Still wat St water dead zone & collimat dead zone & col - - PowerPoint PPT Presentation

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Still wat St water dead zone & collimat dead zone & col - - PowerPoint PPT Presentation

Still wat St water dead zone & collimat dead zone & col mated ej ed eject ecta in g in granula lar jet im jet impact ct Wendy W. We W. Zh Zhang Ni Nicholas G Guttenberg, He Herve T Turlier, Jake E Jake Ellowitz, Si


slide-1
SLIDE 1

We Wendy W.

  • W. Zh

Zhang Ph Physics De Department & James Fr Franck Institute Un University of Chi Chicago cago No Nonequilibrium Dy Dynamics in A in Astrophysics and M strophysics and Material Science aterial Science Ky Kyoto, Japan 2011

St Still wat water dead zone & col dead zone & collimat mated ej ed eject ecta in in g granula lar jet im jet impact ct

Ni Nicholas G Guttenberg, He Herve T Turlier, Jake Jake E Ellowitz, Si Sidney R

  • R. Nagel
slide-2
SLIDE 2

Introdu

  • duction
  • n

De Dense granular flow w is complex heterogeneous heterogeneous fl flow avalanches avalanches

Jaeger, Nagel mustard seeds

heterogeneous heterogeneous s stress fi field fo forc rce n netw twork rks

Zhang, Majmudar & Behringer photoelastic discs

imposed shear

slide-3
SLIDE 3

Introdu

  • duction
  • n

im impact pact  sc scattering st structure

Rutherford’s goldfoil scattering experiment wikipedia

light scattering from light scattering from infrared to x-ray infrared to x-ray dense dense molecular

  • lecular beam

beams s in in ultracold ultracold chem chemistry istry relativistic particle beam relativistic particle beams in collider physics ... s in collider physics ...

slide-4
SLIDE 4

jet jet

Im Impact pact of

  • f dense

dense granul granular ar je jet

  • C

Collim llimated ted (liq (liquid id-lik

  • like)

e) ej ejecta & interior dead zone

  • D

Differ ifferen ent in t inter terio ior s str tructu cture e  sa same ejecta

  • L

Liq iquid id-lik

  • like r

e res esponse e  pe perfect fluid flow dissipationless flow di dissipation = fr frictional fl fluid co continuum flow remains no non-Newtonian in in lim limit to it towards d dis issip ipatio tionle less p perfe fect flu t fluid id flo flow

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slide-5
SLIDE 5

jet jet

1.

  • 1. Introduction

Introduction 2.

  • 2. Ba

Background 3.

  • 3. Ex

Experiments & simulation 4.

  • 4. Mo

Model 5.

  • 5. Discussion

iscussion & Conclusion

  • nclusion

Outline Outline

slide-6
SLIDE 6

jet

loosely packed jet  shower of recoils

dense dense jet jet  ej ejecta co collimated hollow hollow conical conical sheet sheet

Cheng et al. PRL 07

Bac Backgr kgrou

  • und: gr

d: gran anular ar j jet i impac pact col

  • llimat

ated (l d (liqu quid-l d-like ke) e ) ejecta

non-cohesive particles

jet target target holder

non-cohesive glass beads

slide-7
SLIDE 7

Ej Ejecta s a sheet an angl gle c chan ange ges wi with DTar

ar /D

/DJe

Jet redu ducing g DTa

Tar /D

/DJe

Jet

Gran anular ar e ejecta an a angl gle ψ0 agr agree n numerical ally wi with val alues for

  • r wat

water j jet  liqu quid-l d-like ke e ejecta

 w wate ter  g gla lass b beads

slide-8
SLIDE 8

jet jet

Did i d impac pact c creat ate a l a liqu quid ph d phas ase?

"0 = 1# A(DTar /DJet)2 1# B(DTar /DJet)2

dimensionless reaction force dimensionless drag force Mo Mome mentum m balance Wh When DTa

Tar <

<< DJe

Jet

"0 #1$ A $ B

( )(DTar /DJet)2

 w wate ter  g gla lass b beads

Sam ame ψ0  sam ame A-B

  • B

Bu But i indi dividu dual al v val alues of A an

  • f A and B m

d B may ay di diffe ffer

slide-9
SLIDE 9

Con Context xt

Pozkanser, Voloshin, Ritter... 2008 APS Bonner prize talk Romatschke & Romatschke PRL 2007 Teiser & Wurm, Mon. Not. R. Astron. Soc. 2009

  • E

Ellip lliptic flo tic flow: co : collim llimated ted ejecta ejecta fr from co collis llisio ion o

  • f

gol gold d io ions at relativistic speeds Liq iquid quark- gl gluon uon phase phase with h New ewtoni

  • nian

an vi viscosi scosity? y?

  • F

Formatio tion o

  • f p

f pla lanetis etismals ls fr from d dust a t aggreg egates tes vi via col a collisi sion

  • ns
slide-10
SLIDE 10

jet jet

1.

