A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries

Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further...
Ausführliche Beschreibung

Gespeichert in:

Autor*in:	Huang, Zhe [verfasserIn] Zhu, Jie [verfasserIn] Qiu, Ruijun [verfasserIn] Ruan, Jujun [verfasserIn] Qiu, Rongliang [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2019

Schlagwörter:	Spent lithium-ion battery (power banks) Cobalt and nickel separation Vacuum step-by-step reduction Heat transfer models

Übergeordnetes Werk:	Enthalten in: Journal of cleaner production - Amsterdam [u.a.] : Elsevier Science, 1993, 229, Seite 1148-1157
Übergeordnetes Werk:	volume:229 ; pages:1148-1157

DOI / URN:	10.1016/j.jclepro.2019.05.049

Katalog-ID:	ELV002431181

Internformat


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520			\|a Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further separated. Recovering cobalt and nickel respectively from the electrode powders is important to improve the recovery value of spent lithium-ion battery. According to the analysis of Gibbs free energy of the reduction process of Ni2+ and Co2+, we proposed a cleaner technology of step-by-step vacuum carbon reduction to recover nickel and cobalt in sequence from the electrode powder of spent lithium-ion batteries. The Ni2+ and Co2+ in the spent lithium-ion battery are reduced into nickel and cobalt in vacuum tubular furnace at the temperatures of 691 °C and 873 °C respectively. Nickel and cobalt can be separated in sequence by magnetic separation at the reduction products of different temperatures. Additionally, for energy saving and accurate reduction, we analyzed the heat transfer in the vacuum reduction process and constructed the models for computing the true temperature of electrode powder in crucible. The models are used to compute the accurate reduction temperatures for Co2+ and Ni2+. It will greatly reduce the energy cost in the reduction process which be attributed to sustainable development. The models also can guide the structure design of vacuum tubular furnace for improving the efficiency of heat transfer.
650		4	\|a Spent lithium-ion battery (power banks)
650		4	\|a Cobalt and nickel separation
650		4	\|a Vacuum step-by-step reduction
650		4	\|a Heat transfer models
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700	1		\|a Qiu, Rongliang \|e verfasserin \|4 aut
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matchkey_str	article:09596526:2019----::cenrneegsvntcnlgovcusebserdcinorcvrncbladik
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publishDate	2019
allfields	10.1016/j.jclepro.2019.05.049 doi (DE-627)ELV002431181 (ELSEVIER)S0959-6526(19)31565-3 DE-627 ger DE-627 rda eng 690 330 DE-600 43.35 bkl 85.35 bkl Huang, Zhe verfasserin aut A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further separated. Recovering cobalt and nickel respectively from the electrode powders is important to improve the recovery value of spent lithium-ion battery. According to the analysis of Gibbs free energy of the reduction process of Ni2+ and Co2+, we proposed a cleaner technology of step-by-step vacuum carbon reduction to recover nickel and cobalt in sequence from the electrode powder of spent lithium-ion batteries. The Ni2+ and Co2+ in the spent lithium-ion battery are reduced into nickel and cobalt in vacuum tubular furnace at the temperatures of 691 °C and 873 °C respectively. Nickel and cobalt can be separated in sequence by magnetic separation at the reduction products of different temperatures. Additionally, for energy saving and accurate reduction, we analyzed the heat transfer in the vacuum reduction process and constructed the models for computing the true temperature of electrode powder in crucible. The models are used to compute the accurate reduction temperatures for Co2+ and Ni2+. It will greatly reduce the energy cost in the reduction process which be attributed to sustainable development. The models also can guide the structure design of vacuum tubular furnace for improving the efficiency of heat transfer. Spent lithium-ion battery (power banks) Cobalt and nickel separation Vacuum step-by-step reduction Heat transfer models Zhu, Jie verfasserin aut Qiu, Ruijun verfasserin aut Ruan, Jujun verfasserin aut Qiu, Rongliang verfasserin aut Enthalten in Journal of cleaner production Amsterdam [u.a.] : Elsevier Science, 1993 229, Seite 1148-1157 Online-Ressource (DE-627)324655878 (DE-600)2029338-0 (DE-576)252613988 0959-6526 nnns volume:229 pages:1148-1157 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OPC-GGO 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_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_2336 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 43.35 Umweltrichtlinien Umweltnormen 85.35 Fertigung AR 229 1148-1157
