Injection Molding. Materials. Plastics 2.008. Outline. Polymer. Equipment and process steps. Considerations for process parameters



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Outline 2.008 Polymer Equipment and process steps Injection Molding Considerations for process parameters Design for manufacturing, tooling and defects 1 2.008 spring 2004 S. Kim 2 Materials Solid materials metals ceramics Plastics thermoplastics thermosetts elastomers Plastic: Greek, plastikos, means to form or mold Plastics $400 billion shipments, 2002 US Music LPs, CDs No-sticking TEFLON Stre-e-e-tching SPANDEX www.plasticsdatasource.org Applications Name it 2.008 spring 2004 S. Kim 3 2.008 spring 2004 S. Kim 4 1

Automotive Plastics and Composites Use Exterior doors hoods fenders bumper covers (most cars have soft fascia) Interior instrument panels, door trim, seats, consoles Engine valve covers, intake manifolds, fluid containers, etc. Plastics, Polymers, Macromolecules Poly (many) + mer (structural unit) -[C 2 4 ] n -,poly[ethylene] C C C C Metal: single atoms, metallic bond Ceramic: metallic oxides, ionic bond or dipole interactions, van der Waals bonds spaghetti 2.008 spring 2004 S. Kim 5 2.008 spring 2004 S. Kim 6 Thermoplastic vs. Thermoset Stiffness Amorphous Crystalline (linear) Cross-linked (3D network) Crystallinity Cross-linking 2.008 spring 2004 S. Kim 7 2.008 spring 2004 S. Kim 8 2

Specific Volume: Amorphous vs. Crystalline Injection Molding Machine Vˆ Glassy solid Rubbery Melt Vˆ Brittle Tough and flexible Melt Tg (a) Tg+60 C Tg (b) Tm 2.008 spring 2004 S. Kim 9 2.008 spring 2004 S. Kim 10 Steps of Injection Molding Mold closing Mold filling 2.008 spring 2004 S. Kim 11 2.008 spring 2004 S. Kim 12 3

Packing, holding, cooling Mold opening, part removal Ejector pins 2.008 spring 2004 S. Kim 13 2.008 spring 2004 S. Kim 14 Injection Cycle Time $$$ Typical Cycle of Injection Molding Mold Close 1-2 sec Injection 2-5 sec Pack and old 8-10 sec Part Cool 10-20 sec Screw return 2-5 sec Mold open 1 sec Ejection 1 sec Injection Molding Cycle 2.008 spring 2004 S. Kim 15 2.008-spring-2004 S. Kim2.008 spring 2004 S. Kim Tadmor & Gogos 16 4

Viscosity Injection Molding Parameters Temperature and Pressure: Function (x,y,z) Melt Temperature Control Through Cylinder(Barrel) Frictional eating eating bands for 3 zones Rear zone Center zone (10F-20F hotter) Front Zone (10F-20F hotter) Nozzle Viscosity Shear thinning: paints Shear Thickening Newtonian Shear Thinning Shear Rate 2.008 spring 2004 S. Kim 17 2.008 spring 2004 S. Kim 18 Pressure Control Pressure distribution Injection unit Initial injection pressure Applied to the molten plastic and resulting from the main hydraulic pressure pushing against the back end of the injection screw (or plunger). Packing pressure Injection pressure inside mold Usually 1,000 psi to 5,000 psi Lower than hold and pack pressure between 10,000psi and 20,000 psi old pressure (packing) Pressure Control Compensate shrinkage Rule of thumb: old pressure = 150% of injection pressure. Applied at the end of the initial injection stroke, and is intended to complete the final filling of the mold and hold pressure till gate closure 2.008 spring 2004 S. Kim 19 2.008 spring 2004 S. Kim 20 5