  • 1. Introduction

Introduction 2.

  • 2. Ba

Background 3.

  • 3. Ex

Experiments & simulation

Outline Outline

slide-11
SLIDE 11

target 1 0.5 |u|/U0

Expe Experiment  jet i interior

  • r i

is n not

  • t l

liqu quid-l d-like ke

d e a d z

  • n

e Look at

  • ok at i

impac pact of h

  • f hal

alf a j f a jet pr pressed agai d against gl glas ass side de-v

  • view of j

w of jet i interior

  • r
slide-12
SLIDE 12

(b) 0.2 0.4 <ur(z=0)> m/s θeff = Teff / max(Teff) 0.25 0.25 r /DJet

0.25 0.25 0.5 1

Expe Experiment  dead z ad zon

  • ne i

is c col

  • ld

tran anspar parent t tar arge get

r /DJet

slide-13
SLIDE 13

jet jet

target

"0 #1$ A $ B

( )(DTar /DJet)2

reac action

  • n

for force dr drag ag for force

liqu quid-l d-like ke ejecta ejecta interior

  • r

structure structure

?

slide-14
SLIDE 14

Simulat ation

  • n

red = d = h high gh s spe peed d bl blue = = z zero s

  • spe

peed

jet rigid grains rigid grains inelastic collisions inelastic collisions fric frictio tion b betw tween g gra rain ins sticky target sticky target gr grains immobile after co colliding with target

slide-15
SLIDE 15

Simulat ation

  • n r

repr produ

  • duces e

expe xperiment

norm normalized alized velocity velocity contours contours agree agree quantitatively quantitatively

red = d = h high gh s spe peed d bl blue = = z zero s

  • spe

peed

jet collimated ejecta dead zone

slide-16
SLIDE 16

No de

  • dead z

ad zon

  • ne at

at fr friction

  • nless t

tar arge get

jet

  • coeff. of restitution and/or friction between grains  weak variation

Guttenberg (2011)

slide-17
SLIDE 17

P(ψ−ψ0) ψ−ψ0 0.004 0.01 5

  • 5

 no dead zone  dead zone 0.008

  • 10

10

Diffe fferent i interior

  • r Sam

ame e ejecta

ejecta ejecta angle angle changes changes from rom 45 45° (w (with dead zone)  40 40° (w (without deadzone) ejecta ejecta r remains collimated

slide-18
SLIDE 18

jet jet

1.

  • 1. Introduction

Introduction 2.

  • 2. Ba

Background 3.

  • 3. Ex

Experiments & simulation Sa Same ψ0

0 i

in granular & water jet impact  li liquid phase in granular jet? No No Ej Ejecta ≠ sc scattering pattern (dilute regime)

Outline Outline

"0 #1$ A $ B

( )(DTar /DJet)2

reac action

  • n

for force dr drag ag for force

De Dense jet impact is different  T To see relevant limit, model as continuum insted of simulating as hard spheres

slide-19
SLIDE 19

Fr Friction

  • nless t

tar arge get s simulat ation

  • n r

results  con

  • ntinuum m

mode

  • del of gr
  • f gran

anular ar j jet i impac pact

1.

  • 1. Ma

Mass conservation 2.

  • 2. En

Energy conservation 3.

  • 3. Mo

Mome mentum m conservation No Not assuming hydrodynamic limit obtains Ph Phenomenological

slide-20
SLIDE 20

Fr Friction

  • nless t

tar arge get s simulat ation

  • n r

results  con

  • ntinuum m

mode

  • del of gr
  • f gran

anular ar j jet i impac pact

1.

  • 1. Ma

Mass conservation

density velocity field

incom

  • mpr

pressibl ble fl flow

  • w
slide-21
SLIDE 21

Fr Friction

  • nless t

tar arge get s simulat ation

  • n r

results  con

  • ntinuum m

mode

  • del of gr
  • f gran

anular ar j jet i impac pact

2.

  • 2. Energy

nergy conservation conservation granular granular tem temperature perature

TG = = 0 flow

slide-22
SLIDE 22

Fr Friction

  • nless t

tar arge get s simulat ation

  • n r

results  con

  • ntinuum m

mode

  • del of gr
  • f gran

anular ar j jet i impac pact

3.

  • 3. Mo

Mome mentum m conservation density × acceleration = - pressure gradient + dissipation (shear stress tensor) shear stress = µ pressure elocal shear direction phenomenological friction coefficient

µ

slide-23
SLIDE 23

Fr Friction

  • nless t

tar arge get s simulat ation

  • n r

results  con

  • ntinuum m

mode

  • del of gr
  • f gran

anular ar j jet i impac pact

1.

  • 1. Ma

Mass conservation 2.

  • 2. En

Energy conservation 3.

