who wants to be a cfd expert? in the me 566 course title, cfd for engineering design, what does the...

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Who Wants to Be a CFD Expert? In the ME 566 course title, CFD for Engineering Design , what does the acronym CFD stand for? A. Car Free Day B. Cash Flow Diagram C. Computational Fluid Dynamics Lifelines Phone a Friend Ask the Audience

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Who Wants to Be a CFD Expert?

• In the ME 566 course title, CFD for Engineering Design, what does the acronym CFD stand for?A. Car Free Day

B. Cash Flow Diagram

C. Computational Fluid Dynamics

• Lifelines• Phone a Friend

• Ask the Audience

ME 566 Project

• Mixing in a Model Combustor• You are to determine the effect that the angle of the side inlets has

on mixing in the combustor.

T.-M. Liou and Y.-Y. Wu, Experimental Thermal and Fluid Science 1992, 5:401-409.

• Tasks• You can choose a single angle of 5, 10, 15, or 20 away

from the perpendicular side inlets.

• 3 cases to study

+

1 2

3

• Physical dimensions of the combustor• The length unit is in mm

X

Y

1.58 30

15

15

15

2000

120

Z

Y

• Experimental setup• Hydrocarbon gas mixture is supplied through the axial inlet

• Air is supplied through the two side inlets

• The combustor bulk mean velocity is 23.9 m/s

• The combustor Reynolds number is 4.56104

Air

Air

Gas mixture

• Comments• The experimental results can be used as a guideline.

• To augment the experimental findings on mixing, you can set the temperatures of the side inlet and axial jets to different values and use temperature as a passive fluid marker (i.e. solve the thermal energy equation with no buoyancy force).

Tside

Taxial

Assume adiabatic at walls

CFX-Pre:- Buoyancy Option: Non Buoyant- Heat Transfer Option: Thermal Energy

Project Report

• You report should include• a comment on the validity of the CFD simulation for the

perpendicular angle based on comparison to experimental data

• a clear statement of your findings on the effect of the side inlet angle on mixing within the combustor

• a clear presentation of the computational model’s geometry, boundary conditions and properties. Wherever possible, quantify the influence that the two most significant model parameters have on your solution

• You report should include• a description of the basis of your geometry and mesh designs

• a comment of the applicability of the k model for this flow

• a statement on the degree of convergence obtained by the solver

X

Y

1.58 30

15

15

15

2000

120

Z

Y

Frequently Asked Questions (FAQs)

• How to create a side inlet with an angle :1. Draw a line with dimension L (where L = 15 mm)

2. Draw a line with dimension L/cos (where = 5 ~ 20)3. Join two lines together (Constraints Coincident)

4. Specify the angle between two lines (Dimensions Angle)

1

2

4

L

L/cos

3

Y* = 2

Y* = 1

Y* = 0

X* = 0

L

• What fluid properties should be used for hydrocarbon gas mixture?• You can assume the gas mixture has the same properties as air

• What entrance velocity should be used?• One way to find out entrance velocity is to read U/Uref and V/Uref

from Tables 1A and 1B, where Uref = 23.9 m/s

• What turbulence intensity and length scale values should be used?• One way to find out turbulence intensity is to read u’/Uref and

v’/Uref from Tables 1A and 1B

• For length scale, select the turbulence option: Intensity and Auto Compute Length

• Inlet velocity and turbulence intensity for the side inlet can be found from Table 1A at Y* = 2

• For example, at Y* = 2:• V/Uref = 8.26E-1 at X* = 0.25

• v’/Uref = 1.03E-2 at X* = 0.25

• (V/Uref)avg = 8.27E-1

• (v’/Uref)avg = 1.09E-2

Y* = 2

Y* = 1

Y* = 0

X* = 0

Y* = 2

-8.34E-01-8.32E-01-8.30E-01-8.28E-01-8.26E-01-8.24E-01-8.22E-01-8.20E-01-8.18E-01-8.16E-01

0 0.1 0.2 0.3 0.4 0.5

X*

V/Uref

X* = 0.5

Y* = 2

0.00E+00

5.00E-03

1.00E-02

1.50E-02

2.00E-02

0 0.1 0.2 0.3 0.4 0.5

X*

v'/Uref

X*

Y*

• How to define velocity at the inlet with side angle?• Mass and Momentum Option Cart. Vel. Components

u = -Vsin (m/s), v = -Vcos (m/s), w = 0 (m/s)

V

V Vcos

Vsin

Questions?

Order of Accuracy

• A certain discretisation scheme is used to estimate the temperature in a rectangular fin. The computations are done with a uniform mesh having a spacing of x. Table 1 shows the variation of the predicted heat flux at the base of the fin, , with the mesh spacing.

• Q1: Estimate the order of accuracy of the numerical method. The exact heat flux is 214.3 [watts].

• Q2: The order appears to decrease for the finer meshes. What numerical errors are affecting the solutions obtained with fine meshes?

x [m] [watts]0.05 110.1

0.025 162.80.01 193.8

0.005 204.10.0025 209.2

0.00125 211.90.000625 212.9

bqbq

Table 1

• : error, a: constant, x: mesh spacing, n: order of accuracy

• The order of accuracy is first order

x (m) (watts) 1/2 x1/x2 Order (n)0.05 110.1 104.2

0.025 162.8 51.5 2.02 2 1.020.010 193.8 20.5 2.51 2.5 1.010.005 204.1 10.2 2.01 2 1.01

0.0025 209.2 5.1 2.00 2 1.000.00125 211.9 2.4 2.13 2 1.090.000625 212.9 1.4 1.71 2 0.78

exact bq q bq

na x

11 1

2 22

nn

n

a x x

xa x

1 2

1 2

log

logn

x x

214.3exactq

Who Wants to Be a CFD Expert?

• The order of accuracy appears to decrease for the finer meshes. What numerical errors are affecting the solutions obtained with fine meshes?A. Discretisation error

B. Round-off error

C. Truncation error

• Lifelines• Phone a Friend

• Ask the Audience

x (m) Order (n)0.05 104.2

0.025 51.5 1.020.010 20.5 1.010.005 10.2 1.010.0025 5.1 1.00

0.00125 2.4 1.090.000625 1.4 0.78

Numerical Errors (Sec. 10.2)

• Round-off error• Round-off errors are the result of the computational representation

of real numbers by means of a finite number of significant digits, which is termed the machine accuracy.

• Discretisation error / Truncation error• The discretisation error is associated with the neglected

contributions due to the truncation of high-order terms.

2

2

truncation error

2E P E P

P P

xO x

x x x x

2 2

2 2E PP P

xx

x x

Taylor series expansion