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Article

Water–Organic Solvent Extraction of Phenolic Antioxidants from Brewers’ Spent Grain

by
Antonio Zuorro
,
Annalaura Iannone
and
Roberto Lavecchia
*
Department of Chemical Engineering, Materials and Environment, Sapienza University, 00185 Rome, Italy
*
Author to whom correspondence should be addressed.
Processes 2019, 7(3), 126; https://doi.org/10.3390/pr7030126
Submission received: 7 January 2019 / Revised: 15 February 2019 / Accepted: 18 February 2019 / Published: 1 March 2019
(This article belongs to the Special Issue Green Separation and Extraction Processes)
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Abstract

:
Brewers’ spent grain (BSG) is the most abundant by-product of the brewing process. BSG is currently disposed of or used as a supplement for animal feed, although it contains significant amounts of bioactive compounds of great interest to the pharmaceutical, cosmetic and food sectors. In this study we investigate the feasibility of using a simple solvent extraction procedure to recover phenolic antioxidants from BSG. Acetone–water and ethanol–water mixtures were used as extraction solvents. Phenolic extracts obtained by treatment of BSG with the two solvent systems were characterized in terms of total phenolics and antioxidant activity. For both systems, the extraction yield was maximum at 60% (v/v) organic solvent concentration. At all solvent compositions, mixtures containing acetone provided higher extraction yields. As suggested by the strong correlation between the antioxidant activity of BSG extracts and their phenolic content, the antioxidant capacity of the extracts can be mainly attributed to polyphenols. Overall, the obtained results strongly support the exploitation of BSG as a source of phenolic antioxidants and the possibility of recovering them by a mild and green extraction process.

1. Introduction

Beer is the oldest and most consumed alcoholic beverage in the world. The annual world production of beer is estimated to around 1.8 billion hectoliters, with an average per capita consumption of about 27 L/year [1]. The beverage is usually obtained by fermentation of malted barley, although other types of cereals, such as wheat, rice, corn, spelt and oats, are suitable for its production [2].
From the brewing process, large amounts of solid by-products, including surplus yeast, spent hops and brewers’ spent grain (BSG), are generated. BSG is the most abundant by-product, representing about 85% of the total solid waste [3].
The world production of BSG has been estimated to be on the order of 40 million tons per year [4]. This waste consists primarily of barley grain husks, with minor fractions of pericarp and seed coat layer fragments. Its specific chemical composition depends on several factors, including barley variety, harvest time, malting conditions and the type of adjuncts used in the brewing process [5]. Basically, BSG is a lignocellulosic material, with fiber (cellulose and hemicellulose), protein and lignin being the major constituents. On a dry basis, fiber amounts to about 50% of total weight, while proteins can reach up to 25% [6]. Essential amino acids represent approximately 30% of the total protein content, with lysine being the most abundant (14.3%) [4]. The presence of large amounts of lysine is a peculiarity of barley grain, as most cereals are deficient in this amino acid. For this reason, this waste material is mainly used as protein supplements for animal feed. However, BSG is also a rich source of important bioactive compounds [7]. In particular, phenolic compounds can be present in an amount of up to 8 mg/g [3]. The high levels of phenolic compounds in BSG can be explained by the fact that, during the development of barley seeds, these compounds are specifically accumulated in the grain husk. Ferulic and p-coumaric acids are the main phenolics, followed by caffeic, sinapic and syringic acids [8]. In addition to being powerful antioxidants, these compounds exhibit anti-inflammatory and anti-carcinogenic activities [9], thus supporting the use of BSG as a raw material for the recovery of valuable bioactive phenolics.
In most cases, solid–liquid extraction can be advantageously used for the recovery of natural compounds from untreated or pretreated biomass materials [10,11,12,13]. A large number of studies indicate that the extraction yields and the properties of the recovered compounds are significantly dependent on the structural and compositional features of the plant matrix, the type of compounds and the strength with which they are bound to the matrix [14,15,16]. As a result, a deep knowledge of the characteristics of the system under investigation is required. Furthermore, the process conditions should be carefully controlled in order to maximize the recovery of bioactives while preserving their functional properties. However, a review of the literature shows that, contrary to other polyphenol-containing materials, scarce attention has so far been paid to the recovery of phenolic compounds from BSG [17,18].
In this study we investigate the recovery of phenolic compounds from BSG using two water–organic solvent mixtures: acetone–water and ethanol–water. The main purpose of the study was to compare the extraction yields obtained with the two solvent systems and evaluate the antioxidant activity of the resulting extracts. In addition, we wanted to provide a physical interpretation of the results in terms of solute–solvent affinity. To this end, we used the Hansen solubility parameter (HSP) theory, which is briefly outlined in Appendix A. According to this theory, the affinity between a solute and a solvent can be described by considering three main contributions to the total cohesive energy: the dispersion, the polarity and the hydrogen bonding energies. HSP theory was initially developed in the field of paints and coatings to provide a rigorous tool for the selection of paint components [19]. Subsequently, it was used to describe many other phenomena, such as partial miscibility of liquids, pigment deposition on solid surfaces and the interaction of a drug with excipients or carriers in solid dispersions [20].

