00:01
Here the head loss per unit mass in the pipeline can be written as p1 divided by rho plus alpha 1 multiplied by v1 squared divided by 2 plus gz1 minus p2 divided by r0 plus alpha 2 multiplied by v2 squared divided by 2 plus gz2 is equals to net head loss total head loss.
00:28
Let this is equation number 1.
00:29
Now here the pressure at the two sections in the tube are p1, p2, velocities are v1 v2.
00:34
Since the pipe is horizontal, hence, since pipe is horizontal, pipe is horizontal, hence z1 will be equals to z2 and the diameter of tu is constant.
00:53
So v1 will be equals to v2.
00:56
Assuming, assume, assume kinetic energy correction factor is equals to 1.
01:03
Alpha 1 is equal to alpha 1 is equal to alpha 2 is equal to 1.
01:05
So, so we can put all this value in equation number 1 and we can write, we can write, we can write, p1 minus p2 divided where row is equal to hl total.
01:21
So this term will cancel out each other and this term will also cancel up.
01:26
Out each other.
01:27
So from here we get we get change in pressure del p divided by row is equals to net head loss.
01:35
Let this is equation number two.
01:39
Now at temperature at t is equals to 15 degrees centigrade we know that the density of water is 999 kg per meter cube and the kind of and the dynamic viscosity mu is to 1 .14 multiplied by 10 to the power of minus 3 newton second per meter square, newton second per meter square.
02:02
So we will substitute all this value in equation number 1...