spelling	10.1016/j.jclepro.2019.05.049 doi (DE-627)ELV002431181 (ELSEVIER)S0959-6526(19)31565-3 DE-627 ger DE-627 rda eng 690 330 DE-600 43.35 bkl 85.35 bkl Huang, Zhe verfasserin aut A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further separated. Recovering cobalt and nickel respectively from the electrode powders is important to improve the recovery value of spent lithium-ion battery. According to the analysis of Gibbs free energy of the reduction process of Ni2+ and Co2+, we proposed a cleaner technology of step-by-step vacuum carbon reduction to recover nickel and cobalt in sequence from the electrode powder of spent lithium-ion batteries. The Ni2+ and Co2+ in the spent lithium-ion battery are reduced into nickel and cobalt in vacuum tubular furnace at the temperatures of 691 °C and 873 °C respectively. Nickel and cobalt can be separated in sequence by magnetic separation at the reduction products of different temperatures. Additionally, for energy saving and accurate reduction, we analyzed the heat transfer in the vacuum reduction process and constructed the models for computing the true temperature of electrode powder in crucible. The models are used to compute the accurate reduction temperatures for Co2+ and Ni2+. It will greatly reduce the energy cost in the reduction process which be attributed to sustainable development. The models also can guide the structure design of vacuum tubular furnace for improving the efficiency of heat transfer. Spent lithium-ion battery (power banks) Cobalt and nickel separation Vacuum step-by-step reduction Heat transfer models Zhu, Jie verfasserin aut Qiu, Ruijun verfasserin aut Ruan, Jujun verfasserin aut Qiu, Rongliang verfasserin aut Enthalten in Journal of cleaner production Amsterdam [u.a.] : Elsevier Science, 1993 229, Seite 1148-1157 Online-Ressource (DE-627)324655878 (DE-600)2029338-0 (DE-576)252613988 0959-6526 nnns volume:229 pages:1148-1157 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OPC-GGO 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_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_2336 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 43.35 Umweltrichtlinien Umweltnormen 85.35 Fertigung AR 229 1148-1157
allfields_unstemmed	10.1016/j.jclepro.2019.05.049 doi (DE-627)ELV002431181 (ELSEVIER)S0959-6526(19)31565-3 DE-627 ger DE-627 rda eng 690 330 DE-600 43.35 bkl 85.35 bkl Huang, Zhe verfasserin aut A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further separated. Recovering cobalt and nickel respectively from the electrode powders is important to improve the recovery value of spent lithium-ion battery. According to the analysis of Gibbs free energy of the reduction process of Ni2+ and Co2+, we proposed a cleaner technology of step-by-step vacuum carbon reduction to recover nickel and cobalt in sequence from the electrode powder of spent lithium-ion batteries. The Ni2+ and Co2+ in the spent lithium-ion battery are reduced into nickel and cobalt in vacuum tubular furnace at the temperatures of 691 °C and 873 °C respectively. Nickel and cobalt can be separated in sequence by magnetic separation at the reduction products of different temperatures. Additionally, for energy saving and accurate reduction, we analyzed the heat transfer in the vacuum reduction process and constructed the models for computing the true temperature of electrode powder in crucible. The models are used to compute the accurate reduction temperatures for Co2+ and Ni2+. It will greatly reduce the energy cost in the reduction process which be attributed to sustainable development. The models also can guide the structure design of vacuum tubular furnace for improving the efficiency of heat transfer. Spent lithium-ion battery (power banks) Cobalt and nickel separation Vacuum step-by-step reduction Heat transfer models Zhu, Jie verfasserin aut Qiu, Ruijun verfasserin aut Ruan, Jujun verfasserin aut Qiu, Rongliang verfasserin aut Enthalten in Journal of cleaner production Amsterdam [u.a.] : Elsevier Science, 1993 229, Seite 1148-1157 Online-Ressource (DE-627)324655878 (DE-600)2029338-0 (DE-576)252613988 0959-6526 nnns volume:229 pages:1148-1157 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OPC-GGO 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_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_2336 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 43.35 Umweltrichtlinien Umweltnormen 85.35 Fertigung AR 229 1148-1157
allfieldsGer	10.1016/j.jclepro.2019.05.049 doi (DE-627)ELV002431181 (ELSEVIER)S0959-6526(19)31565-3 DE-627 ger DE-627 rda eng 690 330 DE-600 43.35 bkl 85.35 bkl Huang, Zhe verfasserin aut A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further separated. Recovering cobalt and nickel respectively from the electrode powders is important to improve the recovery value of spent lithium-ion battery. According to the analysis of Gibbs free energy of the reduction process of Ni2+ and Co2+, we proposed a cleaner technology of step-by-step vacuum carbon reduction to recover nickel and cobalt in sequence from the electrode powder of spent lithium-ion batteries. The Ni2+ and Co2+ in the spent lithium-ion battery are reduced into nickel and cobalt in vacuum tubular furnace at the temperatures of 691 °C and 873 °C respectively. Nickel and cobalt can be separated in sequence by magnetic separation at the reduction products of different temperatures. Additionally, for energy saving and accurate reduction, we analyzed the heat transfer in the vacuum reduction process and constructed the models for computing the true temperature of electrode powder in crucible. The models are used to compute the accurate reduction temperatures for Co2+ and Ni2+. It will greatly reduce the energy cost in the reduction process which be attributed to sustainable development. The models also can guide