Two-phase electrolysis process: From the bubble to the electrochemical cell properties

被引:54
作者
Mandin, Ph. [1 ]
Aissa, A. Ait [1 ]
Roustan, H. [2 ]
Hamburger, J. [3 ]
Picard, G. [1 ]
机构
[1] ENSCP, CNRS, LECA,UMR 7575, Lab Electrochim & Chim Analyt, F-75231 Paris 05, France
[2] Alcan, Ctr Rech Voreppe, F-38341 Voreppe, France
[3] Transoft Int, F-93200 St Denis, France
关键词
two-phase electrolysis; modelling bubbles; phenomenological laws;
D O I
10.1016/j.cep.2007.10.018
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
During two-phase electrolysis for aluminium, fluorine or hydrogen production there are bubbles which are created at the electrode which imply a great hydrodynamic acceleration but also a quite important electrical field and electrochemical processes disturbance. This disturbance can lead to the modification of the local current density and to anode effects for example. There are also few local experimental measurements in term of chemical composition, temperature or current density because considered media are often very aggressive (high temperature, very strong reactivity). Then, the modelling and numerical simulation appears to be one important tool to understand and optimize associated processes, though the rigorous validation of numerical calculations is difficult. The goal of the present work is the modelling and the numerical simulation of the local gas production at an industrial scale vertical electrode. Because bubbles modify species, heat and electricity transport and are motion sources, there is a strong coupling between all these phenomena and between the bubble scale and the macroscopic one. Because bubbles are at the origin of all macroscopic disturbances. it appears necessary to investigate phenomenological laws at the bubble scale. The finite volume of the Fluidyn (R) and Fluent (R) software has been used. (C) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:1926 / 1932
页数:7
相关论文
共 14 条
[1]   Transient linear stability of a Simons-process gas-liquid electrochemical flow reactor using numerical simulations [J].
Drake, JA ;
Radke, CJ ;
Newman, J .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (20) :5815-5834
[2]  
DUHAR G, 2003, MECANIQUE, V331
[3]   Transient nucleate boiling under stepwise heat generation for highly wetting fluids [J].
Duluc, MC ;
Stutz, B ;
Lallemand, M .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2004, 47 (25) :5541-5553
[4]   The bubble coverage of gas-evolving electrodes in a flowing electrolyte [J].
Eigeldinger, J ;
Vogt, H .
ELECTROCHIMICA ACTA, 2000, 45 (27) :4449-4456
[5]   BUBBLE EFFECTS ON THE SOLUTION IR DROP IN A VERTICAL ELECTROLYZER UNDER FREE AND FORCED-CONVECTION [J].
HINE, F ;
MURAKAMI, K .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1980, 127 (02) :292-297
[6]  
JANSSEN LPB, 1987, TRANSPORT PHENOMENA
[7]   Application of a two-phase flow model for natural convection in an electrochemical cell [J].
Mat, MD ;
Aldas, K .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2005, 30 (04) :411-420
[8]   INVESTIGATION OF PARTICLE TRAJECTORIES IN 2-PHASE FLOW SYSTEMS [J].
MORSI, SA ;
ALEXANDER, AJ .
JOURNAL OF FLUID MECHANICS, 1972, 55 (SEP26) :193-+
[9]   Modelling and calculation of the current density distribution evolution at vertical gas-evolving electrodes [J].
Philippe, M ;
Jérôme, H ;
Sebastien, B ;
Gérard, P .
ELECTROCHIMICA ACTA, 2005, 51 (06) :1140-1156
[10]   MODELING OF 2-PHASE THERMAL-CONDUCTIVITY [J].
RAGHAVAN, VR ;
MARTIN, H .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1995, 34 (05) :439-446