Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor

The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the pr...
Ausführliche Beschreibung

Gespeichert in:

Autor*in:	Polianczyk, E.V. [verfasserIn] Dorofeenko, S.O. [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2018

Schlagwörter:	Partial oxidation Syngas production Filtration combustion Porous media Reactor design

Übergeordnetes Werk:	Enthalten in: International journal of hydrogen energy - New York, NY [u.a.] : Elsevier, 1976, 44
Übergeordnetes Werk:	volume:44

DOI / URN:	10.1016/j.ijhydene.2018.12.117

Katalog-ID:	ELV001525360

Internformat


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245	1	0	\|a Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor
264		1	\|c 2018
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337			\|a Computermedien \|b c \|2 rdamedia
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520			\|a The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the previously considered conversion in a reversed-flow reactor, such embodiment provides a possibility of attaining high combustion temperature due to efficient heat recuperation, while performing the process continuously without transients associated with the flow reverse. In the moving bed process, the flowrate of the granular material becomes an independent control parameter. A thermodynamic assessment of the macrokinetic conversion regimes as dependent on fuel composition and oxidant gas and fuel supply rates and granular solid flowrate is performed under the assumption that the combustion temperature is self-consistent according to thermodynamic equilibrium with the composition of syngas. Calculations for the methane/air-steam and 2-propanol/air-steam conversion are provided as examples. The calculations show that the process provides a possibility to combine in a stationary continuous process a high combustion temperature with low net heat effect and thus, a high chemical efficiency of conversion. The parametric domain for control parameters providing highly efficient conversion is determined.
650		4	\|a Partial oxidation
650		4	\|a Syngas production
650		4	\|a Filtration combustion
650		4	\|a Porous media
650		4	\|a Reactor design
700	1		\|a Dorofeenko, S.O. \|e verfasserin \|4 aut
773	0	8	\|i Enthalten in \|t International journal of hydrogen energy \|d New York, NY [u.a.] : Elsevier, 1976 \|g 44 \|h Online-Ressource \|w (DE-627)301511357 \|w (DE-600)1484487-4 \|w (DE-576)096806397 \|x 1879-3487 \|7 nnns
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912			\|a GBV_ILN_23
912			\|a GBV_ILN_24
912			\|a GBV_ILN_31
912			\|a GBV_ILN_32
912			\|a GBV_ILN_40
912			\|a GBV_ILN_60
912			\|a GBV_ILN_62
912			\|a GBV_ILN_63
912			\|a GBV_ILN_65
912			\|a GBV_ILN_69
912			\|a GBV_ILN_70
912			\|a GBV_ILN_73
912			\|a GBV_ILN_74
912			\|a GBV_ILN_90
912			\|a GBV_ILN_95
912			\|a GBV_ILN_100
912			\|a GBV_ILN_105
912			\|a GBV_ILN_110
912			\|a GBV_ILN_150
912			\|a GBV_ILN_151
912			\|a GBV_ILN_224
912			\|a GBV_ILN_370
912			\|a GBV_ILN_602
912			\|a GBV_ILN_702
912			\|a GBV_ILN_2003
912			\|a GBV_ILN_2004
912			\|a GBV_ILN_2005
912			\|a GBV_ILN_2006
912			\|a GBV_ILN_2008
912			\|a GBV_ILN_2010
912			\|a GBV_ILN_2011
912			\|a GBV_ILN_2014
912			\|a GBV_ILN_2015
912			\|a GBV_ILN_2020
912			\|a GBV_ILN_2021
912			\|a GBV_ILN_2025
912			\|a GBV_ILN_2027
912			\|a GBV_ILN_2034
912			\|a GBV_ILN_2038
912			\|a GBV_ILN_2044
912			\|a GBV_ILN_2048
912			\|a GBV_ILN_2049
912			\|a GBV_ILN_2050
912			\|a GBV_ILN_2056
912			\|a GBV_ILN_2059
912			\|a GBV_ILN_2061
912			\|a GBV_ILN_2064
912			\|a GBV_ILN_2065
912			\|a GBV_ILN_2068
912			\|a GBV_ILN_2088
912			\|a GBV_ILN_2111
912			\|a GBV_ILN_2112
912			\|a GBV_ILN_2113
912			\|a GBV_ILN_2118
912			\|a GBV_ILN_2122
912			\|a GBV_ILN_2129
912			\|a GBV_ILN_2143
912			\|a GBV_ILN_2147
912			\|a GBV_ILN_2148
912			\|a GBV_ILN_2152
912			\|a GBV_ILN_2153
912			\|a GBV_ILN_2190
912			\|a GBV_ILN_2336
912			\|a GBV_ILN_2470
912			\|a GBV_ILN_2507
912			\|a GBV_ILN_2522
912			\|a GBV_ILN_4035
912			\|a GBV_ILN_4037
912			\|a GBV_ILN_4112
912			\|a GBV_ILN_4125
912			\|a GBV_ILN_4126
912			\|a GBV_ILN_4242
912			\|a GBV_ILN_4251
912			\|a GBV_ILN_4305
912			\|a GBV_ILN_4313
912			\|a GBV_ILN_4322
912			\|a GBV_ILN_4323
912			\|a GBV_ILN_4324
912			\|a GBV_ILN_4325
912			\|a GBV_ILN_4326
912			\|a GBV_ILN_4333
912			\|a GBV_ILN_4334
912			\|a GBV_ILN_4335
912			\|a GBV_ILN_4338
912			\|a GBV_ILN_4393
936	b	k	\|a 52.56 \|j Regenerative Energieformen \|j alternative Energieformen
951			\|a AR
952			\|d 44