  • 3. Mo

Mome mentum m conservation

Incom

  • mpr

pressibl ble fr friction

  • nal

al fl fluid

TG = 0 µ

Bo Boundary conditions: At At un unknown j jet surface, normal stress and tangential stress both 0 stress both 0 At At target, tangential and normal velocity both 0

slide-24
SLIDE 24

Fr Friction

  • nless t

tar arge get s simulat ation

  • n r

results  con

  • ntinuum m

mode

  • del of gr
  • f gran

anular ar j jet i impac pact

1.

  • 1. Ma

Mass conservation 2.

  • 2. En

Energy conservation 3.

  • 3. Mo

Mome mentum m conservation

TG = 0 µ

Choose µ to fit simulated ψ0 quantitatively reproduces u(x) & p(x) in hard sphere simulation

Incom

  • mpr

pressibl ble fr friction

  • nal

al fl fluid

hard sphere simulation

slide-25
SLIDE 25

Fr Friction

  • nless t

tar arge get s simulat ation

  • n r

results  con

  • ntinuum m

mode

  • del of gr
  • f gran

anular ar j jet i impac pact

1.

  • 1. Ma

Mass conservation 2.

  • 2. En

Energy conservation 3.

  • 3. Mo

Mome mentum m conservation

Dissipat pation

  • nless pe

perfe fect fl fluid fl d flow e

  • w emerge

ges wh when we we t take ake t the l limit µ  0

TG = 0 µ

Con Continuou

  • us appr

approac

  • ach i

instead of abr ad of abrupt pt c chan ange ge

slide-26
SLIDE 26

HDZ

DTar

HDZ

µ

Deadz adzon

  • ne s

shrinks ks c con

  • ntinuou
  • usly t

to 0 as

  • 0 as µ  0

slide-27
SLIDE 27

µ

"0 #1$ A $ B

( )(DTar /DJet)2

reac action

  • n

for force dr drag ag for force

Ej Ejecta an a angl gle dom dominat ated by d by con

  • ntribu

bution

  • n fr

from

  • m

reac action

  • n for

force A as as µ  0

slide-28
SLIDE 28

jet jet

1.

  • 1. Introduction

Introduction 2.

  • 2. Ba

Background 3.

  • 3. Ex

Experiments & simulation 4.

  • 4. Model
  • del  al

alternative i interpretation S Same ψ0 b because sm small drag but same reaction force (B (B << A, same A) Di Different di dissipation mechanisms Sa Same limit of perfect fluid flow as dissipation  0 D Dire irect d t demonstra stratio tion th that p t perfe rfect flu t fluid id flo flow is re is rele levant fo for h r hard rd-sp

  • sphere

re je jet im t impact? t?

Outline Outline

"0 #1$ A $ B

( )(DTar /DJet)2

reac action

  • n

for force dr drag ag for force

slide-29
SLIDE 29

Quan antitat ative c check exac xact s sol

  • lution
  • n

2D perfect fluid flow zero surface tension

gr gran anular ar s simulat ation

  • n

2D inelastic / friction non-cohesive

di direct c com

  • mpar

parison

  • n
slide-30
SLIDE 30

Pressure c con

  • ntou
  • urs

local pressure / pressure at target center

Quan antitat ative agr agreement

solid line = granular simulation dashed line = perfect fluid solution

slide-31
SLIDE 31

Discussion

  • n
  • E

Ellip lliptic flo tic flow a at RHIC Sm Small deviation from perfect fluid flow in inte terprette tted a as v very lo low N Newto tonia ian v vis iscosity ity

  • - assumes hydrodynamics

Gr Granular jet imp mpact sm small deviation ≠ l low Newtonian viscosity ap approaches pe perfect fluid flow as frictional flu fluid (alw id (always far-from ays far-from-equ

  • equilibriu

ilibrium)

slide-32
SLIDE 32

fo form rmatio tion o

  • f d

f dead zo zone during during initial initial im impact pact

Discussion

  • n

Teiser & Wurm

  • Mon. Not. R. Astron. Soc. 2009
  • F

Formatio tion o

  • f p

f pla lanetis etismals ls fr from d dust a t aggreg egates tes col collisi sion

  • ns

ejecta ejecta collim collimated ated wi within 1°

40 m/s

Mo Model as frictional fluid impact?

slide-33
SLIDE 33

jet jet

Con Conclusion

  • n

Acknowledgements: Xiang Cheng, Eric Brown, Heinrich M. Jaeger Support: NSF-MRSEC, Keck Foundation, NSF-CBET

Than ank y k you

  • u

Im Impact pact of

  • f dense

dense granul granular ar je jet

  • C

Collim llimated ted (liq (liquid id-lik

  • like)

e) ej ejecta & interior dead zone

  • D

Differ ifferen ent in t inter terio ior s str tructu cture e  sa same ejecta

  • L

Liq iquid id-lik

  • like r

e res esponse e  pe perfect fluid flow di dissipation = fr frictional fl fluid co continuum flow remains no non-Newtonian in in lim limit to it towards d dis issip ipatio tionle less p perfe fect flu t fluid id flo flow