Startseite Performance of green corrosion inhibitors from biomass in acidic media
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Performance of green corrosion inhibitors from biomass in acidic media

  • Andrea Marciales

    Andrea Marciales received her BSc in chemical engineering from the Industrial University of Santander (UIS), Colombia. In 2011, Andrea joined the Colombian Petroleum Institute (ICP) as a consulting engineer for Ecopetrol. She later obtained her MSc in petroleum engineering from the University of Alberta in 2015, working on selection of solvent for unconventional recovery processes. In 2016, she worked as a research assistant at the University of Alberta, focusing on the development of green inhibitors and microbiologically influenced corrosion. In 2017, she joined InnoTech Alberta as a corrosion engineer.

    , Tesfaalem Haile

    Tesfaalem Haile obtained his PhD in civil and environmental engineering from the University of Western Ontario, London, Canada, in 2009. Tesfa has been working in R&D and corrosion consultancy since 2006. He leads several corrosion projects, including corrosion in oil sand thermal and mining operations, investigating MIC in Canadian onshore operations, and testing the efficiency of lignin as a corrosion inhibitor, among others. He is the principal investigator of the projects he manages.

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    , Behzad Ahvazi

    Behzad Ahvazi completed his Bachelor of Science in Honours program at the Department of Chemistry and Biochemistry, and graduated with distinction at Concordia University in Montréal, Québec. His PhD program was completed in 1998 at McGill. Currently, he is working at InnoTech Alberta as a Principal Researcher for Biomass Conversion and Processing Technologies, aimed at developing high-end value-added applications from pulp and lignocellulosic materials such as cellulose nanocrystals and lignin. Dr. Ahvazi is also an adjunct professor in the Department of Mechanical Engineering, University of Alberta.

    , Tri-Dung Ngo

    Tri-Dung Ngo obtained his PhD in mechanical engineering from Concordia University, Montreal, Canada, in 2007. He held a position as lecturer and researcher at Faculty of Chemical Engineering and thereafter Materials Engineering at HCM Polytechnic University from 1997 to 2002. He worked at National Research Council of Canada as a researcher from 2003 to 2014. Dr. Ngo joined InnoTech Alberta as a research scientist in 2014. His research focuses on biomass processing and development of novel, eco-friendly biomaterials. Dr. Ngo is also an adjunct professor at Department of Civil and Environmental Engineering, University of Alberta.

    und John Wolodko

    John Wolodko is currently the AI Strategic Chair in Bio and Industrial Materials, and an associate professor at the University of Alberta in Edmonton, Canada. His areas of research include the development and characterization of sustainable materials from agricultural and forestry feedstocks, life cycle assessment, and materials for the energy sector. Dr. Wolodko is a former Executive Director at AITF (formerly the Alberta Research Council), and has over 20 years R&D experience in advanced materials, manufacturing, testing, and engineering design.

Veröffentlicht/Copyright: 9. Februar 2018

Abstract

There has been a strong interest worldwide in developing suitable technologies that can derive chemicals and materials from renewable biomass in a number of applications, including corrosion inhibitors. In spite of the efficacy of conventional inhibitors in corrosion control, current corrosion inhibitors exhibit toxicity and/or are non-biodegradable. Therefore, industry efforts are leading to the development of non-toxic and environmentally friendly “green” corrosion inhibitors from renewable resources. Extensive studies of different bio-based inhibitors show that a vast number of phytochemicals can be used as efficient corrosion inhibitors. This paper provides a comprehensive review of the corrosion inhibition properties of plant-derived chemicals classified under the parameters provided by botanical chemistry.

1 Introduction

Carbon steel alloys are the workhorse materials in both conventional and non-conventional (oil sands) oil and gas industries. Their carbon content is <0.2% by weight, and the standard specification for seamless carbon and alloy steel mechanical tubing is composed of 0.15–0.2% C, 0.6–0.9% Mn, 0.04% P, and 0.05% S maximum (ASTM International, 2012). These materials are widely used in acidic media constituted by HCl concentrations of 15–25% wt for acidizing and well stimulation jobs (Schmitt, 1958) and corrosive environments with highly concentrated (5–28 wt%) acids, such as hydrochloric, hydrofluoric, acetic, and formic acids, among others, for current applications (Finsgar & Jackson, 2014). Despite their frequent utilization in refineries for plant piping and vessels, downhole tubulars, transmission pipelines, and service utility systems due to their relatively low cost, availability, and ease of fabrication (Bush et al., 2004; Dawson et al., 2010; Ghareba & Omanovic, 2010), they are susceptible to corrosion. Therefore, application of corrosion inhibitors is the most common method to control corrosion due their low cost (Foral & Al-Ubaidi, 1995; Finsgar & Jackson, 2014; Nassar et al., 2016). An inhibitor is a chemical substance that decreases or prevents the corrosion rate by selective adsorption on the metal surface when added in small concentrations to the environment (NACE International, 1973; Chawla & Gupta, 1993; Sastri, 2011; Sharma & Sharma, 2012).

Selection of corrosion inhibitors should take into consideration factors such as toxicity and biodegradability (Papavinasam et al., 2002; Dar, 2011; NACE International, 2014). Hence, industry efforts are leading to the development of non-toxic, biodegradable, and more environmentally friendly “green” corrosion inhibitors (Sharma & Sharma, 2012; Umoren & Eduok, 2016; Umoren et al., 2016) from renewable resources (Singh et al., 2010; Ibrahim et al., 2017). As a result, naturally derived chemicals and materials from renewable biomass (Kleinert & Barth, 2008; Singh et al., 2013), including plant extracts with heterocyclic compounds (Rehan, 2003; Dar, 2011), having nitrogen (Buchweishaija & Mhinzi, 2008; Cojucaru et al., 2009), sulfur (Chauhan & Gunasekaran, 2007), and phosphorus (Saratha & Meenakshi, 2010) as constituent atoms provided a viable alternative for the development of green inhibitors.

This paper provides a comprehensive review of bio-based derived inhibitors tested in strong acids and corrosive environment found in oil and gas applications. The bio-based inhibitors are therefore classified under the parameters provided by botanical chemistry.

2 Conventional chemical inhibitors

Depending on their mechanism of action, inhibitors are classified as anodic, cathodic, or mixed inhibitors. They can also be classified as organic and inorganic inhibitors (Chawla & Gupta, 1993). Anodic inhibitors (or passivators) interfere with the corrosion reaction by accepting electrons on the anode site; meanwhile, the cathodic ones are proton acceptors and they are adsorbed in the cathodic sites.

Additionally, inorganic inhibitors such as tungstate, monovanadate (Abdallah et al., 2006), chromate, zinc, and molybdate are some examples of anodic inhibitors used by the oil and gas industry to control carbon steel corrosion. In spite of their high inhibition efficiency (IE), the aforementioned chemicals are not considered environmentally friendly due to their toxicity to humans and animals (Chawla & Gupta, 1993; Sastri, 2011; LaBrosse & Donovan, 2015). Organic inhibitors are characterized by the presence of high-electron-density hetero atoms of nitrogen, sulfur, oxygen, and phosphorus of an aromatic and/or unsaturated character (Roebuck et al., 1957; Meakins, 1963; Luo et al., 1998; Bentiss et al., 2000; Lagrenée et al., 2001; El-Maksoud & Flouda, 2005; Jafari et al., 2014; Li et al., 2014b; Mazumder et al., 2014).

Most inhibitors are adsorbed at the metal-solution interface, and the efficiency of adsorption depends on their chemical nature, surrounding water chemistry, and type and state of the metal to be protected, as well as the electrochemical potential at the metal-solution interface (Sanyal, 1981). Inhibitors can be adsorbed onto the metal surface through (1) electrostatic attraction between the charged molecules of inhibitors and charged metal surface (electrostatic adsorption), (2) interaction of unshared electron pairs of the molecules with the metal surface, (3) π bond orbital adsorption by the interaction of the presence of conjugated bonds in the inhibitors with the metal, and (4) a combination of (1) and (3) (Khan et al., 2015).

The composition of an organic inhibitor is of great importance in contributing to its effectiveness (NACE International, 1973). Currently, the organic inhibitors most commonly used are characterized by the presence of the following functional groups, among others: nitrogen-based compounds such as amines (primary, secondary, tertiary, and quaternary), amides, esters, ethers, imines, and azoles; aromatic rings such as benzyl, benzoic, and phenyl-based compounds; sulfur-based group such as thiol, mercaptan, and sulfate; alcohol groups; and combinations of them.

The petroleum industry is the main target of corrosion inhibitor supplier companies; in addition, industries with cooling water systems also utilize considerable amounts of corrosion control chemicals, including biocides and oxygen scavengers. The oil and gas industry uses corrosion inhibitors for application in production systems for well stimulation (Quraishi & Jamal, 2001; Finsgar & Jackson, 2014; Singh & Quraishi, 2015), transmission lines (Farquhar et al., 1997; Chen et al., 2000; Benitez et al., 2002; Li et al., 2014a), refineries (Slavcheva et al., 1999; Subramaniyam, 2007), and storage (Watcher et al., 1951; Quraishi & Jamal, 2002; Cano et al., 2005; Tormoen et al., 2006). Imidazoline-based inhibitors are one of the most common chemicals used in sweet (CO2 and/or carbonic acid H2CO3) systems (Gusmano et al., 2006; Liu et al., 2011); amines and other nitrogenous heterocyclic compounds (aliphatic amines, pyridine, and substituted pyridines) are recommended to be used in sour (H2S-containing) environments (Durnie et al., 1999).

Cooling tower piping systems are another major facility known to consume organic inhibitors. These include polyphosphates (hexametaphosphate and metatripolyphosponate) in near-neutral media, phosphonic acids, phosphonates with 1,2,3-benzotriazole (BTA) or sodium benzoate, mercapto and thiazoles (2-mercaptobenzothiazole, 5-mercapto-1-phenyltetrazole) for the near-neutral pH range, aromatic-substituted carboxylates (mono- and dicarboxylic acids of the formula (CH2)n(COOH)2 with 0≤n≤8) with BTA additives at pH 7 or higher, N-lauroyl sarcosinate and sodium dodecyl sulfate (CH3(CH2)11SO4Na) in chloride solutions, polymer-polymer complexes of polymethacrylic acid and polyacrylamide, polypeptides (polyaspartates of M≈1000–2000) when carbonic acid is present, polyvinylpyrrolidone, polyamines, and polymines (polyethyleneimine) in the presence of NaCl, and polyguianidines (polyhexamethylene guanidine phosphate or chloride) for organic corrosion inhibitors (Amjad & Demadis, 2015).

3 Green corrosion inhibitors

Plant extracts containing heteroatoms such as O, N, and S have better adsorptive properties leading to better anti-corrosive behavior (Umoren & Eduok, 2016). Some examples include amino acids and vitamins, such as thiamin, riboflavin, nicotinic acid, tannins, alkaloids, polyphenols, gallic acids, volatile oils, resins, and aromatic oils. As a rule of thumb, N-containing compounds are efficient corrosion inhibitors in HCl solution, and sulfur-containing compounds perform better in H2SO4 media (Sharma & Sharma, 2012). Compounds derived from plant extracts are broadly classified as alkaloids, terpenes, and polyphenols according to botanical chemistry (Ramawat & Mérillon, 2013). The next sections present a summary of the efficiency of corrosion inhibition of the aforementioned chemicals in acidic media. Weight loss (WL) (ASTM International, 2011), potentiodynamic polarization (PP) or cyclic PP (CPP) resistance measurements (ASTM International, 1987; ASTM International, 2014), and electrochemical impedance spectroscopy (EIS) (Mansfeld et al., 1993) were used as test methods. Specimens were characterized by scanning electronic microscopy (SEM) (Khursheed, 2011), Fourier transform infrared spectroscopy (FTIR) (Smith, 2011), and X-ray diffraction (XRD) (Warren, 1990) after testing. The mechanisms of adsorption of the inhibitors studied were fitted to the available adsorption models, i.e. Langmuir, Freunlinch (Rosen & Kunjappu, 2012), Temkin, and Flory-Huggins isotherms (Bockris et al., 2000), along with thermodynamic calculations in order to define if chemical or physical adsorption on the metal was achieved (Rosen & Kunjappu, 2012).

