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Internal flow and air core dynamics in Simplex and Spill-return pressure-swirl atomizers

Abstract

Spill-return (SR) atomizers enhance the construction of Simplex atomizers by addition of a passage in the rear wall of the swirl chamber through which the liquid can be spilled away. It allows to discharge the liquid always at a high pressure and to spray well over a wide flow rate range. The spray characteristics of pressure-swirl atomizers are strongly linked to the internal flow, and the air-core dynamics affect the spray stability. The SR atomizers are rarely investigated and their internal flow is not studied at all. Therefore, in this paper, the Simplex and SR atomizers with a central SR orifice were examined comparatively. Transparent polymethyl methacrylate (PMMA) models of both atomizers scaled 10:1 were manufactured for the visualization and velocity measurements of the flow inside the swirl chamber. The atomizers were examined by means of high-speed imaging, laser-Doppler anemometry and computational fluid dynamics tools. The experimental and numerical results were analysed and compared in terms of the spray cone angle (SCA), discharge coefficient (CD), and the morphology and temporal stability of the air core. The internal flow characteristics between the original and the model were matched using the Reynolds, Swirl and Froude numbers. The test conditions were limited to inlet Reynolds numbers from 750 to 1750. The results show that the addition of the spill passage strongly affects the internal flow even when the spill-line is closed. The air core in the Simplex atomizer is fully developed and stable for all flow regimes. The SR atomizer behaved differently; with the closed spill-line (spill-to-feed ratio, SFR = 0), the air core does not form at all; therefore, the spray is unstable. The reason is that the liquid, contained in the spill-line, is drained back into the swirl chamber due to a recirculation zone found inside the spill-line. Increasing the SFR stabilizes the internal flow, and the spray becomes stable if SFR > 0.15. The air core begins to form for SFR > 0.4. The results suggest that the axially positioned spill orifice is inappropriate and its placing off-axis would improve the spray stability. The results of the 2D numerical simulation matched closely with the experiments in terms of SCA, CD, velocity profiles, and air core morphology which proved its prediction capabilities.

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Internal flow and air core dynamics in Simplex and Spill-return pressure-swirl atomizers

Author: Malý, Milan; Jedelský, Jan; Sláma, Jaroslav; Janáčková, Lada; Sapík, Marcel; Wigley, Graham; Jícha, Miroslav
Publisher: Elsevier
Year: 2018
DOI: 10.1016/j.ijheatmasstransfer.2018.02.090
Source: https://dspace.vut.cz/bitstreams/d6437e34-5aa7-41ac-89c6-6c501ddb794e/download
In e nal low and ai co e dynamics in Simplex
and Spill- e u n p essu e-swi l a omize s
MALÝ, M.; JEDELSKÝ, J.; SLÁMA, J.; JANÁČKOVÁ, L.; SAPÍK, M.; WIGLEY, G.; JÍCHA, M.
In e na ional jou nal o hea and mass ans e
2018, ol. 123, Augus 2018, pp. 805-814
ISSN: 0017-9310
DOI: h ps://doi.o g/10.1016/j.ijhea mass ans e .2018.02.090
Accep ed manusc ip
© 2018. This manusc ip e sion is made a ailable unde he CC-BY-NC-ND 4.0 license
(h p://c ea i ecommons.o g/licenses/by-nc-nd/4.0/), doi: h ps://doi.o g/ 10.1016/j. uel.2013.03.053
Final e sion a ailable om h ps://www.sciencedi ec .com/science/a icle/pii/S0017931017356879
dspace. u b .cz
In e nal low and ai co e dynamics in Simplex and Spill- e u n p essu e-
swi l a omize s
Milan Malý*1, Jan Jedelský1, Ja osla Sláma2, Lada Janáčko á1, Ma cel Sapík1, G aham Wigley3,
Mi osla Jícha1
1 Facul y o Mechanical Enginee ing, B no Uni e si y o Technology, Czech Republic
2 P o yko s. .o, Czech Republic
3 Loughbo ough Uni e si y, Uni ed Kingdom
*Co esponding au ho : milan.maly@ u b .cz
Abs ac
Spill- e u n (SR) a omize s enhance he cons uc ion o Simplex a omize s by addi ion o a passage in
he ea wall o he swi l chambe h ough which he liquid can be spilled away. I allows o discha ge
he liquid always a a high p essu e and o sp ay well o e a wide low a e ange. The sp ay
cha ac e is ics o p essu e-swi l a omize s a e s ongly linked o he in e nal low, and he ai -co e
dynamics a ec he sp ay s abili y. The SR a omize s a e a ely s udied and hei in e nal low is no
s udied a all. The e o e, in his pape , he Simplex and SR a omize s wi h a cen al SR o i ice we e
examined compa a i ely.
