Open Journal of Civil Engineering
Vol.3 No.2A(2013), Article ID:33039,8 pages DOI:10.4236/ojce.2013.32A001

Efficiency of Amino Alcohols as Corrosion Inhibitors in Reinforced Concrete

Ioannis Vyrides1, Eleni Rakanta2, Theodosia Zafeiropoulou2, George Batis2

1Department of Chemical Engineering and Chemical Technology, Imperial College, London, UK

2School of Chemical Engineering, National Technical University of Athens, Athens, Greece

Email: ioannis.vyrides@imperial.ac.uk, erakanta@central.ntua.gr, dia_zaf@mail.ntua.gr, batis@chemeng.ntua.gr

Copyright © 2013 Ioannis Vyrides et al. This is an open access artiQQcle distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

Received May 1, 2013; revised June 2, 2013; accepted June 10, 2013

Keywords: Steel Corrosion; Concrete Durability; Amino Alcohols; Corrosion Inhibitors; Cement Mortars

ABSTRACT

The objective of this paper is to investigate the behaviour of amino alcohol corrosion inhibitors when they are used in reinforced cement mortars either as admixtures in the cement paste or as coating applications on the surface of the rebars. The reinforced cement mortars were exposed to both partial and full immersion in 3.5 wt% NaCl solution. Electrochemical measurements such as half-cell potential and linear polarization technique, as well as weight loss of the embedded rebars were performed in order to obtain information on the corrosion behaviour of the reinforcing steel in cement mortar. Results demonstrate that the amino alcohol corrosion inhibitors offer protection against rebar corrosion in cement mortars.

1. Introduction

Under most conditions concrete provides a reliable protection against corrosion of reinforcing steel, however corrosion remains the most common cause of deterioration of reinforced concrete. In order for corrosion to occur, the presence of an electrolyte such as the aqueous phase in concrete is required. The final result of the corrosion process is the formation of a thick layer of rust which exerts sufficient tensile forces within the concrete to cause cracking of the concrete cover [1]. In an alkaline solution, such as the calcium hydroxide solution in wet cement, a protective oxide film is formed which covers the steel thus passivates it. Corrosion occurs when this protective film is impaired and oxygen is present [2]. Oxygen has the most detrimental effect; chloride is only the catalyst of the corrosion process. Oxygen binds the electrons originally associated with the iron atoms and it is the abstraction of these electrons which allows some iron atoms to dissolve as ferrous ions and then to preipitate as ferric oxides [3]. Without oxygen steel rebar will not corrode in alkaline water even with chloride present [4]. Moreover, the stability of the film depends on the maintenance of a certain minimum pH value above which access of oxygen will not cause corrosion. However, if the access of carbon dioxide reduces the pH to a value 10 or lower the film is impaired, the natural passivity of concrete is thus reduced and under such conditions any access of oxygen will cause corrosion [5]. The presence of chloride ions stimulates corrosion by raising the pH required to stabilize the passive film to a value which may exceed that of a saturated calcium hydroxide solution. The intrusion of chloride ions depends on the porosity and permeability of the concrete material [1]. As the reinforcing steel corrodes, the ferric oxides occupy a volume three to four times greater than the initial reinforcing steel resulting in bursting stresses that crack and spall the concrete cover.

Corrosion inhibitors have been used successfully in steel pipelines, tanks, etc., for many decades. Their use as admixtures to concrete, however, is more recent and more limited. This reluctance is due to the fact that they could not be changed if found to be ineffective, replenished if found to be consumed, or removed if found to have deleterious effects [6]. The flexibility of corrosion inhibitors with regard to dosage and their compatibility with all aspects of construction and operation of structures makes them useful for protection against corrosion. Any inhibitor should have good solubility characteristics and rapidly saturate the corroding surface. Also the physical and durability properties of concrete should not be adversely affected [7].

