Veličković, Ana

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Modeling the biodiesel production using the wheat straw ash as a catalyst

Veličković, Ana; Avramović, Jelena M.; Kostić, Milan; Krstić, Jugoslav; Stamenković, Olivera; Veljković, Vlada B.

(Belgrade : Association of the Chemical Engineers of Serbia, 2021)

TY  - JOUR
AU  - Veličković, Ana
AU  - Avramović, Jelena M.
AU  - Kostić, Milan
AU  - Krstić, Jugoslav
AU  - Stamenković, Olivera
AU  - Veljković, Vlada B.
PY  - 2021
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/4844
AB  - Wheat straw ash (WSA) was investigated as a new catalyst in biodiesel production from sunflower oil. The catalyst was characterized by temperature-programmed decomposition, X-ray powder diffraction, Hg porosimetry, N2 physisorption, and scanning electron microscopy - energy dispersive X-ray spectroscopy methods. The methanolysis reaction was tested in the temperature range of 55–65 oC, the catalyst loading range 10–20 % of the oil weight, and the methanol-to-oil molar ratio range 18 : 1–24 : 1. The reaction conditions of the sunflower oil methanolysis over WSA were optimized by using the response surface methodology in combination with the historical experimental design. The optimum process conditions ensuring the highest fatty acid methyl esters (FAME) content of 98.6 % were the reaction temperature of 60.3 oC, the catalyst loading of 11.6 % (based on the oil weight), the methanol-to-oil molar ratio of 18.3 :1, and the reaction time of 124 min. The values of the statistical criteria, such as coefficients of determination (R2 = 0.811, R2pred = 0.789, R2adj = 0.761) and the mean relative percent deviation (MRPD) value of 10.6 % (66 data) implied the acceptability and precision of the developed model. The FAME content after 4 h of reaction under the optimal conditions decreased to 37, 12, and 3 %, after the first, second, and third reuse, respectively.
AB  - Pepeo pšenične slame (PPS) je korišćen kao katalizator u proizvodnji biodizela iz sunco-kretovog ulja. Karakterizacija katalizatora je izvršena primenom metoda tempera-turski programiranom razgradnjom (temperature-programmed decomposition, TPDe), rentgenskom difrakcijom (X-ray diffraction, XRD), Hg porozimetrijom, N2 fizi-sorpcijom i skenirajućom elektronskom mikrosopijom sa energo-disperzivnom spek-trometrijom (scanning electron microscopy and energy dispersive X-ray spectroscopy, SEM-EDS). Reakcija metanolize istraživana je pri sledećim reakcionim uslovima: tem-peraturni opseg 55-65 °C; količina katalizatora 10-20 % (računato na masu ulja) i opseg molskog odnosa methanol : ulje 18 : 1 – 24 : 1. Optimizacija reakcionih uslova izvršena je metodologijom površine odziva u kombinaciji sa istorijskim eksperimentalnim planom. Maksimalni prinos metil estara masnih kiselina (MEMK) od 98,6 % postignut je pri sledećim optimalnim reakcionim uslovima: temperatura 60,3 oC, količina katalizatora 11,6 % (računato na masu ulja), molski odnos methanol : ulje 18,3 : 1 i vreme trajanja reakcije 124 min. Vrednosti koeficijenata determinacije (R2 = 0,811, R2pred = 0,789, R2adj = 0,761) i srednjeg relativnog odstupanja (10,6 %, 66 podataka) ukazali su na prihvatljivost i pouzdanost razvijenog modela. Sadržaj MEMK nakon 4 h reakcije pri optimalnim uslovima smanjen je na 37, 12 i 3 % nakon prve, druge i treće upotrebe katalizatora, redom.
PB  - Belgrade : Association of the Chemical Engineers of Serbia
T2  - Hemijska industrija
T1  - Modeling the biodiesel production using the wheat straw ash as a catalyst
T1  - Pepeo pšenične slame kao katalizator u proizvodnji biodizela
VL  - 75
IS  - 5
SP  - 257
EP  - 276
DO  - 10.2298/HEMIND210526028V
ER  - 
@article{
author = "Veličković, Ana and Avramović, Jelena M. and Kostić, Milan and Krstić, Jugoslav and Stamenković, Olivera and Veljković, Vlada B.",
year = "2021",
