Functional fungal extracts from the Quorn fermentation co-product as novel partial egg white replacers
- 216 Downloads
Abstract
The production of mycoprotein biomass by Marlow Foods for use in their meat alternative brand Quorn is a potential source of sustainable alternatives to functional ingredients of animal origin for the food industry. The conversion of this viscoelastic biomass into the Quorn meat-like texture relies on functional synergy with egg white (EW), effectively forming a fibre gel composite. In a previous study, we reported that an extract (retentate 100 or R100) obtained from the Quorn fermentation co-product (centrate) via ultrafiltration displayed good foaming, emulsifying, and rheological properties. This current study investigated if a possible similar synergy between EW and R100 could be exploited to partially replace EW as foaming and/or gelling ingredient. The large hyphal structures characteristic of R100 solutions were observed in EW–R100 mixtures, while EW–R100 gels showed dense networks of entangled hyphal aggregates and filaments. R100 foams prepared by frothing proved less stable than EW ones; however, a 75/25 w/w EW–R100 mixture displayed a similar foam stability to EW. Simlarly, R100 hydrogels proved less viscoelastic than EW ones; however, the viscoelasticity of gels prepared with 50/50 w/w and 75/25 w/w EW–R100 proved similar to those of EW gels, while 75/25 w/w EW–R100 gels displayed similar hardness to EW ones. Both results highlighted a functional synergy between the R100 material and EW proteins. In parallel tensiometry measurements highlighted the presence of surface-active material in EW–R100 mixtures contributing to their high foaming properties. These results highlighted the potential of functional extracts from the Quorn fermentation process for partial EW replacement as foaming and gelling agent, and the complex nature of the functional profile of EW–R100 mixtures, with contributions reported for both hyphal structures and surface-active material.
Graphic abstract
Keywords
Quorn Co-product Centrate Egg White ReplacementIntroduction
Due to its excellent foaming properties, egg white is widely used in desserts, cakes, biscuits, and many aerated prepared dishes including soufflés and mousses. Egg white also displays excellent gelling properties used for various cooking or baking applications. However, due to the high environmental costs and market volatility of animal-derived functional ingredients including milk and egg proteins, the food industry is looking for sustainable alternatives [1]. One of the strategies employed consists in screening unexploited co-product streams from the food industry for extraction of potential functional alternatives. In this context, the production of mycoprotein by Marlow Foods for use in their meat alternative product Quorn is a potential source of sustainable functional ingredients. The term mycoprotein refers to the high-protein biomass produced by fermentation of the fungus Fusarium venenatum A3/5 (ATCC PTA-2684) by Marlow Foods, which forms the basis of their Quorn brand products. Mycoprotein contains all essential amino acids [2] and the net protein utilisation value of Fusarium venenatum mycoprotein is comparable to that of milk [3]. Moreover, the fermentation of starch into protein by Fusarium venenatum results in 90% lower emission of greenhouse gases and benefits in terms of land and water footprints in comparison with beef products [4].
Following fermentation, the broth undergoes an RNA-reduction step during which it is first heat-shocked above 68 °C for 30–45 min, then further heated at 90 °C, and finally centrifuged [5]. This heat shock step stops growth, disrupts ribosomes, and activates endogenous RNAases which break down cellular RNA to nucleotides [5]. The resulting solid deposit (mycoprotein biomass) is then processed into a dough ready for conversion to the meat-like texture characteristic of Quorn foods. However, the heat-shock RNA-reduction step also induces diffusion of a fraction of the cell components through the cell wall [5]. The liquid supernatant (centrate) generated by the subsequent centrifugation step thus contains residual hyphal biomass, carbohydrates, nucleotides, and proteins as well as the residues of the fermentation feedstock, and is currently an unexploited co-product stream.
Following centrifugation, the viscoelastic mycoprotein biomass is mixed with egg albumen and the material is discharged into industrial block formers. The pressure exerted allied with the flow characteristics of the mixed material result in the introduction of laminations or layers which can be considered as textural precursors for the final meat-like texture [6]. The mix is heated to 90 °C then chilled and frozen to approximately − 10 °C. This controlled freezing step results in an entangled mass of mycoprotein hyphae with gelled albumen protein within the interstitial space, a system described as fibre gel composite which confers a meat-like texture to the products [6].
