Jen Yang
Yap
a,
Sarini
Mat Yaakob
a,
Nurul Ekmi
Rabat
*b,
Muhammad Rashid
Shamsuddin
c and
Zakaria
Man
b
aDepartment of Chemical Engineering, Universiti Teknologi PETRONAS, Bandar Seri Iskandar 32610, Perak, Malaysia
bCentre for Contaminant Control and Utilization (CencoU), Institute of Contaminant Management, Universiti Teknologi PETRONAS, Bandar Seri Iskandar, 32610, Perak, Malaysia. E-mail: nurulekmi.rabat@utp.edu.my
cCenter for Biofuel and Biochemical Research (CBBR), Institute for Sustainable Living, Universiti Teknologi PETRONAS, 32610 Bandar Seri Iskandar, Perak, Malaysia
First published on 1st April 2020
This study focuses on the release kinetics of inhibitor-loaded nanocontainers and the anti-corrosive properties of epoxy coatings doped and undoped with the nanocontainers. In this work, 1-butyl-3-methylimidazolium chloride [Bmim][Cl] was loaded into halloysite nanotubes (HNTs), and the loaded HNTs were encapsulated with polyethyleneimine (PEI)/polyacrylic acid (PAA) and poly(diallyldimethylammonium chloride) (PDADMAC)/polyacrylic acid (PAA) to allow controlled release upon pH stimuli. The polyelectrolyte layer deposition was characterized using zeta potential analysis, and the release profiles were evaluated in neutral, acidic, and alkaline media. The release kinetics was studied and found to conform to the Ritger–Peppas and Korsmeyer–Peppas model, and the results proved that the combination of weak polyelectrolytes (PEI and PAA) provided a good response for up to 50% release of [Bmim][Cl] in acidic and alkaline media after 72 hours. The loaded HNTs encapsulated with the PEI/PAA combination were incorporated into an epoxy coating matrix and applied on an X52 steel substrate. The corrosion resistance of the coated and uncoated substrates was evaluated using electrochemical impedance spectroscopy (EIS) after immersion in a 3.5 wt% NaCl solution up to 72 hours. An artificial defect was created on the coating prior to immersion to evaluate the active corrosion inhibition ability. The coating doped with the smart pH-responsive halloysite nanotubes showed promising results in corrosion protectiveness even after 72 hours of exposure to a salt solution through EIS and SEM.
Technological advancement has led to the discovery of many types of nanomaterials (nanotubes, nanoribbons, etc.), which can act as miniature reactors for chemical interactions, such as CO2 reduction5–7 and CO2 oxidation;8,9 they are efficient nanocontainers2,10,11 and present the possibility of surface modification (PEMs,12,13 grafting,14etc.) owing to their large available surface areas. Many types of nanocontainers have been explored by researchers to encapsulate inhibitors, such as carbon nanotubes,15 halloysite nanotubes,4,16 polymeric capsules,17,18 and layered double hydroxides.19 Among these, halloysite nanotubes are one of the most cost-effective because they are found naturally, inexpensive, and highly abundant nanostructures with a unique hollow lumen structure that is capable of high loading capacity.20 Halloysite nanotubes possess a unique multilayer structure with a chemical formula of Al2Si2O5(OH)4, where the silica layer is on the exterior and the alumina layer is on the interior. Due to the different compositions of the exterior and interior of the tubular structure, halloysite possesses different surface charges, where the exterior (silica) is negatively charged and the interior (alumina) is positively charged. With this unique property, HNTs can be loaded with various types of functional compounds possessing dissimilar charges and has been proved to provide prolonged release of material. Abdullayev and his coworkers successfully loaded an azole-type corrosion inhibitor into halloysite nanotubes; the HNTs were capable of prolonging release up to 20 to 50 hours.21 Loading of a functional compound into HNTs effectively avoids direct interaction of the functional compound with the coating matrix and external environment while maintaining the coating continuity due to the small size of the HNTs.11
An ionic liquid is a molten salt typically composed entirely of ions that exist in a liquid state below 100 °C.22 It is generally considered to be a green solvent due to advantages such as non-flammable nature, low vapor pressure, and excellent stability over a wide range of temperatures; thus, it an excellent corrosion inhibitor to be used in extreme corrosion conditions.23 A highlight of ionic liquid is that it is a “designable” material, where the chemistry of the cation and anion can be altered to achieve desirable properties. Among the family of ionic liquids, imidazolium compounds have been proved to be effective mixed-type corrosion inhibitors for mild steel due to the presence of –CN– groups.24 The anion counterpart of imidazolium ILs serves as an electron donating group which transfers its electrons to the empty d orbitals of iron in mild steel via chemisorption. On the other hand, the positively charged imidazolium structure will be attracted towards the negatively charged steel surface via electrostatic interaction, resulting in physisorption and formation of a protective monolayer.24,25 Due to this interaction, imidazolium-based ILs are highly suitable for inhibition of corrosion in mild steel.26 However, while the ionic liquid is considered to be an effective corrosion inhibitor, it has only been explored to be mixed in chemical process streams such as acidizing treatment and completion fluid in the oil and gas industry, acid cleaning, acid descaling, acid etching, and acid pickling.27 Applying these techniques allows the usage of a lower grade of steel and improves cost-effectiveness. Direct addition of ionic liquid can cause undesirable changes to coating properties; in the case of epoxy resin, the ionic liquid acts as a latent hardener or curing agent, resulting in loss of corrosion inhibition functionality.28,29 Loading of ionic liquids into nanocontainers unlocks the possibility to incorporate them into coating formulations, providing active corrosion protection, enhanced mechanical properties, and increased service life of the coating.
