Influence of flow on the corrosion inhibition of St52-3 type steel by potassium hydrogen-phosphate
Introduction
The seawater with approximately 3.5% salinity is used by many industries such as shipping, offshore oil and gas production, power plants and coastal industrial plants. The main use of seawater is for cooling purposes but it is also used for fire-fighting, oil-field water injection and for desalination plants [1], [2], [3], [4], [5]. Corrosion and corrosion inhibition of iron and steels in NaCl containing solutions have fundamental academic and industrial importance.
Phosphorous compounds are commonly used to inhibit metals corrosion in aqueous electrolytes. Their use is relatively risk free due to their low toxicity [6], [7], [8]. For example, sodium monofluorophosphate (Na2PO3F) [9], calcium monoflourophosphate (CaPO3F) [10], combination of zinc phosphate/molybdate (Actirox) and calcium ion exchange silica (Shieldex) [11] and phosphate anions [12], [13] have been used to decrease the corrosion rate of different metals in aqueous solutions.
In the industries, the equipments are often submitted to aggressive conditions (flow conditions, high temperature, etc.), involving the early apparition of corrosion. Thus corrosion and corrosion inhibition studies under hydrodynamic conditions are very important for industrial applications. However, there are few studies in literatures about the effect of hydrodynamic conditions on performance of organic and inorganic inhibitors under laminar or turbulent flow. The effect of hydrodynamic conditions on corrosion and corrosion inhibition of some metals and alloys such as copper [14], steel [15], [16], [17], [18], Cu–Ni alloys [19], [20], [21], [22], [23] and nickel–aluminum–bronze (NAB) [24] has been investigated in different media.
Ochoa et al. [25] have reported the influence of flow on corrosion inhibition of carbon steel RDE by fatty amines in association with phosphonocarboxylic acid salts. They showed that the inhibitor film formed at high rotation rate (2000 rpm) was thinner than that formed at low rotation rate (100 rpm). They also deduced that increasing the electrode rotation rate leads to an increase in the cathodic current densities, a decrease in the anodic current densities and corrosion potential shifted toward anodic direction. Cáceres and co-workers [26] have reported the electrochemical parameters and corrosion rate of carbon steel in different concentrations of un-buffered NaCl solutions under hydrodynamic condition using a superposition model. Hamdy et al. [27] have investigated corrosion and erosion–corrosion resistance of mild steel in sulfide-containing NaCl aerated solutions.
Corrosion inhibition of carbon steel using Na3PO4 in simulated interstitial solution of concrete (pH 12.5) contaminated by chloride ions has been studied. The influence of steel pretreatment time and electrode rotation rate on its corrosion behavior was investigated. It was found that for steel electrode immersed in inhibited solution, the inhibition efficiency decreased as electrode rotation rate increased, but when the steel specimen was pretreated in inhibitor containing solution for different immersion times, the inhibition efficiency was not significantly affected by rotation speed [28].
In our previous work, we studied the effect of hydrodynamic conditions on corrosion inhibition of steel in acidic solution using methionine as a green organic inhibitor. It was found that the inhibition performance of methionine improves with increasing the electrode rotation rate [29].
The aim of present research is to investigate the influence of fluid flow on corrosion inhibition of St52-3 type steel in NaCl solution using hydrogen phosphate ion. The St52-3 steel is widely used in most of industrial and constructional works, such as mineral processing equipments, petrochemical and oil industries, power plants, storage tanks etc. Electrochemical methods including potentiodynamic polarization and electrochemical impedance spectroscopy were performed to identify the effect of flow on inhibition efficiencies; scanning electron microscopy, SEM, technique was also used for morphological studies.
Section snippets
Working electrode construction
The working electrode was made of a St52-3 steel rod which was mounted in a polyester resin in such a way that only the end side of electrode was left uncovered and the exposed area was 0.283cm2 (Ø = 6 mm). This assembly was machined to form a rotating disc electrode RDE. An AFMSRX rotator (PINE Instruments Co.) was used to control the electrode rotation speed between 0 and 2400 rpm.