Egg white is a complex system of proteins with different physicochemical properties. Lysozyme (14.3 kDa) is a very basic protein with an isoelectric point at pH 10.5, making it the only egg white protein that is positively charged in physiological conditions [7]. The high foaming properties of egg white could be due to a synergy in adsorption at the air/water interface between the positively charged lysozyme and other negatively charged proteins including ovalbumin and ovotransferrin, with intermolecular interactions occurring between the oppositely charged proteins after their unfolding, which stabilises the air bubbles [8, 9, 10]. Such synergy at the air/water interface has also been reported between lysozyme and whey proteins [11, 12], with intermolecular interactions reported in the bulk solution as well as at the air–water interface, resulting in higher foam stability due to the reduction of electrostatic repulsive interactions in the protein film.
In a previous study [13], we reported that an extract (retentate 100 or R100) obtained via a 100 kDa ultrafiltration of the centrate displayed good foaming stability, emulsifying, and rheological properties (viscosity, viscoelasticity, and gelation). R100 solutions displayed high viscosity, while R100 solutions and hydrogels showed high viscoelasticity. R100 foams displayed high stability, while oil-in-water R100 emulsions showed small and stable oil droplet size distributions. Large hyphal aggregates were reported in R100 solutions and gels, correlating with their high viscosity and viscoelasticity. A dense hyphal network was observed in R100 foams and contributed to their stability. In parallel tensiometry measurements at the oil/water interface highlighted the presence of interfacially active molecules in R100 which formed a rigid film stabilising the oil droplets. A number of functional metabolites and proteins were identified in the centrate, including a cerato-platanin protein, cell membrane constituents (phospholipids, sterols, glycosphingolipids, and sphingomyelins), cell wall constituents (chitin, chitosan, proteins), and guanine and guanine-based nucleosides and nucleotides. The current study investigated if a similar synergy to the one reported between EW and mycoprotein in the formation of the Quorn meat-like texture could be exploited between EW and R100 with a view to partially replacing EW as foaming and/or gelling ingredient. As part of this work, the functional profile (foaming and rheological properties) of a range of mixtures of EW and R100 was characterised.
Materials and methods
Sample preparation
Centrate samples were collected from the Marlow Foods fermenter site at Belasis, Billingham and frozen. Following thawing, the centrate underwent a 100 kDa ultrafiltration step using a Vivaflow 200 crossflow cassette (Sartorius, UK) connected to a Masterflex Easy-Load peristaltic pump (Sartorius, UK). The resulting retentate 100 or R100 (composed of molecules larger than 100 kDa) was freeze-dried in a Super Modulyo unit (Edwards, UK). A commercial agglomerated egg white (EW) powder was used as control.
Nitrogen content
The % nitrogen obtained was then multiplied by the general conversion factor of 6.25 recommended for mycoprotein biomass [15] to obtain a % nitrogen-containing material (NCM). Measurements were repeated three times. The functional profile of the four following samples was then assessed: EW control, R100, 75/25 EW–R100 (75% EW + 25% R100 on w/w basis for specified NCM content), and 50/50 EW–R100 (50% EW + 50% R100 on w/w basis for specified NCM content).
Gel electrophoresis
Sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE) was performed using a Mini-Protean Tetra Cell System with Mini-Protean TGX 4–20% Tris–glycine precast gels (Bio-Rad Laboratories Ltd., UK) according to the methods of Laemmli [16] and Havea et al. [17] with minor modifications. One percent w/w nitrogen-containing material (NCM) solutions of the EW, R100 and 75/25 EW–R100 samples were prepared in deionised water and stirred for 1 h. One set of each solution was sonicated for 3 min at 20 kHz and 50% amplitude using a Sonics Vibra-Cell VCX-500 probe sonicator (Sonics, UK) to provide a reference for protein de-aggregation, while the other set was left untreated.
SDS-PAGE samples were prepared by mixing equal proportions of sample solution and Laemmli 2 × concentrate sample buffer (Sigma Aldrich Ltd., UK) followed by heating at 70 °C for 10 min. The See Blue Plus2 pre-stained standard (Life Technologies Ltd., UK) was used as molecular weight marker. The wells were loaded with 20 μl of sample or 10 μL of marker and the gels were run in Tris/Glycine/SDS buffer (Bio-Rad Laboratories Ltd., UK) at 100 V for 1 h. The gels were subsequently stained in a Coomassie brilliant blue solution (VWR Ltd., UK) for 1 h and destained overnight in the corresponding destaining solution (glacial acetic acid:methanol:deionised water 1:4:5). Gels were scanned using a ChemiDoc XRS + imaging system (Bio-Rad Laboratories Ltd., UK) and analysed using the associated Image Lab software.
