Electrolysis expansion performance of semigraphitic cathode in [K3AlF6/Na3AlF6]-AlF3-Al2O3 bath system

Jie Li , Zhao Fang , Yan-qing Lai , Xiao-jun Lü , Zhong-liang Tian

Journal of Central South University ›› 2009, Vol. 16 ›› Issue (3) : 422 -428.

PDF
Journal of Central South University ›› 2009, Vol. 16 ›› Issue (3) : 422 -428. DOI: 10.1007/s11771-009-0071-x
Article

Electrolysis expansion performance of semigraphitic cathode in [K3AlF6/Na3AlF6]-AlF3-Al2O3 bath system

Author information +
History +
PDF

Abstract

The electrolysis expansion of semigraphitic cathode in [K3AlF6/Na3AlF6]-AlF3-Al2O3 bath system was tested by self-made modified Rapoport apparatus. A mathematical model was introduced to discuss the effects of αCR (cryolite ratio) and βKR (elpasolite content divided by the total amount of elpasolite and sodium cryolite) on performance of cathode electrolysis expansion. The results show that K and Na (potassium and sodium) penetrate into the cathode together and have an obvious influence on the performance of cathode electrolysis expansion. The electrolysis expansion and K/Na penetration rate increase with the increase of αCR. When αCR=1.9 and βKR=0.5, the electrolysis expansion is the highest, which is 3.95%; and when αCR=1.4 and βKR=0.1, the electrolysis expansion is the lowest, which is 1.28%. But the effect of βKR is correlative with αCR. When αCR=1.6 and 1.9, with the increase of βKR, the electrolysis expansion and K/Na penetration rate increase. However, when αCR=1.4, the electrolysis expansion and K/Na penetration rate firstly increase and then decrease with the increase of βKR.

Keywords

aluminum electrolysis / semigraphitic cathode / low temperature electrolysis / electrolysis expansion / K penetration / Na penetration

Cite this article

Download citation ▾
Jie Li, Zhao Fang, Yan-qing Lai, Xiao-jun Lü, Zhong-liang Tian. Electrolysis expansion performance of semigraphitic cathode in [K3AlF6/Na3AlF6]-AlF3-Al2O3 bath system. Journal of Central South University, 2009, 16(3): 422-428 DOI:10.1007/s11771-009-0071-x

登录浏览全文

4963

注册一个新账户 忘记密码

References

[1]

JamesW. E., HalvorK.. Sustainability, climate change, and greenhouse gas emissions reduction: Responsibility, key challenges, and opportunities for the aluminum industry [J]. JOM, 2008, 60(8): 25-31

[2]

JamesW. E.. The evolution of technology for light metals over the last 50 years: Al, Mg, and Li [J]. JOM, 2007, 59(2): 30-38

[3]

LAI Yan-qing, WANG Jia-wei. Commentary on the status quo of low temperature aluminum electrolysis in the Na3A1F6-A12O3 bath system [J]. Light Metal, 2006(9): 37–42. (in Chinese)

[4]

WANG Jia-wei, LAI Yan-qing. Commentary on the status quo of low temperature aluminum electrolysis in M(K or Li)3AlF6-Al2O3 bath system [J]. Light Metal, 2007(1): 31–36. (in Chinese)

[5]

YANG J H, DONALD G G, CATHERINE W, JOHN N H. Alumina solubility in KF-AlF3-based low-temperature electrolyte system [C]// Light Metals 2007. Orlando, 2007: 537–541.

[6]

RolsethS., GudbrandsenH., ThonstadJ.. Low temperature aluminium electrolysis in a high density electrolytes. Part I [J]. Aluminum, 2005, 81(5): 448-450

[7]

RolsethS., GudbrandsenH., ThonstadJ.. Low temperature aluminium electrolysis in a high density electrolytes. Part II [J]. Aluminum, 2005, 81(6): 565-568

[8]

SKYBAKMOEN E, SOLHEIM A, STEREN A. Phase diagram data in the system Na3AlF6-Li3AlF6-AlF3-Al2O3 [C]// Light Metals 1990. Anaheim, 1990: 317–323.

[9]

XUE Ji-lai, LIU Qing-sheng, OU Wen-li. Sodium expansion in carbon/TiB2 cathodes during aluminum electrolysis [C]// Light Metals 2007. Orlando, 2007: 651–654.

[10]

ZolocheyskyA., HopJ. G., ServantT., FoosnasT., OyeH. A.. Rapoport-Samoilenko test for cathode carbon materials II. Swelling with external pressure and effect of creep [J]. Carbon, 2005, 43(6): 1222-1230

[11]

X.-j., LiQ.-y., LaiY.-q., LiJ.. Digital characterization and mathematic model of sodium penetration into cathode material for aluminum electrolysis [J]. Journal of Central South University of Technology, 2009, 16(1): 96-100

[12]

LiQ.-yu.Development and industrial application of wettable inert TiB2 cathodic composite coating for aluminum electrolysis [D], 2003, Changsha, Central South University of Technology: 39-46

[13]

ChuanX.-yun.. Formation mechanism of graphite intercalation compounds [J]. New Carbon Materials, 2000, 15(1): 52-56

[14]

QiuZ.-xian.Smelting aluminum in pre-baked cell [M], 2005, Beijing, Metallurgical Industry Press: 311-314

[15]

ARNE P R, ANNE S, ASBJORN S, FOOSNAES T. The effect of current density on cathode expansion during strat-up [C]// Light Metals 2008. New Orleans, 2008: 973–978.

[16]

XUE J L, OYE H A. Sodium and bath penetration into TiB2-carbon cathodes during laboratory aluminum electrolysis [C]// Light Metals 1992. San Diego, 1992: 773–778.

[17]

DellM. B.In Extractive metallurgy of aluminium [M], 1963, New York, Interscience Publishers: 403-405

[18]

HopJ., StoreA., FoosnaesT., OyeH. A.. Chemical and physical changes of cathode carbon by aluminium electrolysis [J]. Transactions of the Institutions of Mining and Metallurgy, 2005, 114(3): 181-187

[19]

MortenS., OyeH. A.Cathodes in aluminium electrolysis [M], 1994, Düsseldorf, Aluminium-Verlag: 184-190

[20]

ChanB. K. C., ThomasK. M., MarshH.. The interactions of carbons with potassium [J]. Carbon, 1993, 31(7): 1071-1082

[21]

YuriM., OyeH. A.. Absorption of metallic sodium in carbon cathode materials [J]. Carbon, 1996, 34(1): 37-41

AI Summary AI Mindmap
PDF

88

Accesses

0

Citation

Detail

Sections
Recommended

AI思维导图

/