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Pharmaceutics I

Rheology of Suspensions

Dr. Mohammad Bayan Faculty of Pharmacy, Philadelphia University, Amman, Jordan  Introduction:

 Poise and centipoise  Dyne.sec.cm-2

 Newtonian and Non-Newtonian Fluids

Dr. Mohammad Bayan 2  Newton’s law of flow

Dr. Mohammad Bayan 3 (F), F'/A

Strain or Deformation

Velocity Gradient (G), dv/dr

Dr. Mohammad Bayan 4  The Shearing Stress (F) is the force per unit area (F'/A) required to cause flow.

 Rate of Shear or velocity gradient (dv/dr:G) is the velocity difference dv between two planes of liquid separated by an infinite distance dr.

Dr. Mohammad Bayan 5 F'/A = η dv/dr...... (1)  Newton recognized that: •Where η is a constant known as the higher the Viscosity viscosity of a liquid η = F / G...... (2) F = η G...... (3)

•Fluidity is the reciprocal of viscosity the greater shearing stress

F'/A α dv/dr

Dr. Mohammad Bayan 6  Example:  What is the shear rate when an oil is rubbed into the skin with a relative rate of motion between the fingers and the skin of about 10 cm per seconds and the film thickness is about 0.02 cm?

 Rate of Shear dv/dr = G  G= 10 cm per seconds / 0.02 cm = 500 sec -1

Dr. Mohammad Bayan 7  Newtonian flow

Dr. Mohammad Bayan 8  Newtonian flow

 Temperature

 Pressure

 Chemical composition

, simple organic liquids, true solutions, dilute suspensions and dilute emulsions are examples of Newtonian systems.

Dr. Mohammad Bayan 9  Non-Newtonian flow

 Fail to follow Newton’s equation of flow

 Characterised by a change in the viscosity with increasing shear rate

 Examples: colloidal solutions, emulsions, liquid suspensions, and ointments.

Dr. Mohammad Bayan 10 Non-Newtonian flow

Plastic Pseudoplastic Dilatant

Dr. Mohammad Bayan 11  Plastic flow

 Bingham bodies

 Starts after exceeding a certain yield value of shearing stress

 Does not pass through the origin

 Shear-thinning systems

 Elastic below the yield value

Dr. Mohammad Bayan 12  Plastic flow

 Tomatoes Sauce, Honey and Flocculated particles in a concentrated suspension usually show a plastic flow

Dr. Mohammad Bayan 13  Pseudoplastic flow

 No yield value

 The consistency curve begins at origin or at least approach it at low rate of shear

 Shear-thinning systems

 Examples: natural and synthetic gums such as liquid dispersions of tragacanth, sodium alginate, methyl cellulose, and sodium carboxymethyl cellulose

Dr. Mohammad Bayan 14  Pseudoplastic flow

Dr. Mohammad Bayan 15  Dilatant flow

 Exhibit an increase in volume when sheared, and the viscosity increases with shear rate.

 Shear-thickening systems

 High percentage of solids in the formulation (50 % or greater). When shear is removed the system returns to original state of fluidity.

 Example: deflocculated suspension

Dr. Mohammad Bayan 16  Explanation of dilatant flow behaviour

Dr. Mohammad Bayan 17  Dilatant flow

• The inverse of pseudo plastic diagram

Dr. Mohammad Bayan 18   “An isothermal and comparatively slow recovery, on standing of a material whose consistency is lost through shearing”.

 Only applied for plastic and pseudoplastic systems

 Reversible gel–sol transformation

Dr. Mohammad Bayan 19  Upon setting, a network gel forms and provides a rigid matrix that will stabilise suspensions and gels.

 When stressed (by shaking), the matrix relaxes and forms a sol with the characteristics of a liquid dosage form for ease of use.

 A thixotropic agent such as microcrystalline cellulose is incorporated into the suspensions or emulsions to give a high viscosity.

Dr. Mohammad Bayan 20  Rheology of suspensions

 High apparent viscosity at low rates of shear

 At higher rates of shear, the apparent viscosity should fall sufficiently for the product to be poured easily

 External use spread easily without excessive dragging

 Injection pass easily through a hypodermic needle with only moderate pressure

Dr. Mohammad Bayan 21  A flocculated system partly fulfils the previous criteria

 A pseudoplastic or plastic behaviour associated with thixotropy is exhibited as the structure progressively breaks down under shear and then shows time-dependent recovery

 It may not be sufficient to prevent rapid settling, unless a high concentration of dispersed phase is present

 Suspending agents

 A deflocculated system Newtonian behaviour

Dr. Mohammad Bayan 22 Dr. Mohammad Bayan 23