Biomedical subjects

Tharwat Tadros

Publications and source records attributed to Tharwat Tadros.

5 recordsLinked to original sources

PubMed2006

Interaction forces in thin liquid films stabilized by hydrophobically modified inulin polymeric surfactant. 1. Foam films.

Using the interferometric method of Scheludko-Exerowa for investigation of foam films, we have obtained results using a hydrophobically modified inulin polymeric surfactant (INUTEC SP1). Measurements were carried out at constant INUTEC SP1 concentration of 2 x 10(-)(5) mol.dm(-)(3) and at various NaCl concentrations (in the range 1 x 10(-)(4) to 2 mol.dm(-)(3)). At constant capillary pressure of 50 Pa, the film thickness decreased gradually with an increase in NaCl concentration up to 10(-)(2) mol.dm(-)(3) NaCl above which the film thickness remains virtually constant at about 16 nm. This reduction in film thickness with an increase in NaCl concentration is due to the compression of the double layer and at the critical electrolyte concentration (C(el,cr) = 10(-)(2) mol.dm(-)(3)) the electrostatic component of the disjoining pressure is completely screened and the remaining pressure is due to the steric interaction between the adsorbed polymer layers. Disjoining pressure-thickness (Pi-h) isotherms were obtained at C(el) < C(el,cr) (10(-)(4) - 10(-)(3) mol.dm(-)(3)) and C(el) > C(el,cr) (0.5, 1, and 2 mol.dm(-)(3)). In the first case, the disjoining pressure isotherms could be fitted using the classical DLVO theory, Pi = Pi(el) + Pi(vw), and using the constant charge model. At C(el) > C(el,cr), the main repulsion is due to the steric interaction between the polyfructose loops that exist at the air-water interface, i.e., Pi = Pi(st) + Pi(vw). Under these conditions, there is a sharp transition from DLVO to non-DLVO forces. In the latter case, the interaction could be described using the de Gennes' scaling theory. This gave an adsorbed layer thickness of 6.5 nm which is in reasonable agreement with the values obtained at the solid-solution interface. The Pi-h isotherms showed that these foam films are not very stable and they tend to collapse above a critical capillary pressure (of about 1 x 10(3) Pa), and these results could be used to predict the foam stability.

Electrolytes↗

PubMed2004

Formation and stability of nano-emulsions.

This review describes the principles of formation and stability of nano-emulsions. It starts with an introduction highlighting the main advantages of nano-emulsions over macroemulsions for personal care and cosmetic formulations. It also describes the main problems with lack of progress on nano-emulsions. The second section deals with the mechanism of emulsification and the dynamic light scattering technique for measurement of the droplet size of nano-emulsions. This is followed by a section on methods of emulsification and the role of surfactants. Three methods are described for nano-emulsion preparation, namely high energy emulsification (using homogenisers), low energy emulsification whereby water is added to an oil solution of the surfactant and the principle of the phase inversion temperature (PIT). A section is devoted to steric stabilisation and the role of the adsorbed layer thickness. The problem of Ostwald ripening (which is the main instability process of nano-emulsions) is described in some detail. The methods that can be applied to reduce Ostwald ripening are briefly described. This involves the addition of a second less soluble oil phase such as squalene and/or addition of a strongly adsorbed and water insoluble polymeric surfactant. The last part of the review gives some examples of nano-emulsions that are prepared by the PIT method as well as using high pressure homogeniser. A comparison of the two methods is given and the rate of Ostwald ripening is measured in both cases. The effect of changing the alkyl chain length and branching of the oil was investigated using decane, dodecane, tertadecane, hexadecane and isohexadecane. The branched oil isohexadcecane showed higher Ostwald ripening rate when compared with a linear chain oil with the same carbon number.

Journal Article↗

PubMed2004

Application of rheology for assessment and prediction of the long-term physical stability of emulsions.

This review deals with the use of rheology for assessment and prediction of the long-term physical stability of emulsions. It starts with an introduction, highlighting the importance of having accelerated test to predict emulsion stability. This is followed by a section on the stability/instability of emulsion systems, giving a brief summary of the driving force of each instability process and its prevention. The classical techniques that can be applied for assessment of creaming or sedimentation, flocculation, Ostwald ripening, coalescence and phase inversion are briefly described. This is followed by several sections on the application of rheological techniques to assess and predict each of these instabilities. This involves the use of steady state shear stress-shear rate measurements, constant stress (creep) measurements and dynamic (oscillatory) techniques. The last section gives an example of model emulsions to illustrate the correlation between the various break-down processes with the rheological characteristics of the system.