Amino alcohol corrosion inhibitors control corrosion by attacking the cathodic activity, blocking sites where oxygen picks up electrons and is reduced to hydroxyl ion. Also inhibition of corrosion occurs through a mechanism where by amino alcohols displaces chloride ion and forms a durable passivating film. In this view, although the amino alcohols adsorb on non-corroding sites which may seem more cathodic than anodic, they can just as easily be said to adsorb on potentially anodic sites as well [3]. Ormellese et al. [8] suggest that organic corrosion inhibitors reduce the ingress of chloride by filling concrete pores and blocking the porosity of concrete by the formation of complex compounds. Thus, the value of chlorides reaching to the steel surface is significantly less so the corrosion is inhibited. Several studies of the corrosion inhibition effect of amino alcohols for steel report their performance as a function of concentration and pH in saline solutions [9-11]. In particular, the colorimetric and electrochemical study of 2-ethylaminoethanol observed that the molecules do not provide a protective film in neutral media, but rather enhance the corrosion rate. At pH > 10.3 a protective layer of metalhydroxide is formed, which, however, is not completely insoluble. This hydroxide film can be stabilized by adsorption of 2-ethylaminoethanol on the hydroxylated surface and presumably by chelation of the ferrous ion [12,13].

An amino alcohol corrosion inhibitors can be mixed within the fresh concrete (admixture inhibitor), or can be applied on the surface of existing concrete structures. In this study the contribution of both types’ admixtured and spraying applied corrosion inhibitors was investigated. Moreover, when the corrosion action was under progress, the addition of spaying amino alcohol inhibitor was tested. Furthermore, attention was given to the condition that the specimens were exposed, partially immersed in a 3.5 wt% NaCl solution and in a saturated 3.5 wt% NaCl solution.

2. Experimental

2.1. Materials

To achieve the objectives of this investigation cylindrical reinforced cement mortar specimen were constructed. The test specimens were prepared with cement, sand and water in ratio 1:3:0.6. The cement type used was Greek Portland cement and its chemical analysis is shown in Table 1 and the water was tap from Athens water supply network appropriate for preparing specimens according to ELOT 452 [14]. Cylindrical steel rebars of type B500C with dimensions of 12 mm in diameter and 10 mm high were used for the reinforced test specimens. The rebars meet Greek specifications of Hellenic Organization for Standardization, ELOT 1421-3 [15].

Fabrication of the steel for the test specimens simply involved cutting to the consistent length of 100 mm. The test specimens considered for the present study were cylindrical 100 mm in height and 40 mm in diameter. Each contained one steel rebar in the position shown in Figure 1. The cement mortar constituents were mixed in a mortar mixer for approximately 5 minutes till a uniform consistency was achieved. The molds were filled with mortar and vibrated for consolidation using a vibrating table. Copper wire cables were connected to the steel bar for electrochemical measurements. Prior to the preparation, the steel surface was cleaned according to the ISO/DIS 8407.3 Standard [16]. In particular the surface of the steel bars was washed with water and then immersed in strong solution of HCl with organic corrosion inhibitor for 15 min, washed with water and finally washed thoroughly with distilled water to eliminate traces of the corrosion inhibitor and chloride ions. Following that, the surface was cleaned with alcohol and acetone and finally weighed to accuracy of 0.1 mg. Thereafter, the bars were placed in cylindrical moulds where the mortar was cast and stored at ambient conditions in the laboratory for 24 hours. After being demolded, the specimens were placed in water in curing room (RH > 98%, T = 20˚C ± 1.5˚C) for 24 hours and then kept for an additional 7 days at ambient temperature in a laboratory environment to stabilize internal humidity, followed by insulation with epoxy resin of the region shown in Figure 1. The experimental duration of this study was 200 days.

For the purpose of this work 4 series of specimens were partially immersed in a 3.5 wt% NaCl solution and 2 series remained fully immersed in a 3.5 wt% NaCl solution. The addition of the corrosion inhibitor was achieved according to the instruction given by the manufacturer. The analytical series tested in this work are presented in Table 2.