Rheological properties
Viscosity and gelation measurements were performed using a Bohlin Gemini controlled stress rheometer (Malvern Instruments, UK) using cone-and-plate geometry. 10% w/w NCM solutions of EW, R100, 75/25 EW-R100, and 50/50 EW/R100 were prepared in deionised water and stirred for 2 h. To assess the potential contribution of the R100 material to the EW gelling profile, EW solutions at 7.5% and 5% w/w NCM concentrations (matching the respective EW concentrations of the 75/25 EW–R100 and 50/50 EW/R100 samples) were also tested. Measurements were repeated three times.
Viscosity measurements were performed using a 4°/40 mm cone (gap 150 μm) at 20 °C. The instantaneous viscosity (Pa.s) was measured through a shear rate increase from 0.001 to 50 s−1. Prior to gelation tests, the linear viscoelasticity region of each sample was determined via oscillatory measurements of elastic and viscous moduli (G’ and G’’) carried out at 1 Hz over a strain amplitude sweep ranging from 0.00005 to 50. Gelation profiles were then assessed via small-amplitude oscillatory measurements using a 2°/40 mm cone (gap 70 μm) with the applied strain chosen from within the linear viscoelastic region for each sample. The elastic and viscous moduli (G’ and G’’) were measured through a temperature sweep test ranging from 40 to 90 °C in up-down mode (15 min up-sweep and 15 min down-sweep) and the oscillation frequency was 1 Hz.
Texturometry on hydrogels
Ten milliliter solutions of 10% w/w NCM EW, R100, 75/25 EW-R100, and 50/50 EW/R100 were prepared in deionised water and stirred for 2 h. 10 ml solutions of 7.5% and 5% w/w NCM EW were also assessed as controls. The solutions were then heated for 1 h at 95 °C in a water bath and cooled down at 4 °C for 3 h. The resulting gels were tested for hardness using a BDO-FBO5.TS texture analyser (Zwick-Roell, UK) equipped with a 40 mm height/20 mm bottom diameter cylindrical probe. A single compression test was performed at a 1 mm/sec crosshead speed and 10 mm gel penetration depth. Measurements were replicated twice. The results were analysed using the associated testXpert 11.02 software (Zwick-Roell, UK).
Foaming properties
Two types of foaming methods (frothing and gas sparging) were carried out at room temperature (20 °C). Both foaming ability and stability were investigated using a frothing test. Fifteen gram solutions of 1% w/w NCM solutions of EW, R100, 75/25 EW-R100, and 50/50 EW/R100 were prepared in 50 ml glass beakers, which corresponds to an initial volume of 18 cm3 (1.4 cm sample height and 4 cm beaker diameter), and stirred for 1 h. To assess the potential contribution of the R100 material to the EW foaming profile, EW solutions at 0.75% and 0.5% w/w NCM concentrations (matching the respective EW concentrations of the 75/25 EW–R100 and 50/50 EW/R100 samples) were also tested. The solutions were frothed for 1 min using a handheld whisk-type frother (Aerolatte, UK). The height of the resulting foam was measured immediately after whisking and every 10 min until collapse of the foam. The foaming ability was expressed as the initial height of the foam, while the foam stability was determined as the time needed for the foam to fully collapse. Measurements were repeated twice.
A gas-sparging test was also used according to Rudin [18] with minor modifications to assess the stability of foams prepared with EW, R100, and EW–R100 mixture solutions. 40 g solutions of 1% w/w NCM solutions of EW, R100, and 50/50 EW/R100 were stirred for 1 h and transferred to a column, which corresponds to an initial volume of 48 cm3 (3.8 cm sample height and 4 cm column diameter). A 0.5% w/w NCM EW was also tested as control. Gas sparging was carried out at constant flow rate of CO2 (100 cm3/min) until the foam reached the top indicator of the column (at 32.5 cm height from the bottom), which corresponds to a foam volume of 409 cm3. The foam stability was quantified as the time needed for the foam to collapse to the bottom indicator of the column. Measurements were repeated three times.
