A glutathione (GSH) yeast-based biomass (Saccharomyces cerevisiae) was used to investigate GSH stability, solubilization during gastrointestinal digestion and GSH intestinal transport.
A glutathione (GSH) yeast-based biomass (Saccharomyces cerevisiae) was used to investigate GSH stability, solubilization during gastrointestinal digestion and GSH intestinal transport.
A postgrowing procedure was applied to improve intracellular GSH yeast content. The presence of adenine (ADE) in the biotransformation solution (CYS-GLY-GLU mixture) and alternatively, a glucose shot after 4-h incubation, allowed to obtain cells containing about GSH 1·6–1·7% dcw (dry cell weight) (control 0·5%). Yeast samples were subjected to in vitro gastrointestinal digestion and absorption assays employing Caco-2 and HT29-MTX cell lines in different proportions (100/0, 70/30 and 50/50). Trials were also performed to verify intestinal cell viability.
At least 87% of ingested GSH is available in reduced form for intestinal absorption. In vitro GSH transport assays indicated that GSH is poorly absorbed (<20%). Nevertheless, studies in response to oxidative stress induced by H2O2 demonstrated a protective role of the GSH-enriched biomass towards intestinal cell viability.
An enriched GSH yeast-based biomass has been obtained using a postgrowing procedure. Although GSH present in enriched yeasts is poorly absorbed by intestinal cells, this biomass showed an intestinal local protective effect, improving cells viability when a simulated oxidative stress was applied.
Glutathione (GSH) is a tripeptide consisting of L-glutamate, L-cysteine and glycine. It is found in millimolar concentrations (0·2–10 mmol l−1) in all cells, from prokaryotes to eukaryotes, and is the most abundant low molecular thiol in biological systems (Anderson 1998; Ault and Lawrence 2003; Wen et al. 2005; Wang et al. 2007). Intracellularly, GSH is kept in its thiol form by GSSG reductase, a NADPH-dependent enzyme (Anderson 1998). GSH is committed to many physiological processes; however, its functions may be summarized in three main topics: antioxidant, immunity booster and defence molecule (Li et al. 2004). These characteristics make GSH an important biochemical drug for the treatment for numerous diseases, such as HIV infections, liver cirrhosis, gastrointestinal and pancreatic inflammation, as well as neurodegenerative diseases (Townsend et al. 2003; Li et al. 2004). Cellular GSH concentration is markedly reduced in response to protein malnutrition, oxidative stress and many pathological conditions such as Crohn's disease, atherosclerosis and diabetes (Li et al. 2004; Wu et al. 2004). Moreover, studies evidenced that GSH may be therapeutically effective when given in high doses to depleted subjects (Perricone et al. 2009).
Currently, Saccharomyces cerevisiae and Candida utilis are the most commonly used micro-organisms for GSH fermentative production on industrial scale, with a GSH content of 0·1–1% dcw (dry cell weight) (Li et al. 2004). They are rich sources of protein, soluble fibre, minerals (Ca, P, K, Mg, Cu, Fe, Zn, Mn and Cr) and B vitamins, often recommended as a dietary supplement (Yamada and Sgarbieri 2005; Bekatorou et al. 2006). In previous reports (Rollini et al. 2011; Musatti et al. 2013), we focused on the set-up of a postgrowing procedure (biotransformation) for GSH accumulation employing commercial baker's yeast (S. cerevisiae), while most of the published papers concentrated on GSH accumulation in growing cells (Li et al. 2004; Wen et al. 2005; Wei et al. 2008; Liang et al. 2009; Nisamedtinov et al. 2010). The use of a postgrowing procedure employing commercial baker's yeast, a low cost cell source available on the market, represents an alternative strategy to traditional GSH accumulation inside yeast cell, easy and feasible for an industrial up-scale, in particular for nutraceutical applications.
