Email: info@bemachine.cn Tel: +86 135 8442 7912

News

Troubleshooting for the problem of air bubbles on the surface of extrusion blow molding products

Troubleshooting Surface Bubbles in Extrusion Blow-Molded Products

Surface bubbles in extrusion blow-molded products are a common defect that compromises both aesthetics and structural integrity. These bubbles often result from trapped air, moisture, or improper processing conditions. Addressing this issue requires a systematic approach to identify and resolve root causes across material handling, equipment settings, and process control.

Material-Related Causes and Solutions

Moisture Contamination

Resins like PVC and PE are hygroscopic, meaning they absorb moisture from the environment. When processed without proper drying, this moisture vaporizes during melting, forming bubbles. For instance, PVC resins with moisture content exceeding 0.3%–0.5% are prone to bubble formation.

Mitigation Strategies:

  • Pre-dry resins using dehumidifying hoppers or hot-air dryers. For PVC, maintain drying temperatures between 80°C–100°C for 2–4 hours, depending on resin type and particle size.

  • Store resins in climate-controlled warehouses with humidity levels below 50%. Use moisture-barrier packaging for raw materials.

  • Implement a first-in, first-out (FIFO) inventory system to prevent prolonged storage, which increases moisture absorption risk.

Additive Dispersion Issues

Poor dispersion of additives like stabilizers, lubricants, or fillers can create localized weak spots where gases accumulate. For example, insufficient mixing of AC foaming agents in PVC formulations may lead to uneven gas release during blow molding.

Mitigation Strategies:

  • Use high-shear mixers to ensure uniform dispersion of additives. For PVC, maintain mixing temperatures between 100°C–120°C and times of 8–15 minutes, depending on batch size.

  • Optimize additive ratios. Excess lubricants can reduce melt viscosity, allowing gases to escape too easily, while insufficient lubricants may trap gases.

  • Conduct rheological tests to verify melt uniformity before processing.

Equipment-Related Causes and Solutions

Extruder Temperature Control

Inconsistent extruder temperatures can cause resin degradation or incomplete melting, leading to gas entrapment. For example, overheating PVC beyond 190°C triggers thermal decomposition, releasing HCl gas that forms bubbles.

Mitigation Strategies:

  • Implement zone-specific temperature control. For HDPE, set feed zone temperatures at 160°C–180°C, compression zone at 180°C–200°C, and metering zone at 200°C–220°C.

  • Use infrared thermometers or pyrometers to verify actual melt temperatures, as thermocouple errors are common.

  • Install melt pressure sensors to monitor viscosity changes, which indicate temperature-related issues.

Die Design and Maintenance

A poorly designed die can create dead zones where melt stagnates, allowing gases to accumulate. For instance, abrupt changes in die geometry may disrupt melt flow, leading to bubble formation.

Mitigation Strategies:

  • Optimize die land length and taper angles. For tubular film dies, a land length-to-diameter ratio of 3:1 to 5:1 is ideal for smooth flow.

  • Regularly clean dies to remove carbonized deposits, which can obstruct flow channels and trap gases. Use ultrasonic cleaners for intricate die components.

  • Perform flow simulation using software like Polyflow to identify and correct flow irregularities before production.

Process-Related Causes and Solutions

Improper Blow Molding Parameters

Incorrect blow pressure or timing can trap air between the parison and mold, forming surface bubbles. For example, delayed blow initiation may cause the parison to sag, creating folds where air gets trapped.

Mitigation Strategies:

  • Synchronize blow pin activation with parison transfer. Use programmable logic controllers (PLCs) to ensure precise timing, typically within 0.1–0.5 seconds of mold closure.

  • Optimize blow pressure based on parison thickness. For 2mm-thick HDPE parisons, a blow pressure of 4–6 bar is typical, while thicker parisons may require 8–10 bar.

  • Implement differential blow molding for complex shapes, where higher pressure is applied to thick sections and lower pressure to thin sections.

Inadequate Venting

PREVIOUS:Method for treating surface patterns on extrusion blow molding products NEXT:Adjustment techniques for the bending and skewing of the preforms in the extrusion blow molding machine