Abstract
Fifteen percent hydrochloric acid (HCl) solutions are used for some cleaning processes in the petroleum industry. The use of such a corrosive medium is mainly responsible for the corrosion of the stainless steel (SS-410) vessels and pipings. In this study, the corrosion inhibiting properties of Oryza sativa plant extract (OSPE) from agricultural residues are investigated on SS-410 steel surfaces in a 15% HCl medium. Gravimetric analysis showed a maximum corrosion inhibition of 91.92% with 4 g/L OSPE in 15% HCl solution. Scanning electron microscopy (SEM), atomic force microscopy (AFM), and X-ray diffraction studies confirmed the adsorption of OSPE on the SS-410 surface. The adsorption of OSPE on SS-410 followed the Langmuir adsorption isotherm, indicating the formation of a monolayer on the SS-410 surface. The theoretical study confirmed that the anticorrosive effect could be mainly related to the phytochemical 9,12,15-octadecatrienoic acid 2,3-dihydroxypropyl ester. Consequently, the OSPE containing this phytochemical shows an anticorrosive behavior on the SS-410 surface in an acidic 15% HCl solution.
1 Introduction
Every year around 75,000 billion USD are lost due to corrosion. It accounts for 3.4% of world’s GDP loss. In India, corrosion causes loss of 1670 billion USD which is equivalent to 4.2% of the total GDP [1]. Metal corrosion is one of the biggest problems faced by many industries. Efforts are continuously being made to find suitable solutions to this major issue [2], [3], [4], [5], [6], [7]. Fe–Cr–C alloys have been specially developed for components requiring higher mechanical strength and high to medium corrosion resistance. The 400 series stainless steel is one of the martensitic steels widely used in the petroleum industry, especially in oil production and refining for turbine components, fasteners and machine parts [8].
Various industrial processes namely acid pickling, acid cleaning, and descaling, oil well acidization utilizes mineral acids. HCl and sulfuric acid (H2SO4) are commonly used mineral acids [9]. Use of H2SO4 leads to the formation of insoluble products. Therefore, petroleum industries mostly use 15% HCl for descaling purpose as no insoluble products are left after the treatment. In addition, the process is commercially feasible and cost-effective. The use of HCl also has some limitations as it affects the metallic surface of the machine parts during the cleaning process, leading to corrosion [10].
The destruction of metal components can be avoided by using corrosion inhibitors [11, 12]. Most inhibitors that are used in an acid-aggressive environment and prevent the dissolution of the metal by acid attack contain organic compounds as the main components. These compounds contain nitrogen, oxygen and/or sulfur atoms, heterocyclic compounds and π-electrons. The inhibitors for acidic environments are absorbed on the surface of stainless steel by physisorption or chemisorption or both and thus prevent corrosion. Among the different types of corrosion inhibitors, so-called green corrosion inhibitors are preferred as they are environmentally friendly and cost-effective. Green corrosion inhibitors based on plant extracts are of particular interest. The use of plant waste in the extraction of the plant extracts is particularly noteworthy, as it additionally reduces the accumulation of waste in the environment and helps farmers to earn money from waste [13], [14], [15], [16].
Oryza sativa is a grass diverse genus with 25–30 species of deciduous flowering plants in the family Poaceae and is also known as Chawal or Kanak in India. The image of the O. sativa plant is shown in Figure 1 [17]. The O. sativa residues contain various types of phytochemicals as mentioned in Figure 1. After harvesting the seeds most of the vegetative residues are unutilized and discarded to end up as waste in the environment. Most of these residues are burned in India as there are no strategies to fully recycle them, thus the residues contribute to environmental pollution.
The aim of this work is to explore the adsorptive and corrosion inhibiting properties of O. sativa plant extract (OSPE) in order to obtain statements on the use of OSPE as a corrosion inhibitor on SS-410 surfaces in 15% HCl. This work focuses on the efficient use of O. sativa plant residues, which have so far been treated as waste.
2 Experimental
2.1 Oryza sativa plant extract and working electrode preparation
For the preparation of the working electrode, stainless steel samples SS-410 with a diameter of 10 mm were immersed in epoxy resin. The elemental composition of the stainless steel used was Fe (87.2%), Cr (11.14%), Mn (0.82%), Cu (0.43%), C (0.134%), P (0.02%), and Si (0.005%). The surface of the working electrode was abraded with 100, 320, 600, 800, 1000, and 1200 grit emery paper.