The release of the loaded corrosion inhibitor can be designed based on a desired stimulus, and the release rate can be tuned accordingly with the modification of PEMs, thus achieving smart release with prolonged storage capability. Polyelectrolyte multilayers (PEMs) with defined characteristics and tuneable properties can be fabricated via the layer-by-layer (LBL) technique. The LBL technique enables the self-assembled sequential build-up of polymeric layers via deposition of charged polymers alternating between cationic and anionic onto a charged substrate. The deposition through electrostatic attraction can be applied with a wide variety of building blocks, allowing the incorporation of a broad range of functional units.30 PEMs have been constructed that possess distinctive properties based on their individual polyelectrolytes,30,31 molecular weight,32 salt concentration,33,34 and pH.35 It has also been reported that the ultimate properties of PEMs are highly dependent on the outermost assembled layer.36 PEMs fabricated via the LBL technique can be engineered to respond to various stimuli, such as pH level, humidity, temperature, and conductivity.37 Incorporation of pH-responsive PEMs enables the corrosion inhibitor to be contained without deterioration and release when triggered by local changes in pH at the cathodic and anodic areas of corrosion initiation. Yu et al. proved that the deposition of polyelectrolyte layers on HNTs loaded with 2-mercaptobenthiazole can result in more controlled and sustained release.11
In this research, an imidazolium-based ionic liquid was loaded into HNTs. 1-Butyl-3-methylimidazolium chloride [Bmim][Cl] was used because it has been proven to be an effective mixed-type corrosion inhibitor.38 Surface encapsulation of the loaded HNTs with polyethyleneimine (PEI), polydiallyldimethylammonium chloride (PDADMAC), and polyacrylic acid (PAA) via the LBL technique was conducted to achieve smart release upon pH stimulus. The release was analysed in neutral, acidic, and alkaline mediums to observe the effects of pH on the release profile. Finally, the corrosion inhibition of the synthesized smart pH-responsive halloysite nanotubes was evaluated after they were incorporated in an epoxy matrix and coated on a steel substrate.
![]() | ||
Scheme 1 Schematic of (a and b) the loading process of [Bmim][Cl] into the HNTs and (c–e) polyelectrolyte deposition via the LBL technique. |
The release profiles of all the samples were fitted using the Ritger–Peppas and Korsmeyer–Peppas model (power law)39 with a modification of the initial drug release (burst effect) proposed by Kim and Fassihi:40
![]() | (1) |
Sample | Zeta potential (mV) |
---|---|
Blank HNTs | −32.47 |
HNT–[Bmim][Cl] (PEI) | +28.93 |
HNT–[Bmim][Cl] (PEI, PAA) | −11.39 |
HNT–[Bmim][Cl] (PDA) | +33.30 |
HNT–[Bmim][Cl] (PDA, PAA) | −15.57 |
In this research, planar thin films are assumed because the HNTs possess openings at both ends of the tubes, while the radial surface is impenetrable. The Ritger–Peppas and Korsmeyer–Peppas model adequately describes the mass transport phenomena of a porous polymer system containing active compounds. In this research, the polyelectrolyte layer forms a hydrophilic slab; exposure of the PEMs to water causes several changes, including changes in mobility and relaxation of macromolecular chains, leading to changes in the shape and size of the pore distribution.
