Emulsion

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Organogel-Emulsions with Mixtures of β-Sitosterol and γ-Oryzanol: Influence of Water Activity and Type of Oil Phase on Gelling Capability

Journal Title, Volume, Page: 
Journal of Agricultural and Food Chemistry, 60 (13), p 3462–3470
Year of Publication: 
2012
Authors: 
Hassan Sawalha
Chemical Engineering and Material Science, An-Najah National University, P.O. Box 7, Nablus, Palestine
Current Affiliation: 
Chemical Engineering Department, An-Najah National University, Nablus, Palestine
Ruud den Adel
Unilever Research and Development Vlaardingen, Olivier van Noortlaan 120, 3133 AT Vlaardingen, The Netherlands
Paul Venema
Laboratory of Physics and Physical Chemistry of Foods, Department of Agrotechnology and Food Sciences, Wageningen University, Bomenweg 2, 6703 HD Wageningen, The Netherlands
Arjen Bot
Unilever Research and Development Vlaardingen, Olivier van Noortlaan 120, 3133 AT Vlaardingen, The Netherlands
Eckhard Flöter
Unilever Research and Development Vlaardingen, Olivier van Noortlaan 120, 3133 AT Vlaardingen, The Netherlands
Erik van der Linden
Laboratory of Physics and Physical Chemistry of Foods, Department of Agrotechnology and Food Sciences, Wageningen University, Bomenweg 2, 6703 HD Wageningen, The Netherlands
Preferred Abstract (Original): 
In this study, water-in-oil emulsions were prepared from water containing different salt concentrations dispersed in an oil phase containing a mixture of β-sitosterol and γ-oryzanol. In pure oil, the β-sitosterol and γ-oryzanol molecules self-assemble into tubular microstructures to produce a firm organogel. However, in the emulsion, the water molecules bind to the β-sitosterol molecules, forming monohydrate crystals that hinder the formation of the tubules and resulting in a weaker emulsion-gel. Addition of salt to the water phase decreases the water activity, thereby suppressing the formation of sitosterol monohydrate crystals even after prolonged storage times (1 year). When the emulsions were prepared with less polar oils, the tubular microstructure was promoted, which significantly increased the firmness of the emulsion-gel. The main conclusion of this study is that the formation of oryzanol and sitosterol tubular microstructure in the emulsion can be promoted by reducing the water activity and/or by using oils of low polarity.
elhamouz's picture

Droplet Break-Up By In-Line Silverson Rotor–Stator Mixer

Journal Title, Volume, Page: 
Chemical Engineering Science Volume 66, Issue 10, 15 May 2011, Pages 2068-2079
Year of Publication: 
2011
Authors: 
A.El-Hamouz
Department of Chemical Engineering, An-Najah National University, Nablus, West Bank, PO Box 7, The Palestinian Authority, Occupied Palestinian Territory
Current Affiliation: 
Department of Chemical Engineering, An-Najah National University, Nablus, Palestine
S. Hall
School of Chemical Engineering, University of Birmingham, Edgbaston, Birmingham, B15 2TT, UK
M.Cooke
School of Chemical Engineering & Analytical Science, The University of Manchester, Sackville Street, PO Box 88, Manchester,
A.J.Kowalski
Unilever Research & Development, Port Sunlight Laboratory, Quarry Road East, Bebington, Wirral, CH63 3JW, UK
Preferred Abstract (Original): 
Silverson high shear in-line rotor–stator mixers are widely applied in industry for the manufacture of emulsion-based products but the current understanding of droplet breakage and coalescence in these devices is limited. The aim of this paper is to increase the understanding of droplet break-up mechanisms and to identify appropriate literature correlations for in-line rotor–stator mixers. Silicone oils with viscosities ranging from 9.4 to 969 mPa s were emulsified with surfactant in an in-line Silverson at rotor speeds up to 11,000 rpm and flow rates up to 5 tonnes/h. The effect of rotor speed, flow rate, dispersed phase fraction up to 50 wt%, inlet drop size and viscosity ratio on droplet size was investigated. It was found that rotor speed and dispersed phase viscosity have a significant effect on the droplet size, while flow rate, inlet droplet size, viscosity ratio and dispersed phase volume have a lesser effect. The results indicate that low viscosity droplets are broken by turbulent inertial stresses, while droplets smaller than the Kolmogorov length scale are broken by a combination of inertial and viscous stresses. It also appears that the weak dependence of drop size on flow rate enables the energy efficiency of an in-line high shear Silverson to be significantly improved by operating at as high a flow rate as possible.
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