Meaning
Thermoplastic polymer sourced entirely from post-consumer or post-industrial waste streams and compounded to match virgin melt flow behaviour defines circular polypropylene. Processing temperatures, injection speeds, and cooling cycles must account for the narrower molecular weight distribution typical of recycled polymer grades. Parts moulded from this recycled feedstock exhibit acceptable tensile strength when proper gate dimensions compensate for lower impact resistance.
Datasheet values for melt mass-flow rate often show wider batch-to-batch variation than those recorded for virgin polymer grades.
Resin Viscosity
Molecular chains shorten during mechanical recycling because thermal and shear stresses break carbon bonds inside the extruder barrel. Viscosity drops noticeably when the material undergoes repeated extrusion passes, which forces moulders to raise injection pressure and shorten cycle times to prevent short shots. High melt flow rates require lower barrel temperatures to prevent flash along parting lines, whereas low melt flow rates demand elevated nozzle temperatures to fill thin wall sections completely.
Shear thinning behaviour changes as recycled chains mix with residual additives from previous product lifecycles.
Shrinkage Control
Part dimensions deviate from mould cavity geometry because crystallization kinetics shift when secondary nucleation sites are present in the feedstock. Volumetric shrinkage rates increase if packing pressures remain calibrated for virgin resin parameters. Toolmakers adjust cavity dimensions by increasing scaling factors to compensate for the higher crystallinity found in reclaimed polymer chains.
Cooling channel placement dictates warpage severity when heterogeneous material batches cool at uneven rates across the moulded geometry.
Economic Yield
Feedstock pricing fluctuates according to contamination levels and sorting efficiency achieved during municipal or industrial waste collection. Regrind economics depend heavily on cleanliness, moisture content, and the absence of incompatible polymer contaminants such as polyethylene or polystyrene. Virgin material costs twice as much as recycled alternatives, but the price advantage diminishes when high scrap rates outweigh raw material savings during production trials.
Mould operators monitor scrap ratios constantly because small viscosity shifts generate dimensional non-conformity that quickly eliminates material cost benefits.