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The advent of Industry 4.0 has opened a data-rich avenue of predicting and controlling premature degradation of industrial materials. For any industrial construction or manufacturing projects, performing analysis on the structural integrity of materials is crucial for their sustainability.
Corrosion Science: Modern Trends and Applications gives scholars a snapshot of recent contributions and development in the field of material corrosion.The book presents 12 chapters that cover topics such as corrosion testing methods, anti-corrosive coating mechanisms, corrosion in different types of products (electronics, polymers), industrial systems (power plants, concrete constructions and hydraulic systems) and corrosion as a result of environmental characteristics (such as marine surroundings). The breadth of topics covered coupled with the reader-friendly presentation of the book make it highly beneficial for students, research scholars, faculty members and R&D specialists working in the area of corrosion science, material science, solid-state science, chemical engineering, and nanotechnology. Readers will be equipped with the knowledge to understand and plan industrial processes that involve measuring the reliability and integrity of material structures which are impacted by corrosive factors.
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Veröffentlichungsjahr: 2021
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According to the European Federation of Corrosion, the term corrosion signifies an irreversible process due to an interaction with the environment, which causes detrimental effects on the materials permanently. For any industrial applications, this process has a severe impact on revenue. For our health and environment, it can damage several vital sections. There is a severe impact on the GDP of the country as well due to the overall damages. In this sense, the investment of scientific talent for the control of corrosion is always economically justified for mankind.
The overall growth of the Industry 4.0 and subsequent demand for new innovative materials opens a new field of mechanism to control premature degradation of the material. This book entitled ‘Corrosion Science-Modern Trends and Applications’ with twelve high-quality chapters provided the required picture of the recent contribution and development in the field of corrosion.
Chapter 1 presents the accelerating corrosion test method with various operating apparatus designed by ASTM standard guide. Another most important use of electrochemical techniques, namely linear polarization, potentiodynamic polarization and electrochemical impedance spectroscopy, discusses measuring the corrosion rate for coated and painted specimens.
Chapter 2 discusses various anticorrosive coatings, namely barrier, inhibitive, sacrificial, inorganic, and organic coatings. The various modified coatings are introduced to reduce pores and defects observed in conventional coatings.
Chapter 3 reviews corrosion of electronic printing board with the possibilities and types of the corrosion as well as their protective phenomena. The chapter highlights the corrosion in electronic gadgets and printed electronic circuit board since nowadays, which have printed electronic circuit board.
Chapter 4 contains a discussion on protective materials like conductive polymer and its composites such as conducting polymers mixers of magnetic materials and graphene additives on corrosion resistance capabilities.
Chapter 5 discusses corrosion protection in drinking water systems. The chapter presents corrosion of drinking water distribution system (DWDS) based on various parameters like pH of water, the hardness of water, alkalinity of water, buffer intensity, total dissolved oxygen and total inorganic carbon and organic carbon.
Chapter 6 concentrates on the corrosion of concrete. The electrons can move in the steel rebar, and the ions can move in the concrete, which acts as an electrode leading to the corrosion in concrete. To know the damage of the reinforcement in the concrete X-ray microcomputed tomography is employed.
Chapter 7 presents the corrosion effect on the aluminium alloy. The damage caused by the Sulfate Reducing Bacteria (SRB) is discussed here. The microstructure cracking occurs due to many factors like corrosion, mechanical stress, thermal stress and bacterial adherence.
Chapter 8 focuses on the corrosion problems of nuclear waste systems because of the disposal. The discussion between the rate of corrosion of all the nuclear waste packages with the nuclear waste disposal concept and the safety measures of the landfill sites is featured. Furthermore, the corrosion of the various kinds of nuclear waste packages, and the metallic container for the high-level waste packages review given the deterioration or dissipation processes, the experimental in-situ approaches, and the exemplary of corrosion of nuclear waste and lifetime forecasting are presented in this chapter.
