Hydrolysis-induced silver streaks occur when moisture in the resin hydrolyzes in the barrel. Causes include:
Insufficient pre-drying of pellets or reabsorption of moisture in the hopper due to inadequate thermal insulation.
Moisture content exceeding 0.03%, leading to vaporization and resin degradation during melting, generating CO₂ gas trapped in the melt.
Characteristics:
Evenly distributed along the flow direction; severe cases show dense streaks across the surface.
Weakens part strength and causes brittleness.
Solutions:
Thorough drying: Ensure pellet moisture content <0.03%.
Validation method: Sandwich a pellet between glass slides, heat to 280–300°C, and press. No bubbles indicate proper drying.
Hopper modifications:
Install infrared lamps (25–30W/m²) or steam jackets for thermal insulation.
Limit pellet residence time in the hopper to 30–60 minutes.
Caused by resin overheating and degradation during processing, producing CO₂ gas. Common triggers:
Excessive barrel temperatures.
Dead zones in the barrel/nozzle.
Prolonged melt residence time.
Reduced resin molecular weight.
Characteristics:
Irregular distribution (e.g., comet-shaped patterns).
Accompanied by discoloration or brown spots, especially in the sprue.
Solutions:
Reduce barrel temperatures in overheated zones.
Eliminate dead zones via barrel/nozzle cleaning.
Shorten cycle time or switch to a smaller injection machine.
Result from poor part design (e.g., abrupt wall thickness changes), causing air entrapment during filling.
Characteristics:
Fixed distribution along flow direction near thickness transitions.
Often accompanied by sink marks or internal bubbles.
Solutions:
Adjust injection speed:
For mild thickness changes: Use slow speed for stable filling.
For drastic changes: Use high speed + increased pressure to expel air.
Redesign part geometry or improve mold venting.
Caused by improper runner design or blockages:
A. Excessive Sprue Taper Angle (>10°)
Creates air gaps during filling.
Solution: Reduce taper angle to 4–6°; polish or replace the sprue bushing.
B. Undersized Gate
Turbulent flow introduces air.
Solution: Enlarge gate or modify its shape; reduce injection speed.
C. Nozzle Cold Slug Blockage
Solution: Increase nozzle temperature and enlarge mold cold slug wells.
Caused by irregular screw retraction during plastication, introducing air.
Characteristics:
Random distribution with occasional short shots or bubbles.
Solutions:
Reduce rear barrel temperature to prevent pellet clumping.
Increase melt temperature for better plastication.
Adjust back pressure (≥10% of injection pressure).
Optimize hopper heating to avoid pellet agglomeration.
Occur when trapped air merges with weld lines.
Characteristics:
Localized near weld lines.
Solutions:
Modify gate position/design or add venting channels.
Process adjustments:
Adjust injection pressure/speed.
Regulate mold temperature differential between stationary/moving halves.
Melt Flow Index (MFI): Critical for viscosity assessment.
Heat Deflection Temperature (HDT): Determines annealing parameters.
Back Pressure: 3–15 MPa for homogeneous melt.
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