Removal of copper from nickel anode electrolyte through ion exchange

An novel method for removal of copper from nickel anodic electrolyte through ion exchange was studied after cupric deoxidization. Orthogonal design experiments show the optimum conditions of deoxidizing cupric into Cu+ in the nickel electrolyte are the reductive agent dosage is 4.5 times as the theo...

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Published inTransactions of Nonferrous Metals Society of China Vol. 19; no. 1; pp. 253 - 258
Main Author 陈爱良 邱冠周 赵中伟 孙培梅 余润兰
Format Journal Article
LanguageEnglish
Published Elsevier Ltd 01.02.2009
School of Metallurgical Science and Engineering, Central South University, Changsha 410083, China%School of Minerals Processing and Bioengineering, Central South University, Changsha 410083, China%School of Metallurgical Science and Engineering, Central South University, Changsha 410083, China
School of Minerals Processing and Bioengineering, Central South University, Changsha 410083, China
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ISSN1003-6326
DOI10.1016/S1003-6326(08)60261-7

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Abstract An novel method for removal of copper from nickel anodic electrolyte through ion exchange was studied after cupric deoxidization. Orthogonal design experiments show the optimum conditions of deoxidizing cupric into Cu+ in the nickel electrolyte are the reductive agent dosage is 4.5 times as the theoretic dosage and reaction time is 0.5 h at 40℃ and pH 2.0. Ion exchange experiments show that the breakthrough capacity(Y) decreases with the increase of the linear flow rate(X): Y=1.559-0.194X+ 0.006 7X2. Breakthrough capacity increases with the increase of the ratio of height to radius(RRH). The higher the initial copper concentration, the less the breakthrough capacity(BC). SO42- and nickel concentration have no obvious change during the process of sorption, so it is not necessary to worry about the loss of nickel during the sorption process. Desorption experiments show that copper desorption from the resin is made perfectly with NaCl solution added with 4% (volume fraction) H2O2 (30%) and more than 100 g/L CuCl2 solution is achieved.
AbstractList An novel method for removal of copper from nickel anodic electrolyte through ion exchange was studied after cupric deoxidization. Orthogonal design experiments show the optimum conditions of deoxidizing cupric into Cu+ in the nickel electrolyte are the reductive agent dosage is 4.5 times as the theoretic dosage and reaction time is 0.5 h at 40 deg C and pH 2.0. Ion exchange experiments show that the breakthrough capacity(Y) decreases with the increase of the linear flow rate(X): Y=1.559 -0.194X+ 0.006 7X2. Breakthrough capacity increases with the increase of the ratio of height to radius(RRH). The higher the initial copper concentration, the less the breakthrough capacity(BC). SO42i and nickel concentration have no obvious change during the process of sorption, so it is not necessary to worry about the loss of nickel during the sorption process. Desorption experiments show that copper desorption from the resin is made perfectly with NaCl solution added with 4% (volume fraction) H2O2 (30%) and more than 100 g/L CuCl2 solution is achieved.
An novel method for removal of copper from nickel anodic electrolyte through ion exchange was studied after cupric deoxidization. Orthogonal design experiments show the optimum conditions of deoxidizing cupric into Cu+ in the nickel electrolyte are the reductive agent dosage is 4.5 times as the theoretic dosage and reaction time is 0.5 h at 40℃ and pH 2.0. Ion exchange experiments show that the breakthrough capacity(Y) decreases with the increase of the linear flow rate(X): Y=1.559-0.194X+ 0.006 7X2. Breakthrough capacity increases with the increase of the ratio of height to radius(RRH). The higher the initial copper concentration, the less the breakthrough capacity(BC). SO42- and nickel concentration have no obvious change during the process of sorption, so it is not necessary to worry about the loss of nickel during the sorption process. Desorption experiments show that copper desorption from the resin is made perfectly with NaCl solution added with 4% (volume fraction) H2O2 (30%) and more than 100 g/L CuCl2 solution is achieved.
TG1; An novel method for removal of copper from nickel anodic electrolyte through ion exchange was studied after cupric deoxidization. Orthogonal design experiments show the optimum conditions of deoxidizing cupric into Cu+ in the nickel electrolyte are the reductive agent dosage is 4.5 times as the theoretic dosage and reaction time is 0.5 h at 40 ℃ and pH 2.0. Ion exchange experiments show that the breakthrough capacity(Y) decreases with the increase of the linear flow rate(X): Y=1.559-0.194X+ 0.006 7X2. Breakthrough capacity increases with the increase of the ratio of height to radius(RRH). The higher the initial copper concentration, the less the breakthrough capacity(BC). SO42- and nickel concentration have no obvious change during the process of sorption, so it is not necessary to worry about the loss of nickel during the sorption process. Desorption experiments show that copper desorption from the resin is made perfectly with NaCl solution added with 4% (volume fraction) H2O2 (30%) and more than 100 g/L CuCl2 solution is achieved.
An novel method for removal of copper from nickel anodic electrolyte through ion exchange was studied after cupric deoxidization. Orthogonal design experiments show the optimum conditions of deoxidizing cupric into Cu + in the nickel electrolyte are the reductive agent dosage is 4.5 times as the theoretic dosage and reaction time is 0.5 h at 40 °C and pH 2.0. Ion exchange experiments show that the breakthrough capacity( Y) decreases with the increase of the linear flow rate( X): Y=1.559–0.194 X+ 0.006 7 X 2. Breakthrough capacity increases with the increase of the ratio of height to radius(RRH). The higher the initial copper concentration, the less the breakthrough capacity(BC). SO 4 2í and nickel concentration have no obvious change during the process of sorption, so it is not necessary to worry about the loss of nickel during the sorption process. Desorption experiments show that copper desorption from the resin is made perfectly with NaCl solution added with 4% (volume fraction) H 2O 2 (30%) and more than 100 g/L CuCl 2 solution is achieved.
Author 陈爱良 邱冠周 赵中伟 孙培梅 余润兰
AuthorAffiliation School of Minerals Processing and Bioengineering, Central South University, Changsha 410083, China School of Metallurgical Science and Engineering, Central South University, Changsha 410083, China
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CitedBy_id crossref_primary_10_1016_j_molliq_2014_06_016
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Cites_doi 10.1016/S0304-386X(01)00191-8
10.1016/j.jhazmat.2004.06.033
10.1016/S0375-6742(02)00255-8
10.1016/j.electacta.2004.06.004
10.1016/S0304-386X(98)00087-5
10.1016/j.surfcoat.2005.03.017
10.1016/j.solmat.2004.07.045
10.1016/S0257-8972(01)01518-3
10.1016/j.hydromet.2004.03.003
10.1016/S0016-7037(01)00692-5
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Issue 1
Keywords anion ion exchange
nickel anode electrolyte
copper removal
cupric deoxidization
breakthrough capacity
Language English
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Notes 43-1239/TG
anion ion exchange
nickel anode electrolyte; copper removal; cupric deoxidization; anion ion exchange; breakthrough capacity
nickel anode electrolyte
TG142
copper removal
cupric deoxidization
breakthrough capacity
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Snippet An novel method for removal of copper from nickel anodic electrolyte through ion exchange was studied after cupric deoxidization. Orthogonal design experiments...
TG1; An novel method for removal of copper from nickel anodic electrolyte through ion exchange was studied after cupric deoxidization. Orthogonal design...
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StartPage 253
SubjectTerms anion ion exchange
breakthrough capacity
copper removal
cupric deoxidization
nickel anode electrolyte
气-固反应
热力学分析
金属材料
Title Removal of copper from nickel anode electrolyte through ion exchange
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