3.1 Alkaloids

Alkaloids are a group of compounds containing nitrogen in the molecule bonded with at least two carbon atoms, and have at least one ring present in the chemical structure, which may or may not be heterocyclic. They are slightly soluble in water but soluble in ethanol, benzene, ether, and chloroform, and occur in the animal and vegetable kingdom (Aniszewski, 2015). The presence of nitrogen atoms is the main reason why alkaloids exhibit good adsorption properties on metallic surfaces. The bonds established during the adsorption process are attributed to the interaction between free electrons on the metal surface and the N atoms in the ring (Srivastava & Srivastava, 1981). Alkaloid inhibitors, after protonation, can compete with the anionic species of the acidic media (e.g. Cl, SO4−2) for sites at the anodic surfaces on the corroded metal. During the process, the protonated inhibitor losses its associated protons and enters the double-layer region, which eventually chemisorbs by donating electrons to the metal. Additionally, the protonated inhibitor electrostatically adsorbs onto the anion zone, through its cationic form (Bothi Raja & Sethuraman, 2009b). Berberine, an alkaloid extract found in Argemone mexicana (Srivastava & Srivastava, 1981) and Coptis chinensis (Li et al., 2005), showed optimum IE for cold rolled and mild steels with corresponding values of 79.8% and 98.3% sulfuric acid (Table 1). The PP experiments showed berberine as a mixed-type inhibitor affecting the anodic reaction at >1×10−4m H2SO4, and the negative value for the standard free energy of adsorption (ΔGoads=56.37 kJ/mol at 25°C) indicated chemisorption. In addition, the experimental data were better fitted to the Flory-Huggins isotherm, suggesting that one berberine molecule can replace three or more water molecule/iron atom when it is adsorbed on the steel surface (Li et al., 2005).

Table 1:

Inhibition efficiency of berberine alkaloids.

Test condition and method Extract concentration IE% Reference
2 n H2SO4, WL, 1 h 1% v/v 79.8 (Srivastava & Srivastava, 1981)
1 m H2SO4, WL, 3 h 5×10−3m 97.7 (Li et al., 2005)
PP, after 30 min exposure, aerated 5×10−3m 97.88
EIS, after 30 min exposure, aerated 5×10−3m 98.31

Calotropis procera, another plant with alkaloids as active ingredient, was tested for inhibition of steel in NaCl and sulfuric acid media. Srivastava and Srivastava (1981) investigated the corrosion inhibition potential of the aforementioned plant through the WL method using cold rolled mild steel as test specimen. They also tested C. procera leaves, flower, and fruits in 3% NaCl and the fruit in 2 n sulfuric acid media. Later, Bothi Raja and Sethuraman (2009a) studied the IE of the leaves from the same plant in 1 m solution of sulfuric acid when mild steel was exposed using WL, PP, EIS, and SEM. These authors attributed the good performance of C. procera extract to the presence of the calotropin alkaloid obtained from the different parts of this plant. The increase of IE corresponded well with increase of temperature during the experiments, indicating that the main mechanism of inhibition was attributed to chemical adsorption, as was also confirmed by thermodynamic analysis (ΔGoads50 kJ/mol). The data obtained by the experiments are summarized in Table 2. The results followed the Temkin isotherm, and the PP tests revealed that calotropin behaves as an anodic inhibitor (Bothi Raja & Sethuraman, 2009a).

Table 2:

Inhibition efficiency of Calotropis procera alkaloid extracts.

Test condition and method Extract concentration %IE Reference
3% NaCl, WL, 15 days 1% v/v (leaf, flower, or fruit) 73.7–78.7 (Srivastava & Srivastava, 1981)
2 n H2SO4, WL, 1 h 1% v/v (leaf and fruit) 75.3–76.5
1 m H2SO4, WL 1 h, 30°C, 50°C 15 ppm 94.02–95.17 (Bothi Raja & Sethuraman, 2009a)
1 m H2SO4, EIS 15 ppm 96.63
1 m H2SO4, PP 15 ppm 98.22

The leaves of Solanum trilobatum (Shymala & Kasthuri, 2011), Solanum tuberosum (Bothi Raja & Sethuraman, 2009b), and Solanum nigrum (Bothi Raja & Sethuraman, 2010) contain the solasodine alkaloid, which provides high IE in hydrochloric and sulfuric acid media, as portrayed in the values provided by Table 3. Bothi Raja and Sethuraman (2010) compared the efficiency of S. nigrum extract and the isolated solasodine molecule, finding it as the main active ingredient with inhibiting properties. All the PP experiments demonstrated that solasodine extracts behave as a mixed-type inhibitor. However, tests at different concentrations indicated that while the S. trilobatum results fitted to a Langmuir isotherm, those of S. tuberosum and S. nigrum followed the Temkin isotherm. These last two species also showed higher IE with increase in temperature, indicating chemisorption, in addition to decrease of activation energy in the presence of inhibitor (Eafree acid89.9kJmol vs. Eainhibitor69.8kJmol), as the dominant adsorption method (Bothi Raja & Sethuraman 2009b, 2010). Nevertheless, the time of exposure proved to slightly affect the performance of S. trilobatum extract, because the IE decreased from 90.2% to 86.2% when the time exposure increased from 3 to 24 h for the mild steel exposed to 1 n solution of HCl at 30°C (Table 3, row 9) (Shymala & Kasthuri, 2011). When comparing efficiency in different acid media, extracts from S. tuberosum was, in general, more effective in sulfuric acid than hydrochloric acid, probably because of lesser adsorption of sulfate ions in H2SO4 media, leaving more active sites available for the inhibitor to adsorb on the metal surface (Bothi Raja & Sethuraman, 2009b).

Table 3:

Corrosion inhibition efficiency of solasodine alkaloid extracts from Solanum trilobatum, Solanum tuberosum, and Solanum nigrum, and isolated solasodine from Solanum nigrum.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL 2 h, 30°C, 50°C 20 ppm 78.35, 91.37 (Bothi Raja & Sethuraman, 2009b)
1 m HCl, EIS, 25°C 20 ppm 76.12
1 m HCl, PP, 25°C 20 ppm 74.88
1 m H2SO4, WL 2 h, 30°C, 50°C 20 ppm 80.11, 93.28
1 m H2SO4, EIS, 25°C 20 ppm 80.99
1 m H2SO4, PP, 25°C 20 ppm 80.04
1 n HCl, WL 3 h, 30°C 8% v/v 83 (Shymala & Kasthuri, 2011)
1 n HCl, WL, 30°C, 3, 12, and 24 h 10% v/v 90.2, 88.6, 86.2
1 n HCl, 30°C, PP 10% v/v 90.8
1 n HCl, 30°C, EIS 10% v/v 91.4
1 m H2SO4, WL 2 h, 30°C, 50°C 50 ppm 96.7, 99.3 (Bothi Raja & Sethuraman, 2010)
1 m H2SO4, EIS 50 ppm 91
1 m H2SO4, PP 50 ppm 92
1 m H2SO4, EIS 4×10−3m 82
1 m H2SO4, PP 4×10−3m 80

The efficiency of alkaloids found in extracts of Datura metel (Sethuraman & Bothi Raja, 2005; Bothi Raja & Sethuraman, 2008a,b) and Datura stramonium (Bothi Raja & Sethuraman, 2007) have been studied for its IE protecting mild steel in hydrochloric and sulfuric acid media, with results summarized in Table 4. They all have the atropine compounds in common as active ingredients present in the leaves and seeds of these plants. Also, all PP results for D. stramonium extracts indicated mixed-type inhibition, with higher efficiency in sulfuric acid media than its hydrochloric counterpart. For the case of D. metel (Sethuraman & Bothi Raja, 2005), the authors also reported the presence of scopolamine in the obtained extract that chemisorbs on the metal surface and successfully fitted to both Langmuir and Temkin isotherms. A couple of years later, the same authors reported, in a separate work, the efficiency of isolated atropine sulfate (from the same plant seeds) in sulfuric acid media. In this work, they identified four centers of electron source (at the C=O, O-H, C-O-C, and II-electronic cloud of phenyl ring) on atropine molecule, forming atropine sulfate-Fe complex (Bothi Raja & Sethuraman, 2008a). The atropine from D. stramonium also chemisorbed, i.e. Eafree acid>Eainhibitor (as Eafree acid89.9kJmol, while Eainhibitor52.7kJmol) on the mild steel surface, and was fitted to the Temkin isotherm. As it was extracted with chloroform, its basicity led to protonation in acid media, being easily adsorbed on the cathodic sites to reduce H2 gas evolution (Bothi Raja & Sethuraman, 2007).

Table 4:

Inhibition efficiency of Datura metel and Datura stramonium alkaloid extracts in acid media.

Test condition and method Extract concentration %IE Reference
10% H2SO4, WL, 2 h, 30°C, 50°C 30% w/v 82.6, 84.4 (Sethuraman & Bothi Raja, 2005)
10% HCl, WL, 2 h, 30°C, 50°C 30% w/v 77.0, 87.9
10% H2SO4, EIS, 30±1°C 30% w/v 95.2
10% H2SO4, PP, 30±1°C 30% w/v 96.8
10% HCl, EIS, 30±1°C 30% w/v 70.1
10% HCl, PP, 30±1°C 30% w/v 74.9
1 m H2SO4, EIS, 30±1°C 2.4×10−4m 92 (Bothi Raja & Sethuraman, 2008a)
1 m H2SO4, PP, 30±1°C 2.4×10−4m 92
1 m HCl, WL, 2 h, 30°C, 50°C 20 ppm 69.9, 88.1 (Bothi Raja & Sethuraman, 2007)
1 m H2SO4, WL, 2 h, 30°C, 50°C 20 ppm 71.2, 91.5
1 m HCl, EIS, 30°C 20 ppm 70.61
1 m HCl, PP, 30°C 20 ppm 80.05
1 m H2SO4, EIS, 30°C 20 ppm 97.43
1 m H2SO4, PP, 30°C 20 ppm 94.98

Tobacco has also been studied as a potential green corrosion inhibitor for steel during the last three decades (Srivastava & Srivastava, 1981; Davis et al., 2001; Davis & von Fraunhofer, 2003; Loto & Popoola, 2011; Fouda et al., 2014; Bhawsar et al., 2015). With >4000 individual components in tobacco products, including alkaloids, fatty acids, and N-containing compounds (Davis et al., 2001; Davis & von Fraunhofer, 2003; Loto & Popoola, 2011; Fouda et al., 2014), nicotine (Srivastava & Srivastava, 1981) is the main active ingredient identified from the Nicotiana tabacum plant (Bhawsar et al., 2015). Srivastava and Srivastava (1981) tested the IE for 1% concentration of extract from dried tobacco leaves when samples of cold rolled mild steel were immersed in both 2 n H2SO4 and 2 n HCl solution. After 1 h of soaking time, they obtained 87.9% and 87.5% of IE through the WL method for H2SO4 and HCl, respectively. Afterwards, Davis et al. (2001) immersed mild steel in a 10% H2SO4 solution containing 5% of the extract from scrap burley twig and stem by-products of a tobacco processing plant. Through the WL method, they found how after 20 min of experiments, the mild steel samples emerged bright and shiny, and >86% of IE was observed. Later on, the same authors reported in a separate work (Davis & von Fraunhofer, 2003) about 90% IE for tobacco extract when a panel of steel was immersed in salt water after 62 days of experiments, with a visible thin layer of extract deposited on the sample surface. Loto and Popoola (2011) also tested the effectivity of mild steel inhibition for tobacco leaf extract in acid chloride solution (0.5 m H2SO4 and 5% NaCl). They found that 100% concentration of the extract provided the most positive result for inhibiting corrosion (94.21% efficiency) through the 21 days of WL experiments. Moreover, Fouda et al. (2014) reported chemisorption of components of tobacco leaf extract on the carbon steel surface following a Langmuir isotherm, acting as a mixed-type inhibitor in HCl solution, with optimum efficiency values between 90% and 98% obtained from WL, EIS, and PP tests, with %IE increasing with the increase of temperature (Table 5). Bhawsar et al. (2015) also reported that Nicotiana tabacum extracts followed Langmuir adsorption isotherms. Their results described physical adsorption phenomena (ΔGoads10 kJ/mol) with IE decreasing with increase of temperature when tobacco leaf extract was employed for protecting mild steel in H2SO4 solution, as also shown in Table 5.

