Week 4 - CHT Analysis on Exhaust port
AIM:
To simulate the Conjugate Heat Transfer Analysis on exhaust port using ansys fluent.
OBJECTIVES:
- Give a brief description of why and where a CHT analysis is used.
- Maintain the y+ value according to the turbulence model and justify the results.
- Calculate the wall/surface heat transfer coefficient on the internal solid surface & show the velocity & temperature contours in appropriate areas.
- How would you verify if the HTC predictions from the simulations are right? On what factors does the accuracy of the prediction depend on.
CONJUGATE HEAT TRANSFER(CHT):
The Conjugate Heat Transfer (CHT) analysis type allows heat transfer simulation between solid and fluid domains by exchanging thermal energy at the interference between them.
Conjugate Heat Transfer analysis allows for the simulation of heat transfer between solid and fluid domains by exchanging thermal energy at the interfaces between them and transporting via conduction within solids and additionally via convection within fluid domains. Conjugate heat transfer analysis can accurately predict heat transfer by solving all the relevant solid and flow field heat transfer processes simultaneously.
How is Heat Transferred:
Heat can travel from one place to another in several ways. The different modes of heat transfer include:
- Conduction
- Convection
- Radiation
Meanwhile, if the temperature difference exists between the two systems, heat will find a way to transfer from the higher to the lower system.

Conduction:
Conduction is defined as
The process of transmission of energy from one particle of the medium to another with the particles being in direct contact with each other.
An area of higher kinetic energy transfers thermal energy toward the lower kinetic energy area. High-speed particles clash with particles moving at a slow speed, as a result, slow-speed particles increase their kinetic energy. This is a typical form of heat transfer and takes place through physical contact. Conduction is also known as thermal conduction or heat conduction.
Conduction Equation
The rate of conduction can be calculated by the following equation,
`Q=(K.A.(T_(hot)-T_(cold)))/d`
Where,
- Q is the transfer of heat per unit of time
- K is the thermal conductivity of the body
- A is the area of heat transfer
- Thot is the temperature of the hot region
- Tcold is the temperature of the cold region
- d is the thickness of the body
The coefficient of thermal conductivity shows that a metal body conducts heat better when it comes to conduction.
Conduction Examples
Following are the examples of conduction:
- Ironing of clothes is an example of conduction where the heat is conducted from the iron to the clothes.
- Heat is transferred from hands to ice cube resulting in the melting of an ice cube when held in hands.
- Heat conduction through the sand at the beaches. This can be experienced during summers. Sand is a good conductor of heat.
Convection:
Convection is defined as
The movement of fluid molecules from higher temperature regions to lower temperature regions.
Convection Equation
As the temperature of the liquid increases, the liquid’s volume also has to increase by the same factor and this effect is known as displacement. The equation to calculate the rate of convection is as follows,
`Q = h_c *A*(T_s -T_f)`
Where,
- Q is the heat transferred per unit of time
- hc is the coefficient of convective heat transfer
- A is the area of heat transfer
- Ts is the surface temperature
- Tf is the fluid temperature
Convection Examples
Examples of convection include:
- Boiling of water, that is molecules that are denser move at the bottom while the molecules which are less dense move upwards resulting in the circular motion of the molecules so that water gets heated.
- Warm water around the equator moves towards the poles while cooler water at the poles moves towards the equator.
- Blood circulation in warm-blooded animals takes place with the help of convection, thereby regulating the body temperature.
Radiation:
Radiant heat is present in some other form in our daily lives. Thermal radiation are referred to as radiant heat. Thermal radiation is generated by the emission of electromagnetic waves. These waves carry away the energy from the emitting body. Radiation takes place through a vacuum or transparent medium which can be either solid or liquid. Thermal radiation is the result of the random motion of molecules in matter. The movement of charged electrons and protons is responsible for the emission of electromagnetic radiation. Let us know more about radiation heat transfer.
Radiation heat transfer is measured by a device known as a thermocouple. A thermocouple is used for measuring the temperature. In this device sometimes, error takes place while measuring the temperature through radiation heat transfer.
Radiation Equation
As temperature rises, the wavelength in the spectra of the radiation emitted decreases and shorter wavelengths of radiations are emitted. Thermal radiation can be calculated by Stefan-Boltzmann law,
`P = e ∙ σ ∙ A· (Tr – Tc)4`
Where,
- P is the net power of radiation
- A is the area of radiation
- Tr is the radiator temperature
- Tc is the surrounding temperature
- e is emissivity and σ is Stefan’s constant (σ = 5.67 × 10-8Wm-2K-4
Radiation Example
Following are the examples of radiation:
- Microwave radiation emitted in the oven is an example of radiation.
- UV rays coming from the sun is an example of radiation.
- The release of alpha particles during the decaying of Uranium-238 into Thorium-234 is an example of radiation.
SPACECLAIM SETUP:
- load the model into the space claim and change the unit meter.
- if you see extra edges remove them first.
- using extract volume select input and output edges, then execute comments.
- assign names solid volume and fluid volume as two areas.
- assign the final geometry name to move it inside the folder and delete the empty folder.
- enable the share function in the main folder and use the shared topology to share all faces.

