Inhibition of copper corrosion by isatin in aerated 0.5 M H2SO4
Introduction
The chemical industry employs copper and its alloys extensively for condensers, evaporators, fractionating columns, etc. Copper does not displace hydrogen from acid solutions and it is therefore unattacked in non-oxidising acid environments. Nevertheless, most acidic solutions contain dissolved air that enables some corrosion to take place. Many organic molecules are used to inhibit copper corrosion [1], [2], [3], [4], [5], [6].
The primary step in the action of organic corrosion inhibitors in acid solutions is usually adsorption at the metal–solution interface. The adsorption process depends on the electronic characteristic of the molecules (adsorbate), the chemical composition of the solution, nature of the metal surface, temperature of the reaction and on the electrochemical potential at the metal–solution interface [7]. The adsorption requires the existence of attractive forces between the adsorbate and the metal. According to the type of forces, adsorption can be physisorption or chemisorption or a combination of both [8]. Physisorption is due to electrostatic attractive forces between inhibiting organic ions or dipoles and the electrically charged surface of the metal. Chemisorption is due to interaction between unshared electron pairs or π electrons with the metal in order to form a coordinate type of bond. It may take place in presence of heteroatoms (P, Se, S, N, O), with lone-pair electrons and/or aromatic rings in the adsorbed molecules [9], [10], [11], [12], [13].
Isatin is an indole derivative having two carbonyl groups in the 2 and 3 positions. The carbonyl group in the 3-position behaves like a ketone that is very reactive, the other has amidic behaviour [14]. Infrared evidence supports the following structure for isatin and gives no evidence for the enol form [15]:
In the present study the inhibition mechanism, efficiency and adsorptive behaviour of isatin on the corrosion of commercial copper were investigated in aerated 0.5 M H2SO4 solutions in the temperature range 25–55 °C.
Section snippets
Experimental
Copper corrosion inhibition in presence of isatin in aerated 0.5 M H2SO4 was investigated by means of potentiodynamic, gravimetric and spectrophotometric tests and determination of the double layer capacitance at the metal–solution interface.
Isatin was dissolved at concentrations in the range 1.0×10−4–7.5×10−3 M in aerated 0.5 M H2SO4 solutions. Commercial copper specimens (99.994% purity) were discs of 13 mm in diameter. Impurity contents (wt.-ppm): 26.3S, 9.4Ag, 7.9Fe, 7.7Ni, 7.1P, 1 (Sb, As,
Results and discussion
Fig. 2 shows some typical anodic and cathodic polarisation curves carried out at 35 °C in aerated 0.5 M H2SO4 in the absence and presence of various concentrations of isatin. From the polarisation curves the following electrochemical parameters were determined and listed in Table 2, Table 3: corrosion potential (Ecorr), corrosion current density (icorr) determined by extrapolation of the anodic Tafel line to the corrosion potential, limiting current density for oxygen reduction (iL), potential
Conclusions
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Isatin was found to be an effective inhibitor for commercial copper corrosion in aerated 0.5 M H2SO4 at higher concentrations in the temperature range 25–55 °C.
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Some evidence was found for a different corrosion mechanism for copper in solutions containing isatin in contrast to aerated uninhibited solutions of 0.5 M H2SO4.
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The difference between gravimetric and potentiodynamic corrosion rates emphasizes the limitation of the Tafel line extrapolation method in the determination of corrosion rates.
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