Pressure Control Clamp force Pressure Required Total force = projected area times injection pressure (A X P) Rule of thumb 4 to 5 tons/in 2 can be used for most plastics. Example, Part is 10 in by 10 in by 1 in Projected area = Surface area = 10 in x 10 in = 100 in 2 Injection Pressure = 15,000 psi for PC Tonnage required to keep mold closed is 100 in 2 x 15,000 psi= 1,500,000 lbs = 750 tons (note : 2000 lbs = 1 ton) End of filling 2.008 spring 2004 S. Kim 21 10 in Parting line? 10 in 2.008 spring 2004 S. Kim 22 Mold cooling Molding cycle can be shortened by reducing time for cooling and solidification of molten plastics. Solidification time, t thickness 2 /α, thermal diffusitivity Warpage or stress in a part can be generated when mold shrinkage varies due to different thickness, leading internal residual stress difference. Even cooling Mold Temperature Control Mold Temperature Control Mold cooling with water, oil. ot mold for less residual stresses (orientation) Low thermal inertia Uneven cooling warpage, twisting, shrinkage defects Shrinkage can progress for up to 30 days. 2.008 spring 2004 S. Kim 23 2.008 spring 2004 S. Kim 24 6

Flow path ratio -Flow path ratio is the ratio between L (the distance between the gate and the farthest point in the molding dimension) and T (the thickness of the part). -When molding large or thin parts, the flow path ratio is calculated to determine if molten plastics can fill the mold cavity. Rule of thumb Polyethylene (PE) L/T = 280-100 Polypropylene (PP) L/T = 280-150 Polyvinyl chloride (PVC) L/T = 280-70 Polystyrene (PS) L/T = 300-220 Polycarbonate (PC) L/T = 160-90 Acrylonitrile butadienstylene (ABS) L/T = 280-120 Polyamide (PA) L/T = 320-200 2.008 spring 2004 S. Kim 25 Injection molding process window Pmax Pmin Poor quality Low cost Tmin flash Good shortshot Tmax Better weld Degradation burn 2.008 spring 2004 S. Kim 26 Design for Manufacturing Part design Moldable Draft angle Shrinkage Reinforcements (ribs and bosses) Cycle time Appearance (defects) Mold Design Gate balancing Process Control Draft angle - For removing parts from the mold -1-2 o, material, dimension, texture dependent - Cavity side smaller, core side larger. - Crystalline material has more shrinkage. - Amorphous material has smaller shrinkage. 2.008 spring 2004 S. Kim 27 2.008 spring 2004 S. Kim 28 7

Shrinkage Reinforcement Thickness increase L = α L T = α T α: shrinkage rate Resin Shrinkage (%) Polyethylene (PE) 1.5-6.0 Polypropylene (PP) 1.0-3.0 Polyvinyl chloride (PVC) 0.1-0.5 Polystyrene (PS) 0.2-0.6 Polycarbonate (PC) 0.5-0.8 Acrylonitrile butadienstylene 0.3-0.8 Polyamide (PA) 0.6-2.0 Stiffer grade material PP (unfilled), 4,400 psi tensile strength PP (20% glass filled), 7,700 psi Add secondary features, Ribs, bosses 2.008 spring 2004 S. Kim 29 2.008 spring 2004 S. Kim 30 Ribs and Bosses Injection Molded Part Design Base feature + secondary feature (ribs, bosses, holes, etc.) Nominal wall : Keep part thickness as thin and uniform as possible. shorten the cycle time, improve dimensional stability, and eliminate surface defects. For greater stiffness, reduce the spacing between ribs, or add more ribs. Nominal wall thickness should be within +/- 10% chamfered corners 2.008 spring 2004 S. Kim 31 2.008 spring 2004 S. Kim 32 8

Mold Structure Mold Structure - Cavity and core 2.008 spring 2004 S. Kim 33 2.008 spring 2004 S. Kim 34 Mold Structure: Parting line A dividing line between a cavity plate and a core plate of a mold. - Make a parting line on a flat or simple-curved surface so that flash cannot be generated. -Venting gas or air. Two plate mold One parting line 2.008 spring 2004 S. Kim 35 2.008 spring 2004 S. Kim 36 9

