Interakcija imobilisanih ćelija, tkiva i biološki aktivnih molekula u bioreaktorskim sistemima

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Interakcija imobilisanih ćelija, tkiva i biološki aktivnih molekula u bioreaktorskim sistemima (en)
Интеракција имобилисаних ћелија, ткива и биолошки активних молекула у биореакторским системима (sr)
Interakcija imobilisanih ćelija, tkiva i biološki aktivnih molekula u bioreaktorskim sistemima (sr_RS)
Authors

Publications

Microencapsulation of Flavors in Carnauba Wax

Milanović, Jelena; Manojlović, Verica; Lević, Steva; Rajić, Nevenka; Nedović, Viktor; Bugarski, Branko

(MDPI, BASEL, 2010)

TY  - JOUR
AU  - Milanović, Jelena
AU  - Manojlović, Verica
AU  - Lević, Steva
AU  - Rajić, Nevenka
AU  - Nedović, Viktor
AU  - Bugarski, Branko
PY  - 2010
UR  - http://aspace.agrif.bg.ac.rs/handle/123456789/2368
AB  - The subject of this study is the development of flavor wax formulations aimed for food and feed products. The melt dispersion technique was applied for the encapsulation of ethyl vanillin in wax microcapsules. The surface morphology of microparticles was investigated using scanning electron microscope (SEM), while the loading content was determined by HPLC measurements. This study shows that the decomposition process under heating proceeds in several steps: vanilla evaporation occurs at around 200 degrees C, while matrix degradation starts at 250 degrees C and progresses with maxima at around 360, 440 and 520 degrees C. The results indicate that carnauba wax is an attractive material for use as a matrix for encapsulation of flavours in order to improve their functionality and stability in products.
PB  - MDPI, BASEL
T2  - Sensors
T1  - Microencapsulation of Flavors in Carnauba Wax
EP  - 912
IS  - 1
SP  - 901
VL  - 10
DO  - 10.3390/s100100901
ER  - 
@article{
author = "Milanović, Jelena and Manojlović, Verica and Lević, Steva and Rajić, Nevenka and Nedović, Viktor and Bugarski, Branko",
year = "2010",
abstract = "The subject of this study is the development of flavor wax formulations aimed for food and feed products. The melt dispersion technique was applied for the encapsulation of ethyl vanillin in wax microcapsules. The surface morphology of microparticles was investigated using scanning electron microscope (SEM), while the loading content was determined by HPLC measurements. This study shows that the decomposition process under heating proceeds in several steps: vanilla evaporation occurs at around 200 degrees C, while matrix degradation starts at 250 degrees C and progresses with maxima at around 360, 440 and 520 degrees C. The results indicate that carnauba wax is an attractive material for use as a matrix for encapsulation of flavours in order to improve their functionality and stability in products.",
publisher = "MDPI, BASEL",
journal = "Sensors",
title = "Microencapsulation of Flavors in Carnauba Wax",
pages = "912-901",
number = "1",
volume = "10",
doi = "10.3390/s100100901"
}
Milanović, J., Manojlović, V., Lević, S., Rajić, N., Nedović, V.,& Bugarski, B.. (2010). Microencapsulation of Flavors in Carnauba Wax. in Sensors
MDPI, BASEL., 10(1), 901-912.
https://doi.org/10.3390/s100100901
Milanović J, Manojlović V, Lević S, Rajić N, Nedović V, Bugarski B. Microencapsulation of Flavors in Carnauba Wax. in Sensors. 2010;10(1):901-912.
doi:10.3390/s100100901 .
Milanović, Jelena, Manojlović, Verica, Lević, Steva, Rajić, Nevenka, Nedović, Viktor, Bugarski, Branko, "Microencapsulation of Flavors in Carnauba Wax" in Sensors, 10, no. 1 (2010):901-912,
https://doi.org/10.3390/s100100901 . .
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Bioprocess intensification of beer fermentation using immobilised cells

Verbelen, P.J.; Nedović, Viktor; Manojlović, Verica; Delvaux, F.R.; Laskošek-Čukalović, I.; Bugarski, Branko; Willaert, R.