Chapter 9 presents the impact of Microbiologically influenced corrosion (MIC) in various fields like industries related to healthcare, marine, petroleum, and oil. An attempt is made to present MIC and its underlying mechanisms. Cathodic depolarization theory, along with the other mechanisms supporting MIC caused by sulfate/nitrate-reducing bacteria, has been the focus of this chapter.
Chapter 10 recognizes corrosion as a severe problem in the power plant sector. Corrosion gives rise to wastage of material in huge quantities, failure of tubes, leakage of tubes, sudden shutdowns as well as the reduction in the lifetime of components. Also, it reduces the thermal and electrical efficiency of a power plant to a maximum extent leading to minimum maintenance, outage, and replacement cost.
Chapter 11 depicts the impacts of corrosion on significant industries in chemical and fertilizers industries. In this chapter, they focus on corrosion related to chemical and fertilizer industries, the impact of corrosion on their efficiency, corrosion controlling methods and their interrelated phenomena.
Chapter 12 focuses on Marine corrosion, its mechanism, factors affecting corrosion, and several methods adopted for the prevention of corrosion describes with an emphasis on marine corrosion inhibitors. The use of inorganic compounds and paints as corrosion inhibitors is discussed in the chapter.
This chapter presents the accelerating corrosion test method with various operating apparatus designed by ASTM standard guide. It is used to measure the corrosion resistance of coated and painted samples. The important uses of electrochemical techniques are linear polarization, potentiodynamic polarization, and electrochemical impedance spectroscopy. These are discussed in measuring the corrosion rate for coated and painted specimens.
In the early 1900s, the accelerated corrosion test method of metallic coatings was initially established for testing the samples, thereby improving the efficiency and durability. The test processes for corrodibility of nonferrous, ferrous metals, inorganic, and organic coatings were increased. The changes observed were added for useful testing of new materials. The service durability, and quality of samples were tested using accelerated corrosion tests. Further, these were used in material research. The ASTM International, the Society of Automotive Engineers (SAE), the Federation of Societies for Coatings Technologies (FSCT), and others established many accelerated corrosion tests, and provided variations in technical fields as well as industrial materials. As the water-based coating technology continues to evolve, one of the significant challenges that increases their anti-
corrosion performance. Some powder coatings, and their application methods were developed to decrease the usage of solvents, and applications. Subsequently, the material market made a drastic increase in the coatings, and the surface coatings were proven to have longer warranties for market challenges. The oldest accelerated corrosion testing method was ASTM B 117 standard operating Salt Spray (Fog) Apparatus. A recent development was used to measure the corrosion rate of metallic coatings in a “near-shore” atmosphere. A corrosion test was applied to determine the efficiency of material samples, and furthermore, these were used in the development, and modifications for applications in the environmental, and material sciences. Hence, the corrosion rate of the test specimen was measured using the several types of accelerated corrosion testing methods to be described at present.
The corrosion resistivity can be determined by using the Standard test ASTM B 117 for inorganic, and organic coatings applied to the metals [1]. The B 117 Standard was made up of static (constant) condition, and continuous test, which was ideally carried out in multiples within a 24-hour period. The cabinet consists of an atomized solution, which was prepared by using 5% sodium chloride, and 95% by mass of ASTM D 1193 Type IV water. This kind of cabinet can be called a salt Fog chamber. The test samples were exposed to this salt fog environment. The chamber contains an atomized solution which was held at a temperature of 35oC, and 95% relative humidity. To preserve these conditions, the chamber was heated, and it was also necessary to maintain wet conditions at the bottom of the exposure zone. The corrosion resistance of various Al and Al/Zn-coated AZ91D Mg alloys was estimated by the salt spray method. After exposing it within the salt spray chamber for one hour, fast corrosion can be occurred on the bare surface of Mg alloy, causing the loss of metallic lustre. After 8 hr of salt spray test, the Al coated Mg sample maintains its integrity, and the appearance of silver-grey surface indicating improved corrosion resistance [2].
