1. Introduction
The use of Ti–Zr alloys instead of pure titanium is becoming increasingly attractive for medical devices due to the inherent synergistic advantages of the two metals compared to each pure metal alone [
1,
2,
3,
4]. Abutments with a zirconia surface, in addition to excellent aesthetic properties, also have outstanding biocompatibility and good mechanical properties. Although both titanium and zirconium oxides are considered bioinert, problems associated with peri-implant soft tissues that lack hemidesmosome structures, vertical collagen fibers, and effective blood supply pose challenges for improving gingival adhesion to abutments [
5]. Electrochemical treatments such as electrochemical anodization or electrochemical deposition can lead to obtaining a composite or nanostructured coating on titanium and zirconium surfaces and can significantly improve osseointegration and antibacterial properties [
6,
7]. Farrag et al. conducted a clinical study detailed in their article, which investigated the impact of anodized titanium on the health and appearance of peri-implant soft tissue. In this context, anodic oxidation serves as a surface modification method aimed at altering the color of titanium abutments. Titanium naturally forms an oxide layer on its surface immediately upon contact with atmospheric air. The process of anodic oxidation enhances the thickness of this oxide layer, which is influenced by the voltage applied during oxidation. By manipulating the thickness of the oxide layer, distinct colors can be achieved as it interacts with light in various ways [
8].
The anodizing process involves the application of an anodic potential to the surface of a metal, specifically pure titanium or a Ti–Zr 50%/50% alloy, to either dissolve the anode or generate dense oxide films on its surface. This oxide layer forms through ion migration, where ions move in alignment with the electric field. Metal cations are released from the bulk of the metal, while oxygen anions are sourced from the electrolyte, traversing through lattice imperfections, vacancies (both anionic and cationic), and interstitial defects. In the case of titanium and zirconium, the growth rate of the oxide layer is limited by the migration of O
2− ions from the film/electrolyte interface to the metal/oxide interface, where the O
2− ions react with oxidized titanium or zirconium, Ti
4+/Zr
4+ [
9,
10].
The reactions that occur are as follows:
For the Ti–Zr 50%/50% alloy (the anodic potential is high enough to allow simultaneous oxidation of Ti and Zr):
The thickness of the oxide film is directly dependent on the total electric charge in the system, the anodization time, and the density of the oxides. The thickness of the oxide layer is influenced by the overall electric charge within the system, the duration of anodization, and the oxide density. Pauporté et al. investigated the anodic formation of titanium and zirconium oxide films in a NaOH environment using electrochemical impedance spectroscopy and scanning electron microscopy. Their research revealed a strong correlation between the thickness measurements obtained through the EIS technique and direct observations of the films cross-section. This led to the hypothesis that the outer layer of the oxide film contains very small pores, allowing the electrolytic solution to penetrate into the defects of the film [
11]. There is a dispute regarding the crystalline and amorphous nature of the titanium dioxide and zirconium produced on the surface of the metal layer.
Researchers have indicated that the amorphous structure changes to a crystalline form at temperatures between 400 and 600 °C. The temperature at which titanium dioxide or zirconia is transformed from the amorphous phase starts around 300 °C, and the transition is gradual [
12]. It was shown that the anatase (101) crystal plane appears first, and the other crystal planes appear in order. The rutile (110) crystal plane appears first, and the other crystal planes appear in successive order, thus the rutile (110) crystal plane has the lowest energy and is the most stable, so it is not recommended to exceed a temperature of 500 °C for this transition, as the subsequent crystalline forms are gradually less stable [
12,
13,
14].
Liu et al. used the electrochemical anodization technique to improve zirconia surfaces by removing oxygen from solid metal oxides via molten salt electrolysis. They suggested that the anodized zirconia exhibits well-ordered and low microporous contact angles and a slight decrease in monoclinic phase content [
15]. The nanotube structure is characterized by easy control of pore size, large surface area, chemical stability, mechanical stiffness and excellent compatibility [
16,
17]. Tsuchiya et al. showed that electrochemical anodization could form highly organized zirconia nanotubes with diameters of about 50 nm~130 nm and a length of 17 μm [
18]. Guo et al. showed that when zirconia nanotubes were immersed in simulated body fluids for 20–30 days, bone-like apatite could form on the surface of zirconia nanotubes, indicating that zirconia nanotubes could exhibit favorable bioactivity [
19]. Jennes et al. conducted a study in which they systematically reviewed articles dealing with antibacterial surfaces or coatings of implant abutments that can suppress bacterial growth and thus prevent plaque-induced peri-implant inflammatory diseases [
20].
