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Numerical modelling of non-Newtonian
  fluid in a rotational cross-flow MBR


T. R. Bentzen1, N. Ratkovich1, S. Madsen2, J. C.
    Jensen2, S. N. Bak2 & M.R. Rasmussen1
   1Department   of Civil Engineering, Aalborg University – Denmark
                    2Grundfos BioBooster – Denmark




6th IWA Specialist Conference on Membrane Technology for Water
                     & Wastewater Treatment
               October 5, 2011, Aachen - Germany
                                                                 No. 1 of 17
Outline

Introduction & Objectives
• Fouling
• Rotational Cross-Flow MBR

Background
• Non-Newtonian behavior (viscosity)
• Wall shear stress in rotating systems

Methodology
• Experimental measurements & CFD model

Results & discussion
• Wall shear stress

Conclusions
                                          No. 2 of 17
Introduction

Membrane fouling
• Fouling is the main bottleneck of the widespread of MBR systems.
• Decrease permeate flux
• Increase trans-membrane pressure

Control/reduction of fouling
• Process hydrodynamics can decrease and/or control fouling…
   • by increasing liquid cross-flow velocity.
• Increase permeate flux
• Surface shear stress → scouring effect
• Increase mass transfer (cake layer → bulk region)



                                                                 No. 3 of 17
Rotational cross-flow (RCF) MBR (Grundfos
BioBooster®)
• It operates…
   • between 20 – 40 lmh
   • pressurize system (~5 bar)
   • up to 5 times higher sludge
     concentration       than   in
     conventional MBR systems
     (TSS up to 50 g l-1).
• Rotating impellers between
  filtration  membrane      discs
  prevent fouling.
• Impellers ensures low viscosity
  in the reactor biomass due to
  the non-Newtonian behaviour
  of activated sludge (AS).
•     energy consumption and
  flux.                                     No. 4 of 17
Background (I)




                 No. 5 of 17
Background (II)




                  No. 6 of 17
Methodology (I)
Tangential velocity measurements
•   RCF MBR operates between 50 to 350 rpm
•   Experimental tangential velocity measured at 59, 119 and 177 rpm
    with water
•   Measured with Laser Doppler Anemometry (LDA)
•   LDA is an optical technique to measure velocity field in transparent
    media and cannot be used with activated sludge.




                                                                   No. 7 of 17
Methodology (II)


CFD model

•    Star CCM+ v6.04
•    Single phase
•    Rigid body motion
•    Turbulent model
    • k- SST (water) - validation
    • Laminar (AS)
•    Enhanced wall treatment (y+ < 1)




                                        No. 8 of 17
Results (I)
Reynolds number for water




Reynolds number for AS




                            No. 9 of 17
Results (II)
Tangential velocity measurements for water
•   A good agreement between the experimental measurements and the
    CFD simulation results, with an error up to 8 %.




                                                             No. 10 of 17
Results (III)
Shear stress (for water)




 50 rpm          150 rpm




250 rpm          350 rpm


                           No. 11 of 17
Results (IV)
                                                                          Disk type             k
Shear stress for water                                                 Infinite smooth
                                                                                              0.313
                                                                             disks
•   Shear stress at the membrane
                                                                        Smooth disks          0.450
     • Theoretical solution:
                                                                   Disk with vanes       0.650 – 0.840
     • k: velocity coefficient which depends on disk geometry (vanes)
                                                                    Grundfos (14
                                                                                              0.795
                                                                           vanes)




                                                                                             2000 rpm



                                                                       *Torras et al, 2009




                                                                                         No. 12 of 17
Results (V)
Area-weighted average shear stress at the membrane




                                                     No. 13 of 17
Results (VI)
                               250 rpm
Shear stress for AS




     30 g/l           40 g/l   50 g/l




                                        No. 14 of 17
Results (VII)




                250 rpm



                          No. 15 of 17
Results (VIII)




                         Area-weighted average shear stress
                                        (Pa)
                                    AS           AS             AS
                         Water
                 (rpm)           (30 g l-1)   (40 g l-1)     (50 g l-1)
                  50       1.8     13.5         22.6           34.3
                 150       8.2     19.9         29.0           40.7
                 250      13.8     25.5         34.6           46.3
                 350      19.2     30.9         40.0           51.7




                                                           No. 16 of 17
Conclusions

•   A proper validation of the CFD model was made in terms of
    tangential velocity measurements using a LDA system with water.

•   RCF MBR operates with AS and LDA measurements cannot be
    made.

•   CFD model was modified to account for the viscosity of AS.

•   Local shear stress at any place of the membrane surface and area-
    weighted average shear stress was determined.

•   An empirical relationship was made, to determine the area-
    weighted average shear stress in function of the angular velocity (in
    rpm) and the TSS.

                                                                     No. 17 of 17
Thank you for your attention




                               No. 18 of 17
Consultancy services on CFD for MBR
•   CFD has become a frontline tool for virtual simulations (conceptual design
    & performance prediction)
•   CFD not only gives qualitative data very exact quantitative predictions.
•   CFD tools and techniques are extensively validated with experimental and
    analytical results allowing more robust models for R&D.

