rates from microparticles obtained by different procedures. That indicates that only the composition of the particles membrane has an influence on the lidocaine hydrochloride release rate.",
publisher = "Association of the Chemical Engineers of Serbia",
journal = "Chemical Industry & Chemical Engineering Quarterly",
title = "Diffusion of lidocaine hydrochloride from lipid microparticles",
pages = "35-33",
number = "1",
volume = "15",
doi = "10.2298/CICEQ0901033P"
}
Pjanović, R., Stojanović, R., Šajber, M., Veljković, J., Bošković-Vragolović, N.,& Pejanović, S.. (2009). Diffusion of lidocaine hydrochloride from lipid microparticles. in Chemical Industry & Chemical Engineering Quarterly
Association of the Chemical Engineers of Serbia., 15(1), 33-35.
https://doi.org/10.2298/CICEQ0901033P
Pjanović R, Stojanović R, Šajber M, Veljković J, Bošković-Vragolović N, Pejanović S. Diffusion of lidocaine hydrochloride from lipid microparticles. in Chemical Industry & Chemical Engineering Quarterly. 2009;15(1):33-35.
doi:10.2298/CICEQ0901033P .
Pjanović, Rada, Stojanović, Radoslava, Šajber, Milana, Veljković, Jelena, Bošković-Vragolović, Nevenka, Pejanović, Srđan, "Diffusion of lidocaine hydrochloride from lipid microparticles" in Chemical Industry & Chemical Engineering Quarterly, 15, no. 1 (2009):33-35,
https://doi.org/10.2298/CICEQ0901033P . .
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