CONCRETE LIBRARY OF JSCE NO. 39, JUNE 2002 ESTIMATING THE CORROSION RATE OF REINFORCING STEEL IN CONCRETE BY MEASURING POLARISATION RESISTANCE (Translation from Proceedings of JSCE, No. 669/V-50, February 2001) Koichi KOBAYASHI Toyo MIYAGAWA This study looks into polarisation resistance methods. Based on a better understanding of these methods, the aim is to clarify the relationship between corrosion loss and polarisation resistance in reinforced concrete beams that suffer deterioration due to chloride induced corrosion, thus leading to quantitative estimates of steel bar corrosion loss from the polarisation resistance. The results obtained in this study can be summarised as follows: (1) The current flowing upon polarisation flows into the steel bar largely from the inner side of specimen irrespective of the type of counter electrode. (2) Where a double-disk counter electrode is used, the amount of current flowing out from the main counter electrode approximately corresponds to that flowing into the cover side of the steel bar. (3) The amount of corrosion can be calculated more precisely from the polarisation resistance by combining the measurements obtained using the double-pulse method with a large counter electrode and those obtained using the AC impedance method with a double-disk counter electrode. (4) The constant K in the Stern-Geary formula is obtained as 0.0296V in this study. Keywords: chloride induced corrosion, polarization resistance, macro-cell corrosion, double rectangular pulse method, AC impedance method Koichi Kobayashi is an Assistant Professor in the Department of Civil Engineering, Chubu University, Kasugai, Japan. He obtained his Dr. Eng. from Kyoto University in 1999. His research interests relate to chloride induced corrosion of reinforcing steel in concrete. He is a member of JSMS, JCI, and JSCE. Toyo Miyagawa is a Professor in the Department of Civil Engineering, Kyoto University, Kyoto, Japan. He received his Dr. Eng. from Kyoto University in 1985. He is the author of a number of papers dealing with durability, maintenance and repair of reinforced concrete structures. He is a member of ACI, RILEM, CEB, JSMS, JCI and JSCE. - 103 - 1. INTRODUCTION Reinforced concrete structures are intrinsically durable as long as they are properly designed and constructed. In fact, they were once regarded as semi-permanent and maintenance-free. However, it is now known that certain properties of a concrete structure, such as load bearing capacity, deteriorate as time passes. In some cases, the deterioration occurs prematurely and causes many serious problems. In other cases, it progresses slowly over several decades of service. While it is certainly important to construct structures that are durable, it is also essential to provide proper maintenance such that a long service life is achieved. There are several factors which cause deterioration of reinforced concrete structures, one of the major ones being corrosion of the reinforcing steel. To prevent this type of deterioration, it is important to use dense and durable concrete so as to prevent the penetration of chloride ions and carbon dioxide gas, which break down the passive film that forms on the reinforcing steel. Corrosion of steel bars can be recognised when the cover concrete cracks in the direction of the reinforcement. However, by the time a crack is observed, corrosion has already progressed to a significant degree. Moreover, the corrosion reaction accelerates once the cover concrete has cracked, so repairs become more difficult. Accordingly, it is important to properly monitor a reinforced concrete structure and to detect steel corrosion at an early stage. Among various techniques for non-destructive testing, electrochemical test methods are considered most effective for inspecting reinforcing steel corrosion, because the steel corrosion process is an electrochemical reaction. The polarisation resistance method, for instance, is particularly suitable for evaluating the corrosion rate of steel bars. It utilises a relationship between corrosion current and polarisation resistance. More specifically, when the electric potential of a steel bar is forced to change, i. e., when the steel bar is "polarised", the polarisation resistance Rp is equal to the ratio of ∆E to ∆I, where ∆E represents the change in potential of the steel and ∆I represents the change in current. Within reinforced concrete, at the interface between the steel and the pore solution, there exists an electric doublelayer consisting of a Helmholtz layer and a diffusion boundary layer. The pore solution and electric doublelayer can most simply be considered equivalent to an electric circuit, as shown in Fig. 1, consisting of the polarisation resistance Rp, a capacitor Cd, and a resistor representing the resistivity of the concrete Rc. As the response of this circuit, when the steel is polarised, depends on a resistive component and a capacitative component, it is necessary to isolate the polarisation resistance component alone in order to determine the exact corrosion rate. The prevailing methodology in Japan for determining polarisation resistance includes the AC impedance method and the two frequencies method [1]~[5]. The two frequencies method works as follows. When voltage ∆E or current ∆I is applied to the circuit at very high frequency, the reactance of the capacitor becomes negligible and the electric current flows almost entirely through the resistor Rc and the capacitor Cd. In this situation, the response of the circuit can be regarded as that of the resistor alone. On the contrary, when voltage ∆E or current ∆I is applied at very low frequency, the reactance of the capacitor becomes infinite. Therefore, the circuit can be treated as consisting only of the resistor Rc and the polarisation resistance Rp connected in series. Thus, the response of the circuit when high-frequency voltage or current is applied represents the resistance of the resistor, while the response when a low frequency is applied represents the resistance of the resistor and the polarisation resistance. Accordingly, the polarisation resistance is obtained by subtracting the high-frequency result from the low frequency result. In practice, the two frequencies method is often implemented as a double-pulse method, in which two different frequency waveforms are superposed and applied