To develop a commercial bentonite-based product for animal feed aimed at mitigating mycotoxin contamination, the adsorption properties of the raw bentonite sample and its sieved fractions (<0.200 mm, <0.037 mm, and <5 mm) were evaluated. Particular attention was given to the finest fraction (<0.005 mm), since the theoretical particle size range responsible for the highest adsorption capacity of bentonite is typically below 0.005 mm, more precisely 0.002–0.003 mm, where the majority of smectite platelets are concentrated. The characterization included granulometric analysis, chemical composition, heavy metal content, mineralogical composition by X-ray diffraction (XRD), and methylene blue adsorption capacity. The results for the RB and the sieved fractions (IB, 37B and 5B) are presented and compared to assess the impact of particle size reduction on the material’s properties and potential for aflatoxin adsorption, while simultaneously seeking the optimal balance between bentonite quality (adsorption performance) and production cost, as the isolation of particles in the 0.002–0.003 mm range significantly increases processing expenses and, consequently, the final product price.
3.1. Granulometric Analysis
To remove chert from the raw bentonite fraction (RB) and obtain the purified bentonite fraction (IB), the sample was subjected to wet sieving through a 0.200 mm mesh sieve. Particle size distribution analysis revealed that 97% of the particles were smaller than 0.063 mm, while approximately 90% were below 0.0037 mm. Subsequently, sieving at 0.0037 mm was performed, and finally, the <0.005 mm class was separated by centrifugation. The granulometric composition of the IB sample and its sieved fractions B37 and B5 was determined using wet laser diffraction, with the results presented in
Figure 2.
The results showed that for the B37 sample, 100% of the particles were below 0.037 mm, while for the B5 sample, 80% of the particles were below 0.005 mm. Considering that 0.005 mm particles are extremely fine, it is assumed that agglomeration of particles occurred during sieving, drying, and sample preparation for measurement.
These results indicate that sieving, as a cost-effective and simple method, effectively concentrates fine particles, with the <0.037 mm fraction achieving a satisfactory particle size distribution. The even finer particle size distribution in the <0.005 mm fraction is expected to increase the specific surface area, thereby enhancing the adsorption capacity for aflatoxins, since finer particles provide a greater number of accessible adsorption sites.
Figure 2.
Granulometric composition of the IB, 37B and 5B samples using laser diffraction method.
Figure 2.
Granulometric composition of the IB, 37B and 5B samples using laser diffraction method.
The similarity in values between the <0.200 mm and <0.037 mm fractions suggests that the majority of montmorillonite is already concentrated in the finer size range of the initial sample, with incremental benefits from further sieving. Vekiru et.al (2015) [
7] demonstrated that finer particle sizes enhance the surface area available for mycotoxin adsorption, supporting the potential of the <0.037 and <0.005 mm fraction for improved aflatoxin binding.
3.2. Chemical Composition
The chemical composition of the raw, initial and sieved fractions was analyzed to determine the Al₂O₃ content, a key indicator of montmorillonite ((Na,Ca)₀.₃(Al,Mg)₂Si₄O₁₀(OH)₂·nH₂O) concentration, and heavy metal content to assess safety for animal feed applications. The mineralogical analysis, detailed in
Section 3.3, indicates the presence of accessory minerals devoid of aluminum (Al). Consequently, the total Al content in the sample is attributed exclusively to bentonite (montmorillonite). This attribution enables the quantification of bentonite content within the sample. The results are presented in
Table 1 (chemical composition) and
Table 2 (heavy metals).
The Al₂O₃ content, which serves as an indicator of montmorillonite purity, increased progressively with each purification step. In the raw bentonite sample (RB), the Al₂O₃ content was 10.52%, rising to 12.97% in the initial purified fraction (IB) after removal of chert through wet sieving. Further sieving to obtain the <0.037 mm fraction (B37) resulted in an Al₂O₃ content of 13.76%, while the finest <0.005 mm fraction (B5) exhibited the highest value of 16.69%.
Considering the theoretical Al₂O₃ content in pure montmorillonite of 18.57% [
16], these values reflect a substantial enrichment in montmorillonite. Removal of chert from the raw sample increased the montmorillonite content by more than 13%. Subsequent sieving below 0.037 mm provided an additional increase of approximately 4%, yielding a total enrichment of about 17% relative to the raw material. The finest fraction (B5) showed the most pronounced improvement, with over 33% higher montmorillonite content compared to the raw sample.
