Recovery of W(VI) from Wolframite Ore Using New Synthetic Schiff Base Derivative

Abstract

A new synthetic material, namely, (3-(((4-((5-(((S)-hydroxyhydrophosphoryl)oxy)-2-nitrobenzylidene) amino) phenyl) imino) methyl)-4-nitrophenyl hydrogen (R)-phosphonate)), was subjected to a quaternary ammonium salt and named (HNAP/QA). Several characterizations, such as FTIR spectrometry, ¹H-NMR analysis, ¹³C-NMR analysis, ³¹P-NMR Analysis, TGA analysis, and GC-MS analysis, were performed to ensure its felicitous preparation. HNAP/QA is capable of the selective adsorption of W(VI) ions from its solutions and from its rock leachate. The optimum factors controlling the adsorption of W(VI) ions on the new adsorbent were studied in detail. Furthermore, kinetics and thermodynamics were studied. The adsorption reaction fits the Langmuir model. The sorption process of the W(VI) ions is spontaneous due to the negative value of ∆G° calculated for all temperatures, while the positive value of ∆H° proves that the adsorption of the W(VI) ions adsorption on HNAP/QA is endothermic. The positive value of ∆S° suggests that the adsorption occurs randomly. Ultimately, the recovery of W(IV) from wolframite ore was conducted successfully.

1. Introduction

The potential toxicity of heavy metals in aquatic environments varies significantly between their different chemical forms and the fact that they are neither biodegradable nor photodegradable [1]. As a lithophile element, tungsten can be found in wolframite and scheelite ores, where it is recovered as tungstate (WO₄²⁻) and naturally occurs in soils and sediments [2,3]. The concentration of W(VI) in the lithosphere varies from 0.2 to 2.4 mg kg⁻¹ [2,3,4], while in ocean water it is present in the range of 8.0 to 100 mg L⁻¹. On the other hand, in the surface rocks of the Northern Atlantic and the Pacific Oceans, it is in the range of 1.0 to 1.3 mg kg⁻¹ [2,4]. In terms of solubility and dominance, tungstate (WO₄²⁻) predominates over its hydroxyl counterpart. The oxidation state of tungsten ranges from −2 to +6, making it a transition metal. There is a potential for tungstate species to polymerize in mildly acidic conditions, yielding iso-polytungstates, polytungstates, and monotungstates [5]. For example, tungsten inhibits molybdenum metabolism, which, in turn, reduces the biological activity of molybdenum-containing enzymes such phosphatase and adenosine triphosphate enzymes [6]. Even in tiny quantities, tungstate species present a significant hazard. As a result, testing and treating natural water supplies for tungsten is essential [7,8,9]. The disposal of their waste requires proper measurements, as this waste also contains valuable metals, and tossing these heavy metals is perilous due to the depletion of their primary resources, which leads to environmental hazards because of these minerals. Manganese is an important metal that has numerous applications in industry. It should be reprocessed and not disposed of. The high melting point of tungsten has extensive applications, such as manufacturing super alloys for high-temperature tasks, catalysts for redox chemical reactions, and fertilizers and in power plants as a regulator of oxygen and nitrogen compounds to mitigate environmental damage [10,11,12,13]. A hydrometallurgical process is used for the extraction of tungsten from both its ores and industrial effluents. Tungsten is recovered using processes such as solvent extraction [14,15], ion-exchange method [16], chemical precipitation [17], filtration [18], electrolysis and electro-deposition [19].

Tungsten is one of the elements classified as a significant raw material by the European Commission, according to its economic significance and supply chain. In 2022, the average price of tungsten was around USD 270 per metric ton unit of tungsten trioxide [20]. Tungsten has many extensive applications in several industries, such as the automotive industry, defense equipment, chemical, and aviation industries [21]. However, there are stringent restrictions for the production of tungsten in which Mo, V, Si, and P are frequently found in the products as contaminants which violate the European standards of tungsten purity. When manufacturing high-purity tungsten and tungsten products, molybdenum is one of the most difficult contaminants to remove because of its chemical similarity to tungsten [22]. It is common for molybdenum minerals to be found around wolframite and scheelite minerals. According to a previous study from China, the mass ratio of Mo/WO₃ was about 2.0% in W-Mo-Bi-Sn scheelite crystals in the Shizhuyuan mine, while the mass ratio was above 5.0% in Mo‒W scheelite middlings from the Sandaogou mine [23].

The novelty of this work is the synthesis of a new adsorbent material with a high selectivity of W(VI) ions from its aqueous solutions and rock leachate. The prepared material undergoes several characterizations to ensure its successful preparation. The novel adsorbent is used for sorption of W(VI) ions from a synthetic solution and is finally used for the recovery of W(VI) ions from wolframite ore leachate via sorption and precipitation in a pure product.