T anspa en polyme hyl me hac yla e (PMMA) models o bo h a omize s scaled 10:1 we e
manu ac u ed o he isualiza ion and eloci y measu emen s o he low inside he swi l chambe . The
a omize s we e examined by means o high-speed imaging, lase -Dopple anemome y and
compu a ional luid dynamics ools. The expe imen al and nume ical esul s we e analysed and
compa ed in e ms o he sp ay cone angle (SCA), discha ge coe icien (CD), and he mo phology and
empo al s abili y o he ai co e. The in e nal low cha ac e is ics be ween he o iginal and he model
we e ma ched using he Reynolds, Swi l and F oude numbe s. The es condi ions we e limi ed o inle
Reynolds numbe s om 750 o 1750.
The esul s show ha he addi ion o he spill passage s ongly a ec s he in e nal low e en i he spill-
line is closed. The ai co e in he Simplex a omize is ully de eloped and s able o all low egimes.
The SR a omize beha ed di e en ly; wi h closed spill-line (spill- o- eed a io, SFR=0), he ai co e
does no o m a all; he e o e he sp ay is uns able. The eason is ha he liquid, con ained in he spill-
line, is d ained back in o he swi l chambe due o a eci cula ion zone ound inside he spill-line.
Inc easing he SFR s abilizes he in e nal low, and he sp ay becomes s able i SFR > 0.15. The ai co e
begins o o m o SFR > 0.4. The esul s sugges ha he axially posi ioned spill o i ice is inapp op ia e
and i s placing o -axis would imp o e he sp ay s abili y. The esul s o he 2D nume ical simula ion
ma ched closely wi h he expe imen s in e ms o SCA, CD, eloci y p o iles, and ai co e mo phology
which p o ed i s p edic ion capabili ies.
Keywo ds
In e nal low dynamics, P essu e-swi l, anspa en nozzle, CFD
1 In oduc ion
P essu e-swi l (PS) a omize s a e used in many applica ions whe e a la ge su ace a ea o d ople s
is needed, o a su ace mus be coa ed wi h a liquid, e.g. combus ion, i e suspension o ai condi ioning.
PS a omize s a e easy o manu ac u e, eliable and p o ide good a omiza ion quali y. They con e he
p essu e ene gy o he pumped liquid in o kine ic and su ace ene gy o he esul ing d ople s. The liquid
is injec ed ia angen ial po s in o a swi l chambe whe e i gains a swi l mo ion unde which i lea es
he exi o i ice as a conical liquid shee . The cen i ugal mo ion o he swi ling liquid c ea es a low-
p essu e zone in he cen e o he swi l chambe and gene a es an ai co e along he cen eline. The low
inside he a omize is a he complex; i is wo-phase wi h seconda y low e ec s. The e is a s ong link
be ween in e nal low condi ions and he esul ing sp ay cha ac e is ics. Howe e , no all aspec s o he
in e nal low a e well unde s ood. A d awback o he Simplex a omize is ha he d ople size depends
on he inle p essu e, hence on he liquid low a e. The low a e a ies as he squa e oo o he injec ion
p essu e. Thus, doubling he flow a e demands a ou old inc ease in injec ion p essu e, which means
ha he ange o applicable low a es is limi ed and hus he u n-down a io (de ined as a io o
2
maximum liquid flow a e o minimum liquid flow a e which ul ils he equi emen o a omiza ion
quali y) is usually low [1]. This disad an age can be elimina ed using a SR a omize which is basically
a Simplex ype wi h a passage added in he ea wall o he swi l chambe , see Figu e 1. When he spill-
line is closed, he a omize ope a es as a s anda d Simplex ype. When a low injec ion low a e is
equi ed, he liquid is spilled away h ough he spill o i ice while he inle p essu e and he swi l
momen um emain high, and he a omiza ion quali y emains. Howe e , inc easing spilled low a e
causes educ ion in he axial momen um o discha ged liquid which consequen ly leads o change in he
sp ay cone angle (SCA), as he SCA is de e mined by he a io o he swi l momen um o he axial
momen um. Ano he d awback is he equi emen o inc eased pump powe and complica ed o low
me e ing. Fo hese easons, he in e es in SR a omize s o ai c a combus o s declined, howe e , i
he a oma ic con en o gas u bine uels ises, gum o ma ion in he small sized a omize s could pose
se ious p oblems o he a omize blockage [2, 3]. The SR a omize s a e i ually ee o his de ec as
hey ha e no small passages. Beside he ai c a combus o s, he SR a omize we e used in s a iona y
