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1 Oscillatory Flow Mixing; a review Malcolm Mackley Department of Chemical Engineering and Biotechnology University of Cambridge June 2010

OFM Chem Eng Cambridge 2010

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This presentation reviews the way in which Oscillatory Flow Mixing (OFM) was developed from work at Sussex University and then Cambridge University

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Page 1: OFM Chem Eng Cambridge 2010

1

Oscillatory Flow Mixing; a review

Malcolm Mackley

Department of Chemical Engineering and Biotechnology

University of Cambridge

June 2010

Page 2: OFM Chem Eng Cambridge 2010

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Flow Visualisation

Lightsource

1970s

Page 3: OFM Chem Eng Cambridge 2010

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Bristol, 1970 PhD, The Impinging Jet Apparatus

The late Sir Charles Frank and Andrew Keller

Page 4: OFM Chem Eng Cambridge 2010

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Bristol, 1976 Post Doc, The Six Roll Mill

Prof Sir Michael Berry

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Oscillatory Flow Mixing (OFM). Wave Energy devices

Dr Graham Knott

Air turbine generates power

1976-79 Sussex University; Applied Sciences; Material Science Division.

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Go to wave movie Sussex 1978

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Phil Trans Roy Soc

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Chem Eng SciPart 2b project

1980s

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Oscillation and sharp edges

Go to OFM movie

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Oscillatory Flow Mixing, (OFM).

Paul Stonestreet 1990

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Chem Eng SciPart 2b project

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Chem Eng Sci

Tony Howes

Go to OFM Simulation movie

Page 13: OFM Chem Eng Cambridge 2010

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OFM Movie; poetry in motion

Adam Harvey

Go to OFM Harvey movie

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Heat transfer Chen Eng SciPart 2b project

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Mass transfer Cheng Eng SciPart 2b project

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1990s; “Industry will commercialise OFM technology”

1. ICI Wilton, Nylon Monomer. Pilot plant kg /hr for 2 years

2. BP Sunbury Pilot OFM Plant

1990s

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- Oscillator Base Unit

- Feed inlet section

- Shell and baffled tube vessels

- Product outlet section

Chem Eng Oscillatory Flow Reactor (OFR)

Dr Paul Stonestreet

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Chem Eng Lab Scale OFR

Paul Stonestreet, Adam Harvey 1999

Page 19: OFM Chem Eng Cambridge 2010

19Net Flow In

Net FlowOut

Biodiesel Reaction Progressalong Reactor

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• 0.55 m3 total volume

• Ren=500, Reo=2000

• f= 4 Hz, xo=2.4 cm

• 4 X 150mm tubes @ 3.5m

2 units @ 1.1 m3/hr

Approx 50 tonnes/day

Full-scale OFR reactor

Paul Stonestreet

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Prof Xiongwei Ni

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The OFM Meso Reactor

Nuno Reis, Minghzi Zheng

System configuration

Meso tube,diameter d

Smooth constrictions: spacing 3dMinimum constriction diameter 0.4d

Scale- down

2000s

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45º

35 mm, V 4.5 mL

45º

35 mm, V 4.5 mL

a)

b)

L

d d0

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The meso-tube and dimensionless groups

• Geometry

d=5.0 mm, λ=15.2 mm, h=1.6 mm, δ=6.4 mm, β≈45o

• Governing dimensionless groups

dfxo

o2

Re Oscillatory Reynolds number

Strouhal numberox

dSt

4

Net flow Reynolds numberdU

n Re

Smooth Periodic Constrictions Oscillatory flow Meso-Reactor

Fluid oscillation Reynolds number

The ratio of tube diameter to amplitude

Fluid net flow Reynolds number

h

d

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Experimental and ModellingExperiment setup Numerical Modelling

Particle Imaging velocimetry (PIV) system

Phase position for an oscillation cycle

Phase position

0 1

2

3 4 5

6

7 8

X0

The 3-D hexahedral mesh for simulation (Fluent®)

4)()(

2Dtutm

•Periodic boundary condition

u( t) 2fx0 cos(2ft)

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Meso Fluid Mechanics

Minghzi Zheng

Go to OFM PIV movie

Go to OFM LES movie

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Chem EngLab Meso Reactor

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RTD experiment set-up

Probe3

Probe1

Dye Injection

Probe2

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Dispersion model

Z

C

Z

C

uL

DC

2

2

Governing equation Imperfect injection method; numerical fitting

0)(

)()(

dttc

tctC

2

31

/4exp

4 t

t

Pe

t

PetTR

t

dppCptTRtC0 12 )('

2

122 '

N

iiiC tCtC

uL

D

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Model fitting • Net flow with oscillation

• Ren=58, Reo=312, St=0.4

Net flow without oscillation

Ren=58,Reo=0

0 200 400 600 800 1000 12000

0.002

0.004

0.006

0.008

0.01

0.012

0.014

0.016

Time (s)

C(t

) (-

)

(a)

Probe 1

Probe 2

Probe 3

Exp-C(t)1

Exp-C(t)2

Exp-C(t)3

Fit-C(t)3 ' (2->3)

0 100 200 300 400 500 600 700 800 9000

0.002

0.004

0.006

0.008

0.01

0.012

0.014

0.016

0.018

0.02

Time (s)

E(t

) (-

)

b) Exp-E(t)1

Exp-E(t)2

Exp-E(t)3

Fit-E(t)2 (1->2)

Fit-E(t)3 (1->3)

Fit-E(t)3 (2->3)

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Liquid-liquid dispersion

Silicon oil (4.6mPas,2.5%) mixing with water at xo=2 mm

Silicon oil (4.6mPas, 2.5%) mixing with water at f=6Hz

a) f=6Hz

b) f=10Hz

a) xo=3 mm

b) xo=4 mm

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Particles in suspension

Instantaneous velocity vector maps of fluid phase at Reo = 625, x0 = 2 mm, f = 10.0 Hz at vertical position in the presence of 3% (v/v ) amount of ion-exchange particles

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And finally;The BT 1000

Go to BT 1000 movie

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The BT 1000

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What went right with OFM invention.

The science was a lot of fun

What went wrong.

Lack of focus in pushing the technology

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Acknowledgments.A cast of many;

In particular,

Part 2B StudentsPostgraduatesPostdoctorates

Chem Eng support staffBob Skelton

“The Department”“For allowing me the freedom to develop speculative ideas”

Thank you!