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 32 筆
第 28 頁
... shear - stress range of 105.0 to 106.6 dyne / cm2 ( note that the shear stress is the product of the two coordinates in Figs . 4 or 5 , i.e. t = naya since the stress level is unaffected by the Rabinowitsch correction ) . That is , over ...
... shear - stress range of 105.0 to 106.6 dyne / cm2 ( note that the shear stress is the product of the two coordinates in Figs . 4 or 5 , i.e. t = naya since the stress level is unaffected by the Rabinowitsch correction ) . That is , over ...
第 30 頁
... shear - stress ) level exceeds that of the third cross - over point of the " 2 " curves ( i.e. at Q ≈ 88 cm3 / sec ) . That is , solely on the basis of the above analysis of the isothermal results , the high Ap associated with the " 1 ...
... shear - stress ) level exceeds that of the third cross - over point of the " 2 " curves ( i.e. at Q ≈ 88 cm3 / sec ) . That is , solely on the basis of the above analysis of the isothermal results , the high Ap associated with the " 1 ...
第 221 頁
... shear rates in Fig . 7 do not exhibit the shear - thinning behavior evidenced in Fig . 6 even though the Cox - Merz [ 6 ] relation is expected for such a general - purpose PS ... Shear Stress ( Pa ) · 221- Rheology of Highly-Filled Materials.
... shear rates in Fig . 7 do not exhibit the shear - thinning behavior evidenced in Fig . 6 even though the Cox - Merz [ 6 ] relation is expected for such a general - purpose PS ... Shear Stress ( Pa ) · 221- Rheology of Highly-Filled Materials.
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