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A Newly Developed Methodology for Projection of Potential Attenuation and Anode Current Output for Cathodically Polarized Pipelines

机译:阴极极化管道电位衰减和阳极电流输出的新开发方法

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A first principles based equation for potential attenuation along a marine pipeline or riser that is cathodically polarized by multiple, equally spaced, identical galvanic anodes and which incorporates the electrolyte (anode), coating, and metallic path resistances, as well as the pipe polarization resistance, has recently been derived. Finite Difference Method solutions for this equation show that the potential profile consists of a relatively abrupt polarization decay within the first several meters of an anode and an essentially constant potential beyond this for cases where anode spacing is less than about one km (this distance varies with pipe and anode dimensions and properties and with exposure conditions). For anode spacings greater than this, metallic path resistance becomes important such that a potential gradient results along the entire pipe length. Comparison of the FDM solutions for the case of a pipeline of typical dimensions and marine exposure conditions with results from Boundary Element Modeling (BEM) indicates excellent agreement between the two for situations where the metallic resistance is negligible. For cases where this term is not negligible (relatively large anode spacings), the FDM solutions are the more accurate since BEM does not incorporate metallic path resistance. The potential attenuation projected by the classical equation of Uhlig is shown to be non-conservative compared to the FDM and BEM solutions because of its failure to consider the electrolyte component of circuit resistance. Anode current output determinations based upon the derived equation and upon BEM are also in excellent mutual agreement when anode spacing is relatively short. Beyond a certian distance, which is a function of pipe current demand, BEM underestimates anode current output. It is concluded that the derived equation has utility for design of pipeline cathodic protection systems and for analysis of data therefrom, particularly in cases where anode spacing is sufficiently large that metallic path resistance is non-negligible.
机译:第一个基于原理的方程式,用于沿海洋管道或立管的电位衰减,该方程由多个等间距,相同的原电池阳极进行阴极极化,并结合了电解质(阳极),涂层和金属通道电阻,以及管道极化电阻,最近已派生。此方程的有限差分法解决方案表明,电势分布包括在阳极的前几米内相对突然的极化衰减和在阳极间距小于大约1 km的情况下超出此范围的基本恒定的电势(该距离随管道和阳极的尺寸和性能以及暴露条件)。对于大于此的阳极间距,金属路径阻力变得很重要,以致沿整个管道长度产生电势梯度。对于典型尺寸和海洋暴露条件的管道,FDM解决方案与边界元素建模(BEM)结果的比较表明,在金属电阻可忽略不计的情况下,两者之间具有极好的一致性。对于该术语不可忽略的情况(相对较大的阳极间距),由于BEM不包含金属路径电阻,因此FDM解决方案更为准确。与FDM和BEM解决方案相比,由Uhlig的经典方程式预测的电位衰减显示为非保守的,因为它无法考虑电路电阻的电解质成分。当阳极间距相对较短时,基于导出的方程式和基于BEM的阳极电流输出确定也具有极好的一致性。 BEM超出了固定距离,该距离是管道电流需求的函数,因此BEM低估了阳极电流输出。得出的结论是,导出的方程式可用于管道阴极保护系统的设计和从中的数据分析,特别是在阳极间距足够大而金属路径电阻不可忽略的情况下。

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