“equilibrium and transport properties of small alkanes and ......1 “equilibrium and transport...
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1
“Equilibrium and Transport Properties of
Small Alkanes and Alkenes Confined in
Single-W
alled Carbon Nanotubes.”
Fernando J. A. L. Cruz, ErichA. Müller
Imperial College London
f.cruz@
imperial.ac.uk
2
1 –Introduction
1.1 -Motivation
●Separation of close boiling point mixtures (olefin/paraffin) bydistillation are energy
intensive operations.
●Adsorption can play a role in improving this scenario (molecular-level knowledge of
adsorption in confined nanospaces spaces is required).
●For small scale separations (pharmaceuticals, higher added value), nanotube-based
membranes could be good future candidates.
●Extendourexpertisefromflatsurfaces(carbonslitpores) to cilindricalgeommetries.
1.2 –Adsorbents & Methodology
●Carbonnanotubes firstidentifiedintheearly90’s [Iijima1991]: possibleapplications
range fromstoragenanomaterials (H2,CH4) andcompositesfor electronics, to separating
agentsoforganicvaporsandchemicalsensors.
●Studytheadsorptionanddiffusionbehaviouroffluids, whena bulkphaseisexposedto
direct
contact
with
single-walledcarbonnanotubes: ClassicalMolecular Dynamics
(Newton’s3rdlaw) andGrandCanonical Monte Carlosimulations.
3
2 –Single-walledcarbonnanotubes (SWCNT)
Zig-zag(8,0)
arm
chair(5,5)
chiral (8,4)
graphene sheet
hexagonal simmetry
sp2carbons, 1.41 Å
4
3 –Force FieldsandMolecular Models
3.1 –All-atompotential(AA-OPLS)
●nonbondedinteractions: All-atomLennard-Jones(12,6) withexplicitCoulombiccharges
●bondsandangles: harmonic
●dihedrals: triple cosine
●nanotubes : All-atomgraphiticcarbons[Steele1973]
(
)∑∑
−
+
=i
j
ij
ijij
ijij
ij
ijji
ijf
rr
r
eq
qr
U
612
2
4σ
σε
()
[]
[]
[] )
cos(
)cos(
)cos(
i
i
i
i
i
i
i
i
VV
VU
φφ
φφ
31
22
12
12
32
1+
+−
++
=∑
3.2 –United-atompotential(2CLJQ)
●nonbondedinteractions: Lennard-Jones(12,6) beads(CH2, CH3) with
a quadrupole momentatthecenterofmass
()
()
()
()
[]
22
22
2
5
026
12
52
15
51
443
4j
ij
ij
i
ab
ij
ijij
ijij
ijab
ijc
cc
cc
cc
r
Q
rr
rr
U−
+−
+−
+
−
=∑∑
πε
σσ
ε,
3 –Force Fields
δ δδδ+ +++
δ δδδ+ +++
δ δδδ− −−−δ δδδ− −−−
δ δδδ− −−−
δ δδδ− −−− δ δδδ− −−−
δ δδδ− −−−
Q
5
4 –MD Simulations
3.3 –Single-walledcarbonnanotubes
●frozengraphiticcarbonatoms
d (C-C ) = 1.42 Å
squeezingoutoftheπorbitals
●explicitcarbonatoms: corrugatednanotubes
●effectivediameter: fromsurfaceto surface(accessiblevolume)
CRT
eff
DD
σ−
=
6
4 –SimulationsDetails
4.1 –ClassicalMolecular Dynamics
●NVTensemble(Nosé-Hoover thermostat)
●T= 300 K
●timestep = 1 fs(Verletleapfrogalgorithm)
●timescale0.5 –3ns
●Potentialcutoff= 15 Å
●Ewaldsummation (fluids)