simultaneously. Rp The actual electrochemical state of the steel embedded in the concrete is of course much more complex than that represented by the circuit model because of various factors affecting the electrochemical properties of the steel. These include the Warburg impedance, or resistivity to the diffusion of gases and ions, and the mill scale formed on the surface of the steel bar. Thus the results obtained by the two - 104 - Rc Cd Fig. 1 Equivalent electric circuit model frequency method are only approximate values. The AC impedance method involves applying a voltage to the steel bar at varying frequencies and expressing the electrochemical properties of the steel bar in either the complex-plane presentation or the Bode presentation. While the double-pulse method offers easy measurement and good applicability to actual concrete structures, the results obtained are not necessarily reliable due to the various factors mentioned above. On the other hand, the AC impedance method permits much more precise measurement of the polarisation resistance and thereby makes possible evaluation of the corrosion rate of the steel bar. However, it entails a complex, time-consuming measurement procedure. Since estimating corrosion loss necessitates a large number of measurements over time, it is not instantly practicable, either. Another problem to be resolved before precise evaluations of corrosion rate are possible is that the electrochemical behaviour of a steel bar while polarised is not always uniform, because electric current flows through the cover concrete which may have various shapes and consist of various different mixtures. This study looks further into polarisation resistance methods. Based on a better understanding of these methods, the aim is to clarify the relationship between corrosion loss and polarisation resistance in reinforced concrete beams that suffer deterioration due to chloride induced corrosion, thus leading to quantitative estimates of steel bar corrosion loss from the polarisation resistance. 2. EXPERIMENTAL PROCEDURE 2.1 Materials and Mixtures Table 1 shows the mix proportions used for the experimental specimens and Table 2 the materials employed in these mixtures. Three types of ordinary concrete were prepared. In two cases, N15 and N30, chloride ions were added (at 1.5% and 3.0% per unit mass of water, corresponding to 2.75kg and 5.5kg per unit volume of concrete, respectively) to ordinary concrete to simulate chloride-induced corrosion, while no chloride ions were added to mixture NN. The concentration of chloride ions in mixture N15 slightly exceeded the 1.2~2.5kg/m3 threshold for corrosion of reinforcing steel as reported by some researchers [6][7]. These chloride ions were added by blending sodium chloride into the concrete during mixing, and the same mass of sand was removed from the specified mix proportions. Two types of powder-type self-compacting concrete containing limestone powder were prepared: mixture SL (W/C=0.6) had the same water-binder ratio as ordinary concrete so as to obtain normal strength, and mixture SH (W/C=0.4) had a lower water-binder ratio so as to obtain higher strength. Self-compacting concrete was developed to offer superior self-compactability for filling all corners of the formwork without the need for vibration. Thus, it is considered to have advantage for repair work, which often requires injection of concrete into confined spaces. Table 1 Mix proportions NN N15 N30 SL SH W/C (%) W/(C+ Lp) (%) 60 60 60 45 32.4 33.1 s/a (%) 50.0 49.9 49.7 50.0 50.1 Unit mass (kg/m3) W C Lp 183 305 0 170 174 283 387 242 138 S 867 863 858 780 783 - 105 - G 891 800 Air Compressive Water entraining strength reducing agent agent at 28 days NaCl (C+Lp) x % (C+Lp) x % (N/mm2) 0 32.4 4.575 0.25* 0.0053 30.1 9.15 29.2 2.1** 0.01 34.9 0 2.2** 0.01 49.0 * Water-reducing agent ** High-range water-reducing agent Table 2 Materials Ordinary Portland cement ; Specific gravity : 3.15; Cement Blane fineness : 3260cm2/g Limestone powder CaCO3 >95% ; Specific gravity : 2.73; Blane fineness : 6770cm2/g River sand ; Specific gravity : 2.57; Water absorption : 1.80%; Fine aggregate Fineness modulus : 2.63 Crushed stone ; Specific gravity : 2.64; Maximum size : 15mm; Coarse aggregate Fineness modulus : 6.18 Water-reducing agent Lignosulfonic acid High-range water reducing agent Polycarboxylic acid Air-entraining agent Rosin-based anionic surfactant 2.2 Specimens Two types of beam were prepared for this study. The vertical-jointed specimen shown in Fig. 2 was constructed with vertical joints to simulate an uneven chloride ion distribution, causing a macro-cell corrosion circuit to be formed, in a case where the bottom surface of a beam is repaired by patching. Two deformed reinforcing steel bars 10mm in diameter and 700mm in length with mill scale were embedded in these specimens with 20mm of concrete cover (twice the bar diameter). Electrical cables rated at 100 volts and with a resistance of 14Ω/m were soldered to one end of each steel bar after exposing the bare steel by grinding off the mill scale. These connections were used for measuring half-cell potentials and polarisation resistance. The exposed ends of the steel bars were then wrapped with a self-bonding insulating tape and further covered with epoxy resin to prevent the ingress of water. Mixtures NN, SL, and SH were placed as the central part of the vertical-jointed specimen, corresponding to the repaired part of the structure, and mixtures NN, N15, and N30 were placed to form the left and right parts of the specimen, corresponding to the chloride-contaminated part of the structure. The central part was placed on the first day. Water was then sprayed over the joint surfaces, and the left and right parts were placed on the next day. The specimen was demolded on the third day. Table 3 shows the combination of mixtures used in each type of vertical-jointed specimens. Two beams of each discrete type were prepared. In order to investigate the effects of the actual joints, into which chloride ions might penetrate, monolithic specimens using each type of concrete alone were also prepared: specimens NN, N15, N30, SL, and SH. Further, specimens with two joints were prepared using the same concrete throughout: specimens NN-NN-NN, N30-N30-N30, and SL-SL-SL. In this case also, the left and right parts were placed on the second