Wall slip and extrudate instability of 4-arm star polybutadienes in capillary flow

2004 ◽  
Vol 43 (4) ◽  
Author(s):  
Zhiyong Zhu
Keyword(s):  
2006 ◽  
Author(s):  
V. Bertola

The wicking of a model yield-stress fluid (hair-gel solution in water) in a capillary tube is studied experimentally. By changing the hair-gel concentration in the solution, the yield stress varied from 5 to 20 Pa. A simple force balance between capillary and viscous forces suggests that the fluid should stop flowing as soon as the wall shear stress reaches the yield value, at a critical distance from the inlet which is independent of the tube diameter. However, this theoretical argument is not confirmed by experiments, which show that the fluid moves well beyond the critical distance determined theoretically, and that there is a well-defined effect of the tube diameter. It is proposed that such behavior may be determined by wall slip, which causes the flow to switch from the Poiseuille flow regime to the plug flow regime.


AIChE Journal ◽  
1997 ◽  
Vol 43 (3) ◽  
pp. 598-608 ◽  
Author(s):  
Eugene E. Rosenbaum ◽  
Savvas G. Hatzikiriakos

Polymer ◽  
2010 ◽  
Vol 51 (10) ◽  
pp. 2221-2228 ◽  
Author(s):  
Ryohei Komuro ◽  
Koji Kobayashi ◽  
Takashi Taniguchi ◽  
Masataka Sugimoto ◽  
Kiyohito Koyama

e-Polymers ◽  
2008 ◽  
Vol 8 (1) ◽  
Author(s):  
Chun-Sheng Chen

AbstractThe determination of the proper rheological behaviour of the polymer melt within micro structured geometry is vital for accurately simulating the micro moulding. The paucity of suitable equipments is one of main hurdles in the investigation of micro melt rheology. In the present study, a measurement system for the melt viscosity of low and high density polyethylene polymer melts flowing through micro-channels was established. The capillary flow model with Rabinowitsch correction was used in the calculations of the viscosity based on the measured pressure drop and volumetric flow rate. The effect of the morphology structure on the viscosity characteristics for both the LDPE and HDPE resins within micro-channels was investigated and discussed. It was found that the measured viscosity values for LDPE and HDPE in the test ranges are significantly lower (about 40~56% and 22~29% for LDPE and HDPE, respectively, flowing through a channel size of 150μm) than those obtained with a traditional capillary rheometer. Moreover, both the percentage reduction in the viscosity value and the ratio of the slip velocity to the mean velocity increase as the micro-channel size decreases. It can be observed that the rheological behaviours of the HDPE and LDPE resins in microscopic scale are different from those in macroscopic scale as a result of the wall slip effect. It also revealed that the wall slip occurs more easily for the LDPE resin within micro channels than HDPE resin due to enlarged effect of morphology structure.


1999 ◽  
Vol 9 (1) ◽  
pp. 10-16 ◽  
Author(s):  
Karim Bekkour

Abstract Foams have been prepared from water added with a surfactant (Sodium-Dodecyl-Sulfate, SDS) and a polymer (Poly-Ethylene-Oxide, PEO) at different concentrations. This work was devoted to a study of the flow properties of the foams. The pressure drops were measured during flow in capillary tubes (2.5, 3.5 and 4 mm) in laminar regime. It was found a strong dependence of the flow curves on capillary diameter showing that pronounced wall slip effects exist. Two known approaches were applied to quantify the slip velocity: (a) the Mooney method, in which the key assumption is that the slip velocity depends only on the wall shear stress, was not applicable and (b) the Oldroyd-Jastrzebski method, in which the assumption is that the slip velocity depends not only on the wall shear stress but also on the flow geometry, yielded satisfactory results. The determination of the pressure drop coefficient showed that the Metzner and Reed correlation, i.e., the Reynolds analogy based on the generalised Reynolds number, could be applied if the data are corrected for slip effects.


AIChE Journal ◽  
2009 ◽  
Vol 56 (6) ◽  
pp. 1447-1455 ◽  
Author(s):  
Z. Y. Wang ◽  
Y. C. Lam ◽  
X. Chen ◽  
S. C. Joshi

1995 ◽  
Vol 39 (1) ◽  
pp. 139-149 ◽  
Author(s):  
P. J. Halliday ◽  
A. C. Smith

Sign in / Sign up

Export Citation Format

Share Document