The reviewed literature shows that electrochemical treatments such as anodization, electrochemical deposition or any other combined functionalization that include anodization of Zr-containing Ti alloys which lead to an increased corrosion resistance besides improved mechanical properties, have enhanced biocompatibility and a favorable price–performance ratio. These treatments produce a composite or a nanostructured coating on titanium surfaces that can significantly improve adhesion and antibacterial properties [
6,
21,
22,
23,
24,
25]. After comparing the literature data for the most commonly used types of treatment for impact surfaces, it can be stated that (a) the roughness created on the metal surface is determined by the size, shape and velocity of the particles used in the sandblasting process, while in electrochemical anodizing, the nanotube structure is characterized by an easily controllable pore size, large surface area, chemical stability, mechanical strength and excellent compatibility; (b) compared to anodizing, which can be applied to conductive materials, the sandblasting process can also be applied to non-conductive materials such as ceramics or cermets (metallized ceramics), but the results produce anisotropic abrasion with unevenly distributed roughness.
The main disadvantage of the sandblasting technique is that it can slightly change the chemical nature of the surface due to the inevitable contamination by aluminum oxide, whereas with electrochemical anodizing, the surface contamination can come from traces of the remaining electrolytic solution. (c) Unlike blasting and anodizing surface treatments, plasma treatment can remove low-energy surface contaminants, clean and increase surface free energy and improve cell adhesion kinetics. (d) Compared to sandblasting and acid etching techniques, laser treatment carries zero risk of surface contamination, as there is no direct contact between the laser and the biomaterial.
Laser surface treatments, sandblasting and acid etching enhance the wettability of materials by altering their surface characteristics, which are crucial for promoting cell adhesion.
The purpose of this work was to investigate the influence of the anodization and thermal treatment applied to a Ti–Zr alloy on the morphology and composition of the mixed-oxide layer formed at the surface of this alloy and on the hardness of the oxide layer subjected to thermal treatment compared to the untreated ones. This study holds considerable significance as it offers a comparative analysis of distinct and combined functionalization techniques, specifically anodization and thermal treatment, applied to a Ti–Zr alloy. It aims to produce oxide layers with improved characteristics, which could be beneficial for applications in corrosion protection and restorative dentistry.
2. Materials and Methods
The chemical reagents used were of p.a. and were from Sigma-Aldrich/Merk, (Merck KGaA, Darmstadt, Germany). The solutions, where the case is, were prepared using ultra-pure water that have the value of resistivity >18.5 mΩ·cm. The Ti–Zr alloy rods (50% Ti-50% Zr) CSTY202116 (ZrTi-50 +/− 2%, Fe 0.2%, Si 0.5%, Vickers Hardness 300) were purchased from Baoji City Changtai Metals Trading Co., Ltd., Xiamen, China) and were cut in disks with a diameter of 32 mm and thickness of 1.2 mm using a Citizen Cincom (Esslingen, Germany) L20 8M CNC computer-controlled lathe with 6 linear axes and two rotary axes. The chosen composition of 50% titanium and 50% zirconium was selected for its ability to merge the advantageous characteristics of both metals, including biocompatibility, strength, corrosion resistance, osseointegration, and gum adhesion. This formulation also mitigates the predominant influences of either metal during the analytical phase.
The disks were wet polished with 200, 600, 2000 and 4000 Optimus Colad emery paper with sponge support to prevent damaging the surface, followed by a finer finish polish with diamond paste (see
Supplementary Materials Figure S1), and then washed thoroughly and rinsed with distilled water. The disks were immersed in an ultrasonic bath (@40 kHz) containing distilled water with 0.1% liquid detergent for advanced cleaning, for 10 min, rinsed with ultrapure water, dried, immersed in isopropyl alcohol 96%, dried by blowing with air at a pressure of 1.5 bar and subjected to the following treatments:
Sample with index 1–blank sample, control, mixed-oxide layer formed naturally;
Sample with index 2–non-anodized sample, thermally treated at 450 °C;
Sample with index 3–anodized and thermally untreated sample;
Sample with index 4–sample anodized and heat treated at 450 °C.
