Abstract
For highly viscous polymer melts, considerable fluid temperature rises produced by viscous heating can be a disturbing factor in viscosity measurements. By scrutinizing the experimental and simulated capillary pressure losses for polymeric liquids, we demonstrate the importance of applying a viscous heating correction to the shear viscosity, so as to correct for large errors introduced by the undesirable temperature rises. Specifically, on the basis of a theoretical derivation and 3-D nonisothermal flow simulation, an approach is developed for retrieving the equivalent shear viscosity in capillary rheometry, and we show that the shear viscosity can be evaluated by using the average fluid temperature at the wall, instead of the bulk temperature, as previously assumed. With the help of a viscous Cross model in analyzing the shear-dominated capillary flow, it is possible to extract the viscous heating contribution to capillary pressure loss, and the general validity of the methodology is assessed using the experiments on a series of thermoplastic melts, including polymers of amorphous, crystalline, and filler-reinforced types. The predictions of the viscous model based on the equivalent viscosity are found to be in good to excellent agreement with experimental pressure drops. For all the materials studied, a near material-independent scaling relation between the dimensionless temperature rise (Θ) and the Nahme number (Na) is found, Θ ~ Na0.72, from which the fluid temperature rise due to viscous heating as well as the resultant viscosity change can be predicted.
Highlights
Shear viscosity is important for thermally developing flow problems in which the temperature, pressure, and velocity in conduits are continually changing in the flow direction
Because of the highly viscous nature of polymer melts and their low thermal conductivities, experimental and computational evidences for appreciable fluid temperature rises of 10–50 ◦C due to viscous heating have been reported in the literature for various materials in die flows [3,4,6,7,8,13,15,16,17,18,19,20,21], viscous heating can be a disturbing factor in viscosity measurements
We have systematically investigated the viscous heating correction and extracted its contribution to the capillary pressure drop in thermally developing capillary flows for a series of injection molding grade thermoplastic melts
Summary
Shear viscosity is important for thermally developing flow problems in which the temperature, pressure, and velocity in conduits are continually changing in the flow direction. For a simulation of such injection molded parts, an excellent description of the rheological behavior of viscous polymer melts relies on an experimentally measured shear viscosity that is free of the large errors introduced by undesirable effects, such as the temperature deviations due to viscous heating [3,6,7,8,9,10] or the pressure dependence of viscosity [11,12,13,14]. One of the major concerns in using a capillary rheometer to measure melt viscosity is viscous heating (or temperature thinning), it can occur at low shear rates in the presence of extremely viscous materials [5]. Because of the highly viscous nature of polymer melts and their low thermal conductivities, experimental and computational evidences for appreciable fluid temperature rises of 10–50 ◦C due to viscous heating have been reported in the literature for various materials in die flows [3,4,6,7,8,13,15,16,17,18,19,20,21], viscous heating can be a disturbing factor in viscosity measurements
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