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Thermodynamic and transport properties of fluids: towards a LJ-SAFT molecular model valid for n-alkanes

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HAL Id: hal-01051603

https://hal.archives-ouvertes.fr/hal-01051603

Submitted on 25 May 2021

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Thermodynamic and transport properties of fluids:

towards a LJ-SAFT molecular model valid for n-alkanes

Guillaume Galliero, C. Boned, Stephanie Delage Santacreu, Marc Odunlami, F. Montel

To cite this version:

Guillaume Galliero, C. Boned, Stephanie Delage Santacreu, Marc Odunlami, F. Montel. Thermody- namic and transport properties of fluids: towards a LJ-SAFT molecular model valid for n-alkanes.

SAFT2011 discussion meeting. Pau, France, octobre 2011, 2011, pau, France. 2011. �hal-01051603�

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THERMODYNAMIC AND TRANSPORT PROPERTIES OF FLUIDS:

TOWARDS A LJ-SAFT MOLECULAR MODEL VALID FOR N-ALKANES

MODELS AND THEORY

We study the limitations of the Lennard-Jones Chain fluid model (LJ-SAFT) to describe simultaneously all thermophysical properties (equilibrium and transport) of some n-alkanes along the vapor-liquid equilibrium line

Molecules movements numerically computed (Newton equations) Spatial and temporal averages (∼10

3

particles, ∼10 ns)

MOLECULAR DYNAMICS

Guillaume GALLIÉRO

1

, Christian BONED

1

, Stéphanie DELAGE

2

, Marc ODUNLAMI

2

and François MONTEL

3

1

Laboratory of Complex Fluids and their Reservoirs, UMR 5150 TOTAL-CNRS, Pau University, FRANCE.

2

Laboratory of Applied Mathematics, UMR 5142 CNRS, Pau University, FRANCE.

3

TOTAL E&P, CST, Avenue Larribau, Pau, FRANCE.

LJ-SAFT

LJC LJ chain

A = A + A

No H-bonding, no polar and flexible

ALJusing the reference term of Kolafa & Nezbeda, (FPE 1994)

RESULTS

Exact thermophysical properties for a given molecular model

VAPOR-LIQUID EQUILIBRIUM SHEAR VISCOSITY

number of segments: N

+ internal bonds

Freely jointed Lennard-Jones spheres (Lennard-Jones Chain)

1 2 6

L J

4

U r r

σ σ

ε

=        −       

FLUID MODEL

( T , )

0

( ) T

res

( T , )

η ρ = η + η ρ

Dilute gas Residual/Excess viscosity

VISCOSITY MODEL OF LJC

Extended Chapman for η

0

and Rousse approximation for η

res Galliero et al, IECR, 2005,

Galliero and Boned, PRE, 2009, PRE, 2010

Internal rigidity is included by U

flex

= k ε θ ( − θ

0

)

2

600 700

500 600

ρ (kg.m-3)

0 200 400 600

T(K)

200 250 300 350 400 450

ρ (kg.m-3)

0 100 200 300 400

T(K)

100 120 140 160 180 200

NIST Data MD LJ-SAFT

methane n-butane

N=1 for C1, N=2 for C4, N=3 for C7 and N=4 for C10, σand εhave been adjusted

Achainusing the chain term of Johnson et al. (JPC 1994)

Accurate apart close to the critical point

Valid for gas, liquid and supercritical states Based on MD results

(10-6Pa.s) 50 100 200 500 1000

(10-6Pa.s) 50 100 200 500 1000 T (K)

100 120 140 160 180 200

η (10-6Pa.s) 5 10 50 100

20 200

NIST Data LJC Corr.

T (K)

200 250 300 350 400 450

η (10-6Pa.s) 5 10 50 100

20 200 500

n-heptane n-decane

methane n-butane

SAFT 2011 Discussion Meeting, October 24-25, Pau, 2011

As well known this fluid model is correct for n-alkanes

Internal degrees of freedom (such as rigidity) should be included in a SAFT like approach

ρ (kg.m-3)

0 200 400 600

T(K)

300 400 500

ρ (kg.m-3)

0 200 400 600

T(K)

300 400

n-heptane n-decane

but TcSAFT> TcMD> Tc (↗↗↗↗with N)

T (K)

250 300 350 400 450 500 550

η (10

5 10 50 20

T (K)

300 400 500 600

η (10

5 10 50 20

SURFACE TENSION

T (K)

100 200 300 400 500 600

γ (10-3 N.m-1)

0 5 10 15 20 25 30

NIST Data MD

Crossover approach is needed to deal with the critical region

Surface tensions are slightly overestimated A simple correction of the

critical temperature is sufficient The coupling between DGT/DFT and LJ-SAFT

yields good results

Galliero et al., JCP, 2008

η η η

η is well estimated, except at low liquid T when N ↗ ↗ ↗ ↗ This weakness is related to the flexibility of the chain

Temperature (K)

200 250 300 350 400 450

Viscosity (µPa.s)

0 500 1000 1500 2000

NIST Data k = 0 k = 1 k = 10 k = 100 k = 3000

η

is highly affected by the rigidity while thermodynamic

(fluid phase) only weakly

This degree of freedom (rigidity) can be used to improve simply

the fluid model

Concerning thermal conductivity, λ

0

is out of range when N ↗

(internal degrees of freedom) but the λ

res

of LJC is correct

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