Abstract
In recent years, great interest has been shown in pseudocereals for their high nutritional value. Wet milling has been used to obtain macromolecules such as proteins and starches. However, the co-products obtained from this food industry have been studied little. A factorial design Box-benhken was used to study the effect of surfactant concentration (SDS), sodium hydroxide (NaOH) concentration and maceration temperature on structural and colorimetric properties. Structural properties were evaluated by infrared spectroscopy (FTIR-ATR) and color changes by the CIElab tristimulus method (L*, a*, b*). A decrease in temperature and NaOH causes a decrease in lightness (L*), resulting in lower starch content and higher protein content in the co-product. This behavior was correlated with the infrared spectroscopy (FTIR-ATR) spectra. The spectra show a possible structural change in the amylose/amylopectin ratio of the starch granule at 1,012 cmā1, 1,077 cmā1, and 1,150 cmā1 bands, which are associated with glycosidic bonds, these bonds were sensitive to NaOH concentration. While those bands assigned to Amide II (1,563 cmā1) and Amide I (1,633 cmā1), were sensitive to the effect of NaOH and maceration temperature, evidencing that protein content in the co-products is variable and depends significantly on the extraction conditions. The co-products obtained by wet milling could be used in the development of functional foods, such as bread, snacks, pasta and other products.
Introduction
The consumer is currently looking for new products or compounds with high health benefits, therefore, the food industry market is in line with this consumption trend, generating constant changes in the development of new innovative products that meet these needs. The food industry is constantly looking for physical and chemical properties that contribute to improve the quality of these foods, understanding the changes of these properties but improving the functionality of the food (Schoenlechner, 2016; Feine et al., 2019; Giacomini et al., 2019; GarcĆa-Parra et al., 2020). Quinoa originated in South America between Colombia and Chile (GarcĆa-Parra et al., 2021). Evidence has been found that its domestication in Andean peoples dates back to ~3,000ā7,000 B.C. (Bazile et al., 2016; Alandia et al., 2021). This pseudocereal is found at different latitudes and its production can occur under drought conditions (Pulvento et al., 2010; Jacobsen et al., 2012), abiotic stresses (Jacobsen et al., 2003), salinity (Hariadi et al., 2011; Adolf et al., 2013; Shabala et al., 2013), frost (Jacobsen et al., 2005) exhibiting a high tolerance to these environments (Ruiz et al., 2014). These qualities are exploited by breeders in the development of high-yielding cultivars in different regions. Quinoa diversity analyses have been developed under controlled or cold climate conditions and lack information related to grain compositional characteristics (GarcĆa-Parra et al., 2020). Quinoa species show high adaptability to severe edaphoclimatic conditions, mainly related to drastic changes in temperature, salinity stress and lower water and nutrient availability. The high nutritional value of quinoa meets and exceeds that recommended by the World Health Organization (Ruiz et al., 2014). However, its greatest abundance in terms of morphological, ecophysiological, and nutritional diversity occurs in countries such as Ecuador, Bolivia, Peru, and Chile (GarcĆa-Parra et al., 2020, 2021). Alandia et al. (2020), mentioned that this crop was produced in six countries and became a promising crop in more than 120 countries, of which 110 countries produced quinoa ~30 years ago. He also reported that the Andean region covers 76% of world exports with average yields below 1.1 t ha-1. New competitors in the Andean region cover 16% of global exports (Alandia et al., 2021). There is also a report of production in Ontario, Canada to satisfy the great demand, as well as in different parts of India among other countries (Singh, 2011; Mir et al., 2019). However, 74% of world exports are still supplied by Peru and Bolivia (Alandia et al., 2020).
The quinoa has a great nutritional advantage due to its protein and essential amino acid content, but its excellence and importance is not only in the amount of protein but also in its quality. It has been reported that the protein content of these species is between 10 and 20% (KozioÅ, 1992; Abugoch James, 2009; Vega-GĆ”lvez et al., 2010; Nowak et al., 2016; Qin et al., 2018). In recent years, many authors have reported studies related to its techno-functional properties, potential agro-industrial uses and consumption trends (Lamothe et al., 2015; Lopera-Cardona et al., 2016; Guardianelli et al., 2019; Thakur et al., 2019; Nasirpour-Tabrizi et al., 2020). Biological properties have been studied in relation to protein isolate and protein-protein interactions, given the characteristics of quinoa reserve proteins (Haros and Wronkowska, 2016; Gürbüz et al., 2018; Dakhili et al., 2019; Larbi et al., 2019).
