Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier
Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and react...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Dorofeenko, S. O. [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2022 |
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| Anmerkung: |
© Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. |
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| Übergeordnetes Werk: |
Enthalten in: Russian journal of physical chemistry - Moscow : MAIK Nauka, Interperiodica Publ., 2007, 16(2022), 2 vom: Apr., Seite 242-252 |
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| Übergeordnetes Werk: |
volume:16 ; year:2022 ; number:2 ; month:04 ; pages:242-252 |
| Links: |
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| DOI / URN: |
10.1134/S199079312202004X |
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| Katalog-ID: |
SPR05075260X |
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| 100 | 1 | |a Dorofeenko, S. O. |e verfasserin |4 aut | |
| 245 | 1 | 0 | |a Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier |
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| 500 | |a © Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. | ||
| 520 | |a Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and reacting gases. A feature of the reactor is the presence of an additional heat exchanger, where the oxidizer gas is preheated due to the residual heat of the solid heat carrier discharged from the reactor. Theoretically, in the approximation of the absence of heat loss and established thermodynamic equilibrium in the products, the macrokinetic modes of the process are considered depending on the main control parameters: the flow rate of the oxidizer gas, the flow rate of steam, the flow rate of the solid heat carrier, and the fuel composition. A quantitative calculation of the temperature and composition of the products in various combustion modes is carried out for the air-steam conversion of isopropanol and the air conversion of low-caloric pyrolysis gas. It is shown that the scheme under consideration provides a possibility to convert low-caloric gas at a temperature above 1500 K with a chemical efficiency of gasification over 90%. | ||
| 700 | 1 | |a Polianczyk, E. V. |4 aut | |
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10.1134/S199079312202004X doi (DE-627)SPR05075260X (SPR)S199079312202004X-e DE-627 ger DE-627 rakwb eng Dorofeenko, S. O. verfasserin aut Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and reacting gases. A feature of the reactor is the presence of an additional heat exchanger, where the oxidizer gas is preheated due to the residual heat of the solid heat carrier discharged from the reactor. Theoretically, in the approximation of the absence of heat loss and established thermodynamic equilibrium in the products, the macrokinetic modes of the process are considered depending on the main control parameters: the flow rate of the oxidizer gas, the flow rate of steam, the flow rate of the solid heat carrier, and the fuel composition. A quantitative calculation of the temperature and composition of the products in various combustion modes is carried out for the air-steam conversion of isopropanol and the air conversion of low-caloric pyrolysis gas. It is shown that the scheme under consideration provides a possibility to convert low-caloric gas at a temperature above 1500 K with a chemical efficiency of gasification over 90%. Polianczyk, E. V. aut Enthalten in Russian journal of physical chemistry Moscow : MAIK Nauka, Interperiodica Publ., 2007 16(2022), 2 vom: Apr., Seite 242-252 (DE-627)688079938 (DE-600)2653166-5 1990-7923 nnns volume:16 year:2022 number:2 month:04 pages:242-252 https://dx.doi.org/10.1134/S199079312202004X lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 16 2022 2 04 242-252 |
| spelling |
10.1134/S199079312202004X doi (DE-627)SPR05075260X (SPR)S199079312202004X-e DE-627 ger DE-627 rakwb eng Dorofeenko, S. O. verfasserin aut Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and reacting gases. A feature of the reactor is the presence of an additional heat exchanger, where the oxidizer gas is preheated due to the residual heat of the solid heat carrier discharged from the reactor. Theoretically, in the approximation of the absence of heat loss and established thermodynamic equilibrium in the products, the macrokinetic modes of the process are considered depending on the main control parameters: the flow rate of the oxidizer gas, the flow rate of steam, the flow rate of the solid heat carrier, and the fuel composition. A quantitative calculation of the temperature and composition of the products in various combustion modes is carried out for the air-steam conversion of isopropanol and the air conversion of low-caloric pyrolysis gas. It is shown that the scheme under consideration provides a possibility to convert low-caloric gas at a temperature above 1500 K with a chemical efficiency of gasification over 90%. Polianczyk, E. V. aut Enthalten in Russian journal of physical chemistry Moscow : MAIK Nauka, Interperiodica Publ., 2007 16(2022), 2 vom: Apr., Seite 242-252 (DE-627)688079938 (DE-600)2653166-5 1990-7923 nnns volume:16 year:2022 number:2 month:04 pages:242-252 https://dx.doi.org/10.1134/S199079312202004X lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 16 2022 2 04 242-252 |
