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 24 筆
第 172 頁
... interactions have the net effect of producing a Co - distribution that favors low orbit constants relative to the isotropic C - distribution . As can be seen in Fig . 2 , these orbits rotate around the z - axis but never have a large ...
... interactions have the net effect of producing a Co - distribution that favors low orbit constants relative to the isotropic C - distribution . As can be seen in Fig . 2 , these orbits rotate around the z - axis but never have a large ...
第 196 頁
... interactions among fibers are still hydrodynamic even in a semidilute suspension . The purpose of the current study is to calculate theoretically the effect of these hydrodynamic interactions on the center - of - mass position of one ...
... interactions among fibers are still hydrodynamic even in a semidilute suspension . The purpose of the current study is to calculate theoretically the effect of these hydrodynamic interactions on the center - of - mass position of one ...
第 197 頁
... interactions , leading to results that can be expressed as a modified force distribution and a Green's function , taking account of multi - particle interactions . Since two particles in a semi - dilute suspension must interact through ...
... interactions , leading to results that can be expressed as a modified force distribution and a Green's function , taking account of multi - particle interactions . Since two particles in a semi - dilute suspension must interact through ...
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