Some chronic diseases like hypercholesterolemia, hypertension, diabetes can be prevented with adequate intake of active compounds. These compounds are found in significant amounts in pseudocereals such as quinoa and amaranth. On the other hand, great compositional differences (protein, lipids, fiber, and active compounds) have been reported between quinoa cultivars (Orona-Tamayo and Paredes-López, 2017; GarcĆa-Parra et al., 2020).
Nowadays, there are around 17 cultivars, however, Chenopodium quinoa cv. NariƱo, Chenopodium quinoa cv. Blanca Jericó, Chenopodium quinoa cv. Blanca Soraca. and Chenopodium quinoa cv. Tunkahuan are the species that have created strong (GarcĆa-Parra et al., 2020) interest as an agricultural crop in recent years in Colombia, considering that they exceed in their proximal composition and attributes of quality to different cereals, with a high nutritional value of seeds and leaves.
Wet milling is the technological process used in the corn industry for the extraction of its chemical components. In recent years, this process has been implemented in quinoa in order to obtain starch and coproducts (FernÔndez-López et al., 2020). However, there are few studies on the physicochemical and techno-functional properties of the co-products, especially the protein-starch fraction. Therefore, the objective of this study was to determine the relationship between the extraction conditions and the structural properties of the quinoa co-products obtained by wet milling as a function of temperature and variation of surfactant (SDS) and alkali (NaOH) concentration.
Materials and Methods
Quinoa Grain
Quinoa grain was provided by Seguridad Alimentaria de Occidente SEGALCO SAS (PopayƔn, Colombia) with a moisture content of 10.8% (d.b). They were sieved to remove foreign matter and stored in sealed containers at room temperature prior to use. Analytical grade NaOH from Sigma Chemical Co. (St. Louis, MO, USA) and food grade sodium dodecyl sulfate (SDS) (J.T. Baker Co., Phillipsburg, NJ, USA).
Protein-Starch Fraction by Wet-Milling
The protein and starch fractions of the quinoa grain were extracted by the alkaline method (Xiong et al., 2017; Ballester-SÔnchez et al., 2020) quinoa grains (100 g) were soaked in 300 mL of soaking solution with alkali concentration (0.1, 1.6, and 3.0% w/v NaOH) and surfactant concentration (0.1, 0.5, and 0.9% w/v SDS), during 24 h at temperatures 24, 37, and 51°C. Soaked, and drained grains were milled in a planetary mixer of 1 HP (Luna 20 WSM7L, Waring Commercial, USA) at full speed for 2 min. The homogenate was mixed with 200 mL of alkaline/surfactant solution. Then, 50 mL of the mixture was centrifuged in a centrifuge [high-Speed Universal Refrigerated Centrifuge, Hermle Benchmar (Z32HK), Germany] at 15,000 rpm for 15 min. The supernatant (soluble solids) and the mucilaginous layer (protein-starch fraction) were separated and neutralized. The protein-starch fractions were dried in a forced-air oven at 40°C for 48 h and stored in sealed containers until use. The co-product of the wet-milling process was screening in Tyler Ro-Tap test sieve shaker (Combustion Engineering, Inc., W. S. Tyler, Inc., Mentor, Ohio), to obtain a particle size of 150 μm.
Colorimetry of the Co-product of the Quinoa Grain
Colorimetric properties were determined using a Chroma Meter CM-5 Minolta (Konica Minolta, Inc., Japan). Lightness (L*) and red (+a*) and yellow (+b*) color indices were measured spectrophotometrically according to the CIELAB color system (CIE, 1986), with a D65 illuminant and an observation angle of 5°, for 15 treatments. The samples were placed in Petri dishes in a uniform manner, ensuring that the beam of light from the equipment only hit the sample of interest, performing the measurements at different points on the surface of the sample (Homez et al., 2018).