2. Result and Discussions

2.1. Characterizations of the Sorbent

2.1.1. FTIR Analysis

The FTIR spectra of the prepared materials were collected and are presented in Figure 1. The broad peaks at 3385 and 3156 cm⁻¹ are due to the vibrations of –NH and –OH groups, respectively. The band observed at 1588 cm⁻¹ is related to the imine bond C=N, which is the most significant identification of the Schiff base [24]. The intense assignments located at 3049–3063 and 2987–3005 cm⁻¹ are attributed to aromatic and aliphatic υ(C–H), respectively [25,26]. The N–O stretching vibrations in the nitro group occur nearly at 1538 and 1328 cm⁻¹ of the asymmetrical and symmetrical vibrations, respectively. After phosphorylation, the composition of the HNAP was validated by FTIR, and new bands appearing at 2349 cm⁻¹ are assigned to the P–H stretching mode. The assignment at 1170 cm⁻¹ corresponds to the P=O stretching vibration. Moreover, a P–OH stretching vibration is recorded at 990 cm⁻¹ [27]. The quaternization reaction (a reaction with glycidyl trimethyl ammonium chloride) brings numerous –CH₃ groups with which a symmetric stretching vibration appears at 2875 cm⁻¹ [28]. In addition, the two sharp features located at 1463 and 1409 cm⁻¹ are assigned to the C–H stretching mode of the quaternary ammonium salt. The peak obtained at 964 cm⁻¹ is due the asymmetrical stretching vibration of the quaternary nitrogen of quaternary ammonium salt [29].

2.1.2. BET Surface Analysis

The surface area (S_BET) and porosity of HNAP and HNAP/QA were detected using the Brunner–Emmett–Teller theory at 77K. As seen in Figure 2, the N₂ sorption/desorption curves of HNAP and HNAP/QA are defined as IV type isotherms with limited H₃-type hysteresis. This means that HNAP and HNAP/QA are mesoporous-type materials. The HANP/QA surface area (S_BET: 178.4 m² g⁻¹) is higher than that of the HANP surface area of 101.6 m² g⁻¹. In addition, there is a slight increase in the pore volume of HNAP, increasing partly from 0.205 cm³ g⁻¹ for HNAP to 0.288 cm³ g⁻¹ for HNAP/QA after a reaction with glycidyl trimethyl ammonium chloride (

Table 1. Surface area and porosity of HNAP and HNAP/QA.

Substances	SBET (m2 g−1)	Pore Volume (cm3 g−1)	Pore Size (nm)
HNAP	101.6	0.205	2.8
HNAP/QA	178.4	0.288	1.78

).

2.1.3. ¹H-NMR Analysis

¹H-NMR analysis is considered an efficient technique that provides significant information about the protons of the synthetic adsorbent to determine its structure. The principal assignments (δ) observed at 7.31–7.91 ppm are assigned to the protons of –CH in the benzene ring. The assignments at 9.06, 8.84, and 6.28 ppm are due to the protons of –OH, –NH, and –PH, respectively. The characterization of HNAP is illustrated in Figure 3. After modification, significant differences are observed in HNAP/QA spectrum. The chemical shift of the –OH group appears as a doublet at 6.06 ppm with a coupling constant of J = 5.74 Hz. A shift to a lower chemical shift (7.55 ppm, d, 1H, J = 14.3 Hz) is observed for –the PH group due to the modification. Furthermore, new assignments were observed for methyl groups (3.18 ppm, s, 3H, J = 8.2 Hz), methine groups (4.2 ppm, m, 1H, J = 7.46 Hz), and aliphatic methylene groups (4.44 ppm, m, 2H, J = 11.38 Hz).

2.1.4. ¹³C-NMR Analysis

A ¹³C-NMR analysis of both HNAP and HNAP/QA was applied at 100.01 MHz to investigate the number of carbon atoms. As demonstrated in Figure 4A, the main assignments δ located around 126.9–127.5 ppm (s, J = 11.5, 6.9 Hz) are related to the carbon atom attached to the carbon of the imine group, the features at 146.6 ppm (s, J = 11.7, 7.9 Hz, –C=N) are related to the carbon of the imine group, the assignments at 143.8 ppm (s, J = 19.5 Hz) are attributed to the carbon attached to the nitro groups, and the assignments at 158.2 ppm (s, J = 7.5 Hz) are due to the carbon of the benzene ring attached to the phosphonic acid group, while the carbons of the benzene ring show assignments at 116.2–127 ppm (s, J = 3 Hz). Interestingly, the assignments of the de-protonated carbons were shown to be higher when de-shielded than any protonated carbons. After modification, a significant difference is observed in HNAP/QA, as illustrated in Figure 4B. A new feature appearing at 66.5 ppm (s, J = 6, 3.7 Hz, –CH₂) is related to the methylene group attached to the oxygen of the phosphonic acid group, the assignment at 64.2 ppm (s, J = 6.1 Hz, –CH) is related to the carbon attached to the –OH group, the assignment at 67.1 ppm (s, J = 6.1 Hz, –CH₂) is due to the carbon attached to the nitrogen of the quaternary nitrogen group, and finally, the carbons of the methyl groups of the quaternary nitrogen group show assignment at 53.7 ppm (s, J = 4.6 Hz, –CH₃).

