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J. Non-Newtonian Fluid Mech. 165 (2010) 14941504
Contents lists available at ScienceDirect
Journal of Non-Newtonian Fluid Mechanics
journa l homepage: www.e lsev ier .co
Axial C s t
Yu-QuanDepartment of
a r t i c l
Article history:Received 25 JuReceived in reAccepted 29 Ju
Keywords:Bingham uidAxial CouetteConcentric annAnalytical solu
uilleof onmisdepennd the numa mat
1. Introdu
Flows ofby the forcare frequencially in oilwuids exhibit is viscoplasticity, which indicates that the strain ratewill retain zero until a yield stress 0 is reached. Therefore, studiesof annular ows utilizing a variety of viscoplasticmodels have beencarried out during the last several decades.
Some relatively simple models of yield stress uids, which arealso widelyCasson
=
1/20 +
HerschelB
=(
0
and Roberts
=
1/n0
CorresponE-mail add
ma0 =lytich simhavely an
Bird et al. [1], includingowsdrivenbya torque applied to theoutercylinder, an axial motion of the inner cylinder or a constant pres-sure gradient in a concentric annulus. Fordham et al. [2] developeda general method for calculating viscoplastic ows in concentricannuli of arbitrary radius ratio, which is worked for models (1a),
0377-0257/$ doi:10.1016/j.applied in researches, are presented here. They are the
(0)1/2
2
(1a)
ulkley
n1 + 0)
(1b)
onStiff models
(n1)/n +
(0)1/n
n
(1c)
ding author. Tel.: +86 10 6277 1654; fax: +86 10 6278 1824.ress: [email protected] (Y.-Q. Liu).
(1b) and (1c) mentioned above.To the best of our knowledge, analytical solutions possibly
derived for Binghamuidowthrough concentric annuli are nearlyall under the following three conditions:
Rotation of the inner/outer cylinder. Axial moving of the inner cylinder. An axial pressure gradient.
Notice that what Bird et al. [1] reviewed referred to individ-ual instances of the conditions above. From then on, solutions forcombinations of these were found in succession. Bittleston andHassager [3] combined the rotation of the inner cylinder and thepressure gradient together, and considered ow of Bingham uidsboth in a slot and in an annulus. Filip and David [4] investigatedRobertsonStiff uid ow produced by the inner cylinder movingalong its axis and by the pressure gradient imposed in the axialdirection, which is supposed to cover the results for Bingham andpower-law uids. Moreover, Peng and Zhu [5] worked on Bing-hamuids in spiral Couette ow,whichmeant TaylorCouette ow
see front matter 2010 Elsevier B.V. All rights reserved.jnnfm.2010.07.013ouettePoiseuille ow of Bingham uid
Liu , Ke-Qin ZhuEngineering Mechanics, Tsinghua University, Beijing 100084, China
e i n f o
ly 2009vised form 21 June 2010ly 2010
sPoiseuille owulitions
a b s t r a c t
In this paper, the axial CouettePoiseAnalytical solutions of different typestwonew types of ow,which have beedifferent forms of the velocity prolethe Bingham, axial Couette numbers ain the parameter plane of axial Couettow regimes are analyzed from both
ction
non-Newtonian uids through annuli, induced eithering pressure gradient or by the motion of boundaries,tly encountered in various industrial applications, espe-ell drilling. Oneof themost important properties these
Onen=1 or
Anathrougannulithe earm/locate / jnnfm
hrough concentric annuli
ow of Bingham uids through concentric annuli is studied.w are derived. Compared to previous studies, we emphasizesed previously, are found in our results. Hence, there are eightding on values of three dimensionless parameters, which aree radius ratio. Distributions of these eight forms are speciedber vs. Bingham number for various radius ratios. These newhematical and physical perspective.
2010 Elsevier B.V. All rights reserved.
y obtain the Bingham or power-law model by setting0 in (1b) and (1c), respectively.al or semi-analytical solutions of viscoplastic uid owsple geometries, such as pipes, slots and concentricbeen quite thoroughly studied and published. Some ofalytical solutions for Bingham uids were reviewed by
Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504 1495
between two concentric rotating cylinders with the sliding of theinner cylinder.
