Rheology of Liquids Part I Flashcards

1
Q

What is the definition of rheology, and the definition of viscosity?

A

Rheology: study of flow properties of materials
Viscosity: Resistance of a liquid to flow when it is subjected to stress

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2
Q

How to calculate viscosity in general?

A

Shear stress/ Shear rate,

where shear stress = F/A and shear rate = velocity gradient

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3
Q

What are some properties of Newtonian Liquids?

A
  • rheological properties follow Newton’s Law of Flow.
  • viscosity is constant
  • denoted by n = shear stress/shear rate
  • shear rate is directly proportional to shear stress and shows a straight line passing through the origin.
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4
Q

What are some examples of Newtonian liquids?

A
  • water, organic solvents, oils and true solutions
  • some suspensions and emulsions
  • chloroform has lowest dynamic viscosity, glycerol has the highest.
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5
Q

How would you characterise Non-Newtonian liquids graphically?

A
  • any form of graphical deviation that is not a straight line.
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6
Q

What are the different types of flow?

A
  • Plastic flow (bingham flow)
  • Pseudoplastic flow
  • Dilatant flow
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7
Q

How would you describe plastic flow?

A
  • Graphically, it starts off as a slope that is not at the origin, and progresses upwards in a straight line.
  • Liquid behaves as an elastic solid at low shear stress.
  • A certain shear stress equivalent to the yield value must be exerted before appreciable flow begins.
  • At shear stress above yield value, the liquid resembles a Newtonian system.
  • Liquids exhibiting plastic flow are shear thinning.
  • Apparent viscosity dependent on the shear rate.
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8
Q

What is the equation used to express plastic flow/

A

Bingham’s equation,

U = (F-f)/G

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9
Q

What is plastic flow associated with?

A

The presence of flocculated particles in a concentrated suspension.

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10
Q

How would you describe pseudoplastic flow?

A
  • graphically: gently sloping curve
  • the liquid will flow as soon as a shear stress is applied
  • viscosity decreases with increasing shear rate
  • flow curve tends towards linearity at higher shear stress
  • liquids exhibiting pseudoplastic flow are shear-thinning.
  • apparent viscosity is dependent on the shear rate.
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11
Q

What is the equation that is used to express pseudoplastic flow?

A

F^N = n’G

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12
Q

What is pseudoplastic flow associated with?

A
  • polymers in solution

- aqueous dispersions of hydrocolloids

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13
Q

How would you describe dilatant flow?

A
  • curving upwards, increasing at a decreasing rate
  • liquid will flow as soon as a shear stress is applied
  • viscosity increases with increasing shear stress
  • liquids exhibit dilatant flow are shear-thickening.
  • apparently viscosity dependent on the shear rate
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14
Q

What is dilatant flow associated with?

A

High concentrations (>50%) of small, deflocculated particles

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15
Q

What are the degree of changes for non-Newtonian liquid dependent on?

A
  • rate of shear
  • duration of shear
  • frequency of shear
  • structural changes may be reversible or irreversible.
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16
Q

What does a non-Newtonian liquid consist of?

A
  • a solid component, which may be flocculated particles, deflocculated particles or long molecules.
17
Q

What does the degree of structural changes that occur as a result of the shearing of non-Newtonian liquids depend on?

A
  • rate of shear
  • duration of shear
  • frequency of shear
18
Q

Structural changes made to non-Newtonian liquids are irreversible (T/F)?

A

false, they can be reversible as well

19
Q

What does the upcurve and downcurve mean, and why is there a gap between them?

A

upcurve - flow curve obtained from increasing shear rate
downcurve - flow curve obtained from decreasing shear rate
Both curves are non-superimposable on one another, therefore the gap between them.

20
Q

What do the upcurves and downcurves form, and what does the area between them denote?

A

both curves join to form a hysteresis loop, area between them denotes the extent of structural breakdown.

21
Q

What is thixotropy characterised by?

A
  • shear thinning (decrease upon apparent viscosity once shearing forces are applied)
  • upcurve and downcurve are non-superimposable (slow recovery of apparent viscosity)
22
Q

How to reduce recovery of apparent viscosity on the upcurve and the downcurve?

A
  • by applying a gentle rocking or rolling motion, which helps in the reformation of the structure.