Jaćimovski, Darko

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  • Jaćimovski, Darko (16)

Author's Bibliography

Mass transfer in inverse fluidized beds

Jaćimovski, Darko; Šućurović, Katarina; Đuriš, Mihal; Arsenijević, Zorana; Krstić, Sanja; Bošković-Vragolović, Nevenka

(Serbian Chemical Society, 2023)

TY  - JOUR
AU  - Jaćimovski, Darko
AU  - Šućurović, Katarina
AU  - Đuriš, Mihal
AU  - Arsenijević, Zorana
AU  - Krstić, Sanja
AU  - Bošković-Vragolović, Nevenka
PY  - 2023
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/7410
AB  - In this work, the coefficient of fluid-wall mass transfer in an inverse fluidized bed was determined using the adsorption method. The experiments were carried out in a column with a diameter of 45 mm with spherical and non-spherical particles of polypropylene and polyethylene with a diameter of 3.3-4.9 mm and a density of about 930 kg m-3. A diluted solution of methylene blue was used as a fluidization medium, which was adsorbed on part of the surface of the column on silica gel. The obtained results showed that the presence of particles during inverse fluidization does not contribute significantly to mass transfer compared to the influence of particles on transfer in conventional fluidized beds. Therefore, the pseudofluid concept was introduced into the analysis and an empirical correlation was performed to determine the mass transfer coefficient. The obtained results were compared with literature correlations for inverse and conventional fluidized beds.
AB  - У овом раду је одређиван коефицијент преноса масе флуид-зид у инверзнофлуидизованом слоју применом адсорпционе методе. Експерименти су вршени у колони  пречника 45 мм са сферичним и несферичним честицама полипропилена и полиетилена  пречника 3.3-4.9 мм и густине око 930 кг м-3. Као флуидизациони медијум коришћен је  разблажени раствор метиленски плавог који је адсорбован на делу површине колоне на  силикагелу. Добијени резултати показали су да присуство честица при инверзној  флуидизацији не доприноси значајно преносу масе у поређењу са утицајем честица на  пренос масе у конвенционално флуидизованим слојевима. Због тога је у анализу уведен  концепт псеудофлуида и изведена је емпиријска корелација за одређивање коефицијента  преноса масе. Извршено је поређење добијених резултата са литературним корелацијама за  инверзну и конвенционалну флуидизације.
PB  - Serbian Chemical Society
T2  - Journal of the Serbian Chemical Society
T1  - Mass transfer in inverse fluidized beds
T1  - Пренос масе у инверзно флуидизованом слоју
VL  - 88
IS  - 9
SP  - 905
EP  - 919
DO  - 10.2298/JSC230116016J
ER  - 
@article{
author = "Jaćimovski, Darko and Šućurović, Katarina and Đuriš, Mihal and Arsenijević, Zorana and Krstić, Sanja and Bošković-Vragolović, Nevenka",
year = "2023",
abstract = "In this work, the coefficient of fluid-wall mass transfer in an inverse fluidized bed was determined using the adsorption method. The experiments were carried out in a column with a diameter of 45 mm with spherical and non-spherical particles of polypropylene and polyethylene with a diameter of 3.3-4.9 mm and a density of about 930 kg m-3. A diluted solution of methylene blue was used as a fluidization medium, which was adsorbed on part of the surface of the column on silica gel. The obtained results showed that the presence of particles during inverse fluidization does not contribute significantly to mass transfer compared to the influence of particles on transfer in conventional fluidized beds. Therefore, the pseudofluid concept was introduced into the analysis and an empirical correlation was performed to determine the mass transfer coefficient. The obtained results were compared with literature correlations for inverse and conventional fluidized beds., У овом раду је одређиван коефицијент преноса масе флуид-зид у инверзнофлуидизованом слоју применом адсорпционе методе. Експерименти су вршени у колони  пречника 45 мм са сферичним и несферичним честицама полипропилена и полиетилена  пречника 3.3-4.9 мм и густине око 930 кг м-3. Као флуидизациони медијум коришћен је  разблажени раствор метиленски плавог који је адсорбован на делу површине колоне на  силикагелу. Добијени резултати показали су да присуство честица при инверзној  флуидизацији не доприноси значајно преносу масе у поређењу са утицајем честица на  пренос масе у конвенционално флуидизованим слојевима. Због тога је у анализу уведен  концепт псеудофлуида и изведена је емпиријска корелација за одређивање коефицијента  преноса масе. Извршено је поређење добијених резултата са литературним корелацијама за  инверзну и конвенционалну флуидизације.",
publisher = "Serbian Chemical Society",
journal = "Journal of the Serbian Chemical Society",
title = "Mass transfer in inverse fluidized beds, Пренос масе у инверзно флуидизованом слоју",
volume = "88",
number = "9",
pages = "905-919",
doi = "10.2298/JSC230116016J"
}
Jaćimovski, D., Šućurović, K., Đuriš, M., Arsenijević, Z., Krstić, S.,& Bošković-Vragolović, N.. (2023). Mass transfer in inverse fluidized beds. in Journal of the Serbian Chemical Society
Serbian Chemical Society., 88(9), 905-919.
https://doi.org/10.2298/JSC230116016J
Jaćimovski D, Šućurović K, Đuriš M, Arsenijević Z, Krstić S, Bošković-Vragolović N. Mass transfer in inverse fluidized beds. in Journal of the Serbian Chemical Society. 2023;88(9):905-919.
doi:10.2298/JSC230116016J .
Jaćimovski, Darko, Šućurović, Katarina, Đuriš, Mihal, Arsenijević, Zorana, Krstić, Sanja, Bošković-Vragolović, Nevenka, "Mass transfer in inverse fluidized beds" in Journal of the Serbian Chemical Society, 88, no. 9 (2023):905-919,
https://doi.org/10.2298/JSC230116016J . .

Supercapacitive properties of carbon materials activated by alkali metal hydroxides obtained from sucrose

Krstić, Sanja; Dodevski, Vladimir; Čebela, Maria; Rosić, Milena; Egerić, Marija; Vujasin, Radojka; Jaćimovski, Darko

(Belgrade : University of Belgrade, Institute for Multidisciplinary Research, 2023)

TY  - CONF
AU  - Krstić, Sanja
AU  - Dodevski, Vladimir
AU  - Čebela, Maria
AU  - Rosić, Milena
AU  - Egerić, Marija
AU  - Vujasin, Radojka
AU  - Jaćimovski, Darko
PY  - 2023
UR  - https://vinar.vin.bg.ac.rs/handle/123456789/11485
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/6622
AB  - The main aim of this research is to show influence of different hydroxides, applied in carbon materials activation process on the electrochemical properties of activated carbon samples. The carbon material samples were prepared by hydrothermal treatment of sucrose and thermally activated using KOH, NaOH and LiOH by chemical activation method. The electrochemical properties of the obtained carbon material samples were examined by cyclic voltammetry and electrochemical impedance spectroscopy and correlated to their physicochemical properties. Investigated samples showed characteristic capacitor-like behavior. The best result of specific capacitance was obtained for the sample synthesized treated by KOH, while the increase in capacitance follows the arrangement of the growth of ionic radius of a metal from an alkali which is used for activation. Dependence on the type of hydroxide is due to differences in the radii of a metal. The alkalis with larger radii of metal produce wider pores and consequently the structure of a porous layer become more accessible and available to the charge transfer of capacitive response.
PB  - Belgrade : University of Belgrade, Institute for Multidisciplinary Research
C3  - Programme and the Book of Abstracts / 7th Conference of The Serbian Society for Ceramic Materials, 7CSCS-2023, June 14-16, 2023 Belgrade
T1  - Supercapacitive properties of carbon materials activated by alkali metal hydroxides obtained from sucrose
SP  - 102
EP  - 102
UR  - https://hdl.handle.net/21.15107/rcub_vinar_11485
ER  - 
@conference{
author = "Krstić, Sanja and Dodevski, Vladimir and Čebela, Maria and Rosić, Milena and Egerić, Marija and Vujasin, Radojka and Jaćimovski, Darko",
year = "2023",
abstract = "The main aim of this research is to show influence of different hydroxides, applied in carbon materials activation process on the electrochemical properties of activated carbon samples. The carbon material samples were prepared by hydrothermal treatment of sucrose and thermally activated using KOH, NaOH and LiOH by chemical activation method. The electrochemical properties of the obtained carbon material samples were examined by cyclic voltammetry and electrochemical impedance spectroscopy and correlated to their physicochemical properties. Investigated samples showed characteristic capacitor-like behavior. The best result of specific capacitance was obtained for the sample synthesized treated by KOH, while the increase in capacitance follows the arrangement of the growth of ionic radius of a metal from an alkali which is used for activation. Dependence on the type of hydroxide is due to differences in the radii of a metal. The alkalis with larger radii of metal produce wider pores and consequently the structure of a porous layer become more accessible and available to the charge transfer of capacitive response.",
publisher = "Belgrade : University of Belgrade, Institute for Multidisciplinary Research",
journal = "Programme and the Book of Abstracts / 7th Conference of The Serbian Society for Ceramic Materials, 7CSCS-2023, June 14-16, 2023 Belgrade",
title = "Supercapacitive properties of carbon materials activated by alkali metal hydroxides obtained from sucrose",
pages = "102-102",
url = "https://hdl.handle.net/21.15107/rcub_vinar_11485"
}
Krstić, S., Dodevski, V., Čebela, M., Rosić, M., Egerić, M., Vujasin, R.,& Jaćimovski, D.. (2023). Supercapacitive properties of carbon materials activated by alkali metal hydroxides obtained from sucrose. in Programme and the Book of Abstracts / 7th Conference of The Serbian Society for Ceramic Materials, 7CSCS-2023, June 14-16, 2023 Belgrade
Belgrade : University of Belgrade, Institute for Multidisciplinary Research., 102-102.
https://hdl.handle.net/21.15107/rcub_vinar_11485
Krstić S, Dodevski V, Čebela M, Rosić M, Egerić M, Vujasin R, Jaćimovski D. Supercapacitive properties of carbon materials activated by alkali metal hydroxides obtained from sucrose. in Programme and the Book of Abstracts / 7th Conference of The Serbian Society for Ceramic Materials, 7CSCS-2023, June 14-16, 2023 Belgrade. 2023;:102-102.
https://hdl.handle.net/21.15107/rcub_vinar_11485 .
Krstić, Sanja, Dodevski, Vladimir, Čebela, Maria, Rosić, Milena, Egerić, Marija, Vujasin, Radojka, Jaćimovski, Darko, "Supercapacitive properties of carbon materials activated by alkali metal hydroxides obtained from sucrose" in Programme and the Book of Abstracts / 7th Conference of The Serbian Society for Ceramic Materials, 7CSCS-2023, June 14-16, 2023 Belgrade (2023):102-102,
https://hdl.handle.net/21.15107/rcub_vinar_11485 .