day. Cable 30 40 Placed from this side 250 800 300 L part C part 30 80 250 R part 20 D10 0 100 Distance from left end 200 250 300 700 400 500 550 600 700 Halfcell potential Polarization resistance (Double-pulse method) ( ) ( Polarization resistance (AC impedance method) Fig. 2 Vertical-jointed specimen (unit: mm) - 106 - ) Table 3 Vertical-jointed specimens The horizontal-jointed specimen shown in Fig. 3 was constructed with a horizontal joint for the investigation of macro-cell corrosion and micro-cell corrosion. Four deformed reinforcing steel bars 10mm in diameter and 300mm in length with mill scale were embedded in the specimens with a concrete cover of thickness 20mm. Cables were attached as with the vertical-jointed specimens. Mixtures NN, SL, and SH were placed as the bottom layer of the horizontal-jointed specimen on the first day. Water was sprayed over the joint surface, after which mixtures NN, N15, and N30 were placed as the upper layer of the specimen on the next day. The specimen was demolded on the third day. Table 4 shows the combination of mixtures used in each type of horizontal-jointed specimen. Two beams of each discrete type were prepared. Monolithic specimens, NN and N30, were also prepared as with the vertical-jointed specimens. Both vertical-jointed specimens and horizontal-jointed specimens were left in a laboratory at ambient temperature after demolding, and 5% chloride sodium solution was sprayed on them once a day. After demolding, all specimens were held on wood spacers with the placement surface upwards, while their bottom surfaces were kept wet. The compressive strength values of the concrete at the age of 28 days, as given in Table 1, were obtained from cylindrical specimens with a diameter of 100mm and a height of 200mm. These were cured in the same way as the beam specimens. Part C L N15-NN-N15 N15-NN-N30 N30-NN-N30 NN-SL-N15 N15-SL-N15 NN-SL-N30 N15-SL-N30 N30-SL-N30 NN-SH-N15 N15-SH-N15 NN-SH-N30 N15-SH-N30 N30-SH-N30 NN NN-NN-NN N15 N30 N30-N30-N30 SL SL-SL-SL SH N15 NN N30 NN N15 NN N15 N30 NN N15 NN N15 N30 R N15 N30 N15 SL N30 N15 SH N30 NN NN N15 N30 N30 SL SL SH NN N30 SL NN N30 SL 2.3 Test procedure Also shown in Fig. 2 are the half-cell potential measuring points for the steel bars in the vertical-jointed specimens. Measurements at these points were made using a reference electrode of saturated silver chloride through the 20mm concrete cover at intervals of 100mm and at the joints. The polarisation resistance of the steel bars and the electrical resistivity of the cover concrete were measured by applying a double rectangular pulse at a voltage of ±2~20mVp-p and at frequencies of 0.1Hz and 800Hz. A copper plate 100mm in width and 800mm in length was placed in close contact with the cover concrete and used as the counter electrode. The reference electrode, consisting of saturated silver chloride, was attached to the side of the specimen at the bar midpoint in the longitudinal direction. These measurements were made at the ages of 3, 5, 7, and 14 days, and thereafter every one or two weeks. The polarisation resistance of the steel bars was also measured at the age of 160 days using an AC impedance Cable 400 300 30 40 30 20 10 20 20 10 20 Placed from this side T part B part D10 Fig. 3 Horizontal-jointed specimen (unit: mm) - 107 - Table 4 Horizontal-jointed specimens Part T N30-SL N30-SH N30-NN NN N30 N30 B SL SH NN NN N30 Counter electrode 8 40 45 106 Fig. 4 Double-disk counter electrode (unit: mm) 0.03 0.02 0.01 0 R part C part L part N15-NN-N15 N15-NN-N30 N30-NN-N30 NN-SL-N15 N15-SL-N15 NN-SL-N30 N15-SL-N30 N30-SL-N30 NN-SH-N15 N15-SH-N15 NN-SH-N30 N15-SH-N30 N30-SH-N30 NN NN-NN-NN N15 N30 N30-N30-N30 SL SL-SL-SL SH Reference electrode Corrosion loss of steel bar (g/cm2) Guard counter electrode Repaired Repaired with NN with SL Repaired with SH For investigation of influence of joints method with a voltage of ±1~10mV p-p and a Fig. 5 Corrosion loss of steel bars frequency ranging from 10mHz to 10Hz at the (vertical-jointed specimens) points shown in Fig. 2 through the 20mm concrete cover. The counter electrode used for the AC impedance method was a double-disk [10] consisting of a main centre disk 40mm in diameter and an enclosing guard disk 108mm in diameter, as shown in Fig. 4. Polarisation resistance in this case was calculated only from the current between the steel bar and the main centre counter-disk. In addition to the measurements carried out with the reference electrode attached to the centre of the specimen, polarisation resistance was measured using the double-pulse method with the reference electrode attached to the left part or to the right part of the specimen denoted by (O) in Fig. 2. In these measurements, a copper plate measuring 100mm in width and 800mm in length was used as the counter electrode. The four cables connected to the steel bars in the horizontal-jointed specimens were bound into a single bundle to allow macro-cell corrosion current to flow among the steel bars. Further, the macro-cell corrosion current flowing from the bottom bars to the top bars was measured with a amperemeter. One of each type of vertical- and horizontal-jointed specimens was broken up for removal of the steel bars at the age of 160 days. The state of steel corrosion of each steel bar was sketched and the corroded area on the surface was calculated. The corrosion loss of these steel bars was estimated according to a JCI method [8]. 3. CORROSION OF STEEL BARS Fig. 5 shows the average values of corrosion loss over the whole surface area of the two steel bars in each vertical-jointed specimen per unit surface area. Fig. 6 similarly shows the corrosion loss of the steel bars in each horizontal-jointed specimen per unit surface area. Fig. 7 shows macro-cell corrosion losses calculated from macro-cell current in the horizontal-jointed specimens. As can be seen from Fig. 6, uneven chloride ion distribution caused the formation of macro-cell corrosion circuit in the horizontal-jointed specimens. The results shown in Figs. 5 to 7 are discussed in detail in a previous report [9]. 