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J IRAN CHEM SOC (2012) 9:911–921
ꢀ
ꢁ
anodic and this change is negative when the inhibitor is
cathodic [18]. The addition of CMU inhibitor to acid
solution shifts the corrosion potential to more negative and
the maximum shift reported in HCl and in H2SO4 envi-
ronment is 86 and 14 mV, respectively. These results
imply that the CMU inhibitor behaves as cathodic inhibitor
in HCl environment and mixed type inhibitor in H2SO4
environment. It is obvious from the polarization curves that
both anodic and cathodic tafel slopes are shifted in the
presence of inhibitor, indicating that the inhibitor con-
trolled both anodic dissolution and cathodic hydrogen
evolution reaction [19]. The maximum inhibition efficiency
of the CMU inhibitor was found to be 96.21 % in 1 N HCl
for 0.020 N CMU at 333 K and 89.03 % in 1 N H2SO4 for
0.020 N CMU at 303 K.
ꢁEa
icorr ¼ A exp
ð2Þ
RT
ꢀ
ꢁ
ꢀ
ꢁ
ꢀ
ꢁ
RT
Nh
DS0
DH0
RT
icorr
¼
exp
exp
ð3Þ
R
where icorr is the corrosion current density, A is the
Arrhenius constant, Ea is the activation energy, R is the
universal gas constant, N is the Avogadro’s constant, h is
the Planck’s constant, DSꢁ is the change in entropy of
activation and DHꢁ is the change in enthalpy of activation.
Plots of ln(icorr) versus 1,000/T and ln(icorr/T) versus
1,000/T gave straight lines with slopes of -Ea/R and
-DHꢁ/R and intercepts of A and [ln(R/Nh) ? (DSꢁ/R)],
respectively. From the slope and intercepts, values of
activation parameters were calculated and are presented in
Table 7. The activation energy increased in the presence of
CMU and indicated that the inhibitor physically adsorbed
at the initial stage [24]. The energy of activation was
increased with increasing inhibitor concentration, sug-
gesting strong adsorption of inhibitor molecules at mild
steel surface. The increase in activation energy was due to
blocking of corrosion process by the adsorption of CMU
molecules on mild steel surface [25]. The change in energy
of activation was greater than 20 kJ/mol implies that the
inhibition process was controlled by surface reaction [26].
The values of enthalpy of activation DHꢁ and energy of
activation Ea are same, and the values of Ea increased for
corrosion of mild steel in the presence of inhibitor, indi-
cating that the energy barrier for corrosion reaction
increased in the presence of inhibitor without changing the
dissolution mechanism [27].
AC impedance study
The impedance spectra for mild steel in 1 N HCl and
1 N H2SO4 without and with various concentration of
CMU at 303 K are presented as Nyquist plots in Fig. 4.
Impedance parameters derived from Nyquist plots are
given in Table 6. It is observed that the value of charge
transfer resistance (Rct) was found to be increased with
increase in concentration of inhibitor. On the other hand,
the value of double layer capacitance (Cdl) decreased
with increase in inhibitor concentration. A large charge
transfer resistance is associated with slowly corroding
systems [20]. In addition, improved inhibitor protection
is associated with a decrease in metal capacitance [21].
The decrease in double layer capacitance which resulted
from a decrease in the local dielectric constant and/or an
increase in the thickness of the electrical double layer,
suggests that CMU acted via adsorption at the metal/
solution interface [22]. The semicircular appearance of
impedance diagram indicates that the corrosion of mild
steel is mainly controlled by a charge transfer between
inhibitor molecule and mild steel surface [23]. The
maximum inhibition efficiency was found to be 97.46 %
in 1 N HCl for 0.02 N CMU at 303 K and 93.38 % in
1 N H2SO4 for 0.02 N CMU at 303 K. Inhibition effi-
ciency obtained in AC impedance method is in good
agreement with polarization method.
The negative value of entropy of activation (DSꢁ) in the
presence and absence of inhibitor implies that the activated
complex represented rate-determining step with respect to
association rather than dissociation step. This also implies
that a decrease in disorder occurred when proceeding from
reactants to activated complex [28]. In addition, the less
negative values of DSꢁ in the presence of inhibitor imply
that the presence of inhibitor created a near-equilibrium
corrosion system [17].
Adsorption isotherm
In order to understand the inhibition mechanism of corro-
sion, adsorption behavior of organic adsorbate on mild
steel surface must be known. The Langmuir adsorption
isotherm model has been used extensively in the literature
survey for various metal, inhibitor and acid solution system
[17, 19, 25]. The plot of Cinh/h versus Cinh (Figs. 5, 6)
yielded a straight line, provided that the adsorption of
CMU on mild steel surface in HCl and H2SO4 solution
follows Langmuir adsorption isotherm.
Thermodynamic parameters
The thermodynamic activation parameters such as energy
of activation Ea, enthalpy of activation DHꢁ and entropy of
activation DSꢁ for mild steel corrosion in 1 N HCl and 1 N
H2SO4 with and without various concentration of CMU at
303, 318, and 333 K were calculated from an Arrhenius
plot (2) and transition state equations (3) [17].
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