Due to the different position of the plug zone, different typesof the velocity prole may be observed. Assuming the maximumvelocity ofas the chardivide the pBingham none specicformed thisit more preplane Coueporous para
Neverthfor the axiand they dow upon tfor their seRobertsoncan be recofully analytWe have doand Chen aDavid [4], Tthe same af
As we whave somedresults origto errors inthere are twwhich the p
The rest2, a brief inboundary ccorrespondour results,conclusion
2. Geomet
Considehamplasticand R2 as tder moves wstationary.imposed inin Fig. 1.
The goveequations
U = 0
U
t+ (U
where , Uvector, precylindrical
U = Urer +
where Ur, Uazimuthal aof these thr
. Sch
conbelo
0 + = 0 anhile
ijiiji
thermsion
+ (U)T (6)ording to the axisymmetric property of the problem, wee, as Filip and David [4] did, that the only non-zero veloc-ponent is Uz, which is a function only of r. So the continuity
on and the momentum equations for Ur and U are naturallyd, while the momentum equation in the axial direction isd to the following one
= dpdz
(7)
ere rz = rz (r) is the only non-zero component of . Then (4)ced to
0 +0dUz/dr
)dUzdr
|rz | > 0
dUzdr
= 0 |rz | 0
(8)
boundary conditions include the non-slip conditions at the
1= Uc (9a)
2= 0 (9b)Poiseuille ow for Newtonian uids in a circular pipeacteristic velocity for non-dimensionalization, one canarameter plane of rotational/axial Couette number vs.umber into a couple of regions, in any of which onlytype of ow appears. Bittleston and Hassager [3] per-task, while Tsangaris et al. [6] and Chen and Zhu [7] didcisely in their respective work, which considered thettePoiseuille ow of Bingham uids with two equallyllel walls.eless, Filip and David [4] only gave out the restrictionsal Couette number except for the Bingham number,id not outline the distribution of different types ofhe parameter plane. Frankly, this is totally understoodmi-analytical results caused by the complexity of theStiff model. But as we mentioned, the Bingham modelvered by setting n=1 in (1c), which makes their resultsical. Then it is possible to map out the parameter space.ne so, and found it similar to that in Tsangaris et al. [6]nd Zhu [7]. Actually, ow cases presented in Filip andsangaris et al. [6] and Chen and Zhu [7] are essentiallyter comparison.ill show in this paper, ow cases in annular channelsistinctions fromthose inplane channels, andextendinginated from Filip and David [4] to Bingham uids leadsthe parameter plane. More importantly, we stress thato new types of ow, missed in Filip and David [4], witharameter plane is nally able to be fullled.of this paper will be organized as follows. In Sectiontroduction to the geometry, governing equations andonditions is given. In Section 3, the analytical solutionsing todifferent typesofowarederived.Wewill discussand compare them with former works in Section 4. Awill be reached in Section 5.