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10.1134/S199079312202004X doi (DE-627)SPR05075260X (SPR)S199079312202004X-e DE-627 ger DE-627 rakwb eng Dorofeenko, S. O. verfasserin aut Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and reacting gases. A feature of the reactor is the presence of an additional heat exchanger, where the oxidizer gas is preheated due to the residual heat of the solid heat carrier discharged from the reactor. Theoretically, in the approximation of the absence of heat loss and established thermodynamic equilibrium in the products, the macrokinetic modes of the process are considered depending on the main control parameters: the flow rate of the oxidizer gas, the flow rate of steam, the flow rate of the solid heat carrier, and the fuel composition. A quantitative calculation of the temperature and composition of the products in various combustion modes is carried out for the air-steam conversion of isopropanol and the air conversion of low-caloric pyrolysis gas. It is shown that the scheme under consideration provides a possibility to convert low-caloric gas at a temperature above 1500 K with a chemical efficiency of gasification over 90%. Polianczyk, E. V. aut Enthalten in Russian journal of physical chemistry Moscow : MAIK Nauka, Interperiodica Publ., 2007 16(2022), 2 vom: Apr., Seite 242-252 (DE-627)688079938 (DE-600)2653166-5 1990-7923 nnns volume:16 year:2022 number:2 month:04 pages:242-252 https://dx.doi.org/10.1134/S199079312202004X lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 16 2022 2 04 242-252 |
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10.1134/S199079312202004X doi (DE-627)SPR05075260X (SPR)S199079312202004X-e DE-627 ger DE-627 rakwb eng Dorofeenko, S. O. verfasserin aut Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and reacting gases. A feature of the reactor is the presence of an additional heat exchanger, where the oxidizer gas is preheated due to the residual heat of the solid heat carrier discharged from the reactor. Theoretically, in the approximation of the absence of heat loss and established thermodynamic equilibrium in the products, the macrokinetic modes of the process are considered depending on the main control parameters: the flow rate of the oxidizer gas, the flow rate of steam, the flow rate of the solid heat carrier, and the fuel composition. A quantitative calculation of the temperature and composition of the products in various combustion modes is carried out for the air-steam conversion of isopropanol and the air conversion of low-caloric pyrolysis gas. It is shown that the scheme under consideration provides a possibility to convert low-caloric gas at a temperature above 1500 K with a chemical efficiency of gasification over 90%. Polianczyk, E. V. aut Enthalten in Russian journal of physical chemistry Moscow : MAIK Nauka, Interperiodica Publ., 2007 16(2022), 2 vom: Apr., Seite 242-252 (DE-627)688079938 (DE-600)2653166-5 1990-7923 nnns volume:16 year:2022 number:2 month:04 pages:242-252 https://dx.doi.org/10.1134/S199079312202004X lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 16 2022 2 04 242-252 |
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10.1134/S199079312202004X doi (DE-627)SPR05075260X (SPR)S199079312202004X-e DE-627 ger DE-627 rakwb eng Dorofeenko, S. O. verfasserin aut Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and reacting gases. A feature of the reactor is the presence of an additional heat exchanger, where the oxidizer gas is preheated due to the residual heat of the solid heat carrier discharged from the reactor. Theoretically, in the approximation of the absence of heat loss and established thermodynamic equilibrium in the products, the macrokinetic modes of the process are considered depending on the main control parameters: the flow rate of the oxidizer gas, the flow rate of steam, the flow rate of the solid heat carrier, and the fuel composition. A quantitative calculation of the temperature and composition of the products in various combustion modes is carried out for the air-steam conversion of isopropanol and the air conversion of low-caloric pyrolysis gas. It is shown that the scheme under consideration provides a possibility to convert low-caloric gas at a temperature above 1500 K with a chemical efficiency of gasification over 90%. Polianczyk, E. V. aut Enthalten in Russian journal of physical chemistry Moscow : MAIK Nauka, Interperiodica Publ., 2007 16(2022), 2 vom: Apr., Seite 242-252 (DE-627)688079938 (DE-600)2653166-5 1990-7923 nnns volume:16 year:2022 number:2 month:04 pages:242-252 https://dx.doi.org/10.1134/S199079312202004X lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_101 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 16 2022 2 04 242-252 |
