$ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure
Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Mutyala, Suresh [verfasserIn] Yu, Ya-Dong [verfasserIn] Jin, Wei-Guang [verfasserIn] Wang, Zhi-Shuo [verfasserIn] Zheng, Deng-Yue [verfasserIn] Ye, Chun-Rong [verfasserIn] Luo, Binbin [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2019 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: Journal of porous materials - Dordrecht [u.a.] : Springer Science + Business Media B.V, 1995, 26(2019), 6 vom: 22. Juni, Seite 1831-1838 |
|---|---|
| Übergeordnetes Werk: |
volume:26 ; year:2019 ; number:6 ; day:22 ; month:06 ; pages:1831-1838 |
| Links: |
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| DOI / URN: |
10.1007/s10934-019-00779-x |
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| Katalog-ID: |
SPR014760517 |
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| 520 | |a Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. Avrami adsorption kinetic model has suggested adsorption of $ CO_{2} $ on composite material was chemical adsorption and deactivation model suggested an initial rate of adsorption was higher on TEPA incorporated UiO-66. | ||
| 650 | 4 | |a Tetraethylenepentamine |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a UiO-66 |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a CO |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a capture |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Fixed bed reactor |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Adsorption kinetic model |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Deactivation model |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a Yu, Ya-Dong |e verfasserin |4 aut | |
| 700 | 1 | |a Jin, Wei-Guang |e verfasserin |4 aut | |
| 700 | 1 | |a Wang, Zhi-Shuo |e verfasserin |4 aut | |
| 700 | 1 | |a Zheng, Deng-Yue |e verfasserin |4 aut | |
| 700 | 1 | |a Ye, Chun-Rong |e verfasserin |4 aut | |
| 700 | 1 | |a Luo, Binbin |e verfasserin |4 aut | |
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10.1007/s10934-019-00779-x doi (DE-627)SPR014760517 (SPR)s10934-019-00779-x-e DE-627 ger DE-627 rakwb eng 670 ASE 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 bkl Mutyala, Suresh verfasserin aut $ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. Avrami adsorption kinetic model has suggested adsorption of $ CO_{2} $ on composite material was chemical adsorption and deactivation model suggested an initial rate of adsorption was higher on TEPA incorporated UiO-66. Tetraethylenepentamine (dpeaa)DE-He213 UiO-66 (dpeaa)DE-He213 CO (dpeaa)DE-He213 capture (dpeaa)DE-He213 Fixed bed reactor (dpeaa)DE-He213 Adsorption kinetic model (dpeaa)DE-He213 Deactivation model (dpeaa)DE-He213 Yu, Ya-Dong verfasserin aut Jin, Wei-Guang verfasserin aut Wang, Zhi-Shuo verfasserin aut Zheng, Deng-Yue verfasserin aut Ye, Chun-Rong verfasserin aut Luo, Binbin verfasserin aut Enthalten in Journal of porous materials Dordrecht [u.a.] : Springer Science + Business Media B.V, 1995 26(2019), 6 vom: 22. Juni, Seite 1831-1838 (DE-627)310975158 (DE-600)2007476-1 1573-4854 nnns volume:26 year:2019 number:6 day:22 month:06 pages:1831-1838 https://dx.doi.org/10.1007/s10934-019-00779-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OPC-GGO SSG-OPC-GEO SSG-OPC-ASE 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_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 51.45 ASE 50.35 ASE 38.58 ASE 35.90 ASE 33.61 ASE AR 26 2019 6 22 06 1831-1838 |
| spelling |
10.1007/s10934-019-00779-x doi (DE-627)SPR014760517 (SPR)s10934-019-00779-x-e DE-627 ger DE-627 rakwb eng 670 ASE 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 bkl Mutyala, Suresh verfasserin aut $ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. Avrami adsorption kinetic model has suggested adsorption of $ CO_{2} $ on composite material was chemical adsorption and deactivation model suggested an initial rate of adsorption was higher on TEPA incorporated UiO-66. Tetraethylenepentamine (dpeaa)DE-He213 UiO-66 (dpeaa)DE-He213 CO (dpeaa)DE-He213 capture (dpeaa)DE-He213 Fixed bed reactor (dpeaa)DE-He213 Adsorption kinetic model (dpeaa)DE-He213 Deactivation model (dpeaa)DE-He213 Yu, Ya-Dong verfasserin aut Jin, Wei-Guang verfasserin aut Wang, Zhi-Shuo verfasserin aut Zheng, Deng-Yue verfasserin aut Ye, Chun-Rong verfasserin aut Luo, Binbin verfasserin aut Enthalten in Journal of porous materials Dordrecht [u.a.] : Springer Science + Business Media B.V, 1995 26(2019), 6 vom: 22. Juni, Seite 1831-1838 (DE-627)310975158 (DE-600)2007476-1 1573-4854 nnns volume:26 year:2019 number:6 day:22 month:06 pages:1831-1838 https://dx.doi.org/10.1007/s10934-019-00779-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OPC-GGO SSG-OPC-GEO SSG-OPC-ASE 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_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 51.45 ASE 50.35 ASE 38.58 ASE 35.90 ASE 33.61 ASE AR 26 2019 6 22 06 1831-1838 |