This progressive enrichment is particularly significant in the context of regulatory requirements for the use of bentonite as a feed additive. According to the relevant European directive, bentonite products intended for this application must contain at least 70% montmorillonite. Both the B37 and B5 fractions clearly meet this threshold, while the IB fraction is close to compliance. These results demonstrate that simple, cost-effective physical separation techniques, such as wet sieving and centrifugation, can effectively upgrade lower-grade bentonite to meet stringent quality standards for aflatoxin-binding applications in animal nutrition.
Given the intended use of bentonite as an additive in animal feed to mitigate mycotoxin contamination, the analysis of heavy metal content is critical to ensure the material’s safety, as certain heavy metals can be toxic to livestock even at low concentrations. The list of the detected heavy metals in IB, 37B and 5B is given in
Table 2.
Table 2.
The content of heavy metals in raw and samples IB, 37B, and 5B.
Table 2.
The content of heavy metals in raw and samples IB, 37B, and 5B.
| Komp. |
Pb |
As |
Hg |
| |
ppm |
| IB |
65 |
0.95 |
2.3 |
| 37B |
<5 |
<0.01 |
<0.01 |
| 5B |
<5 |
<0.01 |
<0.01 |
The heavy metal content was significantly reduced in the sieved fractions: lead (Pb) was below 5 ppm, and arsenic (As) and mercury (Hg) were below 0.01 ppm in both the <0.037 mm and <0.005 mm fractions, compared to higher (but still low) levels in the initial sample. The reduction in heavy metal content in the sieved fractions enhances their suitability for animal feed, as low contaminant levels minimize health risks. Carraro et al. (2014) [
17] reported that finer bentonite fractions often exhibit lower heavy metal contents due to the removal of coarser impurity phases, supporting the safety of the sieved fractions for feed applications.
3.3. Mineralogical Composition
The mineralogical composition of the RB and its sieved fractions was determined using X-ray powder diffraction (XRD), with diffractograms presented in
Figure 3. The results are summarized in
Table 3.
The RB sample is highly heterogeneous in the raw state, containing only 54.9 wt.% smectite, with quartz (32.2 wt.%) and cristobalite (11.4 wt.%) being the dominant accessory minerals and calcite present in minor amounts (1.5 wt.%). Plagioclases and dolomite are present in trace amount. Such a composition is typical of many volcanogenic Ca/Mg-bentonites in the Balkan region, where alteration of pyroclastic material occurred in a marine or lacustrine environment, preserving significant portions of primary silica phases (cristobalite and quartz) [
18,
19,
20].
Particle-size fractionation proved to be a highly effective purification method. Simple dry sieving to <0.200 mm (sample IB) increased the smectite content to 72.3 wt.%, reducing quartz and cristobalite by approximately 38 % and 42 %, respectively. Further separation of the clay-size fraction (<0.037 mm, sample 37B) using conventional wet sieving provided a modest additional improvement (smectite 75.3 wt.%), indicating that most of the non-clay minerals coarser than ~0.040 mm had already been removed in the first sieving step. In both samples, the presence of plagioclases and dolomite was not detected.
The most significant enrichment was achieved in the ultrafine <0.005 mm fraction (sample 5B), where the smectite content reached 91.2 wt.%. In this fraction, quartz was reduced to 3.9 wt.% and cristobalite to 4.9 wt.%, while calcite was present only in trace amounts. The marked decrease of both quartz and cristobalite with decreasing particle size confirms that these phases occur predominantly as discrete silt- to fine-sand-sized grains or crystalline aggregates, whereas smectite forms sub-micrometer platelets that are easily concentrated in the finest fraction by hydrodynamic separation.
The mineralogical composition of the obtained sample 5B fully complies with the requirements of the Commission Implementing Regulation (EU) No 1060/2013 concerning the authorisation of bentonite as a feed additive for all animal species, which was extended by a regulation in 2021.
The montmorillonite contents estimated from the Al₂O₃ chemical composition showed excellent agreement with those determined by quantitative XRD analysis using the Rietveld refinement method, with differences of only 1–2% across all samples—a discrepancy that is well within acceptable limits for such combined chemical-mineralogical assessments and has negligible impact on the overall interpretations.
The observed trend is consistent with the well-documented density and size difference between smectite (density ~2.2–2.6 g cm⁻³, platelet thickness <0.1–1 μm) and the denser quartz and cristobalite grains (density 2.65 and 2.32 g cm⁻³, respectively, but typically larger crystal size). Consequently, the 5B reaches a purity comparable to or higher than many commercial high-grade calcium bentonites and approaches the quality of the best natural sodium bentonites after only physical processing, without the need for chemical activation or beneficiation by heavy liquids.
These results demonstrate that RB is highly amenable to upgrading by simple and low-cost size-separation techniques, yielding a premium-grade smectite product suitable for animal feed.