O. sativa plant waste was collected from agricultural land near Jalandhar, Punjab, India and its identification was done by Botanical Survey of India, Dehradun. The plants were dried in the sun shade for two days and ground into powder. Hundred grams of the powder was extracted with 450 ml methanol at 75 °C for 72 h. The extracted solution was filtered. The pH of the aqueous solution was nine.
The filtrate was evaporated using a Soxhlet evaporator. The resulting liquid extract was then completely dried in a vacuum desiccator to obtain OSPE. The OSPE was then dissolved in 15% HCl. This solution is used as the corrosive medium in the following. Corrosive medium solutions with different concentrations of OSPE (1 g/L, 2 g/L, 3 g/L, and 4 g/L) were prepared.
2.2 Weight loss measurement
To determine the weight loss, tests were carried out with (1–4) g/L OSPE in 15% HCl medium at room temperature for 24 h [18]. The SS-410 samples measuring 5 cm × 5 cm × 0.3 cm were weighed and immersed in the test solutions both in the presence and absence of OSPE for 24 h. Then, the SS-410 samples were removed from the test solution, rinsed with acetone, dried under nitrogen flow, and weighed.
2.3 Electrochemical impedance spectroscopy
Auto lab electrochemical work station (Metrohm) with three-electrode electrochemical cell was used for the measurements of the electrochemical impedance and the Tafel polarization. The obtained Tafel polarization curves were recorded between −200 mV and +200 mV versus Ag/AgCl (3 M KCl) with a scanning rate of 0.1 mV/s. The electrochemical measurements were conducted at 10 mV amplitude in a frequency range from 100 kHz to 0.01 Hz. The obtained data were calculated by using CHI 760C electrochemical work station software.
2.4 Fourier Transform Infra-Red (FTIR) spectroscopic study
The Fourier Transform Infra-Red (FTIR) spectra were recorded between (500–4000) cm−1 to identify the functional groups present in the phytochemicals of the OSPE. The FTIR 8400S spectrophotometer (Shimadzu) was used for FTIR measurements. The FTIR spectra of OSPE were also recorded at different conditions prior to immersion of SS-410 in 4 g/L OSPE in 15% HCl.
2.5 Ultraviolet-visible spectroscopic study
The preliminary anticorrosion activity of OSPE prepared in 15% HCl solution were investigated using UV-vis 1800 spectrophotometer (Shimadzu). The UV-vis analysis was performed using two set of experiments. In both set of condition, SS-410 was immersed in HCl solution. In the first set of conditions, the UV-vis spectrum of 15% HCl solution containing 4 g/L OSPE was recorded. In the second set of condition, the spectrum was recorded for 15% HCl solution in absence of OSPE.
2.6 Surface investigation
2.6.1 Atomic force microscopic study
The INTEGRA atomic force microscopy (AFM) model (NT-MDT) was used to study the stainless steel surface SS-410. For the AFM study, the SS-410 surface was cleaned with ultrapure water and then with acetone. Samples of the abraded SS-410, the SS-410 immersed in corrosive media and the SS-410 immersed in 15% HCl solution with 4 g/L OSPE were characterized by AFM.
2.6.2 Scanning electron microscopic analysis
The scanning electron microscope (SEM, JEOL) was used for taking the surface micrograph of SS-410. SEM images were captured for polished SS-410 and SS-410 samples immersed in corrosive media in the absence and presence of 4 g/L OSPE.
2.6.3 X-ray diffraction (XRD) analysis
The PHI 5000 Versa Probe III model (Physical Electronics, Inc.) was used for the XRD study. Prior to measurement, the SS-410 stainless steel samples were immersed in a 15% HCl solution with and without 4 g/L OSPE, then the SS-410 samples were dried and measured using the above instrument. The corrosion inhibitor adsorption process on the SS-410 surface was explained on the basis of the XRD study.
2.7 Theoretical studies
The computer programme Hyperchem (8.0) was used for the theoretical studies of the corrosion protection effect of the phytochemicals contained in OSPE. The experiments were analyzed using density functional theory (DFT). The energies of the frontier molecular orbitals were used as the main parameters for this evaluation.