Mass transfer in inverse fluidized beds

Jaćimovski, Darko; Šućurović, Katarina; Đuriš, Mihal; Arsenijević, Zorana; Krstić, Sanja; Bošković-Vragolović, Nevenka

(Serbian Chemical Society, 2023)

TY  - JOUR
AU  - Jaćimovski, Darko
AU  - Šućurović, Katarina
AU  - Đuriš, Mihal
AU  - Arsenijević, Zorana
AU  - Krstić, Sanja
AU  - Bošković-Vragolović, Nevenka
PY  - 2023
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/6303
AB  - In this work, the coefficient of fluid-wall mass transfer in an inverse fluidized bed was determined using the adsorption method. The experiments were carried out in a column with a diameter of 45 mm with spherical and non-spherical particles of polypropylene and polyethylene with a diameter of 3.3-4.9 mm and a density of about 930 kg m-3. A diluted solution of methylene blue was used as a fluidization medium, which was adsorbed on part of the surface of the column on silica gel. The obtained results showed that the presence of particles during inverse fluidization does not contribute significantly to mass transfer compared to the influence of particles on transfer in conventional fluidized beds. Therefore, the pseudofluid concept was introduced into the analysis and an empirical correlation was performed to determine the mass transfer coefficient. The obtained results were compared with literature correlations for inverse and conventional fluidized beds.
AB  - У овом раду је одређиван коефицијент преноса масе флуид-зид у инверзнофлуидизованом слоју применом адсорпционе методе. Експерименти су вршени у колони  пречника 45 мм са сферичним и несферичним честицама полипропилена и полиетилена  пречника 3.3-4.9 мм и густине око 930 кг м-3. Као флуидизациони медијум коришћен је  разблажени раствор метиленски плавог који је адсорбован на делу површине колоне на  силикагелу. Добијени резултати показали су да присуство честица при инверзној  флуидизацији не доприноси значајно преносу масе у поређењу са утицајем честица на  пренос масе у конвенционално флуидизованим слојевима. Због тога је у анализу уведен  концепт псеудофлуида и изведена је емпиријска корелација за одређивање коефицијента  преноса масе. Извршено је поређење добијених резултата са литературним корелацијама за  инверзну и конвенционалну флуидизације.
PB  - Serbian Chemical Society
T2  - Journal of the Serbian Chemical Society
T1  - Mass transfer in inverse fluidized beds
T1  - Пренос масе у инверзно флуидизованом слоју
VL  - 88
IS  - 9
SP  - 905
EP  - 919
DO  - 10.2298/JSC230116016J
ER  - 
@article{
author = "Jaćimovski, Darko and Šućurović, Katarina and Đuriš, Mihal and Arsenijević, Zorana and Krstić, Sanja and Bošković-Vragolović, Nevenka",
year = "2023",
abstract = "In this work, the coefficient of fluid-wall mass transfer in an inverse fluidized bed was determined using the adsorption method. The experiments were carried out in a column with a diameter of 45 mm with spherical and non-spherical particles of polypropylene and polyethylene with a diameter of 3.3-4.9 mm and a density of about 930 kg m-3. A diluted solution of methylene blue was used as a fluidization medium, which was adsorbed on part of the surface of the column on silica gel. The obtained results showed that the presence of particles during inverse fluidization does not contribute significantly to mass transfer compared to the influence of particles on transfer in conventional fluidized beds. Therefore, the pseudofluid concept was introduced into the analysis and an empirical correlation was performed to determine the mass transfer coefficient. The obtained results were compared with literature correlations for inverse and conventional fluidized beds., У овом раду је одређиван коефицијент преноса масе флуид-зид у инверзнофлуидизованом слоју применом адсорпционе методе. Експерименти су вршени у колони  пречника 45 мм са сферичним и несферичним честицама полипропилена и полиетилена  пречника 3.3-4.9 мм и густине око 930 кг м-3. Као флуидизациони медијум коришћен је  разблажени раствор метиленски плавог који је адсорбован на делу површине колоне на  силикагелу. Добијени резултати показали су да присуство честица при инверзној  флуидизацији не доприноси значајно преносу масе у поређењу са утицајем честица на  пренос масе у конвенционално флуидизованим слојевима. Због тога је у анализу уведен  концепт псеудофлуида и изведена је емпиријска корелација за одређивање коефицијента  преноса масе. Извршено је поређење добијених резултата са литературним корелацијама за  инверзну и конвенционалну флуидизације.",
publisher = "Serbian Chemical Society",
journal = "Journal of the Serbian Chemical Society",
title = "Mass transfer in inverse fluidized beds, Пренос масе у инверзно флуидизованом слоју",
volume = "88",
number = "9",
pages = "905-919",
doi = "10.2298/JSC230116016J"
}
Jaćimovski, D., Šućurović, K., Đuriš, M., Arsenijević, Z., Krstić, S.,& Bošković-Vragolović, N.. (2023). Mass transfer in inverse fluidized beds. in Journal of the Serbian Chemical Society
Serbian Chemical Society., 88(9), 905-919.
https://doi.org/10.2298/JSC230116016J
Jaćimovski D, Šućurović K, Đuriš M, Arsenijević Z, Krstić S, Bošković-Vragolović N. Mass transfer in inverse fluidized beds. in Journal of the Serbian Chemical Society. 2023;88(9):905-919.
doi:10.2298/JSC230116016J .
Jaćimovski, Darko, Šućurović, Katarina, Đuriš, Mihal, Arsenijević, Zorana, Krstić, Sanja, Bošković-Vragolović, Nevenka, "Mass transfer in inverse fluidized beds" in Journal of the Serbian Chemical Society, 88, no. 9 (2023):905-919,
https://doi.org/10.2298/JSC230116016J . .

Minimum fluidization velocity and bed expansion of the inverse fluidized bed

Šućurović, Katarina; Jaćimovski, Darko; Đuriš, Mihal; Arsenijević, Zorana; Bošković-Vragolović, Nevenka

(Taylor & Francis, 2023)

TY  - JOUR
AU  - Šućurović, Katarina
AU  - Jaćimovski, Darko
AU  - Đuriš, Mihal
AU  - Arsenijević, Zorana
AU  - Bošković-Vragolović, Nevenka
PY  - 2023
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/5956
AB  - To define the fluid-dynamic properties of inverse fluidized beds, studies of the minimum fluidization velocity and bed expansion were performed in this work. The experiments were performed in
an inverse fluidized bed of polypropylene and polystyrene particles in a cylindrical column using
water and an aqueous glycerol solution of different concentrations as fluidizing medium. The
dependence of the bed porosity on the superficial velocity of the fluid was determined experimentally for all the particles studied and different fluidizing media. The influence of fluidizing
medium viscosity and particle density on the expansion of the inverse fluidized bed and on the
minimum fluidization velocity was investigated. Comparison of the experimental data for the
expansion of the inverse fluidized bed and the values calculated by the Richardson-Zaki
correlation for the conventional fluidized bed showed some deviation, but the experimentally
determined data were found to follow the shape of the Richardson-Zaki curve. In this paper, a
correlation for the expansion of inverse fluidized beds is proposed
PB  - Taylor & Francis
T2  - Particulate Science and Technology
T1  - Minimum fluidization velocity and bed expansion of the inverse fluidized bed
DO  - 10.1080/02726351.2023.2182732
ER  - 
@article{
author = "Šućurović, Katarina and Jaćimovski, Darko and Đuriš, Mihal and Arsenijević, Zorana and Bošković-Vragolović, Nevenka",
year = "2023",
abstract = "To define the fluid-dynamic properties of inverse fluidized beds, studies of the minimum fluidization velocity and bed expansion were performed in this work. The experiments were performed in
an inverse fluidized bed of polypropylene and polystyrene particles in a cylindrical column using
water and an aqueous glycerol solution of different concentrations as fluidizing medium. The
dependence of the bed porosity on the superficial velocity of the fluid was determined experimentally for all the particles studied and different fluidizing media. The influence of fluidizing
medium viscosity and particle density on the expansion of the inverse fluidized bed and on the
minimum fluidization velocity was investigated. Comparison of the experimental data for the
expansion of the inverse fluidized bed and the values calculated by the Richardson-Zaki
correlation for the conventional fluidized bed showed some deviation, but the experimentally
determined data were found to follow the shape of the Richardson-Zaki curve. In this paper, a
correlation for the expansion of inverse fluidized beds is proposed",
publisher = "Taylor & Francis",
journal = "Particulate Science and Technology",
title = "Minimum fluidization velocity and bed expansion of the inverse fluidized bed",
doi = "10.1080/02726351.2023.2182732"
}
Šućurović, K., Jaćimovski, D., Đuriš, M., Arsenijević, Z.,& Bošković-Vragolović, N.. (2023). Minimum fluidization velocity and bed expansion of the inverse fluidized bed. in Particulate Science and Technology
Taylor & Francis..
https://doi.org/10.1080/02726351.2023.2182732
Šućurović K, Jaćimovski D, Đuriš M, Arsenijević Z, Bošković-Vragolović N. Minimum fluidization velocity and bed expansion of the inverse fluidized bed. in Particulate Science and Technology. 2023;.
doi:10.1080/02726351.2023.2182732 .
Šućurović, Katarina, Jaćimovski, Darko, Đuriš, Mihal, Arsenijević, Zorana, Bošković-Vragolović, Nevenka, "Minimum fluidization velocity and bed expansion of the inverse fluidized bed" in Particulate Science and Technology (2023),
https://doi.org/10.1080/02726351.2023.2182732 . .

Heat transfer by liquid convection in particulate fluidized beds

Jaćimovski, Darko; Brzić, Danica; Garić Grulović, Radmila; Pjanović, Rada; Đuriš, Mihal; Arsenijević, Zorana; Bošković-Vragolović, Nevenka

(Belgrade : Serbian Chemical Society, 2022)