4. POLARISATION AREA DEFINITION 4.1 Basic assumptions for simulation Assuming that iron is completely turned into divalent ions during the corrosion reaction, the following theoretical - 108 - 0.010 T part Calculated macro-cell corrosion loss of steel bar (g/cm2) Corrosion loss of steel bar (g/cm2) 0.03 B part 0.02 0.01 0 T part N30 N30 N30 NN B part -NN -SL -SH Repaired N30 0.009 T part 0.008 0.001 0 T part N30 N30 N30 NN B part -NN -SL -SH Repaired Not repaired B part N30 Not repaired Fig. 7 Calculated macro-cell corrosion loss of steel bars (horizontal-jointed specimens) Fig. 6 Corrosion loss of steel bars (horizontal-jointed specimens) correlation exists between corrosion loss and the polarisation resistance of the steel bars: G= M 2 Fa M 1 ∫ Icorr dt = K × 2 Fa × ∫ Rp dt Eq. (1) where: G : corrosion loss (g/cm2) M : atomic mass of iron (= 55.8) Fa : Faraday constant (= 96,500C) Icorr : corrosion current density per unit surface area of steel bar (A/cm2) Rp : polarisation resistance (Ωcm2) K : Stern-Geary constant (V) Using this relationship, the corrosion loss G can be calculated from the polarisation resistance Rp per unit surface area of steel bar if the Stern-Geary constant K is known. However, in order to obtain the polarisation resistance of steel bars embedded in concrete, the polarised area must be determined appropriately, taking into consideration the uneven flow of the polarising current into the steel bars. In order to determine the polarised area, the distributions of electric potential and current flow were simulated using a two-dimensional finite differential method under the following conditions with respect to both longitudinal and cross sections of the specimen being polarised. a. For the sake of simplicity, it was supposed that the concrete was evenly dense and that the distributions of electric potential u(x,y) in the model specimen satisfied the following Laplace equation: ∂ 2u ∂ 2u + =0 ∂x 2 ∂y 2 Eq. (2) b. The analysing models had the same dimensions as the vertical-jointed specimen, and one reinforcing steel bar 10mm in diameter and 700mm in length was embedded in the model with 20mm of concrete cover. c. Polarisations were made with both types of counter electrode mentioned above: one was a rectangular copper sheet covering the entire cover surface of the model, and the other was a double structure 40mm and 108mm in width with an 8mm hole. d. For the sake of simplicity, it was supposed that the potential of the counter electrode was equal to the half-cell potential of the steel bar, E0mV, and that the steel bar was polarised to (E0-10) mV, assuming - 109 - that each of them bore uniform electric potential in themselves respectively, with the potential difference between them being 10mV. e. It was supposed that current flowed from each nodal point in four directions: up, down, left and right. Each flow was through a resistor reflecting the electric resistivity of the concrete. Hence, current was calculated from the electric potential difference between adjacent nodal points, taking account these resistor values. f. It was supposed that the electric potential of the nodal points at the end of the analysing model that were not in contact with the counter electrode was equal to the electric potential of adjacent nodal points inside the specimen. g. Calculation of the electric potential was repeated until the electric potential of all the nodal points reached a state of convergence; that is, when the change in electric potential fell below 0.0001mV. In analysing the 100mm x 100mm lateral cross section, the distance between adjacent nodal points was set at 1mm. The actual electrical resistivity of the cover concrete between the steel bar and the rectangular counter electrode, as obtained in measurements of polarisation resistance in vertical-jointed specimens at the age of 160 days, ranged approximately from 20 to 60Ω. To calculate simply the resistivity between nodal points in the analysing model, it was assumed that a 100mm wide counter electrode lay beneath the bottom of the cover concrete 100mm in width and 20mm in height, while reinforcing steel plate 100mm in width was in contact with the top of the cover concrete, and that the cover concrete consisted of a grid of electrical resistors. Assuming that the resistivity of the concrete between the reinforcing steel plate and the counter electrode was 40Ω based on the actual results mentioned above, the resistivity R between each pair of nodal points was taken to be 200Ω (= 40Ω x (100mm / 1mm) ÷ (20mm / 1mm), where 100mm and 20mm respectively are the width and height of the cover concrete, and 1mm is the distance between nodal points). In analysing the 100mm x 800mm longitudinal section, the distance between adjacent nodal points was set at 2.5mm. As above, it was supposed that a 700mm wide reinforcing steel plate and a 700mm wide counter electrode were in contact with the top and bottom of the cover concrete 700mm in width and 20mm in height, and that the concrete consisted of a grid of resistors. In this case, the concrete resistivity R between each two nodal points was calculated as 1,400Ω (= 40Ω x (700mm / 2.5mm) ÷ (20mm / 2.5mm), where 700mm and 20mm respectively are the width and height of the cover concrete, and 2.5mm is the distance between nodal points). 4.2 Analysis of lateral cross section Figs. 8 (a)-(c) show potential distributions in the 100mm x 100mm lateral cross section of the analysing -6 -8 -8 -4 -8 -6 -4 -2 -2 -2 Counter electrode 100mm 100mm -6 100mm 100mm 100mm 100mm -2 -4 Counter electrode Guard counter electrode Counter electrode (b) (c) (a) Fig. 8 Electric potential distribution in lateral section (unit: mV): (a) with large rectangular counter electrode, (b) with double-disk counter electrode, and (c) with main electrode of double-disk counter electrode - 110 - 35.2µA (40.1%) 35.0µA (40.5%) 28.1µA (38.5%) 52.7µA (59.9%) 51.3µA (59.5%) 45.0µA (61.5%) (a) (b) (c) Fig. 9 Electric current distribution around steel bar in lateral section: (a) with large rectangular counter electrode, (b) with double-disk counter electrode, and (c) with main electrode of double-disk counter electrode model obtained by the analysis. Fig. 8 (a) illustrates the case where the counter electrode is 100mm wide, as used in the double-pulse method measurement. Fig. 8 (b) illustrates the case where the counter electrode has a double structure, as used in the AC impedance method (see Fig. 4). Fig. 8 (c) is a cross sectional illustration of another analysing model in which only the main counter electrode of the double-disk counter electrode is used for polarisation. (No actual measurements were carried out in