Polymers- Injection Moulding and Thermoforming Flashcards
Is injection moulding discrete or continuous?
Discrete
What is good about injection moulding?
Simple of intricate, complex parts of varying sizes can be made. High quality with good dimensional tolerance. Quick
Pressure used in injection moulding
About 100MPa
Costs involved in injection moulding
High initial equipment and mould costs. Low running and per part costs
Sources of scrap from injection moulding
Sprues, runners, flash, out of spec, trimming, start up/shut down. Much can be ground and reused but not many times because the heat cycle changes the properties of the polymer
What types of plastic can be injection moulded?
Most thermoplastics and increasingly thermosets too
General process for injection moulding
Rapid injection of specific quantity of homogenised polymer melt into a closed two part cavity mould. Pressure held on polymer in mould until it solidifies. When temperature low enough the part is removed. Repeat cycle
Set up of injection moulder
Similar to extruder but the single screw can move back and forth in the barrel so is a reciprocating screw.
Injection phase
Injection: prepare molten plastic charge in metering zone of extruder, push screw forwards forcing charge into cavity mould, a check valve prevents charge returning back up screw
Phases after injection
Packing: maintain pressure to ensure mould remains filled.
Cooling: allow plastic to cool and prepare next charge.
Ejection: open mould, eject part and collect.
Repeat
PVT plot for injection moulding
Specific volume against temperature with diagonal lines as isobars. Starts at maximum v and T then straight down to lowest (highest P) isobar. Follows isobar diagonally towards origin. Then horizontal across to top isobar. Follow isobar down to room temperature. Kink at Tg to reduce gradient
Explain the PVT diagram for injection moulding
Liquid enters mould at max temp and is pressurised at constant T so v decrease. Held at high P as T decreases so v decreases (means more pumped in). T drops such that gate freezes and no more enters mould and v constant. Further T drop causes P drop and v drop. Polymer solidifies and RT reached. Contraction in final part roughly 1%
What is fountain flow and what does it cause?
Molten polymer solidifies first near the cold mould wall. Means injected polymer continues to flow through solidified polymer (fountain flow). Final part usually has outer skin of densely packed polymer with core of less dense polymer
Injection phase problems
If polymer solidifies too soon it will block the mould creating a short shot. If polymer injected at too high P it can leak out between two halves of mould causing flash
Packing phase problems
As polymer cools density increases so injection pressure must be maintained until it solidifies. Stopping injection early can lead to polymer falling back into mould creating sink marks or voids. Too high a T can scorch the part