The polymer injection products produced by using the current injection molding method usually have many defects, such as short shot, jetting, sink mark, flow mark, weld mark, and floating fibers. These defects have to be eliminated by using post-processing processes such as spraying and coating, which will cause environment pollution and waste in time, materials, energy and labor. These problems can be solved effectively by using a new injection method, named as variotherm injection molding or rapid heat cycle molding (RHCM). In this paper, a new type of dynamic mold temperature control system using steam as heating medium and cooling water as coolant was developed for variotherm injection molding. The injection mold is heated to a temperature higher than the glass transition temperature of the resin, and keeps this temperature in the polymer melt filling stage. To evaluate the efficiency of steam heating and coolant cooling, the mold surface temperature response during the heating stage and the polymer melt temperature response during the cooling stage were investigated by numerical thermal analysis. During heating, the mold surface temperature can be raised up rapidly with an average heating speed of 5.4°C/s and finally reaches an equilibrium temperature after an effective heating time of 40 s. It takes about 34.5 s to cool down the shaped polymer melt to the ejection temperature for demolding. The effect of main parameters such as mold structure, material of mold insert on heating/cooling efficiency and surface temperature uniformity were also discussed based on simulation results. Finally, a variotherm injection production line for 46-inch LCD panel was constructed. The test production results demonstrate that the mold temperature control system developed in this study can dynamically and efficiently control mold surface temperature without increasing molding cycle time. With this new variotherm injection molding technology, the defects on LCD panel surface occurring in conventional injection molding process, such as short shot, jetting, sink mark, flow mark, weld mark, and floating fibers were eliminated effectively. The surface gloss of the panel was improved and the secondary operations, such as sanding and coating, are not needed anymore.
[1]
Byung Kim,et al.
INCREASING FLOW LENGTH IN THIN WALL INJECTION MOLDING USING A RAPIDLY HEATED MOLD
,
2002
.
[2]
John C. Russ,et al.
Surface analysis of injection molded TV components
,
1998
.
[3]
W. Rohsenow,et al.
Handbook of heat transfer applications
,
1985
.
[4]
J. M. Coulson,et al.
Heat Transfer
,
2018,
Finite Element Method for Solids and Structures.
[5]
J. Whitelaw,et al.
Convective heat and mass transfer
,
1966
.
[6]
J. Collier,et al.
Injection molding of polymeric LIGA HARMs
,
1999
.
[7]
Hans Nørgaard Hansen,et al.
Surface microstructure replication in injection molding
,
2007
.
[8]
Wen-Bin Young,et al.
Micro-injection molding with the infrared assisted mold heating system
,
2007
.
[9]
K. Jansen.
Heat transfer in injection moulding systems with insulation layers and heating elements
,
1995
.
[10]
S. Chen,et al.
Dynamic mold surface temperature control using induction heating and its effects on the surface appearance of weld line
,
2006
.
[11]
Jung-Ki Park,et al.
Weld-line characteristics of polycarbonate/acrylonitrile–butadiene–styrene blends. I. Effect of the processing temperature
,
2005
.
[12]
Sheng-Jye Hwang,et al.
Simulation of infrared rapid surface heating for injection molding
,
2006
.
[13]
Byung Kim,et al.
Development of rapid heating and cooling systems for injection molding applications
,
2002
.
[14]
N. Suh,et al.
Reducing residual stresses in molded parts
,
1989
.
[15]
Yasuo Kurosaki,et al.
A new concept of active temperature control for an injection molding process using infrared radiation heating
,
2002
.
[16]
S. Chen,et al.
SIMULATIONS AND VERIFICATIONS OF INDUCTION HEATING ON A MOLD PLATE
,
2004
.