2. Materials and Methods

2.1. Chemicals and Waste Material

Acetone, ethanol, methanol, sodium carbonate and hydrochloric acid (37%) were purchased from Carlo Erba (Milan, Italy). Gallic acid (3,4,5-trihydroxybenzoic acid), Trolox (6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid), DPPH (2,2-diphenyl-1-picrylhydrazyl) and the Folin–Ciocalteu reagent were obtained from Sigma-Aldrich (Milan, Italy). All chemicals were used as received.
BSG was provided by a brewery in the Province of Rome (Italy). As soon as received, the material was dried to a final moisture content <3% in a forced-air dehydrator (Stöckli, Switzerland) at 50 °C, ground in an electric mill (Moulinex, Ecully, France) to a particle size less than 0.5 mm and stored in the dark at room temperature until use.

2.2. Analytical Methods

Moisture measurements were made by oven drying at 105 °C. The initial phenolic content of BSG was determined by solid‒liquid extraction under agitation, as described in [21]. This method allows for achieving a nearly complete removal of phenolic compounds from the plant material through four extraction stages. In each stage the temperature was kept to 60 °C, the extraction time was 1 h and aqueous acetone (60% v/v) was used as the solvent. The liquid-to-solid ratio was equal to 20, 10, 5 or 5 mL g−1.
Total phenolics were determined by the Folin–Ciocalteu method following the procedure reported elsewhere [22]. Briefly, 200 μL of the sample, 150 μL of Folin–Ciocalteu’s reagent and 5 mL of 0.1 M HCl were put into a glass tube. Then, a 20% w/v Na2CO3 solution was added to a final volume of 10 mL. The tube was kept in the dark at room temperature for 1 h. Finally, the absorbance at 525 nm was measured. The results were expressed as gallic acid equivalents (GAE) using a calibration curve obtained with gallic acid standards between 0.02 and 0.3 g L−1 (Figure S1).
Antioxidant activity was determined by the DPPH method according to Maietta et al. [23]. A work solution of DPPH in methanol at a concentration of 0.05 g L−1 (1.2 10−4 M) was initially prepared. Then, a suitable amount of the sample to be assayed (100–300 μL) was poured into an optical glass cuvette and the DPPH solution was added to obtain a final volume of 4 mL. The cuvette was incubated in the dark at room temperature for 30 min. Finally, the absorbance of the solution at 517 nm was measured against methanol. The antioxidant activity of the sample was evaluated from the values of the initial and final absorbance as 100·(A0–Af)/Af. The results were expressed as Trolox equivalents (TE) using a calibration curve obtained with Trolox standards between 2 and 10 mg L−1 (Figure S2).
Optical measurements were made on a double-beam UV-Vis spectrophotometer (UV-2700, Shimadzu, Kyoto, Japan).

2.3. Extraction Procedure

Batch extraction experiments were carried out in screw-capped sealed glass flasks equipped with a magnetic bar. The flasks were placed in a water bath at 60 ± 0.1 °C. Then, 20 mL of water–organic solvent mixture of the desired composition (0, 20, 40, 60, 80, 100% v/v) and 1 g of BSG were put into the flasks and stirred at 400 rpm for 60 min. After this time, the flasks were rapidly quenched under tap water and an aliquot of the suspension was centrifuged at 7000 × g for 5 min. Finally, the supernatant liquid was removed and assayed for total phenolics and antioxidant activity.