MESHING SETUP:
- using the name selection tool assigns the name input, output, outer wall convection, and inflation.
- using the mesh tool below-mentioned value fill it and get the value of the node and elements.
- then close the meshing.


SOLUTION SETUP:
luent setup:
- After updating the mesh open fluent setup, select a pressure-based solver using the steady-state time simulation and absolute velocity formulation under the general settings.
- Under physics choose the energy option since we are dealing with temperature properties.
- Input the Boundary values at the inlet, 5 m/s as inlet velocity at 700k temperature. Set the outer wall convection boundary to convection type and input a constant value for heat transfer coefficient as 20
- Under materials, properties choose air as the fluid material and aluminum as the solid material
- Enter the reference values as per the geometry and inlet boundary conditions accordingly.
- Initialize by using the hybrid initialization, and the simulations for 400 iterations as it is optimum to achieve a converged solution.
Case 1: Baseline simulation
element size =150mm
sizing element size=50mm
no. of elements=240832
viscous model=k-epsilon
inlet velocity =5m/s
inlet temperature=700k
HT co-efficient=20W/m^2-k






surface heat transfer coefficient :

residuals:

Temperature contour:

VELOCITY PLOT:

TEMPERATURE PLOT:

VELOCITY STREAMLINE PLOT:

WALL HEAT TRANSFER CO-EFFI:

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Case 2 :
element size =100mm
sizing element size=20mm
no. of elements=338717
viscous model=k-epsilon
inlet velocity =5m/s
inlet temperature=700k
HT co-efficient=20W/m^2-k
MESHING CONDITION:

INFLATION :

RESIDUALS:

SURFACE HEAT TRANSFER CO EFFICIENT:

TEMPERATURE CONTOUR:

VELOCITY PLOT:

TEMPERATURE PLOT:

VELOCITY STREAMLINE PLOT:

WALL HEAT TRANSFER CO EFFICIENT:

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Case 3:
element size =100mm
sizing element size=20mm
no. of elements=366372
viscous model=k-omega
inlet velocity =5m/s
inlet temperature=700k
HT co-efficient=20W/m^2-k
MESHING CONDITION:

INFLATION:

RESIDUALS:

SURFACE HEAT TRANSFER CO-EFFI:

TEMPERATURE CONTOUR:

VELOCITY PLOT:

VELOCITY STREAMLINE PLOT:

TEMPERATURE PLOT:

WALL HEAT TRANSFER CO EFFICIENT:

conclusion:
| cases | viscous model | no. of elements |
surface HT coefficient in(W/m^2-K) |
wall HT coefficient in(W/m^2-K) |
| 1 | k-epsilon | 240832 | 21.511 | 214.3 |
| 2 | k-epsilon(refined) | 338717 | 19.68 | 183.6 |
| 3 | k-omega | 366372 | 19.63 | 244.3 |
By comparing 3 cases using the k omega model we can get more accurate because we are dealing with temperature
Wall heat co-efficient is more in the k-omega model as compared to k epsilon
There is no change in the temperature for all cases.
Y plus should be calculated depending upon the solvers.
How would you verify if the HTC predictions from the simulations are right? On what factors does the accuracy of the prediction depend on
According to Bernoulli's mass conservation principle mass is conserved in our model which is clearly explained below.
Let us assume the flow rate from each inlet as Q1, Q2, Q3, Q4 respectively, and Q5 be the flow rate(outflow) from the exhaust manifold.
As mass is neither created nor destroyed, mass flow rates are also balanced as below
Q1+Q2+Q3+Q4=Q5Q1+Q2+Q3+Q4=Q5 -------(1)
we have Q=ρ.A.VQ=ρ.A.V -------(2)
now the equation 1 becomes
A1.V1+A2.V2+A3.V3+A4.V4==A5.V5
as it is an incompressible flow to compensate for the mass flow, velocity is increased, and the overall mass flow rate is conserved.
As velocities are high, the Reynolds number at the outlet manifold will be high.
Nu=f(Re, pr) for forced convection applications,
Nu=hD/k
from the above equations
Nu∝Re,
Nu∝h,
hence, Re∝h
From our simulations, we have observed velocities are high at bend section of outlet manifold hence higher Reynolds number which has high Heat transfer coefficients.
Therefore predictions from our simulations can be considered correct.
Factors influence accuracy of prediction:
- Mesh quality greatly impacts the accuracy of predicted value from our simulations which can be observed from the above contours and maximum values of related parameters like velocity and heat transfer coefficient.
- Appropriate y+ value helps in calculating total layer thickness from the wall for the better capturing of effects near walls, which is HTC in our case.
- An appropriate turbulence model has to be used in accordance with the y+ value which is very important
- Appropriate solvers are one of the most important factors which lead all the calculations in solving the equations
- Inflation layers and boundary conditions