ry, governing equations and boundary conditions
r the steady, laminar and incompressible ow of a Bing-uid between two innite concentric cylinders with R1he inner and outer radii, respectively. The inner cylin-ith a constant velocity Uc while the outer one remains
Also, a constant negative pressure gradient dp/dz 0
0(4)
d represent the deviatoric stress and strain rate ten-their second invariants and are
j/2
j/2(5)
ore, 0 is the yield stress and 0 is the viscosity. Theof is
1496 Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504
together with two continuity conditions for the velocity compo-nents and stress across the yield surface
Uzr=y = Up (10a)
dUzdr
r=y
=
where y is tof the plug
For owmotion ofmomentum
( n)
where =mal to . Sthis problemconsidered
So far, tdimensiona
r = rR2
Uz
where U0 =HagenPoisthe sake ofless forms o
d(rrz)r dr
=
the constitu
rz =(
1 +
d
d
and the bou
Uzr= = Co
Uzr=1 = 0
In thisters: the rB= 0R2/0can be eithe
3. Analytic
No mattrz from (12
rz = r + C
whereC is auid has yione shear of Uz would
Uz = 12 r2
with an extNow we
3.1. Cases corresponding to those in Filip and David [4]
In this part, all ve cases are already studied in Filip and David[4], but they only gave out the restrictions for the axial Couette
r exte reouetts in tay b
Casewi
2.his cylinderfacform
12
Up
12
lyinyiel
or sebe ansion
= Br de
Co +r20 l
r20 l
hichlowin
r2(r
tionsordinould
1 reove
(2r2
ce, a
o
Cor2
Cor2
Casewi
3.his cathe pe ha0 (10b)
he position of the yield surface, and Up is the velocityzone.with a plug zone detached from both cylinders, the
the plug zone, , is determined by conservation of, which is represented by Frigaard et al. [8]
ds =
(
dU
dt
)d (10c)
p+ , is the unit tensor, and n is the outward nor-ince no rotational motions of the plug zone occur in, the conservation of angular momentum will not be
here.he problem is established mathematically. To non-lize it, the following dimensionless variables are used:
= UzU0
rz = rzR20U0(11)
(R22/20)dp/dz is twice of the max velocity ofeuille ow. From here on, the tildes are eliminated forconvenience. Therefore, we can obtain the dimension-f the momentum equation (7)
2 (12)
tive equations (8)
BdUz/dr)
dUzdr
|rz | > B
Uzr
= 0 |rz | B(13)
ndary condition (9a) and (9b)
(14a)
(14b)
problem we have three dimensionless parame-adius ratio =R1/R2 (0, 1), the Bingham numberU0 0, and the axial Couette number Co=Uc/U0, whichr a positive number or a negative one.
al solutions
er what the velocity prole is like, a general solution of) exists:
r(15)
n integral constant. According to (13), once theBinghamelded, the strain rate dUz/dr would not change sign inow zone. Substituting (15) into (13), a general solutionbe
+ C ln r B sgn(
dUzdr
)r + D (16)
ra integral constant D.analyze various cases of the velocity prole in detail.
numbeaccuraaxial Cregionow, m
3.1.1.Flow
in Fig.In t
outer cthe int
The
Uz =
Appat twotions fshoulda dime
r2 r1Afte
Uz =
In wthe fol
2Co + 2
RestricAcc
case sh
0 B Mo
dCo
dr2=
Hen
Co2 Cwhere
Co2 =
Co3 =
3.1.2.Flow
in Fig.In t
whiler= r1, wcept for the Bingham number. We will determine thestrictions of every individual case concerning both theenumberCo and theBinghamnumberB, so that speciche parameter plane CoB, related to specic types ofe recognized.
Ith a plug zone detached from both cylinders, as shown
ase, two shear ow zones are attached to the inner anders respectively with the plug zone between them. Ate r= r1 and r= r2, we have rz =B, where r1 r2 1.of the velocity prole is
r2 + C1 ln r Br + C2 ( r r1)(r1 r r2)
r2 + C3 ln r + Br + C4 (r2 r 1)(17)
g the conditions on both boundaries (14a) and (14b) andd surfaces (10a) and (10b) leads to a set of six equa-ven unknowns: C1, C2, C3, C4, r1, r2 and Up. Eq. (10c)dded due to the equilibrium of the plug zone, which inless form is
(18)
tailed analyses, we nd the velocity prole is
r20 lnr
B(r ) 1
2(r2 2) ( r r1)
n r2 B(1 r2) +12(1 r22) (r1 r r2)
n r B(1 r) + 12(1 r2) (r2 r 1)
(19)
r20 = r1r2 is the position where rz =0, and r2 satisesg implicit expression:
2 B) lnr2 Br2
+ 2B(1 r2) 1 + (B + )2 = 0 (20)
g to r1 r2 1 and (18), the rst restriction of thisbe
(21)
r, we have +B r2 1, and can obtain from (20) that
B) ln r2r2 B
0 (22)
nother restriction for Co should be
Co3 (23)
=1 = (1 B) ln
1 B +12[1 ( + B)2] (24)
=+B = ( + B) ln( + B) +12[(1 B)2 2] (25)
IIth a plug zone attached to the outer cylinder, as shown
se, the shear ow zone is attached to the inner cylinderlug zone is attached to the outer one. At the interfaceve rz =B, where r1 1.
Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504 1497
Fig. 2. Schematic of case I: ow with a plug zone detache
The form of the velocity prole is
Uz ={
12
r2 + C5 ln r Br + C6 ( r r1)0 (r1 r 1)
(26)
Fig. 3. Schem
Applyinyield surfacthree unkn
After de
Uz ={
Co +0
satiwith r1atic of case II: ow with a plug zone attached to the outer cylinder.
2Co + 2r1(r
RestrictionsThe dist
rz = r +
In thiswith r10B1 that
dCo
dr1= (2r
So the o{Co1 CoCo1 Co
where
Co1 = Cor1
Notice tsatised, wd from both cylinders.
g the conditions on the inner boundary (14a) and at thee (10a) and (10b) leads to a set of three equations forowns: C5, C6 and r1.tailed analyses, we nd the velocity prole is
r1(r1 + B) lnr
B(r ) 1
2(r2 2) ( r r1)
(r1 r 1)(27)
sfying the following implicit expression:1 + B) lnr1
2B(r1 ) (r21 2) = 0 (28)
ribution of rz in the annulus is
r1(r1 + B)r
(29)
case we need |rz |r=1| B. Substituting (29) into it1, we get r1 1B, which means 1B r1 1 when, or r1 1 when B>1 . We can obtain from (28)
1 + B) lnr1
0 (30)
nly restriction of this case for Co is
Co2 (0 B 1 ) 0 (B > 1 ) (31)
=1 = (ln + 1 )B +[ln + 1
2(1 2)
](32)
hat for any B0, case II would appear as long as (31) ishich indicates no extra restriction for B in case II.
1498 Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504
Fig. 4. Schema
3.1.3. CaseFlow wit
in Fig. 4.In this ca
while the pr= r2, we ha
The form
Uz ={
Co
12
Applyingyield surfacthree unkno
After de
Uz ={
Co
r2(r
with r2 sati
2Co 2r2(rRestrictions
The distr
rz = r + r
In this(36) into itensure r2 e[B , B + case:
0 B 1 +
chem
rwa,1] aed fo
13tic of case III: ow with a plug zone attached to the inner cylinder.
IIIh a plug zone attached to the inner cylinder, as shown
se, the shear ow zone is attached to the outer cylinderlug zone is attached to the inner one. At the interfaceve rz =B, where r2 1.
Fig. 5. S
Afteand [identi
0 < of the velocity prole is
( r r2)r2 + C7 ln r + Br + C8 (r2 r 1)
(33)
the conditions on the outer boundary (14b) and at thee (10a) and (10b) leads to a set of three equations forwns: C7, C8 and r2.
