Polymer/mold interfacial heat transfer during injection molding

dc.contributor.authorKamala Nathan, D.K.
dc.contributor.authorPrabhu, K.N.
dc.date.accessioned2026-02-04T12:25:15Z
dc.date.issued2024
dc.description.abstractAn experimental injection molding setup was designed and fabricated. The purpose of the setup is to cast polymer components and estimate the polymer/mold interfacial heat flux transients during injection molding. The mold plate is instrumented with K-type thermocouples to record its thermal history continuously during the cyclic process. Experiments were performed at a melt injection temperature of 280°C. Velocity and shear rate profiles were determined to assess the flow behavior of the melt. The spatiotemporal heat flux transients at the interface and the mold surface temperature were estimated using measured temperature data inside the mold as input to an inverse heat conduction problem. The estimated boundary heat flux transients were used to numerically simulate the polymer melt's cooling behavior. From the estimated heat flux and surface temperatures, heat transfer coefficients (HTC) were determined. The peak value of the HTC was 5775 W/m2K and occurred at a mold surface temperature of 35.7°C and polymer surface temperature of 47.4°C. The evolution of the air gap at the interface was quantified using an exponential fit. The estimated air gap width corresponding to peak HTC was about 4 μm and increased to about 100 μm towards the end of the solidification. While the peak heat flux is associated with the start of the formation of polymer skin on the mold surface, the peak HTC corresponds to the onset of nucleation of the air gap or a nonconforming contact. Highlights: An experimental setup to study heat transfer during injection molding. Spatiotemporal heat flux transients (q) were estimated during injection molding. Polymer temperatures were simulated using q, and HTC was determined. The peak HTC indicated the onset of nucleation of an air gap. Evolution of air gap at the interface was modeled using an exponential fit. © 2023 Society of Plastics Engineers.
dc.identifier.citationPolymer Engineering and Science, 2024, 64, 2, pp. 888-900
dc.identifier.issn323888
dc.identifier.urihttps://doi.org/10.1002/pen.26592
dc.identifier.urihttps://idr.nitk.ac.in/handle/123456789/21301
dc.publisherJohn Wiley and Sons Inc
dc.subjectAtmospheric temperature
dc.subjectHeat conduction
dc.subjectInjection molding
dc.subjectInverse problems
dc.subjectMolds
dc.subjectNucleation
dc.subjectPolymer melts
dc.subjectShear flow
dc.subjectSurface temperature
dc.subjectThermocouples
dc.subjectAir-gaps
dc.subjectExponentials
dc.subjectHeat flux transients
dc.subjectHeat transfer co-efficients
dc.subjectIHCP
dc.subjectInterfacial heat transfer
dc.subjectMold surfaces
dc.subjectPolymer molds
dc.subjectPolymer/mold interface
dc.subjectSurface temperatures
dc.subjectHeat flux
dc.titlePolymer/mold interfacial heat transfer during injection molding

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