TY  - JOUR
AU  - Jaćimovski, Darko
AU  - Brzić, Danica
AU  - Garić Grulović, Radmila
AU  - Pjanović, Rada
AU  - Đuriš, Mihal
AU  - Arsenijević, Zorana
AU  - Bošković-Vragolović, Nevenka
PY  - 2022
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/5248
AB  - In this work the theoretical model for heat transfer from a wall to aliquid-solid fluidized bed by liquid convective mechanism has been proposed.The model is based on thickness of boundary layer and film theory. The keyparameter in the model is the distance between two adjacent particles whichcollide with the wall. According to the proposed model, the liquid convectiveheat transfer in a fluidized bed is 4 to 5 times more intense than in a single-phaseflow. Additionally, the wall-to-bed heat transfer coefficient has been measuredexperimentally in water –glass particles fluidized bed, for different particle sizes.Comparison of the model prediction with experimental data has shown that sizeof the particles strongly influences the mechanism of heat transfer. For fineparticles of 0.8 mm in diameter, the liquid convective heat transfer modelrepresents adequately the experimental data, indicating that particle convectivemechanism is negligible. For coarse particles of 1.5 - 2 mm in diameter, theliquid convective heat transfer mechanism accounts for 60 % of the overall heattransfer coefficient
AB  - У овом раду развијен је теоријски модел преноса топлоте конвективним механизмомса зида колоне на течност у партикулативно флуидизованом слоју. Модел је заснован надебљини граничног слоја и теорији филма. Кључни параметар модела је растојање измеђудвe суседне честице које се сударају са зидом колоне. Према предложеном моделу преностоплоте конвекцијом на течност у флуидизованом слоју је 4 до 5 пута интензивнији него уједнофазном току. Коефицијенти преноса топлоте су експериментално одређени уфлуидизованом слоју вода-стаклене сфере, за различите пречнике честица. Поређењеексперименталних резултата и предвиђања модела је показало да пречник честица значајноутиче на механизам преноса топлоте. За веома ситне честице пречника 0.8 mm, моделпреноса топлоте конвекцијом на течност у потпуности репрезентује експерименталнерезултате, указујући да је пренос топлоте честицама занемарљив. За крупне честице,пречника 1.5 -2 mm, конвективни пренос на течност чини 60 % од укупног коефицијентапреноса топлоте
PB  - Belgrade : Serbian Chemical Society
T2  - Journal of the Serbian Chemical Society
T1  - Heat transfer by liquid convection in particulate fluidized beds
T1  - Пренос топлоте конвективним механизмом у партикулативно флуидизованом слоју
VL  - 87
IS  - 7-8
SP  - 911
EP  - 924
DO  - 10.2298/JSC211216020J
ER  - 
@article{
author = "Jaćimovski, Darko and Brzić, Danica and Garić Grulović, Radmila and Pjanović, Rada and Đuriš, Mihal and Arsenijević, Zorana and Bošković-Vragolović, Nevenka",
year = "2022",
abstract = "In this work the theoretical model for heat transfer from a wall to aliquid-solid fluidized bed by liquid convective mechanism has been proposed.The model is based on thickness of boundary layer and film theory. The keyparameter in the model is the distance between two adjacent particles whichcollide with the wall. According to the proposed model, the liquid convectiveheat transfer in a fluidized bed is 4 to 5 times more intense than in a single-phaseflow. Additionally, the wall-to-bed heat transfer coefficient has been measuredexperimentally in water –glass particles fluidized bed, for different particle sizes.Comparison of the model prediction with experimental data has shown that sizeof the particles strongly influences the mechanism of heat transfer. For fineparticles of 0.8 mm in diameter, the liquid convective heat transfer modelrepresents adequately the experimental data, indicating that particle convectivemechanism is negligible. For coarse particles of 1.5 - 2 mm in diameter, theliquid convective heat transfer mechanism accounts for 60 % of the overall heattransfer coefficient, У овом раду развијен је теоријски модел преноса топлоте конвективним механизмомса зида колоне на течност у партикулативно флуидизованом слоју. Модел је заснован надебљини граничног слоја и теорији филма. Кључни параметар модела је растојање измеђудвe суседне честице које се сударају са зидом колоне. Према предложеном моделу преностоплоте конвекцијом на течност у флуидизованом слоју је 4 до 5 пута интензивнији него уједнофазном току. Коефицијенти преноса топлоте су експериментално одређени уфлуидизованом слоју вода-стаклене сфере, за различите пречнике честица. Поређењеексперименталних резултата и предвиђања модела је показало да пречник честица значајноутиче на механизам преноса топлоте. За веома ситне честице пречника 0.8 mm, моделпреноса топлоте конвекцијом на течност у потпуности репрезентује експерименталнерезултате, указујући да је пренос топлоте честицама занемарљив. За крупне честице,пречника 1.5 -2 mm, конвективни пренос на течност чини 60 % од укупног коефицијентапреноса топлоте",
publisher = "Belgrade : Serbian Chemical Society",
journal = "Journal of the Serbian Chemical Society",
title = "Heat transfer by liquid convection in particulate fluidized beds, Пренос топлоте конвективним механизмом у партикулативно флуидизованом слоју",
volume = "87",
number = "7-8",
pages = "911-924",
doi = "10.2298/JSC211216020J"
}
Jaćimovski, D., Brzić, D., Garić Grulović, R., Pjanović, R., Đuriš, M., Arsenijević, Z.,& Bošković-Vragolović, N.. (2022). Heat transfer by liquid convection in particulate fluidized beds. in Journal of the Serbian Chemical Society
Belgrade : Serbian Chemical Society., 87(7-8), 911-924.
https://doi.org/10.2298/JSC211216020J
Jaćimovski D, Brzić D, Garić Grulović R, Pjanović R, Đuriš M, Arsenijević Z, Bošković-Vragolović N. Heat transfer by liquid convection in particulate fluidized beds. in Journal of the Serbian Chemical Society. 2022;87(7-8):911-924.
doi:10.2298/JSC211216020J .
Jaćimovski, Darko, Brzić, Danica, Garić Grulović, Radmila, Pjanović, Rada, Đuriš, Mihal, Arsenijević, Zorana, Bošković-Vragolović, Nevenka, "Heat transfer by liquid convection in particulate fluidized beds" in Journal of the Serbian Chemical Society, 87, no. 7-8 (2022):911-924,
https://doi.org/10.2298/JSC211216020J . .

Movement and velocity of a particle in an inverse fluidized bed

Jaćimovski, Darko; Šućurović, Katarina; Đuriš, Mihal; Arsenijević, Zorana; Bošković-Vragolović, Nevenka

(Informa UK Limited, 2022)

TY  - JOUR
AU  - Jaćimovski, Darko
AU  - Šućurović, Katarina
AU  - Đuriš, Mihal
AU  - Arsenijević, Zorana
AU  - Bošković-Vragolović, Nevenka
PY  - 2022
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/5620
AB  - The movement of particles in the fluidized bed primarily determines the mixing in the bed and determines the transfer intensities that occur between the particles and the fluid. Experimental monitoring of the velocity of the marked particle was performed in an inversely fluidized bed of polypropylene, polyethylene, and polystyrene particles. The velocity of the marked particle was monitored in a two-dimensional column, where water and an aqueous solution of glycerin were used as the fluidization medium. Using the Tracker Video Analysis program (Tracker Video Analysis, Open Source Physics, 2003), the mean velocity of the marked particle was determined, as well as the distance crossed by the marked particle in the x and y directions. The influence of fluidization medium viscosity and particle density on the velocity of the marked particle was investigated. The results of experimental investigations have shown that the particle velocity distribution approximately follows the Maxwell distribution. Comparison of the measured values of the mean velocity in the inversely and conventionally fluidized bed showed a certain deviation. In this paper, a correlation for determining the mean particle velocity in an inversely fluidized bed is proposed.
PB  - Informa UK Limited
T2  - Particulate Science and Technology
T1  - Movement and velocity of a particle in an inverse fluidized bed
DO  - 10.1080/02726351.2022.2119625
ER  - 
@article{
author = "Jaćimovski, Darko and Šućurović, Katarina and Đuriš, Mihal and Arsenijević, Zorana and Bošković-Vragolović, Nevenka",
year = "2022",
abstract = "The movement of particles in the fluidized bed primarily determines the mixing in the bed and determines the transfer intensities that occur between the particles and the fluid. Experimental monitoring of the velocity of the marked particle was performed in an inversely fluidized bed of polypropylene, polyethylene, and polystyrene particles. The velocity of the marked particle was monitored in a two-dimensional column, where water and an aqueous solution of glycerin were used as the fluidization medium. Using the Tracker Video Analysis program (Tracker Video Analysis, Open Source Physics, 2003), the mean velocity of the marked particle was determined, as well as the distance crossed by the marked particle in the x and y directions. The influence of fluidization medium viscosity and particle density on the velocity of the marked particle was investigated. The results of experimental investigations have shown that the particle velocity distribution approximately follows the Maxwell distribution. Comparison of the measured values of the mean velocity in the inversely and conventionally fluidized bed showed a certain deviation. In this paper, a correlation for determining the mean particle velocity in an inversely fluidized bed is proposed.",
publisher = "Informa UK Limited",
journal = "Particulate Science and Technology",
title = "Movement and velocity of a particle in an inverse fluidized bed",
doi = "10.1080/02726351.2022.2119625"
}
Jaćimovski, D., Šućurović, K., Đuriš, M., Arsenijević, Z.,& Bošković-Vragolović, N.. (2022). Movement and velocity of a particle in an inverse fluidized bed. in Particulate Science and Technology
Informa UK Limited..
https://doi.org/10.1080/02726351.2022.2119625
Jaćimovski D, Šućurović K, Đuriš M, Arsenijević Z, Bošković-Vragolović N. Movement and velocity of a particle in an inverse fluidized bed. in Particulate Science and Technology. 2022;.
doi:10.1080/02726351.2022.2119625 .
Jaćimovski, Darko, Šućurović, Katarina, Đuriš, Mihal, Arsenijević, Zorana, Bošković-Vragolović, Nevenka, "Movement and velocity of a particle in an inverse fluidized bed" in Particulate Science and Technology (2022),
https://doi.org/10.1080/02726351.2022.2119625 . .
3
3

Investigation of the dynamics of fluidized bed granulation process

Kaluđerović-Radoičić, Tatjana; Đuriš, Mihal; Jaćimovski, Darko; Arsenijević, Zorana

(Serbian Chemical Society, Belgrade / Srpsko hemijsko društvo, Beograd, 2019)

