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 5 頁
... Rheology of fibrous suspensions ... 161 161 166 171 171 172 178 181 6.3.5 Transient orientation distributions 188 ... Rheological Equipment ...... 217 8.5 Evaluation of the Modified Inner Cylinder . 220 8.6 Rheology of Highly - Filled ...
... Rheology of fibrous suspensions ... 161 161 166 171 171 172 178 181 6.3.5 Transient orientation distributions 188 ... Rheological Equipment ...... 217 8.5 Evaluation of the Modified Inner Cylinder . 220 8.6 Rheology of Highly - Filled ...
第 217 頁
... rheological equipment . 8.4 Rheological Equipment A Haake RV20 coaxial - cylinder system ( Fig . 3 ) was chosen for our investigation for two main reasons . Firstly , it allows the measurement of the time - dependent behavior of the ...
... rheological equipment . 8.4 Rheological Equipment A Haake RV20 coaxial - cylinder system ( Fig . 3 ) was chosen for our investigation for two main reasons . Firstly , it allows the measurement of the time - dependent behavior of the ...
第 226 頁
... rheological data to simulate the flow of filled materials in a mould , we plan to utilize the following approach . By using an injection - moulding machine as our rheometer , we will closely match the unsteady behavior of the actual ...
... rheological data to simulate the flow of filled materials in a mould , we plan to utilize the following approach . By using an injection - moulding machine as our rheometer , we will closely match the unsteady behavior of the actual ...
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