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Corrosion Inhibition of Aluminium using 3-Hydroxy flavone in the Presence of Quarternary Ammonium Salts in NaOH Medium
Corrosion Inhibition of Aluminium using 3-Hydroxy flavone in the Presence of Quarternary Ammonium Salts in NaOH Medium
Journal of the Korean Chemical Society. 2012. Apr, 56(2): 201-206
Copyright © 2012, The Korean Chemical Society
  • Received : November 17, 2011
  • Accepted : February 28, 2012
  • Published : April 20, 2012
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About the Authors
J. Morris Princey
Prabavathi Nagarajan
drprabahod@gmail.com

Abstract
The anticorrosive effect of 3-Hydroxyflavone (3HF) in combination with quarternary ammonium bromide and iodide salts (QAB and QAI) for aluminium corrosion in NaOH medium was studied at the temperature range of 303K-323K using weight loss study, potentiodynamic polarization study and impedance spectroscopic measurements. The results revealed that the inhibition efficiency increases with the inhibitor concentration and it further increases on the addition of quarternary ammonium bromide and iodide salts. The enhanced inhibition efficiency of the inhibitor in the presence of quarternary ammonium salts may be due to synergistic effect. The adsorption process of 3HF on the aluminium surface obeys Langmuir’s adsorption isotherm. The mechanism of adsorption is further supported by Scanning Electron Microscopic study (SEM).
Keywords
INTRODUCTION
Aluminium is an important subject of research because of its abundance and easiness in handling. In addition aluminium is justified by low price, high electrical capacity and high energy density. 1 In order to control aluminuim corrosion, the main strategy is to effectively isolate the metal from the corrosive agents by the use of corrosion inhibitors. Inorganic substances like phosphates, chromates, dichromates and arsenates have been found to be effective corrosion inhibitors but they are toxic in nature. Organic compounds having high electron density at the hetero atoms have the corrosion inhibition efficiency due to the functional groups 2 - 6 present in aromatic and heterocyclic rings along with electron-rich elements like nitrogen, sulfur and oxygen. Corrosion inhibition occurs via adsorption of the compounds on the corroding metal surface and the efficiency of the inhibition depends on the mechanical structural and chemical characteristics 7 of the adsorbed layers. As a contribution to the current interest on eco- friendly corrosion inhibitors, the present study is focused on the inhibiting efficiency of 3HF on aluminium in NaOH medium. Reports on the effects of quarternary ammonium salts in combination with green inhibitors for corrosion inhibition of metals is very scanty. 8 - 10 Therefore the synergistic effect of the additives namely QAB and QAI has also been studied.
EXPERIMENTAL
- Reagents
The commercial aluminium specimen with chemical composition (wt.%): Al (99.594%), Cu (0.002%), Zn(0.003%), Pb(0.100%), Co(0.050%), Ni(0.011%), Fe(0.179%) and Cr (0.082%) was used for the study. The flavonoid compound 3HF ( . 1 ) was purchased from Research Organics, Chennai, and re-crystallized from methanol. All chemicals used were of Analytical Grade.
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3-Hydroxyflavone (3HF).
- Recommended Procedure
The aluminum specimens were abraded with emery paper of different grades before each experiment and washed with de-ionized water and degreased with acetone and dried with a stream of air.
- Weight Loss Study
The aluminium coupons with dimension 3.0×1.0×0.2 cm 3 were used for weight loss studies. The coupons were weighed and the surface areas of all specimens were calculated before and after immersing them in 100 ml test solutions of NaOH with different concentrations for a time period of 2 hours. The weight loss studies were carried out at 303 K, 313 K and 323 K.
The inhibition efficiency was calculated from the corrosion rate 11 using the following equation.
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where CRblank and CRinh . are the corrosion rates in the absence and presence of the inhibitor.
- Electrochemical Measurements
The electrochemical measurements were carried out using a PRINCETON versa STAT Potentiostat-Galvanostat research instrument and a conventional three electrode cell set up. Aluminium was used as the working electrode with an exposed area of 1 cm 2 , saturated calomel as the reference electrode and platinum as the auxiliary electrode. All electrochemical measurements were carried out for the inhibited and uninhibited solutions. The Electrochemical impedance spectroscopy (EIS) measurements were performed at an open circuit potential after 15 minutes of immersion in the test solution with the amplitude of 10 mV. The covered frequency range was 30,000 Hz to 1 Hz. The impedance diagrams are given as Nyquist plots. . 2 represents the electrical equivalent circuit for the ac impedance measurement. The charge transfer values (R ct ) were calculated from the difference in the high frequency values. The capacitance of the double layer (C dl ) was estimated from the frequency ( f ) at which the imaginary component of the impedance (Z") is maximum and obtained using the following equation
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The equivalent circuit model used to fit the ac impedance measurement.
