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 22 筆
第 39 頁
... melt front is still advancing , then ISTAR = IMF and the temperature distribution at the streamwise mid - point location just behind the melt front [ i.e. at X ( IMF ) - .5 * DX ( IMFM1 ) ] is taken as Ti , j , k + 1 = Ti - 1,1 , k + 1 ...
... melt front is still advancing , then ISTAR = IMF and the temperature distribution at the streamwise mid - point location just behind the melt front [ i.e. at X ( IMF ) - .5 * DX ( IMFM1 ) ] is taken as Ti , j , k + 1 = Ti - 1,1 , k + 1 ...
第 41 頁
... ( melt front ) . Upon rearrangement , we have that m3 = m1 + m2 + M4 ( 23 ) which simply indicates that the rate at which mass enters the system at the inlet equals the sum of the rates at which the mass in the fixed control volume ...
... ( melt front ) . Upon rearrangement , we have that m3 = m1 + m2 + M4 ( 23 ) which simply indicates that the rate at which mass enters the system at the inlet equals the sum of the rates at which the mass in the fixed control volume ...
第 58 頁
... melt front continues to advance slightly ; i.e. , since the density is essentially constant in this case , it follows that the melt front must advance since moutlet = Minlet and Minlet will be non - zero , being driven by the imposed ...
... melt front continues to advance slightly ; i.e. , since the density is essentially constant in this case , it follows that the melt front must advance since moutlet = Minlet and Minlet will be non - zero , being driven by the imposed ...
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