The fitted curves and the corresponding parameters are displayed in Fig. 5 and Table 2. The release of [Bmim][Cl] with n < 0.5 indicates that the release was controlled by its low diffusivity in the polyelectrolyte layer as the inner content swells. From Table 2, most of the samples fall within this category, mainly because the encapsulation restricted the release of [Bmim][Cl]. The release exponent of n = 0.5 indicates Fickian diffusion (Case I), where the release of inner content is governed by diffusion across the concentration gradient. The release exponent within the range of 0.5 < n < 1 indicates that the release of [Bmim][Cl] is controlled by the viscoelasticity of the relaxation of polyelectrolyte layers during solvent penetration, causing the anomalous time-dependent effect. Lastly, n = 1 indicates that the release follows zero-order kinetics, in which the [Bmim][Cl] was released at a constant rate.
Sample | Exposed medium | n | k | R 2 |
---|---|---|---|---|
HNT–[Bmim][Cl] | Neutral | 0.74 | 1.39 | 0.9863 |
HNT–[Bmim][Cl] | pH 4 | 0.61 | 2.15 | 0.9718 |
HNT–[Bmim][Cl] | pH 10 | 0.78 | 1.24 | 0.9827 |
HNT–[Bmim][Cl] (PEI) | Neutral | 0.42 | 6.01 | 0.9463 |
HNT–[Bmim][Cl] (PEI) | pH 4 | 0.64 | 5.72 | 0.9956 |
HNT–[Bmim][Cl] (PEI) | pH 10 | 0.34 | 5.09 | 0.9481 |
HNT–[Bmim][Cl] (PEI, PAA) | Neutral | 0.57 | 1.28 | 0.9572 |
HNT–[Bmim][Cl] (PEI, PAA) | pH 4 | 0.42 | 6.23 | 0.9290 |
HNT–[Bmim][Cl] (PEI, PAA) | pH 10 | 0.48 | 5.95 | 0.9895 |
HNT–[Bmim][Cl] (PDA) | Neutral | 0.52 | 3.89 | 0.9901 |
HNT–[Bmim][Cl] (PDA) | pH 4 | 0.43 | 4.15 | 0.9767 |
HNT–[Bmim][Cl] (PDA) | pH 10 | 0.43 | 5.97 | 0.9787 |
HNT–[Bmim][Cl] (PDA, PAA) | Neutral | 1.06 | 0.18 | 0.9940 |
HNT–[Bmim][Cl] (PDA, PAA) | pH 4 | 0.44 | 1.94 | 0.9527 |
HNT–[Bmim][Cl] (PDA, PAA) | pH 10 | 0.48 | 1.54 | 0.9596 |
In the HNT–[Bmim][Cl] (PEI) sample, PEI is a weak acid; therefore, pH changes significantly affect the porosity of the layer. PEI is an attractive cationic polyelectrolyte that is often used for nanoparticle engineering because of its weak-base buffering properties.46 In acidic medium, PEI has greater positive charge density owing to the excess H+ ion protonating the secondary and tertiary amines in the backbone.47 The highly charged PEI displays high intrachain repulsion, resulting in more linear backbone extension.46 When the HNTs encapsulated with PEI were exposed to acidic medium, the highly charged PEI with more linear expansion resulted in a more porous polycationic layer, thus allowing the [Bmim][Cl] with small molecular size to escape. This phenomenon can be observed by the change in the release exponent from 0.42 in neutral medium to 0.64 in the acidic medium of HNT–[Bmim][Cl] (PEI). In alkaline medium, PEI experiences deprotonation due to the lack of H+ ions and loses charge, resulting in low intrachain repulsion; this eventually causes aggregation. The shrinkage of PEI can reduce the permeation of loaded content, resulting in an even smaller release exponent of 0.34. The difference in the release mechanism resulted in very different ultimate releases of 43.10% (neutral), 95.99% (pH 4), and 30.15% (pH 10) after 72 hours, although the release rate constants for all three conditions are similar. With the addition of the PAA layer to the HNT–[Bmim][Cl] (PEI, PAA) sample, the responsiveness of its release in both acidic and alkaline mediums is more pronounced. PAA is a weak polyanion with increasing charge at an elevated pH level. When the pH drops, PAA tends to shrink and prevent PEI from further expansion, restricting the pathway for the loaded content to pass through. On the other hand, PAA is highly charged, resulting in a more linear expansion in the alkaline medium. PAA also possesses unique characteristics of capacity to absorb water.48 When exposed to alkaline medium, the PAA layers swell due to the highly charged linear expansion and absorption of water. This phenomenon causes Fickian diffusion of [Bmim][Cl] in neutral medium, with an n value equal to 0.57; here, the partially charged PEI and PAA act as porous watery shells that enable diffusion based on concentration. Subjecting the material to acidic and alkaline medium causes the release exponent to fall below 0.5. However, the release rate constants in acidic medium and alkaline medium differ considerably from that in neutral medium, namely 6.23 (pH 4), 5.95 (pH 10) and 1.28 (neutral); this is directly reflected in the actual ultimate releases of 14.74% (neutral), 40.66% (pH 4) and 53.27% (pH 10).