3 Results and discussion
3.1 Weight loss measurement
Corrosion inhibition efficiency (IE) of OSPE was calculated for the surface of SS-410 in the presence of 15% HCl medium. The rate of SS-410 corrosion in corrosive media containing different concentration of OSPE was calculated using Equation (1):
where, C R is the corrosion rate (mm year−1), W is the weight loss of stainless steel (SS-410), K the corrosion constant (8.76 × 104), A is the exposed area in cm2, t is the immersion time (h) of SS-410, ρ is the density (7.86 g cm−3) of the steel according to the ASTM G 31-72 standard [19].
The value of corrosion IE and surface coverage (θ) of OSPE was calculated by Equations (2) and (3):
where, the corrosion rate of SS-410 immersed in the corrosive media (15% HCl) and the corrosive media containing OSPE solution was mentioned by
Concentration | Corrosion rate CR/mmy−1 | Inhibition efficiency IE/% | Surface coverage θ | C/θ | Equilibrium adsorption constant Kads/L g−1 |
---|---|---|---|---|---|
15% HCl | 39.01 | ||||
15% HCl + 1 g/L OSPE | 13.181 | 66.21 | 0.6621 | 1.51 | 1.96 |
15% HCl + 2 g/L OSPE | 9.630 | 75.31 | 0.7531 | 2.65 | 1.53 |
15% HCl + 3 g/L OSPE | 6.120 | 84.31 | 0.8431 | 3.55 | 1.81 |
15% HCl + 4 g/L OSPE | 3.152 | 91.92 | 0.9192 | 4.35 | 2.85 |
3.2 Adsorption isotherm studies
Adsorption isotherms are generally used to obtain information on the nature of the interaction of molecules on the substrate surface (here: stainless steel SS-410) by adsorption. In this work, the experimental data were fitted using the adsorption isotherms of Langmuir, Temkin, Frumkin, Freundlich, Flory-Huggins, and El-Awady (Equations (4)–(9)):
The value of regression coefficient (R 2) follows the order: Langmuir isotherm > Freundlich isotherm > Temkin isotherm > El-Awady isotherm > Flory-Huggins isotherm > Frumkin isotherm, as shown in Figure 2A–F. It can be concluded that the adsorption of OSPE on SS-410 best follows the Langmuir adsorption isotherm, since in this case the value of R 2 is closest to one compared to those of the other isotherms. The Langmuir isotherm could indicate that one or more inhibitor units occupy multiple adsorption sites. It also seems to indicate that interactions occur between the metal surface and the OSPE species adsorbed on the SS-410 surface or that a change in the heat of adsorption (enthalpy) occurs with increasing surface coverage [20]. Therefore, Langmuir adsorption isotherm was used for explaining the adsorption behavior of OSPE on the SS-410 surface. The concentration of OSPE used and the value of OSPE surface coverage provided to SS-410 were the main parameter of this study. The function of C/θ and C was recorded and plotted in Figure 2A. K ads is used for equilibrium adsorption constant (Table 1).
3.3 Electrochemical study
3.3.1 Potentiodynamic polarization
The working electrode of SS-410 was immersed in 15% HCl solutions with fixed OSPE concentrations of 1 g/L, 2 g/L, 3 g/L, and 4 g/L. As the results in Table 2 show, the current densities decrease with the increase of OSPE concentration from 1 g/L to 4 g/L.
Corrosive solution | Corrosion potential Ecorr/mV | Corrosion current density I corr/A cm−2 | Inhibition efficiency IE/% |
---|---|---|---|
15% HCl solution | −474.1 | 0.000054003 | – |
15% HCl solution + 1 g/L OSPE | −352.0 | 0.000035064 | 35.07 |
15% HCl solution + 2 g/L OSPE | −352.6 | 0.000032634 | 39.57 |
15% HCl solution + 3 g/L OSPE | −350.0 | 0.000019284 | 64.29 |
15% HCl solution + 4 g/L OSPE | −358.4 | 0.000012615 | 76.64 |
The value of IE was calculated using Equation (10) [21].
where
The polarization curve is shown in Figure 3. The potential scans were performed in the positive direction. The observed behavior indicates that the more inhibitor present in the solution, the better the protection of SS-410. In addition, the results showed that the rate at which OSPE adsorbs on SS-410 depends on the OSPE concentration. The higher the OSPE concentration in the corrosive media, the lower the corrosion current density value, which means an increase in IE.
