Open Access Article
Shahab Shariati*a,
Yadollah Yaminib,
Mohammad Farajic,
Abolfazl Salehd and
Elahe Bozorgzadeh
a
aDepartment of Chemistry, Ra.C., Islamic Azad University, Rasht, Iran. E-mail: Sh.Shariaty@iau.ac.ir; Fax: +98-1313462231
bDepartment of Chemistry, Faculty of Sciences, Tarbiat Modares University, Tehran, Iran
cFood, Halal and Agricultural Products Research Group, Food Technology and Agricultural Products Research Center, Standard Research Institute (SRI), Karaj, Iran
dIranian National Institute for Oceanography and Atmospheric Science (INIOAS), Tehran, Iran
First published on 5th January 2026
In this study, a convenient and sensitive off-line cloud point extraction method (off-line CPE) was developed to preconcentrate trace amounts of aluminium (Al) ions prior to their determination by flow injection (FI) coupled to inductively coupled plasma-atomic emission spectrometry (ICP-AES). The method is based on the formation of a complex between Al3+ and 3, 2′, 4′, 5, 7-penta hydroxy flavone reagent, using Triton X-114 as a non-ionic surfactant to extract the formed complex and facilitate phase separation. Following extraction, the micellar phase containing Al ions was analyzed using ICP-AES coupled with a flow injection system (FI-ICP-AES). The off-line CPE variables were optimized using the Taguchi method, resulting in optimal conditions of pH 4.5, 1000 µg L−1 reagent, 0.1% (w/v) Triton X-114, 0.25 mol L−1 salt concentration, and an equilibrium temperature of 60 °C. Under these conditions, a linear calibration range of 1.0–500 µg L−1 was achieved for determination of Al ions, with a detection limit (DL) of 0.89 µg L−1, an enhancement factor of 54.7, and a relative standard deviation (RSD) below 3.1%. The accuracy and applicability of the proposed off-line CPE/FI-ICP-AES method were evaluated by analyzing Al ions in various aqueous samples, yielding satisfactory and reliable results.
Different preconcentration methods including cloud point extraction20–25, coprecipitation,23 and analytical methods such as sensors,2,26–29 electrothermal atomic absorption spectrometry (ET-AAS),30–32 spectrofluorimtery,28,33–36 and inductively coupled plasma-atomic emission spectrometry (ICP-AES)37 have been used for the determination of aluminum (Al3+) ions. At low concentrations of Al3+ in real samples, suitable enrichment procedures are required for Al3+ determination. The capabilities of micellar systems and other self-assembled molecular assemblies have been acknowledged for a long time and have seen growing use in multiple domains of analytical chemistry recently. Cloud point extraction (CPE) relies on the use of high-concentration solutions of specific uncharged and zwitterionic surfactants, which form a uniform solution under certain environments. Water solubility of the surfactant decreases by altering temperature, pressure, or adding certain substances, causing the solution to become cloudy.38–42
Trace amounts of metals in complex matrices have been analysed using CPE methods, which present a practical alternative to conventional extraction techniques,43,44 that require large volumes of toxic and costly solvents. Such solvents pose significant risks to human health and the environment. In contrast, CPE methods are faster, safer, and more efficient, employing environmentally friendly surfactants that align with the principles of green analytical chemistry. For trace metal analyse, CPE is commonly adjusted to incorporate hydrophobic molecules through ligand complexation to enhance extraction efficiency. Upon heating, this mixture move into the cloud point phase, facilitating straightforward separation using centrifugation. When suitable chemicals and conditions are utilized, extraction at ambient temperature is reliable and effective, requiring only a brief period to finish.30,38,45–49
In this study, we combined off-line cloud point extraction with flow injection for sample introduction into the analytical instrument. A straightforward and adaptable system (off-line CPE/FI-ICP-AES) was developed to preconcentrate and determine Al ions in aqueous samples. During off-line CPE preconcentration, the hydrophobic chelate formed between Al3+ ions and 3, 2′, 4′, 5, 7-pentahydroxy flavone (morin) was extracted into the surfactant phase, which was subsequently injected into the FI-ICP-AES for further analysis.
