Robust Process Development and Scientific Molding 2010
DOI: 10.3139/9783446433427.fm
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Robust Process Development and Scientific Molding

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Cited by 16 publications
(29 citation statements)
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“…As the melt polymer flows toward the end of the mold, the air inside the unfilled region of the mold is compressed, making an opposite pressure to the flow. If there are no vents in the mold, the pressure of the polymer flow might be unable to overcome the counter pressure, which hinders the flow of the molten polymer and result in an incomplete filling of the mold 30 . As mentioned by Kazmer, the lack of venting can form a short shot in the molded product and may cause the phenomenon known as "dieseling" and defects known as "burn marks" 1 .…”
Section: Simulation Results: Mold With No Venting Systemmentioning
confidence: 99%
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“…As the melt polymer flows toward the end of the mold, the air inside the unfilled region of the mold is compressed, making an opposite pressure to the flow. If there are no vents in the mold, the pressure of the polymer flow might be unable to overcome the counter pressure, which hinders the flow of the molten polymer and result in an incomplete filling of the mold 30 . As mentioned by Kazmer, the lack of venting can form a short shot in the molded product and may cause the phenomenon known as "dieseling" and defects known as "burn marks" 1 .…”
Section: Simulation Results: Mold With No Venting Systemmentioning
confidence: 99%
“…Nevertheless, the decrease of the polymer viscosity due to a higher temperature along the cross section might compete with this phenomenon. Such behavior may lead to the arising of residual stresses in the polymer flow due to high shear rate values associated with the reduction of the molten polymer viscosity, as in the case of too high injection temperatures 29,30 . Another factor that should be considered in this analysis is the constant and slow cooling of the melt polymer.…”
Section: First Set Of Experimental Runs: Mold With No Venting Systemmentioning
confidence: 99%
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“…From the calculated flow front velocity and the increase in melt pressure (together with information on the flow channel geometry h sim i ), based on the equation of Hagen–Poiseuille, machine‐independent parameters such as the wall shear stress τ i , the shear rate 0.25emγ˙i, and the melt viscosity η i expressed in Eqs . 5–7 , can be derived between the event points . τi=normalΔpihsim0.25emi2()xsim0.25emi+1xsim0.25emi γ˙i=0,772*6vihsimi ηi=Δpihsim0.25emi212()xsim0.25emi+1xsim0.25emivi …”
Section: Proposition Of the New Methods For Determining The Flow Frontmentioning
confidence: 99%
“…Optimal setting of injection moulding process variables plays a very important role in controlling the quality of the injection moulded products (Mathivanan, Nouby and Vidhya, 2010). Applying and using design of experiments (DOEs) in injection moulding are relatively simple as compared to its use in other manufacturing or production processes, because most responses to process changes are linear (Kulkarni, 2010).…”
Section: Introductionmentioning
confidence: 99%