Letícia Aliberti Galego Alves da Silvaa, Morgane Malardb, Patricia Aparecida de Campos Bragaa, Adriana Pavesi Arissetto Bragottoa, Marie Gallissotb, Pi Nyvall Collenb, Juliana Buenoc, Liliana de Oliveira Rochaa,*
c Olmix Group, Piracicaba, Brazil (jbueno@olmix.com).
*Corresponding author: Rocha, L. O. Department of Food Science and Nutrition (DECAN), Food Engineering Faculty (FEA), State University of Campinas (UNICAMP), Monteiro Lobato Street, 80, Campinas, São Paulo, Brazil, 13083- 862. E-mail: lrocha@unicamp.br.
Abstract
Mycotoxins are toxic secondary metabolites produced by fungi, and frequently encountered in cereals that compose a major part of livestock diets. Fumonisin B1 (FB1) is one of the most prevalent toxins in feed, posing a risk to animal health and productivity. Considering mycotoxin mitigation strategies, adsorbents are an advantageous alternative for reducing mycotoxin uptake by animals. In this context, the main objective of this study was to develop an in vitro protocol for FB1 adsorption and assess the binding efficacy of five formulated products composed of inorganic clay and algae extracts. For this purpose, algae-based formulations were provided by Olmix (Bréhan, France), and multiple parameters were evaluated for in vitro testing, such as pH and mycotoxin concentration. After the selection of adequate conditions, the adsorption capacities of five algae-based products were compared. Results indicate that the adsorption capacity of the algae-based products is mainly linked to the presence of algae, especially green algae; which present a high polysaccharide content in their cell walls as binding sites for mycotoxins. The use of algae for mycotoxin adsorption remains underexplored, but the findings of the present work indicate that algae-based products are effective for FB1 control in animal feed.
Keywords:
Adsorption
mycotoxin
mitigation
feed
physical methods
Introduction
A
Mycotoxins are toxic secondary metabolites produced by filamentous fungi, including species within the
Aspergillus,
Penicillium and
Fusarium genera. These microorganisms are known to infect cereals at multiple stages of production, ranging from field to storage; and result in a persistent risk of mycotoxin contamination throughout the entire production chain (Daou et al.
2021; Xu et al.
2023). Considering that cereals are major components of regular livestock diets, animals become vulnerable to the ingestion of contaminated grains. This exposure may lead to reduced performance, such as lower feed intake, milk yield, and growth efficiency and/or fertility (Vila-Donat et al.
2018; Xu et al.
2022a; Kihal et al.
2022).
Among the most commonly detected toxins in feed are Aflatoxins (AFs), Ochratoxin A (OTA), Trichothecenes, Zearalenone (ZEN) and Fumonisins (FBs) (Awuchi et al. 2022). Considering FBs, Fumonisin B1 (FB1) is the predominant compound encountered, especially in maize and its by-products (Beccaccioli et al. 2021; Pamphile and Azevedo 2002). Therefore, the occurrence of FB1 in animal feed has been documented worldwide, with reports from Europe, the Americas, Asia and Africa showing contamination levels ranging from 24.5% to 100% (Gao et al. 2023).
A
The presence of FB
1 in products intended for animal consumption is concerning, as it has been linked with equine leukoencephalomalacia and porcine pulmonary edema. Additionally, its ingestion can also result in the reduction of feed intake, lower egg production, hepatic necrosis, and thymic cortical atrophy in poultry (Awuchi et al.
2021; Chen et al.
2021; Schrenk 2022; Yang et al.
2020). Effects on ruminants are briefly described, with previous studies showing lower milk yield after FB
1 ingestion by dairy cattle; whereas adult beef cattle seem to be more resistant, exhibiting only mild hepatic necrosis (Diaz et al. 2000; Osweiler et al.
1993; Smith
2018).
Therefore, economic pressures, particularly in the livestock industry, are motivating producers to seek effective solutions to prevent the adverse effects of mycotoxins on animal health and productivity. However, if grain contamination has already occurred, preventative measures are no longer feasible. Consequently, the implementation of mitigation strategies intended for the removal, degradation or inactivation of toxins becomes crucial. Therefore, integrated approaches that combine multiple strategies are essential to guarantee safe mycotoxin levels in animal feed (Shi et al. 2018; Xu et al. 2022a).
Described methods include chemical, biological and physical treatments of grain. Chemical agents, such as ammonia, hydrogen peroxide, and organic acids, are highly effective in reducing mycotoxin levels. Nevertheless, the use of such reagents can make raw materials inedible for animals and contributes to environmental pollution. Biological strategies involve the use of enzyme-producing microorganisms to degrade or bio-transform toxins, which presents challenges for in-field application due to environmental interactions. Lastly, physical methods include sorting and separation, floating and segregation by density, irradiation, ultrasound treatment, dehulling, milling and adsorption (Luo et al. 2018; Peng et al. 2018).
Adsorption involves the use of an adsorbing agent (AA), which forms mycotoxin–adsorbent complexes through direct binding with the toxins. This process reduces mycotoxin bioaccessibility and, therefore, intestinal absorption; as the formed complexes are excreted via feces. As a consequence, this also leads to a decrease in mycotoxin uptake and in its spread to target organs (Boudergue et al. 2009; Xu et al. 2022a). In contrast with other mitigation strategies, which aim to diminish mycotoxin levels during feed production, AAs are used as feed additives. Additionally, the main advantages of such binders are their cost, safety and ease of administration through inclusion in feed (Peng et al. 2018).
Among employed AAs are organic (yeast cell wall, yeast cell wall beta-D-glucan fraction, oat and alfalfa fibers) and inorganic (bentonites, montmorillonites, zeolite and activated carbon) compounds (Kihal et al. 2022). In general, inorganic binders are highly efficient in adsorbing AFs, due to the high polarity and small molecule size of these toxins. However, such products are relatively inefficient in adsorbing other mycotoxins, especially Fusarium toxins, such as Deoxynivalenol (DON) and ZEN. In this context, the use of organic binders is recommended (Vila-Donat et al. 2018).
Considering the FB1 molecule size and its structural conformation, adsorption may be a challenging issue, especially with inorganic products. To address this limitation, adsorption can be increased through the incorporation of biological components, such as algae extracts, to inorganic binders. This modification enhances the interlayer spaces of clays, increasing surface area and resulting in more binding sites for mycotoxins (Cai et al. 2024; Oguz et al. 2022; Rasheed et al. 2020; Wang et al. 2023; Xu et al. 2022b).
Algal extracts are appealing options for AAs, as they are well-known for their biosorption/bioremediation of heavy metals (Cheng et al. 2019; Lin et al. 2020). These organisms’ cell walls contain a wide range of proteins and polysaccharides, such as β-D-glucans, that are potential binding sites for mycotoxins. Additionally, other algal compounds could also be responsible for adsorption capacity, such as chlorophyll and chlorophyllin; which may also form complexes with mycotoxins, reducing their bioaccessibility (Simonich et al. 2007).