abstract = "Wheat straw ash (WSA) was investigated as a new catalyst in biodiesel production from sunflower oil. The catalyst was characterized by temperature-programmed decomposition, X-ray powder diffraction, Hg porosimetry, N2 physisorption, and scanning electron microscopy - energy dispersive X-ray spectroscopy methods. The methanolysis reaction was tested in the temperature range of 55–65 oC, the catalyst loading range 10–20 % of the oil weight, and the methanol-to-oil molar ratio range 18 : 1–24 : 1. The reaction conditions of the sunflower oil methanolysis over WSA were optimized by using the response surface methodology in combination with the historical experimental design. The optimum process conditions ensuring the highest fatty acid methyl esters (FAME) content of 98.6 % were the reaction temperature of 60.3 oC, the catalyst loading of 11.6 % (based on the oil weight), the methanol-to-oil molar ratio of 18.3 :1, and the reaction time of 124 min. The values of the statistical criteria, such as coefficients of determination (R2 = 0.811, R2pred = 0.789, R2adj = 0.761) and the mean relative percent deviation (MRPD) value of 10.6 % (66 data) implied the acceptability and precision of the developed model. The FAME content after 4 h of reaction under the optimal conditions decreased to 37, 12, and 3 %, after the first, second, and third reuse, respectively., Pepeo pšenične slame (PPS) je korišćen kao katalizator u proizvodnji biodizela iz sunco-kretovog ulja. Karakterizacija katalizatora je izvršena primenom metoda tempera-turski programiranom razgradnjom (temperature-programmed decomposition, TPDe), rentgenskom difrakcijom (X-ray diffraction, XRD), Hg porozimetrijom, N2 fizi-sorpcijom i skenirajućom elektronskom mikrosopijom sa energo-disperzivnom spek-trometrijom (scanning electron microscopy and energy dispersive X-ray spectroscopy, SEM-EDS). Reakcija metanolize istraživana je pri sledećim reakcionim uslovima: tem-peraturni opseg 55-65 °C; količina katalizatora 10-20 % (računato na masu ulja) i opseg molskog odnosa methanol : ulje 18 : 1 – 24 : 1. Optimizacija reakcionih uslova izvršena je metodologijom površine odziva u kombinaciji sa istorijskim eksperimentalnim planom. Maksimalni prinos metil estara masnih kiselina (MEMK) od 98,6 % postignut je pri sledećim optimalnim reakcionim uslovima: temperatura 60,3 oC, količina katalizatora 11,6 % (računato na masu ulja), molski odnos methanol : ulje 18,3 : 1 i vreme trajanja reakcije 124 min. Vrednosti koeficijenata determinacije (R2 = 0,811, R2pred = 0,789, R2adj = 0,761) i srednjeg relativnog odstupanja (10,6 %, 66 podataka) ukazali su na prihvatljivost i pouzdanost razvijenog modela. Sadržaj MEMK nakon 4 h reakcije pri optimalnim uslovima smanjen je na 37, 12 i 3 % nakon prve, druge i treće upotrebe katalizatora, redom.",
publisher = "Belgrade : Association of the Chemical Engineers of Serbia",
journal = "Hemijska industrija",
title = "Modeling the biodiesel production using the wheat straw ash as a catalyst, Pepeo pšenične slame kao katalizator u proizvodnji biodizela",
volume = "75",
number = "5",
pages = "257-276",
doi = "10.2298/HEMIND210526028V"
}
Veličković, A., Avramović, J. M., Kostić, M., Krstić, J., Stamenković, O.,& Veljković, V. B.. (2021). Modeling the biodiesel production using the wheat straw ash as a catalyst. in Hemijska industrija
Belgrade : Association of the Chemical Engineers of Serbia., 75(5), 257-276.
https://doi.org/10.2298/HEMIND210526028V
Veličković A, Avramović JM, Kostić M, Krstić J, Stamenković O, Veljković VB. Modeling the biodiesel production using the wheat straw ash as a catalyst. in Hemijska industrija. 2021;75(5):257-276.
doi:10.2298/HEMIND210526028V .
Veličković, Ana, Avramović, Jelena M., Kostić, Milan, Krstić, Jugoslav, Stamenković, Olivera, Veljković, Vlada B., "Modeling the biodiesel production using the wheat straw ash as a catalyst" in Hemijska industrija, 75, no. 5 (2021):257-276,
https://doi.org/10.2298/HEMIND210526028V . .
5