gas u bines [4] and indus ial bu ne s [5]. Howe e , he abo e-men ioned ad an ages o SR a omize s
a e c ucial in special applica ions ha equi e a ine sp ay a e y low low a e, e.g. decon amina ion
de ices [6], o o a omiza ion o was e uels and liquids con aining impu i ies whe e la ge dimensions
o low c oss-sec ions a e necessa y o p e en he a omize om clogging, o in applica ions whe e
pneuma ic a omize s a e no allowed bu he wide egula ion ange is equi ed. The s udied spill- e u n
a omize is o iginally used in a combus ion chambe o small u boje ai c a engine manu ac u ed by
PBS Velká Bí eš, a.s., Czech Republic.
Be o e he ad en o compu a ional luid dynamics, a numbe o au ho s a emp ed o desc ibe
he in e nal low o Simplex a omize by ela i ely simple analy ical app oaches. One o he i s was
p esen ed by Taylo [7] who ocused on an in iscid analysis using Be noulli’s equa ion and he p inciple
o maximal low. Taylo de i ed an equa ion o he discha ge coe icien (CD) and he sp ay cone angle
(SCA) solely dependen on he a omize cons an k = 2·Ap/(π·do·ds), whe e Ap is he o al a ea o he
inle po s, do, and ds a e de ined in Figu e 1. Simila esul s we e ound independen ly by o he au ho s,
and hese wo ks ha e been compa ed and e iewed by Chinn [8, 9]. Resul s ob ained by he in iscid
heo y a e no gene ally in good ag eemen wi h expe imen s. Howe e , indings om he in iscid
heo y may be used as a basis o design imp o emen s.
The expe imen al co ela ions o CD we e ound o be mo e complex han he in iscid heo y
p edic ed. Rizk and Le eb e [10] de i ed a semi-empi ical co ela ion whe e, besides he cons an k,
he a io ds/do had a s ong in luence. Jones [11] ound a weak dependence o CD on he leng h o he
swi l chambe and exi o i ice, and liquid iscosi y. Balles e [12] added a dependence on he inle
p essu e. Benjamin [13] ollowed he wo k o Jones [11] and ound in e se ends o some pa ame e s.
Wimme and B enn [14] heo e ically unco e ed a ela i ely s ong e ec o he liquid iscosi y on CD,
which was la e expe imen ally con i med by Maly e al. [15].
The in e nal low cha ac e is ics, especially he ai co e s abili y, we e in es iga ed by a ew
au ho s. Halde [16] in es iga ed he ai co e shape in 21 di e en anspa en a omize s a a ious inle
mass low a es o wa e . Two limi ing alues o Reynolds numbe (Re) we e conduc ed o he incep ion
o he ai co e o each a omize . Below he lowe limi , he ai co e was no o med a all, while abo e
he uppe limi , i was always ound o be s able. He obse ed ha he limi ing Re dec eases wi h an
inc ease in do/ds and a dec ease in Ap/ds. The s able ai co e had a cylind ical shape, and o la ge Re
alues, i was almos cons an in diame e . Fo Re alues close o he limi ing alue, he diame e o he
ai co e inc eased sha ply wi h inc easing Re. A simila concep o limi ing alues o Re was in oduced
by Lee e al. [17]. In his expe imen al wo k, a anspa en a omize wi h diesel and ke osene used o e
a ange o inle p essu es and empe a u es. They deduced ha he ai co e s abili y was a unc ion o Re
ela ed o he exi o i ice, Reo. I was s able o Re > 3300; a lowe alues i became uns able un il o
Reo below 2400, whe e he e was no ai co e a all due o insu icien cen i ugal o ces, and he sp ay
luc ua ed s ongly. Kim e al. [18] in es iga ed he in luence o diame e and leng h o he swi l chambe
on he ai co e s abili y. A omize s wi h a a io o swi l chambe heigh o i s diame e hs/ds highe han
1.27 demons a ed an uns able ai co e. The au ho s [18] desc ibed he uns able ai co e as ha ing a
o a ing and double helical s uc u e. Moon [19] ound a limi ing alue o he swi l numbe S0 = 0.6,
which ensu ed a s able ai co e. The same limi ing alue o S0 was also p oposed by Pa k [20] o swi ling
je s. SR a omize s ha e a ely been s udied, and hei in e nal low has no been documen ed so a o
he bes o ou knowledge. Especially he e ec o he spill o i ice a angemen on he in e nal low is
3
no a all clea . The liquid spill can be ealized by a single axial o i ice, by se e al o -axis o i ices, o
by an annula slo [21]. The simples designs use a single, axially placed spill o i ice bu he p oblems
wi h sp ay s abili y we e epo ed [21-23], especially unde ope a ing egimes wi h a closed spill-line.
