High-temperature CO

Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the mic...
Ausführliche Beschreibung

Gespeichert in:

Autor*in:	Li, Hailong [verfasserIn] Qu, Mingyu [verfasserIn] Hu, Yingchao [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2019

Schlagwörter:	CO Li Pyroligneous acid Modification Sintering

Übergeordnetes Werk:	Enthalten in: Fuel processing technology - New York, NY [u.a.] : Science Direct, 1977, 197
Übergeordnetes Werk:	volume:197

DOI / URN:	10.1016/j.fuproc.2019.106186

Katalog-ID:	ELV003120503

Internformat


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520			\|a Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the microstructures. The commonly used acids such as acetic acid, citric acid and gluconic acid are too expensive, restricting the application of this modification technique. In addition, in the typical Li4SiO4-based CO2 capture looping system, CO2 usually exists in the desorption reactor. However, the effect of the existence of CO2 at the desorption stage on adsorption performance has been rarely studied. Focusing on these two issues, this work employed pyroligneous acid (PA), a low-cost by-product of the fast pyrolysis of biomass, to modify the microstructures of Li4SiO4. It was found that modification by pyroligneous acid (PA) successfully improved the microstructures and enhanced the surface area of Li4SiO4 adsorbent. As a result, the obviously improved CO2 adsorption performance was achieved. In addition, the test results under CO2-containing desorption atmospheres indicated that the existence of CO2 at the desorption stage decreased the adsorption performance due to the severe sintering caused by the existence of CO2 at the desorption stage.
650		4	\|a CO
650		4	\|a Li
650		4	\|a Pyroligneous acid
650		4	\|a Modification
650		4	\|a Sintering
700	1		\|a Qu, Mingyu \|e verfasserin \|4 aut
700	1		\|a Hu, Yingchao \|e verfasserin \|4 aut
773	0	8	\|i Enthalten in \|t Fuel processing technology \|d New York, NY [u.a.] : Science Direct, 1977 \|g 197 \|h Online-Ressource \|w (DE-627)300898681 \|w (DE-600)1483666-X \|w (DE-576)09618860X \|7 nnns
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936	b	k	\|a 58.21 \|j Brennstoffe \|j Kraftstoffe \|j Explosivstoffe
951			\|a AR
952			\|d 197

