Standard preparation of Cd2+ at different concentrations for the standard line
Atomic absorption spectrometry (AAS 7000) was used to detect the presence and concentration of cadmium in the experiment. The standard line should be obtained, the benchmark wherein all other adsorptions fall within that armpit. If para-ventures exist, any range of values falls outside that preset value and cannot be detected by the AAS. The Cd2+ standard solution was prepared at different concentrations from 0 mg/L to 5 m/L.
Standard concentration preparation of cadmium for the standard calibration curve/line
Standard calibration curves should be utilized to determine the analyte concentration in the given samples before detection, especially when using AAS/UVS, since this approach provides a more accurate sense of detection. Standard calibration curves are frequently used in analytical chemistry for quantitative and qualitative analysis. The standard curve in this study was obtained in the following manner:
- Cadmium standard storage solution: 0.5000 g of metal cadmium powder (spectral pure) was weighed and dissolved in 25 mL (1+5) HNO3 (slightly thermally dissolved). The solution was cooled, transferred to a 500 mL volumetric flask, diluted with distilled deionized water, and fixed. This solution contained 1000 mg of cadmium per litre (this solution was the finished product we bought).
- For the cadmium standard, 10.0 ml of cadmium standard storage liquid was added to a 100 mL volumetric flask, diluted with water to the marking line, shaken well, and set aside. This solution contained 100 mg of cadmium per litre.
- The 5.0 mL diluted standard solution was drained into another 100 mL volumetric flask and diluted to the marked line to obtain a standard solution containing 5 mg of cadmium per litre.
In such studies, five (5) standard concentrations of cadmium were usually prepared from 0, 1, 2, 3, 4, and 5 mg/L, but 0 mg/L was used as a buffer solution or distilled water only.
The Standard Line of the Adsorption Isotherm
The sorption kinetics should always be standardized in agreement with the sorption data of the Langmuir (R2 = 0.093-0.98) and Freundlich (R2 = 0.90- 0.99) isotherms (Ahmad, Munir et al., 2018) for the calibration curve. The fig. 3 graph confirms that the analogy holds for the Langmuir and Freundlich isotherms.
An adsorption isotherm is an adherence phenomenon wherein an adsorbent at a particular given mass of solute can adsorb the adsorbate at a defined equilibrium concentration at a contestant temperature. The mathematical expression is expressed as follows:
qe is the equilibrium adsorption capacity (mg/g-1) and is the amount of metal absorbed per specific amount of adsorbent, according to these authors 23. This research investigated the adsorption of cadmium pollutants by nZVI composites doped with hydrochar.
Selection of the Best Material for the Adsorption Capacity of Cadmium
However, some researchers may argue that this stage involves trial and error. However, this approach is very intuitive and provides a wealth of information regarding the research design. Proper material selection is one of the most essential aspects of any analytical and laboratory research. This approach is crucial for coherence, systematic data collection, and qualitative analysis.
A series of tests were conducted at various ratios and concentrations to determine the best material with the best sorption capacity and removal efficiency. After examining all the findings from many trials, the best material ratio was 1:4, which was the ratio of nZVI to hydrochar. This ratio was adopted for all the preceding experiments.
Fig. 1. graph clearly shows that the 4:1 ratio was the best ratio with a high adsorption capacity compared to the other ratios (4:1 or 1:4).
Preparation of the composites (nZVI/hydrochar)
After the preparation of hydrochar as described in the section above, the required ratio of the powdered hydrochar was synthesized together with the green tea in the correct proportion per the design of the experiment. These nZVI composites, as they are often called, were used in all the experiments for both adsorption and all the other characterizations. As explained above, when the nZVI/hydrochar composite was synthesized at a ratio of 1:4, the material was also converted to 4:1, as shown in the graph below. This ratio was calculated for every 1.1 g of nZVI, and the hydrochar yield was 0.275 g (1.1/4). The mass ratio of nZVI was calculated from the molecular weight of Fe2(SO4)3. XH2O. Approximately 1/3 of the biosorbent (hydrochar) was doped with nZVI in this study because of its maximum adsorption capacity and removal efficiency. One can deduce from this mathematical analysis that the hydrochar biosorbent is an efficient material for the environmental remediation of contaminated water and soil.
