Current Issue Cover
Advanced Search
Founded in 1987， Bimonthly
Supervisor：Jiangxi University Of Science And Technology
Sponsored by：Jiangxi University Of Science And Technology
Jiangxi Nonferrous Metals Society
ISSN：1674-9669
CN：36-1311/TF
CODEN YJKYA9
Volume 4 Issue 3
Jun.  2013
Turn off MathJax
Article Contents
Abstract
References
Related Articles
YANG Shao-hua, XIE Bao-ru, YANG Feng-li, LI Ming-zhou. The behavior of anode bubbles in aluminum electrolytic cell[J]. Nonferrous Metals Science and Engineering, 2013, 4(3): 20-24. DOI: 10.13264/j.cnki.ysjskx.2013.03.014
Citation: YANG Shao-hua, XIE Bao-ru, YANG Feng-li, LI Ming-zhou. The behavior of anode bubbles in aluminum electrolytic cell[J]. Nonferrous Metals Science and Engineering, 2013, 4(3): 20-24. DOI: 10.13264/j.cnki.ysjskx.2013.03.014
shu

The behavior of anode bubbles in aluminum electrolytic cell

  • School of Metallurgy and Chemical Engineering, Jiangxi University of Science and Technology, Ganzhou 341000, China

More Information
  • Received Date: February 25, 2013
  • Published Date: June 29, 2013
    Graphical Abstract
    • Abstract
  • This paper studies the behavior of anode bubbles by transparency cell. Anode bubbles grew gradually at anode bottom. The bubbles generated on anode side were smaller than those of anode bottom. Obvious phenomena that diameter of anode bubbles opposite to the cathode was the smallest in all bubbles were observed. The bubbles generated on the anode surface don't collect into bigger bubbles, which is different from the bubbles generated in other parts of anode. The bubbles generated at anode bottom overflow electrolyte by moving between anode and cathode. The diameter of anode bubbles affects cell voltages. Cell voltage increases by 0.21V with diameter of anode bubbles increasing 3 mm. The cell voltage changes by 0.16 V when anode bubbles generated at anode bottom separated from anode at 0.5 A/cm2. The value was 0.12 V at 0.3 A/cm2.
    • FullText(HTML)
    • References (22)
  • [1]
    薛玉卿, 周乃君, 包生重.铝电解槽内阳极气泡运动的冷态模拟[J].中国有色金属学报, 2006(10): 1823-1828. http://www.cnki.com.cn/Article/CJFDTOTAL-ZYXZ200610027.htm
    [2]
    László I. Kiss, Sándor Poncsák, Jacques Antille. Simulation of the bubble layer in aluminum electrolysis cells[C]//Light Metals. Warrendale: TMS, 2005: 559-564.
    [3]
    Fortin S, Gerhardt M, Gesing A J. Physical modeling of bubble behavior and gas release from aluminum reduction cell anodes[C]// Warrendale: TMS, 1984, 721-741.
    [4]
    Shekhar R, Evans J W. Physical modeling studies of electrolyte flow due to gas evolution and some aspects of bubble behavior inadvance hall cells:Part i.flow and interpolar resistance in cells with a grooved anode[J].Metall. Mater. Trans. B, 1995, 25(3):330-340. doi: 10.1007%2FBF02663383
    [5]
    杨帅, 张红亮, 徐宇杰, 等.铝电解槽预焙阳极开槽对气泡排出的影响[J].中南大学学报:自然科学版, 2012, 48(12):4617-4625. http://www.cnki.com.cn/Article/CJFDTOTAL-ZNGD201212006.htm
    [6]
    王志刚, 张红亮.槽型对5kA级惰性阳极铝电解槽流场影响仿真[J].有色冶金设计与研究, 2012, 33(4):7-10. http://www.cnki.com.cn/Article/CJFDTOTAL-YSYJ201204005.htm
    [7]
    赵秋月, 张廷安.CFD技术在铝电解中的应用[J].轻金属, 2011(12):30-33. http://www.cnki.com.cn/Article/CJFDTOTAL-QJSS201112010.htm
    [8]
    张红亮, 王志刚, 李劼, 等.铝电解金属陶瓷惰性阳极气体及电解质流场仿真[J].中南大学学报:自然科学版, 2010, 41(4):1256-1262. http://www.cnki.com.cn/Article/CJFDTOTAL-ZNGD201004008.htm
    [9]
    Shekhar R, Evans J W. Physical modeling studies of electrolyte flow due to gas evolution and some aspects of bubble behavior in advanced hall cells: part ⅱ. flow and interpolar resistance in cells with a grooved anode[J]. Metall. Mater. Trans. B, 1995, 25B, 341-349. doi: 10.1007%2FBF02663383
    [10]
    Shekhar R, Evans J W. Physical modeling studies of electrolyte flow due to gas evolution and some aspects of bubble behavior in advanced hall cells: part ⅲ. predicting the performance of advanced hall cells[J]. Metall. Mater. Trans. B, 1996, 27(1):19-27. doi: 10.1007/BF02915072
    [11]
    徐君莉, 石忠宁, 高炳亮, 等.铝电解金属阳极上气泡析出行为[J].中国有色金属学报, 2002, 14 (2):298-301. http://www.cnki.com.cn/Article/CJFDTOTAL-ZYXZ200402026.htm
    [12]
    GAO Bing-liang, LI Hai-tao, WANG Zhao-wen, et al. A new study on bubble behavior on carbon anode in aluminum electrolysis[C]// Light Metals, Warrendale: TMS, 2005:571-575.
    [13]
    ZHANG Yan-li, HOU Guang-hui, QIU Shi-lin. New developments of bubble behaviors on anode in aluminum smelting cells[J].Light metals, 2007, 12:41-44.
    [14]
    Grjotheim K, Kvande H, QIU Zhu-xian, et al. Interfacial phenomena in molten salt electrolysis[J].Aluminum, 1989, 65(2):157-162.
    [15]
    Laszlo J K, Sandor P. Effect of the bubble growth mechanism on the spectrum of voltage fluctuations in the reduction cell[C]// Light Metals, Warrendale: TMS, 2002: 365-370.
    [16]
    Xue J, Oye H. Bubble behavior-cell voltage oscillation during aluminum electrolysis and the effects of sound and ultrasound[C]//Light Metals, Warrendale: TMS, 1995: 265-270.
    [17]
    Hyde T H, Welch B J. The gas under anodes in aluminum smelting cells (partⅠ):Measuring and modeling bubble resistance under horizontally oriented electrodes[C]// Light Metals.Warrendale:TMS, 1997:333-340.
    [18]
    YANG Shao-hua, YANG Feng-li, LIU Qing-sheng, et al. Study on behavior of anode bubble[C]//Light Metals. Warrendale:Minerals, Metals & Materials Soc, 2009:65-68.
    [19]
    Aaberg R J, Ranum V, Williamson K, et al. The gas under anodes in aluminum smelting cells (part Ⅱ): Gas volume and bubble layer characteristics[C]//Light Metals. Warrendale: TMS, 1997:341-346.
    [20]
    Gorodetskii V V. Chlorine evolution on highly porous metal oxide anodes and the origin of the low:polarizability portion in polarization curves at large currents[J].Russian Journal of Electrochemistry, 39, 2003(6):650-659. https://www.researchgate.net/publication/237996926_Chlorine_Evolution_on_Highly_Porous_Metal_Oxide_Anodes_and_the_Origin_of_the_Low-Polarizability_Portion_in_Polarization_Curves_at_Large_Currents
    [21]
    Sadoway D R. A materials systems approach to selection and testing of nonconsumable anode for the hall cell[C]// Light Metals. Warrendale: TMS, 1990: 403-407.
    [22]
    Kai Grjotheim, Halvor Kvande, LI Qing-feng, et al. Metal production by molten salt electrolysis[C]//Xuzhou:China University of Mining and Technology Press, 1998:151-155.
    • Related Articles