TY  - CONF
AU  - Kaluđerović-Radoičić, Tatjana
AU  - Đuriš, Mihal
AU  - Jaćimovski, Darko
AU  - Arsenijević, Zorana
PY  - 2019
UR  - https://www.shd.org.rs/index.php/abstracts-56
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3293
AB  - In this paper, experimental investigation of the dynamics of the process of fluidized bed granulation was performed, in order to find optimal process conditions and binder concentration to achieve the desired granules development. The experiments were performed in batch system using corn flour as starting material. Ten experiments were performed in which sucrose solution of different concentrations (20, 30, 35 and 40 %) was used as binder. The temperature of the system was kept constant during the granulation process and amounted to 40-50°C. Samples were taken from the fluidized bed at time intervals of 3 min. The dynamics of granulation was examined by determining three different factors (bulk density, moisure content and particle size distribution) for each of the samples. It has been found that bulk density continuously decreases during the granulation process, while in the drying phase it remains constant. Particle size distribution has shown that the average diameter of the projected surface increases uniformly during the process. By comparing all of the three investigated factors, it was shown that the best quality of granules is achieved using 35 % sucrose solution .
AB  - U ovom radu izvršeno je eksperimentalno ispitivanje procesa mokre granulacije u fluidizovanom sloju u cilju pronalaženja optimalnih uslova izvođenja procesa i sastava veziva kojim će se ostvariti željena dinamika razvoja granula. Ispitivanje je izvršeno u šaržnom sistemu, a korišćeno je kukuruzno brašno kao polazni materijal. Izvršeno je 10 eksperimenata u kojima je kao vezivno sredstvo korišćen rastvor saharoze različitih koncentracija: 20, 30, 35 i 40 %. Temperatura je održavana konstantnom tokom procesa granulacije i iznosila je 40-50C. Uzorci su iz sloja uzimani u jednakim vremenskim intervalima od 3 min. Dinamika granulacije ispitivana je određivanjem tri različita faktora (nasipne gustina, vlažnosti i raspodele veličine čestica) za svaki od uzoraka. Utvrđeno je da nasipna gustina kontinualno opada tokom izvođenja procesa granulacije, dok u fazi sušenja ostaje konstantna. Raspodela veličina čestica je pokazala da srednji prečnik projektovane površine ravnomerno raste tokom procesa. Poređenjem sva tri ispitivana faktora pokazano je da se najbolji kvalitet granula postiže korišćenjem 35 % rastvora saharoze kao vezivnog sredstva.
PB  - Serbian Chemical Society, Belgrade / Srpsko hemijsko društvo, Beograd
C3  - 56th Meeting of the Serbian chemical Society - Book of Abstracts / 56. Savetovanje Srpskog hemijskog društva - Kratki izvodi radova, Niš 7-8.9. 2019.
T1  - Investigation of the dynamics of fluidized bed granulation process
T1  - Ispitivanje dinamike granulacije praškastih materijala u fluidizovanom sloju
SP  - 36
UR  - https://hdl.handle.net/21.15107/rcub_cer_3293
ER  - 
@conference{
author = "Kaluđerović-Radoičić, Tatjana and Đuriš, Mihal and Jaćimovski, Darko and Arsenijević, Zorana",
year = "2019",
abstract = "In this paper, experimental investigation of the dynamics of the process of fluidized bed granulation was performed, in order to find optimal process conditions and binder concentration to achieve the desired granules development. The experiments were performed in batch system using corn flour as starting material. Ten experiments were performed in which sucrose solution of different concentrations (20, 30, 35 and 40 %) was used as binder. The temperature of the system was kept constant during the granulation process and amounted to 40-50°C. Samples were taken from the fluidized bed at time intervals of 3 min. The dynamics of granulation was examined by determining three different factors (bulk density, moisure content and particle size distribution) for each of the samples. It has been found that bulk density continuously decreases during the granulation process, while in the drying phase it remains constant. Particle size distribution has shown that the average diameter of the projected surface increases uniformly during the process. By comparing all of the three investigated factors, it was shown that the best quality of granules is achieved using 35 % sucrose solution ., U ovom radu izvršeno je eksperimentalno ispitivanje procesa mokre granulacije u fluidizovanom sloju u cilju pronalaženja optimalnih uslova izvođenja procesa i sastava veziva kojim će se ostvariti željena dinamika razvoja granula. Ispitivanje je izvršeno u šaržnom sistemu, a korišćeno je kukuruzno brašno kao polazni materijal. Izvršeno je 10 eksperimenata u kojima je kao vezivno sredstvo korišćen rastvor saharoze različitih koncentracija: 20, 30, 35 i 40 %. Temperatura je održavana konstantnom tokom procesa granulacije i iznosila je 40-50C. Uzorci su iz sloja uzimani u jednakim vremenskim intervalima od 3 min. Dinamika granulacije ispitivana je određivanjem tri različita faktora (nasipne gustina, vlažnosti i raspodele veličine čestica) za svaki od uzoraka. Utvrđeno je da nasipna gustina kontinualno opada tokom izvođenja procesa granulacije, dok u fazi sušenja ostaje konstantna. Raspodela veličina čestica je pokazala da srednji prečnik projektovane površine ravnomerno raste tokom procesa. Poređenjem sva tri ispitivana faktora pokazano je da se najbolji kvalitet granula postiže korišćenjem 35 % rastvora saharoze kao vezivnog sredstva.",
publisher = "Serbian Chemical Society, Belgrade / Srpsko hemijsko društvo, Beograd",
journal = "56th Meeting of the Serbian chemical Society - Book of Abstracts / 56. Savetovanje Srpskog hemijskog društva - Kratki izvodi radova, Niš 7-8.9. 2019.",
title = "Investigation of the dynamics of fluidized bed granulation process, Ispitivanje dinamike granulacije praškastih materijala u fluidizovanom sloju",
pages = "36",
url = "https://hdl.handle.net/21.15107/rcub_cer_3293"
}
Kaluđerović-Radoičić, T., Đuriš, M., Jaćimovski, D.,& Arsenijević, Z.. (2019). Investigation of the dynamics of fluidized bed granulation process. in 56th Meeting of the Serbian chemical Society - Book of Abstracts / 56. Savetovanje Srpskog hemijskog društva - Kratki izvodi radova, Niš 7-8.9. 2019.
Serbian Chemical Society, Belgrade / Srpsko hemijsko društvo, Beograd., 36.
https://hdl.handle.net/21.15107/rcub_cer_3293
Kaluđerović-Radoičić T, Đuriš M, Jaćimovski D, Arsenijević Z. Investigation of the dynamics of fluidized bed granulation process. in 56th Meeting of the Serbian chemical Society - Book of Abstracts / 56. Savetovanje Srpskog hemijskog društva - Kratki izvodi radova, Niš 7-8.9. 2019.. 2019;:36.
https://hdl.handle.net/21.15107/rcub_cer_3293 .
Kaluđerović-Radoičić, Tatjana, Đuriš, Mihal, Jaćimovski, Darko, Arsenijević, Zorana, "Investigation of the dynamics of fluidized bed granulation process" in 56th Meeting of the Serbian chemical Society - Book of Abstracts / 56. Savetovanje Srpskog hemijskog društva - Kratki izvodi radova, Niš 7-8.9. 2019. (2019):36,
https://hdl.handle.net/21.15107/rcub_cer_3293 .

Investigation of the dynamics of fluidized bed granulation process

Kaluđerović-Radoičić, Tatjana; Đuriš, Mihal; Jaćimovski, Darko; Arsenijević, Zorana

(Serbian Chemical Society, Belgrade / Srpsko hemijsko društvo, Beograd, 2019)

TY  - CONF
AU  - Kaluđerović-Radoičić, Tatjana
AU  - Đuriš, Mihal
AU  - Jaćimovski, Darko
AU  - Arsenijević, Zorana
PY  - 2019
UR  - https://www.shd.org.rs/index.php/proceedings-56
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3303
AB  - In this paper, experimental investigation of the dynamics of the process of fluidized bed granulation was performed, in order to find optimal process conditions and binder concentration to achieve the desired granules development. The experiments were performed in batch system using corn flour as starting material. Ten experiments were performed in which sucrose solution of different concentrations (20, 30, 35 and 40 %) was used as binder. The temperature of the system was kept constant during the granulation process and amounted to 40-50°C. Samples were taken from the fluidized bed at time intervals of 3 min. The dynamics of granulation was examined by determining three different factors (bulk density, moisure content and particle size distribution) for each of the samples. It has been found that bulk density continuously decreases during the granulation process, while in the drying phase it remains constant. Particle size distribution has shown that the average diameter of the projected surface increases uniformly during the process. By comparing all of the three investigated factors, it was shown that the best quality of granules is achieved using 35 % sucrose solution .
AB  - U ovom radu izvršeno je eksperimentalno ispitivanje procesa mokre granulacije u fluidizovanom sloju u cilju pronalaženja optimalnih uslova izvođenja procesa i sastava veziva kojim će se ostvariti željena dinamika razvoja granula. Ispitivanje je izvršeno u šaržnom sistemu, a korišćeno je kukuruzno brašno kao polazni materijal. Izvršeno je 10 eksperimenata u kojima je kao vezivno sredstvo korišćen rastvor saharoze različitih koncentracija: 20, 30, 35 i 40 %. Temperatura je održavana konstantnom tokom procesa granulacije i iznosila je 40-50C. Uzorci su iz sloja uzimani u jednakim vremenskim intervalima od 3 min. Dinamika granulacije ispitivana je određivanjem tri različita faktora (nasipne gustina, vlažnosti i raspodele veličine čestica) za svaki od uzoraka. Utvrđeno je da nasipna gustina kontinualno opada tokom izvođenja procesa granulacije, dok u fazi sušenja ostaje konstantna. Raspodela veličina čestica je pokazala da srednji prečnik projektovane površine ravnomerno raste tokom procesa. Poređenjem sva tri ispitivana faktora pokazano je da se najbolji kvalitet granula postiže korišćenjem 35 % rastvora saharoze kao vezivnog sredstva.
PB  - Serbian Chemical Society, Belgrade / Srpsko hemijsko društvo, Beograd
C3  - 56th Meeting of the Serbian chemical Society - Proceedings / 56. Savetovanje Srpskog hemijskog društva - Knjiga radova, Niš 7-8.9. 2019.
T1  - Investigation of the dynamics of fluidized bed granulation process
T1  - Ispitivanje dinamike granulacije praškastih materijala u fluidizovanom sloju
SP  - 55
EP  - 59
UR  - https://hdl.handle.net/21.15107/rcub_cer_3303
ER  - 
@conference{
author = "Kaluđerović-Radoičić, Tatjana and Đuriš, Mihal and Jaćimovski, Darko and Arsenijević, Zorana",
year = "2019",
abstract = "In this paper, experimental investigation of the dynamics of the process of fluidized bed granulation was performed, in order to find optimal process conditions and binder concentration to achieve the desired granules development. The experiments were performed in batch system using corn flour as starting material. Ten experiments were performed in which sucrose solution of different concentrations (20, 30, 35 and 40 %) was used as binder. The temperature of the system was kept constant during the granulation process and amounted to 40-50°C. Samples were taken from the fluidized bed at time intervals of 3 min. The dynamics of granulation was examined by determining three different factors (bulk density, moisure content and particle size distribution) for each of the samples. It has been found that bulk density continuously decreases during the granulation process, while in the drying phase it remains constant. Particle size distribution has shown that the average diameter of the projected surface increases uniformly during the process. By comparing all of the three investigated factors, it was shown that the best quality of granules is achieved using 35 % sucrose solution ., U ovom radu izvršeno je eksperimentalno ispitivanje procesa mokre granulacije u fluidizovanom sloju u cilju pronalaženja optimalnih uslova izvođenja procesa i sastava veziva kojim će se ostvariti željena dinamika razvoja granula. Ispitivanje je izvršeno u šaržnom sistemu, a korišćeno je kukuruzno brašno kao polazni materijal. Izvršeno je 10 eksperimenata u kojima je kao vezivno sredstvo korišćen rastvor saharoze različitih koncentracija: 20, 30, 35 i 40 %. Temperatura je održavana konstantnom tokom procesa granulacije i iznosila je 40-50C. Uzorci su iz sloja uzimani u jednakim vremenskim intervalima od 3 min. Dinamika granulacije ispitivana je određivanjem tri različita faktora (nasipne gustina, vlažnosti i raspodele veličine čestica) za svaki od uzoraka. Utvrđeno je da nasipna gustina kontinualno opada tokom izvođenja procesa granulacije, dok u fazi sušenja ostaje konstantna. Raspodela veličina čestica je pokazala da srednji prečnik projektovane površine ravnomerno raste tokom procesa. Poređenjem sva tri ispitivana faktora pokazano je da se najbolji kvalitet granula postiže korišćenjem 35 % rastvora saharoze kao vezivnog sredstva.",
publisher = "Serbian Chemical Society, Belgrade / Srpsko hemijsko društvo, Beograd",
journal = "56th Meeting of the Serbian chemical Society - Proceedings / 56. Savetovanje Srpskog hemijskog društva - Knjiga radova, Niš 7-8.9. 2019.",
title = "Investigation of the dynamics of fluidized bed granulation process, Ispitivanje dinamike granulacije praškastih materijala u fluidizovanom sloju",
pages = "55-59",
url = "https://hdl.handle.net/21.15107/rcub_cer_3303"
}
Kaluđerović-Radoičić, T., Đuriš, M., Jaćimovski, D.,& Arsenijević, Z.. (2019). Investigation of the dynamics of fluidized bed granulation process. in 56th Meeting of the Serbian chemical Society - Proceedings / 56. Savetovanje Srpskog hemijskog društva - Knjiga radova, Niš 7-8.9. 2019.
Serbian Chemical Society, Belgrade / Srpsko hemijsko društvo, Beograd., 55-59.
https://hdl.handle.net/21.15107/rcub_cer_3303
Kaluđerović-Radoičić T, Đuriš M, Jaćimovski D, Arsenijević Z. Investigation of the dynamics of fluidized bed granulation process. in 56th Meeting of the Serbian chemical Society - Proceedings / 56. Savetovanje Srpskog hemijskog društva - Knjiga radova, Niš 7-8.9. 2019.. 2019;:55-59.
https://hdl.handle.net/21.15107/rcub_cer_3303 .
Kaluđerović-Radoičić, Tatjana, Đuriš, Mihal, Jaćimovski, Darko, Arsenijević, Zorana, "Investigation of the dynamics of fluidized bed granulation process" in 56th Meeting of the Serbian chemical Society - Proceedings / 56. Savetovanje Srpskog hemijskog društva - Knjiga radova, Niš 7-8.9. 2019. (2019):55-59,
https://hdl.handle.net/21.15107/rcub_cer_3303 .