Attenuated Total Reflectance-Fourier Transform-Infrared Spectroscopy
Spectra were obtained on an FT-IR spectrometer model IRAFFINITY-1S (Shimadzu, Inc., Shelton CT, Japan) with a MIRacle 10 attenuated total reflectance (ATR) accessory (Shimadzu, Inc., Shelton CT, Japan) with a single reflection diamond crystal at an incidence angle of 45°. Measurements were obtained by taking the average of 45 scans with a resolution of 4 cmā1 at 25°C. Happ-Genzel apodization was used, with a magnitude phase correction. A flat tip was used to obtain an intimate contact between sample and crystal, without pressure control. A background spectrum was recorded in air (without sample) prior to each measurement. Spectra were acquired between 500 and 4,000 cmā1 and the mean of the replicates for each sample was reported. Spectral analysis was performed using OriginPro version 2016. Spectra were both baselines corrected and normalized (between 0 and 1). Software was employed to generate a second derivative and Fourier-transform self-deconvolution of the 700 and 2,000 cmā1 region. Deconvolved spectra were used to calculate peak intensity. The Gaussian function was applied to fit the deconvolved spectra. The relative area was calculated in each spectrum peak and area ratios of the bands at 1,032 and 1,005 cmā1 was used as convenient indexes of short-range starch conformation. As well as, to determine changes in the secondary structure of the proteins, between the bands at 1,600 to 1,700 cmā1 (Roa Acosta et al., 2020).
Statistical Analysis
To analyze the effect of the process variables on the structural and colorimetric properties, a Box-Behnken design was used (Table 1), applying the response surface method (RSM), this design was modeled by means of a second order polynomial equation to obtain response surfaces (Equation 1). A quadratic model with interactions was chosen according to the methodology described by Ballester-SƔnchez et al. (2020) with some modifications (Roa-Acosta et al., 2020). In the response surface methodology (RSM), the studied responses (YK, K = 1, ... p) are fitted to the code factors (xi, i = 1, ... n) by the following polynomial model associated to the experimental design:
Where the coefficients a0, ai, and aii represent the constant, linear, and quadratic effects, respectively, and aij represents the interaction effect of coded factors xi and xj. The performance of models was evaluated by the adjusted coefficient of determination () (Equation 2) and mean square error (MSE) (Equation 3).
Where, Ec is the standard deviation associated with the sample; Eex is the standard deviation associated with the model estimations; yex represents the experimental values; yc represents the estimated values, and n is the number of experimental data points used for the model training and validation. The Statgraphics software package (Statistical Graphics Corporation, Virginia, Washington, DC, USA) was used for statistical analysis of the experimental design results. The significance of the effect of the wet-milling treatment on physical-chemical properties of protein-starch fraction was evaluated by two-way ANOVA. For all statistical analyses, a significance level of p <0.05 was adopted using Prism 6 (GraphPad Software Inc., San Diego, CA, USA).