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10.1007/s10934-019-00779-x doi (DE-627)SPR014760517 (SPR)s10934-019-00779-x-e DE-627 ger DE-627 rakwb eng 670 ASE 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 bkl Mutyala, Suresh verfasserin aut $ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. Avrami adsorption kinetic model has suggested adsorption of $ CO_{2} $ on composite material was chemical adsorption and deactivation model suggested an initial rate of adsorption was higher on TEPA incorporated UiO-66. Tetraethylenepentamine (dpeaa)DE-He213 UiO-66 (dpeaa)DE-He213 CO (dpeaa)DE-He213 capture (dpeaa)DE-He213 Fixed bed reactor (dpeaa)DE-He213 Adsorption kinetic model (dpeaa)DE-He213 Deactivation model (dpeaa)DE-He213 Yu, Ya-Dong verfasserin aut Jin, Wei-Guang verfasserin aut Wang, Zhi-Shuo verfasserin aut Zheng, Deng-Yue verfasserin aut Ye, Chun-Rong verfasserin aut Luo, Binbin verfasserin aut Enthalten in Journal of porous materials Dordrecht [u.a.] : Springer Science + Business Media B.V, 1995 26(2019), 6 vom: 22. Juni, Seite 1831-1838 (DE-627)310975158 (DE-600)2007476-1 1573-4854 nnns volume:26 year:2019 number:6 day:22 month:06 pages:1831-1838 https://dx.doi.org/10.1007/s10934-019-00779-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OPC-GGO SSG-OPC-GEO SSG-OPC-ASE 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_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 51.45 ASE 50.35 ASE 38.58 ASE 35.90 ASE 33.61 ASE AR 26 2019 6 22 06 1831-1838 |
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10.1007/s10934-019-00779-x doi (DE-627)SPR014760517 (SPR)s10934-019-00779-x-e DE-627 ger DE-627 rakwb eng 670 ASE 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 bkl Mutyala, Suresh verfasserin aut $ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. Avrami adsorption kinetic model has suggested adsorption of $ CO_{2} $ on composite material was chemical adsorption and deactivation model suggested an initial rate of adsorption was higher on TEPA incorporated UiO-66. Tetraethylenepentamine (dpeaa)DE-He213 UiO-66 (dpeaa)DE-He213 CO (dpeaa)DE-He213 capture (dpeaa)DE-He213 Fixed bed reactor (dpeaa)DE-He213 Adsorption kinetic model (dpeaa)DE-He213 Deactivation model (dpeaa)DE-He213 Yu, Ya-Dong verfasserin aut Jin, Wei-Guang verfasserin aut Wang, Zhi-Shuo verfasserin aut Zheng, Deng-Yue verfasserin aut Ye, Chun-Rong verfasserin aut Luo, Binbin verfasserin aut Enthalten in Journal of porous materials Dordrecht [u.a.] : Springer Science + Business Media B.V, 1995 26(2019), 6 vom: 22. Juni, Seite 1831-1838 (DE-627)310975158 (DE-600)2007476-1 1573-4854 nnns volume:26 year:2019 number:6 day:22 month:06 pages:1831-1838 https://dx.doi.org/10.1007/s10934-019-00779-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OPC-GGO SSG-OPC-GEO SSG-OPC-ASE 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_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 51.45 ASE 50.35 ASE 38.58 ASE 35.90 ASE 33.61 ASE AR 26 2019 6 22 06 1831-1838 |
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10.1007/s10934-019-00779-x doi (DE-627)SPR014760517 (SPR)s10934-019-00779-x-e DE-627 ger DE-627 rakwb eng 670 ASE 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 bkl Mutyala, Suresh verfasserin aut $ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. Avrami adsorption kinetic model has suggested adsorption of $ CO_{2} $ on composite material was chemical adsorption and deactivation model suggested an initial rate of adsorption was higher on TEPA incorporated UiO-66. Tetraethylenepentamine (dpeaa)DE-He213 UiO-66 (dpeaa)DE-He213 CO (dpeaa)DE-He213 capture (dpeaa)DE-He213 Fixed bed reactor (dpeaa)DE-He213 Adsorption kinetic model (dpeaa)DE-He213 Deactivation model (dpeaa)DE-He213 Yu, Ya-Dong verfasserin aut Jin, Wei-Guang verfasserin aut Wang, Zhi-Shuo verfasserin aut Zheng, Deng-Yue verfasserin aut Ye, Chun-Rong verfasserin aut Luo, Binbin verfasserin aut Enthalten in Journal of porous materials Dordrecht [u.a.] : Springer Science + Business Media B.V, 1995 26(2019), 6 vom: 22. Juni, Seite 1831-1838 (DE-627)310975158 (DE-600)2007476-1 1573-4854 nnns volume:26 year:2019 number:6 day:22 month:06 pages:1831-1838 https://dx.doi.org/10.1007/s10934-019-00779-x lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OPC-GGO SSG-OPC-GEO SSG-OPC-ASE 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_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 51.45 ASE 50.35 ASE 38.58 ASE 35.90 ASE 33.61 ASE AR 26 2019 6 22 06 1831-1838 |
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Enthalten in Journal of porous materials 26(2019), 6 vom: 22. Juni, Seite 1831-1838 volume:26 year:2019 number:6 day:22 month:06 pages:1831-1838 |
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Tetraethylenepentamine UiO-66 CO capture Fixed bed reactor Adsorption kinetic model Deactivation model |