High efficiency disperse dryer - an innovative process for drying of solutions, suspensions and pastes in a fluidized bed of inert particles

Đuriš, Mihal; Kaluđerović-Radoičić, Tatjana; Jaćimovski, Darko; Arsenijević, Zorana

(Belgrade : Association of Chemical Engineers of Serbia, 2019)

TY  - JOUR
AU  - Đuriš, Mihal
AU  - Kaluđerović-Radoičić, Tatjana
AU  - Jaćimovski, Darko
AU  - Arsenijević, Zorana
PY  - 2019
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3393
AB  - In this paper, an innovative fluidized bed dryer with inert particles is presented. The system can be used for drying of solutions, suspensions and pastes in order to obtain a powdered product. The experiments were performed in a pilot-scale dryer with a cylindrical column 0.215 m in diameter and 1.2 mm height, with glass spheres as inert particles. The material used for drying was CuSO4 solution. The effects of operating conditions on the dryer throughput and product quality were investigated. Main performance criteria, i.e. specific water evaporation rate, specific heat consumption and specific air consumption, were quantified. Nearly isothermal conditions were found due to thorough mixing of the particles. The energy efficiency of the dryer was also assessed. Simple heat and mass balances predicted the dryer performance quite well.
AB  - U ovom radu je predstavljen inovativni sušionik sa fluidizovanim slojem inertnih čestica. Prikazani sistem može da se koristi za sušenje rastvora, suspenzija i pasti u cilju dobijanja praškastog produkta. Eksperimenti su rađeni na pilot postrojenju čiji je centralni deo cilindrična kolona prečnika 215 mm i visine 1200 mm. Korišćene su staklene sfere kao inertne čestice. U radu je prikazano sušenje rastvora CuSO4. Ispitivan je uticaj operativnih uslova na performanse sistema za sušenje, kao i na 
kvalitet praškastog produkta. Kvantifikovani su glavni parametri koji opisuju performanse sušionika, kao što su specifična brzina isparavanja, specifična potrošnja toplote i specifična potrošnja vazduha. Usled intenzivnog mešanja u fluidizovanom sloju postižu se približno izotermni uslovi sušenja. Izvršena je procena energetske efikasnosti sušenja. Jednostavni bilansi prenosa mase i toplote adekvatno predviđaju radni režim sistema za sušenje.
PB  - Belgrade : Association of Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - High efficiency disperse dryer - an innovative process for drying of solutions, suspensions and pastes in a fluidized bed of inert particles
T1  - Visokoefikasni disperzni sušionik – Inovativni proces sušenja rastvora, suspenzija i pasti u fluidizovanom sloju inertnih čestica
VL  - 73
IS  - 4
SP  - 213
EP  - 222
DO  - 10.2298/HEMIND190626021D
ER  - 
@article{
author = "Đuriš, Mihal and Kaluđerović-Radoičić, Tatjana and Jaćimovski, Darko and Arsenijević, Zorana",
year = "2019",
abstract = "In this paper, an innovative fluidized bed dryer with inert particles is presented. The system can be used for drying of solutions, suspensions and pastes in order to obtain a powdered product. The experiments were performed in a pilot-scale dryer with a cylindrical column 0.215 m in diameter and 1.2 mm height, with glass spheres as inert particles. The material used for drying was CuSO4 solution. The effects of operating conditions on the dryer throughput and product quality were investigated. Main performance criteria, i.e. specific water evaporation rate, specific heat consumption and specific air consumption, were quantified. Nearly isothermal conditions were found due to thorough mixing of the particles. The energy efficiency of the dryer was also assessed. Simple heat and mass balances predicted the dryer performance quite well., U ovom radu je predstavljen inovativni sušionik sa fluidizovanim slojem inertnih čestica. Prikazani sistem može da se koristi za sušenje rastvora, suspenzija i pasti u cilju dobijanja praškastog produkta. Eksperimenti su rađeni na pilot postrojenju čiji je centralni deo cilindrična kolona prečnika 215 mm i visine 1200 mm. Korišćene su staklene sfere kao inertne čestice. U radu je prikazano sušenje rastvora CuSO4. Ispitivan je uticaj operativnih uslova na performanse sistema za sušenje, kao i na 
kvalitet praškastog produkta. Kvantifikovani su glavni parametri koji opisuju performanse sušionika, kao što su specifična brzina isparavanja, specifična potrošnja toplote i specifična potrošnja vazduha. Usled intenzivnog mešanja u fluidizovanom sloju postižu se približno izotermni uslovi sušenja. Izvršena je procena energetske efikasnosti sušenja. Jednostavni bilansi prenosa mase i toplote adekvatno predviđaju radni režim sistema za sušenje.",
publisher = "Belgrade : Association of Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "High efficiency disperse dryer - an innovative process for drying of solutions, suspensions and pastes in a fluidized bed of inert particles, Visokoefikasni disperzni sušionik – Inovativni proces sušenja rastvora, suspenzija i pasti u fluidizovanom sloju inertnih čestica",
volume = "73",
number = "4",
pages = "213-222",
doi = "10.2298/HEMIND190626021D"
}
Đuriš, M., Kaluđerović-Radoičić, T., Jaćimovski, D.,& Arsenijević, Z.. (2019). High efficiency disperse dryer - an innovative process for drying of solutions, suspensions and pastes in a fluidized bed of inert particles. in Hemijska industrija
Belgrade : Association of Chemical Engineers of Serbia., 73(4), 213-222.
https://doi.org/10.2298/HEMIND190626021D
Đuriš M, Kaluđerović-Radoičić T, Jaćimovski D, Arsenijević Z. High efficiency disperse dryer - an innovative process for drying of solutions, suspensions and pastes in a fluidized bed of inert particles. in Hemijska industrija. 2019;73(4):213-222.
doi:10.2298/HEMIND190626021D .
Đuriš, Mihal, Kaluđerović-Radoičić, Tatjana, Jaćimovski, Darko, Arsenijević, Zorana, "High efficiency disperse dryer - an innovative process for drying of solutions, suspensions and pastes in a fluidized bed of inert particles" in Hemijska industrija, 73, no. 4 (2019):213-222,
https://doi.org/10.2298/HEMIND190626021D . .

Diskontinualni granični sloj i analogije prenosa u pakovanim, fluidizovanim i transportnim sistemima tečnost-čestice

Jaćimovski, Darko

(Универзитет у Београду, Технолошко-металуршки факултет, 2017)

