Ragheb T, Geddes L A
Hillenbrand Biomedical Engineering Center, Purdue University, W. Lafayette, IN 47907.
Ann Biomed Eng. 1991;19(2):151-63. doi: 10.1007/BF02368466.
The objective of this study was to characterize the polarization impedance (resistance and capacitance) of several common metal/0.9% saline interfaces operated at low-current density and to thereby provide a useful reference for those wishing to calculate the impedance of such electrodes. The series-equivalent resistance (R) and capacitive reactance (Xc) of stainless steel, platinum, silver, MP35N, palladium, aluminum, rhodium and copper electrodes, all having a surface areas S = 0.005 cm2 and all in contact with 0.9% saline, were measured as a function of frequency (100 Hz to 20 kHz) at low-current density (0.025 mA/cm2). For all the metals tested, both R and Xc decreased with increasing frequency and the relationships were linear on a log-log plot. That is, R and Xc exhibited power-law behavior (R = A/f alpha and Xc = B/f beta). However, it was not generally true that A = B and alpha = beta = 0.5 as stated in the Warburg low-current density model. Furthermore, the Fricke constant phase model in which alpha = beta and phi = 0.5 pi beta was found not to be applicable in general. In particular, the constraint that alpha = beta was a good approximation for most of the metals tested in this study, but the constraint that phi = 0.5 pi beta did not hold in general. Although the Warburg low-current density model provides a useful conceptual tool, it is not the most accurate representation of the electrode-electrolyte interface. The Fricke constant phase model is a better representation of electrode behavior, but it also may not be valid in general. We have found that a better representation is provided by the general power-law model R = A/f alpha and Xc = B/f beta, where A, B, alpha, and beta depend on the species of both the metal and electrolyte and A and B depend, in addition, on electrode area. Using this model and the data presented in this study, the impedance of an electrode-electrolyte interface operated at low-current density may be calculated as formula see text where S is the surface area of the electrode in cm2.
本研究的目的是表征在低电流密度下运行的几种常见金属/0.9%盐水界面的极化阻抗(电阻和电容),从而为那些希望计算此类电极阻抗的人提供有用的参考。测量了表面积S = 0.005 cm²且均与0.9%盐水接触的不锈钢、铂、银、MP35N、钯、铝、铑和铜电极的串联等效电阻(R)和容抗(Xc),作为频率(100 Hz至20 kHz)在低电流密度(0.025 mA/cm²)下的函数。对于所有测试的金属,R和Xc均随频率增加而降低,并且在对数-对数图上关系呈线性。也就是说,R和Xc表现出幂律行为(R = A/f^α且Xc = B/f^β)。然而,如瓦尔堡低电流密度模型所述,A = B且α = β = 0.5并不普遍成立。此外,发现弗里克常数相位模型(其中α = β且φ = 0.5πβ)一般不适用。特别是,α = β的约束对于本研究中测试的大多数金属是一个很好的近似,但φ = 0.5πβ的约束一般不成立。尽管瓦尔堡低电流密度模型提供了一个有用的概念工具,但它不是电极-电解质界面最准确的表示。弗里克常数相位模型是电极行为的更好表示,但它一般也可能不成立。我们发现,由一般幂律模型R = A/f^α且Xc = B/f^β提供了更好的表示,其中A、B、α和β取决于金属和电解质的种类,此外A和B还取决于电极面积。使用该模型和本研究中给出的数据,在低电流密度下运行的电极-电解质界面的阻抗可按公式计算(见原文),其中S是以cm²为单位的电极表面积。