Table 5:

Inhibition efficiency of tobacco and Nicotiana tabacum alkaloid extracts in acid media.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 25°C, 3 h 300 ppm 94.2 (Fouda et al., 2014)
1 m HCl, WL, 3 h, 35°C, 45°C 300 ppm 96.9, 98.3
1 m HCl, EIS, 25°C 300 ppm 90.4
1 m HCl, PP, 25°C 300 ppm 98.8
2 m H2SO4 WL, 6 h, 30°C, 40°C 10 g/l 94.13, 80.92 (Bhawsar et al., 2015)

The alkaloids extracted from Xylopia ferruginea (atheroline, aphorpine, and tetrahydroberberine) (Elyn Amira et al., 2011) were tested in 1 m HCl media and identified as predominantly anodic inhibitors (Bothi Raja et al., 2011). In a first study, Elyn Amira et al. (2011) compared the results from extracts obtained through different solvents: methanol/water (ME), hexane (HE), and chloroform (CP), as reported in Table 6. All the results successfully fitted to a Langmuir isotherm, evidencing physisorption (ΔGoads29.5 kJ/mol). Figure 1 shows the protonation of its cationic form of the N heteroatom and -NH group for the atheroline alkaloids present in this plant, as a mechanism of inhibition for this alkaloid. This was later confirmed by the FTIR analysis carried out by the same authors in their second report (Bothi Raja et al., 2011). These studies also showed that the extracts obtained from the bark of the plant provide better results than its leaves, as seen in the last section of Table 6.

Table 6:

Inhibition efficiency of Xylopia ferruginea alkaloid extract in HCl media.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 27±2°C, 2 h, ME, HE, CP 500 ppm 82–92 (Elyn Amira et al., 2011)
1 m HCl, PP, 27±2°C, ME, HE, CP 500 ppm 86–91
1 m HCl, EIS, 27±2°C, ME, HE, CP 500 ppm 82–93
1 m HCl, EIS, BK, and LV 30±2°C 100 ppm 88 and 87 (Bothi Raja et al., 2011)
1 m HCl, PP, BK, and LV 30±2°C 100 ppm 92 and 85
Figure 1: 
            Protonation of Xylopia ferruginea atheroline alkaloids in acid medium.
            Reproduced with permission from Elyn Amira et al. (2011).
Figure 1:

Protonation of Xylopia ferruginea atheroline alkaloids in acid medium.

Reproduced with permission from Elyn Amira et al. (2011).

Another plant studied for inhibition due to its alkaloid content is black pepper. This flowering vine contains piperine alkaloid, which is a condensation product of piperic acid and piperidine. These constituents were tested for inhibition of cold rolled steel in sodium chloride, hydrochloric acid (Srivastava & Srivastava, 1981), and sulfuric acid media (Srivastava & Srivastava, 1981; Bothi Raja & Sethuraman, 2008b). The results are shown in Table 7. When tested in H2SO4 media, the WL experiments confirmed an increase of IE with increase in temperature, indicating chemisorption (ΔGoads=42.31 kJ/mol) (Dahmani et al., 2010). The PP experiments for the black pepper extract showed mixed-type inhibition properly fitted to a Temkin isotherm. The presence of a chemisorbed layer was confirmed by the analysis of the SEM images obtained from metal substrates immersed in sulfuric acid solution in the presence of piperine extract (Bothi Raja & Sethuraman, 2008b).

Table 7:

Results for inhibition efficiency of piperine alkaloid extracts.

Test condition and method Extract concentration %IE Reference
3% NaCl, WL, 15 h 1 g/ml 25 (Srivastava & Srivastava, 1981)
2 n H2SO4, WL, 1 h 1 g/ml 76.9
2 n HCl, WL, 1 h 1 g/ml 87.5
1 m H2SO4, WL, 2 h, 30°C, 50°C 20 ppm ~91, ~95 (Bothi Raja & Sethuraman, 2008b)
1 m H2SO4, EIS 20 ppm 90
1 m H2SO4, PP 20 ppm 90

3.2 Terpenes and terpenoids

The terpenoids, sometimes called isoprenoids, can be described as modified terpenes, where methyl groups are replaced or removed, oxygen atoms removed or added (hydrogenated/dehydrogenated), or the carbon skeleton is modified by oxidation or rearrangement. Terpenoids are molecules constructed from two or more isoprene units of five carbon atoms (C5H8), and they are always present in the molecules of terpenes. Therefore, the general formula for most natural terpenoid hydrocarbon is (C5H8)n, where n represents the number of carbon atoms present in the structure (Ramawat & Mérillon, 2013).

Several plant extracts contain essential oils based in terpenoid units as active ingredient with inhibition properties effective for protection of steel in acidic media. Sharma et al. (2015) provided a review for the potential of Azadirachta indica triterpene extract as a corrosion inhibitor for mild steel in HCl, HNO3, and H2SO4 media. The authors found that extracts obtained from this plant behave as a mixed inhibitor that chemisorbs on the steel surface following the Langmuir isotherm. In addition, this study also reported several active ingredients, such as meliantrol, azadirachtin, nimbin, nimbidin, and salanin, as compounds present in this plant able to reduce biological corrosion caused by sulfate-reducing bacteria by approximately 50%.

Another example, Mentha pulegium, contains R-(+)-pulegone as the main ingredient of the pennyroyal essential oil extracted from this plant. This oil behaved as a cathodic corrosion inhibitor in HCl media, providing IEs around 72–80%, as depicted in the first three rows of Table 8. The experiments concluded that pulegone inhibited corrosion of steel by geometrically blocking the reduction of H+ ions on the cathodic sites, following the Frumkin isotherm model. This essential oil chemisorbs on the steel with the pulegone aromatic ring perpendicular to surface at low concentrations, changing to parallel orientation when the concentration of this extract is increased (Bouyanzer et al., 2006a,b). Another essential oil from a mint variety, Mentha rotundifolia, was also tested for corrosion inhibition of carbon steel in 1 m HCl solution by gravimetric, EIS, and polarization methods (Khadraoui et al., 2016). Their results suggested that menthalactone is the main active ingredient of this essential oil, and present mixed-type inhibition (anodic and cathodic), with both physical and chemical adsorption following the Langmuir adsorption isotherm. The results are summarized in the last five rows of Table 8.

Table 8:

Inhibition efficiency of essential oil of Mentha variety terpenes.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 6 h, 25°C 3 ml/l 80 (Bouyanzer et al., 2006a,b)
1 m HCl, PP 3 ml/l 78
1 m HCl, EIS 3 ml/l 72
1 m HCl, WL, 6 h, 25°C 2 ml/l 87 (Khadraoui et al., 2016)
1 m HCl, PP 2 ml/l 89
1 m HCl, EIS 2 ml/l 81.96
1 m HCl, WL, 1 h, 34.85°C 2 ml/l 86
1 m HCl, WL, 1 h, 44.85°C 2 ml/l 85

1,8-Cineol (also called eucalyptol) and camphor are the main active ingredients of the rosemary essential oil extracted from Rosmarinus officinalis (Bendahou et al., 2006). This essential oil inhibited corrosion of steel as cathodic inhibitor when tested in H3PO4 (Bendahou et al., 2006) and H2SO4 (El Ouariachi et al., 2010) media, with efficiencies around 60%, as detailed in Table 9. The authors suggested that 1,8-cineol is the active component inhibiting the steel. Rosmarinus extract is more efficient in sulfuric acid than in H3PO4 solutions (El Ouariachi et al., 2010).

Table 9:

Inhibition efficiency of rosemary oil terpenes.

Test condition and method Extract concentration %IE Reference
2 m H3PO4 WL, 6 h, 25°C 10 g/l 70.4 (Bendahou et al., 2006)
2 m H3PO4 WL, 2 h, 35–75°C 10 g/l 64.61–50.77
2 m H3PO4, PP, 25°C 10 g/l 73
2 m H3PO4, EIS, 25°C 10 g/l 71
0.5 m H2SO4, WL, 6 h, 25°C 1 g/l 59 (El Ouariachi et al., 2010)
0.5 m H2SO4, EIS, 6 h, 25°C 1 g/l 57

Several Thymus varieties have been studied as corrosion inhibitors by different authors. Elbouchtaoui et al. (2014) identified borneol as the major component (followed by camphor and α-terpineol) of analyzed Thymus pallidus essential oil extract. This extract showed mixed-type inhibitor behavior and dominant cathodic effect when tested for mild steel in 1 m HCl solution. The results for this oil are displayed in the first four rows of Table 10. Similar results were also obtained by Ibrahim et al. (2012), who tested Thyme leaves for their mild steel IE in a 2 m HCl solution. The results, also shown in Table 10, are close to the efficiency values found by Elbouchtaoui et al. (2014). Furthermore, all of the previous authors (Ibrahim et al., 2012; Elbouchtaoui et al., 2014) concluded that physisorption fitted to the Langmuir isotherm. FTIR analysis and thermodynamic calculations (20.9 kJ/molΔGoads18.2 kJ/mol) revealed decrease of protection of steel with increase of temperature. Premkumar et al. (2008) identified thymol extracted from Thymus vulgar plant as a volatile corrosion inhibitor. This extract, also called thyme by these authors, was tested by impregnation at different concentrations on craft papers that were further wrapped to steel samples immersed in a jar containing 0.01 n HCl and 100% humidity in an air-tight environment. With temperature set at 40°C, the experiments were run for 14 days. After evaluating the thyme efficiency through WL and PP, the authors obtained the results displayed in rows 9 and 10 of Table 10. They concluded that thyme was an effective mixed-type volatile corrosion inhibitor that obeyed the Temkin adsorption isotherm.

Table 10:

Corrosion inhibition efficiency of terpene extracts from Thyme species plant.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 25°C, 6 h 1 g/l 87.81 (Elbouchtaoui, et al., 2014)
1 m HCl, 25°C, EIS 1 g/l 88.75
1 m HCl, 25°C, PP 1 g/l 87.92
2 m HCl, WL, 25°C, 7 days 400 ppm 80 (Ibrahim et al., 2012)
2 m HCl, 25°C, PP 400 ppm 75
2 m HCl, EIS, 25°C and 50°C 400 ppm 78 and 67
0.01 n HCl, WL, 100% humidity, air tight, 40°C, 14 days 1000 mg/ft2 78.64 (Premkumar et al., 2008)
0.01 NaCl, PP, 100% humidity, air tight, 40°C, 14 days 1000 mg/ft2 66.78
1 m HCl, WL, 35°C, 6 h 2 g/l 93.6 (El Hajjaji et al., 2016)
1 m HCl, 2 h, 40°C and 60°C 12 g/l 94 and 96
1 m HCl, PP, 35°C 2 g/l 95.7
1 m HCl, EIS, 35°C 2 g/l 93
0.5 m H2SO4, PP, 25°C 12 g/l 75.3 (Fattah-alhosseini & Hamrahi, 2016)
0.5 m H2SO4, EIS, 25°C 12 g/l 89.24

Thyme vulgaris was also studied as a corrosion inhibitor for mild steel in 1 m HCl solutions by El Hajjaji et al. (2016). These authors identified thymol, along with γ-terpinene and p-cymene, as the main active ingredients of the essential oil obtained from this plant. After evaluating its performance through thermodynamic calculations from WL experiments at different temperatures, they concluded that the inhibition of steel occurred by chemisorption (58.71kJmolEafree acid47.37kJmolEafree acid) (El Hajjaji et al., 2016) on the metal following the Langmuir isotherm. However, their electrochemical measurements (PP and EIS) were performed with the addition of pelargonium, providing evidence of mixed-type inhibitor behavior (Table 10). Fattah-alhosseini and Hamrahi (2016) also tested Thyme vulgaris by immersing samples of API 5L carbon steel immersed in H2SO4 media in the presence of this essential oil. As also found by Premkumar et al. (2008), they concluded from the experiments that thyme extract behaved as a mixed-type inhibitor by physically adsorbing (ΔGoads=17.9 kJ/mol) on the steel surface following the Temkin isotherm, with maximum efficiency obtained at 12 g/l, as shown in Table 10.

Essential oil from Lavandula dentata provided IE between 86% and 95%, as seen in Table 11. In these tests, mild steel was exposed to 1 m HCl media at 35°C. The experimental results determined that this extract inhibited this metal from corrosion by acting as a mixed-type inhibitor, with data properly modeled by the Langmuir isotherm (Bouammali et al., 2013).

