Compressible Flow credits Logo credits
Potto Home Contact Us

Potto Home

About Potto

Chapters:

  Content
  Introduction
  Sound
  Isentropic
  Shock
  Gravity
  Isothermal
  Fanno
  Rayleigh
  Tank
  Piston
  Oblique
  Prandtl-Meyer
  Hard copy
  Gas Dynamics Tables

Other things:
Other resources
Download Area
calculators

Other Resources

  FAQs
  Compare Other Books
  Articles

Potto Statistics

License

Feedback

next up previous index
Next: Isothermal Nozzle (T=constant) Up: Nozzle Flow With External Previous: Nozzle Flow With External   Index

Isentropic Nozzle (Q=0)

The energy equation for isentropic nozzle provides


Utilizing equation (4.27) when $ ds =0$ leads to


For the isentropic process $ dP = const \times k \rho^{k-1} d\rho$ when the $ const = P / \rho^{k}$ at any point of the flow. The equation (7.2) becomes

$\displaystyle \overbrace{\overbrace{P \over \rho^k}^{any\;point} k {\rho^k \ove...
...\rho} + UdU= k \overbrace{P \over \rho}^{RT} { d\rho \over \rho} UdU = f(x')dx'$ (7.3)
$\displaystyle { kRT d\rho \over \rho} + UdU = {c^{2} \over \rho} d\rho + UdU = f(x')dx'$    

The continuity equation as developed earlier (mass conservation equation isn't effected by the gravity)


Substituting $ d\rho / \rho$ from equation 7.3, into equation (7.2) moving $ d\rho$ to the right hand side, and diving by $ dx'$ yields
Rearranging equation (7.5) yields
And further rearranging yields
Equation (7.7) can be rearranged as
Equation (7.8) dimensionless form by utilizing $ x = x' / \ell$ and $ \ell$ is the nozzle length
And the final form of equation (7.9) is

The term $ {\ell f(x) \over c^2 }$ is considered to be very small ( $ 0.1\times 10/100000 < 0.1$ %) for ``standard'' situations. The dimensionless number, $ \ell f(x) \over c^2$ sometimes referred as Ozer number determines whether gravity should be considered in the calculations. Nevertheless, one should be aware of value of Ozer number for large magnetic fields (astronomy) and low temperature, In such cases, the gravity effect can be considerable.

As it was shown before the transition must occur when $ M=1$ . Consequently, two zones must be treated separately. First, here the Mach number is discussed and not the pressure as in the previous chapter. For $ M < 1$ (the subsonic branch) the term $ {2 \over \left( 1
-M^2 \right)}$ is positive and the treads determined by gravity and the area function.

$\displaystyle \left[ {1 \over A } {dA \over dx} + {\ell f(x) \over c^2 } \right]
> 0 \Longrightarrow d(M^2) > 0
$

or conversely,

$\displaystyle \left[ {1 \over A } {dA \over dx} + {\ell f(x) \over c^2 } \right]
< 0 \Longrightarrow d(M^2) < 0
$

For the case of $ M>1$ (the supersonic branch) the term $ {2 \over \left( 1
-M^2 \right)}$ is negative and therefore

$\displaystyle \left[ {1 \over A } {dA \over dx} + {\ell f(x) \over c^2 } \right]
> 0 \Longrightarrow d(M^2) < 0
$

For the border case $ M=1$ , the denominator $ 1-M^2=0$ , is zero either $ d(M^2) = \infty$ or

$\displaystyle \left[ {1 \over A } {dA \over dx} + {\ell f(x) \over c^2 } \right] = 0.
$

And the $ dM$ is indeterminate. As it was shown in chapter (4) the flow is chocked ($ M=1$ ) only when

It should be noticed that when $ f(x)$ is zero, e.g. horizontal flow, the equation (7.11) reduced into $ {dA \over dx} = 0 $ that was developed previously.

The ability to manipulate the location provides a mean to increase/decrease the flow rate. Yet this ability since Ozer number is relatively very small.

This condition means that the critical point can occurs in several locations that satisfies equation (7.11). Further, the critical point, sonic point is $ {dA \over Ax} \neq 0$ If $ f(x)$ is a positive function, the critical point happen at converging part of the nozzle (before the throat) and if $ f(x)$ is a negative function the critical point is diverging part of the throat. For example consider the gravity, $ f(x) = -g$ a flow in a nozzle vertically the critical point will be above the throat.


next up previous index
Next: Isothermal Nozzle (T=constant) Up: Nozzle Flow With External Previous: Nozzle Flow With External   Index
Created by:Genick Bar-Meir, Ph.D.
On: 2007-11-21