(2010)

TY  - CHAP
AU  - Verbelen, P.J.
AU  - Nedović, Viktor
AU  - Manojlović, Verica
AU  - Delvaux, F.R.
AU  - Laskošek-Čukalović, I.
AU  - Bugarski, Branko
AU  - Willaert, R.
PY  - 2010
UR  - http://aspace.agrif.bg.ac.rs/handle/123456789/2154
AB  - Beer production with immobilised yeast has been the subject of research for approximately 30 years but has so far found limited application in the brewing industry, due to engineering problems, unrealised cost advantages, microbial contaminations and an unbalanced beer flavor (Linko et al. 1998; Brányik et al. 2005; Willaert and Nedović 2006). The ultimate aim of this research is the production of beer of desired quality within 1-3 days. Traditional beer fermentation systems use freely suspended yeast cells to ferment wort in an unstirred batch reactor. The primary fermentation takes approximately 7 days with a subsequent secondary fermentation (maturation) of several weeks. A batch culture system employing immobilization could benefit from an increased rate of fermentation. However, it appears that in terms of increasing productivity, a continuous fermentation system with immobilization would be the best method (Verbelen et al. 2006). An important issue of the research area is whether beer can be produced by immobilised yeast in continuous culture with the same characteristic as the traditional method. In beer production, as opposed to a process such as bio-ethanol production, the goal is to achieve a particular balance of different secondary metabolites rather than the attainment of high yields of one product. Any alterations of the fermentation procedure can thus have serious implications on the flavor profile. At present, only beer maturation and alcohol-free beer production are obtained by means of commercial-scale immobilised yeast reactors, because in these processes no real yeast growth is required. Immobilised cell physiology control and fine-tuning of the flavor compounds formation during long-term fermentation processes remain the major challenges for successful application of immobilised cell technology on an industrial scale. The key factors for the implementation of this technology on an industrial level are carrier materials, immobilization technology and bioreactor design. The purpose of this chapter is to summarise and discuss the main cell immobilization methods, process requirements, available carrier materials and bioreactor designs aimed for better yeast physiology control and fine-tuning of the flavor formation during beer fermentation process. Further, it will provide an overview on the latest important breakthroughs, accomplished in understanding of the effects of immobilization on yeast physiology, metabolism and fermentation behaviour.
T2  - Encapsulation Technologies for Active Food Ingredients and Food Processing
T1  - Bioprocess intensification of beer fermentation using immobilised cells
EP  - 325
SP  - 303
DO  - 10.1007/978-1-4419-1008-0_11
ER  - 
@inbook{
author = "Verbelen, P.J. and Nedović, Viktor and Manojlović, Verica and Delvaux, F.R. and Laskošek-Čukalović, I. and Bugarski, Branko and Willaert, R.",
year = "2010",
