Views: 258420 Author: Site Editor Publish Time: 2026-07-17 Origin: Site
Insufficient depth or width of vent slots on mold cavities, excessively long glue-sealing sections, and trapped gas at dead corners of ribs or bosses.
During high-speed plastic filling, enclosed gas undergoes drastic adiabatic compression, heating up rapidly to 1000~2000°C and triggering gas autoignition.
Extreme high temperatures break down the flame retardant system, cracking flame retardant materials and releasing massive acidic free radicals. These acidic free radicals absorb moisture from ambient air and precipitate a strongly acidic liquid film on the mold mirror surface.
The acidic liquid film forms micro galvanic cells with the iron-carbon mold steel, triggering continuous electrochemical corrosion. This results in pockmarks, white haze, rust stains and damaged polished layers on the mirror finish.
Optimize mold design to completely eliminate gas trapping.
Promptly remove residual acidic crystalline deposits on molds with mild alkaline mold cleaner to prevent recurring corrosion.
Zero rust formation on mirror-finished molds.
Anyone who processes flame-retardant PC resins knows that mid-run machine shutdowns pose major risks.
Brominated flame retardants or antimony-based composite additives rapidly degrade chemically at 280°C. This degradation weakens the mechanical properties of finished parts and releases highly toxic, severely corrosive hydrogen halide gas.
If shutdown lasts more than 10 minutes: Purge all material from the barrel completely.
If shutdown lasts more than 30 minutes: Perform thorough barrel purging with PP or HDPE.
Failure to comply will damage molded products, corrode the barrel, and create health hazards for operators.
Take halogen-free flame-retardant glass-filled nylon as an example.
Halogen-free flame retardants require high loading levels, which drastically raise the shear viscosity of the compound. Excessive screw shear force breaks down flame retardants into acidic gas, causing yellow discoloration and silver streaks on molded parts.
Reduce screw rotation speed. Minimize backpressure while maintaining uniform melt consistency (uniform melt temperature, density and viscosity inside the melting zone).
Lower injection speed to avoid shear overheating of flame retardants as material flows through the gate.
Flame-retardant resins carry high material costs. To cut expenses, some manufacturers add excessive proportions of recycled sprue/runner scrap and reuse scrap indefinitely. This practice leads to soaring defect rates and degraded tensile strength & flame retardancy of finished components.
Flame retardants are small inorganic molecules. Repeated exposure to high injection pressure and temperatures of 200~300°C causes their precipitation and migration, which degrades flame retardant performance.
Multiple recycling cycles disrupt the material’s crystallization rate and molecular chain entanglement. If recycled scrap is processed under virgin material molding parameters, microscopic crystalline delamination occurs inside parts, amplifying stress concentration and reducing mechanical strength.
Conduct verification tests on maximum acceptable scrap loading ratios and recycling cycles before mass use of recycled flame-retardant scrap.
Compile standardized work instructions for scrap handling and corresponding standard molding parameters only after confirming compliance of product strength and flame retardancy.
Centralize scrap collection and implement scientific injection molding recycling protocols.
Injection molding is fundamentally a process of balancing driving force (pressure) and resistance (cavity pressure). During injection, cavity resistance changes continuously as the melt fills the mold, meaning injection pressure is never constant—even at a fixed speed. The article compares two control approaches: variable closed-loop systems, where injection speed dominates and pressure adjusts automatically, and open-loop proportional valve systems, where pressure and speed must be set manually and interact with each other. It concludes that multi-stage pressure settings are valuable for protecting molds and ensuring stable production, particularly in multi-cavity applications.
This article examines the relationship between injection stroke and screw length-to-diameter (L/D) ratio in injection molding machines. Because the screw retracts during plasticization, a longer injection stroke reduces the effective L/D ratio, creating axial temperature gradients that cause inconsistent melt temperature and uneven part quality—especially in multi-cavity molds. Increasing the L/D ratio improves mixing and reduces axial temperature variation. The article recommends limiting injection stroke to approximately four times the diameter of the B screw and concludes that long-stroke, low-L/D designs suit single-cavity products with modest quality requirements, while constrained stroke and higher L/D ensure multi-cavity product consistency.
This article explains the differences between A, B, and C injection-molding screws, which are distinguished primarily by diameter and length-to-diameter ratio. A-type screws offer high pressure and excellent mixing for engineering materials and precision thin-walled parts; B-type screws are the versatile default for over 70% of general-purpose plastics; C-type screws provide high capacity for large, thick-walled components. Three selection rules are provided: keep shot size within 30%–70% of screw capacity, choose fine high-pressure screws for transparent parts, and specify wear-resistant alloys for fiber-reinforced materials.
Screw cleaning is critical to product quality in modified plastics production, yet often overlooked. This article analyzes four common cleaning methods for twin-screw extruders—resin cleaning, disassembly and manual cleaning, flame cleaning, and water-based cleaning—covering their operational principles, key process steps, precautions, and limitations. It provides practical guidance for selecting and combining cleaning methods based on material characteristics, equipment condition, quality requirements, and cost-effectiveness, while emphasizing standardized operations and regular maintenance to extend equipment service life.
For PVC plastic extrusion production lines, feeding method selection depends on material form and process requirements. Three common systems are compared: spring feeders (quick to clean, suitable for frequent color changes but poor with high-filler powders), screw feeders (high flow rate and anti-bridging, ideal for high-filler powders but not for fiber-reinforced materials), and vacuum feeders (dust-free and closed-loop, best for cleanrooms and fiber reinforcement but limited at high output).
Most screw breakages are caused by the reasons mentioned above. Regular inspection of the gearbox, ensuring adequate heating temperature, avoiding material interruptions, strictly following formulas, and preventing foreign objects in raw materials can effectively reduce the risk of screw breakage.
This article cautions against pursuing excessively short injection molding cycles (e.g., 2.8 seconds), outlining 20 improper high-speed practices and their consequences. It covers material degradation, gas entrapment, mold and machine component fatigue, hydraulic system damage, and mechanical failures, emphasizing that aggressive cycle reduction compromises part quality and equipment reliability rather than yielding genuine efficiency gains.