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Thesis Defence : 02 December 2010
Citation preview
NEED OF STUDYING LUNAR Dust
1. Manned mission
2. Establish permanent base
3. Mine lunar soil
4. Dust removing techniques
5. Control inside a capsule
Source: <www.U-LunaProject.org>
PROBLEMS WITH LUNAR DUST
1. Dangerous to human beings
2. Accumulation on engineering devices
3. Difficult to remove
4. Shape
5. Size
6. Wide existence
Source:<http://cientifica.eu>
Part ITracking of Irregular Shaped Particle
Part IIModeling and Simulation
of Lunar Dust Remover
PART I: TASKS
1. Literature review
2. Effect of shape on force coefficients
3. Tracking algorithm
4. Application of UDF
5. Particle tracking
6. Results
Various Shapes
STUDY OF SHAPE
Source:<www.sandgrains.com>
Moon dust from Apollo 11
ALGORITHM IMPLEMENTATION
In House ProgramConcept demonstration
Algorithm
User Defined Functions(UDF)FeasibleCost effective
MOTION STUDY
Translation(CD & CL)
Rotation(T & θ)
+
(Time Step)
From θ T
α=T/I
ω = ω0 + αt
θp = θ0 + ωt + ½ αt2
θf = tan-1(Vyrel/Vxrel)
θ = θp - θf
θ CD and FD
θ0 = θ and ω0= ω
Stepsor
Domain
TRANSLATION
STOP
STARTI, m, θ, CD, CL & T
CD & CL
Y
N
MODEL TO STUDY TRANSLATION
V
Elliptical barrier tilted at different angle
0.05 X 0.1 m2D flow path
FORCES ACTING ON THE BARRIER
FD = Drag force (N)
FD = CD 1/2 ρ V2 A
FL = Lift force (N)
FL = CL 1/2 ρ V2 A
CD = Drag coefficientCL = Lift coefficientρ = Density of fluidV = Flow velocityA = Characteristic frontal area of the body
Velocity vectors at elliptical barrier
VARIATION WITH ANGLE
Variation of Coefficient of Drag
Variation of Coefficient of Lift
VARIATION OF CD WITH ANGLE
From θ T
α=T/I
ω = ω0 + αt
θp = θ0 + ωt + ½ αt2
θf = tan-1(Vyrel/Vxrel)
θ = θp - θf
θ CD and FD
θ0 = θ and ω0= ω
Stepsor
Domain
ROTATION
STOP
STARTI, m, θ, CD, CL & T
Torque T
Y
N
STUDY OF TORQUE
Torque = Force × Displacement
Pressure Force Shear Force
VARYING TORQUE WITH ANGLE
UDF FOR ELLIPTICAL PARTICLE
Relative Angle
Relative Reynolds Number
Drag
Lift
STRAIGHT CHANNEL
Spherical Particle Track
Comparison of Spherical & Elliptical
Particle Track
ELBOW CHANNEL
Spherical Particle Track
Comparison of Spherical & Elliptical
Particle Track
From the study of forces
CD and CL decreases with Re
T increases with Re
Graph follows similar pattern
SHAPE is important factor
RESULTS AND DISCUSSION
Dust Remover
Air Filter
Enclosed Capsule Wall
Air Circulation Line
Outer Door
Inlet
Outlet
Inner Door
PART II : LUNAR DUST REMOVER
Blower
BOUNDARY CONDITIONS AND PARAMETERS
Boundary Conditions
1.Inlet : Velocity inlet
2.Outlet : Pressure Outlet
3.Sidewall : Wall
4.Object : Wall
Parameters
1.Velocity = 4 m/s
2.Swirl components :Radial = 0.3
Tangential = 0.3Axial = -1
3. Re = 250,000
0 Sec
18
RECTANGULAR MODEL
Pro-E modelVelocity Pathlines
Simple flow Particle Track
Swirl flow
CYLINDRICAL MODEL
Pro-E model
Particle Track
Simple flow
Velocity Pathlines
Swirl flow
0 Sec
11.8 1
0 m/s
MORE DUST REMOVER MODEL
Pear Shaped ModelDome Shaped Model
DOME SHAPED MODEL
Particle track
Swirl flow
Velocity pathlines and vectors
Simple flow
PEAR SHAPED MODEL
Particle track
Swirl flow
Velocity vectors
Swirl flow
Model Flow typeParticle Escaped
out of 100
In 30 Sec. In 60 Sec.
RectangularSimple 28 37
Swirl 30 54
CylindricalSimple 52 75Swirl 32 50
Dome ShapeSimple 85 89
Swirl 57 87
Pear ShapeSimple 47 49
Swirl 100 100
COMPARISON: PARTICLE ESCAPED
COMPARISON OF MODELS
Particles Removed
Out of 100
Models
From the study of Lunar dust remover Pear Shaped Model:
I.Particle Escaped = 100
II.Maximum Time = 21 Sec
III.Mass of Air Needed = 12.6 kg
IV.Better Design
RESULTS AND DISCUSSION
CONCLUSION
1. UDF for lift, drag and torque
2. Tracking of elliptical particle
3. Model: Pear shaped
4. Flow: Swirl
FUTURE WORK
1. UDF for 3D
2. Study for other Re
3. Body force: Electric Charges
THANK YOUTHANK YOU
QUESTIONS?QUESTIONS?