In Table 2 test series that were partially immersed in

Table 1. Chemical analysis of OPC.

Figure 1. Schematic representation of a reinforced mortar specimen.

Table 2. Test series used in the present study.

the solution are indicated with “A” whereas full immersion is characterized by using the letter “B” in the code name of the series. Furthermore, “RS” stands for reference specimens and “DS” for data specimens where the inhibitor is either sprayed or as an admixture. Finally, the numbers on the code names show the time interval before the corrosion inhibitor was sprayed on the surface of the specimens.

The corrosion inhibitor used in this study was based on partially neutralized amino alcohols which is an adsorption inhibitor. Specifically, N-N-diethylaminoethanol is absorbed onto the steel surface forming organic films which protect both the anodic and cathodic sections of the rebar [17]. Besides, the transportation of surface applying amino alcohols inhibitor into concrete depends on the concrete quality, the porosity and the humidity [18, 19].

2.2. Methods

The following methods were employed in this study for the evaluation of the protective action of coatings against corrosion:

a) Half-Cell Potential Measurements versus Time:

During the exposure of the specimens in the corrosive environment the half-cell potential of steel rebars was periodically measured versus a saturated calomel electrode (SCE) and a high impedance voltmeter. According to ASTM C876 Standard [20] corrosion potentials (Ecorr) more negative than −350 mV, with respect to SCE, indicate greater than 90% probability of active reinforcement corrosion. Values less negative than −200 mV SCE indicate a probability of corrosion below 5%, while those falling between −200 and −350 mV SCE indicate uncertainty of corrosion.

b) Linear Polarization Technique (LPR):

The corrosion of reinforced concrete is an electrochemical process. For this reason it is possible to obtain the information on the state of corrosion with the application of external electrical stimulation and measurement of the subsequent electrical response. Hence, the linear polarization resistance method was used to measure corrosion rates over various time periods Although the corrosion of steel in concrete is an electrochemical process and does not obey to Ohm’s law it has been shown that Ohms’s law will be approximately true if polarization applied to the steel does not exceed ±20 mV. Thus the resulting current is linearly plotted versus potential. The test setup for the linear polarization resistance techniques (LPR) included a EG&G Model 263 Potensiostat/Galvanostat. Additionally the computer program Softcorr III developed by EG&G Princeton Research was used for applying the potential scan, analyzing the parameters of icorr and Rp. The linear polarization resistance of steel reinforcement was evaluated at a scan rate of 0.15 mV/s. The corrosion current density was measured using the DC linear polarization resistance method. The resistance to polarization Rp (Ω·cm2) was determined by conducting a linear polarization scan in the range of 20 mV of the open circuit potential and the corrosion current density icorr [μA/cm2] was then calculated using the Stern-Geary equation:

(1)

where B is a constant based on the anodic and cathodic Tafel constants where a value of 26 mV has been adopted for active corroding steel bars and 52 mV for passive conditions and Α (cm2) is the exposed area of the rebar.

This method has been considered to be a relatively simple and reliable technique to assess the rate of reinforcement corrosion in cement mortars. The corrosion level is considered negligible when icorr is less than 0.1 μA/cm2, it is considered low in the range between 0.1 and 0.5, moderate from 0.5 to 1 and high for values higher than 1 μA/cm2 [21].

c) Weight Loss Measurements of Steel Rebars:

The corrosion rate of reinforcing steel was determined by measuring the mass loss of the steel bars in different times. The steel bars were cleaned from any corrosion products according to the ISO/DIS 8407.3 Standard [16] and were weighted to accuracy of 0.1mg. The average mass loss was calculated from the difference between the initial and the final weight of each steel bar.

