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- AMILAN™ Nylon Resin
- Injection-molding
- Molding conditions
Molding conditions
The following descriptions speak to the feasibility of using nylon to form a product (flowability and fill characteristics) and what molding conditions are most appropriate when working from a product drawing.
Polymer flowability
Polymer flowability is affected by the cavity shape (molded product thickness and shape complexity, as well
as flow resistance), grade, molding machine performance (maximum injection pressure, injection rate, mold
clamp pressure), molding conditions (polymer temperature, injection pressure) and gate cross section surface
area.
Figure 7.1 shows the results from a ribbon-shaped (5 mm width, 1-3 mm depth) spiral flow test. Please
consider the above factors in interpreting the results.
The flow ratio is the value arrived at by dividing the greatest possible distance that can be reached by the
polymer flowing into the cavity from the gate by the product thickness. Injection pressure represents net
plunger pressure. The flow ratio becomes smaller with greater product thicknesses.
To apply the flow ratio to general molded products, use a correction coefficient of 0.55 to 0.75 in light of
the above-mentioned factors.
< Exercise 1 >
Estimate the smallest moldable thickness of a 200 mmφ disc. Assume a material of CM1017 and the use of
direct gates that fill from the center.
< Answer >
Based on Figure 7.1, 1/t = 162 (assuming a material of CM1017, an injection pressure of 70 MPa and a polymer
temperature of 245°C). Using a correction coefficient of 0.7, 162 × 0.7 = 113. Because the gates
fill from the center, 1 = 200/2 = 100 mm. Thus, 100/113 ≈ 0.9 mm. So the smallest possible thickness
is 0.9 mm.
Figure 7.1: Nylon flow ratio
Melt viscosity
Melt viscosity can be used to compare the flowability of polymers. To calculate melt viscosity, discharge
molten polymer at different temperature levels at a constant load with a constant nozzle using a Koka flow
tester (a constant-load orifice-type flow tester). Calculate the melt viscosity based on the amount of
molten polymer discharged.
Formula 21: μ=πR4P/8LQ
Whereas:
μ: Melt viscosity (Pa・S)
R: Nozzle radius(5×10-5)(m)
P: Pressure (2)(MPa)
L: Nozzle length(1×10-4)(m)
Q: Discharge velocity(m3/s)
Figure 7.2 shows the melt viscosity of each nylon grade. From the graph, refer to the molding condition
settings for each grade. Generally, 100-300Pa・S is reasonable for injection-molding applications. That is
supported in particular by the fact that nylon has far greater flowability than other thermoplastic resins.
Figure 7.2: Change in melt viscosity of Toray nylon grades as a function of temperature