ASTM G 85 was observed to be the modified salt fog test, which includes five annexes. The primary one is the acetic acid-salt fog test, in which the salt solution was prepared according to the B 117. Afterwards, the pH values were maintained within the range from 3.1 to 3.3 to the acetic acid. The acetic acid-salt spray test can be used for decorative chromium plating on steel [3]. The test duration should be 144-240 h. It can be used to test the metallic coatings, inorganic, and organic coatings for resistance to the highly corrosive environment in comparison with the ASTM B 117.
In the case of the second annex of the cyclic acidified salt fog testing, the ASTM G 43 was used for exfoliated tests on certain aluminium alloys [3]. It was generally indicated as the MASTMAASIS test, which can be used for exfoliation testing of aluminium. This test uses 5% of sodium chloride solution, and it makes it easy to adjust pH in the range of 2.8 to 3.0 with acetic acid. The test duration was noted to be 6 h cycle of ¾ h spray; 2 h dry air purge and ¾ h soak at high humidity. The temperature of chamber exposure was held at 49oC, and the tower of humidity was operated at 57oC. During the purge cycle, the objective of the test can be the drying process of samples, and further leaving a white corrosion product.
In annexe 3, this testing can increase the application for manufacturing the control of exfoliation-resistant heat treatments used in producing 2, 5, and 7 K series of aluminium alloys. Then, the pH value was observed to be 2.5 - 3.0, and the testing method was operated at 49°C. The modified method was used to test the corrosion rate of organic coatings applied on metallic substrates while the testing procedure was operated between 24 to 35°C. At the time of this test operated at 1 to 2 ml/h, the collection rate specified for fog cycles was the same as the use of B 117 Standard. However, 2 h cycles were used for the whole test period. Due to the cyclic nature of this test, it was necessary to develop and confirm proper condensate collection rates by using 16 h salt fog test to be conducted periodically [4]. The apparatus in the test chamber must be controlled, and hence that will cycle the exposure zone run throughout ½ h salt spray, 1 ½ h of soaking time at 98% of relative humidity.
Standard ASTM G85 Annex 4 is a salt/SO2 fog (spray) test, which can be performed using either sodium chloride solution or synthetic sea salt solution. Like the salt spray test, it was performed at 35oC. The fog may be continuous or infrequent. In case of the operation of the cycle during the test period, the sulfur dioxide can be injected into a chamber. Herein, for ½ h salt fog, and ½ h SO2 were injected into a chamber. These were soaked for 2 h. Hence, the Navy developed the same kind of test used to find the exfoliating corrosion on aircraft carriers [5].
0.35% of ammonium sulfate, and 0.05% of sodium chloride in 0.60% by mass of ASTM D 1193 Type IV water were used to prepare the electrolyte solution, which was necessary to perform the test. When compared with the standard salt fog test, this solution was found to be more dilute and was operated using 2 h cycle time. This consists of 1 h fog at ambient 24oC ± 3oC and less than 75% of relative humidity followed by 1 h dry off at 35oC. Hence, at controlled room temperature, the test samples were exposed to 1 h of salt fog. Afterwards, the sample was dried at 35oC for one hour. The pH value of collected condensate falls in the range of 5.0 to 5.4. Due to the cyclic nature of this test, a distinct salt fog test with a duration of 16 h can be required to develop and confirm good collection rates. Due to the changes in humidity of this testing procedure, and the cyclic salt test, the cabinet needs a valve that allows the atomized air to bypass the humidifying tower, and time devices to control the duration of cycle, spray, temperature variations, and airflow. This was noticed as a modified British Rail “Prohesion” testing, which was established in the 1960s for the coated metals in industrial sectors [6]. This kind of test method was used to test the paints and coatings on steel materials.
The painted metals were exposed to salt for/UV environment and tested using standard ASTM D 5894. This was incorporated with a cycle of UV exposure followed by G 85 Annex 5 exposure zone [7]. The cycle period of UV exposure introduced environmental impact to the condition of test, and originated results which were like the direction of the field. Two distinct cabinets are required instead of the salt fog/UV chamber.
