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Article

Ultrasound-Assisted Multi-Enzymatic System for the Preparation of ACE Inhibitory Peptides with Low Bitterness from Corn Gluten Meal

1
School of Biology and Food Engineering, Chuzhou University, Chuzhou 239000, China
2
School of Food and Biological Engineering, Jiangsu University, Zhenjiang 212013, China
3
Key Laboratory of Environment Correlative Dietology, College of Food Science and Technology, Huazhong Agricultural University, Ministry of Education, Wuhan 430070, China
4
Department of Biosystems Engineering and Soil Science, The University of Tennessee, Knoxville, TN 37996, USA
*
Authors to whom correspondence should be addressed.
These authors contributed equally to this study.
Present address: Instituto de Agroquímica y Tecnología de Alimentos (IATA-CSIC), 46980 Paterna, Valencia, Spain.
Processes 2021, 9(12), 2170; https://doi.org/10.3390/pr9122170
Submission received: 5 November 2021 / Revised: 24 November 2021 / Accepted: 29 November 2021 / Published: 2 December 2021
(This article belongs to the Topic Innovative Food Processing Technologies)

Abstract

:
The promising angiotensin converting enzyme (ACE) inhibitory peptides derived from corn protein usually have strong bitterness and thus limit their use among consumers. To prepare ACE inhibitory peptides with low bitterness, two energy-efficient types of ultrasound pretreatment were introduced into the multi-enzymatic system of corn gluten meal. The results showed that Flavourzyme–Protamex sequential enzymolysis produced the peptides with high ACE inhibitory activity and the lowest bitterness compared with other enzymolysis conditions. During the optimized sequential enzymolysis, the divergent ultrasound pretreatment with a frequency of 40 kHz for 60 min exhibited higher ACE inhibitory activity (65.36%, accounting for 73.84% of the highest ACE inhibitory activity) and lower bitterness intensity of peptides, compared with an energy-gathered ultrasound. The results of the study showed that, on the one hand, divergent ultrasound pretreatment induced the highest intrinsic fluorescence of protein, with more hydrophobic amino acid residues exposed for cleavage by exopeptidases, which leads to a reduction in bitterness. On the other hand, the amino acid composition analysis proved that more Tyr, Ile, and Val moieties, instead of Leu (bitterest substance), and more peptide fractions with a molecular weight >1000 Da should be the structural features of high ACE inhibitory peptides.

Graphical Abstract

1. Introduction

Corn has an eminent position in food crops across the world. Corn gluten meal is the major by-product of the corn starch process [1]. It contains approximately 60% protein that is high in hydrophobic amino acids, particularly Glu, Leu, Pro, and Phe [2], making it ideal for the preparation of angiotensin converting enzyme (ACE) inhibitory peptides [3]. Research has shown that ACE inhibitory peptides generally consist of hydrophobic amino acid residues at the C- and/or N- terminus, and these peptides contain amino acid residues with hydrophobic side chains [4,5]. The bioactive peptides from corn gluten meal obtained by enzymatic hydrolysis have been shown to possess ACE inhibitory properties [6,7]. The enzymes commonly used in the preparation of ACE inhibitory peptides are endopeptidases, such as Alcalase and Neutrase. These endopeptidases release peptides by cleaving hydrophobic amino acid peptide bonds in the protein chain, resulting in the N- and/or C- terminus of the ACE inhibitory peptides containing hydrophobic amino acid residues (i.e., Leu, Ile, Val, Tyr, Phe, and Trp) [8]. These hydrophobic amino acid residues are related to the bitterness of the ACE inhibitory peptides [9]. In the literature, the contribution of hydrophobic amino acid residues at the N- and/or C-terminus to the bitterness can be evident, probably owing to their binding to the human taste G-protein coupled receptors followed by the activation of associated organoleptic signaling processes [10]. Therefore, these ACE inhibitory peptides always have a pronounced bitter taste [11,12,13], which impedes their acceptance by consumers and limits their utilization in the food industry. Exopeptidases, such as pancreatin, cleave peptide bonds at the terminus of peptides. Hence, in the latter stage, the removal of hydrophobic amino acids at the N- or C-terminus with exopeptidases can reduce the bitterness. Most of the previous research has focused on the ACE inhibitory activity of peptides. However, systematic research on both ACE inhibitory activity and the bitterness of peptides is unavailable.
To tackle bitterness during the production of ACE inhibitory peptides, diverse debittered methods have been developed, including selective separation of bitter peptides [14], embedding [15], enzymatic debittering [16], and the Maillard reaction [17]. Among them, debittering driven by enzymatic hydrolysis is a process utilizing widely used exopeptidases, or a combination of endopeptidases and exopeptidases. Li and colleagues [18] reported that the debittering effect of the combined use of endo- and exopeptidases was better than the single use of exopeptidases for soy peptides, which was due to the production of more hydrophilic amino acid residues at the C-terminus with endopeptidases. Furthermore, exopeptidases can remove the hydrophobic amino acids related to bitterness at the N- or C-terminus of peptides. Thus, the resultant hydrolysates tend to exhibit less bitterness and maintain amino acid composition as much as possible. Nevertheless, it is worthwhile to note that, in some cases, the use of the additional exopeptidases may result in the cleavage of key amino acid residues relevant to peptides with bioactive potential, compromising their bioactivity and functional properties [19].
In recent decades, physical processing methods, typically ultrasound, have been reported to enable more active sites of the enzyme to be exposed, resulting from the altered structure of the protein and hydration process. Ultrasound pretreatment could transform the hydrophobic enzyme restriction sites from the inside to the outside [20,21], affecting the cleavage sequence of enzyme restriction sites, which can lead to peptides with more hydrophobic amino acid residues at the N- or C-terminus. It is then possible to further debitter, via the cleavage of the hydrophobic amino acid residues at the N- or C-terminus of peptides by exopeptidases. If the side chain of amino acid residues had a highly hydrophobic amino acid, it may have been important in enhancing the activity of the peptides. Bryan and colleagues reported that peptides with a hydrophilic moiety in the side chain exhibited greatly diminished biological activity, whereas those with hydrophobic side chains enhanced growth inhibition activity [22]. However, to date, there is no information about the preparation of ACE inhibitory peptides with low bitterness via an ultrasound-assisted multi-enzymatic system.
Therefore, the objectives of the present study were to investigate the effects of the ultrasound-assisted multi-enzymatic system on bitterness and ACE inhibitory activity of corn gluten meal hydrolysates (CGMHs). First, the multi-enzymatic system was optimized by analyzing the bitterness and ACE inhibitory activity of CGMHs obtained by hydrolysis using different proteases including endopeptidases, exopeptidases, and proteases of a complex type. Furthermore, the effects of energy-gathered ultrasound and divergent ultrasound pretreatments on the hydrolysis of corn gluten meal under the optimum multi-enzymatic system were comparatively studied with extrusion expansion. Finally, the possible debittering mechanism driven by the combined ultrasound pretreatments and enzymolysis of corn gluten meal was unraveled. The key finding of this study is expected to provide a good reference for the development of corn-derived peptides in the food industry.