The potentiodynamic polarization (PDP) measurements were carried out at a sweep range from -1.7 V to -1.3 V. By the Tafel extrapolation method, electrochemical parameters like corrosion current density (I corr ) and corrosion potential (E corr ). The percentage inhibition efficiency can be obtained from the electrochemical measurements using the following formulae
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where Icorr . and Icorr . are the corrosion current densities without and with the inhibitor.
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where R ct and R’ ct are the charge transfer resistance values in the absence and presence of the inhibitor respectively.
- SEM Analysis
The aluminium specimens were immersed in 1 M NaOH with an optimum concentration of the inhibitor and without the inhibitor for 2 hours. Then, they were removed, rinsed quickly with acetone and dried. The surface morphology was studied using a Hitachi Model S-3000H (Resolution- 3.5 nm) scanning electron microscope.
RESULTS AND DISCUSSION
- Weight Loss Study
The values of percentage inhibition efficiency (IE%) obtained for different concentrations of the inhibitor at different temperatures are given in 1 . From the data it can be seen that the inhibition efficiency increases as the concentration of the inhibitor increases due to the adsorption of the inhibitor 12 on the metal surface. It is also seen that the inhibition efficiency of the inhibitor decreases with increase in temperature 13 suggesting physisorption. This may be due to the desorption of the inhibitor molecules 14 from the metal surface at higher temperatures.
Effect of temperature on the inhibition efficiency of 3HF alone and in the presence of quarternary ammonium salts on aluminium in 1 M NaOH by weight loss method
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Effect of temperature on the inhibition efficiency of 3HF alone and in the presence of quarternary ammonium salts on aluminium in 1 M NaOH by weight loss method
Thermodynamic parameters for the inhibition of corrosion of aluminium in 1 M NaOH by 3HF
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Thermodynamic parameters for the inhibition of corrosion of aluminium in 1 M NaOH by 3HF
The thermodynamic parameters were also calculated ( 2 ) From the IE (%) values, activation energy (E a ) was calculated using Arrhenius equation. The free energy of adsorption (Δ G°ads ) at different temperatures was calculated using the following equation 15
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where R is the molar gas constant, T is the absolute temperature and 55.5 is the molar concentration of moles of water in mol/dm -3 . Kads . is given by the following expression
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where θ is the degree of surface coverage ( 3 ). and C is the concentration of the inhibitor. The enthalpy of activation, Δ Hoads . is another criterion from which the mode of adsorption can be probed. Δ Hoads . was obtained by applying the transition state equation.
Effect of 3HF alone and along with of quarternary ammonium salts on rate of corrosion and surface coverage for aluminium in 1M NaOH at 303 K
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Effect of 3HF alone and along with of quarternary ammonium salts on rate of corrosion and surface coverage for aluminium in 1M NaOH at 303 K
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Thermodynamic plot for HPC at 303, 313 and 323 ± 1 K.
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where CR is the corrosion rate, h the Planck’s constant, N the Avogadro’s number, Δ So the entropy of activation, T the absolute temperature and R the universal gas constant. A plot of log ( CR/T ) against 1/ T ( . 3 ) was made for the blank and different concentrations of the inhibitor. From the slope value, Δ Hοads values were computed.
The negative values of Δ Goads . suggest that the adsorption of the inhibitor on to the aluminum surface is a spontaneous process and the adsorbed layer is stable. 16 The presence of the inhibitor increases the value of the activation energy (E a ) indicating physical adsorption 17 - 19 of the inhibitor on the metal surface. The enthalpy changes (Δ Hoads .) are negative indicating the exothermic 20 nature of the adsorption process.
- Potentiodynamic Polarization (PDP) Measurements
The anodic and cathodic polarization curves for aluminium in 1 M NaOH solution with and without the inhibitor are shown in . 4 and 5 . It is clear that both cathodic (hydrogen evolution) and anodic (metal dissolution) reactions of aluminium were inhibited with the increasing concentration of the inhibitor. The result suggests that it is a mixed type of inhibitor. The values of the polarization parameters (I corr ., E corr . and IE%) are listed in 4 . As the inhibitor concentration increases, the I corr . value decreases thereby increasing the inhibition efficiency.
