Nozzle Exit Velocity | Determine Gas Velocity

  • Thread starter Thread starter Mathias Thomsen
  • Start date Start date
  • Tags Tags
    Nozzle Velocity
AI Thread Summary
To determine the gas velocity at the nozzle exit for carbon dioxide flowing through a well-insulated nozzle, apply the Steady Flow Energy Equation (S.F.E.E.), which simplifies to h1 + v1^2/2 = h2 + v2^2/2 under the assumption of negligible potential energy and heat transfer. The specific enthalpy values (h1 and h2) must be obtained from CO2 property tables based on the given inlet and outlet conditions. An initial attempt using Bernoulli's equation yielded an incorrect velocity of 362 m/s, while the expected result is 265 m/s. It is crucial to accurately reference the correct thermodynamic properties to solve for the exit velocity. Proper application of these principles will lead to the correct determination of gas velocity at the nozzle exit.
Mathias Thomsen
Messages
1
Reaction score
0

Homework Statement


Carbon dioxide gas flows through a well-insulated nozzle operating at steady state. Potential energy effects are neglected.

Inlet:
T1 = 500 K
p1 = 5 bar
v1 = 100 m/s

Outlet:
T2 = 460 K
p2 = 3 bar
v2 = ?

How do I determine the gas velocity at the nozzle exit?

Homework Equations



Bernoulli's equation?

The Attempt at a Solution



Bernoulli's equation, but it didn't give me the right answer. The result should be 265 [m/s] according to my lector.

My try:

rho1:= p1/(R·T1)

rho2:= p2/(R·T2)

p1+(1/2)·rho1·v1^2 = p2+(1/2)·rho2·v2^2

solved for v2:

v2 = 362 m/s
 
Physics news on Phys.org
Thanks for the post! Sorry you aren't generating responses at the moment. Do you have any further information, come to any new conclusions or is it possible to reword the post?
 
Nozzle is a steady flow device. So, applying Steady Flow Energy Equation (S.F.E.E.) ,

h1 + v12/2 + Z1g + dQ/dm = h2 + v22/2 + Z2g + dW/dm

Here h1 , h2 → sp. enthalpy at inlet and outlet resp.
v1 , v2 → vel. at inlet and outlet resp.
Z1 , Z2 → elevation of inlet and oulet sections above arbitrary datum
dQ/dm → net heat transfer per kg of CO2 thru Control Surface
dW/dm → net work transfer per kg of CO2 thru C.S.

Potential energy changes are neglected ⇒ Z1g =0 , Z2g = 0
As nozzle is well insulated ⇒ dQ/dm = 0
Also dW/dm =0

⇒ h1 + v12/2 = h2 + v22/2 ... (1)

Now to find the values of h1 and h2 under given conditions you will have to refer to CO2 property tables.
(Steam tables are the most common ones. I tried to look up for CO2 tables on the net but couldn't find the right one. There are some online applications too where the user inputs values of P and T and the app display enthalpy & other thermodynamic prop. values under given conditions. It didn't work out for me. However, do check it for yourself.)

Once values of h1 and h2 are known simply substitute them in eqn. (1)

Hope this helps ! Thank you :) :)
 
Back
Top