2. Materials and Methods

2.1. Materials

Corn gluten meal (protein content of 60.21%) was provided by Shandong Tiancheng Biotechnology Co., Ltd. (Shandong, China); Alcalase (3.59 × 105 U/g), Neutrase (4.90 × 105 U/g), Flavourzyme (1.62 × 105 U/g), papain (3.25 × 104 U/g), trypsin (1.64 × 105 U/g), and pancreatin (3.80 × 105 U/g) were purchased from Pang Bo Bioengineering Co., Ltd. (Shanghai, China); Protamex (activity of 1.03 × 105 U/g) was purchased from Henan Baichuang Biotechnology Co., Ltd. (Qi Hebi, China); ANS (1-Anilino-8-naphthalenesulfonic acid) and FAPGG (N-[3-(2-Furyl)acryloyl]-Phe-Gly-Gly) were purchased from Sigma-Aldrich Corp (Burlington, MA, USA). All other chemicals and solvents used in the experiment were of analytical grade.

2.2. Energy-Gathered Ultrasound Pretreatment

In an ultrasound processor (Shangjia Biotechnology Co., Wuxi, China; Model GA92-II DB), 2000 mL of sample suspensions were sonicated with a 2.0 cm immersion of the ultrasonic probe as shown in Figure 1b. The process of energy-gathered ultrasound was monitored under the conditions set at an ultrasound on-time of 3 s, ultrasound off-time of 3 s, total working time of 30 min, ultrasonic power of 300 W, and the initial temperature of 25 °C. Specifically, the sample suspensions were stirred and preheated at 25 °C using a water bath for 30 min, and then subjected to energy-gathered ultrasound pretreatment.

2.3. Optimization of Enzymatic Hydrolysis Parameters

In this study, the hydrolysis of corn gluten meal pretreated by energy-gathered ultrasound was divided into two steps.
In first-step hydrolysis, 27 g of corn gluten meal was dispersed in 400 mL of deionized water and mixed for 5 min. The suspension was then preheated at the optimum temperature for the proteases using a water bath for 10 min, and the pH was adjusted to the optimum pH for the selected protease with 1 M NaOH. The optimal temperature and pH conditions of each protease were set as follows: Flavourzyme (50 °C, pH 7.0), Alcalase (50 °C, pH 8.0), Neutrase (50 °C, pH 7.0), papain (55 °C, pH 7.0), and trypsin (40 °C, pH 7.5) [23]. For each of the selected proteases, a dose of 800 mg was added to initiate the enzymatic reaction for different enzymolysis times (10, 20, 30, 40, 60, 80, and 100 min), before the reaction was terminated using a boiling water bath for 10 min to inactivate the proteases. Meanwhile, the pH was stabilized by continuously titrating with a 1 M NaOH solution and the temperature was held constant by using a thermostat water bath (HH-6, Jintan Fuhua Instrument Factory, Jiangsu, China).
In second-step hydrolysis, as soon as the hydrolysates were cooled down to room temperature, they were adjusted to the optimum temperature and pH of the selected exopeptidase. The optimal temperature and pH conditions of each exopeptidase were set as follows: pancreatin (37 °C, pH 8.0) and Protamex (50 °C, pH 7.0). Protamex and pancreatin are common debittering proteases [24]. Afterwards, a dose of 5% [E/S] of the selected exopeptidase was added to the hydrolysates obtained in the first-step hydrolysis, followed by a water bath for enzymolysis for a fixed time of 30 min. Meanwhile, the temperature was set to the optimum temperature for the selected exopeptidase. The reaction was terminated using a boiling water bath for 10 min to inactivate the exopeptidase. Finally, the suspension was cooled down to room temperature and the pH was adjusted to 7.0. Then, the suspension was centrifuged at 12,000 r/min for 5 min. The resulting supernatant was used to determine the ACE inhibitory activity and bitterness for the optimization of enzyme and hydrolysis time. Corn gluten meal suspension without enzymolysis was set as the control.

