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 88 筆
第 166 頁
... constants of the suspended fibers in order to determine the orbit constant distribution , p ( C ) . They used a particle- averaged method to calculate p ( C ) by determining the orbit constant of about 500 different particles in a ...
... constants of the suspended fibers in order to determine the orbit constant distribution , p ( C ) . They used a particle- averaged method to calculate p ( C ) by determining the orbit constant of about 500 different particles in a ...
第 238 頁
... constant viscosity model indicated in Table 4 corresponds to the best fit of capillary - rheometer data for the ... constant viscosity fit in Fig . 1 is replaced by the 5 - constant viscosity fit shown in Fig . 3 , with model constants ...
... constant viscosity model indicated in Table 4 corresponds to the best fit of capillary - rheometer data for the ... constant viscosity fit in Fig . 1 is replaced by the 5 - constant viscosity fit shown in Fig . 3 , with model constants ...
第 247 頁
... constant values at late times based upon the 5 - constant model indicate that the mass inflow is sufficient in this case to essentially supply the additional mass associated with the increasing density due to cooling . In contrast , the ...
... constant values at late times based upon the 5 - constant model indicate that the mass inflow is sufficient in this case to essentially supply the additional mass associated with the increasing density due to cooling . In contrast , the ...
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