Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption
Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Zhu, Hai [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2022 |
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| Schlagwörter: |
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| Anmerkung: |
© The Author(s), under exclusive licence to Springer Nature B.V. 2022 |
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| Übergeordnetes Werk: |
Enthalten in: Research on chemical intermediates - Dordrecht : Springer Netherlands, 1989, 48(2022), 8 vom: 16. Juli, Seite 3613-3631 |
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| Übergeordnetes Werk: |
volume:48 ; year:2022 ; number:8 ; day:16 ; month:07 ; pages:3613-3631 |
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| DOI / URN: |
10.1007/s11164-022-04772-z |
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SPR047660317 |
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| 520 | |a Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction. | ||
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| 650 | 4 | |a Biomass activated carbon |7 (dpeaa)DE-He213 | |
| 650 | 4 | |a Chloramphenicol wastewater |7 (dpeaa)DE-He213 | |
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| 700 | 1 | |a Zhou, Dan |4 aut | |
| 700 | 1 | |a Wang, Haiyang |4 aut | |
| 700 | 1 | |a Xu, Dan |4 aut | |
| 700 | 1 | |a Li, Haixia |0 (orcid)0000-0002-6676-3305 |4 aut | |
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10.1007/s11164-022-04772-z doi (DE-627)SPR047660317 (SPR)s11164-022-04772-z-e DE-627 ger DE-627 rakwb eng Zhu, Hai verfasserin aut Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2022 Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction. Coconut fiber (dpeaa)DE-He213 Biomass activated carbon (dpeaa)DE-He213 Chloramphenicol wastewater (dpeaa)DE-He213 Adsorption (dpeaa)DE-He213 Mechanism (dpeaa)DE-He213 Qiu, Junqiang aut Zhou, Dan aut Wang, Haiyang aut Xu, Dan aut Li, Haixia (orcid)0000-0002-6676-3305 aut Enthalten in Research on chemical intermediates Dordrecht : Springer Netherlands, 1989 48(2022), 8 vom: 16. Juli, Seite 3613-3631 (DE-627)328186511 (DE-600)2045085-0 1568-5675 nnns volume:48 year:2022 number:8 day:16 month:07 pages:3613-3631 https://dx.doi.org/10.1007/s11164-022-04772-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_206 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_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_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_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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2022 8 16 07 3613-3631 |
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10.1007/s11164-022-04772-z doi (DE-627)SPR047660317 (SPR)s11164-022-04772-z-e DE-627 ger DE-627 rakwb eng Zhu, Hai verfasserin aut Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2022 Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction. Coconut fiber (dpeaa)DE-He213 Biomass activated carbon (dpeaa)DE-He213 Chloramphenicol wastewater (dpeaa)DE-He213 Adsorption (dpeaa)DE-He213 Mechanism (dpeaa)DE-He213 Qiu, Junqiang aut Zhou, Dan aut Wang, Haiyang aut Xu, Dan aut Li, Haixia (orcid)0000-0002-6676-3305 aut Enthalten in Research on chemical intermediates Dordrecht : Springer Netherlands, 1989 48(2022), 8 vom: 16. Juli, Seite 3613-3631 (DE-627)328186511 (DE-600)2045085-0 1568-5675 nnns volume:48 year:2022 number:8 day:16 month:07 pages:3613-3631 https://dx.doi.org/10.1007/s11164-022-04772-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_206 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_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_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_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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2022 8 16 07 3613-3631 |
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10.1007/s11164-022-04772-z doi (DE-627)SPR047660317 (SPR)s11164-022-04772-z-e DE-627 ger DE-627 rakwb eng Zhu, Hai verfasserin aut Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2022 Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction. Coconut fiber (dpeaa)DE-He213 Biomass activated carbon (dpeaa)DE-He213 Chloramphenicol wastewater (dpeaa)DE-He213 Adsorption (dpeaa)DE-He213 Mechanism (dpeaa)DE-He213 Qiu, Junqiang aut Zhou, Dan aut Wang, Haiyang aut Xu, Dan aut Li, Haixia (orcid)0000-0002-6676-3305 aut Enthalten in Research on chemical intermediates Dordrecht : Springer Netherlands, 1989 48(2022), 8 vom: 16. Juli, Seite 3613-3631 (DE-627)328186511 (DE-600)2045085-0 1568-5675 nnns volume:48 year:2022 number:8 day:16 month:07 pages:3613-3631 https://dx.doi.org/10.1007/s11164-022-04772-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_206 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_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_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_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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2022 8 16 07 3613-3631 |
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10.1007/s11164-022-04772-z doi (DE-627)SPR047660317 (SPR)s11164-022-04772-z-e DE-627 ger DE-627 rakwb eng Zhu, Hai verfasserin aut Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2022 Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction. Coconut fiber (dpeaa)DE-He213 Biomass activated carbon (dpeaa)DE-He213 Chloramphenicol wastewater (dpeaa)DE-He213 Adsorption (dpeaa)DE-He213 Mechanism (dpeaa)DE-He213 Qiu, Junqiang aut Zhou, Dan aut Wang, Haiyang aut Xu, Dan aut Li, Haixia (orcid)0000-0002-6676-3305 aut Enthalten in Research on chemical intermediates Dordrecht : Springer Netherlands, 1989 48(2022), 8 vom: 16. Juli, Seite 3613-3631 (DE-627)328186511 (DE-600)2045085-0 1568-5675 nnns volume:48 year:2022 number:8 day:16 month:07 pages:3613-3631 https://dx.doi.org/10.1007/s11164-022-04772-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_206 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_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_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_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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2022 8 16 07 3613-3631 |
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10.1007/s11164-022-04772-z doi (DE-627)SPR047660317 (SPR)s11164-022-04772-z-e DE-627 ger DE-627 rakwb eng Zhu, Hai verfasserin aut Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2022 Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction. Coconut fiber (dpeaa)DE-He213 Biomass activated carbon (dpeaa)DE-He213 Chloramphenicol wastewater (dpeaa)DE-He213 Adsorption (dpeaa)DE-He213 Mechanism (dpeaa)DE-He213 Qiu, Junqiang aut Zhou, Dan aut Wang, Haiyang aut Xu, Dan aut Li, Haixia (orcid)0000-0002-6676-3305 aut Enthalten in Research on chemical intermediates Dordrecht : Springer Netherlands, 1989 48(2022), 8 vom: 16. Juli, Seite 3613-3631 (DE-627)328186511 (DE-600)2045085-0 1568-5675 nnns volume:48 year:2022 number:8 day:16 month:07 pages:3613-3631 https://dx.doi.org/10.1007/s11164-022-04772-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_206 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_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_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_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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 48 2022 8 16 07 3613-3631 |
