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Development of technologies and products based on mineral raw materials and waste biomass for protection of natural resources for safe food production

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Development of technologies and products based on mineral raw materials and waste biomass for protection of natural resources for safe food production (en)
Развој технологија и производа на бази минералних сировина и отпадне биомасе у циљу заштите ресурса за производњу безбедне хране (sr)
Razvoj tehnologija i proizvoda na bazi mineralnih sirovina i otpadne biomase u cilju zaštite resursa za proizvodnju bezbedne hrane (sr_RS)
Authors

Publications

Effects of different mechanical treatments on structural changes of lignocellulosic waste biomass and subsequent Cu(II) removal kinetics

Lopičić, Zorica; Stojanović, Mirjana; Marković, Smilja; Milojković, Jelena V.; Mihajlović, Marija L.; Kaluđerović Radoičić, Tatjana S.; Kijevčanin, Mirjana Lj.

(Elsevier, 2019)

TY  - JOUR
AU  - Lopičić, Zorica
AU  - Stojanović, Mirjana
AU  - Marković, Smilja
AU  - Milojković, Jelena V.
AU  - Mihajlović, Marija L.
AU  - Kaluđerović Radoičić, Tatjana S.
AU  - Kijevčanin, Mirjana Lj.
PY  - 2019
UR  - http://dais.sanu.ac.rs/123456789/2312
AB  - In this paper, the character of structural changes induced by different mechanical treatments to Prunus persica stones (PSs), and its subsequent effect on biosorption kinetics of Cu(II) were investigated. PSs were processed in vibratory disk mill (PS-V) and ultra-centrifugal mill (PS-C) and characterized by XRD, BET, SEM and FTIR spectroscopy. It was shown that PS-V was smaller and more reactive with less crystallinity index and hydrogen bond intensity compared to PS-C. In opposite, surface area of the PS-C was bigger than that of the PS-V. The total pore volume was about threefold, while the volume of micro pores was 9.29 times higher in PS-Cs than in PS-Vs.

The kinetics of Cu(II) biosorption by both PSs was tested through various kinetic models: pseudo-first and pseudo-second order rate equations, Elovich equation, Boyd model, Weber–Morris and Urano–Tachikawa intraparticle diffusion model. For both sample types, Cu(II) biosorption occurred through combination of intraparticle and film diffusion mechanism, while kinetic results were best described by the pseudo-second order kinetic model. At the same time, the results indicated that together with kinetic rate the biosorption capacity of PS-C (21.20 mg g−1) was higher than that of PS-V (16.30 mg g−1).

Mechanical activation like crushing and grinding will change material particle size, specific surface area and porosity, as well as its crystallinity. However, this paper elucidates that such physical structural changes will impact on heavy metal ions removal efficiency. This investigation suggests that the type of size reduction in lignocellulosic biosorbent preparation plays a very important role in overall biosorption performance, so it should be carefully considered every time when the mechanical treatment of material is necessary to be applied.
PB  - Elsevier
T2  - Arabian Journal of Chemistry
T1  - Effects of different mechanical treatments on structural changes of lignocellulosic waste biomass and subsequent Cu(II) removal kinetics
SP  - 4091
EP  - 4103
VL  - 12
IS  - 8
DO  - 10.1016/j.arabjc.2016.04.005
ER  - 
@article{
author = "Lopičić, Zorica and Stojanović, Mirjana and Marković, Smilja and Milojković, Jelena V. and Mihajlović, Marija L. and Kaluđerović Radoičić, Tatjana S. and Kijevčanin, Mirjana Lj.",
year = "2019",
url = "http://dais.sanu.ac.rs/123456789/2312",
abstract = "In this paper, the character of structural changes induced by different mechanical treatments to Prunus persica stones (PSs), and its subsequent effect on biosorption kinetics of Cu(II) were investigated. PSs were processed in vibratory disk mill (PS-V) and ultra-centrifugal mill (PS-C) and characterized by XRD, BET, SEM and FTIR spectroscopy. It was shown that PS-V was smaller and more reactive with less crystallinity index and hydrogen bond intensity compared to PS-C. In opposite, surface area of the PS-C was bigger than that of the PS-V. The total pore volume was about threefold, while the volume of micro pores was 9.29 times higher in PS-Cs than in PS-Vs.

The kinetics of Cu(II) biosorption by both PSs was tested through various kinetic models: pseudo-first and pseudo-second order rate equations, Elovich equation, Boyd model, Weber–Morris and Urano–Tachikawa intraparticle diffusion model. For both sample types, Cu(II) biosorption occurred through combination of intraparticle and film diffusion mechanism, while kinetic results were best described by the pseudo-second order kinetic model. At the same time, the results indicated that together with kinetic rate the biosorption capacity of PS-C (21.20 mg g−1) was higher than that of PS-V (16.30 mg g−1).