On the other hand, the strong/weak combination of PDADMAC and PAA, in which PDADMAC is a strong polycation, will show a lower response to pH changes.31 The deposition of a single layer of PDADMAC in the HNT–[Bmim][Cl] (PDA) sample showed a release exponent of 0.52; this exhibits release near to Fickian diffusion, where the release depends on the concentration gradient. Exposure to both acidic and alkaline medium changes the release mechanism to 0.43, which exhibits restricted release, while the inner content swells with solvent penetration. The ultimate release of HNT–[Bmim][Cl] (PDA) reached 42.70% (neutral), 30.89% (pH 4) and 42.86% (pH 10). The addition of another layer of PAA further restricts the release of [Bmim][Cl]. This effect can be seen in HNT–[Bmim][Cl] (PDA, PAA) subjected to neutral medium, where the release exponent was 1.06 but the release rate constant was only 0.18. The encapsulation of PDADMAC and PAA creates a porous watery outer shell caused by high association of water molecules with the carboxylate groups; this allows constant rate diffusion but a significantly low release rate due to restriction by the organic environment of PDADMAC, which does not favour water.31 When subjected to acidic medium, the restriction increases as the PAA layer loses charge and shrinks, resulting in a release exponent of only 0.44. In alkaline medium, the PAA layer swells, causing the release to be near to Fickian diffusion. All three mediums afforded similar ultimate releases of 16.65% (neutral), 18.60% (pH 4) and 15.07% (pH 10) at 72 hours.
Corrosion initiation or an incoming external solution can cause pH changes to affect the stability of a complex, triggering release of the inner content.49 To develop an effective smart responsive nanocontainer containing a corrosion inhibitor, the PEMs should be tuned to release when triggered by pH changes while remaining stable in neutral medium. From the release kinetics of the samples, it can be observed that the weak polyelectrolyte displayed high response towards pH changes, while the strong polyelectrolyte retained its stability throughout the pH variation. Responsiveness towards either acidic or alkaline medium is highly dependent on the types of polyelectrolytes deposited and their configuration. This effect can be seen clearly in the HNT–[Bmim][Cl] (PEI) sample, where the loaded HNTs were deposited with single layer PEI. Due to the nature of PEI, the release responsiveness of the layer favoured acidic medium while providing a lower release rate in alkaline medium. The HNT–[Bmim][Cl] (PEI, PAA) sample appears to be an excellent candidate as an effective smart-responsive nanocontainer because it can respond to both acidic and alkali mediums; it was selected for evaluation of its anti-corrosion performance.
![]() | ||
Fig. 6 (A) Simple randles circuit (R(RQ)) for the BS sample; (B) Randles circuit (R(R(RQ)Q)) for the SE and SH samples. |
For the bare steel (BS) sample, a simple Randles circuit of R(QR) was employed which involves the resistance of the solution (Rs), double layer capacitance (Qdl) and charge transfer resistance (Rct). The Nyquist diagram did not show the perfect semicircle of a pure capacitor, which can be attributed to two reasons: frequency dispersion due to interfacial porosity or roughness and the kinetic dispersion effect.50,51 Hence, to model the imperfect capacitor, the constant phase element (Q) was preferred. The impedance of the constant phase element can be computed from the formula below:
![]() | (2) |
For steel coated with bare epoxy (SE) and epoxy with the addition of smart pH-responsive halloysite nanotubes loaded with the [Bmim][Cl] (SH) sample, a Randles circuit ECM of R(R(QR)Q) was used to fit the data, as shown in Fig. 6. In the high-frequency range, the electric current was distributed uniformly throughout the coating area, presenting as a semicircle fitted with a parallel circuit (Rpore, Qcoat), corresponding to the pore resistance and dielectric behavior of the coating. When the frequency range moves to the lower range, the electrical current is focused at the active corrosion site, which occurs where the artificial defect was created. This phenomenon was fitted with another parallel circuit of (Rct, Qdl) in series with Rpore, corresponding to charge transfer resistance and double layer capacitance, respectively (Fig. 6).
