Three-dimensional computational fluid dynamics simulations are performed for the flow of air through microfibrous materials for void fractions of 0.41 and 0.47 and face velocities ranging between 0.04ms and 1.29ms. The microfibrous materials consist of activated carbon powder with diameters of 137×106m entrapped in a matrix of cylindrical fibers with diameters of 8×106m. These sintered microfibrous materials are a new class of patented materials with properties that are advantageous compared to traditional packed beds or monoliths. Microfibrous materials have demonstrated enhanced heat and mass transfer compared to packed beds of particles of similar dimensions. In this paper, the simulations are used to predict the pressure drop per unit length through the materials and to analyze the details of the flow that are difficult to interrogate experimentally. Various geometric approximations are employed in order to allow the simulations to be performed in an efficient manner. The Knudsen number, defined as the ratio of the mean free path between molecular collisions to the fiber diameter, is 0.011; thus, velocity-slip boundary conditions are employed and shown to have only a minor effect on the pressure drop predictions. Significant effort is made to estimate numerical errors associated with the discretization process, and these errors are shown to be negligible (less than 3%). The computational predictions for pressure drop are compared to available experimental data as well as to two theory-based correlations: Ergun’s equation and the porous media permeability equation. The agreement between the simulations and the experiments is within 30% and is reasonable considering the significant geometric approximations employed. The errors in the simulations and correlations with respect to experimental data exhibit the same trend with face velocity for both void fractions. This consistent trend suggests the presence of experimental bias errors that correlate with the face velocity. The simulations generally underpredict the experimental pressure drop for the low void fraction case and overpredict the experimental pressure drop for the high void fraction case.

1.
Novochinskii
,
I. I.
,
Song
,
C.
,
Ma
,
X.
,
Liu
,
X.
,
Shore
,
L.
,
Lampert
,
J.
,
Farrauto
,
R. J.
, 2004, “
Low Temperature H2S Removal From Steam-Containing Gas Mixtures With ZnO for Fuel Cell Application. 1. ZnO Particles and Extrudates
,”
Energy Fuels
0887-0624,
18
, pp.
576
583
.
2.
Song
,
C. S.
, and
Ma
,
X. L.
, 2004, “
Ultra-deep Desulfurization of Liquid Hydrocarbon Fuels: Chemistry and Process
,”
International Journal of Green Energy
,
1
(
2
), pp.
167
191
.
3.
Cahela
,
D. R.
,
Chang
,
B. K.
,
Karanjikar
,
M.
,
Luna
,
E. A.
, and
Tatarchuk
,
B. J.
, 2004, “
Microfibrous and Micro-Structured Adsorbents and Catalysts Media: Enhancement in Effectiveness Caused by Static Mixing
,”
AIChE Annual Meeting Conference Proceedings
,
Austin, TX
.
4.
Lu
,
Y.
,
Sathitsuksanoh
,
N.
,
Yang
,
H. Y.
,
Chang
,
B. K.
,
Queen
,
A. P.
, and
Tatarchuk
,
B. J.
, 2005, “
Microfibrous Entrapped ZnO-Supported Srbent or High Contacting Efficiency H2S Removal From Reformate Streams in PEMFC Applications
,”
Microreactor Technology and Process Intensification
(
ACS Symposium Series
),
Y.
Wang
and
J. D.
Holladay
, eds.,
American Chemical Society
,
Washington DC
, Vol.
914
, pp.
406
422
.
5.
Chang
,
B. K.
,
Lu
,
Y.
, and
Tatarchuk
,
B. J.
, 2006, “
Microfibrous Entrapment of Small Catalyst or Sorbent Particulates for High Contacting Efficiency Removal of Trace Contaminants Including CO and H2S From Practical Reformates for PEM H2-O2 Fuel Cells
,”
Chem. Eng. J.
0300-9467,
115
, pp.
195
202
.
6.
Lu
,
Y.
, and
Tatarchuk
,
B. J.
, 2003, “
Microfibrous Entrapped Supported-Zno Sorbents With High Contacting Efficiency for Trace H2S Removal in PEMFV Applications
,”
Abstracts of Papers, 226th ACS National Meeting
,
New York
, Sept. 7–11.
7.
Karniadakis
,
G.
,
Beskok
,
A.
, and
Aluru
,
N.
, 2005,
Microflows and Nanoflows: Fundamentals and Simulation
2nd ed.,
Springer-Verlag
,
New York
, Chaps. 1–4.
8.
Barber
,
R. W.
,
Emerson
,
D. R.
,
Gu
,
X. J.
, and
Zhang
,
Y.
