Particle Separation Efficiency in Canonical Vortex Tube Separator Arrays.pptx

jubel6 8 views 15 slides Mar 07, 2025
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About This Presentation

This study focuses on the development of a custom-designed Particle Separation Rig wind tunnel at the Virginia Techโ€™s Advanced Propulsion and Power Lab (๐ด๐‘ƒ๐‘ƒ๐ฟ) to enable a detailed
investigation into the particle separation efficiency of Vortex Tube Separator (๐‘‰๐‘‡ ๐‘†) arrays,
pro...


Slide Content

Jubel Kurian, Pranay V. Patel, K. Todd Lowe, and Wing F. Ng Advanced Propulsion and Power Lab, Virginia Tech AIAA SciTech Forum, 6 th -10 th January 2025 Copyright ยฉ by Virginia Polytechnic Institute and State University Published by the American Institute of Aeronautics and Astronautics, Inc., with permission. Particle Separation Efficiency in Canonical Vortex Tube Separator Arrays

2 Introduction & Motivation CH-47 rotorcraft operating in brown-out conditions in a very dusty environment 1 Sand ingestion in engines up to 2-4 lbs /min 2 Causes significant compressor erosion 3 Leads to engine failure , high maintenance and shortened lifespans 4 Solution : Engine Air Particle Separators (EAPS) Vortex Tube Separators (VTS)

3 Singular Vortex Tube Separator CH-47 rotorcraft operating in brown-out conditions in a very dusty environment 1

4 How Does a VTS Work? Helical Vanes Separation Region FLOW Dirty Air Clean Air VTSs filter particles by employing Centrifugal Forces in a vortical airstream. Inlet Large Particle Small Particle Filtered Unfiltered

5 VTS Test Article and Scaling The test array has 7 VTS tubes and was scaled up by 2.5x (a) (b) (c) Upstream and downstream sections with 7 VTS tubes . Assembled with part 'C' sliding into 'Bโ€™. Fully assembled VTS array in scavenge casing.

ย  ย  6 Background and Theory Particle Separation Efficiency ( ) ย  Non-Dimensional Parameters of Interest = Airflow rate through VTS = Separation region length = Critical radius of separation H = Helical vane pitch length ย  Where, ย  Ratio of inertial to viscous forces within the flow. ย  ย  Ratio of particle inertia to fluid drag, determining particle-following ability in a flow. ย  (1) = 52,000 for the inlet of each separator ย 

7 Experimental Setup โ€“ VTS Particle Separation Rig Scavenge Flow Rate: (7% of Inlet flow rate) 3*9 = 27 SCFM Sand Feed Rate: ~ 0.18 g/s Core Flow : ~ 10.0 m/s inlet flow velocity

8 Particle Feeding System Nozzle exit placement w.r.t VTS inlet.

9 Particle Used for Testing Soda Lime Glass Spheres (SLGS) MIL-E-5007C (CSPEC) Shape: Spherical, Uniform shape Size Range: 3-6 ฮผ m and 63-75 ฮผ m Composition: Silica, Na 2 CO 3 , CaCO 3 Density: 2.50 g/cm 3 Shape: Irregular, Non-uniform shape Size Range: 1-1000 ฮผ m Composition: Silica, Trace Metal Oxides Density: 2.65 g/cm 3

10 Results โ€“ Boundary Condition Validation The PSR's velocity profiles matched HSWT data closely, with minor deviations, confirming reliability for VTS sand ingestion testing.

11 Results โ€“ Particle Separation Efficiency SLGS Particles CSPEC Particles Varying separation efficiencies due to hygroscopic behavior, with smaller particles (3-6 ฮผm ) averaging 41.4ยฑ5.3% efficiency and larger particles (65-75 ฮผm ) ranging from 20% to 91%, with a positive correlation to increasing humidity. Consistent and stable separation efficiencies between 85% and 95% (mean: 88.7ยฑ1.5%), unaffected by humidity variations due to their non-hygroscopic nature.

12 Results โ€“ Stokes Number Analysis Stokes Number Impact: Low St particles showing low separation efficiency while larger particles with higher Stokes numbers achieved higher efficiency. Theoretical vs. Experimental: Experimental results match theoretical predictions for small SLGS particles (could be coincidental!) but diverge for larger SLGS and CSPEC particles. Equation 1 does not take array effects into account.

13 Conclusion Boundary conditions validation demonstrate strong reliability of the experimental methodology. Evident role of Stokesโ€™ number in separation efficiency. SLGS particles are hygroscopic in nature, leading to variable separation efficiency, while CSPEC particles provided consistent results due to their non-hygroscopic nature. VTS arrays validated in separating particles across a range of particle types and sizes and has highlighted the significant influence of particle properties and environmental factors on performance. This lays the foundation for future experimental studies on VTS, along with benchmarking separation efficiency data for particles meeting current military specifications. Future work include: New VTS design configurations, new particle types, r efine theoretical models to better account for irregular particle shapes and array configurations, and perform numerical simulations to validate against the experimental data.

14 References https://australianaviation.com.au/2022/01/in-praise-of-the-chinook/ Pall, D., โ€œVortex Air Cleaner Assembly having Uniform Particle Removal Efficiency throughout the Array of Air Cleanersโ€, US Patent 3520114, 1968 Potts, J., โ€œWhy an Engine Air Particle Separator (EAPS)?โ€, Gas Turbine and Aeroengine Congress and Exposition, 1990, Brussels, Belgium Van der Walt, J. P., Nurick , A., โ€œErosion of Dust-Filtered Helicopter Turbine Engines Part 1โ€, Journal of Aircraft, Vol. 32, 1995, pp. 106-111 Collins, A. S., โ€œDevelopment of a Novel Probe for Engine Ingestion Sampling in Parallel With Initial Developments of a High-speed Particle-laden Jet,โ€ Ph.D. thesis, Virginia Tech, 2021. Acharya, A. S., โ€œAerodynamic Interactions in Vortex Tube Separator Arrays,โ€ Doctoral dissertation, Virginia Tech, 2023.