Furthermore, the inclusion of algae as feed additives may not only help prevent the adverse effects of mycotoxins but also promotes improved animal health (Perali et al. 2020). Algae display high bioactive compound content, which can act as prebiotics and therefore enhance animal immunity. In addition, production performance (i.e. weight gain, feed intake, and feed conversion rate) may also be increased, since algae are rich in proteins, vitamins, and minerals (Fraga-Corral et al. 2023; Makkar et al. 2016; Yadavalli et al. 2023).
Estimating the adsorbent efficiency of different products is indispensable, since it depends on the type of adsorbent, its physico-chemical properties, and the target mycotoxins. In vivo testing of mycotoxin binding efficacy of a large number of adsorbents is challenging, due to the complexity and cost; making in vitro analyses powerful tools for assessing and ranking the efficacy of various AAs. Nevertheless, experimental conditions for in vitro tests reported in the literature may vary widely, making it difficult to establish reliable protocols (Boudergue et al. 2009; Faucet-Marquis, 2014). Considering the information cited above, the aim of this study is to develop an in vitro protocol for FB1 adsorption to evaluate and compare the binding efficacy of products composed of inorganic clay and algae extracts, in order to identify the most effective formulation for FB1 adsorption in livestock feed.
Material and Methods
Mycotoxin binders
Five AA formulations were provided by Olmix (Bréhan, France) for the development of this study. All products consisted of inorganic clay mixed with algae extracts, including red and green algae. They were each labeled with a code (A1 to A5) and their characteristics are summarized in Table 1. For the development and validation of the in vitro method, only A2 was employed; with the other formulations used only for efficacy testing. Additionally, activated charcoal (AC) was used as a positive control for adsorption tests.
Table 1
Products used for FB1 adsorption in the current study.
|
Code
|
Product description
|
|
A1
|
Bentonite combined with dry green algae
|
|
A2
|
Bentonite combined with green algae extract, under development
|
|
A3
|
Bentonite combined with green algae extract, for commercial use
|
|
A4
|
Bentonite combined with red algae extract, under development
|
|
A5
|
Bentonite combined with red algae extract, for commercial use
|
[Please, insert Table 1 file here]
Chemicals and reagents
FB1 external standards were acquired from Sigma-Aldrich (Fallavier, France), with stock solutions prepared in acetonitrile/water (50/50; v/v) for long-term storage at -20 ºC and further dilution (calibration curves and experiments). The solvents used for the FB1 external standard dilution, mobile phase and buffer preparation for subsequent analysis by high-performance liquid chromatography coupled with a triple quadrupole mass spectrometry (LC-MS/MS), were HPLC grade and purchased from J.T. Baker (Phillipsburg, USA). In addition, validation of the in vitro method was performed using citrate buffer (C6H8O7 • H2O and C6H5O7Na3 • 2H2O; 0,1 M) containing 10% methanol, adjusted to pH 3, 5 and 7.
Chromatographic conditions and method validation
LC-MS/MS for mycotoxin quantification was performed using the Agilent 1290 Infinity LC-System (Agilent Technologies, Santa Clara, USA) coupled to a 6460 triple quadrupole (Agilent Technologies, Santa Clara, USA) mass spectrometer, at the Food Toxicology Laboratory, Food Engineering School, State University of Campinas (UNICAMP).
The Zorbax SB-C8 column (3.0 mm x 100 mm; 1.8 µm) was used for chromatographic separation at 25 ºC. The analyses were performed in isocratic mode, using 30% of 0.1% (v/v) formic acid in water (mobile phase A) and 70% of 0.1% (v/v) formic acid in methanol (mobile phase B), with a flow rate of 0.35 mL/min and injection volume of 3 µL.
Mass spectrometry conditions were: Electrospray Source Ionization in the positive mode (ESI+) with gas temperature at 300°C, gas flow at 10 L/min, nebulizer at 35 psi, sheath gas flow at 10 L/min, sheath gas temperature at 350°C, capillary voltage at 3.0 kV and nozzle voltage at 0.5 kV. Ultrapure nitrogen was used in the nebulizer and as collision gas.
For FB1, m/z 722 (precursor), m/z 353 (quantifier transition) and m/z 334 (qualifier transition) were monitored. The fragmentor applied was 185 V and collision energies were 40 eV for both quantifiers and qualifier transitions. Data acquisition and analyses were performed using MassHunter software workstation version 7.00 (Agilent Technologies, Santa Clara, USA) in selected reaction monitoring (SMR) mode, using a dwell time of 100 ms per channel.
The linearity of FB1 was obtained based on calibration curves in the matrices (Figure S1; citrate buffer 0.1 M with 10% methanol at pH 3, 5, and 7). FB1 standard was prepared at seven concentrations (0.5, 1, 2.5, 5, 7.5, 10, and 12.5 µg/mL) in triplicates, and subsequently analyzed under the conditions previously described (Sun et al. 2018). All linearities (R2) obtained were ≥ 0.99 at pHs 3, 5, and 7 (Figure S1). Recovery was evaluated in triplicates on the same day as the analysis, with results ranging from 95% to 110% for citrate buffer at pH 3, 5, and 7 (EC 2006). The limits of detection (LODs) and the limits of quantification (LOQs) for each matrix are provided in Table S1; these were calculated through the minimum concentration detected with a 3x and a 10x signal-noise ratio, respectively.
Furthermore, precision was assessed at three FB1 concentration levels (2.5 µg/mL, 5 µg/mL and 7.5 µg/mL) by analyzing five replicates of each level in citrate buffer pH 5, without the presence of adsorbent. Intra-day precision was assessed by analyzing all replicates on the same day under the same conditions. Inter-day precision was determined by repeating the procedure on three different days. The results were expressed as the coefficient of variation (CV%) for each level (Table S2). All CV% values were within the acceptable limits of ≤ 20%, in accordance with SANTE/11312/2021 (EC 2021) (Table S2).
The selectivity of the method was assessed by analyzing blank and fortified samples (2.5 µg/mL of FB1) in citrate buffer (pH 3, 5, and 7). The fortified samples exhibited well-defined peaks in the qualifier transition (m/z 334) with consistent retention times ranging from 1.928 to 1.955 minutes (Figure S2). No interfering peaks were observed in the blank samples at the corresponding retention times, demonstrating the selectivity of the method for FB1 analysis (Figure S2).