Surface tension
One percent w/w NCM solutions of EW, R100, and 75/25 EW–R100 were serially diluted to obtain 0.5%, 0.25%, and 0.1% w/w NCM solutions. The surface tension of the solutions was measured using the Du Nouy method with an EZ-Pi Plus tensiometer (Kibron, UK). Deionised water was used as control with a surface tension reading of 72 mN/m. 1.5 ml of solution was placed into a sterile cup holder. Triplicate measurements were carried out at 20 °C.
Confocal microscopy
EW, R100, 75/25 EW-R100, and 50/50 EW/R100 solutions, foams, and hydrogels were imaged using a Leica TCS2 confocal laser scanning microscope (Leica Microsystems, Germany). 1% and 10% w/w NCM solutions were prepared in deionised water supplemented with the fluorescent dye rhodamine B, respectively, stirred for 1 h and 2 h, and imaged. Foams and hydrogels were prepared following the procedures described in the foaming and texturometry sections and imaged. The dye was excited at 514 nm, the collection range was 600–700 nm, and a 10x/0.25 dry lens was used. Micrographs were recorded at a resolution of 512 × 512 pixels and analysed using the manufacturer’s software (Leica Software Development Kit DM SDK version 4.2.1).
Human/animal rights
This article does not contain any studies with human or animal subjects.
Results and discussion
Characterisation of EW–R100 mixtures
The NCM content of the R100 and agglomerated EW samples were, respectively, 55.2% and 91.8% based on Kjeldahl measurements. The NCM content of the R100 fraction obtained was similar to the one measured in our previous study (56.7%) [13].
Confocal microscopy of EW, R100, and 75/25 EW–R100 solutions (1% w/w NCM concentration, rhodamine, magnification × 10). a EW, b 75/25 EW-R100, and c R100
SDS-PAGE of native and sonicated EW, R100, and EW–R100 solutions (1% w/w NCM, original pH, and high-contrast gel scan). (1) See blue marker, (2) untreated R100, (3) sonicated R100, (4, 5) untreated 75/25 EW-R100, (6, 7) sonicated 75/25 EW-R100, (8) untreated EW, (9) sonicated EW, and (10) see blue marker
The disappearance of the protein A band and the weaker monomeric lysozyme band observed in the EW–R100 mixture suggested the possible aggregation of monomeric and dimeric lysozyme forms with R100 proteins. Aggregation between the positively charge lysozyme and negatively charged whey proteins through electrostatic interactions has previously been reported [11, 12].
Another explanation for the EW–R100 gel profile was the potential binding of monomeric and dimeric lysozyme forms to fungal cell walls. Lysozymes, also known as muramidases or N-acetylmuramide glycanhydrolases, are a family of enzymes binding and catalysing the hydrolysis of β-1-4 glycosidic bonds within peptidoglycans contained in bacterial cell walls, resulting in antimicrobial effects [24]. Due to their chemical similitude with peptidoglycan (both type of polysaccharides contain β-1-4 linked N-acetylglucosamine units), chitin and chitosan contained in fungal cell walls have also been reported as viable binding and hydrolysis substrates for a number of lysozymes including egg white lysozyme [25, 26].
Rheological properties of EW–R100 mixtures
Viscosity profiles of EW, R100, and EW–R100 mixtures during shear rate increase (10% w/w NCM concentration, original pH, n = 3)
Gelation profiles (elastic modulus G’) of EW–R100 mixtures (10%, 7.5%, or 5% w/w NCM concentration, original pH, n = 3)
Confocal microscopy of EW, R100, and 75/25 EW–R100 gels (10% w/w NCM concentration, original pH, rhodamine, and magnification × 10). a EW, b 75/25 EW-R100, and c R100
R100 gels proved less viscoelastic than 7.5% EW ones; however, 75/25 EW–R100 gels displayed a higher viscoelasticity than 7.5% EW ones (Fig. 4), highlighting a synergistic interaction between the R100 material and egg albumen. As reported by Finnigan [6], the mixing of mycoprotein biomass and egg albumen during the production of Quorn mince and pieces introduces laminations which can be considered as textural precursors for the final meat-like texture. In the current study, such interaction could be due to the binding of lysozyme to chitin and chitosan contained in fungal cell walls [25, 26], which was supported by the SDS-PAGE results with the respective disappearance and weakening of the dimeric and monomeric lysozyme bands when EW was mixed with R100 (Fig. 2).