3.4. Cation Exchange Capacity (CEC) and Methylene Blue Adsorption
The cation exchange capacity (CEC) through methylene blue adsorption capacity was evaluated to assess the adsorption properties of the raw sample and its sieved fractions. For all samples, CEC was measured using the methylene blue method, and methylene blue adsorption capacity was quantified. The results are presented in
Table 4.
The cation exchange capacity (CEC), determined using the methylene blue method, showed a progressive increase with the degree of purification. In the raw bentonite sample (RB), the CEC was 43.76 meq/100 g. After removal of chert to obtain the initial purified fraction (IB), it increased to 55.64 meq/100 g. The <0.037 mm fraction (B37) exhibited a slightly higher value of 56.11 meq/100 g, while the finest <0.005 mm fraction (B5) displayed the highest CEC of 70.30 meq/100 g.
These results clearly demonstrate that the removal of chert significantly enhances the cation exchange capacity of the bentonite. However, the difference between the IB and B37 fractions is negligible. This can be attributed to the fact that the IB sample already contains over 90% of particles in the <0.037 mm class, which is primarily responsible for the cation exchange capacity in both samples. Furthermore, the specific surface area, which plays a crucial role in determining CEC, is very similar between these two fractions due to the high proportion of the <0.037 mm particles.
In contrast, the <0.005 mm fraction (B5) exhibits a substantially higher CEC, which can be explained by its significantly greater montmorillonite content and markedly higher specific surface area resulting from the much finer particle size. These findings underscore the effectiveness of particle size fractionation in improving the functional properties of bentonite, particularly for applications requiring high cation exchange capacity, such as aflatoxin adsorption in animal feed.
Coarser fractions, which may include quartz or other non-clay minerals, show reduced adsorption efficiency due to lower surface area and fewer active binding sites [
21]. Grant et al [
22] also notes that the effectiveness of clay for mycotoxin binding is influenced by its purity and particle size. Finer fractions, which are richer in smectite, show higher adsorption efficiency, while coarser fractions may contain accessory minerals (e.g., quartz, feldspar) that dilute the adsorptive capacity. While cristobalite is not explicitly mentioned, the principle of non-adsorptive minerals reducing efficiency in coarser fractions applies.
3.5. Mycotoxin Adsorption
As stated in the Introduction, bentonite intended for use as an aflatoxin-binding feed additive (1m558) must meet the purity criteria defined in Commission Implementing Regulation (EU) No 1060/2013, including a minimum dioctahedral smectite content of 70 %, cation exchange capacity typically in the range 70–80 meq/100 g or higher, and specified limits for accompanying minerals.
Based on the physicochemical and mineralogical characterization presented, all investigated samples except the raw bentonite (RB) met this regulatory requirement. Consequently, sample RB was excluded from the subsequent aflatoxin B1 adsorption experiments.
Figure 4 illustrates the efficiency of aflatoxin B1 (AfB1) removal at various initial aflatoxin concentrations. It can be observed that, at lower initial concentrations, all three tested samples effectively—and in most cases completely—remove the aflatoxin. From this perspective, all samples meet the requirement specified by European regulations, which mandate an AfB1-binding capacity exceeding 90% under standardized conditions (at pH 5.0, with an initial AfB1 concentration of 4 mg/L and an adsorbent dosage of 0.02% (w/v)). At higher initial concentrations, samples 5B and 37B continue to maintain a high degree of aflatoxin removal, whereas the efficiency of sample IB begins to decline.
The obtained results were interpreted through the application of adsorption isotherms. The experimental data are presented in
Figure 5 and Table 5. Overall, the results align well with expectations based on the structural and compositional characteristics of the investigated bentonite samples.
The highest adsorption capacity for aflatoxin B1 (AfB1) was achieved with sample 5B, followed by sample 37B, and then sample IB. This order of performance can be primarily attributed to differences in particle size distribution and the resulting specific surface area, which directly influence the accessibility of adsorption sites.
Sample IB contains approximately 90% of particles in the >0.037 mm fraction, whereas sample 37B comprises over 80% of particles in the <0.005 mm fraction. Sample 5B, which exhibited the highest adsorption performance, has an even finer particle size distribution, with a predominant fraction below 0.005 mm. Finer particles generally provide a larger external specific surface area and better dispersion in aqueous media, thereby enhancing the availability of active adsorption sites on the montmorillonite surfaces and edges.
Given that all three samples have a relatively high montmorillonite content, the observed differences in adsorption capacity are unlikely to arise primarily from variations in bulk mineralogical composition. Instead, specific surface area and the accessibility of adsorption sites are the dominant factors. The swelling behavior of montmorillonite, enabled by its 2:1 layer structure and high cation exchange capacity, allows interlayer expansion and exposure of internal surfaces [
10]. In finer fractions, however, the increased external surface area and reduced diffusion limitations further facilitate efficient interaction with the relatively large and polar AfB1 molecules.