Table 11:

Inhibition efficiency of terpenes extracted from Lavandula dentata.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 35°C, 4 h 2% wt 95 (Bouammali, et al., 2013)
1 m HCl, PP, 35°C 2% wt 84
1 m HCl, EIS, 35°C 2% wt 86

The main active ingredients identified in Salvia officinalis essential oil are 1,8-cineole, α-thujone, and β-pinene, which provide inhibition of steel when immersed in 1 m HCl solution. The results are displayed in Table 12. The WL experiments carried out at different temperatures evidenced that this oil adsorbs physically (ΔGadso=10.6 kJ/mol) on the metal surface (El ouadi et al., 2014).

Table 12:

Inhibition efficiency of Salvia terpenes.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 1 h, 30–60°C 8 ml/l 70–51 (El ouadi et al., 2014)
1 m HCl, PP, 25°C 8 ml/l 85.05
1 m HCl, EIS, 25°C 8 ml/l 77.82
0.5 m H2SO4 WL, 25°C after 6 h 2 g/l 86.12 (Znini et al., 2012)
0.5 m H2SO4 WL, 2 h, 30–70°C 2 g/l 70–74
0.5 m H2SO4 PP, 25°C 2 g/l 84.16
0.5 m H2SO4 EIS, 25°C 2 g/l 85.45

When terpenes found on Salvia aucheri boiss were tested for protection of steel in H2SO4 solution, they were found as a mixed-type, dominant anodic corrosion inhibitor that chemisorbs (Eainhibitor=50.65kJmol<Eafree acid=54kJmol) on the metal surface following the Langmuir isotherm model. The authors identified camphor, 1,8-cineol, and camphene as the main active ingredients present in this essential oil, which protect the steel by forming a film or complex in the acidic solution, causing geometric blocking of the electrode surface (Table 12) (Znini et al., 2012).

The nails of Eugenia caryophyllata (Chaieb et al., 2005), also named giroflier, provide essential oil rich in eugenol and acetyleugenol derivates. These components present in the oil yielded mixed-type inhibitory efficiency for protection against corrosion of steel immersed in HCl media at different temperatures. As seen in Table 13, both eugenol and acetyleugenol showed an increase in IE as the test temperature was elevated following the Langmuir isotherm. These results led the authors to confirm chemisorption after carrying out thermodynamic analysis (35.03 kJ/molΔGoads32.96 kJ/mol).

Table 13:

Inhibition efficiency of terpenes extracted from nail of giroflier.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 25°C, 6 h, eugenol 0.173 g/l 80 (Chaieb et al., 2005)
1 m HCl, WL, 25°C, 6 h, acetyleugenol 0.173 g/l 91
1 m HCl, WL, 1 h, 25–55°C, eugenol 0.173 g/l 57–78
1 m HCl, WL, 1 h, 25–55°C, acetyleugenol 0.173 g/l 64–87
1 m HCl, PP, 25°C, eugenol 0.115 g/l 64
1 m HCl, PP, 25°C, acetyleugenol 0.173 g/l 75
1 m HCl, EIS, 25°C, eugenol 0.173 g/l 74
1 m HCl, EIS, 25°C, acetyleugenol 0.173 g/l 80.5

1,8-Cineol, also called eucalyptol, is the main monoterpene identified as an active ingredient present in Eucalyptus oil extracted from Eucalyptus leaves by Bouyanzer et al. (2006a,b). Their experimental results are summarized in rows 2–4 of Table 14. They suggested that the inhibitor chemisorb s(Eainhibitor=53.86kJmol<Eafree acid=56.58kJmol) following the Frumkin adsorption isotherm. Rekkab et al. (2012) mentioned palmitic, oleic, and linoleic acid as main components in their extract obtained from Eucalyptus oil for protection of steel in half-molar sulfuric acid media. The efficiency values obtained by these authors are also given in rows 5–8 of Table 14. Although their efficiency values are in the same range (69–76%) as those obtained by Bouyanzer et al. (2006a,b), their results differ from the results obtained by the previous authors in both the mechanism of adsorption and inhibition. Rekkab et al. (2012) concluded that their Eucalyptus extract behaved as a mixed-type inhibitor that physisorbs (Eainhibitor=62.63kJmol>Eafree acid=38.81kJmol) on the steel surface following the Langmuir isotherm. In another result, citronellal, citronellol, and isopulegol, along with a lower proportion of 1,8-cineol, were the major constituents identified by Gualdrón et al. (2013) in their Eucalyptus oil extracted for protection of steel in 0.5 m HCl media. The results are displayed from rows 9 and downwards in Table 14. Their thermodynamic analysis and experimental results concluded that eucalyptus extract protects the steel by physisorption (Eainhibitor=23.86kJmol>Eafree acid=9.33kJmol) on the metal, behaving as a mixed-type inhibitor.

Table 14:

Eucalyptus essential oil (terpenes) efficiency as a corrosion inhibitor.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 25°C, 6 h 3 ml/l 72 (Bouyanzer et al., 2006a,b)
1 m HCl, WL, 1 h, 40–70°C 3 ml/l 73–76
1 m HCl, PP, 25°C 3 ml/l 68
0.5 m H2SO4, WL, 25°C, 6 h 6 g/l 76 (Rekkab et al., 2012)
0.5 m H2SO4, WL, 1 h, 35–55°C 6 g/l 68–46
0.5 m H2SO4, PP, 25°C 6 g/l 81
0.5 m H2SO4, EIS, 25°C 6 g/l 79
0.5 m HCl, WL, 25°C, 4 h 5 g/l 92 (Gualdrón et al., 2013)
0.5 m HCl, WL, 4 h, 60°C and 110°C 5 g/l 73 and 70
0.5 m HCl, PP, 25°C 5 g/l 91.1
0.5 m HCl, EIS, 25°C 5 g/l 84.6

Several varieties of Artemisia plant have been studied due to their inhibition properties for protection of steel in different acid media, including HCl, H2SO4, and H3PO4. The composition and contribution of specific active ingredients vary depending on the species location, with all of them having in common the presence of terpenes such as camphene, 1,8-cineol, chrysanthenone, α- and β-thujone, and camphor. Consequently, these differences in composition from one extract to another implies that there is no unique answer or generalization rule for the inhibitor behavior (anodic, cathodic, or mixed) in the acid media studied, as well as a unique physical or chemical adsorption phenomenon type. Furthermore, the inhibition protection provided for steel from some of the Artemisia extracts also are in a wide range of values, from 60% to 95%, depending on the temperature, environment, and plant origin, as can be seen in Table 15.

Table 15:

Inhibition efficiency of terpenes from different varieties of Artemisia essential oil.

Test condition and method Extract concentration %IE Reference
0.5 m H2SO4, WL, 25±0.5°C 10 g/l 95 (Bouklah & Hammouti, 2006)
0.5 m H2SO4, PP, 25±0.5°C 10 g/l 91
0.5 m H2SO4, EIS, 25±0.5°C 10 g/l 94
1 m HCl, PP, 25±2°C 800 ppm 85.9 (Huang et al., 2013)
1 m HCl, EIS, 25±2°C 800 ppm 88.9
1 m HCl, WL, 35°C, 6 h 19 g/l 76 (Bouyanzer & Hammouti, 2004)
1 m HCl, WL, 1 h, 35–80°C 19 g/l 76–85
1 m HCl, PP, 30°C 19 g/l 76
1 m HCl, EIS, 30°C 19 g/l 69
2 m H3PO4, WL, after 2 h 6 g/l 74 (Benabdellah et al., 2006)
2 m H3PO4, PP, 2 h, 35–75°C 6 g/l 69.1–54.4
2 m H3PO4, PP, 25°C 6 g/l 79.4
2 m H3PO4, EIS, 25°C 6 g/l 74.4
0.5 m H2SO4, WL, 25°C, 6 h 1 g/l 74 (Ouachikh et al., 2009)
0.5 m H2SO4, WL, 1 h, 40°C and 70°C 1 g/l 64 and 73
0.5 m H2SO4, PP, 25°C 1 g/l 73

Bouklah and Hammouti (2006) tested Artemisia oil from Moroccan plants for protection of steel in 0.5 m H2SO4 solution at 25°C and higher temperatures. From their results, including thermodynamic analysis, they found that their oil behaved as a mixed-type inhibitor that chemisorbs (ΔGoads32.9 kJ/mol) on the metal surface following the Langmuir isotherm. They also identified davanone as the main active ingredient along with the terpenes mentioned previously (rows 2–4 in Table 15) (Bouklah & Hammouti, 2006). Figure 2A shows davanone tautomeric equilibrium, and Figure 2B and C show davanone formation of intramolecular hydrogen bond and the formation of Fe(II)-davanone complex as a mechanism of inhibition for this sesquiterpenoid ketone, respectively. Another Artemisia variety, i.e. Artemisia halodendron (Huang et al., 2013), provided good IE for steel when tested in 1 m HCl (Table 15). The experimental results led the authors to conclude that Halodendron extract behaved as a mixed-type inhibitor, which protects the steel in the HCl media by the formation of a film or layer on the metal surface.

Figure 2: 
            Davanone oil adsorption phenomena: (A) tautomeric equilibrium, (B) formation of intramolecular hydrogen bond, and (C) formation of Fe(II)-davanone complex.
            Reproduced with permission from Bouklah and Hammouti (2006).
Figure 2:

Davanone oil adsorption phenomena: (A) tautomeric equilibrium, (B) formation of intramolecular hydrogen bond, and (C) formation of Fe(II)-davanone complex.

Reproduced with permission from Bouklah and Hammouti (2006).

The essential oil extracted from Moroccan Artemisia vulgaris contains camphor as the main ingredient (44%), followed by germacrene D (16%), trans-pinocarveol (11%), α-selinene (9%), α-caryophyllene (9%), and ketone (3%). The efficiency of these components is also displayed in Table 15. Additionally, the Frumkin isotherm described the adsorption phenomena, which was physical at lower temperature and chemical at high temperatures (Bouyanzer & Hammouti, 2004). Artemisia herba alba from Algeria was tested in H3PO4 media, as seen in Table 15. The main active ingredient present in the Algerian sample was identified as β-thujone, which constitutes about 31.5–41.23% of the extract. The other ingredients were identified as camphor (16.2–24.58%), 1.8-cineol (0.12–9.86%), camphene (3.14–4.25%), and sabinene (0.45–2.33%), among other essential oils. Therefore, when these ingredients were tested for inhibition of mild steel in aggressive media, it was found that this extract creates a barrier for access of the hydrogen ions, by geometrical blocking of the electrode surface due to cathodic and physical corrosion inhibition behavior (Eainhibitor=61.3kJmol>Eafree acid=51.3kJmol) (Benabdellah et al., 2006). The other sample of the oil extracted from A. herba alba was tested; in this case, the version that originated from Morocco offered protection for protection of steel in 0.5 m H2SO4, and the results are displayed in the last three rows of Table 15. This sample has chrysanthenone as main ingredient with 30.6% contribution, followed by camphor with 23.4%. Other components include camphene (4.5%), filifone (4.3%), and β-thujone (2.7%). The experiments performed for this essential oil revealed that the extract behaved as a cathodic inhibitor. Additionally, an increase in IE was observed with an increase in temperature (Ouachikh et al., 2009).

Consequently, it is possible to conclude from the results provided by different authors on Artemisia essential oil extract that this oil is more efficient for protection of steel for different media/environment in the following decreasing order: 0.5 m H2SO4>2 m H3PO4>1 m HCl.

Chamomilla recutita was studied by Hmamou et al. (2012), as a corrosion inhibitor for C38 steel exposed to 1 m HCl solution at different temperatures (Table 16). The main ingredients identified in this extract were linoleic acid (54.8%), oleic acid (23.5%), palmitic acid (10.7%), linolenic acid (6.2%), and stearic acid (3.6%). The PP, EIS, and WL experiments showed good correlation in the results, concluding that Chamomile oil behaved as a good mixed-type inhibitor, where the adsorption and efficiency were found to be independent of the change in temperature.