Indexfelder

author_variant	e p ep s d sd
matchkey_str	article:18793487:2018----::ovrinfyrcrosoyteigsncutrlwoigeflr
hierarchy_sort_str	2018
bklnumber	52.56
publishDate	2018
allfields	10.1016/j.ijhydene.2018.12.117 doi (DE-627)ELV001525360 (ELSEVIER)S0360-3199(18)34085-0 DE-627 ger DE-627 rda eng 660 620 DE-600 52.56 bkl Polianczyk, E.V. verfasserin aut Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor 2018 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the previously considered conversion in a reversed-flow reactor, such embodiment provides a possibility of attaining high combustion temperature due to efficient heat recuperation, while performing the process continuously without transients associated with the flow reverse. In the moving bed process, the flowrate of the granular material becomes an independent control parameter. A thermodynamic assessment of the macrokinetic conversion regimes as dependent on fuel composition and oxidant gas and fuel supply rates and granular solid flowrate is performed under the assumption that the combustion temperature is self-consistent according to thermodynamic equilibrium with the composition of syngas. Calculations for the methane/air-steam and 2-propanol/air-steam conversion are provided as examples. The calculations show that the process provides a possibility to combine in a stationary continuous process a high combustion temperature with low net heat effect and thus, a high chemical efficiency of conversion. The parametric domain for control parameters providing highly efficient conversion is determined. Partial oxidation Syngas production Filtration combustion Porous media Reactor design Dorofeenko, S.O. verfasserin aut Enthalten in International journal of hydrogen energy New York, NY [u.a.] : Elsevier, 1976 44 Online-Ressource (DE-627)301511357 (DE-600)1484487-4 (DE-576)096806397 1879-3487 nnns volume:44 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 52.56 Regenerative Energieformen alternative Energieformen AR 44
spelling	10.1016/j.ijhydene.2018.12.117 doi (DE-627)ELV001525360 (ELSEVIER)S0360-3199(18)34085-0 DE-627 ger DE-627 rda eng 660 620 DE-600 52.56 bkl Polianczyk, E.V. verfasserin aut Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor 2018 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the previously considered conversion in a reversed-flow reactor, such embodiment provides a possibility of attaining high combustion temperature due to efficient heat recuperation, while performing the process continuously without transients associated with the flow reverse. In the moving bed process, the flowrate of the granular material becomes an independent control parameter. A thermodynamic assessment of the macrokinetic conversion regimes as dependent on fuel composition and oxidant gas and fuel supply rates and granular solid flowrate is performed under the assumption that the combustion temperature is self-consistent according to thermodynamic equilibrium with the composition of syngas. Calculations for the methane/air-steam and 2-propanol/air-steam conversion are provided as examples. The calculations show that the process provides a possibility to combine in a stationary continuous process a high combustion temperature with low net heat effect and thus, a high chemical efficiency of conversion. The parametric domain for control parameters providing highly efficient conversion is determined. Partial oxidation Syngas production Filtration combustion Porous media Reactor design Dorofeenko, S.O. verfasserin aut Enthalten in International journal of hydrogen energy New York, NY [u.a.] : Elsevier, 1976 44 Online-Ressource (DE-627)301511357 (DE-600)1484487-4 (DE-576)096806397 1879-3487 nnns volume:44 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 52.56 Regenerative Energieformen alternative Energieformen AR 44
allfields_unstemmed	10.1016/j.ijhydene.2018.12.117 doi (DE-627)ELV001525360 (ELSEVIER)S0360-3199(18)34085-0 DE-627 ger DE-627 rda eng 660 620 DE-600 52.56 bkl Polianczyk, E.V. verfasserin aut Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor 2018 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the previously considered conversion in a reversed-flow reactor, such embodiment provides a possibility of attaining high combustion temperature due to efficient heat recuperation, while performing the process continuously without transients associated with the flow reverse. In the moving bed process, the flowrate of the granular material becomes an independent control parameter. A thermodynamic assessment of the macrokinetic conversion regimes as dependent on fuel composition and oxidant gas and fuel supply rates and granular solid flowrate is performed under the assumption that the combustion temperature is self-consistent according to thermodynamic equilibrium with the composition of syngas. Calculations for the methane/air-steam and 2-propanol/air-steam conversion are provided as examples. The calculations show that the process provides a possibility to combine in a stationary continuous process a high combustion temperature with low net heat effect and thus, a high chemical efficiency of conversion. The parametric domain for control parameters providing highly efficient conversion is determined. Partial oxidation Syngas production Filtration combustion Porous media Reactor design Dorofeenko, S.O. verfasserin aut Enthalten in International journal of hydrogen energy New York, NY [u.a.] : Elsevier, 1976 44 Online-Ressource (DE-627)301511357 (DE-600)1484487-4 (DE-576)096806397 1879-3487 nnns volume:44 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 52.56 Regenerative Energieformen alternative Energieformen AR 44
