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Alternating Field Electronanofluidization

Abstract

The use of fluidized beds to remove submicron particles from gases has been investigated since 1949. High efficiency removal was achieved in the 1970’s by imposing an electric field on a fluidized bed of semi-insulating granules that were able to collect the charged pollutant entrained in the fluidizing gas. In spite of their extended use nowadays, the collection efficiency of electrofluidized beds (EFB) is still hindered by gas bypassing associated to gas bubbling and the consequent requirement of too high gas flow and pressure drop. In this paper we report on the electromechanical behavior of an EFB of insulating nanoparticles. When fluidized by gas, these nanoparticles form extremely porous light agglomerates of size of the order of hundreds of microns that allow for a highly expanded nonbubbling fluidized state at reduced gas flow. It is found that fluidization uniformity and bed expansion are additionally enhanced by an imposed AC electric field for field oscillation frequencies of several tens of hertzs and field strengths of the order of 1 kV/cm. For oscillation frequencies of the order of hertzs, or smaller, bed expansion is hindered due to electrophoretic deposition of the agglomerates onto the vessel walls, whereas for oscillation frequencies of the order of kilohertzs, or larger, electrophoresis is nullified and bed expansion is not affected. According to a proposed model, the size of nanoparticle agglomerates stems from the balance between shear, which depends on field strength, and van der Waals forces. The optimum field strength for enhancing bed expansion produces an electric force on the agglomerates similar to their weight force, while the oscillation velocity of the agglomerates is similar to the gas velocity.

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Alternating Field Electronanofluidization

Author: Espin, M. J.; Valverde Millán, José Manuel; Sánchez Quintanilla, Miguel Angel; Castellanos, Antonio
Publisher: American Institute of Physics
Year: 2009
DOI: 10.1063/1.3180095
Source: https://idus.us.es/bitstreams/658ed850-9ed4-4460-b237-e668456226d2/download
AIP Con e ence P oceedings 1145, 97 (2009); h ps://doi.o g/10.1063/1.3180095 1145, 97
© 2009 Ame ican Ins i u e o Physics.
Al e na ing Field Elec onano luidiza ion
Ci e as: AIP Con e ence P oceedings 1145, 97 (2009); h ps://doi.o g/10.1063/1.3180095
Published Online: 01 July 2009
M. J. Espin, J. M. Val e de, M. A. S. Quin anilla, and A. Cas ellanos
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Al e na ing Field Elec onano luidiza ion
M.
J.
Espin ,
J.
M.
Val e de†,
M. A.
S.
Quin anilla†
and
A. Cas ellanos†
Depa men
o
Applied Physics
II.
Uni e si y
o
Se ille.
A enida Reina Me cedes
s/n,
41012
Se ille,
Spain.
†Facul y o
Physics.
Uni e si y
o
Se ille.
A enida Reina Me cedes
s/n,
41012
Se ille,
Spain.
Abs ac . The use o luidized beds o emo e submic on pa icles om gases has been in es iga ed since 1949. High
e iciency emo al was achie ed in he 1970’s by imposing an elec ic ield on a luidized bed o semi-insula ing g anules
ha we e able o collec he cha ged pollu an en ained in he luidizing gas. In spi e o hei ex ended use nowadays, he
collec ion e iciency o elec o luidized beds (EFB) is s ill hinde ed by gas bypassing associa ed o gas bubbling and he
consequen equi emen o oo high
gas
low
and
p essu e
d op.
In his pape we epo on he elec omechanical beha io o
an
EFB o insula ing nanopa icles. When
luidized
by
gas,
hese nanopa icles o m ex emely po ous ligh agglome a es o
size o he o de o hund eds o mic ons ha allow o a highly expanded nonbubbling luidized s a e a educed gas low. I
is ound ha luidiza ion uni o mi y and bed expansion a e addi ionally enhanced by an imposed AC elec ic ield o ield
oscilla ion equencies o se e al ens o he zs
and
ield s eng hs o he o de o 1
kV/cm.
Fo oscilla ion equencies o he
o de o he zs, o smalle , bed expansion is hinde ed due o elec opho e ic deposi ion o he agglome a es on o he essel
walls,
whe eas o oscilla ion equencies o he o de o kilohe zs, o
la ge ,
elec opho esis is nulli ied
and bed
expansion
is no
a ec ed.
Acco ding o
a
p oposed
model,
he size o nanopa icle agglome a es
s ems
om he balance be ween
shea ,
which depends
on
ield
s eng h,
and an
de Waals
o ces.
