Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO

In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low vi...
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Autor*in:	Meng, Fanli [verfasserIn] Fu, Kun [verfasserIn] Wang, Xueli [verfasserIn] Wang, Yixiao [verfasserIn] Wang, Lemeng [verfasserIn] Fu, Dong [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2023

Schlagwörter:	Carbon dioxide Non-aqueous absorbent Absorption/desorption Water resistance Cycle

Übergeordnetes Werk:	Enthalten in: Energy - Amsterdam [u.a.] : Elsevier Science, 1976, 286
Übergeordnetes Werk:	volume:286

DOI / URN:	10.1016/j.energy.2023.129631

Katalog-ID:	ELV065803000

Internformat


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520			\|a In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low viscosity, and environmentally friendly properties. The optimization of the mass fraction resulted in a composition of 60 wt% EHA and 40 wt% DMSO, considering factors such as absorption capacity, absorption rate, and viscosity. At a desorption temperature of 373 K, the CO2-loaded EHA-DMSO exhibited a desorption efficiency of approximately 98 %. The estimation of desorption energy (E t) consumption, using the method of electric energy consumption, revealed that EHA-DMSO achieved approximately a 50 % reduction in E t compared to the MEA (30 wt%) absorbent. Even with a water content of 10 %, E t was reduced by around 40 %. Additionally, the absorbent demonstrated notable advantages in terms of water resistance and cycle performance. The advantages of environmental friendliness and easy availability of raw materials suggest that the EHA-DMSO absorbent holds a promising potential for broader application in the field of CO2 capture from flue gas.
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700	1		\|a Wang, Lemeng \|e verfasserin \|4 aut
700	1		\|a Fu, Dong \|e verfasserin \|4 aut
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912			\|a GBV_ILN_2049
912			\|a GBV_ILN_2050
912			\|a GBV_ILN_2055
912			\|a GBV_ILN_2056
912			\|a GBV_ILN_2059
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912			\|a GBV_ILN_2106
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912			\|a GBV_ILN_4251
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912			\|a GBV_ILN_4306
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912			\|a GBV_ILN_4323
912			\|a GBV_ILN_4324
912			\|a GBV_ILN_4325
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912			\|a GBV_ILN_4333
912			\|a GBV_ILN_4334
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publishDate	2023
allfields	10.1016/j.energy.2023.129631 doi (DE-627)ELV065803000 (ELSEVIER)S0360-5442(23)03025-6 DE-627 ger DE-627 rda eng 600 VZ 50.70 bkl Meng, Fanli verfasserin aut Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO 2023 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low viscosity, and environmentally friendly properties. The optimization of the mass fraction resulted in a composition of 60 wt% EHA and 40 wt% DMSO, considering factors such as absorption capacity, absorption rate, and viscosity. At a desorption temperature of 373 K, the CO2-loaded EHA-DMSO exhibited a desorption efficiency of approximately 98 %. The estimation of desorption energy (E t) consumption, using the method of electric energy consumption, revealed that EHA-DMSO achieved approximately a 50 % reduction in E t compared to the MEA (30 wt%) absorbent. Even with a water content of 10 %, E t was reduced by around 40 %. Additionally, the absorbent demonstrated notable advantages in terms of water resistance and cycle performance. The advantages of environmental friendliness and easy availability of raw materials suggest that the EHA-DMSO absorbent holds a promising potential for broader application in the field of CO2 capture from flue gas. Carbon dioxide Non-aqueous absorbent Absorption/desorption Water resistance Cycle Fu, Kun verfasserin aut Wang, Xueli verfasserin aut Wang, Yixiao verfasserin aut Wang, Lemeng verfasserin aut Fu, Dong verfasserin aut Enthalten in Energy Amsterdam [u.a.] : Elsevier Science, 1976 286 Online-Ressource (DE-627)320597903 (DE-600)2019804-8 (DE-576)116451815 1873-6785 nnns volume:286 GBV_USEFLAG_U GBV_ELV SYSFLAG_U 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_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_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 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_2034 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 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_4338 GBV_ILN_4393 GBV_ILN_4700 50.70 Energie: Allgemeines VZ AR 286