To design an adequate dietary supplementation, it is necessary to evaluate whether a supplement remains intact after the digestion processes and whether it is absorbed by the epithelium to reach the systemic circulation. The in vitro combination of a simulated gastrointestinal digestion and a cellular model of intestinal epithelium to emulate absorption has been demonstrated useful to evaluate the aspects related to the processes of solubilization and absorption of a compound in the gastrointestinal tract, and hence to study the bioavailability (Au and Reddy 2000). The term ‘bioavailability’ refers to the fraction of an ingested compound that is solubilized during gastrointestinal digestion and reaches the systemic circulation (Calatayud et al. 2010). Cellular models derived from colorectal cancers (Caco-2 and HT29-MTX) have provided a useful tool for these studies. These cell types have conserved parts of the programme of epithelial differentiation, expressing many genes of differentiated intestinal epithelial cells and maintaining in turn, the ability to form monolayers of polarized cells once they have reached confluence in culture (Hidalgo et al. 1989; Lesuffleur et al. 1990).
GSH bioavailability has been studied in vivo by several authors but up to now with discordant results. Hagen et al. (1990) and Rahman and MacNee (1992) affirmed that plasma GSH concentration in rats increased from approximately 15 to 30 μmol l−1 after oral GSH administration, indicating that oral supplementation may be useful to enhance GSH tissue availability. Likewise, Aw et al. (1991) reported that in mice oral GSH intake can increase GSH concentrations in several tissues following its depletion. On the contrary, Witschi et al. (1992) reported that in humans, systemic GSH availability is negligible, and it is not possible to increase circulating GSH to a clinical beneficial extent by an oral administration of a single dose of 3 g.
This study was aimed at obtaining a GSH-enriched S. cerevisiae biomass and investigating GSH solubilization and stability during gastrointestinal digestion. GSH absorption by intestinal epithelium in vitro models was also analysed, and trials were also performed to verify whether GSH supplementation may be a useful strategy to improve intestinal cell viability.
Samples of commercial baker's yeast (Saccharomyces cerevisiae) in compressed form, identified as Fala (Lesaffre, Trecasali-Parma, Italy), were employed. Fresh yeast cells (i.e. 1 day of storage time) were suspended (5% dcw) in 10 ml of a biotransformation solution (identified as CYS-GLY-GLU mixture) containing the three GSH precursor amino acids and the following compounds (g l−1): glucose 80, sodium citrate 10, ammonium sulfate 7, monobasic potassium phosphate 3·5, magnesium sulfate 0·5, cysteine 4, glycine 4 and glutamic acid 4. The reaction mixture was incubated at 28°C and 200 rev min−1. CYS-GLY-GLU mixture alone or added with adenine (ADE, 0·5 g l−1), adenosine (ADO, 1·5 g l−1), dithiothreitol (DTT, 3 g l−1) or a combination of ADO/DTT or ADE/DTT were tested, as well as a further glucose (50 g l−1), after 4-h incubation with CYS-GLY-GLU mixture with or without ADE (Table 1). Aliquots were collected at the beginning and after 24-h incubation and then analysed for intracellular GSH contents.
|(2) + ADO||1·5||–||–||–|
|(3) + DTT||–||3·0||–||–|
|(4) + ADE||–||–||0·5||–|
|(5) + ADO + DTT||1·5||3·0||–||–|
|(6) + ADE + DTT||–||3·0||0·5||–|
|(7) control + glu||–||–||–||50|
|(8) + ADE + glu||–||–||0·5||50|
Yeast samples were lyophilized to faithfully reproduce the form usually marketed. Cells were suspended in distilled water (20% dcw), placed in stainless steel trays as a thin layer and then frozen at −40°C for 4 h. Cell dehydration was carried out at 25°C and 1·33 Pa for 30 h in an Minifast MFD 01 lyophilizer (Edwards, Crawley, UK), until a maximum residual humidity of 5–8% was reached.
GSH standard solutions at two different concentrations (40 and 200 mg l−1, equivalent to 0·13–0·65 mmol l−1) were employed for bioaccessibility tests, as well as one GSH-enriched yeast sample obtained from the biotransformation experiments described above (trial 4, GSH 1·63 ± 0·15% dcw), and one commercial baker's yeast in compressed form (control, 0·45 ± 0·05% dcw). Yeast samples were both lyophilized before use.