Table 1
| Treatment | T (°C) | SDS (p/v) | NaOH (p/v) | Coded variable | |||||
|---|---|---|---|---|---|---|---|---|---|
| X1 | X2 | X3 | P (%) | S (%) | F (%) | ||||
| 1* | 37 | 0.50% | 1.60% | 0 | 0 | 0 | 31 | 28.3 | 2.9 |
| 2 | 24 | 0.50% | 0.20% | ā1 | 0 | ā1 | 21 | 26.5 | 2.0 |
| 3 | 51 | 0.90% | 1.60% | 1 | 1 | 0 | 31 | 27.7 | 2.9 |
| 4 | 37 | 0.90% | 3.00% | 0 | 1 | 1 | 47 | 28.0 | 4.4 |
| 5 | 24 | 0.10% | 0.20% | ā1 | ā1 | ā1 | 25 | 25.7 | 2.3 |
| 6* | 37 | 0.50% | 1.60% | 0 | 0 | 0 | 33 | 29.2 | 3.1 |
| 7 | 24 | 0.90% | 1.60% | ā1 | 1 | 0 | 22 | 27.2 | 2.0 |
| 8 | 24 | 0.50% | 3.00% | ā1 | 0 | 1 | 29 | 25.8 | 2.7 |
| 9 | 37 | 0.90% | 0.20% | 0 | 1 | ā1 | 18 | 26.3 | 1.7 |
| 10 | 37 | 0.10% | 3.00% | 0 | ā1 | 1 | 35 | 31.3 | 3.3 |
| 11 | 51 | 0.50% | 0.20% | 1 | 0 | ā1 | 27 | 25.7 | 2.5 |
| 12* | 37 | 0.50% | 1.60% | 0 | 0 | 0 | 29 | 27.7 | 2.7 |
| 13 | 51 | 0.10% | 1.60% | 1 | ā1 | 0 | 33 | 28.0 | 3.1 |
| 14 | 51 | 0.50% | 3.00% | 1 | 0 | 1 | 44 | 30.6 | 4.1 |
| 15 | 37 | 0.10% | 0.20% | 0 | ā1 | ā1 | 24 | 26.1 | 2.2 |
Box-Behnken experimental design for the study of wet milling, real, and coded variables.
Temperature, X1; Sodium Dodecyl Sulfate, X2; Sodium Hydroxide, X3; P, protein. Central points of the design (1*, 6*, 12*). The experiments were performed in triplicate (n = 3).
Results and Discussion
In this research, the concentrations of sodium dodecyl sulfate (SDS), sodium hydroxide (NaOH) and temperature were controlled (Table 1). The process conditions were established in order to obtain different yields of the co-products, and possibly modify the physical and structural properties of the starches and proteins present. Color is an important physical property in the perception of food by consumers.
Colorimetry of the Co-product of the Quinoa Grain
The CIElab space was used for color measurement. The lightness (L*), red (+a*) and yellow (+b*) indices were determined spectrophotometrically allowing the color of different products and compounds to be established quantitatively (Kowalski et al., 2016). The color change in the fractions obtained under different extraction conditions by wet milling was determined. Figure 1A shows that the Lightness (L*) has high values, when simultaneously decreasing the temperature and sodium hydroxide (NaOH), indicating higher amount of starch and lower amount of protein in the co-product showing brown colorations in the co-product, i.e., when using high temperatures and high concentrations of sodium hydroxide (NaOH) in the wet milling process, the separation of the protein from the starch fraction is efficient.
Figure 1

Estimated of L*, a*, b* coordinates by response surface modeling. Correlation of brightness values (L*) as a function of temperature and sodium hydroxide (NaOH) concentration, in the separation of proteins from the starch fraction in the co-product.
It was evidenced that the a*, b* coordinates were affected by the increase of NaOH concentration and maceration temperature, showing that at low process conditions, the values of both coordinates decrease, being inversely proportional to the behavior of the Lightness (L*). A second-degree polynomial equation was used to determine the response surface to estimate the Lightness . The a* (Figure 1B) coordinate has values between 3.0 and 7.1, suggesting that the analyzed samples tend to have light red colors, while the b* (Figure 1C) coordinate presents values between 11.08 and 19.80, showing a light yellow. Some authors such as Oli et al. (2016) have reported that the values of L*, a*, and b* in rice samples change according to their shape (husk, brown or milled) and variety, in their study, they also stated that the lightness increases and the values of a* and b* decrease when removing the husk and the bran layer of the rice, where the highest amount of protein is found. Quispe Ramirez (2017), also evaluated the effect of corn starch concentration in cheese, on colorimetric characteristics (L*, a*, b*) finding that as the concentration of starch in the product increases, the L* value increases, presenting a lighter color in the samples studied (Brend et al., 2012; Ballester-SƔnchez et al., 2020). With the colorimetric analysis it is possible to determine the effect of the process conditions on the color of the co-products. In this study, the Lightness data (L*) agree with the data obtained through the structural analysis performed by FTIR-ATR, where it is observed that the higher the intensity of the protein bands of Amide I and Amide II, the lower the Lightness values, indicating a lower passage of light through the analyzed sample, which could be due to a higher protein content in the co-product.