Electrochemical measurements
All electrochemical tests were performed with conventional three-electrode configuration: a Pt rod as counter
Effect of inhibitor concentration
Fig. 1 shows the Nyquist plots for corrosion of St52-3 in the presence of three concentrations of K2HPO4 (10−3, 5 × 10−4 and 10−4 M) under static conditions. It is clear that the corrosion resistance of the steel sample increases with the increase of inhibitor concentration. According to these results the concentration of 10−3 M K2HPO4 was selected for studies under hydrodynamic conditions.
Potentiodynamic polarization measurements
Fig. 2a and b shows typical potentiodynamic polarization curves of St52-3 samples under static conditions and
Conclusion
The influence of flow on corrosion inhibition of St52-3 steel using K2HPO4 in 3.5% NaCl solution was studied. It was shown that all corrosion parameters were dependent on the electrode rotation rate. Ecorr had a strong shift toward more positive values under electrode rotation. This shift was attributed to the increased mass transfer of oxygen from bulk of solution to the electrode surface. However, in the presence of phosphate ions, the displacement of Ecorr was not as high as the blank. The
Acknowledgements
The authors thank Eng. M. Rahimi for preparation of steel samples and University of Tabriz for financial support.
References (42)
Anodic dissolution of Armco iron in 0.5 M H2SO4 in the presence of adsorbed chloride ions
Hydrometallurgy
(1996)- et al.
Atmospheric corrosion of different steels in marine, rural and industrial environments
Corros. Sci.
(1999) - et al.
Influence of organic matter on orthophosphate corrosion inhibition for copper pipe in soft water
Corros. Sci.
(2004) - et al.
The effect of calcium ions on the adsorption of phosphonic acid: a comparative investigation with emphasis on surface analytical methods
Electrochim. Acta
(1994) - et al.
A corrosion inhibition study of a carbon steel in neutral chloride solutions by zinc salt/phosphonic acid association
Corros. Sci.
(1995) - et al.
Preliminary testing of Na2PO3F as a curative corrosion inhibitor for steel reinforcements in concrete
Cem. Concr. Res.
(1992) - et al.
Calcium mono fluorophosphate: a new class of corrosion inhibitors in NaCl medium
J. Electroanal. Chem.
(2004) - et al.
Corrosion control of galvanized steel using a phosphate/calcium ion inhibitor mixture
Corros. Sci.
(2003) - et al.
Inhibition of chloride localized corrosion of mild steel by PO43−, CrO42−, MoO42− and NO2− anions
Appl. Surf. Sci.
(2000) Inhibition of steel pitting corrosion in HCl by some inorganic anions
Appl. Surf. Sci.
(2005)
Corrosion inhibition of copper in chloride solutions by pyrazole
Corros. Sci.
Hydrodynamic effect on the behavior of a corrosion inhibitor film: characterization by electrochemical impedance spectroscopy
Electrochim. Acta
The effect of molybdate concentration and hydrodynamic effect on mild steel corrosion inhibition in simulated cooling water
Corros. Sci.
Electrochemical corrosion behavior of X-65 steel in the simulated oil sand slurry. I: effects of hydrodynamic conditions
Corros. Sci.
Aminotriazole as corrosion inhibitor of Cu–30Ni alloy in 3% NaCl in presence of ammoniac
Electrochim. Acta
Influence of flow on the corrosion inhibition of carbon steel by fatty amines in association with phosphonocarboxylic acid salts
Corros. Sci.
Determination of electrochemical parameters and corrosion rate of carbon steel in un-buffered sodium chloride solutions using a superposition model
Corros. Sci.
Evaluation of corrosion and erosion–corrosion resistances of mild steel in sulfide-containing NaCl aerated solutions
Electrochim. Acta
Corrosion inhibition of carbon steel in alkaline chloride media by Na3PO4
Electrochim. Acta
Effect of hydrodynamic conditions on the inhibition performance of l-methionine as a “green” inhibitor
Electrochim. Acta
Effect of chloride ions on the corrosion behavior of steel in 0.1 M citrate
Electrochim. Acta
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