Cathodic Protection Design of a Pipe Laying Vessel Based on Numerical Simulation
摘 要
在全寿命期内, 铺管船水下结构腐蚀防护状态处于动态过程。因此, 依据实际情况设计腐蚀防护方案十分必要。采用数值模拟计算方法预报腐蚀防护状态, 并通过缩比模型试验验证了此方法的准确性。在此基础上设计了两种腐蚀防护方案: “单纯外加电流阴极保护”和“外加电流+牺牲阳极辅助的联合阴极保护”。并通过数值模拟计算预报了两种方案下的腐蚀防护状态。经过对比发现, 使用“外加电流+牺牲阳极辅助的联合阴极保护”时, 表面电位分布更均匀, 阳极屏面积及电源功率都有较明显的减小, 水下结构处于更为良好的腐蚀防护状态。
Abstract
Corrosion protection status of the pipe laying vessel underwater structure is under a dynamic process in the lifecycle. Thus, it is necessary to design the corrosion protection program according to the practical situation. In this paper, numerical simulation method was used to predict the corrosion protection status and the accuracy of the method was evaluated by the scale model test. Then two cathodic protection plans were considered, which were “impressed current cathodic protection” and “sacrificial anode and impressed current joint cathodic protection”. The corrosion protection status was predicted by the numerical simulation for these two protection plans. After comparison it was found that the application of “sacrificial anode and impressed current joint cathodic protection” enhanced the uniformity of potential distribution. The area of the anode shield and the power of two DC electrical sources were reduced by a large margin. All the submerged structures were in good protection.
中图分类号 TG174.41 DOI 10.11973/fsyfh-201511013
所属栏目 应用技术
基金项目 国家科技重大专项(2011ZX05027-002)
收稿日期 2015/7/14
修改稿日期
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联系人作者宋世德(peterssd@qq.com)
备注宋世德(1974-), 讲师, 博士, 从事腐蚀传感器研究,
引用该论文: YANG Lu-jia,ZHONG Wen-jun,CAO Ya-zhou,LIU Fu-guo,SONG Shi-de,HUANG Yi. Cathodic Protection Design of a Pipe Laying Vessel Based on Numerical Simulation[J]. Corrosion & Protection, 2015, 36(11): 1072
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参考文献
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【2】马桂君,刘福国,王伊诺,等. 船体压载舱牺牲阳极阴极保护的数值模拟[J]. 腐蚀与防护,2014,35(3):257-260.
【3】刘福国,尹鹏飞,张国庆,等. 海洋石油平台外加电流阴极保护延寿修复技术[J]. 腐蚀与防护,2015,36(3):276-280.
【4】赵景波,吴建华,姚萍. 舰船双区域外加电流阴极保护系统的优化[J]. 腐蚀与防护,2013,34(12):1114-1118.
【5】李成杰,杜敏. 深海钢铁材料的阴极保护技术研究及发展[J]. 中国腐蚀与防护学报,2013,33(1):10-15.
【6】吴世刚,常斌. 多点阴极保护技术的研究与应用[J]. 化工设备与防腐蚀,2003,6(2):64-66.
【7】王晨,顾望平. 12.5×104 m3储油罐底板阴极保护方案比选[J]. 石油化工设备技术,2003,24(3):45-49.
【8】方志刚, 黄一. 铝合金船体阴极保护系统的数值模拟仿真[J]. 船舶工程, 2012, 33(4): 73-76.
【9】王爱萍,杜敏,陆长山,等. 海洋平台复杂节点阴极保护电位分布的有限元法计算[J]. 中国海洋大学学报:自然科学版,2007,37(1):129-134.
【10】侯志强,邢少华. 压载水舱阴极保护设计与保护效果评价[J]. 材料保护,2008,41(6):67-68.
【11】赵景波,吴建华,姚萍. 舰船双区域外加电流阴极保护系统的优化[J]. 腐蚀与防护,2013,34(12):1114-1118.
【12】HUANG Y,IWATA M,NAGAI K. BEM analysis of the potential distribution on a tubular structure under cathodic protection[J]. Journal of the Society of Naval Architects of Japan,1993(174):777-986.
【13】HUANG Y,IWATA M,MOTOMURA T. A study on protection potential monitoring system for a large scale floating structure[J]. Journal of the Society of Naval Architects of Japan,1998,184:443-452.
【14】郝宏娜,李自力,王太源,等. 阴极保护数值模拟计算边界条件的确定[J]. 油气储运,2011,30(7):504-507.
【15】WANG Y,KARISALLEN K J. Comparison of impressed current cathodic protection numerical modeling results with physical scale modeling data[J]. Corrosion,2010,66(10):105001-105015.
【16】WANG Y,KARISALLEN K J. Validating impressed current cathodic protection numerical modelling results using physical scale modelling data[C]//Corrosion 2008.[S.l.]:NACE International,2008.
【17】梁成浩,于楠,吴建华,等. 船体双区域外加电流阴极保护缩比模型模拟研究[J]. 大连理工大学学报,2008,48(5):656-660.
【18】B/T 3108-1999船体外加电流阴极保护系统[S].
【19】方志刚,黄一. 复杂结构阴极保护设计中电流屏蔽效应数值模拟仿真[J]. 舰船科学技术,2012,34(9):98-102.
【20】HUANG Y,FANG Z G. Studying on shielding effect in the sacrificial anode cathodic protection system[C]//Advanced Materials Research.[S.l.]:[s.n.],2012,567:275-282.
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