Cell culture grade water (B. Braun Medical S.A., Spain) was used throughout the in vitro digestion assay. Enzymes and bile salts for in vitro gastrointestinal digestion were all purchased from Sigma: porcine pepsin (enzymatic activity 944 U mg−1 protein), porcine pancreatin (activity equivalent to 4 × US Pharmacopoeia specifications/mg pancreatin) and bile extract (glycine and taurine conjugates of hyodeoxycholic and other bile salts). The study was carried out using the simulated digestion process proposed by Laparra et al. (2003) modified for a yeast biomass.
Samples (1–3 g for yeast biomass, and 40 and 200 mg l−1 for GSH solutions) were weighed, 25 ml of cell culture grade water was added and pH adjusted to 2·0 with 6 mol l−1 HCl. Freshly prepared pepsin solution (10% w v−1 pepsin in 0·1 mol l−1 HCl) was added to provide 2 mg pepsin g−1 sample. Sample was made up to 30 ml with cell culture grade water and incubated in a shaking water bath (120 strokes min−1) at 37°C for 2 h. Gastric digests were then raised up to pH 6·0 by dropwise addition of 1 mol l−1 NaHCO3. The pancreatin-bile extract mixture (0·4% w v−1 pancreatin and 2·5% w v−1 bile extract in 0·1 mol l−1 NaHCO3) was added to provide 0·5 mg pancreatin g−1 sample and 3 mg bile extract g−1 sample, and the incubation at 37°C continued for additional 2 h. After the intestinal digestion step, pH was adjusted to 7·2 by dropwise addition of 0·5 mol l−1 NaOH. Digests were then transferred to polypropylene centrifuge tubes and centrifuged at 10 600 × g for 30 min at 4°C to separate the soluble (bioaccessible) fraction. All trials were performed in triplicate. GSH and GSSG contents were evaluated in the obtained bioaccessible fractions.
GSH transport through the intestinal epithelium was investigated using Caco-2 cell line and cocultures of Caco-2 and HT29-MTX cells. Caco-2 cells were obtained from the European Collection of Cell Cultures (ECACC, number 86010202, Salisbury, UK). Cell maintenance was performed in 75 cm2 flasks to which 10 ml of pH 7·4 Dulbecco's modified Eagle's medium (DMEM) with 4·5 g glucose l−1. DMEM was supplemented with 10% (v v−1) foetal bovine serum, 1% (v v−1) nonessential amino acids, 1 mmol l−1 sodium pyruvate, 10 mmol l−1 HEPES (N-2-hydroxyethylpiperazine-N'-2-ethanesulfonic acid), 100 U penicillin ml−1, 0·1 mg streptomycin ml−1 and 0·0025 mg amphotericin B ml−1 (DMEMc).
HT29-MTX cells were kindly provided by Dr. T. Lesuffleur (Institut National de la Santé et de la Recherche Médicale, INSERM UMR S938, France) (Lesuffleur et al. 1990). Cells maintenance was performed in 25 cm2 flasks to which 5-ml medium were added, consisting of DMEM at pH 7·4 containing 4·5 g glucose l−1 and supplemented with 10% (v v−1) foetal bovine serum, 100 U penicillin ml−1, 0·1 mg streptomycin ml−1, 0·0025 mg amphotericin B ml−1 and 1 mmol l−1 sodium pyruvate (HT-DMEMc).
Both cell lines were incubated at 37°C, 5% CO2 and 95% relative humidity atmosphere, changing the medium every 2–3 days. When cell monolayer reached 80% confluence, cells were detached by mean of a trypsin solution (0·5 mg l−1) containing 0·22 g EDTA l−1 and subsequently reseeded at a density of 5 × 104 cells cm−2. All reagents used were purchased from PAA Laboratories GmbH (Germany).
Throughout the study, Caco-2 cell cultures were used between passages 20 and 35, while HT29-MTX cells were used between passages 40 and 50.
Transport tests were performed in 6-well plates equipped with a polyester membrane porous support (diameter 24 mm, pore size 0·4 μm; Transwell®, Costar Corp, Corning Incorporated, Corning, NY, USA); this insert separates the well into an apical (upper) and a basolateral (lower) compartment. Cells were seeded (5 × 104 cells cm−2) on the apical side to produce monolayers of Caco-2 and of Caco-2/HT29-MTX (70/30 and 50/50 proportions). Subsequently, 1·5-ml medium (DMEMc for Caco-2 and HT-DMEMc for cocultures) was added to the apical chamber and 2 ml to the basolateral one. Cells were incubated at 37°C, 5% CO2 and 95% relative humidity, changing the medium every 2–3 days until cell differentiation was attained (13–15 days postseeding). During cell growth and differentiation in Transwell®, cell monolayer integrity was assessed daily from the sixth postseeding day onward by measuring the transepithelial electrical resistance (TEER) using a Millicell®-ERS (Millipore Corporation, Madrid, Spain).