It has already been reported that the inhibition is anodic when the maximum shift of the corrosion potential (E corr) in the acidic solution is greater than 85 mV [22, 23]. It can be concluded that OSPE follows an anodic inhibition mechanism. The OSPE inhibitor is adsorbed on the SS-410 surface, forming a protective film or barrier that causes a large anodic shift, thereby reducing the corrosion rate. In addition, the potential shift forces the metallic surface into the passivation region. With 4 g/L OSPE in 15% HCl solution, a maximum IE of 76.44% was achieved.
3.3.2 Electrochemical impedance spectroscopy
The working electrode of SS-410 was immersed in 15% HCl solutions with different concentration of OSPE. Figure 4 shows the Nyquist plots. Each of the curves shown contains a semicircle representing a constant time, which is due to the charge transfer resistance. As the OSPE concentration increases from 1 g/L to 4 g/L, the diameter of the circle increases. However, this also means an increase in IE, which was calculated using Equation (11) [8].
Here R
ct and
Corrosive solution | Charge transfer resistance R ct/Ω cm−2 | Inhibition efficiency IE/% |
---|---|---|
15% HCl solution | 180.21 | – |
15% HCl solution + 1 g/L OSPE | 258.73 | 30.34 |
15% HCl solution + 2 g/L OSPE | 285.78 | 36.94 |
15% HCl solution + 3 g/L OSPE | 439.48 | 58.99 |
15% HCl solution + 4 g/L OSPE | 667.57 | 73.00 |
It was found that the corrosion rate increases with increasing temperature in HCl solutions without OSPE as well as in HCl solutions with OSPE. Similarly, it was observed that the inhibition effect of the inhibitor decreases with decreasing temperature. The interface between the electrode and the adjacent solution forms a boundary layer known as the double layer capacitance (dlc). It is an important feature of the electrical double layer. At the boundary between the two layers, the charges on the surface of the electrode and the electrolyte are opposite. The dlc values decreased with increasing OSPE concentration. This decrease indicates the adsorption of molecules form the OSPE solution on the surface of SS-410.
The electrochemical impedance spectroscopy (EIS) results agreed with the potentiodynamic polarization (PDP) results. Based on the results, it can be assumed that the active components of the OSPE are involved in the chemical adsorption on the SS-410 surface. The IE decreased with increasing incubation temperature and increased with increasing OSPE concentration. This is due to the fact that OSPE tends to adsorb more on the SS-410 surface at lower temperatures and higher OSPE concentration. The observed difference between the percentage IE values obtained with EIS and PDP could be due to the different nature of the technique used. PDP measurements provided the real-time kinetics of the electrochemical processes (polarization in a wide potential range with a possible irreversible change due to the measurement process), while EIS data are usually obtained at the OCP (open circuit potential) and provide measurements of the total interfacial resistance at the electrode-electrolyte interface [26, 27].
3.4 FTIR spectroscopic study
The FTIR spectrum presented in Figure 7 indicates the presence of the different functional groups in the OSPE. The peak at 3327 cm−1 indicates the presence of the O–H group and the peak at 988 cm−1 indicates the C=O stretching. The peak at 1429 cm−1 can be attributed to the vibrations of the aromatic ring. The corrosion-inhibiting property of OSPE can be attributed to the heteroatoms present in the extract [26, 27].
3.5 UV-visible spectroscopic study
Figure 8 shows the UV-vis spectra of OSPE in 15% HCl solutions before and after immersion of the stainless steel sample SS-410. A higher UV-vis absorption intensity was observed for the OSPE solution before immersion of the stainless steel sample compared to the OSPE solution after immersion of SS-410 sample (after the corrosion test). In both cases, peaks representing the π–π* and n–π* transitions are observed at 214 nm and 360 nm, respectively. The intensity of the visible UV peak of OSPE in 15% HCl solution after the stainless steel sample was immersed, was lower compared to the sample before immersion of SS-410. This decrease in peak intensity clearly shows the adsorption of OSPE components on the SS-410 surface, causing the free (not adsorbed) components to decrease, resulting in a decrease in peak intensity [28, 29].
