Recent content by lingesh

A stream of water at 300 Deg K flowing into a mixture at a velocity of 5m/s. Another stream of water at 400 Deg K is flowing in at 8 m/s.How to calculate the final velocity and temperature of the fluid after mixing? Please find the attached image? If it requires any c/s dimensions please assume..

i am really sorry..i got busy on some other project..so i can't do it now...

My opinion is, as the Area is uniform, acc to continuity eqn Q=A.V,i.e velocity at both ends is same,which makes RHS ZERO..

can you share the 3d model? i will try to simulate..

I thought its SSB. 5wl^3/384EI THAT gives 128.5mm. Whats new value from simulation? There will be 5 to 10% error between FEA and theoretical value..

Deflection at centre is =WL^3/48EI With your values as its in spreadsheet, i got 16mm..What value you are expecting?

You can refer this as a reference.

from ur calculations,i observed you are considering shaft as hollow,whereas actual model has 1" hole only for small length.So actual wt of this shaft should be more than what you have taken.

My basic understanding as per the formula is Re no proportional to velocity.If considering density,c/s and viscocity factors constant,Re no depends upon velocity.Thus as the velocity increases,boundary layer thickness vanishes to zero,flow becomes turbulent and Re no is higher. Only first part...

If those upward force components F1...Fn are equal in magnitude,then you can simplify it as UDL. If they are different and varying gradually you can consider it as UVL and solve the problem.

yes, thickness is constant and volume is conserved..

Hi, How can i calculate the blank dia required for a torispherical dish?Please share any formulas if you have.. OD=1332 MM THICKNESS 6MM

Thanks...

Hi, I am a bit confused about the units of MI...I read that MI of rectangle is b*d^3/12,so unit is mm^4..Also i read in wiki that unit of MI is kg.mm^2... Both are correct,but why this difference is?

Oh I made a mistake while quoting that...actually it s from DEvens..