TY  - THES
AU  - Jaćimovski, Darko
PY  - 2017
UR  - http://eteze.bg.ac.rs/application/showtheses?thesesId=5654
UR  - https://fedorabg.bg.ac.rs/fedora/get/o:17299/bdef:Content/download
UR  - http://vbs.rs/scripts/cobiss?command=DISPLAY&base=70036&RID=49910799
UR  - http://nardus.mpn.gov.rs/123456789/9298
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/2538
AB  - U ovom radu eksperimentalno je ispitivan diskontinualni granični sloj ianalogije prenosa količine kretanja, toplote i mase u fluidizovanim i pakovanimslojevima i pri hidrauličkom transportu sistema tečnost-čestice. Cilj ovog rada je upravopovezivanje karakteristika graničnog sloja sa prenosom količine kretanja, toplote imase, sa akcentom na analogije između ovih prenosa. Fenomenološkim pristupom ovojproblematici, daje se doprinos koji bi olakšao teorijsko razmatranje višefaznih sistematečnost-čestice (pakovani sloj, fluidizovani sloj, vertikalni transport), koji su izuzetnosloženi.Za izvođenje eksperimentalnog dela istraživanja u ovoj doktorskoj disertacijikorišćeni su različiti sistemi: standardne kolone različitih prečnika sa omotačem ili bezomotača, sa pakovanim, fluidizovanim i transportnim sistemima u cilju dobijanjaparametara za koeficijente prenosa količine kretanja, mase i toplote i segmentiranekolone sa fluidizovanim česticama u cilju dobijanja parametara na koje utiče debljinagraničnog sloja. Sva eksperimentalna merenja su izvršena u širokom opseguhidrodinamičkih uslova: brzina strujanja fluida, veličina čestica čvrste faze i poroznostislojeva.Kao rezultat istraživanja razvijen je novi teorijski model za prenos mase i toplotezasnovan na analizi graničnog sloja koji se u disperznom sistemu formira od sudara dosudara čestica. Na osnovu modela dobijena je debljina difuzionog i termičkog graničnogsloja, izvedene su jednačine za korelisanje koeficijenata prelaza, Sherwood-ovog iNusselt-ovog broja i faktora prenosa mase i toplote. Na osnovu uspostavljenog modelaizvedena je jednačina za određivanje maksimalne vrednosti koeficijenata prelaza toplotei poroznosti sloja pri kojoj do nje dolazi.U ovom radu je uspostavljena analogija prenosa količine kretanja, mase i toploteu partikulativno fluidizovanim slojevima zasnovana na modelu graničnog sloja.Postojeća analogija u fluidizovanom sloju, data na osnovu normalizovanih vrednostikoeficijenta trenja čestice-fluid i faktora prenosa mase proširena je na analogiju sva triprenosa. Dobijeni model je upotrebljen za definisanje faktora prenosa mase i toplote priminimalnoj fluidizaciji i transportu čestica...
AB  - In this thesis the discontinued boundary layer and the analogues amongmomentum, heat and mass transfer were examined experimentally for fluidized andpacked beds and for hydraulic transport in liquid-particles systems. The aim of thispaper is to connect the characteristics of the boundary layer with the momentum, heatand mass transfer, with an emphasis on analogies between these phenomena. Transportphenomena approach to this problem provides a contribution that facilitates theoreticaldescription of multiphase liquid-particles systems (packed beds, fluidized beds, verticaltransport), which are extremely complex.Different experimental systems have been used to perform the research in thisdissertation: standard columns of different diameters with or without heating jacket,with packed and fluidized beds and transport systems in order to obtain parameters forthe momentum, heat and mass transfer coefficients, and segmented fluidized bedscolumns in order to obtain parameters influenced by the thickness of the boundary layer.All experimental measurements were performed in a wide range of hydrodynamicconditions: fluid velocities, solid particles sizes and bed voidages.As a result of this research, a new theoretical model for mass and heat transfer sdeveloped. Model is based on the analysis of the boundary layer, which in dispersesystems forms between the two adjacent particles collisions. Based on the model, thethickness of the concentration and thermal boundary layer was obtained and theequations for correlating the transfer coefficients with Sherwood and Nusselt numbersand the mass and heat transfer factors were derived. On the basis of the establishedmodel, the equation for determining the maximum value of the heat transfer coefficientand the bed voidage for this value is derived. In this thesis, the analogue based on the boundary layer model for themomentum, mass and heat transfer in particulate fluidized beds is established. Theexisting analogy for the fluidized beds, based on the normalized values of the frictioncoefficient fluid-particles and the mass transfer factor, has been extended to analogy forall three phenomena. The obtained model was used to define the mass and heat transferfactors at the minimum fluidization and transport of particles...
PB  - Универзитет у Београду, Технолошко-металуршки факултет
T2  - Универзитет у Београду
T1  - Diskontinualni granični sloj i analogije prenosa u pakovanim, fluidizovanim i transportnim sistemima tečnost-čestice
UR  - https://hdl.handle.net/21.15107/rcub_nardus_9298
ER  - 
@phdthesis{
author = "Jaćimovski, Darko",
year = "2017",
abstract = "U ovom radu eksperimentalno je ispitivan diskontinualni granični sloj ianalogije prenosa količine kretanja, toplote i mase u fluidizovanim i pakovanimslojevima i pri hidrauličkom transportu sistema tečnost-čestice. Cilj ovog rada je upravopovezivanje karakteristika graničnog sloja sa prenosom količine kretanja, toplote imase, sa akcentom na analogije između ovih prenosa. Fenomenološkim pristupom ovojproblematici, daje se doprinos koji bi olakšao teorijsko razmatranje višefaznih sistematečnost-čestice (pakovani sloj, fluidizovani sloj, vertikalni transport), koji su izuzetnosloženi.Za izvođenje eksperimentalnog dela istraživanja u ovoj doktorskoj disertacijikorišćeni su različiti sistemi: standardne kolone različitih prečnika sa omotačem ili bezomotača, sa pakovanim, fluidizovanim i transportnim sistemima u cilju dobijanjaparametara za koeficijente prenosa količine kretanja, mase i toplote i segmentiranekolone sa fluidizovanim česticama u cilju dobijanja parametara na koje utiče debljinagraničnog sloja. Sva eksperimentalna merenja su izvršena u širokom opseguhidrodinamičkih uslova: brzina strujanja fluida, veličina čestica čvrste faze i poroznostislojeva.Kao rezultat istraživanja razvijen je novi teorijski model za prenos mase i toplotezasnovan na analizi graničnog sloja koji se u disperznom sistemu formira od sudara dosudara čestica. Na osnovu modela dobijena je debljina difuzionog i termičkog graničnogsloja, izvedene su jednačine za korelisanje koeficijenata prelaza, Sherwood-ovog iNusselt-ovog broja i faktora prenosa mase i toplote. Na osnovu uspostavljenog modelaizvedena je jednačina za određivanje maksimalne vrednosti koeficijenata prelaza toplotei poroznosti sloja pri kojoj do nje dolazi.U ovom radu je uspostavljena analogija prenosa količine kretanja, mase i toploteu partikulativno fluidizovanim slojevima zasnovana na modelu graničnog sloja.Postojeća analogija u fluidizovanom sloju, data na osnovu normalizovanih vrednostikoeficijenta trenja čestice-fluid i faktora prenosa mase proširena je na analogiju sva triprenosa. Dobijeni model je upotrebljen za definisanje faktora prenosa mase i toplote priminimalnoj fluidizaciji i transportu čestica..., In this thesis the discontinued boundary layer and the analogues amongmomentum, heat and mass transfer were examined experimentally for fluidized andpacked beds and for hydraulic transport in liquid-particles systems. The aim of thispaper is to connect the characteristics of the boundary layer with the momentum, heatand mass transfer, with an emphasis on analogies between these phenomena. Transportphenomena approach to this problem provides a contribution that facilitates theoreticaldescription of multiphase liquid-particles systems (packed beds, fluidized beds, verticaltransport), which are extremely complex.Different experimental systems have been used to perform the research in thisdissertation: standard columns of different diameters with or without heating jacket,with packed and fluidized beds and transport systems in order to obtain parameters forthe momentum, heat and mass transfer coefficients, and segmented fluidized bedscolumns in order to obtain parameters influenced by the thickness of the boundary layer.All experimental measurements were performed in a wide range of hydrodynamicconditions: fluid velocities, solid particles sizes and bed voidages.As a result of this research, a new theoretical model for mass and heat transfer sdeveloped. Model is based on the analysis of the boundary layer, which in dispersesystems forms between the two adjacent particles collisions. Based on the model, thethickness of the concentration and thermal boundary layer was obtained and theequations for correlating the transfer coefficients with Sherwood and Nusselt numbersand the mass and heat transfer factors were derived. On the basis of the establishedmodel, the equation for determining the maximum value of the heat transfer coefficientand the bed voidage for this value is derived. In this thesis, the analogue based on the boundary layer model for themomentum, mass and heat transfer in particulate fluidized beds is established. Theexisting analogy for the fluidized beds, based on the normalized values of the frictioncoefficient fluid-particles and the mass transfer factor, has been extended to analogy forall three phenomena. The obtained model was used to define the mass and heat transferfactors at the minimum fluidization and transport of particles...",
publisher = "Универзитет у Београду, Технолошко-металуршки факултет",
journal = "Универзитет у Београду",
title = "Diskontinualni granični sloj i analogije prenosa u pakovanim, fluidizovanim i transportnim sistemima tečnost-čestice",
url = "https://hdl.handle.net/21.15107/rcub_nardus_9298"
}
Jaćimovski, D.. (2017). Diskontinualni granični sloj i analogije prenosa u pakovanim, fluidizovanim i transportnim sistemima tečnost-čestice. in Универзитет у Београду
Универзитет у Београду, Технолошко-металуршки факултет..
https://hdl.handle.net/21.15107/rcub_nardus_9298
Jaćimovski D. Diskontinualni granični sloj i analogije prenosa u pakovanim, fluidizovanim i transportnim sistemima tečnost-čestice. in Универзитет у Београду. 2017;.
https://hdl.handle.net/21.15107/rcub_nardus_9298 .
Jaćimovski, Darko, "Diskontinualni granični sloj i analogije prenosa u pakovanim, fluidizovanim i transportnim sistemima tečnost-čestice" in Универзитет у Београду (2017),
https://hdl.handle.net/21.15107/rcub_nardus_9298 .

Mass transfer and concentration boundary layer in a particulate fluidized bed

Jaćimovski, Darko; Garić Grulović, Radmila; Vucetic, Nemanja; Pjanović, Rada; Bošković-Vragolović, Nevenka

(Elsevier, 2016)

TY  - JOUR
AU  - Jaćimovski, Darko
AU  - Garić Grulović, Radmila
AU  - Vucetic, Nemanja
AU  - Pjanović, Rada
AU  - Bošković-Vragolović, Nevenka
PY  - 2016
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1931
AB  - The aim of this study was to analyze the concentration boundary layer for a comprehensive description of the mass transfer in systems with fluidized particles. Mass transfer from the wall of the column to the fluid in the presence of inert fluidized particles was experimentally investigated using the dissolution method. Experiments were carried out in a column 34 mm in diameter, divided by height into six segments. In all runs, mass transfer rates were determined in the presence of fluidized spherical glass particles 1.10 mm, 1.94 mm and 2.98 mm in diameter, using water as the fluidized medium. The analysis of the boundary layer shows the effect of particles presence on mass transfer in fluidized systems. The theoretical model was established based on boundary layer theory, and the impact of particles on the shortening of the boundary layer length, due to their collision with the wall of the column. The theoretically derived model was compared with experimentally obtained data and with data calculated from available literature correlations. Very good agreement was found between the model, experimental data, and published correlations (especially the correlation by Pickett et al. 12]).
PB  - Elsevier
T2  - Powder Technology
T1  - Mass transfer and concentration boundary layer in a particulate fluidized bed
VL  - 303
SP  - 68
EP  - 75
DO  - 10.1016/j.powtec.2016.09.025
ER  - 
@article{
author = "Jaćimovski, Darko and Garić Grulović, Radmila and Vucetic, Nemanja and Pjanović, Rada and Bošković-Vragolović, Nevenka",
year = "2016",
abstract = "The aim of this study was to analyze the concentration boundary layer for a comprehensive description of the mass transfer in systems with fluidized particles. Mass transfer from the wall of the column to the fluid in the presence of inert fluidized particles was experimentally investigated using the dissolution method. Experiments were carried out in a column 34 mm in diameter, divided by height into six segments. In all runs, mass transfer rates were determined in the presence of fluidized spherical glass particles 1.10 mm, 1.94 mm and 2.98 mm in diameter, using water as the fluidized medium. The analysis of the boundary layer shows the effect of particles presence on mass transfer in fluidized systems. The theoretical model was established based on boundary layer theory, and the impact of particles on the shortening of the boundary layer length, due to their collision with the wall of the column. The theoretically derived model was compared with experimentally obtained data and with data calculated from available literature correlations. Very good agreement was found between the model, experimental data, and published correlations (especially the correlation by Pickett et al. 12]).",
publisher = "Elsevier",
journal = "Powder Technology",
title = "Mass transfer and concentration boundary layer in a particulate fluidized bed",
volume = "303",
pages = "68-75",
doi = "10.1016/j.powtec.2016.09.025"
}
Jaćimovski, D., Garić Grulović, R., Vucetic, N., Pjanović, R.,& Bošković-Vragolović, N.. (2016). Mass transfer and concentration boundary layer in a particulate fluidized bed. in Powder Technology
Elsevier., 303, 68-75.
https://doi.org/10.1016/j.powtec.2016.09.025
Jaćimovski D, Garić Grulović R, Vucetic N, Pjanović R, Bošković-Vragolović N. Mass transfer and concentration boundary layer in a particulate fluidized bed. in Powder Technology. 2016;303:68-75.
doi:10.1016/j.powtec.2016.09.025 .
Jaćimovski, Darko, Garić Grulović, Radmila, Vucetic, Nemanja, Pjanović, Rada, Bošković-Vragolović, Nevenka, "Mass transfer and concentration boundary layer in a particulate fluidized bed" in Powder Technology, 303 (2016):68-75,
https://doi.org/10.1016/j.powtec.2016.09.025 . .
9
4
9

Optimal pixel resolution for sand particles size and shape analysis

Đuriš, Mihal; Arsenijević, Zorana; Jaćimovski, Darko; Kaluđerović-Radoičić, Tatjana

(Elsevier, 2016)