In parallel, our previous study [13] showed the presence of compounds with known gelling properties in the centrate, including cell wall and membrane constituents which concentrated in the R100 fraction as part of the hyphal aggregates and contributed to the EW–R100 gelling profile. The gelifiers reported included chitin and chitosan [28, 29], phytosterols and phytosterol esters [34], ceramides and sphingomyelins [35], glycosphingolipids [36], inulin [30], galactan [31], and nucleobases, nucleosides, and nucleotides (including guanine-based compounds) and their derivatives [32].
Hardness profile of EW, R100, and EW–R100 hydrogels (10% or 7.5% w/w NCM concentration, original pH, n = 3)
The combined rheological and textural results also highlighted the possibility of re-introducing centrate extracts back into the process at the manufacturing stage as partial egg albumen replacers while maintaining the characteristic fibre gel composite structure of Quorn products.
Foaming properties of EW–R100 mixtures
Foam stability of EW, R100, and 50/50 EW–R100 as determined by the Rudin method (1% or 0.5% w/w NCM concentration, original pH, n = 3)
Foaming ability and stability profiles of EW, R100, and EW–R100 mixtures (1% or 0.75% w/w NCM concentration, original pH, n = 3)
Confocal microscopy of EW, R100, and 75/25 EW–R100 foams prepared by frothing (1% w/w NCM concentration, original pH, rhodamine, and magnification × 10). a EW, b 75/25 EW-R100, and c R100
In addition, depending on their hydrophobicity, the possible concentration of Fusarium venenatum cells and/or spores in the R100 fraction as a result of the ultrafiltration process could also have contributed to the stabilisation of R100 and EW–R100 foams as the shapes and sizes of bacterial cells, viruses, and spores fall within the range for stabilisation of biphasic dispersions including foams and emulsions [37]. Moreover, a correlation between foam stability and cell surface hydrophobicity was reported for different strains of Acinetobacter calcoaceticus [38].
Surface tension of EW, R100, and 75/25 EW–R100 solutions (1% w/w NCM concentration, original pH, n = 3)
The higher foam stability exhibited by 75/25 EW–R100 in comparison with 0.75% EW following frothing (Fig. 8) could also be due to the presence of surface-active aggregates formed between lysozyme and R100 proteins, as suggested by the respective weakening and disappearance of monomeric and dimeric lysozyme bands on the 75/25 EW–R100 SDS-PAGE profile (Fig. 2). Due to its high isoelectric point (10.7), lysozyme was charged positively in the 75/25 EW–R100 mixture and possibly combined with negatively charged proteins present in R100 through electrostatic interactions. Such aggregation process was previously reported between lysozyme and negatively charged whey proteins [11, 12].
Similarly, a synergy in adsorption at the air/water interface between lysozyme and negatively charged R100 proteins when foamed together could also have contributed to the higher foam stability exhibited by 75/25 EW–R100 in comparison with 0.75% EW following frothing (Fig. 8) and by 50/50 EW–R100 in comparison with 0.5% EW following gas sparging (Fig. 7). In this case, intermolecular interactions between the oppositely charged proteins occur at the interface after the unfolding of the proteins, which stabilises the air bubbles due to the reduction of electrostatic repulsive interactions in the protein film. Such synergy at the air/water interface was previously reported between the two egg white proteins lysozyme and ovalbumin [8]. Synergistic effects between lysozyme and whey proteins were shown to result from intermolecular interactions in the bulk solution as well as at the air–water interface, resulting in higher foam stability [11, 12].
The combined foaming, microscopy, and tensiometry results highlighted that surface-active material present in R100 and/or synergistically combining with EW proteins contributed to the high stability of EW–R100 foams, while the dense hyphal network observed in these foams contributed via physical stabilisation of the air bubbles. Foam-positive material present in R100 included hyphal aggregates, fungal cells, foaming molecules, and hyphal fragments or molecules released from hyphal aggregates during the foaming process. These results highlighted the potential of R100 for use as partial replacer of EW as foaming agent.
Conclusions
The study investigated if a similar synergy to the one reported between EW and mycoprotein in the formation of the Quorn meat-like texture could be exploited between EW and a functional extract from the Quorn fermentation co-product (R100). The viscoelasticity and hardness of 75/25 EW–R100 hydrogels proved similar to 10% EW ones and higher than 7.5% EW ones. Frothed 75/25 EW–R100 foams showed similar stability to 1% EW ones and higher stability than 0.75% EW ones, while gas-sparged 50/50 EW–R100 foams proved as stable as 1% EW ones and more stable than 0.5% EW ones. These results highlighted the potential of centrate extracts for partial EW replacement as foaming and gelling agent.