Transport assays were first performed employing GSH standard solutions (3 and 10 mmol l−1), as follows: 1·5 ml of the standard solution prepared in Hank's balanced salt solution (HBSS, PAA) supplemented with 20 mmol l−1 pH 5·5 o-2-(N-morpholine) ethanesulfonic acid (MES, Sigma, Spain) was added to the apical compartment, and 2 ml of HBSS with 10 mmol l−1 pH 7·2 HEPES to the basolateral compartment. For the evaluation of the apparent permeability coefficients (Papp), at established timepoints (15, 30, 60, 120, 180 and 240 min), 300 μl was removed from the basolateral compartment and replaced with an equal volume of fresh medium (HBSS with 10 mmol l−1 HEPES). GSH determination was carried out in the aliquots obtained at each time point as well as in the apical residual medium collected at the end of the experiment.
As regards the transport studies using bioaccessible fractions resulting from the gastrointestinal digestion, GSH standards (3 and 10 mmol l−1) or GSH-enriched yeast samples were employed. These samples were first inactivated by heating for 4 min at 100°C to inhibit protease activities and then cooled by immersion in an ice bath. Glucose (final concentration 5 mmol l−1, Sigma) was then added to facilitate cell viability. If necessary, NaCl (10 mmol l−1, Panreac) was used to adjust the osmolarity to 310 ± 10 mOsm kg−1 using a freezing point osmometer (Automatic Micro-Osmometer Type 15 Löser, Löser Messtechnik, Germany). Aliquots of 1·5 ml of the inactivated bioaccessible fraction supplemented with 20 mmol l−1 pH 5·5 MES was added to the apical chamber and 2 ml of HBSS supplemented with 10 mmol l−1 pH 7·2 HEPES to the basolateral compartment.
The apparent permeability coefficients (Papp) were calculated from Equation 1:
Besides the calculation of the apparent permeability, the rate of transport of bioaccessible fractions of GSH standards (3 and 10 mmol l−1) and GSH-enriched yeasts was also evaluated, performing transport assays for 2 h, without taking aliquots at different timepoints. For quantification of GSH transport, GSH contents were determined in the acceptor (apical) and donor (basolateral) medium collected at the end of the experiment. The percentages of transport to the basolateral compartment were calculated with respect to the initial quantity of GSH added.
During GSH cell transport trials, cell monolayer integrity was evaluated by measuring: (i) TEER at several incubation times, including the start and end of the experiment, and (ii) Papp of the paracellular transport marker lucifer yellow (LY), added at 100 μmol l−1 concentration to the apical compartment in the control and in GSH treated cells. Fluorescence of LY transported to the basolateral compartment was measured with a fluorescence microplate reader (PolarSTAR OPTIMA, BMG-Labtech, Ortenberg, Germany) at excitation/emission wavelengths of 485/520 nm. To evaluate any possible interactions of LY with GSH uptake and transport, parallel experiments were performed with and without paracellular marker, which demonstrated the absence of interferences. The limits established for considering that the cell monolayer integrity was maintained were as follows: TEER between 80% and 120% with respect to the control; LY Papp ≤0·5 × 10−6 cm s−1.
Cell viability assays were performed employing sodium resazurin (7-hydroxy-3H-phenoxazin-3-one-10-oxide sodium salt, Sigma). The assay is based on the ability of viable, metabolically active cells to reduce resazurin to resorufin and dihydroresorufin, measurable by colorimetric methods. This conversion is intracellular, facilitated by mitochondrial, microsomal and cytosolic oxidoreductases (O'Brien et al. 2000; Rocha et al. 2011).
