9
Assessing the transferability of common top-down and bottom-up coarse-grained molecular models for molec- ular mixtures. Thomas D. Potter, a Jos Tasche, a and Mark R. Wilson *a Supplementary Material Table S 1 Scaling factors used, and iterations required, for IBI optimisa- tion. The numbers in parenetheses are, respectively, the number of iter- ations after which only the R-R interaction and pressure were optimised, and the α used for the iterations after this. x oct Iterations α f 0.0 62 0.1 0.0005 0.2 183 0.4 0.0005 0.3 248 0.3 0.0005 0.5 278 0.35 0.0005 0.7 300 (297) 0.35 (0.15) 0.0005 0.8 266 (271) 0.35 (0.2) 0.0005 1.0 56 0.5 0.001 Table S 2 Scaling factors used, and iterations required, for the MS-IBI optimisation. The numbers in parenetheses are the number of MS-IBI iterations which were carried out, after which pressure correction was applied. For the MS-3c and MS-4c models the same η value was used for each reference concentration, for the MS-2t model, a different η value was used at each temperature. Model Iterations η f MS-3c 319 (300) 0.2 0.0004 MS-4c 310 (295) 0.2 0.0004 MS-2t 248 0.7 at 238 K, 0.5 at 378 K 0.0001 Calculation of mixing free energies Free energies of mixing were calculated using the methodology described by Darvas et al., 1 which is based on the thermodynamic cycle shown in Figure S1. ΔA pure and ΔA sol were calculated from the vaporisation free energies, Δ vap A of octane, benzene, and the relevant mixture, as described in Equations 1 and 2. The free energy of mixing of two ideal gases, ΔA ideal was calculated ana- a Department of Chemistry, Durham University, South Road, Durham, DH1 3LE, United Kingdom. * Author for correspondence. E-mail: [email protected] Fig. S 1 Thermodynamic cycle used to calculate ΔA mix for octane and benzene. lytically using Equation 3. The free energy of mixing, Δ mix A, was then calculated from Equation 4. ΔA pure = x oct Δ vap A oct + x ben Δ vap A ben (1) ΔA mixed = -Δ vap A mixture (2) ΔA ideal = RT (x oct ln x oct + x ben ln x ben ) (3) Δ mix A = ΔA pure + ΔA mixed + ΔA ideal (4) Vaporisation free energies were calculated in a similar way to solvation free energies. However, instead of decoupling the inter- molecular interactions for one molecule, the intermolecular inter- actions are simultaneously decoupled for all the molecules in the system. The same soft-core parameters and strategies for picking λ points were used as for solvation free energies. In this case, all simulations were run in the NVT ensemble, so the results are Helmholtz free energies of mixing. Simulations of pure octane and benzene were carried out at their equilibrium densities, as calculated from NpT atomistic simulations. The vol- umes for each mixture were then calculated from V mixture = x oct V oct + x ben V ben (5) 1–9 | 1 Electronic Supplementary Material (ESI) for Physical Chemistry Chemical Physics. This journal is © the Owner Societies 2018

Assessing the transferability of common top-down and …Assessing the transferability of common top-down and bottom-up coarse-grained molecular models for molec- ular mixtures. Thomas

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Page 1: Assessing the transferability of common top-down and …Assessing the transferability of common top-down and bottom-up coarse-grained molecular models for molec- ular mixtures. Thomas

Assessing the transferability of common top-down andbottom-up coarse-grained molecular models for molec-ular mixtures.

Thomas D. Potter,a Jos Tasche,a and Mark R. Wilson∗a

Supplementary Material

Table S 1 Scaling factors used, and iterations required, for IBI optimisa-tion. The numbers in parenetheses are, respectively, the number of iter-ations after which only the R-R interaction and pressure were optimised,and the α used for the iterations after this.

xoct Iterations α f0.0 62 0.1 0.00050.2 183 0.4 0.00050.3 248 0.3 0.00050.5 278 0.35 0.00050.7 300 (297) 0.35 (0.15) 0.00050.8 266 (271) 0.35 (0.2) 0.00051.0 56 0.5 0.001

Table S 2 Scaling factors used, and iterations required, for the MS-IBIoptimisation. The numbers in parenetheses are the number of MS-IBIiterations which were carried out, after which pressure correction wasapplied. For the MS-3c and MS-4c models the same η value was usedfor each reference concentration, for the MS-2t model, a different η valuewas used at each temperature.