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Dorofeenko, S. O. |
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Dorofeenko, S. O. Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier |
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Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier |
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Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier |
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Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier |
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Dorofeenko, S. O. Polianczyk, E. V. |
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10.1134/S199079312202004X |
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conversion of low caloric fuels to synthesis gas in the filtration combustion mode in a moving layer of a granulated heat carrier |
| title_auth |
Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier |
| abstract |
Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and reacting gases. A feature of the reactor is the presence of an additional heat exchanger, where the oxidizer gas is preheated due to the residual heat of the solid heat carrier discharged from the reactor. Theoretically, in the approximation of the absence of heat loss and established thermodynamic equilibrium in the products, the macrokinetic modes of the process are considered depending on the main control parameters: the flow rate of the oxidizer gas, the flow rate of steam, the flow rate of the solid heat carrier, and the fuel composition. A quantitative calculation of the temperature and composition of the products in various combustion modes is carried out for the air-steam conversion of isopropanol and the air conversion of low-caloric pyrolysis gas. It is shown that the scheme under consideration provides a possibility to convert low-caloric gas at a temperature above 1500 K with a chemical efficiency of gasification over 90%. © Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. |
| abstractGer |
Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and reacting gases. A feature of the reactor is the presence of an additional heat exchanger, where the oxidizer gas is preheated due to the residual heat of the solid heat carrier discharged from the reactor. Theoretically, in the approximation of the absence of heat loss and established thermodynamic equilibrium in the products, the macrokinetic modes of the process are considered depending on the main control parameters: the flow rate of the oxidizer gas, the flow rate of steam, the flow rate of the solid heat carrier, and the fuel composition. A quantitative calculation of the temperature and composition of the products in various combustion modes is carried out for the air-steam conversion of isopropanol and the air conversion of low-caloric pyrolysis gas. It is shown that the scheme under consideration provides a possibility to convert low-caloric gas at a temperature above 1500 K with a chemical efficiency of gasification over 90%. © Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. |
| abstract_unstemmed |
Abstract The possibility of converting low-caloric fuels into synthesis gas by their partial oxidation in a moving porous layer of a granular heat carrier is theoretically studied. The process is considered in a new version of the reactor with a counterflow of a solid granular heat carrier and reacting gases. A feature of the reactor is the presence of an additional heat exchanger, where the oxidizer gas is preheated due to the residual heat of the solid heat carrier discharged from the reactor. Theoretically, in the approximation of the absence of heat loss and established thermodynamic equilibrium in the products, the macrokinetic modes of the process are considered depending on the main control parameters: the flow rate of the oxidizer gas, the flow rate of steam, the flow rate of the solid heat carrier, and the fuel composition. A quantitative calculation of the temperature and composition of the products in various combustion modes is carried out for the air-steam conversion of isopropanol and the air conversion of low-caloric pyrolysis gas. It is shown that the scheme under consideration provides a possibility to convert low-caloric gas at a temperature above 1500 K with a chemical efficiency of gasification over 90%. © Pleiades Publishing, Ltd. 2022. ISSN 1990-7931, Russian Journal of Physical Chemistry B, 2022, Vol. 16, No. 2, pp. 242–252. © Pleiades Publishing, Ltd., 2022. Russian Text © The Author(s), 2022, published in Khimicheskaya Fizika, 2022, Vol. 41, No. 3, pp. 29–40. |
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Conversion of Low Caloric Fuels to Synthesis Gas in the Filtration Combustion Mode in a Moving Layer of a Granulated Heat Carrier |
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