Indexfelder

author_variant	h l hl m q mq y h yh
matchkey_str	lihailongqumingyuhuyingchao:2019----:iheprt
hierarchy_sort_str	2019
bklnumber	58.21
publishDate	2019
allfields	10.1016/j.fuproc.2019.106186 doi (DE-627)ELV003120503 (ELSEVIER)S0378-3820(19)30959-2 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Li, Hailong verfasserin aut High-temperature CO 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the microstructures. The commonly used acids such as acetic acid, citric acid and gluconic acid are too expensive, restricting the application of this modification technique. In addition, in the typical Li4SiO4-based CO2 capture looping system, CO2 usually exists in the desorption reactor. However, the effect of the existence of CO2 at the desorption stage on adsorption performance has been rarely studied. Focusing on these two issues, this work employed pyroligneous acid (PA), a low-cost by-product of the fast pyrolysis of biomass, to modify the microstructures of Li4SiO4. It was found that modification by pyroligneous acid (PA) successfully improved the microstructures and enhanced the surface area of Li4SiO4 adsorbent. As a result, the obviously improved CO2 adsorption performance was achieved. In addition, the test results under CO2-containing desorption atmospheres indicated that the existence of CO2 at the desorption stage decreased the adsorption performance due to the severe sintering caused by the existence of CO2 at the desorption stage. CO Li Pyroligneous acid Modification Sintering Qu, Mingyu verfasserin aut Hu, Yingchao verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 197 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:197 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_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_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_2034 GBV_ILN_2038 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_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 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_4335 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 197
spelling	10.1016/j.fuproc.2019.106186 doi (DE-627)ELV003120503 (ELSEVIER)S0378-3820(19)30959-2 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Li, Hailong verfasserin aut High-temperature CO 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the microstructures. The commonly used acids such as acetic acid, citric acid and gluconic acid are too expensive, restricting the application of this modification technique. In addition, in the typical Li4SiO4-based CO2 capture looping system, CO2 usually exists in the desorption reactor. However, the effect of the existence of CO2 at the desorption stage on adsorption performance has been rarely studied. Focusing on these two issues, this work employed pyroligneous acid (PA), a low-cost by-product of the fast pyrolysis of biomass, to modify the microstructures of Li4SiO4. It was found that modification by pyroligneous acid (PA) successfully improved the microstructures and enhanced the surface area of Li4SiO4 adsorbent. As a result, the obviously improved CO2 adsorption performance was achieved. In addition, the test results under CO2-containing desorption atmospheres indicated that the existence of CO2 at the desorption stage decreased the adsorption performance due to the severe sintering caused by the existence of CO2 at the desorption stage. CO Li Pyroligneous acid Modification Sintering Qu, Mingyu verfasserin aut Hu, Yingchao verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 197 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:197 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_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_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_2034 GBV_ILN_2038 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_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 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_4335 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 197
allfields_unstemmed	10.1016/j.fuproc.2019.106186 doi (DE-627)ELV003120503 (ELSEVIER)S0378-3820(19)30959-2 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Li, Hailong verfasserin aut High-temperature CO 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the microstructures. The commonly used acids such as acetic acid, citric acid and gluconic acid are too expensive, restricting the application of this modification technique. In addition, in the typical Li4SiO4-based CO2 capture looping system, CO2 usually exists in the desorption reactor. However, the effect of the existence of CO2 at the desorption stage on adsorption performance has been rarely studied. Focusing on these two issues, this work employed pyroligneous acid (PA), a low-cost by-product of the fast pyrolysis of biomass, to modify the microstructures of Li4SiO4. It was found that modification by pyroligneous acid (PA) successfully improved the microstructures and enhanced the surface area of Li4SiO4 adsorbent. As a result, the obviously improved CO2 adsorption performance was achieved. In addition, the test results under CO2-containing desorption atmospheres indicated that the existence of CO2 at the desorption stage decreased the adsorption performance due to the severe sintering caused by the existence of CO2 at the desorption stage. CO Li Pyroligneous acid Modification Sintering Qu, Mingyu verfasserin aut Hu, Yingchao verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 197 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:197 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_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_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_2034 GBV_ILN_2038 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_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 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_4335 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 197
allfieldsGer	10.1016/j.fuproc.2019.106186 doi (DE-627)ELV003120503 (ELSEVIER)S0378-3820(19)30959-2 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Li, Hailong verfasserin aut High-temperature CO 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the microstructures. The commonly used acids such as acetic acid, citric acid and gluconic acid are too expensive, restricting the application of this modification technique. In addition, in the typical Li4SiO4-based CO2 capture looping system, CO2 usually exists in the desorption reactor. However, the effect of the existence of CO2 at the desorption stage on adsorption performance has been rarely studied. Focusing on these two issues, this work employed pyroligneous acid (PA), a low-cost by-product of the fast pyrolysis of biomass, to modify the microstructures of Li4SiO4. It was found that modification by pyroligneous acid (PA) successfully improved the microstructures and enhanced the surface area of Li4SiO4 adsorbent. As a result, the obviously improved CO2 adsorption performance was achieved. In addition, the test results under CO2-containing desorption atmospheres indicated that the existence of CO2 at the desorption stage decreased the adsorption performance due to the severe sintering caused by the existence of CO2 at the desorption stage. CO Li Pyroligneous acid Modification Sintering Qu, Mingyu verfasserin aut Hu, Yingchao verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 197 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:197 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_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_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_2034 GBV_ILN_2038 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_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 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_4335 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 197