Caco-2 cells were seeded at a density of 6·25 × 104 cells cm−2 in 96-well plates for 5 days and subsequently exposed for 1 h at 37°C to GSH standard solutions (3 and 10 mmol l−1, prepared in HBSS) or GSH-enriched yeast (after in vitro digestion and thermal inactivation). Afterwards, 2, 10 and 20 mmol l−1 H2O2 (Panreac) were added to cells and incubated for further 2 h. Additionally, cells without pretreatment with GSH (solution or enriched yeasts) were exposed to 2, 10 or 20 mmol l−1 H2O2.
After exposure, the medium was withdrawn and 150 μl resazurin solution (10 μg ml−1 in MEM) was added. Well plates were incubated for 2 h at the same conditions. 100 μl for each reaction mixture was transferred to a 96-well plate, and resazurin reduction was measured colorimetrically (570 and 600 nm) using a microplate reader (PolarSTAR OPTIMA).
Determination of intracellular yeast GSH was carried out as reported by Musatti et al. (2013). Briefly, samples were centrifuged (10 600 g, 10 min), and collected cells were washed with distilled water, suspended in 0·5 g ascorbic acid l−1 and then thermally treated at 100°C for 10 min to open cell structure and release GSH. After cooling in ice bath, samples were centrifuged (10 600 g, 10 min) to eliminate cell residues and intracellular GSH of supernatant fractions were determined.
GSH and GSSG identification and quantification were carried out by HPLC (L-7000 System, Merck Hitachi, Darmstadt, Germany) equipped with a UV detector (210 nm), using a Purospher® RP-18 endcapped column (250 × 4 mm, Merck). The elution was performed with 25 mmol l−1 NaH2PO4 (pH 2·8, flow rate 0·3 ml min−1) at 30°C. GSH and GSSG concentrations were calculated with respect to a calibration curve of aqueous standards of GSH and GSSG (5–50 mg l−1). Standard GSH and GSSG were purchased from Sigma, and HPLC-grade water was obtained through a Milli-Q A10 Gradient System (Millipore Corporation, Milano, Italy).
One factor analysis of variance (Microsoft 2003) was applied to detect: (i) differences in the GSH intracellular content (% dcw) among biotransformation solutions, (ii) viability differences of Caco-2 cells. Duncan test was applied to detect means differences among the tested conditions. Differences were considered significant for P < 0·05.
Trials were performed by suspending yeast (5% dcw) in a biotransformation solution containing glucose and the three precursor amino acids involved in GSH synthesis (CYS-GLY-GLU), as previously reported (Rollini et al. 2011). Nevertheless, because GSH biosynthesis is ATP-dependent, some ATP-related molecules were also added for comparison purposes (Liang et al. 2010; Musatti et al. 2013). Direct ATP addition was not chosen due to its high cost; instead, ADE and adenosine (ADO), which can be considered as ATP precursors, were tested. Trials were also performed by adding DTT, an ATPase inhibitor.
As reported in Fig. 1, all tested conditions led to a significant (P < 0·05) GSH increase respect to control samples with only the CYS-GLY-GLU mix (trial 1, GSH level 0·98% dcw). Glucose added was always consumed by the yeast in the first 3- to 4-h incubation, leaving at the end of the reaction a residual concentration of 5 mg glucose l−1 (HPLC detection limit). High GSH level was evidenced in the presence of 0·5 g ADE l−1 (trial 4, GSH 1·63% dcw), with about a 170% increase. The incorporation of ADO, led a limited GSH increase (about 115%, from 0·98 to 1·11% dcw, trial 2). The presence of DTT only inhibited GSH production when ADE was incorporated (trial 6). The addition to the reaction mixture of further 50 g glucose l−1 after 4-h incubation (trial 7, GSH 1·67% dcw) increased intracellular GSH, similarly to what observed when ADE was present in the medium (trial 4). However, glucose addition when ADE was present (trial 8) did not cause further GSH increase.
Trials were first performed employing GSH standard solutions (40 and 200 mg l−1 comparatively). Results related to GSH and GSSG content at the beginning of incubation (to) and after the gastric and intestinal steps are reported in Fig. 2. At the highest concentration (200 mg l−1), a very limited amount of GSH (up to 10%) was oxidized to GSSG, while an oxidation of approximately 25% took place when 40 mg GSH l−1 was used. This oxidation mainly occurred after the intestinal digestion phase and may be due to the temperature (37°C) maintained for 4 h and/or the neutral pH of intestinal stage.
