Polymer_2 Flashcards

Additives and Blends Compounding Extrusion (37 cards)

1
Q

What is an Additive?

A

A substance added to polymers to add certain properties.

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2
Q

What are Reinforcements additive type? Name some.

A

Additives which improve mechanical properties.

Short fibres such as glass. Long fibres such as glass, carbon, Kevlar etc.

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3
Q

What are Toughening Agents additive type? Name some.

A

Additives which improve the toughness of the polymer if it is brittle.

Rubber particles. Copolymerise (e.g. ABS).

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4
Q

What are Fillers additive type? Name some.

A

Used to ‘bulk’ out or increase the volume while maintaining similar properties.

Extenders such as wood flour or calcium carbonate, talc etc. Enhancers such as mica (heat resistance), carbon black (conductivity).

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5
Q

What are Coupling Agents additive type? Name some.

A

Used to improve appearance and adhesion qualities of polymer.

Silanes (e.g. RSi(OR)3)
Stearic acic, C17H35-CO2H.

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6
Q

What are Stabilisers additive type? Name some.

A

Helps prevent polymers from breaking down.

HCl scavengers (e.g. organo-tin compounds).
UC protectors (e.g. phenones).
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7
Q

What are Pigments & Dyes additive type? Name some.

A

Used to change the colour of the polymer.

Colorants such as titanium dioxide (brilliant white), metal oxides.
Also calcium carbonate (white) and carbon black black).

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8
Q

What are Plasticisers, lubricants, processing aids additive type? Name some.

A

Low molecular weight compounds that help with the plasticising, lubrication or processing of a polymer.

Low molecular weight compounds (e.g. PE in PVC).

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9
Q

What are Curing Agents additive type? Name some.

A

Used to cure a polymer or improve the cross-linking between linear chains.

Pe can be crosslinked with dicumyl peroxide.

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10
Q

What are Blowing Agents additive type? Name some.

A

Used to make foams. Low boiling points.

Physical (e.g. pentane in PS).
Chemical (e.g. hydrazine compounds).

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11
Q

What are Flame Retardants additive type? Name some.

A

Used to retard flames in polymers. Reduced the flammability of polymers.

Halogenated compounds (Cl or Br containing). They are being phased out for environmental and health reasons.

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12
Q

What are Other additive types? Name some.

A

Biocides reduced biological activity in the polymer. (e.g. organic copper compounds)

Anti-static agents (e.g. fatty acid amines).

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13
Q

What are Polymer Blends and Polymer Mixtures?

A

Polymer = Pure system
Polymer Blend = Mixture of two or more pure polymers.
Polymer Mixture = Pure Polymer + Anything else.
Plastic = Mixture of one or more pure polymers and one or more additives.

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14
Q

What are Miscible blends?

A

Complete mixing on a molecular scale. Basic rule: ‘like dissolves like’ (e.g. PET & PBT).

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15
Q

What are Immiscible blends?

A

Phase separated. Not completely mixed. Most common.

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16
Q

Miscibility is controlled by the Gibbs free energy of mixing (Change in Gmix) and rheological properties. Show this equation.

A

∆𝐺𝑚𝑖𝑥 = ∆𝐻𝑚𝑖𝑥 −𝑇∆𝑆𝑚𝑖𝑥. Memorise!

Polymers are already highly disorders so mixing them yields little entropic (∆𝑆𝑚𝑖𝑥) benefit.
Therefore enthalpy dominates but there are relatively few combinations of polymers that can physically bond to provide enthalpic (∆𝐻𝑚𝑖𝑥) benefit.
Also need to match viscosity.

17
Q

Polymer-additive mixtures are required to be homogenous to obtain desired properties. Describe distribution and dispersion.

A

Good distribution means the sample volume is filled. Good dispersion means particles are separated.

18
Q

Describe Compounding in terms of polymer mixtures. Also name the processes behind compounding.

A

A generic term for obtaining a homogenous blend or mixture.
Compounded plastic. Concentrate or ‘masterbatch’.

Process:
Feeding
Mixing
Filtering
Pelletisation
19
Q

Describe Feeding in Compounding. Name the feeders type systems.

A

A hopper containing polymer granules/powder/ chip/ beads/ pellets.

Additive feeders
Solid, gravimetric control
-Dust control
-Shakers
Liquid, volumetric control.

Sometimes ‘bridging’ may occur where the polymer is stuck in the hopper feeders.

20
Q

Describe Mixing in Compounding. Name the Mixing type systems.

A

Batch mixers.
- Small scale
- Heat and shear mix with intermeshing blades
Continuous mixers
- Large scale
- Heat and high shear mix with non-intermeshing parallel screws.
Screw extruders
- Heat and shear mixing
- Single screw for large scale mixing of easy to mix compounds.
- Twin screws (co-rotating or counter-rotating) for more efficient large scale mixing.