FTIR-ATR Spectral Analysis of the Flours
Roa-Acosta et al. (2020) have reported that there is a correlation between the contents (starch, protein and lipids) and the intensities of the bands (1,150 cmā1; 1,648 cmā1; 2,925 cmā1), respectively (Figure 2). These authors observed an appropriate fit of these bands with the contents of protein (5ā47%), starch (73ā99%), lipids (2ā23%), and that this relationship is independent of the sample, whether whole flour, endosperm flour, defatted flour and protein concentrates isolated by milling (Figure 3A). Proteins and peptides have three main absorption bands in the mid-infrared (MIR): amide I band, amide II band and amide III band region. According to Zhu et al. (2011), the bands between 1,200 and 1,700 cmā1 are the spectral range that are mainly assigned to the protein structure (e.g., amide I and amide II) and some specific amino acids (e.g., glutaminic acid). The N-H stretching bond (3,400ā3,200 cmā1) is a characteristic band related to the vibrations of the amide groups in the polymers that allows the identification of the physical structure of the polymers (Schmidt et al., 2005). The most sensitive spectral region of secondary structural components of proteins corresponds to the amide I band (1,700ā1,600 cmā1) that comes from the stretching vibration of the C=O double bond carbonyl groups of peptide bonds (80% C-C=O stretch, 10% CāN stretch) (Kong and Yu, 2007; Bock et al., 2013; Sivam et al., 2013). This spectral region is useful for the analysis of the specific secondary structural composition and its conformational changes of the protein according to studies performed by other authors (Kong and Yu, 2007; Liu et al., 2009; Shen et al., 2014; Luo et al., 2016): β-sheet (1,612ā1,625 cmā1, 1,625ā1,640 cmā1), α-helix (1,650ā1,660 cmā1), β-turn (1,667ā1,678 cmā1, 1,660ā1,668 cmā1), and random coil (1,637ā1,645 cmā1) (Siwatch et al., 2017). However, this absorption is ~1,660 cmā1 and is masked by the water signal from ~1,560 to 1,715 cmā1. This region is considered a vulnerable zone for secondary structure changes compared to the amide-II band. The amide-II band (1,580ā1,480 cmā1) is mainly due to a bending of the N-H bond and stretching of the C-N (60%NāH bend, 30% CāN stretch, and 10% CāC stretch) bond vibrations (Güler et al., 2011; Bock et al., 2013; Sivam et al., 2013). The band at 1,652 cmā1 corresponding to the stretching of the carbonyl C=O bond and the band at 1,545 cmā1, to the effect of N-H bending and C-N stretching. Consequently, these two bands are the most common for the study of proteins and are known as amide I and amide II vibrations (Cremer and KaletunƧ, 2003). The exact vibrational frequencies of the amide I and amide II bands depend on the nitrogen in the N-H bond/bond and carbon in the C=O bond/bond that is used or not used in protein and peptide bonding/binding (Poulsen et al., 2016). Similarly, the amide III band, ranging from 1,400 to 1,200 cmā1, is associated with C-N stretching and N-H bond flexion.
Figure 2

Intensity of the bands referring to proteins, carbohydrates and lipids at different treatments. Values represent the mean and deviation of duplicates. The different letters (a-i) show the significant difference between the treatments (p <0.05), evaluating parametric and non-parametric behaviors to carry out a deeper analysis. Central design treatments (*1, *6, *12).
Figure 3

Normalized spectra of four treatments (A), Normalized spectra of the starches (B), Normalized spectra of the proteins (C), Normalized spectra of the lipids (D).