tailed analyses, we nd the velocity prole is
( r r2)2 B) ln r B(1 r) +
12(1 r2) (r2 r 1)
(34)
sfying the following implicit expression:
2 B) ln r2 + 2B(1 r2) (1 r22) = 0 (35)
ibution of rz in the annulus is
2(r2 B)r
(36)
case,rz |r= B should be satised. Substituting
with r2 1, we have B r2 B+ . In order toxists, there must be an intersection between intervals] and [,1], which induces the restriction for B in this
(37)
13
< < 1
We can
dCo
dr2= (2r2
which is vaCo:
0 < 13
13
< < 1
where
Co4 = Cor2
Co5 = Cor2
3.1.4. CaseShear o
in Fig. 5.In this ca
is dependenthat in planatic of case IV: shear ow dominant throughout the annulus (Co
Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504 1499
Fig. 6. Schem
The form
Uz = 12 r2
Applyingleads to a sedetailed an
Uz =[Co
RestrictionsThe dist
rz = r + C
Case IV d
Co B(1
As ln 0), as shown
se, theplug zonedoesnot exist, either. In Tsangaris et al.n and Zhu [7], cases IV and V are organized together andas Pure shear ow. Here we split them apart becauseof the restriction for Co, which will be shown below.of the velocity prole is
+ C11 ln r + Br + C12 (48)
cases. Howparameterinto three r
(1) Co5 (2) 0 Co(3) 0 Co
Apparenarea, whichin annular c
3.2.1. CaseAnother
shown in FiIn this c
outer cylindthe interfacPay attentiotrated in thand dUz/dr
The form
Uz =
12
Up
12B(1 ) 12(1 2) ln r
ln B(1 r) + 1
2(1 r2) (49)
ribution of rz in the annulus is
Co + B(1 ) 1/2(1 2)r ln
(50)
emands rz B throughout r1, which gives) + 1/2(1 2) + r(r B) ln (51)imum of the right side of (51) depends on the valuef 0B2, the maximum is reached when r= , result-
(52a)
2, the maximum is reached when r=B/2, resulting in(52b)
>2, the maximum is reached when r=1, resulting in
(52c)
) + 12(1 2) B
2
4ln (53)
+ 1 )B +[ln + 1
2(1 2)
](54)
ses discovered by us
ouettePoiseuille owof Binghamuids in plane chan-es of ow consist of the ve cases discussed above andlug ow case, where no ow actually occurs due to thebetween the yield stress and the applied pressure gra-
he parameter plane CoB is fully lled with these sixever, for that in annular channels, a blank area in theplane CoB remains to be identied, which is dividedegions:
Co Co6 2 B 1 + Co6 1 + B 2 Co7 B 2tly none of the cases given above can occupy this blankimplies an essential requirement for new types of owhannels besides those already presented.
VIowwith a plug zone detached from both cylinders, asg. 7.ase, two shear ow zones are attached to the inner anders respectively with the plug zone between them. Ate r= r1 and r= r2, we have rz =B, where r1 r2 1.n to the differences between case VI and case I concen-e inner shear ow zone, where dUz/dr < 0 in case VI>0 in case I.of the velocity prole is
r2 + C13 ln r + Br + C14 ( r r1)(r1 r r2)
r2 + C15 ln r + Br + C16 (r2 r 1)(55)
1500 Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504
Fig. 7. Schemcylinders.
Applyingat two yieldfor seven uadded duesionless for
r1 + r2 = BAfter de
Uz =
Co r1r1
with r2 sati
2Co + 2r2(r
RestrictionsAccordin
case should
2 B 2Consequ
r1 B 1 rMoreove
dCo
dr2= (r1
chem.
ce, a
Co Coatic of case VI: another ow with a plug zone detached from both
the conditions on both boundaries (14a) and (14b) andsurfaces (10a) and (10b) leads to a set of six equationsnknowns: C13, C14, C15, C16, r1, r2 and Up. Eq. (10c) isto the equilibrium of the plug zone, which in a dimen-
Fig. 8. Scylinder
Hen{Co5Co8m is
(56)
tailed analyses, we nd the velocity prole is
r1r2 lnr
+ B(r ) 1
2(r2 2) ( r r1)
r2 ln r2 B(1 r2) +12(1 r22) (r1 r r2)
r2 ln r B(1 r) +12(1 r2) (r2 r 1)
(57)
sfying the following implicit expression:
