Chemical and Biomedical Engineering - Research Publications

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    Heat induced denaturation, aggregation and gelation of almond proteins in skim and full fat almond milk
    Devnani, B ; Ong, L ; Kentish, S ; Gras, S (Elsevier BV, 2020-09-30)
    The effect of thermal treatment (45-95 ⁰C for 30 minutes) on the structure of almond milk proteins was assessed, as the unfolding and association of these proteins in response to heat is not well understood. Above 55 ⁰C, protein surface hydrophobicity and particle size increased and alpha helical structure decreased, reducing the stability of skim or full fat milk. Fractal protein clusters were observed at 65-75 ⁰C and weakly flocculated gels with a continuous protein network occurred at 85-95 ⁰C, resulting in gels with high water holding capacity and a strength similar to dairy gels. The presence of almond fat increased gel strength but led to a more heterogenous microstructure, which may be improved by homogenisation. Elasticity could also be increased with protein concentration. This study improves our understanding of the heat stability of almond milk proteins and indicates their potential as a gelling ingredient for vegan and vegetarian products.
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    The role of cations in regulating reaction pathways driven by Bacillus circulans β-galactosidase
    Karimi Alavijeh, M ; Meyer, AS ; Gras, S ; Kentish, SE (Elsevier, 2020-09-01)
    A β-galactosidase (EC 3.2.1.23) from Bacillus circulans (Biolacta FN5) can catalyse transgalactosylation reactions with lactose as a donor. In addition to their function as cofactors and structural stabilisers in biocatalytic reactions, cations can play a role in salt-bridge interactions and electrostatic charge screening of proteins. In this work, we investigated the impact of calcium, magnesium, sodium and potassium, commonly found in dairy whey systems, on the transgalactosylation kinetics of the β-galactosidase from Bacillus circulans. Both molecular modeling and quantitative experimental methods were used to assess enzyme aggregation and resulting loss in enzyme activity that is initiated by high concentrations of these cations. The effect of this loss in activity with time was studied during the transgalactosylation of N-acetylglucosamine (GlcNAc) to N-acetyllactosamine (LacNAc) using lactose as the donor. No significant change in hydrolysis or transgalactosylation reaction kinetics was observed at low concentrations of divalent cations (Ca2+ or Mg2+) or up to 100 mM of monovalent cations (Na+ or K+). The enzymatic yield and selectivity, however, were significantly affected at concentrations of 100 mM of Ca2+ or Mg2+. These changes were the result of both the loss in enzyme activity and a reduction in the reaction rate constant for hydrolysis and formation of the undesired isomer, Allo-LacNAc. In particular, addition of magnesium enhanced the selectivity for LacNAc over Allo-LacNAc, with no significant reduction in the LacNAc yield. These findings suggest that cations can be employed to regulate the action of β-galactosidase during transgalactosylation through the formation of protein aggregates.
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    The application of forward osmosis to dairy processing
    Chen, GQ ; Gras, SL ; Kentish, SE (Elsevier, 2020-09-01)
    This work assesses the feasibility for concentrating process streams within dairy processing facilities using commercial forward osmosis membranes; to increase their total solids concentrations before entering energy intensive unit operations including thermal evaporators and spray dryers. These streams include demineralised whey, lactose, whey protein concentrate, sweet whey and skim milk. FTSH2O cellulose acetate (CTA) and Aquaporin flat sheet membranes are used with magnesium chloride concentrations of 1.66 ± 0.12 M as the draw solution. The experimental data are fitted to conventional mathematical models for forward osmosis, further modified by considering the nonlinear relationship between osmotic pressure and solute concentration. The diffusion coefficients of magnesium chloride in 1.6 M solutions at 10 °C, 20 °C and 50 °C are obtained and reported for the first time. Minimal fouling and a significantly smaller degree of concentration polarisation was observed on the membrane surface during lactose concentration compared to the concentration of other dairy solutions, due to the absence of proteins and calcium phosphate salts. The transfer of magnesium into the concentrated products was monitored and shown to be below 100 mg per 100 g dry powder. Acid cleaning alone was not effective in recovering pure water flux, and enzyme cleaners at neutral pH were needed given the limited pH tolerance (3–8) of the CTA membranes. Total solids concentrations of the concentrated dairy streams by forward osmosis (up to 40%) exceed those which can be achieved by nanofiltration and reverse osmosis (i.e., 15–20%). This study shows that forward osmosis is an effective approach to concentrate relevant dairy streams to achieve high concentration factors (e.g. >4 for sweet whey samples) without jeopardising product quality.
