Presentation is loading. Please wait.

Presentation is loading. Please wait.

CP502 Advanced Fluid Mechanics

Similar presentations


Presentation on theme: "CP502 Advanced Fluid Mechanics"— Presentation transcript:

1 CP502 Advanced Fluid Mechanics
Compressible Flow Part 01_Set 01: Steady, quasi one-dimensional, isothermal, compressible flow of an ideal gas in a constant area duct with wall friction

2 Incompressible flow assumption is not valid if Mach number > 0.3
What is a Mach number? Definition of Mach number (M): M ≡ Speed of the flow (u) Speed of sound (c) in the fluid at the flow temperature For an ideal gas, specific heat ratio specific gas constant (in J/kg.K) R. Shanthini Feb 2012 absolute temperature of the flow at the point concerned (in K)

3 For an ideal gas, = M = c u u Unit of u = m/s
Unit of c = [(J/kg.K)(K)]0.5 = [J/kg]0.5 = (N.m/kg)0.5 = [kg.(m/s2).m/kg]0.5 = [m2/s2]0.5 = m/s R. Shanthini Feb 2012

4 quasi one-dimensional flow
constant area duct quasi one-dimensional flow compressible flow steady flow isothermal flow ideal gas wall friction Diameter (D) is a constant speed (u) u varies only in x-direction x Density (ρ) is NOT a constant Mass flow rate is a constant Temperature (T) is a constant Obeys the Ideal Gas equation is the shear stress acting on the wall R. Shanthini Feb 2012 where is the average Fanning friction factor

5 Friction factor: For laminar flow in circular pipes:
          where Re is the Reynolds number of the flow defined as follows: For lamina flow in a square channel:                For the turbulent flow regime:                                                               Quasi one-dimensional flow is closer to turbulent velocity profile than to laminar velocity profile. R. Shanthini Feb 2012

6 Ideal Gas equation of state:
temperature pressure specific gas constant (not universal gas constant) volume mass Ideal Gas equation of state can be rearranged to give K Pa = N/m2 kg/m3 J/(kg.K) R. Shanthini Feb 2012

7 Problem 1 from Problem Set 1 in Compressible Fluid Flow:
Starting from the mass and momentum balances, show that the differential equation describing the quasi one-dimensional, compressible, isothermal, steady flow of an ideal gas through a constant area pipe of diameter D and average Fanning friction factor shall be written as follows: where p, ρ and u are the respective pressure, density and velocity at distance x from the entrance of the pipe. (1.1) R. Shanthini Feb 2012

8 p p+dp D u u+du dx x Write the momentum balance over the differential volume chosen. (1) steady mass flow rate cross-sectional area shear stress acting on the wall is the wetted area on which shear is acting R. Shanthini Feb 2012

9 p p+dp D u u+du dx x (1.1) Equation (1) can be reduced to Substituting
Since , and , we get (1.1) R. Shanthini Feb 2012

10 Problem 2 from Problem Set 1 in Compressible Fluid Flow:
Show that the differential equation of Problem (1) can be converted into which in turn can be integrated to yield the following design equation: where p is the pressure at the entrance of the pipe, pL is the pressure at length L from the entrance of the pipe, R is the gas constant, T is the temperature of the gas, is the mass flow rate of the gas flowing through the pipe, and A is the cross-sectional area of the pipe. (1.2) (1.3) R. Shanthini Feb 2012

11 It is a constant for steady, isothermal flow in a constant area duct
The differential equation of problem (1) is in which the variables ρ and u must be replaced by the variable p. (1.1) Let us use the mass flow rate equation and the ideal gas equation to obtain the following: and and therefore It is a constant for steady, isothermal flow in a constant area duct R. Shanthini Feb 2012

12 Using , and in (1.1) we get (1.2) R. Shanthini Feb 2012

13 p pL L Integrating (1.2) from 0 to L, we get which becomes (1.3)
R. Shanthini Feb 2012

14 Problem 3 from Problem Set 1 in Compressible Fluid Flow:
Show that the design equation of Problem (2) is equivalent to where M is the Mach number at the entry and ML is the Mach number at length L from the entry. (1.4) R. Shanthini Feb 2012

15 We need to relate p to M! Design equation of Problem (2) is
which should be shown to be equivalent to where p and M are the pressure and Mach number at the entry and pL and ML are the pressure and Mach number at length L from the entry. (1.3) (1.4) We need to relate p to M! R. Shanthini Feb 2012

16 We need to relate p to M! which gives
= constant for steady, isothermal flow in a constant area duct Substituting the above in (1.3), we get (1.4) R. Shanthini Feb 2012

17 Summary Design equations for steady, quasi one-dimensional, isothermal,compressible flow of an ideal gas in a constant area duct with wall friction (1.1) (1.2) (1.3) (1.4) R. Shanthini Feb 2012


Download ppt "CP502 Advanced Fluid Mechanics"

Similar presentations


Ads by Google