The o me app oaches o s udy he in e nal low we e mos ly expe imen al [24, 25] and analy ical
[8, 9, 26]. The applica ion o CFD has g ea ly simpli ied design p ocess o he a omize due o inc ease
in compu ing pe o mance in ecen yea s. In 1997, Yule and Chinn [27] conduc ed one o he i s
nume ical s udies using a 2D simula ion. They assumed a lamina low e en o Re = 50,000; an in e nal
ai -co e was cap u ed by he Volume o Fluid (VOF) me hod. They epo ed he di e ence be ween
nume ical calcula ions and he expe imen o be less han 3%. Simila ly a 2D lamina se up was used by
Amini [28] and Mandal [29]; bo h au ho s epo ed a close ma ch wi h expe imen al da a. Summe [30]
compa ed 2D and 3D simula ions wi h a lamina solu ion and ound only a small di e ences be ween
hem. Madsen [31] es ed lamina and u bulen k-ε models oge he wi h a La ge Eddy Simula ion
(LES). The u bulen model o e es ima ed he u bulen iscosi y; he ai -co e was no o med a all.
The lamina model was compa able o he LES p edic ions. Va ious models o cap u e he liquid–ai
in e ace we e in es iga ed by Baha anchi [32]. A geome ical econs uc ion scheme was ound o be
an op imal me hod o cap u ing he ai co e. While he e a e some pape s p o iding CFD simula ions
o Simplex a omize s, no nume ical simula ion o SR a omize we e ound.
Due o he lack o published esul s on SR a omiza ion, he p esen s udy in es iga ed
expe imen ally and nume ically he in e nal low o SR a omize . Fi s ly he wo k examines he
possibili y o p edic he a omize cha ac e is ics such as CD and SCA, and he eloci y ield in he swi l
chambe , using a ela i ely simple 2D simula ion. The main ocus is o elucida e on he sp ay
luc ua ions, epo ed in ou p e ious wo ks [22, 33], and o de e mine hei sou ce. Fu he mo e, he
in e nal low cha ac e is ics a e o be compa ed wi h a Simplex a omize .
2 A omize geome ies and liquid p ope ies
The expe imen s we e pe o med using bo h Simplex and SR a omize designs. In o de o
examine he in e nal low, he a omize s we e manu ac u ed as anspa en copies. Due o he small
dimensions o he o iginal a omize s (see Figu e 1), i was impossible o manu ac u e hem and o
examine hei lows di ec ly. To sol e his issue, he anspa en e sions we e designed as en imes
scaled copies. The scaled a omize s ha e a modula cons uc ion (Figu e 2, igh ). The assembly consis s
o h ee pa s, each made om PMMA. The bo om pa con ains he swi l chambe wi h he exi o i ice,
he cen al one o ms he angen ial inle po s, while he op pa is a plain wall, in he case o Simplex
a omize o , con ains he spill o i ice in he case o he SR a omize . This modula cons uc ion allows
o each pa o be eplaced by ano he one o a di e en geome y o shape. The su aces o each pa
we e g ound and polished o achie e he anspa ency su icien o op ical access.
Figu e 1. A ske ch o he o iginal SR a omize wi h he main dimensions in millime es. The Simplex a omize
has he same geome y and size, bu he spill-line o i ice is missing. The anspa en a omize has he same
shape, and all dimensions a e 10 imes la ge .
