Cornell Injection Molding Program Progress Report No. 16: Covering the Period from January 1990 Through December 1991College of Engineering, Cornell University, 1991 - 351 頁 |
搜尋書籍內容
第 1 到 3 筆結果,共 58 筆
第 39 頁
... ( tk ) . The corresponding time increment , Atk , is chosen such that ūмF ( tk ) * Atk = CDX⭑LEXPT , resulting in a uniform streamwise mesh during this early phase of = the calculation . However , once Atk calculated from the - 39 -
... ( tk ) . The corresponding time increment , Atk , is chosen such that ūмF ( tk ) * Atk = CDX⭑LEXPT , resulting in a uniform streamwise mesh during this early phase of = the calculation . However , once Atk calculated from the - 39 -
第 40 頁
... calculated UMF from the first time step ) , we no longer advance the melt front ( and therefore no longer add additional nodes ) but continue the calculation with Atk = DTMMAX . It is during this latter phase that region II arises ...
... calculated UMF from the first time step ) , we no longer advance the melt front ( and therefore no longer add additional nodes ) but continue the calculation with Atk = DTMMAX . It is during this latter phase that region II arises ...
第 181 頁
... calculated assuming the rp - distributions are Gaussian with the standard deviations given above . For both aspect ratios , the resulting -distributions were nearly identical to the p - distribution calculated assuming a monodisperse rp ...
... calculated assuming the rp - distributions are Gaussian with the standard deviations given above . For both aspect ratios , the resulting -distributions were nearly identical to the p - distribution calculated assuming a monodisperse rp ...
內容
SUMMARY i | 9 |
CALCULATIONS RELATED TO VISCOSITY MODELLING | 13 |
SPIRALFLOW ANALYSIS INCLUDING VARIABLEDENSITY | 34 |
14 個其他區段未顯示
常見字詞
7-constant Anczurowski aspect ratio Bézier patch birefringence boundary curve calculated cavity CIMP cm³/sec constant continuity equation control volume cooling corresponding Couette device Cross model density diffusivity dilute regime distribution domain dyne dyne/cm² equation experimental results extensional fiber filling stage finite-difference finite-element flow length flow rate formulation free surface function gapwise gradient Gregory patch hydrodynamic increasing indicate injection molding injection-molding interactions interface layer Lpred material measured melt front mesh method Newtonian fluid nodes noted obtained orbit orientation packing pressure parameter particles Phys polymer polystyrene post-filling stage power-law predictions processing conditions R₁ radial region rheological rheometer rotation semi-dilute regime semi-dilute suspension Shaqfeh shear flow shear rate shear stress shown in Fig simple shear simulation slender-body theory SMCV SMCV's spiral flow sprue Table temperature thermal thickness vectors velocity disturbance viscoelastic viscosity model volumetric flow rate wall whereas zero อน