New rheological developments for reactive processing of poly(ε-caprolactone)

被引:5
作者
Cassagnau, Philippe [1 ]
Gimenez, Jerome [1 ]
Bounor-Legare, Veronique [1 ]
Michel, Alain [1 ]
机构
[1] Univ Lyon 1, Lab Mat Polymeres & Biomat, CNRS, UMR 5627, F-69622 Villeurbanne, France
关键词
rheology; reactive extrusion; polymerisation; poly(epsilon-caprolactone);
D O I
10.1016/j.crci.2006.06.005
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
This short review aims to show how an integrated activity on reactive processing have been developed these last years in our laboratory. We can say that the originality of this approach is based on combining developments in chemistry, in line instrumentation, and rheology aspects. Our rheological works can be divided into four important contributions: rheo-physics, rheo-chemistry, rheo-mixing and rheo-processing. These different parts are illustrated from the epsilon-caprolactone polymerisation in bulk and dispersed media. Rheo-physics studies allowed us to calculate the molecular weight distribution and chain structures of in situ polymerised poly(epsilon-caprolactone) samples. From rheo-chemistry works, we are now able to predict the variation of the complex shear modulus versus the extent of the polymerisation. The developments of new rheological tools such as rheo-mixer enable us to investigate complex mixing situations encountered in reactive polymer blends and formulations. Lastly, a rheo-processing approach based on the in-line measurement of the viscosity in a slit rheometer at the die exit of the extruder allows us to envisage its application to the experimental control of the reactive processing in extruder.
引用
收藏
页码:1351 / 1362
页数:12
相关论文
共 22 条
[1]   Quantitative analysis of mixer-type rheometers using the Couette analogy [J].
Aït-Kadi, A ;
Marchal, P ;
Choplin, L ;
Chrissemant, AS ;
Bousmina, M .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2002, 80 (06) :1166-1174
[2]   URETHANE POLYMERIZATION IN A COUNTERROTATING TWIN-SCREW EXTRUDER [J].
BOUILLOUX, A ;
MACOSKO, CW ;
KOTNOUR, T .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (11) :2431-2436
[3]   From dynamic moduli to molecular weight distribution: A study of various polydisperse linear polymers [J].
Carrot, C ;
Guillet, J .
JOURNAL OF RHEOLOGY, 1997, 41 (05) :1203-1220
[4]  
Carrot C, 1996, J APPL POLYM SCI, V61, P1887, DOI 10.1002/(SICI)1097-4628(19960912)61:11<1887::AID-APP4>3.0.CO
[5]  
2-F
[6]   Rheological study of mixing in molten polymers: 2-mixing of reactive systems [J].
Cassagnau, P ;
Fenouillot, F .
POLYMER, 2004, 45 (23) :8031-8040
[7]   Rheological study of mixing in molten polymers: 1-mixing of low viscous additives [J].
Cassagnau, P ;
Fenouillot, F .
POLYMER, 2004, 45 (23) :8019-8030
[8]   RHEOLOGY OF POLYDISPERSE POLYMERS - RELATIONSHIP BETWEEN INTERMOLECULAR INTERACTIONS AND MOLECULAR-WEIGHT DISTRIBUTION [J].
CASSAGNAU, P ;
MONTFORT, JP ;
MARIN, G ;
MONGE, P .
RHEOLOGICA ACTA, 1993, 32 (02) :156-167
[9]   Reactive blending by in situ polymerization of the dispersed phase [J].
Cassagnau, P ;
Nietsch, T ;
Bert, M ;
Michel, A .
POLYMER, 1999, 40 (01) :131-138
[10]   Generic dynamic model for simulation and control of reactive extrusion [J].
Choulak, S ;
Couenne, F ;
Le Gorrec, Y ;
Jallut, C ;
Cassagnau, P ;
Michel, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (23) :7373-7382