Journal Article↗

PubMed2003

Interaction forces between particles containing grafted or adsorbed polymer layers.

The interaction forces between particles containing grafted or adsorbed polymer layers have been investigated using rheological and surface force measurements. Polystyrene latex dispersions with grafted poly(ethylene oxide) (PEO) chains (M=2000) were used for the rheological measurements. Results were also obtained for latex dispersions stabilised with adsorbed graft copolymers of poly(methyl methacrylate-methacrylic acid) with methoxy capped PEO chains (M=750). The relative viscosity eta(r)-volume fraction phi curves for the latex dispersions with grafted PEO chains were established for three particle radii of 77.5, 306 and 502 nm. For comparison the eta(r)-phi curve was calculated using the Dougherty-Krieger equation. This allows one to obtain the adsorbed layer thickness delta as a function of phi. The results showed a decrease of delta with increase of phi, which was attributed to the interpenetration and/or compression of the PEO chains on increasing phi. Viscoelastic measurements as a function of phi showed a change from predominantly viscous to predominantly elastic response at a critical volume fraction, which indicated the onset of the strong steric repulsion when the polymer layers begin to overlap. A similar trend was obtained with the latex particles containing adsorbed graft copolymer layers. A scaling law was used to fit the elastic part of the logG'-log phi curve (where G' is the elastic modulus). This fit could be used to estimate the compressibility of the PEO chains. The correlation of the rheology of concentrated sterically stabilised dispersions with interparticle interactions was investigated by measuring the energy-distance curves for the graft copolymer that was adsorbed on smooth mica sheets. Using de Gennes scaling theory, it was possible to calculate the energy of interaction between the polymer layers. The high frequency modulus of the latex dispersions was obtained as a function of the volume fraction and the results were compared with those calculated from the potential of the mean force. The trends in the variation of the modulus with volume fraction were similar for the experimental rheological results and those calculated using the directly measured interaction forces. The above results demonstrated the powerful use of rheological measurements for studying the interaction between sterically stabilised dispersions in concentrated systems.

Adsorption↗

PubMedDate not supplied

Principles of emulsion stabilization with special reference to polymeric surfactants.

This overview summarizes the basic principles of emulsion stabilization with particular reference to polymeric surfactants. The main breakdown processes in emulsions are briefly described. A section is devoted to the structure of polymeric surfactants and their conformation at the interface. Particular attention is given to two polymeric surfactants that are suitable for oil-in-water (O/W) and water-in-oil (W/O) emulsions. For O/W emulsions, a hydrophobically modified inulin (HMI), obtained by grafting several alkyl groups on the backbone of the inulin (polyfructose) chain, is the most suitable. For W/O emulsions, an A-B-A block copolymer of polydroxystearic acid (PHS), the A chains, and polyethylene oxide (PEO), the B chain, is the most suitable. The conformation of both polymeric surfactants at the O/W and W/O interfaces is described. A section is devoted to the interaction between emulsion droplets containing adsorbed polymer surfactant molecules. This interaction is referred to as steric stabilization, and it is a combination of two main effects, namely, unfavorable mixing of the A chains, referred to as the mixing interaction, Gmix, and loss of configurational entropy on significant overlap of the stabilizing chains, referred to as elastic interaction, Gel. The criteria for effective steric stabilization are summarized. O/W emulsions based on HMI are described, and their stability in water and in aqueous electrolyte solutions is investigated using optical microscopy. Very stable emulsions can be produced both at room temperature and at 50 degrees C. The reason for this high stability is described in terms of the multipoint anchoring of the polymeric surfactant (by several alkyl groups), the strong hydration of the inulin (polyfructose) chains, and the high concentration of inulin in the adsorbed layer. W/O emulsions using PHS-PEO-PHS block copolymer can be prepared at a high volume fraction of water, varphi, and these emulsions remain fluid up to high varphi values (> 0.6). These emulsions also remain stable for several months at room temperature and at 50 degrees C. The last two sections are concerned with the problems of creaming or sedimentation and phase inversion. Creaming or sedimentation can be prevented by the use of "thickeners" in the continuous phase. These molecules produce non-Newtonian systems that will have a high residual or zero shear viscosity. The latter, which may exceed 1000 Pas, can also be prevented by control of the bulk (or elastic) modulus of the system. Phase inversion in O/W emulsions can also be prevented using HMI, since this polymeric surfactant is not soluble in the oil phase. As long as coalescence and Ostwald ripening are prevented, the emulsions can remain stable for very long times both at room temperature and at 50 degrees C.

Cosmetics↗