abstract = "Beer production with immobilised yeast has been the subject of research for approximately 30 years but has so far found limited application in the brewing industry, due to engineering problems, unrealised cost advantages, microbial contaminations and an unbalanced beer flavor (Linko et al. 1998; Brányik et al. 2005; Willaert and Nedović 2006). The ultimate aim of this research is the production of beer of desired quality within 1-3 days. Traditional beer fermentation systems use freely suspended yeast cells to ferment wort in an unstirred batch reactor. The primary fermentation takes approximately 7 days with a subsequent secondary fermentation (maturation) of several weeks. A batch culture system employing immobilization could benefit from an increased rate of fermentation. However, it appears that in terms of increasing productivity, a continuous fermentation system with immobilization would be the best method (Verbelen et al. 2006). An important issue of the research area is whether beer can be produced by immobilised yeast in continuous culture with the same characteristic as the traditional method. In beer production, as opposed to a process such as bio-ethanol production, the goal is to achieve a particular balance of different secondary metabolites rather than the attainment of high yields of one product. Any alterations of the fermentation procedure can thus have serious implications on the flavor profile. At present, only beer maturation and alcohol-free beer production are obtained by means of commercial-scale immobilised yeast reactors, because in these processes no real yeast growth is required. Immobilised cell physiology control and fine-tuning of the flavor compounds formation during long-term fermentation processes remain the major challenges for successful application of immobilised cell technology on an industrial scale. The key factors for the implementation of this technology on an industrial level are carrier materials, immobilization technology and bioreactor design. The purpose of this chapter is to summarise and discuss the main cell immobilization methods, process requirements, available carrier materials and bioreactor designs aimed for better yeast physiology control and fine-tuning of the flavor formation during beer fermentation process. Further, it will provide an overview on the latest important breakthroughs, accomplished in understanding of the effects of immobilization on yeast physiology, metabolism and fermentation behaviour.",
journal = "Encapsulation Technologies for Active Food Ingredients and Food Processing",
booktitle = "Bioprocess intensification of beer fermentation using immobilised cells",
pages = "325-303",
doi = "10.1007/978-1-4419-1008-0_11"
}
Verbelen, P.J., Nedović, V., Manojlović, V., Delvaux, F.R., Laskošek-Čukalović, I., Bugarski, B.,& Willaert, R.. (2010). Bioprocess intensification of beer fermentation using immobilised cells. in Encapsulation Technologies for Active Food Ingredients and Food Processing, 303-325.
https://doi.org/10.1007/978-1-4419-1008-0_11
Verbelen P, Nedović V, Manojlović V, Delvaux F, Laskošek-Čukalović I, Bugarski B, Willaert R. Bioprocess intensification of beer fermentation using immobilised cells. in Encapsulation Technologies for Active Food Ingredients and Food Processing. 2010;:303-325.
doi:10.1007/978-1-4419-1008-0_11 .
Verbelen, P.J., Nedović, Viktor, Manojlović, Verica, Delvaux, F.R., Laskošek-Čukalović, I., Bugarski, Branko, Willaert, R., "Bioprocess intensification of beer fermentation using immobilised cells" in Encapsulation Technologies for Active Food Ingredients and Food Processing (2010):303-325,
https://doi.org/10.1007/978-1-4419-1008-0_11 . .
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Modeling of microenvironmetal restricted yeast cell growth within Ca-alginate microbead