The
op imum ield s eng h o
enhancing bed expansion
p oduces
an
elec ic o ce
on he
agglome a es simila o hei weigh
o ce,
while
he
oscilla ion eloci y o
he
agglome a es is simila
o he
gas
eloci y.
Keywo ds: Fluidized
beds,
Nanopowde s,
Fil e s
PACS:
47.55.Lm,
81.07.Wx, 84.30.Vn
INTRODUCTION
E icien emo al o dus and mis om gases by pass-
ing hese h ough a bed o luidized solids was i s
claimed by Meisne and Mickley in 1949 [1]. Almos
wo decades
la e ,
p ac ical p oblems such as educing
ai pollu ion om diesel exhaus and il a ion o smoke
emissions om asphal ic pa emen ecycling p ocess,
mo i a ed Melche o de elop elec o luidized beds o
collec ion o submic on pa icles [2]. Melche and co-
wo ke s s essed a luidized bed by imposing an elec-
ic ield ha e ec i ely pola ized he millime e sized
pa icles.
These
semi-insula ing pa icles
hen se ed
he
unc ion o con en ional elec os a ic p ecipi a o s, ac -
ing as collec ion si es
o
he cha ged
pollu an s en ained
in he luidizing gas. In compa ison o elec os a ic p e-
cipi a o s, he collec ion su ace a ea pe uni olume o
elec o luidized
beds
is g ea ly
inc eased,
making i pos-
sible o educe he gas esidence ime and olume o
he il e [2]. A majo conce n ha bese s classical lu-
idized bed il e s lies in he bypassing o he con ami-
nan s h ough gas bubbles. Gas bubbling is he ypical
beha io ound in luidized
beds
o millime e
sized
pa -
icles [3], p o iding li le gas-solid con ac and hampe -
ing eac ion e iciency.
Powde s o mode a e densi y nanopa icles (such as
silica) can be uni o mly luidized and expe ience a
an-
si ion o elu ia ion a high gas eloci ies wi h ull sup-
p ession
o isible bubbles
[4].
In his pape
we
s udy he
beha io o
an
elec o luidized
bed
o d y silica nanopa -
icles,
which shows agglome a e pa icula e luidiza ion
in he absence o ex e nally applied elec ic
ield.
Sam-
ples we e subjec ed o DC and AC elec ic ields in o -
de o check he in luence o he equency o he ex-
e nal ield and o de e mine he size and cha ge o he
powde .
The supp ession
o
gas
bubbles in
luidized
beds
o nanopa icles has been causally ela ed o he o ma-
ion o po ous ligh agglome a es. A phenomenological
app oach o p edic he beha io o gas- luidized beds
o nanopa icles is o conside agglome a es
as
e ec i e
low-densi y
sphe es which
may exhibi nonbubbling
gas-
luidiza ion simila ly o coa se pa icles luidized by
liq-
uids.
In his way, he Richa dson-Zaki (RZ) equa ion,
o iginally in ended o desc ibe he expansion o
uni-
o m liquid- luidized beds [6], can be modi ied o
con-
side uni o m gas- luidiza ion o nanopa icle agglome -
a es
[4]
p (1)
whe e g is
he
supe icial
gas
eloci y, p is he e minal
se ling eloci y o a single pa icle, φ is he pa icle
olume
ac ion,
ka = d /dp is he a io o agglome a e
size o pa icle size, and D =
lnNa/ka,
whe e Na is he
numbe o pa icles in he agglome a e.
CPl
145,
Powde s and G ains 2009, P oceedings o he 6 In e na ional Con e ence on
Mic omechanics o G anula Media edi ed by M. Nakagawa and S. Luding
© 2009 Ame ican Ins i u e o Physics 978-0-7354-0682-7/09/S25.00
97
0.005
0.004
0.003
0.002
0.001
Solidlike - ... ,
T ansi ional
egime
egl„c
Uni o m luidlike egime
0 0.5 1 1.5 2 2.5 3
, (cm/s)
FIGURE 1. Pa icle olume ac ion as a unc ion o supe -
icial
gas
eloci y o luidiza ion wi hou ex e nal elec ic ield
applied.
The solid line ep esen s he modi ied RZ equa ion i
o he da a in he uni o m luidlike
egime.
The pho og aphs in
he inse illus a e bed expansion.