The ASTM B 368 Standard [8] was established by the American Electroplaters, and Surface Finishers Society (AESF) [9], which was used initially in the improvement of metallic coatings, in addition to decorative coatings. These were exposed to highly corrosive environments. It was observed to be a significant challenge to provide a prompt evaluated service for testing the specification of the product in research studies. It became necessary to provide controlled manufacture possessing the environment friendly in nature. This type of modification can be done with human effort. The modified primer B117 salt spray test is the standard B 368. The transformation can be done by adjusting the pH of the 5% salt solution within the range of 6-7, and then adding 0.25 g of copper chloride reagent per liter of salt solution. This test can be operated at the temperature in the exposure zone of 49°C. This runs continuously for 6 to 170 hours as admitted between seller and purchaser. During regular days, it was noted to be necessary to check the temperature within the exposure zone. That is, for “short” duration, the chamber must be opened periodically to operate the samples and reload solution. Another modified salt fog test can become the consistency of test exposure circumstances. Mass loss of nickel coupons was used in the standard ASTM B 368 rather than the steel used in the B 117 standard. The corrosion test chamber devices equipped with the B 368 standard achieve the need for the Standard ASTM B 117 and will resist the increasing temperature. This test uses a powerful electrolyte solution.
ASTM B 380 [10], corrodkote test was established by AES to enhance the efficiency of decorative painting used in the industry of automobile. The corrodkote test uses a mixture contains ferric chloride, kaolin, cupric nitrate, and ammonium chloride (NH4Cl) in the distilled water [11]. The test uses those samples which were practiced with the mixture. These were injected in the humidity chamber maintained at 38oC, and 80 and 90% of relative humidity without condensation on parts. The test period was about 24 h per cycle [11]. A final process of the test, and the cleaning of samples were done by using moderated working water. To get the final corrosion product, these cleaned samples were needed to exposure to salt fog or humidity.
The corrosion resistance of metal with organic coatings can be tested by using the Filiform test as standard ASTM D 2803 [12]. According to ASTM B 117, the test begins with a salt exposure immediate after 70 to 90% of relative humidity which needs to be maintained for the exposure of humidity. The differences in the test can produce the change in the duration of the salt fog exposure, and the amount of relative humidity percentage. The test method of filiform corrosion for the painting on the aluminum wheels, and aluminum wheel trim was incorporated with the CASS test. This test exposure for 6 h before the humidity cycle [13]. Filiform type corrosion was recognized by thread-like filaments as obtained under clear as well as a coated aluminum powder [14].
ASTM D 2247, Standard practice for testing water resistance of coatings in 100% relative humidity was widely used. The water-resistance of coated samples was tested using this method. The temperatures of both cabinet, and humidity tower were fixed at 38oC. The device should be a water container with an electrical heating element or test container with pipe assembly arrangement for dispersion of air. Due to this kind of built, it makes condensation occurring on the samples. In case of the modified salt fog chamber B 117, first, remove the fogging apparatus, and then replaced by a water container or the pipe assembly arrangement for dispersion of air. The water height in the water container with the heating process can be decreased to a position above within the humidifying water.
The corrosive gas test can be treated as a mixture of gas placed into a large humidity environment, and widely used for porosity test. The following examples are listed of these tests:
The moisture SO2 test can practice using standard ASTM G 87.Blended Flowing gas test can be used by standard ASTM B 827.In the presence of SO2, the saturated humid atmospheres have used the test such as standard DIN 50018.The moisture SO2 test operated by ASTM G 87, and later, it was modelled by the DIN 50018, and is often called the test of Kesternich. The low concentrations of SO2 gas were added into 100% of the humid atmosphere for conducting the test. A temperature of 40oC was required to maintain this test. The DIN 50018, and G 87 were used in electronic industrial society, as well as on both secured devices (ASTM D 6294) [15], and roofing materials. A recent study for oil coatings (D 3794) test was also conducted by G87. Due to the other gases such as carbon dioxide lead the variation in the trial.
