Suspension (chemistry): Difference between revisions
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[[Image:colloidal_dispersion.jpg|frame|right|Major destabilisation mechanisms for liquid dispersions]] |
[[Image:colloidal_dispersion.jpg|frame|right|Major destabilisation mechanisms for liquid dispersions]] |
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These destabilisations can be classified into two major processes: |
These destabilisations can be classified into two major processes: |
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:1-Migration phenomena : |
:1-Migration phenomena : whe '''hi'''reby the difference in density between the continuous and dispersed phase, leads to gravitational phase separation. In the case of suspensions [[sedimentation]] occurs as the dispersed phase is denser than the continuous phase. |
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:2-Particle size increase phenomena: whereby the suspended particles join together and increase in size. Below are the two types of this phenomena. |
:2-Particle size increase phenomena: whereby the suspended particles join together and increase in size. Below are the two types of this phenomena. |
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Revision as of 15:21, 24 February 2011
In chemistry, a suspension is a heterogeneous fluid containing solid particles that are sufficiently large for sedimentation. Usually they must be larger than 1 micrometer.[1] The internal phase (solid) is dispersed throughout the external phase (fluid) through mechanical agitation, with the use of certain excipients or suspending agents. Unlike colloids, suspensions will eventually settle. An example of a suspension would be sand in water. The suspended particles are visible under a microscope and will settle over time if left undisturbed. This distinguishes a suspension from a colloid, in which the suspended particles are smaller and do not settle.[2] Colloids and suspensions are different from solutions, in which the dissolved substance (solute) does not exist as a solid, and solvent and solute are homogeneously mixed.
A suspension of liquid droplets or fine solid particles in a gas is called an aerosol or particulate. In the atmosphere these consist of fine dust and soot particles, sea salt, biogenic and volcanogenic sulfates, nitrates, and cloud droplets.
Suspensions are classified on the basis of the dispersed phase and the dispersion medium, where the former is essentially solid while the latter may either be a solid, a liquid, or a gas.
In modern chemical process industries, high shear mixing technology has been used to create many novel suspensions.
Suspensions are unstable from the thermodynamic poin of view; however, they can be kinetically stable over a large period of time, which determines their shelf life. This time span needs to be measured to ensure the best product quality to the final consumer. “Dispersion stability refers to the ability of a dispersion to resist change in its properties over time.” D.J. McClements. [3]
Destabilisation phenomena of a dispersion
These destabilisations can be classified into two major processes:
- 1-Migration phenomena : whe hireby the difference in density between the continuous and dispersed phase, leads to gravitational phase separation. In the case of suspensions sedimentation occurs as the dispersed phase is denser than the continuous phase.
- 2-Particle size increase phenomena: whereby the suspended particles join together and increase in size. Below are the two types of this phenomena.
- reversibly (flocculation)
- irreversibly (aggregation)
Technique monitoring physical stability
Multiple light scattering coupled with vertical scanning is the most widely used technique to monitor the dispersion state of a product, hence identifying and quantifying destabilisation phenomena[4][5][6][7]. It works on concentrated dispersions without dilution. When light is sent through the sample, it is backscattered by the particles. The backscattering intensity is directly proportional to the size and volume fraction of the dispersed phase. Therefore, local changes in concentration (sedimentation) and global changes in size (flocculation, aggregation) are detected and monitored.
Accelerating methods for shelf life prediction
The kinetic process of destabilisation can be rather long (up to several months or even years for some products) and it is often required for the formulator to use further accelerating methods in order to reach reasonable development time for new product design. Thermal methods are the most commonly used and consists in increasing temperature to accelerate destabilisation (below critical temperatures of phase inversion or chemical degradation). Temperature affects not only the viscosity, but also interfacial tension in the case of non-ionic surfactants or more generally interactions forces inside the system. Storing a dispersion at high temperatures enables to simulate real life conditions for a product (e.g. tube of sunscreen cream in a car in the summer), but also to accelerate destabilisation processes up to 200 times.
Mechanical acceleration including vibration, centrifugation and agitation are sometimes used. They subject the product to different forces that pushes the particles / droplets against one another, hence helping in the film drainage. However, some emulsions would never coalesce in normal gravity, while they do under artificial gravity[8]. Moreover, segregation of different populations of particles have been highlighted when using centrifugation and vibration.[9]
Common examples
- Mud or muddy water, is where soil, clay, or silt particles are suspended in water
- Flour suspended in water, as pictured to the right (at the top of the page)
- Paint
- Chalk powder suspended in water
- Dust particles suspended in air
- Algae in water
See also
References
- ^ Chemistry: Matter and Its Changes, 4th Ed. by Brady, Senese, ISBN 0471215171
- ^ The Columbia Electronic Encyclopedia, 6th ed.
- ^ “Food emulsions, principles, practices and techniques” CRC Press 2005.2- M.P.C. Silvestre, E.A. Decker, McClements Food hydrocolloids 13 (1999) 419-424
- ^ I. Roland, G. Piel, L. Delattre, B. Evrard International Journal of Pharmaceutics 263 (2003) 85-94
- ^ C. Lemarchand, P. Couvreur, M. Besnard, D. Costantini, R. Gref, Pharmaceutical Research, 20-8 (2003) 1284-1292
- ^ O. Mengual, G. Meunier, I. Cayre, K. Puech, P. Snabre, Colloids and Surfaces A: Physicochemical and Engineering Aspects 152 (1999) 111–123
- ^ P. Bru, L. Brunel, H. Buron, I. Cayré, X. Ducarre, A. Fraux, O. Mengual, G. Meunier, A. de Sainte Marie and P. Snabre Particle sizing and characterisation Ed T. Provder and J. Texter (2004)
- ^ J-L Salager, Pharmaceutical emulsions and suspensions Ed Françoise Nielloud,Gilberte Marti-Mestres (2000)
- ^ P. Snabre, B. Pouligny Langmuir, 24 (2008) 13338-13347