The quantity of the nZVI/hydrochar composite (concentration: 500 mg/L) for the adsorption capacity experiment.
The mass (0,025 g) of the nZVI/Hyrochar composites was used for all the preceding adsorption experiments.
Characterization of Materials
The main goal of the material matrix is to provide a thorough and valuable overview of the techniques used to classify and characterize a wide range of materials, inherently by emphasizing each technique's theoretical components, an in-depth analysis of how each grain of material is arranged in its morphological outlooks 18,24,25as been performed. Material characteristics are the inherent nature of scientific materials being ascribed for research purposes. The behaviour of materials is dynamic, especially when subjected to mechanical or chemical stress. However, the innate properties of these laboratory materials are crucial for experimental purposes. The technical concept behind this elusory of material phenomenon is to reduce the failure time and keep equipment close to its design life span. The scanning rate was 10° for every minute, and the scanning angle ranged from 10° to 80°. The amorphous crystalline peak of both hydrochar and the magnetic nanoparticle composites was distorted. XRD can further reveal the chemical composition of known or unknown chemical constituents 24. In such analytical studies, material composition plays a crucial role in determining the inherent traits of each studied sample.
SEM of Nanozero-Valent Iron Hydrochar
There is always a deep sense of analytical explanation of the structure of nanoscale zero-valent iron (nZVI) and how its particles evolve during the reaction. To understand how the removal process occurs, further investigations of the morphological orientation under different characteristic conditions are needed. SEM is a significant method for adequately investigating nZVI materials' dynamics. The scanning showed good electrical conductivity based on the images shown in Fig. 2.
Two different samples were photographed—the hydrochar and nZVI/hydrochar composites—using scanning electron microscopy (SEM). The hydrochar in Fig. 2(b) differs slightly from the starting material in Fig. 2(a). The clicking doom shape of the hydrochar indicated the type of process it underwent during hydrolysis and dehydration. After further grinding the probes in the figures for the composite, the hydrochar protruded deeper into the nZVI matrix, almost overshadowing the nZVI. The nanoparticles of the nZVI/hydrochar composites and hydrochar were studied under these conditions. The orientation of these samples clearly showed the crystal growth texture on the surface of these particles. Both of the particle images have platy dendrite structures. The dispersion further exhibited nanosized particles within 1 to 10 nm in diameter. According to some of the related literature. This result in Fig. 2. indicated that the average size of any nanosized particle ranges typically from 1 to 30 nm in diameter. Interestingly, the dendrite structures fade away as the SEM image size increases or the particle size increases. It is always good for the photographic image to be in a particular range for good imagery. The scanning results showed the dendritic texture of the nZVI composite. The pigmentation within the lattice structure further confirmed the magnetic nZVI composite indicated by nanozero-valent iron materials 26,27.
Transmission electron microscopy (TEM)
The crystallographic orientation of the grains was determined, as was the arrangement of the atomic planes in the polycrystalline sample 28. The nZVI particles had diameters ranging from 10–200 nm without the need for additional reducing agents based on the particular experiment at 25°C. In general, nZVI offers a suitable approach for improving the stability and reactivity of renewable resources, especially carbon materials, under the umbrella of hydrochar. The scanning analysis shows that nZVI aggregates and moves toward the targeted area during nanoremediation. The nanoparticles can agglomerate due to their metallic ability and emulsify contaminants into harmless substances. This is one of the reasons nanotechnology is used in groundwater remediation due to its unique characteristics.
Fourier Transform Infrared Spectroscopy (FTIR) Analysis of nZVI and Hydrochar
Fourier transform infrared spectroscopy (FTIR) is a sampling technique used to observe materials in their solid or liquid state 29–32. Owing to the nature of the experiments, this research was limited to the observation of both hydrochar and nZVI composites in their solid-state about their adsorbent nanoparticles. Here, the principal goal of this experiment was to determine how the raw nZVI and hydrochar data are converted into spectral data when the source of light is focused on the principal angle of the observed solid materials (hydrochar and nZVI composite). The nature of the absorbance can be deduced by the wavelength of the light applied to the observed material. The vertical axis is the transmittance (T) as a percentage (%), and the horizontal axis is the wavenumber in cm-1. The spectrum was described within the periphery of the boundary conditions.
