Basic formula for compound A:
98% LLDPE/LDPE+GL+GM
Process: loss in weight feeding system-> high torque twin screw extruder-> water ring die face pelletizing
Parameters:
Model | Screw Diameter (mm) | L/D | Screw RPM | Main Motor KW | Torque Grade T/N3 | Output kg/h |
HT-63 | 62.4 | 32-68 | 300-900 | 110-315 | 12.3 | 350-1000 |
HT-72 | 71 | 32-68 | 300-900 | 160-450 | 11.8 | 600-2000 |
HT-85 | 81 | 32-68 | 300-900 | 220-630 | 11.2 | 800-2500 |
HT-95 | 93 | 32-68 | 300-900 | 355-900 | 11.8 | 1200-3000 |
Basic formula for compound B
95% LLDPE+antioxidant+GL
Process: standard twin screw extruder -> water cooling strand pelletizing
Model | Screw Diameter (mm) | L/D | Screw RPM | Main motor KW | Torque Grade T/N3 | Capacity kg/h |
SHJ-30 | 30 | 32-68 | 400/500/600 | 11 | 5.8 | 5-50 |
SHJ-36 | 35.6 | 32-68 | 500/600/700/800 | 15-18.5-22 | 5.7 | 20-80 |
SHJ-42 | 41.2 | 32-68 | 500/600/700/800 | 22-30-37 | 5.7 | 50-120 |
SHJ-50 | 50.5 | 32-68 | 500/600/700/800 | 37-45-55 | 5.8 | 80-200 |
Then mix 95% of compound A and 5% compound B material for the XLPE Cable extrusion