2.1.5. ³¹P-NMR Analysis

A ³¹P-NMR analysis with an energy of 200.01 MHz is presented in Figure 5. The primary assignments of the HNAP/QA phosphorus atoms are observed at 6.53 ppm as singlets.

2.1.6. GC-MS Analysis

Figure 6 depicts the GC-MS chromatogram of HNAP/QA. It reveals that the most stable fragment [m/z]⁺ is [C₃₂H₄₄N₆P₂O₁₂Cl₂]˙, with a molecular weight of 837.58 g/mol and a relative abundance of 35%. The obvious peak at 78 g/mol with a relative abundance of 99% is due to the [C₆H₆]˙ benzene ring [C₆H₆]˙ or the [C₃H₇Cl]˙ propyl chloride. The fragments of nitro benzene [C₆H₅NO₂]˙, tropolium cation [C₇H₇]˙, and para-phenylene diamine [C₆H₈N₂]˙ have molecular weights of 123, 91, and 108 g/mol. The tiny peak at 64 g/mol with a relative abundance of 5% illustrates the formation of an ethyl chloride fragment [C₂H₆Cl]˙. The molecular weight of 36 g/mol is related to the [HCl]˙ fragment, which explains the liberation of hydrogen chloride gas. Moreover, the molecular weight of 95 g/mol refers to the formation of the quaternary trimethyl ammonium chloride moiety [C₃H₁₀NCl]˙. The recorded fragment with a molecular weight of 140 g/mol is due to para nitro phenol [C₆H₅NO₂]˙. An important note should be made for the fragmentation pattern mechanism for the compounds containing chlorine atoms. This fragmentation mechanism is most important where chlorine is a good leaving group. When one chlorine atom is present, M and M + 2 isotopic peaks become very significant, where M represents the molecular ion peak (M = 837 with an A% of 35% and M + 2 = 839 with an A% of 21). If the compound contains two chlorine atoms, a M + 4 isotopic peak should be observed, as well as an intense M + 2 peak (M + 4 = 841 with an A% of 10%). In addition, the thermal analysis of HNAP/QA is introduced in a supplementary file Figure S1.

2.2. Sorption of W(VI) Ions

Different factors were studied to optimize the sorption of W(VI) ions on the HNAP/QA ligand, as described below.

2.2.1. Influence of pH on W(VI) Ion Sorption

It is noteworthy that the pH value of the aqueous solution has a crucial impact on the adsorption of W(VI) ions. Changing the pH value has an obvious influence on not only the protonated/deprotonated active sites of the HNAP/QA but also the speciation of the tungsten ions formed. The pH value and metal content can affect the formation of W(VI) ions, as reported previously in in the literature [30]. Tungsten is a predominantly anionic species at pH values of over 2.0. Tungsten’s cationic species are completely absent at these pH levels. Since most W(VI) is found in anionic species, the adsorption behavior of W(VI) ions with HNAP/QA was studied in relation to the pH value. Given that WO₃(s) formation is possible at pH values below 2.0 in solutions [31], the obtained data (shown in Figure 7) demonstrate a general observed trend that the adsorption of W(VI) ions increased gradually from a pH 1.0 to 4.0 and reached a maximum adsorption efficiency at pH 4.5. The W(VI) ions sorption then decreased as the pH increased past a value of 4.5. At a pH value of 4.5, the percentage of absorbed tungsten reached a plateau of greater than 80% and then decreased gradually as a function of pH between pH 5.0 and pH 8.0. Understanding the tungsten solution species helps interpret this pH change.

For pH values between 2.0 and 8.0, W(VI) ions are present in the form of polynuclear anionic species, such as [W₁₂O₃₉]⁻, [W₁₂O₄₁]¹⁰⁻, and [W₆O₂₀(OH)]⁵⁻, while the formation of a neutral species, WO₂, occurs at higher pH values. As the pH of a solution rose from 7.5 to 9.0, the adsorption percentage of W(VI) decreased. Furthermore, the active site of the HNAP/QA sorbent is the quaternary ammonium chloride moiety, which acts as anion exchanger. This can be explained by a shift in the species distribution. A pH of 4.5 is the most suitable pH for the adsorption of W(VI) ions in this study.