Effect of pH and FB1 concentration on adsorption capacity
pH
Three different pH levels (3, 5 and 7) were evaluated, to determine the optimal level to proceed with the trials. For this purpose, three FB1 working solutions (5 µg/mL) were prepared in citrate buffer with 10% methanol at pH 3, 5 and 7, separately. Next, 5 mL of each solution was pipetted into 50 mL polypropylene tubes containing either: 0.1% (w/v) of A2, according to manufacturer instructions; 0.1% (w/v) of activated charcoal (AC; AC positive control); or no adsorbent (control without adsorbent); in triplicates (Faucet-Marquis et al. 2014)
Samples were then incubated (30 minutes; 37ºC; 8 x g) and centrifuged (15 minutes; 8586 x g). Subsequently, 1 mL of supernatant from each sample was retrieved, filtered by syringe filter (0.22 µm) and analyzed with HPLC-MS/MS (item 2.3.). After chromatographic analyses, the adsorption percentage of each test was calculated based on Eq.
1:
where
Cads is the adsorbed mycotoxin yield (µg/mL) and
C0 is the concentration of FB
1 in the controls without adsorbent (µg/mL) (Joannis-Cassan et al.
2011).
Four FB1 concentrations (1 µg/mL, 2.5 µg/mL, 5 µg/mL, and 10 µg/mL) were prepared in 5mL of pH 5 citrate buffer (10% methanol) as solvent. Considering the evaluated product should demonstrate a high affinity and capacity to adsorb mycotoxins at its low inclusion rate in livestock diets, 0.1% (w/v) of product A2 was employed.
The tests were performed in triplicates, using 0.1% (w/v) of AC as positive control (AC positive control) and mycotoxin working solution without adsorbent as control without adsorbent. Next, the tubes were incubated (30 minutes; 37 ºC; at 8 x g) and centrifuged (15 minutes; at 8586 x g). After, approximately 1 mL of the supernatant was withdrawn, filtered by syringe filter (0.22 µm), and taken for HPLC-MS/MS analysis using the conditions described above (item 2.3.); and adsorption percentage was calculated based on Formula 1.
Considering the previously determined optimal pH (item 2.4.1.), 5 mL of increasing amounts of FB1 (0.5, 1, 2.5, 5, and 7.5 µg/mL) were incubated in 50 mL polypropylene tubes with 0.1% (w/v) of adsorbent (A2), 0.1% (w/v) of AC (AC positive control) or without adsorbent (control without adsorbent). All tests were performed in triplicates and incubation conditions were 37 ºC, with rotation 8 x g for 30 min. Next, all samples were centrifuged (15 minutes; 8586 x g) and 1 mL of their supernatants were withdrawn separately, filtered by syringe filter (0.22 µm), and taken for HPLC-MS/MS analysis; as formerly described (item 2.3.).
This step was performed to determine the ideal intermediate concentration of FB
1, to evaluate the adsorption capacity of different algae-based products. For this purpose, the adsorption percentage of each concentration was calculated based on Formula 1 (item 2.4.1). Moreover, an isotherm curve was also elaborated by plotting the variations in the residual FB
1 concentration after adsorption in µg/mL (
Ceq) against the quantity of adsorbed FB
1 per gram of adsorbent (
Qeq), calculated using Formula 2:
where C0 is the concentration of FB1 in the blank controls (µg/mL), m is the mass of adsorbent in grams and V is the final volume of the solution in liters.
Additionally, the data obtained for the isotherm curve was fitted into two different models, Freundlich and Hill (Joannis-Cassan et al.
2011). In this regard, the first assumes the sorption occurs on a heterogeneous surface and is described by Formula 3:
where KF is a constant representing the capacity of the adsorbent to bind to the mycotoxin (milligram 1 − (1 ∕ nF) × liter 1 ∕ nF per gram) and nF is a constant concerning the affinity of the adsorbent (Joannis-Cassan et al. 2011).
As for the Hill model, it is usually employed to describe the adsorption of diverging compounds onto a heterogeneous substrate (Joannis-Cassan et al.
2011), using Formula 4:
where QHmax is the maximal mycotoxin adsorption corresponding to the site saturation (mg/g), KD symbolizes the Hill constant (mg/L) and nH corresponds to the cooperativity coefficient of the interaction among product and toxin (Joannis-Cassan et al. 2011).
Evaluation of adsorption capacity of five algae-based products
The ideal conditions (pH and FB1 concentration) obtained from the last steps (item 2.4) were applied, to compare FB1 adsorption capacities of five different algae-based products (Table 1). Tests were performed using 0.1% (w/v) of each product (A1-A5), 0.1% (w/v) of AC (AC positive control) and no adsorbent (control without adsorbent) in triplicates. FB1 working solutions (2.5 µg/mL) were prepared in citrate buffer, pH 5 (0.1 M) with 10% methanol, and pipetted (5 mL) into 50 mL polypropylene tubes containing either the test products, AC (AC positive control), or no product (control without adsorbent). All tubes were incubated (30 minutes; 37 ºC; 8 x g) and centrifuged (15 minutes; 8586 x g), followed by the removal of 1 mL of each supernatant. Samples were then filtered by syringe filter (0.22 µm) and taken for HPLC-MS/MS analysis according to item 2.3. Adsorption efficacy was calculated based on Formula 1 (item 2.4.1).
Statistical analysis
Mean and standard deviation calculations of assay replicates were performed in Microsoft Excel 2016. The equilibrium point isotherm with two model fits (Freundlich and Hill model) was elaborated by plotting the experimental data and other resources in R software (R Core Team 2025). Lastly, unpaired t-test results for the adsorption of red algae and green algae-based products were obtained from GraphPad Prism software version 8, with no correction for multiple comparisons (GraphPad, 2018, v. 8.0.1).
Results
Effect of pH and FB1 concentration on adsorption capacity
Effect of pH
The pH level is an influential parameter for in vitro adsorption tests (Faucet-Marquis et al. 2014). Thus, three different assays were performed: at pH level 3, 5, and 7. All of the AC positive control samples showed adsorption levels above 90%, as expected (Table 2). Conversely, the A2 product adsorption performance varied greatly according to the pH.
Table 2
Effect of different pH levels on FB1 (5 µg/mL) adsorption by the A2 algae-based product.
|
Product
|
pH
|
Mean adsorption (%) ± SD
|
Mean recovery (%) ± SD
|
|
A2
|
3
|
88.06 ± 0.011
|
95.63 ± 0.04
|
|
5
|
48.06 ± 0.032
|
96.59 ± 0.039
|
|
7
|
2.8 ± 0.018
|
110.97 ± 0.026
|
|
AC
|
3
|
91.8 ± 0.001
|
95.63 ± 0.04
|
|
5
|
91.72 ± 0.002
|
96.59 ± 0.039
|
|
7
|
95.12 ± 0.001
|
110.97 ± 0.026
|
At a lower pH level (3), FB1 adsorption was the highest (88.06%±0.011) and the closest to the AC positive control samples. When pH was increased to 5, the adsorption was reduced almost by half to 48.06%±0.032. Lastly, at pH 7, FB1 adsorption was the closest to 0% (2.8%±0.018), and showed a very high coefficient of variation, ruling it out as an alternative.
