DynamarTM泰乐玛聚合物加工助剂在塑料软包装业的应用 We have many PowerPoint templates that has been specifically designed to help anyone e (MPa) control PPA pressure decrease 10-18 % with PPA present Experiment 1: Comparing with and without PPA Energy Consumption versus % LLDPE 实验 2 Effect on melt temperature at constant die pressure and output Experiment 2: Comparing with and without PPA Melt Temperature versus %LLDPE EXPERIMENT 3 Effect on output at constant die pressure and melt temperature Experiment 3:Comparing with and without PPA output versus %LLDPE TENSILE STRENGTH versus LDPE/LLDPE COMPOSITION Tensile Strength (MPa) % ELONGATION versus LDPE/LLDPE COMPOSITION % Elongation TEAR STRENGTH versus LDPE/LLDPE COMPOSITION TEAR STRENGTH (KN/m) % Transmission %Haze CONCLUSIONS Using PPA : *Allowing higher LLDPE ratios to be used in the LDPE/LLDPE blends *Allowing higher outputs at equivalent die pressures *Allowing low melt temperatures at equivalent die pressures * Increase the physical properties of the film by increase the concentration of LLDPE in an LDPE/LLDPE resin blend to decrease resin costs Equipment Extruder: Dyneon Kiefel blown film line grooved barrel, 40mm, 24/1 L/D Die: 40mm diameter, die gap Materials Base Resin: HMW-HDPE, 10 HLMI, dens. PPAs: 3% FX-9613 in 2 MI LLDPE 3% FX-5920A in 2 MI LLDPE 3% FX-5911X in 2 MI LLPDE HMW-HDPE Blown Film Trial Blown film Run Conditions Melt temperature: 205ºC Output: 15 kg/hr Shear rate: 640 s-1 Procedure Run base resin for 30-60 minutes Run base resin +700ppm PPA for 2 hours Blown film Gate Pressure Reduction 2500 2600 2700 2800 2900 3000 3100 3200 0
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Time (hrs) Gate Pressure (psi) FX-5911X FX-9613 FX-5920A 700ppm PPA in 10 HLMI HMW-HDPE Blown film Blown film Equipment Extruder: Dyneon Collin blown film line Smooth barrel, 45mm, 25L/D Die: 50mm diameter, die gap Materials Base Re