allfieldsGer	10.1016/j.ijhydene.2018.12.117 doi (DE-627)ELV001525360 (ELSEVIER)S0360-3199(18)34085-0 DE-627 ger DE-627 rda eng 660 620 DE-600 52.56 bkl Polianczyk, E.V. verfasserin aut Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor 2018 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the previously considered conversion in a reversed-flow reactor, such embodiment provides a possibility of attaining high combustion temperature due to efficient heat recuperation, while performing the process continuously without transients associated with the flow reverse. In the moving bed process, the flowrate of the granular material becomes an independent control parameter. A thermodynamic assessment of the macrokinetic conversion regimes as dependent on fuel composition and oxidant gas and fuel supply rates and granular solid flowrate is performed under the assumption that the combustion temperature is self-consistent according to thermodynamic equilibrium with the composition of syngas. Calculations for the methane/air-steam and 2-propanol/air-steam conversion are provided as examples. The calculations show that the process provides a possibility to combine in a stationary continuous process a high combustion temperature with low net heat effect and thus, a high chemical efficiency of conversion. The parametric domain for control parameters providing highly efficient conversion is determined. Partial oxidation Syngas production Filtration combustion Porous media Reactor design Dorofeenko, S.O. verfasserin aut Enthalten in International journal of hydrogen energy New York, NY [u.a.] : Elsevier, 1976 44 Online-Ressource (DE-627)301511357 (DE-600)1484487-4 (DE-576)096806397 1879-3487 nnns volume:44 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 52.56 Regenerative Energieformen alternative Energieformen AR 44
allfieldsSound	10.1016/j.ijhydene.2018.12.117 doi (DE-627)ELV001525360 (ELSEVIER)S0360-3199(18)34085-0 DE-627 ger DE-627 rda eng 660 620 DE-600 52.56 bkl Polianczyk, E.V. verfasserin aut Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor 2018 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the previously considered conversion in a reversed-flow reactor, such embodiment provides a possibility of attaining high combustion temperature due to efficient heat recuperation, while performing the process continuously without transients associated with the flow reverse. In the moving bed process, the flowrate of the granular material becomes an independent control parameter. A thermodynamic assessment of the macrokinetic conversion regimes as dependent on fuel composition and oxidant gas and fuel supply rates and granular solid flowrate is performed under the assumption that the combustion temperature is self-consistent according to thermodynamic equilibrium with the composition of syngas. Calculations for the methane/air-steam and 2-propanol/air-steam conversion are provided as examples. The calculations show that the process provides a possibility to combine in a stationary continuous process a high combustion temperature with low net heat effect and thus, a high chemical efficiency of conversion. The parametric domain for control parameters providing highly efficient conversion is determined. Partial oxidation Syngas production Filtration combustion Porous media Reactor design Dorofeenko, S.O. verfasserin aut Enthalten in International journal of hydrogen energy New York, NY [u.a.] : Elsevier, 1976 44 Online-Ressource (DE-627)301511357 (DE-600)1484487-4 (DE-576)096806397 1879-3487 nnns volume:44 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 52.56 Regenerative Energieformen alternative Energieformen AR 44
language	English
source	Enthalten in International journal of hydrogen energy 44 volume:44
sourceStr	Enthalten in International journal of hydrogen energy 44 volume:44
format_phy_str_mv	Article
bklname	Regenerative Energieformen alternative Energieformen
institution	findex.gbv.de
topic_facet	Partial oxidation Syngas production Filtration combustion Porous media Reactor design
dewey-raw	660
isfreeaccess_bool	false
container_title	International journal of hydrogen energy
authorswithroles_txt_mv	Polianczyk, E.V. @@aut@@ Dorofeenko, S.O. @@aut@@
publishDateDaySort_date	2018-01-01T00:00:00Z
hierarchy_top_id	301511357
dewey-sort	3660
id	ELV001525360
language_de	englisch
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author	Polianczyk, E.V.
spellingShingle	Polianczyk, E.V. ddc 660 bkl 52.56 misc Partial oxidation misc Syngas production misc Filtration combustion misc Porous media misc Reactor design Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor
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topic_title	660 620 DE-600 52.56 bkl Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor Partial oxidation Syngas production Filtration combustion Porous media Reactor design
topic	ddc 660 bkl 52.56 misc Partial oxidation misc Syngas production misc Filtration combustion misc Porous media misc Reactor design
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title	Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor
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title_full	Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor
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title_sort	conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor
title_auth	Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor
abstract	The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the previously considered conversion in a reversed-flow reactor, such embodiment provides a possibility of attaining high combustion temperature due to efficient heat recuperation, while performing the process continuously without transients associated with the flow reverse. In the moving bed process, the flowrate of the granular material becomes an independent control parameter. A thermodynamic assessment of the macrokinetic conversion regimes as dependent on fuel composition and oxidant gas and fuel supply rates and granular solid flowrate is performed under the assumption that the combustion temperature is self-consistent according to thermodynamic equilibrium with the composition of syngas. Calculations for the methane/air-steam and 2-propanol/air-steam conversion are provided as examples. The calculations show that the process provides a possibility to combine in a stationary continuous process a high combustion temperature with low net heat effect and thus, a high chemical efficiency of conversion. The parametric domain for control parameters providing highly efficient conversion is determined.
abstractGer	The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the previously considered conversion in a reversed-flow reactor, such embodiment provides a possibility of attaining high combustion temperature due to efficient heat recuperation, while performing the process continuously without transients associated with the flow reverse. In the moving bed process, the flowrate of the granular material becomes an independent control parameter. A thermodynamic assessment of the macrokinetic conversion regimes as dependent on fuel composition and oxidant gas and fuel supply rates and granular solid flowrate is performed under the assumption that the combustion temperature is self-consistent according to thermodynamic equilibrium with the composition of syngas. Calculations for the methane/air-steam and 2-propanol/air-steam conversion are provided as examples. The calculations show that the process provides a possibility to combine in a stationary continuous process a high combustion temperature with low net heat effect and thus, a high chemical efficiency of conversion. The parametric domain for control parameters providing highly efficient conversion is determined.
abstract_unstemmed	The conversion of hydrocarbons to synthesis gases via partial oxidation in a non-premixed filtration combustion is considered in a continuous reactor wherein filtration medium/inert solid matrix comprises a moving bed of a granular material flowing countercurrently to the gas flow. Similar to the previously considered conversion in a reversed-flow reactor, such embodiment provides a possibility of attaining high combustion temperature due to efficient heat recuperation, while performing the process continuously without transients associated with the flow reverse. In the moving bed process, the flowrate of the granular material becomes an independent control parameter. A thermodynamic assessment of the macrokinetic conversion regimes as dependent on fuel composition and oxidant gas and fuel supply rates and granular solid flowrate is performed under the assumption that the combustion temperature is self-consistent according to thermodynamic equilibrium with the composition of syngas. Calculations for the methane/air-steam and 2-propanol/air-steam conversion are provided as examples. The calculations show that the process provides a possibility to combine in a stationary continuous process a high combustion temperature with low net heat effect and thus, a high chemical efficiency of conversion. The parametric domain for control parameters providing highly efficient conversion is determined.
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title_short	Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor
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doi_str	10.1016/j.ijhydene.2018.12.117
up_date	2024-07-06T21:40:18.037Z
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Conversion of hydrocarbons to synthesis gas in a counterflow moving bed filtration combustion reactor

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