2 B) lnB r2r2
1 + (B )2 + 2B(1 r2) = 0 (58)
g to r1 r2 1 and (56), the rst restriction of thisbe
(59)
ently, the value ranges for r1 and r2 are
B
2 r2 B (2 B 1 + )
1 B
2 r2 1 (1 + < B 2)
(60)
r, we can obtain form (58) that
r2) lnr1r2
0 (61)
where
Co8 = Cor2
3.2.2. CaseAnother
shown in FiAs we ca
with case Vbelong to o
In this cawhile the pr= r1, we haences betwow zone, w
The form
Uz ={
12
0
Applyinyield surfacthree unkn
After de
Uz ={
Co +0atic of case VII: another ow with a plug zone attached to the outer
nother restriction for Co should be
Co6 (2 B 1 + ) Co6 (1 + B 2) (62)=1 = (B 1) lnB 1
+ 1
2[1 (B )2] (63)
VIIowwith a plug zone attached to the outer cylinder, asg. 8.n see, blank regions (1) and part of (2) have been lledI.Wewill demonstrate that the rest of the blank regionsnly one new case.se, the shear ow zone is attached to the inner cylinderlug zone is attached to the outer one. At the interfaceve rz =B, where r1 1. Pay attention to the differ-een case VII and case II concentrated in the inner shearhere dUz/dr0 in case II.of the velocity prole is
r2 + C17 ln r + Br + C18 ( r r1)(r1 r 1)
(64)
g the conditions on the inner boundary (14a) and at thee (10a) and (10b) leads to a set of three equations forowns: C17, C18 and r1.tailed analyses, we nd the velocity prole is
r1(r1 B) lnr
+ B(r ) 1
2(r2 2) ( r r1)
(r1 r 1)(65)
Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504 1501
with r1 satisfying the following implicit expression:
2Co + 2r1(r1 B) lnr1
+ 2B(r1 ) (r21 2) = 0 (66)
RestrictionsThe dist
rz = r + r
In this c r1 1, wthis case:
B 1 + Afterwa
follows:{ r1 B r1 1
We can
dCo
dr1= (2r
which is va{0 Co 0 Co
So far, th
3.2.3. CasePure pluIn this c
In fact, it hlimit situatiwhich reve
4. Results
4.1. Divisio
For the aconcentric alytically. Wwith corres
Co1 = (ln
Co2 = (1
Co3 = ( +Co4 = ( l
Co5 = (B
Co6 = B2
4Co7 = (ln
Co8 = (B
Accordinobserved wDue to distIII, we illuswith B [0Figs. 9(a) a
Fig. 9. Phase diagram with =0.25: (a) full map and (b) upper half.
cation points of at least three ow cases, from the left corre-ng consecutively to B=2, B=1 , B=1+ , B=2 in Fig. 9(b)1 , B=2, B=1+ , B=2 in Fig. 10(b).
ce the radius ratio appears in three out of four demarca-ints, it has signicant effects upon regions of ow cases. Asases, regions of cases I, VI and VII become narrower in width. 9(b) and 10(b), for the value ranges for B are [0,1 ],and, [1 + ,2.5] respectively. More importantly, deter-whether cases I and VI have an intersection between theiranges for B. When [0, 1/3], an intersection B [2,1 ]and cases I and VI are possible to occur under same B, asrestrictions for Co are satised. When [1/3, 1], no such
menon exists.setting =0.9, we illustrate the variation of the phase dia-hen 1, as shown in Fig. 11. It seems that cases I and
greatly depressed. Considering the longitudinal coordinate,er, all cases are greatly depressed except for cases IV and V.
mparison to results of Filip and David [4]
ip and David [4] studied the axial CouettePoiseuille ow ofsonStiff uids (1c), which is thought to include the resultsgham uids, as (1c) reduces to (4) by setting n=1. Natu-comparison between our results and theirs is supposed to
formed.ribution of rz in the annulus is
1(r1 B)r
(67)
ase we need |rz |r=1| B. Substituting (67) into it withe get r1 B1, which induces the restriction for B in
(68)
rds, the value range for r1 is identied for different B as
1 (1 + B 2)(B > 2)
(69)
obtain from (66) that
1 B) lnr1
0 (70)
lid for (69), and leads to the restriction for Co:
Co8 (1 + B 2)Co7 (B > 2)
(71)
e parameter plane CoB has been lled up.