FTIR typically has several points on the graph (sharp peaks) for characterising the adsorption band. However, before chemical analysis, the FTIR results of the nanoparticle composites. They are both nZVI/hydrochar composites, but their FTIR results might differ before and after adsorption, allowing us to determine the meteorological orientation of their particle sizes and bandwidths in wide spectral bands. Both experiments were performed under different conditions to assess the reliability and sorption capacity of the nZVI/hydrochar for pollutant removal. Fourier transform infrared spectroscopy was carried out to identify the functional groups in the adsorbents range of 500-4000 cm-1. The shape of the particles plays a vital role in determining the position of this band. It was discovered that particle size explicitly influences the width and intensity of peaks in the infrared (IR) spectrum. The width of the peak narrows, and the intensity increases as the particle size increases. According to the figure above, the bandwidth corresponding to the wavenumber 3270 cm-1 corresponds to the OH functional group, which participates in chemical bonding.
Zeta potential and particle size analysis
The zeta potential (ZP) helps to understand and control colloidal suspensions. Therefore, nanoparticles (ZPs) were tested using a zeta-steel meter (Malvern nano ZS90). Five milligrams of each nanomaterial was added to a 50 ml beaker containing 10 ml of distilled water containing 0.01 mM NaCl as a background solution to make a 500 mg/L Hydrochar-nZVI suspension. Because of the instability of the nZVI particles, the mixture was first sonicated, after which the pH was adjusted with HCl or NaOH to obtain the desired pH. The suspension mixture was vortexed for 10 min, after which the particles were allowed to settle before being injected into a zeta potential sample holder for testing. (ZP) was measured at pH values of 5.5, 6, and 7, and a ζ potential scatter diagram was finally generated to determine the isoelectric point and point of zero charge for the synthesized nanoparticles. Regardless of the technique used to create them, all nZVIs naturally possess the ZP. Every possible method generates nZVI with a unique ZP. How nanoparticles attract to one another and aggregate in the process depends on their (ZP) or electric potential. According to the output of the zeta sizer, particles are considered stable if their potential is more remarkable than +29.3 mV and less than -29.3 mV. The maximum instability and aggregation occur at zero as shown in Fig. 3(a), (b), (c).
Particle Size Distribution of nZVI
The same experiments, which were investigated for zeta potentials under different experimental conditions, further analyzed the zeta potentials to determine the size distribution of the particles in combination with nZVI in solution.
The same quantitative evaluation and analysis performed to determine the ZP concentration, intensity, and size using a zetazizer were also carried out for hydrochar alone with different concentrations of a background solution of NaCl: 1 mM, 5 mM, and 10 mM. The reason is that the particle sizes are significant when these particles are agglomerated in an aqueous solution, which indicates the effectiveness of their sorption capacity and removal efficiency in water remediation. Therefore, studying material kinetics in such experiments is highly important to ensure reliability and accuracy. Another reason that we wanted to be sure of compatibility is that both materials of the nZVI composite would have the same potential and dynamics shown in Fig.4 (33–35.
Adsorption capacity at different concentrations but with a single pH of 6.0
Fig. 5 was the adsorption of cadmium by rice husk with the nZVI composite at different concentrations was carried out with the required adsorbate and an optimum pH of 6.0 at temperatures between 25 and 30°C, and a batch experiment was carried out. The adsorbate was the CdCl2 pollutant at different concentrations ranging from 5 mg/L to 200 mg/L. The cadmium concentrations in the aqueous solution before adsorption and after equilibrium were determined by an AAS 7000 instrument at a constant pH of 6.0. As explained in the previous sections, the adsorption isotherm depicts an equilibrium concentration curve of a solute on the surface of the adsorbent, which is designated qe, relative to the solute concentration in the liquid, which is also designated Ce.