The method novelty and enhanced analytical performance are achieved through a synergistic integration of three key components: morin as a selective chelating agent for Al3+, Taguchi experimental design for systematic and robust multivariable optimization of the extraction process, and the off-line coupling of CPE with FI-ICP-AES for efficient analyte introduction. This triad directly addresses the principal constraints of CPE method for aluminum—namely, susceptibility to interferences from non-optimal chelation, inefficiencies from univariate optimization, and potential dilution or transfer losses. Consequently, the protocol delivers the superior analytical metrics including an expanded linear dynamic range and a significantly lowered detection limit, there by advancing the state-of-the-art in trace aluminum determination.
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| Fig. 1 Schematic diagram of the six-port injection valve containing loop (L) in conjugation of FI to ICP-AES. (a) Load position, and (b) inject position. | ||
In FI-ICP-AES, the plasma was first activated during the sample loading step, with the injection valve set to the “load” position. Following several injection cycles, a cleaning solution was introduced into the loop to ensure thorough washing and purification. Using a Hamilton syringe, 180 µL of the surfactant-rich phase was injected into the six-port injection valve containing the loop to fill it completely. Subsequently, the valve was switched to the “inject” position, and the rinsing solution was pumped through the loop by a peristaltic pump. This process rinsed the sample through the loop into the nebulizer, enabling measurement of the Al emission at the appropriate wavelength during atomization. The instrument operated in time-scan mode, recording the emission intensity of Al at the specified wavelength during each injection as a function of time. The emission intensity was calculated as the difference between the peak intensity of the emission spectrum and its baseline value, as detailed in the following equation and Fig. 2.
| Peak height intensity = max (all of points)−Average (baseline points at the left of the peak) |
Morin contains two active sites for chelation: the 3-hydroxy and 4-oxo sites, as well as the 5-hydroxy 4-oxo site. Additionally, the 2,3 dihydroxy system can also act as a chelating agent, capable of forming a 7-membered chelate with Al3+. Studies indicate that when measuring Al3+ through spectrophotometry and fluorimetry, an acetate medium with a pH of 3.5 to 6.5 is ideal for forming complexes.50–52 The stoichiometric ratio of the Al-morin complex is influenced by the solvent used and the solution pH. In a methanol solution, Al3+ forms two types of complexes with morin at stoichiometries 1
:
1 and 1
:
2, while in acidic methanol solutions containing 0.1 mol L−1 nitric acid, only 1
:
1 complexes are formed. The absorption spectrum of morin exhibits a maximum peak at 355 nm, which decreases in intensity in aqueous solutions at pH 4.5 (using 0.05 mol L−1 ammonium acetate).51,52 Increasing the concentration of Al3+ ions causes the absorption band of morin at 355 nm to diminish, while a new absorption band appears at 413 nm.52 This red shift in the absorption spectrum of morin is attributed to the formation of a complex between Al3+ ions and morin, likely due to coordination of the lone pair of electrons on the oxygen donor atom with the Al3+ ion, resulting in reduced electron density on the chromophore. The stoichiometry of the complex formed between Al3+ and morin has been investigated using the molar ratio method in solutions with uncontrolled pH.52 The molar ratio curve at a wavelength of 415 nm for uncontrolled pH exhibited an inflection point at an Al3+/M = 1.5 ratio, indicating a stoichiometry of 3
:
2 (Al3M2) for the complex. While the molar ratio curves at wavelengths 355 and 413 nm at pH = 4.5 (amunium acaetate) exhibited an inflection point at an Al3+/M = 1 ratio, indicating a stoichiometry of 1
:
1 (AlM) for the complex.52
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| Fig. 4 Effects of instrumental variables including (A) viewing height (B) nebulizer pressure (C) rinsing solvent type, and (D) rinsing solvent rate on the Al emission intensity in ICP-AES. | ||
The maximum emission intensity in the plasma, evaluated relative to the plasma height above the coil, can be affected by the element type, solvent, sample matrix, power supply, and nebulizer gas pressure. For optimizing the viewing height, argon gas was purged with a plasma gas flow rate of 15 L min−1, an auxiliary flow rate of 1.5 L min−1, and the RF generator operating at 40 MHz frequency. Fig. 4(A) illustrates the signal intensity as a function of time for a 10 mg L−1 Al3+ solution using the FI method, based on several consecutive injections at each viewing height. As observed, the highest emission intensity was recorded at the lower viewing height. Consequently, a height of 6 mm above the induction coil was selected as the optimal viewing height to achieve greater sensitivity and reproducibility. Fig. 5 shows the effect of viewing height for a 10 mg L−1 Al3+ solution analyzed using the FI method, based on multiple consecutive injections recorded in time-scan mode at each viewing height.