Table 16:

Inhibition efficiency of terpenes from Chamomile essential oil.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 25°C, 8 h 2 g/l 89 (Hmamou et al., 2012)
1 m HCl, PP, 25°C 2 g/l 90
1 m HCl, EIS, 25°C 2 g/l 92
1 m HCl, PP, 35–55°C 2 g/l 84–86

3.3 Hydroxyl group: alcohols and phenols

Alcohols and phenols are organic derivatives of water in which a hydrogen atom is replaced by an alkyl group and aromatic ring, respectively, and can act as hydrogen bond donors and acceptors (Patai, 1993). The presence of hydroxyl groups can be found in the molecular structures of naturally occurring polysaccharides (Ravve, 2000), which could exhibit corrosion inhibition properties. Umoren and Eduok (2016) provided a review of carbohydrate polymers as corrosion inhibitors, in which several carbohydrate polymers, such as exudate and cellulose gums, starch, pectin, chitosan, carrageenan, dextrins, and alginates, were evaluated as viable sources of corrosion inhibitors.

Although phenols share some characteristics with alcohols, they have distinct properties and reactions; therefore, they are not classified as alcohols. Phenols can take part in intermolecular hydrogen bonding and have higher boiling points than aromatic compounds lacking the phenolic group (Patrick, 2004). In the context of plant derivatives, phenols and polyphenols should be strictly referred to as secondary natural metabolites (Lattanzio, 2013).

3.3.1 Quinones and napthoquinones

Quinones are aromatic rings with two ketone substitutions. These compounds are highly reactive, and switch between diphenol (or hydroquinone) and diketone (or quinone) easily through oxidation and reduction potential, providing a source of stable free radicals (Cowan, 1999). Napthoquinones (C6-C4) are a class of quinone pigments widespread in nature (Lattanzio, 2013). For instance, henna contains lawsone, which is a very popular plant extract with dyeing properties. This compound, technically named 2-hydroxy-1,4-napthoquinone, has been studied for corrosion inhibition of steel in acid media (Chetuani & Hammouti, 2003; El-Etre et al., 2005; Ostovari et al., 2009; Abdollahi & Shadizadeh, 2012).

Lawsonia inermis or Lawsonia alba (Al-Sehaibani, 2000), most commonly known as henna, is rich in lawsone, resin, tannin, coumarins, gallic acid, and sterols (El-Etre et al., 2005). This extract was studied by several authors for protection of steel in different media.

El-Etre et al. (2005) tested henna extract for protection of different metals, including steel. Their experiments with steel in different media revealed that the IE is dependent on the concentration of the extract and pH of the environment. IEs increase with increase of pH: %IE (alkaline)<%IE (neutral)<%IE (acid) is shown in Table 17 (rows 2–4). The formation of metal-Lawsonia complex is shown in Figure 3. The authors proposed delocalization of the lone pair of electrons on the hydroxyl group in the presence of metal cations as the mechanism of inhibition for the lawsone molecule. Abdollahi and Shadizadeh (2012) studied the inhibitive effects of henna leaf extract on N80 API steel immersed in regular stimulation mud acid (HCl/HF 12:3 wt%) at 28°C. The inhibition properties of henna extract were also tested in mud acid samples containing standard doses of separated and combined commercial additives currently applied by service companies in the upstream industry. The list of additives was surfactant, multi-function surfactant, suspended agent, iron control agent, anti-sludge, and a mutual solvent. All experiments were performed at 28°C. The WL and EIS experiments (Table 17) in pure mud acid revealed that henna extract indeed reduced the corrosion rate of steel. In addition, the performance of the inhibitor was proportional to its concentration, i.e. higher IE was achieved when the concentration of inhibitor was increased. The authors showed evidence that this extract behaved as a cathodic inhibitor. Furthermore, the performance of henna in mud acid+additives by EIS and PP experiments showed that only iron control additives applied to the mud improved henna inhibition, while the others were detrimental to it. Therefore, the authors concluded that the corrosion rate depends on the chemical nature of the electrolyte and the medium temperature (Abdollahi & Shadizadeh, 2012).

Table 17:

Inhibition efficiency of henna (Lawsonia extract) polyphenols.

Test condition and method Extract concentration %IE Reference
0.1 m NaOH, PP, 30±1°C 800 ppm 69.56 (El-Etre et al., 2005)
0.1 m NaCl, PP, 30±1°C 800 ppm 91.01
0.1 m HCl, PP, 30±1°C 800 ppm 95.78
HCl/HF 12/3 wt%, WL, 28°C, 8 h 1.6 g/l 84.21 (Abdollahi & Shadizadeh, 2012)
HCl/HF 12/3 wt%, EIS, 28°C 1.6 g/l 81.11
HCl/HF 12/3 wt%, EIS, 28°C 1.6 g/l+iron control agent 82.83
1.6 g/l+multifunction surfactant 79.83
1.6 g/l+suspended agent 77.16
1.6 g/l+mutual solvent 76.87
1.6 g/l+surfactant 76.73
1.6 g/l+antisludge 74.40
1.6 g/l+blend all additives 72.75
HCl/HF 12/3 wt%, PP, 28°C 1.6 g/l 96.92
1.6 g/l+multifunction surfactant 94.34
1.6 g/l+suspended agent 91.30
1.6 g/l+mutual solvent 86.08
1.6 g/l+surfactant 87.39
1.6 g/l+antisludge 84.34
1.6 g/l+blend all additives 82.60
1 m HCl, PP, 25°C 1.2 g/l 92.06 (Ostovari et al., 2009)
1 m HCl, EIS, 25°C 1.2 g/l 90.34
1 m HCl, WL, after 6 h, 25°C, 60°C 1.2 g/l 92.59, 37.95
1 m HCl, PP, 25°C 1 g/l lawsone 94.44
0.9 g/l gallic acid 63.25
0.7 g/l α-d-glucose 48.18
5.8 g/l tannic acid 34.73
1 m HCl, EIS, 25°C 1 g/l lawsone 92.82
0.9 g/l gallic acid 61.39
0.7 g/l α-d-glucose 50.28
5.8 g/l tannic acid 32.13
Figure 3: 
              Formation of metal-Lawsonia complex.
              Reproduced with permission from El-Etre et al. (2005).
Figure 3:

Formation of metal-Lawsonia complex.

Reproduced with permission from El-Etre et al. (2005).

Ostovari et al. (2009) also studied henna (Table 17) and the components present in its extract in order to evaluate their individual contribution to protection of mild steel in 1 m HCl solution by WL at different temperatures and electrochemical studies at 25±1°C (PP and EIS). These components were identified as lawsone, gallic acid, α-d-glucose, and tannic acid by the use of gas chromatography and mass spectrometry. Due to the fact that they represent only 18% wt of Lawsonia plant, their individual IE was tested using commercially available samples of these compounds.

One the one hand, the values of enthalpy of adsorption (ΔHads=−54.76 kJ/mol) led the authors to conclude chemisorption as the adsorption phenomena, which was represented by the Langmuir adsorption isotherm (Ostovari et al., 2009). However, their calculated values for apparent activation energy increases when henna concentration is increased (Eainhibitor46.21kJmol>Eafree acid=27.06kJmol), which is an observed behavior of chemisorption (Bothi Raja & Sethuraman, 2008a, 2009b). On the other hand, the PP results from the individual henna constituents revealed that all of them behave as a mixed-type inhibitor and all the EIS results indicated a decrease of the double-layer capacitance values in the presence of these components. However, not all of them equally impact the ability of henna extract to protect steel in the acid solution. The trend of %IE values from both experiments was the same. Therefore, it was concluded that the efficiency was, in decreasing order, %IE lawsone>%IE gallic acid>α-d-glucose>tannic acid. In consequence, it established lawsone as the main responsible component for the good performance of henna in the experiments, due to the fact that this molecule has better IE when compared to the other ingredients present in this plant extract, and it contributes to 1.02% (i.e. major component) of its composition (Ostovari et al., 2009).

3.3.2 Flavones, flavonols, isoflavonoids, and flavanols

Flavonoids are a class of hydroxylated phenolic substance occurring with a C6-C3-C6 unit linked to an aromatic ring. This flavonoid group includes mainly flavones, flavanols, and flavanols (Cowan, 1999; Oliveira et al., 2013).

Cardozo et al. (2010, 2014) studied orange peels as source of corrosion inhibitor for protection of steel. They claimed that orange peel (da Cunha Ponciano Gomes et al., 2011) provided good results due to the fact that it contains the highest concentration of flavonoids among citrus fruits (Cardozo et al., 2014) (Table 18). Orange peel extract also behaved as a mixed-type inhibitor that physisorbs (Eainhibitor=74.9kJmol>Eafree acid=51.5kJmol) on the steel surface following the Langmuir isotherm (da Cunha Ponciano Gomes et al., 2011; Cardozo et al., 2014).

Table 18:

Inhibition efficiency of orange peel polyphenols.

Test condition and method Extract concentration %IE Reference
1 m HCl, PP, 25°C 400 ppm 95 (Cardozo et al., 2010)
1 m HCl, WL, 25°C, 4–24 h 400 ppm 92–95
1 m HCl, WL, 4 h, 25–60°C 400 ppm 92–80
1 m HCl, WL, 25°C, 4–24 h 400 ppm 91–95 (Cardozo et al., 2014)
1 m HCl, PP, 25°C 600 ppm 91
1 m HCl, EIS, 25°C 600 ppm 90

The flowers of Ixora coccinea contain vitexin and diosmetin flavonols (Nagarajan & Sulochana, 2006) that protect steel from corrosion when this metal was exposed to 1 m HCl solution at 30°C. The results displayed in Table 19 concluded that these components behaved as a mixed-type inhibitor covering the steel surface by following the Langmuir adsorption isotherm.

Table 19:

Inhibition efficiency of polyphenols found in Ixora coccinea.

Test condition and method Vitexin concentration %IE Reference
1 m HCl, WL, 30°C, 4 h 10 μg/ml 71.85 (Nagarajan & Sulochana, 2006)
Vitexin concentration +10−5m QAS %IE
10 μg/ml 77.82
Diosmetin concentration %IE
10 μg/ml 76.13
Diosmetin concentration +10−5m QAS %IE
10 μg/ml 77.48

Ethyl acetate obtained from Uncaria gambir was examined as an inhibitor for steel in different pH media by Hussin and Kassim (2010). This plant, with (+)-catechin and (+)-epicatechin flavan monomers besides alkaloids as major ingredients provided a concentration-independent inhibition behavior. The optimum %IE for different experiments is shown in Table 20. The authors showed evidence of the formation of a catechin complex on the steel surface by using SEM micrographs and energy-dispersive X-ray analysis of the mild steel surface, comparing the surfaces of steel before the experiments, with those without and with inhibitors (Hussin & Kassim, 2010).

Table 20:

Inhibition efficiency of ethyl acetate from Uncaria gambir terpenes for protection of steel in acid media.

Test condition and method Extract concentration %IE Reference
pH 5 media, WL, 25°C after 7 days 150 ppm 67.88 (Hussin & Kassim, 2010)
WL, 25°C after 7 days, pH 3

WL, 25°C after 7 days, pH 5

WL, 25°C after 7 days, pH 7
150 ppm

150 ppm

150 ppm
44.16

67.88

34.21
pH 5 media, PP, 25°C 150 ppm 91.79
PP, 25°C, pH 3

PP, 25°C pH 5

PP, 25°C pH 7
150 ppm

150 ppm

150 ppm
7.18

91.77

37.77

3.3.3 Tannins

The name “tannin” is derived from the French “tanin,” i.e. tanning substance (Lattanzio, 2013). Therefore, tannins are capable of tanning leather (Cowan, 1999), with the ability to precipitate alkaloids, gelatin, and other proteins (Lattanzio, 2013). This group is also characterized by having a relatively high molecular weight (between 500 and 3000), and is divided into two broad categories: hydrolyzable tannins and condensed tannins (Cowan, 1999). Tannins are soluble in water, and their ability to adsorb heavy metal ions must be treated chemically to immobilize the phenolic polymers present in them (Rahim & Kassim, 2008).

