What would you recommend as the best way to really cement these concepts and derivations so that you remember them long after the class is over? I find that I forget the material quickly and have to recap every time it's needed.
Pressure on the streamline and plate tend to cancel out because Prandtl simplified the y-momentum equation (NS Equation for y) to give dp/dy = 0. In other words, The pressure on the streamline is of the same order as on the plate.
How can you just put density out from the integral in the mass balance equation as if it is constant in all section 1 and 2? and also why is density supposed constant between inlet and outlet of the plate? are we talking of incompressible fluids in this case? did I miss something? :)
Really helpful! Thanks for posting!
Hlo i thought yu completed yur graduation ✨
What would you recommend as the best way to really cement these concepts and derivations so that you remember them long after the class is over? I find that I forget the material quickly and have to recap every time it's needed.
thats just how it goes, if you don't use it you'll probably lose it
what about the pressure forces on control volume
Pressure on the streamline and plate tend to cancel out because Prandtl simplified the y-momentum equation (NS Equation for y) to give dp/dy = 0.
In other words, The pressure on the streamline is of the same order as on the plate.
help on modeling spray impinging hot flat plate, thanks
How can you just put density out from the integral in the mass balance equation as if it is constant in all section 1 and 2? and also why is density supposed constant between inlet and outlet of the plate? are we talking of incompressible fluids in this case? did I miss something? :)
this is a theory of incompressible boundary layers
what is a C.V. analysis
Its part of reynolds transport therom equation
Control Volume
very helpful.
Thanks. ¡¡¡
thank-you