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8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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ON-LINE MEASUREMENT OFRHEOLOGICAL PARAMETERS FOR
FEEDBACK CONTROL
Alex van der Spek, Zdoor BV, The Netherlands
Bob Maron, CiDRA Minerals Processing, USA
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Objective• Client motivation: Water and land reclamation from existing tailings
impoundment
• CiDRA motivation: develop on-line rheology “measurement” with existingtechnology
2
Mature Fine Tailings,
non-Newtonian slurry
flocculant
Newtonian slurry, large
solids + water carrier fluid
Recovered
water
solids
Short pipe “reactor”
• Technical Goal:
• Constraints:
• velocity high enough for throughput, adequate mixing of flocculant, and...
• velocity low enough to NOT break down flocks after they form, and...
• Correct flocculant dosage to achieve agglomeration
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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On-line rheology measurement
methods investigated
1. Monitor velocity profile change
2. Measure wall shear rate from velocity profile, assume
rheological model, cross plot vs wall shear stress from
pressure drop
3. Monitor degree of turbulence from energy spectrum of
vorticity
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Key concept
length scales and flow
4
Solid particlesVortical structures
If...
Vortical Structure size>>
solid particle size
...Then
NO INTERACTION
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Key concept
length scales and flow
5
Solid particlesVortical structures
If...
Vortical Structure size ≈ solid particle size
...Then
INTERACTION !!
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Length scales and energy propagationKolmogorov Theory of homogeneous isotropic turbulence
Max vortical
length scale,
pipe diameter
≥ vortical
length scalerange
Min vortical
length scale,
Kolmogorov
length scale,
~200 um
≥ >>
Constant bulk velocity, energy propagation
Turbulent vortices transport energy from larger to shorter length scales (vortices)
heatmechanical
energy
6
1000 100 10 1 0.1 0.01
Length scale (mm)
Particle size,
fines
~ 40 um max
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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7
Amplifiers and
Digitizers
Sensor Array
∆ ∆ ∆ ∆ ∆ ∆ ∆
∆
∆ ∆
∆ ∆
∆
∆
∆
L = Velocity
∆T
Velocity
Measurement via
Tracking of
VorticalStructures
Vortical Structures - use in SONARtrac
Volumetric Flow Measurement
Rev 10
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Slope of RidgeDetermines Flow
Velocity
Size2Velocity/Length2
Size3Velocity/Length3
1/λ1
U/λ1
U/λ3
1/λ3/λ2
U/λ2
Wave Number
F r e q u e n c y
Temporal / Spatial Decomposition
Wavenumber-frequency (K-ω
plot
Each spatial wavelength has a discrete
temporal frequency ( Frequency= Velocity/ Length -> f=U/λ
Size1Velocity/Length1
Frequency
Sonar Array Processing for Volumetric Flow
8
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Kolmogorov Theory predicts Vortical power spectra...
is measured by Sonar array
9
=
⁄ *
⁄
=1
∗ ∗ ( )
Where,
Sonar array infers (by direct measurement) Power Spectra vs wavenumber, therefore...