2.4. Statistical Analysis

Extraction experiments were carried out in duplicate, while analytical measurements were repeated at least three times. All results were expressed as mean ± standard deviations. The values of the coefficient of variation (standard deviation over mean) were always <4%. Statistical analysis was performed using Microsoft Excel 2010.

3. Results

3.1. Extraction of Phenolic Compounds

The initial moisture content of BSG was 79.8 ± 0.4 wt % and was reduced to 2.8 ± 0.1 wt % after drying. The overall phenolic content, as determined by the four-stage extraction procedure, was 4.126 mg GAE g−1. About 90% of the total amount of phenolic compounds was recovered in the first two stages and less than 2% in the fourth stage (Figure 1).
Experiments aimed at assessing the effects of solvent type and composition on the amount of recovered phenolics gave the results listed in Table 1. In the same table, the antioxidant activity of the extracts determined by the DPPH assay are reported. In both solvent systems, the two quantities exhibited a non-monotonic trend with solvent composition, with a maximum at 60% (v/v) acetone or ethanol. From the phenolic content of BSG, the percent extraction yields, defined as the ratio between the amount of recovered phenolic compounds and the total amount of the same compounds, was obtained (Figure 2).
At every solvent composition, systems containing acetone resulted in higher yields compared to ethanol–water. At the optimum composition (60% v/v), the percent extraction yields in aqueous acetone and ethanol were equal to 70.6% and 50.9%, respectively. The corresponding antioxidant activities of the extracts were 1.28 and 0.85 mg TE g−1.
For both solvent systems, a sharp linear dependence (R2 > 0.9) was observed when the antioxidant activity of the extracts was plotted against the concentration of phenolic compounds (Figure 3).

3.2. Analysis of HSPs

HSPs were used to estimate the affinity of phenolic compounds for the investigated solvents. Three of the major phenolics present in BSG, that is, ferulic, caffeic and p-coumaric acids, were selected as representatives of the whole class of phenolic compounds in this material (Figure 4). Their partial solubility parameters (δD, δP, δH) were calculated from Equations (A5)–(A7) using the group contribution values reported in [24]. Then, the total solubility parameter (δT) was determined from Equation (2). The molar volumes were estimated by the group contribution method of Fedors [25]. The results are presented in Table 2.
Hansen solubility parameters and molar volumes of solvent components (water, acetone and ethanol) were taken from the literature [26]. HSPs of mixed solvents (δmix) were determined from Equation (A8).
Finally, the solubility parameter distance (R) for the three phenolic compounds in the acetone–water and ethanol–water mixtures was calculated using Equation (4), leading to the results displayed in Figure 5.