2.4. Optimization of Ultrasound Pretreatment Equipment

Corn gluten meal was pretreated with two different kinds of ultrasound pretreatments (divergent ultrasound and energy-gathered ultrasound). Corn gluten meal suspensions were hydrolyzed under the optimum enzymatic hydrolysis parameters. The ACE inhibitory activity and the bitterness intensity were set as variables for the optimization of the ultrasound pretreatment. Corn gluten meal suspension without ultrasound pretreatment was set as the control.

2.4.1. Divergent Ultrasound

Sample suspensions were conducted in an ultrasonic bath reactor developed by our research group, shown in Figure 1a, equipped with five different frequencies (24, 28, 33, 40, and 68 kHz). Each ultrasonic generator had a total power of 600 W. The whole ultrasonic radiation volume was 4000 mL, including 3600 mL of distilled water and 400 mL of the corn gluten meal suspensions. The process of divergent ultrasound was monitored under conditions set at an ultrasonic frequency of 28 kHz, ultrasonic power of 600 W, ultrasonic time of 30 min, and ultrasonic pulse on- and off- time of 6 and 3 s, respectively.

2.4.2. Energy-Gathered Ultrasound

The method of energy-gathered ultrasound pretreatment of corn gluten meal suspension was according to Section 2.2.

2.4.3. Positive Control

Corn gluten meal suspension with extrusion expansion pretreatment was set as the positive control. Briefly, corn gluten meal (added with 30% water) was pretreated with a twin-screw extrusion cooker (Brabender Technology Co., Duisburg, Germany; DSE 20/400). The extrusion expansion process was monitored at the following temperatures: I-zone temperature of 85 °C, II-zone temperature of 110 °C, and III-zone temperature of 120 °C. The corn gluten meal was dried at a temperature of 105 °C to a constant weight. After drying, 24.57 g of this extruded corn gluten meal (deducted its initial moisture 9%) was dispersed in 400 mL of deionized water and mixed for 5 min.

2.5. Optimization of Ultrasound Pretreatment Parameters

To optimize the ultrasound pretreatment parameters, 27 g of corn gluten meal was dispersed in 400 mL of deionized water and mixed for 5 min. Sample suspensions were pretreated with ultrasound pretreatment. The divergent ultrasound pretreatment was conducted under the following conditions: ultrasonic time for 30 min and ultrasonic frequencies of 24, 28, 33, 40, and 68 kHz; under the optimized ultrasonic frequency and ultrasonic times for 20, 40, 60, 80, and 100 min. The ACE inhibitory activity and the bitterness were set as variables for the optimization of ultrasound pretreatment parameters. The flow chart of the optimization test is shown in Figure 1c, including the optimization of enzymatic hydrolysis parameters, ultrasound pretreatment equipment, and ultrasound pretreatment parameters.

2.6. Determination of the Degree of Hydrolysis (DH)

The pH-stat method was chosen according to Adler–Nissen [25] to determinate DH (%) using the following equations:
α = 10 pH-pK 1 + 10 pH-pK
DH ( % ) = N b × B × 100 α × M p × h tot
where B is the NaOH solution volume being consumed, mL; Nb is the concentration of NaOH solution, M; α is the average dissociation degree of α-NH2 in the substrate, influenced by the particular temperature and pH of hydrolysis, which is calculated according to Equation (1); Mp is the mass of the hydrolyzed protein, g; htot is the mole number of peptide bonds per quality of protein, which is 9.2 mmol/g for corn gluten meal.

2.7. Determination of ACE Inhibitory Activity

The ACE inhibitory activity was determined according to the method of Actis–Goretta [26] with some modifications. The sample was diluted 50-fold using distilled water. In a 37 °C incubator (BXP-6, Lichen Technology Co., Ltd., Shanghai, China), 100 μL of the sample dilution and 50 μL of ACE was mixed with 50 μL of 1.0 mM FAPGG, dissolved in 0.08 M HEPES buffer containing 0.3 M NaCl (pH 8.3) for 30 min. Then the absorbance difference of the sample before and after the reaction was measured at 340 nm with a multi-wavelength microplate reader (Tecan Infinite PRO TWIN 200, Tecan Co., Ltd., Zürich, Switzerland) and recorded as b1 and b2. The blank was prepared according to the above method, but the sample dilution was replaced by the same volume of 0.08 M HEPES buffer. The absorbance difference of the blank was also measured and recorded as a1 and a2. The ACE inhibitory activity (%) was calculated according to the equation:
ACE   inhibitory   rate   ( % ) = ( a 1 - a 2 ) - ( b 1 - b 2 ) a 1 - a 2 × 100

2.8. Sensory Evaluation of Bitterness

Following the methodology provided by Minagawa and colleagues [27], a sensory evaluation of the bitter taste in hydrolysates was implemented by panelists (4 females and 4 males, aged between 25 and 30). The standard solution is based on the concentration of quinine, and E (E = 8 × 10−8 mol/L) is the minimum value. At each sensory evaluation, panelists were presented with solutions of E, 5E, 50E, 500E, and 1250E of quinine, which had been labeled as 0, 1, 2, 3, and 4 on the bitter scale (0, no bitterness; 1, weakly bitter; 2, bitter; 3, strongly bitter; and 4, extremely bitter). The solution of E of quinine was used as the standard for no bitterness. Panelists then evaluated the bitterness scores of the assayed samples in a randomized order on the basis of the quinine standards they had tasted and panelists were asked to rinse their mouths entirely with double distilled water between tasting the hydrolysate samples.