The synthesis of CaO loaded onto Al2O3 from calcium acetate and its application in transesterification of the sunflower oil

Marinković, Dalibor; Stanković, Miroslav; Veličković, Ana; Avramović, Jelena M.; Cakić, Milorad D.; Veljković, Vlada B.

(Tehnološki fakultet, Leskovac, 2015)

TY  - JOUR
AU  - Marinković, Dalibor
AU  - Stanković, Miroslav
AU  - Veličković, Ana
AU  - Avramović, Jelena M.
AU  - Cakić, Milorad D.
AU  - Veljković, Vlada B.
PY  - 2015
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/1774
AB  - Transesterification of sunflower oil was carried out over CaO loaded onto γ-Al2O3 as heterogeneous base catalysts. The solid base catalysts were syn­thesized by the modified wet impregnation of calcium acetate monohydrate onto neutral γ-Al2O3, calcined at different temperatures in an inert atmosphere and characterized by FESEM, XRPD and FTIR techniques. The catalyst con­taining 5.5 wt. % CaO supported on γ-Al2O3 calcined at 700°C exhibited the highest FAME yield at mild reaction conditions (60°C, atmospheric pressure, methanol-to-oil molar ratio of 9:1 and 0.51% of active species-CaO by weight of oil). The best CaO/γ-Al2O3 catalyst showed a similar or lower catalytic activity than some other CaO-based catalysts at a smaller amount of the catalyst (at least two times less than in other studies).
AB  - Transesterifikacija jestivog suncokretovog ulja izvršena je korišćenjem CaO nanešenog na γ-Al2O3 kao heterogenog baznog katalizatora. Katalizator je si-ntetisan korišćenjem modifikovane metode mokre impregnacije gde je kalcijum acetat monohidrat kao precursor nanešen na neutralnu γ-Al2O3. Karakterizacija katalizatora je urađena korišćenjem sledećih metoda: FESEM, XRPD i FTIR. Na katalitičku aktivnost, a samim tim i prinos metil estara masnih kiselina, utiču morfologija i sastav katalizatora pripremljenog kalcinacijom na različitim temperatu­rama. U reakciji transesterifikacije suncokretovog ulja pri umerenim reakcionim uslovima (60°C, molski odnos metanola:ulja 9:1 i količina CaO 0,51% u odnosu na masu ulja) katalitički najaktivniji je katalizator sa 5,5 mas. % CaO nanešenih na nosač i kalcinisan na 700°C. U poređenju sa literaturnim rezultatima drugih katalizatora baziranih na CaO, primenjenim u sličnim reakcionim uslovima CaO/ γ-Al2O3 je pokazao sličnu ili nižu katalitičku aktivnost. Razlog tome je zato što je u ovom radu korišćena najmanje dva puta manja količina katalizatora po eksperimentu u odnosu na istraživanja sa kojima je vršeno poređenje.
PB  - Tehnološki fakultet, Leskovac
T2  - Advanced Technologies
T1  - The synthesis of CaO loaded onto Al2O3 from calcium acetate and its application in transesterification of the sunflower oil
T1  - Sinteza CaO nanešenog na Al2O3 od prekursora kalcujum acetata i njegova primena u transesterifikaciji suncokretovog ulja
VL  - 4
IS  - 1
SP  - 26
EP  - 32
DO  - 10.5937/savteh1501026M
ER  - 
@article{
author = "Marinković, Dalibor and Stanković, Miroslav and Veličković, Ana and Avramović, Jelena M. and Cakić, Milorad D. and Veljković, Vlada B.",
year = "2015",
