Food Hydrocolloids 129 (2022) 107607
2
network formation (Nguyen, Chassenieux, Nicolai, & Schmitt, 2017).
Mung bean is a leguminous plant widely cultivated in many parts of
the world (Du et al., 2018). Mung bean is rich in sugar, protein, trace
elements, and essential vitamins, and its protein content ranges from 19
to 33% making it one of the best protein sources for new food product
development (Ebert, Chang, Yan, & Yang, 2017). Mung bean protein
(MBP) consists of globulin, albumin, prolamin, and gluten fractions, and
is rich in lysine, one of the principal essential amino acids (Lee & Chin,
2013). Furthermore, MBP has several reported physiologically benets,
including antioxidative potential, antiproliferative capacity, and anti-
hypertension activity (Gupta, Srivastava, & Bhagyawant, 2018). In Asia,
MBP is considered as a value-added by-product of mung bean starch
processing. Nevertheless, the application of such legume proteins in the
food industry has been limited for its poor functional properties,
including solubility, gelling capacity, and emulsifying activity. Avail-
able processing technologies that show promise to modify plant protein
structures, solubility, and functionality characteristics have been
described by Akharume, Aluko, and Adedeji (2021). In particular,
pH-shifting treatment, which induces structural modication of pro-
teins, i.e., an increased exposure of hydrophobic groups and enhanced
molecular exibility, has been successfully utilized to modulate func-
tional properties of legume seed proteins (Jiang, Wang, & Xiong, 2018).
This technique would conceivably promote the structure-forming ca-
pacity in legume-based acid gels.
In the preparation of fermentation-induced foods, it is desirable to
include fermentable ingredients for nutritional and functional benets.
Quinoa (Chenopodium quinoa Willd.), which consists of plentiful starch
(32%–69%), protein (15%), balanced amino acids, and abundant min-
erals as well as vitamins, has remarkable nutritional properties (James,
2009). As natural stabilizers in acidic protein gel system, starch could
reduce syneresis and improve the texture of acid gels, thus, meeting the
increasing “clean label” demand (Wang, Kristo, & LaPointe, 2020). In
addition, protein in quinoa could interact with MBP in the network
matrix formation to improve the texture properties of the gel.
In the present study, fermentation-induced (43 ◦C for 8 h) gels were
prepared from the pH
12
-treated (2%) or native (2%) MBP mixed with 3%
w/v coconut oil (CNO). The amount of oil added was correspondent to a
typical commercial full-fat yogurt (Gharibzahedi & Chronakis, 2018);
and 0.1% (w/w protein) transglutaminase was applied to promote
protein aggregation as described above. On the other hand, alkaline
pH-shifting treatment was done to modify the protein structure to
improve emulsifying, cross-linking, and gelling potential of the
fermentation-induced gels. Quinoa our hydrolysate as a ller was used
to modulate the gel network. Furthermore, the relationship between
protein structure, oil imbedment, and fermentation-induced gel char-
acter was elucidated.
2. Materials and methods
2.1. Materials
Quinoa (Chenopodium quinoa Willd.) seeds, imported from Bolivia,
were purchased from a local market. Quinoa was crushed with a micro
multifunctional grinder (CS–1000Y, Wuyi Haina Appliances Co. Ltd.,
Zhejiang, China) and then sieved through 60 mesh to obtain quinoa
our. MBP was donated by Shuangta Food Co., Ltd (Yantai city, Shan-
dong, China). Coconut oil was obtained from a local store.
α
-Amylase (5
U/mg) was purchased from Sigma-Aldrich (St. Louis, MO, USA), and
β-Amylase (32270 SBAB/g) was purchased from Genencor Bio-Products
Co. Ltd. (Wuxi, China). Neutral protease (154,438 U/g) was obtained
from Nanning Pangbo Biological Engineering Co. LTD (Guangxi, China).
Transglutaminase was donated by Ajinomoto Co., Inc. (Kawasaki,
Japan). Starter cultures (a blend of L. bulgaricus, S. thermophilus, Ker
microora, B. lactis, B. longum, and B. infantis) was purchased from
Kunshan Baishengyou Biological Technology Co. Ltd. (Jiangsu, China).
All other reagents and solvents were of analytical grade.
