Application of polymeric coatings to fibers can be accomplished by drawing a fiber through a bath of molten polymer: see schematic below. R Wire 2kR Molten Polymer →V Let's assume steady, isothermal, and incompressible flow. i. Using Navier-Stokes equations in a cylindrical coordinate system along with appropriate boundary conditions, derive an expression for the z velocity as a function of the radial coordinate r. ii. Show that the amount of polymer coated per unit time, say M, is given by M =p¹Vk²(1-2Ink)-1] where p denotes the density of the molten (liquid) polymer. iii. In good engineering design it is important to be able to control the product parameters (coating thickness in the present case) by varying process variables (draw speed). From this point of view, can the proposed design be improved? If so, how?

Elements Of Electromagnetics
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Author:Sadiku, Matthew N. O.
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Application of polymeric coatings to fibers can be accomplished by drawing a fiber through a
bath of molten polymer: see schematic below.
Wire2kR
Molten Polymer
→V
Let's assume steady, isothermal, and incompressible flow.
i. Using Navier-Stokes equations in a cylindrical coordinate system along with appropriate
boundary conditions, derive an expression for the z velocity as a function of the radial
coordinate r.
ii. Show that the amount of polymer coated per unit time, say M, is given by
R²V [k²(1-2Ink)-1]
M=p²
2 lnk
where p denotes the density of the molten (liquid) polymer.
iii. In good engineering design it is important to be able to control the product parameters
(coating thickness in the present case) by varying process variables (draw speed). From this
point of view, can the proposed design be improved? If so, how?
Transcribed Image Text:Application of polymeric coatings to fibers can be accomplished by drawing a fiber through a bath of molten polymer: see schematic below. Wire2kR Molten Polymer →V Let's assume steady, isothermal, and incompressible flow. i. Using Navier-Stokes equations in a cylindrical coordinate system along with appropriate boundary conditions, derive an expression for the z velocity as a function of the radial coordinate r. ii. Show that the amount of polymer coated per unit time, say M, is given by R²V [k²(1-2Ink)-1] M=p² 2 lnk where p denotes the density of the molten (liquid) polymer. iii. In good engineering design it is important to be able to control the product parameters (coating thickness in the present case) by varying process variables (draw speed). From this point of view, can the proposed design be improved? If so, how?
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