Improvement of the Polarization Resistance Method

Bibliographic Information

Other Title
  • 分極抵抗法の改良について
  • 分極抵抗法の改良について--初期定電流過渡曲線からの分極抵抗の測定
  • ブンキョク テイコウホウ ノ カイリョウ ニ ツイテ ショキ テイデンリュウ
  • 初期定電流過渡曲線からの分極抵抗の測定
  • Measurement of the polarization resistance from the initial transient curve under a constant current

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Description

Polarization resistance to obtain an instantaneous corrosion rate has been measured from the steady state potential reached after charging of the double layer when a constant current was applied. In neutral solution, however, the potential never attain to that state but gradually increase owing to the presence of the rust formed on the surface. This makes the measurement inaccurate.<br>The present method consists of a short time polarization (0.5sec) and a determination of the steady state potential in accordance with the following theoretical transient equation.<br>ln[i(2Rp+Rsol)]-E=ln(2iRp)-t/CpRp<br>where the term, i(2Rp+Rsol), corresponds to the steady state potential and this was determined by curve fitting.<br>Two sheets of mild steel were immersed in tap water in parallel, apart 1cm. A constant current of 5μA/cm2 was applied between the two and the potential build-up curve was recorded with a transient converter. This method was found to have advantages over the conventional method in that<br>1) Solution resistance between the specimens (Rsol) and pseudo capacity (Cp) can also be measured as well as polarization resistance (Rp).<br>2) Reference electrode is not necessary and simple two electrodes method is applicable due to the accurate determination of Rsol.<br>3) Short-time polarization ensures no disturbance of natural corrosion state.<br>4) Measuring apparatus are simple compared with other non-steady state methods.<br>Another interesting information was also derived through this research in that abnormally large value of Cp was due to the continuous electrochemical change in rust oxidation state during the polarization.

Journal

  • CORROSION ENGINEERING

    CORROSION ENGINEERING 34 (4), 215-221, 1985

    Japan Society of Corrosion Engineering

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