4. Discussion

The results presented here indicate that BSG is a good source of phenolic compounds, their total amount being on the order of 4 mg GAE per g of dry waste. For comparison, a value of 4.61 mg g−1 was obtained by Szwajgier et al. [27] using ferulic acid esterase from Lactobacillus acidophilus to favor the release of phenolic compounds from BSG. Meneses et al. [17] evaluated the effect of different solvents on the extraction of phenolics from BSG and recovered 3.59 mg g−1 (pure water) to 9.9 mg g−1 (aqueous acetone) of total phenolic compounds. In another study by Socaci et al. [18], the amount of recovered phenolic compounds ranged from 0.41 mg g−1 (pure ethanol) to 1.14 mg g−1 (aqueous acetone). Although these values are, on average, lower than those found in other fruit or vegetable wastes, such as apple and berry fruit peels [28,29] or spent coffee grounds [30], the large availability throughout the year of BSG at low or no cost makes it a promising raw material for the recovery of phenolic compounds. It should also be considered that the levels of these compounds are highly dependent on barley variety and growth conditions and could be increased through appropriate cultivation practices. Interestingly, as attested by the strong correlation between phenolic content and antioxidant activity, this class of compounds seems to be the main one responsible for the antioxidant properties of BSG extracts.
Regarding the influence of solvent type and composition on the extraction yields, from Figure 2 it can be seen that aqueous mixtures containing 60% v/v organic solvent were the most effective. Of the two organic solvents, acetone provided a higher recovery of phenolic compounds over the entire solvent composition range. Similar results were obtained in other studies on BSG [17,18] or different plant materials, such as spent coffee grounds [22], artichoke waste [31], mango by-products [32] and beetroot [33].
It is generally agreed that the existence of an optimal solvent composition in aqueous solvents is due to the fact that phenolic compounds exhibit a wide range of solubilities in single mixture components and are often more soluble in solvents less polar than water [22,34]. Thus, the observed differences in the extraction efficiencies by the two solvent systems can be primarily ascribed to differences in their affinity for the phenolic compounds present in BSG. An estimation of the contribution of affinity to the overall extraction yield can be made by comparing the Hansen solubility parameters of the solutes with those of the solvent. To this end, ferulic acid, p-coumaric acid and caffeic acid were selected as representatives of the whole class of BSG phenolics [27]. During plant development, these and other phenolic compounds accumulate in the husk of barley grain, where ferulic acid, accounting for approximately 68% of total phenolics, reaches concentrations from about 150 μg g−1 to over 400 μg g−1 [35].
As can be seen in Figure 5, the solubility parameter distance for the three phenolic compounds in aqueous acetone was generally lower than that in aqueous ethanol, suggesting that they have a higher affinity for acetone than for ethanol. Furthermore, in acetone–water mixtures, R exhibited a non-monotonic trend with the organic solvent concentration and a minimum located approximately between 60% and 80% (v/v) appeared. This behavior indicates that the solubility parameters of solute and solvent exhibit a different dependence on the composition of the mixture and that at a certain composition they become very close to each other, leading to the observed minimum. However, an examination of the results displayed in Figure 2 and Figure 5 reveals that the affinity of phenolic compounds for the solvent cannot completely explain the observed dependence of extraction yields on mixture type and composition. This is particularly true for the ethanol–water system, as the solubility parameter distance of the three phenolic compounds decreases monotonically with the concentration of ethanol in the mixture. On the other hand, it should be considered that the extraction of a natural substance from a plant material is a very complex heterogeneous process involving different steps, such as the penetration of solvent molecules in the plant matrix, the breakage of solute–matrix interactions and the solubilization of the solute. Therefore, in addition to affinity, factors related to the other process steps should be considered.
In cereal grains, phenolic compounds are mainly located in the pericarp, which constitutes the outermost part of the grain [36]. As a result, the solvent molecules must penetrate the cell walls of the plant tissue before reaching the solutes. Plant cell walls are composite three-dimensional structures containing cellulose, hemicellulose and pectin as major polysaccharide components [37]. Small amounts of proteins with a structural or functional role are also present. Cellulose is organized in microfibrils with a diameter of 2–10 nm composed of well-packed hydrogen-bonded stretches of crystalline cellulose and less ordered amorphous regions. These cellulose microfibrils are assembled into fibers of larger diameter cross-linked by hemicelluloses and embedded in a gel-like matrix of pectic polysaccharides [38].
Plant tissue is poorly permeable to the solvent, but its compactness can be reduced by swelling. This phenomenon originates from the adsorption of polar solvent molecules on the hydroxyl and carboxyl groups of cellulose fibers [22]. Following adsorption, the distances between the fibers increase, causing expansion of the material and thus increasing the penetration of the solvent into the plant tissue [22]. Swelling by protic solvents, such as water and ethanol, occurs mainly within the amorphous region of cellulose [39], leading to an appreciable disruption of the strong hydrogen bonded network. In contrast, swelling by aprotic solvents, such as acetone, depends more on solvent‒cellulose dipolar interactions [40]. Due to its small molar volume and high hydrogen bonding capability, water is a powerful swelling agent, which supports its key role in the recovery of phenolic compounds from BSG and other plant materials. It can therefore be hypothesized that the observed optimum in the extraction yields at 60% (v/v) solvent composition is the result of two main factors: affinity of phenolic compounds for solvent components and solvent effects related to the swelling of the plant tissue. As for the second factor, water can be expected to play the major role due to its high swelling capacity.
However, other solvent-related factors may also contribute to the observed behavior. For example, it is known that phenolic compounds in cereals can be either in free or bound forms [41]. Bound phenolic compounds are ester- or ether-linked to cell wall polysaccharides [42]. Solvent components can promote the breakage of these bonds, favoring the release of phenolic compounds. Finally, organic solvents like acetone and ethanol may also cause protein denaturation [43]. The underlying mechanisms are complex and only partially elucidated, as an organic solvent may affect different types of the interactions responsible for protein stability, such as the electrostatic, hydrogen bonding and hydrophobic ones. The resulting effects are solvent- and protein-specific, and usually increase with the organic solvent concentration. Since BSG has a high protein content, up to 25% on a dry weight basis [6], denaturation of structural proteins by solvent components can be expected to contribute to weakening and loosening the cell-wall structure, improving the penetration of solvent molecules and the recovery of phenolic compounds.