VIIIg owase, the Bingham uid stays stationary in the annulus.as been involved in all the cases except IV and V as aon. As long as Co /= 0, shear ow will absolutely occur,als Co=0 and B1 as the restrictions of this case.
and discussion
n of the parameter plane
xial CouettePoiseuille ow of Bingham uids throughnnuli, all eight types of owhave been solved fully ana-e derive eight critical axial Couette numbers Co1 Co8ponding value ranges for B, which are
+ 1 )B +[ln + 1
2(1 2)
]B 0
B) ln
1 B +12[1 ( + B)2] 0 B 1
B) ln ( + B) + 12[(1 B)2 2] 0 B 1
n + 1 )B +[2 ln + 1
2(1 2)
]0 B 2
) ln (B ) + 12[(1 B)2 2] 2 B 1 +
ln B(1 ) + 12(1 2) 2 B 2
+ 1 )B +[ln + 1
2(1 2)
]B 2
1) lnB 1
+ 1
2[1 (B )2] 1 + B 2
(72)
g to (72), distributions of various ow cases areith Co1 Co8 drawn on the parameter plane CoB.inctions between [0, 1/3] and [1/3, 1] in casetrate the distributions by setting =0.25 and =0.5,2.5], as shown in Figs. 9 and 10. Red lines innd 10(a) refer to case VIII, while red circles stand for
demarspondiand B=
Sintion po increin Figs[2,2]minesvalue rexists,long aspheno
Bygram wVI arehowev
4.2. Co
FillRobertfor Binrally, abe per
1502 Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504
Fig. 10
In [4], Fider V to beis equal todependingthemovingdimensionl
T0 =20PR
=PR2K
(Apparen
between {Co =
(
Co = (
First we, their ow
(1) P > 0(2) P > 0(3) P > 0(4) P < 0(5) P < 0(6) P < 0. Phase diagram with =0.5: (a) full map and (b) upper half.
lip and David set the axial velocity of the inner cylin-positive all along, while the pressure gradient P, whichdp/dz in this paper, can be either positive or negative,on assisting or opposing the drag on the uid caused byinner cylinder. Besides the radius ratio , the other twoess parameters are dened as:
(73)
R
V
)n(74)
tly, and T0 are equal to our and B. The connectionand Co isn=1)1
P > 0n=1)1
P < 0(75)
perform some qualitative comparisons. Basing on P andcases consist of the following six ones
> cr1,2cr1,2 cr2,3 < cr2,3 > cr4,5cr4,5 cr5,6 < cr5,6
(76)
Fig.
which corrI(Co 0(2) P > 0(3) P > 0(4) P < 0(5) P < 0(6) P < 011. Phase diagram with =0.9: (a) full map; (b) upper half.
espond consecutively to our cases I (Co>0), III, V,and IV, and are essentially the same as those in plane,7]. None of them involve cases VI and VII in this paper.come to quantitative comparisons. The critical num-are
( + T0 1) T1/n0 + 1
+T0
[ ( + T0)
]1/nd
}n
( 1) T1/n0 + 1
[ ( T0)
]1/nd
}n
+ T0 1) T1/n0 + 1T0
(1 T0
)1/n
d
]n
1) T1/n0 + 1
(1 + T0
)1/n
d
]n(77)
ting (77) into (76), with n=1 and (75), we have
0 < Co < Co3Co3 Co Co4Co > Co4Co2 < Co < 0Co1 Co Co2Co < Co1
(78)
Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504 1503
where
Co3 =(
cr
Co4 =(
cr
Co2 = (
Co1 = (
ExpressiAs seen
to those foCo1 Co4 eFig. 10, (78correct in thstart to app
4.3. Analys
It is neceVI and VII illustrated i
It iswellby stress pcan be writonic decrethe stress pemergencestress protionally, altof the stresFig. 12. Illustration of analyses in Sectio
1,2
n=1)1
2,3
n=1)1
cr4,5
n=1)1
cr5,6
n=1)1
(79)
ons of Co1 Co4 are in (72).from above, when results of Filip and David [4] reducer Bingham uids, only cases IV and critical numbersmerge, with no restrictions for B at all. From Fig. 9 and) match the lower half of the parameter plane, but aree upper half only if B2. Once B>2, cases VI and VIIear, which their results cannot describe.