EXPERIMENTAL SETUP AND RESULTS
The luidized bed appa a us consis ed o a e ical 2.54
cm in e nal dia. polyca bona e essel, 16.2 cm in heigh ,
which is i ed a he bo om wi h
a
sin e ed s ainless s eel
pla e,
ha ing
a
po e size o
5
jim, ha ac s as gas dis ibu-
o . The luidiza ion cell is is placed be ween wo pa allel
squa e elec odes o 14 cm o side leng h. The dis ance
be ween he elec odes is ixed o I = 8 cm. One o he
elec odes is g ounded and high ol age V is applied o
he opposi e elec ode om an oscilla o /ampli ie ne -
wo k. The elec ic ield s eng h wi hin he bed can be
aken as app oxima ely cons an (E ~ V/l). The powe
supply sys em allowed us o p o ide peak ield s eng hs
up o E0 ~ 2 kV/cm o e
a
equency ange up o 10 kHz.
Di e en ypes o wa e o m, sinusoidal, squa e and
i-
angula shape, we e applied. The low o gas (d y ai )
o he column was con olled by means o a MKS low
con olle wi h a ull ange om 0 o 2000 cm3/min. The
ma e ial es ed in he expe imen s was p e-sie ed (using
a sie e opening o 500 jim) Ae osil©R974 , which is a
hyd ophobic SiO2 nanopowde wi h a pa icle densi y o
pp
=2250 kg/m3, and pa icle size dp = 12 nm.
In Figu e 1 we ha e plo ed expe imen al da a o
</>
as
a unc ion o g in he absence o ex e nal ield applied.
The bed expands mono onously as g is inc eased. By
i ing he da a o g s.
</>
o he modi ied Richa dson-
Zaki equa ion (Eq. 1), i is ob ained d** = 226jUm and
D = 2.588, which is in good ag eemen wi h p e ious
measu emen s [4].
Figu e 2 shows expe imen al da a on
</>
as a unc ion
o g and o di e en alues o he s eng h o he c oss-
low elec os a ic ield applied. The main e ec o he
elec ic ield is an inc ease o F om local obse a-
ions [7], i is seen ha he dynamics is uled by elec-
0.012
4 0.01
0.008
0.006
0.004
0.002
0
A 4 kV/cm
o 2.6kV/cm
• 1.3 kV/cm
- 0 kV/cm
2 3
(cm/s)
FIGURE 2. . A e age pa icle olume ac ion o he lu-
idized bed φ as a unc ion o he supe icial gas eloci y g
o di e en s eng hs o he elec os a ic ield applied.
(Hz)
FIGURE 3. Rela i e a ia ion o he pa icle olume ac-
ion
as a
unc ion o
he
oscilla ion equency o he al e na ing
elec ic
ield.
Peak ield s eng h is ixed o 1.25 kV/cm. Da a
is shown o h ee di e en alues o he supe icial
gas
eloc-
i y g. The inse shows elec opho e ic deposi ion (1Hz) and
enhanced
bed
expansion (20 Hz).
opho e ic deposi ion a he
wall.
In he s a iona y s a e,
luidiza ion quali y is hampe ed and bed expansion is de-
c eased.
Insula ing d y pa icles in a luidized bed accumu-
la e a signi ican amoun o cha ge. Mos in es iga ions
sugges ha he main cause o he cha ge build-up on
g anula ma e ials du ing indus ial handling and p o-
cessing is con ac cha ging [5]. Cha ges a e exchanged
whene e any wo su aces come in o con ac wi h each
o he e en o cases whe e he bulk ma e ials a e he
same due o su ace impu i ies and impe ec ions. The
elec opho e ic o ce on ou agglome a es is Fe ~
Q**E,
whe e Q** is hei cha ge. Using he S okes’ law o
an isola ed agglome a e, i can be es ima ed Q** =
3nnd** *h*/E,
whe e n is he gas iscosi y and
*h*
is
he e minal eloci y o he agglome a e. We ha e ana-
lyzed he ajec o ies o some agglome a es a he ini ial
s age o applica ion o he elec ic ield by means o a
98
E=1.25kV/cm, =1Hz £=125
kV/cm,
= 20 Hz E=1.25kV/cm, =1 kHz
FIGURE 4. Pho og aphs o he elec onano luidized bed il-
lus a ing bed expansion o h ee di e en equencies o he
al e na ing elec ic ield (indica ed)
as
compa ed o
bed
expan-
sion in he
absence
o ex e nally applied elec ic
ield.
Supe i-
cial
gas
eloci y is ixed o g = 2.7 cm/s.
-0.15
E0
(kV/cm)
•Squa e
—•— Sinusoidal
—±—
T iangula
0.2 0.4
Ems (kV/cm)
0.1
0.01
0.
A+%
• /
1
-0.15
-0.2
FIGURE 5. Rela i e a ia ion o he pa icle olume ac-
ion o he elec onano luidized bed as a unc ion o he ield
s eng h
o
h ee
di e en wa e o m
ypes.