MD box : 30 ×
30 ×302Å(60 ×60 ×302Å) ; SWCNT box : 30×30 ×
52Å(60 ×60 ×
52Å)
NCRT≈800 atoms(L
z=52 Å), N
fluid= 150-1200 atoms(density)
4.2 –GrandCanonical Monte Carlo
●µVTensemble
●Tpure= 300 K, 260 K ≤Tmix≤450 K
●cycles total= 30 ×106, cycles production= 5 ×106
●Potentialcutoff= 20 Å
●GCMC box : 25 ×25 ×
53 Å
7
5 –Equilibriumandadsorptionresults
5.1 -Adsorptionofpure
fluids
Bulkfluidequilibration@300K (t> 0.1ns)
Bulk ethylene being adsorbed onto a zig-zagSWCNT (16,0)
●fluids: 4 ×10-4≤pbulk≤53.6 bar
8
5 –Results
●typeI isotherms(IUPAC)
●similar behaviourwithSipsandTothisotherms
●overestimationwiththe2CLJQ (inaccuraterigidbehaviourandstaticchargedistributionfor
flexiblemoleculeslikeC2H6); convergenceafterp ≈10 bar [Cruz 2008]
●C2H6ispreferentiably adsorbedatlowp(dispersiveenergy); cross-overaround3 −6 bar
(activatedcarbons, slitpores, higherDSWCNTs); atmedium-highpressureC2H4isthe
dominantspecies(entropicfactor / packingefficiency) ; isosteric heatsofadsorption(q
iso=
−∆H)
()
[]t
ts
bP
bP
CC
Toth
1
1+
=µ
µ:
()
()nn
s
bP
bP
CC
Sips
1
1
1+
=µ
µ:
0
50
100
150
200
250
300
350
400
AA-OPLS
2CLJQ
0.01
1E-3
0.1
110
C2H4
Surface Coverage (µµµµmol/m2)
p / bar
050100
150
200
250
300
350
400
AA-OPLS
2CLJQ
C2H
6
Surface Coverage (µµµµmol/m2)
p / bar
0.01
1E-3
0.1
110
9
5 –Results
11.7 bar
1.45 bar
0.28 bar
pbulk
25 bar
10
5 –Results
●armchair(9,9) andchiral (12,6) nanotubes presentsimilar lowpressure(p< 1 bar)
adsorptioncapacities(−3.4 % to 7 %)
●nanotubes loadingcapacityseemsto bea quadraticfunctionofthetubes’diameter
(4.46 Å, 6.80 Å, 9.15 Å, 11.49 Å, 13.83 Å)
05
1015
20
020406080100
120
140
C2H
4 (9.5 Å)
C2H
6 (10 Å)
Surface Coverage (µµµµmol/m
2)
D / Å
11
5 –Results
5.2 -Separationofbinary
mixtures(C
2H4/C
2H6)
i )refinery mixture (90 mol % C
2H4), p= 1 bar
●Sdecreaseswith
T(high temperatures reduce
the energetic differences between molecules);
Selectivity’s
values
are similar
to larger
nanotubes andotherporegeommetries
ii )equimolar mixture, 0.1 ≤
p≤30 bar
●Sdecreasesrapidlyupto p≈10bar, andfrom
thenonwardsgainsa monotonical behaviour.
●the higher selectivity values coincide with the
low pressure regions, where ethane is the
preferentially adsorbed species
bulk
ethylene
ethane
nanotube
ethylene
ethane
xx
xx
S)
/(
)/
(=
250
300
350
400
450
1234
1 bar
Selectivity
T / K
05
1015
2025
3001234
200K
300K
400K
Selectivity
p / bar
12
6.1 -Methodology
●Once the adsorption runs were finished, the upper volume of the simulation cell,
containing the nanotube and the adsorbed molecules, was separated from the bulk fluid
and replicated four times along the z-axis to produce a 30 ×
30 ×206Åsupercell
containing ca.3000 graphitic carbon atoms.