abstract = "Transesterification of sunflower oil was carried out over CaO loaded onto γ-Al2O3 as heterogeneous base catalysts. The solid base catalysts were syn­thesized by the modified wet impregnation of calcium acetate monohydrate onto neutral γ-Al2O3, calcined at different temperatures in an inert atmosphere and characterized by FESEM, XRPD and FTIR techniques. The catalyst con­taining 5.5 wt. % CaO supported on γ-Al2O3 calcined at 700°C exhibited the highest FAME yield at mild reaction conditions (60°C, atmospheric pressure, methanol-to-oil molar ratio of 9:1 and 0.51% of active species-CaO by weight of oil). The best CaO/γ-Al2O3 catalyst showed a similar or lower catalytic activity than some other CaO-based catalysts at a smaller amount of the catalyst (at least two times less than in other studies)., Transesterifikacija jestivog suncokretovog ulja izvršena je korišćenjem CaO nanešenog na γ-Al2O3 kao heterogenog baznog katalizatora. Katalizator je si-ntetisan korišćenjem modifikovane metode mokre impregnacije gde je kalcijum acetat monohidrat kao precursor nanešen na neutralnu γ-Al2O3. Karakterizacija katalizatora je urađena korišćenjem sledećih metoda: FESEM, XRPD i FTIR. Na katalitičku aktivnost, a samim tim i prinos metil estara masnih kiselina, utiču morfologija i sastav katalizatora pripremljenog kalcinacijom na različitim temperatu­rama. U reakciji transesterifikacije suncokretovog ulja pri umerenim reakcionim uslovima (60°C, molski odnos metanola:ulja 9:1 i količina CaO 0,51% u odnosu na masu ulja) katalitički najaktivniji je katalizator sa 5,5 mas. % CaO nanešenih na nosač i kalcinisan na 700°C. U poređenju sa literaturnim rezultatima drugih katalizatora baziranih na CaO, primenjenim u sličnim reakcionim uslovima CaO/ γ-Al2O3 je pokazao sličnu ili nižu katalitičku aktivnost. Razlog tome je zato što je u ovom radu korišćena najmanje dva puta manja količina katalizatora po eksperimentu u odnosu na istraživanja sa kojima je vršeno poređenje.",
publisher = "Tehnološki fakultet, Leskovac",
journal = "Advanced Technologies",
title = "The synthesis of CaO loaded onto Al2O3 from calcium acetate and its application in transesterification of the sunflower oil, Sinteza CaO nanešenog na Al2O3 od prekursora kalcujum acetata i njegova primena u transesterifikaciji suncokretovog ulja",
volume = "4",
number = "1",
pages = "26-32",
doi = "10.5937/savteh1501026M"
}
Marinković, D., Stanković, M., Veličković, A., Avramović, J. M., Cakić, M. D.,& Veljković, V. B.. (2015). The synthesis of CaO loaded onto Al2O3 from calcium acetate and its application in transesterification of the sunflower oil. in Advanced Technologies
Tehnološki fakultet, Leskovac., 4(1), 26-32.
https://doi.org/10.5937/savteh1501026M
Marinković D, Stanković M, Veličković A, Avramović JM, Cakić MD, Veljković VB. The synthesis of CaO loaded onto Al2O3 from calcium acetate and its application in transesterification of the sunflower oil. in Advanced Technologies. 2015;4(1):26-32.
doi:10.5937/savteh1501026M .
Marinković, Dalibor, Stanković, Miroslav, Veličković, Ana, Avramović, Jelena M., Cakić, Milorad D., Veljković, Vlada B., "The synthesis of CaO loaded onto Al2O3 from calcium acetate and its application in transesterification of the sunflower oil" in Advanced Technologies, 4, no. 1 (2015):26-32,
https://doi.org/10.5937/savteh1501026M . .
1

Preparation of CaO/γ-Al2O3 catalyst for biodiesel fuels. The catalytic activity in relation to thermal treatment

Marinković, Dalibor; Stanković, Miroslav; Nedić-Vasiljević, Bojana; Veličković, Ana; Avramović, Jelena M.