TY  - JOUR
AU  - Đuriš, Mihal
AU  - Arsenijević, Zorana
AU  - Jaćimovski, Darko
AU  - Kaluđerović-Radoičić, Tatjana
PY  - 2016
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1899
AB  - In this paper, the influence of different scanning resolutions and the use of image analysis softwares for the image analysis, SigmaScan Pro, Image) and Matlab, on size and shape factors commonly used in particles characterization were investigated. In our previous paper [1] the characterization of polydisperse sand particles was performed, and the need had arisen to examine the impact of different scanning resolutions on shape factors in more detail. The particles analyzed were the polydisperse fractions of quartz filtration sand with sieve diameters in the intervals of 0.85-1.030 mm, 1.406-1.600 mm and 2.00-2.83 mm. The particles size and shape were analyzed using the scanned image of about 150 particles in each fraction. In addition, the images of circles of similar dimensions were generated to serve as reference particles. The scanning resolutions used in this study were from 75 to 4800 dpi, and grayscale thresholds were optimized for discrimination of the particles from the background. The obtained results indicate that the resolution (i.e. the pixel size) and the algorithms used in image analysis softwares have significant influence on the obtained shape factors. The most significant effect was observed in the calculated values of the particles perimeters, while the effect was less pronounced in the results obtained for the particles projected area. The analysis of images of generated circles confirmed that the resolution had the largest effect on particle perimeter. The use of the resolutions of 300-600 dpi for the determination of particle shape and size can be recommended for particles of similar to 1 mm and larger, because of reasonable results, low storage space and less time for image analysis.
PB  - Elsevier
T2  - Powder Technology
T1  - Optimal pixel resolution for sand particles size and shape analysis
VL  - 302
SP  - 177
EP  - 186
DO  - 10.1016/j.powtec.2016.08.045
ER  - 
@article{
author = "Đuriš, Mihal and Arsenijević, Zorana and Jaćimovski, Darko and Kaluđerović-Radoičić, Tatjana",
year = "2016",
abstract = "In this paper, the influence of different scanning resolutions and the use of image analysis softwares for the image analysis, SigmaScan Pro, Image) and Matlab, on size and shape factors commonly used in particles characterization were investigated. In our previous paper [1] the characterization of polydisperse sand particles was performed, and the need had arisen to examine the impact of different scanning resolutions on shape factors in more detail. The particles analyzed were the polydisperse fractions of quartz filtration sand with sieve diameters in the intervals of 0.85-1.030 mm, 1.406-1.600 mm and 2.00-2.83 mm. The particles size and shape were analyzed using the scanned image of about 150 particles in each fraction. In addition, the images of circles of similar dimensions were generated to serve as reference particles. The scanning resolutions used in this study were from 75 to 4800 dpi, and grayscale thresholds were optimized for discrimination of the particles from the background. The obtained results indicate that the resolution (i.e. the pixel size) and the algorithms used in image analysis softwares have significant influence on the obtained shape factors. The most significant effect was observed in the calculated values of the particles perimeters, while the effect was less pronounced in the results obtained for the particles projected area. The analysis of images of generated circles confirmed that the resolution had the largest effect on particle perimeter. The use of the resolutions of 300-600 dpi for the determination of particle shape and size can be recommended for particles of similar to 1 mm and larger, because of reasonable results, low storage space and less time for image analysis.",
publisher = "Elsevier",
journal = "Powder Technology",
title = "Optimal pixel resolution for sand particles size and shape analysis",
volume = "302",
pages = "177-186",
doi = "10.1016/j.powtec.2016.08.045"
}
Đuriš, M., Arsenijević, Z., Jaćimovski, D.,& Kaluđerović-Radoičić, T.. (2016). Optimal pixel resolution for sand particles size and shape analysis. in Powder Technology
Elsevier., 302, 177-186.
https://doi.org/10.1016/j.powtec.2016.08.045
Đuriš M, Arsenijević Z, Jaćimovski D, Kaluđerović-Radoičić T. Optimal pixel resolution for sand particles size and shape analysis. in Powder Technology. 2016;302:177-186.
doi:10.1016/j.powtec.2016.08.045 .
Đuriš, Mihal, Arsenijević, Zorana, Jaćimovski, Darko, Kaluđerović-Radoičić, Tatjana, "Optimal pixel resolution for sand particles size and shape analysis" in Powder Technology, 302 (2016):177-186,
https://doi.org/10.1016/j.powtec.2016.08.045 . .
19
10
19

Analogy between momentum and heat transfer in liquid-solid fluidized beds

Jaćimovski, Darko; Garić Grulović, Radmila; Grbavčić, Željko; Bošković-Vragolović, Nevenka

(Elsevier, 2015)

TY  - JOUR
AU  - Jaćimovski, Darko
AU  - Garić Grulović, Radmila
AU  - Grbavčić, Željko
AU  - Bošković-Vragolović, Nevenka
PY  - 2015
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1759
AB  - Wall-to-bed heat transfer in particulate fluidized beds of spherical particles was studied. Experiments were performed using spherical glass particles of 0.80-2.98 mm in diameter with water in a 25.4 mm I.D. copper tube equipped with a steam jacket. Heat transfer data related to the fluid-particle interphase drag coefficient were obtained and compared with previous results for wall-to-bed mass transfer in fluidized beds [Bogkovit et aL, Powder Technol., 79 (1994) 217]. All the data for momentum, heat and mass transfer in particulate fluidized beds of spherical particles, showed the existence of an analogy among these three phenomena.
PB  - Elsevier
T2  - Powder Technology
T1  - Analogy between momentum and heat transfer in liquid-solid fluidized beds
VL  - 274
SP  - 213
EP  - 216
DO  - 10.1016/j.powtec.2014.11.010
ER  - 
@article{
author = "Jaćimovski, Darko and Garić Grulović, Radmila and Grbavčić, Željko and Bošković-Vragolović, Nevenka",
year = "2015",
abstract = "Wall-to-bed heat transfer in particulate fluidized beds of spherical particles was studied. Experiments were performed using spherical glass particles of 0.80-2.98 mm in diameter with water in a 25.4 mm I.D. copper tube equipped with a steam jacket. Heat transfer data related to the fluid-particle interphase drag coefficient were obtained and compared with previous results for wall-to-bed mass transfer in fluidized beds [Bogkovit et aL, Powder Technol., 79 (1994) 217]. All the data for momentum, heat and mass transfer in particulate fluidized beds of spherical particles, showed the existence of an analogy among these three phenomena.",
publisher = "Elsevier",
journal = "Powder Technology",
title = "Analogy between momentum and heat transfer in liquid-solid fluidized beds",
volume = "274",
pages = "213-216",
doi = "10.1016/j.powtec.2014.11.010"
}
Jaćimovski, D., Garić Grulović, R., Grbavčić, Ž.,& Bošković-Vragolović, N.. (2015). Analogy between momentum and heat transfer in liquid-solid fluidized beds. in Powder Technology
Elsevier., 274, 213-216.
https://doi.org/10.1016/j.powtec.2014.11.010
Jaćimovski D, Garić Grulović R, Grbavčić Ž, Bošković-Vragolović N. Analogy between momentum and heat transfer in liquid-solid fluidized beds. in Powder Technology. 2015;274:213-216.
doi:10.1016/j.powtec.2014.11.010 .
Jaćimovski, Darko, Garić Grulović, Radmila, Grbavčić, Željko, Bošković-Vragolović, Nevenka, "Analogy between momentum and heat transfer in liquid-solid fluidized beds" in Powder Technology, 274 (2015):213-216,
https://doi.org/10.1016/j.powtec.2014.11.010 . .
2
1
2

Analogy between momentum and heat transfer in liquid-solid fluidized beds

Jaćimovski, Darko; Garić Grulović, Radmila; Grbavčić, Željko; Bošković-Vragolović, Nevenka

(Elsevier, 2015)

TY  - JOUR
AU  - Jaćimovski, Darko
AU  - Garić Grulović, Radmila
AU  - Grbavčić, Željko
AU  - Bošković-Vragolović, Nevenka
PY  - 2015
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/3199
AB  - Wall-to-bed heat transfer in particulate fluidized beds of spherical particles was studied. Experiments were performed using spherical glass particles of 0.80-2.98 mm in diameter with water in a 25.4 mm I.D. copper tube equipped with a steam jacket. Heat transfer data related to the fluid-particle interphase drag coefficient were obtained and compared with previous results for wall-to-bed mass transfer in fluidized beds [Bogkovit et aL, Powder Technol., 79 (1994) 217]. All the data for momentum, heat and mass transfer in particulate fluidized beds of spherical particles, showed the existence of an analogy among these three phenomena.
PB  - Elsevier
T2  - Powder Technology
T1  - Analogy between momentum and heat transfer in liquid-solid fluidized beds
VL  - 274
SP  - 213
EP  - 216
DO  - 10.1016/j.powtec.2014.11.010
ER  - 
@article{
author = "Jaćimovski, Darko and Garić Grulović, Radmila and Grbavčić, Željko and Bošković-Vragolović, Nevenka",
year = "2015",
abstract = "Wall-to-bed heat transfer in particulate fluidized beds of spherical particles was studied. Experiments were performed using spherical glass particles of 0.80-2.98 mm in diameter with water in a 25.4 mm I.D. copper tube equipped with a steam jacket. Heat transfer data related to the fluid-particle interphase drag coefficient were obtained and compared with previous results for wall-to-bed mass transfer in fluidized beds [Bogkovit et aL, Powder Technol., 79 (1994) 217]. All the data for momentum, heat and mass transfer in particulate fluidized beds of spherical particles, showed the existence of an analogy among these three phenomena.",
publisher = "Elsevier",
journal = "Powder Technology",
title = "Analogy between momentum and heat transfer in liquid-solid fluidized beds",
volume = "274",
pages = "213-216",
doi = "10.1016/j.powtec.2014.11.010"
}
Jaćimovski, D., Garić Grulović, R., Grbavčić, Ž.,& Bošković-Vragolović, N.. (2015). Analogy between momentum and heat transfer in liquid-solid fluidized beds. in Powder Technology
Elsevier., 274, 213-216.
https://doi.org/10.1016/j.powtec.2014.11.010
Jaćimovski D, Garić Grulović R, Grbavčić Ž, Bošković-Vragolović N. Analogy between momentum and heat transfer in liquid-solid fluidized beds. in Powder Technology. 2015;274:213-216.
doi:10.1016/j.powtec.2014.11.010 .
Jaćimovski, Darko, Garić Grulović, Radmila, Grbavčić, Željko, Bošković-Vragolović, Nevenka, "Analogy between momentum and heat transfer in liquid-solid fluidized beds" in Powder Technology, 274 (2015):213-216,
https://doi.org/10.1016/j.powtec.2014.11.010 . .
2
1
2

Momentum, heat, and mass transfer analogy for vertical hydraulic transport of inert particles

Jaćimovski, Darko; Garić Grulović, Radmila; Grbavčić, Željko; Đuriš, Mihal; Bošković-Vragolović, Nevenka

(Association of Chemical Engineers of Serbia, 2014)

