TORELINA® PPS Resin

Technical Information|Thermal Properties|Melt Viscosity Properties

A thermoplastic resin is in the solid state at temperatures less than the melting point, and when it is heated above the melting point, it melts and thus exhibits fluidity. The degree of stickiness of a liquid is expressed as its viscosity. Likewise, there are several methods of expressing the viscosity of a thermoplastic resin (fluidity) when it melts. Representative methods include melt mass-flow rate (MFR), melt volume-flow rate (MVR), a method using a measuring instrument such as a capillary rheometer, and bar flow evaluation using an actual injection molding machine.
In general, the melt viscosity properties tend to depend on the molecular weight of the PPS polymer. For reinforced grades and elastomer improvement grades, however, the fluidity is not necessarily correlated to the molecular weight because of the influence of the reinforcement content and other factors.

Ⅰ. Melt Mass-Flow Rate (MFR)

Fig. 6.9  Melt mass-flow rateFig. 6.9 Melt mass-flow rate

The MFR is a fluidity index, obtained by applying a constant weight to a specimen melted in a heating cylinder to extrude it through an orifice (from one marked line to another) and converting the discharge amount into a weight per ten minutes (units: g/10 minutes). (Fig. 6.9) With the same cylinder temperature and loading conditions, the higher the MFR value, the better the fluidity.
Usually, however, PPS is a non-Newtonian fluid that varies with the shear rate (or time), so if the apparent shear rate changes greatly with the molding conditions and the shape of the molded product, as in injection molding, the fluidity during molding may not match the MFR. In this case, melt viscosity measurement using a capillary rheometer, described in the next section, can be used.

Ⅱ. Capillary Rheometer

Fig. 6.10  Capillary rheometerFig. 6.10 Capillary rheometer

A capillary rheometer is used for that test method whereby the specimen melted in a cylinder is extruded through a capillary, in the same way as with the MFR. This method differs from the MFR method, however, in that the fluidity can be determined as melt viscosity (units: Pa・s), not as the resin weight per unit time. As shown in the schematic diagram (Fig. 6.10), a capillary rheometer detects the load when the molten resin is extruded with a piston at a constant rate, using a load cell, after which the melt viscosity is determined by applying Formulas 6.2 to 6.5. For PPS, which is a non-Newtonian fluid, the detected load (shear stress) varies with the piston rate (shear rate), so that the shear rate dependence of the melt viscosity can be determined by changing the piston rate at will. Note, however, that the shear rate determined by calculation is called the apparent shear rate (or shear stress), not the true shear rate (or shear stress) on the capillary wall. If the shear rate is used in CAE analysis, it is corrected to a true value, using Bagley correction, Rabinowitsch correction, and so on, to improve analysis accuracy. This technical document refers to uncorrected shear rate and shear stress, unless stated otherwise.

Fig. 6.11  Sear rate dependence (320℃, L/D = 40/1)Fig. 6.11 Sear rate dependence (320℃, L/D = 40/1)
Fig. 6.12  Temperature dependence (L/D = 40/1, shear Fig. 6.12 Temperature dependence (L/D = 40/1, shear

In general, the shear rate dependence of the melt viscosity is expressed as a double logarithmic chart to indicate the properties over a wide range. PPS is classified as a pseudoplastic fluid because the melt viscosity varies with the shear rate and, in particular, the melt viscosity decreases as the shear rate increases.
Fig. 6.11 shows the melt viscosity of glass fiber reinforced PPS of "TORELINA," relative to the shear rate. The slope of the shear rate dependence depends a combination of factors, such as the polymer structure and the additive type. For PPS, in particular, the slope of the shear rate dependence differs depending on whether it is cross-linked PPS or linear PPS. For cross-linked PPS, the slope is large because the sensitivity is high relative to the shear rate, whereas for a linear PPS, the slope tends to be small.
The melt viscosity is temperature-dependent, and decreases as the temperature rises. (Fig. 6.12) In injection molding, mold filling may be improved by increasing the injection speed. The reason for this is believed to be that viscosity decreases occur with high shear rates (shear rate dependence) and, in addition, the resin temperature rises due to shear heating (temperature dependence) also have an influence. If the fluidity is to be judged using the melt viscosity properties, an appropriate shear rate range must be confirmed according to the molding method and the shape. In injection molding, a rough guide for fluidity is an area of about 100 to 1000 (/s).

The shear rate dependence of the melt viscosity of various grades of TORELINA is shown in Figs. 6.13 to 6.21. In general, the higher the reinforcement content, the lower the fluidity, but TORELINA A575W20 and A495MA1 both offer excellent fluidity.

[General reinforced grades]

1 A504X90 (standard) and A604

  • Fig. 6.13  Shear rate dependence (A504X90)Fig. 6.13 Shear rate dependence (A504X90)
  • Fig. 6.14  Shear rate dependence (A604)Fig. 6.14 Shear rate dependence (A604)

2 A310MX04 (standard) and A610MX03

  • Fig. 6.15  Shear rate dependence (A310MX04)Fig. 6.15 Shear rate dependence (A310MX04)
  • Fig. 6.16  Shear rate dependence (A610MX03)Fig. 6.16 Shear rate dependence (A610MX03)

[Elastomer improvement grades]

3 A575W20, A673M, and A495MA1

  • Fig. 6.17  Shear rate dependence (A575W20)Fig. 6.17 Shear rate dependence (A575W20)
  • Fig. 6.18  Shear rate dependence (A673M)Fig. 6.18 Shear rate dependence (A673M)
  • Fig. 6.19  Shear rate dependence (A495MA1)Fig. 6.19 Shear rate dependence (A495MA1)

[Unreinforced grades]

3 A900 and A670T05

  • Fig. 6.20  Shear rate dependence (A900)Fig. 6.20 Shear rate dependence (A900)
  • Fig. 6.21  Shear rate dependence (A670T05)Fig. 6.21 Shear rate dependence (A670T05)

Ⅲ. Bar flow

The bar flow is used in a fluidity evaluation method using an actual injection molding machine and a mold. The bar flow depends on the molding conditions and the shape, so that it can be used to relatively judge the fluidity by specifying fixed conditions for the molding temperature, mold temperature, injection pressure, injection speed, and test shape, among others. The bar flow is a fluidity index that considers not only the melt viscosity but also other factors such as the solidification properties of the material. As such this index is very practical.
The spiral flow bar flow (convoluted type) for a 1-mm thickness of TORELINA is given in Table. 6.5. The bar flow differs depending on the reinforcement content and whether PPS is improved with elastomers.TORELINA"A575W20 offers excellent fluidity, however. In injection molding, a material with a higher fluidity can satisfy a wider range of molding conditions, and can be used to form a wider variety of shapes.

Table. 6.5 Spiral bar flow (1 mm t) of TORELINA

Item Units Glass fiber reinforced Glass + filler reinforced Elastomer improvement Unreinforced
A504X90 A604 A310MX04 A610MX03 A673M A575W20 A495MA1 A900 A670T05
Bar flow mm 135 120 105 90 150 200 140 200 150
  • ※ Molding conditions (settings): Molding temperature: 320℃, mold temperature: 130℃, injection pressure: 98 MPa, and injection speed: 100 mm/s