Between pH levels 3 and 5, the former presented a lower coefficient of variation and standard deviation. However, its adsorption level is too high and similar to AC, which could hinder comparisons among products. Alternatively, pH 5 presented an ideal and intermediate adsorption rate, with an adequate coefficient of variation and higher recovery, when compared to pH 3. In this context, all further assays were carried out at pH 5.
[Please, insert Table 2 file here]
Effect of FB1 concentration
To evaluate the effect of FB1 concentration on the adsorption capacity, 1 µg/mL, 2.5 µg/mL, 5 µg/mL, and 10 µg/mL of FB1 were tested, considering 0.1% (w/v) of the product A2 and citrate buffer at pH 5. All the recovery tests were acceptable, ranging between 97% and 109% (EC, 2006). AC positive control assays exhibited the highest adsorption rates (Table 3). Moreover, FB1 adsorption by A2 ranged from 33%±0.01 (1 µg/mL), to 45%±0.04 (5 µg/mL). In this context, higher adsorption was observed for 2.5 µg/mL of FB1 (Table 3), with no statistical difference when compared to FB1 at 5 µg/mL. Nevertheless, when FB1 concentration was 10 µg/mL, mean adsorption dropped by 10%, indicating that higher FB1 concentrations might cause saturation in the binding sites of the product (i.e. 10 mg of FB1:1 g of the product).
Table S1
Limits of detection (LOD) and quantification (LOQ) for FB1 in citrate buffer at pH 3, 5, and 7.
|
Matrix
|
LOD (µg/mL)
|
LOQ (µg/mL)
|
|
Citrate Buffer pH 3
|
0.013
|
0.039
|
|
Citrate Buffer pH 5
|
0.061
|
0.184
|
|
Citrate Buffer pH 7
|
0.127
|
0.385
|
Table S2
Method precision for FB1 analysis. Intra-day precision was evaluated using five replicates at each FB1 concentration on the same day at pH 5. Inter-day precision was assessed over three separate days, with five replicates per level analyzed each day at pH 5.
| |
|
|
Precision
|
|
FB1 concentration (µg/mL)
|
Mean FB1 levels recovered (µg/mL)
|
SD
|
Intra-day (%)
|
Inter-day (%)
|
|
2.5
|
2.04
|
0.23
|
8.9%
|
11.4%
|
|
5.0
|
4.63
|
0.59
|
13.5%
|
12.7%
|
|
7.5
|
7.71
|
0.12
|
7.3%
|
1.5%
|
| SD: standard deviation. |
Table 3
Effect of FB1 concentration on the adsorption of A2 algae-based product at pH 5.
|
Product
|
FB1 (µg/mL)
|
Mean adsorption (%) ± SD
|
Mean recovery (%) ± SD
|
|
A2
|
1
|
33 ± 0.01
|
109 ± 0.02
|
|
2.5
|
44 ± 0.02
|
97 ± 0.14
|
|
5
|
45 ± 0.04
|
98 ± 0.03
|
|
10
|
36 ± 0.04
|
103.1 ± 0.04
|
|
AC
|
1
|
86 ± 0.0005
|
109 ± 0.02
|
|
2.5
|
80 ± 0.001
|
97 ± 0.14
|
|
5
|
92 ± 0.003
|
98 ± 0.03
|
|
10
|
95 ± 0.0002
|
103.1 ± 0.04
|
[Please, insert Table 3 file here]
Equilibrium point and isotherm curve
After selecting pH 5 for the in vitro adsorption test, an isotherm curve was elaborated with different FB1 concentrations (0.5, 1, 2.5, 5, and 7.5 µg/mL). As a result, the experimental data were used to build an equilibrium isotherm curve (Fig. 1), which shows an exponential relationship among Ceq, Qeq and non-saturation of the adsorbent’s binding sites.
Considering the two models applied for curve fitting, the Freundlich model demonstrates agreement with the experimental data; predominantly at lower FB1 concentrations. In contrast, the Hill model displays a better fit at higher mycotoxin levels. Thus, the Freundlich model seems to be the most suitable for the acquired experimental data due to its significant n factor; which reflects the non-linear nature of the adsorption. Additionally, the Hill model is mostly related to the binding of multiple species and presents many uncertainties in the conditions of the present study; contributing to its unsuitability to the experimental data (Joannis-Cassan et al. 2011).
The highest adsorption percentage was observed at 7.5 µg/mL (61%±0.03), followed by 5 µg/mL (40%±0.01), 1 µg/mL (32%±0.01), 2.5 µg/mL (30%±0.04) and 0.5 µg/mL (29%±0.01).
Despite observing higher adsorption rates for FB1 at concentrations of 7.5 and 5 µg/mL during this experiment, the recovery tests approached the upper limit of 110% for concentrations of 0.5, 1, 5, and 7.5 µg/mL. In contrast, a recovery rate of 97% was achieved at 2.5 µg/mL. Consequently, this concentration was selected for the comparison of the five different algae-based products. In addition, while conducting the previous experiment, the FB1 concentration of 2.5 µg/mL achieved a mean adsorption of 44%±0.02; therefore, further corroborating this choice for future product comparisons.
[Please insert Fig. 1 file here]
Adsorption capacity of five algae-based products
To compare five different algae-based formulations, in vitro adsorption tests that employed the ideal conditions from previous analyses (pH 5; 2.5 µg/mL FB1) were performed, and the results are shown in Fig. 2. Disregarding the AC positive control, the greatest adsorption performance was achieved by A2 (48%±0.05), followed by A3 (42%±0.04), A1 (38.5%±0.03), A4 (38%±0.03) and A5 (34%±0.05). Additionally, the Qeq of the tested products showed the same pattern as the adsorption percentage, where A2 exhibited the highest values (1.022 µg of FB1 adsorbed per mg of product) and A5 the lowest (0.718 µg of FB1 adsorbed per mg of product).
Three green algae-based and two red algae-based formulas were tested. In this regard, a significant difference (p < 0.05) was found between the adsorption performance of products containing green algae (mean adsorption = 43.06 ± 0.06) and red algae (mean adsorption = 36.25 ± 0.05); suggesting that green algae-based formulations may be more efficient in adsorbing FB1.