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Enthalten in Research on chemical intermediates 48(2022), 8 vom: 16. Juli, Seite 3613-3631 volume:48 year:2022 number:8 day:16 month:07 pages:3613-3631 |
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Coconut fiber Biomass activated carbon Chloramphenicol wastewater Adsorption Mechanism |
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Zhu, Hai @@aut@@ Qiu, Junqiang @@aut@@ Zhou, Dan @@aut@@ Wang, Haiyang @@aut@@ Xu, Dan @@aut@@ Li, Haixia @@aut@@ |
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<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000caa a22002652 4500</leader><controlfield tag="001">SPR047660317</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20230519225009.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">220723s2022 xx |||||o 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1007/s11164-022-04772-z</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)SPR047660317</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(SPR)s11164-022-04772-z-e</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="041" ind1=" " ind2=" "><subfield code="a">eng</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Zhu, Hai</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2022</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="500" ind1=" " ind2=" "><subfield code="a">© The Author(s), under exclusive licence to Springer Nature B.V. 2022</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Coconut fiber</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Biomass activated carbon</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Chloramphenicol wastewater</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Adsorption</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Mechanism</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Qiu, Junqiang</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Zhou, Dan</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Wang, Haiyang</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Xu, Dan</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Li, Haixia</subfield><subfield code="0">(orcid)0000-0002-6676-3305</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Research on chemical intermediates</subfield><subfield code="d">Dordrecht : Springer Netherlands, 1989</subfield><subfield code="g">48(2022), 8 vom: 16. 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|
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Zhu, Hai |
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Zhu, Hai misc Coconut fiber misc Biomass activated carbon misc Chloramphenicol wastewater misc Adsorption misc Mechanism Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption |
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Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption Coconut fiber (dpeaa)DE-He213 Biomass activated carbon (dpeaa)DE-He213 Chloramphenicol wastewater (dpeaa)DE-He213 Adsorption (dpeaa)DE-He213 Mechanism (dpeaa)DE-He213 |
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misc Coconut fiber misc Biomass activated carbon misc Chloramphenicol wastewater misc Adsorption misc Mechanism |
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misc Coconut fiber misc Biomass activated carbon misc Chloramphenicol wastewater misc Adsorption misc Mechanism |
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Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption |
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synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption |
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Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption |
| abstract |
Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction. © The Author(s), under exclusive licence to Springer Nature B.V. 2022 |
| abstractGer |
Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction. © The Author(s), under exclusive licence to Springer Nature B.V. 2022 |
| abstract_unstemmed |
Abstract A series of activated carbon (CFAC-n, n = 1,2,3,4) adsorbents of higher adsorption capacity were synthesized through coconut fiber carbon (CFAC-0) and KOH activator (CFAC-0:KOH = 1:1, 1:2, 1:3, 1:4), respectively, by the heating method for chloramphenicol (CHL) adsorption. The pore diameter, pore volume, specific surface area and surface functional groups of CFAC-n were determined by several characterizations such as BET, XRD, Raman, TEM, FTIR and XPS. The adsorption kinetics of CFAC-n for CHL removal were investigated and the kinetic parameters were also calculated. According to the results, the adsorption capacity onto CFAC-n was positively correlated to the specific surface area. CFAC-3 possessed the largest specific surface area (1755 $ m^{2} $ $ g^{−1} $) and the best adsorption amount (523.0 mg $ g^{−1} $). The adsorption conditions (adsorbent dosage, antibiotic initial concentration, adsorption temperature and pH value) of CFAC-3 showed to be directly related to the adsorption effect. In addition, it was found that the CHL adsorption onto CFAC-n was well suitable for fitting with pseudo-second-order kinetic model and Elovich kinetics model. The adsorption isotherm was carried on and it was found that CHL adsorption onto CFAC best fitted to Freundlich and Temkin model. Those results revealed that the adsorption process was heterogeneous adsorption by main chemisorption. The adsorption capacity for CHL onto CHAC-3 was much higher than those of reported low-cost adsorbents. The adsorption included mainly hydrogen bond and π–π conjugation interactions, and electrostatic interaction. © The Author(s), under exclusive licence to Springer Nature B.V. 2022 |
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Synthesis of coconut fiber activated carbon for chloramphenicol wastewater adsorption |
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https://dx.doi.org/10.1007/s11164-022-04772-z |
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Qiu, Junqiang Zhou, Dan Wang, Haiyang Xu, Dan Li, Haixia |
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Qiu, Junqiang Zhou, Dan Wang, Haiyang Xu, Dan Li, Haixia |
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10.1007/s11164-022-04772-z |
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2024-07-03T14:10:18.254Z |
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| score |
7.3996487 |