R100 foams prepared by frothing proved less stable than 7.5% EW ones; however, a 75/25 w/w EW–R100 mixture displayed a higher foam stability than 7.5% EW ones. Similarly, R100 gels proved less viscoelastic than 7.5% EW ones; however, 75/25 EW–R100 gels displayed a higher viscoelasticity than 7.5% EW ones. Both results highlighted a functional synergy between the R100 material and EW proteins.
In parallel tensiometry measurements highlighted the presence of surface-active material in EW–R100 mixtures contributing to their high foaming properties. In particular, the SDS-PAGE profile of EW–R100 mixtures indicated a possible aggregation of monomeric and dimeric forms of lysozyme with R100 proteins and/or fungal cells, contributing to their foaming and rheological properties. The results highlighted the complex nature of the functional profile of EW–R100 mixtures, with contributions reported for both hyphal structures and surface-active material.
Future work will assess the partial functional replacement of EW ingredients by centrate extracts in food formulations. Additional studies are needed to further understand the potential synergy between EW and R100 and the contribution of both hyphal structures and surface-active molecules to EW–R100 functionality. Finally, this study highlights the possibility of re-introducing Quorn fermentation co-product extracts back into the process at the manufacturing stage as partial egg albumen replacers.
Notes
Acknowledgements
The authors wish to thank Dr. Tim Finnigan and Dr. Sue Gordon from Marlow Foods for their support during this project.
Funding
This work was supported by the Engineering and Physical Sciences Research Council [Grant Number EP/J501682/1 Foaming and Fat Replacer Ingredients].
Compliance with ethical standards
Conflict of interest
The authors declare that they have no conflict of interest.
Compliance with ethics requirements
This article does not contain any studies with human or animal subjects.
References
- 1.McMichael J, Powles C, Butler R (2007) Food, livestock production, energy, climate change, and health. Lancet 370:1253–1263PubMedCrossRefGoogle Scholar
- 2.Denny A, Aisbitt B, Lunn J (2008) Mycoprotein and health. Br Nutr Bull 33:298–310CrossRefGoogle Scholar
- 3.Edelman J, Fewell A, Solomons GL (1983) Myco-protein—a new food. Nutr Abstr Rev Clin Nutr 53:471–480Google Scholar
- 4.Finnigan TJA, Lemon M, Allen B, Patton I (2010) Mycoprotein LCA and food 2030. Asp Appl Biol 102:81–90Google Scholar
- 5.Ward PN (1996) A process for the reduction of nucleic acid content for a fungus imperfectus. WO Patent 95/23843Google Scholar
- 6.Finnigan T (2011) Mycoprotein: origins, production and properties. In: Phillips GO, Williams PA (eds) Handbook of food proteins. Woodhead Publishing, SawstonGoogle Scholar
- 7.Lechevalier V, Croguennec T, Pezennec S, Guérin-Dubiard C, Pasco M, Nau F (2003) Ovalbumin, ovotransferrin, lysozyme: three model proteins for structural modifications at the air–water interface. J Agric Food Chem 51:6354–6361PubMedCrossRefGoogle Scholar
- 8.Floch-Fouéré C, Pezennec S, Lechevalier V, Beaufils S, Desbat B, Pezolet M, Renault A (2009) Synergy between ovalbumin and lysozyme leads to non-additive interfacial and foaming properties of mixtures. Food Hydrocoll 23(2):352–365CrossRefGoogle Scholar
- 9.Lechevalier V, Périnel E, Jeanete R, Lesaffre C, Croguennec T, Guérin-Dubiard C, Pasco M, Nau F (2005) Evidence for synergy in the denaturation at the air–water interface of ovalbumin, ovotransferrin and lysozyme in ternary mixture. Food Chem 92:79–87CrossRefGoogle Scholar
- 10.Domadaran S, Anand K, Razumovsky L (1998) Competitive adsorption of egg white proteins at the air–water interface: direct evidence for electrostatic complex formation between lysozyme and other egg proteins at the interface. J Agric Food Chem 46:872–876CrossRefGoogle Scholar
