|
Abstract The research status of numerical calculation of cathodic protection potential distribution is discussed, including the building of mathematical model, the chosen of boundary conditions and numerical calculation methods. The problems exiting in this field and the developing directions are proposed.
|
Received: 27 May 2006
|
[1]Degiorgi V G,Wimmer S A.Geometric details and modeling accu-racy requirements for shipboard impressed current cathodic protec-tion system modeling[J].Engineering Analysis with Boundary El-ements,2005,29:15-28 [2]Degiorgi V G,Thomas E D,Lucas K E.Scale effects and verifica-tion of modeling of ship cathodic protection systems[J].Engi-neering Analysis with Boundary Elements,1998,22:41-59 [3]Zamani N G.Boundary element simulation of the cathodic protec-tion system in a prototypic ship[J].Appl.Math.Comput,1988,26:119-134 [4]Bialecki R A,Ostrowski Z,Kassab A J,et al.Coupling BEM,FEM and analytic solutions in steady-state potential problems[J].Engineering Analysis with Boundary Elements,2002,26:597-611 [5]Douglas P R,Mark E O.A mathematical model for the cathodic protection of tank bottoms[J].Corros.Sci.,2005,47:849-868 [6]Santiago J A F,Tells J C F.A solution technique for cathodic pro-tection with dynamic boundary conditions by the boundary element method[J].Advances in Engineering Software,1999,30:663-671 [7]Hassanein A M,Glass G K,Buenfeld N R.Protection current dis-tribution in reinforced concrete cathodic protection systems[J].Cem.Concr.Compos.,2002,24:159-167 [8]Degiorgi V G.Evaluation of perfect paint assumptions in modeling of cathodic protection systems[J].Engineering Analysis with Boundary Elements.,2002,26:435-445 [9]Kranc S C,Alberto A S.Detailed modeling of corrosion macrocells on steel reinforcing in concrete[J].Corros.Sci.,2001,43:1355-1372 [10]Qiu F,Xu N X.Potential and current distribution on pipelines cathodically protected with ribbon sacrificial anodes[J].J.Chin.Soc.Corros.Prot.,1997,17(2):106-110(邱枫,徐乃欣.用带状牺牲阳极对埋地钢管实施阴极保护时的电位和电流分布[J].中国腐蚀与防护学报,1997,17(2):106-110) [11]Qiu F,Xu N X.Potential distribution on cathodically protected steel pipe piles[J].J.Chin.Soc.Corros.Prot.,1997,17(1):12-18(邱枫,徐乃欣.码头钢管桩阴极保护时的电位分布[J].中国腐蚀与防护学报,1997,17(1):12-18) [12]Qiu F,Xu N X.Potential distribution on cathodically protected external tank bottom[J].J.Chin.Soc.Corros.Prot.,1996,16(1):29-36(邱枫,徐乃欣.钢质贮罐底板外侧阴极保护时的电位分布[J].中国腐蚀与防护学报,1996,16(1):29-36) [13]Zhang M D,Du Y L.Calculating potential distributions of ca-thodically protected subsea pipeline with finite difference method[J].J.Chin.Soc.Corros.Prot.,1994,14(1):77-81(张鸣镝,杜元龙等.有限差分法计算海底管道阴极保护时的电位分布[J].中国腐蚀与防护学报,1994,14(1):77-81) [14]Qian H J,Liu X G,et al.Numerical simulation of cathodic pro-tection inside pipes(II)-calculating the potential distribution in-side large-size pipes by using the finite difference method[J].Chem.Eng.Mach.,1997,24(5):281-284(钱海军,刘小光,张树霞等.管内阴极保护的数值模拟(II)-有限差分法计算大口径管内的电位分布[J].化工机械,1997,24(5):281-284) [15]Liu M,Yin Z A,et al.Calculation of potential distribution over cathodically protected inter-surface of pipe under flow condition[J].J.Dalian Univ.Technol.,1998,38(5):599-302(刘曼,殷正安,战广深.流动场管内阴极保护的电位分布计算[J].大连理工大学学报,1998,38(5):599-302) [16]Liang X W,Wu Z Y,et al.Optimal control of current in an im-pressed cathodic protection system[J].J.Tianjin Inst.Text.Sci.Technol.,1999,18(1):37-40(梁旭魏,吴中元等.阴极保护系统中电流的优化控制[J].天津纺织工学院学报,1999,18(1):37-40) [17]Ma W P,Zhang G Z,et al.Numerical modeling of deepwell an-ode to cathodic protection of bottom plate of tank[J].Oil Gas Stor-age and Transportation,2004,23(9):31-35(马伟平,张国忠.深井阳极对储罐底板阴极保护的数值模拟[J].油气储运,2004,23(9):31-35) [18]Liang X W,Wu Z Y,et al.Study on the computer assistant op-timization design for the regional cathodic protection system[J]J.Tianjin Inst.Text.Sci.Technol.,1998,17(5):90-94(梁旭魏,吴中元等.油田区域性阴极保护计算机辅助优化设计研究[J].天津纺织工学院学报,1998,17(5):90-94) [19]Meng X J,Wu Z Y,et al.Improvement of algorithm for regional cathodic protection model[J].J.Chin.Soc.Corros.Prot.,1998,18(3):221-224(孟宪级,吴中元等.区域性阴极保护数学模型算法的改进[J].