2.9. Characterization by Intrinsic Fluorescence Spectra

The intrinsic fluorescence emission spectra of corn gluten meal (0.4 mg/mL, w/v) samples were profiled at room temperature (25 ± 1 °C) with a fluorescence spectrophotometer (Model Cary Eclipse, Varian Inc., Palo Alto, CA, USA). An excitation wavelength of 280 nm (slit 10.0 nm), emission wavelength range of 320–520 nm (slit 5.0 nm), and scanning speed of 120 nm/min were set.

2.10. Hydrophobic Amino Acid Composition Analysis

The amino acid composition was determined using an automatic amino acid analyzer (S433D, Saikam Scientific Instruments Co., Ltd., Leipzig, Germany) according to the method described by Zhang and colleagues [28] with some modifications. A 100 mg sample was hydrolyzed in 10 mL of 6 M HCl (110 °C, 24 h). The hydrolysates were then cooled and dried in a vacuum desiccator at 45 °C, and the amino acid composition was determined.

2.11. Measurement of Molecular Weight Distribution of Hydrolysates

TOSOH Bioscience, LLC provided a TSK gel G2000 SWXL 300 mm × 7.8 mm (flow rate of 0.5 mL/min, sample injection of 20 μL, column temperature of 30 °C) for the analysis of the molecular weight distribution of the hydrolysates. The mobile phase (0.02 M phosphate buffer having 0.25 M NaCl, pH 7.2) eluted at a flow rate of 0.5 mL/min. A molecular weight calibration curve was prepared from the average elution volume of the standards: bacitracin (1422 Da), Gly-Gly-Tyr-Arg (451.2 Da), and Glycyl-Glycyl-Glycine (189.1 Da). (Sigma Co., Burlington, MA, USA). UNICORN 5.0 software (Amersham Biosciences Co., Piscataway, NJ, USA) was used to analyze the chromatographic data.

2.12. Statistical Analysis

The analysis of results was performed using an ANOVA under a significance level of p < 0.05 with SPSS 13.0 software (IBM Corporation, New York, NY, USA) and the significant differences between means were detected by an LSD test. All graphs were created using OriginPro8.0 (Origin Lab Corporation, Northampton, MA, USA). All data are presented as means with standard errors (n = 3).

3. Results and Discussion

3.1. ACE Inhibitory Activity of CGMHs

Figure 2a shows the effects of hydrolysis time on ACE inhibitory activity of CGMHs prepared using five different commercial proteases (Neutrase, Alcalase, Flavourzyme, trypsin, and papain) combined with Protamex. The chosen protease and hydrolysis time had significant effects on the ACE inhibitory activity of the CGMHs, as different proteases and hydrolysis times can produce different types of peptides [29,30]. Notably, the ACE inhibitory activity of the CGMHs produced from Neutrase-Protamex (NP) sequential enzymolysis varied from 19.29% to 88.51%, and the highest ACE inhibitory activity value, at 88.51%, was obtained after 40 min of Neutrase hydrolysis. The CGMHs obtained by Alcalase-Protamex (AP) sequential enzymolysis had various ACE inhibitory activity ranging from 40.89% to 69.37%. The ACE inhibitory activity of CGMHs achieved using Flavourzyme-Protamex (FP) sequential enzymolysis was in the range of 19.87% to 40.44%, and the highest ACE inhibitory activity value, at 40.44%, was achieved after 20 min of Flavourzyme hydrolysis. Among five kinds of sequential enzymolysis, NP was the highest, followed by AP, FP, papain-Protamex (PP), and trypsin-Protamex (TP). CGMHs produced by FP showed high ACE inhibitory activity, which was similar to the results of Suh and colleagues [31], who found that hydrolysates prepared from corn gluten by Flavourzyme showed high ACE inhibitory activity (IC50: 0.18 mg solid). Flavourzyme is a complex-type (endo- and exo-type) enzyme and is recommended for the production of debittered hydrolysates. Regarding debittered hydrolysates, Protamax produces a lower amount of Glu, and higher Leu and Ile, resulting in the bitter taste [31]. Ko and colleagues [32] reported that among the nine proteases Protamex, Kojizyme, Neutrase, Flavourzyme, Alcalase, pepsin, trypsin, α-chymotrypsin, and papain, Protamex hydrolysates of flesh tissue possessed the highest ACE inhibitory activity. The possible mechanism was that Protamex could release potent ACE inhibitory peptides from debittered hydrolysates by Flavourzyme [33].
The effect of hydrolysis time on the ACE inhibitory activity of CGMHs produced by five different commercial proteases in combination with pancreatin are shown in Figure 2b. The ACE inhibitory activities owing to the hydrolysis of five different proteases (Neutrase, Alcalase, Flavourzyme, trypsin, and papain) combined with pancreatin varied, ranging from 8.40% to 71.67%. Among the five kinds of sequential enzymolysis, it was clear that the Neutrase-pancreatin (NPa) sequential enzymolysis obtained the highest ACE inhibitory activity with a value of 71.67% after 80 min of Neutrase hydrolysis. The second highest ACE inhibitory activity (52.66%) was produced by Alcalase-pancreatin (APa) sequential enzymolysis after 40 min of Alcalase hydrolysis. As a whole, the ACE inhibitory activity of CGMHs prepared using five different commercial proteases combined with Protamex was higher than that combined with pancreatin. This can be explained by the fact that Protamex was beneficial to the preparation of high ACE inhibitory peptides [34]. Another possible reason might be that pancreatin had higher exo-peptidase activity than Protamex, and thus pancreatin could cleave more hydrophobic amino acid residues exposed at the N- or C-terminus [35].