2.2. pH-shifting treatment of MBP
Structurally modied protein was prepared by alkaline pH treatment
as described previously (Jiang, Chen, & Xiong, 2009). For the purpose of
ensuring adequate protein unfolding, pH 12 was chosen as the modi-
fying condition. Briey, MBP solution (60 mg/mL, pH 7.0) was titrated
to pH 12 with 2 M NaOH at room temperature, held at this pH for 0.5 h
to induce partial unfolding, and then titrated back to 7.0 with 2 M HCl to
allow refolding. The residual salt was negligible (<0.03 M in ionic
strength) and therefore was not removed before fermentation.
2.3. Enzymatic pretreatment of quinoa our
Quinoa our was pretreated with mixed hydrolytic enzymes to
obtain hydrolysate (QFH). Briey, 25% (w/w) quinoa our was sus-
pended in deionized water, stirred for 2 h at room temperature (23 ◦C)
and then heated at 100 ◦C for 1 h to inactivate endogenous enzymes and
pregelatinize the starch. After cooling to room temperature,
α
-Amylase
(0.1% w/w) and β-Amylase (0.1% w/w) were added. The mixture was
adjusted to pH 5.0 and then incubated at 55 ◦C for 2 h to allow starch
hydrolysis. Thereafter, the pH was adjusted to 7.0 and neutral protease
(0.1%) was then added. After incubation at 50 ◦C for 1 h to initiate
proteolysis, the hydrolysate was heated at 100 ◦C for 15 min to inacti-
vate the enzymes. The resulting QFH contained 4.5 g/100 mL of
reducing sugar as measured by the 3,5-dinitrosalicylic acid (DNS)
method (Deshavath, Mukherjee, Goud, Veeranki, & Sastri, 2020) and
10.6 g/100 mL of total solutes as determined by a digital Brix refrac-
tometer (PAL-1, ATAGO, Tokyo, Japan). Furthermore, the viscosity,
measured with a viscometer (Brookeld Asset Management Inc., Tor-
onto, Canada), was found to be 54 mPa⋅s.
2.4. Preparation of the fermentation-induced gels
A predetermined volume of MBP (60 mg/mL) was mixed with QFH
to obtain a nal mixture of a 30 mg/mL protein where MBP and QFH
accounted for 2/3 and 1/3 of this nal protein content. For treatment
gels with emulsied oil, coconut oil was added at this time (see below).
The mixture was stirred at room temperature for 30 min and then
blended at 13,600 rpm for 3 min using an Ultra-Turrax blender (T18,
IKA, Staufen, Germany), followed by a two-stage high pressure ho-
mogenization (180 bar/30 bar) using an AH-2010 homogenizer (ATS
Engineering Inc., Ontario, Canada). After that, the mixture was heated at
95 ◦C for 10 min and then rapidly chilled to 40 ◦C in an ice water bath.
Starter cultures (0.6% w/w) were added to initiate fermentation (43 ◦C
for 8 h). The pH of the mixture decreased from 7.0 to 4.0–4.5 during the
fermentation time (data not shown) and a fermentation-induced acid
gel, designated “Con”, was formed. For treatment gels, coconut oil (3%
w/w) was added before the above described blending (homogenization)
to obtain the gel named “+Oil” and the size of dispersed oil droplets was
measured by dynamic light scattering (DLS) using a Nano Brook Omni
(Brookhaven Instruments, Holtsville, New York, USA) as described in a
previous study (Jiang, Jin, et al., 2018). Transglutaminase (TG, 0.1%
w/w protein) was added with starter cultures to obtain the gel named
“+TG”. Finally, both coconut oil (3% w/w, added before blending) and
TG (0.1% w/w protein, added with starter cultures) to obtain the gel
named “+Oil +TG”. All four types of gels were ripened for 12 h at 4 ◦C
before being subjected to the following analyses.
2.5. Rheological tests
Rheological measurement was conducted using a stress-controlled
DHR-3 rheometer (TA Instruments, New Castle, Delaware, USA) with
a parallel plate (40 mm diameter and 1 mm gap). Composite
fermentation-induced gel samples were thinly sliced and carefully
loaded in the rheometer. Samples were allowed to rest for 2 min to
release the stress before measurements. The linear viscoelastic region
Y. Nie et al.