PVC pipe extrusion involves unique challenges and specific processing strategies compared to other polymers like polyolefins (PO). While POs (PE, PP) are typically extruded as a real melt on single screw extruders, PVC processing involves transforming a dry blend into a rubber-like solid "melt" through heat and shear in double screw extruders. Double screw extruders are preferred for PVC dry blend due to their positive displacement transport, independence from barrel friction, and self-wiping capability, which reduces the need for high levels of heat stabilizer. Single screw extruders, while lower in investment and maintenance for applications like glass fibre reinforcement, are less suited for flood-fed PVC dry blend and require grooved intakes for granular PVC or specific designs for dry blend.
Optimal PVC processing aims to create a homogeneous melt with a well-developed network of tie molecules connecting crystallites. This structure is crucial for the pipe's long-term strength, ductility, and stiffness. Processing conditions influence this structure; too low shear/temperature results in sintered material, while excessive shear/temperature leads to degradation and network destruction. Screw design is paramount in achieving the desired gelation level, ideally 85-95%, which can be measured using fusion tests like DSC, DCMT, or the ASTM Acetone test.
Double screw extruder design aspects like parallel vs. conical configurations impact processing capability. Parallels are favored for larger machines due to greater design freedom for screw profiles and improved gearbox technology. Conicals are often limited by shorter screw length available for melt mixing at the tip, especially at higher outputs. Intake and venting design are critical; the intake allows atmospheric venting, helping air escape and aiding dry blend heating. A powder lock and vacuum venting remove air and volatiles, though too high vacuum can cause premature gelation in the vent zone, trapping air. An early vent design is beneficial for quick gelling materials and foaming, providing more length for downstream mixing.
Screw tip design includes features like mixers (e.g., Starke mixers) that homogenize the melt through elongation flow, which generates less heat than shear flow.
Die head design is another critical factor. Spider dies are common for PVC due to their central feed and short residence time, important for PVC's heat sensitivity. Overcoming spider line welding issues, where melt sectors divided by spider legs don't fully fuse, is achieved through sufficient die compression and melt deformation. Double compression dies, which compress the melt twice with an intermediate relaxation zone, improve spider line quality, wall distribution, and allow a wider processing window and larger pipe diameter ranges. This also reduces the risk of burning by handling external lubricants better.
PVC formulations include stabilizers, lubricants, colorants, fillers (CaCO3), and impact modifiers. The balance of these, particularly lubricants, significantly affects processing and pipe quality, preventing burning caused by hang-ups in the die. High filler levels can aid stiffness but affect pourability and require appropriate dosing feeders. Processing foam core pipe is especially demanding, requiring precise temperature control and specific die designs to manage gas expansion and achieve consistent foam structure.