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NEED OF STUDYING LUNAR Dust ,[object Object],[object Object],[object Object],[object Object],[object Object],Source: <www.U-LunaProject.org>
PROBLEMS WITH LUNAR DUST ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Source:<http://cientifica.eu>
Part I Tracking of Irregular Shaped Particle Part II Modeling and Simulation  of Lunar Dust Remover
PART I: TASKS ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
[object Object],STUDY OF SHAPE ,[object Object],[object Object]
ALGORITHM IMPLEMENTATION  ,[object Object],[object Object],Algorithm ,[object Object],[object Object],[object Object]
MOTION STUDY  (Time Step) Translation (C D  & C L ) Rotation (T &  θ ) +
TRANSLATION  From θ    T α=T/I   ω = ω 0  + αt θ p  = θ 0  + ωt + ½ αt 2 θ f  = tan -1 (Vy rel /Vx rel ) θ = θ p  - θ f   θ    C D  and F D θ 0  = θ and ω 0 = ω Steps or Domain STOP START I, m, θ, C D , C L  & T C D  & C L   Y N
MODEL TO STUDY TRANSLATION V Elliptical barrier tilted at different angle 0.05 X 0.1 m 2D flow path
FORCES ACTING ON THE BARRIER ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Velocity vectors at elliptical barrier
VARIATION WITH ANGLE Variation of Coefficient of Drag Variation of Coefficient of Lift
VARIATION OF C D  WITH ANGLE
ROTATION  From θ    T α=T/I   ω = ω 0  + αt θ p  = θ 0  + ωt + ½ αt 2 θ f  = tan -1 (Vy rel /Vx rel ) θ = θ p  - θ f   θ    C D  and F D θ 0  = θ and ω 0 = ω Steps or Domain STOP START I, m, θ, C D , C L  & 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
[object Object],[object Object],[object Object],[object Object],[object Object],RESULTS AND DISCUSSION
PART II : LUNAR DUST REMOVER Dust Remover Air Filter Enclosed Capsule Wall Air Circulation Line Inlet Outlet Blower Outer Door Inner Door
BOUNDARY CONDITIONS AND PARAMETERS ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
RECTANGULAR MODEL Pro-E model Velocity Pathlines Simple flow  Particle Track Swirl flow  0 Sec 18
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 Model Dome 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
COMPARISON: PARTICLE ESCAPED Model Flow type Particle Escaped out of 100 In 30 Sec. In 60 Sec. Rectangular Simple 28 37 Swirl 30 54 Cylindrical Simple 52 75 Swirl 32 50 Dome Shape Simple 85 89 Swirl 57 87 Pear Shape Simple 47 49 Swirl 100 100
COMPARISON OF MODELS Particles Removed Out of 100 Models
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],RESULTS AND DISCUSSION
CONCLUSION ,[object Object],[object Object],[object Object],[object Object]
FUTURE WORK ,[object Object],[object Object],[object Object]
THANK YOU QUESTIONS?

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Irregular Particle Tracking and Lunar Dust Remo

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  • 4. Part I Tracking of Irregular Shaped Particle Part II Modeling and Simulation of Lunar Dust Remover
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  • 7.
  • 8. MOTION STUDY (Time Step) Translation (C D & C L ) Rotation (T & θ ) +
  • 9. TRANSLATION From θ  T α=T/I ω = ω 0 + αt θ p = θ 0 + ωt + ½ αt 2 θ f = tan -1 (Vy rel /Vx rel ) θ = θ p - θ f θ  C D and F D θ 0 = θ and ω 0 = ω Steps or Domain STOP START I, m, θ, C D , C L & T C D & C L Y N
  • 10. MODEL TO STUDY TRANSLATION V Elliptical barrier tilted at different angle 0.05 X 0.1 m 2D flow path
  • 11.
  • 12. VARIATION WITH ANGLE Variation of Coefficient of Drag Variation of Coefficient of Lift
  • 13. VARIATION OF C D WITH ANGLE
  • 14. ROTATION From θ  T α=T/I ω = ω 0 + αt θ p = θ 0 + ωt + ½ αt 2 θ f = tan -1 (Vy rel /Vx rel ) θ = θ p - θ f θ  C D and F D θ 0 = θ and ω 0 = ω Steps or Domain STOP START I, m, θ, C D , C L & T Torque T Y N
  • 15. STUDY OF TORQUE Torque = Force × Displacement Pressure Force Shear Force
  • 17. UDF FOR ELLIPTICAL PARTICLE Relative Angle Relative Reynolds Number Drag Lift
  • 18. STRAIGHT CHANNEL Spherical Particle Track Comparison of Spherical & Elliptical Particle Track
  • 19. ELBOW CHANNEL Spherical Particle Track Comparison of Spherical & Elliptical Particle Track
  • 20.
  • 21. PART II : LUNAR DUST REMOVER Dust Remover Air Filter Enclosed Capsule Wall Air Circulation Line Inlet Outlet Blower Outer Door Inner Door
  • 22.
  • 23. RECTANGULAR MODEL Pro-E model Velocity Pathlines Simple flow Particle Track Swirl flow 0 Sec 18
  • 24. CYLINDRICAL MODEL Pro-E model Particle Track Simple flow Velocity Pathlines Swirl flow 0 Sec 11.8 1 0 m/s
  • 25. MORE DUST REMOVER MODEL Pear Shaped Model Dome Shaped Model
  • 26. DOME SHAPED MODEL Particle track Swirl flow Velocity pathlines and vectors Simple flow
  • 27. PEAR SHAPED MODEL Particle track Swirl flow Velocity vectors Swirl flow
  • 28. COMPARISON: PARTICLE ESCAPED Model Flow type Particle Escaped out of 100 In 30 Sec. In 60 Sec. Rectangular Simple 28 37 Swirl 30 54 Cylindrical Simple 52 75 Swirl 32 50 Dome Shape Simple 85 89 Swirl 57 87 Pear Shape Simple 47 49 Swirl 100 100
  • 29. COMPARISON OF MODELS Particles Removed Out of 100 Models
  • 30.
  • 31.
  • 32.