Top:
Da a
is shown
as a unc ion o he peak ield s eng h E0. Bo om: Da a is
shown as a unc ion o he oo -mean-squa ed ield s eng h
E ms.
elec ic ield oscilla ion equency
and
supe icial
gas
e-
loci y a e
ixed
o 20 Hz
and
g = 2.7
cm/s,
espec i ely.
CMOS high-speed came a. The agglome a e cha ge o
he agglome a es manually acked was ound o be o
he o de o 10-14C, gi ing a cha ge o mass a io
Qm
in he ange 10-5 -10-4C/kg.
In he case o an al e na ing
ield,
i is expec ed ha
he cha ged agglome a es will be o ced o oscilla e a
he ield equency. Figu e 3 shows he ela i e a ia ion
A*/*,
Uni o m luidlike
egime
FIGURE 6. Rela i e a ia ion o he pa icle olume ac ion
o he elec onano luidized bed as a unc ion o he supe icial
gas eloci y. Elec ic ield oscilla ion equency and s eng h
a e ixed o 500 Hz and E0 = 1.25 kV/m (squa e wa e), espec-
i ely. The lines a e p edic ed cu es by he model. Solid line:
complex-agglome a e cha ge
Q^*
= 1.9 x 10~14 C. Do ed line:
Q** = 1 x 10-14 C. Dashed line: Q** = 3 x 10"14 C
o he pa icle olume ac ion ( φ/φ0, whe e φo is he
pa icle olume ac ion in he absence o ex e nal elec-
ic ield) o
he
elec onano luidized
bed as a
unc ion o
he oscilla ion equency o a ixed peak ield s eng h
(E0 =
1.25
kV/cm).
Fo equencies o
he
o de o he zs
he main mechanism is s ill elec opho e ic deposi ion o
he agglome a es on he walls, which gi es ise o bed
channeling and
collapse.
In
he ange
o in e media e
e-
quencies, be ween ens and hund eds o he zs, he op-
posi e beha io is
obse ed.
Bed
expansion is g ea ly
en-
hanced by he al e na ing
ield.
Finally, o equencies
o he o de o kilohe zs
and
la ge ,
he al e na ing ield
has no app eciable e ec on bed expansion (see
Fig.
4).
The e ec o he s eng h o he ield in he ange o in-
e media e oscilla ion equencies and wa e o m ype is
shown in Fig. 5. Bed expansion is u he enhanced as
he s eng h o he ield is inc eased. The da a ma ches
o
a
single
end when
i is
plo ed
agains
he
oo -mean-
squa ed
ield
E ms,
which indica es ha
enhanced bed
ex-
pansion is he esul o a ime a e aged
p ocess.
F om a
log-log plo (see inse ) i is obse ed ha φ/φ0 scales
as he
ield s eng h
squa ed,
which is p opo ional o he
kine ic ene gy gained by he agglome a es du ing one
semipe iod. This sugges s a possible ole o collisions
be ween agglome a es o di e en cha ge on deagglom-
e a ion.
DISCUSSION
A change o he pa icle olume ac ion when he
ield is u ned on could be a ibu able o a a ia ion
o he complex-agglome a e size. In o de o es ima e
99
heo e ically
he
complex-agglome a e size, simple-
agglome a es, which exis be o e luidiza ion
[4],
will
be conside ed as e ec i e pa icles unde going agglom-
e a ion
due
o
a ac i e o ces be ween each o he
[8].
This a ac i e o ce
is
coun e balanced
by
he gas
low
shea
o
suppo he weigh
o
he complex-agglome a e
in
he
g a i y ield plus
he
shea
due o
hei o ced
oscilla ions
in he
elec ic
ield.
The
balance be ween
he o e all ime-a e aged shea
and he
a ac i e o ce
de e mines
he
size
o
he
complex-agglome a es.
The
complex-agglome a e weigh o ce
W** is
balanced
by
he
hyd odynamic ic ion om
he
su ounding
gas,
which ac s mainly
a i s
su ace
due o he
low
sc eening e ec . Using
a
sp ing model
[8],
he
ypical
s ain
on he
su ace
o he
complex-agglome a e
can
be es ima ed
as
jg ~
w**/K**R**.
He e
W** =
N*W*,
whe e
N* is
he
numbe
o
simple-agglome a es
in he
complex-agglome a e and
W*
is
he
simple-agglome a e
weigh o ce.