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Potentiodynamic polarization curves for aluminium in 1 M NaOH with and without the inhibitor at different concentrations.
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Potentiodynamic polarization curves for aluminium in 1 M NaOH with the quarternary ammonium salts.
Potentiodynamic polarization parameters for aluminum in 1 M NaOH with and without the inhibitor at different concentrations
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Potentiodynamic polarization parameters for aluminum in 1 M NaOH with and without the inhibitor at different concentrations
- Electrochemical Impedance Spectroscopy (EIS) Measurements
The EIS of aluminium in 1 M NaOH is summarized as Nyquist plots in . 6 The plots clearly show that the addition of increasing amounts of the inhibitor causes an increase in electrochemical impedance. 20 The Nyquist plots show three parts: the capacitive loop in the high frequency region, the inductive loop in the middle frequency region and the capacitive loop in low frequency region. The values of R ct , C dl and IE(%) are given in 5 . The complete inspection of the values shows that R ct values increases while C dl values decreases with increase in the inhibitor concentration. This may be due to the increased surface coverage which led to an increase in IE(%).
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Nyquist plots of aluminium in 1 M NaOH with and without the inhibitor at different concentrations.
Corrosion parameters obtained from EIS measurements for aluminium in 1 M NaOH with and without the inhibitor at different concentrations
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Corrosion parameters obtained from EIS measurements for aluminium in 1 M NaOH with and without the inhibitor at different concentrations
- Adsorption Behavior
To ascertain the nature of adsorption of 3HF on aluminium in 1 M NaOH attempts were made to fit various isotherms such as Freundlich, Temkin, Langmuir and Frumkin. However the best fit was obtained ( . 7 ) only with Langmuir adsorption which supports the monolayer adsorption of the inhibitor on the aluminium surface.
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Langmuir adsorption isotherm for 3HF.
Synergistic effect of QAB and QAI on the inhibition efficiency of 3HF (from weight loss studies)
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Synergistic effect of QAB and QAI on the inhibition efficiency of 3HF (from weight loss studies)
- Synergistic Effect
The inhibition efficiency of the inhibitor was found to be enhanced with the addition of n-tetrabutylammonium bromide and n-tetrabutylammonium iodide along with 3HF. Similar observations has been reported 22 earlier and the enhancement of the inhibition efficiency was ascribed to the synergistic effect. The inhibition efficiency of the inhibitor increases with the addition of the quarternary ammonium salts at all temperatures studied. This can be attributed to the stabilization of adsorbed quarternary salts by electrostatic interaction with the inhibitor. This leads to greater surface coverage and higher inhibition efficiency. The synergistic effect of I - is found to be greater than Br - suggesting a possible role by ionic radii in the adsorption process. Synergism can be assessed in terms of the synergism parameter ( Sθ ) according to the following relationship 23
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where θ 1+2 = ( θ 1 + θ 2 )−( θ 1 θ 2 ), θ 1 is the surface coverage by flavonoid compounds, θ 2 the surface coverage of the additive and θ ' 1+2 is the measured surface coverage for flavonoids in combination with additives.
- SEM Analysis
The SEM images of aluminum were recorded ( . 8 and 9 ) after immersion in 1 M NaOH with and without the inhibitor for a time period of 2 hours to establish the interaction of the organic molecules with the metal surface. The images of SEM confirm the changes in the surface morphology. In the absence of the inhibitor, extensive corrosion is suffered by the metal surface which is evident by the presence of hemispherical deep pits and corrosion products ( . 8 ) which is due to the attack of the alkali on the surface. The specimen immersed in the alkali along with the inhibitor has a less corroded surface. This indicates that the inhibitor molecules hinder the dissolution of aluminium by forming an organic protective film on the metal surface and thereby reducing the rate of corrosion.
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SEM image of Al specimen kept in 1 M NaOH for 2 hours at 303 K.
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SEM image of Al specimen kept in 1 M NaOH along with 3HF for 2 hours at 303 K.
