๐๐จ๐๐๐ฒ'๐ฌ ๐๐๐๐๐๐๐๐๐ ๐๐ก๐๐ซ๐ : ๐๐ซ๐๐ง๐ฌ๐๐๐ซ ๐ฅ๐ข๐ง๐ ๐๐๐ฌ๐ข๐ ๐ง ๐ข๐ฌ ๐จ๐๐ญ๐๐ง ๐จ๐ฏ๐๐ซ๐ฅ๐จ๐จ๐ค๐๐
๐๐จ๐๐๐ฒ'๐ฌ ๐๐๐๐๐๐๐๐๐ ๐๐ก๐๐ซ๐
๐๐ซ๐๐ง๐ฌ๐๐๐ซ ๐ฅ๐ข๐ง๐ ๐๐๐ฌ๐ข๐ ๐ง ๐ข๐ฌ ๐จ๐๐ญ๐๐ง ๐จ๐ฏ๐๐ซ๐ฅ๐จ๐จ๐ค๐๐ — ๐ฒ๐๐ญ ๐ข๐ญ ๐ข๐ฌ ๐๐ซ๐๐ช๐ฎ๐๐ง๐ญ๐ฅ๐ฒ ๐ญ๐ก๐ ๐ซ๐จ๐จ๐ญ ๐๐๐ฎ๐ฌ๐ ๐จ๐ ๐ซ๐๐ฌ๐ข๐ง ๐๐๐ ๐ซ๐๐๐๐ญ๐ข๐จ๐ง ๐๐ง๐ ๐ ๐๐ฅ ๐๐๐๐๐๐ญ๐ฌ ๐ข๐ง ๐๐ฑ๐ญ๐ซ๐ฎ๐๐๐ ๐๐ข๐ฅ๐ฆ ๐ฉ๐ซ๐จ๐๐ฎ๐๐ญ๐ฌ.
In extrusion, transfer lines must balance two competing demands: minimizing pressure consumption while maintaining sufficient wall shear stress to prevent resin stagnation. A pipe that is too large reduces pressure drop but allows polymer to linger at the wall, degrading over time and appearing as gels or black specks in the final product.
Key design parameters to address both concerns:
- Target wall shear stress of 20 to 30 kPa to ensure continuous material renewal at the pipe wall
- Design the transfer line as short as possible, since pressure consumption is directly proportional to pipe length
- Use clam-shell type elbows with a bend radius at least five times the pipe diameter
- Ensure all pipes and connections are the same diameter to eliminate ledges and stagnation points
Two blown film case studies demonstrate that reducing transfer line diameter to reach the recommended shear stress range eliminated persistent gel and black speck defects without imposing unmanageable pressure consumption.
Full analysis and supporting equations are available in the complete article. https://lnkd.in/euaePEDU
source : Plastics Technology

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