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Mutyala, Suresh @@aut@@ Yu, Ya-Dong @@aut@@ Jin, Wei-Guang @@aut@@ Wang, Zhi-Shuo @@aut@@ Zheng, Deng-Yue @@aut@@ Ye, Chun-Rong @@aut@@ Luo, Binbin @@aut@@ |
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All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. 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|
| author |
Mutyala, Suresh |
| spellingShingle |
Mutyala, Suresh ddc 670 bkl 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 misc Tetraethylenepentamine misc UiO-66 misc CO misc capture misc Fixed bed reactor misc Adsorption kinetic model misc Deactivation model $ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure |
| authorStr |
Mutyala, Suresh |
| ppnlink_with_tag_str_mv |
@@773@@(DE-627)310975158 |
| format |
electronic Article |
| dewey-ones |
670 - Manufacturing |
| delete_txt_mv |
keep |
| author_role |
aut aut aut aut aut aut aut |
| collection |
springer |
| remote_str |
true |
| illustrated |
Not Illustrated |
| issn |
1573-4854 |
| topic_title |
670 ASE 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 bkl $ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure Tetraethylenepentamine (dpeaa)DE-He213 UiO-66 (dpeaa)DE-He213 CO (dpeaa)DE-He213 capture (dpeaa)DE-He213 Fixed bed reactor (dpeaa)DE-He213 Adsorption kinetic model (dpeaa)DE-He213 Deactivation model (dpeaa)DE-He213 |
| topic |
ddc 670 bkl 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 misc Tetraethylenepentamine misc UiO-66 misc CO misc capture misc Fixed bed reactor misc Adsorption kinetic model misc Deactivation model |
| topic_unstemmed |
ddc 670 bkl 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 misc Tetraethylenepentamine misc UiO-66 misc CO misc capture misc Fixed bed reactor misc Adsorption kinetic model misc Deactivation model |
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ddc 670 bkl 51.45 bkl 50.35 bkl 38.58 bkl 35.90 bkl 33.61 misc Tetraethylenepentamine misc UiO-66 misc CO misc capture misc Fixed bed reactor misc Adsorption kinetic model misc Deactivation model |
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$ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure |
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$ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure |
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Mutyala, Suresh |
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Journal of porous materials |
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Mutyala, Suresh Yu, Ya-Dong Jin, Wei-Guang Wang, Zhi-Shuo Zheng, Deng-Yue Ye, Chun-Rong Luo, Binbin |
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$ co_{2} $ capture using amine incorporated uio-66 in atmospheric pressure |
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$ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure |
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Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. Avrami adsorption kinetic model has suggested adsorption of $ CO_{2} $ on composite material was chemical adsorption and deactivation model suggested an initial rate of adsorption was higher on TEPA incorporated UiO-66. |
| abstractGer |
Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. Avrami adsorption kinetic model has suggested adsorption of $ CO_{2} $ on composite material was chemical adsorption and deactivation model suggested an initial rate of adsorption was higher on TEPA incorporated UiO-66. |
| abstract_unstemmed |
Abstract Composite material, tetraethylenepentamine (TEPA) incorporated UiO-66 was prepared by impregnation method to study $ CO_{2} $ capture in a fixed bed reactor, atmospheric pressure. All synthesized adsorbents were characterized using PXRD, $ N_{2} $ adsorption–desorption isotherms, FT-IR, TGA, SEM, and Elemental analysis. Characterization results have revealed that incorporated TEPA was present within pores of UiO-66. $ CO_{2} $ adsorption was higher on TEPA incorporated UiO-66 compared to UiO-66. It was due to the chemical interaction between –$ NH_{2} $ and $ CO_{2} $. High $ CO_{2} $ adsorption capacity 3.70 mmol $ g^{−1} $ was obtained on 30TEPA/UiO-66 at 75 °C, 1 bar. Because of more flexibility and high dispersive nature of TEPA at this temperature. The same $ CO_{2} $ adsorption capacity was obtained in each adsorption cycle without decomposition of the amine on 30TEPA/UiO-66. Avrami adsorption kinetic model has suggested adsorption of $ CO_{2} $ on composite material was chemical adsorption and deactivation model suggested an initial rate of adsorption was higher on TEPA incorporated UiO-66. |
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$ CO_{2} $ capture using amine incorporated UiO-66 in atmospheric pressure |
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| score |
7.401636 |