3. Results and Discussion

3.1. Half-Cell Potential Measurements

Half-cell potentials of the specimens that were partially immersed in 3.5 wt% NaCl solution for 200 days are shown in Figure 2. In the cement mortar specimens without corrosion inhibitor (RSA) the corrosion poten-

Figure 2. Half-cell potential measurements versus time in cement mortar specimens partially immersed in 3.5 wt% NaCl solution.

tials were more negative than −300 mV SCE right from the initial stages of exposure and −620 mV SCE after 200 days of exposure. The half-cell potentials of specimens which an amino alcohol inhibitor was used as an admixture (DSA) show an increase of the potential values in the anodic direction during the first 90 days, attaining values around −195 mV. After that the potential slightly decays to values around −270 mV and finally reaches steady values around −170 mV indicating the passivity of reinforcing steel even after 200 days of exposure. The spraying applied amino alcohol corrosion inhibitor (DSA14) during the first 125 days of exposure remains practically constant with the time at values around −420 mV. However, after the first 125 days the half-cell potentials values are higher than the initial ones by −100 mV and remain in that value (−328 mV) until the end of the experiment. According to ASTM this is an indication of uncertainty of corrosion [20]. In the cement mortar specimens (DSA3M) that an amino alcohol inhibitor was applying by spraying at specimens’ surface after 3 months the potential sharply decays to values around −620 mV. This decay of potential suggests loss of passivation. After the surface applying inhibitors at the 90th day there is a gradual increase in the half-cell potential values followed by stabilization at around −450 mV.

Despite the fact that these values are an indication of 90% probability of active reinforcement corrosion [20], the addition of the amino alcohol spaying inhibitor shows its effect on the cement mortar samples in the first days of the applying by significantly increase of the half-cell potential. The half-cell potentials results show that the effect of the inhibitor addition on the corrosion rate of reinforcing steel is dependent on the method of application. Thus, when the inhibitor is sprayed on specimens the corrosion inhibition is delayed comparatively to the situation in which the inhibitor is added into the cement mortar mixture.       

Figure 3 depicts the half-cell potentials of control speci-mens and specimens that an amino alcohol inhibitor was used as an admixture. Both types were fully immersed in 3.5% wt. NaCl solution for 200 days. There is a tendency for the decreasing of potential from values range of −100: −200 mV to values of −600 mV for the both types of specimens.

The decrease in the specimens with amino alcohol corrosion inhibitor was more gradual compared to the rapid decrease of the specimens without corrosion inhibitor during the period 0 - 150 days. However, this is a very slightly indication of the better performance of the corrosion inhibitor because these values are below −350 mV. The amino alcohol corrosion inhibitor may displace chloride ion to create a passive film so the anodic reaction of iron are lower compared to the specimens without inhibitors during this period (0 - 150 days) [20]. Despite this dramatic decrease in the values of the half-cell potential for the both specimens probably the generation of ferrous oxide did not take place due to the absence of oxygen (fully immersed in 3.5% wt. NaCl solution). As a consequence, without oxygen caused by water saturation, iron will dissolve in excess of electron but will remain stable in solution as there is no compensating cathodic reaction so the potential is very negative. This shows the weakness of potential measurements in an environment without oxygen [22].

3.2. Linear Polarization Measurements

In previous works electrochemical experiments pointed out that amino alcohol corrosion inhibitor increased the corrosion resistance of steel samples immersed in solution simulating the concrete pore solution contaminated with chloride [23-30]. In fact, X-ray photoelectron spectroscopy analysis revealed that the inhibitors form a film containing nitrogen species, which seem to complex the

Figure 3. Half-cell potential measurements versus time in cement mortar specimens fully immersed in 3.5 wt% NaCl solution.

chloride ions [23]. Previous different electrochemical measurements also showed that the amino alcohol inhibitors can reduce the corrosion rate even when steel is under corrosion attack [23-25]. Considering these results, the present work studies the ability of amino alcohol inhibitor to resist corrosion by measuring the corrosion current density in 3.5 wt% NaCl solution.