allfieldsSound	10.1016/j.fuproc.2019.106186 doi (DE-627)ELV003120503 (ELSEVIER)S0378-3820(19)30959-2 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Li, Hailong verfasserin aut High-temperature CO 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the microstructures. The commonly used acids such as acetic acid, citric acid and gluconic acid are too expensive, restricting the application of this modification technique. In addition, in the typical Li4SiO4-based CO2 capture looping system, CO2 usually exists in the desorption reactor. However, the effect of the existence of CO2 at the desorption stage on adsorption performance has been rarely studied. Focusing on these two issues, this work employed pyroligneous acid (PA), a low-cost by-product of the fast pyrolysis of biomass, to modify the microstructures of Li4SiO4. It was found that modification by pyroligneous acid (PA) successfully improved the microstructures and enhanced the surface area of Li4SiO4 adsorbent. As a result, the obviously improved CO2 adsorption performance was achieved. In addition, the test results under CO2-containing desorption atmospheres indicated that the existence of CO2 at the desorption stage decreased the adsorption performance due to the severe sintering caused by the existence of CO2 at the desorption stage. CO Li Pyroligneous acid Modification Sintering Qu, Mingyu verfasserin aut Hu, Yingchao verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 197 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:197 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_150 GBV_ILN_151 GBV_ILN_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_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_2034 GBV_ILN_2038 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_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 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_4335 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 197
language	English
source	Enthalten in Fuel processing technology 197 volume:197
sourceStr	Enthalten in Fuel processing technology 197 volume:197
format_phy_str_mv	Article
bklname	Brennstoffe Kraftstoffe Explosivstoffe
institution	findex.gbv.de
topic_facet	CO Li Pyroligneous acid Modification Sintering
dewey-raw	660
isfreeaccess_bool	false
container_title	Fuel processing technology
authorswithroles_txt_mv	Li, Hailong @@aut@@ Qu, Mingyu @@aut@@ Hu, Yingchao @@aut@@
publishDateDaySort_date	2019-01-01T00:00:00Z
hierarchy_top_id	300898681
dewey-sort	3660
id	ELV003120503
language_de	englisch
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author	Li, Hailong
spellingShingle	Li, Hailong ddc 660 bkl 58.21 misc CO misc Li misc Pyroligneous acid misc Modification misc Sintering High-temperature CO
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topic_title	660 DE-600 58.21 bkl High-temperature CO CO Li Pyroligneous acid Modification Sintering
topic	ddc 660 bkl 58.21 misc CO misc Li misc Pyroligneous acid misc Modification misc Sintering
topic_unstemmed	ddc 660 bkl 58.21 misc CO misc Li misc Pyroligneous acid misc Modification misc Sintering
topic_browse	ddc 660 bkl 58.21 misc CO misc Li misc Pyroligneous acid misc Modification misc Sintering
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title	High-temperature CO
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title_full	High-temperature CO
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title_sort	high-temperature co
title_auth	High-temperature CO
abstract	Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the microstructures. The commonly used acids such as acetic acid, citric acid and gluconic acid are too expensive, restricting the application of this modification technique. In addition, in the typical Li4SiO4-based CO2 capture looping system, CO2 usually exists in the desorption reactor. However, the effect of the existence of CO2 at the desorption stage on adsorption performance has been rarely studied. Focusing on these two issues, this work employed pyroligneous acid (PA), a low-cost by-product of the fast pyrolysis of biomass, to modify the microstructures of Li4SiO4. It was found that modification by pyroligneous acid (PA) successfully improved the microstructures and enhanced the surface area of Li4SiO4 adsorbent. As a result, the obviously improved CO2 adsorption performance was achieved. In addition, the test results under CO2-containing desorption atmospheres indicated that the existence of CO2 at the desorption stage decreased the adsorption performance due to the severe sintering caused by the existence of CO2 at the desorption stage.
abstractGer	Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the microstructures. The commonly used acids such as acetic acid, citric acid and gluconic acid are too expensive, restricting the application of this modification technique. In addition, in the typical Li4SiO4-based CO2 capture looping system, CO2 usually exists in the desorption reactor. However, the effect of the existence of CO2 at the desorption stage on adsorption performance has been rarely studied. Focusing on these two issues, this work employed pyroligneous acid (PA), a low-cost by-product of the fast pyrolysis of biomass, to modify the microstructures of Li4SiO4. It was found that modification by pyroligneous acid (PA) successfully improved the microstructures and enhanced the surface area of Li4SiO4 adsorbent. As a result, the obviously improved CO2 adsorption performance was achieved. In addition, the test results under CO2-containing desorption atmospheres indicated that the existence of CO2 at the desorption stage decreased the adsorption performance due to the severe sintering caused by the existence of CO2 at the desorption stage.
abstract_unstemmed	Li4SiO4 has been demonstrated as a promising adsorbent for CO2 capture. However, Li4SiO4 adsorbents from the conventional solid-state method usually exhibit dense microstructures and, thus, poor CO2 capture performance. Treating Li4SiO4 with organic acids has been proved effective to improve the microstructures. The commonly used acids such as acetic acid, citric acid and gluconic acid are too expensive, restricting the application of this modification technique. In addition, in the typical Li4SiO4-based CO2 capture looping system, CO2 usually exists in the desorption reactor. However, the effect of the existence of CO2 at the desorption stage on adsorption performance has been rarely studied. Focusing on these two issues, this work employed pyroligneous acid (PA), a low-cost by-product of the fast pyrolysis of biomass, to modify the microstructures of Li4SiO4. It was found that modification by pyroligneous acid (PA) successfully improved the microstructures and enhanced the surface area of Li4SiO4 adsorbent. As a result, the obviously improved CO2 adsorption performance was achieved. In addition, the test results under CO2-containing desorption atmospheres indicated that the existence of CO2 at the desorption stage decreased the adsorption performance due to the severe sintering caused by the existence of CO2 at the desorption stage.
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title_short	High-temperature CO
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up_date	2024-07-06T18:33:33.616Z
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