| 220 - 220 |
Third of a series - Pioneering polymer industry developments - The first successful mathematical-computer modeling of a complex industrial process: Toyobo and melt spinning
White JL |
| 221 - 232 |
Polymer flow velocity in the helical channel in dependence of a coordinate system
Sikora R, Sasimowski E |
| 233 - 241 |
Non-isothermal transient startup of a starved flow modular co-rotating twin screw extruder
Kim EK, White JL |
| 242 - 254 |
Numerical simulations and experiments in a double-Couette flow geometry
Teverovskiy M, Manas-Zloczower I, Elemans P, Rekers G |
| 255 - 259 |
Dynamic analysis of melting in injection extruder
Yung KL, Xu Y, Lau F |
| 260 - 267 |
Production of pipe with uniform wall thickness: How to compensate for gravity sag
Pittman JFT, Farah IA |
| 268 - 272 |
Assessment of LDPE melt strength by use of rheotens mastercurves
Bernnat A, Wagner MH, Chai CK |
| 273 - 283 |
Analysis of flow and heat transfer in liquid composite molding
Yu B, Chiu HT, Ding Z, Lee LJ |
| 284 - 290 |
Solidification criterion on shrinkage predictions for semi-crystalline injection moulded samples
Pontes AJ, Pantani R, Titomanlio G, Pouzada AS |
| 291 - 296 |
Polymer melt rheology at high shear rates
Haddout A, Villoutreix G |
| 297 - 303 |
Factors affecting the stability of gas penetration in gas assist injection molded bifurcation parts
Liu SJ, Wu YC |
| 304 - 312 |
Transient polymer flow rate in injection mold filling
Chan WL, Daver F, Friedl C |
| 313 - 316 |
Flow analysis of injection-press molding process
Tsutsubuchi M, Kitayama T, Togawa Y, Nishio T, Kutschera H |
| 317 - 326 |
Properties of injection molded in situ composites based on PPS and a melt processable glass
Young RT, Baird DG |
| 327 - 331 |
A new approach in offline-optimization of the injection molding process
Kuhmann K, Meckbach S, Zhao G, Ehrenstein GW, Jeltsch-Fricker R |