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| Fig. 5 Optimal viewing height design for a 10 mg L−1 Al3+ solution using the flow injection method, based on multiple consecutive injections at each viewing height. | ||
Nebulizer pressure influences signal intensity in two main ways. First, increasing nebulizer pressure enhances nebulization efficiency, allowing more analyte species to enter the plasma. However, higher pressure shortens the residence time of species within the plasma, potentially reducing their opportunity for excitation and emission. The optimal nebulizer pressure depends on factors such as viewing height, RF power, and sample flow rate. As shown in Fig. 4(B), at a viewing height of 6 mm, the signal intensity versus nebulizer pressure plot indicates 160 kPa as the optimal pressure value.
One of the most critical variables affecting the preconcentration process is the choice of solvent used to reduce the viscosity of the surfactant-rich phase and facilitate its rinsing from the loop. Even a small increase in the amount of organic solvents can disrupt micelle aggregates, thereby lowering the viscosity of the surfactant-rich phase. A selection of common organic solvents was investigated. To prevent baseline shifts in the injection system, it is ideal that the diluent for the surfactant-rich phase and the rinsing solvent of the loop to be of the same type; otherwise, baseline fluctuations may occur. Pure organic solvents, due to their high vapour pressure, can cause plasma quenching or instability, which compromises analytical performance. Therefore, mixtures of organic solvents with water were employed to balance these effects. Several diluents were evaluated, including 0.5 mol L−1 nitric acid, 20% (v/v) methanol in distilled water, 20% (v/v) 1-propanol in distilled water, 50% (v/v) 1-propanol in 0.5 mol L−1 nitric acid, and 50% (v/v) 1-propanol in distilled water. As indicated in Fig. 4(C), the 50% (v/v) 1-propanol in distilled water delivered the best performance and was selected as the optimal diluent for the system.
To investigate the flow rate of rinsing solvent from the loop, the rinsing solvent (50% (v/v) 1-propanol in distilled water) was circulated through the loop containing the sample using the peristaltic pump at different flow rates (viewing height = 6 mm, nebulizer pressure = 160 kPa). The emission intensity of Al was measured after three injections at each flow rate. As shown in Fig. 4(D), a flow rate of 12 rpm was identified as optimal. To investigate the effect of rinsing solvent and loop volume, loops with volumes of 100 and 160 µL were used. The volume of rinsing solvent was varied from 70 to 220 µL (70–130 µL for the 100 µL loop and 150–220 µL for the 160 µL-loop). The most stable condition was observed when the rinsing solvent completely filled the loop. Based on these results, the 160 µL loop was selected, and 150 µL of rinsing solvent was added to the surfactant-rich phase (resulting in a final volume after mixing with surfactant-rich phase in the range of 165–175 µL). The optimized ICP-AES instrumental parameters are summarized in Table 1.