4
Due o he en imes model scale i is necessa y o ma ch he low o he o iginal and scaled
a omize s so he ele an dimensionless numbe s mus be conside ed. Re is de ined as he a io o ine ial
o ce o he iscous o ce. In he case o he swi l a omize , he mos common de ini ion o Re is ela ed
o he inle po s [34] as:
ν
p
d
p
wRe =
(1)
whe e wp is he mean eloci y in he inle po s, calcula ed as a olume ic low a e di ided by he o al
c oss-sec ion o inle po s,
ν
is he liquid kinema ic iscosi y, and dp is he hyd aulic diame e o he
inle po s:
)
p
b
p
h(
p
b
p
h
p
d+= 2
(2)
, o dimensions, see igu e 1. The Re alues o he scaled model mus ma ch hose o he o iginal o
keep he same in e nal low cha ac e . The Swi l numbe S0 is use ul in de e mining he a io o he
angula momen um o he axial momen um. I can be calcula ed as a unc ion o he in e nal geome y
[34]:
0
S R A
op
π
=
(3)
whe e R is a adius o low en y o he swi l chambe and Ap is he o al c oss-sec ion o he inle po s.
I is ob ious ha he swi l numbe s o he o iginal and scaled a omize s a e iden ical. The F oude
numbe (F ) shows he e ec o g a i y in compa ison wi h he ene gy o he bulk low and is calcula ed
as:
22
2( )
Q
F g
o oa o
π
=
−
(4)
whe e Q is he olume low a e and oa is he adius o he ai co e in he exi o i ice. To minimize he
e ec o g a i y, i is necessa y o keep F >> 1, as in he o iginal a omize case. The F oude numbe
o he lowes p essu e used was 6.9 hus he e ec o he g a i y was small. Sp ay ela ed dimensionless
numbe s, such as Webe numbe and Ohneso ge numbe di e be ween he o iginal and scaled
a omize s by an o de o magni ude hus he sp ay pa ame e s we e no in es iga ed excep o he sp ay
cone angle, SCA, close o he exi o i ice.
Table 1 lis s he expe imen al low egimes wi h hei dimensionless numbe s. The ope a ing
egimes we e de i ed om hose used in p e ious s udy [22]. The main con ol pa ame e was he inle
p essu e o he o iginal a omize s and consequen ly i s mass low a e, om which he Re was calcula ed.
The SR a omize was e alua ed wi h bo h he closed spill-line o simula e he maximum injec ion a e
and a ious spill- o- eed (SFR) egimes. Ke osene- ype Je A-1 ep esen ing he commonly used uel
was used in bo h he o iginal and modelled a omize . Howe e , he e ac i e index o ke osene di e s
om he e ac i e index o he PMMA by abou 0.05 a 660 nm wa eleng h a 25 °C which dis u bs
he op ical measu emen close o he in e nal su aces o he anspa en model. A liquid wi h a e ac i e
index e y close o he PMMA should be used o educe he op ical dis o ions. Fo his pu pose, se e al
di e en liquids and mix u es we e e alua ed o de e mine he mos sui able. Pa acymene (p-cymene o
1-Me hyl-4-(p opan-2-yl)benzene) was chosen. I is a colou less, anspa en o ganic compound wi h a
e ac i e index di e en om Plexiglas by less han 0.001 a 660 nm wa eleng h and a 25 °C. I also
has a ela i ely low agg essi eness o PMMA; howe e , a e a ew hou s o measu emen , i did cause
c acks in hose pa s whe e inc eased in e nal s esses may be an icipa ed, i.e. in he icini y o bol s and
h eads; hus, i was only used o high-speed imaging. The physical p ope ies o Je A-1 a e
σ = 0.029 kg/s2, μl = 0.0016 kg/(m·s), ρl = 795 kg/m3 and p-cymene: σ = 0.028 kg/s2, μl = 8×10-
4 kg/(m·s), ρl = 850 kg/m3.