Rahim and Kassim (2008) provided a review of recent development related to the use of tannins as corrosion inhibitors in acidic and near-neutral solution, and as an ingredient in pre-treatment formulations. They stated that an IE of >80% was achieved at acid pH 0 and pH 0.5 for all tannins, and that condensed mangrove tannins are superior to mimosa and chestnut counterparts at pH 4.0. Additionally, the authors stated that variations of acid pH range influence the inhibition behavior of tannins, e.g. the mimosa tannins chemisorbed on the steel surface when tested in sulfuric acid solution at pH range from 1 to 3, providing mixed-type inhibition. At 0.5 m HCl, the mangrove tannins behaved as a cathodic inhibitor that also chemisorbed on the metal surface via sharing the donor (-OH) electrons or aromatic π-electrons; however, when chestnut tannins were tested in a 2 m HCl solution, the bonding between inhibitor and steel surface was of the physical type. In the presence of 3.5% NaCl and pre-rusted steel alone, the Ecorr of mangrove tannins decreases, becoming more negative. Lastly, tannins in pre-treatment formulation have the reduction capability to convert active rust into more corrosion-resistant compounds by the interaction of its polyphenolic moieties with iron oxides and oxyhydroxides, forming ferric-tannates as the major product (Rahim & Kassim, 2008).

3.3.4 Stilbenes

These are a class of plant phenolics with a unit structure possessing two aromatic rings joined by a methylene bridge (C6-C2-C6). The most famous representative stilbene is named resveratrol, which occurs in Polygonum cuspidatum root and Vitis species (Shen et al., 2013). Combretum bracteosum extract, which was tested for protection of steel, also contains stilbenes and other types of phenolic compounds able to inhibit corrosion of steel (Okafor et al., 2009).

Combretum bracteosum is rich in tannins, saponins, and stilbenes, among other phytochemicals. The extract obtained from the leaves of this plant was tested as an inhibitor for corrosion of mild steel at different concentrations (0.1–4 g/l) in different acidic solutions of H2SO4 (2–5 m) at different temperatures (30–60°C) (Okafor et al., 2009). The experiments measured IE through WL and hydrogen evolution methods, and the results are displayed in Table 21. From these experiments, Okafor et al. (2009) deducted that this extract protects steel by its physisorption (53.79kJmolEainhibitor>45.51kJmolEafree acid) on this metal surface following the Frumkin isotherm. Also, from Table 21, it can be observed that inhibition was favored by the high concentration of extract and low temperatures, e.g. 4 g/l at 30°C yielded maximum %IE values through both methods. However, the reverse conditions have a negative impact on the protection of steel.

Table 21:

Inhibition efficiency of Combretum bracteosum polyphenols.

Test condition and method Extract concentration %IE Reference
2 m H2SO4, WL, 30°C, 12 h 2 g/l 58.38 (Okafor et al., 2009)
5 m H2SO4, HE, 30°C, 12 h, 30–60°C 2 g/l 83.5–34.0
5 m H2SO4, HE, 30°C, 12 h, 30–60°C 4 g/l 88.3–60.5

The peels of mango and cashew fruits, obtained as by-products for their use in the food process industry, have been studied as corrosion inhibitors by Cardozo et al. (2010, 2014) and da Cunha Ponciano Gomes (2011). As a result from their study, it was found that mango and cashew peels contain important amounts of polyphenols and heterosides that protected steel from corrosion when these extracts were tested in 1 m HCl media. The efficiency results, summarized in Table 22, concluded that the peel compounds behaved as a mixed-type inhibitor that physisorbed (75.5kJmolEacashew>65.8kJmolEamango>51.5kJmolEafree acid) on the steel surface following the Langmuir isotherm.

Table 22:

Inhibition efficiency of polyphenols extracted from mango and cashew peels.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 25°C, mango peels, 4 h, 24 h 400 ppm 92, 97 (Cardozo et al., 2014)
1 m HCl, PP, 25°C, mango peels 600 ppm 96
1 m HCl, EIS, 25°C, mango peels 600 ppm 94
1 m HCl, PP, 25°C, mango peels 600 ppm 91 (Cardozo et al., 2010)
1 m HCl, WL, 25°C, mango peels, 4 h, 24 h 400 ppm 80, 96
1 m HCl, WL, 4 h, mango peels, 25–60°C 400 ppm 80–62
1 m HCl, WL, 25°C, cashew peels, 4 h, 24 h 400 ppm 82, 93
1 m HCl, PP, 25°C, cashew peels 600 ppm 80
1 m HCl, WL, 25°C, cashew peels, 4 h, 24 h 400 ppm 82, 93
1 m HCl, WL, 4 h, cashew peels, 25–60°C 400 ppm 82–50

Coffee senna is rich in polyphenol-based structures such as anthraquinones, emodin glycosides, chrysophanol, aloe-emodin, quercetine, rhamnosides, and rhein and vitexin alkaloids (Wagstaff, 2008). Thus, Akalezi et al. (2013) studied the ability of the extract from leaves of this plant to protect mild steel in 1 m HCl and 0.5 m H2SO4 solutions. The results from the studies are shown in Table 23. All experiments exhibited an increase in %IE with an increment of extract concentration used. The authors mentioned that a slight shift took place in the corrosion potential into the anodic direction in the HCl solution, while an opposite trend occurred in H2SO4 media. It is believed that the difference in behavior in the HCl media is because the Cl ions are strongly adsorbed on the metal surface. Gravimetric experiments realized in the 30–60°C temperature range showed an increase of %IE with an increase in temperature, indicating chemisorption (63.35kJmolEafree acid>37.59kJmolEainhibitor) of coffee senna phytochemicals on the steel surface (Akalezi et al., 2013). Commercial coffee varieties (Coffea arabica and Coffea canephora) were studied for protection of steel in 1 m HCl solution at different temperatures and immersion times by Vasconcelos et al. (2011). The major phenolic compounds identified by the authors in the coffee ground extracts were cholorogenic acids (monoesters or diesters of quinic acid with transhydroxycinnamic acid), such as caffeoylquinic, feruloylquinic, dicaffeoylquinic, and feruloylquinic acids. The results shown in Table 24 led the authors to conclude that the extract provided mixed inhibition of steel by chemisorption (41.9kJmolEafree acid>16.8kJmolEainhibitor) on the steel surface modeled by the Langmuir isotherm.

Table 23:

Inhibition efficiency of coffee senna extract with polyphenols.

Test condition and method Extract concentration %IE Reference
1 m HCl, WL, 40–60°C 1000 ppm 76.64–96.4 (Akalezi et al., 2013)
0.5 m H2SO4, WL, 40–60°C 1000 ppm 82.4–95.8
1 m HCl, EIS, 30°C 1000 ppm 80.5
0.5 m H2SO4, EIS, 30°C 1000 ppm 78.7
1 m HCl, PP, 30°C 1000 ppm 70.4
0.5 m H2SO4, PP, 30°C 1000 ppm 75.12
Table 24:

Inhibition efficiency of coffee ground extract polyphenols for protection of steel in acid media.

Test condition and method Extract concentration %IE Reference
1 m HCl, PP, 25°C, decoction 400 ppm 83.5 (Vasconcelos et al., 2011)
1 m HCl, PP, 25°C, infusion 400 ppm 88.1
1 m HCl, EIS, 25°C, decoction 400 ppm 93
1 m HCl, EIS, 25°C, infusion 400 ppm 95
1 m HCl, WL, 25°C, infusion, 24–72h 400 ppm 97–80
1 m HCl, WL, 2 h infusion, 25–55°C 400 ppm 76–91

3.3.5 Lignin

Lignin is an amorphous, highly branched polyphenolic macromolecule with a complex structure and high molecular weight, consisting primarily of phenylpropanoic units cross-linked together in three dimensions via a radical coupling process during its biosynthesis (Wardrop, 1971). Lignin contains several important functional groups (Adler, 1957), including para-hydroxyphenyl, aliphatic hydroxyl, and carboxylic acid groups, which has an impact on its overall reactivity. The corrosion inhibition properties of lignin are attributed to the aforementioned functional groups. Several studies have been performed since the 1980s (Srivastava & Srivastava, 1981; Forostyan & Prosper, 1983; Schilling & Brown, 1988), in order to analyze the IE of lignin derivatives, taking into consideration the extraction process (Akbarzadeh et al., 2011; Altwaiq et al., 2011; Abu-Dalo et al., 2013; Hussin et al., 2016), plant origin (Alaneme & Oulesegun, 2012; Zulkafli et al., 2014), chemical composition (Akbarzadeh et al., 2012), and chemical modifications (Schilling & Brown, 1988; Ouyang et al., 2006; Vagin et al., 2006; Ren et al., 2008; Hussin et al., 2015a). The chemical structure of lignin is highly irregular, and the overall reactivity of several lignins depends on their chemical structures and functional groups (Adler, 1957), including para-hydroxyphenyl (H), aliphatic hydroxyl, and carboxylic acid groups. Softwoods contain almost exclusively guaiacyl (G) units, whereas hardwoods contain both syringyl (S) and guaiacyl units.

For corrosion applications, three major C6-C3 phenylpropanoid units of lignin have been identified with anti-corrosion properties. These are p-coumaryl, coniferyl, and sinapyl alcohol (Hussin et al., 2015b). The study carried out by Forostyan and Prosper (1983) is perhaps the first work to document the properties of lignin as a corrosion inhibitor for steel in acid media. Their experiments tested different lignins obtained from sunflower husks and fir sawdust in a 5% H2SO4 aqueous solution with 5 g of different lignin types (native lignin, ammoniated native lignin, chlorinated hydrolysis lignin, and ammoniated hydrolyzed lignin) with constant stirring at 24°C during 24 h. Their results suggested a direct relationship between the presence of carboxyl groups (or COOH) in lignin structure or modifications, and the IE. The higher the COOH content, the higher the corrosion protection, which in their case occurred for the ammoniated hydrolyzed lignin. Also, they proposed the hydroxyl (OH) group as the second functional group affecting the inhibitory properties in the lignin molecule, and that the presence of nitrogen does not have a great effect on their protection efficacy.

Later, Vagin et al. (2006) compared the protection of steel caused by the electropolymerization of water-soluble lignosulfonates to COREXIT SXT-1003 inhibitor for carbon steel electrodes immersed in test brine, with air-saturated environment at room conditions. The voltammetry analysis of solutions containing lignosulfonate showed that an increase of concentration of KCl from 0.1 to 1 m in brine caused a decrease in oxidation potential to a cathodic shift of values around 1 V. This potential shift indicated that hydrophobic interactions resulted in an increase of interfacial lignosulfonates concentration with the increase of ionic strength. Additionally, when the steel electrode was tested with COREXIT, the corrosion rate was decreased only by 1.5 times, with respect to steel electrode soaked in brine solution alone. Meanwhile, the sulfonate lignin derivative showed a 3.7 times decrease of corrosion rate under the same conditions.

The properties of different types of lignin were investigated by different authors. Altwaiq et al. (2011) tested alkali lignin extracted from sawdust of a maple wood tree as a corrosion inhibitor for mild steel and other metals in 1 m HCl solution. Their experiments consisted in measuring the WL experienced in a period of time by steel immersed in the acidic solution, with different concentrations of alkali lignin dissolved in 10 ml of ethylene glycol, compared to the same solution without lignin extract. They concluded that alkali lignin does not stop the corrosion completely but inhibits the corrosion process by decreasing the corrosion rate. Additionally, they found that the higher the concentration of alkali lignin in solution, the higher the efficiency, and increasing time of exposure weakened the inhibition effect (Table 25).

Table 25:

Inhibition efficiency of alkali lignin from sawdust maple tree for steel in 1 m HCl.

Test condition and method Lignin concentration %IE Reference
1 m HCl, room T, WL, 12–24 h 100 ppm 32.3–36.9 (Altwaiq et al., 2011)
1 m HCl, room T, WL, 12–24 h 300 ppm 47.1–37.2
1 m HCl, room T, WL, 12–24 h 700 ppm 50.7–44.3
1 m HCl, room T, WL, 12–24 h 1000 ppm 52.2–51.2
1 m HCl, room T, WL, 12–24 h 1500 ppm 64.9–54.1

Hussin et al. (2014) also compared the IE of lignins extracted through different methods: kraft, soda, and organosolv from oil palm fronds (Elaeis guineensis Jacq.). After analyzing the performance of electrochemical studies for all lignin dissolved in methanol and 0.5 m HCl solution in the presence of mild steel, they found better IE when soda lignin was employed, followed by organosolv and kraft. The results of EIS and PP tests, as shown in Table 26, suggest that lignin behaved as a mixed-type inhibitor protecting steel by forming a layer over the metal surface.

Table 26:

Inhibition efficiency of lignins extracted from oil palm fronds extracted through soda, organosolv, and kraft methods.

