期刊文献+

FPSO工艺水舱阳极快速消耗原因分析 被引量:6

Reasons for Rapid Consumption of Anodes in Process Water Tank of FPSO
下载PDF
导出
摘要 目的研究FPSO工艺水舱中铝牺牲阳极消耗过快的原因。方法参照GB 17848—1999牺牲阳极电化学性能试验方法,对比水舱环境与普通环境下,在役阳极的电化学性能数据,并模拟水舱环境,监测阳极工作时实际的发生电流与工作电位等情况,据此分析牺牲阳极在工艺水舱中消耗过快的原因。结果在常温(25℃)、常温充空气、高温(65℃)充空气等条件下,阳极的电化学容量分别是2522.07、2464.29、1943.74Ah/kg,且高温(65℃)充空气环境下阳极的晶间腐蚀较其他两组试验严重许多,说明温度是影响阳极电化学容量的关键因素。在模拟工艺水舱环境下,实测的阳极发生电流最高可达100m A。将工艺水与海水1:5稀释后,实测的保护电流密度最高达45m A,说明工艺水中存在大量的去极化剂,是造成阳极快速消耗的又一重要因素。结论工艺水舱环境下,阳极发生严重的晶间腐蚀,严重影响了阳极的电化学容量,使阳极寿命缩短。工艺水成分中含大量去极化剂,使船舱所需的保护电流密度大大增加,促使阳极发生电流加大,亦缩短了阳极的实际服役寿命。 Objective To research the reason for rapid consumption of sacrificial anodes in process water tank of FPSO. Methods According to the test methods in national standard 17848-1999, through comparing water tank environment and common environment, the water tank environment was simulated based on data on electrochemical performance of anode on active service to monitor current and potential of the anode during working, to analyze the reason why the anodes in process water tank are consumed so fast. Results The electrochemical capacities of the anode were 2522.07, 2464.29 and 1943.74Ah/Kg respectively in 25 degrees Celsius, 25 degrees Celsius with air inflation and 65 degrees Celsius with air inflation. Besides, the intercrystalline corrosion of anode was the most serious in 65 degrees Celsius with air inflation. It showed that the temperature was the key factor that influenced electrochemical capacity. In the simulated process water tank environment, the anode current could go to 100 mA, but in diluted process water, one liter of process water was mixed with 5 liter of seawater, it only went to 45mA. It showed the process water contained plenty of depolarizer, which was another important factor for rapid consumption of the anode. Conclusion In the process water tank environment, the anodes has serious inter-crystalline corrosion which greatly affects the electrochemistry capacity of the anode and shortens its service life. The plenty of depolarizer in the process water increases the protection current density required by the cabin, increase the current anode and shortens the actual service life of the anode。
作者 廖宏越 蔡德纯 蒋满军 王琦 陈亚林 张伟 杨朝晖 LIAO Hong-yue;CAI De-chun;JIANG Man-jun;WANG Qi;CHEN Ya-lin;ZHANG Wei;YANG Zhao-hui(CNOOC China Co., Ltd. Zhanjiang branch, Zhanjiang 524057, China;Shanghai Environment Project Technology Branch Company, Zhanjiang 524057, China;Marine Biology Institute of Shandong Province, Qingdao 266100, China;NCS Testing Technology Co., Ltd., Qingdao 266071, China;CISRI Qingdao Research Institute for Marine Corrosion, Qingdao 266071, China)
出处 《装备环境工程》 CAS 2019年第4期132-135,共4页 Equipment Environmental Engineering
关键词 工艺水舱 牺牲阳极 快速消耗 去极化剂 process water tank sacrificial anode rapid consumption depolarizer
  • 相关文献

参考文献6

二级参考文献17

  • 1王胜利.化工容器及设备破坏分析本身及保护措施的试验研究:(学位论文)[M].广州:华南理工大学工业装置与控制工程系,1988..
  • 2蒋小涌.铝合金牺牲阳极在湿度淡水的性能研究:(学位论文)[M].广州:华地理工大学工业装备与控制工程系,1991..
  • 3苏志辉.热水锅炉牺牲阳极保护系统的研究:(学位论文)[M].广州:华南理工大学工业装置与控制工程系,1996..
  • 4蒲志强.用于高温海水及海泥中铝合金牺牲阳极的研究:(学位论文)[M].广州:华南理工大学工业装备与控制工程系,1993..
  • 5李永广.在役海底管线牺牲阳极评价及优质铝阳极的研究:(学位论文)[M].广州:华南理工大学工业装备与控制工程系,1998..
  • 6火时中.电化学保护[M].北京:化学工业出版社,1988..
  • 7Jensen F O.Testing of zine anodes of offshore buried pipelines at elevatad temperature. Matefials Performances, 1978, 17(9) : 9.
  • 8Ashworth V,Intergranular dissolution of zinc alloy sacrificial anodes in seawter at elevated temperature.British Corrosion Journal,1979,14(1):46.
  • 9Schrieber C F.Effect of hostile marine environment on the AI-Zn-In -Si sacrificial anode,Materials Performance,1988.27(7):70.
  • 10Houghton C J,Offshore testing of aluminum anodes.Materials Protection and Performance,1971,10(5):29.

共引文献25

同被引文献49

引证文献6

二级引证文献1

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部