this case.) Figs. 9 (a)-(c) are diagrams showing the current flows into the steel bars. The length and direction of each arrow represent the amount and direction of the current. As these diagrams make clear, the distribution of electric potential in the analysing model with the rectangular counter electrode is very similar to that of the model with the double structure counter electrode. The current flow distributions in the three analysing models are also similar to each other, with current flowing into the steel bar not only from the cover concrete side but also from the upper side. The ratio of current flowing into the steel bar from the upper side of the cross section to the entire current flow is as high as 40% in all cases (see Fig. 9). With respect to the model specimen with the double structure electrode, the current flowing from the main electrode accounts for 59.6% of all current from the counter electrode, including the guard electrode, almost matching the 59.5% (see Fig. 9 (b)) of current flowing into the steel bar from the cover concrete side relative to the entire current flow. Consequently, it is assumed that all current from the main counter electrode flows into the cover concrete side of the steel bar, and that only this side is polarised by the main counter electrode. Based on this assumption, one-half of the nominal circumference of the steel bar is used in calculating the polarised area of the steel bar in the case of specimens with the double-disk electrode. Regarding the analysing model with the large rectangular counter electrode that covers the entire surface of the specimen, the current flowing into the steel bar from the upper part of the analysing model is significant, and therefore the entire circumference of the steel bar is taken account in calculating the polarised area of the steel bar. With respect to the analysing model with only the main counter electrode of the double-disk, the ratio of the current flowing into the steel bar from the upper part of the specimen is 38.5%, as shown in Fig. 9 (c), almost the same as in the other two cases, although the width of the counter electrode is less. This implies that the guard electrode restrains current from scattering. 4.3 Analysis of longitudinal section Fig. 10 (a) shows the potential distribution in a longitudinal section of the analysing model with the 800mm long rectangular counter electrode while Fig. 10 (b) shows the model with the double structure counter electrode at the center of the model. As can be seen, the potential distributions in these two specimens differ from each other. Fig. 11 shows the intensity and direction of current in the vicinity of the double-disk electrode. Current from the main counter electrode flows up vertically into the steel bar, while the current from the guard electrode tends to diverge. - 111 - C L C L 800mm 100mm 800mm Counter electrode Guard counter electrode Counter electrode (a) (b) Fig. 10 Electric potential distribution in longitudinal section; (a) with large rectangular counter electrode, (b) with double-disk counter electrode Distance from centre of specimen (cm) 8 6 4 2 C L 0 2.0 1.5 1.0 0.5 0 Guard counter electrode Counter electrode Fig. 11 Electric potential and current distribution in longitudinal section around double-disk counter electrode Location of steel bar Current into steel bar or from counter electrode (µA) Distance from top surface of specimen (cm) Steel bar C L 2.0 33.3% 1.5 1.0 0.5 31.7% 0 40 30 20 10 0 Distance from centre of specimen (cm) Location of Location of double-disk rectangular electrode electrode Type of counter electrode Double-disk Rectangular Current into steel bar Current from counter electrode Fig. 12 shows the intensity of current flowing from or Fig. 12 Current flows out from the counter electrodes and into the steel bar in the longitudinal section into the nodal points which represent the counter electrode or steel bar. In the case of the double-disc counter electrode, 33.3% of all current originates from the main counter electrode. Meanwhile, the current flowing into the steel bar just above the main counter electrode including the center hole accounts for 31.7% of the current flowing into the whole surface area of the steel bar. Thus the intensity of current flowing out from the main counter electrode almost matches the intensity of current flowing into the steel bar just over the main counter electrode. Therefore, in conjunction with the assumption mentioned above with respect to the analysis of the lateral section, it can be considered that the polarised area of the steel bar is equal to half the surface area of the steel bar over the main counter electrode. In this study, the polarised area of the steel bar is calculated as 4cm x 3cm / 2 = 6cm2 , where 4cm is the diameter of the main counter electrode, and 3cm is the nominal circumference of the steel bar. It should be noted, however, that this result may lack precision, because it is obtained from two- dimensional analysis while the double-disk counter electrode is actually circular. On the other hand, in the case of the counter electrode measuring 800mm in length, the current intensity is distributed almost evenly along the steel bar, except for areas at its ends, as shown in Fig. 12. The ratio of current flowing into the steel bar from upper side of analysing model is only a few percent in the analysis of the longitudinal section. However, it was ascertained from analysis of the lateral section that a considerable amount of current does flow into the steel bar from the upper side of analysing model, and therefore it must be taken into consideration. Thus the polarized area of the steel bar in the specimen with the rectangular counter - 112 - Corrosion rate index of steel bar by AC impedance method (1/kΩ/cm2) 1 0.1 ● ● ●● ● ● ● ● ● ●● ●● ● ●● ●● ● ● ●● ●● ●●❍ ■ ■■ ■■■ ● **-SL-** ❍ SL (Vertical joint) 0.01 ❍ ❍ ❍ ❍ 0.01 ❍ 0.1 ■■ ■■ ■■ ■■ ■ ■ ■■ ■ ■ ■ ■■ ■ ✩ ✩ ★★ ★ ✩ ★ ★✩ ★ ✩ ✩✩ ★★ ★ ★ ✩ ★ ★★★ ★ ★ ★✩ ■ **-SH-** ❏ SH (Vertical joint) ✩ ✩ ★ **-NN-**, ✩ NN, N15, N30 (Vertical joint) ■ ❏❏■ ✩ ✩✩ ✩ ✩ 1 0.01 0.1 0.1 1 0.01 Corrosion rate index of steel bar by rectangular pulse method (1/kΩ/cm2) 1 Fig. 13 Relationships between corrosion rate indexes by the two methods electrode was considered to be 70cm x 3cm = 210cm2, where 70cm is the length of the steel bar, and 3cm is the nominal