- 11.Howell NK, Yeboah NA, Lewis DFV (1995) Studies on the electrostatic interactions of lysozyme with alpha-lactalbumin and beta-lactoglobulin. Int J Food Sci Technol 30(6):813–824CrossRefGoogle Scholar
- 12.Kuropatwa M, Tolkach A, Kulozik U (2009) Impact of pH on the interaction between whey and egg white proteins as assessed by foamability of their mixtures. Food Hydrocoll 23:2174–2181CrossRefGoogle Scholar
- 13.Lonchamp J, Clegg PS, Euston SR (2019) Foaming, emulsifying and rheological properties of extracts from a co-product of the Quorn fermentation process. Eur Food Res Technol. https://doi.org/10.1007/s00217-019-03287-z CrossRefGoogle Scholar
- 14.Lynch JM, Barbano DM, Fleming JR (1998) Indirect and direct determination of the casein content of milk by Kjeldahl nitrogen analysis: collaborative study. J AOAC Int 81:763–774PubMedGoogle Scholar
- 15.Sadler MJ (2003) Mycoprotein. In: Caballero B, Trugo M, Finglas PM (eds) Encyclopedia of food sciences and nutrition (second edition). Academic Press, CambridgeGoogle Scholar
- 16.Laemmli UK (1970) Cleavage of structural proteins during the assembly of the head of bacteriophage T4. Nature 227:680–685PubMedPubMedCentralCrossRefGoogle Scholar
- 17.Havea P, Watkinson P, Kuhn-Sherlock B (2009) Heat-induced whey protein gels: protein–protein interactions and functional properties. J Agric Food Chem 57:1506–1512PubMedCrossRefGoogle Scholar
- 18.Rudin AD (1957) Measurement of the foam stability of beers. J Inst Brew 63(6):506–509CrossRefGoogle Scholar
- 19.Zhang J, Zhang J (2016) The filamentous fungal pellet and forces driving its formation. Crit Rev Biotechnol 36(6):1066–1077PubMedCrossRefPubMedCentralGoogle Scholar
- 20.Nyman J, Lacintra MJ, Westman JO, Berglin M, Lundin M, Lennartsson PR, Taherzadeh MJ (2013) Pellet formation of zygomycetes and immobilization of yeast. New Biotechnol 30(5):516–522CrossRefGoogle Scholar
- 21.Onuma K, Inaka K (2008) Lysozyme dimer association: similarities and differences compared with lysozyme monomer association. J Cryst Growth 310(6):1174–1181CrossRefGoogle Scholar
- 22.Desfougères Y, Lechevalier V, Pezennec S, Artzner F, Nau F (2008) Dry-heating makes hen egg white lysozyme an efficient foaming agent and enables its bulk aggregation. J Agric Food Chem 56(13):5120–5128PubMedCrossRefGoogle Scholar
- 23.Narai-Kanayama A, Hanaishi T, Aso K (2016) Mechanistic investigation of capability of enzymatically synthesized polycysteine to cross-link proteins. Biochem Biophys Rep 7:338–346PubMedPubMedCentralGoogle Scholar
- 24.McKenzie HA, White FH (1991) Lysozyme and alpha-lactalbumin: structure, function, and interrelationships. Adv Protein Chem 41:173–315PubMedCrossRefGoogle Scholar
- 25.Ruckenstein E, Zeng X (1997) Macroporous chitin affinity membranes for lysozyme separation. Biotechnol Bioeng 56:610–617PubMedCrossRefGoogle Scholar
- 26.Nordtveit RJ, Vårum KM, Smidsrød O (1994) Degradation of fully water-soluble, partially N-acetylated chitosans with lysozyme. Carbohydr Polym 23:253–260CrossRefGoogle Scholar
- 27.Porcel EMR, Casas Lopez JL, Sanchez Perez JA, Fernandez Sevilla JM, Chisti Y (2005) Effects of pellet morphology on broth rheology in fermentations of Aspergillus terreus. Biochem Eng J 26:139–144CrossRefGoogle Scholar
- 28.Lapasin R, Stefancic S, Delben F (1996) Rheological properties of emulsions containing soluble chitosan. Agro Food Ind High Tech 7:12–17Google Scholar
- 29.Quintela S, Villarán MC, López De Armentia I, Elejalde E (2012) Ochratoxin a removal from red wine by several oenological fining agents: bentonite, egg albumin, allergen-free adsorbents, chitin and chitosan. Food Addit Contam Part A 29(7):1168–1174CrossRefGoogle Scholar