[Please insert Fig. 2 file here]
Discussion
In vitro adsorption tests are generally used as a screening method for the efficacy assessment of mycotoxin binders. Some of the main advantages of performing such assays are their lower cost and quicker results, when compared to in vivo analyses. However, most of the studies on in vitro adsorption trials do not present standardized and repeatable conditions, especially regarding the pH levels and mycotoxin concentration (Faucet-Marquis et al. 2014; Kihal et al. 2022). This is particularly important, as these assays represent the gold standard used by most companies developing adsorbents for livestock feed, since they mimic the animal gastrointestinal system. During digestion, mycotoxins ingested with feed can be bound by the adsorbent, reducing their absorption and subsequent biotransformation in the liver. Consequently, lower toxin levels reach systemic circulation, decreasing their transfer through the food chain into animal-derived products such as milk, eggs or meat (Avantaggiato et al. 2006; Kihal et al. 2023). Thus, validating a robust adsorption protocol is essential to ensure both animal and food safety.
The adsorption capacity of mineral products, such as bentonites, is directly linked to their physico-chemical characteristics, especially their interlayer spaces’ conformation/charge and cation exchange capacity. The latter is highly influenced by the pKa of the adsorbent (point zero charge) and the medium’s pH level. In this regard, when the pH level of the medium is lower than the pKa of the adsorbent, it results in a loss of charge and lower cation exchange capacity. Conversely, when the medium’s pH level is higher than the bentonite’s pKa, it becomes more electronegative and adsorption capacity is increased (Du et al. 2021; Kihal et al. 2022).
Considering that FB1 is a highly polar compound, minor pH alterations can result in structural modifications as well as protonation/deprotonation of carbonyl groups. In acidic conditions, the FB1 molecule is protonated, while in neutral-alkaline pH it exists as an anion (Momany and Dombrink-Kurtzman 2001; Šegvić and Pepeljnjak 2001). The results of the present study, show that adsorption was higher at pH 3, which is not consistent with the physico-chemical characteristics of FB1 and bentonites. At this pH range, the cation exchange capacity and electronegativity of the AA should be low; which considerably reduces the binding performance when only bentonite is utilized (Barrientos-Velázquez et al. 2016).
The results obtained from the current study suggest that the adsorption of FB1 by the algae-based product complex occurs mainly due to the presence of algae in the interlayers of bentonites. Algae mycotoxin adsorption mechanisms are not yet well understood. However, it is known that algal cell walls contain polymers, such as β-D-glucans, xylans, galactanes and mannans. These components are likely key contributors to the adsorption capacity of algae, as they can bind to mycotoxins through Van der Walls interactions or hydrogen bonds (Cheng et al. 2019; Fraga-Corral et al. 2023; Jouany et al. 2005; Yiannikouris et al. 2006). Such interactions are not based on charge exchange but rather depend on the structural stability of the polysaccharide molecules. In the case of β-D-glucans and other glucose-based polymers, this stability is pH-dependent. Under acidic conditions (pH 3), the structural rigidity of these polysaccharides increases, which improves their ability to bind to mycotoxins. Conversely, at neutral pH levels (5–7), the molecules are less stable and can suffer conformational changes, which might hinder mycotoxin adsorption (Faucet-Marquis et al. 2014; Yiannikouris et al. 2004; Yiannikouris 2006).
Therefore, the low FB1 adsorption observed at pH 5–7 likely reflects the reduced activity of the algae component, due to pH-sensitive structural changes. Simultaneously, the bentonite may not have attained sufficient surface electronegativity to effectively contribute to adsorption at this pH interval. Altogether, this suggests that pH 5–7 likely represents an intermediate zone, where neither components perform optimally, leading to the observed decrease in overall adsorption efficiency. Moreover, our results also support the evidence that the modification of inorganic mineral products (i.e. bentonites) by adding organic extracts may increase their adsorption capacity; since previous reports indicate FB1 adsorption by clays alone is moderate to low (Elliott et al. 2020).
In this respect, Rasheed et al. (2020), through the addition of orange peel extracts to pure bentonite, obtained efficient in vitro adsorption of Aflatoxin B1 (AFB1), FB1, and OTA. In their study, FB1 adsorption exceeded 80% in buffered solutions at pH 2.5 and pH 7, as well as in simulated gastric fluids (acidic conditions). However, when the reaction was performed in simulated intestinal fluids (near-neutral conditions), the performances was considerably reduced to under 20% (Rasheed et al. 2020). These observations are consistent with our results, in which higher adsorption efficiency was also observed at acidic pH 3. Structurally, the organic components were found within the interlayers of the clay, like the algae-based products, generating additional binding sites for mycotoxins. The authors suggested that FB1 might have formed peripheral interactive forces, especially Van der Waals interactions with the organic fraction of the product (Rasheed et al. 2020).
Additionally, Oguz et al. (2022) evaluated the adsorption efficacy of clays, plant extracts, and glucomannans, individually and in combination, using in vitro methods. For FB1, the authors reported moderate binding levels for clays and glucomannans alone. However, when plant extracts and glucomannans were added to a mixture of clays, there was a 20% increase in the adsorption capacity of the product, particularly under acidic conditions (pH 3), where FB1 adsorption reached 54.61%. (Oguz et al. 2022). These findings corroborate the results of the current study, in which FB1 adsorption by algae-modified clay was greatest at pH 3.
A
As for
in vivo studies, Tsiouris et al. (
2021), by adding yeast cell walls and silymarin to clays, observed the reduction of adverse effects related to AFB
1 and OTA in broiler chicks. Treated animals also showed healthier intestinal conditions after ingesting the formulated product, which could hinder the development of gut pathogens, such as
Escherichia coli,
Clostridium perfringens,
Salmonella spp. and
Campylobacter spp. (Tsiouris et al.
2021). In addition, El-Nekeety et al. (
2017) also formulated an organically modified clay and, as a result, the product was able to efficiently adsorb FB
1 and ZEN, reducing their toxic effects in rats.
An isotherm curve was constructed to characterize FB1 adsorption by one algae-based formulation, to select an optimal concentration for testing different products (Boudergue et al. 2009; Joannis-Cassan et al. 2011). The shape of the curve resembled those observed in other studies involving FBs and organically modified clays (Baglieri et al. 2013). According to Baglieri et al. (2013) and Lemke et al. (1998), such a profile indicates the binding of the mycotoxin to specific sites. Furthermore, the data revealed that binding site saturation was not achieved at the tested concentrations; however, our preliminary results suggest that an FB1 concentration of 10 µg/mL combined with 0.1% (w/v) of adsorbent may saturate the binding sites of the product.
Additionally, two different models were applied for isotherm curve fitting: the Freundlich model and the Hill model. The Freundlich model is applicable to non-linear multilayer adsorption, showing the exponential distribution of the active binding sites and their energies. In contrast, the Hill model describes cooperative interactions in biological systems and is mainly related to the binding of different species. Therefore, the Freundlich model appears to better fit the conditions and experimental data of the current study when compared to the Hill model (Al-Ghouti and Da’ana 2020; Rajahmundry et al. 2021).