circumference of the steel bar. 5. COMPARISON OF POLARISATION RESISTANCE MEASURED BY TWO METHODS 5.1 Estimation of corrosion rate Using the polarised areas thus obtained, the polarisation resistance and corrosion rate index can be calculated in accordance with Eq. (1). In this study, the reciprocal of the polarisation resistance, 1/Rp (1/Ω/cm 2), is defined as the corrosion rate index, because it is proportional to the corrosion current density (which corresponds to the corrosion rate). With the AC impedance method, it was difficult to determine the exact polarisation resistance from the incomplete circle obtained in the complex-plane presentation when the corrosion rate was very low. Since hardly any corrosion has occurred in a steel bar with a corrosion rate index under 0.01 (1/Ω/cm2), it is safe to regard the corrosion rate index as 0.01 (1/Ω/cm2) in such cases, if 1/ Rp < 0.01 (1/Ω/cm2 ). The corrosion rate indexes obtained by the double-pulse method and the AC impedance method are plotted in Fig. 13. As can be seen, they differ greatly from each other. The reason for these large differences is that although the polarisation resistance distribution in the vertical-joint specimens is non-uniform because of the uneven chloride concentration, this was not taken into account in the analysis of polarisation area in the previous section. In this section, the effects of polarisation resistance will also be taken into account so as to obtain more precise distributions of electric potential and current in the specimens. 5.2 Simulation for determining effect of polarisation resistance The following condition was added to a~g listed in the section 4.1 above. h. Left and right parts of the analysing model measuring 250mm each from either end consist of chloride contaminated concrete, while the 300mm long central part consists of sound concrete. Specimen N30-SH-N30, which conforms to this condition, was used in analysing the potential and current distributions in a longitudinal section of the analysing model under polarisation. The distance between nodal points representing concrete and the steel bar was set at 2.5mm. The electrical resistivity of the cover concrete between the steel bar and the large rectangular counter electrode of vertical- jointed specimen N30 was measured as 40Ω by the double-pulse method. Based on this value, the resistance between nodal points in the left and right parts of the model, consisting of mixture N30, was calculated as R1=1,400Ω as in the analysis in the - 113 - previous section. As for the resistance between nodal points representing concrete in the central part of the model, this was calculated as R2=1.5R1 because the electrical resistivity of the cover concrete in vertical-jointed specimen SH was 60Ω. Table 5 Resistivity between nodal points Specimen N30-SH-N30 Part L&R C Electrical resistivity (Ω) R 1.5R Current into steel bar or from counter electrode (µA) 1 1 Furthermore, additional nodal points were allotted to the interface between the concrete and the steel bar, and the electrical Polarization 4R1 13R1 resistivity between these points and points in the neighboring resistance (Ω) concrete was treated as the polarisation resistance. The polarisation resistance of the steel bar in the C Location of steel bar L left and right parts of specimen N30-SH-N30 obtained by actual measurements using the AC 1.6 impedance method was about 2,000Ωcm2. Based on this value, the resistivity between nodal points 1.2 representing polarisation resistance and nodal 31.8% points in the neighboring concrete was calculated with sound 0.8 as Rp1=5,333Ω (=2,000Ωcm2 x (1cm ÷ 2.5mm) ÷ 36.2% Cl1.5cm (= one-half of the nominal circumference of the steel bar)) ≈ 4R1 . As for the central part of 0.4 the model, the resistivity was calculated as Rp2 ≈ 31.1% 27.8% 33.4% 13R1 , based on the measured value, 7,000Ωcm2, 0 of polarisation resistance in the central part of 40 30 20 10 0 specimen N30-SH-30. Distance from centre of specimen (cm) Location of rectangular electrode 5.3 Polarisation behaviour of steel bar It was supposed that the steel bar uniformly polarises to (E0 -10)mV when polarised by an external voltage source, because the potential of the steel bar evens out although the half-cell potential is distributed unevenly along the reinforcing steel. The concrete resistivity and polarisation resistance used for calculation by a finite differential method are as shown in Table 5. Location of double-disk electrode Type of counter electrode Double-disk Rectangular Current into steel bar Current from counter electrode Fig. 14 Distributions of current flows out from the counter electrodes and into the steel bar considering the effect of polarization resistance Fig. 14 shows the calculated current distributions flowing from the counter electrode and into the steel bar for three cases: one using the large rectangular counter electrode, and two using the double-disk electrode located to the left or in the centre. In the case with the rectangular counter electrode, less current flowed into the steel bar in the central higher resistivity and polarisation resistance section than in the left part, where the chloride-contaminated concrete was. Moreover, the intensity of current flowing into steel bar was smaller in all three cases than shown in Fig. 12, where the effect of polarisation resistance was not taken into account, despite the use of an identical value of electric resistivity for chloride-contaminated concrete. This difference is attributable to the effect of the polarisation resistance, which was larger than the concrete resistivity. The effect of polarisation resistance is considered to be even more significant in the part consisting of sound concrete, where the polarisation resistance of the steel bar was relatively larger. Accordingly, it is assumed that the polarisation resistance should be taken into consideration in order to obtain more precise determinations of the electric potential distribution in a specimen. With the 800mm long counter electrode, current flowing from the upper side of the specimen into the steel bar was negligible in the analysis of longitudinal section. Thus, the entire model specimen can be treated as an electrical circuit consisting of a resistor R' representing the concrete resistivity and a polarisation resistance Rp' connected in series. The total amount of current