CONCLUSION
The flavonoid compound 3HF was found to be an effective inhibitor for the corrosion of aluminium in alkaline medium. Electrochemical measurements revealed that 3HF acts as a mixed type of inhibitor. The adsorption of the inhibitor molecules was found to follow Langmuir adsorption isotherm. The data obtained from weight loss studies, potentiodynamic polarization and electrochemical impedance spectroscopic measurements were found to be in good agreement. The inhibition efficiency of 3HF is temperature dependant and the increase in temperature leads to decrease in the inhibition efficiency of the inhibitor. Synergism studies show that the inhibition efficiency of the flavonoid compound increases with the addition of quarternary ammonium bromide and iodide salts. The SEM analysis also provided a supporting evidence for the adsorption of the inhibitor on the metal surface.
Acknowledgements
The authors would like to thank the Principal and Management of Bishop Heber College (Autonomous), Tiruchirapalli -620 017 for the encouragement and the UGC (New Delhi) for financial support.
References
Elewady G. Y. , El-Said I. A. , Fouda A. 2008 Int. J. Electrochem. Sci. 3 644 -
Pourbiax M. 1974 Atlas of electrochemical equilibra in aqueous solution NACE Cebelcor Houston 10 -
Nisancioglu K. 1992 Corrosion of aluminium alloys Proceedings of ICAA3 239 -
Gomma G. K. 1998 Mater. Chem. Phys. 55 243 -    DOI : 10.1016/S0254-0584(98)00084-4
Umoren S. A. , Ogbobe I. , Ebenso E. E. , Ekpe U. 2006 J. Pigment & Resin Tech. 35 (5) 284 -    DOI : 10.1108/03699420610692896
Oguzie E. E. 2006 Mater. Chem. Phys. 99 (2-3) 441 -    DOI : 10.1016/j.matchemphys.2005.11.018
Oguzie E. E. 2007 Corros. Sci. 49 1527 -    DOI : 10.1016/j.corsci.2006.08.009
Oguzie E. E. 2005 Mater. Lett. 59 1076 -    DOI : 10.1016/j.matlet.2004.12.009
Oguzie E. E. 2006 Pigment & Resin Tech. 35 (6) 334 -    DOI : 10.1108/03699420610711335
Oguzie E. E. 2005 Pigment & Resin Tech. 34 (6) 321 -    DOI : 10.1108/03699420510630336
Ebenso E. E. , Alemu H. , Umoren A. , Obot I. B. 2008 Int. J. Electrochem. Sci. 3 1325 -
Obot I. B. 2009 Int. J. Electrochem. Sci. 4 1277 -
Elewady G. Y. , El-Said I. A. , Fouda A. S. 2008 Int. J. Electrochem. Sci. 3 644 -
Oguzie E. 2008 Portugaliae Electrchimica Acta 26 303 -    DOI : 10.4152/pea.200803303
Qurashi M. A. , Ishatiaque Ahamad , Ashish Kumar Singh , Sudhish Shukala Lal Vakil Singh B. 2008 Mater. Chem. Phys. 112 1035 -    DOI : 10.1016/j.matchemphys.2008.07.011
Chauhan L. R. , Gunasekaran G. 2007 Corros. Sci. 49 1143 -    DOI : 10.1016/j.corsci.2006.08.012
Umoren S. A. , Obot I. B. , Ebenso E. E. 2008 E-J. Chem. 5 355 -    DOI : 10.1155/2008/138407
Umoren S. A. , Obot I. B. , Akpabio L. E. 2008 Pigment & Resin Tech. 37 98 -    DOI : 10.1108/03699420810860455
Umoren I. B. , Obot E. E. , Ebenso P. C. , Okafor O. , Ogbobe E. E. 2006 Anti-Corros. Methods and Mater. 53 (5) 752 -    DOI : 10.1108/00035590610692554
Desai P. S. , Vashi R. T. 2010 Indian Journal of Chemical Tech. 17 50 -
Ehteram Noor A. 2009 J. Appl. Electrochem. 39 1465 -    DOI : 10.1007/s10800-009-9826-1
Oguzie E. E. , Onuchukwu A. I. , Okafor P. C. , Ebenso E. E. 2006 Pigment & Resin Tech. 35 (2) 63 -    DOI : 10.1108/03699420610652340
Larabi L. , Harek Y. , Traisnel M. , Mansri A. 2004 J. Appl. Electrochem. 34 833 -    DOI : 10.1023/B:JACH.0000035609.09564.e6