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 48 筆
第 9 頁
... simulation and prediction of optimum process control . During the current reporting period we have continued our studies related to modelling the shear viscosity of polymer melts and its effect upon flow simulations . For example , a ...
... simulation and prediction of optimum process control . During the current reporting period we have continued our studies related to modelling the shear viscosity of polymer melts and its effect upon flow simulations . For example , a ...
第 9 頁
... simulation models ( Progress Report # 2 , September 1975 ) . In the third period , the experimental and numerical simulation program was extended from one - dimensional to two - dimensional - flow mold configura- tions . The numerical ...
... simulation models ( Progress Report # 2 , September 1975 ) . In the third period , the experimental and numerical simulation program was extended from one - dimensional to two - dimensional - flow mold configura- tions . The numerical ...
第 152 頁
... simulation . Presently , it is determined by trial and error . In the future , we hope to establish a systematic means of determining its value . 5.3 Examples In this section , advancing fluid fronts along planar and axisymmetric ...
... simulation . Presently , it is determined by trial and error . In the future , we hope to establish a systematic means of determining its value . 5.3 Examples In this section , advancing fluid fronts along planar and axisymmetric ...
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