TY  - JOUR
AU  - Jaćimovski, Darko
AU  - Garić Grulović, Radmila
AU  - Grbavčić, Željko
AU  - Đuriš, Mihal
AU  - Bošković-Vragolović, Nevenka
PY  - 2014
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1465
AB  - Wall-to-bed momentum, heat and mass transfer in the vertical liquid-solids flow, as well as in the single phase flow, were studied. The aim of this investigation was to establish the analogy among those phenomena. Also, effect of particle concentration on momentum, heat and mass transfer was studied. The experiments in hydraulic transport were performed in 25.4 mm I.D. cooper tube equipped with a steam jacket, using spherical glass particles of 1.94 mm in diameter and water as a transport fluid. The segment of the transport tube used for mass transfer measurements had internal coating made of benzoic acid. In the hydraulic transport two characteristic flow regimes were observed: turbulent and parallel particle flow regime. The transition between two characteristic regimes (Y* = 0), occurs at a critical voidage ε ≈ 0.85. The vertical two-phase flow was con­sidered as the pseudofluid, and modified mixture-wall friction coefficient (fw) and modified mixture Reynolds number (Rem) were introduced for system characterization. Experimental data show that the wall-to-bed momentum, heat and mass transfer coefficients, in vertical flow of pseudofluid, for the turbulent regime are significantly higher than in parallel regime. Wall-to-bed, mass and heat transfer coefficients in hydraulic transport of particles were much higher than in single-phase flow for lower Reynolds numbers (Re  LT  15000), while for high Reynolds numbers (Re > 15000), there was not significant difference. The experimental data for wall-to-bed momentum, heat and mass transfer in vertical flow of pseudofluid in parallel particle flow regime, verify analogy among these three phenomena.
AB  - U ovom radu prikazani su rezultati eksperimentalnih ispitivanja prenosa količine kretanja, toplote i mase zid-fluid u vertikalnom hidrauličkom transportu inertnih čestica i pri strujanju fluida u cevi istog prečnika. Eksperimentalna ispitivanja vršena su istovremenim merenjem potrebnih parametara za definisanje navedenih prenosa. Cilj ovih ispitivanja bio je određivanje koeficijenata prenosa pri vertikalnom hidrauličkom transportu inertnih čestica i uspostavljanje analogije tri prenosa. Eksperimentalni sistem predstavljala je vertikalna transportna cev prečnika 25,4 mm snabdevena omotačem za zagrevanje parom, kao i segmentom transportne cevi prepariranim rastopom benzoeve kiseline. Kao fluid korišćena je voda, a vršen je transport staklenih sfernih čestica prečnika 1,94 mm. U rezultatima su prikazani dobijeni koeficijenti trenja, prelaza toplote i prelaza mase. Korišćenjem koncepta pseudofluida, pokazano je postojanje analogije prenosa količine kretanja, toplote i mase u transportnoj cevi za paralelni režim strujanja.
PB  - Association of Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - Momentum, heat, and mass transfer analogy for vertical hydraulic transport of inert particles
T1  - Analogija prenosa količine kretanja, toplote i mase pri vertikalnom hidrauličkom transportu inertnih čestica
VL  - 68
IS  - 1
SP  - 15
EP  - 25
DO  - 10.2298/HEMIND130207025J
ER  - 
@article{
author = "Jaćimovski, Darko and Garić Grulović, Radmila and Grbavčić, Željko and Đuriš, Mihal and Bošković-Vragolović, Nevenka",
year = "2014",
abstract = "Wall-to-bed momentum, heat and mass transfer in the vertical liquid-solids flow, as well as in the single phase flow, were studied. The aim of this investigation was to establish the analogy among those phenomena. Also, effect of particle concentration on momentum, heat and mass transfer was studied. The experiments in hydraulic transport were performed in 25.4 mm I.D. cooper tube equipped with a steam jacket, using spherical glass particles of 1.94 mm in diameter and water as a transport fluid. The segment of the transport tube used for mass transfer measurements had internal coating made of benzoic acid. In the hydraulic transport two characteristic flow regimes were observed: turbulent and parallel particle flow regime. The transition between two characteristic regimes (Y* = 0), occurs at a critical voidage ε ≈ 0.85. The vertical two-phase flow was con­sidered as the pseudofluid, and modified mixture-wall friction coefficient (fw) and modified mixture Reynolds number (Rem) were introduced for system characterization. Experimental data show that the wall-to-bed momentum, heat and mass transfer coefficients, in vertical flow of pseudofluid, for the turbulent regime are significantly higher than in parallel regime. Wall-to-bed, mass and heat transfer coefficients in hydraulic transport of particles were much higher than in single-phase flow for lower Reynolds numbers (Re  LT  15000), while for high Reynolds numbers (Re > 15000), there was not significant difference. The experimental data for wall-to-bed momentum, heat and mass transfer in vertical flow of pseudofluid in parallel particle flow regime, verify analogy among these three phenomena., U ovom radu prikazani su rezultati eksperimentalnih ispitivanja prenosa količine kretanja, toplote i mase zid-fluid u vertikalnom hidrauličkom transportu inertnih čestica i pri strujanju fluida u cevi istog prečnika. Eksperimentalna ispitivanja vršena su istovremenim merenjem potrebnih parametara za definisanje navedenih prenosa. Cilj ovih ispitivanja bio je određivanje koeficijenata prenosa pri vertikalnom hidrauličkom transportu inertnih čestica i uspostavljanje analogije tri prenosa. Eksperimentalni sistem predstavljala je vertikalna transportna cev prečnika 25,4 mm snabdevena omotačem za zagrevanje parom, kao i segmentom transportne cevi prepariranim rastopom benzoeve kiseline. Kao fluid korišćena je voda, a vršen je transport staklenih sfernih čestica prečnika 1,94 mm. U rezultatima su prikazani dobijeni koeficijenti trenja, prelaza toplote i prelaza mase. Korišćenjem koncepta pseudofluida, pokazano je postojanje analogije prenosa količine kretanja, toplote i mase u transportnoj cevi za paralelni režim strujanja.",
publisher = "Association of Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "Momentum, heat, and mass transfer analogy for vertical hydraulic transport of inert particles, Analogija prenosa količine kretanja, toplote i mase pri vertikalnom hidrauličkom transportu inertnih čestica",
volume = "68",
number = "1",
pages = "15-25",
doi = "10.2298/HEMIND130207025J"
}
Jaćimovski, D., Garić Grulović, R., Grbavčić, Ž., Đuriš, M.,& Bošković-Vragolović, N.. (2014). Momentum, heat, and mass transfer analogy for vertical hydraulic transport of inert particles. in Hemijska industrija
Association of Chemical Engineers of Serbia., 68(1), 15-25.
https://doi.org/10.2298/HEMIND130207025J
Jaćimovski D, Garić Grulović R, Grbavčić Ž, Đuriš M, Bošković-Vragolović N. Momentum, heat, and mass transfer analogy for vertical hydraulic transport of inert particles. in Hemijska industrija. 2014;68(1):15-25.
doi:10.2298/HEMIND130207025J .
Jaćimovski, Darko, Garić Grulović, Radmila, Grbavčić, Željko, Đuriš, Mihal, Bošković-Vragolović, Nevenka, "Momentum, heat, and mass transfer analogy for vertical hydraulic transport of inert particles" in Hemijska industrija, 68, no. 1 (2014):15-25,
https://doi.org/10.2298/HEMIND130207025J . .
1

Segregation in water fluidized beds of sand particles

Đuriš, Mihal; Garić Grulović, Radmila; Arsenijević, Zorana; Jaćimovski, Darko; Grbavčić, Željko

(Elsevier Science Sa, Lausanne, 2013)

TY  - JOUR
AU  - Đuriš, Mihal
AU  - Garić Grulović, Radmila
AU  - Arsenijević, Zorana
AU  - Jaćimovski, Darko
AU  - Grbavčić, Željko
PY  - 2013
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1291
AB  - Fluidization experiments were conducted on four fractions of filtration (quartz) sand using columns of 144 and 64 mm i.d. The size distribution of the fractions obtained by sieving followed an approximately modified normal (Gaussian) particle size distribution with respect to the projected particle diameter, while the shape factor decreased linearly with increasing projected particle diameter. The expansion characteristics of the sand particles followed a Richardson-Zaki relationship. The intercept velocity, i.e., the extrapolated value of the fluid superficial velocity to epsilon=1 on the plot log (U) vs. log (epsilon), agreed quite well with the experimentally determined mean free settling velocity of the cloud of about 30 randomly selected particles. During fluidization, the beds were hydraulically separated into 10 sub-fractions, which are then analyzed. For the mixture d(p)=0.75-1.25 mm during fluidization at an overall bed expansion of 35%, the bed partially segregated since, remarkably, the smallest particles were concentrated at the top, while the largest particles were concentrated in the bottom zone. In the remaining part of the bed (about 80% of total mass), the particles were well mixed. Similar experiments were performed with sand mixtures d(p)=1.60-2.00 mm, d(p)=1.40-2.00 mm and d(p)=1.166-2.00 mm. By analyzing the particle size distribution at the bottom and at the top of the bed, it was concluded that the bed was well mixed if the sieving ratio of the largest to smallest sieve opening was less than about 1.5.
PB  - Elsevier Science Sa, Lausanne
T2  - Powder Technology
T1  - Segregation in water fluidized beds of sand particles
VL  - 235
SP  - 173
EP  - 179
DO  - 10.1016/j.powtec.2012.10.004
ER  - 
@article{
author = "Đuriš, Mihal and Garić Grulović, Radmila and Arsenijević, Zorana and Jaćimovski, Darko and Grbavčić, Željko",
year = "2013",
abstract = "Fluidization experiments were conducted on four fractions of filtration (quartz) sand using columns of 144 and 64 mm i.d. The size distribution of the fractions obtained by sieving followed an approximately modified normal (Gaussian) particle size distribution with respect to the projected particle diameter, while the shape factor decreased linearly with increasing projected particle diameter. The expansion characteristics of the sand particles followed a Richardson-Zaki relationship. The intercept velocity, i.e., the extrapolated value of the fluid superficial velocity to epsilon=1 on the plot log (U) vs. log (epsilon), agreed quite well with the experimentally determined mean free settling velocity of the cloud of about 30 randomly selected particles. During fluidization, the beds were hydraulically separated into 10 sub-fractions, which are then analyzed. For the mixture d(p)=0.75-1.25 mm during fluidization at an overall bed expansion of 35%, the bed partially segregated since, remarkably, the smallest particles were concentrated at the top, while the largest particles were concentrated in the bottom zone. In the remaining part of the bed (about 80% of total mass), the particles were well mixed. Similar experiments were performed with sand mixtures d(p)=1.60-2.00 mm, d(p)=1.40-2.00 mm and d(p)=1.166-2.00 mm. By analyzing the particle size distribution at the bottom and at the top of the bed, it was concluded that the bed was well mixed if the sieving ratio of the largest to smallest sieve opening was less than about 1.5.",
publisher = "Elsevier Science Sa, Lausanne",
journal = "Powder Technology",
title = "Segregation in water fluidized beds of sand particles",
volume = "235",
pages = "173-179",
doi = "10.1016/j.powtec.2012.10.004"
}
Đuriš, M., Garić Grulović, R., Arsenijević, Z., Jaćimovski, D.,& Grbavčić, Ž.. (2013). Segregation in water fluidized beds of sand particles. in Powder Technology
Elsevier Science Sa, Lausanne., 235, 173-179.
https://doi.org/10.1016/j.powtec.2012.10.004
Đuriš M, Garić Grulović R, Arsenijević Z, Jaćimovski D, Grbavčić Ž. Segregation in water fluidized beds of sand particles. in Powder Technology. 2013;235:173-179.
doi:10.1016/j.powtec.2012.10.004 .
Đuriš, Mihal, Garić Grulović, Radmila, Arsenijević, Zorana, Jaćimovski, Darko, Grbavčić, Željko, "Segregation in water fluidized beds of sand particles" in Powder Technology, 235 (2013):173-179,
https://doi.org/10.1016/j.powtec.2012.10.004 . .
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