flowing into all nodal points in the steel bar was 68.6µA. Hence, Rp'=E ÷ I -R'=10mV ÷ 68.6µA - 40Ω (or 60Ω) = 106Ω (or 86Ω). In turn, the polarisation resistance Rp - 114 - between the nodal points was calculated as follows: Rp=106Ω (or 86Ω) x (steel surface area on the cover concrete side 52.5cm2) ≈5,600Ωcm 2 (or 4,500Ωcm 2). These values are smaller than 7,000Ωcm2, which is the assumed polarisation resistance of the sound concrete part, and are 2.5 to 2.8 times larger than 2,000Ωcm2, which is the polarisation resistance of the chloride-contaminated part. 0.5 -iZ" (kΩ) 10Hz ❍ ❍ ❍ ❍ ❍ ❍ ❍ ❍ 0.01Hz ❍ ▲❍▲ N30-SH-N30 ❍ ◆◆▲◆▲◆ ◆◆ ▲ ❍ ▲▲ ▲ ❍ ◆ ◆ ◆ ◆ ◆◆◆ ▲ ▲ ▲ ▲ ▲ 0 0 This leads to a conclusion that, when evaluating the deterioration of an RC member subjected to macro-cell corrosion where a corroded area and a sound area coexist, the polarisation resistance cannot be determined precisely if a large rectangular counter electrode is used. 0.01Hz 0.1Hz 100mHz 0.1Hz 0.5 Z' (k Ω) 1 ◆ 100mm ❍ 400mm ▲ 700mm Fig. 15 Examples of complex-plane presentation of electrochemical proprieties of steel bars obtained in this study It should be noted, however, that this study is based on the assumption that the electric potential distribution when the bar is in a polarised state is uniform in the longitudinal direction of the steel bar, and that the actual electrical behaviour of the steel bar being polarised is not known. In fact, the actual values of polarisation resistance measured by the double-pulse method with the reference electrode on the sound part differed from the results when the reference electrode was on the chloridecontaminated part. Furthermore, it has been reported that the polarisation resistance of the cathode region in a macro-cell corrosion circuit is small even in the absence of corrosion [10]. Thus, further investigation will be necessary to clarify the electrochemical behaviour of reinforcing steel bars in concrete suffering macrocell corrosion. In the case in which the double structure counter electrode was placed at the centre of the specimen, the current flowing out from the main counter electrode accounted for 31.8% of the total current from the entire counter electrode, while the ratio of the current flowing into the steel bar just above the main counter electrode (including the centre hole) to the total current flow into the steel bar was 31.1%. In the case in which the counter electrode was placed on the left part of the specimen, these ratios were 36.2% and 33.4%, respectively. From these results, it can be concluded that almost all of the current flowing out from the main counter electrode flows into the part of the steel bar just above it. In summary, polarisation resistance can be measured more precisely by the AC impedance method using a double-disk counter electrode. 6. STUDY OF CONSTANT K As mentioned in Section 4, in order to calculate the amount of corrosion loss from the polarisation resistance, constant K must be given. The measured polarisation resistance of the anode region is affected not only by the anode reaction of the macrocell circuit but also by both the anode and cathode reactions of micro-cell corrosion. Moreover, the polarisation resistance obtained with the use of the rectangular counter electrode is influenced by the macrocell cathode reaction. However, it is impossible in - 115 - Corrosion loss of steel bar (g/cm2) Furthermore, as is obvious from the examples of steel bar electrochemical properties in complex-plane presentation as shown in Fig. 15, the polarisation resistance obtained by the double-pulse method at two frequencies (0.1 and 800Hz in this study) differs considerably from the result obtained by the AC impedance method, particularly when the polarisation resistance is large. 0.025 0.020 0.015 0.010 0.005 0 ● ❍ ❍ ❍ ● ● ●● ❍ ● ● ●● ● ● ● with two or three ●● concrete mixtures ❍❍ ● with one concrete ❍ ● mixture ● ● ❍ ❍ ❍● ❍ ❍ ❍●● ❍● 0 0.2 0.4 0.6 0.8 1.0 2 1 M ) (g/V/cm ×∫ dt 2Fa Rp Fig. 16 Relationship between corrosion loss and corrosion rate index by double-pulse method Specimen Ratio **-SL-N30 6.47 (2.15) **-SH-N30 5.31 (1.76) **-NN-N30 5.75 (1.91) N30, N30-N30-N30 3.01 (1.00) Corrosion loss of steel bar (g/cm2) Table 6 Ratios of corrosion rate index in verticaljointed specimens (Results by AC impedance method/those by double-pulse method; Values in brackets are normalized ratios divided by the ratio for specimens N30 and N30-N30-N30) 0.025 ● ● ● 0.020 ●●● ● ● ●●● ● ●● ● ● 0.015 0.010 ● 0.005 ● y = 0.0296x R =0.8776 0 0 ** =NN, N15,N30 0.2 0.4 0.6 0.8 1.0 M 1 2 dt (g/V/cm ) ×∫ ′ 2 Fa Rp Fig. 17 Relationship between corrosion loss and practice to precisely isolate these component effects corrosion rate index by double-pulse method from the measured polarisation resistance so as to modified by considering the results obtained obtain the micro-cell corrosion loss and macro-cell by AC impedance method corrosion loss independently. Further investigation needs to be carried out to clarify the implications of the physical and electrochemical properties of steel bars in macro-cell corrosion circuits. As for the possibility of estimating corrosion loss by the AC impedance method using a double-disk counter electrode, this is not practical, because it would require measurement of the polarisation resistance at a large number of points. With the above in view, the overall corrosion loss of the steel bar as a whole was calculated first from the polarisation resistance measured by the simple double-pulse method with the use of the large rectangular counter electrode. Fig. 16 shows the relationship between corrosion loss and integrated corrosion rate index up to the age of 160 days. This index is the reciprocal of polarisation resistance obtained by the double-pulse method using the large rectangular counter electrode multiplied by M/2Fa. The corrosion loss per unit surface area was obtained by dividing the total corrosion loss caused by both macro-cell corrosion and micro-cell corrosion with the surface area of the steel bar (210cm2). The gradient of this graph corresponds to constant K in Eq.