spelling	10.1016/j.energy.2023.129631 doi (DE-627)ELV065803000 (ELSEVIER)S0360-5442(23)03025-6 DE-627 ger DE-627 rda eng 600 VZ 50.70 bkl Meng, Fanli verfasserin aut Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO 2023 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low viscosity, and environmentally friendly properties. The optimization of the mass fraction resulted in a composition of 60 wt% EHA and 40 wt% DMSO, considering factors such as absorption capacity, absorption rate, and viscosity. At a desorption temperature of 373 K, the CO2-loaded EHA-DMSO exhibited a desorption efficiency of approximately 98 %. The estimation of desorption energy (E t) consumption, using the method of electric energy consumption, revealed that EHA-DMSO achieved approximately a 50 % reduction in E t compared to the MEA (30 wt%) absorbent. Even with a water content of 10 %, E t was reduced by around 40 %. Additionally, the absorbent demonstrated notable advantages in terms of water resistance and cycle performance. The advantages of environmental friendliness and easy availability of raw materials suggest that the EHA-DMSO absorbent holds a promising potential for broader application in the field of CO2 capture from flue gas. Carbon dioxide Non-aqueous absorbent Absorption/desorption Water resistance Cycle Fu, Kun verfasserin aut Wang, Xueli verfasserin aut Wang, Yixiao verfasserin aut Wang, Lemeng verfasserin aut Fu, Dong verfasserin aut Enthalten in Energy Amsterdam [u.a.] : Elsevier Science, 1976 286 Online-Ressource (DE-627)320597903 (DE-600)2019804-8 (DE-576)116451815 1873-6785 nnns volume:286 GBV_USEFLAG_U GBV_ELV SYSFLAG_U 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_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_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 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_2034 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 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_4338 GBV_ILN_4393 GBV_ILN_4700 50.70 Energie: Allgemeines VZ AR 286
allfields_unstemmed	10.1016/j.energy.2023.129631 doi (DE-627)ELV065803000 (ELSEVIER)S0360-5442(23)03025-6 DE-627 ger DE-627 rda eng 600 VZ 50.70 bkl Meng, Fanli verfasserin aut Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO 2023 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low viscosity, and environmentally friendly properties. The optimization of the mass fraction resulted in a composition of 60 wt% EHA and 40 wt% DMSO, considering factors such as absorption capacity, absorption rate, and viscosity. At a desorption temperature of 373 K, the CO2-loaded EHA-DMSO exhibited a desorption efficiency of approximately 98 %. The estimation of desorption energy (E t) consumption, using the method of electric energy consumption, revealed that EHA-DMSO achieved approximately a 50 % reduction in E t compared to the MEA (30 wt%) absorbent. Even with a water content of 10 %, E t was reduced by around 40 %. Additionally, the absorbent demonstrated notable advantages in terms of water resistance and cycle performance. The advantages of environmental friendliness and easy availability of raw materials suggest that the EHA-DMSO absorbent holds a promising potential for broader application in the field of CO2 capture from flue gas. Carbon dioxide Non-aqueous absorbent Absorption/desorption Water resistance Cycle Fu, Kun verfasserin aut Wang, Xueli verfasserin aut Wang, Yixiao verfasserin aut Wang, Lemeng verfasserin aut Fu, Dong verfasserin aut Enthalten in Energy Amsterdam [u.a.] : Elsevier Science, 1976 286 Online-Ressource (DE-627)320597903 (DE-600)2019804-8 (DE-576)116451815 1873-6785 nnns volume:286 GBV_USEFLAG_U GBV_ELV SYSFLAG_U 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_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_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 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_2034 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 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_4338 GBV_ILN_4393 GBV_ILN_4700 50.70 Energie: Allgemeines VZ AR 286
