Process optimization and kinetics of microwave assisted transesterification of crude glycerol for the production of glycerol carbonate

School of Engineering

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https://doi.org/10.1039/d0se01383h
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Keywords

Activation energy, Calcium oxide, Carbonation, Lime, Molar ratio, Optimization, Rate constants, Transesterification, Boxbehnken design (BBD), Conventional heating, Low-activation energy, Microwave assisted transesterification, Optimized conditions, Predictive accuracy, Process parameters, Reaction temperature, Glycerol

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Process optimization and kinetics of microwave assisted transesterification of crude glycerol for the production of glycerol carbonate. / Teng, W.K.; Yusoff, R.; Aroua, M.K. et al.
In: Sustainable Energy and Fuels, Vol. 5, No. 1, 07.01.2021, p. 274-282.

Research output: Contribution to Journal/Magazine › Journal article › peer-review

Bibtex

@article{3cbd34a68b5644788a80f6af6de14723,

title = "Process optimization and kinetics of microwave assisted transesterification of crude glycerol for the production of glycerol carbonate",

abstract = "The production of glycerol carbonate (GC) from industrial grade crude glycerol was catalyzed by calcium oxide (CaO) via microwave assisted transesterification (MAT). Influencing process parameters including reaction temperature, time and molar ratio of dimethyl carbonate/glycerol (DMC/Gly) were examined and optimized by applying Box Behnken Design (BBD). The reaction was modelled into a reduced cubic model with good predictive accuracy. A high GC yield of 99.5% was achieved with 1 wt% CaO at optimized conditions such as reaction temperature of 65 °C, reaction time of 3 min and DMC/Gly molar ratio of 2.5. The study performed on the reaction kinetics suggests that the reaction follows an irreversible second order rate equation. A relatively low activation energy of 4.53 kJ mol-1 was determined for the microwave assisted transesterification of crude glycerol for the production of GC. The values of rate constants between 45 °C to 65 °C were in the range of 0.023-0.026 L mol-1 min-1, which are of one magnitude order higher than that of the conventional heating. ",

keywords = "Activation energy, Calcium oxide, Carbonation, Lime, Molar ratio, Optimization, Rate constants, Transesterification, Boxbehnken design (BBD), Conventional heating, Low-activation energy, Microwave assisted transesterification, Optimized conditions, Predictive accuracy, Process parameters, Reaction temperature, Glycerol",

author = "W.K. Teng and R. Yusoff and M.K. Aroua and G.C. Ngoh",

year = "2021",

month = jan,

day = "7",

doi = "10.1039/d0se01383h",

language = "English",

volume = "5",

pages = "274--282",

journal = "Sustainable Energy and Fuels",

issn = "2398-4902",

publisher = "ROYAL SOC CHEMISTRY",

number = "1",

}

RIS

TY - JOUR

T1 - Process optimization and kinetics of microwave assisted transesterification of crude glycerol for the production of glycerol carbonate

AU - Teng, W.K.

AU - Yusoff, R.

AU - Aroua, M.K.

AU - Ngoh, G.C.

PY - 2021/1/7

Y1 - 2021/1/7

N2 - The production of glycerol carbonate (GC) from industrial grade crude glycerol was catalyzed by calcium oxide (CaO) via microwave assisted transesterification (MAT). Influencing process parameters including reaction temperature, time and molar ratio of dimethyl carbonate/glycerol (DMC/Gly) were examined and optimized by applying Box Behnken Design (BBD). The reaction was modelled into a reduced cubic model with good predictive accuracy. A high GC yield of 99.5% was achieved with 1 wt% CaO at optimized conditions such as reaction temperature of 65 °C, reaction time of 3 min and DMC/Gly molar ratio of 2.5. The study performed on the reaction kinetics suggests that the reaction follows an irreversible second order rate equation. A relatively low activation energy of 4.53 kJ mol-1 was determined for the microwave assisted transesterification of crude glycerol for the production of GC. The values of rate constants between 45 °C to 65 °C were in the range of 0.023-0.026 L mol-1 min-1, which are of one magnitude order higher than that of the conventional heating.

AB - The production of glycerol carbonate (GC) from industrial grade crude glycerol was catalyzed by calcium oxide (CaO) via microwave assisted transesterification (MAT). Influencing process parameters including reaction temperature, time and molar ratio of dimethyl carbonate/glycerol (DMC/Gly) were examined and optimized by applying Box Behnken Design (BBD). The reaction was modelled into a reduced cubic model with good predictive accuracy. A high GC yield of 99.5% was achieved with 1 wt% CaO at optimized conditions such as reaction temperature of 65 °C, reaction time of 3 min and DMC/Gly molar ratio of 2.5. The study performed on the reaction kinetics suggests that the reaction follows an irreversible second order rate equation. A relatively low activation energy of 4.53 kJ mol-1 was determined for the microwave assisted transesterification of crude glycerol for the production of GC. The values of rate constants between 45 °C to 65 °C were in the range of 0.023-0.026 L mol-1 min-1, which are of one magnitude order higher than that of the conventional heating.

KW - Activation energy

KW - Calcium oxide

KW - Carbonation

KW - Lime

KW - Molar ratio

KW - Optimization

KW - Rate constants

KW - Transesterification

KW - Boxbehnken design (BBD)

KW - Conventional heating

KW - Low-activation energy

KW - Microwave assisted transesterification

KW - Optimized conditions

KW - Predictive accuracy

KW - Process parameters

KW - Reaction temperature

KW - Glycerol

U2 - 10.1039/d0se01383h

DO - 10.1039/d0se01383h

M3 - Journal article

VL - 5

SP - 274

EP - 282

JO - Sustainable Energy and Fuels

JF - Sustainable Energy and Fuels

SN - 2398-4902

IS - 1

ER -

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