Model Iterations η fMS-3c 319 (300) 0.2 0.0004MS-4c 310 (295) 0.2 0.0004MS-2t 248 0.7 at 238 K, 0.5 at 378 K 0.0001

Calculation of mixing free energiesFree energies of mixing were calculated using the methodologydescribed by Darvas et al.,1 which is based on the thermodynamiccycle shown in Figure S1. ∆Apure and ∆Asol were calculated fromthe vaporisation free energies, ∆vapA of octane, benzene, and therelevant mixture, as described in Equations 1 and 2. The freeenergy of mixing of two ideal gases, ∆Aideal was calculated ana-

a Department of Chemistry, Durham University, South Road, Durham, DH1 3LE, UnitedKingdom.∗ Author for correspondence. E-mail: [email protected]

Fig. S 1 Thermodynamic cycle used to calculate ∆Amix for octane andbenzene.

lytically using Equation 3. The free energy of mixing, ∆mixA, wasthen calculated from Equation 4.

∆Apure = xoct∆vapAoct + xben∆vapAben (1)

∆Amixed =−∆vapAmixture (2)

∆Aideal = RT (xoct lnxoct + xben lnxben) (3)

∆mixA = ∆Apure +∆Amixed +∆Aideal (4)

Vaporisation free energies were calculated in a similar way tosolvation free energies. However, instead of decoupling the inter-molecular interactions for one molecule, the intermolecular inter-actions are simultaneously decoupled for all the molecules in thesystem. The same soft-core parameters and strategies for pickingλ points were used as for solvation free energies.

In this case, all simulations were run in the NVT ensemble, sothe results are Helmholtz free energies of mixing. Simulations ofpure octane and benzene were carried out at their equilibriumdensities, as calculated from NpT atomistic simulations. The vol-umes for each mixture were then calculated from

Vmixture = xoctVoct + xbenVben (5)

Journal Name, [year], [vol.], 1–9 | 1

Electronic Supplementary Material (ESI) for Physical Chemistry Chemical Physics.This journal is © the Owner Societies 2018

Page 2: Assessing the transferability of common top-down and …Assessing the transferability of common top-down and bottom-up coarse-grained molecular models for molec- ular mixtures. Thomas

0.0 0.2 0.4 0.6 0.8 1.0xoct

−1.4

−1.2

−1.0

−0.8

−0.6

−0.4

−0.2

0.0

0.2∆Amix

/ kJ

mol−1

IBIHFMAtomisticMS-4c

Fig. S 2 Helmholtz free energies of mixing of octane-benzene mixtures,using atomistic, IBI, MS IBI and HFM models.

Mixing free energy results are plotted in Figure S2

References1 M. Darvas, P. Jedlovszky and G. Jancsó, J. Phys. Chem. B, 2009,

113, 7615–7620.

2 | 1–9Journal Name, [year], [vol.],

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0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

U /

kJ m

ol−1

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

U /

kJ m

ol−1

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4r / nm

−1.5

−1.0

−0.5

0.0

0.5

1.0

U /

kJ m

ol−1

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4r / nm

−1.5

−1.0

−0.5

0.0

0.5

1.0

a) b)

c) d)

e) f)

Fig. S 3 Non-bonded potentials parametrised using IBI for the a) A-A, b) A-B, c) B-B, d) A-R, e) B-R, f) R-R interactions. Each potential in each plotparametrised at a different octane concentration: 20% (blue), 30% (green), 50% (red), 70% (cyan) and pure octane or benzene (yellow).

