one dimensional flow with heat addition l.
Download
Skip this Video
Download Presentation
One Dimensional Flow with Heat Addition

Loading in 2 Seconds...

play fullscreen
1 / 56

One Dimensional Flow with Heat Addition - PowerPoint PPT Presentation


  • 192 Views
  • Uploaded on

One Dimensional Flow with Heat Addition. P M V Subbarao Professor Mechanical Engineering Department I I T Delhi. A Gas Dynamic Model for Cross Country Gas Pipe Lines…. Ideal Flow in A Constant Area Duct with heat Transfer. Mach equation gives. Mach equation in Momentum equation gives.

loader
I am the owner, or an agent authorized to act on behalf of the owner, of the copyrighted work described.
capcha
Download Presentation

PowerPoint Slideshow about 'One Dimensional Flow with Heat Addition' - shiloh


Download Now An Image/Link below is provided (as is) to download presentation

Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author.While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server.


- - - - - - - - - - - - - - - - - - - - - - - - - - E N D - - - - - - - - - - - - - - - - - - - - - - - - - -
Presentation Transcript
one dimensional flow with heat addition

One Dimensional Flow with Heat Addition

P M V Subbarao

Professor

Mechanical Engineering Department

I I T Delhi

A Gas Dynamic Model for Cross Country Gas Pipe Lines…..

slide3

Mach equation gives

Mach equation in Momentum equation gives

Mach equation in Energy equation gives

slide5

Integrating from point 1 to point 2:

In subsonic flow, heat addition increases the Mach Number.

In supersonic flow, heat addition decreases the Mach Number.

Addition of heat leads the flow to move towards M=1.

Removal of heat leads the flow to move away from M=1.

Therefore T0 will be maximum when M=1.

variation of stagnation temperature with mach number
Variation of Stagnation Temperature with Mach Number

Heat Removal

Heat Removal

T0

Heat Addition

Heat Addition

M=1

M

total heat addition or removal
Total Heat Addition or Removal

Total heat transfer per unit mass flow rate

relation between m 1 and m 2
Relation Between M1 and M2

Adiabatic ideal flow:

slide11

Similarly, for an ideal flow with heat addition

and for an ideal flow with heat removal

relation between m 1 and m 212

Adiabatic

Heat Removal

Relation Between M1 and M2

Heat Addition

M2

M1

slide15

Adiabatic

Heat Removal

Heat Addition

M1

maximum end condition
Maximum End Condition
  • If heat is added to the flow, the Mach number tends towards one.
  • If heat is removed from the flow, the Mach number tends away from one.
  • All the properties of the flow can be conveniently written in terms of conditions that exist when M2 = 1.
temperature entropy relation
Temperature Entropy Relation
  • Traditionally, heat addition or removal is characterized through relative temperature – entropy variations.
  • Entropy signifies the quality of heat transfer process.
  • An explicit relation between entropy and temperature is very useful in evaluating the heat transfer process.

On integration till maximum end point.

slide20

The pressure ratio equation gives:

Substitute M2 in equation for temperature ratio :

slide21

The roots of the equation are:

This allows the variation of temperature ratio with change in entropy to be found for any value of g.

rayliegh line
Rayliegh Line

One dimensional ideal flow with heat transfer is called as Rayliegh flow.

maximum entropy and maximum temperature points
Maximum Entropy and Maximum Temperature Points
  • Entropy will be maximum when M=1.
  • Heat addition moves the Mach number towards 1 and vice versa.
  • The point of maximum temperature occurs not at M=1.
  • This value can be found by differentiating temperature ratio equation.
slide24

M corresponding to Tmax:

Tmax occurs at M<1 and

variable area with heat transfer
Variable Area with Heat Transfer

Conservation of mass for steady flow:

Conservation of momentum for ideal steady flow:

slide27

Conservation of energy for ideal steady flow:

Ideal Gas law:

Combining momentum and gas law:

slide34

For heat addition, M=1,dA will be positive.

For heat removal, M=1,dA will be negative.

one dimensional flow with heat transfer friction

One Dimensional Flow with Heat Transfer & Friction

P M V Subbarao

Associate Professor

Mechanical Engineering Department

I I T Delhi

A Gas Dynamic Model for Gas Cooled High Heat Release Systems…..

governing equations
Governing Equations

Nonreacting, no bodyforces, viscous work negligible

Conservation of mass for steady flow:

Conservation of momentum for frictional steady flow:

Conservation of energy for ideal steady flow:

slide39

Ideal Gas law:

Mach number equation:

slide41

Combine conservation, state equations– can algebraically show

So we have three ways to change M of flow

– area change (dA): previously studied

– friction: f > 0, same effect as –dA

– heat transfer:heating, q’’’ > 0, like –dA cooling, q’’’ < 0, like +dA

mach number variations
Mach Number Variations
  • Subsonic flow (M<1): 1–M2 > 0
  • – friction, heating, converging area increase M (dM > 0)
  • – cooling, diverging area decrease M (dM < 0)
  • • Supersonic flow (M>1): 1–M2 < 0
  • – friction, heating, converging area decrease M (dM < 0)
  • – cooling, diverging area increase M (dM > 0)
sonic flow trends
Sonic Flow Trends

• Friction

– accelerates subsonic flow, decelerates supersonic flow

– always drives flow toward M=1

– (increases entropy)

• Heating

– same as friction - always drives flow toward M=1

– (increases entropy)

• Cooling

– opposite - always drives flow away from M=1

– (decreases entropy)

nozzles sonic throat
Nozzles : Sonic Throat

• Effect on transition point: sub  supersonic flow

• As M1, 1–M20, need { } term to approach 0

• For isentropic flow, previously showed

– sonic condition was dA=0, throat

• For friction or heating, need dA > 0

– sonic point in diverging section

• For cooling, need dA < 0

– sonic point in converging section

mach number relations
Mach Number Relations

• Using conservation/state equations can get equations for each TD property as function of dM2

slide46
Constant Area, Steady Compressible Flow withFriction Factor and Uniform Heat Flux at the Wall Specified
  • Choking limits and flow variables for passages are important parameters in one-dimensional, compressible flow in heated
  • The design of gas cooled beam stops and gas cooled reactor cores, both usually having helium as the coolant and graphite as the heated wall.
  • Choking lengths are considerably shortened by wall heating.
  • Both the solutions for adiabatic and isothermal flows overpredict these limits.
  • Consequently, an unchoked cooling channel configuration designed on the basis of adiabatic flow maybe choked when wall heat transfer is considered.
slide49
The local Mach number within the passage will increase towards the exit for either of two reasons or a combination of the two.
  • Both reasons are the result of a decrease in gas density with increasing axial position caused either by
  • (1) a frictional pressure drop or
  • (2) an increase in static temperature as a result of wall heat transfer.

Constant area duct:

slide51

Multiply throughout by M2

For a uniform wall heat flux q’’

choking length
Choking Length

K :non dimensional heat flux

M1

ad