the structure design of vacuum tubular furnace for improving the efficiency of heat transfer. Spent lithium-ion battery (power banks) Cobalt and nickel separation Vacuum step-by-step reduction Heat transfer models Zhu, Jie verfasserin aut Qiu, Ruijun verfasserin aut Ruan, Jujun verfasserin aut Qiu, Rongliang verfasserin aut Enthalten in Journal of cleaner production Amsterdam [u.a.] : Elsevier Science, 1993 229, Seite 1148-1157 Online-Ressource (DE-627)324655878 (DE-600)2029338-0 (DE-576)252613988 0959-6526 nnns volume:229 pages:1148-1157 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OPC-GGO 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_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_2336 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 43.35 Umweltrichtlinien Umweltnormen 85.35 Fertigung AR 229 1148-1157
allfieldsSound	10.1016/j.jclepro.2019.05.049 doi (DE-627)ELV002431181 (ELSEVIER)S0959-6526(19)31565-3 DE-627 ger DE-627 rda eng 690 330 DE-600 43.35 bkl 85.35 bkl Huang, Zhe verfasserin aut A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries 2019 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further separated. Recovering cobalt and nickel respectively from the electrode powders is important to improve the recovery value of spent lithium-ion battery. According to the analysis of Gibbs free energy of the reduction process of Ni2+ and Co2+, we proposed a cleaner technology of step-by-step vacuum carbon reduction to recover nickel and cobalt in sequence from the electrode powder of spent lithium-ion batteries. The Ni2+ and Co2+ in the spent lithium-ion battery are reduced into nickel and cobalt in vacuum tubular furnace at the temperatures of 691 °C and 873 °C respectively. Nickel and cobalt can be separated in sequence by magnetic separation at the reduction products of different temperatures. Additionally, for energy saving and accurate reduction, we analyzed the heat transfer in the vacuum reduction process and constructed the models for computing the true temperature of electrode powder in crucible. The models are used to compute the accurate reduction temperatures for Co2+ and Ni2+. It will greatly reduce the energy cost in the reduction process which be attributed to sustainable development. The models also can guide the structure design of vacuum tubular furnace for improving the efficiency of heat transfer. Spent lithium-ion battery (power banks) Cobalt and nickel separation Vacuum step-by-step reduction Heat transfer models Zhu, Jie verfasserin aut Qiu, Ruijun verfasserin aut Ruan, Jujun verfasserin aut Qiu, Rongliang verfasserin aut Enthalten in Journal of cleaner production Amsterdam [u.a.] : Elsevier Science, 1993 229, Seite 1148-1157 Online-Ressource (DE-627)324655878 (DE-600)2029338-0 (DE-576)252613988 0959-6526 nnns volume:229 pages:1148-1157 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OPC-GGO 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_224 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2056 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 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_2336 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4313 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4393 43.35 Umweltrichtlinien Umweltnormen 85.35 Fertigung AR 229 1148-1157
language	English
source	Enthalten in Journal of cleaner production 229, Seite 1148-1157 volume:229 pages:1148-1157
sourceStr	Enthalten in Journal of cleaner production 229, Seite 1148-1157 volume:229 pages:1148-1157
format_phy_str_mv	Article
bklname	Umweltrichtlinien Umweltnormen Fertigung
institution	findex.gbv.de
topic_facet	Spent lithium-ion battery (power banks) Cobalt and nickel separation Vacuum step-by-step reduction Heat transfer models
dewey-raw	690
isfreeaccess_bool	false
container_title	Journal of cleaner production
authorswithroles_txt_mv	Huang, Zhe @@aut@@ Zhu, Jie @@aut@@ Qiu, Ruijun @@aut@@ Ruan, Jujun @@aut@@ Qiu, Rongliang @@aut@@
publishDateDaySort_date	2019-01-01T00:00:00Z
hierarchy_top_id	324655878
dewey-sort	3690
id	ELV002431181
language_de	englisch
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author	Huang, Zhe
spellingShingle	Huang, Zhe ddc 690 bkl 43.35 bkl 85.35 misc Spent lithium-ion battery (power banks) misc Cobalt and nickel separation misc Vacuum step-by-step reduction misc Heat transfer models A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries
authorStr	Huang, Zhe
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topic_title	690 330 DE-600 43.35 bkl 85.35 bkl A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries Spent lithium-ion battery (power banks) Cobalt and nickel separation Vacuum step-by-step reduction Heat transfer models
topic	ddc 690 bkl 43.35 bkl 85.35 misc Spent lithium-ion battery (power banks) misc Cobalt and nickel separation misc Vacuum step-by-step reduction misc Heat transfer models
topic_unstemmed	ddc 690 bkl 43.35 bkl 85.35 misc Spent lithium-ion battery (power banks) misc Cobalt and nickel separation misc Vacuum step-by-step reduction misc Heat transfer models
topic_browse	ddc 690 bkl 43.35 bkl 85.35 misc Spent lithium-ion battery (power banks) misc Cobalt and nickel separation misc Vacuum step-by-step reduction misc Heat transfer models
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title	A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries
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title_full	A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries
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author_browse	Huang, Zhe Zhu, Jie Qiu, Ruijun Ruan, Jujun Qiu, Rongliang
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author-letter	Huang, Zhe
doi_str_mv	10.1016/j.jclepro.2019.05.049
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title_sort	a cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries
title_auth	A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries
abstract	Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further separated. Recovering cobalt and nickel respectively from the electrode powders is important to improve the recovery value of spent lithium-ion battery. According to the analysis of Gibbs free energy of the reduction process of Ni2+ and Co2+, we proposed a cleaner technology of step-by-step vacuum carbon reduction to recover nickel and cobalt in sequence from the electrode powder of spent lithium-ion batteries. The Ni2+ and Co2+ in the spent lithium-ion battery are reduced into nickel and cobalt in vacuum tubular furnace at the temperatures of 691 °C and 873 °C respectively. Nickel and cobalt can be separated in sequence by magnetic separation at the reduction products of different temperatures. Additionally, for energy saving and accurate reduction, we analyzed the heat transfer in the vacuum reduction process and constructed the models for computing the true temperature of electrode powder in crucible. The models are used to compute the accurate reduction temperatures for Co2+ and Ni2+. It will greatly reduce the energy cost in the reduction process which be attributed to sustainable development. The models also can guide the structure design of vacuum tubular furnace for improving the efficiency of heat transfer.
abstractGer	Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further separated. Recovering cobalt and nickel respectively from the electrode powders is important to improve the recovery value of spent lithium-ion battery. According to the analysis of Gibbs free energy of the reduction process of Ni2+ and Co2+, we proposed a cleaner technology of step-by-step vacuum carbon reduction to recover nickel and cobalt in sequence from the electrode powder of spent lithium-ion batteries. The Ni2+ and Co2+ in the spent lithium-ion battery are reduced into nickel and cobalt in vacuum tubular furnace at the temperatures of 691 °C and 873 °C respectively. Nickel and cobalt can be separated in sequence by magnetic separation at the reduction products of different temperatures. Additionally, for energy saving and accurate reduction, we analyzed the heat transfer in the vacuum reduction process and constructed the models for computing the true temperature of electrode powder in crucible. The models are used to compute the accurate reduction temperatures for Co2+ and Ni2+. It will greatly reduce the energy cost in the reduction process which be attributed to sustainable development. The models also can guide the structure design of vacuum tubular furnace for improving the efficiency of heat transfer.
abstract_unstemmed	Waste power banks (a kind of lithium-ion battery) are widely generated along with the growing widespread use of mobile phone. Vacuum carbon reduction is encouraged to recover cobalt and nickel from spent lithium-ion battery. However, the mixed nickel and cobalt particles are difficult to be further separated. Recovering cobalt and nickel respectively from the electrode powders is important to improve the recovery value of spent lithium-ion battery. According to the analysis of Gibbs free energy of the reduction process of Ni2+ and Co2+, we proposed a cleaner technology of step-by-step vacuum carbon reduction to recover nickel and cobalt in sequence from the electrode powder of spent lithium-ion batteries. The Ni2+ and Co2+ in the spent lithium-ion battery are reduced into nickel and cobalt in vacuum tubular furnace at the temperatures of 691 °C and 873 °C respectively. Nickel and cobalt can be separated in sequence by magnetic separation at the reduction products of different temperatures. Additionally, for energy saving and accurate reduction, we analyzed the heat transfer in the vacuum reduction process and constructed the models for computing the true temperature of electrode powder in crucible. The models are used to compute the accurate reduction temperatures for Co2+ and Ni2+. It will greatly reduce the energy cost in the reduction process which be attributed to sustainable development. The models also can guide the structure design of vacuum tubular furnace for improving the efficiency of heat transfer.
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title_short	A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries
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author2	Zhu, Jie Qiu, Ruijun Ruan, Jujun Qiu, Rongliang
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up_date	2024-07-07T00:42:18.123Z
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A cleaner and energy-saving technology of vacuum step-by-step reduction for recovering cobalt and nickel from spent lithium-ion batteries

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