Cornell Injection Molding Program Progress Report No. 15: Covering the Period from September 1988 Through January 1990College of Engineering, Cornell University, 1990 - 338 頁 |
搜尋書籍內容
第 1 到 3 筆結果,共 28 筆
第 152 頁
... linear representation shown in Fig . 1 , with end - point coordinates as follows : Cp ( T ) = ( 1.11,1.38,1.83,2.24 ) x 107 erg gm ° C ( 1 ) " " at T = ( 0,66,100,240 ) ° C As incorporated into PACK1D - G , Cp ( T ) can be evaluated by ...
... linear representation shown in Fig . 1 , with end - point coordinates as follows : Cp ( T ) = ( 1.11,1.38,1.83,2.24 ) x 107 erg gm ° C ( 1 ) " " at T = ( 0,66,100,240 ) ° C As incorporated into PACK1D - G , Cp ( T ) can be evaluated by ...
第 233 頁
... linear and can also be solved by the so - called Linear Theory iterative method which requires no initial condition [ 8 ] . Because the Darcy - Weisbach correlation is implicit , we use the Hazen - Williams correlation [ 8 ] to generate ...
... linear and can also be solved by the so - called Linear Theory iterative method which requires no initial condition [ 8 ] . Because the Darcy - Weisbach correlation is implicit , we use the Hazen - Williams correlation [ 8 ] to generate ...
第 272 頁
... linear - shrinkage results . Specifically , the sensitivity of the linear - shrinkage measurements to varying process conditions is larger by a factor of 10 or 20 compared with expectations based upon the volumetric - shrinkage ...
... linear - shrinkage results . Specifically , the sensitivity of the linear - shrinkage measurements to varying process conditions is larger by a factor of 10 or 20 compared with expectations based upon the volumetric - shrinkage ...
常見字詞
air traps apparent viscosity behavior best-fit boundary calculated candidate curves candidate points Carreau model cavity-filling COOL3D cooling rate corresponding Cross model density determined developed elements equation experiments Figure filling stage flow rate flow-front region fluid Fraction of solid function gate geometry glycerin Hieber increase injection molding injection-molding injection-molding process instant linear lines and air material melt front mesh MOLDFLOW Newtonian Newtonian fluid node numerical optimization particles Pb alloy PMMA polygon polypropylene polystyrene post-filling stage power-law predicted melt-front advancement pressure drop pressure traces processing conditions Progress Report relative viscosity results in Fig rheological rheometer segments semi-solid alloy shear rate shear stress shown in Fig shrinkage simulation solid fraction Styron surface suspension SWEEP2D swept area symbols Table thermal conductivity thermoset thickness torque V₁ velocity vertex curve viscoelastic viscosity model volume fraction volumetric volumetric flow rate warpage weld lines yield stress