3.2. Evaluation of the Bitterness Sensation and Intensity of CGMHs

Figure 3a shows the effects of hydrolysis time on the bitterness intensity of CGMHs prepared by five different proteases in combination with Protamex. Among the five kinds of sequential enzymolysis, AP sequential enzymolysis obtained the highest bitterness intensity with the value of 3.75 after 20 min of Alcalase hydrolysis. The second highest bitterness intensity (3.30) was derived by the treatment of NP sequential enzymolysis after 40 min of Neutrase hydrolysis. FP sequential enzymolysis showed the lowest bitterness intensity (2.39) after 20 min of Flavourzyme hydrolysis. It was not surprising that Alcalase and Neutrase had the tendency to hydrolyze at hydrophobic amino acid residue positions. It was reported that peptides with hydrophobic amino acid residues at the C-terminal had high bitterness [36]. Fu and colleagues [37] reported that hydrolysates of bovine muscle and porcine plasma produced by Flavourzyme elicited low bitterness. The difference in bitterness of CGMHs indicated the presence of multiple cleavage sites on peptides that were acted upon by proteases of various origins and types. After all, Flavourzyme has not only endo-peptidase activity, but also exo-peptidase activity compared to Alcalase or Neutrase.
The effects of hydrolysis time on the bitterness intensity of CGMHs produced by five different proteases in combination with pancreatin are illustrated in Figure 3b. The results show that APa sequential enzymolysis obtained the highest bitterness intensity (3.49) after 10 min of Alcalase hydrolysis, followed by hydrolysates produced from NPa sequential enzymolysis after 80 min of Neutrase hydrolysis (with the value of 3.04). The CGMHs obtained by Flavourzyme-pancreatin (FPa) sequential enzymolysis had various bitterness intensities ranging from 3.11 to 3.19. The trypsin-pancreatin (TPa) sequential enzymolysis showed the lowest bitterness intensity with a range of 2.49 to 2.65. As a whole, the bitterness intensity of CGMHs prepared using five different commercial proteases combined with Protamex, was higher than that combined with pancreatin, except for FP and TP sequential enzymolysis. This indicated that the ACE inhibitory activity of CGMHs was not all positively correlated with bitterness intensity. These findings were consistent with those of Wu and colleagues [38], who discovered no significant relationship between ACE inhibitory activity and bitterness intensity in di- and tri-peptides. Pripp and colleagues [12] found that the relationship between peptide bitterness intensity and ACE inhibitory activity was weaker for oligopeptides than dipeptides.
The bitterness sensation of the CGMHs prepared by TP, TPa, and FP sequential enzymolysis were generally acceptable to the panelists. Among these three enzymatic combinations, the ACE inhibitory activity of the CGMHs produced by FP was highest with the value of 40.44%. Based on the integrated consideration of ACE inhibitory activity and bitterness intensity, CGMHs produced by FP sequential enzymolysis were favorable for the preparation of ACE inhibitory peptides with low bitterness. Therefore, FP sequential enzymolysis was the optimum multi-enzymatic hydrolysis preparation of corn gluten meal.

3.3. Effects of Ultrasound Pretreatment on the Enzymolysis of Corn Gluten Meal

Figure 4 shows the effects of divergent ultrasound pretreatment on ACE inhibitory activity and bitterness intensity of CGMHs under optimum multi-enzymatic hydrolysis parameters. In the multi-enzymatic system, divergent ultrasound pretreatment had significant effects on the ACE inhibitory activity and bitterness intensity of CGMHs. The divergent ultrasound pretreatment performance in ACE inhibitory activity (with its value of 55.31%) did not show any significant difference compared to extrusion expansion pretreatment. In terms of energy consumption and safety, divergent ultrasound pretreatment was superior to extrusion expansion pretreatment. The divergent ultrasound pretreatment in ACE inhibitory activity increased markedly by 20.11% compared to energy-gathered ultrasound pretreatment with its value of 46.05%. Similarly, Jin [39] reported that divergent ultrasound pretreatment is more suitable for the enzymolysis of corn gluten meal compared to energy-gathered ultrasound pretreatment. The possible reason was that divergent ultrasound is plate type, the ultrasonic energy distribution in the reaction system is more uniform, and energy-gathered ultrasound only produces instantaneous high temperature, high pressure, and shear force at the tip of the ultrasonic probe [40]. Therefore, for corn gluten meal with strong hydrophobicity, divergent ultrasound pretreatment can prevent the exposed hydrophobic groups from rearrangement.
Regarding bitterness intensity, the divergent ultrasound pretreatment was close to extrusion expansion pretreatment (p > 0.05) with the value of 2.26. The bitterness intensity from the divergent ultrasound pretreatment decreased significantly by 5.8% (p < 0.05) compared to energy-gathered ultrasound pretreatment with a value of 2.40. Thus, the divergent ultrasound pretreatment contributed to the higher ACE inhibitory activity and lower bitterness intensity of the final product compared with energy-gathered ultrasound pretreatment. Considering energy consumption and safety, the divergent ultrasound pretreatment was the optimum pretreatment of corn gluten meal.

