non-newtonian
TRANSCRIPT
Non-Newtonian Fluids
Non-Newtonian Flow
Goals• Describe key differences between a Newtonian
and non-Newtonian fluid• Identify examples of Bingham plastics (BP) and
power law (PL) fluids• Write basic equations describing shear stress
and velocities of non-Newtonian fluids• Calculate frictional losses in a non-Newtonian
flow system
Non-Newtonian FluidsNewtonian Fluid
dr
duzrz
Non-Newtonian Fluid
dr
duzrz
η is the apparent viscosity and is not constant for non-Newtonian fluids.
η - Apparent ViscosityThe shear rate dependence of η categorizes
non-Newtonian fluids into several types.
Power Law Fluids: Pseudoplastic – η (viscosity) decreases as shear rate
increases (shear rate thinning)
Dilatant – η (viscosity) increases as shear rate increases (shear rate thickening)
Bingham Plastics:
η depends on a critical shear stress (0) and then becomes constant
Non-Newtonian Fluids
Newtonian
Bingham Plastic:
Pseudoplastic:
Dilatant:
sludge, paint, blood, ketchup
latex, paper pulp, clay solns.
quicksand
Modeling Power Law FluidsOswald - de Waele
dr
du
dr
duK
dr
duK z
n
z
n
zrz
1
where:K = flow consistency indexn = flow behavior index
Note: Most non-Newtonian fluids are pseudoplastic n<1.
eff
Modeling Bingham Plastics
0 rz 0dr
duz Rigid
0 rz 0 dr
duzrz
Frictional Losses Non-Newtonian Fluids
Recall:
Applies to any type of fluid under any flow conditions
24
2V
D
Lfh f
Laminar Flow
Mechanical Energy Balance
WhzgVp
fˆ
2
2
0 0 0
MEB (contd)
Combining:
p
VL
Df
2
2
4
1
Momentum Balance
gw FFSpSpVVm 22111122 0 0
prrL rz 22
rzr
Lp 2
Power Law Fluidn
zrz dr
duK
nn
z rKL
p
dr
du 11
2
1
Rr 0zuBoundary Condition
Velocity Profile of Power Law FluidCircular Conduit
n
n
n
nn
z rRn
n
KL
pu
111
12
1
Upon Integration and Applying BC
Power Law (contd)
Need bulk average velocity
drruR
dSuS
V zS
2
112
n
nn
Rn
n
KL
pV
11
132
1
p
VL
Df
2
2
4
1
Power Law Results (Laminar Flow)
↑ Hagen-Poiseuille (laminar Flow) for Power Law Fluid ↑
Recall
1
2 132
n
nn
n
D
VLKnn
p
Laminar Friction FactorPower Law Fluid
Define a Power Law Reynolds Number
K
DV
n
nRe
nnnn
PL
23
132
PLRef
16
nn
nn
DV
Knn
f
2
1 132
Turbulent Flow
2,
133
35242100Re
n
nncriticalPL
Power Law Fluid Example
A coal slurry is to be transported by horizontal pipeline. It has been determined that the slurry may be described by the power law model with a flow index of 0.4, an apparent viscosity of 50 cP at a shear rate of 100 /s, and a density of 90 lb/ft3. What horsepower would be required to pump the slurry at a rate of 900 GPM through an 8 in. Schedule 40 pipe that is 50 miles long ?
P = 1atmP = 1atm
L = 50 miles
7273792.0
759.11442202.0
1)4.0(3
4.02
759.1281.323474.0
1
60
min1
48.7
31
min
900
792.0100
50'
'
6.1
6.1
3
4.04.0
4.03
~
6.1
4.01
'
smkg
sm
mkg
mRE
s
m
ft
m
ftsgal
ftgalV
sm
kg
scPK
r
V
r
VK
N
app
n
HpkWsm
skg
Power
s
kg
m
kgm
s
mm
s
msm
m
mhW
Figf
V
D
LfhW
hg
Zg
g
VPW
fp
fp
fcc
p
13001.9701000
845,119.81
9.8114420323.0759.1
845,112
760.1
202.0
804600048.04
11.50048.0
24
2
2
2
32
2
2
2
2
2
Bingham Plastics
Bingham plastics exhibit Newtonian behavior after the shear stress exceeds o. For flow in circular conduits Bingham plastics behave in an interesting fashion.
Bingham Plastics
Unsheared Core
crr 20
2 cc
cz rRr
uu
crr
01
2
R
rrRu rzz
Sheared Annular Region
Laminar Bingham Plastic Flow
73
4
Re3Re61
Re
16
BPBPBP f
HeHef
20
2
D
He
VD
BPRe
Hedstrom Number
(Non-linear)
Turbulent Bingham Plastic Flow
Hex
BPa
ea
f5109.2
193.0
146.01378.1
Re10
Bingham Plastic ExampleDrilling mud has to be pumped down into an oil well that is 8000 ft deep. The mud is to be pumped at a rate of 50 GPM to the bottom of the well and back to the surface through a pipe having an effective diameter of 4 in. The pressure at the bottom of the well is 4500 psi. What pump head is required to do this ? The drilling mud has the properties of a Bingham plastic with a yield stress of 100 dyn/cm2, a limiting (plastic) viscosity of 35 cP, and a density of 1.2 g/cm3.
P = 4500 psi
P = 14.7 psi
L = 8000 ft
cms
g
cm
dyn
sftlb
ftlb
sft
ft
N
sft
lb
cP
sftlb
cP
ft
lb
ft
lb
s
ft
ftgal
ft
s
galV
ftAreaftftD
o
m
m
RE
m
m
mm
22
33
2
3
2
100100
13550235.0
388.74276.13333.0
0235.04107197.6
35
88.744.622.1
276.10873.0
1
48.760
min
min50
0873.03333.012
4
m
f
f
m
f
m
f
p
fcc
p
lb
lbftWp
slblbmft
sft
ft
ft
lb
lbft
ftlb
ftin
in
lb
W
hg
Zg
g
VPW
f
cmsg
cmsg
cmg
incm
in
N HE
96533980008626
2.322
276.1
3333.0
800014.048000
88.74
1447.144500
2
14.0
1001.1
35.0
1002.1
54.24
2
2
3
2
2
2
2
52
23
2