From the analysis of the Nyquist plot as shown in Fig. 7 and Table 3, the bare steel (BS) sample showed an increasing trend in Rct from 129.78 Ω cm−2 at the 1st hour of exposure to 201.07 Ω cm−2 after 72 hours of exposure owing to the formation of stable oxide films as a result of corrosion, which offers slight resistance towards the propagation of the current. The decrease of the Rct value from 24 hours to 72 hours may be due to detachment of the thick accumulation of oxide layer. When an artificial defect was created on the epoxy-coated mild steel sample, ions in the surrounding solution came into contact with the metal substrate, leading to corrosion initiation without hindrance. The formation of thick oxide layers, as shown in the SEM images in Fig. 8b, provides a certain limitation of the corrosion at the defective coating area, leading to an increase in charge transfer resistance from 7337 Ω cm−2 at the 1st hour of exposure to 12677 Ω cm−2 after 72 hours of exposure. When the coating continuity of the SH sample was damaged due to the artificially induced crack, the embedded SH nanoparticles exposed to the surrounding environment experienced pH changes due to localized corrosion. The inner content was released as the polyelectrolyte layer experienced changes due to pH changes in the surroundings. The released [Bmim][Cl] was able to undergo both chemisorption and physisorption onto the negatively charged mild steel surface, thus forming a protective layer that provided a significantly higher charge transfer resistance of 170
210 Ω cm−2 at the 1st hour of exposure.25 The charge transfer resistance further increased to 310
760 Ω cm−2 at 72 hours of exposure with the continuous release of [Bmim][Cl] from the embedded SH nanoparticles. The Rpore values in the SE and SH samples showed a decreasing trend with increasing immersion time. As the immersion time increases up to 72 hours, the decreasing trend of Rpore may be caused by the increase in the exposed area.52 This may be due to propagation of the corrosion site, which leads to slight delamination of the coating. The decrease of Rpore, however, could be compensated with the increasing Rct as a result of the inhibition effect of [Bmim][Cl]. Comparing the SEM images from Fig. 8 for both the SE and SH samples after immersion, one can observe a distinct visual difference in the amount of corrosion product above the metal substrate. This phenomenon was in agreement with the EDS results as shown in Table 4, where the oxygen weight percent of the SE sample increased from 0.5 wt% to 21.2 wt% and that of the SH sample increased from 1.2 wt% to 10 wt%. The presence of nitrogen and chloride in the scratched area of the SH sample proved the release of [Bmim][Cl] from the nanotubes, and the inhibition of [Bmim][Cl] results in lower formation of corrosion product, as indicated by the oxygen weight percentage.
Sample | Immersion time (Hr) | R s (Ω cm2) | R pore (Ω cm2) | R ct (Ω cm2) |
---|---|---|---|---|
BS | 1 | 2.9 | — | 129.78 |
24 | 2.43 | — | 252.73 | |
72 | 2.19 | — | 201.07 | |
SE | 1 | 105.03 | 1035.5 | 7337 |
24 | 105.31 | 858.4 | 12![]() |
|
72 | 114.15 | 978.15 | 12![]() |
|
SH | 1 | 407.11 | 163![]() |
170![]() |
24 | 456.38 | 132![]() |
222![]() |
|
72 | 550.84 | 23![]() |
310![]() |
![]() | ||
Fig. 8 SEM images of SE (a) before and (b) after and of SH (c) before and (d) after 72 hours of immersion in 3.5 wt% NaCl solution. |
Sample | Immersion | % weight percent ratio of elements | |||||
---|---|---|---|---|---|---|---|
Fe | C | O | N | Cl | Na | ||
SE | Before | 90.8 | 8.3 | 0.5 | — | — | — |
After | 70.9 | 7 | 21.2 | — | 0.4 | 0.4 | |
SH | Before | 83.3 | 14.9 | 1.2 | — | — | — |
After | 79.2 | 8.5 | 10 | 0.8 | 0.2 | 0.1 |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/d0ra01215g |
This journal is © The Royal Society of Chemistry 2020 |