1 / 20

Project #4: Simulation of Fluid Flow in the Screen-Bounded Channel in a Fiber Separator

Project #4: Simulation of Fluid Flow in the Screen-Bounded Channel in a Fiber Separator. Lana Sneath and Sandra Hernandez 4 th year - Biomedical Engineering Faculty Mentor: Dr. Urmila Ghia Department of Mechanical and Materials Engineering. NSF Type 1 STEP Grant, Grant ID No.: DUE-0756921.

idola-yang
Download Presentation

Project #4: Simulation of Fluid Flow in the Screen-Bounded Channel in a Fiber Separator

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript


  1. Project #4: Simulation of Fluid Flow in the Screen-Bounded Channel in a Fiber Separator Lana Sneath and Sandra Hernandez 4th year - Biomedical Engineering Faculty Mentor: Dr. Urmila Ghia Department of Mechanical and Materials Engineering • NSF Type 1 STEP Grant, Grant ID No.: DUE-0756921

  2. Outline • Motivation • Introduction to Bauer McNett Classifier (separator) • Problem Description • Goals & Objectives • Methodology • Verification Case • Porous Boundary Model • Future Work 1

  3. Problem Background • Toxicity of asbestos exposure varies with length of asbestos fibers inhaled • Further study of this effect requires large batches of fibers classified by length • The Bauer McNett Classifier (BMC) provides a technology to length-separate fibers in large batches Figure 1: Bauer McNett Classifier (BMC) Figure 2:Schematic of BMC 2

  4. = deep open channel Background – Bauer McNett Classifier (BMC) Open to atmosphere • Fiber separation occurs in the deep narrow channel with a wire screen on one side wall • Fibers align with local shear stress vectors [1] • For successful length-based separation, the fibers must be parallel to the screen Wire Screen B A C AL 1. Civelekogle-Scholey, G., Wayne Orr, A., Novak, I., Meister, J.-J., Schwartz, M. A., Mogilner, A. (2005), “Model of coupled transient changes of Rac, Rho, adhesions and stress fibers alignment in endothelial cells responding to shear stress”, Journal of Theoretical Biology, vol 232, p569-585 Figure 3: Top View of One BMC Tank 3

  5. Background – Bauer McNett Classifier (BMC) Figure 4:Fibers parallel to screen Figure 5:Fibers perpendicular to screen Off-plane angle 0° Off-plane angle 90° 4 Fibers length larger than mesh opening Fibers length smaller than mesh opening

  6. Deep Open Channel Dimensions • General Dimensions: • Length (x) = 0.217 m • Height (y) = 0.2 m • Width (z) = 0.02 m • Aspect ratio = 10; Deep open channel • Screen dimensions: • Length (x) = 0.1662 m • Height (y) = 0.1746 m • Thickness (z) = 0.0009144 m Figure 6: General Dimensions screen Figure 7: Porous Model Dimensions

  7. Goals and Objectives Goal: Numerically study the fluid flow in a deep open channel Objectives: a) Verify boundary conditions and variables of the porous model • Simplified porous plate problemasverification case b) Simulate and study the flow in the open channel of the BMC apparatus, modeling the screen as a porous boundary c) Determine the orientation of shear stress vector on the porous boundary

  8. Methodology Computational Grid • Create channel geometry in CFD software • Generate grid of discrete points • Determine the proper boundary conditions to model the porous boundary • Verification case: Laminar flow over a porous plate • Enter boundary conditions into the CFD software • Run simulation • Determine shear stress from flow solutions • Interpret results Figure 8: Porous Model Channel Geometry in FLUENT Table 1: Distribution of grid points and smallest spacing near boundaries

  9. Boundary Conditions • u, v, w are the x, y, and z components of velocity, respectively • Average Inlet Velocity= 0.25m/s • Turbulent Flow (Reynolds Number >5000) • Reynolds Stress Model • Transient Simulation Solid Wall Model Porous Boundary Model Figure 9: Boundary Conditions 8 Free-Slip Wall, v=0, du/dy=0, dw/dy=0 No-Slip Wall, u = v = w = 0 Inlet, u = u(y,z), v = w =0 Porous-Jump, Permeability(K) = 9.6e-10, Pressure-Jump Coefficient(C2)=7610.7 1/m, screen thickness = 9e-4 m; Values correspond to a 16 mesh [5] Outlet, pstat = 0

  10. Verification Case - Porous Plate Objective • Determine proper boundary conditions to • use in the Porous Boundary Model case • Verify fluid flow behavior • Observe how axial flow is inhibited by • the plate Methodology: • Create 2D geometry in Gambit • Calculate Reynolds number for Laminar flow • Generate grid points • Run simulations in FLUENT • Run 4 different cases: changing the mesh boundary condition to determine it’s effect • Interpret results Figure 10: Laminar Flow Across Porous Flat Plate 9

  11. Verification Case - Boundary Conditions (1 of 2) Case #1: All Solid Walls Case #2: Two Walls, One Pressure Outlet 10

  12. Verification Case - Boundary Conditions (2of 2) Case #3: One Wall and Two Pressure Outlets Case #4: All Pressure Outlets 11

  13. Verification Case - Velocity Magnitude Contours Case #1: Velocity Magnitude Contours for All Walls Case #2: Velocity Magnitude Contours for Two Walls and One Pressure Outlet Case #3: Velocity Magnitude Contours for One Wall and Two Pressure Outlets Case #4: Velocity Magnitude Contours for All Pressure Outlets • Conclusion: • All cases show a boundary layer and flow crossing the porous plate 12

  14. Verification Case - Streamlines for Case #1: All Walls

  15. VerificationCase – Darcy’s Law Table 2: Pressure Drop Verification via Darcy’s Law • Conclusion: • Hand calculations were equivalent to FLUENT’s values. • Better understanding how FLUENT uses the porous-jump condition. 13

  16. Porous Boundary Open Channel - Velocity Magnitude Contours Figure 11: Isometric View of Axial Variation of Velocity on Central Plane Figure 12: Front View of Axial Variation of Velocity on Central Plane 14

  17. Porous Boundary Open Channel - Shear Stress Figure 13: Axial Variation of Shear Stress on the Back Wall at y=0.1 z= 0 Figure 14: Axial Variation of Shear Stress on Screen at y=0.1 z= 0.02 Figure 15: Axial Variation of Velocity at Line y=0.1, z=0.01 15

  18. Future Work • Continue running the porous boundary open channel model until the fluid flow solution has been calculated for at least 3 minutes to achieve a steady state solution • Investigate reasoning behind the zero shear stress at the porous boundary • Compare verification case results for pressure drop calculations to literature • Interpret results further 16

  19. Acknowledgements • Dr. Ghia for being an excellent faculty mentor and taking the time to make sure we fully understood the concepts behind our research. • Graduate Students Prahit, Chandrima, Deepak, Nikhil, and Santosh for taking time out of their schedule to teach us the software and help us with any problems we encountered. • Funding for this research was provided by the NSF CEAS AY REU Program, Part of NSF Type 1 STEP Grant, Grant ID No.: DUE-0756921 17

  20. Appendix: Porous Plate Calculation • Darcy’s Law pressure drop calculations: 18

More Related