5. Conclusions

The results of this study indicate that BSG is a potentially valuable source of phenolic antioxidants that could be easily recovered by extraction with aqueous organic solvents. We have also shown that an optimal solvent composition exists that maximizes the extraction yields and is likely the result of different solvent-related effects.
Like other agro-industrial waste, the characteristics of BSG can vary both with the type of raw materials used and the process conditions. Therefore, further research should be devoted to investigating other types of BSG and characterizing the phenolic extracts obtained. A deeper insight into the role of solvent components in the recovery of phenolic components should also be gained in future studies.

Supplementary Materials

The following are available online at https://www.mdpi.com/2227-9717/7/3/126/s1, Figure S1: Figure S1. Calibration curves for evaluation of total phenolics, Figure S2: Calibration curves for evaluation of DPPH antioxidant activity.

Author Contributions

A.Z. designed the experiments, analyzed the data and wrote the paper; A.I. performed the experiments; R.L. contributed to the design of experiments, interpreted the data and wrote the paper.

Funding

This research was partially supported by grants from Sapienza University of Rome (Italy).

Conflicts of Interest

The authors declare no conflict of interest.

Appendix A. HSP Theory

The classic solubility theory developed by Hildebrand and Scott [44] states that the solubility parameter of a substance (δ) can be expressed as the square root of the cohesive energy density:
δ = Δ E v m ,
where ΔE is the cohesive energy and vm is the molar volume.
Hansen proposed to evaluate the total cohesive energy as the sum of three contributions: the dispersion energy (related to the Van der Waals forces), the polarity energy (related to permanent dipoles) and the hydrogen bonding energy [26]. Accordingly, the total solubility parameter (δT) can be determined from the three individual parameters as follows:
δ T 2 = δ D 2 + δ P 2 + δ H 2 ,
where δD, δP and δH represent the dispersion, the polar and the hydrogen-bonding solubility parameters.
The affinity of a solute for a solvent can therefore be evaluated by comparing the values of the corresponding total solubility parameters. In particular, the closer the two parameters, the higher the solubility of the solute in that solvent. In Hansen space, the distance (dAB) between the points representing the solute (δD,A, δP,A, δH,A) and the solvent (δD,B, δP,B, δH,B), calculated as:
d A B = ( δ D , A − δ D , B ) 2 + ( δ P , A − δ P , B ) 2 + ( δ H , A − δ H , B ) 2 ,
which provides a measure of the solute–solvent affinity.
Some authors suggested that good miscibility is achieved if d ≤ 5 MPa0.5 [45]. However, Hansen and Skaarup [46] proposed to modify the above equation by defining the solubility parameter distance (R) between the two components as:
R = 4 ( δ D , A − δ D , B ) 2 + ( δ P , A − δ P , B ) 2 + ( δ H , A − δ H , B ) 2 ,
Small R-values indicate a high solubility of A in B, as the interaction forces acting between the molecules of the two components are similar.
Hoftyzer and van Krevelen developed a group contribution method to estimate the partial solubility parameters of polymers and pure organic compounds. They provided the following equations [24]:
δ D = ∑ F D , i v m
δ P = ∑ F P , i 2 v m
δ H = ∑ E H , i v m ,
where FD,i, FP,i and FH,i are the group contributions to individual solubility parameters and vm is the molar volume of the substance.
Finally, in the case of multicomponent solvents, the HSPs of the solvent (δmix) can be determined as follows:
δ m i x = ∑ i φ i δ i ,
where φi is the volume fraction of the i-th component in the solvent mixture and δi is the partial or total HSP of that component.