Three plate mold Mold Structure: Undercut, Slide core Two parting lines 2.008 spring 2004 S. Kim 37 2.008 spring 2004 S. Kim 38 Melt Delivery Sprue A sprue is a channel through which to transfer molten plastics injected from the injector nozzle into the mold. Runner A runner is a channel that guides molten plastics into the cavity of a mold. Gate -Delivers the flow of molten plastics. -Quickly cools and solidifies to avoid backflow after molten plastics has filled up in the cavity. -Easy cutting from a runner -Location is important to balance flow and orientation and to avoid defects. Gate A gate is an entrance through which molten plastics enters the cavity. 2.008 spring 2004 S. Kim 39 2.008 spring 2004 S. Kim 40 10

Fan gate, Film gate, Direct gate Gate Positioning Point 1: Set a gate position where molten plastics finish filling up in each cavity simultaneously. Same as multiple points gate. Point 2: Set a gate position to the thickest area of a part. This can avoid sink marks due to molding (part) shrinkage. Point 3: Set a gate position to an unexposed area of part or where finishing process can be easily done. Point 4: Consider weldline, molecular orientation. 2.008 spring 2004 S. Kim 41 2.008 spring 2004 S. Kim 42 Runner cross section Runner balancing Runner cross section that minimizes liquid resistance and temperature reduction when molten plastics flows into the cavity. -Too big - Longer cooling time, more material, cost -Too small - short shot, sink mark, bad quality -Too long - pressure drop, waste, cooling ot runner, runnerless mold 2.008 spring 2004 S. Kim 43 Balanced Not balanced 2.008 spring 2004 S. Kim 44 11

Defects Molding defects are caused by related and complicated reasons as follows: * Malfunctions of molding machine * Inappropriate molding conditions * Flaws in product and mold design * Improper Selection of molding material Weldline This is a phenomenon where a thin line is created when different flows of molten plastics in a mold cavity meet and remain undissolved. It is a boundary between flows caused by incomplete dissolution of molten plastics. It often develops around the far edge of the gate. Cause Low temperature of the mold causes incomplete dissolution of the molten plastics. Solution Increase injection speed and raise the mold temperature. Lower the molten plastics temperature and increase the injection pressure. Change the gate position and the flow of molten plastics. Change the gate position to prevent development of weldline. 2.008 spring 2004 S. Kim 45 2.008 spring 2004 S. Kim 46 Flashes Flashes develop at the mold parting line or ejector pin installation point. It is a phenomenon where molten polymer smears out and sticks to the gap. Cause Poor quality of the mold. The molten polymer has too low viscosity. Injection pressure is too high, or clamping force is too weak. Solution Avoiding excessive difference in thickness is most effective. Slow down the injection speed. Apply well-balanced pressure to the mold to get consistent clamping force, or increase the clamping force. Enhance the surface quality of the parting lines, ejector pins and holes. Short shot This is the phenomenon where molten plastics does not fill the mold cavity completely. and the portion of parts becomes incomplete shape. Cause The shot volume or injection pressure is not sufficient. Injection speed is so slow that the molten plastics becomes solid before it flows to the end of the mold. Solution Apply higher injection pressure. Install air vent or degassing device. Change the shape of the mold or gate position for better flow of the plastics. 2.008 spring 2004 S. Kim 47 2.008 spring 2004 S. Kim 48 12

Warpage Sink marks This deformation appears when the part is removed from the mold and pressure is released. Cause Uneven shrinkage due to the mold temperature difference (surface temperature difference at cavity and core), and the thickness difference in the part. Injection pressure was too low and insufficient packing. Solution Take a longer cooling time and lower the ejection speed. Adjust the ejector pin position or enlarge the draft angle. Examine the part thickness or dimension. Balance cooling lines. Increase packing pressure. -Equal cooling from the surface -Secondary flow -Collapsed surface Sink Mark ts ts < t t 2.008 spring 2004 S. Kim 49 2.008 spring 2004 S. Kim 50 CAE (computer aided engineering) Process simulation Material data base CAD MOLDFLOW C-Flow 2.008 spring 2004 S. Kim 51 2.008 spring 2004 S. Kim 52 13