Test condition and method Lignin concentration %IE Reference
0.5 m HCl, PP, 28±2°C, soda

0.5 m HCl, PP, 28±2°C, organosolv

0.5 m HCl, PP, 28±2°C, kraft
500 ppm

500 ppm

500 ppm
98.67

97.21

85.89
(Hussin et al., 2014)
0.5 m HCl, EIS, 28±2°C, soda

0.5 m HCl, EIS, 28±2°C, organosolv

0.5 m HCl, EIS, 28±2°C, kraft
500 ppm

500 ppm

500 ppm
85.81

81.84

67.85

They proposed that the difference between the lignin samples is attributed to their composition, which is affected by the pulping process. The authors believed that during soda pulping, scission of β-O-4 bonds occurs, leading to the production of phenolic OH groups, which, combined with low molecular weight, provides better lignin quality for inhibition properties. The authors also examined the surface of the steel samples after the electrochemical experiment finished by SEM analysis and also performed XRD surface analysis of steel immersed for 24 h in 1 g/l lignin in methanol solution as per ASTM B117. The surface analysis revealed the presence of ferric lignates on a smooth surface with contents of lepidocrocite (L: γ-FeOOH), magnetite (M: Fe3O4), and traces of geothite (G: α-FeOOH). These results confirm, along with the electrochemical studies, the formation of a protective layer of lignin on the steel. The authors also suggested that inhibition takes place through the interaction of oxygen donation of electrons and sulfur with the metal ion surface (Hussin et al., 2014).

In order to find the impact of different improved lignin samples obtained from oil palm (Elais guineensis) fronds, the lignins extracted by soda, kraft, and organosolv pulping were ultra-filtrated in a 5-kDa interval membrane and tested for corrosion inhibition of mild steel in acid media by Hussin et al. (2016). They found that IE was better when soda lignin was employed, followed by organosolv and kraft types. After the ultra-filtrated lignin samples were dissolved in a small volume of methanol (1% v/v) to increase solubility, the solutions for different concentrations of lignin were diluted with 0.5 m HCl in order to carry out the experiments. All electrochemical studies were performed at 28±2°C, while the gravimetric tests took place at different temperatures with the objective to identify the existence of physical or chemical adsorption. The electrochemical results, included in Table 27, indicated that this ultra-filtrated lignin behaved as a mixed-type inhibitor. This finding suggested 500 ppm as the optimal concentration. The alkali lignin behaved predominantly as a cathodic inhibitor, while the organosolv showed mainly anodic behavior. For both EIS and PP experiments, the efficiency obtained by soda lignin was superior to that of organosolv, followed by kraft lignin. In addition, the thermodynamic analysis (ΔGoads25.51 kJ/mol) indicated that all lignin samples are physically adsorbed on the steel following the Langmuir isotherm.

Table 27:

Inhibition efficiency of ultra-filtrated lignins extracted from oil palm fronds by soda, organosolv, and kraft methods.

Test condition and method Lignin concentration %IE Reference
0.5 m HCl, PP, 28±2°C, soda 800 ppm 87.76 (Hussin et al., 2016)
0.5 m HCl, PP, 28±2°C, organosolv 500 ppm 83.94
0.5 m HCl, PP, 28±2°C, kraft 500 ppm 81.11
0.5 m HCl, EIS, 28±2°C, soda 500 ppm 87.22
0.5 m HCl, EIS, 28±2°C, organosolv 500 ppm 83.65
0.5 m HCl, EIS, 28±2°C, kraft 500 ppm 81.42

Therefore, in order to evaluate the most convenient method for pulping lignin for production of corrosion inhibitors, kraft and soda lignins extracted from oil palm empty fruit bunch were compared by Akbarzadeh et al. (2011) through gravimetric and electrochemical studies. The steel samples were immersed in solutions containing kraft (KL) and soda (SL) lignin at different concentrations (50, 100, 200, and 400 ppm) with 3.5% NaCl, with pH adjusted to 6 and 8 by addition of 0.1 m NaOH at 25°C under naturally aerated conditions during 240 h.

On the one hand, the results from WL experiments in Table 28 showed that IE increased with concentration, until a value from which the IE did not improve any further but instead remained constant if the inhibitor concentration increased. It is suspected that this behavior is explained by the adsorption of the lignin molecules on the steel surface through the polyphenolic monomers with electron-donating groups. These results were successfully fitted to the Langmuir isotherm.

Table 28:

Kraft and soda lignin performance in 3.5% NaCl solution at pH 6 and 8.

Test condition and method Lignin concentration %IE Reference
3.5% w/v NaCl, WL, 25°C, soda, pH 6, 240 h 400 ppm

800 ppm
88.70

91.55
(Akbarzadeh et al., 2011)
3.5% w/v NaCl, WL, 25°C, soda, pH 8, 240 h 400 ppm

800 ppm
87.33

90.73
3.5% w/v NaCl, WL, 25°C, kraft, pH 6, 240 h 400 ppm

800 ppm
88.14

91.02
3.5% w/v NaCl, WL, 25°C, kraft, pH 8, 240 h 400 ppm

800 ppm
86.12

89.38
3.5% w/v NaCl, PP, 25°C, soda, pH 6 400 ppm

800 ppm
93.75

95.01
3.5% w/v NaCl, PP, 25°C, kraft, pH 6 400 ppm

800 ppm
91.01

92.60
3.5% w/v NaCl, EIS, 25°C, soda, pH 8 400 ppm

800 ppm
90.00

91.55
3.5% w/v NaCl, EIS, 25°C, kraft, pH 8 400 ppm

800 ppm
93.65

94.97

In contrast, the electrochemical studies, also displayed in Table 28, exposed the mixed inhibition behavior of both types of lignin, and while the PP results concluded that the SL achieved higher protection, the EIS data reported better results for the KL. Additionally, the EIS tests suggested that in both SL and KL, the increase of inhibitor concentration caused an increase in the electrical resistance and diameter of capacitive loops, and these were due to the formation of a protective film onto the metal surface. This film was later confirmed by the X-ray microanalysis along with the FTIR spectra for inhibited steel samples that evidenced the formation and deposition ferric-lignin components. In addition, Akbarzadeh et al. (2011) also reported that SL has better adsorption than KL, with ΔGoads values between −23.40 and −22.01 kJ/mol, establishing that both lignin types are first adsorbed physically and then chemically.

During the separate studies, the same authors investigated key ingredients naturally present in lignin that directly impact its inhibition properties. As a result, the individual and synergistic effects of three monomers of SL, p-coumaric acid (CA), ferulic acid (FA), and hydroxybenzoic acid (HB), were tested by Akbarzadeh et al. (2012) for the corrosion inhibition of mild steel in 3.5% w/v NaCl media by PP and linear polarization resistance (LPR) duplicate measurements.

In order to isolate the individual effect of these monomers, air stagnant solutions of 100, 200, 400, and 800 ppm of each individual monomer were prepared with neutral (7) pH adjusted at 25°C. The results are displayed in Table 29 for the electrochemical studies of individual components. Their analysis established that lignin monomers behaved as a mixed-type inhibitor, creating a protective layer on its metal surface. This phenomenon was explained by the displacement of protons (H+) in solution, caused by the presence of carbonyl and carboxyl groups in the molecule. As a result, the IE of individual monomers is in the following decreasing order: CA>FA>HB (Akbarzadeh et al., 2012).

Table 29:

Inhibition efficiency of individual lignin monomers in neutral NaCl solution.

Test condition and method Lignin concentration %IE Reference
3.5% w/v NaCl, PP, 25°C, CA 400 ppm

800 ppm
88.51

90.21
(Akbarzadeh et al., 2012)
3.5% w/v NaCl, PP, 25°C, FA 400 ppm

800 ppm
87.53

89.83
3.5% w/v NaCl, PP, 25°C, HB 400 ppm

800 ppm
48.01

13.98
3.5% w/v NaCl, EIS, 25°C, CA 400 ppm

800 ppm
60.5

65.0
3.5% w/v NaCl, EIS, 25°C, FA 400 ppm

800 ppm
53.1

60.0
3.5% w/v NaCl, EIS, 25°C, HB 400 ppm

800 ppm
33.8

38.2

However, the thermodynamic nature of inhibition of steel by lignin is not defined yet. Thus, Yahya et al. (2015) intended to clarify it by studying the temperature effect in the efficiency and adsorption phenomena of lignin in low carbon steel coupons through WL methods. They found that lignin fitted properly to the Langmuir isotherm and also its optimum concentration to maximize metal inhibition. In order to accomplish this analysis, the steel samples were soaked in a 1 m HCl solutions during 3 h at the presence of lignin concentrations between 500 and 2500 ppm and at a temperature range of 30–70°C. After the calculation of IEs, the authors proceeded with thermodynamic calculations using the Arrhenius plot and transition equations. The %IE values disclosed that at >500 ppm, the %IE reached a plateau, and its values are not consistent until 1000 ppm of lignin is employed. They suggested that this was probably because lower concentrations than this value are unfavorable for lignin molecules competing with the Cl ions in solution. Additionally, 50°C is the optimum temperature to attain the higher efficiency value, and at temperatures higher than this value, the vibration of lignin molecules might impede the formation of coordinated bond with atoms in steel interface, and desorption of lignin will occur. Moreover, the authors suggested chemical adsorption based on the proximity of Ea values at 1500–2000 ppm to the chemisorption threshold (78.95 kJ/mol≤Ea≤79.85 kJ/mol). Additionally, Ea≤80 kJ/mol for other concentrations, along with 40 kJ/molΔGoads20 kJ/mol as a possible explanation for the comprehensive (chemical and physical) adsorption behavior of lignin.

Later, another thermodynamic analysis of inhibition by lignin was realized (Alaneme & Oulesegun, 2012). The authors studied the efficiency of protection of medium-carbon low-alloy steel for soda lignin extracted from Tithonia diversifolia (sunflower) stems in 1 m H2SO4 solution in a temperature range of 30–60°C with an exposure time of 12 days. The authors found 55.5% ≤IE≤78.8% for different temperatures, with the thermodynamic parameters indicating physisorption (Ea80 kJ/mol and ΔGoads20 kJ/mol). The experimental data were fitted to the Langmuir isotherm.

In previous analyses, several authors reported some of the lignin samples as insoluble materials (Ren et al., 2008; Abu-Dalo et al., 2013). Therefore, different attempts to modify their structures have been done in several studies in order to improve their practical use and effectivity as corrosion inhibitors. Some reports found in the literature show, for example, the formation of a water-soluble polyamine-aldehyde lignin, as described by the patent from Schilling and Brown (1988), the graft copolymerization of soda lignin (Ren et al., 2008), the incorporation of scavengers in lignin molecule (Hussin et al., 2015a), and the variation of the sulfonation degree on kraft lignin (Ouyang et al., 2006; Abu-Dalo et al., 2013). The improvement of lignin by graft copolymerization of soda lignin with acrylamide and dimethyl diallyl ammonium chloride (DMDAAC) was accomplished by Ren et al. (2008). This modification was done with the aim of adding hydrophilic groups containing nitrogen, which provides better electrostatic adsorption of lignin to the steel surface. These molecular changes resulted in IEs >85% for experiments run at 25°C and 80°C in a 10% HCl solution, as can be observed in Table 30. Also, the electrochemical analysis showed that grafted lignin behaved as a mixed-type inhibitor preferentially anodic at low temperatures but predominantly cathodic at high temperatures. After applying the Arrhenius equation and fitting the data to the Temkin isotherm, the authors concluded that this modified lignin adsorbs chemically to the steel surface through the positively charged nitrogen atoms (N+) and negatively charged metal surface. The authors also revealed the inhibition enhancement of the inhibition effect as a consequence of the amphiphilic nature of the new molecule. The hydrophilic portion of the amide and the DMDAAC group would form links with the lonely sp2 orbital electrons from Fe atoms. Meanwhile, the hydrophobic part of the compound (lignin) would isolate the metal from the solution, creating a barrier to chloride ions (Ren et al., 2008).

Table 30:

Inhibition efficiency of grafted lignin copolymer.

