THE BEHAVIOUR OF THE EXHAUST GASES EVICTED FROM THE …
Transcript of THE BEHAVIOUR OF THE EXHAUST GASES EVICTED FROM THE …
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THE BEHAVIOUR OF THE EXHAUST
GASES EVICTED FROM THE SHIP
FUNNEL
PREPARED BY:
Yaşar GUL
M.Sc. Naval Architect
Delta Marine Engineering Co.
Ergin ESIRGEMEZ
B.Sc. Aeronautical Eng.
Delta Marine Engineering Co.
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Problem Description
• The gases evicted from the ship funnel is moving inverse and through the
engine room, so that the people in the engine room are complaining about the
gases.
• We investigate the movement of the gases evicted from the exhaust of the ship
funnel by using commercial CFD Software FLUENT 6.0.
• We tried to design the funnel to avoid the inverse movement of the gases
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Computational Aspects
• FLUENT CFD Software, based on finite volume
method, is used for all analyses.
• Species transport model is used to investigate the
movement of the gases.
• For viscous model, standart k-e model is chosen.
• Analyses are run in the PC which has dual
proccessor and 2 GB RAM.
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• Fluent can model the species transport with or without
chemical reactions.
• In this work since the gases evicted from the funnel are
analyzed, specieaes transport model without chemical
reactions is used.
• For this model FLUENT predicts the local mass fraction of
each species, through the solution of a convection-
diffusion equation for the ith species.
• This conservation equation takes the folloing general form:
Theoretical Aspects
iY
( ) ( )iiiii
SRJYYt
++⋅−∇=⋅∇+∂
∂ rrυρρ
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Theoretical Aspects
• Ri is the net rate of production by chemical reaction, Si is the rate of
creation by addition from the dispersed phase plus any user defined
sources, Ji is the diffusion flux of species i, which arises due to
concentration gradients.
ii,miYρDJ ∇−=
r
i
t
t
miiY
ScDJ ∇
+−=
µρ ,
r
An equation of this form will be solved for N-1 species, where N is the
total number of fluid phase chemical species present in the system, and the
Nth mass fraction is determined as one minus the sum of the N-1 solved
mass fractions.
for laminar flow
for turbulent flow
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Solution Process
We have tree different cases for the funnel design
First Case Second Case Third Case
Find efficient model for
the same condition
Investigate the efficient
model for the different
condition
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Model For The First Case
Figure 1. Grid for the superstructure (Initial Design)
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Model For The Second Case
Figure 2. Grid for the superstructure (Second Design)
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Model For The Third Case
Figure 3. Grid for the superstructure (Final Design)
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Mesh and Analyze Summary
Table 1. Mesh summary for the models
Model Cells Faces Nodes
Initial Model 2257444 6763999 2255751
Second Model 2257444 6763063 2254884
Final Model 2257444 6763483 2255229
Table 2. Analyze Summary
Analyse Method Finite Volume Method
Analyze Type Species Transport
Turbulence Method Standart k-e
PC CPU*2, 1024 MB Ram
Computational Time 25 Hours
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Boundary Condition
InletOutlet
Wall
Figure 4. Boundary Condition Type
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Boundary Condition
Table 3. The ship velocities for each model
Model Ship Velocity
Initial Model 14 knots
Second Model 14 knots
Final Model 14 knots
Efficient Model (Final Model) 14, 12, 8, 0 knots
Table 4. Gases’ Velocities and Temperatrures
The Gases Evicted From Velocity Temperature
Machine Room 41 m/sn 277 C
Boiler room 6.4 m/sn 340 C
Table 5. Gas contents for air and exhaust gas
Air Exhaust Gas
O2 % 21 % 13
N2 % 79 % 75.8
CO2 % 5.45
H2O % 5.75
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Initial Design Results
Figure 5. The gases’ behaviour for the initial design
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Figures 6. Velocity Vectors at the different part of the funnel
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Ship Velocity = 14 m/sn
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Second Design Results
Figure 7. The gases’ behaviour for the second design
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Figure 8. Velocity vectors in front of the funnel
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Ship Velocity = 14 m/sn
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Final Design Results
Figure 9. The gases’ behaviour for final design
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Figure 10. Velocity vectors in front of the funnel
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Ship Velocity = 14 m/sn
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Ship Velocity = 12 m/sn
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Ship Velocity = 8 m/sn