Analysis of the errors associated with typical pulverized coal char combustion modeling assumptions for oxy-fuel combustion
In CFD models of pulverized coal combustion, which often have complex, turbulent flows with millions of coal particles reacting, the char combustion sub-model needs to be computationally efficient. There are several common assumptions that are made in char combustion models that allow for a compact,...
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Published in | Combustion and flame Vol. 160; no. 8; pp. 1499 - 1509 |
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Main Authors | , , |
Format | Journal Article |
Language | English |
Published |
Amsterdam
Elsevier Inc
01.08.2013
Elsevier |
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Abstract | In CFD models of pulverized coal combustion, which often have complex, turbulent flows with millions of coal particles reacting, the char combustion sub-model needs to be computationally efficient. There are several common assumptions that are made in char combustion models that allow for a compact, computationally efficient model. In this work, oft used single- and double-film simplified models are described, and the temperature and carbon combustion rates predicted from these models are compared against a more accurate continuous-film model. Both the single- and double-film models include a description of the heterogeneous reactions of carbon with O2, CO2, and H2O, along with a Thiele based description of reactant penetration. As compared to the continuous-film model, the double-film model predicts higher temperatures and carbon consumption rates, while the single-film model gives more accurate results. A single-film model is therefore preferred to a double-film model for a simplified, yet fairly accurate description of char combustion. For particles from 65 to 135μm, in O2 concentrations ranging from 12 to 60vol.%, with either CO2 or N2 as a diluent, particle temperatures from the single-film model are expected to be accurate within 270K, and carbon consumption rate predictions should be within 16%, with greater accuracies for a CO2 diluent and at lower bulk oxygen concentrations. A single-film model that accounts for reactant penetration and both oxidation and gasification reactions is suggested as a computationally efficient sub-model for coal char combustion that is reasonably accurate over a wide range of gas environments. |
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AbstractList | In CFD models of pulverized coal combustion, which often have complex, turbulent flows with millions of coal particles reacting, the char combustion sub-model needs to be computationally efficient. There are several common assumptions that are made in char combustion models that allow for a compact, computationally efficient model. In this work, oft used single- and double-film simplified models are described, and the temperature and carbon combustion rates predicted from these models are compared against a more accurate continuous-film model. Both the single- and double-film models include a description of the heterogeneous reactions of carbon with O2, CO2, and H2O, along with a Thiele based description of reactant penetration. As compared to the continuous-film model, the double-film model predicts higher temperatures and carbon consumption rates, while the single-film model gives more accurate results. A single-film model is therefore preferred to a double-film model for a simplified, yet fairly accurate description of char combustion. For particles from 65 to 135 mu m, in O2 concentrations ranging from 12 to 60 vol.%, with either CO2 or N2 as a diluent, particle temperatures from the single-film model are expected to be accurate within 270 K, and carbon consumption rate predictions should be within 16%, with greater accuracies for a CO2 diluent and at lower bulk oxygen concentrations. A single-film model that accounts for reactant penetration and both oxidation and gasification reactions is suggested as a computationally efficient sub-model for coal char combustion that is reasonably accurate over a wide range of gas environments. In CFD models of pulverized coal combustion, which often have complex, turbulent flows with millions of coal particles reacting, the char combustion sub-model needs to be computationally efficient. There are several common assumptions that are made in char combustion models that allow for a compact, computationally efficient model. In this work, oft used single- and double-film simplified models are described, and the temperature and carbon combustion rates predicted from these models are compared against a more accurate continuous-film model. Both the single- and double-film models include a description of the heterogeneous reactions of carbon with O2, CO2, and H2O, along with a Thiele based description of reactant penetration. As compared to the continuous-film model, the double-film model predicts higher temperatures and carbon consumption rates, while the single-film model gives more accurate results. A single-film model is therefore preferred to a double-film model for a simplified, yet fairly accurate description of char combustion. For particles from 65 to 135μm, in O2 concentrations ranging from 12 to 60vol.%, with either CO2 or N2 as a diluent, particle temperatures from the single-film model are expected to be accurate within 270K, and carbon consumption rate predictions should be within 16%, with greater accuracies for a CO2 diluent and at lower bulk oxygen concentrations. A single-film model that accounts for reactant penetration and both oxidation and gasification reactions is suggested as a computationally efficient sub-model for coal char combustion that is reasonably accurate over a wide range of gas environments. |
Author | Shaddix, Christopher R. Lighty, JoAnn S. Hecht, Ethan S. |
Author_xml | – sequence: 1 givenname: Ethan S. surname: Hecht fullname: Hecht, Ethan S. email: ehecht@sandia.gov organization: Department of Chemical Engineering, University of Utah, Salt Lake City, UT 84112, USA – sequence: 2 givenname: Christopher R. surname: Shaddix fullname: Shaddix, Christopher R. organization: Combustion Research Facility, Sandia National Laboratories, Livermore, CA 94550, USA – sequence: 3 givenname: JoAnn S. surname: Lighty fullname: Lighty, JoAnn S. organization: Department of Chemical Engineering, University of Utah, Salt Lake City, UT 84112, USA |
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Keywords | Coal combustion Gasification Oxy-fuel Error analysis Computational fluid dynamics Char Fuel Oxycombustion Theoretical study Pulverized coal Combustion Modeling |
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SubjectTerms | Applied sciences Carbon Carbon dioxide Coal Coal combustion Combustion Combustion of solid fuels Combustion. Flame Computational efficiency Computational fluid dynamics Energy Energy. Thermal use of fuels Exact sciences and technology Fuel processing. Carbochemistry and petrochemistry Fuels Gasification Mathematical models Oxy-fuel Penetration Solid fuel processing (coal, coke, brown coal, peat, wood, etc.) Theoretical studies. Data and constants. Metering |
Title | Analysis of the errors associated with typical pulverized coal char combustion modeling assumptions for oxy-fuel combustion |
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