ASTM B 827, Standard practice for conducting the blended flowing gas test can be widely used in the electronic industry. The testing method uses a combination of various gases at controlled temperature, and humidity to produce the required conditions. The MFG test requires equipment of a more complex nature than corrosive gas tests.
The corrosion tests include a single step or more steps involved for salt fog exposure, humidity, and drying, ambient temperature. SAE J2334, Standard practice for cosmetic corrosion lab testing, was used in the automotive industry to produce good results in response to field exposure. The test method is:
The humid stage at 50oC and 100% of humidity meet at 6-h.At ambient conditions, salt fog exposure duration is 15 min.The dry period at 60oC and then 50% of humidity maintained for 17 h and 45 min, respectively.The test duration is 60 cycles, and longer cycles were used for heavier coating systems. The use of corrosion coupons was incorporated in the test method for monitoring the corrosion activity within the chamber. A minimum of six coupons made of 25.4 x 50.8 mm AISI 1006-1010 steel was used. The coupons are cleaned, weighted, and mounted in a nonmetallic rack. One coupon from each end of the rack was removed, cleaned, and reweighted every 20 cycles. At present, zero mass loss numbers for each cycle were discussed. The evaluation of the corrosion resistance of metals in the presence of environments will be more effective for chloride ions. For instance, sodium chloride from a seawater source. Due to the cyclic nature of this test, the test samples were exposed to modification of atmospheres during the time duration.
Most the industrial markets using the technique of electrochemical corrosion can be suitable for the evaluation of service duration of metallic coatings. This technique was used to determine the corrosion resistance and improving the factors to protect from corrosion. In addition, the environment was characterized by oxidizing power. The environment contains a strong tendency of oxidizing materials. The direct current dependence of electrochemical processes was demonstrated in this chapter. Since linear polarization, and Potentiodynamic polarization techniques used the application of direct current. Electrochemical impedance spectroscopy (EIS) is another technique using the application of alternating current. This determines the frequency dependency mechanism in the process of corrosion and measures the variation in polarization resistance.
In case of the linear polarization method, within the potential range of 10 - 20 mV, the current was determined from the anodic to the cathodic direction. At the potential corrosion range, the current against potential plot shows linearity nature. The calculated slope of this plot gives the resistance of polarization. The pre-determined of anodic and cathodic Tafel constants in the Stern-Geary equation applied to calculate the corrosion current. Potentiodynamic polarization technique was applied to study the corrosion properties of passivating metals, and alloys. Electrochemical Impedance Spectroscopy determines the reaction of corroded systems to the “ac” perturbation potentials. Nowadays, most and wide use of this technique measures the corrosion resistance, and passivation in metals. The study of inhibitors was to prevent corrosion, properties of a sacrificial, barrier, and efficiency of polymer-based coatings like paints.
Linear polarization resistance technique measures the rapid corrosion rates, and it uses the environment like the ionic conducting liquid. The same kinds of materials were required to prepare two or three cylindrical electrodes in the LPR probe. The smallest d.c. potential ΔE of 20 mV is applied between two electrodes. The flow of current Δi across the two polarized electrodes was measured after a short duration. The linear polarization resistance RP was measured from the ratio of voltage to current, and from the Stern-Geary equation, the corrosion current shows inversely proportional relationship to RP.
(1)The corrosion rate is calculated from Icor using Faraday's law if the constant B is known.
B can be electrochemically measured by using the anodic and cathodic Tafel slopes.