allfieldsGer	10.1016/j.energy.2023.129631 doi (DE-627)ELV065803000 (ELSEVIER)S0360-5442(23)03025-6 DE-627 ger DE-627 rda eng 600 VZ 50.70 bkl Meng, Fanli verfasserin aut Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO 2023 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low viscosity, and environmentally friendly properties. The optimization of the mass fraction resulted in a composition of 60 wt% EHA and 40 wt% DMSO, considering factors such as absorption capacity, absorption rate, and viscosity. At a desorption temperature of 373 K, the CO2-loaded EHA-DMSO exhibited a desorption efficiency of approximately 98 %. The estimation of desorption energy (E t) consumption, using the method of electric energy consumption, revealed that EHA-DMSO achieved approximately a 50 % reduction in E t compared to the MEA (30 wt%) absorbent. Even with a water content of 10 %, E t was reduced by around 40 %. Additionally, the absorbent demonstrated notable advantages in terms of water resistance and cycle performance. The advantages of environmental friendliness and easy availability of raw materials suggest that the EHA-DMSO absorbent holds a promising potential for broader application in the field of CO2 capture from flue gas. Carbon dioxide Non-aqueous absorbent Absorption/desorption Water resistance Cycle Fu, Kun verfasserin aut Wang, Xueli verfasserin aut Wang, Yixiao verfasserin aut Wang, Lemeng verfasserin aut Fu, Dong verfasserin aut Enthalten in Energy Amsterdam [u.a.] : Elsevier Science, 1976 286 Online-Ressource (DE-627)320597903 (DE-600)2019804-8 (DE-576)116451815 1873-6785 nnns volume:286 GBV_USEFLAG_U GBV_ELV SYSFLAG_U 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_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_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 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_2034 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 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_4338 GBV_ILN_4393 GBV_ILN_4700 50.70 Energie: Allgemeines VZ AR 286
allfieldsSound	10.1016/j.energy.2023.129631 doi (DE-627)ELV065803000 (ELSEVIER)S0360-5442(23)03025-6 DE-627 ger DE-627 rda eng 600 VZ 50.70 bkl Meng, Fanli verfasserin aut Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO 2023 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low viscosity, and environmentally friendly properties. The optimization of the mass fraction resulted in a composition of 60 wt% EHA and 40 wt% DMSO, considering factors such as absorption capacity, absorption rate, and viscosity. At a desorption temperature of 373 K, the CO2-loaded EHA-DMSO exhibited a desorption efficiency of approximately 98 %. The estimation of desorption energy (E t) consumption, using the method of electric energy consumption, revealed that EHA-DMSO achieved approximately a 50 % reduction in E t compared to the MEA (30 wt%) absorbent. Even with a water content of 10 %, E t was reduced by around 40 %. Additionally, the absorbent demonstrated notable advantages in terms of water resistance and cycle performance. The advantages of environmental friendliness and easy availability of raw materials suggest that the EHA-DMSO absorbent holds a promising potential for broader application in the field of CO2 capture from flue gas. Carbon dioxide Non-aqueous absorbent Absorption/desorption Water resistance Cycle Fu, Kun verfasserin aut Wang, Xueli verfasserin aut Wang, Yixiao verfasserin aut Wang, Lemeng verfasserin aut Fu, Dong verfasserin aut Enthalten in Energy Amsterdam [u.a.] : Elsevier Science, 1976 286 Online-Ressource (DE-627)320597903 (DE-600)2019804-8 (DE-576)116451815 1873-6785 nnns volume:286 GBV_USEFLAG_U GBV_ELV SYSFLAG_U 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_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_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 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_2034 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4242 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_4338 GBV_ILN_4393 GBV_ILN_4700 50.70 Energie: Allgemeines VZ AR 286
language	English
source	Enthalten in Energy 286 volume:286
sourceStr	Enthalten in Energy 286 volume:286
format_phy_str_mv	Article
bklname	Energie: Allgemeines
institution	findex.gbv.de
topic_facet	Carbon dioxide Non-aqueous absorbent Absorption/desorption Water resistance Cycle
dewey-raw	600
isfreeaccess_bool	false
container_title	Energy
authorswithroles_txt_mv	Meng, Fanli @@aut@@ Fu, Kun @@aut@@ Wang, Xueli @@aut@@ Wang, Yixiao @@aut@@ Wang, Lemeng @@aut@@ Fu, Dong @@aut@@
publishDateDaySort_date	2023-01-01T00:00:00Z
hierarchy_top_id	320597903
dewey-sort	3600
id	ELV065803000
language_de	englisch
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author	Meng, Fanli
spellingShingle	Meng, Fanli ddc 600 bkl 50.70 misc Carbon dioxide misc Non-aqueous absorbent misc Absorption/desorption misc Water resistance misc Cycle Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO
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topic_title	600 VZ 50.70 bkl Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO Carbon dioxide Non-aqueous absorbent Absorption/desorption Water resistance Cycle
