Polymer Flashcards

1
Q

Properties compared to metals

A

Lower strength, hardness, stiffness, density and T resistance

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2
Q

Polymer Properties (6)

A
  • High strength or modulus to weight
  • Low electrical and thermal conductivity
  • R to corrosion and chemicals
  • Relatively low cost
  • Variety of colours
  • Easy processing
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3
Q

Amorphous Thermoplastics

Architecture and structure

A
  • Random molecular structure
  • Easy to thermoform (soften over range of T)
  • e.g. polycarbonate, acrylic, PETG, PVS, ABS
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4
Q

Semicrystalline Thermoplastics

Architecture and structure

A
  • Separated domains - amorphous and crystalline or highly ordered molecular structure
  • Have two transition Ts
  • e.g. polyolefins, PEEK, PET, POM
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5
Q

Thermoset

Architecture and structure

A
  • Network is amorphous but the cahins are cross-linked
  • Strengthens when heated - cannot be remoulded or heated after initial forming
  • e.g. epoxy, silicones, polyurethanes and phenolics
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6
Q

Tg of Amorphous Thermoplastics

Properties

A
  • Can be formed at T>Tg
  • At Tg - leathery (can be pressed into shape)
  • > Tg - rubbery
  • <Tg - relatively little mobility
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7
Q

What do processing techniques rely on?

A
  • Heat, pressure and time
  • Type of polymer and its response to heat, pressure and length of processing time
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8
Q

What form of plastic get’s processed?

(5)

A
  • Powders
  • Doughs
  • Granules
  • Sheets
  • Liquid resins
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9
Q

Parameter’s of Processing

Considerations

A
  • Tool cost
  • Cycle time
  • Material cost
  • Shape compatability
  • Scrap
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10
Q

Phases

A
  1. Heating - to soften or melt plastic
  2. Shaping/forming - under constraints of some kind
  3. Cooling - to retain shape
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11
Q

Extrusion

A
  • High volume - raw thermoplastic is melted and formed into a continuous profile
  • Produces constant cross section - e.g. pipe, UPVC window frames
  • Constitues largest production technique for plastic products by volume of material
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12
Q

Screw Extruder

Steps

A
  1. Raw material (granules) are fed into hopper
  2. Hopper delivers material into barrel
  3. The screw drives material along barrel through various sections - feed, melt and pumping/metering section
  4. Melt passes through filter screen and breaker plate to remove contaminants and removing the materials rotational memory
  5. Filtered melt is forced thorugh the die to produce shaped extrudate
  6. Extrudate is pulled and cooled
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13
Q

Screw Sections

Extruding Machine

A
  1. Feed - polymer conveyed to melt section, little friction or compression
  2. Melt - polymer compressed by screw and forced against wall, melt film forms due to shearing along wall and melt pool collected againt screw shelf
  3. Pumping/metering - remaining solids disperse in melt. Pressure builds up in die

  1. Highly efficient melting process. 2. Much less efficient
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14
Q

End of Extruder

Parts and what happens

A
  • Filter screen - captures un-melted polymer
  • Breaker plate - changed helical movement into longitudinal translation movements (also improves final mixing)
  • Sensors (T+P) - enable process monitoring and optimisation
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15
Q

Extruder Screw Design

A
  • Aim to achieve: full melting of plastic, avoid overheating, ensure melt homogeneity, max throughout rate
  • L of each section and detailed geometry can be changed to accomodate different polymers
  • Pins can be added to improve mixing
  • Vents along screw allow water vapour to escape
  • Some machines have twin or tripled screw designs
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16
Q

Extrusion Die

Two types

A
  • Annular - enables cable coating, film blowing
  • Shaped - complex cross-section
17
Q

Die Swell

(Barus Effect)

A
  • Extrusion forces polymer chains into alignment
  • Soft extrudate relaxes on exit of die (changing cross-section)
  • Die shape is designed to compensate for relaxation
  • For complex shapes, relaxation is hard to predict (iteration and design experience is needed)
18
Q

Cooling Extrudate

A
  • Cooling rate and uniformity is important to minimise shrinkage and distortion
  • Cooling achieved by blowing air, in water, in cooled vacuums (to prevent collapsing)
  • When cooling amorphous polymers, the T needs to be <Tg to freeze the final part dimensions
19
Q

Extrusion of Tubes and Pipes

A
  • The die contains a mandrel in the shape of the hole
  • This mandrel is attached to the die by one or more ‘bridges’
  • As the material encounters bridges it is forced to seperate, but it flows around the bridges and joins up again
  • Air may be pumped into the centre of the die to stop tube collapsing
20
Q

Extruded Wire

A
  • Electric cable is extruded and coated in plastic insulation
  • A constant feed rate of wire and extrusion ensures a uniform thickness
  • The wire is checked continusously for total coverage with plastic and marked automatically with a roller
21
Q

Sheet and Film

A
  • Sheet >0.5mm thickness
  • Film <0.5mm thickness
  • Produced using a special flat die called coat hanger die
  • Distributes polymer evenly
  • Can be adjusted to create different thicknesses
  • Extrudate first taken up on cooled rolls and then rubber coated pull-off rolls
22
Q

Thin Film and Bags

A
  • Thin film (<0.254mm) products - e.g. plastic bags, cling film - are made from blown films
  • A thin walled tube is extruded vertically and expanded by compressed air
  • Thickness is controlled by pressure of air, speed of tube and a cooling ring that surrounds the “balloons”
  • Slitting knives turn the tube film into a continuous sheet or it is pinched to create bags

Blow ratio = ratio of blown : to extruder d (typically 3:1)