K** is he
complex-agglome a e sp ing
cons an , which, using
a
heo y
on he
elas ic p ope ies
o andom pe cola ing sys ems, can be ob ained om
he
simple-agglome a e sp ing cons an
K*
and he elas ici y
exponen J3
(K** ~
K*/{k* ,
whe e
k* is
he
a io
o
complex-agglome a e adius
R**
o
simple-agglome a e
adius R* and
J3
=
3
in
3D). When he al e na ing elec ic
ield is u ned
on,
he o ced complex-agglome a e oscil-
la ions gi e ise
o
an
addi ional shea o ce
o
balance
he elec ic o ce
Q**E.
The
oo -mean-squa ed shea
s ain
is
hus inc eased
up o
j ms
=
V yg)2
+
(YE)2,
whe e
JE
~
Q**E ms/K**R**.
Thus,
he
shea o ce,
which ac s
on he
simple-agglome a es a ached
o
he
ou e laye
o he
complex-agglome a e,
is
Fs ~
K*Y msR*
~
(k*)D+W(W*)2
+
(Q*E ms)2. He e
i
is
assumed
N* = (k*)D and
ha
he
complex-
agglome a e cha ge
is
equally dis ibu ed among
he
simple-agglome a es
(Q** =
N*Q*,
whe e
Q* is he
simple-agglome a e cha ge). Simple-agglome a es
a ach
o he
complex-agglome a e
as
long
as he
shea o ce
is
smalle han
he
a ac i e o ce. Thus,
he limi condi ion
Fs = F dW
leads
o he
equa ion
k* ~
5o1/(D+2)
o
es ima ing
he
complex-agglome a e
size
d**,
whe e
he
agglome a e Bond numbe
Bo is
de ined
as he
a io
o he
a ac i e o ce
F dW o
V(w*)2
+
(Q*E ms)2.
The
simple-agglome a e weigh
is
W* =
NPWP,
whe e Wp
is
he nanopa icle weigh
and
Np
is
he numbe
o
p ima y nanopa icles
in
he simple-
agglome a e, which
is
assumed
o be Np =
(d*/dp)D.
The simple-agglome a e cha ge
Q* is
needed
o
es ima e
he complex-agglome a e size. P o ided ha simple-
agglome a es
a e
unal e ed
by he
elec ic
ield,
i is
Q*
=
Q*0*/N%,
whe e
Q*0*
and
N%
a e he
complex-
agglome a e cha ge and numbe
o
simple-agglome a es
in
he
complex-agglome a e
o E = 0,
espec i ely.
Thus
k*=k*01+ Q 0* ™
(2)
whe e
k*0
=
d^*/d*
is
he
ela i e complex-agglome a e
size
in
he absence
o
elec ic
ield.
Using a ypical alue
o
F dW
=
10 nN,
d* =
30,11m, and
D =
2.5
-
2.6 [4],
i
is p edic ed
d*0*
~
150^m
in
he absence
o
applied elec-
ic
ield.
Eq.
2
can
be
used
in
he
modi ied
RZ
equa-
ion
(Eq.
1).
Figu e
6
shows
he
ela i e a ia ion
o
he pa icle olume ac ion
as
a
unc ion
o
he
supe -
icial gas eloci y
o
an
imposed ex e nal ield
o
peak
s eng h
E0 =
1.25
kV/cm.
The
lines ep esen
he
p e-
dic ions
by
he model
o
di e en alues
o
he
complex-
agglome a e cha ge. Complex-agglome a e size
in he
absence
o
elec ic ield and ac al dimension
a e
aken
om ou p e ious de i a ion based on bed expansion
ex-
pe imen al da a
(d** =
226 /im,
D =
2.588). Rema k-
ably, he p edic ion i s
o
he da a
in
he luidlike egime
o
a
alue
o
he
complex-agglome a e cha ge
(Q*0*
=
1.9
x
10-14
C)
simila
o he
o de
o
magni ude
es i-
ma ed
by
acking agglome a e ajec o ies.
The
model
p edic ion
is
howe e qui e sensi i e
o
he
agglome a e
cha ge. Conside able de ia ion om he da a
is
ob ained
o o he cha ge alues
o
same o de
o
magni ude.
This
p e en s
us
om
a
conclusi e s a emen
on
he
model
alidi y. Mo eo e , he ole
o
collisions
on
deagglome -
a ion
is no
conside ed
by
he model.
ACKNOWLEDGMENTS
We acknowledge Spanish Go e nmen Agency Minis e-
io
de
Ciencia
y
Tecnologia (con ac FIS2006-03645)
and
Jun a
de
Andalucia (con ac FQM 421).
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