Journal Name, [year], [vol.], 1–9 | 3

Page 4: Assessing the transferability of common top-down and …Assessing the transferability of common top-down and bottom-up coarse-grained molecular models for molec- ular mixtures. Thomas

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

U /

kJ m

ol−1

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

U /

kJ m

ol−1

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4r / nm

−1.5

−1.0

−0.5

0.0

0.5

1.0

U /

kJ m

ol−1

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4r / nm

−1.5

−1.0

−0.5

0.0

0.5

1.0

a) b)

c) d)

e) f)

Fig. S 4 Non-bonded potentials parametrised using HFM for the a) A-A, b) A-B, c) B-B, d) A-R, e) B-R, f) R-R interactions. Each potential in each plotparametrised at a different octane concentration: 20% (blue), 30% (green), 50% (red), 70% (cyan) and pure octane or benzene (yellow).

4 | 1–9Journal Name, [year], [vol.],

Page 5: Assessing the transferability of common top-down and …Assessing the transferability of common top-down and bottom-up coarse-grained molecular models for molec- ular mixtures. Thomas

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

U /

kJ m

ol−1

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

U /

kJ m

ol−1

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4−1.5

−1.0

−0.5

0.0

0.5

1.0

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4r / nm

−1.5

−1.0

−0.5

0.0

0.5

1.0

U /

kJ m

ol−1

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4r / nm

−1.5

−1.0

−0.5

0.0

0.5

1.0

a) b)

c) d)

e) f)

Fig. S 5 Non-bonded potentials parametrised using MS IBI for the a) A-A, b) A-B, c) B-B, d) A-R, e) B-R, f) R-R interactions. Potentials from the MS-3c(blue), MS-4c (green) and MS-2t (red) models.

Journal Name, [year], [vol.], 1–9 | 5

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Fig. S 6 Coarse grained bonded potentials from Boltzmann inversion of the pure reference systems at 298 K: a) octane A-B (blue) and B-B (green)bonds, b) octane angle, c) octane dihedral and d) benzene bond (not used in simulations).

6 | 1–9Journal Name, [year], [vol.],

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Fig. S 7 Bonded distributions for pure octane and benzene systems from atomistic (blue), IBI (green) and HFM (red) simulations at 298 K. a) octaneA-B bond, b) octane angle, c) octane dihedral and d) benzene bond distribution.

Journal Name, [year], [vol.], 1–9 | 7

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0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.60.00.20.40.60.81.01.21.41.61.8

g(r)

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.60.0

0.2

0.4

0.6

0.8

1.0

1.2

1.4

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.60.00.20.40.60.81.01.21.41.61.8

g(r)

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.60.0

0.2

0.4

0.6

0.8

1.0

1.2

1.4

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6r / nm

0.00.20.40.60.81.01.21.41.61.8

g(r)

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6r / nm

0.00.20.40.60.81.01.21.41.6

a) b)

c) d)

e) f)

Fig. S 8 Non-bonded distributions from simulations of the MS-3c (green) and MS-4c (red) models, compared to atomistic simulation results (blue). Theplots show: a) A-A at 20% octane, b) R-R at 20%, c) A-A at 50%, d) R-R at 50%, e) A-A at 80%, f) R-R at 80%.

8 | 1–9Journal Name, [year], [vol.],

Page 9: Assessing the transferability of common top-down and …Assessing the transferability of common top-down and bottom-up coarse-grained molecular models for molec- ular mixtures. Thomas

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.60.0

0.5

1.0

1.5

2.0

g(r)

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.60.00.20.40.60.81.01.21.41.6

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.60.00.20.40.60.81.01.21.41.6

g(r)

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.60.0

0.2

0.4

0.6

0.8

1.0

1.2

1.4

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6r / nm

0.0

0.2

0.4

0.6

0.8

1.0

1.2

1.4

g(r)

0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6r / nm

0.0

0.2

0.4

0.6

0.8

1.0

1.2

a) b)

c) d)

e) f)

Fig. S 9 Non-bonded distributions from simulations of the MS-2t model simulated at: constant-NV T and the correct atomistic density (green), constant-NPT and 1 bar pressure (red); and the atomistic model (blue). The plots show: a) A-A at 238 K, b) A-A at 378 K, c) A-B at 238 K, d) A-B at 378 K, e)B-B at 238 K, f) B-B at 378 K.

Journal Name, [year], [vol.], 1–9 | 9