3.4. Effects of Ultrasonic Frequency and Ultrasonic Time on the Enzymolysis of Corn Gluten Meal

Figure 5a,b show the ACE inhibitory activity and bitterness of CGMHs prepared by divergent ultrasound pretreatment at different ultrasonic frequencies (24–68 kHz) and ultrasonic times (20–100 min).
It was clear that the ACE inhibitory activity of CGMHs increased significantly (p < 0.05) with an increase in ultrasonic frequency, peaking at 40 kHz (with a value of 59.67%), and then gradually dropped with increasing ultrasonic frequency. This finding was in accordance with the result of Yang and colleagues [41], who reported that the ACE inhibitory activity of hydrolysates prepared from the sonicated defatted wheat germ protein at different frequencies increased significantly by 31.94% compared to the control. The bitterness intensity of CGMHs had no significant difference (p > 0.05) with the increase in ultrasonic frequency, which was stabilized at around 2.26. A possible explanation for this may be that the difference in bitterness intensity caused by ultrasonic frequency was offset by the effect of Flavourzyme [42].
Figure 5b shows that the bitterness of CGMHs was observed to be stabilized at around 2.26, showing no significant difference (p > 0.05) regardless of the increase in ultrasonic time. Different ultrasonic times had prominent effects on the ACE inhibitory activity of CGMHs. The ACE inhibitory activity of CGMHs reached a maximum (65.36%) when ultrasonic time reached up to 60 min compared with the enzymatic hydrolysis conditions having the highest ACE inhibitory activity (88.51%); although ACE inhibitory activity accounted for 73.84% of the highest ACE inhibitory activity, bitterness intensity was decreased by one level from bitter (3.27) to weakly bitter. Therefore, the optimal divergent ultrasound parameters were as follows: an ultrasonic frequency of 40 kHz and ultrasonic time of 60 min.

3.5. Intrinsic Fluorescence Spectra

Intrinsic fluorescence spectroscopy has been widely used to sensitively measure the protein conformational changes resulting from the alteration of the polarity microenvironment [43]. The main aromatic amino acids, such as Tyr, Phe, and Trp, exposed to the protein surface could emit intrinsic fluorescence. Figure 6 shows that corn gluten meal samples pretreated by divergent ultrasound have higher fluorescence intensities compared to samples pretreated with either energy-gathered ultrasound or extrusion expansion, though all of the pretreated samples displayed greater fluorescence intensities compared with the control. This indicates that divergent ultrasound pretreatment exposed more hydrophobic amino acids towards the protein surface than other pretreatments. Therefore, the divergent ultrasound pretreatment was beneficial to produce the peptides with more hydrophobic amino acids under the hydrolysis of Flavorzyme. Additionally, those hydrophobic amino acids were not only at the N- or C-terminus of peptides, but also in the side chain of amino acid residues, so it is possible to further debitter, including favorable cleavage of the hydrophobic amino acid residues at the N- or C-terminal of peptides with hydrolysis using Protamex. Furthermore, more hydrophobic amino acids in the side chains of amino acid residues are beneficial to improving the ACE inhibitory activity of CGMHs. In brief, the divergent ultrasound pretreatment of corn gluten meal might change the protein conformation with an enhanced exposure of hydrophobic amino acids towards the protein surface [44]. Our results indicated that the ultrasound-induced unfolding of the structure of corn gluten meal protein potentially reduced the bitterness intensity of CGMHs. Due to this, the enzyme accessibility to the interior structure of proteins could probably be improved [41].

3.6. Hydrophobic Amino Acid Composition of CGMHs

Peptide bitterness is related to hydrophobic amino acid content and molecular weight distribution [37]. The hydrophobic amino acid content of CGMHs with different treatments can be found in Table 1. The optimum conditions were as follows: FP sequential enzymolysis, with a divergent ultrasound pretreatment using an ultrasonic frequency of 40 kHz and an ultrasonic time of 60 min. The results indicated that the total hydrophobic amino acid content of CGMHs under the conditions producing the highest ACE inhibitory activity reached up to 55.7%, which was increased by 5.1% (p < 0.05) compared with that of CGMHs under the optimum conditions. The Leu and Ala content of CGMHs under the conditions producing the highest ACE inhibitory activity was significantly higher than that under the optimum conditions. Ney [45] reported that the bitterness intensity of di-peptides containing Leu was almost twice as strong as that of di-peptides containing other hydrophobic amino acids. Furthermore, the total hydrophobic amino acid content of CGMHs under the optimum conditions was mostly explained by the higher abundance of Tyr, Ile, Val, and Met (Table 1). This was consistent with the study done by Jia and colleagues [3], who reported that the structural characteristics of ACE inhibitory peptides were that their terminal amino acids were enriched in Tyr, Val, Ala, Ile, Leu, Pro, Trp, and Phe. Although both CGMHs produced under the optimum conditions and under the conditions having the highest ACE inhibitory activity had ACE inhibitory peptides, the structural characteristics of peptides prepared under these two conditions were apparently different, which probably altered the bitterness intensity of CGMHs, as confirmed in Figure 2, Figure 3 and Figure 5.