3.6 Surface investigation
3.6.1 Scanning electron microscopy
The surface morphology of SS-410 in 15% HCl solution was analyzed by SEM. Figure 9 shows SEM images of (A) an abraded SS-410 sample, (B) an SS-410 sample immersed in 15% HCl solution without OSPE, and (C) an SS-410 sample immersed in 15% HCl solution with 4 g/L OSPE. From the SEM analysis, the SS-410 sample immersed in 15% HCl solution shows a rough and corroded surface, while the surface of the SS-410 sample immersed in OSPE with 15% HCl solution appears smooth due to the corrosion-inhibiting effect of OSPE [30, 31].
3.6.2 Atomic force microscopy
Figure 9 shows the images of (A) the abraded SS-410 sample, (B) the SS-410 sample immersed in the 15% HCl solution without OSPE, and (C) the SS-410 sample immersed in the 15% HCl solution with 4 g/L OSPE solution obtained by AFM. The value of surface roughness for the abraded SS-410 sample and the SS-410 sample immersed in 15% HCl solution are 26.83 nm and 939.14 nm, respectively. The significant increase in surface roughness after immersion in the HCl solution without OSPE indicates the degree of corrosion, as the surface of the abraded SS-410 samples loses smoothness due to corrosion [32, 33]. The SS-410 sample immersed in HCl with 4 g L−1 OSPE had a comparatively lower surface roughness of 311.67 nm, which can be attributed to the corrosion-inhibiting effect of the phytochemicals contained in the OSPE.
3.6.3 X-ray diffraction (XRD) study
XRD spectra were obtained for SS-410, SS-410 immersed in 15% HCl and SS-410 immersed in 15% HCl with 4 g/L OSPE. It can be seen from Figure 10 that the intensity of the iron peak at (40–50)° is weak in the case of the SS-410 sample immersed in 15% HCl compared to the unexposed SS-410 sample and the SS-410 sample immersed in HCl with OSPE. The presence of iron oxide peaks at (20–30)° in the SS-410 sample immersed in 15% HCl without OSPE also confirmed the formation of iron oxide as a result of corrosion. These peaks were absent in the unexposed SS-410 sample and in the SS-410 sample immersed in 15% HCl with 4 g/L OSPE. The XRD study confirms the protective effect of OSPE against corrosive media on the surface of SS-410 [34].
3.7 Theoretical studies
3.7.1 Frontier molecular orbitals and their parameters
The frontier molecular orbital density distributions (LUMO and HOMO) of the optimum structures of phytochemicals presents in OSPE are shown in Figure 11. The key parameters of quantum chemical calculations are: energy of the highest occupied molecular orbital (E
HOMO), energy of the lowest unoccupied molecular orbital (E
LUMO), the energy gap between LUMO and HOMO (ΔE), the back donation energy (
The change in the parameters of the theoretical study make clear how the phytochemicals contained in the OSPE interacted with the SS-410 surface (see Table 4). The energy of highest occupied molecular orbital follows the order: 9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester > tetradecanoic acid > 28-homotyphasterol which indicated the order of donation of electrons to the vacant orbital of iron. 9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester has the lowest ΔE (1.339 eV), demonstrating the good stability of the [9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester-Fe] complex. The higher value of ΔE-back donation of 9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester compared to the other two compounds shows the higher stability of the [Fe-9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester] complex. Hence, the inhibition effect follows the order 9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester > tetradecanoic acid > 28-homotyphasterol. Therefore, 9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester can be assumed to be the most essential component in the inhibition performance of the OSPE.