After determining the FB1 concentration to be 2.5 µg/mL from the isotherm curve, five different algae-based products were tested. The results showed adsorption percentages from 48% (A2) to 34% (A5). Moreover, green algae-based products exhibited significantly higher adsorption compared to those derived from red algae. This contrast may be attributed to the distinct compositions of the red and green algae cell walls (Romera et al. 2008). Red algae cell walls contain sulfated polysaccharides composed of galactanes serving as potential adsorption sites, whereas green algae have glycoprotein-rich walls with diverse functional groups (amino, carboxyl, sulfate, hydroxyl) acting as binding domains (Romera et al. 2008). At present, there are no studies comparing mycotoxin adsorption by multiple products containing different types of algae. However, both algal extracts and live algae have been widely used for heavy metal biosorption, with results showing that green algae generally display higher adsorption capacity than red algae, consistent with our findings (Boukarma et al. 2024; Romera et al. 2006).
Considering the use of only algae or algae-based products for mycotoxin adsorption, Perali et al. (2020) tested the binding efficacy of Lithothamnium calcareum, for the adsorption of AFB1 in broiler chicks. As a result, the authors showed not only a reduction of adverse effects related to mycotoxin ingestion, but also an improved body weight, weight gain, and feed intake in the animals treated with L. calcareum (Perali et al. 2020). Conversely, another study involving DON and algae-modified clay, showed that the AA was not effective in adsorbing the toxin nor in avoiding the adverse effects related to DON in nursery pigs; possibly due to a low affinity of the product to this mycotoxin (Frobose et al. 2016).
Altogether, when preventive measures against mycotoxin contamination in animal feed are ineffective, adsorbents are recommended to reduce toxin uptake and prevent productivity losses (Boudergue et al. 2009; Jouany, 2007; Vila-Donat et al. 2018). FB1, one of the most commonly found toxins in feed, has a complex and elongated structure, which makes its adsorption challenging. Therefore, it is essential to test and evaluate novel AAs to mitigate its adverse effects and enhance livestock performance (Gao et al. 2023; Oguz et al. 2022; Shi et al. 2018; Xu et al. 2022a). In this context, incorporating algae into livestock diets may simultaneously contribute to mycotoxin adsorption and improve animal health and immunity (Fraga-Corral et al. 2023; Yadavalli et al. 2023).
In vitro adsorption tests are useful tools for evaluating the adsorption capacity of multiple agents on a small scale, with lower cost and analysis time when compared to in vivo assays. However, adsorption mechanisms are complex, especially when dealing with organic-based products, with conditions such as pH, saturation of the adsorbent, and type of mycotoxin influencing the product performance being important. In this regard, the evaluation of multiple test parameters in the present study resulted in an adequate in vitro FB1 adsorption protocol to screen different algae-based products. The results also showed different adsorption capacities of the formulations evaluated, showing that green algae were more efficient than red algae-based products. Such findings may indicate that the different compositions of these organisms’ cell walls can influence their performance in FB1 adsorption. In summary, the evaluated products, particularly those containing green algae, show promising potential for reducing FB1 exposure in livestock. However, further research is needed to assess their efficacy across different feed matrices and under simulated digestion conditions, as well as through in vivo studies on FB1 bioavailability. This is especially relevant given that the inclusion of algae in livestock diets has already been linked to improvements in animal health.
A
Acknowledgement
The authors would like to thank the Olmix Group (Bréhan, France) for the partnership and funding, The São Paulo Research Foundation (FAPESP, Project number: 2023/16635-7) and the Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq, Project number: 140978/2023-2).
A
Author Contribution
Conceptualization: MG, LOR; Methodology: LAGAS, MM, PACB; Validation: LAGAS, MM; Investigation: LAGAS, MM, PACB; Data curation: LAGAS, MM; Visualization: LAGAS, MM; Resources: APAB, MG, PNC, JB; Writing – original draft: LAGAS; Writing – review and editing: LAGAS, MM, APAB, MG, PNC, JB, LOR; Supervision: MG, LOR; Project administration: MG, LOR; Funding acquisition: MG, PNC, JB, LOR.
Electronic Supplementary Material
Below is the link to the electronic supplementary material
A
Data Availability
Data supporting this study are available from the corresponding author (Rocha, L. O.) under request.
References
Al-Ghouti MA, Da’ana DA (2020) Guidelines for the use and interpretation of adsorption isotherm models: A review. J Hazard Mater 393:122383. https://doi.org/10.1016/j.jhazmat.2020.122383
A
Avantaggiato G, Solfrizzo M, Visconti A (2005) Recent advances on the use of adsorbent materials for detoxification of
Fusarium mycotoxins. Food Addit Contam 22:379–388.
https://doi.org/10.1080/02652030500058312
Awuchi CG, Ondari EN, Nwozo S et al (2022) Mycotoxins’ Toxicological Mechanisms Involving Humans, Livestock and Their Associated Health Concerns: A Review. Toxins (Basel) 14:167. https://doi.org/10.3390/toxins14030167
Awuchi CG, Ondari EN, Ogbonna CU et al (2021) Mycotoxins Affecting Animals, Foods, Humans, and Plants: Types, Occurrence, Toxicities, Action Mechanisms, Prevention, and Detoxification Strategies—A Revisit. Foods 10:1279. https://doi.org/10.3390/foods10061279
Baglieri A, Reyneri A, Gennari M, Nègre M (2013) Organically modified clays as binders of fumonisins in feedstocks. J Environ Sci Health Part B 48:776–783. https://doi.org/10.1080/03601234.2013.780941
Barrientos-Velázquez AL, Marroquin Cardona A, Liu L et al (2016) Influence of layer charge origin and layer charge density of smectites on their aflatoxin adsorption. Appl Clay Sci 132–133:281–289. https://doi.org/10.1016/j.clay.2016.06.014
Beccaccioli M, Salustri M, Scala V et al (2021) The Effect of Fusarium verticillioides Fumonisins on Fatty Acids, Sphingolipids, and Oxylipins in Maize Germlings. Int J Mol Sci 22:2435. https://doi.org/10.3390/ijms22052435
Boudergue C, Burel C, Dragacci S et al (2009) Review of mycotoxin-detoxifying agents used as feed additives: mode of action, efficacy and feed/food safety. EFSA Supporting Publications 6:1. https://doi.org/10.2903/sp.efsa.2009.EN-22
Boukarma L, Aziam R, Aboussabek A et al (2024) Novel insights into crystal violet dye adsorption onto various macroalgae: Comparative study, recyclability and overview of chromium (VI) removal. Bioresour Technol 394:130197. https://doi.org/10.1016/j.biortech.2023.130197
Cai Y (Tina), McLaughlin M, Zhang K (eds) (2020) Advancing the FDA/Office of Regulatory Affairs Mycotoxin Program: New Analytical Method Approaches to Addressing Needs and Challenges. J AOAC Int 103:705–709. https://doi.org/10.1093/jaocint/qsz007
Chen J, Wei Z, Wang Y et al (2021) Fumonisin B1: Mechanisms of toxicity and biological detoxification progress in animals. Food Chem Toxicol 149:111977. https://doi.org/10.1016/j.fct.2021.111977
Cheng SY, Show P-L, Lau BF et al (2019) New Prospects for Modified Algae in Heavy Metal Adsorption. Trends Biotechnol 37:1255–1268. https://doi.org/10.1016/j.tibtech.2019.04.007
Daou R, Joubrane K, Maroun RG et al (2021) Mycotoxins: Factors influencing production and control strategies. AIMS Agric Food 6:416–447. https://doi.org/10.3934/agrfood.2021025
A
Díaz MA, Pereyra MM, Picón-Montenegro E et al (2020) Killer Yeasts for the Biological Control of Postharvest Fungal Crop Diseases. Microorganisms 8:1680.