A house made with a thermostated electrical double-insulated refractory cylindrical longitudinal furnace (300 mm external diameter and 500 mm total length) was used for thermal treatment. Its core was a hallow cylinder on the inside with an internal diameter of 60 mm, provided with a K-type thermocouple temperature probe (−50 °C~1300 °C). The cylindrical, longitudinal ceramic element is wrapped in a high-power electrical resistance material connected to a variable voltage a.c. power supply with the possibility of varying the voltage applied to the resistor terminals at will. Adjusting the applied voltage directly influences the current passing through the resistor, allowing for precise control of the temperature within the ceramic tube. To enhance energy efficiency, the space between the active component and the outer cylinder is filled with refractory chamotte, which serves to insulate and direct the heat produced by the resistor towards the inner ceramic cylinder. By managing the applied voltage, the furnace can maintain a wide range of regulated temperatures from 60 to 600 °C over prolonged durations.
The furnace was calibrated prior to use (basically, the applied voltage was set to the desired value and the temperature in the furnace was recorded after 15 min using the temperature probe and the digital thermometer connected to the temperature probe). The furnace was brought to the desired temperature before each experiment and kept there for 15 min to achieve thermal equilibrium before the sample was inserted. A blank control sample with the mixed-oxide layer formed naturally was also initially tested to see whether it was a compact one and whether it offers a certain degree of protection against corrosion attacks. To achieved this, two well-established electrochemical techniques were used: open circuit potential, OCP, and electrochemical impedance spectroscopy, EIS. OCP measurements are also required as a preliminary conditioning stage for EIS measurements.
OCP is also known as open circuit voltage, zero current potential, corrosion potential, equilibrium potential, or resting potential. This measurement is a fundamental electrochemical technique used to assess the susceptibility and development of a reaction in a specific corrosion environment. In measuring open circuit potential, the test material is placed in an electrolyte in conjunction with a stable, non-polarizable reference electrode and the evolution of the material’s potential relative to the reference electrode is monitored. This is also called corrosion potential monitoring. The reference electrode is a non-polarizable one with a very high internal resistance, e.g., gigaohms, so that the value of the current passing through the circuit made of the two electrodes is practically zero. In this way the potential difference between the two electrodes can be considered as an electromotive voltage.
If the value of the potential increases over time, progressing towards more electronegative values, this indicates an increase in the protective capacity of the passivation layer on the metal surface, indicating greater corrosion resistance. On the other hand, when the potential values tend to go toward more electropositive values, this may indicate a greater susceptibility to the reaction in the chosen electrolyte. Electrochemical impedance spectroscopy is a non-destructive electrochemical analysis method that provides information about the electrochemical properties of the tested systems. This technique measures the impedance, i.e., resistance to alternating current, at the interface of the electrochemical system. One of the important parameters measured in EIS is the charge transfer resistance, which indicates the degree of difficulty in the transfer of charges from the electrode to the surface of the electrochemical interface.
In EIS, impedance is measured as a function of frequency and is plotted as a Nyquist plot or Bode plot. The analysis of these diagrams can provide detailed information about the electrochemical processes taking place at the interface of the analyzed system such as charge transfer resistance, electric double layer capacity etc. Charge transfer resistance (Rct) is one of the important parameters in EIS. This is defined as the resistance to the transfer of charges from the electrode surface to the electrochemical interface and is influenced by the properties of the electrochemical interface, the structure and composition of the medium, as well as the properties of the deposited oxide layer, essentially its thickness. Being a directly measurable quantity, the assessment will be quantitative. Rct can be obtained from the Nyquist plot, which is a graphical representation of measured impedance versus frequency.
Impedance is usually measured by applying an alternating potential to the electrochemical cell and measuring the current in the cell. When a sinusoidal potential is applied, the response is an alternating current signal containing the frequency and shape of the signal. The current signal can be analyzed as a sum of sinusoidal functions. Electrochemical impedance is usually measured with a small excitation signal, so the cell response is pseudolinear. The equipment used for the above experimental determinations was a computer controlled Voltalab 40 potentiostat/galvanostat, equipped with EIS module and digital data acquisition system, where the recordings of the potential data in the open circuit, as well as electrochemical impedance spectra, were carried out. For EIS, a potential disturbance of 10 mV above the given voltage value of OCP in the frequency range of 100 kHz–100 mHz was used. The full experimental protocol, as well as the complete depiction of all operational parameters is found in the
Supplementary Materials Figure S2–S6, integrated part of this paper.
