| 298 - 298 |
Pioneers of polymer processing - Thomas Hancock - The first polymer processing innovator .1.
White JL |
| 299 - 309 |
The extensional flow mixer, EFM
Luciani A, Utracki LA |
| 310 - 319 |
Continuous polymerization of caprolactam-polyether sulfone solutions in a twin screw extruder to form reactive polyamide-6/polyether sulfone blends and their melt spun fibers
Kye H, White JL |
| 320 - 328 |
Biodegradable poly(lactic acid) with high molecular weight
Miyoshi R, Hashimoto N, Koyanagi K, Sumihiro Y, Sakai T |
| 329 - 340 |
Acceleration of chemical reaction in reactive extrusion accompanied by devolatilization
Chen L, Hu GH, Lindt JT |
| 341 - 346 |
Viscous-elastic effects in a PA 6 melt - Cause of unevennesses in melt-spun yarns
Beyreuther R |
| 347 - 351 |
Gear pump performance in polypropylene filament yarn uniformity
Shumpert BB, Padsalgikar AD, Ellison MS, Hosangadi GS, Henshaw I |
| 352 - 362 |
Physically-based model of thermoplastics injection molding for control applications
Rafizadeh M, Patterson WI, Kamal MR |
| 363 - 368 |
Effect of pressure and shear stress on crystallization behaviors in injection molding
Ito H, Minagawa K, Takimoto J, Tada K, Koyama K |
| 369 - 372 |
The crystallinity of PVC and its effect on physical properties
Bao Y, Weng Z, Huang Z, Pan Z |
| 373 - 382 |
Molecular orientation in polycarbonate induced by cooling stresses - On the origin of the surface maximum
WimbergerFriedl R |
