Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts
Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with incre...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Zhang, Yajie [verfasserIn] Liew, Kongyong [verfasserIn] Li, Jinlin [verfasserIn] Zhan, Xiaodong [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2010 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: Catalysis letters - Dordrecht [u.a.] : Springer Science + Business Media B.V, 1988, 139(2010), 1-2 vom: 08. Juli, Seite 1-6 |
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| Übergeordnetes Werk: |
volume:139 ; year:2010 ; number:1-2 ; day:08 ; month:07 ; pages:1-6 |
| Links: |
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| DOI / URN: |
10.1007/s10562-010-0407-z |
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| Katalog-ID: |
SPR011332271 |
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| 520 | |a Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h. | ||
| 650 | 4 | |a Fischer–Tropsch Synthesis |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Lanthanum |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Cobalt |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Titania |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Catalyst |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a Liew, Kongyong |e verfasserin |4 aut | |
| 700 | 1 | |a Li, Jinlin |e verfasserin |4 aut | |
| 700 | 1 | |a Zhan, Xiaodong |e verfasserin |4 aut | |
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10.1007/s10562-010-0407-z doi (DE-627)SPR011332271 (SPR)s10562-010-0407-z-e DE-627 ger DE-627 rakwb eng 540 660 ASE 35.17 bkl Zhang, Yajie verfasserin aut Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts 2010 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h. Fischer–Tropsch Synthesis (dpeaa)DE-He213 Lanthanum (dpeaa)DE-He213 Cobalt (dpeaa)DE-He213 Titania (dpeaa)DE-He213 Catalyst (dpeaa)DE-He213 Liew, Kongyong verfasserin aut Li, Jinlin verfasserin aut Zhan, Xiaodong verfasserin aut Enthalten in Catalysis letters Dordrecht [u.a.] : Springer Science + Business Media B.V, 1988 139(2010), 1-2 vom: 08. Juli, Seite 1-6 (DE-627)306717638 (DE-600)1501518-X 1572-879X nnns volume:139 year:2010 number:1-2 day:08 month:07 pages:1-6 https://dx.doi.org/10.1007/s10562-010-0407-z 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.17 ASE AR 139 2010 1-2 08 07 1-6 |
| spelling |
10.1007/s10562-010-0407-z doi (DE-627)SPR011332271 (SPR)s10562-010-0407-z-e DE-627 ger DE-627 rakwb eng 540 660 ASE 35.17 bkl Zhang, Yajie verfasserin aut Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts 2010 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h. Fischer–Tropsch Synthesis (dpeaa)DE-He213 Lanthanum (dpeaa)DE-He213 Cobalt (dpeaa)DE-He213 Titania (dpeaa)DE-He213 Catalyst (dpeaa)DE-He213 Liew, Kongyong verfasserin aut Li, Jinlin verfasserin aut Zhan, Xiaodong verfasserin aut Enthalten in Catalysis letters Dordrecht [u.a.] : Springer Science + Business Media B.V, 1988 139(2010), 1-2 vom: 08. Juli, Seite 1-6 (DE-627)306717638 (DE-600)1501518-X 1572-879X nnns volume:139 year:2010 number:1-2 day:08 month:07 pages:1-6 https://dx.doi.org/10.1007/s10562-010-0407-z 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.17 ASE AR 139 2010 1-2 08 07 1-6 |
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10.1007/s10562-010-0407-z doi (DE-627)SPR011332271 (SPR)s10562-010-0407-z-e DE-627 ger DE-627 rakwb eng 540 660 ASE 35.17 bkl Zhang, Yajie verfasserin aut Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts 2010 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h. Fischer–Tropsch Synthesis (dpeaa)DE-He213 Lanthanum (dpeaa)DE-He213 Cobalt (dpeaa)DE-He213 Titania (dpeaa)DE-He213 Catalyst (dpeaa)DE-He213 Liew, Kongyong verfasserin aut Li, Jinlin verfasserin aut Zhan, Xiaodong verfasserin aut Enthalten in Catalysis letters Dordrecht [u.a.] : Springer Science + Business Media B.V, 1988 139(2010), 1-2 vom: 08. Juli, Seite 1-6 (DE-627)306717638 (DE-600)1501518-X 1572-879X nnns volume:139 year:2010 number:1-2 day:08 month:07 pages:1-6 https://dx.doi.org/10.1007/s10562-010-0407-z 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.17 ASE AR 139 2010 1-2 08 07 1-6 |
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10.1007/s10562-010-0407-z doi (DE-627)SPR011332271 (SPR)s10562-010-0407-z-e DE-627 ger DE-627 rakwb eng 540 660 ASE 35.17 bkl Zhang, Yajie verfasserin aut Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts 2010 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h. Fischer–Tropsch Synthesis (dpeaa)DE-He213 Lanthanum (dpeaa)DE-He213 Cobalt (dpeaa)DE-He213 Titania (dpeaa)DE-He213 Catalyst (dpeaa)DE-He213 Liew, Kongyong verfasserin aut Li, Jinlin verfasserin aut Zhan, Xiaodong verfasserin aut Enthalten in Catalysis letters Dordrecht [u.a.] : Springer Science + Business Media B.V, 1988 139(2010), 1-2 vom: 08. Juli, Seite 1-6 (DE-627)306717638 (DE-600)1501518-X 1572-879X nnns volume:139 year:2010 number:1-2 day:08 month:07 pages:1-6 https://dx.doi.org/10.1007/s10562-010-0407-z 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.17 ASE AR 139 2010 1-2 08 07 1-6 |