Mechanical activation like crushing and grinding will change material particle size, specific surface area and porosity, as well as its crystallinity. However, this paper elucidates that such physical structural changes will impact on heavy metal ions removal efficiency. This investigation suggests that the type of size reduction in lignocellulosic biosorbent preparation plays a very important role in overall biosorption performance, so it should be carefully considered every time when the mechanical treatment of material is necessary to be applied.",
publisher = "Elsevier",
journal = "Arabian Journal of Chemistry",
title = "Effects of different mechanical treatments on structural changes of lignocellulosic waste biomass and subsequent Cu(II) removal kinetics",
pages = "4091-4103",
volume = "12",
number = "8",
doi = "10.1016/j.arabjc.2016.04.005"
}
12
10
15

Application of raw peach shell particles for removal of methylene blue

Marković, Smilja; Stanković, Ana; Lopičić, Zorica; Lazarević, Slavica; Stojanović, Mirjana; Uskoković, Dragan

(Elsevier, 2015)

TY  - JOUR
AU  - Marković, Smilja
AU  - Stanković, Ana
AU  - Lopičić, Zorica
AU  - Lazarević, Slavica
AU  - Stojanović, Mirjana
AU  - Uskoković, Dragan
PY  - 2015
UR  - http://dais.sanu.ac.rs/123456789/3524
AB  - A possibility to apply raw, powdered peach shells (PS) as a biosorbent for water purification was studied. The PSs are locally available as a solid waste in a fruit juice factory; methylene blue (MB) was chosen as representative of common pollutants in textile industry wastewater. The phase composition of prepared particles was identified by XRD. The particle morphology was characterized by FE-SEM, while the size distribution was measured by a laser light-scattering particle size analyzer. The BET specific surface area was determined from N2 adsorption/desorption experiments. The effect of operating parameters: the biosorbent amount (50-1000 mg/100 mL), contact time (10-180 min), solution pH (2-12) and initial concentration (10-100 ppm) on biosorption efficiency was examined. Optimal conditions for MB removal were found to be: the biosorbent amount of 400 mg/100 mL and pH 5.5. A high efficiency of MB removal was established after 180 min: 99% for [MB]i = 10 ppm and 76% for [MB]i = 100 ppm. Biosorption is well described by the Freundlich- and BET-type isotherms, implicating heterogeneous adsorption sites and interconnections between adsorbed molecules. The FTIR spectroscopy results indicate hydrogen bonding between the dye and the biomass. The obtained results shown that raw peach shell particles could be used as an efficient low-cost biosorbent for dye removal from water. © 2015 Elsevier Ltd.
PB  - Elsevier
T2  - Journal of Environmental Chemical Engineering
T1  - Application of raw peach shell particles for removal of methylene blue
SP  - 716
EP  - 724
VL  - 3
IS  - 2
DO  - 10.1016/j.jece.2015.04.002
ER  - 
@article{
author = "Marković, Smilja and Stanković, Ana and Lopičić, Zorica and Lazarević, Slavica and Stojanović, Mirjana and Uskoković, Dragan",
year = "2015",
url = "http://dais.sanu.ac.rs/123456789/3524",
abstract = "A possibility to apply raw, powdered peach shells (PS) as a biosorbent for water purification was studied. The PSs are locally available as a solid waste in a fruit juice factory; methylene blue (MB) was chosen as representative of common pollutants in textile industry wastewater. The phase composition of prepared particles was identified by XRD. The particle morphology was characterized by FE-SEM, while the size distribution was measured by a laser light-scattering particle size analyzer. The BET specific surface area was determined from N2 adsorption/desorption experiments. The effect of operating parameters: the biosorbent amount (50-1000 mg/100 mL), contact time (10-180 min), solution pH (2-12) and initial concentration (10-100 ppm) on biosorption efficiency was examined. Optimal conditions for MB removal were found to be: the biosorbent amount of 400 mg/100 mL and pH 5.5. A high efficiency of MB removal was established after 180 min: 99% for [MB]i = 10 ppm and 76% for [MB]i = 100 ppm. Biosorption is well described by the Freundlich- and BET-type isotherms, implicating heterogeneous adsorption sites and interconnections between adsorbed molecules. The FTIR spectroscopy results indicate hydrogen bonding between the dye and the biomass. The obtained results shown that raw peach shell particles could be used as an efficient low-cost biosorbent for dye removal from water. © 2015 Elsevier Ltd.",
publisher = "Elsevier",
journal = "Journal of Environmental Chemical Engineering",
title = "Application of raw peach shell particles for removal of methylene blue",
pages = "716-724",
volume = "3",
number = "2",
doi = "10.1016/j.jece.2015.04.002"
}
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