Pajić-Lijaković, Ivana; Plavsić, M.; Nedović, Viktor; Bugarski, Branko

(2008)

TY  - CONF
AU  - Pajić-Lijaković, Ivana
AU  - Plavsić, M.
AU  - Nedović, Viktor
AU  - Bugarski, Branko
PY  - 2008
UR  - http://aspace.agrif.bg.ac.rs/handle/123456789/1638
AB  - Aim. A phase-field mathematical model was formulated to describe yeast cell growth within the Ca-alginate microbead during air-lift bioreactor cultivation. Model development was based on experimentally obtained data for the intra-bead yeast cell volume fraction profile within the microbead after reaching the equilibrium state for cells (150 h), as well as, total yeast cell volume fraction per microbead and microbead volume as functions time. Microbead with growing yeast cells is treated as a two-phase system. one phase represents the cell agglomerates, while the other is the alginate hydrogel matrices. The interactions between phases are simulated using the Langevin class, non-conservative phasefield model based on the reduction of the modeling resolution. The model considered the growth of small domains of one phase (cell agglomerates) as nucleation. Methods. Total yeast cell volume fraction in the beads was estimated by using Thoma counting chamber after dissolution of beads. Local cell volume fraction per microbead layers is calculated from experimentally determined surface fraction of cells for various microbead cross sections by image analysis. Microbead volume is estimated by measuring the microbead diameter. Diameters of microbeads were measured using the optical microscope equipped with a micrometric device. Results. The proposed model offered the only one model parameter, which represents the specific measure of microenvironmental restrictive action to the cell growth dynamics. The optimal value of this model parameter is obtained by comparison analysis between experimental data and model predictions. Conclusion. Besides giving useful insights into the dynamics of restrictive cell growth within the Ca-alginate microbead, the model can be used as a tool to design/optimize the performance of microbead and studying the microenvironmental restrictive mechanism action of the cell growth.
C3  - Minerva Biotecnologica
T1  - Modeling of microenvironmetal restricted yeast cell growth within Ca-alginate microbead
EP  - 102
IS  - 2
SP  - 99
VL  - 20
UR  - https://hdl.handle.net/21.15107/rcub_agrospace_1638
ER  - 
@conference{
author = "Pajić-Lijaković, Ivana and Plavsić, M. and Nedović, Viktor and Bugarski, Branko",
year = "2008",
abstract = "Aim. A phase-field mathematical model was formulated to describe yeast cell growth within the Ca-alginate microbead during air-lift bioreactor cultivation. Model development was based on experimentally obtained data for the intra-bead yeast cell volume fraction profile within the microbead after reaching the equilibrium state for cells (150 h), as well as, total yeast cell volume fraction per microbead and microbead volume as functions time. Microbead with growing yeast cells is treated as a two-phase system. one phase represents the cell agglomerates, while the other is the alginate hydrogel matrices. The interactions between phases are simulated using the Langevin class, non-conservative phasefield model based on the reduction of the modeling resolution. The model considered the growth of small domains of one phase (cell agglomerates) as nucleation. Methods. Total yeast cell volume fraction in the beads was estimated by using Thoma counting chamber after dissolution of beads. Local cell volume fraction per microbead layers is calculated from experimentally determined surface fraction of cells for various microbead cross sections by image analysis. Microbead volume is estimated by measuring the microbead diameter. Diameters of microbeads were measured using the optical microscope equipped with a micrometric device. Results. The proposed model offered the only one model parameter, which represents the specific measure of microenvironmental restrictive action to the cell growth dynamics. The optimal value of this model parameter is obtained by comparison analysis between experimental data and model predictions. Conclusion. Besides giving useful insights into the dynamics of restrictive cell growth within the Ca-alginate microbead, the model can be used as a tool to design/optimize the performance of microbead and studying the microenvironmental restrictive mechanism action of the cell growth.",
journal = "Minerva Biotecnologica",
title = "Modeling of microenvironmetal restricted yeast cell growth within Ca-alginate microbead",
pages = "102-99",
number = "2",
volume = "20",
url = "https://hdl.handle.net/21.15107/rcub_agrospace_1638"
}
Pajić-Lijaković, I., Plavsić, M., Nedović, V.,& Bugarski, B.. (2008). Modeling of microenvironmetal restricted yeast cell growth within Ca-alginate microbead. in Minerva Biotecnologica, 20(2), 99-102.
https://hdl.handle.net/21.15107/rcub_agrospace_1638
Pajić-Lijaković I, Plavsić M, Nedović V, Bugarski B. Modeling of microenvironmetal restricted yeast cell growth within Ca-alginate microbead. in Minerva Biotecnologica. 2008;20(2):99-102.
https://hdl.handle.net/21.15107/rcub_agrospace_1638 .
Pajić-Lijaković, Ivana, Plavsić, M., Nedović, Viktor, Bugarski, Branko, "Modeling of microenvironmetal restricted yeast cell growth within Ca-alginate microbead" in Minerva Biotecnologica, 20, no. 2 (2008):99-102,
https://hdl.handle.net/21.15107/rcub_agrospace_1638 .
6
6

Ca-alginate hydrogel mechanical transformations - The influence on yeast cell growth dynamics

Pajić-Lijaković, Ivana; Plavsić, Milenko; Bugarski, Branko; Nedović, Viktor

(Elsevier, Amsterdam, 2007)