3.7. Molecular Weight Distribution of CGMHs

As shown in Table 2, our results found that the molecular weight distribution of CGMHs prepared under the conditions having the highest ACE inhibitory activity and under the optimum conditions had the highest percentage (57.15% and 51.09%, respectively) in the 500–1000 Da peptide fraction. However, the percentages of over 1500, 1000–1500, and below 500 Da fraction for those CGMHs were relatively low (Table 2).
Apart from that, compared to those prepared under the optimum conditions, the CGMHs prepared under the conditions having the highest ACE inhibitory activity had a higher percentage of molecular weight in the 500–1000 Da fraction, which was increased by 11.9% (Table 2). Additionally, under both conditions, the CGMHs had a close percentage of molecular weight of <500 Da, which had no significant difference (p > 0.05). However, the CGMHs under the optimum conditions had a higher percentage of molecular weight of 1000–1500 Da and >1500 Da, which increased by 44.5% and 45.7%, respectively, compared with the cases where the highest ACE inhibitory activity was obtained (Table 2). Hence, those peptides with a molecular weight of >1000 Da were probably related to the reduction of bitterness intensity. Our results coincided well with the results of Fu and colleagues [37], who reported that the bitter taste of protein hydrolysates was positively correlated with a peptide fraction of 500–1000 Da.

4. Conclusions

The multi-enzymatic system of FP sequential enzymolysis could produce CGMHs with relatively high ACE inhibitory activity and the lowest bitterness compared with other sequential enzymolysis. In the FP sequential enzymolysis reaction, divergent ultrasound pretreatment was superior to energy-gathered ultrasound pretreatment in ACE inhibitory activity and bitterness intensity of CGMHs. In terms of energy consumption and safety, divergent ultrasound pretreatment was better than extrusion expansion pretreatment, though they had no significant difference in ACE inhibitory activity. Following divergent ultrasound pretreatment with a frequency of 40 kHz for 60 min, the ACE inhibitory activity (65.36%) accounted for 73.84% of the highest ACE inhibitory activity, and the relative bitterness intensity was decreased from 3.27 to 2.26. We further proposed that the molecular mechanism of divergent ultrasound pretreatment promotes ACE inhibitory activity of CGMHs and decreases their bitterness. Divergent ultrasound pretreatment resulted in an increase of intrinsic fluorescence intensity, hydrophobic amino acid content of Tyr, Ile, and Val, and more peptides with a molecular weight >1000 Da, but had a decreased content of the hydrophobic amino acid Leu. Overall, the divergent ultrasound-assisted protein multi-enzymatic system should be an effective approach to prepare ACE inhibitory peptides with low bitterness from corn gluten meal.

Author Contributions

Conceptualization and validation, S.H. and Y.L.; methodology, X.Y.; investigation, data curation and writing—original draft preparation, S.H.; writing—review and editing, Y.L., C.L., S.R. and Y.D.; resources, supervision and project administration, Y.L. and H.M.; funding acquisition, Y.L., W.Q. and H.M. All authors have read and agreed to the published version of the manuscript.

Funding

This paper was supported by the National Natural Science Foundation of China [31872892 and 31701538], the Natural Science Foundation of Jiangsu Universities [17KJB550001] and the Advanced Talents Research Fund of Jiangsu University [16JDG049].

Institutional Review Board Statement

Not applicable.

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Data Availability Statement

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Acknowledgments

The authors greatly appreciated the financial support obtained from the National Natural Science Foundation of China [31872892 and 31701538], the Natural Science Foundation of the Jiangsu Higher Education Institutions of China [17KJB550001] and the Research Foundation for Advanced Talents of Jiangsu University [16JDG049].

Conflicts of Interest

No conflict of interest exits in the submission of this manuscript, and manuscript that is enclosed is approved by all authors for publication. Neither the entire paper nor any part of its content has been published or has been accepted elsewhere. And it is not being submitted to any other journal.