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    Utilisation of salty whey ultrafiltration permeate with electrodialysis
    Talebi, S ; Kee, E ; Chen, GQ ; Bathurst, K ; Kentish, SE (Elsevier, 2019-12-01)
    Salty whey is a waste by-product that incurs increasingly high disposal costs for the dairy industry. This study investigated electrodialysis of the ultrafiltration permeate of salty whey as either a concentrate for the treatment of sweet whey or as a source of lactose and salt. The type of concentrate (0.1 m NaCl or salty whey permeate) did not affect the rate of sweet whey demineralisation or the energy consumed per tonne of whey, but less sodium and more divalent cations were removed when salty whey permeate was used as the concentrate. Salty whey permeate could be effectively demineralised using either 0.1 m NaCl or a second stream of salty whey permeate as the concentrate. The concentrate purity could be enhanced using monovalent selective membranes without increasing the energy consumption of the process (3.2 ± 0.3 kWh per kg of NaCl removed from the diluate at 15 V).
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    Enhanced CO2 bio-utilization with a liquid-liquid membrane contactor in a bench-scale microalgae raceway pond
    Xu, X ; Martin, GJO ; Kentish, SE (Elsevier Ltd, 2019-12-01)
    Microalgae are able to absorb CO2 generated from sources such as flue gas to produce biomass with high lipid content. In this research, an immersed liquid-liquid membrane contactor was investigated to deliver CO2 captured by a chemical solvent to the microalgae culture via semipermeable membranes. Experiments showed that the CO2 mass transfer could be facilitated by using a thinner membrane support layer, or avoiding a support altogether, as the support was liquid filled which reduced the mass transfer coefficient. In order to better condition the culture media, the solvent flow was controlled by pH feedback. This scenario showed comparable biomass productivity (0.10 g L-1 d-1) to the conventional direct bubbling method, but with a lower energy cost and higher CO2 utilization efficiency. Further, a pond liner was formed from flat sheet membranes as a more effective alternative to a hollow fiber arrangement. The optimized system achieved a CO2 utilization efficiency of up to 90% compared to 47% with the uncontrolled hollow fiber membrane system and 11% for air sparging, thereby reducing the CO2 released to the atmosphere.
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    Critical review of strategies for CO2 delivery to large-scale microalgae cultures
    Zheng, Q ; Xu, X ; Martin, GJO ; Kentish, SE (CHEMICAL INDUSTRY PRESS, 2018-11-01)
    Microalgae have great, yet relatively untapped potential as a highly productive crop for the production of animal and aquaculture feed, biofuels, and nutraceutical products. Compared to conventional terrestrial crops they have a very fast growth rate and can be produced on non-arable land. During microalgae cultivation, carbon dioxide (CO2) is supplied as the carbon source for photosynthesising microalgae. There are a number of potential CO2 supplies including air, flue gas and purified CO2. In addition, several strategies have been applied to the delivery of CO2 to microalgae production systems, including directly bubbling CO2-rich gas, microbubbles, porous membrane spargers and non-porous membrane contactors. This article provides a comparative analysis of the different CO2 supply and delivery strategies and how they relate to each other.
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    Separation Technologies for Salty Wastewater Reduction in the Dairy Industry
    Chen, GQ ; Gras, SL ; Kentish, SE (Taylor & Francis, 2019-10-02)
    The wastewater discharged by cheese manufacturing processes is highly saline. This waste is generated from whey demineralization, chromatography and clean-in-place processes. Salty effluent can be diluted with other effluents and discharged as trade waste but the high salinity can trigger penalties imposed by local water authorities. Alternatively, such waste can be sent to evaporation ponds, but in some areas in Australia, environmental impacts regarding land degradation, odor and dust have prevented further pond construction. Similar concentrate and brine management issues are emerging in the seawater desalination and mining industries. This paper reviews a range of commercial and emerging separation technologies that may be suitable to both reduce the costs of salty wastewater treatment and to improve the recoveries of dairy and salt-based products. These technologies have been commercialized or applied at a laboratory scale to the fields of desalination and brine concentration. Each technology is discussed in terms of its principle of operation and suitability for treating high-salinity dairy wastewater. The potential energy requirement and processing cost of each technology is identified with respect to feed water salinity, to provide additional insights into the energy and cost efficiencies of these technologies.