Figure 4 depicts the corrosion current density icorr on rebars of the cement mortar specimens that were partially immersed in 3.5 wt% NaCl solution for 200 days. As it is shown icorr values of the rebars without inhibitor increases with the exposure time from 2.2 μA/cm2 to 4.5 μA/cm2, values typical of high corrosion levels. It is also depicted that the usage of the corrosion inhibitor as an admixture (DSA) resulted in lower icorr values (0.45 μA/cm2) which are indicative of low corrosion activity. For the specimens that the corrosion inhibitor was sprayed on the surface (DSA14), moderate corrosion values were achieved (0.78 μA/cm2).

These results show that the performance of the admixture amino alcohol inhibitor was better compared to the sprayed corrosion inhibitor. The admixture corrosion inhibitor occurs homogeneously inside the cement paste and as a result it is easier to generate the passive film to the surface of steel. Moreover, it is more effective in reducing the porosity of the cement paste by forming complex compounds with chlorides [8]. In contrast, the behavior of the sprayed corrosion inhibitor depends on the values of the diffusion coefficients of the inhibitor and the diffusion coefficient of chlorides.

The behavior of the sample that was kept 3 months in the corrosive environment with no inhibitor (DSA3M) in order to develop stronger corrosion activity and was afterwards sprayed with the inhibitor must be noted.

During the first period icorr values slightly decrease from 3.2 μA/cm2 to 3.1 μA/cm2. After the inhibitor application in the surface of the specimen icorr decreases to 0.86 μA/cm2. This behaviour clearly shows that this inhibitor is able to decrease the corrosion rate of the steel even when it is initially under localized corrosion attack.

Figure 4. Corrosion current density versus time in cement mortar specimens partially immersed in 3.5 wt% NaCl solution.

This points out that the amino alcohol corrosion inhibitor is capable of diffusing through the cement and inhibiting the electrochemical corrosion process by passivation of the anodic and cathodic spots. This is an indication that a barrier layer is built up in the surface of the steel since icorr values remain constant under the corrosive environment. Despite the significant reduction in the corrosion activity after the addition of the amino alcohol inhibitor, corrosion was not fully eliminated and a moderate level was achieved (0.86 μA/cm2).

Results of the linear polarization testing for control specimens and specimens with the corrosion inhibitor as an admixture that were fully immersed in 3.5% wt. NaCl solution for 200 days are presented in Figure 5.

Control specimens slightly decrease icorr values from 0.87 μA/cm2 to 0.82 μA/cm2 after 200 days of exposure. When using the amino alcohol inhibitor as an admixture, icorr values are reduced from 0.7782 μA/cm2 to 0.6882 μA/cm2. These values are lower than those obtained in the partially immersed specimens due to the saturated environment and to the absence of oxygen that restrains the corrosion process. This difference, after 200 days, is more significant for the control specimens. In fact, icorr for the control specimens when are partially immersed is approximately 4.5 μA/cm2 whereas in the case of full immersion is 0.8 μA/cm2. However, the performance of the admixture inhibitor is slightly better under partially immersed solution compared to the performance under saturated environment.

Even under saline saturate environment the action of corrosion amino alcohol inhibitor is slightly better compared to the sample without inhibitor. This can be contributed to the formation of a complex compound (passive film) among the amino alcohol inhibitor, the chloride, the cement materials and the steel. As a result the anodic reaction of iron is in less extend. However, oxygen, a main parameter for the induced corrosion in the system is absent. Thus, the electrochemical corrosion process is not generated.

Figure 5. Corrosion current density versus time in cement mortar specimens fully immersed in 3.5 wt% NaCl solution.

3.3. Weight Loss Measurements of Corroded Steel Rebars

At the end of the exposure period the cement mortar specimens were carefully broken and the embedded steel bars were recovered. They were visually examined to assess their corrosion state qualitatively and then cleaned according to the ISO/DIS 8407.3 Standard [16] in an aqueous solution of hydrochloric acid containing a proprietary pickling restrainer which served to dissolve the corrosion products and cementitious debris without causing significant attack on the underlying steel.