Trials were also performed employing untreated and GSH-enriched yeasts, both in lyophilized form, with a GSH content of 0·5 and 1·6% dcw, respectively. At the beginning of the digestion (t0), about 90% of the total GSH was found bioaccessible and this value increased to 98% at the end of the digestion (data not shown). Previous trials of gastrointestinal digestion on baker's yeast in compressed form (not lyophilized) showed that GSH bioaccessibility was only about 20% (data not shown). Thus, the lyophilization process applied contributed to increase GSH bioaccessibility. It is known that lyophilization process damages yeast cell structure in a way that GSH can be easily released (Musatti et al. 2013).
Gastrointestinal digestion tests produced a very limited GSH oxidation (Fig. 3), up to 13% in the control yeast sample and up to 7% in the case of GSH-enriched yeast. These results confirm what previously evidenced for GSH standard solutions.
In all transport assays performed, the TEER and LY permeability values were maintained within the limits established for considering the integrity of the monolayer to be intact.
The Papp indicates the rate at which a compound passes across the intestinal cell monolayer and is a useful parameter for comparative studies, because values are adjusted by the surface of the monolayer, exposure time and concentration of the used compound. The Papp values obtained after 240 min exposure to GSH standard solutions were as follows: 9·9 × 10–7 cm s−1 for 3 mmol l−1 and 1·2 × 10−6 cm s−1 for 10 mmol l−1. Using cocultures of Caco-2/HT29-MTX (50/50 and 70/30), the Papp values for a 10 mmol l−1 GSH solution were found similar to those obtained in Caco-2 monocultures alone (8·1 × 10−7 and 7·0 × 10−7 cm s−1 for 50/50 and 70/30, respectively).
Table 2 shows the percentage of GSH transported through Caco-2 or coculture monolayers after 120 min exposure to either the bioaccessible fractions of GSH standard solutions (3 and 10 mmol l−1) and of enriched yeast samples (GSH ≈ 3 mmol l−1). Transport rates were generally low (2·2–7·9%) and remained unchanged in presence of yeast. The incorporation of HT29-MTX cells to the monolayer produced a significant GSH transport increase, with values reaching 7% of the GSH initially added, in both standards and yeasts.
|Cell line||Transported GSH (%)|
|Std 3 mmol l−1||Std 10 mmol l−1||Yeast|
|Caco-2||2·16 ± 0·06||2·33 ± 0·18||2·23 ± 0·05|
|Co-culture 70/30||3·25 ± 0·31||3·35 ± 0·33||3·92 ± 0·36|
|Co-culture 50/50||6·96 ± 0·40||7·58 ± 0·25||7·93 ± 0·84|
Trials were performed to elucidate the possible protective role of GSH and GSH-enriched yeast on Caco-2 cell viability exposed to an oxidant (H2O2). As expected, Caco-2 cells viability decreases after H2O2 exposure, and this decrease was found H2O2 concentration-dependent. Figure 4 reports the results obtained by adding GSH-enriched yeast (1 h contact time) before H2O2 addition. For comparison purposes, pretreatments with 3 and 10 mmol l−1 standard GSH solutions were also performed. To be noted that a control test with yeast not containing GSH could not be performed because all S. cerevisiae strains have a physiological GSH content.
Results showed that pretreatment with GSH-enriched yeast reduced intestinal cell death caused by H2O2. Future studies will verify whether lower GSH levels in yeast would furnish the same results here reported and will be aimed at investigating whether other yeast components (i.e. folates) may be involved, in association with GSH, in reducing oxidative stresses.
The yeast Saccharomyces cerevisiae is one of the most studied micro-organisms, widely used in traditional fermentation processes like wine, beer and bread making, but nowadays, it also has numerous applications in other industrial productions such as bioethanol, production of enzymes and is employed as dried-yeast for food supplement (Yamada and Sgarbieri 2005; Bekatorou et al. 2006). It has been shown that the use of yeast favours the bioavailability of certain supplements; for example, selenium bioavailability in a selenium-enriched yeast increases up to 135–165% (approximately 1·5-fold) in terms of tissue selenium content and 105–197% (up to 2-fold) in terms of GPx activity, compared with selenite (Yoshida et al. 1999). The aim of the present study was to obtain S. cerevisiae with a high GSH content for a new food supplement formulation and to investigate the fate of the ingested GSH.