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Figure 1. Amount of recovered phenolic compounds per unit weight of dry solid (q) in each extraction stage, with the associated recovery percentages.
Figure 1. Amount of recovered phenolic compounds per unit weight of dry solid (q) in each extraction stage, with the associated recovery percentages.
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Figure 2. Percent phenolic extraction yields in water–organic solvent mixtures.
Figure 2. Percent phenolic extraction yields in water–organic solvent mixtures.
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Figure 3. Antioxidant activity (AA) of BSG extracts against total phenolic compounds concentration (c) in water–organic solvent systems.
Figure 3. Antioxidant activity (AA) of BSG extracts against total phenolic compounds concentration (c) in water–organic solvent systems.
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Figure 4. Molecular structures of the three major phenolic compounds in BSG.
Figure 4. Molecular structures of the three major phenolic compounds in BSG.
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Figure 5. Hansen solubility parameter distance (R) of ferulic, p-coumaric and caffeic acids in water–organic solvent mixtures.
Figure 5. Hansen solubility parameter distance (R) of ferulic, p-coumaric and caffeic acids in water–organic solvent mixtures.
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Table
Table 1. Concentration of phenolic compounds (c) and antioxidant activity (AA) of water–organic solvent extracts from brewers’ spent grain (BSG). Data are expressed as mean ± standard deviation (n = 3).
Table 1. Concentration of phenolic compounds (c) and antioxidant activity (AA) of water–organic solvent extracts from brewers’ spent grain (BSG). Data are expressed as mean ± standard deviation (n = 3).
Solventv/v (%)c (mg GAE/L)AA (mg TE/L)
Water1000.013 ± 0.0020.011 ± 0.001
Acetone200.073 ± 0.0030.034 ± 0.003
400.101 ± 0.0060.051 ± 0.003
600.160 ± 0.0050.064 ± 0.005
800.091 ± 0.0040.048 ± 0.004
1000.022 ± 0.0010.017 ± 0.002
Ethanol200.034 ± 0.0020.019 ± 0.003
400.083 ± 0.0040.029 ± 0.003
600.106 ± 0.0050.043 ± 0.005
800.067 ± 0.0040.033 ± 0.004
1000.023 ± 0.0020.019 ± 0.003
Table
Table 2. Molecular properties and Hansen solubility parameters of solvent components (MW: molecular weight; MV: molar volume; δi: Hansen solubility parameters).
Table 2. Molecular properties and Hansen solubility parameters of solvent components (MW: molecular weight; MV: molar volume; δi: Hansen solubility parameters).
CompoundMW
(Da)		MV
(cm3/mol)		δD
(MPa0.5)		δP
(MPa0.5)		δH
(MPa0.5)		δT
(MPa0.5)
Water18.0118.0215.51642.347.8
Acetone58.0873.4015.510.47.019.9
Ethanol46.0758.6815.88.819.426.5
Ferulic acid194.19136.222.75.715.628.1
Caffeic acid180.16108.925.510.021.434.8
p-Coumaric acid164.16117.920.45.616.026.5

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Zuorro, A.; Iannone, A.; Lavecchia, R. Water–Organic Solvent Extraction of Phenolic Antioxidants from Brewers’ Spent Grain. Processes 2019, 7, 126. https://doi.org/10.3390/pr7030126

AMA Style

Zuorro A, Iannone A, Lavecchia R. Water–Organic Solvent Extraction of Phenolic Antioxidants from Brewers’ Spent Grain. Processes. 2019; 7(3):126. https://doi.org/10.3390/pr7030126

Chicago/Turabian Style

Zuorro, Antonio, Annalaura Iannone, and Roberto Lavecchia. 2019. "Water–Organic Solvent Extraction of Phenolic Antioxidants from Brewers’ Spent Grain" Processes 7, no. 3: 126. https://doi.org/10.3390/pr7030126

APA Style

Zuorro, A., Iannone, A., & Lavecchia, R. (2019). Water–Organic Solvent Extraction of Phenolic Antioxidants from Brewers’ Spent Grain. Processes, 7(3), 126. https://doi.org/10.3390/pr7030126

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