Observation of l-cysteine enhanced zinc dissolution during cathodic polarization and its consequences for corrosion rate measurements

2015 ◽  
Vol 184 ◽  
pp. 203-213 ◽  
Author(s):  
V. Shkirskiy ◽  
P. Keil ◽  
H. Hintze-Bruening ◽  
F. Leroux ◽  
P. Volovitch ◽  
...  
1974 ◽  
Vol 27 (11) ◽  
pp. 2467 ◽  
Author(s):  
DB Matthews ◽  
PG Capps

The rate and morphology of zinc dissolution were studied in a Leclanche electrolyte of composition 0.5 mol dm-3 ZnCl2 and 5 mol dm-3 NH4Cl. A gelled electrolyte layer 2 x 10-3 m thick on the zinc surface was found to reduce the corrosion rate by an order of magnitude and to promote even dissolution. The corrosion results are interpreted in terms of a diffusion-controlled cathodic reaction involving O2 dissolution and metallic impurity deposition.


Author(s):  
K.K. Taha ◽  
Musa E. Mohamed ◽  
S.A. Khalil ◽  
S.A. Talab

Brass as an alloy composed mainly of copper is great industrial uses such as heat exchangers and similar other facility due to its good thermal properties. Due to the presence of the considerable ratio of zinc the alloy suffers from zinc dissolution or dezincification. Dezincification rate increases with the increase in the ratio of zinc in the alloy. In this study benzothiazole (BTH) and its substituent’s 2-methylbenzothiazole (MeBTH), 2-aminobenzothiazole (ABTH), 2-mercaptobenzothiazole (MBTH) and 2-phenylbenzothiazole (PhBTH) have been used as corrosion inhibitors for α-brass in stirred 0.1 M HClO4. The methods of investigation include weight loss, Tafel and linear polarizations and electrochemical impedance spectroscopy. The order of inhibition efficiency (%E) was calculated and the values obtained has indicated the sequence of inhibition efficiency was found to be BTH < MeBTH < ABTH < PhBTH < MBTH. The calculated values of thermodynamic parameters support this order. The inhibitors were found to suppress the corrosion rate by the formation of films which were identified by IR, SEM and EDAX techniques.


2020 ◽  
Vol 2020 (48) ◽  
pp. 35-42
Author(s):  
R.M. Dzhala ◽  
◽  
B.Ya. Verbenets’ ◽  
V.R. Dzhala ◽  
V.P. Lozovan ◽  
...  

The electromagnetic method of non-contact current measurements makes it possible to quickly monitor the state of passive (insulating coatings) and active (cathodic polarization) corrosion protection of underground pipelines (UP); detect places of unsatisfactory insulation, determine the transient resistance and its components (resistances of soil, insulating layer, polarization) in different sections, the area of insulation damage, the current distribution of cathodic protection of UP. In combination with contact measurements of direct and alternating voltages, ohmic and polarization potentials, it is possible to determine the polarization resistance and estimate the corrosion rate.


CORROSION ◽  
1972 ◽  
Vol 28 (11) ◽  
pp. 421-423 ◽  
Author(s):  
D. A. JONES

Abstract The criterion of cathodic protection is that level of cathodic potential change (polarization) which is sufficient to give adequate protection for a given application. Ideally, it is preferred to polarize to the reversible potential of the anodic reaction, but this potential is often impossible to determine by experiment or to calculate from theory for complex corrosive electrolytes. Polarization to a specific potential (e.g., −0.85 volts) or to various potential changes (e.g., 100 to 300 mv) have also been proposed, but none have been universally accepted. Electrochemical kinetic theory has been very successful in predicting and correlating the corrosion behavior of metals. However, the theory has not been applied to cathodic protection until recently. It has been shown that the anodic Tafel constant determines the cathodic polarization necessary to effect a given reduction in corrosion rate. Thus, polarization required to obtain a given degree of protection can be predicted if the anodic Tafel constant is known. Determining the anodic Tafel constant may be difficult for complex structures in service. However, even an estimate from a small sample in the required corrosive would be very helpful in making the criterion of cathodic protection more quantitative.