https://doi.org/10.3390/microorganisms8111680
Du W, Yang Y, Hu L et al (2021) Combined determination analysis of surface properties evolution towards bentonite by pH treatments. Colloids Surf Physicochem Eng Asp 626:127067–112712. https://doi.org/10.1016/j.colsurfa.2021.127067
EC – European Commission (2006) Commission regulation (EC) No 1881/2006 of 19 December 2006 setting maximum levels for certain contaminants in foodstuffs. Off J Eur Union L 364:5–24 Last consolidated version available from: https://eur-lex.europa.eu/legal-content/DE/AUTO/?uri=CELEX:02006R1881-20180319
EC – European Commission (2021) SANTE/11312/2021: Analytical quality control and method validation procedures for pesticide residue analysis in food and feed. Off J Eur Union L. Last consolidated version available from: https://food.ec.europa.eu/system/files/2023-11/pesticides_mrl_guidelines_wrkdoc_2021-11312.pdf
Elliott CT, Connolly L, Kolawole O (2020) Potential adverse effects on animal health and performance caused by the addition of mineral adsorbents to feeds to reduce mycotoxin exposure. Mycotoxin Res 36:115–126. https://doi.org/10.1007/s12550-019-00375-7
El-Nekeety AA, El-Kady AA, Abdel-Wahhab KG et al (2017) Reduction of individual or combined toxicity of fumonisin B1 and zearalenone via dietary inclusion of organo-modified nano-montmorillonite in rats. Environ Sci Pollut Res 24:20770–20783. https://doi.org/10.1007/s11356-017-9721-y
Faucet-Marquis V, Joannis-Cassan C, Hadjeba-Medjdoub K et al (2014) Development of an in vitro method for the prediction of mycotoxin binding on yeast-based products: case of aflatoxin B1, zearalenone and ochratoxin A. Appl Microbiol Biotechnol 98:7583–7596. https://doi.org/10.1007/s00253-014-5917-y
Fraga-Corral M, Otero P, Echave J et al (2023) Algal Extracts as Preventive Mechanism for Mycotoxins Development. IECT 2023. MDPI, Basel Switzerland, p 5
Frobose HL, Erceg JA, Fowler SQ et al (2016) The progression of deoxynivalenol-induced growth suppression in nursery pigs and the potential of an algae-modified montmorillonite clay to mitigate these effects12. J Anim Sci 94:3746–3759. https://doi.org/10.2527/jas.2016-0663
Gao Z, Luo K, Zhu Q et al (2023) The natural occurrence, toxicity mechanisms and management strategies of Fumonisin B1: A review. Environ Pollut 320:121065. https://doi.org/10.1016/j.envpol.2023.121065
Joannis-Cassan C, Tozlovanu M, Hadjeba-Medjdoub K et al (2011) Binding of Zearalenone, Aflatoxin B1, and Ochratoxin A by Yeast-Based Products: A Method for Quantification of Adsorption Performance. J Food Prot 74:1175–1185. https://doi.org/10.4315/0362-028X.JFP-11-023
Jouany JP (2007) Methods for preventing, decontaminating and minimizing the toxicity of mycotoxins in feeds. Anim Feed Sci Technol 137:342–362. https://doi.org/10.1016/j.anifeedsci.2007.06.009
Jouany J-P, Yiannikouris A, Bertin G (2005) How yeast cell wall components can alleviate mycotoxicosis in animal production and improve the safety of edible animal products. J Anim Feed Sci 14:171–190. https://doi.org/10.22358/jafs/70361/2005
Kihal A, Rodríguez-Prado M, Calsamiglia S (2022) The efficacy of mycotoxin binders to control mycotoxins in feeds and the potential risk of interactions with nutrient: a review. J Anim Sci 100:1–14. https://doi.org/10.1093/jas/skac328
Lemke SL, Grant PG, Phillips TD (1998) Adsorption of zearalenone by organophilic montmorillonite clay. J Agric Food Chem 46(9):3789–3796
Lin Z, Li J, Luan Y, Dai W (2020) Application of algae for heavy metal adsorption: A 20-year meta-analysis. Ecotoxicol Environ Saf 190:110089. https://doi.org/10.1016/j.ecoenv.2019.110089
Luo Y, Liu X, Li J (2018) Updating techniques on controlling mycotoxins - A review. Food Control 89:123–132. https://doi.org/10.1016/j.foodcont.2018.01.016
Makkar HPS, Tran G, Heuzé V et al (2016) Seaweeds for livestock diets: A review. Anim Feed Sci Technol 212:1–17. https://doi.org/10.1016/j.anifeedsci.2015.09.018
Momany FA, Dombrink-Kurtzman MA (2001) Molecular Dynamics Simulations on the Mycotoxin Fumonisin B 1. J Agric Food Chem 49:1056–1061. https://doi.org/10.1021/jf000842h
Oguz H, Bahcivan E, Erdogan T et al (2022) In vitro mycotoxin binding capacities of clays, glucomannan and their combinations. Toxicon 214:93–103. https://doi.org/10.1016/j.toxicon.2022.05.006
Osweiler GD, Kehrli ME, Stabel JR et al (1993) Effects of fumonisin-contaminated corn screenings on growth and health of feeder calves. J Anim Sci 71:459–466. https://doi.org/10.2527/1993.712459x
Pamphile JA, Azevedo JL (2002) Molecular characterization of endophytic strains of Fusarium verticillioides (= Fusarium moniliforme) from maize (Zea mays. L). World J Microbiol Biotechnol 18:391–396. https://doi.org/10.1023/A:1015507008786
Peng W-X, Marchal JLM, van der Poel AFB (2018) Strategies to prevent and reduce mycotoxins for compound feed manufacturing. Anim Feed Sci Technol 237:129–153. https://doi.org/10.1016/j.anifeedsci.2018.01.017
Perali C, Magnoli AP, Aronovich M et al (2020) Lithothamnium calcareum (Pallas) Areschoug seaweed adsorbs aflatoxin B1 in vitro and improves broiler chicken’s performance. Mycotoxin Res 36:371–379. https://doi.org/10.1007/s12550-020-00402-y
A
Piazzolitto R, J. D RM et al (2011) Binding of Aflatoxin B1 to Lactic Acid Bacteria and Saccharomyces cerevisiae in vitro: A Useful Model to Determine the Most Efficient Microorganism. In: Guevara-Gonzalez RG (ed) Aflatoxins - Biochemistry and Molecular Biology. InTech, London, pp 323–346
Rajahmundry GK, Garlapati C, Kumar PS et al (2021) Statistical analysis of adsorption isotherm models and its appropriate selection. Chemosphere 276:130176. https://doi.org/10.1016/j.chemosphere.2021.130176
Rasheed U, Ain QU, Yaseen M et al (2020) Modification of bentonite with orange peels extract and its application as mycotoxins’ binder in buffered solutions and simulated gastrointestinal fluids. J Clean Prod 267:122105. https://doi.org/10.1016/j.jclepro.2020.122105
Romera E, González F, Ballester A et al (2006) Biosorption with Algae: A Statistical Review. Crit Rev Biotechnol 26:223–235. https://doi.org/10.1080/07388550600972153
A
Romera E, González F, Ballester A et al (2007) Comparative study of biosorption of heavy metals using different types of algae. Bioresour Technol 98:3344–3353.
