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 15 筆
第 172 頁
... rotation and translation causes particles to pass by each other without making contact . In addition , Evans showed that the hydrodynamic interactions between a pair of fibers calculated from slender - body theory do not cause fibers to ...
... rotation and translation causes particles to pass by each other without making contact . In addition , Evans showed that the hydrodynamic interactions between a pair of fibers calculated from slender - body theory do not cause fibers to ...
第 199 頁
... rotation and have a rotation rate of O ( 1 / rp ) . Fibers in flipping orbits rotate out of the x - z plane . In these orbits , fibers remain aligned ( O ( 1 / rp ) angle from the x direction ) for long O ( rp ) times . Such fibers rotate ...
... rotation and have a rotation rate of O ( 1 / rp ) . Fibers in flipping orbits rotate out of the x - z plane . In these orbits , fibers remain aligned ( O ( 1 / rp ) angle from the x direction ) for long O ( rp ) times . Such fibers rotate ...
第 227 頁
... rotating coaxial cylinder system , a liquid is placed in the annular space between the two cylinders . In the present ... rotation ( 4 ) viscosity is a scalar ( 5 ) motion is steady ( 6 ) no relative motion between the cylinders and the ...
... rotating coaxial cylinder system , a liquid is placed in the annular space between the two cylinders . In the present ... rotation ( 4 ) viscosity is a scalar ( 5 ) motion is steady ( 6 ) no relative motion between the cylinders and the ...
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