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SLIP FLOW IN RECTANGULAR MICROTUBES
Microscale Thermophysical Engineering, 1998Microscale fluid dynamics has received intensive interest due to the extraordinary advances in electronic device miniaturization, where the peaks of temperature from hotspots must be reduced by a coolant flowing in a microchannel. One of the most meaningful microscale effects is the emergence of slip flow. The present analysis is concerned with the 2-D
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Journal of Fluids Engineering, 2017
A solution of the problem of Poiseuille slip flow through an eccentric cylindrical annulus is obtained in bipolar coordinates. The solution is in excellent agreement with the two published limiting cases of slip flow through concentric annuli and no-slip flow through eccentric annuli.
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A solution of the problem of Poiseuille slip flow through an eccentric cylindrical annulus is obtained in bipolar coordinates. The solution is in excellent agreement with the two published limiting cases of slip flow through concentric annuli and no-slip flow through eccentric annuli.
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Applied Scientific Research, 1966
A solution is presented for the flow of a viscous incompressible fluid in the entrance region of an annulus with slip occurring at the walls. The condition is imposed that the pressure drop found from momentum considerations should be the same as that from mechanical energy considerations.
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A solution is presented for the flow of a viscous incompressible fluid in the entrance region of an annulus with slip occurring at the walls. The condition is imposed that the pressure drop found from momentum considerations should be the same as that from mechanical energy considerations.
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Nature, 1947
The Poiseuille type of equation for capillaries of any shape takes the form, for capillaries of any cross-section, where k0 = 2 and m = r/2 for a circular capillary of radius r, and k0 has generally values between 2 and 3 for other shapes1. Application of this to granular beds follows by putting u = ue. ɛ. L/Le, m = ɛ/Sσ(1 — ɛ), k = k0. (Le/L)2, whence
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The Poiseuille type of equation for capillaries of any shape takes the form, for capillaries of any cross-section, where k0 = 2 and m = r/2 for a circular capillary of radius r, and k0 has generally values between 2 and 3 for other shapes1. Application of this to granular beds follows by putting u = ue. ɛ. L/Le, m = ɛ/Sσ(1 — ɛ), k = k0. (Le/L)2, whence
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Hall and ion slip effects on MHD rotating flow of elastico-viscous fluid through porous medium
International Communications in Heat and Mass Transfer, 2020M Veera Krishna, Ali Chamkha
exaly
Slip length measurement in rectangular graphene nanochannels with a 3D flow analysis
Carbon, 2022Qin-Yi Li +2 more
exaly