Polymer Processing Flashcards

1
Q

What is polymer extrusion?

A

Well suited for large scale processes (the backbone of thermoplastic polymer processing), versatile for:

  • melting
  • blending
  • and conveying/transporting to downstream processes
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2
Q

How does polymer extrusion work?

A

plastic pellets are fed through a hopper into a cylinder where it is moved with a screw. Heat is added to melt the polymer and the screw both transports it and mixes the polymer

*different screw types exist to maximize shear or elongation flow
**difficult to model due to mass flow and phase transitions

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3
Q

What types of mixing are shear and elongation flow good for?

A

shear = distributive mixing
elongation = dispersive mixing

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4
Q

How is compounding done in polymer extrusion?

A
  • blending of polymers and additives to create specific formulation
  • can be done inline (directly to feed) or in a downstream process,

*attempting to get well-blended polymers

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5
Q

What is blown film extrusion?

A
  • a high throughput technique used for manufacturing continuous thin films
  • ideal for packaging, barrier applications, and membranes
  • done by stretching films biaxially through a blowing process (like blowing bubble gum) - improves strength and durability
  • requires knowledge and experience to maintain stability (don’t want bubble to collapse)
    *can create thin films as low as 20 micrometers
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6
Q

What is cast film and sheet extrusion?

A
  • ideal for continuous manufacturing of films and sheets (few microns to few mm in thickness)
  • uses rollers to stretch film and to apply tension as polymer cools
  • uses specialized dyes that allow polymer to relax before orifice of extruder and thus allow to be stretched into sheets
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7
Q

What is profile extrusion?

A
  • polymer is extruded directly into final product shape using specialized profile die
  • commonly used for tubing and pipes but also for more complex geometries

*polymer contorts slightly after leaving mold (so molds are often made slightly larger)

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8
Q

What is coextrusion?

A
  • simultaneous extrusion of multiple polymers into a single combined flow. Very commonly used in packaging and barrier materials
  • combination in melt state allows interdiffusion between layers and a cohesive interface - we want dissimilar layers to act like a single material, rather than 2 glued together

*need to match flow and viscoelastic properties to avoid flow instabilities at the boundary layer

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9
Q

What is melt memory and die swell?

A

As polymer leaves extruder through the die, the polymer is compact and squeezed together. However, the chains do not like this, so when it exits the die, it will swell to a larger size

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10
Q

How can die swell be reduced?

A
  1. make die longer (gives more time for chain relaxation)
  2. increase temperature (relaxation depends on temp)
  3. slow down polymer movement through channel (more travel time + less stress applied to polymer)
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11
Q

What happens to shear (and flow) for a newtonian fluid?

A

Assumes: no slip condition + well-developped uniaxial flow

  • flow becomes a half circle, reaching its maximum at the center of the pipe
  • shear is highest at the walls and lowest at the center of the pipe
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12
Q

What happens to shear (and flow) for a shear thinning fluid?

A

shear thinning: viscosity decreases with higher shear, thus increasing speed

  • Flow: no slip, then increases much faster than newtonian before becoming near flat as it crosses the pipe
  • shear - similar shape as newtonian fluid, but curves a bit as change in viscosity causes shear to increase more drastically as it approaches the walls
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13
Q

What are the processing condition strategies employed for multiphase flows in coextrusion?

A

at the junction we want introduction of two flows to occur as smoothly as possible. This is done by controlling channel design:

  • want well-developed laminar flows
  • minimal difference in layer velocities
  • small angle between channels

*need to account for viscoelastic effects since we have normal forces perpendicular to flow (want to flow with this force) and polymers may have different viscoelastic effects (ex. different viscosities)

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14
Q

What is the Kelvin-Helmholtz instability?

A

Turbulent flow is generated at the interface between 2 fluids moving at different speeds

*this can be seen in polymers (if the coextruders are moving at different speeds then will get undesired swirling motion of polymers into each other)

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15
Q

What is viscous encapsulation?

A

A thermodynamically-driven phenomenon observed in layered polymer flows - lower viscosity polymer migrates to pipe walls and higher viscosity polymer moves to center of pipe, causing it to be encapsulated (low viscosity takes less E to flow on the outside so they will naturally thermodynamically move there - more shear at walls)

  • minimize effect by having viscosity ratio close to 1 (at around 3.6 ratio start to get full encapsulation)

*this can be done by selecting a shear rate where the polymers viscosities are similar

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16
Q

What is elastic layer rearrangement?

A

Recall: polymers experience normal forces perpendicular to flow

if the channel is square or rectangular, will be secondary flows due to unbalanced normal stresses, causing swirling forces at edges
- this causes layers to rearrange - which is a huge issue in packaging (or other applications) where want uniform predictable layers

17
Q

How can elastic layer rearrangement be mitigated?

A
  • more difficult to mitigate (cylindrical pipe may not be possible - say for thin films)

Possibilities:
- use simulation to predict forces and attempt to design channel to minimize effects
- higher processing temperatures (minimizes elastic effects)
- lower Mw resins (lowers elastic effects)