2.2.2. Effect of HNAP/QA Dose

Figure 8 shows the impact of HNAP/QA dosage on the sorption percentage of W(VI) ions. The experiment was applied by boosting the adsorbent quantity from 0.01 to 0.2 g while holding all other variables stable at a 250 mg L⁻¹ W(VI) ion concentration and room temperature. High concentrations of HNAP/QA expose more of the tungsten’s surface, leading to a higher rate of adsorption. The adsorption was improved noticeably as the dose was raised from 0.01 to 0.08 g. There was a little noticeable change in the adsorption process after adding more adsorbents. The percentage of metal adsorbed determines the sorption capacity of HNAP/QA, and the data show that the greatest adsorption efficiency of tungsten was achieved at 0.08 g of HNAP/QA.

2.2.3. Kinetics Study

By analyzing kinetic profile, we can learn not only how long it takes to reach equilibrium but also how stable the material is, how it interacts with the target solute, and which stage in the sorption mechanism is ultimately responsible for regulating the process [32]. In fact, sorption occurs on the easily accessible active sites at the surface of the sorbent and the first exterior layers of the material, and almost 84% of total sorption occurs within the first 30 min of contact. The second stage involves a more gradual sorption caused by diffusion inside the sorbent’s pores. As presented in Figure 9, after 60 min of agitation, the equilibrium time was achieved because the WO₄²⁻ ions were adsorbed continuously from the solution until equilibrium was accomplished, and then no further change was observed after the increase in time.

The linear forms of Lagergren’s pseudo-first-order (PFO) and second-order (PSO) rate expression were used to predict the order of the kinetic adsorption process of W(VI) ions on HNAP/QA, as presented in equations below [33,34,35,36]:

$$\log (q_e-q_t)=\log q_e-\frac{K_{1}t}{2.303}$$

(1)

$$\frac{t}{q_t}=\frac{t}{q_e}+\frac{1}{K_2{q}_e^2}$$

(2)

where K₁ represents the PFO rate constant (min⁻¹), K₂ is defined as the rate constant of the PSO (g mg⁻¹ min⁻¹), and the quantities of WO₄²⁻ ions sorbed at any moment are denoted by q_t (mg g⁻¹). As provided in Figure 10, the log(q_e − q_t) vs. the agitation time (t) shows that the PFO model does not match the adsorption of WO₄²⁻ species on HNAP/QA. The calculated q_e value is 110.535 mg g⁻¹ (

Table 2. Kinetic parameters of W(VI) ions adsorbed on HNAP/QA.

PFO Kinetic				PSO Kinetic
K1	qe(cal)	R2	qe(exp)	K2	qe(cal)	R2
0.11469	110.535	0.9737	62.44	0.00145	66.225	0.9965

), higher than the value of the experimental q_e (62.44 mg g⁻¹). Nonetheless, the PSO model has a significantly higher value of R² (0.9965), which is close to unity, as listed in Table 2. Furthermore, the calculated q_e value, 66.225 mg g⁻¹, is also very close to the experimental value of q_e, 62.44 mg g⁻¹. The data point to a better match of the PSO equation to the adsorption of WO₄²⁻ ions on HNAP/QA. Thus, the chemical adsorption process of sharing/exchanging electrons between WO₄²⁻ species and HNAP/QA is best described as pseudo-second-order kinetics [37,38,39].

2.2.4. Effect of the Initial W(VI) Concentration

With the aim of determining the distribution of W(VI) ions between the aqueous and HNAP/QA phases, a study was conducted at 25 °C with 20 mL of several solutions of W(VI), ranging in initial concentrations from 250 to 1500 mg L⁻¹, and 0.08 g of HNAP/QA for 60 min. Figure 11 illustrates that the q_e of HNAP/QA rises regularly as the concentration of W(VI) ions increases. As a result, the optimal starting HNAP/QA adsorbent concentration in this study was determined to be 1250 mg/L.

2.2.5. Isotherm Study

Isotherm models representing the equilibrium distribution between the liquid and solid phases of the sorption system were attained. Langmuir, Freundlich, and Dubinin–Radushkevich isotherm models provide a valuable insight into the affinity of the HNAP/QA sorbent to the target W(VI) ions, the maximal sorption capacity at which the sorbent is saturated, and the binding mechanism between the W(VI) ions and HNAP/QA. Initially, the Langmuir isotherm model is expressed using the given equation below [40,41]:

$$\frac{C_e}{q_e}=\frac{C_e}{q_m}+\frac{1}{q_m{K}_l}$$

(3)

where C_e symbolizes the concentration at equilibrium (mg L⁻¹), q_e and q_m represent the amount adsorbed and the maximal amount adsorbed (mg g⁻¹), and K₁ refers to the apparent heat change. The Langmuir equation assumes a uniform sorption energy, and sorption occurs as a monolayer devoid of sorbent molecule interactions. As provided in Figure 12A and

Table 3. Isotherms parameters of W(VI) ions adsorbed on HNAP/QA.