In a three-electrode probe, the test sample was considered as the first electrode, the second one was an additional electrode, and the last and third one could be reference electrodes opposite to the potential of the sample. The current will be passed through the test electrode, and the additional electrode. The ohmic drop of electrode probe could be responsible for reducing the errors. In addition, it was applicable for low ionic conductivity liquids. Numerous linear polarization resistance techniques with a signal having a high frequency can be used to
determine the ohmic (IR) drop across two or three-electrode probes. The use of the LPR probes with suitable conductive to only conductive media like pure water.
Many studies on linear polarization were reported to observe the corrosion resistance, inhibitors that prevent corrosion, the study of passivation of metals; properties of sacrificial type barrier, and efficiency of polymer-based coatings due to the deposition on the metallic samples [16-22]. Mennenoh and Engel reported [16] that the use of polarization technique capable to examine the strong inhibitors can prevent corrosion on steel in baths. Linear polarization techniques were used [17-19] to measure the resistance of polarization, and the rate of corrosion for several barriers and sacrificial type coatings. Electrodeposited zinc-nickel-cadmium coatings usually contain high polarization resistance (low rate of corrosion) as compared with the other coatings examined in 0.5 M H3BO3+0.2M Na2SO4 solution at pH of 6.5 [18]. Electrodeposited Zn-Co coatings offer high corrosion resistance (higher RP value) as compared with pure Zn coatings.
When alloy type or metallic sample is exposed to a specific atmosphere, they become passive at a specified potential region and that potential can be measured using the potentiodynamic polarization technique. It estimates the capability of the metal to passivate immediately and passivation of metals causes the critical current density. The metal and alloys became passive when they were exposed to a corrosive atmosphere. The corrosion rate of this passive metal and alloys can be measured by using potentiodynamic polarization technique. This technique allows the estimation of the active corrosion region, the current density, the commencement of passivation, the initial potential for passivation, the flow of current across the passivation region, and the potential period over the passivated region. Nanostructured ZrO2-TiO2 multi-layer composite coating was deposited on AISI 304 stainless steel and its corrosion rate in simulated marine water was evaluated by using potentiodynamic polarization test. The corrosion resistance was increased with increasing thickness coating. Moreover, the increase in corrosion in potential can be responsible for low corrosion current.
The electrochemical cell can be made from three electrodes. First one is the test sample which can act as a working electrode. The coated/uncoated test sample must have surface exposure with an area of cross section of 1-cm2. The second one is the reference electrode which is the saturated calomel electrode (SCE), and the last one is the cylindrical shape platinum electrode which may serve as a counter electrode. Further, 3.5 weight % of NaCl aqueous solution was added into the electrochemical samples, and the measurements were performed at the temperature 20oC. Measurements by the EIS were operated at the region of the corrosive potential of the test samples within the frequency range from 0.01 to 10,000 Hz. The EIS measurement device uses the sinusoidal voltage (amplitude: ±10 mV). Hence, the EIS measurement data were analyzed in terms of Bode (logarithm of the impedance modulus |Z| against phase angle as a function of the logarithm of the frequency f) diagram and Nyquist plots. The impedance spectra can be analyzed through the model of equivalent circuits.
The electroless nickel-zinc-phosphorous and electrodeposited nickel-zinc alloy provide a magnitude 2 KΩ resistance of barrier. The resistance of barrier coatings was improved by increasing the nickel concentration during the deposition. Since the strength of corrosion protection was decided using organic coatings and the service duration of these coatings measured with the application of the EIS technique [23-38]. It can be a potential technique to collect special parameters of the system to determine the primary period of their response and degradation in the properties of barrier coatings [23, 36, 37]. The variation in the coating capacitance was identified and correlated with the water [31]. The variation in the resistance can be expressed as the permeability of ionic specimens in the electrolyte [39-41]. The EIS can be capable of measuring the separation into constituent layers of the epoxy layer electro-coated on the phosphate applied for steel in 3.5% sodium chloride solution which was exposed into the atmosphere [29]. The parameters of coatings were calculated using an analogue circuit model. The area of separated layers was determined by the resistance of pore and the frequency of break point. The measurements on an area of corrosion comparable with obtained. The properties of barrier epoxy/amine and epoxy/ phenolic coated soft steel can be estimated with EIS when a specimen is exposed to 3.5% sodium chloride solution in the atmosphere [30].