(1). However, there are large variations in this gradient between specimens of different types. Specifically, constant K was 0.0566(V) in the case of jointed specimens with uneven chloride distribution, whereas it was 0.0252(V) in the case of specimens with an uniform chloride distribution. This difference is attributable to the use of a counter electrode covering the entire surface of the cover concrete, which results in both anode and cathode regions of the macro-cell being polarised together. Table 6, derived from Fig. 13, shows the ratios of corrosion rate index according to the AC impedance method to that according to the double-pulse method for specimens that include an N30 part at 160 days. As this shows, the results obtained by the two methods differed greatly, even in the case of specimens consisting only of N30 and considered to have an even chloride distribution in the longitudinal direction. The reasons for these large discrepancies are discussed here. First, the underside of the steel bar is more likely to corrode because of the formation of a water membrane caused by bleeding. Further, the lower part of the specimens was kept wet by water spraying in the experiments, leading to the formation of an anode on the lower half of the steel bar on the cover concrete side and an cathode on the upper half of the steel bar. Accordingly, the corrosion rate index obtained by the AC impedance method was larger than the mean value of corrosion of the entire circumference of the steel bar, because of use of the double-disk counter electrode with which only the lower half of the steel bar is polarised. The large difference between the two methods is also attributable to same degree to the difference in frequency used for measuring the polarisation resistance. Assuming that the corrosion rates are overestimated equally in all specimens when the double-disk counter electrode was used, the ratios shown in Table 6 can be normalised, as shown in brackets, by dividing by 3.01 - 116 - double-pulse method (rectangular electrode) AC impedance method (double-disk electrode) defining polarisation area Rp1 (Icorr1) defining polarisation area Rp2 (Icorr) ratio effect of circumferential distribution of corrosion corrosion loss nomalised ratio constant K Rp' (I corr') effect of macro-cell and applied frequency Fig. 18 Flow chart representing this study (the value obtained for specimens N30 and N30-N30-N30 with most even chloride distributions). As mentioned above, the overall polarisation resistance of a specimen with macro-cell corrosion measured with the large rectangular counter electrode was calculated to be 2.5 to 2.8 times larger than the polarisation resistance of the corroded area alone. The normalised ratios in Table 6 for the jointed specimens are about twice as large for the specimens consisting of N30 alone. This confirms, therefore, that in addition to the difference in frequency used for polarisation resistance measurements and the circumferentially uneven distribution of corrosion rate around the steel bar, the large difference between polarisation resistance values obtained by the two methods with the two different counter electrodes contributes to the uneven distribution of corrosion rate along the steel bar due to macro-cell corrosion. Based on the assumptions made here, the corrosion rate indexes in Fig. 16 are corrected by multiplying them with the normalised ratios shown in brackets in Table 6, and the results are re-plotted in Fig. 17. This figure shows only the results for specimens using mixture N30. As can be seen, the variations were reduced to an insignificant level, with the constant K being 0.0296(V). It is thus demonstrated that the "apparent" polarisation resistance obtained using the double-pulse method with the large rectangular counter electrode can be corrected to a more realistic value by integrating the results obtained using the AC impedance method with the doubledisk counter electrode. This means it is possible to predict corrosion loss more accurately from the polarisation resistance. The constant K obtained in this study also falls within the range 0.017 to 0.050(V), which has previously been reported as a reasonable range [11]. The procedure followed in this study is summarised in the form of a flow chart in Fig. 18. 7. CONCLUSION The results obtained in this study can be summarised as follows: (1) The current flowing upon polarisation flows into the steel bar largely into the side of the steel bar not facing the counter electrode, irrespective of the type of electrode. - 117 - (2) Where a double-disk counter electrode is used, the amount of current flowing out from the main counter electrode approximately corresponds to that flowing into the cover side of the steel bar. (3) The amount of corrosion can be calculated more precisely from the polarisation resistance by combining the measurements obtained using the double-pulse method with a large counter electrode and those obtained using the AC impedance method with a double-disk counter electrode. (4) The constant K in the Stern-Geary formula is obtained as 0.0296V in this study. The AC impedance method, which uses low frequencies for measurement, together with the double-disk counter electrode, which restricts diffusion of the polarisation current, gives results that accurately reflect the polarisation resistance of the steel bar. On the other hand, it entails time-consuming measurements at a large number of measuring points, and is not immediately applicable to the actual maintenance of RC structures. However, as demonstrated in this study, it can be used to advantage if combined with the more simple doublepulse method. For example, it can be used to add corrections to the results obtained by the double-pulse method with a large counter electrode, so as to obtain a more precise corrosion rate whenever necessary. It should be noted that the relationship between the polarisation resistance values obtained respectively by the two methods varies depending on the corrosion distribution, half cell potential, age of the concrete, and various other factors. Therefore, the electrochemical properties of a reinforcing steel bar suffering macro-cell corrosion should further be investigated, and the constant K in the Stern-Geary formula considered further. 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Reports, No. 68, pp. 42-47, 1997 (in Japanese) [11] JSCE Subcommittee for Studies on Steel Corrosion and Corrosion Protection in Concrete, "State of the art and future trends related to steel corrosion, corrosion protection and repair", Concrete Engineering Series, 1997 (in Japanese) - 118 -