21
Q

Describe Filtering in Compounding.

A

Screens remove contaminants and control flow.

22
Q

Describe Pelletisation in Compounding.

A

Creates a sensibly sized solid polymer for use in major processing techniques.
Strand polymer extruded (forced through die, cool, dry, chop).

23
Q

Describe the Extrusion process after compounding.

A

Homogenised molten plastic is forced through an open-ended die or aperture.

Continuous process.

Creates parts with a constant cross-section (e.g. tubes, fibres, sheets etc.)

Potentially ‘infinite’ length.

Often a pre-cursor to other processes.

  • Sheets for thermoforming
  • Pellets for injection moulding

Most thermoplastics can be extruded.

Scrap/Waste from out of specification and edge trim etc.

24
Q

Describe an Extruder.

A

Archimedes screw pumps molten polymer along screw.

Flight depth and material channel decreases along the screw.

Polymer molecules shear against each other causing melting.

Also heat/cool the barrel as necessary.

A Breaker plate removes the spiral motion, makes the flow linear.

Screen pack filters for contaminants and controls the flow.

25
What is the Flight depth and material channel in an Extruder split into? Describe them.
Feed zone, Melting zone and Metering zone. As the polymer reaches the die, the space between flights decreases which increase the friction and so the heat.
26
Describe the Extruder screw type and their designs. Name some properties for the screws.
Single or twin screw alternatives. Modern screws have a modular design - Feeding - Mixing - Compression - Metering ``` Capacity - 8g to tonnes/hour Screw speed - 60 to 360 rpm Diameter - 5 to 300mm Length - 20 to 30x diameter Channel depth - 0,02 to 0.07x diameter Compression ratio - 2 to 4 ```
27
Name the 4 typical Extruder Screw Designs.
Standard (feed, compression, metering). Standard plus venting section to allow evolved gases to escape. PVC type for amorphous(non-crystalline) polymers which progressively soften through a glass transition. Nylon type for crystalline polymers which have a sharp melting point.
28
Describe an Extruder Die. What do they need to account for?
A well designed extruder die should shape the extrudate while maintaining a uniform extrudate velocity with minimal pressure drop. Need to account for: - Shear-tinning behaviour - Viscoelastic behaviour Dies can vary from simple shapes to complex designs.
29
Describe Extruder 'die swell' in Extruder dies.
Extruder 'die swell' is caused by velocity unification and viscoelastic relaxation. This is eliminated using a non-orthogonal aperture or a long or tapered die.
30
Describe 'Residual stress' in a Extrudate and prevention methods.
'Residual stress' in the extrudate can lead to frozen in stresses which warps the part. This is eliminated using constant wall thickness or other designs.
31
Describe Profile Extrusion.
Produces simple continuous 2D parts. Polymer orientation. Mechanical properties in polymers are lined up with the direction of the flow. Examples: tubes < 12mm and pipes > 12 mm. Can co-extrude with reinforcement or lining (garden hosepipe).
32
Describe Sheet/Film Extrusion.
Homogenised molten plastic is forced through a slot or 'coat hanger' die Polymer orientation. Thickness varies - Flims < 0.3mm - Sheets > 0.3mm Multi layer films use extra extruders - Crisp packets
33
Describe Sheet/Film Extrusion Coating.
Extruded plastic film is coated onto a non-polymeric substrate. Cardboard + LDPE (milk cartons) - Prevents leakage - Adhesive layer Aluminium foil + LDPE (yoghurt pot lids)
34
Design Film Blowing.
Homogenised molten plastic is forced through a ring or annular die and blown into a bubble. Air is stopped when design thickness achieved. Need a polymer with good melt strength such as branched PE. Polymer orientation. Axial orientation when pulled up and circumferential orientation from blowing. Bi-Axial orientated films. Makes cylindrical films ideal for plastic bags and packaging.
35
Describe Fibre Spinning.
Many small filaments are extruded through a spinneret die. - Twisted or coated/sized to form a fibre. - Woven into fabric. Polymer orientation. Uni-axial orientation of fibres. Not always a circular cross-section (e.g. hollow fibres) Melt spinning of nylon and polyester fibres. Gel spinning of Kevlar or Dyneema (UHMWPE fibres).
36
Describe Non-woven Fabrics.
Fibres exit die and randomly align into a mat. Embossing fuses the fibres into a fabric removing the need to weave. Not strong but absorbent (nappies etc.) Rayon (a cellulose fibre) used to be popular for this application but now PP and PET are preferred.
37
Describe Wire & Cable Coatings.
Insulated coating is applied to wire and cables from a tubular die (also called over-jacketing) Commonly use LDPE or plasticised PVC High temperature applications use cross-linked PE.