PLATES is GIVEN by: \(u = \frac{1}{{2\mu }}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)(dy - {y^2})\)Now\(\frac{{du}}{{dy}} = \frac{1}{{2\mu }}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)\left( {d - 2y} \right)\)Shear stress distribution, τ is given by\(\tau = \frac{{\mu \;du}}{{dy}}\)\(\tau = \frac{1}{2}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)\left( {d - 2y} \right)\)From above, following can be concluded:1. Shear Stress distribution, ‘τ’ is linear.2. At y = d/2 i.e. mid point; τ = 0 i.e. At center shear stress = 0.3. At y = 0 i.e. at boundary; \(\tau = {\tau _{MAX}} = \frac{1}{2}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)\left( d \right)\) i.e. shear stress is maximum at boundary.∴ Shear stress is maximum at the plate boundaries and zero at plane \(\frac{d}{2}\) away from each plate

"> PLATES is GIVEN by: \(u = \frac{1}{{2\mu }}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)(dy - {y^2})\)Now\(\frac{{du}}{{dy}} = \frac{1}{{2\mu }}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)\left( {d - 2y} \right)\)Shear stress distribution, τ is given by\(\tau = \frac{{\mu \;du}}{{dy}}\)\(\tau = \frac{1}{2}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)\left( {d - 2y} \right)\)From above, following can be concluded:1. Shear Stress distribution, ‘τ’ is linear.2. At y = d/2 i.e. mid point; τ = 0 i.e. At center shear stress = 0.3. At y = 0 i.e. at boundary; \(\tau = {\tau _{MAX}} = \frac{1}{2}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)\left( d \right)\) i.e. shear stress is maximum at boundary.∴ Shear stress is maximum at the plate boundaries and zero at plane \(\frac{d}{2}\) away from each plate

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In a laminar flow between two fixed plates held parallel to each other at a distance d, the shear stress is:1) Maximum at plane \(\frac{d}{2}\) away from each plate and zero at the plate boundaries.2) Zero throughout the passage.3) Maximum at the plate boundaries and zero at plane \(\frac{d}{2}\) away from each plate.Which of the above statements is/are correct?

Heat Transfer Laminar Flow in Heat Transfer 11 months ago

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The velocity distribution through laminar flow in fixed parallel PLATES is GIVEN by: \(u = \frac{1}{{2\mu }}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)(dy - {y^2})\)Now\(\frac{{du}}{{dy}} = \frac{1}{{2\mu }}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)\left( {d - 2y} \right)\)Shear stress distribution, τ is given by\(\tau = \frac{{\mu \;du}}{{dy}}\)\(\tau = \frac{1}{2}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)\left( {d - 2y} \right)\)From above, following can be concluded:1. Shear Stress distribution, ‘τ’ is linear.2. At y = d/2 i.e. mid point; τ = 0 i.e. At center shear stress = 0.3. At y = 0 i.e. at boundary; \(\tau = {\tau _{MAX}} = \frac{1}{2}\left( {\frac{{ - \partial P}}{{\partial x}}} \right)\left( d \right)\) i.e. shear stress is maximum at boundary.∴ Shear stress is maximum at the plate boundaries and zero at plane \(\frac{d}{2}\) away from each plate

Posted on 01 Nov 2024, this text provides information on Heat Transfer related to Laminar Flow in Heat Transfer. Please note that while accuracy is prioritized, the data presented might not be entirely correct or up-to-date. This information is offered for general knowledge and informational purposes only, and should not be considered as a substitute for professional advice.

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