topic	ddc 600 bkl 50.70 misc Carbon dioxide misc Non-aqueous absorbent misc Absorption/desorption misc Water resistance misc Cycle
topic_unstemmed	ddc 600 bkl 50.70 misc Carbon dioxide misc Non-aqueous absorbent misc Absorption/desorption misc Water resistance misc Cycle
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title	Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO
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title_full	Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO
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author_browse	Meng, Fanli Fu, Kun Wang, Xueli Wang, Yixiao Wang, Lemeng Fu, Dong
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title_sort	study on absorption and regeneration performance of eha-dmso non-aqueous absorbent for co
title_auth	Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO
abstract	In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low viscosity, and environmentally friendly properties. The optimization of the mass fraction resulted in a composition of 60 wt% EHA and 40 wt% DMSO, considering factors such as absorption capacity, absorption rate, and viscosity. At a desorption temperature of 373 K, the CO2-loaded EHA-DMSO exhibited a desorption efficiency of approximately 98 %. The estimation of desorption energy (E t) consumption, using the method of electric energy consumption, revealed that EHA-DMSO achieved approximately a 50 % reduction in E t compared to the MEA (30 wt%) absorbent. Even with a water content of 10 %, E t was reduced by around 40 %. Additionally, the absorbent demonstrated notable advantages in terms of water resistance and cycle performance. The advantages of environmental friendliness and easy availability of raw materials suggest that the EHA-DMSO absorbent holds a promising potential for broader application in the field of CO2 capture from flue gas.
abstractGer	In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low viscosity, and environmentally friendly properties. The optimization of the mass fraction resulted in a composition of 60 wt% EHA and 40 wt% DMSO, considering factors such as absorption capacity, absorption rate, and viscosity. At a desorption temperature of 373 K, the CO2-loaded EHA-DMSO exhibited a desorption efficiency of approximately 98 %. The estimation of desorption energy (E t) consumption, using the method of electric energy consumption, revealed that EHA-DMSO achieved approximately a 50 % reduction in E t compared to the MEA (30 wt%) absorbent. Even with a water content of 10 %, E t was reduced by around 40 %. Additionally, the absorbent demonstrated notable advantages in terms of water resistance and cycle performance. The advantages of environmental friendliness and easy availability of raw materials suggest that the EHA-DMSO absorbent holds a promising potential for broader application in the field of CO2 capture from flue gas.
abstract_unstemmed	In previous work by Fu et al. (2021, 2022), the performance of 2-ethylhexylan-1-amine (EHA) and diglyme absorbents for carbon dioxide (CO2) capture from flue gas was demonstrated. In this study, dimethyl sulfoxide (DMSO) was selected as a replacement for diglyme due to its high boiling point, low viscosity, and environmentally friendly properties. The optimization of the mass fraction resulted in a composition of 60 wt% EHA and 40 wt% DMSO, considering factors such as absorption capacity, absorption rate, and viscosity. At a desorption temperature of 373 K, the CO2-loaded EHA-DMSO exhibited a desorption efficiency of approximately 98 %. The estimation of desorption energy (E t) consumption, using the method of electric energy consumption, revealed that EHA-DMSO achieved approximately a 50 % reduction in E t compared to the MEA (30 wt%) absorbent. Even with a water content of 10 %, E t was reduced by around 40 %. Additionally, the absorbent demonstrated notable advantages in terms of water resistance and cycle performance. The advantages of environmental friendliness and easy availability of raw materials suggest that the EHA-DMSO absorbent holds a promising potential for broader application in the field of CO2 capture from flue gas.
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title_short	Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO
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author2	Fu, Kun Wang, Xueli Wang, Yixiao Wang, Lemeng Fu, Dong
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doi_str	10.1016/j.energy.2023.129631
up_date	2024-07-07T00:18:18.227Z
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Study on absorption and regeneration performance of EHA-DMSO non-aqueous absorbent for CO

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