Expression for rate of flow through venturimeter :
Consider a venturimeter fixed in a horizontal pipe through
which a fluid is flowing (say water) as shown in figure 4.
Let d1 = diameter at inlet or at section 1
p1 =Pressure at section 1
v1 = velocity of fluid at section 1
a1 = area at section 1= (π/4)*d1 2
And d2, p2, v2, a2 are corresponding values at section 2
Applying Bernoulli’s equation at section 1 & 2 we get
(p1/ρg) + (v1 2 /2g) + (z1) = (p2/ρg) + (v2 2 /2g) + (z2)
As pipe is horizontal, hence z1=z2
(p1/ρg) + (v1 2 /2g) = (p2/ρg) + (v2 2 /2g) or
(p1-p2)/ρg = (v2 2 /2g) - (v1 2 /2g) ---- (1)
But (p1-p2)/ρg, is the difference of pressure head at sections 1 & 2 and it is equal to ‘h’ or
(p1-p2)/ρg = h
Substituting the value of (p1-p2)/ρg in the above eqn. (1) we
Get, h = (v2 2 /2g) - (v1 2 /2g) ---- (2)
now applying continuous equation at sections 1 & 2 a
1v1= a2v2 or v1 = (a2v2)/ a1
substitute the value of v1 in equation (2)
h= (v2 2 /2g) - [(a2v2/ a1) 2 /2g] = (v2 2 /2g)[1-(a2 2 /a1 2 )]
= (v2 2 /2g)[(a1 2 - a2 2 )/ a1 2 ]
v2 2 =2gh [a1 2 /( a1 2 - a2 2 )]
Therefore v2 =√[2gh {a1 2 /( a1 2 - a2 2 )}]
v2 = [a1 /√( a1 2 - a2 2 )]* √(2gh)
Discharge Q = a2v2
Qth = a2*[a1 /√( a1 2 - a2 2 )]* √(2gh) ---- (3)
Equation (3) gives the discharge under ideal conditions and is called theoretical discharge. Actual discharge will be less than theoretical discharge.
Qact = Cd[a1a2 /√( a1 2 - a2 2 )]*√(2gh)]
Where Cd is coefficient of venturimeter and its value is less than 1.
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