The adsorption isotherms (
Figure 5) confirm that sample 5B displays the steepest initial slope and highest plateau, indicating stronger affinity and greater maximum adsorption capacity (q
max). This is consistent with its higher proportion of ultrafine particles, which minimize mass transfer resistances and maximize utilization of both external and interlayer sites. In contrast, the coarser particles in sample IB result in lower effective surface area available for rapid adsorption, leading to reduced overall capacity despite comparable montmorillonite content.
These findings highlight the critical role of particle size reduction in optimizing bentonite-based adsorbents for mycotoxin binding. Mechanical processing to obtain finer fractions can significantly enhance adsorption efficiency without altering the intrinsic chemical properties of the clay mineral. Moreover, all samples particularly 5B and 37B maintained high binding efficiencies across a range of AfB1 concentrations, meeting regulatory requirements for practical application in feed decontamination.
In comparison with chemically modified bentonites, the mechanical particle size reduction approach employed in the present study offers a viable, practical, and more sustainable alternative for enhancing AfB1 adsorption capacity.
Numerous studies have shown that chemical modifications such as intercalation with organic cationic surfactants, incorporation of metal ions (e.g., Cu and Zn), acid activation, thermal treatment, or the use of nano-montmorillonite composites can significantly improve the binding efficiency of bentonites toward AfB1 and other mycotoxins.
For instance, intercalation with hexadecyltrimethylammonium bromide (HTAB) leads to an obvious increase in interlamellar spacing and hydrophobic character of montmorillonite; bentonite modified by acid and HTAB exhibits excellent adsorption capacity for AfB1 and zearalenone (ZEA) in both acidic and alkaline conditions compared with raw montmorillonite. Similarly, nano-montmorillonite modified with stearyl trimethyl ammonium bromide showed 36% higher sorption capacity [
23,
24].
Incorporation of metal ions also enhances performance: Cu-modified bentonite increased adsorption capacity from 40.98 mg/g to 66.2 mg/g, while Zn-modified bentonite reached 60.17 mg/g [
25,
26,
27].
Acid activation increases the surface area and porosity of the clay mineral, creating more binding sites for mycotoxins [
28]. These modifications generally increase interlayer spacing, hydrophobicity, or specific surface area, resulting in higher adsorption capacities—particularly for simultaneous binding of polar (AfB1) and non-polar mycotoxins such as zearalenone or deoxynivalenol.
However, such chemical treatments involve additional processing steps, potential environmental concerns due to chemical waste, higher production costs, and questions regarding long-term stability and regulatory approval for feed applications. In contrast, the mechanical grinding used here to produce ultrafine particles (<0.005 mm predominant in samples 5B and 37B) achieved superior AfB1 adsorption without any chemical alteration. This improvement stems from increased external specific surface area, better dispersion in aqueous media, and reduced diffusion limitations, providing greater access to the inherent adsorption sites on montmorillonite surfaces and edges.
The adsorption capacities observed in the finer fractions align with or surpass those of many unmodified bentonites and approach the performance of some chemically modified variants, while offering clear advantages in simplicity, cost-effectiveness, environmental friendliness, and safety. Mechanical processing preserves the natural mineral composition and cation exchange properties, avoiding risks of interfering with nutrient bioavailability or introducing residues that could affect animal health.
Furthermore, all tested samples—especially the mechanically refined ones—met the stringent European regulatory criteria for AfB1 binding (>90% at standardized conditions), confirming the practical viability of this non-chemical strategy for mycotoxin mitigation in animal feeds. Overall, this approach provides a straightforward, scalable, and sustainable method to optimize natural bentonite resources for effective aflatoxin detoxification.
The adsorption of aflatoxin B1 (AfB1) onto montmorillonite-rich bentonites is primarily driven by chemisorption, involving strong interactions such as coordination bonds and ion-dipole forces between the carbonyl groups (especially the β-dicarbonyl system) of AfB1 and exchangeable interlayer cations (e.g., Ca²⁺, Na⁺), often supplemented by electron donor-acceptor processes or water bridging [
29,
30,
31]. This chemisorptive character is supported by high adsorption enthalpies (>40 kJ/mol), spontaneous exothermic reactions, and minimal desorption across a wide pH range, ensuring stable complexes in the gastrointestinal tract.
By reducing particle size and increasing specific surface area through mechanical processing, new opportunities arise for enhanced chemisorption in addition to improved ion exchange, due to greater accessibility of active sites on surfaces and edges.