Steady flow energy equation :
For steady flow energy equation , Consider a control volume, in which mass ∆m1/∆t enters through inlet with parameters
U = internal energy
v = Velocity
V = specific volume ( V1 = V2 )
P = pressure
Z= potential head
Similarly mass ∆m2/∆t exits through outlet.
Therefore mass concentrationin control volume is
(∆m/∆t) control volume = ∆m1/∆t – ∆m2/∆t
•(∆E/∆t) in = internal energy+ flow work + kinetic energy+ potential energy + heat
Therefore , (∆E/∆t) in = ∆m1/∆t { U1 + P1V1 + v12/2 + gZ1 } + ∆Q/∆t
At exit , (∆E/∆t)out = ∆m2/∆t { U2 + P2V2 + v2 2/2 + gZ2 } + ∆W/∆t
(E/∆t) control volume= (∆E/∆t)in – (∆E/∆t)out
(E/∆t) control volume= ∆m1/∆t { h1 + v12/2 + gZ1 } + ∆Q/∆t – ∆m2/∆t { h2 + v2 2/2 + gZ2} – ∆W/∆t
Assumptions :
• (∆m/∆t) control volume = 0
• (E/∆t) control volume= 0
Here , (∆m/∆t) control volume = ∆m1/∆t – ∆m2/∆t = 0
So , ∆m1/∆t = ∆m2/∆t = m
Similarly,
(∆E/∆t)in = (∆E/∆t)out
Therefore ,
m{ h1 + v12/2 + gZ1 } + ∆Q/∆t = m{ h2 + v2 2/2 + gZ2 } + ∆W/∆t
this is Steady flow energy equation or SFEE .
Bernoulli Equation :
from Steady flow energy equation
m{ h1 + v12/2 + gZ1 } + ∆Q/∆t = m{ h2 + v2 2/2 + gZ2 } + ∆W/∆t
Assume ,
(a)No heat transfer
(b) No work transfer
(c)No change in internal energy
(d)No change in density ( p = constant)
Then ,
m{ h1 + v12/2 + gZ1 } + ∆Q/∆t = m{ h2 + v2 2/2 + gZ2 } + ∆W/∆t
and
U1 + P1V1 + v12/2 + gZ1 = U2 + P2V2 + v2 2/2 + gZ2
As , Specific Volume = 1/ Density
i.e., V = 1/ p
Therefore
P1/p + v1 2/2 + gZ1 = P2 /p+ v2 2/2+ gZ2
P1/pg + v1 2/2g + Z1 = P2 /pg+ v22/2g+ Z2
This is Bernoulli Equation
Conclusion :
Hence both Steady flow energy equation and Bernoulli Equation are based on energy conservation and Bernoulli Equation is limited form of steady flow energy equation .
This is also known as the first law of thermodynamics for open system.