๐“๐จ๐๐š๐ฒ'๐ฌ ๐Š๐๐Ž๐–๐‹๐„๐ƒ๐†๐„ ๐’๐ก๐š๐ซ๐ž : ๐“๐ซ๐š๐ง๐ฌ๐Ÿ๐ž๐ซ ๐ฅ๐ข๐ง๐ž ๐๐ž๐ฌ๐ข๐ ๐ง ๐ข๐ฌ ๐จ๐Ÿ๐ญ๐ž๐ง ๐จ๐ฏ๐ž๐ซ๐ฅ๐จ๐จ๐ค๐ž๐

๐“๐จ๐๐š๐ฒ'๐ฌ ๐Š๐๐Ž๐–๐‹๐„๐ƒ๐†๐„ ๐’๐ก๐š๐ซ๐ž

๐“๐ซ๐š๐ง๐ฌ๐Ÿ๐ž๐ซ ๐ฅ๐ข๐ง๐ž ๐๐ž๐ฌ๐ข๐ ๐ง ๐ข๐ฌ ๐จ๐Ÿ๐ญ๐ž๐ง ๐จ๐ฏ๐ž๐ซ๐ฅ๐จ๐จ๐ค๐ž๐ — ๐ฒ๐ž๐ญ ๐ข๐ญ ๐ข๐ฌ ๐Ÿ๐ซ๐ž๐ช๐ฎ๐ž๐ง๐ญ๐ฅ๐ฒ ๐ญ๐ก๐ž ๐ซ๐จ๐จ๐ญ ๐œ๐š๐ฎ๐ฌ๐ž ๐จ๐Ÿ ๐ซ๐ž๐ฌ๐ข๐ง ๐๐ž๐ ๐ซ๐š๐๐š๐ญ๐ข๐จ๐ง ๐š๐ง๐ ๐ ๐ž๐ฅ ๐๐ž๐Ÿ๐ž๐œ๐ญ๐ฌ ๐ข๐ง ๐ž๐ฑ๐ญ๐ซ๐ฎ๐๐ž๐ ๐Ÿ๐ข๐ฅ๐ฆ ๐ฉ๐ซ๐จ๐๐ฎ๐œ๐ญ๐ฌ.




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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