In this work, the structural composition of quinoa flour was analyzed by FT-IR analytical technique. For this purpose, the different flour treatments produced changes in the intensities of the characteristic regions of the lipid-related regions around 3,010ā2,800 cmā1 and 1,770ā1,710 cmā1 (Muik et al., 2007), the protein-related regions of amide I around 1,580ā1,700 cmā1 and amide II around 1,580ā1,480 cmā1 (Shotts et al., 2018) and the saccharide region around 942ā1,184 cmā1 (Bock et al., 2013; Sivam et al., 2013) becoming reliable spectral regions for the differentiation of flour. Figure 2 shows the intensities of the bands at 1,633 cmā1 (amide I) and 1,563 cmā1 (amide II), which were associated with the protein content in the co-products. It is observed that the intensity of amide I is greater than amide II. It is important to note that the 1,563 cmā1 band was more sensitive to changes in protein content than the 1,633 cmā1 band, which makes it more suitable for monitoring the extraction process of quinoa protein. For example, the intensity (sample-T9) was lower than observed in sample (T14), this means an increase of the vibrations (functional group-NH2) in sample T14, and therefore, higher protein content (Figure 2).
The glycosidic bands at 1,077 and 1,150 cmā1 were associated with amylaceous content by the C-O-C vibrations functional group (Roa Acosta et al., 2020). For example, the intensity (sample-T9) was lower than observed in sample (T10), this means an increase of the vibrations (functional group-C-O-C) in sample T10, and therefore, higher starch content. Figure 2 shows the intensities between 2,800 and 3,000 cmā1, which are characteristic of lipids (Valenzuela et al., 2013; Siwatch et al., 2017; GarcĆa-Salcedo et al., 2018). It has been reported that the bands at 2,922 and 2,854 cmā1 (corresponding to the symmetric and asymmetric stretching of the CH2 aliphatic groups, respectively) and that at 1,745 cmā1 (attributed to the stretching of the ester carbonyl group) are associated with lipids (Cueto et al., 2018; Cervantes-RamĆrez et al., 2020; Rolandelli et al., 2021). The lipid peaks (Figure 3D) are found at an approximate wavenumber of 2,854 cmā1 corresponding to symmetric stretching vibrations and 2,924 cmā1 corresponding to asymmetric stretching vibrations (in both cases of the CH2 acyl groups) (Herrero et al., 2017). It can also be observed the change in the intensities of each of the spectra, which is generally attributed to changes in the conformational order of the lipid acyl chains and an increase in their dynamics (Valenzuela et al., 2013; Herrero et al., 2017; Bet et al., 2018). The absorptions at 2,922 and 2,854 cmā1, attributed to the asymmetric and symmetric stretching vibration of aliphatic CH2 groups, increased after roasting due to oxidation reactions (Abbas Ali et al., 2017; Jogihalli et al., 2017). Consequently, the variations in lipid contents after maceration processes in this work are in agreement with what was observed in FT-MIR spectra. Rolandelli et al. (2020, 2021) and other authors (Mir et al., 2017; Cueto et al., 2018) have reported that the formation of amylose-lipid complexes during extrusion can explain these modifications in that region of the spectrum of flours. At the end of the maceration process (time > 24 h), the intensity of the amide I and amide II bands starts to decrease in the co-productos. This is because it increases protein in the leaching water. Due to the significant differences (p <0.05) in the protein, starch, and lipid contents present in the co-products, the need arises to study the effects of the extraction conditions on this fraction.
Effect of the Maceration Conditions on the Co-product
Figure 3B shows a spectral region between bands (1,005 and 1,050 cmā1) to study the internal structure of the starch granule (GarcĆa-Salcedo et al., 2018; Roa-Acosta et al., 2020). Variations in the intensities corresponding to the polysaccharide region can be attributed to the different content and type of starch and other types of polysaccharides present in the flour. These variations are in agreement with what has been observed by other authors (942ā1,184 cmā1) (Warren et al., 2016b; VelĆ”squez-Barreto et al., 2021), evidencing a significant effect of the maceration process on the structure of starch granules. These could be related to the mashing treatment to the change in starch structure. The literature reports, that the absorbances 1,047 and 1,022 cmā1 are related to short-range molecularly ordered chain clusters of starch or crystalline structures and amorphous regions, respectively (van Soest et al., 1995; Smits et al., 1998; Warren et al., 2016a; Nhouchi and Karoui, 2018). Therefore, it is to be expected that the maceration treatment influences the disorganization of the ordered starch chains in the granules, as observed in the different treatments.