Can evaluate energy dissipation (i.e. rheology information) rate without differential pressure
Wavenumber k (1/ft)
F r e q u e n c y ( H z )
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Kolmogorov Theory
Vortical power spectra
10
= 2
3� −5
3� Wavenumber k (rad/ft)
P o w e r ( d B )
r e 2 0 u P a
Wavenumber k (rad/ft)
Power vs wavenumber spectra follow Kolmogorov Theory
F r e q u e n c y ( H z )
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Sonar array measures Vortical Power Quality
11
High Vortical
Power Quality =
low loss
propagation of
coherent power
Rev 10
Same velocities, but different Power Quality Spectra vs Wavenumber
Low Vortical
Power Quality =
high loss
propagation of
coherent power
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Sonar flow profile meter
Vortical Power Quality (and flow) at 5 heights
Coherent StCoherent StV 90°
V 180°
V 0°
V 45°
V 135°
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0.00 0.20 0.40 0.60 0.80 1.00 1.20 1.40 1.60 1.80 2.00 2.20 2.40
CAUDAL (m/seg)
A L T U R A
( N O R M
A L I Z A D A
profile
Reference flow rate
profile side sensor
V 0°
V 45°
V 90°
V 135°
V 180°
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Test setup
Velocity profile,
non-Newtonian
Bingham flow, Velocity profile,
Newtonian
Turbulent flow,
with agglomerated
solids
Mature Fine Tailings
Non-settling fines
agglomerationLarge flocks in water-
based carrier fluid
water
solids
mixer
flowShort pipe “reactor”
13
Sonar
flow
profile
Sonar
flow
profile
Sonar
flow
profile
Flocculant
injection
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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14
NO flocculant, non-Newtonian flow
Non-Newtonian Bingham flow
No velocity profile change
With flocculant, Newtonian flow
NO velocity profile change top-bottom
time
V e l o c i t y P r o f i l e ( m / s )
Pipe bottom
Pipe top
Sonar array & Velocity Profile
Rev 10
Stop
flocculent
Pipe bottom
Pipe top
----- upstream
----- midstream
----- downstream
time
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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15
NO flocculant, non-Newtonian flow
Non-Newtonian Bingham flow
No velocity profile change
With flocculant, Newtonian flow
NO velocity profile change top-bottom
time
V e l o c i t y P r o f i l e ( m / s )
Pipe bottom
Pipe top
Sonar array & Velocity Profile
Rev 10
Stop
flocculent
Pipe bottom
Pipe top
----- upstream
----- midstream
----- downstream
time
Upstream Midstream Downstream
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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16
NO flocculant, non-Newtonian flow
Non-Newtonian Bingham flow
No velocity profile change
With flocculant, Newtonian flow
NO velocity profile change top-bottom
time
V e l o c i t y P r o f i l e ( m / s )
Pipe bottom
Pipe top
Sonar array & Velocity Profile
Rev 10
Stop
flocculent
Pipe bottom
Pipe top
----- upstream
----- midstream
----- downstream
time
Upstream Midstream Downstream
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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17
NO flocculant
Non-Newtonian Bingham flow
Low-loss energy propagation
With flocculant
Newtonian flow
High-loss energy propagation
V o r t i c a l P o w e r Q u a l i t y
Pipe bottom
Pipe top
Sonar array & Vortical Power Quality
Rev 10
Stop
flocculent
----- upstream
----- midstream
----- downstream
time
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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up-stream mid-stream down-stream
Histograms, Vortical Power Quality
c o u n t
18
Vortical Power Quality (VPQ) changes with rheology
V
o r t i c a l P o w e r Q u
a l i t y
agglomerationLarge flocks in water-
based carrier fluid
water
mixer
Sonar
VPQSonar
VPQ
time
solids
MFT flocculantSonar
VPQ
8/9/2019 S1_11_10_Robert_Maron_rev.pdf
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Possible ImplementationMeasuring real-time rheology change with Sonar Array Flow Meter
19
Sonar
flow
meter
Sonar
flow
meter
Sonar
flowmeter
up-stream mid-stream down-stream
Histograms, Vortical Power Quality (VPQ)
c o u n t
VPQ VPQ VPQ
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SummaryMeasuring rheology change with Sonar Array Flow Meter
20
• Agglomeration → Rheology change → Length scale change (particle size change)
• Length scale → Vortical Energy Transport (Kolmogorov Theory)
• Sonar array measures Vortical Energy Transport (power vs. wavenumber)
• Power vs. wavenumber “integrated” into Vortical Power Quality (standard measurement)
• rheology change → Change in Sonar Vortical Power Quality → real-time measurement
• Future work: move from “integrated” Vortical Power Quality figure of merit...to (better?)
spectrum measurement