Applying a postgrowing procedure to a commercial baker's yeast, already available on the market, has increased its GSH intracellular content. This procedure represents an alternative strategy easy and feasible for an industrial up-scale, to the traditional growth-related GSH accumulation. Commercial baker's yeast generally has a GSH content of about 0·5% dcw; owing to a biotransformation procedure with CYS-GLY-GLU mixture, a GSH content of about 1% dcw is reached. The addition of adenine to the mixture or glucose, after 4-h incubation, increases GSH content up to 1·7% dcw, a threefold increase respect to the physiological yeast GSH content. The proposed product falls within the description proposed by the Directive 2002/46/EC and the subsequent Regulation 1170/2009 (Commission Regulation 2009). This biomass can be considered as a concentrated source of protein, soluble fibre, minerals and B vitamins as well as a concentrated GSH source. The maximum GSH daily supplementation in Italy, 50 mg, can only be achieved after ingestion of 3 g of the proposed yeast.
Yeast samples were lyophilized to faithfully reproduce the dose form usually marketed. The lyophilization process, as demonstrated in this study, facilitates GSH solubilization during its passage through the gastrointestinal tract, and therefore, increases its availability for further absorption through the intestinal epithelium. In addition, gastrointestinal digestion does not negatively affect GSH levels, only inducing a limited oxidation (7–13%). Therefore, it can be concluded that 87–93% of ingested GSH should be available for its absorption in the reduced form.
There are various in vitro models for evaluating intestinal absorption in humans, although the one that is most widely used is the Caco-2 cell line. This cell line, derived from colon adenocarcinoma, differentiates spontaneously in culture, producing a monolayer of epithelial cells, which shares many of the morphological and functional characteristics of mature enterocytes (Hidalgo et al. 1989). There are studies showing that Caco-2 cells express numerous transporters of the human small intestine, and therefore, they are considered a good model for the evaluation of intestinal transport mechanisms (Maubon et al. 2007). This model is currently the most commonly employed for in vitro study of absorption of pharmaceuticals and nutrients. Numerous studies demonstrate that it is possible to correlate the apparent permeability coefficients obtained in Caco-2 cells with the magnitude of in vivo absorption, although the suitability of this correlation depends on the nature of the transport of the compound. In the present work we took into account the study conducted by Yee (1997), according to which a compound with a Papp in Caco-2 monolayers < 1 × 10−6 cm s−1 has low in vivo absorption (0–20%), one with a Papp between 1 and 10 × 10−6 cm s−1 has moderate in vivo absorption (20–70%) and one with a Papp>10 × 10−6 cm s−1 has high absorption (70–100%).
The Papp values obtained in the present study classify GSH as an element with a low in vivo absorption (<20%) at pH 5·5, typical value of the duodenum. This parameter was not found to be modified when Caco-2/HT29-MTX co-cultures were used, model which more realistically emulates the intestinal wall where both cell types (absorptive cells and mucus secreting cells) coexist in variable proportions depending on the part of the intestinal tract. Furthermore, results indicate that GSH present within an enriched yeast biomass is transported similarly a GSH standard solution.
Although GSH supplementation does not substantially increase its systemic levels, GSH presence was found beneficial towards intestinal cells viability. Especially in a form of an enriched biomass, GSH could protect intestinal cells when these are subjected to oxidative stress, here simulated by the use of H2O2. The results of the present study demonstrate an increase in viability of cells treated with enriched yeasts when a situation of oxidative stress is induced. Gastrointestinal tract is one of the major target for oxidative stress damage due to the constant exposure to diet-derived oxidants, mutagens, and carcinogens as well as to endogenously generated reactive oxygen species (Couto et al. 2012). Thus, ingested GSH may have local protective effect, acting together with GSH coming from the biliary efflux.
This work was partly supported by the Spanish Ministry of Science and Innovation (AGL2009-10100). In order to carry out this study Marta Calatayud received Personnel Training Grants from the Spanish Ministry of Science and Education.
No conflict of interest declared.