MAKE THE TOOLING CHANGEOVER TO CONCEPT EXTRU-TECH LIMITED EXTRUSION TOOLING TECHNOLOGY CONCEPT EXTRU-TECH LIMITED TEL: 44 (0)
QUALITY THE KEY TO SUCCESS CONCEPT SHEATHING, STRIPING & SKINNING CROSSHEADS
CONCEPT TORPEDO SPIDERS
CONCEPT SHEATHING CROSSHEAD 40 MM TO 75 MM
STATE OF THE ART TECHNOLOGY
CONCEPT BREAKER PLATES NO JOB TOO SMALL
TO SCALE - SEE MOBILE PHONE
FLOWPATH FOR CREATIVE 150 SHEATHING & STRIPING CROSSHEAD
Concept Extru-Tech DESIGN AND MANUFACTURE CROSSHEADS AND DIES TO MATCH: PRODUCTION OUTPUT MATERIAL RHEOLOGY CET USE COMPUPLAST TECHNOLOGY TO OPTIMISE THE FLOW OF MELT THROUGH THE DIE
Side Fed Dies n The center mandrel is supported below the entry point of the material. n Polymer enters from the side and flows around the center mandrel. Inlet Exit Land Body Mandrel Extension Mandrel Adapter Inflation Air
Balancing of flow is required to ensure uniform distribution n Material will prefer to take the shortest path from the entrance to the exit. n This will result in more material flowing along the inlet side.
Side Fed Die Inlet Outlet Through Hole
Unwrapped Side Fed Die Inlet Channel Restriction Chamber Outlet
Path Comparison Inlet P1 P2 For uniform flow Q1 Q2
Side Fed Die Potential Problems Weld Line Thick Thin Thickness Variation, Period = 2
SPIRAL MANDREL TECHNOLOGY FOR 3 LAYER PETROLEUM PIPE
Spiral Mandrel Dies n Commonly used for tubular (blown) film production since 1950’s. n In more recent years applied to pipe and blow molding dies
Spiral Mandrel Die & Body
Spiral Mandrel Flow Field DIE INLET ENTRY PORT DIE EXIT INFLATION AIR
Unwrapped View Use periodicity to simplify analysis o oo oo
Qin Qs1 Qs2 Qs3 P1= P2 Flow Path Comparison
More Complicated Analysis Flow between plates Flow in ‘U’ channel Flow from lower channels Leakage out of channel Flow from previous section channels
Fully 3-D Flow Field
Weld Line Orientation Spider DieSpiral Die
Design Evaluation Flow Distribution Good Design Uniform Thickness Poor Design Periodic Thickness Equal to # of Spirals
Design Evaluation Circumferential Position Channel Flow Channel Position Slow Initial Leakage Fast Initial Leakage Flow Variation
Position [°] Thickness variation [%] Run 1 Run 2 Simulation Spiral Mandrel Die Comparison with experiment
Potential Problem Rapid reduction in channel flow will result in the remainder of the channel having too little material flow and consequently a high residence time If sufficient material leaks out prior to the first spiral overlap, then it is quite likely that this will result in a visual defect in the final product. A type of Port Line
Design Evaluation Additional Criteria n Final Distribution n Velocity/Shear Rate/Shear Stress n Pressure Drop n Sensitivity to Material Changes n Sensitivity to Process Conditions n Sensitivity to Manufacturing Tolerances
Calculation Methods n Step by step calculations n Develop analytical expressions related to the geometry and solve for the correct dimensions. n Control Volume Method analysis n Finite Element Method analysis
STACKED DIES Each layer is added sequentially. Each distribution module can have the same surface area. All layers (except the inner layer) can have the same residence time.
CONCEPT 150 CROSSHEAD
GENERAL ARRANGEMENT
WALL SHEAR STRESS FIELD 150 CROSSHEAD THE PROCESS OF SIMULATING FLOW THROUGH THE DIE SHOWING THE SHEAR STRESS
WALL SHEAR RATE FIELD 150 CROSSHEAD THE PROCESS OF SIMULATING FLOW THROUGH THE DIE SHOWING THE SHEAR RATE
PRESSURE FIELD 150 CROSSHEAD THE PROCESS OF SIMULATING FLOW THROUGH THE DIE SHOWING THE PRESSURE DROP THROUGH THE DIE
AVERAGE RESIDENCE TIME FIELD 150 CROSSHEAD THE PROCESS OF SIMULATING FLOW THROUGH THE DIE SHOWING THE MATERIAL RESIDENCE TIME
BULK TEMPERATURE FIELD 150 CROSSHEAD THE PROCESS OF SIMULATING FLOW THROUGH THE DIE SHOWING THE TEMPERATURE VARIATIONS
CONCEPT GUIDE PINS
CET 420 CALIBRATOR
POLYMER FLOW DISTRIBUTOR CET HAVE SOLUTIONS TO YOUR PROBLEMS
PROUD OF A HIGHLY SKILLED WORKFORCE
CET CRAFTMANSHIP CET EXTRUSION TOOLING
SPIRAL MANDREL INNER DIE
PROVIDING YOU WITH QUALITY TOOLS TO MANUFACTURE YOUR QUALITY PRODUCTS