S. no | Phytochemicals | E HOMO/eV | E LUMO/eV | ΔE/eV | η/eV | σ/eV−1 | ΔE B.D/eV |
---|---|---|---|---|---|---|---|
1 | tetradecanoic acid | 18.960 | 20.629 | 1.669 | 0.834 | 1.199 | −0.417 |
2 | 9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester | 1.226 | 2.719 | 1.493 | 0.746 | 1.339 | −0.186 |
3 | 28-homotyphasterol | −6.487 | −1.234 | 5.253 | 2.626 | 0.380 | −0.656 |
3.7.2 Mulliken charge distribution
Mulliken charges have long been employed to investigate the adsorption active sites and the donor-acceptor electron interaction between inhibitor and iron atoms [3, 4, 39, 40]. In the gas phase, the optimal shape and Mulliken charges of neutral and protonated inhibitor atoms were studied. Table 5 represented the C and O atomic charges derived via Mulliken charges in this study. The major active atoms that could form coordinating bonds due to the lone electron pairs and empty d-orbital of iron atoms were: O9 and O20 for tetradecanoic acid, O1, O5, O8, and O37 for 9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester, and O19, O27, and O36 for 28-homotyphasterol. In addition, some carbon atoms in protonated inhibitors have a significant negative charge, which might function as active sites.
Tetradecanoic acid | |||||
---|---|---|---|---|---|
Atom | Mullikin charge | Atom | Mullikin charge | Atom | Mullikin charge |
C1 | −0.065 | C7 | 0.260 | C15 | 0.704 |
C2 | −0.044 | O9 | −0.431 | C16 | −0.301 |
C3 | 0.0895 | C11 | −0.065 | O20 | −1.105 |
C4 | −0.037 | C12 | 0.044 | ||
C5 | 0.069 | C13 | 0.008 | ||
C6 | −0.041- | C14 | −0.040 | ||
9,12,15-octadecatrienoic acid-2,3-dihydroxypropyl ester | |||||
O1 | −0.387 | C11 | −0.110 | C20 | −0.096 |
C2 | 0.199 | C13 | −0.079 | C21 | −0.864 |
C3 | 0.146 | C14 | 0.008 | C22 | −0.887 |
C4 | 0.200 | C15 | 0.410 | C23 | −0.100 |
O5 | −0.396 | C16 | 1.142 | C24 | −0.482 |
C7 | 0.152 | C17 | −0.133 | C25 | −0.192 |
O8 | −0.403 | C18 | 0.295 | C26 | −0.145 |
C10 | −0.589 | C19 | −0.440 | O37 | −1.05 |
28-homotyphasterol | |||||
C1 | −0.011 | C12 | −0.081 | C24 | 0.017 |
C2 | −0.077 | C13 | −0.122 | C25 | −0.292 |
C3 | 0.220 | C14 | −0.093 | C26 | −0.146 |
C4 | −0.080 | C15 | −0.081 | O27 | −0.99 |
C5 | −0.010 | C16 | −0.078 | O29 | −0.399 |
C6 | 0.024 | C17 | −0.027 | C31 | −0.010 |
C7 | 0.419 | O19 | −0.578 | C32 | −0.145 |
C8 | −0.064 | C20 | −0.009 | C33 | −0.038 |
C9 | −0.016 | C21 | 0.203 | C35 | 0.287 |
C10 | −0.155 | C22 | 0.153 | O36 | 0.399 |
C11 | −0.003 | C23 | −0.014 |
3.7.3 Proposed mechanism of adsorption
The mechanism of corrosion inhibition of SS-410 by OSPE in 15% HCl solution can be explained on the basis of molecular adsorption. There are two possible mechanisms: i) the donor-acceptor interactions between the π-electrons of OSPE and the empty d-orbitals of the SS-410 surface; ii) the interaction between the electrons of the heteroatoms in the inhibitor and the empty d-orbital of iron in SS-410, as shown in Figure 12. Many researchers have investigated plant extracts for their corrosion inhibitory potential in acidic media, especially in HCl, at different extract concentrations. In these studies, higher concentrations of plant extracts were also used in less acidic media. In the present study, the corrosion inhibitory properties of OSPE in 15% HCl solution were investigated to address the problem of petroleum industry in real time. Since plant wastes are used as inhibitor source, the use of OSPE in higher concentration would not affect the environment. The comparative analysis of some of the reported plant inhibitors with the plant we studied, O. stavia, is shown in Table 6 [40], [41], [42], [43], [44], [45], [46], [47], [48], [49], [50], [51], [52].