Simila ly designed es benches we e used o es ing o bo h he o iginal and scaled a omize s,
see Figu e 2. The es liquids we e supplied o he a omize (8) om a uel ank (1) ia a il e (2) by a
gea pump o a cen i ugal pump (3) o he o iginal and he scaled a omize espec i ely. The mass low
was egula ed by a ying he pump speed. The uel lowing h ough he inle line was me e ed by he
Co iolis mass low me e Mass 2100 Di3 i ed wi h he Mass 6000 ansmi e (Siemens AG, GE) (4)

5
wi h an accu acy ±0.1% o he ac ual low a e. S a ic inle o e -p essu e was measu ed by a piezo-
esis i e p essu e senso DMP 331i (BD SENSORS s. .o., CZ) (7). The unce ain y in he p essu e
sensing was 0.05 kPa and 2 kPa o he scaled and he o iginal a omize espec i ely as di e en senso s
we e used in each case. The inle line was also equipped wi h a empe a u e senso PR-13 made by
OMEGA Enginee ing, INC., USA wi h an e o o 0.2 °C. The spill-line had a piezo- esis i e p essu e
senso DMP 331i (BD SENSORS s. .o., CZ) (9), a ball al e (11) and a posi i e displacemen low
me e KOBOLD DOM-S05 wi h accu acy ±1% o he ac ual low a e (KOBOLD Mess ing GmbH,
GE) (10). The calcula ed unce ain y o CD a Re = 1021was 0.14 % and 0.25 % o o iginal and scaled
Simplex a omize espec i ely. The a omized liquid was cap u ed by a collec ion chambe and ou ed
back in o he uel ank. Fuel mis and apou s we e en ila ed by a an. The a omize was moun ed o a
CNC posi ioning sys em wi h a posi ional e o less han 0.1 mm.
Figu e 2 Le : Schema ic layou o liquid supply. Righ : A Schema ic o he scaled anspa en a omize
Table 1 Ope a ing low egimes, ke osene, S0 = 3.87
O iginal a omize
Scaled a omize
Re
Δp
ml
CD
F
Δp
ml
CD
F
[–]
[MPa]
[kg/h]
[–]
[–]
[kPa]
[kg/h]
[–]
[–]
Simplex
755
0.5
5.41
0.387
137
5
53.8
0.378
6.9
Simplex
1021
1
7.31
0.369
293
10
73.1
0.366
9.3
Simplex
1252
1.5
8.97
0.365
359
15
88.2
0.362
11.4
SR
1075
0.5
7.7
0.542
308
5
69.4
0.483
9.8
SR
1431
1
10.25
0.519
411
10
93.4
0.466
13.0
SR
1731
1.5
12.4
0.510
497
15
110.0
0.454
15.7
SR, SFR 0.4
1676
1
12.0
0.378
481
10
103
0.3
15
(2) (3)
(7)
(5)
(6)
(1)
(8)
(4)
(11)
(9)
(10) (12)
6
Figu e 3. High-speed isualiza ion, p-cymene, 1 MPa, Simplex, c oss-sec ion a, b and c placed 2.5, 8 and 13
mm om he op o he swi l chambe
3 Expe imen al and nume ical se ups
Following subchap e s documen he se ups o he expe imen al app oach using a high-speed
came a and lase -Dopple anemome y (LDA) and he CFD simula ions.
3.1 Expe imen al se up
The expe imen s we e pe o med on he cold es bench a oom empe a u e. A Pho on SA-Z
high-speed came a was used o documen he spa ial and empo al beha iou o he ai co e. The
a omize was illumina ed by a backg ound ligh using an LED panel. Th ee eco ds we e acqui ed a
each ope a ing egime; he i s was a gene al image showing he whole a omize while he o he wo
obse ed he exi o i ice and he op o he swi l chambe in close up, see Figu e 3. The came a ame
a e was 4,000 and 20,000 ps o he gene al image; he esolu ion was 1024 × 1024 px, and he shu e
speed was se o 20 μs. The close-up eco ds used a ame a e o 28,000 ps, esolu ion 768 × 904 px,
and a shu e ime o 10 μs. Mean and RMS images we e calcula ed o each egime. The ai co e
dimensions we e cap u ed by MATLAB code based on he Canny edge de ec o . The ai co e
luc ua ions we e analysed using he Fas Fou ie T ans o m (FFT) in he c oss-sec ion b. The FFT was
applied o he ime- esol ed ai co e su ace cap u ed by he Canny edge de ec o . Ano he FFT was
used on he a e age pixel in ensi ies o e a ec angle 3 × 3 px placed nea he ai co e bounda y o e i y
he p e ious FFT app oach. The ai co e dimensions we e measu ed a h ee c oss-sec ions (a, b and c)
o e he swi l chambe and one c oss-sec ion a he ip o he exi o i ice.