Models	Parameters
Langmuir isotherm	Equation	y = 0.003x + 0.1832
	qmax (mg g−1)	333.33
	K1	0.0164
	R²	0.9937
Freundlich isotherm	Equation	y = 0.3982x + 1.5077
	Kf (mg g−1)	32.189
	1/n (mg min g−1)	0.3982
	R²	0.9894
D-R isotherm	Equation	y = −0.0064x + 5.7831
	qD (mg g−1)	324.76
	BD (Mol2 kJ−2)	0.0064
	E (kJ mol−1)	8.8388
	R²	0.9621
Practical Capacity	qe(exp) (mg g−1)	326.75

, the adsorption of W(VI) ions on HNAP/QA is shown to be Langmuir-like, indicating a monolayer of W(VI) ions covering the surface of HNAP/QA; the R² value approaches 0.99, and the Langmuir equilibrium constant K_l has a value of 0.0164 L mmol⁻¹. The Langmuir model predicts a maximum adsorption capacity of W(VI) ions on HNAP/QA of 333.33 mg g⁻¹, which is very close to the experimental adsorption capacity of 326.75 mg g⁻¹.

Secondly, the Freundlich isotherm denotes the multilayer sorption of ions onto the surface of the sorbent material, as described in the equation below [42,43]:

$$\log q_e=\log K_f+\frac{1}{n}\log C_e$$

(4)

where K_f corresponds to the adsorption capacity of HNAP/QA (mg g⁻¹) and n is a constant. The smaller the 1/n value, the stronger the interaction between the metal ions, the adsorbent and the working adsorbate. Additionally, 1/n = 1 signifies linear adsorption, which results in the same adsorption energies across all sites. According to the Freundlich isotherm, the binding strength decreases when the number of binding sites is increased [44]. The data in Table 3 and the plot in Figure 12B reveal that the Freundlich isotherm does not agree with the sorption of W(VI) ions on HNAP/QA, for which the K_f value (32.189 mg g⁻¹) is significantly lower when compared with the q_e(exp).

Lastly, the Dubinin–Radushkevich isotherm model is applied to differentiate between physical and chemical sorption because of adsorption heterogeneity [45,46,47]. It calculates the surface energy heterogeneity. The following is a linear formula of the Dubinin–Radushkevich model, calculated from the following equations:

$$\ln q_e=\ln q_D-B_D{(\epsilon )}^2$$

(5)

$$\epsilon =RT\ln (1+\frac{1}{C})$$

(6)

where B_D (mol² kJ⁻²) represents the energy of sorption, and ε symbolizes the Polanyi potential. B_D offers an opportunity to determine the adsorption energy E (kJ mol⁻¹) of W(VI) ions on HNAP/QA [48].

$$E=\frac{1}{\sqrt{2B_D}}$$

(7)

If the calculated value of E is less than 8.0 kJ mol⁻¹, the sorption process is defined as physisorption, while if the value of E is 8.0 < E < 16.0 kJ mol⁻¹, the sorption is believed to be chemisorption [49,50]. The data obtained from Figure 12C and listed in Table 3 show the E value is 8.839 kJ mol⁻¹. Therefore, the sorption of W(VI) ions on HNAP/QA is chemisorption process. The result is convenient with the Langmuir isotherm, which suggests a monolayer sorption.

2.2.6. Thermodynamics Study

The impact of temperature on the adsorption process was investigated using a 1250 mg L⁻¹ W(VI) solution, a pH value of 4.5, and 0.08 g (dry mass) of HNAP/QA at 298, 313, 323, 333, and 343 K. As demonstrated in Figure 13, the reaction rate rose gradually when the temperature was increased. As a result, the adsorption is considered an endothermic process; therefore, increasing the ambient temperature of the system is the correct choice to speed up the adsorption.

The thermodynamic parameters controlling the sorption system (ΔG°, ΔH°, and ΔS°) were mathematically determined from the Van ’t Hoff equations as follows [51,52]:

$$\mathrm{l}\mathrm{o}\mathrm{g}Kd=\frac{\Delta S}{2.303R}-\frac{\Delta H}{2.303RT}$$

(8)

$$\Delta G°=\Delta H°-T\Delta S°$$

(9)

where T is a symbol of the temperature of the system (K), and R stands for the gas constant (8.314 J mol⁻¹ K⁻¹). Both ∆H° and ∆S° can be calculated from the slope and the intercept of log K_d against the 1/T plot, as illustrated in Figure 14. The correlation coefficient is valued at R² = 0.9956. The values of the thermodynamic parameters are tabulated in

Table 4. Thermodynamic parameters of W(VI) ions adsorbed on HNAP/QA.

ΔS° (J mol−1 K−1)	ΔH° (kJ mol−1)	ΔG° (kJ mol−1)
75.887	10.36	298 K	313 K	323 K	333 K	343 K
		−21.89	−22.81	−23.54	−24.27	−25.0

; the negative value of ∆G° for all temperatures proves that the adsorption of W(VI) ions on HNAP/QA occurs spontaneously. In addition, the positive values of ∆H° and ∆S° indicate the endothermicity and randomness of the W(VI) sorption process.