, 2006, “
Rarefied Gas Dynamics in Micro-Devices
,” URL: http://www.cse.clrc.ac.uk/ceg/c4m/rgd.shtmlURL: http://www.cse.clrc.ac.uk/ceg/c4m/rgd.shtml.
9.
Panton
,
R. L.
, 1996,
Incompressible Flow
, 2nd ed.,
Wiley
,
New York
, pp.
359
401
.
10.
Versteeg
,
H. K.
, and
Malalasekera
,
W.
, 1996,
An Introduction to Computational Fluid Dynamics
,
Addison-Wesley
,
Reading, MA
.
11.
Reddy
,
J. N.
, and
Gartling
,
D. K.
, 1994,
The Finite Element Method in Heat Transfer and Fluid Dynamics
,
CRC
,
Boca Raton, FL
.
12.
Karniadakis
,
G. E.
, and
Sherwin
,
S. J.
, 1999,
Spectral/HP Element Methods for CFD
,
Oxford University Press
,
New York
.
13.
Beskok
,
A.
, 1996, “
Simulations and Models for Gas Flows in Microgeometries
,” Ph.D. thesis, Princeton University.
14.
Beskok
,
A.
, and
Karniadakis
,
G. E.
, 1999, “
A Model for Flows in Channels, Pipes, and Ducts at Micro and Nano Scales
,”
Microscale Thermophys. Eng.
1089-3954,
3
, pp.
43
77
.
15.
Hennighausen
,
K.
, 2001, “
Fluid Mechanics of Microscale Flight
,” Ph.D. thesis, University of Minnesota.
16.
Tang
,
G. H.
,
Tao
,
W. Q.
, and
He
,
L. Y.
, 2005, “
Gas Slippage Effect on Microscale Porous Flow using the Lattice Boltzmann Method
,”
Phys. Rev. E
1063-651X,
72
(
5
),
056301
.
17.
Papathanasiou
,
T. D.
,
Markicevic
,
B.
, and
Dendy
,
E. D.
, 1990, “
A Computational Evaluation of the Ergun and Forchheimer Equations for Fibrous Porous Media
,”
Phys. Fluids
1070-6631,
13
(
10
), pp.
2795
2805
.
18.
Andrade
,
J. S.
,
Costa
,
U. M. S.
,
Almeida
,
M. P.
,
Makse
,
H. A.
, and
Stanley
,
H. E.
, 1999, “
Inertial Effect on Fluid Flow Through Disordered Porous Media
,”
Phys. Rev. Lett.
0031-9007,
82
(
26
), pp.
5249
5252
.
19.
Hicks
,
R. E.
, 1970, “
Pressure Drop in Packed Beds of Spheres
,”
Ind. Eng. Chem. Fundam.
0196-4313,
9
(
3
), pp.
500
502
.
20.
Harris
,
D. K.
,
Cahela
,
D. C.
, and
Tatarchuk
,
B. J.
, 2001 “
Wet Lay-up and Sintering of Metal—Containing Microfibrous Composites for Chemical Processing Opportunities
,”
Composites, Part A
1359-835X,
32
, pp.
1117
1126
.
21.
Cahela
,
D. R.
,
Tatarchuk
,
B. J.
, 2001, “
Permeability of Sintered Microfibrous Composites for Heterogeneous Catalysis and Other Chemical Processing Opportunities
,”
Catal. Today
0920-5861,
69
, pp.
33
39
.
22.
2005, FLUENT 6.2 User’s Guide, Vols.
1–3
.
23.
McNenly
,
M. J.
,
Gallis
,
M. A.
, and
Boyd
,
I. D.
, 2003, “
Slip Model Performance for Micro-scale Gas Flows
,”
36th AIAA Thermophysics Conference
, Paper No. AIAA-2003–4050.
24.
Anderson
,
J. D.
, Jr.
, 1995,
Computational Fluid Dynamics: The Basics with Applications
,
McGraw-Hill
,
New York
, pp.
253
264
.
25.
Roy
,
C. J.
, 2005, “
Review of Code and Solution Verification Procedures for Computational Simulation
,”
J. Comput. Phys.
0021-9991,
205
(
1
), pp.
131
156
.
26.
Roache
,
P. J.
, 1998,
Fundamentals of Computational Fluid Dynamics
,
Hermosa
, NM, pp.
487
500
.
27.
Ergun
,
S.
, 1952, “
Fluid Flow Through Packed Columns
,”
Chem. Eng. Prog.
0360-7275,
48
(
2
), pp.
89
94
.
28.
Middleman
,
S.
, 1998,
An Introduction to Fluid Dynamics: Principles of Analysis and Design
. 2nd ed.,
Wiley
,
New York
, pp.
411
421
.
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