Flavor-protein interactions for four plant protein isolates and whey protein isolate with aldehydes

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LWT - Food Science and Technology 185 (2023) 115177
Available online 14 August 2023
0023-6438/© 2023 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-
nc-nd/4.0/).
Flavor-protein interactions for four plant protein isolates and whey protein
isolate with aldehydes
Silvia J.E. Snel
a
,
b
, Mirela Pascu
c
, Igor Bodn´
ar
c
, Shane Avison
c
, Atze Jan van der Goot
b
,
Michael Beyrer
a
,
*
a
Institute of Life Technologies, University of Applied Sciences and Arts Western Switzerland, CH-1950, Sion, Switzerland
b
Food Process Engineering, Agrotechnology and Food Sciences Group, Wageningen University & Research, Bornse Weilanden 9, 6708 WG, Wageningen, the Netherlands
c
Firmenich S.A., Rue de la Berg`
ere 7, Meyrin 2, CH-1217, Geneva, Switzerland
ARTICLE INFO
Keywords:
Pea
Soy
Chickpea
Faba bean
Covalent interactions
ABSTRACT
Aldehydes are important avor molecules to consider in plant-based products. Here, the avor retention of a
series of saturated aldehydes and mono-unsaturated aldehydes (2-alkenals) with different chain lengths (C4, C6,
C8, and C10) in dispersions with protein isolates of pea, soy, fava bean, chickpea, and whey (as reference) was
analyzed with APCI-TOF-MS. The headspace concentrations of alkenals were lower than aldehydes, meaning
alkenals were retained more than saturated aldehydes. The retention was modeled by assuming hydrophobic
interactions and covalent interactions. The ratio between the hydrophobic interaction parameter and the co-
valent parameter showed that covalent interactions are mainly important for butanal and butenal (C4). For the
other aldehydes, hydrophobic interactions became increasingly important. Correlations were found between the
chemical interaction parameters and the cysteine and methionine content of the different proteins. The obtained
model parameters for each set of proteins and avors allow the prediction of avor retention when developing a
avored product with high protein content.
1. Introduction
Diet patterns must change to be able to feed the growing world
population in a sustainable matter (Aiking & de Boer, 2018; Broekema
et al., 2020). A route to reach this goal is to replace meat and dairy with
plant-based products. Nevertheless, plant-based products are considered
less appealing by consumers, because of their taste and off-notes (Michel
et al., 2021). Currently, a key success factor for plant products that
should replace meat is a high similarity in texture, avor, and nutritional
value. In case of meat, avors are developed when heating the product
(Ramalingam et al., 2019). The heating of meat generates different
volatile avor compounds such as alkenes, alcohols, aldehydes, ketones,
ethers, esters, carboxylic acids, and sulfur-containing compounds (Kale
et al., 2022). Plant-based products do not undergo a similar avor
development and often have distinct avors of their own, which are
frequently perceived as off-notes (Wang et al., 2022). In order to have a
similar avor prole, avor compounds are added to plant-based
products that both mask plant avor and create meat-like avors.
However, avors can strongly interact with the proteins present in
plant-based products, making them less effective (Guichard, 2002).
Protein-avor retention is mostly hydrophobic, but depending on the
type of avor also irreversible covalent interactions, reversible
hydrogen bonds, ionic bonds, and van der Waalss forces can lead to
avor retention (Wang & Arnteld, 2014). Aldehydes, for example, can
interact covalently with the amine or thiol groups of the proteins, apart
from hydrophobic interactions (Anantharamkrishnan & Reineccius,
2020b). Aldehydes can react in Schiff base formation, whereas alkenals
are also capable of forming Michael adducts (Anantharamkrishnan
et al., 2020a).
An efcient route to determine avor retention is through comparing
the equilibrium headspace concentration in a avored protein disper-
sion to a control without protein (Gremli, 1974; Wang & Arnteld, 2015;
Zhou & Cadwallader, 2006). However, this approach is time-consuming
and therefore often only a few chemicals are studied, which makes it
challenging to get a full overview of avor retention in protein products.
A more pragmatic method is to model experimental data to predict
avor partitioning. Harrison and Hills developed a mathematical model
to predict avor release for both hydrophilic and hydrophobic
* Corresponding author.
E-mail address: michael.beyrer@hevs.ch (M. Beyrer).
Contents lists available at ScienceDirect
LWT
journal homepage: www.elsevier.com/locate/lwt
https://doi.org/10.1016/j.lwt.2023.115177
Received 21 April 2023; Received in revised form 5 August 2023; Accepted 8 August 2023
LWT 185 (2023) 115177
2
compounds from a liquid containing macromolecules (Harrison & Hills,
1997). This model was applied to describe avor retention in whey and
sodium caseinate dispersions (Viry et al., 2018). For esters and alcohols,
good predictions were obtained by only assuming hydrophobic in-
teractions to explain avor retention (Viry et al., 2018). For aldehydes,
stronger retention was observed, which was attributed to the specic
covalent interactions that proteins and aldehydes can undergo (Viry
et al., 2018). Therefore, the model was extended with a covalent inter-
action parameter to describe aldehyde retention (Viry et al., 2018).