The electrochemical tests described above were carried out in a three-electrode electrochemical cell made of PTFE (a glass cell is not suitable as the fluoride ions from the electrolyte attack the glass and this leads to a decrease in the available fluoride ion concentration); the working electrode was a Ti–Zr alloy disk (active immersed surface of 25.26 cm
2); a saturated silver/silver chloride reference electrode was used (Radiometer Analytical), fitted with a Luggin capillary; a mesh platinum electrode was used as the auxiliary electrode; and the electrolyte was the anodizing solution presented in
Table 1. To avoid accidental cross-contamination, the disks were held by a Ti medical Grade 4 rod with a slit at the holding points slightly smaller than the disk thickness, so that the disk is held in place by pressure and friction (see
Supplementary Materials Figures S2–S6).
A number of four Ti–Zr alloy samples (50%/50%, mass percentages), coded as above, were considered for testing the combined anodization/oxide thermal conversion effect. A ceramic support was used to allow for an easy introduction of the samples in the furnace, as shown in
Figure 1 and
Figure 2. The anodization was carried out in a PTFE beaker (to prevent the loss of fluoride) employing a two-electrode cell, in a mixed potentiostatic and galvanostatic setup, using a constant current–constant voltage power supply SPS-12003N (Umax = 120 V, Imax = 3 A) provided with precision digital ammeter, voltmeter and wattmeter. If the anodization is performed at voltages above 30 V, then the conversion of the amorphous phase into the crystalline phase of Ti and Zr oxides is performed at temperatures between 400 and 500 °C.
The following anodizing stages and the thermal conversion were chosen for this procedure:
Determination of the working current density: the sample is pre-anodized at a constant voltage of 35 V for 180 s. At the end of the period, the value of the current is read.
The configuration of the anodizing electrical source is changed from potentiostatic to galvanostatic, and the value of the anodizing current is kept constant and equal to the value determined in the pre-anodization stage. Knowing the required current density and measuring the surface area of the sample allows for straightforward calculation of the anodization current. The anodization process is performed in galvanostatic mode, maintaining a constant current to ensure that the electrochemical reaction rate remains stable, as the current density directly influences this rate during the anodization.
The sample is anodized for a period of 30 min, following the variation of the anodizing voltage over time.
The thermal conversion was carried out for a period of 15 min, in the presence of excess air supplied by introducing an air flow of 5 L/min, (see
Supplementary Materials Table S1 for the flow rate calibration) timed from the point when the furnace reached the temperature of 450 °C, and this temperature was kept constant by the thermostating device.
SEM/EDX analysis was performed using an Apreto S microscope (Thermo Fisher Scientific, Waltham, MA, USA) equipped with an EDAX Inc., Mahwah, NJ, USA, device. The SEM micrographs were recorded applying an accelerating voltage of 10 kV and a current of 6.3 pA, standard ETD, scale 20–400 μm, magnification 70×–40,000×, while the elemental composition was determined based on the data recorded using the TEAMTM software V1.10. (15 kV and 1.6 nA).
For the comparative evaluation of the hardness of mixed oxides obtained by anodization versus anodization and thermal treatment, we used the Shore scale employing a modified Shore hardness tester. The Shore hardness is rated on the International RHardness Degree scale normalized in centigrade, from 0 to 100. The higher the number indicated, the harder the material will be. Values between different Shore classes can be made equivalent to each other or to other scales (e.g., Rockwell or Brinell) using either tables, equivalence charts or regression equations (see
Supplementary Materials Figures S7–S11 and
Table S3). A modified certified Hardness Shore D digital tester type 560-10D (certification number 0021787/2024 certified for ISO 868/2003 stan [
26]) supplied by Heli Innovation Ltd., Sofia, Bulgaria with a penetration force of 44.5 N and a 0.5 D resolution was used to assess the differences in hardness of the obtained mixed oxides between anodized disks and anodized and thermally treated disks. This was mounted on a specially constructed stand to ensure a reproducible perpendicular position, and the conical probe was replaced with a tronconical one. A correction factor K was determined to take into consideration the shape of the tronconical probe versus the conical one. The measurements were carried out in series of 5 replicated tests.