●Molecular displacementhasbeenmonitoredfor 0.5 ns: bulkandconfinedfluids.
●0.026 ≤ρ/mol�L–1≤15.751 (C2H4)
●0.011 ≤ρ/mol�L–1≤14.055 (C2H6)
6 –Dynamicalproperties
13
6.2 -Porecontact
●A previouslyreportedhelicaldiffusivepathfor pureC2’s inzig-zagSWCNT’s[Mao2000],
hasalsobeenobservedherefor denseconfinedfluidsandcorrespondingbinary
mixtures(wallsimmetryandC –C bonds) .
ethaneSWCNT
●Notsurprisingly, chiral tubesexhibita more pronouncedspirallingeffect!
●No coherentdisplacementfor armchairtubes.
14
5 –Results
Ddt
dr
Fickian
∝2
:
22
Bdt
dr
Ballistic
∝:
6.3 -Effectivediffusion
●Linear behaviour=> Fickian-typediffusion=> self-diffusion(effective), D(10-8m2/s,)
()()
[]2
061
rt
rdtd
D−
=
()()
[]2
20
rt
rr
MSD
−=
=
50100
150
200
250
300
1
2,5x10
3
5,0x10
3
7,5x10
3
1,0x10
4
C2H
4 @ (16,0)SWCNT
MSD / ÅÅÅÅ2
t / ps
Ballistic
Fickian
15
5 –Results
6.3 -Effectivediffusion
●increaseofD, withdecreaseofmoleculesinsidethetube, untilltransitionto outsidethe
Fickian regime: ρ< 5.5 mol�L–1(@SWCNT) [Cruz 2008]
●lowdensitysystems: ballisticandmixedtyperegimes (freespaceavailablefor molecular
jumps)
●no significative influenceoftheSWCNT’ssimmetryontheFickian diffusivities(Zig-zag,
armchairandchiral nanotubes)
110
100
1000
1
101
102
103
104
105
106
C2H4 @ bulk
MSD / ÅÅÅÅ2
t / ps
ρρρρρρ
110
100
1000
1
101
102
103
104
105
106
C2H6 @ bulk
MSD /
ÅÅÅÅ2
t / ps
ρρ
110
100
1000
1
101
102
103
104
105
106
C2H4 @ bulk
MSD / ÅÅÅÅ2
t / ps
ρ
16
5 –Results
6.3 -Scalinglaws
●confined phase diffusion data can be estimated by the knowledgeof the corresponding
bulk fluid structural properties, and this idea can become immediately appealing when
one keeps in mind practical and industrial applications (e.g.nanofluidics).
●Dbulk= A �ρ–B : empiricalcorrelationverifiedfor ethylene, againstexperimental data upto
ρ≈9.9 mol�L–1(discrepancieslessthan5 %).
00,01
0,1
110
100
10-8
10-7
10-6
10-5
10-4
SWCNT
bulk
C2H4
D / mmmm2s-1
ρ ρρρ / mol�L-1
00,01
0,1
110
100
10-8
10-7
10-6
10-5
10-4
SWCNT
bulk
C2H6
D / mmmm2s-1
ρ ρρρ / mol�L-1
17
7 –Conclusions& Futurework
7.1 -Conclusions
●Resultsseem to show that the adsorption and transport behaviourof the pure fluids is
relatively independent of host simmetry.
●Relatively small changes in the nanotube diameter can have a marked effect on the
transport and adsorption properties. Further work would be required to confirm the
present findings in a larger pore with/temperature range.
●Ethane is the preferred adsorbed species (low p), ethylene diffusivities are larger than
those of ethane, although the difference is relatively minor.
●Confinedfluids’diffusiondata canbeestimatedfromthecorrespondingbulkphases
(scalinglaw).
7.2 -Perspectives
●C3fluidsandtheirbinarymixtures(D-ρscalinglaw).
18
Acknowledgements
EPSRCGrantEP/D035171/1, UK