2.2.7. Effect of Foreign Metal Ions on Selectivity

In order to investigate the selectivity of HNAP/QA toward the uptake capacity of W(VI) ions in the presence of different existing metal ions, the sorption process of W(VI) ions was conducted employing several ion solutions of Mo(VI), V(V), Ca(II), Cu(II), and Pb(II) with different concentrations ranging between 10 and 500 mg L⁻¹. The obtained data in Figure 15 illustrate that the selectivity strength of the HNAP/QA material was slightly affected by the high concentrations of V(V), Ca(II), Cu(II), and Pb(II) ions. Impressively, the uptake of W(VI) ions was intensely influenced by the presence of Mo(VI) ions. It is more likely that the ability of the HNAP/QA material to adsorb cations through the chelation mechanism with a lone pair of electrons on the hydroxyl groups as well as the phosphine group of oxygen results in a reduction in the selectivity of the HNAP/QA sorbent to some extent. In the case of Mo(VI), both metals have the same chemical properties; therefore, both cations compete for the same binding sites, causing an obvious decrease in the adsorption efficiency. However, the HNAP/QA adsorbent is still effective in the case of the presence of several ions in the system. The result indicates that the HNAP/QA adsorbent demonstrates a high selectivity of W(VI) ions compared to other elements.

2.3. Desorption–Regeneration Study

The desorption of a metal-loaded sorbent was investigated not only for the possibility of reusing of the sorbent but also for the recovery of the valuable metal ion. Firstly, different types of eluents were used for the desorption of W(VI) ions, such as ascorbic acid, HCl, NH₄Cl, NaOH, and NH₄OH solutions (0.25 M), which were used as eluting agents at room temperature for 10 min. The obtained data in Figure 16A show that the best eluent for the efficient recovery of W(VI) is NH₄Cl, which is capable of recovering 79.2% of loaded W(VI) ions on HNAP/QA. Secondly, the influence of the concentration of NH₄Cl on the recovery of W(VI) ions was then studied using several concentrations varying from 0.25 to 2.0 M, as shown in Figure 16B. The obtained data show that 0.5 M NH₄Cl achieved a recovery of 92.6% of the loaded W(VI) ions on HNAP/QA. Lastly, the influence of the desorption time was assessed by ranging the elution period between 5 and 50 min. Figure 16C demonstrates that 20 min was sufficient for the recovery of almost 79.2% of the W(VI) ions from the loaded sorbent. It is completely clear that when the metal-loaded HNAP/QA was investigated before and after desorption with 0.5 M NH₄Cl for 20 min at an ambient temperature, no presence of W(VI) ions was detected after desorption; it is an evident that all W(VI) ions were recovered back to the solution, as provided in Figure 17.

2.4. Recovery of W(VI) Ions from Wolframite Ore

One of the most important and promising areas is Gabal (G) Qash Amir, in the extreme southeastern part of Egypt. It is considered a rich area with economic and strategic metals such as Mn, Zr, Ta, U, Nb, and W. In the last decade, many new W-rich mineralizations were discovered in the studied area of new Gabal Qash Amir [40,41,42,43,44,45]. The region known as G. Qash Amir is in the extreme southeastern corner of the Egyptian Eastern Desert; it is located approximately 28 km southwest of Abu-Ramad city and not far from the border of Sudan, bounded by longitudes 36°10′59″–36°14′24″ E and latitudes 22°14′07″–22°15′21″ N. This area is a section of the Arabian-Nubian shield zone.

2.4.1. Pre-Concentration of Wolframite Ore

A working technological ore sample was precisely collected from a mineralized invading quartz vein within G. Qash Amir wolframite granite. A bulk sample (10 kg, containing around 0.43% w/w of WO₃) was ground using a roll mill crusher and jaw crushers to diminish the mineral particles to a size of less than 1.0 mm. The gravity concentration was performed using a lab wet Wilfley shaking table (Holman-Wilfley Ltd., Redditch, UK); this operation allowed for the production of a W-rich concentrate (about 83.0 g). The next step in the pre-processing consisted of a magnetic separation utilizing a high-intensity induced magnetic roll separator (Carpco Model MLH (13) III-5, Outokumpu Technology, Inc., Jacksonville, FL, USA) to recover wolframite-rich minerals (Figure 18).

2.4.2. Characterizations of the Wolframite Ore

Wolframite is a tungsten mineral that mainly consists of manganese tungsten oxide (Fe,Mn)WO₄; it is the intermediate mineral between ferberite (Fe²⁺ rich) and hübnerite (Mn²⁺ rich). The semi-quantitative analysis of wolframite samples shows the preponderance of both W and Mn elements (88.8%, w/w) and the presence of a non-negligible fraction of silicate and iron. The wolframite sample was confirmed using SEM-EDX and XRD characterizations, as can be seen in Figure 19 and

Table 5. Chemical compositions of wolframite sample.