中国腐蚀与防护学报,1998,18(3):221-224) [20]Machczynski W.Computer simulation of cathodic protection of un-derground conductors of arbitrary[A].Corrosion Asia'94[C].Sin-gapour,1994,1098-1 [21]Li X Y,Weng Y J.Calculating potential distribution on exterior of tank bottoms by analytical algorithm[J].Acta Pet.Sin.,1998,19(3):98-114(李相怡,翁永基.金属储罐底板外侧阴极保护电位分布的解析计算法[J].石油学报,1998,19(3):98-114) [22]Morgan,John.Cathodic Protection[M]Texas:National Associa-tion of Corrosion Engineers,1987,159-161 [23]Uhlig H H,Weng Y J.Corrosion and Corrosion Control(the Third Edition)[M].Beijing:Petroleum Industry Publishing Company,1985,516(Uhlig H H著,翁永基译.腐蚀与腐蚀控制(第三版)[M].北京:石油工业出版社,1985,516) [24]Emenike C O.Mathematical modeling of cathodic protection sys-tems for oil and gas facilities[J].Anti-Corrosion Methods and Materials,1995,42(4):6 [25]Glass G K,Buenfeld N R.On the current density required to protect steel in atmospherically exposed concrete structure[J].Corros.Sci.,1995,37(10):1643-1646 [26]Glass G K,Buenfeld N R,Hassanein A M.Monitoring the pas-sivation of steel in concrete induced by cathodic protection[J].Corros.Sci.,1997,39(8):1451-1458 [27]Ashworth V.Cathodic Protection-Theory and Practice[M].Lon-don:Ellis Horwood Limited,1986,31 [28]Thompson N G.Exploring the complexity of the mechanism of ca-thodic protection[A].Corrosion/94(NACE)[C].Baltimore,1994,580 [29]Tighe-Ford D J,Botten R A,et al.Study of design criteria for ship impressed-current cathodic protection by stylized modeling[J].Corros.Prev.Control,1990,37(2):5-11 [30]Chen S W,Hartt W H.Cathodic polarization characteristic of steel in sea water and a new approach for cathodic protection system design[J].Corros.Sci.Prot.Technol.,1996,8(1):17-25(陈绍伟,Hartt W H.钢在海水中的阴极极化特点及阴极保护系统设计中的新途径[J].腐蚀科学与防护技术,1996,8(1):17-25) [31]Emenike C O.Mathematical modeling of cathodic protection sys-tems for oil and gas facilities[J].Anti-Corrosion Methods and Materials,1995,42(4):6 [32]Doig P,Flewitt P E J.A finite difference numerical analysis ofgalvanic corrosion[J].Electrochem.J.Soc.,1979,126(12):2057-2063 [33]Strommen R,Arild R.Computerized techniques applied in design of offshore cathodic protection systems[J].Mater.Performance,1981,20(4):15-20 [34]Helle H P E,Beek G H M,Ligtelijin J T.Numerical determina-tion of potential distributions and current densities in multi-elec-trode systems[J].Corrosion,1981,37(9):522-530 [35]Kasper R G,April M G.Electro galvanic finite element analysis of partially protected marine structures[J].Corrosion,1983,39(5):181-188 [36]Munn R S.A Mathematical model for a galvanic anode cathodic protection system[J].Mater.Performance,1982,21(8):29-36 [37]Chin D T,Sabde G M.Current Distribution and electrochemical environment in a cathodically protected crevice[J].Corrosion,2000,56(3):229-237 [38]Chin D T,Sabde G M.Modeling transport process and current distribution in a cathodically protected crevice[J].Corrosion,2000,56(8):783-793 [39]Cherry B W,Foo M,Siauw T H.Boundary element method analy-sis of the potential field associated with a corroding electrode[J].Corrosion,1986,42(11):654-662 [40]Brichau F,Deconinck J.A numerical model for cathodic protec-tion of buried pipes[J].Corrosion,1994,50(1):39-49 [41]Liu X D,Lin X,et al.Numerical calculation of electric field of12kV/31.5kA vacuum circuit breaker arc chamber[J].J.Shenyang Univ.Technol.,2003,25(4):294-298(刘向东,林莘等.12kV/31.5Ka真空断路器灭弧室电场的数值计算[J].沈阳工业大学学报,2003,25(4):294-298) [42]Yu H L,Cui Q L,et al.Analysis of3D thermo-electric field po-tential for300kA aluminum electrolysis cell using ANSYS[J].Non-Ferrous Mining and Metallurgy,2004,20(3):30-32(喻海良,崔青玲等.300Ka铝阳极电解槽三维电热场电位AN-SYS分析[J].有色矿冶,2004,20(3):30-32) [43]Lu B X,Wang Z Z,et al.Voltage response analysis for fault transmission line[J].J.North China Electric Power University,2002,29(2):31-33(卢斌先,王泽忠等.故障传输线的电压响应分析[J].华北电力大学学报,2002,29(2):31-33) |
No Suggested Reading articles found! |
|
|
Viewed |
|
|
|
Full text
|
|
|
|
|
Abstract
|
|
|
|
|
Cited |
|
|
|
|
|
Shared |
|
|
|
|
|
Discussed |
|
|
|