The lower the concentration of the pollutant, which is the metal of ion (Cd2+), in this study, the greater the percentage remover efficiency was. There was a direct inverse reciprocal relationship between the absorption isotherm and the removal efficiency of heavy metals. In this study, hydrochar doped with the nZVI composite was shown to have high removal efficiency, with a percentage (%) of 97.56% shown in Fig.5.
Table 1 Adsorption and Removal Capacity of Cadmium on nZVI/Hydrochar with mass (0,025g) of nZVI/Hyrochar composites
No.
|
Initial conc. (mg/L)
|
Equilibrium Conc:(mg/L)
|
Removal Capacity(mg/g)
|
1
2
3
4
5
6
7
|
7.553
17.509
23.598
96.65
96.65
157.32
232.09
|
0.18
5.85
11.24
20.66
81.49
139.43
211.15
|
14.7374
23.32
24.721
29.34
31.11
35.79
41.88
|
In the analysis of Table 1, there was a sense in which an increase in adsorption capacity decreased removal efficiency. When the concentration of the pollutant is high, it is the inverse proportionality of the removal efficiency. In this study, the lower the concentration of the pollutant, the metal ion (Cd2+), the higher the percentage remover efficiency; there is a direct inverse reciprocal relationship between absorption isotherm and removal efficiency of heavy metals. In this study, it was investigated that hydrochar that was doped with nZVI composites has a high-efficiency removal rate of 97.56%.
Adsorption capacity of single concentrations with variable pH values
pH is an important controlling factor for the operation of control experiments, and pH is an indicator of temperature; thus, it is crucial to determine whether a system usually works. This approach helps to stabilize the working solution or analyte, especially in control experiments. The pH was determined by a pH meter (METTLER TOLEDO, China) in all the experiments carried out in this study. The pH was adjusted according to the required value by adding concentrated/diluted NaOH solution and HCl for alkalinity or acidity.
Fig. 6(a) and (b) showed the effect of the system on pH control and removal, which was investigated using a pH meter. In anoxic solution, nitrogen flow was introduced into the aqueous solution. NaOH and HCl were used for pH adjustment to eliminate and control other ionic disturbances in the solution. The results of the analysis of the different pH values ranging from 4.0 to 5.0 to 6.0, 7.0, and 8.0 were investigated with a single pollutant concentration of 400 mg/L CdCl2, and the results were obtained from complete detection with AAS after 3 hours of adsorption. These findings revealed that the equilibrium kinetic sorption capacity increased with increasing pH and that the percentage removal efficiency increased with decreasing pH; that is, there was an inverse proportionality. Increasing the pH from 6.0 to 8.0 ideally evoked a substantial increase in the adsorption capacity of the isotherm of the adsorbate in an aqueous solution of the CdCl2 adsorbent. Subsequently, from pH 4.0 to 5.0, the adsorption capacity decreases gradually but with a high removal efficiency, according to the literature 36. This qualitative anomalous behaviour of pH values on the quantity of cadmium that was adsorbed was previously studied and described in the literature by 37–39
Table 2 Removal capacity of cadmium using nZVI/Hydrochar in 10 mM NaCl solution at different pHs
No.
|
pH
|
Equilibrium Conc. Of Cd (mg/L)
|
Removal Capacity of Material (mg/g)
|
1.
|
4.0
|
162.078
|
3.2
|
2.
|
5.0
|
158.498
|
7.21
|
3.
|
6.0
|
160.685
|
13.72
|
4.
|
7.0
|
150.279
|
23.64
|
5.
|
8.0
|
122.793
|
78.62
|
Table 2 Illustrates the effect of the system on pH control, and removal was investigated using a pH meter. In anoxic solution, the Nitrogen flow was introduced into aqueous solution. NaOH and HCl were used to adjust pH to eliminate and control other ion disturbances in the solution. The analysis on the conducted study of different pH ranges from 4.0, 5.0, 6.0, 7.0 and 8.0 was investigated with a single pollutant concentration of 400 mg/L CdCl2, and results were obtained from the detection with AAS after adsorption of 3 hours. From those findings, it was observed that the equilibrium kinetics adsorption capacity increases with an increase in pH, and the percentage removal efficiency increases with decreases in pH; that is to say, there is inverse proportionality.