Element	Concentration (%)
WO3	77.13
MnO	8.99
SiO2	0.58
Al2O3	0.3
Fe2O3	3.9
SO3	0.49
CaO	7.57
Others	1.04

.

2.4.3. Extraction of Tungsten Oxide

The first stage is the tungsten leaching from W-concentrate; this process was carried out with HCl (30% w/w HCl solution) to eliminate most of the Mn and Fe content [53]. The acid-leaching step was performed using continuous stirring at 400 rpm for 3 h at 110 °C and a 1:1.5 solid to liquid (S/L) ratio. Secondly, the wolframite sample was subjected to alkaline leaching using 300 g of NaOH (40%, w/w, NaOH solution); the leaching process was applied at 400 rpm and a S/L ratio of 1:3 for 2 h at 130 °C. The alkaline leaching process allowed for the dissolution of almost all the W-content and some traces of Mn and Fe. The obtained leachate was analyzed, and the W concentration is listed in

Table 6. Chemical compositions of wolframite leachate.

Element	Concentration (%)
WO3	89.46
MnO	0.004
SiO2	0.46
Al2O3	0.3
Fe2O3	0.002
CaO	7.57

.

The leachate was filtered, and the pH was adjusted to 4.5. The HNAP/QA adsorbent was used to adsorb W(VI) ions from the leachate; the adsorption process was conducted based on the best controlling factors studied previously (pH 4.5, agitation time of 60 min, 2.0 g of HNAP/QA, and 250 mL of leachate at room temperature). Adsorption was accomplished, and the W(VI) content was recoverable through the separation of HNAP/QA in 0.5 M of NH₄Cl for 20 min at room temperature. Later, the W(VI) ions were precipitated from the eluate using 30% HCl. A yellow WO₃·nH₂O product was formed. Finally, the precipitate was rinsed multiple times with ultrapure water and heated at 70–90 °C for 30 min to dry. This was followed by calcination at 500 °C for 2 h. The final product was characterized using SEM-EDX analysis, and the data are shown in Figure 20.

The EDX patterns indicate the W and O as the major elements and no notable impurities, while the SEM image shows the irregular shape of WO₃ to be a flower-like structure. A flow sheet summarizing the recovery of W(VI) ions from the wolframite ore is provided in Figure 21.

3. Materials and Methods

3.1. Chemicals and Reagents

P-phenylenediamine and 2-hydroxy-5-nitrobenzenaldehyde were purchased from Thermo Fisher Scientific (Morris Plains, NJ, USA). Shanghai Makclin Biochemical Co., Ltd. (Shanghai, China) provided the glycidyl trimethyl ammonium chloride (95%), AlCl₃, and NaOH. Phosphorus oxychloride, sodium tungstate (Na₂WO₄⋅2H₂O), NaCl, CHCl₃, CDCl₃, dimethyl sulfoxide, and CH₃OH were purchased from Sigma-Aldrich (St. Louis, MO, USA). All chemicals were of a very high purity level and required no further processing before use. All the experimental solutions were prepared using ultrapure water of 18.2 MΩ·cm. Thin paper chromatography (PC) was utilized to explore the synthesis process. Furthermore, a basic UV lamp set to 250 nm and an eluent comprising a combination of 1:1 v/v ethanol and ethyl acetate were used to identify spots formed on the PC.

3.2. Preparation of the Adsorbent (HNAP/QA)

A methanolic solution of 2-hydroxy-5-nitrobenzenaldehyde (10 mL, 25 mmol) was added drop-wise to a 10 mL methanolic solution of p-phenylenediamine (25 mmol) in the presence of an acid (2 mL of 98% H₂SO₄) with stirring. The mixture was allowed to reflux at 70 °C for 6 h. The reaction’s volume decreased by half under a vacuum. An orange-yellow precipitate was formed, which was filtered, washed out multiple times by methanol, and left to air-dry overnight. The TLC was used to monitor the progress of the condensation reaction. The produced Schiff base (3,3′-((1,4-phenylenebis(azaneylylidene))-bis(methaneylylidene))-bis(4-nitrophenol)) was provided a PZN abbreviation, and the final yield was determined as 90%. The produced material was subjected to phosphorylation, which took place through an interaction with 0.2 g of AlCl₃ and 25 mL phosphorus oxychloride with vigorous stirring for 30 h at a temperature of 110 °C (Scheme 1). AlCl₃ and POCl₃ were used as phosphorylating agents to introduce a phosphonic acid group. The AlCl₃ aids in the release of HCl during the reaction. A pale yellow precipitate was formed, separated through filtration, rinsed numerous times with ultrapure water and methanol, and allowed to dry overnight in the air. The produced material was named HNAP, referring to phosphorylated beads of (3-(((4-((5-(((S)-hydroxyhydrophosphoryl)oxy)-2-nitrobenzylidene) amino) phenyl) imino) methyl)-4-nitrophenyl hydrogen (R)-phosphonate)); its purity was assessed using TLC and was found to be 94.0%, (Scheme 1).

