Cornell Injection Molding Program Progress Report No. 16: Covering the Period from January 1990 Through December 1991College of Engineering, Cornell University, 1991 - 351 頁 |
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第 1 到 3 筆結果,共 30 筆
第 98 頁
... FREE - SURFACE FLOW 4.1 Introduction Incompressible viscous flow with moving free surfaces has drawn broad attention because of its important application in environmental engineering , die casting , polymer processing and many other ...
... FREE - SURFACE FLOW 4.1 Introduction Incompressible viscous flow with moving free surfaces has drawn broad attention because of its important application in environmental engineering , die casting , polymer processing and many other ...
第 99 頁
... free surfaces is required , however , the fixed - mesh is a viable candidate ... surface by a function called the fractional volume of liquid ( VOF ) , f ... free surface . According to the definition in MAC [ 1 , 2 ] , cells without ...
... free surfaces is required , however , the fixed - mesh is a viable candidate ... surface by a function called the fractional volume of liquid ( VOF ) , f ... free surface . According to the definition in MAC [ 1 , 2 ] , cells without ...
第 100 頁
... free - surface flow . For example , Kheshgi and Scriven [ 9 ] solved the Navier- Stokes equations and the kinematic equation ( 1 ) by using the penalty - function approach to predict the migration of a free surface along pre - selected ...
... free - surface flow . For example , Kheshgi and Scriven [ 9 ] solved the Navier- Stokes equations and the kinematic equation ( 1 ) by using the penalty - function approach to predict the migration of a free surface along pre - selected ...
內容
SUMMARY i | 9 |
CALCULATIONS RELATED TO VISCOSITY MODELLING | 13 |
SPIRALFLOW ANALYSIS INCLUDING VARIABLEDENSITY | 34 |
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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