TY - JOUR
T1 - Physicochemical Characterization and Kinetic Modeling concerning Combustion of Waste Berry Pomace
AU - Osman, Ahmed I.
AU - Young, Thomas J.
AU - Farrell, Charlie
AU - Harrison, John
AU - Al-Muhtaseb, Ala'A H.
AU - Rooney, David W.
N1 - Funding Information:
The authors would like to acknowledge the support given by the EPSRC project. A.I.O. wishes to acknowledge the support of The Bryden Centre project (Project ID VA5048) and the Renewable Engine project (Project ID IVA5033) which was awarded by The European Union’s INTERREG VA Programme, managed by the Special EU Programmes Body (SEUPB), with match funding provided by the Department for the Economy in Northern Ireland and the Department of Business, Enterprise and Innovation in the Republic of Ireland. The authors are grateful to South West College and the Centre for Renewable and Sustainable Technology (CREST) for the use of AKTS and the bomb calorimeter. The authors would like to thank Mr. Patrick McNicholl for proofreading the manuscript. The authors acknowledge the support given by the School of Chemistry and Chemical Engineering, Queen’s University Belfast and Elmgrove Foods Ltd.
Publisher Copyright:
©
PY - 2020/11/30
Y1 - 2020/11/30
N2 - Herein waste biomass (blackberry pomace) was physicochemically characterized along with its thermochemical products. This is coupled with the evaluation of the kinetic triplet (activation energy, pre-exponential constant, and the rate of reaction) and thermal predictions for the combustion process for the first time via the AKTS thermokinetics package. The main kinetic modeling method employed was the differential isoconversional analysis; however, the Flynn-Wall-Ozawa and ASTM E-698 methods were used as comparisons. The model was developed and validated from experimental DSC and TGA data, resulting in an excellent match (R2 = 0.99544 and 0.99194, respectively). The activation energies were evaluated using the ASTM-E698 method (88.64 kJ mol-1) and Flynn-Wall-Ozawa methods (50-140 kJ mol-1). The differential isoconversional method showed that activation energy values were in the range of 84-197 kJ mol-1 for the combustion of berry pomace. Isothermal predictions based on the model were indicated at temperatures of 560 and 600 °C; the reaction had achieved 100% completion (α = 1) after 30 and 6 min, respectively. For the nonisothermal prediction, the heating rates of 50, 75, and 100 °C/min have a two-stage rate profile with a maximum peak in the first stage of the reaction. Thereafter, the reaction rate increases once again but not to the same effect as the first initial stage. For instance, at 100 °C/min, stages 1 and 2 are reported as 0.005381 and 0.005148 s-1,respectively. Overall, this study demonstrates the success of the approach in modeling the thermochemical conversion of berry pomace as waste stream biomass.
AB - Herein waste biomass (blackberry pomace) was physicochemically characterized along with its thermochemical products. This is coupled with the evaluation of the kinetic triplet (activation energy, pre-exponential constant, and the rate of reaction) and thermal predictions for the combustion process for the first time via the AKTS thermokinetics package. The main kinetic modeling method employed was the differential isoconversional analysis; however, the Flynn-Wall-Ozawa and ASTM E-698 methods were used as comparisons. The model was developed and validated from experimental DSC and TGA data, resulting in an excellent match (R2 = 0.99544 and 0.99194, respectively). The activation energies were evaluated using the ASTM-E698 method (88.64 kJ mol-1) and Flynn-Wall-Ozawa methods (50-140 kJ mol-1). The differential isoconversional method showed that activation energy values were in the range of 84-197 kJ mol-1 for the combustion of berry pomace. Isothermal predictions based on the model were indicated at temperatures of 560 and 600 °C; the reaction had achieved 100% completion (α = 1) after 30 and 6 min, respectively. For the nonisothermal prediction, the heating rates of 50, 75, and 100 °C/min have a two-stage rate profile with a maximum peak in the first stage of the reaction. Thereafter, the reaction rate increases once again but not to the same effect as the first initial stage. For instance, at 100 °C/min, stages 1 and 2 are reported as 0.005381 and 0.005148 s-1,respectively. Overall, this study demonstrates the success of the approach in modeling the thermochemical conversion of berry pomace as waste stream biomass.
KW - Biomass
KW - Combustion
KW - Isoconversional
KW - Kinetic modeling
KW - Pomace
KW - Thermal analysis
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U2 - 10.1021/acssuschemeng.0c07390
DO - 10.1021/acssuschemeng.0c07390
M3 - Article
AN - SCOPUS:85096930912
SN - 2168-0485
VL - 8
SP - 17573
EP - 17586
JO - ACS Sustainable Chemistry and Engineering
JF - ACS Sustainable Chemistry and Engineering
IS - 47
ER -