The phosphorylated beads (HNAP) were subjected to quaternization; this reaction occurred through the reflux of 4.5 g of HNAP in a three-necked flask containing a solution of 12.0 g of glycidyl trimethyl ammonium chloride with vigorous stirring for 36 h at 100 °C. The final product was separated by filtration and washed out several times with ultrapure water and methanol to remove the unreacted materials and solvent. The product was dried then overnight in the air. The produced material, HNAP/quaternary ammonium salt, was named (HNAP/QA). All synthesized chemicals were provided with names in accordance with the IUPAC nomenclature.

3.3. Instrumentation

We tested the adsorbent using the following spectroscopic techniques: FTIR (Nicolet™ iS50, Thermo Fischer Scientific, Morris Plains, NJ, USA), mass spectra using a Hitachi M-8000 unit, Tokyo, Japan, SEM-EDX using a Hitachi S 4160 FE SEM, Tokyo, Japan, and NMR in a 500 MHz field using a Bruker Fourier 80, Billerica, MA, USA. The concentrations of ions were measured using inductively coupled plasma mass spectrometry (ICP-MS) (NexION 1000, PerkinElmer, Waltham, MA, USA).

3.4. Adsorption and Elution Experiments

A tungstate stock solution of 1000 mg L⁻¹ was prepared by dissolving a proper weight of sodium tungstate (Na₂WO₄⋅2H₂O) in a 0.01 M NaCl solution. The sorption experiment was conducted in three independent batches, each of which was made from the stock solution. HCl and NaOH, at concentration of 0.1 M each, were administered to adjust the acidity of the solution. For the standard batch sorption tests, the experiments were carried out using a 20 mL of 250 mg L⁻¹ W(VI) ion solution for 30 min and 0.1 g of HNAP/QA at 25 °C, unless stated otherwise. The pH of the aqueous medium was changed from 1.0 to 6.0 to study the impact of the pH value. In addition, the experiments were performed at an amount of adsorbent between 0.01 and 0.2 g for a period of 30 min and a 250 mg L⁻¹ W(VI) ion solution at a pH of 4.5 and at room temperature to investigate the effect of the adsorbent dose. The sorption time was studied likewise by varying the contact time between 5 and 90 min. Finally, the effect of temperature was investigated between 25 and 70 °C. The adsorption efficiency (S%) of the W(VI) ions and the adsorption capacity (q_e) were calculated using equations below:

$$S\%=\frac{C_o-C_e}{C_o}\times 100$$

(10)

$$q_e=(C_o-C_e)\times \frac{V}{m}$$

(11)

where C_o and C_e (mg L⁻¹) are the W(VI) ion concentrations in the liquid phase at the beginning and end of the experiment, respectively, and q_e (mg g⁻¹) symbolizes the sorption capacity. In this equation, V (L) represents the volume of the working solution, and m (g) corresponds to the dry weight of the HNAP/QA.

3.5. Desorption Experiments

Desorption is a crucial step in recycling a sorbent material and recovering W(VI) ions. Once the adsorption experiment was completed, desorption tests were performed using the adsorbent in a batch system. NaOH, NH₄OH, HCl, NH₄Cl, and ascorbic acid were among the desorptive substances investigated in this study. The desorption time and the concentration of the desorptive substances were also studied. The concentrations of the metal ions in the supernatant were detected using ICP-MS.

4. Conclusions

HNAP/QA, which is an abbreviation of (3-(((4-((5-(((S)-hydroxyhydrophosphoryl)oxy))-2-nitrobenzylidene) amino) phenyl) imino) methyl)-4-nitrophenyl hydrogen (R)-phosphonate), is a new synthetic adsorbent material. HNAP/QA has a high selectivity for W(VI) ions from its aqueous solution. Several characterization techniques, such as FTIR, GC-MS, TGA, and NMR analyses, were used to ensure its successful preparation. The optimal factors influencing the retention of W(VI) ions on the new adsorbent were thoroughly examined and found to be a pH of 4.5 and 30 min of sorption time at room temperature. Kinetics and thermodynamics were also investigated; the adsorption reaction follows a Langmuir model. The sorption process of the W(VI) ions is spontaneous due to the negative value of ∆G° for all temperature values, while the positive value of ∆H° indicates that the adsorption on HNAP/QA is an endothermic mechanism. In addition, the positive value of ∆S° proposes an increase in the randomness of the adsorption activities in the investigated system. Finally, HNAP/QA was successfully used for the adsorption of W(VI) ions from wolframite ore, and pure W(VI) ions were separated via precipitation.