TY  - JOUR
AU  - Pajić-Lijaković, Ivana
AU  - Plavsić, Milenko
AU  - Bugarski, Branko
AU  - Nedović, Viktor
PY  - 2007
UR  - http://aspace.agrif.bg.ac.rs/handle/123456789/1494
AB  - A mathematical model was formulated to describe yeast cell growth within the Ca-alginate microbead during air-lift bioreactor cultivation. Model development was based on experimentally obtained data for the intra-bead cell concentration profile, after reached the equilibrium state, as well as, total yeast cell concentration per microbed and microbead volume as function of time. Relatively uniform cell concentration in the carrier matrix indicated that no internal nutrient diffusion limitations, but microenvironmental restriction, affected dominantly the dynamics of cell growth. Also interesting phenomenon of very different rates of cell number growth during cultivation is observed. After some critical time, the growth rate of cell colonies decreased drastically, but than suddenly increased again under all other experimental condition been the same. It is interpreted as disintegration of gel network and opening new free space for growth of cell clusters. These complex phenomena are modeled using the thermodynamical, free energy formalism. The particular form of free energy functional is proposed to describe various kinds of interactions, which affected the dynamics of cell growth and cause pseudo-phase transition of hydrogel. The good agreement of experimentally obtained data and model predictions are obtained. In that way the model provides both, the quantitative tools for further technological optimization of the process and deeper insight into dynamics of cell growth mechanism.
PB  - Elsevier, Amsterdam
T2  - Journal of Biotechnology
T1  - Ca-alginate hydrogel mechanical transformations - The influence on yeast cell growth dynamics
EP  - 452
IS  - 3
SP  - 446
VL  - 129
DO  - 10.1016/j.jbiotec.2007.01.017
ER  - 
@article{
author = "Pajić-Lijaković, Ivana and Plavsić, Milenko and Bugarski, Branko and Nedović, Viktor",
year = "2007",
abstract = "A mathematical model was formulated to describe yeast cell growth within the Ca-alginate microbead during air-lift bioreactor cultivation. Model development was based on experimentally obtained data for the intra-bead cell concentration profile, after reached the equilibrium state, as well as, total yeast cell concentration per microbed and microbead volume as function of time. Relatively uniform cell concentration in the carrier matrix indicated that no internal nutrient diffusion limitations, but microenvironmental restriction, affected dominantly the dynamics of cell growth. Also interesting phenomenon of very different rates of cell number growth during cultivation is observed. After some critical time, the growth rate of cell colonies decreased drastically, but than suddenly increased again under all other experimental condition been the same. It is interpreted as disintegration of gel network and opening new free space for growth of cell clusters. These complex phenomena are modeled using the thermodynamical, free energy formalism. The particular form of free energy functional is proposed to describe various kinds of interactions, which affected the dynamics of cell growth and cause pseudo-phase transition of hydrogel. The good agreement of experimentally obtained data and model predictions are obtained. In that way the model provides both, the quantitative tools for further technological optimization of the process and deeper insight into dynamics of cell growth mechanism.",
publisher = "Elsevier, Amsterdam",
journal = "Journal of Biotechnology",
title = "Ca-alginate hydrogel mechanical transformations - The influence on yeast cell growth dynamics",
pages = "452-446",
number = "3",
volume = "129",
doi = "10.1016/j.jbiotec.2007.01.017"
}
Pajić-Lijaković, I., Plavsić, M., Bugarski, B.,& Nedović, V.. (2007). Ca-alginate hydrogel mechanical transformations - The influence on yeast cell growth dynamics. in Journal of Biotechnology
Elsevier, Amsterdam., 129(3), 446-452.
https://doi.org/10.1016/j.jbiotec.2007.01.017
Pajić-Lijaković I, Plavsić M, Bugarski B, Nedović V. Ca-alginate hydrogel mechanical transformations - The influence on yeast cell growth dynamics. in Journal of Biotechnology. 2007;129(3):446-452.
doi:10.1016/j.jbiotec.2007.01.017 .
Pajić-Lijaković, Ivana, Plavsić, Milenko, Bugarski, Branko, Nedović, Viktor, "Ca-alginate hydrogel mechanical transformations - The influence on yeast cell growth dynamics" in Journal of Biotechnology, 129, no. 3 (2007):446-452,
https://doi.org/10.1016/j.jbiotec.2007.01.017 . .
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