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    Organic solvent nanofiltration of binary vegetable oil/terpene mixtures: Experiments and modelling
    Abdellah, MH ; Liu, L ; Scholes, CA ; Freeman, BD ; Kentish, SE (ELSEVIER, 2019-03-01)
    Bio-derived solvents such as ρ-cymene, d-limonene and α-pinene represent feasible alternatives to n-11 hexane for the extraction of vegetable oils. However, the large-scale utilization of these solvents is 12 still limited mainly owing to their high boiling points and latent heats of vaporization. In this work, the 13 performance of composite polydimethylsiloxane/polyacrylonitrile (PDMS/PAN) organic solvent 14 nanofiltration membranes in the recovery of these solvents from their binary mixtures with canola oil 15 is investigated. The sorption isotherms of the mixtures were first studied using free-standing PDMS 16 films and the multicomponent Flory-Huggins model used to determine the resulting interaction 17 parameters. The partial solvent uptake decreased with increasing oil concentration in the mixture. On 18 the other hand, the partial oil uptake in the solvent mixture was higher than that of the pure oil which 19 was attributed to the swelling effects induced by solvents. The effects of feed concentration (10-30 20 wt. % oil), feed temperature (25-40 °C), transmembrane pressure (5-30 bar), and cross-flow velocity 21 (18-52 cm s-1) on the membrane performance were then studied in a cross-flow membrane setup. 22 Maxwell-Stefan formulations were combined with the ternary Flory-Huggins solubility model to 23 successfully describe these flux data.
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    The effects of medium salinity on the delivery of carbon dioxide to microalgae from capture solvents using a polymeric membrane system
    Zheng, Q ; Martin, GJO ; Kentish, SE (SPRINGER, 2019-06-01)
    Efficient provision of carbon dioxide to microalgae is one of the major challenges to cost-effective large-scale cultivation. Previously, we have demonstrated the effectiveness of a novel membrane system in delivering CO2 to a marine strain of Chlorella sp. from CO2-loaded solvents. In this approach, the solvent is pumped through a non-porous hollow fibre membrane immersed in a microalgae medium, allowing passive transfer of CO2 that is utilised by the microalgae to enhance their growth, while simultaneously regenerating the solvent. In this article, we compare the growth of both fresh water and marine strains of algae using this membrane delivery system. While the fresh water medium has less pH buffering capacity and can dissolve less CO2, it proves similarly effective in delivering CO2 to the growing algae. Both the freshwater and marine species of Chlorella have slightly higher growth rates than the other species tested—Dunaliella tertiolecta and Haematococcus pluvialis. However, due to the lower osmotic pressure of the fresh water medium, more water is drawn through the membrane into the solvent than when the salt water medium is used. In conclusion, while CO2 delivery through the membrane system is effective for both salt and fresh water media, better performance is obtained for the salt water medium.
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    Fouling and in-situ cleaning of ion-exchange membranes during the electrodialysis of fresh acid and sweet whey
    Talebi, S ; Chen, GQ ; Freeman, B ; Suarez, F ; Freckleton, A ; Bathurst, K ; Kentish, SE (ELSEVIER SCI LTD, 2019-04-01)
    This work investigated the fouling of ion-exchange membranes during the electrodialysis of sweet and acid dairy whey. Fresh whey was used, rather than solutions made up in the laboratory, giving a unique perspective. While membrane fouling occurred in all experiments, the effects on system performance were limited. Reductions in the current during pure NaCl circulation fell to a minimum of 80% of the original value after 5 h of whey processing. The use of an alkaline concentrate resulted in the strongest increase in system resistance, but the mineral deposits formed appeared to detach readily, thereby reducing these effects. The use of an acidic concentrate gave significantly greater rates of lactic acid removal, which is important in industrial applications. A solution of HCl with a pH of 1.0 ± 0.15 was effective for in-situ cleaning of the mineral deposits. However, protein deposits were not readily removed using the recommended base cleaning formula of 3% NaCl at a pH of 9.2 ± 0.2.