Sedimentation Kinetics of Composite nZVI
The sedimentation experiment was also carried out, as explained in the methodology section. Sedimentation is a phenomenon in which magnetic nanoparticles are characterized using dynamic scattering UV‒vis spectroscopy. Nanoparticles are redox-active constituents with smaller particles but larger surface areas. The sedimentation experiments showed that the nanoparticles cluster and aggregate to form sediment. It was observed that over time lapses or an interval of time, one could see that the rate of aggregation and sedimentation was dependent on the particle size, concentration aqueous condition, and the ionic strength of settlement. The analysis further revealed that nanoparticle aggregation and sedimentation predict the transportation and fate of particles in media for remediation. The dynamic light scattering in the suspended solution with various concentrations of nanoparticles (Co = 1.8685 g/L) further revealed that the aggregate particles were concentrated with the formation of a gel structure due to the strong magnetic attraction between ferromagnetic nanoparticles, which further reflects sedimentation kinetics 40.
The iron concentration in the aqueous solution drastically decreased with time. This phenomenon agrees with hygienic environmental norms for domestic or municipal water. Instead of these findings, the iron concentration should be kept at 0.4 mg/L. With three different concentrations of the electrolyte background solution of NaCl (1, 5, and 10 mM), the iron concentration was reduced from the investigated result to the environmental standard concerning time. Fig.8. shows the trend of the iron concentration. These sedimentation kinetics further confirmed that nano zero-valent iron doped with hydrochar is effective for water cleaning 41
Nanotechnology
This research focuses on using Nanoscale zero-valent iron (nZVI) composite materials for wastewater remediation, particularly in eliminating persistent/recalcitrant pollutants in surface water and groundwater. nZVI particles, typically sized between 5-40nm, have shown effectiveness in reducing organic and inorganic impurities. The study highlights nZVI's practical applicability, including its emulsification of a wide range of contaminants, colloidal properties, long durability, high efficiency in iron utilization, and various contaminant removal modes. The research emphasizes nZVI's recognition as a highly effective adsorbent and ideal technology for in-situ remediation of heavy metals in contaminated groundwater or wastewater. Batch experiments were conducted to characterize the nZVI surface and assess its effectiveness in removing cadmium ions from water. The study explored the impact of solution properties such as pH, initial cadmium concentration, sorbent dosage, ionic strength, and competitive ions on cadmium removal by nZVI. The results indicated that nZVI effectively removed Cd (2+) ions through adsorption, decreasing removal in the presence of competitive cations. The research demonstrated that Cd (2+) removal increased with higher solution pH, reaching a maximum at pH 8.0, and identified chemisorption or physisorption processes as potential mechanisms for Cd (2+) adsorption on nZVI. The study underscores nZVI as an effective remediation process for various organic and inorganic pollutants in contaminated water sources. It suggests that the unique properties of iron nanoparticles contribute to their effectiveness in removing recalcitrant contaminants, making nZVI a significant player in 21st-century environmental remediation efforts. In specific literature reviews, the synthesis methods of interest are often denoted as "top-down" and "bottom-up."
The latter explicitly encompasses laboratory and commercial micrometre to millimetre-sized nano zero-valent iron (nZVI) production. This study focuses primarily on the bottom-up approach, explicitly addressing the antithesis of Fe2(SO4), which effectively reduces Fe2 in the liquid phase 42. The significance of nZVI in removing recalcitrant organic and inorganic contaminants cannot be overstated. Their unique properties, validated through characterization techniques such as X-RD, FTIR, TEM, SEM, etc. underscore their advantages over other technologies. In light of these considerations, this research contributes to the attainment of global standards established by organizations such as the World Health Organization (WHO), Environmental Protection Agency (EPA), and the European Drinking Water Directive. Notably, these standards stipulate that the cadmium content in municipal water should not exceed 0.005 mg/L, both in the water supply and wastewater effluence. This investigation seeks to identify viable approaches to align with and uphold these stringent regulatory benchmarks 13 .