- 30.Mensink MA, Frijlink HW, van der Voort Maarschalk K, Hinrichs WLJ (2015) Inulin, a flexible oligosaccharide I: review of its physicochemical characteristics. Carbohydr Polym 130:405–419PubMedCrossRefGoogle Scholar
- 31.Delattre C, Fenoradosoa TA, Michaud P (2011) Galactans: an overview of their most important sourcing and applications as natural polysaccharides. Braz Arch Biol Technol 54(6):1075–1092CrossRefGoogle Scholar
- 32.Peters GM, Davis JT (2016) Supramolecular gels made from nucleobase, nucleoside and nucleotide analogs. Chem Soc Rev 45:3188–3206PubMedCrossRefGoogle Scholar
- 33.Zhu C, Ma Y, Zhou C (2010) Densities and viscosities of sugar alcohol aqueous solutions. J Chem Eng Data 55(9):3882–3885CrossRefGoogle Scholar
- 34.Matheson A, Dalkas G, Clegg PS, Euston SR (2018) Phytosterol-based edible oleogels: a novel way of replacing saturated fat in food. Nutr Bull 43(2):189–194PubMedPubMedCentralCrossRefGoogle Scholar
- 35.Castro BM, de Almeida RF, Silva LC, Fedorov A, Prieto M (2007) Formation of ceramide/sphingomyelin gel domains in the presence of an unsaturated phospholipid: a quantitative multiprobe approach. Biophy J 93(5):1639–1650CrossRefGoogle Scholar
- 36.Westerlund B, Slotte JP (2009) How the molecular features of glycosphingolipids affect domain formation in fluid membranes. Biochimica et Biophysica Acta (BBA)-Biomembranes 1788(1):194–201CrossRefGoogle Scholar
- 37.Lam S, Velikov KP, Velev OD (2014) Pickering stabilization of foams and emulsions with particles of biological origin. Curr Opin Colloid Interface Sci 19(5):490–500CrossRefGoogle Scholar
- 38.Rosenberg M, Rosenberg E (1985) Bacterial adherence at the hydrocarbon–water interface. Oil Petrochem Pollut 2(3):155–162CrossRefGoogle Scholar
- 39.Frischmann A, Neudl S, Gaderer R, Bonazza K, Zach S, Gruber S, Spadiut O, Friedbacher G, Grothe H, Seidl-Seiboth V (2013) Self-assembly at air/water interfaces and carbohydrate binding properties of the small secreted protein EPL1 from the fungus Trichoderma atroviride. J Biol Chem 288:4278–4287PubMedCrossRefGoogle Scholar
- 40.Bonazza K, Gaderer R, Neudl S, Przylucka A, Allmaier G, Druzhinina IS, Grothe H, Friedbacher G, Seidl-Seiboth V (2015) The fungal cerato-platanin protein EPL1 forms highly ordered layers at hydrophobic/hydrophilic interfaces. Soft Matter 11(9):1723–1732PubMedCrossRefGoogle Scholar
- 41.Li X, Jin Z, Gao F, Lu J, Cai G, Dong J, Yu J, Yang M (2014) Characterization of barley serpin Z7 that plays multiple roles in malt and beer. J Agric Food Chem 62(24):5643–5650PubMedCrossRefGoogle Scholar
- 42.Specker C, Niessen L, Vogel RF (2014) In vitro studies on the main beer protein Z4 of Hordeum vulgare concerning heat stability, protease inhibition and gushing. J Inst Brew 120:85–92CrossRefGoogle Scholar
- 43.Moonen H, Bas H (2004) Mono- and diglycerides. In: Whitehurst RJ (ed) Emulsifiers in food technology. Blackwell Publishing Ltd, OxfordGoogle Scholar
- 44.Keller RCA, Orsel R, Hamer RJ (1997) Competitive adsorption behaviour of wheat flour components and emulsifiers at an air–water interface. J Cereal Sci 25:175–183CrossRefGoogle Scholar
- 45.Kharkwal H, Panthari P, Pant MK, Kharkwal H, Kharkwal AC, Joshi DD (2012) Foaming glycosides: a review. IOSR J Pharm 2(5):23–28Google Scholar
- 46.Al-Ahmad K (2015) The definition, preparation and application of rhamnolipids as biosurfactants. Int J Nutr Food Sci 4(6):613–623CrossRefGoogle Scholar
- 47.Xu W, Gu H, Zhu X, Zhong Y, Jiang L, Xu M, Song A, Hao J (2015) CO2-controllable foaming and emulsification properties of the stearic acid soap systems. Langmuir 31(21):5758–5766PubMedCrossRefGoogle Scholar
Copyright information
Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made.