In the Figure 3C some spectrals variations were observed, this could be due to the effect of maceration conditions (temperature, NaOH, SDS). These changes affect the 1,633 cmā1 band, which is related with the secondary structure of the protein present in the quinoa flours (Roa Acosta et al., 2020; Roa-Acosta et al., 2020). The observed signal for amide I and II is possible due to β-sheet, α-helix, random coil conformations (Kotsiou et al., 2021, 2022). Consequently, the maceration temperature could give rise to α-helix structures corresponding to intermediate stages of α-helix folding/unfolding and less stretched structures (Kong and Yu, 2007). These variations could indicate a partial unfolding of the protein due to the maceration temperature applied to the flour, an effect that produces conformational changes in the proteins. These changes are more evident when increases in β-Sheet and β-turn structures are evidenced, and consequently a decrease in α-helix type structures. The above references explain the change in the shape of the spectra.
Figure 4 shows a positive effect (yellow color) on amide I (1,633 cmā1), glycosidic II (1,077 cmā1), and lipid I (2,852 cmā1) bands. This means that, by increasing the hydroxide concentration, the extraction process is favored in the range of concentrations studied. This effect is since sodium ions attack the interaction between the starch granule and protein, therefore, by increasing the concentration of these ions it will cause a leaching effect of the proteins. Likewise, the positive effect of temperature on protein extraction is mainly due to the fact that an increase in the temperature, produces an increase in the kinetic constants of hydration, therefore, it facilitates the entry of the reagent on protein / starch interaction (Mistry and Eckhoff, 1992; Lai, 2001; BeMiller, 2018).
Figure 4

Standardized pareto diagram (left) and main effect (right) of the maceration on the structure of lipids (A), proteins (amide I y amide II) (B), and starch (glycosidic I and II) presents in the co-product (C).
A quadratic effect of temperature is observed on the amide II band, this means that there is a critical temperature from which the effect of temperature on protein extraction changes direction. If the critical temperature is exceeded, then the extraction yield is decreased, therefore, it would be highly likely that this protein would be lost in the process water (Beck et al., 2017a,b). Figure 4 shows better the effects of operating conditions on the intensity of the amides, for example, low concentrations of NaOH (ā1) and low temperatures (ā1), the intensity of the amides is low, that is that the concentration of protein in the mixture decreases, however, as these variables increase, the intensity of the NH2 group increases (Vera et al., 2019). The decrease in protein content may be due to the increase in the diffusion coefficients, which are affected by the increase in temperature. This phenomenon increases the soluble solids in the maceration waters. The concentration of SDS had a negative effect on the extraction efficiency of starch and lipids, this is due to the surfactant effect of SDS, which adheres to lipid molecules and allows them to be easily leached by water. Figure 5 shows the different response surfaces, which were modeled by a second-order polynomial equation. Figure 5 shows the behavior of starches, proteins, and lipids when they are subjected to different extraction conditions. The statistical significance test for each effect consists of comparing its mean square against an estimate of the experimental error. In this case, 3 effects have a P <0.05, indicating that they are significantly different from zero with a confidence level of 95.0%.
Figure 5

Estimated of lipids (2,852 and 2,921 cmā1) band absorbance (A), amide I and II (1,633 and 1,563 cmā1) band absorbance (B), glycosidic (1,077 and 1,150 cmā1) bond absorbance (C) by response surface modeling.
Dakhili et al. (2019) found that protein configurations are affected by heat treatments, generating conformational and aggregation changes, causing the albumin and globulin denaturation present in the quinoa grain; The heating in the wet milling could cause a splitting of the secondary structures, which caused the dissociation and/or aggregation at the level of the quaternary structure of the proteins, which affected the solubility and modified the extraction of these in the wet milling (Loubes and Tolaba, 2014). On the other hand, in a study by Radosavljevic et al. (1998), it was shown that high concentrations of sodium hydroxide improves the starch extraction process, that is, it facilitates a better separation with the protein, in said study two concentrations of sodium hydroxide were used, 0.25% was used in the first solution, obtaining a recovery of 72.4% ± 5.4 of starch with a protein content (impurity) of 0.40% ± 0.12 , while with the 1% NaOH solution 79.4% ± 1.1 of starch was obtained with a protein content of 0.08 ± 0.001. The present work shows the same behavior, since as shown in the Figure 2, treatments (T4, T8, T10, and T14) with 3%w/v of NaOH, obtained higher intensities in the protein region compared to other treatments of lower concentration as treatment T11 which worked at 0.20%w/v of NaOH. It can be said that high starch yield and low protein content in the starch granules are indicators of a good wet milling process (Myers and Fox, 1994; Ballester-SÔnchez et al., 2019, 2020). On the other hand, the higher protein yield in the co-product is also since albumins are the main protein fraction in the Quinoa grain, which is from 42 to 46% of the total proteins, which are highly soluble in alkaline solutions (Roa et al., 2015; Orona-Tamayo and Paredes-López, 2017; Roa-Acosta et al., 2020).