| RF generator power (kW) | 1.65 | Viewing height (mm) | 6 |
| Frequency of RF generator (MHz) | 40 | Pump rate (rpm) | 12 |
| Plasma gas flow rate (L min−1) | 15.0 | Al wavelength (nm) | 396.162 |
| Auxiliary gas flow rate (L min−1) | 1.5 | Loop volume (µl) | 160 |
| Nebulizer pressure (kPa) | 160 | Rinsing solvent | 50% v/v of 1-propanol |
Analysis of variance (ANOVA) was utilized to analyse the results and assess the contribution of each experimental parameter.53 Key statistical metrics, including the F-ratio, sum of squares (SS), percent contribution (PC%), and purified sum of squares (SS′) for both error and experimental factors, were calculated and are presented in Table 2.
| Factor | DFa | SSb | MSc | F-ratiod | SS′e | PCf (%) |
|---|---|---|---|---|---|---|
| a DF: degree of freedom; DF for each parameter = number of levels of each parameter − 1; DF for total results = number of total results − 1; DF for error = DF for total results – ∑ DF for each parameter.b SS: sum of squares.c MS: mean squares.d F-ratio: F(4,29), critical value is 2.70 (P < 0.05).e SS′: purified sum of squares.f PC (%): percentage contribution. | ||||||
| pH | 4 | 784 150 115 |
196 125 28.8 |
6.08 | 655 386 236 |
4.47 |
| Surfactant | 4 | 123 495 7213 |
308 739 303 |
9.56 | 1 105 842 299 |
7.99 |
| Ionic strength | 4 | 4 509 692 |
11 274 229 |
0.35 | −84 017 999 |
0.61 |
| Temperature | 4 | 45 618 069.89 |
114 045 175 |
3.53 | 327 065 785 |
2.36 |
| L/M | 4 | 1 038 079 580 |
2 595 198 949 |
80.40 | 1 025 168 088 |
74.09 |
| Error | 29 | 9 360 831 261 |
3 227 872.9 |
158 165 770 |
11.43 | |
| Total | 49 | 1 383 761 490 |
||||
The sum of squares of error (SS error) was calculated by subtracting the sum of squares of the factors from the total sum of squares. Based on the ANOVA results, the ligand-to-metal molar ratio (L/M; PC% = 74.09%) was identified as the most significant factor affecting the extraction of Al3+, followed by surfactant concentration % (PC% = 7.99%), solution pH (PC% = 4.74%), solution temperature (PC% = 2.36%), and ionic strength (PC% = 0.61%). For each factor, the Fisher ratio (F), was determined by dividing the variance of the factor by the variance of the error. The critical F-value (Fcritical(4,29)) was 2.70 at a significance level of P = 0.05. Comparing the calculated F-values in Table S1 with Fcritical, indicated that pH (F = 6.08), surfactant concentration (F = 9.56), temperature (F = 3.53) and L/M molar ratio (F = 80.40) significantly influenced the extraction process as their F-values exceeded the critical value (F-values > Fcritical).
In the extraction of metal ions by CPE method, a hydrophobic complex is first formed and then extracted into a reduced volume of micelles to achieve preconcentration. The efficiency of this extraction process depends on the pH at which complex formation occurs. In this research, the effect of solution pH on complex formation was evaluated in the pH range of 4.0 to 7.0 using a sodium acetate solution, along with NaOH or HNO3. As shown in Fig. 6, the emission intensity reached its maximum at pH 4.5. Therefore, pH 4.5 was selected for the following extraction steps.
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| Fig. 6 Effect of experimental factors investigated by Taguchi method (the levels of each factor were added to the top of the column). | ||
The salt effect was investigated by adding sodium acetate to the solution, in the concentrations ranging from 0.05 to 0.75 mol L−1. Similar extraction results were achieved with sodium acetate concentrations of 0.25 to 0.5 mol L−1. Consequently, 0.25 mol L−1 was chosen as the optimum value for further experiments (Fig. 6).
Triton X-114 was selected because of its commercial availability in a highly purified and homogeneous form, low toxicity, and cost-effectiveness, low cloud point temperature and dense micelle-rich phase, making it a suitable surfactant for CPE.