•   Software expertise:
    •   CAD:               Rhino
    •   Meshing:           GAMBIT, ICEM, Star CCM+
    •   Solver:            Star CCM+, CFX, Fluent

•   Domain expertise
    •   CAD repair for meshing
    •   Moving mesh
    •   Turbulence modelling
    •   Multiphase modelling

                                                                          No. 19 of 17

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Numerical modelling of non-Newtonian fluid in a rotational cross-flow MBR

  • 1. Numerical modelling of non-Newtonian fluid in a rotational cross-flow MBR T. R. Bentzen1, N. Ratkovich1, S. Madsen2, J. C. Jensen2, S. N. Bak2 & M.R. Rasmussen1 1Department of Civil Engineering, Aalborg University – Denmark 2Grundfos BioBooster – Denmark 6th IWA Specialist Conference on Membrane Technology for Water & Wastewater Treatment October 5, 2011, Aachen - Germany No. 1 of 17
  • 2. Outline Introduction & Objectives • Fouling • Rotational Cross-Flow MBR Background • Non-Newtonian behavior (viscosity) • Wall shear stress in rotating systems Methodology • Experimental measurements & CFD model Results & discussion • Wall shear stress Conclusions No. 2 of 17
  • 3. Introduction Membrane fouling • Fouling is the main bottleneck of the widespread of MBR systems. • Decrease permeate flux • Increase trans-membrane pressure Control/reduction of fouling • Process hydrodynamics can decrease and/or control fouling… • by increasing liquid cross-flow velocity. • Increase permeate flux • Surface shear stress → scouring effect • Increase mass transfer (cake layer → bulk region) No. 3 of 17
  • 4. Rotational cross-flow (RCF) MBR (Grundfos BioBooster®) • It operates… • between 20 – 40 lmh • pressurize system (~5 bar) • up to 5 times higher sludge concentration than in conventional MBR systems (TSS up to 50 g l-1). • Rotating impellers between filtration membrane discs prevent fouling. • Impellers ensures low viscosity in the reactor biomass due to the non-Newtonian behaviour of activated sludge (AS). • energy consumption and flux. No. 4 of 17
  • 5. Background (I) No. 5 of 17
  • 6. Background (II) No. 6 of 17
  • 7. Methodology (I) Tangential velocity measurements • RCF MBR operates between 50 to 350 rpm • Experimental tangential velocity measured at 59, 119 and 177 rpm with water • Measured with Laser Doppler Anemometry (LDA) • LDA is an optical technique to measure velocity field in transparent media and cannot be used with activated sludge. No. 7 of 17
  • 8. Methodology (II) CFD model • Star CCM+ v6.04 • Single phase • Rigid body motion • Turbulent model • k- SST (water) - validation • Laminar (AS) • Enhanced wall treatment (y+ < 1) No. 8 of 17
  • 9. Results (I) Reynolds number for water Reynolds number for AS No. 9 of 17
  • 10. Results (II) Tangential velocity measurements for water • A good agreement between the experimental measurements and the CFD simulation results, with an error up to 8 %. No. 10 of 17
  • 11. Results (III) Shear stress (for water) 50 rpm 150 rpm 250 rpm 350 rpm No. 11 of 17
  • 12. Results (IV) Disk type k Shear stress for water Infinite smooth 0.313 disks • Shear stress at the membrane Smooth disks 0.450 • Theoretical solution: Disk with vanes 0.650 – 0.840 • k: velocity coefficient which depends on disk geometry (vanes) Grundfos (14 0.795 vanes) 2000 rpm *Torras et al, 2009 No. 12 of 17
  • 13. Results (V) Area-weighted average shear stress at the membrane No. 13 of 17
  • 14. Results (VI) 250 rpm Shear stress for AS 30 g/l 40 g/l 50 g/l No. 14 of 17
  • 15. Results (VII) 250 rpm No. 15 of 17
  • 16. Results (VIII) Area-weighted average shear stress (Pa) AS AS AS Water (rpm) (30 g l-1) (40 g l-1) (50 g l-1) 50 1.8 13.5 22.6 34.3 150 8.2 19.9 29.0 40.7 250 13.8 25.5 34.6 46.3 350 19.2 30.9 40.0 51.7 No. 16 of 17
  • 17. Conclusions • A proper validation of the CFD model was made in terms of tangential velocity measurements using a LDA system with water. • RCF MBR operates with AS and LDA measurements cannot be made. • CFD model was modified to account for the viscosity of AS. • Local shear stress at any place of the membrane surface and area- weighted average shear stress was determined. • An empirical relationship was made, to determine the area- weighted average shear stress in function of the angular velocity (in rpm) and the TSS. No. 17 of 17
  • 18. Thank you for your attention No. 18 of 17
  • 19. Consultancy services on CFD for MBR • CFD has become a frontline tool for virtual simulations (conceptual design & performance prediction) • CFD not only gives qualitative data very exact quantitative predictions. • CFD tools and techniques are extensively validated with experimental and analytical results allowing more robust models for R&D. • Software expertise: • CAD: Rhino • Meshing: GAMBIT, ICEM, Star CCM+ • Solver: Star CCM+, CFX, Fluent • Domain expertise • CAD repair for meshing • Moving mesh • Turbulence modelling • Multiphase modelling No. 19 of 17