es of cases VI and VII
ssary to analyzemore detailly the appearances of casesrstly presented in this paper. The following analyses aren Fig. 12.known that velocity proles are essentially determinedroles. For ow in plane channels, the stress proletten as xy = y+C, which exhibits a linearly mono-asing distribution. By altering the integral constant C,role is shifted parallelly throughout, leading to theof cases IV. For that in annular channels, however, thele is rz = r+C/r, which is not linear any more. Addi-erations of C give rise to more complicated variationss prole. For C>0, the stress prole remains monotonic
decreasing,although rthen monodecreasingVI appears.decreasingnot speciallsolving pro
Physicalof the plugrz |r=r1 = means theygradient torz |r=r2 = tangent stras well as thfound in plastresses exiOn the otheleading to dit enables tcases VII an
5. Conclus
We deCouettePoannuli, whdimensionln 4.3.
leading again to the emergence of cases IV. For C
1504 Y.-Q. Liu, K.-Q. Zhu / J. Non-Newtonian Fluid Mech. 165 (2010) 14941504
B and the axial Couette number Co. Domains belonging to all formsare validated in the parameter plane CoB for various radiusratios with fully analytical boundaries.
Compared to earlier researches, we emphasize that two brand-new ow cases are discovered, and restrictions concerning thedimensionless parameters for each of the eight forms are preciselyveried. After careful comparisonwith results from Filip and David[4], we show that they missed these two ow cases, and gave outincorrect restrictions for several cases.
Finally, we explain why the two brand-new ow cases,which are impossible to appear in plane channels, emerge inannular channels both mathematically and physically. Resultsand analyses presented in this paper might be instructive forsolving ows of viscoplastic uids in annuli or other geome-tries.
Acknowledgements
This research is supportedby theNationalNatural Science Foun-dation of China under Grant No. 10772097. The nal manuscript
benets from comments and suggestions provided by two refer-ees. In particular, we are indebted to a referee whose questionshave enriched the contents of the paper.
References
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[2] E.J. Fordham, S.H. Bittleston, M.A. Tehrani, Viscoplastic ow in centered annuli,pipes and slots, Ind. Eng. Chem. Res. 30 (1991) 517524.
[3] S.H. Bittleston, O. Hassager, Flow of viscoplastic uids in a rotating concentricannulus, J. Non-Newtonian Fluid Mech. 42 (1992) 1936.
[4] P. Filip, J. David, Axial CouettePoiseuille ow of power-law viscoplastic uidsin concentric annuli, J. Petrol. Sci. Eng. 40 (2003) 111119.
[5] J. Peng, K.Q. Zhu, Linear stability of Bingham uids in spiral Couette ow, J. FluidMech. 512 (2004) 2145.
[6] S. Tsangaris, C. Nikas, G. Tsangaris, P. Neofytou, Couette owof a Binghamplasticin a channel with equally porous parallel walls, J. Non-Newtonian Fluid Mech.144 (2007) 4248.
[7] Y.L. Chen, K.Q. Zhu, CouettePoiseuille ow of Bingham uids between twoporous parallel plates with slip conditions, J. Non-Newtonian Fluid Mech. 153(2008) 111.
[8] I.A. Frigaard, S.D. Howison, I.J. Sobey, On the stability of Poiseuille ow of aBingham uid, J. Fluid Mech. 263 (1994) 133150.
Axial CouettePoiseuille flow of Bingham fluids through concentric annuliIntroductionGeometry, governing equations and boundary conditionsAnalytical solutionsCases corresponding to those in Filip and David [4]Case ICase IICase IIICase IVCase V
New cases discovered by usCase VICase VIICase VIII
Results and discussionDivision of the parameter planeComparison to results of Filip and David [4]Analyses of cases VI and VII
ConclusionAcknowledgementsReferences