Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst

Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conv...
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Autor*in:	Didenko, L. P. [verfasserIn] Savchenko, V. I. Arutyunov, V. S. Sementsova, L. A.

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2008

Schlagwörter:	Steam Petroleum Chemistry Methane Conversion Coke Formation Steam Reform

Anmerkung:	© Pleiades Publishing, Ltd. 2008

Übergeordnetes Werk:	Enthalten in: Petroleum chemistry - Berlin : Springer, 1962, 48(2008), 1 vom: Jan., Seite 22-27
Übergeordnetes Werk:	volume:48 ; year:2008 ; number:1 ; month:01 ; pages:22-27

Links:	Volltext

DOI / URN:	10.1134/S0965544108010040

Katalog-ID:	SPR020184352

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520			\|a Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam.
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650		4	\|a Methane Conversion \|7 (dpeaa)DE-He213
650		4	\|a Coke Formation \|7 (dpeaa)DE-He213
650		4	\|a Steam Reform \|7 (dpeaa)DE-He213
700	1		\|a Savchenko, V. I. \|4 aut
700	1		\|a Arutyunov, V. S. \|4 aut
700	1		\|a Sementsova, L. A. \|4 aut
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856	4	0	\|u https://dx.doi.org/10.1134/S0965544108010040 \|z lizenzpflichtig \|3 Volltext
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matchkey_str	article:15556239:2008----::tarfrigfehnmxuewtehlnoeaids
hierarchy_sort_str	2008
publishDate	2008
allfields	10.1134/S0965544108010040 doi (DE-627)SPR020184352 (SPR)S0965544108010040-e DE-627 ger DE-627 rakwb eng Didenko, L. P. verfasserin aut Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2008 Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam. Steam (dpeaa)DE-He213 Petroleum Chemistry (dpeaa)DE-He213 Methane Conversion (dpeaa)DE-He213 Coke Formation (dpeaa)DE-He213 Steam Reform (dpeaa)DE-He213 Savchenko, V. I. aut Arutyunov, V. S. aut Sementsova, L. A. aut Enthalten in Petroleum chemistry Berlin : Springer, 1962 48(2008), 1 vom: Jan., Seite 22-27 (DE-627)331503778 (DE-600)2051391-4 1555-6239 nnns volume:48 year:2008 number:1 month:01 pages:22-27 https://dx.doi.org/10.1134/S0965544108010040 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2008 1 01 22-27
spelling	10.1134/S0965544108010040 doi (DE-627)SPR020184352 (SPR)S0965544108010040-e DE-627 ger DE-627 rakwb eng Didenko, L. P. verfasserin aut Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2008 Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam. Steam (dpeaa)DE-He213 Petroleum Chemistry (dpeaa)DE-He213 Methane Conversion (dpeaa)DE-He213 Coke Formation (dpeaa)DE-He213 Steam Reform (dpeaa)DE-He213 Savchenko, V. I. aut Arutyunov, V. S. aut Sementsova, L. A. aut Enthalten in Petroleum chemistry Berlin : Springer, 1962 48(2008), 1 vom: Jan., Seite 22-27 (DE-627)331503778 (DE-600)2051391-4 1555-6239 nnns volume:48 year:2008 number:1 month:01 pages:22-27 https://dx.doi.org/10.1134/S0965544108010040 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2008 1 01 22-27
allfields_unstemmed	10.1134/S0965544108010040 doi (DE-627)SPR020184352 (SPR)S0965544108010040-e DE-627 ger DE-627 rakwb eng Didenko, L. P. verfasserin aut Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2008 Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam. Steam (dpeaa)DE-He213 Petroleum Chemistry (dpeaa)DE-He213 Methane Conversion (dpeaa)DE-He213 Coke Formation (dpeaa)DE-He213 Steam Reform (dpeaa)DE-He213 Savchenko, V. I. aut Arutyunov, V. S. aut Sementsova, L. A. aut Enthalten in Petroleum chemistry Berlin : Springer, 1962 48(2008), 1 vom: Jan., Seite 22-27 (DE-627)331503778 (DE-600)2051391-4 1555-6239 nnns volume:48 year:2008 number:1 month:01 pages:22-27 https://dx.doi.org/10.1134/S0965544108010040 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2008 1 01 22-27
allfieldsGer	10.1134/S0965544108010040 doi (DE-627)SPR020184352 (SPR)S0965544108010040-e DE-627 ger DE-627 rakwb eng Didenko, L. P. verfasserin aut Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2008 Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam. Steam (dpeaa)DE-He213 Petroleum Chemistry (dpeaa)DE-He213 Methane Conversion (dpeaa)DE-He213 Coke Formation (dpeaa)DE-He213 Steam Reform (dpeaa)DE-He213 Savchenko, V. I. aut Arutyunov, V. S. aut Sementsova, L. A. aut Enthalten in Petroleum chemistry Berlin : Springer, 1962 48(2008), 1 vom: Jan., Seite 22-27 (DE-627)331503778 (DE-600)2051391-4 1555-6239 nnns volume:48 year:2008 number:1 month:01 pages:22-27 https://dx.doi.org/10.1134/S0965544108010040 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2008 1 01 22-27