Conclusion
It was evidenced that the color of the starch-protein fractions was affected by the maceration conditions used in the wet milling process. In this color change, it was observed that the Lightness (L*) agrees with that observed in the structural analysis by FTIR, concluding that the higher the intensity of the protein bands of Amide I and Amide II, the lower the Lightness values, indicating a lower passage of light through the analyzed sample, evidencing a higher protein content in the co-product. In this structural analysis, it was observed that in the maceration process the intensity of the bands of amide I and amide II decreases, due to the increase of the protein content in the leaching water, and in part also, to the protein, starch, and lipid contents in the co-products. In addition, the combined effect of temperature and sodium hydroxide modified the internal structure of the starch granule and the tertiary structure of the protein. Consequently, the effect the protein content in the co-products. Therefore, the need arises to study the effects of the extraction conditions on these fractions and their technical-functional properties for the development of new functional foods, and also serves as a basis for optimizing the maceration stage in wet milling for the utilization of co-products from quinoa grain. Although these results are promising for the development of new products, it is necessary to quantify the components present in the process water, as well as the formulation of products based on the by-product and to carry out the respective shelf-life study under refrigeration and ambient temperature conditions. on the other hand, it is necessary to establish the rheological behaviors, thermal properties and the structure of the gels formed to obtain and analyze the changes of the by-product when subjected to gelatinization.
Publisher's Note
All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.
Statements
Data availability statement
The original contributions presented in the study are included in the article/supplementary material, further inquiries can be directed to the corresponding author/s.
Author contributions
VO-G, JS-D, and DR-A: methodology, formal analysis, and investigation. AF-Q and JB-G: conceptualization, investigation, supervisión, content, and data curation. JS-D: writing. VO-G and DR-A: writing original draft. All authors contributed to the article and approved the submitted version.
Acknowledgments
The authors acknowledge support from Project Quinoa (SGR) BPIN 2020000100052 and ID code 5637, Universidad del Cauca, Universidad del Valle for technical support, and National University Open and Distance (UNAD) for technical support.
Conflict of interest
The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.
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Summary
Keywords
SDS, NaOH, maceration temperature, FTIR-ATR, starch, protein
Citation
Ortiz-Gómez V, FernÔndez-Quintero A, Roa-Acosta DF, Bravo-Gómez JE and Solanilla-Duque JF (2022) Physicochemical Characterization of Quinoa (Chenopodium quinoa cv. Nariño) Co-products Obtained by Wet Milling. Front. Sustain. Food Syst. 6:851433. doi: 10.3389/fsufs.2022.851433
Received
09 January 2022
Accepted
02 February 2022
Published
09 March 2022
Volume
6 - 2022
Edited by
Leonardo SepĆŗlveda, Autonomous University of Coahuila, Mexico
Reviewed by
Miguel A. Medina-Morales, Universidad Autónoma de Coahuila, Mexico; Didier Bazile, Centre de Coopération Internationale en Recherche Agronomique pour le Développement (CIRAD), France
Updates
Copyright
© 2022 Ortiz-Gómez, FernÔndez-Quintero, Roa-Acosta, Bravo-Gómez and Solanilla-Duque.
This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.
*Correspondence: Jose Fernando Solanilla-Duque jsolanilla@unicauca.edu.co
This article was submitted to Sustainable Food Processing, a section of the journal Frontiers in Sustainable Food Systems
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