CORROSION ◽  
1978 ◽  
Vol 34 (12) ◽  
pp. 428-433 ◽  
Author(s):  
D. A. JONES

Abstract The corrosion rates of low alloy steel and carbon steel in 0.1 N NaCI were accelerated by factors of 4 to 6 when an alternating current density of 30 mA/cm2 (60 cps) was applied in dilute salt solutions purged with nitrogen. Tests with low frequency alternating anodic and cathodic current showed that both steels polarized more rapidly in the cathodic direction than in the anodic. Thus, the anodic half-cycle of AC did not have time to restore the potential to its original value after the preceding cathodic half-cycle. The result is a net cathodic polarization which accelerates or “depolarizes” the anodic metal-dissolution reaction by lowering the anodic Tafel slope. Depolarization of the anodic reaction was confirmed by polarization measurements in the presence of AC. Depolarization of the anodic reaction by AC was also observed in aerated solutions, but the corrosion rate was controlled by diffusion of dissolved oxygen, and no increase in corrosion rate was measured. Possible mechanisms of anodic depolarization are discussed.


2011 ◽  
Vol 690 ◽  
pp. 365-368 ◽  
Author(s):  
Zhi Ming Shi ◽  
Andrej Atrens

Plug-in specimens enable measurement of reliable Mg polarization curves. Cathodic polarization curves were measured for high purity Mg in 3.5% NaCl saturated with Mg(OH)2using (i) mounted specimens and (ii) plug-in specimens. Polarization curves yielded the corrosion current densityicorrand the corresponding corrosion ratePi, which was compared with corrosion rates evaluated from hydrogen evolution,PH, and weight loss,PW. Mounted specimens producePivalues three times larger than plug-in specimens, due to crevice corrosion in the mounted specimens. Plug-in specimens had no crevice and allow simultaneous measurement ofPHandPi. Piwas less thanPHand indicated an apparent valence of 1.45 in support of the existence of the uni-positive Mg+ion.


Author(s):  
Mark Yunovich ◽  
Neil G. Thompson

Corrosion caused by the discharge of 60 Hz AC current from a pipeline in a high voltage AC (HVAC) corridor has been discussed and studied over the past 20 or more years. More recent studies in Europe have specifically addressed these corrosion issues following several failures attributed to the presence of AC discharge from the pipeline. Very few corrosion failures in North America have been specifically attributed to what is termed AC-enhanced corrosion (ACEC). One missing area of research is well-controlled laboratory experiments in soil environments. This study proposed a mechanism of ACEC that is based on conventional electrochemistry using the same equivalent analog circuits used to discuss other corrosion processes. It was shown that only a small amount of the 60 Hz AC current discharge passes through the resistive component of the equivalent circuit, which results in corrosion (metal loss) reactions. The AC current passing through this resistive component produces both anodic and cathodic polarization shift (sine wave dependent) resulting in a net increase in the average corrosion rate as compared to the free-corrosion rate. The proposed model for ACEC does not invoke any new electrochemical concepts and is based on the conventional (DC) treatment of the corrosion processes; the model excludes treatment of cases with imposed cathodic protection current. The amount of ACEC is dependent on the magnitude of AC current that passes through the resistive component of the parallel resistive-capacitive electrochemical interface. ACEC is characterized by the rapid formation of a diffusion controlled (Warburg) process for corrosion in soils. Although diffusion controlled, the overall impedance decreases as the total AC current increases. The model suggests that AC currents (60Hz) cause anodic (positive) polarization shifts during the positive portion of the imposed AC sinewave along with cathodic polarization shifts in the negative portion of the AC sinewave; the net result is an increase in the average oxidation (metal loss) current as compared to the free-corrosion condition. The proposed model for the ACEC mechanism showed excellent correlation with the experimental results. The research work was made possible by the funding from PRCInternational.


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