Core definition: The foaming agent decomposes to generate gas before the material exits the die (at the barrel end, the merging core, or within the mold cavity); the gas has already expanded and depressurized inside the mold, so no further foaming occurs after the material leaves the die, and the density does not decrease. Many technicians mistakenly assume an "insufficient foaming agent" and blindly add more AC, only to find that the mixture becomes increasingly poor with each addition.
During the production of wood-plastic door frames, many factories encounter the issue of excessive product density—where the product fails to foam or expand even when an adequate amount of foaming agent has been used. This problem directly leads to higher costs, substandard mechanical properties, or even failure to meet delivery requirements. Many production personnel attempt to adjust process parameters blindly, yet consistently fail to identify the root cause. In reality, this often occurs because the material foams prematurely inside the extruder head, but upon demolding, it shrinks back and ceases to foam further. To address this situation, we will now outline a comprehensive troubleshooting approach—arranged in ascending order of complexity—to help you quickly pinpoint the cause of the malfunction and resolve it.
1. The material discharged from the mold appears loose or soft; however, upon ejection from the mold, it rapidly contracts and becomes compact. When just extruded from the mold lip, the material may appear slightly swollen or porous; after being moved a distance of 20–50 cm, it immediately retracts, hardens, and its cross-section becomes dense. The finished product exhibits a relatively high density, with fine pores or even no pores at all.
2. Comparison: Normal free foaming – the material continues to expand over a certain distance after being removed from the mold before final setting; no significant shrinkage occurs.
3. The mold opening exhibits persistent micro-bubbles, material overflow-induced foaming, or accumulation of carbon deposits/porous material residue on the mold lip; the edge of the mold lip often bears a loose, porous layer of yellow or white foamed debris that quickly reappears after cleaning; the surface of the mold opening's material layer shows scattered small bubbles or pinholes.
4. The surface of the material strip often exhibits small pores, pinholes, hollow grooves, or transverse bubble patterns; these occur when gas forms bubbles within the mold cavity and is then ruptured by the mold lip, resulting in surface pinholes or broken-bubble patterns.
5. The head pressure exhibits significant fluctuations or is too low; the main motor current is unstable. When gas forms a gas cushion within the mold, the pressure cannot be established, resulting in erratic readings on the pressure gauge; under the same rotational speed feeding condition, the head melting pressure is significantly below the normal, qualified foaming pressure range.
6. Stop the machine and remove the mold; there is loose, porous residual material on the inner walls of the merging core and the mold cavity. Stop the machine to clean the mold; the waste material adhering to the inner walls of the flow channels is not dense or hard material, but porous, sponge-like loose material blocks – this is the most sufficient evidence!
1. During normal production, a short piece of material is rapidly cut off when the die opening aligns precisely with the lip opening, and this piece is immediately immersed in cold water for rapid cooling to lock in the internal structure;
2. Then, a 30 cm section of material from the foaming completion zone is cut off for cooling;
3. Cut open and examine the cross-section:
· Sample placed directly against the die mouth → The interior is already filled with fine bubbles = Pre-forging foaming inside the extruder head
· The sample is in close contact with the mold cavity → the material is uniformly dense and free of bubbles; bubbles only form as the process progresses = delayed decomposition of the foaming agent or insufficient foaming.
Same formula, same main unit / feeding system:
· The head melting pressure is too low or exhibits significant fluctuations;
· The measured melt temperature exceeds the allowable foaming temperature range specified in the formulation; → Strong suspicion of premature foaming (excessive shear heating or extensive decomposition of AC within the mold).
Only reduce the set temperatures of the combined core, machine head, and die by 3–5°C; leave all other parameters unchanged.
· If lowering the nozzle temperature results in an increase in nozzle pressure, noticeable foaming of the finished product, and a decrease in density – then it can be confirmed that the issue was due to premature foaming inside the nozzle.
· If the material still does not expand fully after cooling, while its density remains unchanged, the issue lies not in the premature foaming process, but rather in an insufficient foaming agent/activator or insufficient melt strength.
|
Phenomenon |
Pre-filling foaming process for the machine head interior |
Insufficient foaming (failure to foam) |
|
The mold cavity is in close contact with the sampling section. |
Existing fine pores |
Overall dense solid |
|
Mold ejection variation |
Initially slightly swollen, then retracting and hardening |
The discharge material remains consistently dense, with almost no expansion. |
|
Head pressure |
Low level with significant volatility |
The pressure can be either high or low; in most cases, it remains relatively stable. |
|
Mold scrap |
Porous, loose, spongy structure |
Dense hard material |
|
Operation Direction |
Cooling head, reduced internal slippage, increased melt strength, reduced shear heat |
Fine-tune AC/activator, increase plasticizing section temperature, and add foaming regulator |
1. Lower the temperatures of the combined core → machine head → mold (by 3–5°C per adjustment; avoid excessive single reductions).
2. Reduce internal lubricants (e.g., stearic acid); excessive internal lubrication or overly rapid plasticization can easily lead to premature foaming.
3. Appropriately reduce the main machine's rotational speed to minimize shear heat (Key point! For high-fill wood-plastic composites, the shear heat is significantly higher than the apparent temperature).
4. Check the amount of foaming agent used to ensure that the melt strength effectively traps the gas.
5. Check the ratio of AC foaming agent to activator; do not add in excess.
1. Excessive vacuum in the exhaust section: This draws away the gas, resulting in no visible foaming; this does not indicate premature foaming at the machine head; adjust the vacuum test range downward.
2. Excessive moisture content in wood powder: the formation of water vapor creates irregular large bubbles and voids rather than uniform, fine bubbles – verification for dried wood powder.