The effect of surfactant concentration on the extraction efficiency was examined within the Triton X-114 concentration range of 0.05 to 0.4% w/v. As observed in Fig. 6, quantitative extraction was achieved at 0.1% w/v. Lower surfactant concentrations led to reduced extraction efficiency, likely due to insufficient aggregate formation to effectively capture the formed complex. Conversely, at concentrations above 0.1% w/v, a decrease in emission intensity was observed, which can be attributed to the increased volume of the micelle-rich phase. Therefore, 0.1% w/v Triton X-114 was selected as the optimal concentration to ensure high extraction efficiency and effective enrichment factor.
The stoichiometric ratio of Al
:
morin complexes is influenced by factors such as the solvent and solution pH. Specifically, at pH 4.5, a 1
:
1 stoichiometric complex (AlM) is formed. The relationship between emission intensity and reagent concentration was studied by altering the molar ratio of morin to Al from 2 to 40. The findings indicated that a morin to Al molar ratio of 40 yielded the highest extraction efficiency. Consequently, this ratio was chosen as the optimal ligand-to-metal (L/M) ratio. Fig. 6 illustrates the variation of extraction efficiency with different L/M molar ratio.
Employing the lowest possible equilibration temperature is desirable to balance effective complexation with efficient phase separation. With increasing equilibration temperatures, the phase volume of non-ionic surfactants typically diminishes. Consequently, optimal analyte preconcentration during CPE is achieved at temperatures significantly above the surfactant's cloud point temperature (CPT).
The phase separation temperature is influenced by surfactant concentration and can be modified by the addition of other substances such as salts, ligand, etc. It was determined that 60 °C is adequate for complex extraction, and thus was selected for further experiments. Fig. 6 displays how extraction efficiency varies with equilibration temperature.
Based on the results of repetitive extraction experiments following the OA25 design, the optimum conditions of off-line CPE variables were pH 4.5, a L/M molar ratio of 40, 0.1% (w/v) Triton X-114, 0.25 mol L−1 salt concentration, and an equilibrium temperature of 60 °C. To investigate the precision of the proposed off-line CPE/FI-ICP-AES method for Al3+ analysis, five replicate extractions were performed on 10 mL solutions containing 100 µg L−1 Al3+ under optimum conditions. The empirical mean emission intensity after five repetitive extractions was 14
524.4 ± 853.74 (standard deviation), which agrees well with the Taguchi method-predicted value of 14
334.41 ± 1161.99.
| Ion | Concentration (mg L−1) | Cx/CAl | Recovery (%) |
|---|---|---|---|
| a Highly interferent. | |||
| Na+, K+ | 200 | 2000 | 116.8 |
| 150 | 1500 | 100.6 | |
| Alkaline | 200 | 200 | 131.3 |
| Earth metal metals | 150 | 1500 | 113.4 |
| 100 | 1000 | 97.24 | |
| Ni2+ | 100 | 1000 | 101.2 |
| Mg2+ | 100 | 1000 | 120.2 |
| 50 | 500 | 93.9 | |
| Pb2+ | 100 | 1000 | 103.4 |
| Zn2+ | 100 | 1000 | 98.9 |
| Co2+ | 100 | 1000 | 97.2 |
| F− | 5 | 50 | 56.6 |
| 0.5 | 5 | 98.9 | |
| Cd2+ | 50 | 500 | 100.8 |
| Fe3+ | 5 | 50 | HIa |
| 5 | 50 (0.01 mol L−1 SCN−) | HI | |
| 0.5 | 5 (0.02 mol L−1 SCN−) | 91.6 | |
| Hg2+ | 5 | 50 | 81.4 |
| 0.5 | 5 | 85.8 | |
| 50 (0.01 mol L−1 KI) | 50 | 101.8 | |