The LDA, a FlowExplo e (Dan ec Dynamics A/S), was employed o he poin -wise
measu emen o he eloci y o indi idual pa icles inside he anspa en a omize . The swi l eloci y
componen was measu ed in h ee c oss-sec ions ac oss he swi l chambe (see Figu e 3 igh ). The axial
dis ances om he op o he swi l chambe we e 2.5, 8 and 13 mm o c oss-sec ions a, b and c
espec i ely, and 50, 38 and 25 measu emen poin s we e aken on each c oss-sec ion. The dis ance
be ween wo su ounding poin s was 0.25 mm. The LDA was con igu ed in he backsca e mode. A
buil -in, diode-pumped solid-s a e lase gene a ed a beam wi h 660 nm wa eleng h. The beam was spli
in o wo pa allel beams wi h he powe o 30 mW each. One o he beams was shi ed by 80 MHz. A
con e ging ansmi ing/ ecei ing lens wi h 150 mm ocal leng h was used o o m an ellipsoidal
measu emen olume wi h he size o app. 0.1 × 0.1 × 0.8 mm. Dan ec BSA P80 signal p ocesso was
used o p ocess he measu ed signal. BSA low so wa e 5.20 was used o con ol he da a acquisi ion
and he ollowing se ing was used: Pho omul iplie sensi i i y 700 V, signal gain 20 dB, eloci y cen e
2.4 m/s, eloci y span 4.8 m/s. The measu emen was limi ed o 10,000 samples acqui ed o a 10-second
acquisi ion du a ion a each measu ed poin . A epea abili y e o based on h ee consequen
measu emen s was less han 4%. The measu ing olume posi ion ela i e o he LDA posi ioning sys em
had o be co ec ed due o he di e en e ac i e index o he a omize body and he liquid as [35]:
)
1
11
(
2
1
1
2
−+
=
Sn
R
n
n
R
S
,
(5)
7
whe e S1 is he i ual dis ance o measu emen olume om he a omize wall, S2 is he eal
dis ance o measu emen olume, R is he diame e o he swi l chambe a measu emen plane, n1 and
n2 a e he e ac i e indexes o PMMA and ke osene espec i ely. The measu ed eloci y was mul iplied
by co ec ion coe icien k el based on he simpli ied app oach om [35] as:
R
S
n
n
el
k2
)1(1
2
1−+=
. (6)
The co ec ion ac o eached he maximum o 1.04 o ke osene a he a omize axis. In posi ions
close o he ai -co e, he aw eloci y da a we e il e ed since he s ong noise was gene a ed by he
e lec ion om he ai co e su ace. The il a ion p ocess seeks o he Gaussian dis ibu ion in he
eloci y his og am, and he mean eloci y was calcula ed only om he da a which sa is ied he Gaussian
dis ibu ion.
The low ace pa icles we e SL75 e-sphe es wi h a mean diame e o 45 μm. Thei S okes
numbe , based on he swi l eloci y and diame e o he swi l chambe , was less han 0.01 o each
egime, which ensu ed a su icien ly small low aceabili y e o .
3.2 Nume ical se up
Conse a ion o mass (con inui y) and conse a ion o momen um (Na ie –S okes) equa ions
we e sol ed nume ically using Ansys Fluen 17.2. The low simula ion was conduc ed as a ansien 2D
axisymme ic model. A Volume o Fluid (VOF) model wi h he geo- econs uc scheme was used o
cap u e he bounda y o he ai co e. The 3D inle bounda y condi ion was se o conse e he mass low
a e in he adial di ec ion and ensu e he same angula momen um in he angen ial di ec ion. The
p essu e ou le bounda y condi ion was applied on he ou e bounda ies wi h no-slip condi ions applied
on he wall bounda ies. A lamina low was assumed due o he low Re alues inside he inle po s, and
also because inside he swi l chambe , he adial o ces o he swi l end o lamina ise he low [34]. The
simula ions we e pe o med o bo h he o iginal and scaled a omize s. The SR a omize was simula ed
including a 4-mm long pa o he spill-line geome y (see Figu e 10 in sec ion 4.3). The spill low in
he egime wi h SFR = 0.4 was se as a nega i e liquid sou ce ac oss he en i e spill-line. I was no
possible o se he p essu e bounda y condi ion o he spill-line wall as he solu ion was e y uns able.
