Question: Problem 1 ( 2 0 pts ) Oil with the density of 9 0 0 k g m 3 and the kinematic viscosity of 4

Problem 1(20 pts)
Oil with the density of 900kgm3 and the kinematic viscosity of 4.210-4m2s is discharged by a 3-mm-diameter and 2-m long horizontal pipe from a reservoir to the atmosphere. The height of the liquid level above the center of the pipe is 2.5m. Neglect the minor losses and determine,
a) The type of the flow in the pipe
b) The entrance length, Le
c) The equation of the velocity profile in the pipe
d) The equation of the shear stress profile in the pipe
e) The shear stress at r=1mm from the center
FORMULAS
Re=VD=VDvar,=dudy=w2rD
Q=VA,=(+t)dudy=dudy-bar(u'v')
P1+z1+V122g+HP-HT-??hL=P2+z2+V222g,w=pD4L=8VD=f8V2
hf=f(LD)V22g=8fLQ2g2D5=4wLD,Q=D4p128L
p=2Lr=4LwD=32LVD2=hL,Vc=pD216L
p-LsinL=2r,u(r)=(pD216L)(1-(2rD)2)=Vc(1-(2rD)2)
LeD=0.06Re for Laminar flow Vc-(?bar(u))u**=2.5ln(Ry)or(?bar(u))vc=(1-rR)1n
LeD=4.4Re16 for Turbulent flow VVc=2n2(n+1)(2n+1)
=dudy=w2rD
=(+t)dudy=dudy-bar(u'v')
w=pD4L=8VD=f8V2
Q=D4p128L
Vc=pD216L
u(r)=(pD216L)(1-(2rD)2)=Vc(1-(2rD)2)
Vc-(?bar(u))u**=2.5ln(Ry)or(?bar(u))Vc=(1-rR)1n
VVc=2n2(n+1)(2n+1)
Problem 1 ( 2 0 pts ) Oil with the density of 9 0

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