Mass loss of all specimens that were partially immersed in the corrosive environment was obtained at 135, 165 and 200 days and the results are shown in Figure 6. Control specimens demonstrate higher mass loss values at all intervals which shows that in the absence of inhibitors the corrosion activity strongly increases with time, leading to higher mass loss. The specimens with addition of the corrosion inhibitor as admixture demonstrate a slightly increase of the mass loss versus time. The mean value of the mass loss at 200 days for the aforementioned specimens is 40 mg which is approximately similar to the value indicated by the specimens where the corrosion inhibitor was sprayed dafter 14 days.

The specimens that were sprayed with the corrosion inhibitor after 3 months of exposure attained a slow increase in the mass loss which is 44 mg after 200 days. These results show the inhibitory effects of amino alcohol corrosion inhibitor in reducing the corrosion even when it is under progress. In the case of the specimens that were fully immersed in 3.5 wt% NaCl solution both types of specimens showed similar trend in mass loss values and specifically after 200 days mas loss was 28.6 mg and 27.5 mg for control specimens and inhibitor amino alcohol admixture respectively as demonstrated in Figure 7.

It should be noted that the difference in the mass loss

Figure 6. Mass loss of reinforcing steel bars time dependence partially immersed in 3.5 wt% NaCl solution.

Figure 7. Mass loss of reinforcing steel bars time dependence fully immersed in 3.5 wt% NaCl solution.

of the fully immersed specimens in 3.5 wt% NaCl solution both in control and in treated with corrosion inhibittor cement mortar specimens is not significantly important. This fact suggests that the absence of oxygen in the pores of cement mortar mass reduces the corrosion rates of steel reinforcements. This behaviour is in disagreement with the half-cell potential results which showed very negative results due to the absent of cathodic reaction. In fact, the specimens with the amino alcohol inhibitor show slightly more efficient in chloride attack than the control specimens. This difference can be explained as a result of inhibition of the anodic reaction on the steel due to the form of passive film by the amino alcohol. This could be an indication that the creation of the passive film could be independent on the presence of oxygen.

Moreover, the mass loss of the control specimens under partial immersed NaCl solution is dramatically higher compared with the mass loss at saturate NaCl solution. These results are in line with the results of the linear polarization analysis. In addition the mass loss of admixture inhibitor is also higher under partial immersed NaCl solution compared with the saturated environment. However, the results of the corrosion rate at linear polarization analysis showed slightly better performance of the admixture inhibitor at partially immersed NaCl solution.

The absent of oxygen in the saturated environment contribute to the elimination of the cathodic reaction so there is a possibility of a slightly wrong estimation of the corrosion current density.

4. Conclusions

The following conclusions can be drawn from this investigation:

1) The amino alcohol types of corrosion inhibitors studied in this work (admixture and sprayed corrosion inhibitor) reduce the corrosion rate of the reinforcing steel when the specimens were partially immersed in a 3.5 wt% NaCl solution. In fact, according to the results of half-cell potential and linear polarization, admixture type is slightly more efficient in the cement mortar specimens than the surface applied amino alcohols corrosion inhibitors.

2) In cement mortar specimens fully immersed in 3.5 wt% NaCl both control and admixture amino alcohol treated specimens demonstrate low corrosion activity because pores of cement mortar are filled with water and oxygen cannot penetrate.

3) There is a decrease of the corrosion activity on steel in the addition of the amino alcohol spaying inhibitor in cement mortar samples even when the cement mortar specimens are initially under localized corrosion attack (partially immersed in a 3.5 wt% NaCl).

From the above, the goal of this paper to test the inhibitory action of the amino alcohol corrosion inhibitor under corrosive environments was achieved.

However, further research needs to be held regarding the mechanism that the amino alcohol corrosion inhibitor acts under the presence of high chloride concentration which diffuses in the cement. Moreover, the characteristic of the passive layer that is created by the inhibitor on the steel surface under different corrosive environment (partially corrosive environment or saturated environment) and under different addition method of the inhibitor (as admixture or sprayed) can be investigated.

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