https://doi.org/10.1016/j.biortech.2006.09.026
A
Schrenk D, Bignami M, Bodin L et al (2022) Assessment of information as regards the toxicity of fumonisins for pigs, poultry and horses. EFSA J 20:1–26.
https://doi.org/10.2903/j.efsa.2022.7534
Šegvić M, Pepeljnjak S (2001) Fumonisins and their effects on animal health - A brief review. Vet Arh 71:1–25
Shi H, Li S, Bai Y et al (2018) Mycotoxin contamination of food and feed in China: Occurrence, detection techniques, toxicological effects and advances in mitigation technologies. Food Control 91:202–215. https://doi.org/10.1016/j.foodcont.2018.03.036
Simonich MT, Egner PA, Roebuck BD et al (2007) Natural chlorophyll inhibits aflatoxin B1-induced multi-organ carcinogenesis in the rat. Carcinogenesis 28:1294–1302. https://doi.org/10.1093/carcin/bgm027
Smith GW (2018) Fumonisins. In: Gupta R (ed) Veterinary Toxicology, 3rd edn. Elsevier, Amsterdam, pp 1003–1018
Sun Z, Song A, Wang B et al (2018) Adsorption behaviors of aflatoxin B1 and zearalenone by organo-rectorite modified with quaternary ammonium salts. J Mol Liq 264:645–651. https://doi.org/10.1016/j.molliq.2018.05.091
Tsiouris V, Tassis P, Raj J et al (2021) Investigation of a Novel Multicomponent Mycotoxin Detoxifying Agent in Amelioration of Mycotoxicosis Induced by Aflatoxin-B1 and Ochratoxin A in Broiler Chicks. Toxins (Basel) 13:367. https://doi.org/10.3390/toxins13060367
Vila-Donat P, Marín S, Sanchis V, Ramos AJ (2018) A review of the mycotoxin adsorbing agents, with an emphasis on their multi-binding capacity, for animal feed decontamination. Food Chem Toxicol 114:246–259. https://doi.org/10.1016/j.fct.2018.02.044
Wang Q, Zhang S, Li Z et al (2023) Design of hyper-cross-linked polymers with tunable polarity for effective preconcentration of aflatoxins in grain. Chem Eng J 453:139544. https://doi.org/10.1016/j.cej.2022.139544
Xu M, Wang J, Zhang L et al (2022a) Construction of hydrophilic hypercrosslinked polymer based on natural kaempferol for highly effective extraction of 5-nitroimidazoles in environmental water, honey and fish samples. J Hazard Mater 429:128288. https://doi.org/10.1016/j.jhazmat.2022.128288
Xu R, Kiarie EG, Yiannikouris A et al (2022b) Nutritional impact of mycotoxins in food animal production and strategies for mitigation. J Anim Sci Biotechnol 13:69–88. https://doi.org/10.1186/s40104-022-00714-2
Xu R, Yiannikouris A, Shandilya UK, Karrow NA (2023) Comparative Assessment of Different Yeast Cell Wall-Based Mycotoxin Adsorbents Using a Model- and Bioassay-Based In Vitro Approach. Toxins (Basel) 15:104. https://doi.org/10.3390/toxins15020104
Yadavalli R, Valluru P, Raj R et al (2023) Biological detoxification of mycotoxins: Emphasizing the role of algae. Algal Res 71:103039. https://doi.org/10.1016/j.algal.2023.103039
Yang C, Song G, Lim W (2020) Effects of mycotoxin-contaminated feed on farm animals. J Hazard Mater 389:122087. https://doi.org/10.1016/j.jhazmat.2020.122087
Yiannikouris A, André G, Poughon L et al (2006) Chemical and Conformational Study of the Interactions Involved in Mycotoxin Complexation with β-d-Glucans. Biomacromolecules 7:1147–1155. https://doi.org/10.1021/bm050968t
Yiannikouris A, François J, Poughon L et al (2004) Influence of pH on Complexing of Model β-d-Glucans with Zearalenone. J Food Prot 67:2741–2746. https://doi.org/10.4315/0362-028X-67.12.2741
Figure 1
Figure 2
Supplementary material
In vitro adsorption of Fumonisin B1 by multiple algae-modified clay formulations
Letícia Aliberti Galego Alves da Silvaa, Morgane Malardb, Patricia Aparecida de Campos Bragaa, Adriana Pavesi Arissetto Bragottoa, Marie Gallissotb, Pi Nyvall Collenb, Juliana Buenoc, Liliana de Oliveira Rochaa,*
a State University of Campinas (UNICAMP), Food Engineering School (FEA), Department of Food Science and Nutrition (DECAN), Campinas, São Paulo, Brazil (leticia.aliberti@hotmail.com; pbraga@unicamp.br; pavesi@unicamp.br; lrocha@unicamp.br).
b Olmix Group, Bréhan, France (mmalard@olmix.com; mariegalissot@hotmail.com; pnyvall@olmix.com)
c Olmix Group, Piracicaba, Brazil (jbueno@olmix.com).
*Corresponding author: Rocha, L. O. Department of Food Science and Nutrition (DECAN), Food Engineering Faculty (FEA), State University of Campinas (UNICAMP), Monteiro Lobato Street, 80, Campinas, São Paulo, Brazil, 13083- 862. E-mail: lrocha@unicamp.br.