Cornell Injection Molding Program Progress Report No. 17: Covering the Period from December 1991 Through February 1993College of Engineering, Cornell University, 1993 - 418 頁 |
搜尋書籍內容
第 1 到 3 筆結果,共 26 筆
第 218 頁
... resin in the cavity must remain as low as possible so that the contact time between fiber and resin increases . Sometimes the mold is vacuumed before the resin is injected ; this reduces the possibility of air entrapment by the fiber ...
... resin in the cavity must remain as low as possible so that the contact time between fiber and resin increases . Sometimes the mold is vacuumed before the resin is injected ; this reduces the possibility of air entrapment by the fiber ...
第 219 頁
... resins available in the market for RTM are normally formulated with a longer pot life to avoid resin gelation before the cavity gets filled . As a result , the assumption of isothermal flow is usually implemented in the study of cavity ...
... resins available in the market for RTM are normally formulated with a longer pot life to avoid resin gelation before the cavity gets filled . As a result , the assumption of isothermal flow is usually implemented in the study of cavity ...
第 227 頁
... resin during each particular time period . Equation ( 8 ) can be solved by the control - volume / finite- element ... resin viscosity , the porosity of the fiber mats after preforming and the permeability of the preform be known ...
... resin during each particular time period . Equation ( 8 ) can be solved by the control - volume / finite- element ... resin viscosity , the porosity of the fiber mats after preforming and the permeability of the preform be known ...
常見字詞
ABAQUS aligned Alloys analysis behavior boundary conditions calculated CIMP cm³/gm Composites constant cooling corresponding crystallization curve cylinder Darcy's Law data points density developed diffusivity direction disk effect equation et.al experimental results fiber mat fiber orientation Figure finite-element fluid formulation function gapwise gradient heat hydrodynamic i-PP injection molding injection-molded interactions interface isothermal kerosine layer linear liquid material matrix measurements melt mesh metal method microstructure mid-plane Newtonian Newtonian fluid nodes Non-Newtonian Fluid nondimensional numerical obtained orientation tensor PANLITE parameters particles permeability planar plotted Polym post-filling power-law predictions pressure region resin Reynolds number Rheocasting rheological rotation semi-dilute semi-solid shear flow shear rate shear stress SHELL10 shown in Fig shrinkage simple shear simulation slurry solid fraction solidification stress structure surface surface tension suspension temperature thermal thickness thin cavity Thixotropic tracer transverse values vector velocity disturbance viscoelastic viscosity wire deformation