The all quad s uc u ed mesh wi h an a e age skewness o 0.058 and an a e age aspec a io o
1.18 was c ea ed (Figu e 4), and he mesh independence es was ca ied ou o ou di e en elemen
base sizes in e ms o CD, SCA and he ai co e diame e (da) a he end o he exi o i ice (do) in a
dimensionless o m as da/do (see Table 2). The e was a signi ican di e ence be ween he meshes o
11,684 and 22,669 elemen s. This di e ence dec eased wi h u he inc ease in he numbe o elemen s,
and he mesh wi h 46,765 elemen s was chosen as a good comp omise be ween he accu acy and he
calcula ion speed. Two sizes o an ou low a ea, which is an a i icial a ea downs eam o he a omize
ou le , we e also es ed. A calcula ion o ou imes la ge ou low a ea e ealed he same esul s as he
o iginal one, see esul s o meshes wi h 68,610 and 46,765 elemen s.
Table 2. Mesh independence es
Numbe o elemen s
CD [–]
da/do [–]
SCA [deg]
11,684
0.392
0.655
58
22,669
0.365
0.707
58
46,765
0.358
0.710
57
68,610*
0.359
0.710
57
90,684
0.356
0.711
56
*The base size o he elemen s was he same as in he case o 46,765 elemen s. The ou low a ea was
ou imes la ge .
8
Figu e 4. Le : Nume ical domain and i s mesh. Righ : Typical esul s ob ained wi h he wa y su ace o he ai
co e, phase dis ibu ion: 1 = ai , 0 = liquid.
4 Resul s and discussion
The ai co e shape and s abili y play a key ole in he o ma ion o he liquid shee a he discha ge
o i ice. A desc ip ion o he ai co e dynamics is based on high-speed image eco ds and nume ical
simula ions. The discha ge pa ame e s a e discussed in e ms o CD and SCA. The measu ed swi l
eloci y p o iles se ed o consequen alida ion o he nume ical simula ions.
4.1 Ai co e shape and sp ay cone angle
In a compa a i e manne , he high-speed eco ds wi h bo h ke osene and p-cymene as he wo king
liquid a e shown in Figu e 5. Fo he ke osene image, he e a e da ke egions owa ds he edge o he
swi l chambe . This is caused by ligh e ac ion a he swi l chambe wall. I is no e iden in he
a omize cen e due o he small ela i e cu a u e. This is sol ed using he liquid wi h he same
e ac i e index as he a omize body which can be seen o he esul s o p-cymene.
The ai co e was ully de eloped in he case o all he Simplex a omize s. I was cylind ically
shaped and inc eased in i s diame e inside he exi o i ice; such beha iou was also desc ibed by o he
au ho s [16, 17, 28]. The dimensionless diame e o he ai co e in he exi o i ice was da/do = 0.72 ± 0.02
o all he inle p essu es and bo h liquids wi h no e iden co ela ions o Re. Inside he swi l chambe ,
da/do = 0.47 ± 0.03 and i was also almos independen o Re. Bo h indings a e in acco dance wi h o he
au ho s [16, 36, 37] who epo ed he independen ai co e size o high Re egimes, while Halde and
Som [16] ound a sligh ly inc easing ai co e diame e wi h Re. Ins abili ies, in he o m o ai co e
luc ua ions, bo h in he axial and adial di ec ion (Figu e 6), we e obse ed a he op o he swi l
chambe . These luc ua ions a e linked wi h he wa y s uc u e on he ai co e su ace. The equency
o he su ace wa es = 32 ± 4 Hz was es ima ed using he FFT analysis o images o he Simplex
a omize wi h p-cymene a Re = 1021. A simila analysis was epo ed by Sume e al. [30] who used a
simila ly sized a omize , bu wi h he eloci y in he inle po s app oxima ely en imes highe ; hey
ound wa e equencies o = 273 Hz. Chinn e al. in [38] s udied he su ace wa es on he ai co e and
desc ibed h ee dis inc i e ypes o su ace wa es: helical s ia ions, s a iona y wa es and andom
ipples. They no ed ha he s a iona y wa es we e esponsible o changes in he liquid shee hickness.
The same phenomenon was also e iden in ou eco ds. The helical s ia ions, which a e caused by ini e
numbe o he inle po s, we e no obse ed he e.