  • Related Articles

    [1]FANG Yi, ZHAO Wenning, HAN Xiuxun. Effects of thickness of absorption layer and buffer layer on the performance of Cu3BiS3 solar cell[J]. Nonferrous Metals Science and Engineering, 2021, 12(2): 50-55. DOI: 10.13264/j.cnki.ysjskx.2021.02.007
    [2]HE Jiangfan, WU Peijia, GUANG Weixin, LI Xin, SHU Qing. Synthesis and selectivity of anode material La0.75Sr0.25Cr0.5Mn0.5O3-δ for solid oxide fuel cell[J]. Nonferrous Metals Science and Engineering, 2018, 9(5): 33-36, 48. DOI: 10.13264/j.cnki.ysjskx.2018.05.006
    [3]WAN Zhanghao, XU Zhifeng, HUANG Jindi, YAN Kang. Three-phase stirring simulation of H2SO4-O2-copper anode slime and grey comprehensive evaluation in vertical reactor[J]. Nonferrous Metals Science and Engineering, 2018, 9(4): 21-28. DOI: 10.13264/j.cnki.ysjskx.2018.04.004
    [4]LIU Yuandong, YUAN Le, YU Runlan. Overview of high-cell-density cultivation of microorganisms[J]. Nonferrous Metals Science and Engineering, 2015, 6(4): 76-80. DOI: 10.13264/j.cnki.ysjskx.2015.04.016
    [5]GUO Hai-dong, LIANG Zeng-sen. Analysis and Treatment of Abnormity of Current Circuit of Five Terminal Prebaked Reduction Cell[J]. Nonferrous Metals Science and Engineering, 2010, 24(3-4): 170-173.
    [6]XING Li, HE Jian-zhong, GAO De-jin, HANG Chang-qing, FENG Feng-ming, XING Hua. Development and Application of Pre-baked Anode Electrolytic Cell Clamping Conductive Fixture[J]. Nonferrous Metals Science and Engineering, 2010, 24(3-4): 164-169.
    [7]TIAN Ying-fu. The Simulation Model of the Constitution of Aluminum Electrolytic Cell Anode Pitch and Its Energy Consumption[J]. Nonferrous Metals Science and Engineering, 2010, 24(3-4): 161-163.
    [8]GAO Jun, LI Bo. Disrepair Analysis Of 200 kA Aluminum Reduction Cell and Medium Repair' s Practice[J]. Nonferrous Metals Science and Engineering, 2008, 22(1): 39-40, 47.
    [9]ZHOU Ke-liang, LIANG Ling. Ration Pouring Control System for Lead Anode Plate Based on Profibus[J]. Nonferrous Metals Science and Engineering, 2006, 20(4): 21-23.
    [10]LI Guo-lin, HUANG Qi, LIAN Zhong-jun, ZHAO Jun. The Optimized Structural Transformation of the Work Bin Discharge Pipe of Aluminium Electrolysing Cell[J]. Nonferrous Metals Science and Engineering, 2006, 20(3): 47-48.

Catalog

    Get Citation
    PDF
    XML

    Article Metrics

    Article views (62) PDF downloads (5) Cited by()
    Related

    Copyright © 2010 Editorial Department of Nonferrous Metals Science and Engineering All rights reserved

    Address：11th floor, bishop building, University of science and technology, No. 86, Hongqi Avenue, Ganzhou City, Jiangxi Province  Tel：0797-8312555

    Supported by: Beijing Renhe Information Technology Co., Ltd.  Baidu Analytics

    /

    DownLoad:  Full-Size Img  PowerPoint
    Return
    Return