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 83 筆
第 104 頁
... equation is required to determine the interface position . In equation ( 2 ) , the pressure of the liquid on the free surface is decided by the equilibrium of the normal stress on the interface and , in equation ( 3 ) , the liquid ...
... equation is required to determine the interface position . In equation ( 2 ) , the pressure of the liquid on the free surface is decided by the equilibrium of the normal stress on the interface and , in equation ( 3 ) , the liquid ...
第 110 頁
... equation and is solved by its coupling with the continuity equation via equation ( 7 ) or ( 8 ) . The pressure of the air , assumed to be constant and uniform , is taken as the reference . Before each iteration , it must be determined ...
... equation and is solved by its coupling with the continuity equation via equation ( 7 ) or ( 8 ) . The pressure of the air , assumed to be constant and uniform , is taken as the reference . Before each iteration , it must be determined ...
第 228 頁
... equation ( 4 ) for the case of a large gap between the concentric cylinders . Differentiating the equation with respect to the stress at the inner cylinder surface , ta , yields ( noting that tb = a2ta / b2 ) : ΦΩ dτa = 11 ta [ χτα ) ...
... equation ( 4 ) for the case of a large gap between the concentric cylinders . Differentiating the equation with respect to the stress at the inner cylinder surface , ta , yields ( noting that tb = a2ta / b2 ) : ΦΩ dτa = 11 ta [ χτα ) ...
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