In a single step cycle of performance, EIS became a strong technique to study the properties of electrochemistry and chemistry at the interface/barrier of metal-electrolyte [42, 43]. Even if a small ac-current or voltage is applied in the EIS technique, it does not have a significant effect on electrochemical activity in an electrochemical cell. The information is well known if the process occurs in the electrolytes with low conductivity. Since this technique uses direct current processes without free error, the potential can estimate the phenomenon at the interface between metal and electrolyte. Hence, this technique is used to measure the capacitance of electrode, the mechanical processes of electrochemical activity and corrosion on the kinetics of charge transfer. EIS technique used to measure the resistance of polarization with more accuracy. The use of multi-frequency excitations made possible measuring the capacity of processes of corrosion at distinct rates. Bode and Nyquist plots were used for the analysis of data related to impedance. Moreover, it can be necessary to obtain the same results of ac for Bode diagrams and an analogue circuit. It can be achieved by adjusting the resistances and capacitances.
At grain boundaries, the localized corrosion like cracks and pits can be used for an evaluation of such corrosion rates which is quite difficult using the EIS technique [44]. Recently, the estimation of localized corrosion process was done using scanning electrochemical microscopy (SECM), localized electrochemical impedance spectroscopy (LEIS), and scanning Kelvin probe (SKP) [45, 46]. Subsequently, these techniques were used to evaluate the properties of the passive film [47, 48]. Spatial resolution electrochemical spectroscopy dependency of LEIS technique was used to measure the corrosive resistant materials capacitance to inhibit the occurrence of corrosion process. These were wear testing corrosion, pit growth corrosion, and coating degradation. This method was used to measure the variations during the growth of pit corrosion [49, 50]. The authors reported that the limitations in spatial resolution and the mathematical formulation of this method can be controlled using the known parameters [51-56]. Even though numerous results were reported in this field, the illustration of the localized corrosion mechanism can be understood as well in the present cases [57].
The capacitance of coating may lead the primer variation in the properties of the coating, and it can be determined using the EIS technique [58]. The previous scientists reported that [59] the protection polymer coatings were studied using EIS tool. Moreover, the data of EIS can be analyzed, and simulated by various methods. In the case of protective coating dopant, element dependency model, it introduced the impedance of Warburg [60] to plot the spectra of electrochemical impedance. The literature [61] describes the applications of EIS for the estimation of the properties of anticorrosive coatings and the studies on inhibitors to prevent corrosion in metal and alloy-based coatings, passivated films. The corrosion behavior can be studied using the EIS method in various fields like biomedical, reinforced concrete, and microbiological. At certain dynamic conditions, the modern impedance technique was used, which is known as dynamic electrochemical impedance spectroscopy (DEIS) [62, 63]. Since it depends on modern dynamic electrochemical techniques like pulse cyclic voltammetry, this powerful technique can be used to measure the rate of generation and repeated passivation of pits with intermediate stable.
This chapter explained the various accelerated corrosion tests, namely salt fog, modified salt spray, acidified test, salt/SO2 test, CASS test, and cyclic corrosion test. The test specimen was corroded under salt spray exposure. Electrochemical techniques were employed to coated and painted samples to measure the corrosion resistance. Linear polarization method measures the polarization resistance of coated specimen which can be used as a working electrode in an electrochemical cell. OCP vs. time measurements of the samples revealed that the pit corrosion potential was decreased while increasing OCP. The potentiodynamic polarization estimates the corrosion resistance of coated test samples using electrochemical cell. The EIS technique can be the response of the electrochemical cell to the applied ac-potential. The impedance is, in general, the ratio of ac-voltage to ac-current. The Bode and Nyquist plots of tested samples were analyzed through equivalent circuits which were used to measure the corrosion resistance.
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