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Figure 1. (a) Diagram of the divergent ultrasound equipment; (b) Diagram of the energy-gathered ultrasound equipment. 1: Ultrasonic probe; 2: Ultrasonic controller; (c) Experimental flow chart.
Figure 1. (a) Diagram of the divergent ultrasound equipment; (b) Diagram of the energy-gathered ultrasound equipment. 1: Ultrasonic probe; 2: Ultrasonic controller; (c) Experimental flow chart.
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Figure 2. (a) Effect of hydrolysis time on the ACE inhibitory activity of CGMHs using different proteases in combination with Protamex; (b) Effects of hydrolysis time on the ACE inhibitory activity of CGMHs using different proteases in combination with pancreatin. Significant differences between results are indicated by different letters (p < 0.05).
Figure 2. (a) Effect of hydrolysis time on the ACE inhibitory activity of CGMHs using different proteases in combination with Protamex; (b) Effects of hydrolysis time on the ACE inhibitory activity of CGMHs using different proteases in combination with pancreatin. Significant differences between results are indicated by different letters (p < 0.05).
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Figure 3. (a) Effect of hydrolysis on the bitterness intensity of CGMHs using different proteases in combination with Protamex; (b) Effects of hydrolysis on the bitterness intensity of CGMHs using different proteases in combination with pancreatin. Significant differences between results are indicated by different letters (p < 0.05).
Figure 3. (a) Effect of hydrolysis on the bitterness intensity of CGMHs using different proteases in combination with Protamex; (b) Effects of hydrolysis on the bitterness intensity of CGMHs using different proteases in combination with pancreatin. Significant differences between results are indicated by different letters (p < 0.05).
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Figure 4. Effect of ultrasound pretreatment on the ACE inhibitory activity and bitterness intensity of CGMHs under optimal multi-enzymatic hydrolysis parameters. Significant differences between results are indicated by different letters (p < 0.05).
Figure 4. Effect of ultrasound pretreatment on the ACE inhibitory activity and bitterness intensity of CGMHs under optimal multi-enzymatic hydrolysis parameters. Significant differences between results are indicated by different letters (p < 0.05).
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Figure 5. (a) The effect of ultrasonic frequency on the ACE inhibitory activity and bitterness of CGMHs under optimal multi-enzymatic hydrolysis parameters; (b) The effect of ultrasonic time on the ACE inhibitory activity and bitterness of CGMHs under optimal multi-enzymatic hydrolysis parameters. Significant differences between results are indicated by different letters (p < 0.05).
Figure 5. (a) The effect of ultrasonic frequency on the ACE inhibitory activity and bitterness of CGMHs under optimal multi-enzymatic hydrolysis parameters; (b) The effect of ultrasonic time on the ACE inhibitory activity and bitterness of CGMHs under optimal multi-enzymatic hydrolysis parameters. Significant differences between results are indicated by different letters (p < 0.05).
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Figure 6. Intrinsic fluorescence emission spectra of proteins subjected to different ultrasound pretreatments.
Figure 6. Intrinsic fluorescence emission spectra of proteins subjected to different ultrasound pretreatments.
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Table 1. Comparison of hydrophobic amino acid contents (%, m/m) for enzymatic hydrolysates with different bitterness.
Table 1. Comparison of hydrophobic amino acid contents (%, m/m) for enzymatic hydrolysates with different bitterness.
Name of Amino AcidsHA Mass Fraction/%HB Mass Fraction/%
Pro9.0 ± 0.03 a8.9 ± 0.06 a
Tyr5.2 ± 0.04 b5.4 ± 0.09 a
Phe5.6 ± 0.06 a5.6 ± 0.04 a
Leu16.8 ± 0.07 a13.6 ± 0.03 b
Ile4.1 ± 0.02 b4.6 ± 0.01 a
Val4.7 ± 0.03 b5.4 ± 0.02 a
Ala8.0 ± 0.07 a6.7 ± 0.06 b
Met2.3 ± 0.03 b2.8 ± 0.04 a
Total amino acids55.7 ± 0.04 a53.0 ± 0.04 b
HA: Hydrolysate under the conditions having the highest ACE inhibitory activity; HB: Hydrolysate under the optimum conditions. Significant differences between results are indicated by different letters (p < 0.05).
Table 2. Comparison of the molecular weight distribution for enzymatic hydrolysates with different bitterness.
Table 2. Comparison of the molecular weight distribution for enzymatic hydrolysates with different bitterness.
Molecular Weight (Da)>15001000–1500500–1000<500
HA Proportion (%)9.96 ± 1.32 b7.57 ± 1.89 b57.15 ± 1.16 a25.32 ± 2.67 a
HB Proportion (%)14.51 ± 1.19 a10.94 ± 2.34 a51.09 ± 2.53 b23.46 ± 1.58 a
HA: Hydrolysate under the conditions having the highest ACE inhibitory activity; HB: Hydrolysate under the optimum conditions. Significant differences between results are indicated by different letters (p < 0.05).
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Huang, S.; Li, Y.; Li, C.; Ruan, S.; Qu, W.; Ding, Y.; Ye, X.; Ma, H. Ultrasound-Assisted Multi-Enzymatic System for the Preparation of ACE Inhibitory Peptides with Low Bitterness from Corn Gluten Meal. Processes 2021, 9, 2170. https://doi.org/10.3390/pr9122170

AMA Style

Huang S, Li Y, Li C, Ruan S, Qu W, Ding Y, Ye X, Ma H. Ultrasound-Assisted Multi-Enzymatic System for the Preparation of ACE Inhibitory Peptides with Low Bitterness from Corn Gluten Meal. Processes. 2021; 9(12):2170. https://doi.org/10.3390/pr9122170

Chicago/Turabian Style

Huang, Shanfen, Yunliang Li, Chengliang Li, Siyu Ruan, Wenjuan Qu, Yanhua Ding, Xiaofei Ye, and Haile Ma. 2021. "Ultrasound-Assisted Multi-Enzymatic System for the Preparation of ACE Inhibitory Peptides with Low Bitterness from Corn Gluten Meal" Processes 9, no. 12: 2170. https://doi.org/10.3390/pr9122170

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