Well Log Interpretation and Petrophysical Analisis in [Autosaved]
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
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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)
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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
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.
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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)
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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 %.
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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
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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
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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.
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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