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10.1007/s10562-010-0407-z doi (DE-627)SPR011332271 (SPR)s10562-010-0407-z-e DE-627 ger DE-627 rakwb eng 540 660 ASE 35.17 bkl Zhang, Yajie verfasserin aut Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts 2010 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h. Fischer–Tropsch Synthesis (dpeaa)DE-He213 Lanthanum (dpeaa)DE-He213 Cobalt (dpeaa)DE-He213 Titania (dpeaa)DE-He213 Catalyst (dpeaa)DE-He213 Liew, Kongyong verfasserin aut Li, Jinlin verfasserin aut Zhan, Xiaodong verfasserin aut Enthalten in Catalysis letters Dordrecht [u.a.] : Springer Science + Business Media B.V, 1988 139(2010), 1-2 vom: 08. Juli, Seite 1-6 (DE-627)306717638 (DE-600)1501518-X 1572-879X nnns volume:139 year:2010 number:1-2 day:08 month:07 pages:1-6 https://dx.doi.org/10.1007/s10562-010-0407-z 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_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_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_4012 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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 35.17 ASE AR 139 2010 1-2 08 07 1-6 |
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Fischer–Tropsch Synthesis Lanthanum Cobalt Titania Catalyst |
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Zhang, Yajie @@aut@@ Liew, Kongyong @@aut@@ Li, Jinlin @@aut@@ Zhan, Xiaodong @@aut@@ |
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The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Fischer–Tropsch Synthesis</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Lanthanum</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Cobalt</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Titania</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Catalyst</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Liew, Kongyong</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Li, Jinlin</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Zhan, Xiaodong</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Catalysis letters</subfield><subfield code="d">Dordrecht [u.a.] : Springer Science + Business Media B.V, 1988</subfield><subfield code="g">139(2010), 1-2 vom: 08. 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Zhang, Yajie |
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Zhang, Yajie ddc 540 bkl 35.17 misc Fischer–Tropsch Synthesis misc Lanthanum misc Cobalt misc Titania misc Catalyst Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts |
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540 660 ASE 35.17 bkl Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts Fischer–Tropsch Synthesis (dpeaa)DE-He213 Lanthanum (dpeaa)DE-He213 Cobalt (dpeaa)DE-He213 Titania (dpeaa)DE-He213 Catalyst (dpeaa)DE-He213 |
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ddc 540 bkl 35.17 misc Fischer–Tropsch Synthesis misc Lanthanum misc Cobalt misc Titania misc Catalyst |
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ddc 540 bkl 35.17 misc Fischer–Tropsch Synthesis misc Lanthanum misc Cobalt misc Titania misc Catalyst |
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Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts |
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Zhang, Yajie Liew, Kongyong Li, Jinlin Zhan, Xiaodong |
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fischer–tropsch synthesis on lanthanum promoted co/$ tio_{2} $ catalysts |
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Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts |
| abstract |
Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h. |
| abstractGer |
Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h. |
| abstract_unstemmed |
Abstract Lanthanum promoted titania-supported cobalt catalysts were prepared using incipient wetness impregnation method. The catalysts were characterized by XRD, TPR and TPD. The catalytic activity for Fischer–Tropsch synthesis was evaluated in a fixed-bed reactor. The activity increased with increasing La content except at high loadings. Furthermore, La promoter increased methane and $ CO_{2} $ selectivity, suppressed the formation of $ C_{5+} $ products. Graphical Abstract TPR profiles of prepared catalysts. (a) Co–Ti–0La; (b) Co–Ti–1/2000La; (c) Co–Ti–1/200La; (d) Co–Ti–1/120La; (e) Co–Ti–1/20La; (f) Co–Ti–1/20La recalcined at 673 K for 6 h. |
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1-2 |
| title_short |
Fischer–Tropsch Synthesis on Lanthanum Promoted Co/$ TiO_{2} $ Catalysts |
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https://dx.doi.org/10.1007/s10562-010-0407-z |
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| author2 |
Liew, Kongyong Li, Jinlin Zhan, Xiaodong |
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Liew, Kongyong Li, Jinlin Zhan, Xiaodong |
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| doi_str |
10.1007/s10562-010-0407-z |
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2024-07-03T21:59:33.755Z |
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| score |
7.3982153 |