Plant name | Concentration/g L−1 | Corrosive media | Inhibition efficiency/% | Reference |
---|---|---|---|---|
Oryza sativa | 4.0 | 15% HCl | 91.92 | Present study |
Marrubium vulgare L. | 8.0 | 1 M HCl | 86.51 | [40] |
Tender arecanut | 4.5 | 0.5 M HCl | 95.50 | [41] |
Polyaspartic acid | 10 | 5 M H2SO4 | 80.33 | [42] |
Pectin | 8 | 2 M HCl | 94.40 | [43] |
Matricaria recutita | 7.2 | 1 M HCl | 93.28 | [44] |
Opuntia ficus indica | 5.0 | 1 M HCl | 91.76 | [45] |
Malus domestica | 5.0 | 0.5 M HCl | 87.9 | [46] |
Ocimum basilicum L. | 5.7 | 0.5 M HCl | 90.10 | [47] |
Citrus sinensis | 4.0 | 5 M HCl | 93.38 | [48] |
Barley agriculture waste | 5.0 | 1 M HCl | 97.10 | [49] |
Phyllanthus muellerianus | 6.7 | 3.5% NaCl | 97.58 | [50] |
Verbena | 6.0 | 1 M HCl | 81.10 | [51] |
Thymus vulgaris | 10.0 | 5 M H2SO4 | 88.60 | [52] |
Xylopia aethiopica | 10.0 | 5 M H2SO4 | 47.80 | [52] |
Zingiber officinale | 10.0 | 5 M H2SO4 | 79.60 | [52] |
4 Conclusions
OSPE was investigated as a corrosion inhibitor for SS-410 stainless steel. Various techniques confirmed the corrosion-inhibiting effect of OSPE. Gravimetric analysis showed a maximum of 91.92% at a concentration of 4 g/L OSPE in 15% HCl solution. PDP analysis showed that OSPE exerted mixed corrosion inhibition. SEM and AFM studies confirmed a remarkable change in the morphology of the SS-410 surface when exposed to a corrosive solution; the presence of OSPE attenuated the corrosive effect of the HCl solution. The mechanism of corrosion inhibition is based on adsorption. The adsorption of the inhibitor molecules was best fitted with the Langmuir adsorption isotherm. The theoretical quantum chemical calculations also supported the corrosion inhibition due to adsorption of inhibitor molecules from the OSPE. The parameters studied also showed that the 9,12,15-octadecatrienoic acid 2,3-dihydroxypropyl ester present in the OSPE was mainly responsible for the corrosion inhibitory performance.
About the authors
Nishant Bhardwaj received his M.Sc. degree in Industrial Chemistry from Punjab University, India in 2016 and his B.Sc. degree in Industrial Chemistry from Kurukshetra University, India. He is currently pursuing his Ph. D in Organic Chemistry, under the supervision of Dr. Vineet Kumar, School of Biosciences and Bioengineering, Lovely Professional University, India. His research area mainly focuses on the development of effective green corrosion inhibitors for metal protection for industrial applications.
Pooja Sharma received her M.Sc. degree in Biotechnology from DAV University, India in 2017 and her B.Sc. degree in Medical Lab Technology from Punjab Technical University, India. She is currently pursuing her Ph. D in Biotechnology under the supervision of Dr. Vineet Kumar, School of Biosciences and Bioengineering, Lovely Professional University, India. Her research focuses on synthesis of green nanomaterials and their applications in biomedical corrosion and also the development of nanomaterials for theranostic applications.
Vineet Kumar is currently working as Assistant Professor at the Department of Biotechnology, LPU, Jalandhar, India. Previously he was UGC-DSK postdoctoral fellow (2013-2016) at Panjab University, Chandigarh, India. His areas of interest include natural plant products, green synthesis of nanoparticles, nanotoxicity testing and application of nanoparticles. He has published many articles and books in these areas. He is also serving as editorial board member for various journals. https://orcid.org/0000-0002-8772-679X.
Acknowledgment
Authors are thankful to Lovely Professional University for the support and the provision of the central instrumental facility.
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Author contributions: All the authors have accepted responsibility for the entire content of this submitted manuscript and approved submission.
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Research funding: None declared.
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Conflict of interest statement: The authors declare no conflicts of interest regarding this article.
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