Test condition and method Lignin concentration %IE Reference
10% HCl, WL, 25°C 500 ppm

1000 ppm
91.77

96.58
(Ren et al., 2008)
10% HCl, EIS, 25°C 500 ppm

1000 ppm
90.53

97.37
10% HCl, WL, 80°C 500 ppm

1000 ppm
88.53

96.55
10% HCl, EIS, 80°C 500 ppm

1000 ppm
80.11

85.54

Another alternative documented in the literature is the modification of insoluble organosolv lignin from oil palm fronds by the incorporation of aromatic scavengers: 2-napthol (AHN EOL) and 1,8-dihydroxyanthraquinone (AHD EOL) (Hussin et al., 2015a). The efficiencies of the obtained samples were tested (after being dissolved in a small volume of methanol) by electrochemical studies (i.e. PP, EIS) at 28±2°C and gravimetric methods at different temperatures in a 0.5 m HCl solution. The authors concluded that both modified EOL lignins (AHN and AHD) were better for inhibiting steel in acid media than the original organosolv lignin. The results, as shown in Table 31, demonstrated that AHD EOL yielded higher inhibition than AHN; this difference was attributable to the presence of more polar hydroxyl functional groups in the 1,8-dihydroxyantraquinone than in naphthol, increasing the hydrophilicity of lignin, promoting dissolution in water. The thermodynamic analysis from the WL methods suggested that the inhibitor adsorbs physically to the steel following the Langmuir isotherm.

Table 31:

Inhibition efficiency of organosolv lignin modified with oxygen scavengers.

Test condition and method Lignin concentration %IE Reference
0.5 m HCl, EIS, 28±2°C 250 ppm

500 ppm
65.05

89.14
(Hussin et al., 2015a,b)
0.5 m HCl, EIS, 28±2°C, AHD EOL 250 ppm

500 ppm
86.99

93.42
0.5 m HCl, PP, 28±2°C, AHN EOL 250 ppm

500 ppm
60.77

84.04
0.5 m HCl, PP, 28±2°C, AHD EOL 250 ppm

500 ppm
78.14

89.96

Other studies on the partial or total modification of the kraft lignin structure tested previously include the work done by Abu-Dalo et al. (2013). They compared sulfonated kraft lignins to phosphate inhibitor for water distribution systems. They found 0.3–0.4 mg/l as the optimum concentration of lignosulfonates as viable options for preventing corrosion and pit formation in water pipelines. For their experiments, different concentrations of commercially obtained lignin were tested in solutions of water samples obtained from the pre-stabilized water (PRSW) stage from the post-dam water treatment in New York versus the samples obtained from the post-stabilized water at the same plant. The results from the corrosion tests (LPR, EIS, and PP) are shown in Tables 32 and 33, respectively. The authors suggested that the LPR values in Table 32 evidenced the corrosion occurring in the water treatment plant that can be treatable with any of the sulfonated lignin studied if a dosage between 0.4 and 0.5 mg/l is used, as supported by the EIS and PP results from LS_A in Table 33. However, they also found that LS_E and LS_C would be good inhibitors, because at low pH, more sulfonated groups, rather than phenolic sites, would be available for adsorption in anionic form to approach the positively charged metal surface (in acidic media), enhancing the electrostatic attractions between the H3O+/metal interface and lignin molecules.

Table 32:

Linear polarization resistance of water samples before lignosulfonate application (Abu-Dalo et al., 2013).

Reference group OCP (mV) Corrosion rate (μm/year)
Pre-stabilized water (solution tested) −569.4 61.69
Post-stabilized water (5 ppm zinc orthophosphate) −583.3 34.08
Table 33:

Inhibition efficiency of tested lignosulfonates.

Test condition and method Lignin concentration %IE Reference
PRSW, EIS, 25°C, LS_A

PRSW, EIS, 25°C, LS_B

PRSW, EIS, 25°C, LS_C

PRSW, EIS, 25°C, LS_D

PRSW, EIS, 25°C, LS_E
0.1 ppm

0.1 ppm

0.1 ppm

0.1 ppm

0.1 ppm
47.0

43.0

87.0

40.0

85.0
(Abu-Dalo et al., 2013)
PRSW, EIS, 25°C, LS_A

PRSW, EIS, 25°C, LS_B

PRSW, EIS, 25°C, LS_C

PRSW, EIS, 25°C, LS_D

PRSW, EIS, 25°C, LS_E
5 ppm

5 ppm

5 ppm

5 ppm

5 ppm
55.0

62.4

67.6

32.1

84.7
PRSW, EIS, 25°C, LS_A only

0.3 ppm

0.4 ppm
72.3

86.4
PRSW, PP, 25°C, LS_A only

0.3 ppm

0.4 ppm
72.1

86.2

Lignosulfonates were also studied for inhibition of corrosion and scale deposition in recirculating cooling water systems by Ouyang et al. (2006). Initially, they compared the performance of sulfate lignin (SL) obtained from mason pine with 1-hydroxyethane-1,1-diphosphonic acid (or HEDP, a commercial scale and corrosion inhibitor) for carbon steel immersed in a naturally aerated stagnant solution at 60°C during 14 days. The solution consisted of 0.005 m calcium chloride (CaCl2), 0.002 m sodium bicarbonate (NaHCO3), 0.002 m magnesium sulfate (MgSO4), and 0.01125 m sodium chloride (NaCl), with different concentrations of SL. Due to the poor performance of SL when compared to HEDP for this set of experiments (results in Table 34), it was decided to modify the sulfate lignins by grafting it with acrylic acid onto SL. This modification added more negative charge than the original SL owing to the presence of carboxyl in the new molecule. Therefore, the structural changes in the SL structure reflected an improved efficiency (about 96%) for mixed-type inhibition at the same dosage of HEDP. However, this new SL does not overcome the scale inhibition performance of HEDP or the turbidity of the solution. In this regard, the authors suggested further research in order to surpass these disadvantages, as the grafted SL promises to be a viable alternative for corrosion inhibition in cooling water systems (Ouyang et al., 2006).

Table 34:

Inhibition efficiency of grafted sulfonate lignin vs. HEDP for cooling water systems.

Test condition and method Lignin concentration %IE Reference
Sampled solution, WL, 60°C, after 14 days 500 ppm SL 19.8 (Ouyang et al., 2006)
Sampled solution, WL, 60°C, after 14 days 200 ppm HEDP 42.7
Sampled solution, PP, 25°C 500 ppm grafted SL 96.5

Different samples of commercial lignosulfonates were tested for protection of steel in acid media by Abu-Dalo et al. (2016). WL experiments were performed at 25°C in a closed test tube for an extended period of time along with gravimetric tests carried out during 24 h at different temperatures (25°C, 40°C, and 60°C). The results showed that IE depends on the lignin concentration and the ionic strength between the solution and the pH of the lignin sample, as shown in Table 35. The performance of lignin in decreasing order was Reax 88A>Reax 100M>Reax 88B. Additional analysis concluded that lignin adsorbed to the steel following the Langmuir isotherm. Furthermore, FTIR analysis and energy-dispersive spectroscopy evidenced the formation of a protective layer of lignin on the steel surface by the development of an Fe+2-S-lignin complex (Abu-Dalo et al., 2016).

Table 35:

Inhibition efficiency of different lignosulfonate samples in acidic media.

Test condition and method Lignin concentration %IE Reference
2 mg/l HCl, WL, 25°C, 6 h, Reax 88A 500 ppm

700 ppm
55.88

60.97
(Abu-Dalo et al., 2016)
2 mg/l HCl, WL, 25°C, 12 h, Reax 88A 500 ppm

700 ppm
63.91

71.64
2 mg/l HCl, WL, 25°C, 24 h, Reax 88A 500 ppm

700 ppm
83.74

85.52
2 mg/l HCl, WL, 25°C, 6 h, Reax 88B 500 ppm

700 ppm
36.77

39.21
2 mg/l HCl, WL, 25°C, 12 h, Reax 88B 500 ppm

700 ppm
42.32

45.99
2 mg/l HCl, WL, 25°C, 24 h, Reax 88B 500 ppm

700 ppm
53.38

56.40
2 mg/l HCl, WL, 25°C, 6 h, Reax 100M 500 ppm

700 ppm
31.51

36.67
2 mg/l HCl, WL, 25°C, 12 h, Reax 100M 500 ppm

700 ppm
44.52

47.08
2 mg/l HCl, WL, 25°C, 24 h, Reax 100M 500 ppm

700 ppm
57.56

61.06

4 Concluding remarks

  • Among the plant-derived corrosion inhibitors reviewed in this paper, alkaloid-based inhibitors were reported to be the most efficient in protecting steels in acidic media, and chemisorption was found to be the main mechanism of inhibition, with efficiency ranging from 80% to 95%.

  • The high efficiency attained by the alkaloid-based inhibitors was due to the presence of nitrogen atoms in pyrrolic rings that protonate in aqueous media, hence outcompeting hydrogen ions from the acidic solution for chemisorption.

  • The efficiency of corrosion inhibition of terpene-based chemicals was found to be between 60% and 80% in acidic media, and the inhibition mechanism was reported to be mixed type or cathodic. Most cathodic terpene inhibitors were reported to chemisorb on metal surface.

  • The efficiency of corrosion inhibition of polyphenols was reported to be influenced by the composition and location of the phenol groups, and the corrosion inhibition performance was reported to be similar to the essential oils (terpene based).

  • Despite their low solubility in water, lignin extracts from various plants were reported to be efficient corrosion inhibitors. Opportunity exists to functionalize lignin formulations for application in high-temperature environments and water systems.

About the authors

Andrea Marciales

Andrea Marciales received her BSc in chemical engineering from the Industrial University of Santander (UIS), Colombia. In 2011, Andrea joined the Colombian Petroleum Institute (ICP) as a consulting engineer for Ecopetrol. She later obtained her MSc in petroleum engineering from the University of Alberta in 2015, working on selection of solvent for unconventional recovery processes. In 2016, she worked as a research assistant at the University of Alberta, focusing on the development of green inhibitors and microbiologically influenced corrosion. In 2017, she joined InnoTech Alberta as a corrosion engineer.

Tesfaalem Haile

Tesfaalem Haile obtained his PhD in civil and environmental engineering from the University of Western Ontario, London, Canada, in 2009. Tesfa has been working in R&D and corrosion consultancy since 2006. He leads several corrosion projects, including corrosion in oil sand thermal and mining operations, investigating MIC in Canadian onshore operations, and testing the efficiency of lignin as a corrosion inhibitor, among others. He is the principal investigator of the projects he manages.

Behzad Ahvazi

Behzad Ahvazi completed his Bachelor of Science in Honours program at the Department of Chemistry and Biochemistry, and graduated with distinction at Concordia University in Montréal, Québec. His PhD program was completed in 1998 at McGill. Currently, he is working at InnoTech Alberta as a Principal Researcher for Biomass Conversion and Processing Technologies, aimed at developing high-end value-added applications from pulp and lignocellulosic materials such as cellulose nanocrystals and lignin. Dr. Ahvazi is also an adjunct professor in the Department of Mechanical Engineering, University of Alberta.

Tri-Dung Ngo

Tri-Dung Ngo obtained his PhD in mechanical engineering from Concordia University, Montreal, Canada, in 2007. He held a position as lecturer and researcher at Faculty of Chemical Engineering and thereafter Materials Engineering at HCM Polytechnic University from 1997 to 2002. He worked at National Research Council of Canada as a researcher from 2003 to 2014. Dr. Ngo joined InnoTech Alberta as a research scientist in 2014. His research focuses on biomass processing and development of novel, eco-friendly biomaterials. Dr. Ngo is also an adjunct professor at Department of Civil and Environmental Engineering, University of Alberta.

John Wolodko

John Wolodko is currently the AI Strategic Chair in Bio and Industrial Materials, and an associate professor at the University of Alberta in Edmonton, Canada. His areas of research include the development and characterization of sustainable materials from agricultural and forestry feedstocks, life cycle assessment, and materials for the energy sector. Dr. Wolodko is a former Executive Director at AITF (formerly the Alberta Research Council), and has over 20 years R&D experience in advanced materials, manufacturing, testing, and engineering design.

Acknowledgments

The authors would like to thank Dr. Tamer Crosby for providing scientific review.

  1. Funding: The authors would like to thank Alberta Innovates for funding the project.

  2. Conflicts of interest: The authors declare to have no conflicts of interest regarding this article.

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Received: 2017-08-10
Accepted: 2017-11-20
Published Online: 2018-02-09
Published in Print: 2018-06-27

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