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1 April 18, 2012 Aerosol Sampling 1 April 18, 2012 Aerosol Sampling

1 April 18, 2012 Aerosol Sampling - PowerPoint Presentation

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1 April 18, 2012 Aerosol Sampling - PPT Presentation

Prepared by Enrico Da Riva Gennaro Bozza 12042012 G Bozza E Da Riva ISOLDE facility aerosol results No Simulation Status 1 Sampling Tube 45 Degrees Cut operation 3ms Done 2 Sampling ID: 802247

bozza 2012 riva sampling 2012 bozza sampling riva efficiency april fluent particles starccm inlet stack degrees results tube transport

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Slide1

1

April 18, 2012

Aerosol Sampling

Prepared by: Enrico Da Riva, Gennaro Bozza12-04-2012

G. Bozza, E. Da Riva

ISOLDE facility aerosol results

Slide2

No.

Simulation

Status

1

Sampling

Tube, 45 Degrees Cut, operation (3m/s)

Done

2Sampling Tube, 45 Degrees Cut, flush (8m/s)Done3Sampling Tube, coaxial, operation (3m/s)Done4Sampling Tube, coaxial, flush (8m/s)Done5Sampling Tube, shrouded, operation (3m/s)Not done6Sampling Tube, shrouded, flush (8m/s)Not done7Bend, 45 degrees and Rb=1Done8Bend, 45 degrees and Rb=3Done9Bend, 90 degrees and Rb=1Done10Bend, 90 degrees and Rb=3Done11Straight pipe, 10m long, D = 1.12m Almost done12Final Enlargement, 7cm longFirst conclusions available13Complete Isolde Ventilation ductDone

Remaining simulations

G. Bozza, E. Da Riva

2

April 18, 2012

Slide3

G. Bozza, E. Da Riva

3

April 18, 2012

Table of ContentsTransport efficiency (90° bend)ISOLDE (stack + sampling pipe)

Slide4

G. Bozza, E. Da Riva

4

April 18, 2012

Transport efficiency (90° bend)

Slide5

Geometry

G. Bozza, E. Da Riva

5April 18, 2012

D = 10 cm, flow rate = 20 m3 h-1Different bending radius (R/D = 1, R

/D = 3)

All possible orientations

Slide6

Settings sensitivity

G. Bozza, E. Da Riva

6April 18, 2012

Modifying Drag law, Saffman’s force, Step Length Factor, Integration schemeDefault settingsAnalytic

All other settings

Slide7

StarCCM+

vs. Fluent results for the 90° bend

G. Bozza, E. Da Riva7April 18, 2012

0.1 μmx

y

R/D=3

R/D=1

Slide8

StarCCM+

vs. Fluent results for the 90° bend

G. Bozza, E. Da Riva8April 18, 2012

1 μmxy

Slide9

StarCCM+

vs. Fluent results for the 90° bend

G. Bozza, E. Da Riva9April 18, 2012

10 μmxy

long stretch

horizontal

No-gravity & long stretch vertical

Slide10

Trapped particle distribution (example)

G. Bozza, E. Da Riva

10April 18, 2012

dp=10 μm,

Slide11

Long stretch horizontal (R

/D=1)

G. Bozza, E. Da Riva11April 18, 2012

Transport Efficiency

Simulation StarCCM

Simulation Fluent

Correlation

Particle 0.1μm95%87%100%Particle 1μm40%86%99%Particle 10μm5%28%33%This table shows that Fluent results are much closer to the correlation than StarCCM+ results.The 15% of efficiency underestimation of Fluent, compared to the correlation, is explainable in the following way: Fluent overestimates the turbulent inertial deposition compared to the correlation.Simulation vs. correlation

Slide12

G. Bozza, E. Da Riva

12

April 18, 2012

Turbophoresis

Fluent

StarCCM+

Unlike STARCCM+, in Fluent the effects of the

turbophoresis are not relevant.InletDownstream of the elbowAlmost the same (very uniform) distribution at every cross section

Slide13

Conclusions 1/2

G. Bozza, E. Da Riva

13April 18, 2012

Turbulent inertial deposition:negligible in StarCCM and CorrelationRelevant in Fluent (15% with L ~ 100D)Gravity:StarCCM:

Fluent:

 

: Gravity deposition is the dominant phenomenon : Relevant influence of the elbow but not of the bending radius of the elbow.Negligible influence of the gravityStarCCM+ vs FluentTransport efficiency

Slide14

G. Bozza, E. Da Riva

14

April 18, 2012

Transport Losses %

Elbow

Straight stretch

L

=10mTOTALTurbulent depositionGravitational deposition0.1 μm~5%~10%~0%~15%1 μm~5%~10%~0%~15%10 μm horizontal~10%~35%~25%~70%10 μm vertical~10%~35%~0%~45%Conclusions 2/2Some rough numbersD = 10 cm, flow rate = 20 m3 h-1

Slide15

G. Bozza, E. Da Riva

15

April 18, 2012

2. ISOLDE (stack + sampling pipe)

Slide16

G. Bozza, E. Da Riva

16

April 18, 2012

ISOLDEMachine Mode: Qmain = 7500

m3/hFlush Mode

: Qmain

= 15000 m3/hStack (main pipe)Sampling pipe

Slide17

G. Bozza, E. Da Riva

17

April 18, 2012

Tables4

3

To instrumentation

After the inlet

1Before the Sampling point2Entering the inletMachine Mode: Qmain = 7500 m3/h0.1μm1μm10μm1- Particles before the sampling point Nst125726212571081255855Particles supposed to enter the sampling inlet: 4191419041862- Particles entering the sampling inlet Ni4758473047663- Particles after the inlet, outside of the stack Nis3419366239714- Particles reaching the instrumentation Nout13361324375Aspiration efficiency: Ni/Ns114%

113%

114%

Transport efficiency:

Nout

/Ni

28%

28%

8%

Sampling

efficiency = Asp eff * Trans eff

32%

32%

9%

Machine Mode:

Q

main

= 7500 m

3

/h

0.1

μ

m

1

μ

m

10

μ

m

1- Particles

before the sampling point

Nst

1257262

1257108

1255855

4191

4190

4186

2- Particles entering the sampling inlet

Ni

4758

4730

4766

3- Particles

after the inlet, outside of the stack

Nis

3419

3662

3971

4- Particles

reaching the instrumentation

Nout

1336

1324

375

Aspiration efficiency:

Ni/Ns

114%

113%

114%

Transport efficiency:

Nout

/Ni

28%

28%

8%

Sampling

efficiency = Asp eff * Trans eff

32%

32%

9%

Slide18

G. Bozza, E. Da Riva

18

April 18, 2012

Eddies (sampling inlet)Strong recirculation zone which might negatively affect the measurementWhat to do: avoid this geometry, and use a recommended one (coaxial or

shrouded)

Slide19

G. Bozza, E. Da Riva

19

April 18, 2012

Eddies (enlargment)The diverging angle of the final enlargement is too large. Therefore, a separation of the boundary layer occurs and the result is a recirculation zone which might negatively affect the sampling efficiency.What to do: modify the geometry, and possibly eliminate the enlargement.

Slide20

Conclusions

G. Bozza, E. Da Riva

20April 18, 2012

Simulations for the machine case (7500 m3 h-1 in the stack, 25 m3 h-1 in the sampling) were run.Generally, we can distinguish two groups of particles with different behaviour:0.1 ÷ 1 μm → ~ 30% Sampling Efficiency10 μm → ~ 10% Sampling EfficiencyRecirculation zones at the inlet and at the final enlargement which could negatively affect the measurement.Next steps: simulations for the flush mode, simulation for the only stack.

Slide21

What can be already recommended: multiple shrouded probes for sampling

G. Bozza, E. Da Riva

21April 18, 2012

Because it is necessary to design sampling systems to operate under both normal and accident conditions (when proportionately higher concentrations of large particles could be present), it is customary to sample isokinetically. Under the ANSI standard, for large ducts it is recommended that rakes of isokinetic probes be used to span the duct cross section, ostensibly to collect representative samples. (A Predictive Model for aerosol transmission through a shrouded Probe, HONGRUI GONG, SUMIT CHANDRA, ANDREW R. MCFARLAND, AND N. K. ANAND).