(Society of Physical Chemists of Serbia, 2014)

TY  - CONF
AU  - Marinković, Dalibor
AU  - Stanković, Miroslav
AU  - Nedić-Vasiljević, Bojana
AU  - Veličković, Ana
AU  - Avramović, Jelena M.
PY  - 2014
UR  - http://www.socphyschemserb.org/en/events/pc2014/
UR  - https://cer.ihtm.bg.ac.rs/handle/123456789/2914
AB  - A heterogeneous base catalyst (CaO/γ-Al2O3) for biodiesel production from sunflower oil was prepared by the impregnation method. The catalyst was characterized by means of MIP and XRD methods. The catalytic activity of the nitrate-derived CaO/γ-Al2O3 was determined in relation to the
calcination temperature ranging from 425 to 500 °C. The reaction was carried out in a batch type of reactor equipped with a reflux condenser. The maximum yield of biodiesel of almost 95% was achieved with the catalyst calcined at 475 °C under the following reaction conditions: reaction
temperature of 60 °C, methanol to oil molar ratio of 12/1, reaction time of 5 h.
PB  - Society of Physical Chemists of Serbia
C3  - Physical Chemistry 2014 - 12th International Conference on fundamental and applied aspects of Physical chemistry
T1  - Preparation of CaO/γ-Al2O3 catalyst for biodiesel fuels. The catalytic activity in relation to thermal treatment
VL  - 1
SP  - 288
EP  - 291
UR  - https://hdl.handle.net/21.15107/rcub_cer_2914
ER  - 
@conference{
author = "Marinković, Dalibor and Stanković, Miroslav and Nedić-Vasiljević, Bojana and Veličković, Ana and Avramović, Jelena M.",
year = "2014",
abstract = "A heterogeneous base catalyst (CaO/γ-Al2O3) for biodiesel production from sunflower oil was prepared by the impregnation method. The catalyst was characterized by means of MIP and XRD methods. The catalytic activity of the nitrate-derived CaO/γ-Al2O3 was determined in relation to the
calcination temperature ranging from 425 to 500 °C. The reaction was carried out in a batch type of reactor equipped with a reflux condenser. The maximum yield of biodiesel of almost 95% was achieved with the catalyst calcined at 475 °C under the following reaction conditions: reaction
temperature of 60 °C, methanol to oil molar ratio of 12/1, reaction time of 5 h.",
publisher = "Society of Physical Chemists of Serbia",
journal = "Physical Chemistry 2014 - 12th International Conference on fundamental and applied aspects of Physical chemistry",
title = "Preparation of CaO/γ-Al2O3 catalyst for biodiesel fuels. The catalytic activity in relation to thermal treatment",
volume = "1",
pages = "288-291",
url = "https://hdl.handle.net/21.15107/rcub_cer_2914"
}
Marinković, D., Stanković, M., Nedić-Vasiljević, B., Veličković, A.,& Avramović, J. M.. (2014). Preparation of CaO/γ-Al2O3 catalyst for biodiesel fuels. The catalytic activity in relation to thermal treatment. in Physical Chemistry 2014 - 12th International Conference on fundamental and applied aspects of Physical chemistry
Society of Physical Chemists of Serbia., 1, 288-291.
https://hdl.handle.net/21.15107/rcub_cer_2914
Marinković D, Stanković M, Nedić-Vasiljević B, Veličković A, Avramović JM. Preparation of CaO/γ-Al2O3 catalyst for biodiesel fuels. The catalytic activity in relation to thermal treatment. in Physical Chemistry 2014 - 12th International Conference on fundamental and applied aspects of Physical chemistry. 2014;1:288-291.
https://hdl.handle.net/21.15107/rcub_cer_2914 .
Marinković, Dalibor, Stanković, Miroslav, Nedić-Vasiljević, Bojana, Veličković, Ana, Avramović, Jelena M., "Preparation of CaO/γ-Al2O3 catalyst for biodiesel fuels. The catalytic activity in relation to thermal treatment" in Physical Chemistry 2014 - 12th International Conference on fundamental and applied aspects of Physical chemistry, 1 (2014):288-291,
https://hdl.handle.net/21.15107/rcub_cer_2914 .