Modeling of Filtration Combustion of Carbon
Abstract The kinetics of the overall reactions of carbon gasification at temperatures up to 1600 K is studied. The kinetic characteristics of the reactions are taken into account in a distributed mathematical model of filtration combustion of carbon. By computational experiment at different values o...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Becker, A. V. [verfasserIn] |
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| Format: |
Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2004 |
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| Schlagwörter: |
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| Anmerkung: |
© MAIK “Nauka/Interperiodica” 2004 |
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| Übergeordnetes Werk: |
Enthalten in: Theoretical foundations of chemical engineering - Kluwer Academic Publishers-Plenum Publishers, 1967, 38(2004), 5 vom: Sept., Seite 510-515 |
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| Übergeordnetes Werk: |
volume:38 ; year:2004 ; number:5 ; month:09 ; pages:510-515 |
| Links: |
|---|
| DOI / URN: |
10.1023/B:TFCE.0000043804.82560.fb |
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OLC2054254878 |
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| 520 | |a Abstract The kinetics of the overall reactions of carbon gasification at temperatures up to 1600 K is studied. The kinetic characteristics of the reactions are taken into account in a distributed mathematical model of filtration combustion of carbon. By computational experiment at different values of process control parameters (the gas flow rate, the fraction of the oxidant in the gas, and the mass ratio of carbon to the inert material in the combustible mixture), it is found that, in the wave of filtration combustion of carbon under superadiabatic conditions, carbon gasification can predominately yield either $ CO_{2} $ or CO. | ||
| 650 | 4 | |a Combustion | |
| 650 | 4 | |a Filtration | |
| 650 | 4 | |a Mathematical Model | |
| 650 | 4 | |a Control Parameter | |
| 650 | 4 | |a Process Control | |
| 700 | 1 | |a Polianczyk, E. V. |4 aut | |
| 700 | 1 | |a Volkova, N. N. |4 aut | |
| 700 | 1 | |a Manelis, G. B. |4 aut | |
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10.1023/B:TFCE.0000043804.82560.fb doi (DE-627)OLC2054254878 (DE-He213)B:TFCE.0000043804.82560.fb-p DE-627 ger DE-627 rakwb eng 660 VZ Becker, A. V. verfasserin aut Modeling of Filtration Combustion of Carbon 2004 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © MAIK “Nauka/Interperiodica” 2004 Abstract The kinetics of the overall reactions of carbon gasification at temperatures up to 1600 K is studied. The kinetic characteristics of the reactions are taken into account in a distributed mathematical model of filtration combustion of carbon. By computational experiment at different values of process control parameters (the gas flow rate, the fraction of the oxidant in the gas, and the mass ratio of carbon to the inert material in the combustible mixture), it is found that, in the wave of filtration combustion of carbon under superadiabatic conditions, carbon gasification can predominately yield either $ CO_{2} $ or CO. Combustion Filtration Mathematical Model Control Parameter Process Control Polianczyk, E. V. aut Volkova, N. N. aut Manelis, G. B. aut Enthalten in Theoretical foundations of chemical engineering Kluwer Academic Publishers-Plenum Publishers, 1967 38(2004), 5 vom: Sept., Seite 510-515 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:38 year:2004 number:5 month:09 pages:510-515 https://doi.org/10.1023/B:TFCE.0000043804.82560.fb lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 38 2004 5 09 510-515 |
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10.1023/B:TFCE.0000043804.82560.fb doi (DE-627)OLC2054254878 (DE-He213)B:TFCE.0000043804.82560.fb-p DE-627 ger DE-627 rakwb eng 660 VZ Becker, A. V. verfasserin aut Modeling of Filtration Combustion of Carbon 2004 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier © MAIK “Nauka/Interperiodica” 2004 Abstract The kinetics of the overall reactions of carbon gasification at temperatures up to 1600 K is studied. The kinetic characteristics of the reactions are taken into account in a distributed mathematical model of filtration combustion of carbon. By computational experiment at different values of process control parameters (the gas flow rate, the fraction of the oxidant in the gas, and the mass ratio of carbon to the inert material in the combustible mixture), it is found that, in the wave of filtration combustion of carbon under superadiabatic conditions, carbon gasification can predominately yield either $ CO_{2} $ or CO. Combustion Filtration Mathematical Model Control Parameter Process Control Polianczyk, E. V. aut Volkova, N. N. aut Manelis, G. B. aut Enthalten in Theoretical foundations of chemical engineering Kluwer Academic Publishers-Plenum Publishers, 1967 38(2004), 5 vom: Sept., Seite 510-515 (DE-627)129601438 (DE-600)241412-0 (DE-576)015095061 0040-5795 nnns volume:38 year:2004 number:5 month:09 pages:510-515 https://doi.org/10.1023/B:TFCE.0000043804.82560.fb lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 38 2004 5 09 510-515 |
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Abstract The kinetics of the overall reactions of carbon gasification at temperatures up to 1600 K is studied. The kinetic characteristics of the reactions are taken into account in a distributed mathematical model of filtration combustion of carbon. By computational experiment at different values of process control parameters (the gas flow rate, the fraction of the oxidant in the gas, and the mass ratio of carbon to the inert material in the combustible mixture), it is found that, in the wave of filtration combustion of carbon under superadiabatic conditions, carbon gasification can predominately yield either $ CO_{2} $ or CO. © MAIK “Nauka/Interperiodica” 2004 |
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Abstract The kinetics of the overall reactions of carbon gasification at temperatures up to 1600 K is studied. The kinetic characteristics of the reactions are taken into account in a distributed mathematical model of filtration combustion of carbon. By computational experiment at different values of process control parameters (the gas flow rate, the fraction of the oxidant in the gas, and the mass ratio of carbon to the inert material in the combustible mixture), it is found that, in the wave of filtration combustion of carbon under superadiabatic conditions, carbon gasification can predominately yield either $ CO_{2} $ or CO. © MAIK “Nauka/Interperiodica” 2004 |
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Abstract The kinetics of the overall reactions of carbon gasification at temperatures up to 1600 K is studied. The kinetic characteristics of the reactions are taken into account in a distributed mathematical model of filtration combustion of carbon. By computational experiment at different values of process control parameters (the gas flow rate, the fraction of the oxidant in the gas, and the mass ratio of carbon to the inert material in the combustible mixture), it is found that, in the wave of filtration combustion of carbon under superadiabatic conditions, carbon gasification can predominately yield either $ CO_{2} $ or CO. © MAIK “Nauka/Interperiodica” 2004 |
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V.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Modeling of Filtration Combustion of Carbon</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2004</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">ohne Hilfsmittel zu benutzen</subfield><subfield code="b">n</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Band</subfield><subfield code="b">nc</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="500" ind1=" " ind2=" "><subfield code="a">© MAIK “Nauka/Interperiodica” 2004</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract The kinetics of the overall reactions of carbon gasification at temperatures up to 1600 K is studied. The kinetic characteristics of the reactions are taken into account in a distributed mathematical model of filtration combustion of carbon. By computational experiment at different values of process control parameters (the gas flow rate, the fraction of the oxidant in the gas, and the mass ratio of carbon to the inert material in the combustible mixture), it is found that, in the wave of filtration combustion of carbon under superadiabatic conditions, carbon gasification can predominately yield either $ CO_{2} $ or CO.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Combustion</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Filtration</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Mathematical Model</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Control Parameter</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Process Control</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Polianczyk, E. 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