allfieldsSound	10.1134/S0965544108010040 doi (DE-627)SPR020184352 (SPR)S0965544108010040-e DE-627 ger DE-627 rakwb eng Didenko, L. P. verfasserin aut Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Pleiades Publishing, Ltd. 2008 Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam. Steam (dpeaa)DE-He213 Petroleum Chemistry (dpeaa)DE-He213 Methane Conversion (dpeaa)DE-He213 Coke Formation (dpeaa)DE-He213 Steam Reform (dpeaa)DE-He213 Savchenko, V. I. aut Arutyunov, V. S. aut Sementsova, L. A. aut Enthalten in Petroleum chemistry Berlin : Springer, 1962 48(2008), 1 vom: Jan., Seite 22-27 (DE-627)331503778 (DE-600)2051391-4 1555-6239 nnns volume:48 year:2008 number:1 month:01 pages:22-27 https://dx.doi.org/10.1134/S0965544108010040 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2008 1 01 22-27
language	English
source	Enthalten in Petroleum chemistry 48(2008), 1 vom: Jan., Seite 22-27 volume:48 year:2008 number:1 month:01 pages:22-27
sourceStr	Enthalten in Petroleum chemistry 48(2008), 1 vom: Jan., Seite 22-27 volume:48 year:2008 number:1 month:01 pages:22-27
format_phy_str_mv	Article
institution	findex.gbv.de
topic_facet	Steam Petroleum Chemistry Methane Conversion Coke Formation Steam Reform
isfreeaccess_bool	false
container_title	Petroleum chemistry
authorswithroles_txt_mv	Didenko, L. P. @@aut@@ Savchenko, V. I. @@aut@@ Arutyunov, V. S. @@aut@@ Sementsova, L. A. @@aut@@
publishDateDaySort_date	2008-01-01T00:00:00Z
hierarchy_top_id	331503778
id	SPR020184352
language_de	englisch
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author	Didenko, L. P.
spellingShingle	Didenko, L. P. misc Steam misc Petroleum Chemistry misc Methane Conversion misc Coke Formation misc Steam Reform Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst
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topic_title	Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst Steam (dpeaa)DE-He213 Petroleum Chemistry (dpeaa)DE-He213 Methane Conversion (dpeaa)DE-He213 Coke Formation (dpeaa)DE-He213 Steam Reform (dpeaa)DE-He213
topic	misc Steam misc Petroleum Chemistry misc Methane Conversion misc Coke Formation misc Steam Reform
topic_unstemmed	misc Steam misc Petroleum Chemistry misc Methane Conversion misc Coke Formation misc Steam Reform
topic_browse	misc Steam misc Petroleum Chemistry misc Methane Conversion misc Coke Formation misc Steam Reform
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title	Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst
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title_full	Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst
author_sort	Didenko, L. P.
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author_browse	Didenko, L. P. Savchenko, V. I. Arutyunov, V. S. Sementsova, L. A.
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author-letter	Didenko, L. P.
doi_str_mv	10.1134/S0965544108010040
title_sort	steam reforming of methane mixtures with ethylene over an industrial nickel catalyst
title_auth	Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst
abstract	Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam. © Pleiades Publishing, Ltd. 2008
abstractGer	Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam. © Pleiades Publishing, Ltd. 2008
abstract_unstemmed	Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam. © Pleiades Publishing, Ltd. 2008
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title_short	Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst
url	https://dx.doi.org/10.1134/S0965544108010040
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author2	Savchenko, V. I. Arutyunov, V. S. Sementsova, L. A.
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up_date	2024-07-03T14:25:15.198Z
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P.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2008</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">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="500" ind1=" " ind2=" "><subfield code="a">© Pleiades Publishing, Ltd. 2008</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract Steam reforming of methane mixtures with ethylene (1.4–3.8 vol % $ C_{2} %$ H_{4} $) in the presence of the industrial nickel catalyst S11-9-09 (12.8 wt % Ni/α-$ Al_{2} %$ O_{3} $) at 750°C was studied. It was shown that the addition of ethylene to the methane-steam mixture reduces the conversion of methane to carbon oxides and increases coke formation. The unfavorable effect of ethylene on the reaction decreases with an increase in the ratio of the catalytic surface area to the free reaction volume. Presumably, this effect is caused by an increase in the contribution of the heterogeneous component of steam reforming, a change that results in an increase in the rate of the interaction of the formed coke with steam.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Steam</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Petroleum Chemistry</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Methane Conversion</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Coke Formation</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Steam Reform</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Savchenko, V. 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Steam reforming of methane mixtures with ethylene over an industrial nickel catalyst

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