Recently, this model was applied to predict avor retention in four plant
proteins and whey dispersions with esters, and ketones, assuming hy-
drophobic interactions only (Snel et al., 2023). Apart from esters and
ketones, aldehydes are an important chemical class to consider for the
avoring of plant-based products such as meat analogues. Therefore,
probing the interactions between plant proteins and aldehydes is
essential and could give great insights into the applicability of the model
when covalent interactions are involved. Furthermore, it would high-
light the relative contribution of hydrophobic and covalent interactions
for aldehyde retention.
This study describes the retention of aldehydes by plant proteins and
applies a avor partitioning model to analyze the results. The proteins
studied are pea protein isolate (PPI), soy protein isolate (SPI), chickpea
protein isolate (CPPI), and fava bean protein isolate (FBPI). Besides,
whey protein isolate (WPI) will be included as a control. The investi-
gated avors include a series (C4, C6, C8, C10) of saturated aldehydes
and 2-mono-unsaturated aldehydes (alkenals), from now on addressed
as aldehydes and alkenals. Furthermore, the obtained partitioning pa-
rameters will be correlated with amino acid composition.
2. Theory: avor partitioning models
Harrison and Hills (1997) developed a rst-order mathematical
model to predict avor release from an aqueous solution containing
polymers at equilibrium conditions. In the case of proteins, avors can
interact with the proteins through either hydrophobic interactions or
specic covalent interactions. The avor-partitioning model will be
shortly summarized here. The partition coefcient (Kf
wg)at equilibrium
between avor concentration in the water phase (ce
fw)and gas phase (ce
fg)
is dened as:
Kf
wg =ce
fg
ce
fw
(1)
When protein is added to the water phase, part of the avors could
interact with the protein. When we consider that the avor-protein
interaction is a reversible, rst-order reaction, the global interaction
constant (Kf
p)between protein P and avor F is dened as:
Kf
p=ce
fp
ce
pce
fw
(2)
in which ce
fp and ce
p are the concentrations of protein-retained avor in
the dispersion at equilibrium, and protein. Since in the experimental set-
up, protein concentration exceeds the avor concentration largely, c
p
is
simplied as the total concentration of protein in the dispersion that
thus remains constant during the experiment. Now, the effective parti-
tion coefcient Keff
wg between avor in the gas phase and the water-
protein phase becomes:
Keff
wg =ce
fg
ce
ft
(3)
in which ce
ft is the total avor in the water system. The mass balance
reads:
cft =cfp +cfw (4)
In which c
ft
equals c
fw
when no protein is present in the water phase.
Using the mass balance and eq. (1) and eq. (2), we can describe Keff
wg as:
Keff
wg =Kf
wg
1+Kf
pce
p
(5)
When avor retention is dominated by hydrophobic interactions, we
could approach the interaction constant with:
Kf
p=apPf
ow (6)
in which a
p
and Pf
ow are the hydrophobic interaction parameter and the
octanol-water partition coefcient. For aldehydes, the covalent inter-
action has to be taken into account, leading to (Viry et al., 2018):
Kf
p=apPf
ow +KAld (7)
in which K
Ald
is the covalent interaction parameter between aldehydes
and proteins. For alkenals, this parameter becomes K
alk
. Aldehydes can
interact with proteins through a condensation reaction (Schiff base
adduct), and alkenals can have an additional conjugate addition
(Michael adduct, Fig. 1) (Anantharamkrishnan et al., 2020a). The total
contribution of both reactions is captured in the parameters K
ald
or K
alk
.
3. Methods and materials
3.1. Materials
Soy protein isolate (SPI, Supro® 500E A) was obtained from Solae
(St. Louis, United States). Pea protein isolate (PPI, Nutralys® F85M) was
obtained from Roquette Fr`
eres S.A. (Lestrem, France). Fava bean protein
isolate (FBPI, FFBP-90-C-EU) and chickpea protein isolate (CPPI, FCPP-
70) were both obtained from AGT Foods (Regina, Canada). Whey pro-
tein isolate (WPI, BiPRO) was obtained from Davisco Foods Interna-
tional (Minnesota, USA). Amino acid content was measured in a
Fig. 1. Schematical representation of the chemical reactions possible between
the amine group of amino acids and butanal (A), and trans-2-butenal (B), and
the thiol group of cysteine with trans-2-butenal (C) (Anantharamkrishnan &
Reineccius, 2020b). Butanal and trans-2-butenal are chosen in this example to
represent aldehydes and alkenals respectively. SB =schiff base, MA =
michael adduct.
S.J.E. Snel et al.
Flavor-protein interactions for four plant protein isolates and whey protein isolate with aldehydes.pdf

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