| Cu2+ | 10 | 100 | Highly interferent |
| 5 | 50 | 65.4 | |
| 5 (0.02 mol L−1 SCN−) | 50 | 76.1 | |
| 5 (0.01 mol L−1 ascorbic + 0.01 mol L−1) KI) acid + 0.01 M KI) | 50 | 97.9 | |
The outcomes demonstrated that Na+ and K+ ions (at 150 mg L−1), alkaline earth ions, Ni2+, Pb2+, Zn2+ and Co2+ ions (at 100 mg L−1), as well as Mn2+ ions (at 50 mg L−1), showed no interference effect on Al analysis by the proposed method. However, certain ions, including Fe3+, Cu2+, Hg2+, and F− caused interference in the CPE of Al3+ under the specified conditions. Further experiments revealed that Fe3+ ions at a concentration of 5 mg L−1 produced severe interfering effect on the Al analysis. By reducing Fe3+ concentration to 0.5 mg L−1 and addition of 0.02 mol per L thiocyanate (SCN−) to the sample, this interference is resolved. This effect is likely due to the possible reaction of Fe3+ and SCN− ions forming Fe(SCN)x3−x. Interference from Cu2+ at 5 mg L−1 (50 times the Al3+ concentration) was completely eliminated by the addition of 0.01 mol per L ascorbic acid and KI. Ascorbic acid reduced Cu2+ to Cu+, which then reacts with I− to form CuI2− complex, thus resolving Cu2+ interference. Similarly, Hg2+ interference was completely removed by adding 0.01 mol per L KI, resulting in the formation of HgI2. In solution, F− ions react with Al3+ to form a soluble AlF63− complex, which reduces the amount of free Al3+ available for complexation with morin. Reducing F− concentration to 0.5 mg L−1, eliminated interference, and this concentration is logical for tap and surface water samples that usually have F− levels below this value. F− concentrations in standard drinking and bottled waters usually do not exceed this value. For matrices with inherently higher fluoride content, such as seawater or certain ground waters, the routine dilution performed prior to ICP-AES measurement sufficiently lowers the fluoride concentration to eliminate interference, thereby guaranteeing reliable aluminum quantification in diverse aqueous environments.
A summary of these results is provided in Table 3.
| Analytical technique | LOD (µg L−1) | RSD (%) | LDR (µg L−1) | Ref. |
|---|---|---|---|---|
| a Ultrasound assisted dispersive liquid–liquid microextraction-flow injection.b Flame atomic absorption spectroscopy.c Flow-batch sequential injection system. | ||||
| CDots-FIA-fluorescent sensors | 7.0 | <13 | 40–3000 | 10 |
| Spectrophotometry | 0.01 | — | 0.01–800 | 54 |
| CDs@ZIF-90-fluorescent sensors | 21.87 | — | 27–5400 | 33 |
| Fluorimetry | 1.3 | 0.8 | 50–200 | 55 |
| UA-DLLME-FI-fluorimetrya | 1.7 | 0.95 | 11–180 | 56 |
| Spectrofluorimetry | 2.7 | < 5 | 2.7–300 | 57 |
| SPE-FAASb | 6.8 | 0.4–1.9 | 23–5000 | 58 |
| Fluorimetry | 68 | — | 1000–8000 | 59 |
| Reflectance spectroscopy | 3000 | <5.0 | 10 000–125000 |
60 |
| FI-BSI-spectrophotometryc | 2 | 0.8–1.3 | 7.5–625 | 61 |
| Stripping voltammetry | 2.3 | 1.9 | 2.3–6.3 | 62 |
| DSFME-spectrophotometry | 0.09 | 2–4 | 0.28–500 | 63 |
| Off-line CPE/FIA-ICP-AES | 0.89 | 3.1 | 1.0–500 | This study |
| Sample | Mineral water | Tap water | Sea water |
|---|---|---|---|
| Determined (µg L−1) | 3.4 ± 0.6 | 9.6 ± 1.6 | 9.5 ± 0.5 |
| Spiked (µg L−1) | 10 | 10 | 10 |
| Found (µg L−1) | 12.7 ± 1.4 | 20.4 ± 0.9 | 18.5 ± 1.1 |
| Relative recovery | 94.8 | 104.1 | 94.9 |
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